nistUNITED STATES

DEPARTMENT OF COMMERCE

TECHNOLOGY ADMINISTRATION

NATIONAL INSTITUTE OF STANDARDS

AND TECHNOLOGY

NAT l INST. OF STAND » TECH R.I.C

A111D3 T2flT3D

NIST

PUBLICATIONS

NIST Technical Note 1346

/VaZL

i

Tables for the Thermophysical Properties

of Ethane

Daniel G. Friend

James F. Ely

Hepburn Ingham

Thermophysics Division

Chemical Science and Technology Laboratory

National Institute of Standards and Technology

Boulder, Colorado 80303-3328

January 1993

*^TE8 Of *

U.S. DEPARTMENT OF COMMERCE, Barbara Hackman Franklin, Secretary

TECHNOLOGY ADMINISTRATION, Robert M. White, Under Secretary for Technology

NATIONAL INSTITUTE OF STANDARDS AND TECHNOLOGY, John W. Lyons, Director
National Institute of Standards and Technology Technical Note

Natl. Inst. Stand. Technol., Tech. Note 1346, 316 pages (January 1993)

CODEN:NTNOEF

U.S. GOVERNMENT PRINTING OFFICE

WASHINGTON: 1992

For sale by the Superintendent of Documents, U.S. Government Printing Office, Washington, DC 20402-9325
CONTENTS

LIST OF TABLES iv

LIST OF FIGURES iv

LIST OF SYMBOLS AND UNITS v

ABSTRACT viii

1 . INTRODUCTION 1 2. THERMODYNAMIC PROPERTIES AND THEIR ALGEBRAIC REPRESENTATION 2 2 . 1 Fixed Point Constants 2

2 . 2 Liquid- Vapor Saturation Boundary 4

2 . 3 Ideal Gas Equation 5 2.4 Residual Helmholtz Energy 6 2 . 5 Derived Property Equations 6 3. TRANSPORT PROPERTIES AND THEIR ALGEBRAIC REPRESENTATION 11

3 . 1 Dilute Gas Correlations 11

3 . 2 Excess Property Correlations 12

3 . 3 Critical Enhancement Correlation 14

4. SUMMARY OF UNCERTAINTIES ASSOCIATED WITH THE CORRELATIONS 15

4.1 Two -Phase Boundary 15

4 . 2 Ideal Gas Properties 16

4 . 3 Thermodynamic Properties 16

4.4 Transport Properties 20

4.4.1 Viscosity 20

4.4.2 Thermal Conductivity 21

5 . ACKNOWLEDGMENTS 22

6 . REFERENCES 22

7 . APPENDICES 28

Appendix A: Comparisons between experimental

data and the correlations 28

Appendix B: Tables for the thermophysical properties

of ethane 112

Appendix C: Listing of a FORTRAN 77 program to calculate

the thermophysical properties of ethane 283

in
LIST OF TABLES

1. Fixed point constants and other parameters used in the correlations. 3 2. Coefficients for liquid-vapor boundary correlations 5

3. Coefficients needed for ideal gas Helmholtz energy, eq (5) 6 4. Exponents and coefficients for the residual Helmholtz energy 4> , eq (6) 7 5

Ideal gas Helmholtz energy and its derivatives 8 6

Residual Helmholtz energy and its derivatives 9

7

Thermodynamic property equations 10

8

Coefficients for dilute gas transport properties 12

9Coefficients for excess transport properties 13

Bl. Properties of ideal gas at 0.1 MPa and dilute gas

transport properties 112

B2 . Properties along saturation boundary 121

B3. Properties in the single-phase region along isobars 127

B4Properties in the single-phase region along isotherms 239

LIST OF FIGURES

AlSaturated vapor pressure 30

A2 . Saturated liquid density 36

A3 . Saturated vapor density 42

A4A. Ideal gas entropy 45

A4B. Ideal gas isobaric heat capacity 47

A4C

Ideal gas enthalpy 49

A5 . Second virial coefficient 51

A6APVT data- -pressure deviations 54

A6B. PVT data- -density deviations 59

A7

Isochoric molar heat capacity 67

A8

Isobaric molar heat capacity 70

A9

Molar heat capacity of the saturated liquid 72

A10. Sound speed in the single-phase fluid 74

All

Sound speed in the saturated liquid 76

A12

Viscosity at zero density 78

A13

Thermal conductivity at zero density 81

A14

Viscosity at elevated pressures 84

A15Thermal conductivity at elevated pressures 97

IV
LIST OF SYMBOLS AND UNITS

Symbol Description SI Units

(used in text)

REFERENCE

Roman

A

B

C

i n t

G

G

i Si H

H

i J

i

j

i k

M

r N

A n

i P

Q.

i

Molar Helmholtz energy

Second virial coefficient

(2 2 ) * Coefficients in Q ' Molar isobaric heat capacity

Molar isochoric heat capacity

Crossover function in A

c r f Contribution from internal modes

Molar Gibbs energy

Coefficients in p Coefficients in r/ e Molar enthalpy

Coefficients in P

a Coefficients in p

J»mol 1 a

ctL

ctV Coefficients in A

e x Boltzmann constant

Relative molecular mass Avogadro constant

Coefficients in 4> Pressure

Coefficients in <f>* Wavenumber cutoff

Gas constant

id

dm «mol

J«mol »K

J«mol *K

J«mol

J«mol

J-K

mol

MPa

nm

J«mol «K

eq (4)

table 7 eq (10) .table 8 table 7 table 7 eqs (15,17)

eqs (11,12)

,

table 8 table 7 eq (2) , table 2 eq (13) .table 9 tables 1 ,

7

eq (1) .table 2 eq (3) .table 2 eq (14) .table 9 table 1 table 1 table 1 eq (6) .table 4

eq (5) , table 3 eq (17)

table 1

Exponent of 5

Molar entropy J»mol »K

eqs (6,13,14),

tables 2, 9 table 7
LIST OF SYMBOLS AND UNITS (CONT'D)

Symbol Description SI Units

(used in text)

s. Exponent of r

t Reduced temperature, kT/e

T Temperature, IPTS-68

T Reduced temperature, (T -T)/T

U Molar internal energy u Unified atomic mass unit w Speed of sound

Z Compressibility factor, P/RTp

REFERENCE

- eqs (6,13 14)

tables 29

- eqs (9,10 12)

K -

- eqs (1-3)

T I' 1 J»mol table 7 kg table 1 -1 m»s table 7

- eq (3)

Greek

B Scaling° exponent in p T ,p

ctL CTV

7 Potential parameter

5 Reduced density, p/p

e Scaling exponent in P , 2 -a

e Energy parameter

e/k Energy parameter

r\ Shear viscosity

A Thermal conductivity

| Correlation length

p Molar density

a Distance parameter

r Reduced inverse temperature, T /T

<f> Reduced Helmholtz energy, A/RT

(2 2)*

CI ' Reduced collision integral

- eqs (2,3),

table(2)

- Ref. [13]

- eq (1) , table 2)

J See e/k

K table(l)

/xPa»s

iW • m • K

eq (7)

eq (8)

run mol'dm

eqs (15,16)

nm table 1

- eqs (4-6)

- eqs (9,10)

Superscripts

id Ideal gas contribution

r Residual contribution

eq (4) , table 1 eq (4)

VI
Symbol

LIST OF SYMBOLS AND UNITS (CONT'D)

Description SI Units

(used in text)

REFERENCE

Subscripts

c Value at critical point

cr Critical contribution

ex Excess contribution

t Value at triple point

tL.tV Value at triple point in liquid, vapor

o Value at saturation boundary

ctL.ctV Value in saturated liquid, vapor

5 Partial derivative with respect to 8

t Partial derivative with respect to r Value at zero density

table 1 eqs (8,15)

eqs (7,8,13,14)

table 1 table 1 eq (1)

eqs (2,3)

tables 5-7

tables 5-7

eqs (7-9,11)

Throughout this paper, extensive physical quantities are given on a molar

basis. The elementary entities are the ethane (C„H,) molecules.

Vll
TABLES FOR THE THERMOPHYSICAL PROPERTIES OF ETHANE

Daniel G. Friend, James F. Ely, and Hepburn Ingham

Thermophysics Division

National Institute of Standards and Technology

Boulder, Colorado 80303

The thermophysical properties of ethane are tabulated for a large range of

the fluid state based on recently formulated correlations. For the

thermodynamic properties, temperatures from 90 to 625 K at pressures less

than 70 MPa are included; for the viscosity, the corresponding range is 90-

500 K with pressures to 60 MPa; for the thermal conductivity the range is

90-600 K with pressures to 70 MPa. In addition to the tables of

properties, algebraic expressions and associated tables of coefficients are given to allow additional property calculations. Graphical comparisons

between experimental property determinations and the correlation are also

given both for primary data used in the formulation of the correlations and

for additional data. A listing of a FORTRAN program for the evaluation of

ethane thermophysical properties is included.

Key words

correlation; density; equation of state; heat capacity; ethane; phase

boundary; pressure; speed of sound; thermal conductivity; thermophysical

properties; transport properties; virial coefficients; viscosity.
1. INTRODUCTION

We have recently developed correlations for several of the

thermophysical properties of ethane [1], including an equation of state

analogous to that proposed by Schmidt and Wagner [2], equations for the

liquid-vapor phase boundary, and correlations for the fluid viscosity and

thermal conductivity. Details of the development and error analysis of the

formulations have been presented elsewhere [1] ; in this paper, we summarize

our equations and present extensive graphical comparisons of the

correlations with experimental data and tables of properties based on these

correlations. We have also included the listing for a FORTRAN program

which can be used interactively to calculate properties of ethane. The

correlations are similar in form to those published previously for methane

[3], and this report is analogous to the earlier Technical Note on the

properties of methane [4]. A separate Internal Report [5] gives a full

tabular listing of experimental data considered in the development of the

ethane correlations.

The rationale for these new correlations and the present set of tables was discussed in Ref . [1] . Briefly summarized, earlier extensive works

include those of Goodwin et al. [6], Sychev et al. [7], and Younglove and Ely

[8]. Our correlations account for some new experimental measurements, and more important, the form of the residual Helmholtz free energy

correlation, first proposed by Schmidt and Wagner [2], gives an excellent

description of the thermodynamic surface and describes the critical region

extremely well for a classical equation of state. The new ancillary

equations for the phase boundary incorporate the results of lowest order

scaling theory, and both viscosity and thermal conductivity correlations

improve the description of the fluid properties when compared to previous

correlations. Our current description of the enhancement of the thermal

conductivity is based on the very recent mode-coupling work of Olchowy and

Sengers [9] . The economic importance of ethane, as a major constituent

of natural gas, makes the use of improved thermophysical properties

correlations especially desireable. Also, the present correlations should

prove useful as reference equations for corresponding- states models for

mixtures and other pure fluids. These equations, together with the

similar study of methane, will assist in the development of correspondingstates formalisms.

-1-
The next two sections give the algebraic forms for the fluid

property correlations of thermodynamic and transport properties, with

brief narrative. The List of Symbols and Units given above is a useful

adjunct to the equations, and tables of needed coefficients and

constants are interspersed throughout the text. Extensive discussion of

the development of the equations and evaluation of fitted coefficients

was given in Ref. [1]. Figures which follow, in Appendix A, give the

comparisons between the correlations and experimental data; these

include both primary data, used in the determination of the coefficients

in the equation, and secondary data, which were not explicitly used for

any of a number of reasons as discussed in Ref. [1]. The next set of

tables, in Appendix B, gives values of the thermophysical properties for

convenient values of the temperature, density, or pressure. Finally,

this report concludes with a listing of a FORTRAN 77 program, in

Appendix C, which allows interactive evaluation of many thermophysical

properties for any state point within the range of the correlations.

2. THERMODYNAMIC PROPERTIES

AND THEIR ALGEBRAIC REPRESENTATION

2.1 Fixed Point Constants

Values for the critical and triple-point constants, intermolecular

potential parameters (for transport properties using the 11-6-8, 7=3

potential), reference values for ideal gas properties, and miscellaneous

constants are given in table 1. Details of the selection process and

quoted uncertainties are given in Ref. [1]. The values of the critical

constants, including all the quoted digits and disregarding the associated

uncertainties, are needed for evaluating the correlating equations below.

The fundamental constants in table 1 agree with the values most recently

recommended by CODATA [10].

-2-
Table 1. Fixed point constants and other parameters used in the

correlations

Triple Point: T = 90.352 ± 0.005 K

a

t P = 1.130 ± 0.005 Pa

t

p T = 21.667 ± 0.01 mol.dm" 3 K tL

p = 1.504 ± 0.02 mol.dam" 3 p tv

Critical Point: T = 305.33 ± 0.04 K

b

c

P = 4.8718 ± 0.005 MPa

c

-3

p = 6.87 ± 0.1 mol^dm

c

Z = 0.279 34 ± 0.005

c Intermolecular

Potential e/k = 245.0 K a = 0.436 82 ran Parameters

Ideal Gas (at 298.15 K and 0.101 325 MPa)

Reference Point S ld = 229.12 J.K^.mol" 1

Values

H

ld = 11.874 kJ-mol" 1

Miscellaneous

Relative molecular mass...M = 30.070

r Universal gas constant... R = 8.314 510 J'mol «K

-23 -1

Boltzmann constant... k = 1.380 658 x 10 J'K

23 -1

Avogadro constant... N = 6.022 136 7 x 10 mol

-27

Unified atomic mass unit..u = 1.660 540 2 x 10 kg

b

This corresponds to 90.360 K on ITS-90 scale.

This corresponds to 305.32 K on ITS-90 scale.
2.2 Liquid-Vapor Saturation Boundary

Three ancillary equations for the pressure, liquid density, and

vapor density along the two-phase boundary are described in this

section. Although the full equation of state can be used with the

Maxwell construction method to evaluate these quantities, these

equations include theoretically inspired scaling terms and therefore are more accurate in the critical region. The development of the equations

was discussed in Ref. [1].

For the saturated vapor pressure P the equation

P (T) - P exp [ H.T*/(1-T*) + H_T* + H T*

£ + H T*

2 + H T^

3

], (1)

where T =(T -T)/T , is used. The necessary constants and critical exponent

are given in table 2

The densities of the saturated liquid p and saturated vapor

p are given by

av ° J

PnJ (T) = oL Prc

1 +

*B *2 *3 *4 n G.T p+ G T + G T + G T

1 + G,T

4

(1-/S)

(2)

and

P (T) =

av

R T

1+P (T)r

o s^- 1 1+

J T

p + J.T p + J (T +T ) + J T

1 + J.T

4

1

(3)

respectively. In eq (3), Z = P /(RT p ) is the critical compressibility

factor given in table 1, r = T_/T, and P (T) must be evaluated from eq (1). The

C o constants are again found in table 2. Figures Al , A2 , and A3 in Appendix A

give comparisons between experimental phase boundary measurements and

the quantities calculated by eqs (1-3).

4-
Table 2. Coefficients for liquid-vapor boundary correlations

Saturated Vapor Saturated Liquid Saturated Vapor Dens ity

Pressure eq (1) Density eq (2) eq (3)

e = 1.90 £ = 0.355 P = 0.355

H = -7.955 315

H^ = 1.532 827

H^ = 14.780 68

H^ =-13.431 79

H^ = 4.704 891

G = 1.930 740

Gy = -0.653 985 6

G = 0.814 136 2 G = -0.339 743

G = -0.383 814 1

J = -0.748 371 9

j" = -1.372 895

J^ = -1.192 597

J if = 1.861 505

j; = 1.313 649

4

2.3 Ideal Gas Equation

The thermodynamic surface is described by an equation for the molar

Helmholtz energy, A. Thus, the important derived properties can be

obtained by simple, analytical differentiation. The Helmholtz energy is

divided into ideal gas and residual constituents according to

A(p,T) = A

ld + A

r = RT^ = RT(<?>ld + 4?) . (4)

All the derived thermodynamic properties can similarly be divided into

ideal and residual contributions as discussed below.

Our ideal gas correlation is based on the spectroscopically derived

data of Chao et al. [111. With the definitions 5 = p/p and r = T /T, the

c c dimensionless ideal gas contribution to the Helmholtz energy is written as

4> ±d

(8,T) = A

ld

/ RT

Q1 + In 5 + Q

2 In r + Q 3 r" 1/3 +

Q4

t' 2/3 + Q5 r"

1 + Q6

In (1 - eV) (5)

with the coefficients Q. given in table 3. Equation (5) must be evaluated

at the experimental density and temperature, although for many

thermodynamic properties, there is no density (or pressure) dependence in

the required derivatives, as discussed below. The constants in table 3 incorporate integration constants necessary to give the standard values of

the entropy and enthalpy reported in table 1. A figure comparing the

spectroscopic data and the correlations is given in Appendix A.

-5-
Table 3. Coefficients for ideal gas Helmholtz energy, eq (5)

Qn = -28.594 991 Q4 = -3.307 573 5 Q

= -23.446 765 Q = -0.559 566 78

Q = 3.815 947 6 <

- 5.072 226 7 Q = 8.602 129 9 <

= -5.507 487 4

2.4 Residual Helmholtz Energy

The residual term in eq (4) for the Helmholtz energy was correlated

by a 32-term function introduced by Schmidt and Wagner [2]. The resulting

equation of state has been called the SWEOS , and the coefficients for

the ethane fluid were obtained by a multiproperty least-squares regression

as described in Ref. [1]. Explicitly, we write

13

k

r s

r

i d 8 T i=l

24

r s

c

i i no t i=14 x

32

-8

i=25n 8

i (6)

with 8 = p/p and t = T /T, as before. The coefficients n and the

c c i exponents r and s are given in table 4.

2.5 Derived Property Equations

One can evaluate many of the thermodynamic properties of ethane by

taking the appropriate derivatives of the Helmholtz energy as given in

eqs (4-6). In tables 5 and 6 we have collected the coefficients necessary

to calculate the six lowest order derivatives for the ideal gas and

residual contributions to the Helmholtz energy. In our notation, the first

isothermal (reduced) density derivative of the (reduced) residual free

energy is denoted

4> r

8

8<f> (8,t)

88 RT

3A (p,T)

dp

and similarly for other derivatives.

-6
Table 4. Exponents and coefficients for the residual Helmholtz energy <f> eq (6)

i r.11s. n.

l

c r. s.

5 l r l

110 0.462 154 305 60

2 1 1.5 -0.192 369 363 87 X 10

3 1 2.5 0.398 786 040 03

4 2 -0.5 0.160 545 323 72 X 10

5 2 1.5 0.128 952 422 19

6 2 2 0.354 583 204 91 X lO'J"

7 3 0.349 278 445 40 X 10"

8 3 1 -0.113 061 833 80 X 10"

9 3 2.5 -0.398 090 327 79 X 10"^

10 6 0.830 319 368 34 X 10

11 7 2 0.459 215 751 83 X 10~ 3 12 7 5 0.175 302 879 17 X 10~£

13 8 2 -0.709 195 161 26 X 10

,2

-o r r. s. e 5 l t l

14 1 5 -0.234 361 622 49

15 1 6 0.845 746 976 45 X 10

16 2 3.5 0.148 610 520 10

17 2 5.5 -0.100 168 578 67

18 3 3 -0.592 648 243 88 X 10

19 3 7 -0.412 635 142 17 X 10"|

20 5 6 0.218 551 618 69 X 10"^

21 6 8.5 -0.745 527 209 58 X 10"^

22 7 4 -0.988 590 855 72 X 10"^

23 8 6.5 0.102 084 164 99 X 10

24 10 5.5 -0.521 896 558 47 X 10" 3

-8A r r. s. e 6 l t i

25 2 22 0.985 921 620 30 X 10"^

26 3 11 0.468 651 408 56 X 10"

27 3 18 -0.195 580 116 46 X 10~7

28 4 11 -0.465 571 616 51 X 10"^

29 4 23 0.328 779 053 76 X 10

30 5 17 0.135 720 901 85

31 5 18 -0.108 464 714 55

32 5 23 -0.675 028 369 03 X 10

7-
To calculate derivatives of the ideal gas contribution to the free

energy, one is guided by the form of eq (5). The left-most column of table

5 lists the factors necessary for the various derivatives, and the

remaining columns give the coefficients of these factors directly beneath

the heading which indicates the quantity to be calculated. The resulting

terms are to be added as in eq (5). The values of the Q. parameters are obtained from table 3.

Table 5. Ideal gas Helmholtz energy and its derivatives

eq (5) ( =1 )

A id

T

( =-i5)

2 ± id

T 6

TT

X A ld

( =6 r

)

1 \

l Q

2 -1 -«2

In 5 1

In r «2

r "V3 % -Q3/3 4Q

3 /9

-2/3

T ^4 - 2 <V3 10Q

4/9

-1

T % -*5 2Q

5 In (1 - eQ7

r

) %

(e-V-l)- 1 -w

eV (eV -I)"

2 2 2 -V>7 T

For derivatives of the residual Helmholtz energy, eq (6) and tables

4 and 6 can be used. As in eq (6), the derivatives are obtained by

summing 32 terms of three general types. Each of the terms has

factors consisting of powers of the reduced density and temperature with

the explicit exponents r. and s. and coefficients n. given for each

value of i in table 4. The additional exponential factor, with its

argument either the second or fourth power of the density, is indicated

in the column heading of table 6 where appropriate. The remaining

coefficients relevant to the derivative being calculated are given in

the appropriate row in that table.

8
Table 6. Residual Helmholtz energy and its derivatives

r. s. n. 8

x t L

l (i = 1 to 13)

,2

-8 r. s. e n. 5 1 t

L

l (i = 14 to 24)

-8A r . s . e n. 8

L r L l (i = 25 to 32)

*

r

1 1 1

H

T

S

r.

i r. - 2S

2

1 r. - 45

4

l

T s

l s1 s

l

5 *88 r.(r.-l) 11

[r.(r -1)

-2(2r +1)5

Z+45 ]

[r.(r -1)

-4(2r +3)5„

V165 8

]

T 6

TT

s.(s.-l) 11 s.(s.-l) 11 s.(s.-l) 11

St *\t r . s

l l s.(r.-25 2

) l l s.(r.-45 4

) l l

In table 7, the most common thermodynamic properties of interest have

been expressed in terms of the reduced derivatives of the Helmholtz

energy as discussed above. All nominally extensive quantities (that is,

the various thermodynamic potentials and heat capacities) are given

per mole. It is straightforward to calculate, by using these tables,

the most useful thermodynamic properties of ethane. In Figures A4-9 of

Appendix A, we give comparisons of experimental data and correlated values

for the PVT surface, second virial coefficient, isochoric heat capacity,

isobaric heat capacity, heat capacity of the liquid along the saturation

boundary, and speed of sound.

9-
Table 7. Thermodynamic property equations

Pressure

:

P(p,T) = pRT ( 1 + 6**)

Internal Energy: U(p,T) = RT ( r/d + r/ ) T T

Enthalpy: H(p,T) = RT ( 1 + r^

ld + T<f> r + 6<t> V

c ) T TO

Gibbs Energy: G(p,T) = RT ( 1 + 4> ±d + 4> X + 8<t> X

c )

Helmholtz Energy: A(p,T) = RT ( tf ld + f )

Entropy: s(p,T) = -r ( /

d + <f> r

- r^d- r4> r

) T T

Isochoric Heat Capacity: Cv

(p,T) - -R ( r 2 ^ + T 2

t

rTr )

Isobaric Heat Capacity:

( 1 + St* - Sr<j, r

) 2 C („,T) - C („,T) + R

P r 2 r

1 + 2t *

t + s *ss

Saturated Liquid

Heat Capacity:

C

aL m -

Cv

( <WT > if>

- R ( 1 + S*

z

s

- ST**, ) / d

°L

aL

Speed of Sound: 2 RT C

p

(P ' T)

r 2 r W (.P.-U - (,llZO<P f IO "Per; UN M C (p,T)

S SS

A r v

Second Virial

Coefficient:

1 B(T) = — lim <j> r

P 5^0

c

10-
3. TRANSPORT PROPERTIES

AND THEIR ALGEBRAIC REPRESENTATION

The viscosity and thermal conductivity are correlated as the sum of

terms representing the temperature dependent dilute gas contribution, a temperature and density dependent excess contribution and, for the thermal

conductivity, a contribution from the critical enhancement. The viscosity

is given by

r?(p,T) = r/ (T) + r/^p.T), (7)

and the expression for thermal conductivity is

A(p,T) = A Q

(T) + A ex(p,T) + A cr(p,T) (8)

These terms are explicitly described in this section.

3.1 Dilute Gas Correlation

Our expression for the dilute gas viscosity is from the Chapman- Enskog

theory [12]. Using the appropriate constants from table 1, we find

r? Q

(T) = 12.0085 Jt / fl (2 ' 2) *(t) /zPa-s, (9)

where the reduced temperature t = kT/e . The collision integral Q

has been approximated for the 11-6-8, 7 = 3 intermolecular potential

function [13]

9

(2,2)*

Q (2,2)* } c. t

t (i " l)/3 - 1]

i=l

(10)

with coefficients C. listed in table 8. The collision integrals tabulated

in Ref. [13] were compared to eq (10) in table A10 of Ref. [4]; experimental

values of rj. are compared to values calculated from eq (9) in Figure A10

-11-
Table 8. Coefficients for dilute gas transport properties

(2 2)*

fi U '^ , eq (10) f

lnt , eq (12)

C

c

l

c

2

c

3

C

5

-3.032 813 828 1

16.918 880 086 f

l 1.710 414 7 -37.189 364 917

41.288 861 858 f

2

-0.693 648 2 -24.615 921 140

c

8

8.948 843 095 9

-1.873 924 504 2 0.209 661 013 90

-9.657 043 707 4 x 10

For the thermal conductivity A. of the dilute gas, we have chosen a modified Eucken model [14] with resulting equation

A_(T) = 0.276 505 r? A (T) [ 3.75 - f. (r%ld + 1.5) ] mW-m"

1 ^" 1

. (11)

u U int tt

In eq (11) , f . is the dimensionless function defined by int J

f int = f

l + < f2 /

C > (12)

with the fitted coefficients f also given in table 8, and the viscosity

should be expressed in /xPa»s, as in eq (9). The quantity r <f> in eq (11)

T T can be evaluated from tables 3 and 5. Figure A12 of Appendix A gives

comparisons between experimental values for the dilute gas thermal

conductivity and values calculated from eq (11)

3.2 Excess Property Correlations

For the excess viscosity, we use the rational polynomial

11

r) (p.T) = 15.977

ex

i=l

r. s.

c L 1 x-5

i=10

r. s

c 1 1 g±

5 r

-i-l

//Pa* s , (13)

-12
where the exponents r. and s. and the dimensionless fitted coefficients g. are given in table 9. Comparisons between experimental viscosities

and viscosities calculated using eq (7) with eqs (9) and (13) are given in Figure A13 of Appendix A.

The excess thermal conductivity A has been correlated to a J ex polynomial in 5 and t ;

A (p,T) = 4.417 86 ex ),

r. s.

o r i=l

mW»m »K (14)

The exponents and dimensionless fitting coefficients for eq (14) are included in table 9.

Table 9. Coefficients for excess transport properties

^x- e q ( 13 > ex

eq (14)

i r.

l l °i

r.

l

s

l h

1 1 0.471 770 03 1 0.960 843 22

2 1 1 -0.239 503 11 2 2.750 023 5 3 2 0.398 083 01 3 -0.026 609 289

4 2 1 -0.273 433 35 4 -0.078 146 729

5 2 1.5 0.351 922 60 5 0.218 813 39

6 3 -0.211 013 08 1 1.5 2.384 956 3 7 3 2 -0.004 785 79 3 1 -0.751 139 71

8 4 0.073 781 29

9 4 1 -0.030 425 255

10 1 -0.304 352 86

11 1 1 0.001 215 675

13-
3.3 Critical Enhancement Correlation

The remaining term in eq (8) is the critical enhancement of the

thermal conductivity which is easily observed in a broad region around the

critical point. We have correlated this using a simplified mode coupling

model developed by Olchowy and Sengers [9]. After evaluating the

universal, fluid dependent, and correlated constants, we write

8 C

P -1 -1

A (p,T) = 1.55 - — F(5,r) mW-m

X .K \ (15)

T r\ £

where the molar isobaric heat capacity is measured in J«mol «K , the

correlation length, £ defined below, is in run, and the viscosity is

expressed in /xPa«s in eq (15).

The correlation length used in eq (15) is calculated from

0.507 r 2 r -1 r 2 r -1 0.507

i = 0.428 (8t) [(l+28<t> +8 <f> ) - (1+25^(1/2) + 5 <£(l/2)) ] run.

8 88 8 88

(16)

The dimensionless crossover or damping function in eq (15) is given by

F = -n

-q

D

e [l+^oVos2 )]" 1 c -cv

e - 1 +

C

P

-1

cv

tan (qcO + q^ Vcv

(17)

and q = 0.545 nm is the only adjustable parameter in the theory.

Because we are using a classical equation of state to evaluate the heat

capacities in eqs (15) and (17) and the derivatives in eq (16), the

damping function will not extrapolate well in the asymptotically

critical region.

14-
4. SUMMARY OF UNCERTAINTIES

ASSOCIATED WITH THE CORRELATIONS

The examination of the deviations of our correlations from

experimental data using deviation plots such as included in Appendix A and

in Ref. [1], tabular comparisons between the data and the correlations such

as in Ref. [5], the assessment of the experiments themselves and their

reported accuracies, and comparisons of these correlations with previously

published equations have allowed us to estimate the uncertainties

associated with the correlations in various regions of the phase diagram.

In this section, we will summarize the results of our assessment so that the

equations and the tables in Appendix B can be used appropriately; details

concerning the establishment of these uncertainties are given in Ref. [1].

4.1 Two-Phase Boundary

First, for the pressure along the liquid-vapor saturation boundary, we have considered the uncertainties of both the triple point and critical

point pressures (table 1) and the quality of both the primary and other

experimental data. We estimate that either the ancillary eq (1) or the

SWEOS will provide values of the saturation pressures accurate within 0.1%

above T = 165 K, within 1% between 130 and 165 K, and within 5% for

temperatures from the triple point to 130 K where the vapor pressure is

less than 0.003 MPa.

The coexistence densities can also be calculated from the ancillary

equations, eqs (2) and (3), or using the SWEOS. In the critical region,

the ancillary equations express the theoretically described behavior with

a critical exponent of 0.355. The SWEOS, while approximating this

flattened coexistence dome quite well, approaches the critical point with

the mean field exponent of 0.5, and thus cannot accurately describe this

region. Both equations are constrained to give the reported critical

density at the critical temperature. For the density of the saturated

liquid, either the ancillary equation or the value of the density from the

-15-
SWEOS can be used with an estimated uncertainty of 0.1% from the triple

point to 200 K, of 0.3% from 200 K to 304 K, and about 1.5% between 304 K

and the critical point at 305.33 K.

At temperatures below 250 K, the density of the saturated vapor is less

-3

than 1 mol'dm , and direct measurements are sparse and uncertain. In the

critical region, there is a large scatter in the data. Our analysis

indicates that either the ancillary equation or the SWEOS will generate

values for the density of the saturated vapor with uncertainties as follows: from T to 130 K, 5%; from 130 to 240 K, 1.5%; from 240 to 303 K,

0.3%; and from 303 to T , 5%.

c

4.2 Ideal Gas Properties

The disagreement between thermodynamic extrapolations of the ideal gas

isobaric heat capacity [43] and the spectroscopically derived data [11] has

not been satisfactorily resolved. We estimate the uncertainty in the ideal

gas correlation as follows: for the enthalpy, 1.5%; for the isobaric heat

capacity, 1.5%; and for the entropy, 1.0%; all from the triple -point

temperature to 700 K.

4.3 Thermodynamic Properties

In this section, we discuss the uncertainties associated with the full

equation of state. We begin with the second virial coefficient and note

that there are no data below 150 K. The SWEOS has not been constrained to

provide physically reasonable values of B in this region and cannot be

used to evaluate the virial series below 150 K. The Boyle temperature of

ethane is well above the maximum temperature considered in this study;

extrapolation of our SWEOS correlation gives a value near 747 K. Our

assessment of the data and correlation leads to an estimate of the

uncertainty in second virial coefficients calculated from the SWEOS as follows. At temperatures from 150 to 200 K, there is an uncertainty of

-16-
10%; from 200 to 250 K, this decreases to 3%; from 250-500 K, 1%; and from

500 to 600 K, the maximum temperature considered, the estimated uncertainty

is 2%.

The PVT surface is considered next, and both the calculation of

pressure with temperature and density as independent variables and the

calculation of density with temperature and pressure as independent

variables are discussed. There are problems when calculating pressures

from the SWEOS (or using any equation of state) in regions where the

isotherms are very steep (as in a pressure versus density plot in the low

temperature liquid region). Also, when the PV isotherms are very flat, in

the critical region, it is difficult to calculate accurate fluid densities.

Our examination of both primary and other experimental data, including

the experimental technique, reported uncertainty of the data, purity of the

fluid ethane, and deviations from the SWEOS and other equations of state,

have led us to these guidelines concerning the uncertainty of a PVT surface

generated from the SWEOS. For the vapor at temperatures below 250 K, where

the vapor pressure is about 1.3 MPa and the vapor density is about 0.8

-3

mol'dm , calculations of both density and pressure from the SWEOS have

uncertainties of about 0.1%. Liquid densities in this temperature range

also have uncertainties of 0.1%; the calculation of pressure from a liquid

density at these low temperatures is much more difficult. For pressures

less than 10 MPa, the percent deviation in pressure may be very large, and

it increases near the saturation boundary. Typically, the absolute

deviation is within about 1 MPa. For higher pressures, the uncertainty

ranges from 5% at temperatures below 200 K down to 1% for temperatures from

200 to 250 K.

Temperatures from 250 K to 300 K are still far enough from the

critical point that accurate density calculations from the SWEOS are possible. For the vapor in this range, we estimate an uncertainty of 0.2%

for both density and pressure calculations. For the liquid state near the

saturation boundary at the lower temperatures of this range, to 265 K,

large percentage deviations are possible. For pressures greater than 5 MPa

or temperatures from 265 to 300 K, we estimate the uncertainty in the

pressure calculation as 3%. Critical phenomena evidently do not lead to

-17-
problems for the SWEOS for calculations at subcritical temperatures below

-4

305.3 K: at 305.3 K, the reduced temperature, (T -T)/T is about 10 , but

~ the two-phase region excludes densities between about 6.4 and 7.4 mol«dm , that is, within about 7% of the critical density. For the vapor at

temperatures between 300 and 305.3 K, we estimate the uncertainty in both

density and pressure calculations as less than 0.5%. For the liquid in

this temperature range, uncertainties in both density and pressure

calculations are estimated as 0.5% at pressures to 10 MPa, but the density

uncertainty drops to 0.1% above 10 MPa.

When conditions are very close to the critical point, that is, with

temperatures from 305.3 to 307 K with pressures between 4.6 and 5.2 MPa,

the uncertainty in calculated densities may be 5%; the uncertainty in

pressure in this region is 0.2%. Outside this critical region, from 305.3

to 315 K, the uncertainty in density is estimated at 0.3% and the

uncertainty in pressure is 1% for pressures below 40 MPa and 3% for

pressures above 40 MPa. For the higher supercritical temperatures, we estimate the uncertainty in density as 0.2% for pressures below 40 MPa and

0.5% for higher pressures. The pressure uncertainties are 0.5% for

pressures below 40 MPa and 3% for higher pressures.

Theoretical and observational evidence indicates a divergence in the

isochoric heat capacity described by C ~(T-T ) along the critical

isochore; a ~ 0.11. This critical exponent is not approximated well by the

SWEOS, which gives the classical value, a = 0. Calculation of the

isochoric heat capacity using the SWEOS is not recommended for temperatures

-3

from 305 to 306 K with densities between 5.5 and 8.0 mol«dm

Uncertainties of 10%, in C calculations, are estimated for temperatures

*- -3

from 305 to 307 K with densities between 5 and 8.5 mol»dm . Outside this

general critical region, we estimate the uncertainty in calculation of the

isochoric heat capacity as 2.5%.

We estimate the uncertainty in calculations of the isobaric heat

capacity from the SWEOS as 1.5% throughout the liquid and vapor states at

temperatures below 290 K and in the supercritical region above 320 K. An

exception is made for the compressed liquid with densities above 20

-3

mol»dm , where the uncertainty increases to 4%. At points closer to the

-18-
critical point, but outside a region bounded by 305 and 307 K and by 5 and

-3

8.5 mol • dm , the uncertainty is 6%. At points within this boundary, we

note that C as calculated by the classical SWEOS diverges along the

critical isochore with the mean field exponent of 1 rather than the

observed exponent of about 1.2; in addition, roundoff error causes the

12 -1 -1

finite value of C ~4 x 10 J»mol »K at the critical point. Thus,

percent errors can be very large in this region, but physical measurements

of these extremely large heat capacities are exceedingly difficult.

We estimate the uncertainty in calculations of the heat capacity of

the saturated liquid, C T , from our SWEOS as 3.5% from the triple point to

ctL 145 K and 0.6% from 145 to 280 K. Closer to the critical point, the usual

problems with the classical equation of state occur; the uncertainty

increases to 5% for temperatures from 280 to 303 K. For temperatures

between 303 and T very large errors are possible.

It is difficult to correlate the sound speed to within the reported

experimental accuracies while obtaining good agreement with other data and

using the classical SWEOS formulation. The problems are most serious at

high densities and near the critical point. We can summarize our observations by the following guidelines for the use of the SWEOS in

calculating the speed of sound in ethane. Below 100 K, in the saturated or compressed liquid, we estimate the uncertainty as 1%. Between 100 and 225

K, the liquid-phase sound speed has an uncertainty of 0.6%. Between 225 K

and 290 K and above 310 K, the uncertainty increases to about 1%. Between

_3 290 and 310 K, for densities outside the range 5 to 10 mol* dm , a 2%

uncertainty is estimated. Closer to the critical point, the uncertainty

ranges to 10%; at points between 305 and 306 K, with densities from 5 . 5 to

-3

8 mol«dm , the classical SWEOS cannot be used: rather than vanishing at

the critical point, the calculated sound speed is about 181 m»s . For the

gas below 290 K, we estimate an uncertainty of 0.6%. For pressures above

35 MPa at subcritical temperatures and above 12 MPa for supercritical

temperatures, there are no data and we estimate an uncertainty of 2%.

The comparisons with experimental data (and the process of determining

the coefficients of the SWEOS) , only probe four derivatives of the

r r r r dimensionless , residual Helmholtz energy, namely <f> c , <j> .

, <f> , and <f> . TT T

-19-
While this SWEOS should describe the actual thermodynamic surface quite

well, additional uncertainties will enter any calculation which requires

other derivatives of <f> or integrals of the Helmholtz function. We

hesitate to make any quantitative estimates of the errors involved in

calculating any thermodynamic quantities not discussed in this section, but

we conjecture that these errors will be comparable to those found with any

other precise equation of state for ethane.

4.4 Transport Properties

4.4.1 Viscosity

From the dispersion of the data and correlations, the quoted

experimental accuracies associated with the data, and a study of the use of

the 11-6-8 intermolecular potential in the Chapman- Enskog dilute gas

theory, we estimate that the correlation of eqs (9) and (10) will give

dilute gas viscosities for ethane with associated uncertainties of 1% from

300 K to 375 K and 1.5 % above that range. In the region from 250 K to 300

K, the estimated uncertainty is 1.5%. For lower temperatures, data are extremely sparse or nonexistent. We anticipate that the theory, with this

potential function, will extrapolate well, but we increase our error estimate to 5% for temperatures from the triple point to 250 K.

We next examine the viscosity of ethane at elevated pressures. From

the triple-point temperature to 250 K, we estimate the uncertainty in the

correlation for the vapor phase as 5%. We estimate a 2.5% uncertainty for

the vapor viscosity at temperatures from 250 K to the critical point. Our

correlation does not account for any critical enhancement in the viscosity;

therefore, the critical region, 305-306 K and 6-7.5 mol«dm , should be

excluded when making calculations with this viscosity correlation. For the

liquid from the triple point to the critical point for pressures from the

saturation boundary to 30 MPa, we estimate the uncertainty of the

correlation as 2%. For higher pressures, the uncertainty increases to

about 5%. We estimate the uncertainty of the viscosity correlation in the

-20-
supercritical region as generally 2%. At pressures greater than 50 MPa,

the uncertainty increases to 5%, and in the critical region, from 305 to

-3

307 K and 5 to 8.5 mol»dm (but excluding the region 305 to 306 K and 6 to 7.5

-3

mol'dm as indicated above), the uncertainty is also 5%. The viscosity

correlation can have a zero in the denominator, corresponding to a singularity, within the fluid region; this occurs well outside the range of

any data and the stated range of the correlation. In addition to the usual

warnings concerning extrapolation beyond the range of the correlating

equation, any user is cautioned about this singularity, which can be a problem only at pressures exceeding 220 MPa.

4.4.2 Thermal Conductivity

There are few data for the dilute gas thermal conductivity at very low

temperatures. At the lowest temperatures, between the triple point and 200

K, where the vapor pressure is about 0.2 MPa, the correlation for the

dilute gas thermal conductivity could give errors in excess of 10%. In the

range 200 to 350 K, the uncertainty in the correlation is about 3%, and

between 350 K and 600 K we estimate the uncertainty as 4%.

We have estimated the uncertainty associated with our correlation for

the thermal conductivity of ethane at elevated pressures. In the gas

phase, the large uncertainty in the dilute gas contribution dominates at

temperatures below 200 K; the uncertainty in the total thermal conductivity

is 10% for the gas at these low temperatures. For temperatures from 200 K

to T the uncertainty in the gas phase thermal conductivity is about 3%.

For the compressed liquid, we estimate uncertainties of 2% to the upper

pressure limit of 70 MPa. The asymptotically critical region extending

.3

from 305 to 306 K with densities between 6 and 7.5 mol»dm " can still give

large errors; our value of the thermal conductivity at the critical point

is about 1.5 kW«m «K , not infinity. In the more general critical region

.3 bounded by 305 and 307 K from 5 to 8.5 mol«dm , we estimate the

uncertainty as 10%. At supercritical temperatures, the uncertainty is 4%

.3 for densities less than 2 mol»dm and 2% for higher densities. For

temperatures between 307 and 360 K, and densities between 5 and 8.5

-3

mol'dm , the critical enhancement contribution remains substantial, and i uncertainty of 5% is estimated.

21
ACKNOWLEDGMENTS

We gratefully acknowledge support from the Office of Standard Reference

Data of the National Institute of Standards and Technology. We thank

B.S. Coultrip, M. H. Nguyen, P. Ma, and J. Weimer for assistance with

data compilation, properties tabulations, and graphics.

6. REFERENCES

1. D.G. Friend, H. Ingham, J.F. Ely, "Thermophysical Properties of

Ethane," J. Phys . Chem. Ref. Data 20, 275 (1991).

2. R. Schmidt and W. Wagner, Fluid Phase Equil. 19, 175 (1985).

3. D.G. Friend, J.F. Ely, H. Ingham, J. Phys. Chem. Ref. Data 18, 583

(1989).

4. D.G. Friend, J.F. Ely, H. Ingham, "Tables of the Thermophysical

Properties of Methane," Natl. Inst. Stand. Technol., Technical Note

1325 (1989).

5. D.G. Friend, J.F. Ely, H. Ingham, "Tables of Experimental Data used for

the Correlation of the Thermophysical Properties of Ethane," Natl. Inst.

Stand. Technol., NISTIR 3953 (1990).

6. R.D. Goodwin, H.M. Roder, G.C. Straty, Natl. Bur. Stand. (U.S.),

Technical Note 684 (1976).

7. V.V. Sychev, A. A. Vasserman, A.D. Kozlov, V.A. Zagoruchenko , G.A.

Spiridonov, V.A. Tsymarny, Thermodynamic Properties of Ethane

(Hemisphere Publishing, Washington, 1987), T.B. Selover Jr., English

Language Edition Ed.

8. B.A. Younglove and J.F. Ely, J. Phys. Chem. Ref. Data 16, 577 (1987).

9. G.A. Olchowy and J.V. Sengers , Phys. Rev. Lett. 61, 15 (1988) and

Int. J. Thermophys. 10, 417 (1989).

10. E.R. Cohen and B. N. Taylor, J. Res. Natl. Bur. Stand. (U.S.) 92, 85

(1987).

-22
11. J. Chao, R.C. Wilhoit, B.J. Zwolinski, J. Phys . Chem. Ref. Data 2, 427

(1973).

12. J.O. Hirschfelder, C.F. Curtiss, R.B. Bird, Molecular Theory of Gases

and Liquids (Wiley, New York, 1967).

13. M. Klein, H.J.M. Hanley, F.J. Smith, P.Holland, Natl. Bur. Stand.

(U.S.), Monograph 47 (1974).

14. R.C. Reid, J.M. Prausnitz, and B.E. Poling, The Properties of Gases and

Liquids (McGraw-Hill, New York, 4th Ed., 1987).

15. C.H. Barkelew, J.L. Valentine, CO. Hurd, Trans. Amer. Inst. Chem. Eng.

43, 25 (1947)

16. G.F. Carruth and R. Kobayashi , J. Chem. Eng. Data 18, 115 (1973).

17. C.H. Chui and F.B. Canfield, Trans. Faraday Soc. 67, 2933 (1971);

M.Y. Shana'a and F.B. Canfield, Trans. Faraday Soc. 64, 2281 (1968).

18. L. Djordjevich and R.A. Budenholzer, J. Chem. Eng. Data 15, 10 (1970).

19. D.R. Douslin and R.H. Harrison, J. Chem. Thermodynamics 5, 491 (1973).

20. L.C. Kahre, J. Chem. Eng. Data 18, 267 (1973).

21. A.G. Loomis and J.E. Walters, J. Amer. Chem. Soc. 48, 2051 (1926).

22. V.M. Miniovich and G.A. Sorina, Russ. J. Phys. Chem. 45, 306 (1971).

23. A.K. Pal, G.A. Pope, Y. Arai, N.F. Carnahan, R. Kobayashi, J. Chem.

Eng. Data 21, 394 (1976).

24. G.A. Pope, Ph.D. Thesis (Dept. Chem. Eng.), Rice University (1971).

25. F. Porter, J. Amer. Chem. Soc. 48, 2055 (1926).

26. J. Regnier, J. Chimie Physique 69, 942 (1972).

27. W.T. Ziegler, B.S. Kirk, J.C. Mullins, A.R. Berquist, Technol. Report

No. 2, Proj . A-764, Eng. Expt. Sta. , Georgia Inst. Technol., Atlanta,

GA (Dec. 1964).

28. A.W. Tickner and F.P. Lossing, J. Phys. Colloid Chem. 55, 733 (1951).

29. G.C. Straty and R. Tsumura, J. Res. Natl. Bur. Stand. (U.S.) 80A, 35

(1976).

30. R.D. Goodwin, H.M. Roder, G.C. Straty, Natl. Bur. Stand. (U.S.),

Technical Note 684 (1976).

31. R.J. Gugnoni, J.W. Eldridge, V.C. Okay, T.J. Lee, AIChE J. 20,

358 (1974).

32. W.M. Haynes and M.J. Hiza, J. Chem. Thermodynamics 9, 179 (1977).

-23-
33. J. Klosek and C. McKinley, Proc. 1st Inter. Conf . on LNG , Paper 22,

Chicago (1968).

34. C.R. McClune, Cryogenics 16, 289 (1976).

35. J.E. Orrit and J.M. Laupretre, Adv. Cryo. Eng. 23, 573 (1978); J.E.

Orrit and J.F. Olives, "Density of liquefied natural gas and its

components ," distributed at Fourth International Conference on Liquefied Natural Gas, Algeria (1974).

36. M.W. Pestak, R.E. Goldstein, M.H.W. Chan, J.R. de Bruyn, D.A.

Balzerini, N.W. Ashcroft, Phys . Rev. B 36, 599 (1987).

37. J.B. Rodosevich and R.C. Miller, AIChE J. 19, 729 (1973).

38. P. Sliwinski, Z. Phys. Chem. Neue Folge 63, 263 (1969).

39. J.R. Tomlinson, Natural Gas Processors Association Technol. Publ. TP-1,

Tulsa, OK (1971).

40. F. Porter, J. Am. Chem. Soc. 48, 2055 (1926).

41. K.M Pamidimukkala, D. Rogers, G.B. Skinner, J . Phys . Chem. Ref. Data

11, 83 (1982).

42. TRC Thermodynamic Tables- Hydrocarbons , Thermodynamics Research Center,

Texas A6cM University, College Station, TX (Oct. 31, 1985).

43. K. Bier, J. Kunze , G. Maurer, J. Chem. Thermodynamics 8, 857 (1976);

K. Bier, J. Kunze, G. Maurer, H. Sand, J. Chem. Eng. Data 21, 5 (1976).

44. A. Furtado, Ph.D. Thesis (Dept. Chem. Eng.), University of Michigan,

Ann Arbor, MI (1973).

45. J.H. Dymond and E.B. Smith, The Virial Coefficients of Pure Gases and

Mixtures, Clarendon Press, Oxford (1980).

46. A. Eucken and A. Parts, Z. Phys. Chem. B20, 184 (1933).

47. H.E. Tester, in Thermodynamic Functions of Gases. Vol. 3, F. Din, ed.

,

Butterworths Scientific Publications, London (1961).

48. R.D. Gunn, M.S. Thesis, Univ. Calif. (Berkeley) 1958.

49. J. A. Huff and T.M. Reed III, J. Chem. Eng. Data, 8, 306 (1963).

50. S.D. Hamann and W.J. McManamey, Trans. Faraday Soc. 49, 149 (1953).

51. H.H. Reamer, R.H. Olds, B.H. Sage, W.N. Lacey, Ind. Eng. Chem. 36, 957

(1944)

24
52. A.E. Hoover, I. Nagata, T.W. Leland, and R. Kobayashi, J. Chem. Phys

48, 2633 (1968).

53. J.D. Lambert, G.A.H. Roberts, J.S. Rowlinson, and V.J. Wilkinson,

Proc. R. Soc. London A196, 113 (1949).

54. H. Mansoorian, K.R. Hall, and P.T. Eubank, Proc. 7 th Symp. on Thermophysical Properties, A. Cezairliyan, ed. , Amer. Soc. Mech.

Eng., New York, 456 (1977).

55. M.L. McGlashan and D.J. Potter, Proc. R. Soc. London A267, 478 (1962).

56. A. Michels, W. Van Straaten, J. Dawson, Physica 20, 17 (1954).

57. V.K. Strein, R.N. Lichtenthaler , B. Schramm, Kl. Schafer, Ber.

Bunsenges. Phys. Chem. 75, 1308 (1971).

58. J. A. Beattie, C. Hadlock, N. Poffenberger, J. Chem. Phys. 3, 93 (1935).

59. G.J. Besserer and D.B. Robinson, J. Chem. Eng. Data 18, 137 (1973).

60. Ye. A. Golovskiy, E.P. Mitsevich, V.A. Tsymarnyy, "Measurement of the

Density of Ethane at 90.2U-270.21 K and at Pressures to 604.09 bar,"

VNIIEGazprom Dep. No. 39M USSR (1978); data have been tabulated in

Ref. [52].

61. N.E. Khazanova and E.E. Sominskaya, Russ. J. Phys. Chem. 45, 87 (1971).

62. W.W.R. Law, "A Continuously Weighed Pycnometer Providing Densities for

CO + Ethane Mixtures between 240 and 350 K at Pressures to 35 MPa,"

Ph.D. Thesis, Texas A&M University (1986).

63. W.R. Parrish, Fluid Phase Equil. 18, 279 (1984).

64. J.V. Sengers , personal communication, Univ. Maryland, Inst. Phys. Sci.

and Technol., College Park, MD 1988.

65. C.B. Wallace Jr., I.H. Silberberg, J.J. McKetta, Petrol. Refiner,

Hydrocarbon Processing 43 No. 10, 177 (1964).

66. H.M. Roder, J. Res. Natl. Bur. Stand. (U.S.) 80A, 739 (1976).

67. T. Miyazaki, A.V. Hejmaki, J.E. Powers, J. Chem. Thermodynamics 12, 105

(1980).

68. R. Wiebe, K.H. Hubbard, M.J. Brevoort, J. Am. Chem. Soc. 52, 611

(1930).

69. R.K. Witt and J.D. Kemp, J. Am. Chem. Soc. 59, 273 (1937).

70. V.E. Terres, W. Jahn, H. Reissmann, Brennstoff-Chemie 38, 129 (1957).

71. R. Tsumura and G.C. Straty, Cryogenics 17, 195 (1977).

72. G.R. Poole and R.A. Aziz, Can. J. Phys. 50, 721 (1972).

-25-
73. E. Vangeel, Katholieke Universiteit , Leuven, Belgium, private

communication to D.E. Diller, Natl. Bur. Stand. (U.S.), (1974); data

were tabulated in table 17 of Ref . [6]

.

74. Y.Abe, J.Kestin, H.E. Khalifa, Physica 93A, 155 (1978).

75. H.Adzumi, Bull. Chem. Soc. Jpn. 12, 199 (1937).

76. L.T. Carmichael and B.H. Sage, J. Chem. Eng. Data 8, 94 (1963).

77. P.M. Craven and J.D. Lambert, Proc. R. Soc. London 205A, 439 (1951).

78. A.G. De Rocco and J.O. Halford, J. Chem. Phys . 28, 1152 (1958).

79. E. Eakin, K.E. Starling, J. P. Dolan, R.T. Ellington, J. Chem. Eng. Data

7, 33 (1962).

80. R. Fleeter, J. Kestin, W.A. Wakeham, Physica 103A, 521 (1980).

81. H. Iwasaki and M. Takahashi, J. Chem. Phys. 74, 1930 (1981).

82. J. Kestin, S.T. Ro, W.A. Wakeham, Trans. Far. Soc. 67, 2308 (1971).

83. J. Kestin, H.E. Khalifa, W.A. Wakeham, J. Chem. Phys. 66, 1132 (1977).

84. J.D. Lambert, K.J. Cotton, M.W. Pailthorpe, A.M. Robinson, J.Scrivins,

W.R.F. Vale, R.M. Young, Proc. R. Soc. London 231A, 280 (1955).

85. V.M. Trautz and K.G. Sorg, Ann. Phys. 10, 81 (1931).

86. H. Vogel, Ann. Physik 43, 1235 (1914).

87. A. A. Clifford, E. Dickinson, P. Gray, J. Chem. Soc. London, Trans.

Faraday Soc. 172, 1997 (1976).

88. T.F. Gilmore and E.W. Comings, AIChE J. 12, 1172 (1966).

89. F.G. Keyes, Trans. ASME. , 809 (1954).

90. B. Le Neindre, R. Tufeu, P. Bury, P. Jahannin, B. Vodar, in Proc. 8th

Int. Conf. Therm. Conduct., C.Y. Ho and R.E. Taylor, eds., Plenum, NY

(1969), p. 229.

91. D.E. Leng and E.W. Comings, Ind. Eng. Chem. 49, 2042 (1957).

92. J.M. Lenoir, W.A. Junk, E.W. Comings, Chem. Eng. Progress 49, 539

(1953).

93. J. Millat, M. Ross, W.A. Wakeham, M. Zalaf, Int. J. Thermophys . 9, 481

(1988).

94. R.C. Prasad and J.E. Venart, Int. J. Thermophys. 5, 367 (1984).

95. H.M. Roder and C.A. Nieto de Castro, High Temp. -High Pressures 17, 453

26-
(1985).

96. R. Tufeu, Y. Garrabos , B. Le Neindre, in Proc . 16th Conf . Therm.

Conduct., D.C. Larsen, ed. , Plenum, NY (1983), p. 605.

97. L.V. Yakush, N.A. Vanicheva, L.S. Zaitseva, Inz.-Fiz. Zh. 37, 1071

(1979); tr. in J. Eng. Phys . 37, 1071 (1979).

98. J.D. Baron, J.G. Roof, F.W. Wells, J. Chem. Eng. Data 4, 283 (1959).

99. D.E. Diller and J.M. Saber, Physica 108A, 143 (1981); and D.E. Diller,

Proc. 8th Symp. on Thermophysical Properties , J.V. Sengers , ed. , Amer.

Soc. Mech. Eng., New York (1982) p. 219.

100. D.E. Diller, unpublished data, Natl. Inst. Stand. Technol., Boulder, CO

(1991).

101. S.F. Gerf and G.I. Galkov, Zh. Tekh. Fiz . 10, 725 (1940).

102. S.F. Gerf and G.I. Galkov, Zh. Tekh. Fiz. 11, 801 (1941).

103. A. S. Smith and G.G. Brown, Industrial and Eng. Chem. 35, 705 (1943).

104. H.J. Strumpf, A.F. Collings, C.J. Pings, J. Chem. Phys. 60, 3109

(1974).

105. G.W. Swift, J. Lohrenz, F. Kurata, AIChE J. 6, 415 (1960).

106. V. A. Van Itterbeek and 0. Van Paemel, Physica 8, 133 (1941).

107. L.T. Carmichael, V. Berry, B.H. Sage, J. Chem. Eng. Data 8, 281 (1963).

108. P. Desmarest and R. Tufeu, Int. J. Thermophys . 8, 293 (1987).

109. R. Mostert, H.R. van den Berg, P.S. van der Gulik, J.V. Sengers, J.

Chem. Phys. 92, 5454 (1990).

110. R. Mostert, H.R. van den Berg, P.S. van der Gulik, Int. J. Thermophys.

10, 409 (1989).

lll.H.M. Roder, Natl. Bur. of Stand. (U.S.), NBSIR 84-3006 (1984).

-27-
Appendix A

Comparisons between experimental data and the correlations

This appendix contains graphical and statistical comparisons for the

experimental data and correlations used in our study of the thermophysical

properties of ethane. We have included both primary data, used to

determine the final coefficients in the correlating equations, and other

data. The complete set of data has been tabulated in Ref.[5].

The deviation plots are given on a percentage basis according to Dev = 100 (Cal - Exp) /Exp where Cal is the value calculated from the correlation

and Exp is the value from experiment. With only a few exceptions, the

experimental values for both independent and dependent variables used for

these comparisons were taken directly from the cited literature source. Those exceptions include conversion to SI units (and, in a few cases, to

IPTS-68), correction of obvious typographical errors, and adjustments as described in the notes. A few data from the cited sources were omitted

because the correction for obvious typographical errors was not clear, they

lay outside the range of state variables which we considered, or they lay

inside the solid, metastable, or two-phase region according to our correlations. These comparisons include some, especially older, data which

were not included in the statistical summaries or in the figures of

Ref . [1] . The values of the independent variables are indicated on the

abcissa and in the figure headings.

Summary statistics are given for each reference and are defined as follows

:

= - Z I AAD = - / | Cal.al . - Exp .

|

,

N i 1 X

-28-
1 \

BIAS = - / (Cal. - Exp.)

,

z_ 1 N i and

RMS = - 1 (Cal. Exp.)

2

- BIAS

2 N

l

1/2

The quantity N above represents the number of points in the data set, and

the summation over the index i is over all N points. These statistics give

dimensioned quantities; the analogously defined dimensionless statistics

are based on percentage deviations. Thus, AAD-%, BIAS-%, and RMS-% are defined as above, but with the quantity (Cal. - Exp.) replaced by

100 (Cal. - Exp.)/ Exp.

.

For each property illustrated in the figures, we list the references

from which primary data were obtained. In some instances, data from a single reference were included in both the primary and secondary (not used

to determine the final coefficients in the correlations) categories. In

this case, the figure legend indicates "2nd" for the secondary data and a separate entry and different symbol are used for the primary data; also,

two sets of statistics are given: for the primary data and for the entire

data set. Details concerning data selection were given in Ref. [1]. Only

the first author is given in the figure legends and captions; the full

bibliographic reference is given in the numbered reference list of Sec. 6.

29-
<r

Z>

CO

CO

LLI ec

Qo

<

>

o

LLI <

cc

Z>

<

CO

o

<

>

LU

Q

10.14

0.00

-10.14

4.47 o.oo

-4.47

3.24

0.00

-3.24

3.88

0.00

-3 88

4.64

0.00

-4.64

90.00 —98.00 K

e

°A° ° O

10

I—i—i i 1 1 1 1| An i i i 1

1

151.12 - 160.01 K

0.87 i Q o u

98.55

10"

106.00 K

10

.-5

o o

B-A

O A3

e- "l

1

1—i—i—rr 10" 10

108.00 - 116.00 K

o@ofb

-&r —I—I—I I I fll I

1—I—I I I I 1

1

10

6 10

4 10

116.00 - 126.00 K

-H- -a—

o o o

t2t

1 1 1 1—I—TT

10

126.00 - 135.00 K

10

O0OC£3

~i—i i i 1 1 rf -3 n—i—i i i i 1

1

10 10* 10

135.74 - 143.27 K

1.5-r- Q Q u o

0.0

-1.5

1.17 0.00

-1.17

A

10

3 1

1

1—I—TT143.37 - 151.00 K 03^

A

m

10'

n—

r

-i—i—i i i 1 1

1

10' 10" 10

-1

o.oo

-0.87

0.59

0.00

-0.59

0.69

0.00

-0.69

0.51

0.00

-0.51

0.48

0.00

-0.48

0.46

0.00

-0.45

0.37

0.00

-0.37

• •

00

"i

1—i—

r

10

161.00 - 1 68.90 K

10

"^

1 1—»i 1—i—i

rr 10" 10

169.18 - 175.00 K

»*Qo

i n=n—i—i

r~r 10

175.71 - 180.25 K

10

-1

10

-2 i—

r

181.00 - 185.14 K

10

1

1—I—I I I I 1 1—I Mill

10 10 10

185.48 - 190.00 K

^—i

1 1—i—i—i—

n

10"' 10

190.79 - 199.91 K

-A^#-

10

-1 i—i i i 10"

PRESSURE (MPa) PRESSURE (MPa)

O- BflRKEXEH A" CflRRUTH X- OJOROJEVICH H- LOOMIS Q- REGNIER • - ROSSINI O- TICKNER D- ZIEGLER O- ZIEGLER (2ND) A- RNCILLRRT EQ.

( 15)

( 16)

( 18)

( 21)

( 26)

( 27)

( 28)

t 27)

( 27)

( 1)

0- BARKELEW ( 15) +- CHUI 1 17) X- OJOROJEVICH ( 18) H- LOOMIS ( 21) H- POPE ( 241 B- PORTER ( 25) •-ROSSINI I 27) D- STRflTY ( 29)

- STRRH (2N0I ( 29) D- ZIEGLER ( 27) O- ZIEGLER (2ND) I 27) A" ANCILLARY EQ. ( 1)

Figure A1. Saturated vapor preesure. (Statistical comparlaions begin on page 32.)

-30
0.06

0.00

LU -0.06

CC

D

CO 0.04

CO 0.00

LU

CC -0.04

OL

cc 0.05

o

Q- 0.00

<

>

-0.05

O

LU

0.09

h- 0.00

<

CC -0.09

Z)

h-

<

0.12

CO 0.00

200.00 - 210.00 K

Q-

^fln

i—i—i i i 10' 10

u 210.00 - 225.00 K

r4

n

-3

u

El

i i i i i i i i 10" 10

u 225.10 - 238.15 K

1

1—i—i—i

i i i 10" 1 10

u 238.77 - 246.81 K —i—i—i i i 1 1

1

1

1—i—i i i i 10' 1 10° 10'

247.82 - 253.03 K

o

<

>

LU

Q

-0.12

0.19

0.00

-0.19

0.22

0.00

-0.22

1 1 1 1—i

i i i 10° 10

1 253.15 - 263.28 K

an

o

«n 1 1—i—ir~r icr 10

1 263.38 - 273.15 K

0.22

0.00

-0.22

0.2

0.0

-0.2

0.17

0.00

-0.17

0.1

0.0

-0.1

0.13

0.00

-0.13

0.05

0.00

-0.05

275.00 - 280.00 K 9

1 1 1—i—i—i—

n

10° 10'

280.04 - 288.75 <

1

1 ® i

1—i—|—|—

r

10

J 10

1 290.00 - 298.15 K

1

1 1 1—i—i

rr 10

J 10

1 298.15 - 303.15 K

x

1

1 1—i—i—i—r~r 10

J 10

1 303.47 - 304.80 K

1

1 1—i—i—i—

n

- 10

u 10'

304.92 - 305.33 K

"1 11 1—I—TT

"1 1

I I I

10" 10'

PRESSURE (MPa)

10° 10'

PRESSURE (MPa)

O- 6ARKELEW ( 15) O- OOUSLIN I 19) X- niNIOVICH ( 22) <£- PAL ( 23)

ffi- POPE 1 24) El- PORTER I 25)

- STRflTY ( 29) A" ANCILLARY EO. ( t) O * 6ARKELEW ( 15) O- OOUSLIN ( 19) V - KAHRE ( 20) $- PAL ( 23) 2 - POPE ( 24)

gj - PORTER ( 25)

- STRATY ( 29) A- ANCILLARY EO. ( 1)

Figure A1. (continued)

31 -
Figure Al . Saturated vapor pressure.

The comparisons are based on the Maxwell construction using the full

SWEOS. Primary data for the SWEOS were obtained from the ancillary eq (1)

and are indicated in the plots. Primary data for eq (1) were obtained from

Douslin [19], Pal [23], Pope [24], Straty [29] and Ziegler [27]. Points

out of range were from Tickner [28]: 91.35 K, 10.1%; 94.45 K, 19.1%; 98.55

K, 21.9%; 101.85 K, 22.2%; 105.35 K, 21.3%; 110.55 K, 23.1%; 114.65 K,

20.1%.

Statistical comparisons between experimental saturated vapor pressures and

the ancillary eq (1) are given first; comparisons between the data and the

SWEOS are given next with the suffix "2" on each statistical category.

Data from Barkelew [15]

Number of Points: 20

AAD% = 0.292 BIAS% = -0.127

AAD2% = 0.300 BIAS2% = -0.111

Absolute Deviations:

AAD = 1.101 BIAS = -0.242

AAD2 = 1.289 BIAS2 = 0.099

RMS% = 0.717

RMS2% = 0.724

RMS = 2.578 kPa

RMS2 = 2.870 kPa

Data from Carruth [16]

Number of Points: 6 AAD% = 2.173 BIAS% = -0.351

AAD2% = 2.177 BIAS2% = -0.352

Absolute Deviations:

AAD = 0.009 BIAS = 0.004

AAD2 = 0.009 BIAS2 = 0.004

RMS%

RMS2%

= 2.512

= 2.512

RMS = RMS2 = 0.012 kPa

0.012 kPa

Data from Chui [17]

Number of Points: 2 AAD% =36.078 BIAS% =-36.078

AAD2% =36.080 BIAS2% =-36.080

Absolute Deviations:

AAD = 0.262 BIAS = -0.262

AAD2 = 0.262 BIAS2 -0.262

RMS% =35.936

RMS2% =35.932

RMS = 0.228 kPa

RMS2 = 0.227 kPa

Data from Djordjevich [18]

Number of Points : 6

AAD% = 1.384

AAD2% = 1.385

Absol

AAD =2.400

AAD2 = 2.481

Data from Douslin

Number of Points:

Weighted Data:

Number of Points:

BIAS% = -0.615

BIAS2% = -0.604

ute Deviations:

BIAS = 2.189

BIAS2 = 2.277

[19]

18

AAD% = 0.013

18

BIAS% = -0.007

AAD2% = 0.024 BIAS2% = 0.019

Absolute Deviations:

AAD = 0.369 BIAS = -0.279

AAD2 = 0.567 BIAS2 = 0.361

RMS% = 1.921

RMS2% = 1.920

RMS = 3.345 kPa

RMS2 = 3.484 kPa

RMS% = 0.016

RMS2% = 0.018

RMS = 0.464 kPa

RMS2 = 0.519 kPa

-32-
Data from Kahre [20]

Number of Points: 5 AAD% = 0.558 BIAS% = 0.456

AAD2% = 0.587 BIAS2% = 0.503

Absolute Deviations:

AAD =19.916 BIAS = 17.798

AAD2 =20.998 BIAS2 = 19.241

RMS% = 0.402

RMS2% = 0.397

RMS =15.129 kPa

RMS2 =15.103 kPa

Data from Loomis [21]

Number of Points: 34

AAD% = 0.450 BIAS% = -0.444

AAD2% = 0.449 BIAS2% = -0.444

Absolute Deviations:

AAD = 0.353 BIAS = -0.351

AAD2 = 0.350 BIAS2 = -0.349

RMS% = 0.140

RMS2% = 0.141

RMS = 0.182 kPa

RMS2 = 0.179 kPa

Data from Miniovich [22]

Number of Points: 11

AAD% = 0.028 BIAS% = -0.019

AAD2% = 0.034 BIAS2% = -0.028

Absolute Deviations:

AAD = 1.312 BIAS = -0.908

AAD2 = 1.621 BIAS2 = -1.316

RMS%

RMS2%

= 0.025

= 0.026

RMS = RMS2 = 1.198 kPa

1.213 kPa

Data from Pal [23]

Number of Points: 50

AAD% = 0.066 BIAS% = 0.001

AAD2% = 0.073 BIAS2% = 0.025

Absolute Deviations:

AAD = 1.863 BIAS = 0.837

AAD2 = 2.076 BIAS2 = 1.385

RMS% = 0.103

RMS2% = 0.103

RMS = 2.476 kPa

RMS2 = 2.449 kPa

Weighted Data:

Number of Points 47

AAD% 0.051 BIAS% = 0.013

AAD2% = 0.058 BIAS2% = 0.037

Absolute Deviations:

= 1.720 BIAS = 0.778 = 1.943 BIAS2 = 1.352

AAD

AAD2

RMS% = 0.060

RMS2% = 0.058

RMS = 2.201 kPa

RMS2 = 2.162 kPa

Data from Pope [24]

Number of Points: 11

AAD% 0.115 BIAS% = -0.007

AAD2% = 0.093 BIAS2% = 0.022

Absolute Deviations:

1.692 BIAS = -1.306

0.981 BIAS2 = -0.554

AAD

AAD2

RMS% = 0.191

RMS2% = 0.185

RMS = 1.663 kPa

RMS2 = 1.323 kPa

Weighted Data:

Number of Points: 9

AAD% = 0.049 BIAS% = -0.038

AAD2% = 0.024 BIAS2% = -0.007

Absolute Deviations:

AAD = 1.399 BIAS = -1.322

AAD2 = 0.569 BIAS2 = -0.450

RMS%

RMS2%

= 0.040

= 0.026

RMS = RMS2 = 1.170 kPa

0.544 kPa

-33
Data from Porter [25]

Number of Points: 20

AAD% = 0.211 BIAS% = -0.035 RMS% = 0.259

AAD2% = 0.198 BIAS2% = -0.007 RMS2% = 0.256

Absolute Deviations

AAD = 2.808 BIAS = -1.209 RMS =4.114 kPa

AAD2 = 2.482 BIAS2 = -0.659 RMS2 = 4.015 kPa

Data from Regnier [26]

Number of Points: 9

AAD% = 3.563 BIAS% = 0.337

AAD2% = 3.578 BIAS2% = 0.334

Absolute Deviations:

AAD = 0.014 BIAS = 0.014

AAD2 = 0.014 BIAS2 = 0.014

RMS% = 4.232

RMS2% = 4.247

RMS = 0.016 kPa

RMS2 = 0.016 kPa

Data from Rossini (via Ziegler [27])

Number of Points

AAD%

AAD2%

AAD

AAD2

22

0.147 BIAS% = -0.142

0.148 BIAS2% = -0.141

Absolute Deviations:

0.065 BIAS = -0.065

0.064 BIAS2 = -0.064

RMS%

RMS2%

= 0.067

= 0.071

RMS = RMS2 = 0.048 kPa

: 0.045 kPa

Data from Tickner [28]

Number of Points: 10

AAD% =17.099 BIAS% = 17.099 RMS% = 5.890

AAD2% =17.094 BIAS2% = 17.094 RMS2% = 5.868

Absolute Deviations:

AAD = 0.024 BIAS =0.024 RMS = 0.027 kPa

AAD2 = 0.024 BIAS2 = 0.024 RMS2 = 0.028 kPa

Data from Straty [29]

Number of Points: 44

AAD% = 0.043 BIAS% = 0.010

AAD2% = 0.055 BIAS2% = 0.031

Absolute Deviations:

AAD = 0.526 BIAS = 0.280

AAD2 = 0.830 BIAS2 = 0.707

RMS% = 0.056

RMS2% = 0.064

RMS = 0.791 kPa

RMS2 = 1.158 kPa

Weighted Data:

Number of Points 43

BIAS% = 0.016

AAD2% = 0.051 BIAS2% = 0.037

Absolute Deviations:

= 0.537 BIAS = 0.288

= 0.848 BIAS2 = 0.724

AAD% = 0.039

AAD

AAD2

RMS% = 0.044

RMS2% = 0.052

RMS = 0.799 kPa

RMS2 = 1.166 kPa

34
Data from Ziegler [27]

These data were adjusted by Goodwin [30]

Number of Points: 10

Weighted Data:

Number of Points: 10

AAD% = 0..028 BIAS% = -0.013 RMS% = 0.028

AAD2% = 0..033 BIAS2% = -0.016

Absolute Deviations:

RMS2% = 0.034

AAD = ,005 BIAS = -0.005 RMS = 0.006 kPa

AAD2 = .006 BIAS2 = -0.005 RMS2 = 0.006 kPa

Data from Ziegler (unadj ) [27]

Number of Points: 50

AAD% = 1.371 BIAS% = 1.361 RMS% = 0.889

AAD2% = 1.372 BIAS2% = 1.362 RMS2% = 0.891

Absolute Deviations:

AAD = 0.049 BIAS =0.038 RMS = 0.057 kPa

AAD2 = 0.048 BIAS2 = 0.038 RMS2 = 0.056 kPa

Data from ancillary equation [1]

Number of Points: 43

AAD2% = 0.020 BIAS2% = 0.015 RMS2% = 0.023

Absolute Deviations:

AAD2 = 0.321 BIAS2 = 0.321 RMS2 = 0.617 kPa

35
CO

z

LU

Q

Q

O

Q

LU

<

a:

<

CO

O

>

LU

Q

0.02

0.00

-0.02

0.07

0.00

-0.07

0.07

0.00

-0.07

0.07

0.00

-0.07

0.06

0.00

-0.06

0.1

0.0

-0.1

0.08

0.00

-0.08

91.00 - 101.00 K

D

-F 1 1 1- 1 1 1 1

21.25 21.50 21.75

102.58 - 108.15 K

m

_s_

-V-T0.07

0.00

-0.07

0.08

0.00

-0.08

156.00 - 163.15 K

ffl 55 JEL

V

-Q

—1 1 1

1

1 1 1

1

18.75 19 19.25

165.65 - 174.11 K

_a_

21 21.25

108 93 - 115.77 K TM 77 TM

18.50 18.75 19

176.00 - 186.00 K

C) •

E3 -&- -Bvj. io n nn — nffl S ffl ffl n u.uu

-0.13-—r—

r—

1

, rX-^-

20.75 21 116.00 - 123.15 K

m

^TT _&. B*

—i

1 1 1 1 1 1 1 1

20.25 20.50 20.75

125.00 - 132.77 K "

v * v

-I 1 1- -I 1 1 1- 20 20.25 20.50

133.16 - 143.15 K

„ »—Q- <&

-i—i—i—i- v

19.50 19.75 20 20.25

143.72 - 154.66 K

-B- V ^

-i 1 1 1-

0.09

0.00

0.09

0.09

0.00

-0.09

0.08

0.00

-0.08

0.02

0.00

-0.02

18 18.25 18.50

187.95 - 199.01 K

n n

x

l

, , ,

1

1 1 1 1 1

1 1 r^T- 17.25 17.50 17.75 18

200.00 - 212.62 K

-Q-2- -O- -Q.

;

1 1 1

1

1 1 1 1

1

1 1 1 r

- 16.75 17 17.25 17.50

214.94 - 225.70 K

ffl -Q-V- -B- — t->:

1 1

]

1 1 1 1 [

1 1 r~ 16 16.25 16.50 16.75

226.00 - 240.70 K

a a

19.25 19.50 19.75 15.25 16.25

DENSITY (mol/dm3

) DENSITY (mol/dm ) O- CHUI ( 17) V- HflYNES ( 32) X • KLOSEK ( 33) ^- tlC CLUNE ( 34)

ffi- ORRIT ( 35)

ffl- ORRIT (2ND) t 35) • - RODOSEVtCH ( 37) D- HNCILLFIR-f EQ. ( 1)

O- CHUI ( 17) X- GOODWIN I 30) V- HflYNES ( 32) ^- nc CLUNE ( 34) H- ORRIT ( 35)

ffl- ORRIT (2N0) 1 35) -ANCILLARY EO. ( 1)

Figure A2. Saturated liquid density. (Statistical comparisions begin on page 38.)

36
t

CO

z

LU

Q

Q

O

Q

LU

Z>

CO

o

>

LU

Q

0.43

0.00

-0.43

0.41

0.00

-0.41

0.44

0.00

-0.44

0.31

0.00

-0.31

0.37

0.00

-0.37

0.17

0.00

-0.17

0.35

0.00

-0.35

241.00 - 253.15 K

o

-X-9- -X- -X14.5 15.5

255.37 - 268.41 K

_&_*_ XV _X_ +

13.50

269.25 - 283.15 K

14.75

O

X X

+

18-

XV

i

1 1 1 1 tct 1 1 1 1 1 1 r 12.25 12.75 13.25 13.75

283.20 - 293.18 K

o

3«-

X

-r0.75

0.00

-0.75

1.43

0.00

-1.43

2.07

0.00

-2.07

2.47

0.00

-2.47

303.38 - 304.15 K

-Bca ®

q

8.50 8.75 9 9.25

304.30 - 304.84 K

H0 Bots

ffi 000

1 1 l—l 1

1 1

1 1

1 11 I I 8 8.25 8.50 8.75

304.87 - 305.10 K 0Q Q0 00 00

-l 1 r- -i 1 1 r- 7.75 8 8.25

305.12 - 305.26 K 00000

-±-

i 1 1 r- -i 1 1 1— 11.25

293.18

12.50 7.50 7.75

299.22 K

3 O

-i-

~5T DENSITY (mol/dm

3

) A- OOUSLIN ( 19) f- 00U5LIN (2ND

I

( 19) ©- MINIOVICH ( 22) gl- PflL ( 23) 0- PESTBK ( 36) 10.25

299.72 - 301.73 K

11.50

- SLIWINSKI (2ND) ( 38) ^

-Q-

-X- -B- 9.50 9.75 10

302.14 - 303.23 K

10.25

*

i—I—i—i—i—i—|—i

9.25 9.50 9.75

3' DENSITY (mol/dm3

) A- OOUSLIN f- OOUSLIN (2ND) X- GOODWIN O- GUGNONI V- HflYNES S- KflHRE ©- fllNlOVICH a- PAL 0- PESTHK O- SLIWINSKI

( 19)

I 19)

( 30)

t 31)

( 32)

I 20)

I 22)

( 23)

( 36)

( 38)

- SLIWINSKI (2ND) ( 38)

• TOriLINSON ( 39) X- ANCILLARY EO. t 1)

Figure A2. (continued)

-37
Figure A2 . Saturated liquid density.

The comparisons are based on the Maxwell construction using the full

SWEOS . Primary data for the SWEOS were obtained from the ancillary eq (2)

and are indicated in the plots. Primary data for eq (2) were obtained from

Douslin [19], Sliwinski [38], Chui [17], Rodosevich [37], Haynes [32],

McClune [34], and Orrit [35].

Statistical comparisons between experimental saturated liquid densities

and the ancillary eq (2) are given first; comparisons between the data and

the SWEOS are given next with the suffix "2" on each statistical category.

Data from Chui [17]

Number of Points: 3

Weighted Data:

Number of Points: 3

AAD% = 0.013 BIAS% = 0.013

AAD2% = 0.015 BIAS2% = 0.015

Absolute Deviations:

AAD = 0.00 BIAS = 0.00

AAD2 = 0.00 BIAS2 = 0.00

Data from Douslin [19]

Number of Points: 12

RMS% = 0.009

RMS2% = 0.003

RMS =

RMS2 =

-3

0.00 mol.dm

0.00 mol .dm"

AAD% = 0.201 BIAS% = -0.201 RMS% = 0,.114

AAD2% = 0.260 BIAS2% = -0.032 RMS2% = 0,.313

Absolute Deviations:

•3

•3 AAD = 0.02 BIAS = -0.02 RMS = 0,,02 mol-•dm

AAD2 = 0.03 BIAS2 = -0.01 RMS2 = 0,.03 mol-•dm

Weighted Data:

Number of Points: 3 AAD% = 0.039 BIAS% = -0.039 RMS% = 0,,007

AAD2% = 0.145 BIAS2% = 0.049 RMS2% = 0..178

Absolute Deviations: 3

3

AAD = 0.00 BIAS = 0.00 RMS = 0.,00 mol-dm

AAD2 = 0.01 BIAS2 = 0.00 RMS2 = 0,,02 mol«'dm

Data from Goodwin [30]

Number of Points: 12

AAD% = 0.183 BIAS% = -0.183

AAD2% = 0.175 BIAS2% = -0.175

Absolute Deviations:

AAD = 0.03 BIAS = -0.03

AAD2 = 0.03 BIAS2 = -0.03

Data from Gugnoni [31]

Number of Points: 4

AAD% = 0.596 BIAS% = -0.092

AAD2% = 0.621 BIAS2% = -0.022

Absolute Deviations:

AAD = 0.08 BIAS = -0.01

AAD2 = 0.09 BIAS2 = 0.00

RMS% = 0.084

RMS2% = 0.087

II

CM II

CO

CO

-3

0.01 mol • dm

0.01 mol* dm"

RMS% = 0.762

RMS2% = 0.745

RMS = RMS2 =

-3

0.11 mol* dm „ 0.10 mol.dm"

-38
Data from Haynes [32]

Weighted Data:

Number of Points: 22

AAD% = 0.028 BIAS% = -0.023

AAD2% = 0.034 BIAS2% = -0.014

Absolute Deviations:

AAD = 0.01 BIAS = 0.00

AAD2 = 0.01 BIAS2 = 0.00

RMS% = 0.028

RMS2% = 0.041

RMS = 0.01 mol-dm

RMS2 = 0.01 mol-dm

-3

-3

Data from Kahre [20]

Number of Points: 5 AAD% = 0.224 BIAS% = -0.224

AAD2% = 0.210 BIAS2% = -0.181

Absolute Deviations:

AAD = 0.02 BIAS = -0.02

AAD2 = 0.02 BIAS2 = -0.02

RMS% = 0.165

RMS2% = 0.270

RMS = 0.02 mol-dm

RMS2 = 0.03 mol-dm

-3

-3

Data from Klosek [33]

Number of Points: 8 AAD% = 0.084 BIAS% = 0.055

AAD2% = 0.087 BIAS2% = 0.053

Absolute Deviations:

AAD = 0.02 BIAS = 0.01

AAD2 = 0.02 BIAS2 = 0.01

RMS% = 0.084

RMS2% = 0.090

RMS = 0.02 mol-dm

RMS2 = 0.02 mol-dm

Data from McClune [34]

Number of Points: 17

Weighted Data:

umber of Points: 17

AAD% = 0.020 BIAS% = -0.007 RMS% = 023

AAD2% = 0.017 BIAS2% = -0.006

Absolute Deviations:

RMS2% = 018

AAD = 0.00 BIAS = 0.00 RMS = 00 mol-dm

AAD2 = 0.00 BIAS2 = 0.00 RMS2 = 00 mol-dm

Data from Miniovich [22]

Number of Points: 5 AAD% = 0.426 BIAS% = -0.426

AAD2% = 0.234 BIAS2% = 0.018

Absolute Deviations:

AAD = 0.03 BIAS = -0.03

AAD2 = 0.02 BIAS2 = 0.00

RMS% = 0.343

RMS2% = 0.274

RMS = 0.03 mol-dm

RMS2 = 0.02 mol-dm

-3

-3

39
Data from Orrit [35]

Number of Points : 46

AAD% = 0.052 BIAS% = 0.048

AAD2% = 0.057 BIAS2% = 0.052

Absolute Deviations:

AAD = 0.01 BIAS = 0.01

AAD2 = 0.01 BIAS2 = 0.01

RMS% = .031

RMS2% = .032

RMS = .01 mol'dm

RMS2 = .01 mol'dm

-3

Weighted Data:

Number of Points

:

13

AAD% 0.051 BIAS% = 0.035

AAD2% = 0.056 BIAS2% = 0.038

Absolute Deviations:

0.01 BIAS = 0.01

0.01 BIAS2 = 0.01

AAD

AAD2 =

RMS% = 0.044

RMS2% = 0.047

RMS = 0.01 mol'dm

RMS2 = 0.01 mol'dm

-3

Data from Pal [23]

Number of Points : 11

AAD% = 0.376 BIAS% = -0.376

AAD2% = 0.353 BIAS2% = -0.332

Absolute Deviations:

AAD = 0.05 BIAS = -0.05

AAD2 = 0.05 BIAS2 = -0.05

RMS% = .121

RMS2% = .166

RMS = .02 mol'dm

RMS2 = .02 mol'dm

-3

-3

Data from Pestak [36]

Number of Points: 39

AAD% = 0.598 BIAS% = 0.598

AAD2% = 1.033 BIAS2% = 1.008

Absolute Deviations:

AAD = 0.05 BIAS = 0.05

AAD2 = 0.08 BIAS2 = 0.08

RMS% = .461

RMS2% = ,827

RMS = .03 mol'dm

RMS2 = .06 mol'dm

-3

Data from Rodosevich [37]

Number of Points : 4

Weighted Data:

Number of Points: 4

AAD% = 0.030 BIAS% = 0.030

AAD2% = 0.030 BIAS2% = 0.030

Absolute Deviations

:

AAD = 0.01 BIAS = 0.01

AAD2 = 0.01 BIAS2 = 0.01

RMS% = ,008

RMS2% = 0,.014

RMS = 0..00 mol'dm

RMS2 = 0,.00 mol'dm

Data fr

Number

AAD%

AAD2%

AAD

AAD2 Weighte

Number

AAD%

AAD2%

AAD

AAD2

om Sliwinski [38]

of Points: 11 = 0.043 BIAS% = 0.019

= 0.217 BIAS2% = 0.179

Absolute Deviations:

= 0.00

= 0.02

d Data:

of Points

= 0.024

= 0.111

BIAS

BIAS2

0.00

0.02

4

BIAS% = 0.011

BIAS2% = 0.071

Absolute Deviations:

0.00 BIAS = 0.00

0.01 BIAS2 = 0.01

RMS% = RMS2% -

RMS =

RMS2 =

0.051

0.263

0.00 mol'dm

0.02 mol'dm

RMS% = 0.026

RMS2% = 0.090

RMS

RMS 2

-3

-3

0.00 mol'dm

0.01 mol'dm

-3

-3

40-
Data from Tomlinson [39]

Number of Points: 7 AAD% = 0.220 BIAS% = -0.220

AAD2% = 0.251 BIAS2% = -0.230

Absolute Deviations

:

AAD = 0.02 BIAS = -0.02

AAD2 = 0.03 BIAS2 = -0.02

RMS% = 0.107

RMS2% = 0.221

RMS = 0.01 mol»dm

RMS2 = 0.02 mol«dm

-3

-3

Data from ancillary equation [1]

Number of Points: 43

AAD2% = 0.030 BIAS2% = 0.017

Absolute Deviations:

AAD2 = 0.004 BIAS2 = 0.002

RMS2% = 0.052

RMS2 = 0.006 mol-dm

-3

41-
0.08

0.00

-0.08

>-

hco 0.26

z 0.00

LUQ -0.26

cc

O 0.24

DL

<

0.00

> -0.24

Q

LU 0.21

h-

< 0.00

CC

Z> -0.21

h-

< 0.63

CO

0.00 ^^^~ -0.63

Z

o 0.29

h-

< 0.00

> -0.29

LU

Q 0.39

0.00

90.35 - 121.00 K

x © -ffi is -1—i i 1 1 1 ii| i i i 1 1 1 ii| 1 i i i m i 10* 10

6 10* 10

126.00 - 160.00 K

-© ©

—i— a±v i

i i imi| 1

i

i rr mv i—i

i i m i 10" 4 10

3 10"

2 10

161.00 - 191.00 K

-1

-©- ffi Hg

H©

1»

l l l l I i n 10* 10

196.00 - 226.18 K

© ©

i i i i i i i r 10

1 10

230.00 - 248.65 K

fe

"ii i i 10' 10°

250.00 - 266.00 K

1 1—I I I I W| 1—i

I I I II l| 10

1 10° 10

1 268.73 - 283.20 K

0.39 i r ~i i i i r

0.53

0.00

-0.53

0.55

0.00

-0.56

0.93

0.00

-0.93

1.24

0.00

-1.24

1.61

0.00

-1.61

2.35

0.00

-2.35

2.21

0.00

-2.21

283.58 - 298.17 K

©

a2

10°

I i i i

1(

298.73 - 302.15 K

r**-i—i—i i i 10" 10

302.16 - 303.84 K

-o1

1 1—"«i—I—I—

r

10° 10

303.94 - 304.66 K

<*>

1 1 1 T*n—i

rr

10" 10

1 304.71 - 305.04 K

o

1 1 1 r^i—i i i 10" 10

1 305.05 - 305.25 K

4-

1 1 1

Till

10

u 10'

305.26 - 305.33 K

o

&-

i

1 r i—i—TT

10 1Q

DENSITY (mol/drri )

10" 10

DENSITY (mol/dm ) O- DOUSLIN ( 19) + - GOODWIN ( 30) X- GOODWIN (2N0) ( 30) H- PORTER ( 40) X" SLIWINSKI ( 38)

ffi- ANCILLARY ED. ( 1)

O-00U5LIN 1 19) A- DOUSLIN (2N0) ( 19) O- niNIOVICH ( 22) V- PESTAK ( 36) H- PORTER I 40) X" SLIWINSKI I 36) ^- SLIWINSKI (2N0) ( 38)

ffi- ANCILLARY EO. (I)

Figure A3. Saturated vapor density. (Statistical comparisions begin on page 43.)

42
Figure A3. Saturated vapor density.

The comparisons are based on the Maxwell construction using the full

SWEOS . Primary data for the SWEOS were obtained from the ancillary eq (3)

and are indicated in the plots. Primary data for eq (3) were obtained from

Goodwin [30], Douslin [19], and Sliwinski [38].

Statistical comparisons between experimental saturated vapor densities

and the ancillary eq (3) are given first; comparisons between the data and

the SWEOS are given next with the suffix "2" on each statistical category.

Data from Douslin [19]

Number of Points: 12

AAD% 0.146 BIAS% = 0.010

AAD2% = 0.296 BIAS2% = -0.207

Absolute Deviations

:

= 0.006 BIAS = 0.002

= 0.013 BIAS2 = -0.012

AAD

AAD2

RMS% = 0.188

RMS2% = 0.291

RMS = 0.008 mol'dm"

RMS2 = 0.014 mol'dm'

Weighted Data:

Number of Points: 7 AAD% = 0.084 BIAS% = 0.055

AAD2% = 0.223 BIAS2% = -0.071

Absolute Deviations:

AAD = 0.003 BIAS = 0.003

AAD2 = 0.008 BIAS2 = -0.006

RMS% = 0.106

RMS2% = 0.289

RMS = 0.005 mol'dm'

RMS2 = 0.013 mol'dm'

Data from Goodwin [30]

Number of Points: 20

AAD% = 0.050 BIAS% = -0.015

AAD2% = 0.124 BIAS2% = -0.016

Absolute Deviations:

AAD = 0.000 BIAS = 0.000

AAD2 = 0.000 BIAS2 = 0.000

RMS% = 0.074

RMS2% = 0.151

RMS 0.001 mol«dm

-3

RMS2 = 0.001 mol-dm

Weighted Data:

Number of Points: 18

AAD% = 0.047 BIAS% = -0.008

AAD2% = 0.131 BIAS2% = -0.011

Absolute Deviations:

AAD = 0.000 BIAS = 0.000

AAD2 = 0.000 BIAS2 = 0.000

RMS% = 0.074

RMS2% = 0.158

RMS 0.001 mol'dm

RMS2 = 0.001 mol'dm

Data from Miniovich [22]

Number of Points : 6

AAD% = 2.115 BIAS% = 2.115

AAD2% = 1.071 BIAS2% = 1.071

Absolute Deviations

:

AAD = 0.121 BIAS = 0.121

AAD2 = 0.061 BIAS2 = 0.061

RMS% = 1.138

RMS2% = 0.653

RMS = 0.079 mol'dm

RMS2 = 0.044 mol'dm

-3

-3

43-
Data from Pestak [36]

Number of Points: 39

AAD% = 0.437 BIAS% = -0.433

AAD2% = 1.162 BIAS2% = -1.162

Absolute Deviations:

AAD = 0.024 BIAS = -0.024

AAD2 = 0.064 BIAS2 = -0.064

RMS% = 0.391

RMS2% = 0.591

RMS = 0.024 mol»dm"

RMS2 = 0.038 mol«dm'

Data from Porter [40]

Number of Points: 14

AAD% = 0.598 BIAS% = -0.427

AAD2% = 0.560 BIAS2% = -0.314

Absolute Deviations:

AAD = 0.005 BIAS = -0.001

AAD2 = 0.005 BIAS2 = 0.000

RMS% = 0.606

RMS2% = 0.642

RMS 0.007 mol»dm

-3

RMS2 = 0.008 mol«dm

Data from Sliwinski [38]

Number of Points: 11

AAD% = 0.295 BIAS% = 0.276

AAD2% = 0.210 BIAS2% = -0.018

Absolute Deviations:

AAD = 0.015 BIAS = 0.014

AAD2 = 0.008 BIAS2 = -0.002

RMS% = 0.333

RMS2% = 0.238

RMS 0.019 mol-dm

RMS2 = 0.010 mol»dm

-3

-3

Weighted Data:

Number of Points: 7 AAD% = 0.109 BIAS% = 0.080

AAD2% = 0.155 BIAS2% = -0.029

Absolute Deviations

AAD = 0.004 BIAS = 0.004

AAD2 = 0.006 BIAS2 = -0.002

RMS% = 0.122

RMS2% = 0.180

RMS = 0.005 mol'dm"

RMS2 = 0.007 mol»dm"

Data from ancillary equation [1]

Number of Points: 43

AAD2% = 0.120 BIAS2% = 0.001

Absolute Deviations:

AAD2 = 0.001 BIAS2 = 0.000

RMS2% = 0.137

RMS2 = 0.002 mol'dm

44
>-

Q-O

<r

\-

z 0.02

LU 0.00

CO

<

-0.02

o

_J 0.02

< 0.00

LU

Q -0.02

50.00 - 200.00 K

s :

t t r i I i

1 1 r I1 1 r t 50 100 150 200

273.15 - 400.00 K +

== 0.03

1—? 1 1 T-1 1 1 1

1 J

I I I I 1 T 270 296 322 348 374 400

400.00 - 700.00 K

O

I-

<

>LLI Q

0.00^-

-0.03

+

u

i

1 1

1 1

1 1 r 400 475 550 625 700

TEMPERATURE (K)

O - chro ( in

A- CHflO (2N0) ( 11) + - PflfllOIMUKKRLfl ( 41) X- TRC ( 42)

Figure A4A. Ideal gas entropy. (Statistical comparisions begin on page 46.)

-45
Figure A4A. Ideal gas entropy.

The comparisons are based on entropies calculated from eq (5) at

0.101 325 MPa (1 atm) . The point from Chao [11] at 298.15 K was used as a primary datum for the ideal gas correlation to fix an integration constant

Statistical comparisons between tabulated ideal gas entropies and the ideal

gas correlation of eq (5) are given.

Data from Chao [11]

Number of Points: 11

AAD% = 0.009 BIAS% = -0.004 RMS% = 0.009

Absolute Deviations: 1

, AAD = 0.019 BIAS = -0.009 RMS = 0.019 J»mol" »K~

Data from Pamidimukkala [41]

Number of Points : 8

AAD% = 0.020 BIAS% = 0.011 RMS% = 0.025

Absolute Deviations: .. 1 AAD = 0.046 BIAS = 0.024 RMS = 0.052 J«mol -K

Data from TRC [42]

Number of Points: 11

AAD% = 0.009 BIAS% = -0.004 RMS% = 0.010

Absolute Deviations: .. .. AAD = 0.020 BIAS = -0.010 RMS = 0.019 J-mol -K

46-
(J

CO

<

CD

<LLJ Q

1.07

0.00

-1.07

1.23

0.00

-1.23

0.91

0.00

-0.91

0.87

50.00 - 133.15 K

n

1

' i x *xx -r*—

50 80

144.26

110

200.00 K

140

x x

1—'—'

x \ —i 1

1

1 r 140 155 170 185 200

200.00 - 273.15 K

V"

^-^ x xx X i x

200 220 240 260

273.16 - 299.82 K

280

O.OO^r

-0.87

+

>: x X0.4

273 282 291 300

300.00 - 333.15 K x~x <

>

LU

Q

O.OJs

-0.4

¥

-yr -*

-i 1 r "i 1-

1.41 0.00

-1.41

1.05

300 317 334

344.26 - 399.82 K + +

x x X

-i—i—|—i—i—|

340 355 370

X

1—'—

r

x

0.11

0.00

-0.11

600.00 - 700.00 K

J)

0.00^

-1.05

X

385 400

400.00 - 500.00 K

x T

-i>

i—i—i—i—

|—i—i—i—i—|—i—i—r—i—I—i—i—i

400 425 450 475 500

TEMPERATURE (K)

O - CHflO ( 11) A- PArilDIMLIKKALA ( 411 f- BIER ( 43) X- RJRTAOO ( 44) O- TRC ( 42)

1—i—i—l—

|—i—l—i—i—|—l—r—I—l—

|—l—i—l—

r

600 625 650 875 700

TEMPERATURE (K)

O- CHflO (11)

A- PflniDlnUKKRLFI I 41) O - TRC ( 42

)

Figure A4B. Ideal gas iaobarlc heat capacity. (Statistical comparislons begin on page 48.)

47
Figure A4B. Ideal gas isobaric heat capacity.

The comparisons are based on isobaric heat capacities calculated from

eq (5) . Primary data for the ideal gas correlation were obtained from Chao

[11].

Statistical comparisons between tabulated ideal gas isobaric heat

capacities and the ideal gas correlation of eq (5) are given.

Data from Chao [11]

Number of Points: 11

Weighted Data:

Number of Points: 11

AAD% = 0.060 BIAS% = -0.024 RMS% = 0.080

Absolute Deviations: - - AAD = 0.026 BIAS = -0.009 RMS = 0.031 J-mol" »K~

Data from Pamidimukkala [41]

Number of Points: 8

AAD% = 0.111 BIAS% = -0.017 RMS% = 0.140

Absolute Deviations: 1 1 AAD = 0.066 BIAS = 0.011 RMS = 0.076 J.mol" »K~

Data from Bier [43]

Number of Points : 9 AAD% = 0.681 BIAS% = 0.680 RMS% = 0.486

Absolute Deviations

1 1 AAD = 0.431 BIAS = 0.430 RMS = 0.317 J«mol" «K~

Data from Furtado [44]

Number of Points: 37

AAD% = 0.666 BIAS% = -0.490 RMS% = 0.503

Absolute Deviations:

AAD = 0.327 BIAS = -0.221 RMS = 0.269 J«mol -K

Data from TRC [42]

Number of Points: 11

AAD% = 0.060 BIAS% = -0.025 RMS% = 0.080

Absolute Deviations

.. .. AAD = 0.027 BIAS = -0.010 RMS = 0.031 J.mol -K

48-
>

CL

_J

<

z

LU

CO

<

o

-J

<

LUQ

O

>

LUQ

0.3

0.0

-0.3

0.04

0.00

0.04

0.02

0.00

-0.02

50.00 - 200.00 K

& * K

2£ +

1 1 1—i

1 r—

Ik

-

1

1 1

]

1 1 1 1 50 100 150 200

273.15 - 400.00 K

*

-&-

-i—i—i—i—r—r- 270 296 322 348 374 400

400.00 - 700.00 K

A

+ 400 475 550 625 700

TEMPERATURE (K)

O - CHRO (11)

A- CHFIO (2ND) (11) + - PflMIDlMUKKFILfl ( 41) X- TRC ( 12)

Figure A4C. Ideal gas enthalpy. (Statistical comparlsions begin on page 50.)

49 -
Figure A4C . Ideal gas enthalpy.

The comparisons are based on enthalpies calculated from eq (5). The

point from Chao [11] at 298.15 K was used as a primary datum for the ideal

gas correlation to fix an integration constant.

Statistical comparisons between tabulated ideal gas enthalpies and the

ideal gas correlation of eq (5) are given.

Data from Chao [11]

Number of Points: 11

AAD% = 0.037 BIAS% = -0.006 RMS% = 0.063

Absolute Deviations: 1 AAD = 1.999 BIAS = -0.238 RMS = 2.284 J»mol"

Data from Pamidimukkala [41]

Number of Points: 8

AAD% = 0.139 BIAS% = -0.128 RMS% = 0.124

Absolute Deviations: 1 AAD =16.528 BIAS =-11.933 RMS =16.929 J«mol

Data from TRC [42]

Number of Points: 11

AAD% = 0.039 BIAS% = 0.001 RMS% = 0.061

Absolute Deviations: .. AAD = 3.683 BIAS =2.162 RMS = 6.607 J-mol"

50-
8.11

0.00

-8.11

hz

LU 7.6

CJ 0.0

UL

LL -7.6

LU

O 7.21 _l 0.00

< -7.21 cc

> 5.83

Q 0.00 Z

o

-5.83

o

LU 5.3

CO

<

>LL! Q

-769.00 - -446.00 dmVmol

-©- -ffl. G -¥fc1.03

183.24 - -156.10 dmVmol

1 11 1

1

1 r-H-T 150 165 180 195 210

-443.00 --370.00 dmVmol

o.oo-^—a

-1.03

o

ii.

-it^-i—i—I—i—i—i—i

n* i ' ! ~~r^

0.72

0.00

-0.72

i

1 1 1 1 1 1 1

1 1 r~ 300 306 312 318 324

-154.00 - -113.60 dmVmol

v -A200 205 210 215 220

-370.00 --325.00 dmVmol

325 374

-111.90 --96.00 dmVmol

a

-i—i—| *r i—rn—pT—i—i—i—i M. i

2.02^-

63A Ck

t—i—i—i—

|—i—

209 214 219 224 229 234

-316.00 --282.00 dmVmol

^L

* + ±_ -r-K 230 235 240 245 250

-280.00 --243.00 dmVmol

_, 0.0

-5.3

2 6.06

a

J£_ + + 240 245 250 255 260

-240.00 - -219.38 dmVmol

0.00^*

-5.06^

0.28

0.00

-0.28

>

i

' ' '

i

' '

i ' ' ' i

' ' - 270 272 274 276 278 280

-214.00 --185.60 dmVmol

0.00

-2.02

0.99

0.00

-0.99

0.38

0.00

-0.38

1.48

0.00

-1.48

373 382 391 400

-90.40 - -72.40 dmVmol

o

,$, *

410 423 436 449

-71.70 - -52.40 dmVmol

JZL o

SL

440 465 470 485 500

-52.00 --19.60 dmVmol

o o

4-

o

—I—I—

I—I—I—I—I—1-1—I—I—I—l—l—I—I—I

500 526 552 578 804 630

TEMPERATURE (K)

280 298.25

TEMPERATURE (K)

O- OOUSLIN A - DYMOND O - GUNN V - HfiMRNN ^- MANSOORIAN

ffi- MC GLfiSHHN 2- MICHELS

ffl- POPE

62- STREIN

( 19)

( 45)

( 46)

( 50)

( 54)

1 55)

( 56)

( 24)

( 57) O- OOUSLIN A- 0W0N0 + - EUCKEN X - EUCKEN O- GUNN EI- HOOVER

X-- LAMBERT ©- MC GLflSHflN S- rtlCHELS

ffl- POPE 63- 5TREIN

( 19)

( 45)

( 46)

( 47)

( 48)

( 52)

( 53)

( 55)

( 56)

( 24)

( 57)

Figure A5. Second viriel coefficient. (Statistical comparlsions begin on page 52.)

51 -
Figure A5 . Second virial coefficient.

The comparisons are based on the SWEOS , using expression from table 7.

Primary data for the SWEOS were from Douslin [19] , Mansoorian [54] , Michels

[56] , and Pope [24]

.

Statistical comparisons between tabulated second virial coefficients and

values calculated from the SWEOS are given.

Data from Douslin [19]

Number of Points: 16

Weighted Data:

Number of Points: 16

AAD% - 0.22 BIAS% = -0.04

Absolute Deviations

:

AAD - 0.13 BIAS = 0.04

RMS% = 0.33

RMS = 0.16 cm

3 .mol

Data from Dymond [45]

Number of Points: 15

AAD% = 1.20 BIAS% = 1.10 RMS%

Absolute Deviations:

AAD - 3.27 BIAS = -3.22 RMS

1.17

3 -1

4.27 cm »mol

Data from Eucken [46]

Number of Points: 15

AAD% = 5.75 BIAS% = -5.75 RMS%

Absolute Deviations:

AAD = 21.78 BIAS = 21.78 RMS

= 1.58

= 10.23 cm

3

«mol"

1

Data from Eucken via Tester [47]

Number of Points: 9

AAD% = 4.80 BIAS% = -4.80

Absolute Deviations

:

AAD = 16.54 BIAS = 16.54

RMS% = 1.82

RMS

3 -1 = 9.37 cm •mol

Data from Gunn [48] reported by Huff [49]

Number of Points: 8

AAD% = 1.58 BIAS% = -1.15

Absolute Deviations:

AAD = 1.22 BIAS = 0.75

RMS% = 2.06

RMS

3 -1 = 1.26 cm «mol

Data from Hamann [50]

Number of Points: 7 AAD% = 1.04 BIAS% = 0.56 RMS%

Absolute Deviations

AAD = 1.18 BIAS = -0.83 RMS

= 1.24

= 1.76 cm »mol

Data from Hoover [52]

Number of Points: 3

AAD% = 3.98 BIAS% = 3.71 RMS%

Absolute Deviations:

AAD = 12.35 BIAS = -11.74 RMS

2.99

3 -1

9.67 cm »mol

52
Data from Lambert [53]; reported by Tester [47]

Number of Points: 11

AAD% = 5.70 BIAS% = -5.70

Absolute Deviations:

AAD = 18.10 BIAS = 18.10

RMS% = 1.38

RMS = 8.87 cm

3

»mol"

Data from Mansoorian [54]

Number of Points: 7 Weighted Data:

Number of Points: 7 AAD% - 1.18 BIAS% = -0.41

Absolute Deviations:

AAD - 1.07 BIAS = 0.16

RMS% = 1.35

RMS = 1.28 cm

3

.mol

Data from McGlashan [55]; reported by Goodwin [30]

Number of Points : 16

AAD% = 1.22 BIAS% = -0.02

Absolute Deviations:

RMS% = 1.93

AAD = 6.57 BIAS 2.42

3 -1

RMS = 13.38 cm «mol

Data from Michels [56]

Number of Points: 7 Weighted Data:

Number of Points: 7 AAD% = 0.13 BIAS% 0.06 RMS% = 0.19

Absolute Deviations

AAD = 0.22 BIAS 0.15

3 -1

RMS = 0.38 cm -mol

Data from Pope [24]

Number of Points: 5 Weighted Data:

Number of Points: 5 AAD% = 1.86 BIAS% = Absolute Deviations:

AAD = 5.60 BIAS = -5.60

1.86 RMS% = 1.18

3 -1

RMS = 4.65 cm •mol

Data from Strein [57]

Number of Points: 11

AAD% = 0.93 BIAS% = 0.46

Absolute Deviations:

AAD = 1.01 BIAS = -0.71

RMS% = 1.07

3 -1

RMS = 1.05 cm 'mol

-53
9.44

0.00

-9.44

8.26

0.00

-8.26

92.14 - 108.00 K

a <b ^ $

o

n

o

i i |i r r r i i | r i » r t i j t- 14 28 42 56 70

108.00 - 122.00 K

-e -zr <h o o

LU

cc 4.92

Z>

CO 0.00

CO -4.92

LU

DC

Q. 4.08

z 0.00

"Z_ -4.08

I I I

| P I I I I I [ I I 1 I I I | ! I 1 I I !

| 14 28 42 56 70

122.00 - 138.00 K

<5 -o-e- o o

-%

' I

I I

|

I I , I , 1 |

, I , I I I | . I ! ! I 14 28 42 56 70

138.00 - 160.36 K

*—^~^£ O- "^

xxy^OBDC^KJ©

o

<

>

LU

a

9.26

0.00

-9.26

i i i i r i

j

i i i i i t

| r n t i t

j

t tt1 rrrrrrrn 14 28 42 56 70

160.39 - 176.28 K

ftfeq^o o *

1 I I I

i

I I I I I I

J

I I I t I r [ I T T rTTT 1 I I I I 14 28 42 56 70

176.72 189.33 K

5.35 i (g>—g—ffl——

0.00

-5.35

1.5

0.0

-1.5

^*- 1—I—'—I—'—'—1—'

r 15 30 45 60

189.75 - 201.83 K

fo^°o &

o o c^c#> V

10

~~

I—'

r 25 40 55

PRESSURE (MPa)

70

O- GOLOVSKIY ( 60) 2- PAL ( 23)

ffl- PAL (2ND! t 23) O- STRflTY ( 29) D- STRATY I2N0) (29)

2.28

0.00

-2.28

0.65

0.00

-0.65

2.21

0.00

-2.21

5.29

0.00

-5.29

0.69

201.95 - 213.51 K

-e- a

gD(yoi6 =a —o O

' o

1 I T I I F TT T I I 1 I I I I I >

J

I I T ( I 1 J

I 1 I T T'T 14 28 42 56 70

215.25 - 224.00 K

o u oh

°cnqpo 3

-©V 10 25

1

1—^T 1

1 r- 40 55 70

224.83 - 235.94 K

-*> e o

o

o<§gb g s°

o ®

T T T 1 T I [' r I' H'TT T T 1 I 1 1 I

1 T r T T T T T J

T T TT 14 28 42 56 70

236.00 - 243.15 K

-Ofo B

^r

15 30 45 60

243.15 - 252.00 K

-e o.oo m-

-0.69

ODqo%

o

c

15 —|

1 1

1

1 r- 30 45 60

1.37

252.00 - 260.00 K

0.00-K

-1.37

°^6>o

oc

4.79

TT I T I I I I I I I l r I 1 I I I' -

]

1 T 7 r f I I | 1 I > I 14 28 42 56 70

260.00 - 267.05 K

0.00-p

-4.79

db g

i i i i I i i i i i i

| r i i i i r -

j rTTT 1 1 i

[

i I t i 14 28 42 56 70

PRESSURE (MPa)

X" OOUSLIN (2ND) ( 19) O- GOLOVSKIY ( 60) El- LAW ( 62) 2- PAL ( 23) EH- PAL (2ND) I 23) O - STRAIT ( 29

)

- STRATY (2ND) (29)

- WALLACE ( 65)

Figure A6A. PVT data- -pressure deviations. (Statistical comparlaions begin on page 58.)

54 -
LU

cc

Z)

CO

CO

LU

CC

a.

O

<

>

LU

Q

5.53

0.00

-5.53

0.19

267.24 - 273.15 K

©€Q4 Xx

15 30 45 60

273.15 - 277.61 K

o.oo-lll

-0.19

o

-a

2.24

0.00

-2.24

1 1 1 r- 9

277.92

m

—

i—:—i—|—i—r- 18 27 36

283.15 K

LULL) 3

IT

Tirjii'rTrr|rTrFTi|iiiiii|TrtT

14 28 42 56 70

283.15 - 288.87 K

0.76 i Wq

0.00

-0.76

1.78

0.00

-1.78

0.27

0.00

-0.27

1.83

A

T"T T I I I I I I rTTTT II m I ] I I I I 1 1

I rTTTTT" 14 28 42 56 70

290.02 - 295.93 K

rTTTTTTTTTTTTTTTTTTTTTTTI 14 28 42 56 70

296.00 - 298.15 K

<P,

-e- -q o

Q -O- )o o

o

iQ i i i

|

i i i i i i

|

i 15 22

o.oo -g

-1.83

29

298.15 - 299.82 K

36

l ff«f'*

1*'"

"X

-i—i—i—|—i—i—i—

14

1

I '

' 28 42

PRESSURE (MPa)

O-BEATTIE ( 58) + - 00USL1N t 19) X- 00USL1N (2ND) ( 19) O- GOLOVSKIY ( 60) V- KHAZAN0VA (61)

H- LAW ( 62) X-fllCHELS ( 56) 2- PAL ( 23) a- PAL I2N0) ( 23) O- 57RATY ( 29) D-S7RATY (2ND) (29)

• TOMLINSON ( 39)

- WALLACE ( 65)

0.58

0.00

-0.58

0.07

0.00

-0.07

0.16

0.00

-0.16

0.06

0.00

-0.06

0.01

0.00

-0.01

0.02

0.00

-0.02

0.03

0.00

-0.03

299.85 - 302.59 K

oo

o o Q® o

1 3- o o

o^ o

2 13 24 35

302.59 - 303.53 K

+ T =F

4- +

T©"

1.5 2.5 3.5 4.5 5.5 6.5

303.56 - 304.34 K

o

Jo

o

o

-Q- jD. 3 34

304.43 - 305.15 K

4.50 4.75

305.23 - 305.37 K

X»< X

1 1 1 1 4.75 5

305.37 - 305.38 K x

-*- XX

X X

i i

1

1

1 i r 2 3 4 5

305.39 - 305.93 K

3K6

4.75

PRESSURE (MPa)

+

X-V00U5LIN

DOUSLIN (2ND) KHAZANOVA

LAW

rtlNIOVICH PAL (2ND) PARRISH

SENGERS STRATY

STRATY (2ND) TOriLINSON

I 19)

I 19)

( 61)

( 62)

( 22)

( 23)

( 63)

( 54)

( 29)

( 29)

( 39)

Figure A8A. (continued)

55
LU

cc

Z>

CO

CO

LU

CC

a.

O

>LLI Q

0.12

0.00

-0.12

0.58

305.96 - 306.58 K

ffl # •

4 5.25

306.62 - 308.23 K

-0.58

0-00-^-#%

V Oq o

o °

-©-

1—'—I

r~ 9 18 27

308.25 - 310.93 K

ffl36

"i 1 1

1

1 1 1

1

1 1 1 1 1 1 r- 3 14 25 36 47

310.93 - 310.95 K

0.73

0.00

-0.73

0.76

0.00

-0.76

1.11 0.00

-1.11

14 28 42 56

311.09 - 312.63 K

70

o o o °° o~^—

c

17 312.65 - 316.48 K34

-M

3

**.

*^o o oo o

2 3

316.48 - 320.00 K

OO0 <&° °

-B-r- i 16 30 44

PRESSURE (MPa)

A- BESSERER V" KHAZANOVA

EI- LAW ©- MIM0V1CH S- PAL

ffl- PAL (2N0) gl- PARRISH Q- REAMER • • SENGERS O- STRATT

( S9)

( 61)

( 62)

( 22)

( 23)

( 23)

( 63)

( 51)

( 64)

( 29) D- STRATT (2ND) (29)

- TOMUNSON ( 39)

0.19

0.00

-0.19

0.09

0.00

0.09

0.67

0.00

-0.67

0.87

0.00

-0.87

0.32

0.00

-0.32

0.09

0.00

-0.09

0.54

0.00

-0.54

320.13 - 323.15 K

O OQCJ

/vT^Cr^

1 13.25

323.15 - 324.79 K

3- + 4- —arr ++-H+H

+

V

2 4 6 8

324.82 - 343.09 K —ffl S

33

343.35 - 344.48 K

^

fftAgA a ^

°Qnfc Q n

ej 0.50 13.75

344.48 - 348.15 K ° o.o0 °oW

WX-tfW&H&t * * » $ A

-i 1 1 1

1

1 1 1 1

1

1 1 1 r- 1.25 4.50 7.75 11 348.15 - 350.00 K

[] =F

1

+ %

E

7 14

350.00

21 28

373.15 K

35

o Oo°°ooooo

M 1 h + + ± + + +

A.

-<-^n -Eft -i—i—i—i—i—i—i- 0.5 2.5 4.5 6.6 8.5 10.5

PRESSURE (MPa)

O-BEATTIE ( 58) A" BESSERER ( 59) +•- OOUSLIN ( 19) EI- LAW ( 62) X-MICHELS ( 561 &- MICHELS (2ND) ( 56)

ffl- PflL (2ND) ( 23) El- PflRRISH I 63) 0- REAMER I 51) •- SENGERS ( 61)

- TOMLINSON ( 39)

- WALLACE ( 65)

Figure ABA. (continued)

56 -
LU

CC

Z>

CO

CO

LU

CC

a.

<

>

LU

a

0.21

0.00

-0.21

0.35

0.00

-0.35

0.1

0.0

-0.1

0.53

0.00

-0.53

0.12

0.00

-0.12

0.78

0.00

-0.78

0.24

0.00

-0 24

373.15 - 377.59 K

&£t

+++++ x X~^< *

1 T | T I 1 I

477.59 - 498.15 K

092 ^oouucoooo

0.00

-0.92

I4- + +

- H| | + BBjT

1 8 15 22 29 36

377.59 - 398.15 K

o O Q Q O

.A fr " A4-A A

A AAAAA AA AA "A

U O Q

A

2 15 28

498.15 - 523.15 K

0.96 i Q0O0CCCO0

41

C"

0.5 11.5 398.15 - 398.16 K

f

rf^JN-++++++.

» x

I x

21

410.93 - 423.15 K

40

qOOO oouooo

+ + ++ +

^ g#l°es es q q a

i

' '

i

' i

i

p

i i ii H a i a g

1 6 11 18 21 423.15 - 444.26 K

•+++ + & $

:r +- + +

_a

1 38

444.26 - 448.15 K

oooooooooo

H 4. + + + + + + + ++ + I +. + Q 00Q

-a

1 10

448.15

19

477.59 K

28

±±

+-K-++++

±*. T++4 h+++^

I 1 1" 14 27 40

PRESSURE (MPa)

O- BERTTIE ( 58) A- BESSERER ( 59) + - OOUSUN ( 19) X- OOUSUN (2ND) 1 19) X- MICHELS ( 56) <&- MICHEL5 (2ND) ( 56) Q- REAMER ( 51)

Figure ASA. (continued)

0.00

-0.96

0.18

^t^^mmQ

+ + 4- Q F3 nn Q

48

523.15 - 573.15 K

0.00^

-0.18

+

^4^Ht-H- ^^tf- +

0.23

0.00

-0.23

-i 1 1

1

1

1 1 1 1

1 r 3 12 21 30 39

573.15 - 623.15 K

,f^^V,^

TTTTrit I I I fTTTTT IT I i in r rT,+TVT

' ff rriTrl 3 10 17 24 31 38

PRESSURE (MPa)

O- BEflTTIE ( 58) + - OOUSLIN ( 19) 0- REflHER ( 51)

57
Figure A6A. PVT data- -pressure deviations.

The comparisons are based on the SWEOS , using expression from table 7 Primary data for the SWEOS were from Douslin [19], Michels [56], Pal [23],

Parrish [63], Sengers [64], and Straty [29]. Points out of range were

Author

Douslin [19]

Temperature , K

243.15

243.15

243.15

263.15

263.15

263.15

Pressure, MPa

31

13

23

06

98

1.91

Deviation, %

63

62

62

12

12

12

Golovskiy [60] 92.45

92.14

144.57

162.11

59.52

12.10

1.92

1.93

66

115

89

61

Khazanova [61] 305.56

305.71

306.22

308.32

308.23

308.76

0.99

0.49

1.85

1.89

1.00

0.50

Pal [23] 157.20

168.03

168.48

176.72

177.38

0.52

1.00

1.66

0.35

1.23

186

125

75

228

65

188.91

208.45

209.05

222.88

223.26

0.67

0.81

1.41

0.76

1.08

72

161

93

122

87

223.57

230.05

230.29

240.74

240.89

1.35

0.81

1.00

1.01

1.11

70

64

52

33

31

Statistical comparisons follow Figure A6B.

58-
>-

t

CO

z

LU

Q

<

>

LU

Q

0.12

0.00

-0.12

0.14

0.00

-0.14

0.05

0.00

-0.05

0.14

0.00

-0.14

0.18-

0.00

-0.18

0.16

0.00

-0.16

0.12

0.00

-0.12

92.14 - 108.00 K

TT-^r -iS&o

21 22

108.00 - 122.00 K

XT

-$-

0.1

0.0

-0.1

0.14

0.00

-0.14^£

201.95 - 213.51 K

o

^

O Q

oCl

o

17.25 18.25

215.25 - 224.00 K

19.25

O

®> QiP %

O

20.50 21.75

122.00 - 138.00 K

-Oh-e- n o

o

* c o

o

20 21 138.00 - 160.36 K

QLU%J^g» @

&-

0.22

0.00

-0.22

0.32

0.00

-0.32

16.50 17.75 19

224.83 - 235.94 K

O ; a rg> %

-=-,

"o OqDaB <*

o

19 20.75

160.39 - 176.28 K

15.75

236.00 - 243.15 K

18.

ffl

ffl ffl 15.25 18

243.15 - 252.00 K

D

-@- O

o

18.25 19.25 20.25

176.72 - 189.33 K

17.75

1 TM «9 1

0.35

0.00 -&-X

-0.35

252.00 - 260.00 K

o

17.75 19.50

189.75 - 201.83 K

0.5 17.5

%tfoQo

—i

1

1

1 r* 17.25 18

$ O

0.26

0.00

-0.26

260.00 - 267.05 K

s

18.75 19.50

3

T

6.5 12 17.5

3i

DENSITY (mol/dm

3

) DENSITY (mol/dm

J

) O- GOLOVSKIT ( SO) 2" PAL ( 23)

ffl- PAL (2ND) C 23) O- STRATI ( 29)

- STRAIT I2ND) (29)

X" OOUSLIN (2ND) ( 19) O- GOLOVSKIT ( 60) B|- LAN ( 62) 2- PAL ( 23)

ffl- PAL (2N0) ( 23) O- STRATI ( 29) D- STRATI (2N0) (29)

- WALLACE ( 65)

Figure A6B. PVT data — density deviations. (Statistical comparislons begin on page 63.)

59
>-

b

CO

z

LUQ

O

<

>

LUQ

0.28

0.00

-0.28

0.28

0.00

-0.28

0.25

267.24 - 273.15 K

1 1 1 1 1 1 1 1 1 [1 1 1 jSTM

299.85 302.59 K

o

8

FR * , 0.75 6.25 11.75

273.15 - 277.61 K

17.25

0.28

0.00

-0.28

2.5 7 302.59

-i 1 1 1

| 5.5

277.92 -

—i—i—|—i—i11 283.15 K

0.14

11.5 303.53 K

16

0.00-^

0.14

++,"+

16.5

0.00^

-0.25

:<

>—'—'—'—

0.75 7 13.25

303.56 - 304.34 K

0.56 -i g»

17.25

0.1

0.0

-0.1

0.36

0.00

-0.36

0.18

0.00

-0.18

0.43

0.00

-0.43

283.15 - 288.87 K

X

cm ll

1 . 1 1

1

1 . 1 1 1 p 1 1 1 1.75 6.75 11.75

290.02 - 295.93 K

16.75

x

2.50 7.25

296.00

-i

i

| i

12

298.16 K

16.75

-O

CD

Cfl%&

0.00

-0.56

1.89

0.00

-1.89

3.27

0.00

-3.27

0.33

30

t

^pOTQgsga ,

-HML

1.75 15

304.43 - 305.15 K

%pjv V

-ffl

11

0.25 15

305.23 - 305.37 K

<? ®*ti

3* S>

-©-^ X X

1

1 I I 1 1 *M 11

1 1 1 1- 4.25 6 7.75 9.50

305.37 - 305.38 K

o.oo ?o<xxxxx* X~

-0.33-1- 1—X- 2^x>#XX

0.75 15.50 0.75 12.60

298.15 - 299.82 K

^S*

3.16

0.00

-3.16

305.39 - 305.93 K

7 V V V

V

1

1 >

s

T 7.75 16.50

DENSITY (mol/dm3

)

0.75 11.50

DENSITY (mol/dm

3

)

Figure

0- BEATTtE ( 58) + - OOUSLIN ( 19) X- OOUSLIN (2N0) ( 19) O- GOLOVSKIT ( 60) V - KHAZANOVA ! 61) H- LAW ( 62) X* MICHELS ( 56) H- pal ( 23)

ffl- PAL (2ND) t 23) O * STRATI [ 29)

- STRATI (2ND) ( 29)

- TOMLINSON ( 39) D- WALLACE ( 65)

A6B. (continued)

-I- -OOUSLIN X" OOUSLIN (2ND) V- KHAZANOVA H" LAW

ffi- MINIOVICH H-PAL

ffl- PAL C2N0) 12- PARRISH •- SENGERS O- STRATI D- STRATI (2N0) - TOMLINSON

I 19)

I 19)

( 61)

I 62)

I 22i

I 23)

I 23)

I 63)

( 64)

I 29)

( 29)

I 39)

60
t

CO

z

LUQ

<

>

LUQ

2.19

0.00

-2.19

0.17

0.00

-0.17

2.53

0.00

-2.53

1.11 0.00

-1.11

0.25

0.00

-0.25

0.33

0.00

-0.33

0.29

0.00

-0.29

305.96 - 306.58 K

V

^7

v v

V

bid ffl

ffl -A^ II

0.25 6 11.75

306.62 - 308.23 K

-o- o

-i r .a

0.29

0.00

-0.29

0.36

320.13 - 323.15 K

4V 81*

1 rfc*~-T |

1 S 1 ! |P 1 0.25 4.50 8.75 13

323.15 - 324.79 K

0.25 15

308.25 - 310.93 K

v u

m w

-a—g;

dV,

ffl- 0.75 15.50

310.93 - 310.95 K

cs B«i

0.50 5.75 11 18.25

311.09 - 312.63 K

-e-o

-©-

o (9^, aa

-I 1 1 r- -1 1 1 1-

-0.36

0.77

0.00

-0.77

0.8

0.0

-0.8

0.37

++4

0.004 3-+1 I

I H-K4-+-4-HHH-+-

' "*" +

+ ^^ +++)&o<x>&>:

7.25 14.50

324.82 - 343.09 K

1—®H!

-I

1 1

1

1 1 F-tD |

1 1 1 r 5.25 9.50 13.75

343.35 - 344.48 K

ffl

ET

-1 1 1 1 1 1 1 1 7.75

344.48 - 348.15 K

15.50

00

)8MMWM x X a o-^'oA.

-0.37-

A

-A $

, °, Q, o , oAo, n, o , 0.25 7.50 14.75

312.65 - 316.48 K

o

D O, • • (Vcocm ,

-a- tf

1 14.25

316.48 - 320.00 K

o o o

-ffl0.18

0.00

-0.18

0.81

0.00

-0.81

l

'

'

i

' ' ' 0.25 2.25 4.25 6.25 8.25

348.15 - 350.00 K

a

+^*++*+++"++

+.¥±+*XXXXX

ad

4.5

350.00

-A ra13.5

373.15 K '' + + + + °o°ooooo F~5~

1.75 15

DENSITY (mol/dm3

) A- BESSERER ( 59) V- KHAZANOVfl (61)

S- LflH ( 62)

ffl- M1NI0VICH ( 22) 2- PAL ( 23)

ffl- PflL (2N0) ( 23) 3- PARRISH ( 63) 0- REAMER ( 51) • - SENGERS ( 64) O- 5TRATY ( 29)

- STRATY (2N0) (29)

- TOnilNSON ( 39)

2.75 5.50

DENSITY (mol/dm

3

) O-BEflTTIE ( 58) A" BESSERER ( 59) + - DOUSLIN ( 19) X- OOUSLIN (2ND) ( 19) H- LAW ( 62) X--MICHELS ( 56) $- MICHELS (2ND) ( 56)

ffl- PAL (2N0I ( 23) H- PARRISH ( 63) 0- REAMER ( 51) • - SENGERS ( 64)

- TOMLINSON ( 39) - WALLACE ( 65)

Figure A6B. (continued)

61 -
>-

t

CO

z

LUQ

O

I-

<

>

LU

Q

0.11

0.00

-0.11

0.74

0.00

-0.74

0.11

0.00

-0.11

0.81

0.00

-0.81

0.14

0.00

-0.14

0.83

0.00

-0.83

0.27

0.00

-0.27

373.15 - 377.59 K

3

Q

^STOafcXX +++

"i r- +++j_+

++x>ooE

0.25 12.50

377.59 - 398.15 K

CCCtaDOCD

-i r 14.75

398.15 - 398.16 K

*+++++++++ '

' ++

i i x*X

0.89

0.00

-0.89

0.99

0.00

-0.99

0.14

477.59 - 498.15 K

w$\

:tepQcrrcq

0.25 12.50

498.15 - 523.15 K

TT HHqgjBP^

^CQOQCTpP?

0.25 8

523.15 - 573.15 K

11.75

0.00^

-0.14 + +» +

-i—i—i i ~i ~ i

*t

*** * ** +

0.75 6.50 12.25

410.93 - 423.15 K

\m$$Q

:tcoaxcco

000 ^eta aMWE^B 0.23

0.75 2.75 4.75 6.75 8.75

573.15 - 623.15 K

°- 00 t^TTTTr*

-0.23

I r —'

i 1 1 r- 0.25 4.75 9.25 13.75

423.15 - 444.26 K

0.75 7.75

l!fiX^&fcfc^ X* ,++ T^^Fg> ++++X

DENSITY (mol/dm

3

) O- BERTTIE ( 58) -(--OOUSLIN ( 19) Q- REAMER ( 51)

0.25 11.25

444.26 - 448.15 K

H

- H-hKH-HH-HH1 I I I 0&$

^boooccco

-i 1 1 1 1 1 1 1 r 0.25 4.50 8.75 13

448.15 - 477.59 K

eQ"

^F. +T*-M=+ + j:#+ +

i 1—1 1 r— 0.25 3.75i—|—i—i—

7.25 10.75

DENSITY (mol/dm3

) O- BERTTIE ( 58) A- 6ESSERER ( 59) + - OOUSLIN ( 19) X- OOUSLIN (2N0) ( 19) X- MICHELS ( 56) <&- MICHELS I2N0) t 56) 0- REAMER ( 51)

Figure A6B. (continued)

-62
Figure A6B. PVT data- -density deviations.

The comparisons are based on the SWEOS , using expression from table 7

Primary data for the SWEOS were from Douslin [19], Michels [56], Pal [23],

Parrish [63], Sengers [64], and Straty [29]. Points out of range were

Author Temperature, K Density, mol»dm Deviation, %

Khazanova [61] 303.25

303.97

303.16

303.17

303.60

303.56

303.26

305.79

318.01

9.21

0.92

0.92

0.46

0.46

0.22

0.22

5.45

2.87

6

-8

-8

-8

-8

-9

-9

-10.8

-12.4

Law [62] 300.00

320.00

10.27

6.78

2.8

5.7

Miniovich [22] 305.36

305.38

70

51

12

15

Pal [23] 305.42

305.74

305.63

79

79

8.10

-11.

-16,

-24,

Statistical comparisons between experimental PVT data and the SWEOS

correlation. Statistics for the calculation of pressure are given first;

comparisons for the calculation of density are given next with the suffix

"2" on each statistical category.

Data from Beattie [58]

Number of Points: 96

AAD%

AAD2%

AAD

AAD2

0.43 BIAS% = 0.43

0.49 BIAS2% = -0.49

Absolute Deviations:

0.04 BIAS = 0.04

RMS% = 0.25

RMS2% = 0.23

RMS = 0.04 MPa

0.013 BIAS2 = -0.013 RMS2 = 0.009 mol»dm'

Data from Besserer [59]

Number of Points: 68

AAD% - 0.67 BIAS% = -0.43

AAD2% - 0.83 BIAS2% = 0.32

Absolute Deviations:

AAD - 0.05 BIAS = -0.04

AAD2 - 0.039 BIAS2 = 0.009 RMS2 =

RMS% = 1.00

RMS2% = 1.37

RMS = 0.09 MPa

0.075 mol»dm

-3

Data from Douslin [19]

Number of Points: 449

AAD%

AAD2%

AAD

AAD2

1.10 BIAS% = 1.07

0.24 BIAS2% = -0.10

Absolute Deviations:

0.04 BIAS - 0.03

RMS% = 6.20

RMS2% = 0.55

RMS 0.12 MPa

0.017 BIAS2 -0.008 RMS2 = 0.040 mol»dm

63
Weighted Data:

Number of Points

AAD%

AAD2%

AAD

AAD2 =

257

0.07 BIAS% = 0.02

0.06 BIAS2% = -0.03

Absolute Deviations:

0.01 BIAS = 0.00

0.003 BIAS2 = -0.001

RMS% = 0.09

RMS2% = 0.07

RMS = 0.02 MPa

RMS2 = 0.005 i -3

Data from Golovskiy [60]

Number of Points: 111

AAD% - 8.88 BIAS% - 8.64 RMS% - 17.72

AAD2% - 0.10 BIAS2% - -0.09 RMS2% - 0.09

Absolute Deviations:

AAD = 1.15 BIAS = 1.09 RMS = 1.68 MPa

AAD2 = 0.019 BIAS2 = -0.017 RMS2 = 0.020 mol-dm"

Data from Khazanova [61]

Number of Points: 86

AAD% = 2.23 BIAS% = 0.55

AAD2% = 3.02 BIAS2% = -1.05

Absolute Deviations:

AAD - 0.06 BIAS = -0.01

AAD2 - 0.093 BIAS2 = 0.001

RMS% = 3.51

RMS2% = 4.26

RMS = 0.08 MPa

RMS2 = 0.170 l -3

Data from Law [62]

Number of Points: 56

AAD% - 2.03 BIAS% = 1.16 RMS% = AAD2% = 0.49 BIAS2% = 0.38 RMS2% = Absolute Deviations:

AAD - 0.16 BIAS = 0.09 RMS = AAD2 = 0.038 BIAS2 = 0.023 RMS2 =

4.57

1.08

0.18 MPa

0.077 mol'dm"

Data from Michels [56]

Number of Points: 101

AAD% = 0.03 BIAS% = -0.01 RMS% = AAD2% = 0.05 BIAS2% = 0.02 RMS2% = Absolute Deviations:

AAD = 0.00 BIAS = 0.00 RMS = AAD2 = 0.001 BIAS2 = 0.001 RMS2 =

0.04

0.06

0.00 MPa

= 0.002 mol»dm'

Weighted Data:

Number of Points 81

AAD% = 0.03 BIAS% = -0.01

AAD2% = 0.04 BIAS2% = 0.02

Absolute Deviations:

AAD - 0.00 BIAS = 0.00

AAD2 = 0.001 BIAS2 = 0.000

RMS%

RMS2%

RMS

= 0.04

= 0.06

= 0.00 MPa

RMS2 = 0.001 mol»dm

-3

Data from Miniovich [22]

Number of Points: 63

AAD% = 0.03 BIAS% = -0.03

AAD2% - 1.41 BIAS2% = 1.11

Absolute Deviations:

AAD - 0.00 BIAS = 0.00

AAD2 - 0.093 BIAS2 = 0.072 RMS2

RMS% = 0.03

RMS2% = 2,.85

RMS = ,00 MPa

0.191 mol'dm

64
Data from Pal [23]

Number of Points: 309

AAD% = 8.38 BIAS% = 8.34

AAD2% - 0.78 BIAS2% = -0.78

Absolute Deviations:

AAD - 0.30 BIAS = 0.27

AAD2 = 0.061 BIAS2 = -0.060

RMS% = 24.68

RMS2% 2.32

RMS = 0.38 MPa

RMS2 = 0.169 mol.dm

-3

Weighted Data:

Number of Points

AAD% =

AAD2% =

AAD

AAD2

45

0.96 BIAS% = 0.70 RMS% =

0.09 BIAS2% = -0.07 RMS2% = Absolute Deviations:

0.47 BIAS = 0.30 RMS =

0.015 BIAS2 = -0.011 RMS2 -

1.05

0.10

0.51 MPa

0.017 mol.dm

-3

Data from Parrish [63]

Weighted Data:

Number of Points: 9

AAD% - 0.32 BIAS% = 0.21

AAD2% = 0.23 BIAS2% = 0.03

Absolute Deviations:

AAD = 0.02 BIAS = 0.02

AAD2 = 0.016 BIAS2 = -0.005

RMS% = 0.26

RMS2% = .35

RMS = .02 MPa

RMS 2 = 0.018 mol<-dm

-3

Data from Reamer [51]

Number of Points: 176

AAD% - 1.13 BIAS% = -1.13

AAD2% - 0.50 BIAS2% = 0.50

Absolute Deviations:

AAD - 0.41 BIAS = -0.41

AAD2 - 0.047 BIAS2 = 0.047

RMS% = RMS2% =

1.22

0.40

RMS = 0.65 MPa

RMS2 = 0.040 mol.dm"

Data from Sengers [64]

Weighted Data:

Number of Points: 30

AAD% - 0.03 BIAS% = 0.01

AAD2% - 0.30 BIAS2% = -0.12

Absolute Deviations:

AAD - 0.00 BIAS = 0.00

AAD2 = 0.021 BIAS2 = -0.010

RMS% = 0.03

RMS2% = 0.55

RMS = 0.00 MPa

RMS 2 = 0.039 mol<• dm

-3

-65-
Data from Straty [29]

Number of Points: 477

AAD% - 2.73 BIAS% = 1.84 RMS% - 6.23

AAD2% - 0.10 BIAS2% = 0.05 RMS2% = 0.47

Absolute Deviations:

AAD - 0.15 BIAS - 0.04 RMS = 0.25 MPa . AAD2 - 0.009 BIAS2 = 0.000 RMS2 = 0.031 mol'dm"

Weighted Data:

Number of Points: 381

AAD% - 1.07 BIAS% = 0.23 RMS% = 2.07

AAD2% - 0.04 BIAS2% = 0.00 RMS2% = 0.06

Absolute Deviations:

AAD - 0.13 BIAS - -0.01 RMS - 0.22 MPa

AAD2 - 0.006 BIAS2 = -0.001 RMS2 = 0.007 mol»dm

-3

Data from Tomlinson [39]

Number of Points : 61

AAD% - 0.48 BIAS% = 0.47 RMS% = 0.33

AAD2% - 0.51 BIAS2% - -0.49 RMS2% - 1.61

Absolute Deviations:

AAD - 0.03 BIAS - 0.03 RMS - 0.03 MPa

AAD2 - 0.040 BIAS2 = -0.039 RMS2 - 0.110 mol'dm"

Data from Wallace [65]

Number of Points: 20

AAD% - 0.06 BIAS% = 0.03 RMS% = 0.08

AAD2% - 0.06 BIAS2% = -0.03 RMS2% = 0.08

Absolute Deviations:

AAD - 0.00 BIAS = 0.00 RMS = 0.00 MPa

AAD2 - 0.000 BIAS2 = 0.000 RMS2 - 0.000 mol-dm"

3

3

66-
2.05

0.00

-2.05

3.32

0.00

1.58 - 1.59 mol/dm ; -e = ? 3-9- o o

288 302 316 330

3.27 - 4.60 mol/dm 3

O O CL

o cP o° Q

O

-3.32 -h 1 1 1 298 329

4.61 - 5.88 mol/dm 3 1.48

0.00^

-1.48

308 313 318 323 328

5.88 - 6.50 mol/dm 3

o o

l 3-A 1

i +

I

c

2.99

0.00

<

>

LU

Q

-2.99^ir-T

O

+

1.48

0.00

-1.48

6.63

0.00

-6.63

3.68

0.00

-3.68

308.5 314 319.5 325

6.50 - 7.88 mol/dm 3

310 315 320 325

7.88 - 8.00 mol/dm

&

-i 1 1 1 1 1 1-

2.21

0.00

9.16 - 11.01 mol/dm :

2.21-S QS ,od cn, Q

308 329

11.02 - 11.05 mol/dm 3 1.86

0.00

,p,o n,p

,

. .°. °.

q

297 304 311 318 325

11.92 - 11.97 mol/dm 3 1.45

0.00

n n O O O O

$ 1.45^—©- U

295 312 329

11.98 - 12.93 mol/dm 3 1.93

0.00

-1.93

1.9

0.0

@-

o o o

o o o o ci

290 327

12.93 - 13.93 mol/dm :

O D O O Ci o o o

-1.9 p !

i | 280 292 304 316 328n 1 ] 1 r2.07

0.00

13.93 - 14.00 mol/dm 3

•2.07-A

o o o o o o o o o

i i r 306 312.25 318.50 324.75

8.00 - 9.16 mol/dm 3

+ T"

O €oo

1

' '

l

' '

l

' ' l' '

l

' '

' 304 309 314 319 324 329

TEMPERATURE (K)

0.78

0.00

-0.78

266 285 304

14.53 - 14.61 mol/dm 3

o c£ o o o

!D i iM—i—i—i

i—i—i—i—i—i—i—I—i—i—i—i—i—

r

C)

272 286 300 314

TEMPERATURE (K)

O - "ODER ( 66) A" ROOER 1 2ND) ( 66) + - SENGERS ( 64)

O-RODER

A- RODER (2ND)

( 66)

I 66)

Figure A7. Isochoric molar heat capacity. (Statistical compariaions begin on page 69.)

-67
1.73

0.00

1.73 pV <

i

i

14.62 - 14.96 mol/dm :

o c

1.18 0.00

—i—|—i—i—i—|—i—i—

i

257 268 279 290 301

14.97 - 15.04 mol/dm3

lis § o9 . ? . ?

o o o

(J

o

<

>

LUQ

2.06

0.00

-2.06

1.91 0.00

260 268 276 284 292

15.04 - 16.10 mol/dm 3

° A&0 ° ° °

-Ai 1 1

3.79

0.00

-3.79

2.82

0.00

-2.82

5.96

0.00

-5.95

18.92 - 19.62 mol/dm :

o o o o c^

-1 1 1

1 1

1

1 r— 151 158.25 181.50 166.75

19.62 - 20.25 mol/dm 3

o o

-: — 1 1 T 1 ^ I 136.75 144 151.25

20.27 - 21.00 mol/dm 3

° Q o o o n

-o

244 273

16.11 - 16.85 mol/dm 3

o o o o an qd

-1.91 -0-, 1 , 1 1

1 r—

i

r—

1

r—

1

1—t

2.96

0.00

-2.96

3.82

0.00

-3.82

3.37

0.00

-3.37

236.5 242 247.5

16.86 - 17.93 mol/dm 3 DOOOCb O 0°

-i—i—i—

|—i—i—i—i (p i—i—i i |

i—n—i—

|—i—i—

n

204 209 214 219 224 229

17.94 - 18.84 mol/dm 3

O c

1 {J

182.5 20

18.86 - 18.91 mol/dm 3

D OA- 1

1 °-^°A 1 |-oi 1

1 1 r 168 171 174 177 180

TEMPERATURE (K)

O- ROOER ( 66) A- ROGER (2N0) ( 66)

i 1 1

1 1 11 1

1

1 r 110 116 122 128 134

TEMPERATURE (K)

O- ROOER ( 66) A" ROOER (2ND) I 66)

Figure A7. (continued)

68 -
Figure A7 . Isochoric molar heat capacity.

The comparisons are based on the SWEOS , using expression from table 7 Primary data for the SWEOS were from Roder [66] and Sengers [64]

Statistical comparisons between tabulated isochoric molar heat capacities

and values calculated from the SWEOS using the reported experimental

densities are given.

Data from Roder [66]

Number of Points: 209

AAD% - 1.32 BIAS% - -0.93 RMS%

Absolute Deviations:

AAD - 0.66 BIAS - -0.46 RMS

1.27

0.63 J.mol'^K" 1

Weighted Data:

Number of Points: 184

AAD% =- 1.16 BIAS% = -0.78 RMS%

Absolute Deviations:

AAD - 0.56 BIAS = -0.36 RMS

= 1.09

= 0.52 J-mol" 1 ^" 1

Data from Sengers [64]

Weighted Data:

Number of Points : 30

AAD% - 3.51 BIAS% - -3.51

Absolute Deviations:

AAD - 2.64 BIAS - -2.64

RMS% = 4.82

RMS = 4.01 J-mol" 1 ^" 1

69
2.46

0.00*

-2.46

—0.00 - 1.72 MPa

=H -QgQoQOq c .

U

<

>LLI Q

1.12 0.00

-1.12

1.85

0.00

-1.85

4.98

0.00

-4.98

3.73

0.00

-3.73

6.55

0.00

-6.55

6.03

0.00

-6.03

i 1 i |

1 r—i

1 1 1 1

1 1 i i 120 240 360 480

1.72 - 2.00 MPa

+++ t OD O

+++ + t—i—i—i—

|—i—i—i—i—|—i—n—i—|—i—i—i—i—[—i—i—

r

130 180 230 280 330 380

2.00 - 3.45 MPa

;^i § ° ° °

-i—i i M i—i—i—i—i—r- 230 280 330 380 430 480

3.45 - 4.67 MPa

w

T O Q n JQ

' U> I I |

I I T I

|

I I I I |T I I 280 330 380 430 480

4.67 - 4.92 MPa

?= T^ OQOQ

r*-

-Hi

rri—i—

|—i—i—i—i—|—i—i—i—i—|—i—i—i

280 330 380 430 480

4.92 - 5.51 MPa

T o

8

-^-T t + ± ' X %

290 320

5.51 - 6.20 MPa #

_Q Q Q Q

—

i

' r— 350 380

jn —i—i—

|—i—i—i—| i i i |—i—i

290 328 366 404 442 480

TEMPERATURE (K)

O- BIER ( 43) A- BIER (2N0) ( 43) + - FURTROO ( 44) X- FURTROO (2ND) (44)

O- MIYRZRKI ( 67)

2.34

0.00

-2.34

3.04

6.20 - 6.90 MPa

+ +, +

+ +1+ +^'

4-,~U

T -4-+ + '

' -|- + + + + n—i—i

\—i—i—i—i—

[—i—i—i—i—i—i—i—i—r* 110 165 220 275 330

0.00 -H

-3.04

2.34

0.00

-2.34

4.17

0.00

-4.17

1.3

0.0

-1.3

—6.90 - 8.62 MPa

&o—Op Q Q Q

d^+ +

i i i—i—i—i—i—ii—i—

r

280 330 380 430 480

8.62 - 10.34 MPa

II I

I HH o o o o

+

240 300 360 420 480

10.34 - 13.79 MPa

\

±.t: -feS"

1 '

—I 1 1

1 I- 110 200 290

13.79 MPa

O +""iX

-\

380

. + + + +++

'^ %

± + + +

l

1

1 | l l l—l 1 r 160 230 300i i 370

TEMPERATURE (K)

O-BIER ( 43) + - FURTROO ( 44) O- MItRZRKI ( 67)

Figure A8. laobaric molar heat capacity. (Statistical comparlaiona begin on page 71.)

70
Figure A8 . Isobaric molar heat capacity.

The comparisons are based on the SWEOS , using expression from table 7 Primary data for the SWEOS were from Bier [43] and Furtado [44]. Points

out of range were

Author

Furtado [44]

Temperature , K

302.87

303.15

304.26

304.82

305.26

305.26

306.48

299.82

Pressure, MPa

4.67

4.67

4.92

4.92

4.92

4.92

4.92

6.90

Deviation, %

20.3

34.2

-39.2

-34.2

-29

-37

31

6

4

2 8.7

Miyazaki [67] 308.15

307.15

307.55

308.55

309.15

313.15

17

17

17

17

17

20

20.7

15.9

20.7

46.9

70.6

10.1

Statistical comparisons between tabulated isobaric molar heat capacities

and values calculated from the SWEOS are given.

Data from Bier [43]

Number of Points: 121

AAD% - 1.25 BIAS% = 0.56 RMS%

Absolute Deviations:

AAD = 2.29 BIAS = 0.52 RMS

2.06

6.17 J«mol" 1

.K"

1

Weighted Data:

Number of Points: 118

AAD% = 1.08 BIAS% = 0.78

Absolute Deviations

AAD = 1.72 BIAS = 1.16

RMS% = 1.18

RMS = 3.80 J.mol" «K~

Data from Furtado [44]

Number of Points: 299

AAD% = 2.22 BIAS% = -0.11

Absolute Deviations:

AAD = 8.32 BIAS = -2.27

RMS% = 5.59

RMS = 38.37 J-mol'-'-'K"

Weighted Data:

Number of Points: 241

AAD% = 1.09 BIAS% = -0.02

Absolute Deviations:

AAD =2.19 BIAS = 0.12

RMS% = 1.63

RMS = 5.15 J.mol

_1

'K"

Data from Miyazaki [67]

Number of Points: 45

AAD% = 7.92 BIAS% = -1.39

Absolute Deviations:

AAD = 46.67 BIAS = 2.97

RMS% = 14.64

RMS =107.38 J»mol" 1 »K"

1

-71
4.22

O.OO^r

-4.22

9.74 - 12.35 moi/dm ;

1 =F Oq

o

TSTO

0.69

0.00

-0.69

19.18 - 19.74 mol/dm 3 \ P n

A A,A *' T U

+ 1 i i

1

CJ

O

l-

<

>

LU

Q

0.31

0.00

-0.31

0.17

0.00

-0.17

0.44

0.00

283.75 301.50 142.75 157.50

12.38 14.74 mol/dm 3 19.75 - 20.25 mol/dm 3 ^—cr &

u o

1 o

1 11 —

©

1.23

0.00

-1.23

f +

257 280

14.75 - 16.06 mol/dm 3 & o

-©- -e

i—i—-Qr"*i—i—i—i—i—r-

-i ,

1

1 1 1

1 r 129.25 133.75 138.25 142.75

20.26 - 20.67 mol/dm 3 2 - 46 ? ? o—ra 4- o-~a ML

0.00

-2.45

228 233 238 243 248 253

16.25 - 17.22 mol/dm 3 °o^oOooo °

118 121.75 125.50 129.25

20.74 - 21.07 mol/dm 3 3.1 -a—©&-p

co +—o

4- o q4

0.44 -JO—i

1 1 1- 204 215 226

17.33 - 18.19 mol/dm 3

1.1

0.0

1.1i !rOO n© o o o O O O

0.97

0.00

-0.97

0.55

0.00

-0.55

—i—i—i—|—i—i—i—i—i—i—|—i—i—i—i—i— 182 189 196 203

18.21 - 18.76 mol/dm 3

-£ o o

i a. — i\i—'

r 168 172.5 177 181.6

18.79 - 19.16 mol/dm 3

0.0

-3.1

3.35

0.00

-3.35

1.7

0.0

-1.7

107 116.25

21.08 - 21.44 mol/dm3

<?

*

96.75 107

21.44 - 21.62 mol/dm ;

JQ. +

+o © CA- Oi

i r—i 1—i r- J"

i i 1 i |

1

1 I i

91.50 94.25 97

TEMPERATURE (K)

O- ROOER I 66) A- WIEBE I 68) + - WITT ( 69)

157.76 161 164.25 167.50

TEMPERATURE (K)

O- ROOER ( 66) A- WIEBE ( 68) + - WITT ( 69)

Figure AS. Molar heat capacity of the saturated liquid. (Statistical compariaiona begin on page 73.)

72 -
Figure A9 . Molar heat capacity of the saturated liquid.

The comparisons are based on the SWEOS , using expression from table 7 Primary data for the SWEOS were from Roder [66].

Statistical comparisons between tabulated molar heat capacities of the

saturated liquid and values calculated from the SWEOS are given.

Data from Roder [66]

Weighted Data:

Number of Points: 106

AAD% = 0.84 BIAS% = 0.31 RMS% = 1.23

Absolute Deviations: 1 1 AAD -= 0.71 BIAS = 0.09 RMS = 1.08 J.mol -K

Data from Wiebe [68]

Number of Points : 41

AAD% - 0.95 BIAS% = 0.60 RMS% = 1.13

Absolute Deviations: , , AAD = 0.67 BIAS = 0.41 RMS = 0.79 J.mol -K

Data from Witt [69]

Number of Points: 39

AAD% = 1.54 BIAS% = 1.38 RMS% = 1.36

Absolute Deviations: 1 1 AAD - 1.31 BIAS = 1.20 RMS = 1.40 J.mol «K

73-
Q

LU

UJ

Q_

CO

o

CO

O

>

LUQ

0.9

3

o.o-s

-0.9

0.9

0.0

-0.9

0.9

0.10 - 1.96 MPa

o

o

-e- R

290 330 370 410 450

1.96 - 3.92 MPa

O u o

"§

e

o ° § o fl

i

1 1 1

1

1 1 1 1 1

1 1 1 r 240 310 380 450

4.12 - 5.22 MPa

o.o4

-0.9

A a!:

A 4- °nOU

0.9

0.0

-0.9

i—i—i—i—

|—i—i—i—i—|—i—i—i—i—|—i—i—i—i—|—i—i—

100 170 240 310 380 450

5.26 - 6.87 MPa

^

~S~

-e- Q

-9-

300 350 400 450

0.9A

0.0

-0.9

6.87 - 7.85 MPa

G

A

& H O Q °

I

' ' '

I 140 202 264 326 388 450

7.85 - 8.83 MPa

0.95 -ta ©-

0.00

-0.95

0.93

A

. AA *_^g C) -&—*> qOqQ

-\—i—i—I—i—i—i—i—

]—i—i—i—i—i—i—i—i—i—i—i—i—

100 170 240 310 380 450

8.83 - 10.18 MPa

*3 H —g-^f

0.00-3

-0.93

4-

1

*

i

'

i

'

i

' ' '

i

' ' i'

' 220 266 312 358 404 450

TEMPERATURE (K)

O- TERRES ( 70) A- TSUMURFI (71) + - TSUMURR (2ND) ( 71)

0.92

0.00

-0.92

0.81

0.00

-0.81

0.9

0.0

-0.9

10.30 - 11.77 MPa

? a^ a a £-a Qy §§ Q

If" O

i—t—i—i—

|—i—i—i—i—|—i—i—i—i—

|—i—

100 170 240 310 380 450

11.77 - 15.51 MPa

A A A A 2 JA

-A A-

-i—i—i—i—

i—

n—I—i—i—i—i—I—i—i—

100 170 240 310 380 450

16.29 21.68 MPa

^-A- A A

-I 1 [

1 1 1 1 1 1

1-

0.9A

100 146 192 238 284 330

21.68 - 28.50 MPa

0.0^

-0.9

A

-AA A A A

A A -N- A

1—i—l—I—r0.9

100 146 192 238 284 330

28.52 - 34.92 MPa

T a ^ A

a a g m

0.0^-

-0.9

A A

A A & ^r

0.81A

T I I

|

I

>

I

| ' ' '

I

' ' ' I' ' 100 146 192 238 284 330

35.33 - 36.83 MPa

0.00

-0.81

120 165 210 255 300

TEMPERATURE (K)

O- TERRES ( 70) A- TSUnuRfl I 71) + - TSUMURFI (2N0) ( 71)

Figure A10. Sound speed in the single-phase fluid. (Statistical compariaions begin on page 75.)

-74
Figure A10. Sound speed in the single-phase fluid.

The comparisons are based on the SWEOS , using expression from table 7 Primary data for the SWEOS were from Terres [70] and Tsumura [71]

Statistical comparisons between tabulated sound speeds and values

calculated from the SWEOS are given.

Data from Terres [70]

Weighted Data:

Number of Points: 92

AAD% = 0.79 BIAS% = -0.40 RMS% = 1.00

Absolute Deviations: - AAD - 2.35 BIAS - -1.11 RMS = 2.98 rs

Data from Tsumura [71]

Number of Points: 156

AAD% - 0.31 BIAS% = -0.09 RMS% = 0.36

Absolute Deviations: 1 AAD - 3.29 BIAS = -1.13 RMS = 4.38 m»s"

Weighted Data:

Number of Points: 109

AAD% = 0.36 BIAS% = -0.16 RMS% = 0.38

Absolute Deviations: - AAD - 4.29 BIAS = -1.70 RMS = 5.07 m-s

75-
2.49 Q—

0.00

Z)

o -2.49

_J

Q 2.17

LLJ 0.00

< -2.17

cc3

1- 1.39

< 0.00

CO

9.25 - 11.01 mol/dm :

AA A A A A + +

18.89 - 19.31 mol/dm 3 0.42 -a o

295 297 299 301 303

11.70 - 13.57 mol/dm 3 A XA w

x

0.00

-0.42

0.54

A X A X \[

154 165

19.42 - 20.04 mol/dm 3 Co

0.00 ^

T

1 1 1 1 1

1 1 1 1 1 1 1 1 1 1 1 1 1- 269 278 283 290

13.93 - 15.19 mol/dm :

0.54 -f

-e- ^A

X

a >:

Q

LU

LLI Q_

CO

Z)O

CO

O

>

LU

Q

-1.39

0.79

0.00

-0.79

0.18

0.00

-0.18

0.31

0.00

-0.31

A & & It % 0.77

135 140.5 146 151.5

20.04 - 20.60 mol/dm 3

O.OO^r

-0.77

TT ~^~^

-g- "#- ->:

244 251 258 265

15.20 - 16.49 mol/dm 3

x A a &

0.81

120 125 130 135

20.61 - 21.14 mol/dm 3 —9

1

'

'

l

' ' ' '

l

' ' '

' I'

' ' '

I ' '

' 220 225 230 235 240 245

0.004

-0.81

id cr X

A X

105 119.75

16.50 - 17.48 mol/dm 3 u

X

A

*

A

1 1 rOk

I

0.81

0.00

-0.81

21.15 - 21.64 mol/dm'

cj-^ cr

X X

-A-

>:

T I 1 1 1" 198 209 220

17.64 - 18.26 mol/dm 3 91

1 i I

1 r- 98 105

-9- XA a: TEMPERATURE (K)

O- POOLE A- TSunuRfl X- VflNGEEL

( 72)

( 71)

I 73)

180.25 185.25 190.25 195.25

18.28 - 18.87 mol/dm 3 0.27 -©

0.00

-0.27

% XA

-i .

1

, 172.75

O

h

165.50 180

TEMPERATURE (K)

O- POOLE t 72) A- TSUMURFI (71)

-f- TSUMURA (2N0) (71)

X- VFINGEEL ( 73)

Figure A11. Sound speed In the saturated liquid. (Statistical comparisions begin on page 77.)

- 76 -
Figure All. Sound speed in the saturated liquid.

The comparisons are based on the SWEOS , using expression from table 7

Primary data for the SWEOS were from Tsumura [71]

.

Statistical comparisons between tabulated sound speeds and values

calculated from the SWEOS are given.

Data from Poole [72]

Number of Points: 25

AAD% - 0.40 BIAS% - 0.39 RMS% - 0.29

Absolute Deviations: - AAD - 7.01 BIAS - 6.88 RMS = 5.39 m^s

Data from Tsumura [71]

Number of Points: 51

AAD% - 0.56 BIAS% = 0.45

Absolute Deviations

AAD = 3.42 BIAS = 1.59

RMS% = 0.70

RMS = 4.15 m»s

Weighted Data:

Number of Points: 47

AAD% = 0.49 BIAS% = 0.37

Absolute Deviations:

AAD - 3.42 BIAS = 1.43

RMS% = 0.63

RMS = 4.26 m»s'

Data from Vangeel [73]

These unpublished data were tabulated in Ref.[6].

Number of Points: 44

AAD% = 0.44 BIAS% = 0.35 RMS% = 0.59

Absolute Deviations:

AAD = 3.86 BIAS = 2.56 RMS = 4.09 m77-
>-

t

CO

O

>

t

CO

z

LLI Q

O

cc

LUN

O

<

>

LU

Q

3.15

0.00

-3.15

1.64

0.00

-1.64

1.25

0.00

-1.25

2.02

0.00

6.40 - 9.26 /zPas

* ztffe

# r i r i i i

o o

i

i i i |i i i

|

i i .

1 to 11.43 - 12.30 yuPa s

L. 1 J

c\ c\r\ — ra V

V

u.uu -

-2.13^5r^—i—i—i a i o

, , , , 1 1 1 1 -r-8 190 212 234 256 278 300

9.28 - 9.47 /iPa'S _

£ -, 1

1 1

1 1 r- 292.50 297.75 303 308.25

9.47 - 9.56 /xPa-s

*X^ *

o

1.29

0.00

-1.29

1.23

0.00

-1.23

363 371 379 387 395

12.40 - 13.90 /xPa-s

V

-0_

o o

T T©- o I TT I

1 I"" I 400 415 430 445 460

14.07 - 15.26 fiPa-s

a?

300.50 308.25

9.60 - 10.10 /iPas

-2.02-W-T-.

-*

o

1.68

0.00

-1.68

1.64

0.00

1—

1—

|—l—l—l—l—l—l—

|—I—l—l—I—l

303 310 317 324

10.10 - 10.64 fiPas

o "i 1 r

x~ -es et

-A-, &—

323 334 345

10.69 - 11.27 /zPa-s

-1.64 -A

X

O

343

I I I

| ft-. A l !

I

|

I 350 357 364

TEMPERATURE (K)

O- ABE A- fiozum

4-- CftRMICHFIEL X - CRRVEN O- OEROCCO V- EflKIN H- FLEETER X- IHflSftKI <&- KESTIN

ffi- KESTIN (2ND) 2" KESTIN S- KESTIN (2ND) (8- LflnSERT Q- TRRUNTZ • - VOGEL

( 74)

( 75)

( 76)

( 77)

( 78)

( 79)

( 80)

( 81)

( 82)

( 82)

( 83)

( 83)

( 84)

( 85)

( 86)

O O

1 I | I I

| Zfl ' ' ' ' [

' ' ' I ' ' [ T T T I 1 I I I I T I I 460 474 488 502 516 530

TEMPERATURE (K)

O- ABE 74) A- AOZuni 75) O- OEROCCQ 78) V- EflKIN 79)

ffi- KESTIN 83) 0- TRRUNTZ 85)

Figure A12. Viscosity at zero density. (Statistical comparisions begin on page 79.)

78
Figure A12. Viscosity at zero density.

The comparisons are based on eq (9), and data have been adjusted

(slightly) to zero density using the correlation of eq (13) as appropriate

Primary data were from Fleeter [80] and Kestin [82,83].

Statistical comparisons between tabulated (adjusted) values of the dilute

gas viscosity and values calculated from eq (9) are given.

Data from Abe [74]

Number of Points : 5 AAD% = 0.49 BIAS% = AAD = 0.05 BIAS

•0.04

•0.01

RMS%

RMS

0.61

0.06 /xPa»s

Data from Adzumi [75]

Number of Points: 9

AAD% = 1.60 BIAS%

AAD = 0.17 BIAS

•1.60

0.17

RMS%

RMS

0.38

0.05 /xPa«s

Data from Carmichael [76]

Number of Points: 3 AAD% = 0.18 BIAS% = 0.18

AAD = 0.02 BIAS = 0.02

RMS%

RMS

0.11

0.01 ^Pa«s

Data from Craven [77]

Number of Points: 4

AAD% = 1.44 BIAS%

AAD = 0.14 BIAS

1.44

0.14

RMS%

RMS

0.51

0.05 /iPa»s

Data from Derocco [78]

Number of Points: 19

AAD% = 1.12 BIAS%

AAD = 0.13 BIAS

•1.12

0.13

RMS%

RMS

0.40

0.05 /iPa»s

Data from Eakin [79]

Number of Points: 11

AAD% = 0.77 BIAS%

AAD = 0.08 BIAS

0.77

0.08

RMS%

RMS

0.41

0.04 /zPa»s

Data from Fleeter [80]

Weighted Data:

Number of Points: 1 AAD% = 0.88 BIAS%

AAD = 0.08 BIAS

0.88

0.08

RMS%

RMS

0.00

0.00 /zPa»s

Data from Iwasaki [81]

Number of Points: 16

AAD% = 1.07 BIAS%

AAD = 0.10 BIAS

1.07

0.10

RMS%

RMS

0.17

0.01 /xPa-s

79
Data from Kestin [82]

Number of Points: 2 AAD% = 1.13 BIAS%

AAD = 0.10 BIAS

1.13 RMS%

0.10 RMS

0.07

0.01 /xPa»s

Weighted Data:

Number of Points: 1

AAD% = 1.05 BIAS%

AAD = 0.10 BIAS

1.05

0.10

RMS%

RMS

0.00

0.00 /xPa»s

Data from Kestin [83]

Number of Points: 5 AAD% = 0.86 BIAS%

AAD = 0.10 BIAS

0.40

0.06

RMS%

RMS

0.88

0.10 /iPa»s

Weighted Data:

Number of Points: 4

AAD% = 0.79 BIAS%

AAD = 0.10 BIAS

•0.79 RMS%

0.10 RMS

0.48

0.07 /xPa«s

Data from Lambert [84]

Number of Points: 4

AAD% = 0.39 BIAS%

AAD = 0.04 BIAS

0.10

0.01

RMS%

RMS

0.45

0.05 /iPa«s

Data from Trautz [85]

Number of Points: 6

AAD% = 0.47 BIAS%

AAD = 0.05 BIAS

0.47

0.05

RMS%

RMS

0.32

0.03 /iPa»s

Data from Vogel [86]

Number of Points: 2 AAD% = 1.93 BIAS%

AAD = 0.13 BIAS

1.21

0.07

RMS%

RMS

1.93

0.13 /iPa»s

-80
>-

3.25

1- 0.00

> -3.25

hCJ

Z) 3.1 Q 0.0 Z

o -3.1

(J

LUX

h-

>

CO

z

LU

Q

O

cc

LUN

o

I-

<

>

LU

Q

13.12 - 21.92 mW/(nrvK)

ffl a w

220 250 280 310

22.03 - 23.20 mW/(mK)

_ffi_ 9

07

-,—*-

5.58

303 306

23.36

309 312 315

27.20 mW/(mK)

0.00-^

-5.58^

7T1$ IT

3.79

0.00

-3.79

4.71

0.00

-4.71

315 320 325 330 335 340

27.40 - 35.74 mW/(mK)

%B D

8 -*- 340 355 370 385 400

36.80 - 67.20 mW/{rrvK)

7 8

' ft 400 438 476

5.75 i

0.00

514 552 590

67.50 - 94.40 mW/(m K)

"V

w

-5.75^

590 625 660 695 730

TEMPERATURE (K)

O- CLIFFORD ( 97) A - CRAVEN ( 77)

-)-- FLEETER t 60) X- GILMORE ( 38) O- KETES ( 89) V- LENEINORE ( 90) g]- LENG ( 91) X- LENOIR ( 92) ^- MILLHT ( 93) ©- PRRSRO ( 94) S- PRR5FI0 (2ND) ( 94)

ffl - RODER ( 95) 81- ROOER (2N01 ( 95) 0- TUFEU ( 96) #- TflKUSH ( 97)

Figure A13. Thermal conductivity at zero density. (Statistical comparisions begin on page 82.)

81
Figure A13. Thermal conductivity at zero density.

The comparisons are based on eq (11) , and data have been adjusted

(slightly) to zero density using the correlation of eq (14) as appropriate

Primary data were from Prasad [94] and Roder [95].

Statistical comparisons between tabulated (adjusted) values of the dilute

gas viscosity and values calculated from eq (11) are given.

Data from Clifford [87]

Number of Points: 1

AAD% = 3.09 BIAS% = -3.09 RMS% =0.00

AAD = 0.69 BIAS = -0.69 RMS = 0.00 mW.m" -K

_

Data from Craven [77]

Number of Points: 1

AAD% = 2.66 BIAS% = -2.66 RMS% =0.00

AAD = 0.72 BIAS = -0.72 RMS = 0.00 mW«m' »K~

Data from Fleeter [80]

Number of Points: 1 AAD% = 3.24 BIAS% = -3.24 RMS% = 0.00

AAD = 0.71 BIAS = -0.71 RMS = 0.00 mW.m" -K~

Data from Gilmore [88]

Number of Points: 2 AAD% = 0.75 BIAS% = 0.75 RMS% =0.31

AAD = 0.21 BIAS = 0.21 RMS = 0.08 mW.m" «K~

Data from Keyes [89]

Number of Points : 2 AAD% = 1.21 BIAS% = -1.21 RMS%

AAD = 0.32 BIAS -0.32 RMS = r - u -1 -1 = 0.27 mW«m «K

Data from Le Neindre [90]

Number of Points: 7 AAD% = 2.02 BIAS% = 1.32 RMS% =2.19

AAD = 1.43 BIAS = 1.25 RMS = 1.73 mW»m" •K"

Data from Leng [91]

Number of Points: 1 AAD% = 2.60 BIAS% = -2.60 RMS% =0.00

AAD = 0.71 BIAS = -0.71 RMS = 0.00 mW«m" «K~

Data from Lenoir [92]

Number of Points: 4

AAD% = 2.52 BIAS% = -2.52 RMS% =1.96

AAD = 0.64 BIAS = -0.64 RMS = 0.49 mW^m -K"

Data from Millat [93]

Number of Points: 4

AAD% = 3.57 BIAS% = -3.57 RMS% = 0.75

AAD = 1.17 BIAS = -1.17 RMS = 0.53 mW«m" «K~

82-
Data from Prasad [94'

Number of Points: 6

AAD% = 0.79 BIAS% = 49 RMS%

AAD = 0.27 BIAS 06 RMS

Weighted Data:

Number of Points : 5

AAD% = 0.65 BIAS% = 29 RMS%

AAD = 0.26 BIAS 01 RMS

°- 73

-1 -1

0.29 mW«m »K

°- 63

-1 -1

0.30 mW«m «K

Data from Roder [95]

Number of Points: 11

AAD% = 1.07 BIAS%

AAD = 0.18 BIAS

0.99 RMS%

0.16 RMS

°' 84

-1 -1

0.12 mW.m -K

Weighted Data:

Number of Points: 7 AAD% = 0.69 BIAS%

AAD = 0.12 BIAS

•0.55 RMS%

0.09 RMS

°- 53

-1 -1

0.09 mW^m «K

Data from Tufeu [96]

Number of Points: 7 AAD% = 1.71 BIAS%

AAD = 0.58 BIAS

0.30 RMS% = 1.85

0.12 RMS = 0.77 mW.m «K

Data from Yakush [97]

Number of Points: 7 AAD% = 3.17 BIAS%

AAD = 1.42 BIAS

0.32 RMS% = 3.59 .. 0.69 RMS = 1.70 mW^m" »K~

-83
>-

CO

O

o

>

o

>

LUQ

1.52

0.00

-1.52

1.11 0.00

-1.11

1.1-

0.0

-1.1

0.54

0.00

-0.54

1.44

0.00

-1.44

2.74

0.00

-2.74

1.61 0.00

-1.61

95.00 - 100.00 K

X

X

X x

A X

X V

21.25

1 ,(V 1 1 1 I 21.50 21 100.00 - 110.00 K

-a-

-x-x

~&* $~

X x X

-1 1 T" 21 21.25

110.00 - 111.10 K

21.50

X

-X- X X x

X

-$-, 1 X- X

20.75 21 21.25

111.40 - 120.00 K

x X* X

X

-&- -,

, 1 1 r 20.75 21 21.25

120.00 126.80 K ^*

x

x

x x

x

x

20.25 20.50

~\ 1 1 1 1 r 20.76 21

1.14 0.00

-1.14

2.8

0.0

-2.8

19.32

0.00

19.32

2.02

0.00

-2.02

1.14 0.00

-1.14

150.00 K x

x v X x x

)( . x ,1

| X x_

' r- 19.25 19.50 19.75 20

150.30 - 166.80 K

x x

18.75 —

|

1 1 1 1

1 r—

19 19.25 19.50

167.30 - 190.00 K

-©-

_X_ _X X- ^r-_&_

17.75 19

193.15 - 200.00 K

-ax xx

x

_X- J*L

17.5 18.5

200.00 - 213.15 K

-x- -x- x Q- -y: -X- o

X

127.20 - 130.00 K

-e

16.75 17.75

215.00 - 240.00 K

x X

X

~x- x X X

r " i 11 i

1 r r 20.25 20.50 20.75

130.00 - 149.50 K

4.59- ffi

n nn X X X

X x > u.uu

-4.59-—1—1—1- ,

1

1 1 1 1

1

'

1 1 T

X

-$- X

x-x

,x x_

1.63

0.00

-1.63

15.25 15.75 16.25 16.75

243.40 - 250.00 K

x

X

"X" ^X.

_X19.25 20.50 15 18.75

3i

DENSITY (mol/dmJ

) DENSITY (mol/dm*)

X- OILLER

<£ - GERF

( 99) (101) X- OILLER I 99) O- OILLER (2ND) I 99) <£- GERF 1101) ©- GERF (102) 0- SWIFT (105) • • VAN ITTERBEEK (106)

Figure A14. Viscosity at elevated pressures. (Statistical comparisions begin on page 94.)

84 -
>-

t

GO

O

CO

>

o

>

LUQ

1.07

0.00

-1.07

0.44

0.00

-0.44

0.76

0.00

-0.76

2.79

0.00

-2.79

7.35

0.00

-7.35

0.86

0.00

-0.86

4.74

0.00

-4.74

250.00 - 265.00 K

a

J*L X —x TM—x

x x x

-I 1 1 13.75 14.75 15.75

270.00 - 290.00 K

-* x

x

l l

1

1 l

1 1 1

1

i 12.25 13.25 14.25

290.00 K * ~x

15.25

x x

>< V X

X

-X.

1 1 1 1 1

1

1 r 11.50 13.25

290.00 K

2.35

0.00

-2.35

5.35

0.00

-5.36

2.62

0.00

-2.62

294.60 - •w . .. 298.15 K

1 ^ x '

—

|

1 1 1

1 16.25

298.15 K

0.50 1.25 2 2.75

298.15 - 299.82 K

-a- i.

£

15

oo

CO*

10.5 11.5 299.82 K

1.33 -r^ a

12.5

i

;

1 1 1 r 0.25 6 11.75

290.00 - 294.26 K

m_

-EB- E3

<fc>

i

1 1 1 [

1 1 1 1 1 1 r 0.25 5 9.75 14.50

294.26 K *

0.00

-1.33

0.73

0.00

-0.73

-A&A —i—i—i—|—i—i—i—i—]—i

10 11.75 13.50

299.82 K

15.25

A

A

-*- X

:< n 1 r i

1 r 12 13.75 15.50

294.26 - 294.60 K

12 12.75 13.50 14.25

299.82 - 301.85 K

0.00-^

-1.43

-*- V R

X

6.09

0.00

-6.09

10.25

301.85 - 303.12 K

13.50 16.75 9.50 9.75

DENSITY (mol/dm3

) DENSITY (mol/dm3

) X- OILLER t 99) O- OILLER (2N0) ( 99) V- OIILER (100) X- EflKtN t 79) a- SMITH (103) 0- SUIFT (105)

A- CRRMICHfiEL ( 76) X- OILLER ( 99) V- OILLER (100) 2- IHflSflKI ( 81) gl- STRUMPF (1041 Q- SHIFT (105)

Figure A14. (continued)

-85
9.44

0.00

-9.44

0.56

0.00

-0.56

303.15 - 305.37 K

-ffi-

-8- _0_

C QQ 305.64 - 305.65 K

571 &$&

Off 1 u.uu 6.98- , , ! , 13.75 7.25

305.37 K

A

A ,.

—r- i |

i i i i i r A 1

R R 305.65 K

D.D

ft ft a s a ax a XX SS ASS M

U.U

-5.5- i | , 1 >-

!— 0.62-fr

3 6

305.37 K

12

CO

O 0.00

o -0.62

CO

>

5.05

z

0.00

z -6.05

o

<

2.18

> 0.00

LU -2.18

^7

tr-fr

0.75 10

305.37 - 305.39 K

_S si

n r- -*- 2.50 7.25

305.39 - 305.41 K

4.33

0.00

-4.33

7.92

0.00

-7.92

6.50 6.75 7 7.25

305.41 - 305.44 K

~1 1 1-

4.99

0.00

-4.99

16.12

0.00

-16.12

25.43

0.00

-25.43

27.27

0.00

1.25 2 2.75

305.65 K

3.50

_aw

3.50 5.25

305.65 K

"H W] —

1

1 1

1 r 6 5.25

305.65 K

5.50

6.25 5.50

305.65 K

~E"

6.50 8.75 7 7.25

306.44 - 305.64 K

-27.27+-MZH 8 |—r^n—,—|

r 5.25 6.25 7.25

305.65 K

8.25

2.05

0.00

-2.06

TT

6.50 9.25

1 1 1 1 1 1 1

1

1 1 1 r~ 8.25 8.75 9.25 9.75

3i

DENSITY (mol/drri ) DENSITY (mol/dm

J

)

A- CflRMICHAEl ( 76) + - CflRMICHBEL (2N0) ( 76)

ffl- SMITH (103) gj- STRUMPF

1 (104) -shift (los)

H- IW6SFIKI S3- STRUMPF

( 81) (104!

Figure A14. (continued)

86 -
CO

O

o

>

<

>

LU

Q

8.88

0.00

-888

5.26

0.00

-6.26

5.0

0.0

-5.0

16.96

0.00

-16.96

22.36

0.00

•22.36

3.09

0.00

-3.09

10.42

0.00

-10.42

305.65 - 305.85 K

M

O Oft 306.14 - 306.15 <

s.ZO Wl ^2&B

m

U.LKJ

-9.26-. , ,

,

, 10.25 7.25

305.85 K

7 rciff 2 S"

-i 1 r- 0.5 1.5 305.85 K

—

|

1 1 r 2.5 3.5

H

3.75 5.50

305.85 K

5.25 5.50

305.85 K

5.75

5.50 5.75

305.86 K

6 6.

& ffi u

-8 1 1 1

5.3

0.0

-5.3

6.53

0.00

-6.53

15.9

0.0

-15.9

16.5

0.0

-16.5

1.85

306.15 K

-l 1 1

1

1 1 1

1 r 1.75 2.75 3.76

306.15 K

4.75

-B-ffi4.75 5.75

306.15 K

-i 1 1- ^

?_

5.50 5.75

306.15 K

ass—s_

5.75 8.50

306.15 K

0.004

-1.85

305.85 - 306.14 K

SI SI EI El WVYWYyVVW

i i | i i i ,

4.34

0.00

-4.34

i—i 1 1

1

; 1 1 1

1

1 1 1 r 8.5 9 9.5 10

306.15 - 306.45 <

-i—i—i—i- 6.50 8.25 10

3

8 10

DENSITY (mol/drn ) DENSITY (mol/drri )

IWflSRKI 5TRUHPF

( 81) (104) 2- IWflSRKI g] - STRUnPF

( 811 (104)

Figure A14. (continued)

87
CO

O

o

en

>

O

<

>

LUQ

5.1

0.0

-5.1

12.79

0.00

-12.79

22.36

0.00

22.36

3.07

0.00

-3.07

12.62

0.00

-12.62

11.24

0.00

-11.24

5.04

0.00

-5.04

306.45 K

4.75

306.45 K

-2 g- -s4.75 5 6.25

306.45 K

3.68

0.00

-3.58

4.63

0.00

-4.63

308.15 K

~2"

-2-S

6.25

308.15 K

^gsaas , g—?-

5.50 6.25

1 K 308.15 K

1 .0 n ffi a a s a 2

U.U

-1.5-

2

r i i | .... | ... . 5.25 5.50

306.45 K

5.75 8 8.5 9 9.5

308.15 - 310.93 K

6.29 -a

8.25 9.25

306.45 - 308.14 K

fflfflfflXX

—1 1 1

1

1 1 1

1

6.50 8.25 10

308.14 - 308.15 K

-i—i—i i 3.25 6.50

308.15 K

,g ffl ffl 2—S ffi—

9.75

0.00

-6.29

2.44

0.00

-2.44

2.15

0.00

-2.16

0.77

0.00

-0.77

1

1 1 1 1 1

1 1 1 1

1 r 9.50 11.25 13

310.93 K

14.75

4

&—i

1 1 1 r 10.25 11.76

310.93 K

13.25 14.75

AAA

fr

0.75 3.75

310.93 K

6.75 9.75

_A_

5.25

-i—i—i—|—i—i—i—|

1 2

"i 1 CT"] 1 r— 3

DENSITY (mol/dm3

) DENSITY (mol/dm3

)

I- STRUtlPF

( 81)

(104) A" CflRniCHREL

ffi- IWflSRKI gl- STRUMPF

1 76)

( 81)

1104)

Figure A14. (continued)

88
>-

t

CO

O

o

>

O

<

>

LU

Q

2.86

0.00

-2.86

4.06

0.00

-4.06

0.38

0.00

-0.38

13.45

0.00

13.45

13.91

0.00

-13.91

13.85

0.00

13.85

14.28

0.00

•14.28

310.93 K A

A

A |

i A

2.5 9

o r>7 319.17 - 319.64 K

z. u / V V

u.uu

-2.07- i I 1

i r 1 Vr- i

310.93 K

-x- XXX X

X

A

"ZT A

1.81 0.00

-1.81

1.75 6.25 10.75 15.25

319.64 - 320.00 K

^X~x?

0.25 2.75

310.93 K

5.25 7.75

X X

0.50

320.00 K

1.46 -X X

14.25

! i i i

I ' ' 'I

' ' '

I "' 'I

' ' 10.231.25 12.25 13.25 14.25 15.25

310.93 - 313.64 K

6.50 9.75 13 16.25

313.65 - 316.47 K

ia ^a

0.00

-1.46

3.4

0.0

-3.4

15.53

x

X

xX X

-X- 4.50 10.25

320.00 K

^x

X

X

o ,° 8 —

e

£ 1 1 1 0.75 4

320.00 - 323.15 K 8* ffl- E3

15.53

6.50 9.75 13

&aa316.48 - 319.14 K

-£—

s

v—vi—'—>—i—'—'—i—'

r_ 6.50 8.75 11 13.25

319.14 - 319.17 K

"3 A — 323.15 K XKt o.4 - sss a s ffi u.u 3.4-—i—i—i—i—|—i—i—i—i—j—i—i—i—i

-EL_5L E

"TXT

-i 1 1 r- 2.50 —

i

'—'

<- 8.75

4.41

0.00

-4.41

0.5

323.15 K

1.5

T&—ff

-i 1 i 1- 15 1.50 3.25

DENSITY (mol/dm3

) DENSITY (mol/dm ) A- CflRMICHflEL ( 76) V-OILLER (100) H- OILLER (2N0) (100) X- EflKIN ( 79) ia-5TRUI1PF (104)

X- OILLER ( 99) O- OILLER (2N0) ( 99) V-OILLER (100) H- IHfiSHKI ( 81) S- SMITH (103}

8-STRUMPF (104)

Figure A14. (continued)

-89
t

CO

O

o

C/)

>

<

>

LU

Q

3.38

0.00

-3.38

323.15 K

-i 1 1 r

2.4 -S

0.0

-2.4

5.25 5.75

323.15 K

6.25 8.75

1.27

0.00

-1.27

0.31

0.00

327.59 - 344.26 K

ti x X * x

—I

1 1 1

1 r 13.50 14.75

344.26 K

-I 1 r- 16

A

-At

6.75 7.25 7.75 8.25

323.15 - 324.82 K

3.11 -m—e——

-0.31 -£—>—i

1 1 [-

10.25 12 344.26 K

13.75

0.00 o$

JD_ 3.1H ' ' 0.25 4.75 9.25 13.75

324.82 - 327.59 K

6.7

0.0

-6.7

2.49

0.00

-2.49

1.69

0.00

-1.69

,c e

-fr

1

1 1 1 1 r 9 12.25

327.59 K

h

0.48

0.00

-0.48

0.94

-a- t

8.25 12.50

0.00^

-0.94

344.26 K

-A AA

-A-

~i 1 1 r- 15.50 1.5 8.5

& A

' ' i' ' '

i

' > '

i

' ' '

i

'

' 4.5 5.5 6.5 7.5 8.5 9.5

327.59 K

XX

—i

1 g i

1

1.54

0.00

-1.54

2.26

344.26 K

J* X_

£x x

X

-x-

-i r~ n 1 r

-

1 344.26 K

X0.00^

-2.26

-X-

-X = 2—

2.63-r^

X X

0.00

0.25 1.75

327.59 K

3.25 4.75

-2.63

X

X A X X*

2.08

0.00

-2.08

2.75 15

344.26 - 348.15 K

14.25

n 1 1 1

1

1 1- 7.75 15.50

3i

DENSITY (mol/drri ) DENSITY (mol/dmJ

) O- BfiRON ( 98) A" CFIRMICHAEL ( 76) X- ERKIN t 79) 2- (WRSRKi ( 81)

A- CRRtllCHflEL X- EflKIN 2- lyflSflKi

( 76)

( 79)

I 81)

Figure A14. (continued)

90
>-

t

CO

O

CJ

to

>

O

I-

<

>

LUO

3.2

0.0

-3.2

3.8

0.0

-3.8

3.6

0.0

-3.6

348.15 K

"S 8-

0.75 1.50

348.15 K

2.25 3

-s

a a a s

1.53

0.00

-1.53

1.03

X

377.59 K

-* r

a- &

377.59 K

o.oo r* x

-1.03

10.25

^*5

X

X

3.25 6.50

348.15 K

6.50 8.25

348.15 - 352.59 K

O %%$&? u.uu

3.24- 1 1 o

i —i

1 1—

1.98

0.00

-1.98

1.47

4.75

352.59 - 360.93 K

9.50

-Q

9?x O

-9^

14.75

o.oo-fc-

-1.47

360.93 K -x X* X X*>:

X

1.45

0.00

-1.45

1.25 13.50

360.93 - 377.59 K

X X g-M

A-

•

i

' I' ' '

I

' ' '

I

' ' 10 11 12 13 14 15

DENSITY (mol/dm

3

) O- BflRON ( 98) A- CRRniCHAEL ( 76) X- EFIKIN t 79) 2- [WflSAKI ( 81)

2.21

0.00

-2.21

1.95

0.00

-1.95

1.37

0.00

-1.37

2.89

0.00

-2.89

2.07

0.00

-2.07

0.252.25 4.25 6.25 8.25 10.25

377.59 - 380.37 K

Z>0

-X- ?1

O

14.75

380.37 - 381.66 K

o

U

-O-i i Q i Q

7.25 9.50

394.26 K

11.75 14

-Xi X

*XX~ X

-1 1 1

1 1

1

1 1

2.25 4.50 6.75

394.26 - 399.54 K

r-7 XX

x x x x*

7

2.50 14.25

399.60 - 399.76 K

tr

-S^T" 5.75 10.50

3i

DENSITY (mol/dm ) O- BARON A" CARMICHAEL V-OILLER X-DWIN

I 98)

( 76)

(100)

( 79)

Figure A14. (continued)

91
t

CO

O

(J

>

O

<

>LLI Q

0.95

0.00

-0.95

2.01

0.00

-2.01

0.78

0.00

-0.78

399.79 - 399.93 K

v

-9r- V

10.25 11.25 12.25 13.25

399.95 - 408.15 K

-Q

v o

e ^r

o-1—'

-i r i

| r- 3 6 9 12

408.15 - 410.93 K

1.93

0.00

-1.93

3.32

0.00

-3.32

444.26 K

H

x

$#f -i—i—i i 0.25 7.25

444.26 477.59 K^ >< *

x

8.75 13

A

-r-A- i i

O 1 477.59 K

Z. la £

4 u.uu

-2.19-

^ i i i

i i i

i

i r 1.75 8.75

O f\ 410.93 K

z.u X

A

U.U

-2.0-

^ A

i i

l

i i 1

1 A

1.43

3.75

410.93 K

^T

7.50 —&—

11.25

0.00-p*

-1.43

2.92

0.00

-2.92

1.15

i—|—i—i—i—i—|—i—r- 0.25 3 5.75 8.50

410.93 - 444.26 K

3.08

0.00

-3.08

2.48

0.00

-2.48

2 4 6

477.59 K

w

-i 1 r Ai i r 3.25

477.59 K

-X- X x

6.50

X* -i—I—i—i—i |

i—

1.6 3.5 5.5 7.5 9.5 11.5 477.59 - 499.63 K

X X

~K~* -x

—i—i—

]—i—i—i—I—i—i—i—

|—i i i—I—i—i—r~ 8.75 9.75 10.75 11.75 12.75 13.75

444.26 K

3.17-

V *

V v v v ,y —*-*

U.UU

-3.17- r 1 1 1

0.00-^

1.15

-a1.3-i-V

V

6.25 12.50

499.63 - 500.10 K

7

0.0

-1.3

V

V

^T

1.50 5.75

DENSITY (mol/dm 3

) DENSITY (mol/dm

3

) O- SflRON ( 98) A- CflRtllCHREL ( 76) + - CRRMICHfiEL (2ND) ( 76) V- OILLER (100) X- EPIKCN ( 79)

A- CflRtllCHAEL ( 76) V-DILLER 1100) X- ERKIN 1 79)

Figure A14. (continued)

-92
>-

t

CO

O

CJ

C/) 3.36

^

0.00

5 -3.36

<

>

LU

Q

O ip 500.12 - 510.93 K

J . 1 o E! X

J.UU

3.18-

X *.1 X X Xi x * —510.93 K * x

X X

2.75

X XX*

T

1 1 1 1 1 1 1- 3.50 6.25

1—'—'—'r_ 9 11.75

3- DENSITY (mol/dmJ

) H- OILLER (2N0) (100) X- EflKIN ( 79)

Figure A14. (continued)

-93
Figure A14. Viscosity at elevated pressures.

The comparisons are based on eqs (7), (9), and (13). Primary data were from Carmichael [76] and Diller [99,100].

Statistical comparisons between tabulated values of the viscosity and

values calculated from eqs (7), (9), and (13) are given.

Data from Baron [98]

Number of Points: 40

Comparisons based on experimental pressures:

AAD% = 1.85 BIAS% = 0.71 RMS% = 2.19

AAD = 0.88 BIAS = 0.44 RMS = 1.34 /iPa»s

Comparisons based on experimental densities:

AAD% = 1.73 BIAS% = 0.39 RMS% = 2.07

AAD = 0.80 BIAS = 0.23 RMS = 1.22 /zPa»s

Data from Carmichael [76]

Comparisons based on experimental pressures:

Number of Points: 226

AAD% = 0.81 BIAS% = -0.07 RMS% = 1.14

AAD = 0.21 BIAS = -0.01 RMS = 0.31 ^Pa«s

Weighted Data:

Number of Points: 222

AAD% = 0.76 BIAS% = -0.02 RMS% = 1.01

AAD = 0.20 BIAS = 0.00 RMS =0.30 /iPa«s

Data from Diller [99]

Number of Points: 164

Comparisons based on experimental pressures:

AAD% = 0.84 BIAS% = -0.17 RMS% = AAD = 1.84 BIAS = 0.02 RMS

Comparisons based on experimental densities

AAD% = 0.87 BIAS% = -0.09 RMS% = AAD = 1.85 BIAS = 0.24 RMS

Weighted Data:

Number of Points: 144

Comparisons based on experimental pressures:

AAD% = 0.69 BIAS% = -0.02 RMS% = 0.84

AAD = 1.93 BIAS = -0.10 RMS = 3.18 /iPa«s

Comparisons based on experimental densities:

AAD% = 0.73 BIAS% = 0.06 RMS% = 0.88

AAD = 1.94 BIAS = 0.15 RMS = 3.20 /xPa«s

Data from Diller [100]

Number of Points: 76

Comparisons based on experimental pressures:

AAD% = 0.96 BIAS% = 0.11 RMS% = 1.23

AAD = 0.34 BIAS = 0.02 RMS = 0.53 /xPa«s

Comparisons based on experimental densities:

AAD% = 1.02 BIAS% = 0.07 RMS% = 1.30

AAD = 0.37 BIAS = 0.00 RMS = 0.58 /zPa«s

1 05

3 40 /uPa« s

1 09

3 39 ^iPa« s

94
Weighted Data:

Number of Points: 72

Comparisons based on experimental pressures:

AAD% = 0.83 BIAS% = 0.03 RMS% = 1.00

AAD = 0.30 BIAS = -0.03 RMS = 0.42 /xPa«s

Comparisons based on experimental densities:

AAD% = 0.89 BIAS% = -0.01 RMS% = 1.07

AAD = 0.33 BIAS = -0.04 RMS = 0.46 /iPa»s

Data from Eakin [79]

Number of Points: 198

Comparisons based on experimental pressures:

AAD% = 1.33 BIAS% = 0.69 RMS% = 1.61

AAD = 0.53 BIAS = 0.41 RMS = 0.77 /iPa-s

Comparisons based on experimental densities:

AAD% = 1.07 BIAS% = 0.41 RMS% = 1.46

AAD = 0.36 BIAS = 0.22 RMS = 0.61 /iPa»s

Data from Gerf [101]

Number of Points: 20

Comparisons based on experimental pressures:

AAD% = 2.13 BIAS% = 0.95 RMS% = 2.46

AAD = 10.00 BIAS = 3.29 RMS = 14.03 ^Pa»s

Comparisons based on experimental densities:

AAD% = 21.17 BIAS% = -18.84 RMS% = 39.44

AAD = 51.25 BIAS = -39.63 RMS =87.70 ^Pa-s

Data from Gerf [102]

Number of Points: 11

Comparisons based on experimental pressures:

AAD% = 11.24 BIAS% = 5.34 RMS% = 11.57

AAD = 11.36 BIAS = 7.80 RMS -11.61 /iPa»s

Comparisons based on experimental densities:

AAD% = 11.43 BIAS% = 5.58 RMS% = 11.64

AAD = 11.55 BIAS = 8.03 RMS = 11.69 /iPa»s

Data from Iwasaki [81]

Number of Points: 402

Comparisons based on experimental pressures:

AAD% = 5.64 BIAS% = -2.03 RMS% = 8.30

AAD = 1.15 BIAS = -0.60 RMS = 1.84 /xPa»s

Comparisons based on experimental densities:

AAD% = 2.42 BIAS% = 2.12 RMS% = 1.89

AAD = 0.40 BIAS = 0.33 RMS = 0.30 /iPa»s

Data from Smith [103]

Number of Points: 15

Comparisons based on experimental pressures:

AAD% = 11.40 BIAS% = 11.13 RMS% = 6.39

AAD = 3.74 BIAS = 3.70 RMS = 2.00 ^Pa»s

Comparisons based on experimental densities:

AAD% = 11.46 BIAS% = 11.23 RMS% = 6.43

AAD = 3.75 BIAS = 3.72 RMS =2.01 /iPa»s

-95-
Data from Strumpf [104]

Number of Points: 105

Comparisons based on experimental densities:

AAD% = 7.35 BIAS% = 7.15 RMS% = 4.65

AAD = 1.63 BIAS = 1.59 RMS = 0.94 /iPa»s

Data from Swift [105]

Number of Points: 14

Comparisons based on experimental pressures:

AAD% = 1.82 BIAS% = 1.27 RMS% = 1.67

AAD = 1.46 BIAS = 1.17 RMS = 1.83 /iPa-s

Comparisons based on experimental densities:

AAD% = 6.62 BIAS% = -3.31 RMS% = 18.21

AAD = 3.04 BIAS = -0.06 RMS = 6.11 /iPa»s

Data from Van Itterbeek [106]

Number of Points: 8

Comparisons based on experimental pressures:

AAD% = 11.52 BIAS% = 11.52 RMS% = 3.32

AAD = 28.76 BIAS = 28.76 RMS = 5.02 /xPa*s

Comparisons based on experimental densities:

AAD% = 10.25 BIAS% = 10.25 RMS% = 4.57

AAD = 26.05 BIAS = 26.05 RMS = 9.47 /zPa«s

96
>-

t

>

Io

Z)Q

z

o

CJ

cc

LU

o

I-

<

>

LU

Q

0.83 o.oo

-0.83

0.91

0.00

-0.91

0.7

0.0

-0.7

0.58

0.00

-0.58

t

0.78

0.00

-0.78

0.81

0.00

111.68 - 111.98 K

® S

-H20.75 21.75

112.02 - 112.29 K

zs _0_

20.75 21.75

112.37 - 134.23 K

B__esL_g

a

Q

20 20.5 21

134.25 - 134.71 K

21.5

rS- 20 21.25

134.74 - 155.13 K

-SB-

§

a Q

19.25 20.25 21.25

155.26 - 155.63 K

0.81 -p M ,-Ses a

0.77

0.00

19.25 20.50

155.64 - 156.17 K

0.77-13 S0.68

0.00

-0.68

0.43

0.00

-0.43

0.45

0.00

-0.45

0.36

0.00

-0.36

0.36

0.00

-0.36

0.42

0.00

-0.42

0.48

0.00

-0.48

156.2 4 - 174.71 K

fXl rm 3 g

« " " —a 1

z

18.50 20.25

174.73 - 175.30 K

-a- M.

-i 1 1 1 r~ ~i 1 r- 18.5 19 19.5 20

175.34 - 194.30 K

tS—

i

1 r 17.50 18.75 20

194.35 - 194.64 K

-a-

"0"

17.5 18.5 19.5

194.64 - 195.05 K

a

-B- -0_

21 0~

^-&h—

?

17.5 18.5

195.10 - 195.46 K

19.5

-B- _0 0_

tS 0"

1 1 1

1

1 r—

17.5 18.5

195.49 - 214.27 K

H19.5

-0_

VT -H19.25 20.50

DENSITY (mol/dm3

)

RODER (111)

16.75 19.50

DENSITY (mol/dm

3

)

0- ROOER (111)

Figure A15. Thermal conductivity at elevated pressures. (Statistical compariaiona begin on page 109.)

97
0.41

0.00

-0.41

>-

0.42

> 0.00

h- -0.42

o

Z)Q 2.52

Z 0.00

o

CJ -2.52

cc

LUX

o

>

LU

Q

214.33 - 214.92 K

_0_

a

1.36

0.00

246.12 - 253.19 K

-s

16.75 17.50 18.25 19

214.93 - 215.64 K

-a- -0

1.36 -B .

1 1

17.75

253.20 - 253.73 K

Q

1.62

0.00

-1.62

1.92

0.00

-1.92

1.7

0.0

-1.7

1.4

0.0

-1.4

-l r-

—I

1

1 1 1 1

1 r— 16.75 17.50 18.25 19

223.60 - 233.47 K

0.00 0.25 0.50

233.53 - 234.69 K

18.25

234.80 - 235.39 K

18.25

235.41 - 243.47 K

18.25

243.57 - 245.88 K

—i i E3 1 o 1 i

1

i

0.00 0.25 0.50

DENSITY (mol/dm3

) 0- ROOER till)

1.06

0.00

-1.06

0.9

0.0

-0.9

1.0

0.0

-1.0

0.54

0.00

-0.54

1.07

0.00

-1.07

0.97

0.00

-0.97

-H- m

17.75

253.86 - 254.40 K

-0

s- $

0.25 9 17.75

254.45 - 263.14 K

-0

1 1

1

1

1 1 1 1

1

1 1 1 r 5 10 15

263.26 - 264.35 K

-0—Ba

264.62 - 273.27 K

-0

_0_ q a

-0- a

273.37 - 274.24 K

-0

13.75

3< DENSITY (mol/dm

J

) 0- ROOER (111)

Figure A15. (continued)

-98
>-

t

>

I-

(J3

QZ

o

o

LU

1.06

0.00

-1.06

0.99

0.00

-0.99

1.26

0.00

-1.26

2.61

0.00

-2.61

4.57

0.00

-4.57

274.30 - 274.80 KTT1

,¥

a

4

1 | 1 . . | 1 1 , 8 12 1(

1.51 s- o.oo m n

-1.51

293.47 - 293.74 K

i—i—i—

274.96 - 275.29 K

a

*5

e*%i

-i 1 1 1 1 1 r~ ir~ 5.75 11.50 17.25

275.33 - 276.11 K

-B-, #

1.03

0.00

-1.03

1.82

1 1 1 1 1

1 1 1 r 4.75 9.50 14.25

293.75 - 294.08 K

er

E3

14.75

294.12 - 294.25 K

0.00 HSZS -1.82

JZ3-

t 1 1 r 0.25 17.25

276.14 - 277.59 K

Q 22ZZI

9- -I 1 1 1 1 r- 5.75 11.50 17.25

277.59 - 284.05 K

o

<

0.8

> 0.0

LU

Q

-0.8

1.54

0.00

-1.54

o

-l 1 1 [

1 1 1

1

1 1 1

1

1 1 r- 4 8 12 16

284.07 - 285.41 K

"0"

-H41

1.75

285.52 293.44 K —ffl

73 £L M.

-i r4.26

0.00

-4.26

2.86

0.00

-2.86

2.18

0.00

-2.18

2.85

0.00

-2.85

2 9.25 16.50

294.25 - 294.37 K

16.75

294.37 - 294.56 K

_0j3_ZI

0.50 16.75

294.58 - 294.72 K

i—i—i—|—i—i—i—|—i—i—i—|~rrr-^—

r

4 8 12 16

294.72 - 294.97 K

ffl

IS H ®® l \

1.75 0.50 18.75

DENSITY (mol/dm 3

) DENSITY (mol/dm

3

) O- CRRHRCHflEL (107)

ffl- PRA5TO ( 94) Q- ROGER (111)

ffl- PRASflO Q- ROOER

( 94) (HI)

Figure A15. (continued)

99
0.76

0.00

294.98 - 295.24 K

e- __ -ei -0.76^

>

o

3

QZ

o

UJ

1.82

0.00

-1.82

7.75 15.50

295.28 - 295.41 <

3.07

0.00

-3.07

10.82

304.13 - 304.85 K

tt a "S 0~

rS- 00 " Qi

1 1 1

1

1 r— 1.25 2.50

304.91 - 305.45 K

t

1—i—|

1—i1—|—i—i—

r

4 8 12 16

295.43 - 295.78 K

0.88 -Hftj

0.00 123330 Q

10.82

0.00

-0.88

-a- 00 i\

1.34 -gg- 0.00-j H-

-1.34 -J

i

1 1 1

1

1 1 1 1 1 1 1 1 r 0.25 5.75 11.25 16.75

295.81 - 296.23 K

12.75

o.oo12.75

1 1 1 1

1

1 1 1 1

1

1 rx* r 2.75 5.50 8.25

305.46 - 305.47 K

-©-

-s

rfi

<

>

LU

Q

0.76

0.00

-0.76

2.96

0.00

-2.96

2.71

0.00

-2.71

16.75

296.26 - 300.94 K

IS 21

0.25 5.50 10.75 16

300.94 - 302.97 K

-aI 4- + ,t ±

+ +

1.25

303.24 - 304.07 K , Q

-i 1 r15.9

0.0

-15.9

14.22

0.00

14.22

5.45

0.00

-5.45

3.48

Till [

1 1 1 r 4 6.75 9.50 12.25

305.48 - 305.57 K

a gff

JE

1.50 3.75 6 8.25

305.57 - 305.59 K

fL w e

"l 1 r- -©- 4 7.25 10.50

305.61 - 305.91 K

aW a s

i—i—i—| , i i -©- |i i—i—|- 0.25 2.25 4.25 6.25 8.25

305.92 - 305.98 K

—|

1 1 ! rfi 1.25 2.50

3

0.00-$

-3.48

A.

i

1 1 r 0.75

I

i (D 4 J 7.25 10.50

3i

DENSITY (mol/dmJ

) DENSITY (mol/dm

J

) + - FLEETER

ffl- PRH5RD 0- ROOER

( 80)

( 94) (111)

©-H05TERT

2- MOSTERT 0- RODER

(109)

(110)

(111)

Figure A15. (continued)

100
2.79

0.00

-2.79

4.44

> 0.00

1- -4.44

(J

Z>

Q 3.51

Z 0.00

o

o -3.51

306.01 - 306.96 K

0.50 9.25

306.96 - 307.05 K

-W

i 1 1

1 fly*-^—

1

1 1 1

1

1 1 r 0.75 4.75 8.75 12.75 18.75

307.05 - 307.59 K

^7"-

<> V

-B5.11 0.00

-5.11

4.19

0.00

-4.19

6.37

308.73 - 308.87 K

<K

-&-

A

i

1 1 1 1 r 0.25 7.25 14.25

308.99 - 310.93 K

AAAAA

a

^/W

4.5 9 13.5

310.93 - 311.33 K

cc

LL1

X

o

<

>

LU

Q

2.86

0.00

-2.86

5.9

0.0

-5.9

11.82

1 1 1 (ill—

0.50 8.25 16

307.60 - 307.69 K

O.OOi

-6.37

-e- XT AA

_A_

—I

1

]

1 1 1

1 1 1.25 5.75 10.25 14.75

311.33 - 311.44 K

2.5 -fr-%

T* 1 1 1

1

1 , 1—

0.25 1.25 2.25

307.71 - 308.02 K

-©-

-i— -©r- i—|—i—i

h="—'—

0.25 3.25 6.25 9.25 12.26

308.02 - 308.16 K

0.00-L^

8 s

11.82 -l 1 1 1 1 1-

0.0

-2.5

5.82

0.00

-5.82

6.24

.A. Q

&-

4.50 10.25

311.46 - 311.72 K

lAA A A

—I

1 I

1

1

1 1 2.25 5.50

311.75 • 311.91 K •

8.75

0.00#

-6.24

a

o g es

-i—i i

3.1

0.0

-3.1

0.25 5.25 10.25 15.25

308.35 - 308.73 K

^A—r-A 1

1 1 1 1 1 1

1 1 1 r 7.5 10 12.5 15

DENSITY (mol/dm3

)

2.96

0.00

-2.96

—

1 1 1 i 3 6.25

311.91 - 312.00 K

9.50

IS

-i 1 11 1 1 r 3.25 5.25 7.25 9.25

DENSITY (mol/dm3

) A - DESMflREST V- LENEINORE <£- MILIAT

ffi - flOSTERT H- MOSTERT 0- ROOER O- TUFEU

(108)

I 90)

( 93) (109)

(110) (111)

( 96)

O " CflRDfiCHFIEL A-OESMflREST V- LENEINORE ©- I10STERT H- MOSTERT 0- ROOER

(107)

(108)

( 90)

1109)

(110) (111) #• ROOER (2ND) (111) O- TUFEU ( 96)

Figure A15. (continued)

101
A RO 312.01 - 312.09 K

4.DO w

u.uu -«

-4.58- t :! I I |

I I I I |I I 'r' i

6.13

312.99 - 313.05 K

0.00-p

-6.13

-a-*vt 00 21

t

>

(J

Z>

Q

Z

o

(J

LU

O

h-

<

>

LU

Q

3.99

0.00

-399

3.26

0.00

-3.26

6.82

0.00

-6.82

6.67

0.00

-6.67

6.79

0.00

-6.79

6.94

0.00

-6.94

0.75 4 7.25 10.50

312.10 - 312.36 K

Q-er -%- ~

Bg^

5.43

0.25 11 313.05 - 313.22 K

000 ^ m

-5.43

2

2.75 6 9.25

312.38 - 312.49 K

s

Q

-B-H- -a h-

-a 0.25 4.50 8.75

312.50 - 312.55 K

a

$ 0~~ Q • h

-

l

1 1 1

]

1

I r^-T—

0.25 3.50 6.75 10

312.56 - 312.67 K

iS- B-

-i 1- 0.75 9.50

312.69 - 312.86 K

IT -Q7.75

312.87 - 312.98 K

(3 q0 FJ

ei

5.92

0.00

-5.92

3.43

0.00

-3.43

5.59

0.00

-5.59

1.91 0.00

-1.91

2.11 0.00

-2.11

0.25 3.25 6.25 9.25

313.24 - 313.35 K

TT ~0~ o» *+- q0 B

0.75 10

313.38 - 313.74 K

a

3 00 Q l\

5.75 11.50

313.75 - 314.02 K

SB

—i 1 1 1- -[-St

iqT3 n El

0.75 8.50 16.25

314.06 - 314.38 K

&%® m

0Q_ i1

[

1 1 1 1

1

1 1 1 r

1 6 11 16

314.44 - 314.63 K

G9 B

Q0

03 i ] S- -H- 1.50 9.25

DENSITY (mol/dm3

) ©-H0STERT (109) 0- RODER (111) • - ROGER (2N0) (111)

16.25

DENSITY (mol/dm3

)

EH- PRflSHO I 94) 0- ROOER 11111 • - RODER (2N0) (111) O - TUFEU I 96

Figure A15. (continued)

102 -
314.63 - 314.80 K •

'

' l T T£J- 1

1 1

>

f-

(J3

Q

Z

o

o

LU

o

>

LU

Q

3.79

0.00

-3.79

0.25 5.50 10.75 16

314.81 - 315.09 K

2.21-1—

^

m

0.00

-2.21

2.18

0.00

-2.18

3.93

0.00

-3.93

2.3

0.0

-2.3

4.45

0.00

1.61 0.00

-1.61

:£J§-

Zfc 3

0.25 15

315.09 K ** * *

1

1 1 X —1 9.25

315.09 - 315.15 K

-* x

x -*—

a el "Xt

16.25

315.15 - 315.19 K

ttA

A A

-i 1 1 1 r

6.25 9 11.75

315.20 - 315.21 K

X * *

X * #x* ,

,

, i i i

i

i i i

z —r— 0.25 5

315.21 K

-xX x ^ V

2.75

0.00

-2.75

6.86

0.00

-6.86

4.18

0.00

-4.18

2.37

0.00

-2.37

4.28

0.00

-4.28

2.54

0.00

-2.54

6.19

0.00

-6.19

—315.21 - 315.29 K

"As

>x

-i 1 r _, ^ , *_

6 11 16

315.35 - 315.52 K

;s MAA

gP Zl

-ffl- 4.5 9

315.53 - 315.84 K

13.5

fflfll

16.25

315.86 - 316.28 K

IB]

-i 1 1-

E*S ZJ

7.75 15.50

316.30 - 316.70 K

M.

ZS ZJ -B- 1 1 1

1 1 1 1 0.50 7.75 15

316.79 - 318.63 K

—i 1 1 1

1

1 1 1 r— 0.75 8.50 16.25

318.64 - 318.74 K

~bP~

-ffl- 9.75 12.50 2.5 15.5

DENSITY (mol/dm3

) DENSITY (mol/dm

3

) A - OESMRREST X- LENOIR 8- MQSTERT

ffl- PRASAD 0- RQOER

1108)

( 92) (109)

( 94) (111)

A- OESMRREST 1108) X" LENOIR ( 92) S3- PRASAD ( 94

Z3- ROOER (111) #- ROOER (2ND) (111) RODER I2N0) (111)

Figure A15. (continued)

103 -
8.34

318.76 - 319.52 K

o.oo-p-

-8.34

>

(J

Z)QZ

o

(J

UJ

X

o

>

LU

Q

4.13

2.25 15.25

319.86 - 319.96 K

0.00-$ ©

-4.13

ffi -©-

3.0

0.0

-3.0

3.26

0.00

-3.26

2.73

0.00

-2.73

1.96

0.00

i

1 1 1

1 1 1 1 r- 4 6.75 9.50 12.25

319.98 - 322.54 K

'AA

(S e11.75

322.55 - 322.74 K

A- II

A^

A^zHr

8.25 —i

1 1 1

1

1 1 1 1 11 1 1 r- 2.75 5.50

322.75 - 323.17 K

2P*

%

n

E—

EzB

i

1 1 1 1 1 r- 5.75 8.50

i—i—i—i

r 0.25 3

323.44 323.87 K

1.96 i3-S -S3.0

0.0

-3.0

2.39

0.00

-2.39

2.36

0.00

-2.36

3.46

0.00

-3.46

3.41

0.00

-3.41

2.8

0.0

323.99 - 324.06 K

a

30 Q q^Q Z] S1 1 1 1 1- 1.25 8.25 15.25

324.10 - 324.23 K

"H" a23

i—'—'—i—'

<~ 5.25 10.50 15.75

324.29 - 324.51 K

eS QQ

n

0.60 15.75

324.54 - 324.69 K

ES a eP

tt ~E q-El

l 1 1 1 JEL

1

1 r*—-i 1 ^3 i 1 1 r~

1 6 11 16

324.71 - 324.86 K

ES Q a a i\

i i

1 1 1 1 r" -H- Till

0.25 5.25 10.25 15.25

324.90 - 325.05 K

2.74

0.00

-2.74

Qp

]

1 1 rtS 1

1 1 r—

r

5 10 16

323.87 - 323.99 K

M°0 -H—

r

es -2.8 -£

0.25 15

325.05 - 325.17 K

-HIS 3 gj

E

4.39

0.00

-4.39 i <# i

i

i i 2.75 16

i 12 16

3' DENSITY (mol/dmJ

) DENSITY (mol/drri ) A'OESMRREST (1081 ffi-MOSTERT (1091

ffi- MOSTERT (110) S3- PRRSP.0 ( 94) gl- PRASAD (2ND) (94)

Q-ROOER (111) O- TUFEU ( 96)

O- KEYES E3- RODER

I 89)

(111)

Figure A15. (continued)

104 -
325.20 - 325.41 K

4.52

0.00

-4.52

>-

3.94

> 0.00

h- -3.94

(J

Z>

a 4.14

z 0.00

o

(J -4.14

_i

< 4.98

2 0.00

cc

LU -4.98

X

h- 7.76 —7

0.00

z -7.76

o

<

5.01

> 0.00

LU -5.01 Q

7.44

0.00

Q 030

i i—i—i—i—i—i1 5.75 10.50 15.25

325.42 - 325.68 K

00 i\ m n-Q0.5 13.5

325.70 - 326.07 K

03

-a- -i 1 1

1 1 r2.65

0.00

-2.65

4.6

0.0

-4.6

3.12

329.82 - 331.78 K

12.25

331.79 - 333.11 K

*" "©—

63

i i i i |

i i i i r 0.75 4 7.25 10.50

333.11 - 335.23 K

0.00-£

-3.12

1 6 11 16

326.08 - 326.64 K

—!

" , Q Q,0

0£J0 Q

-0 1

E

5 15.25

326.75 - 328.17 K

"0

1 1 ^~I 1 3.25 16

328.31 - 329.82 K

X v*

X

X X

-i 1 r 0.25 1.25 2.25 3.25

329.82 <

-7.44

**-

x _* X

X >:

1.8

0.0

-1.8

2.6

0.0

-2.6

5.06

0.00

-5.06

5.62

0.00

-5.62

0.75 6.50 12.25

335.23 - 335.33 K

7T& A a

0-2"^

i

]

1 1 1 1

1

1 1 1 r 0.25 3.75 7.25 10.75

335.34 - 339.45 K

*/& -zrA

^7?

1.75 12.60

340.37 K

x X X >

* * xx*

1 , 1 0.25 11.25

340.37 - 340.93 K

X

-B3.50 7.75 12 0.25 12 DENSITY (mol/dm3

) DENSITY (mol/dm

3

) X- LENOIR ( 92) 0- ROOER (111) • - ROOER (2N0) (111) A " DESHflREST V- LENEINORE

E3- LENG X- LENOIR $- MlLLflT ©-M0STERT

S- HOSTERT

(108)

I 90)

I 91)

( 92)

( 93)

(109)

(110)

Figure A15. (continued)

-105 -
3.16

0.00^

-3.16

340.93 - 344.26 K

o

u

1 1 V

S5

>

Io

Z>

Q

Z

o

o

cc

LLI IE

o

I-

<

>

LU

Q

13

344.26 - 348.15 K

6.58^

n r*n — O

V

O

• V

-Q

u.uu

ft KB

V X X a x

• 0.0O 1 1

1 0.75 13.75

3.33

0.00

-3.33

2.77

0.00

-2.77

3.11 0.00

-3.11

0.91

0.00

-0.91

5.49

348.15 K

-x- -K—*• X

>:

< x

-i—I—l—1 Aj 2.25 7 11.75 16.50

348.15 - 349.07 K

X x X

W

3.75 14.50

349.16 - 350.00 K

JL

ffl

3.15

0.00

-3.15

1.47

0.00

-1.47

3.78

0.00

-3.78

3.85

0.00

-3.85

3.38

0.00

351.18 - 364.49 K

A A * A A A

'

' I —a—i

^E3

8.50 10.75 13 15.25

364.49 - 364.62 K

I A a

A A A

A A A

2.50 —

> r 5.25

364.65 - 379.98 K

A A

A A

-&b | <fr , o & i r^—i 1 0.25 1 1.75 2.50

379.99 - 395.90 K

4^ <S><S>4» <*><£>

1 396.20 - 397.75 K

T 1 1 1

1

1 1 1 1

] r- B m g -3.38^

4.75 9.50 14.25

350.01 - 350.33 K

# -ffl a-

-fflT 1 1 1

1

1 I tSt 1.25 1.75 2.25 2.75

350.38 - 351.16 K

0. 00-£g

-5.49

-ffl2.29

0.00

-2.29

3.65

1.75 12.75

397.75 - 397.97 K

fflfflE

2 14.25

397.98 - 398.83 K

0.00 Ja

T

1.75 6.25 10.75 15.25

3

-3.65

M.

-ffi-T- 5.75 11.50

DENSITY (mol/dn-i ) DENSITY (mol/dm

J

) O - CflRMflCHflEL (107) X- GILMORE ( 88! V- LENEINORE ( 90) S* LENG ( 91)

EB - PRflSfiO ( 94) O - TUFEU ( 96)

A-DESnflREST 1108) <£- nilLAT ( 93)

ffl- PRASAD ( 94)

Figure A15. (continued)

-106 -
>

>

(J

Z>

Q

Z

o

cc

LUX

2.34

0.00

-2.34

0.97

0.00

398.88 - 404.05 K

V

m v^7

5.25 10.50 15.75

404.35 - 407.05 K

;W

o

\7 V V V

0.97 -p r4.5 15.5

407.15 - 410.93 K

6.93 -i

' q Q

0.00-f

-6.93

o o

V 7 v—V~

o

>

LU

Q

4.05

0.00

-4.05

—

1

1

1 1

1

1 r— 3.75 7.50 11.25

425.56 - 425.67 K

<*- <ft & , »

2.39

0.00

-2.39

1.96

0.00

-1.96

2.0

0.0

-2.0

2.24

0.00

-2.24

483.85 - 495.55 K

,-, r

J A I

' ' ' I

, i |

i i i

| . i i 2 4 6 8 10

495.58 - 497.08 K

i i i

i

i > i

i

'

i

' ' '

i 0.5 2.5 4.5 6.5 8.5 10.5

497.08 - 497.48 K

-a—m t±j m

m 3

E32.75 10.50

497.54 - 499.82 K

0.25 1.50

425.69 - 444.26 K

5.78^—-q 0.00

-5.78 -i r-

—i—i—I—i—i—i—

[—i—i—i—

|—i—i—i—|—i—i—r- 1.25 3.25 5.25 7.25 9.25 11.25

499.93 - 500.30 K

3.57 Hggb

0.00

-3.57

'Oooo

6.61

7 444.26 - 482.25 K

o SB Q

0.00 f v V v v 7

-6.61

11.75

500.30 - 500.40 K

2.39 9 O i&Jiffl

1.45

0.00

-1.46

1 1 1 1 1 1 1 1 1 1 1 1- 3.25 6.50 9.75

482.45 - 483.55 K

0.00

-2.39

E

^ V

V v

4 11.75

500.66 - 571.35 K

2.04 -9

i

1 1

1

1 1 1 1 1 1 1 1 1 1 r 10.5 11.5 12.5 13.5 14.5

3

0.00

-2.04

V V v

0.75 11.50

DENSITY (mol/dm

3

) DENSITY (mol/drri ) O- CRRMflCHREl (107) V- LENEINDRE ( 90) ^- HILLFIT ( 93) E3- PRflSRQ ( 94) O- TUFEU ( 96)

V- LENEINDRE ( 90) EB- PRR5flO ( 94) O - TUFEU ( 96)

Figure A15. (continued)

107 -
t

>

I-

(J

Q

Z

o

o

cc

LU

0.00

-2.79

2.58

0.00

-2.58

1.49

0.00

-1.49

C7 571.35 - 572.45 K

7 V v^

V v

1 1

1 1 13.25

572.65 - 599.32 K

m f

1 1 1 11 1 1 1

1

1 1 1 r 0.75 4 7.25 10.50

599.36 - 599.75 K

m a 3

B , CD

3.41 -?

0.75 10

599.76 - 648.75 K

o

>

0.00

-3.41

3.6

0.0

-3.6

4.24

0.00

-4.24

5.62

0.00

-5.62

ffl fflESt

"1 1 1 J- 1

[

1 1 1 1- 3.25 6.50 9.75

648.75 649.35 K

7 V 7 V V v v v v

1 12 649.45 - 724.55 K

7—y-y vvvw v

0.50 12.25

7 V

724.75 - 800.65 K v v v y

v v

i

1 1 1

1

1 1 1 1

1 1 1 1 r 0.60 3.75 7 10.25

DENSITY (mol/dm3

) V- lENEINORE

Efi- PRflSAO

( 90)

( 94)

Figure A15. (continued)

-108
Figure A15. Thermal conductivity at elevated pressures.

The comparisons are based on eqs (8), (11), (12), (14) and (15).

Primary data were from Desmarest [108], Prasad [94], and Roder [111].

Statistical comparisons between tabulated values of the thermal

conductivity and values calculated from eqs (8), (11), (12), (14) and (15) are given.

Data from Carmichael [107]

Number of Points: 31

Comparisons based on experimental pressures:

AAD% = 3.81 BIAS% = 3.51 RMS% =2.59 . AAD = 2.59 BIAS = 2.52 RMS = 1.99 mW.m" »K"

Data from Desmarest [108]

Weighted Data:

Number of Points: 111

Comparisons based on experimental pressures:

AAD% = 1.85 BIAS% = 0.98 RMS% =1.93

AAD = 1.03 BIAS = 0.39 RMS = 1.22 mW.m" »K~

Comparisons based on experimental densities:

AAD% = 1.88 BIAS% = 1.08 RMS% =2.04

AAD = 1.05 BIAS = 0.46 RMS = 1.28 mW-m" «K"

Data from Fleeter [80]

Number of Points: 12

Comparisons based on experimental pressures:

AAD% = 1.60 BIAS% = -1.59 RMS% =1.05 1 - AAD = 0.37 BIAS = -0.37 RMS = 0.24 mW-m -K"

Comparisons based on experimental densities:

AAD% = 1.68 BIAS% = -1.68 RMS% = 0.95 . - AAD = 0.40 BIAS = -0.40 RMS = 0.21 mW»m" »K~

Data from Gilmore [88]

Number of Points: 18

Comparisons based on experimental pressures:

AAD% = 1.80 BIAS% = 0.76 RMS% = 2.74

]

. AAD = 2.55 BIAS = 2.00 RMS =5.29 mW»m" -K"

Data from Keyes [89]

Number of Points: 5 Comparisons based on experimental pressures:

AAD% = 3.12 BIAS% = -3.12 RMS% = 0.89 . , AAD =0.91 BIAS = -0.91 RMS = 0.32 mW-m «K"

Data from Le Neindre [90]

Number of Points : 113

Comparisons based on experimental pressures:

AAD% = 1.63 BIAS% = 1.07 RMS% =1.88 - - AAD = 1.74 BIAS - 1.34 RMS =2.17 mW-m" »K~

Comparisons based on experimental densities:

AAD% = 1.82 BIAS% = 0.09 RMS% = 3.25 . - AAD = 1.89 BIAS = 0.22 RMS =3.02 mW-rn -K"

109
Data from Leng [91]

Number of Points: 12

Comparisons based on experimental pressures:

AAD% = 1.71 BIAS% =- -0.87 RMS% = 1.73 . . AAD = 1.05 BIAS = -0.70 RMS = 1.20 mW»m" »K~

Data from Lenoir [92]

Number of Points: 75

Comparisons based on experimental pressures

:

AAD% = 2.53 BIAS% = 0.26 RMS% = 3.36 . AAD = 1.36 BIAS = 0.05 RMS =2.01 mW.m" »K~

Data from Millat [93]

These data were not available during the development of the correlations

Number of Points: 64

Comparisons based on experimental pressures:

AAD% = 2.62 BIAS% = -2.28 RMS% = 1.60 . . AAD = 0.95 BIAS = -0.85 RMS = 0.65 mW.m" -K~

Comparisons based on experimental densities:

AAD% = 2.61 BIAS% = -2.24 RMS% = 1.62 . . AAD = 0.94 BIAS = -0.84 RMS = 0.65 mW»m" »K"

Data from Mostert [109]

These data were not available during the development of the correlations

Number of Points: 102

Comparisons based on experimental densities:

AAD% = 3.81 BIAS% = -2.69 RMS% = 4.89 . . AAD = 4.69 BIAS = -3.95 RMS - 8.15 mW»m -K"

Data from Mostert [110]

These data were not available during the development of the correlations

Number of Points: 9

Comparisons based on experimental pressures:

AAD% = 5.09 BIAS% = -2.36 RMS% = 5.77 . . AAD = 5.64 BIAS = -3.72 RMS = 6.09 mW-rn «K"

Comparisons based on experimental densities:

AAD% = 6.55 BIAS% = -3.92 RMS% = 7.00 . . AAD = 7.79 BIAS = -5.94 RMS = 8.64 mW-m -K

Data from Prasad [94]

Number of Points: 239

Comparisons based on experimental pressures:

AAD% = 1.67 BIAS% = -0.76 RMS% =2.01

AAD = 1.22 BIAS = -0.74 RMS = 1.43 mW-rn -K

Comparisons based on experimental densities:

AAD% = 1.89 BIAS% = -0.58 RMS% = 2.55 . AAD = 1.30 BIAS = -0.67 RMS = 1.61 mW»m -K

Weighted Data:

Number of Points: 235

Comparisons based on experimental pressures:

AAD% = 1.58 BIAS% = -0.83 RMS% = 1.75 . . AAD = 1.19 BIAS = -0.75 RMS = 1.37 mW-m «K

Comparisons based on experimental densities:

AAD% = 1.78 BIAS% = -0.65 RMS% =2.32

AAD - 1.26 BIAS - -0.68 RMS = 1.54 mW-ra «K

-110-
Data from Roder [111]

Number of Points: 797

Comparisons based on experimental pressures:

AAD% = 1.19 BIAS% = -0.76 RMS% =1.60

AAD = 0.81 BIAS = -0.44 RMS = 1.13 mW.m" »K"

Comparisons based on experimental densities:

AAD% = 1.19 BIAS% = -0.69 RMS% =1.59

AAD = 0.84 BIAS = -0.40 RMS = 1.17 mW»m -K

Weighted Data:

Number of Points: 752

Comparisons based on experimental pressures:

AAD% = 1.01 BIAS% = -0.61 RMS% =1.25

AAD = 0.70 BIAS = -0.33 RMS = 0.92 mW^m" .K~

Comparisons based on experimental densities:

AAD% = 1.03 BIAS% = -0.56 RMS% =1.28

AAD = 0.74 BIAS = -0.30 RMS = 0.99 mW.m -K

Data from Tufeu [96]

Number of Points: 24

Comparisons based on experimental densities:

AAD% = 2.58 BIAS% = 0.92 RMS% =2.78

AAD = 1.80 BIAS = 0.39 RMS = 2.21 mW»m -K

111
Appendix B: Tables for the thermophysical properties of ethane

Table Bl . Properties of ideal gas at 0.1 MPa and dilute gas transport

properties

T A

id

H

id

s ldc id

p n

o Ao K kJ«mol kJ • mo

1

J«mol «K J«mol »K /iPa«s mW • m •

K

90.352 -14.007 3.042 180.39 35.182 3.04 2.91

91. -14.130 3.065 180.64 35.216 3.06 2.94

92. -14.319 3.101 181.03 35.269 3.09 3.00

93. -14.508 3.136 181.41 35.322 3.12 3.06

94. -14.698 3.171 181.79 35.375 3.15 3.11

95. -14.889 3.207 182.16 35.428 3.17 3.17

96. -15.079 3.242 182.53 35.482 3.20 3.23

97. -15.270 3.278 182.90 35.535 3.23 3.28

98. -15.462 3.313 183.27 35.589 3.26 3.34

99. -15.654 3.349 183.63 35.643 3.29 3.40

100. -15.846 3.384 183.99 35.698 3.32 3.46

101. -16.038 3.420 184.34 35.752 3.34 3.51

102. -16.231 3.456 184.69 35.807 3.37 3.57

103. -16.424 3.492 185.04 35.861 3.40 3.63

104. -16.618 3.528 185.39 35.916 3.43 3.69

105. -16.812 3.564 185.73 35.971 3.46 3.75

106. -17.006 3.600 186.08 36.027 3.49 3.81

107. -17.200 3.636 186.41 36.082 3.52 3.86

108. -17.395 3.672 186.75 36.137 3.55 3.92

109. -17.590 3.708 187.08 36.193 3.57 3.98

110. -17.786 3.744 187.41 36.249 3.60 4.04

111. -17.982 3.780 187.74 36.305 3.63 4.10

112. -18.178 3.817 188.07 36.361 3.66 4.16

113. -18.375 3.853 188.39 36.418 3.69 4.22

114. -18.572 3.890 188.71 36.474 3.72 4.28

115. -18.769 3.926 189.03 36.531 3.75 4.34

116. -18.966 3.963 189.35 36.588 3.78 4.41

117. -19.164 3.999 189.66 36.645 3.81 4.47

118. -19.362 4.036 189.97 36.702 3.84 4.53

119. -19.561 4.073 190.28 36.759 3.87 4.59

120. -19.759 4.109 190.59 36.817 3.90 4.65

121. -19.958 4.146 190.90 36.874 3.93 4.71

122. -20.158 4.183 191.20 36.932 3.96 4.78

123. -20.357 4.220 191.50 36.990 3.99 4.84

124. -20.557 4.257 191.80 37.048 4.01 4.90

125. -20.758 4.294 192.10 37.107 4.04 4.96

126. -20.958 4.331 192.40 37.165 4.07 5.03

127. -21.159 4.369 192.69 37.224 4.10 5.09

128. -21.360 4.406 192.98 37.283 4.13 5.15

129. -21.562 4.443 193.27 37.342 4.16 5.22

-112
Table Bl . Properties of ideal gas... (continued)

T A

id

H

id

s ldc

ld

p A

o K kJ »mol kJ 'mol J«mol »K J«mol «K yuPa* s mW • m •

K

130. -21.763 4.480 193.56 37.401 4.19 5.28

131. -21.965 4.518 193.85 37.460 4.22 5.35

132. -22.168 4.555 194.13 37.520 4.25 5.41

133. -22.370 4.593 194.42 37.579 4.28 5.48

134. -22.573 4.631 194.70 37.639 4.31 5.54

135. -22.776 4.668 194.98 37.699 4.34 5.61

136. -22.980 4.706 195.26 37.760 4.37 5.67

137. -23.184 4.744 195.53 37.820 4.41 5.74

138. -23.388 4.782 195.81 37.881 4.44 5.81

139. -23.592 4.820 196.08 37.942 4.47 5.87

140. -23.796 4.857 196.36 38.003 4.50 5.94

141. -24.001 4.896 196.63 38.065 4.53 6.01

142. -24.206 4.934 196.90 38.126 4.56 6.07

143. -24.412 4.972 197.16 38.188 4.59 6.14

144. -24.617 5.010 197.43 38.250 4.62 6.21

145. -24.823 5.048 197.69 38.312 4.65 6.28

146. -25.029 5.087 197.96 38.375 4.68 6.35

147. -25.236 5.125 198.22 38.438 4.71 6.42

148. -25.442 5.163 198.48 38.501 4.74 6.48

149. -25.649 5.202 198.74 38.564 4.77 6.55

150. -25.856 5.241 199.00 38.628 4.80 6.62

151. -26.064 5.279 199.26 38.692 4.83 6.69

152. -26.271 5.318 199.51 38.756 4.86 6.76

153. -26.479 5.357 199.77 38.820 4.89 6.83

154. -26.688 5.396 200.02 38.885 4.92 6.90

155. -26.896 5.435 200.27 38.950 4.96 6.98

156. -27.105 5.474 200.52 39.015 4.99 7.05

157. -27.314 5.513 200.77 39.080 5.02 7.12

158. -27.523 5.552 201.02 39.146 5.05 7.19

159. -27.732 5.591 201.27 39.212 5.08 7.26

160. -27.942 5.630 201.51 39.279 5.11 7.33

161. -28.152 5.669 201.76 39.345 5.14 7.41

162. -28.362 5.709 202.00 39.413 5.17 7.48

163. -28.573 5.748 202.24 39.480 5.20 7.55

164. -28.783 5.788 202.49 39.548 5.23 7.63

165. -28.994 5.827 202.73 39.616 5.26 7.70

166. -29.205 5.867 202.97 39.684 5.30 7.78

167. -29.417 5.907 203.20 39.753 5.33 7.85

168. -29.629 5.947 203.44 39.822 5.36 7.92

169. -29.840 5.986 203.68 39.891 5.39 8.00

-113
Table Bl . Properties of ideal gas... (continued)

T A

ld

H

ld

s ld c

id

p n

o Ao K kJ «mol kJ«mol J«mol «K J»mol »K /j.'Pa* s mW • m •

K

170. -30.053 6.026 203.91 39.961 5.42 8.08

171. -30.265 6.066 204.15 40.031 5.45 8.15

172. -30.477 6.106 204.38 40.102 5.48 8.23

173. -30.690 6.146 204.61 40.173 5.51 8.30

174. -30.903 6.187 204.85 40.244 5.54 8.38

175. -31.117 6.227 205.08 40.316 5.57 8.46

176. -31.330 6.267 205.31 40.388 5.61 8.53

177. -31.544 6.308 205.54 40.460 5.64 8.61

178. -31.758 6.348 205.76 40.533 5.67 8.69

179. -31.972 6.389 205.99 40.606 5.70 8.77

180. -32.186 6.429 206.22 40.680 5.73 8.85

181. -32.401 6.470 206.44 40.754 5.76 8.92

182. -32.616 6.511 206.67 40.829 5.79 9.00

183. -32.831 6.552 206.89 40.903 5.82 9.08

184. -33.046 6.593 207.12 40.979 5.85 9.16

185. -33.262 6.634 207.34 41.054 5.89 9.24

186. -33.478 6.675 207.56 41.131 5.92 9.32

187. -33.694 6.716 207.78 41.207 5.95 9.40

188. -33.910 6.757 208.00 41.284 5.98 9.49

189. -34.126 6.799 208.22 41.362 6.01 9.57

190. -34.343 6.840 208.44 41.439 6.04 9.65

191. -34.560 6.882 208.66 41.518 6.07 9.73

192. -34.777 6.923 208.87 41.597 6.10 9.81

193. -34.994 6.965 209.09 41.676 6.13 9.90

194. -35.212 7.006 209.30 41.755 6.17 9.98

195. -35.429 7.048 209.52 41.836 6.20 10.06

196. -35.647 7.090 209.73 41.916 6.23 10.15

197. -35.865 7.132 209.95 41.997 6.26 10.23

198. -36.084 7.174 210.16 42.079 6.29 10.32

199. -36.302 7.216 210.37 42.160 6.32 10.40

200. -36.521 7.258 210.58 42.243 6.35 10.49

201. -36.740 7.301 210.79 42.326 6.38 10.57

202. -36.959 7.343 211.00 42.409 6.41 10.66

203. -37.179 7.386 211.21 42.493 6.45 10.75

204. -37.398 7.428 211.42 42.577 6.48 10.83

205. -37.618 7.471 211.63 42.662 6.51 10.92

206. -37.838 7.513 211.84 42.747 6.54 11.01

207. -38.059 7.556 212.05 42.833 6.57 11.10

208. -38.279 7.599 212.25 42.919 6.60 11.18

209. -38.500 7.642 212.46 43.005 6.63 11.27

114
Table Bl . Properties of ideal gas... (continued)

T A

id

H

id

K kJ«mol kJ Tnol

210. -38.721 7.685

211. -38.942 7.728

212. -39.163 7.771

213. -39.384 7.815

214. -39.606 7.858

215. -39.828 7.902

216. -40.050 7.945

217. -40.272 7.989

218. -40.495 8.033

219. -40.718 8.076

220. -40.941 8.120

221. -41.164 8.164

222. -41.387 8.209

223. -41.611 8.253

224. -41.834 8.297

225. -42.058 8.342

226. -42.282 8.386

227. -42.507 8.431

228. -42.731 8.475

229. -42.956 8.520

230. -43.181 8.565

231. -43.406 8.610

232. -43.631 8.655

233. -43.856 8.700

234. -44.082 8.745

235. -44.308 8.791

236. -44.534 8.836

237. -44.760 8.882

238. -44.987 8.928

239. -45.213 8.973

240. -45.440 9.019

241. -45.667 9.065

242. -45.894 9.111

243. -46.122 9.157

244. -46.349 9.204

245. -46.577 9.250

246. -46.805 9.297

247. -47.033 9.343

248. -47.261 9.390

249. -47.490 9.437

S C r) X

p o o J*mol «K J»mol »K /iPa«s mW«m »K

212 66

212 87

213 07

213 28

213 48

213 68

213 89

214 09

214 29

214 49

214 69

214 89

215 09

215 29

215 49

215 68

215 88

216 08

216 27

216 47

216 67

216 86

217 06

217 25

217 44

217 64

217 83

218 02

218 22

218 41

218 60

218 79

218 98

219 17

219 36

219 55

219 74

219 93

220 12

220 31

43.092

43.180

43.268

43.357

43.445

43.535

43.625

43.715

43.806

43.898

43.989

44.082

44.174

44.268

44.361

44.456

44.550

44.645

44.741

44.837

44.934

45.031

45.128

45.226

45.324

45.423

45.522

45.622

45.722

45.823

45.924

46.026

46.128

46.230

46.333

46.436

46.540

46.644

46.749

46.854

6 66 11 36

6 69 11 45

6 72 11 54

6 76 11 63

6 79 11 72

6 82 11 81

6 85 11 91

6 88 12 00

6 91 12 09

6 94 12 18

6 97 12 28

7 00 12 37

7 03 12 46

7 06 12 56

7 10 12 65

7 13 12 75

7 16 12 84

7 19 12 94

7 22 13 04

7 25 13 13

7 28 13 23

7 31 13 33

7 34 13 43

7 37 13 52

7 40 13 62

7 43 13 72

7 46 13 82

7 50 13 92

7 53 14 02

7 56 14 12

7 59 14 23

7 62 14 33

7 65 14 43

7 68 14 53

7 71 14 64

7 74 14 74

7 77 14 84

7 80 14 95

7 83 15 05

7 86 15 16

-115-
Table Bl . Properties of ideal gas... (continued)

T A

ld

H

id

s id c

id

P o A

o K kJ«mol kJ«mol J«mol »K J«mol »K /jPa« s mW • m •

K

250. -47.719 9.484 220.49 46.959 7.89 15.26

251. -47.948 9.531 220.68 47.065 7.92 15.37

252. -48.177 9.578 220.87 47.171 7.95 15.48

253. -48.406 9.625 221.06 47.278 7.98 15.58

254. -48.635 9.672 221.24 47.385 8.01 15.69

255. -48.865 9.720 221.43 47.493 8.04 15.80

256. -49.095 9.767 221.62 47.600 8.07 15.91

257. -49.325 9.815 221.80 47.709 8.10 16.02

258. -49.555 9.863 221.99 47.817 8.14 16.13

259. -49.786 9.911 222.17 47.926 8.17 16.24

260. -50.016 9.959 222.36 48.036 8.20 16.35

261. -50.247 10.007 222.54 48.146 8.23 16.46

262. -50.478 10.055 222.73 48.256 8.26 16.57

263. -50.709 10.103 222.91 48.367 8.29 16.68

264. -50.940 10.152 223.09 48.478 8.32 16.79

265. -51.172 10.200 223.28 48.589 8.35 16.90

266. -51.403 10.249 223.46 48.701 8.38 17.02

267. -51.635 10.298 223.64 48.813 8.41 17.13

268. -51.867 10.346 223.83 48.925 8.44 17.25

269. -52.100 10.395 224.01 49.038 8.47 17.36

270. -52.332 10.444 224.19 49.151 8.50 17.47

271. -52.565 10.494 224.37 49.265 8.53 17.59

272. -52.797 10.543 224.55 49.379 8.56 17.71

273. -53.030 10.592 224.74 49.493 8.59 17.82

273.150 -53.065 10.600 224.76 49.510 8.59 17.84

274. -53.264 10.642 224.92 49.608 8.62 17.94

275. -53.497 10.692 225.10 49.723 8.65 18.05

276. -53.730 10.741 225.28 49.838 8.68 18.17

277. -53.964 10.791 225.46 49.953 8.71 18.29

278. -54.198 10.841 225.64 50.069 8.74 18.41

279. -54.432 10.891 225.82 50.185 8.77 18.53

280. -54.666 10.942 226.00 50.302 8.80 18.65

281. -54.901 10.992 226.18 50.419 8.83 18.77

282. -55.135 11.043 226.36 50.536 8.86 18.89

283. -55.370 11.093 226.54 50.653 8.88 19.01

284. -55.605 11.144 226.72 50.771 8.91 19.13

285. -55.840 11.195 226.89 50.889 8.94 19.25

286. -56.075 11.246 227.07 51.007 8.97 19.37

287. -56.311 11.297 227.25 51.126 9.00 19.49

288. -56.546 11.348 227.43 51.245 9.03 19.62

116
Table Bl. Properties of ideal gas... (continued)

T A

id

H

id

s id c

id

p

*1 o A

o K kJ • mo

1

kJ 'mol J«mol »K J •mol »K /iPa» s mW • m • K

289. -56.782 11.399 227.61 51.364 9.06 19.74

290. -57.018 11.451 227.79 51.484 9.09 19.86

291. -57.254 11.502 227.96 51.603 9.12 19.99

292. -57.491 11.554 228.14 51.723 9.15 20.11

293. -57.727 11.606 228.32 51.844 9.18 20.24

294. -57.964 11.657 228.49 51.964 9.21 20.36

295. -58.201 11.710 228.67 52.085 9.24 20.49

296. -58.438 11.762 228.85 52.206 9.27 20.62

297. -58.675 11.814 229.02 52.327 9.30 20.74

298. -58.913 11.866 229.20 52.449 9.33 20.87

298.150 -58.948 11.874 229.23 52.467 9.33 20.89

299. -59.150 11.919 229.37 52.571 9.36 21.00

300. -59.388 11.971 229.55 52.693 9.39 21.13

301. -59.626 12.024 229.73 52.815 9.42 21.25

302. -59.864 12.077 229.90 52.938 9.44 21.38

303. -60.102 12.130 230.08 53.060 9.47 21.51

304. -60.341 12.183 230.25 53.183 9.50 21.64

305. -60.580 12.236 230.43 53.307 9.53 21.77

305.330 -60.658 12.254 230.48 53.347 9.54 21.82

306. -60.818 12.290 230.60 53.430 9.56 21.90

307. -61.057 12.343 230.78 53.554 9.59 22.04

308. -61.297 12.397 230.95 53.677 9.62 22.17

309. -61.536 12.451 231.12 53.801 9.65 22.30

310. -61.776 12.505 231.30 53.926 9.68 22.43

311. -62.015 12.559 231.47 54.050 9.71 22.56

312. -62.255 12.613 231.65 54.175 9.74 22.70

313. -62.495 12.667 231.82 54.299 9.77 22.83

314. -62.735 12.721 231.99 54.424 9.79 22.97

315. -62.976 12.776 232.17 54.549 9.82 23.10

316. -63.216 12.830 232.34 54.675 9.85 23.24

317. -63.457 12.885 232.51 54.800 9.88 23.37

318. -63.698 12.940 232.69 54.926 9.91 23.51

319. -63.939 12.995 232.86 55.052 9.94 23.64

320. -64.180 13.050 233.03 55.178 9.97 23.78

321. -64.422 13.105 233.20 55.304 10.00 23.92

322. -64.663 13.161 233.37 55.430 10.03 24.05

323. -64.905 13.216 233.55 55.557 10.05 24.19

324. -65.147 13.272 233.72 55.683 10.08 24.33

325. -65.389 13.328 233.89 55.810 10.11 24.47

326. -65.631 13.383 234.06 55.937 10.14 24.61

-117-
Table Bl . Properties of ideal gas... (continued)

T A

ld

H

ld

s ld c

id

p o A

K kJ • mo 1 kJ«mol J«mol «K J'mol *K /iPa» s raW • m • K

327. -65.874 13.439 234.23 56.064 10.17 24.75

328. -66.117 13.496 234.41 56.191 10.20 24.89

329. -66.359 13.552 234.58 56.319 10.23 25.03

330. -66.602 13.608 234.75 56.446 10.25 25.17

331. -66.845 13.665 234.92 56.574 10.28 25.31

332. -67.089 13.721 235.09 56.701 10.31 25.45

333. -67.332 13.778 235.26 56.829 10.34 25.59

334. -67.576 13.835 235.43 56.957 10.37 25.74

335. -67.820 13.892 235.60 57.085 10.40 25.88

336. -68.064 13.949 235.77 57.213 10.43 26.02

337. -68.308 14.006 235.94 57.341 10.45 26.17

338. -68.552 14.064 236.11 57.470 10.48 26.31

339. -68.797 14.121 236.28 57.598 10.51 26.46

340. -69.042 14.179 236.45 57.727 10.54 26.60

341. -69.286 14.237 236.62 57.855 10.57 26.75

342. -69.531 14.295 236.79 57.984 10.60 26.89

343. -69.777 14.353 236.96 58.113 10.62 27.04

344. -70.022 14.411 237.13 58.242 10.65 27.18

345. -70.267 14.469 237.30 58.371 10.68 27.33

346. -70.513 14.528 237.47 58.500 10.71 27.48

347. -70.759 14.586 237.64 58.629 10.74 27.63

348. -71.005 14.645 237.81 58.758 10.76 27.77

349. -71.251 14.704 237.97 58.887 10.79 27.92

350. -71.498 14.763 238.14 59.017 10.82 28.07

351. -71.744 14.822 238.31 59.146 10.85 28.22

352. -71.991 14.881 238.48 59.276 10.88 28.37

353. -72.238 14.940 238.65 59.405 10.90 28.52

354. -72.485 15.000 238.82 59.535 10.93 28.67

355. -72.732 15.059 238.99 59.664 10.96 28.82

356. -72.979 15.119 239.15 59.794 10.99 28.97

357. -73.227 15.179 239.32 59.923 11.02 29.12

358. -73.475 15.239 239.49 60.053 11.04 29.27

359. -73.723 15.299 239.66 60.183 11.07 29.43

360. -73.971 15.359 239.82 60.313 11.10 29.58

361. -74.219 15.420 239.99 60.443 11.13 29.73

362. -74.467 15.480 240.16 60.572 11.16 29.88

363. -74.716 15.541 240.33 60.702 11.18 30.04

364. -74.965 15.602 240.49 60.832 11.21 30.19

365. -75.213 15.663 240.66 60.962 11.24 30.34

366. -75.462 15.724 240.83 61.092 11.27 30.50

118
Table Bl . Properties of ideal gas... (continued)

T A

] . d Hld

s

] d c

id

p o o K kJ«mol kJ •mol J «mol

1 .K'1 J«mol «K /xPa* s mW«m ^K" 1

367. -75 .712 15 .785 240 99 61 222 11 29 30 65

368. -75 .961 15 .846 241 16 61 352 11 32 30 81

369. -76 .211 15 .907 241 33 61 482 11 35 30 .97

370. -76 .460 15 .969 241 49 61 612 11 38 31 .12

371. -76 .710 16 031 241 66 61 742 11 40 31 28

372. -76 960 16 092 241 83 61 872 11 43 31 43

373. -77 211 16 154 241 99 62 002 11 46 31 59

374. -77 461 16 216 242 16 62 132 11 49 31 75

375. -77 712 16 279 242 33 62 262 11 51 31 91

376. -77 962 16 341 242 49 62 392 11 54 32 06

377. -78 213 16 403 242 66 62 523 11 57 32 22

378. -78 464 16 466 242 82 62 653 11 60 32 38

379. -78 715 16 529 242 99 62 783 11 62 32 54

380. -78 967 16 592 243 15 62 913 11 65 32 70

381. -79 218 16 655 243 32 63 043 11 68 32 86

382. -79 470 16 718 243 49 63 173 11 71 33 02

383. -79 722 16 781 243 65 63 302 11 73 33 18

384. -79 974 16 844 243 82 63 432 11 76 33 34

385. -80 226 16 908 243 98 63 562 11 79 33 50

386. -80 479 16 971 244 15 63 692 11 81 33 66

387. -80 731 17 035 244 31 63 822 11 84 33 82

388. -80 984 17 099 244 48 63 952 11 87 33 99

389. -81 237 17 163 244 64 64 082 11 90 34 15

390. -81 490 17 227 244 81 64 212 11 92 34 31

391. -81 743 17 292 244 97 64 341 11 95 34 47

392. -81 996 17 356 245 14 64 471 11 98 34 64

393. -82 250 17 420 245 30 64 601 12 00 34 80

394. -82 504 17 485 245 46 64 730 12 03 34 96

395. -82 757 17 550 245 63 64 860 12 06 35 13

396. -83 Oil 17 615 245 79 64 989 12 08 35 29

397. -83 266 17 680 245 96 65 119 12 11 35 46

398. -83 520 17 745 246 12 65 248 12 14 35 62

399. -83 774 17 810 246 28 65 378 12 17 35 79

400. -84 029 17 876 246 45 65 507 12 19 35 95

405. -85 305 18 205 247 27 66 153 12 33 36 79

410. -86 585 18 537 248 08 66 798 12 46 37 63

415. -87 869 18 873 248 89 67 441 12 59 38 47

420. -89 157 19 212 249 71 68 082 12 72 39 33

425. -90 449 19 554 250 52 68 720 12 86 40 19

430. -91 745 19 899 251. 32 69. 357 12 99 41 05

119
Table Bl . Properties of ideal gas... (continued)

T A

id

H

id

s id

c

id

p 1

o Ao K kJ«mol kJ • mo

1

J-mol'^K" 1 J«mol «K /iPa« s mW • m •

K

435. -93.046 20.247 252.13 69.992 13. 12 41.93

440. -94.350 20.599 252.93 70.624 13. 25 42.81

445. -95.658 20.954 253.73 71.254 13. 38 43.69

450. -96.970 21.311 254.53 71.880 13, 50 44.58

455. -98.286 21.672 255.33 72.505 13. 63 45.48

460. -99.607 22.036 256.13 73.126 13. 76 46.38

465. -100.931 22.404 256.92 73.744 13. 89 47.29

470. -102.259 22.774 257.71 74.360 14. 01 48.20

475. -103.591 23.147 258.50 74.972 14. 14 49.12

480. -104.927 23.524 259.29 75.582 14. 26 50.04

485. -106.267 23.903 260.08 76.188 14, 39 50.97

490. -107.611 24.285 260.86 76.791 14. 51 51.90

495. -108.959 24.671 261.64 77.391 14. 64 52.84

500. -110.311 25.059 262.43 77.987 14. 76 53.78

505. -111.666 25.451 263.20 78.580 54.73

510. -113.026 25.845 263.98 79.170 55.68

515. -114.389 26.242 264.76 79.757 56.63

520. -115.757 26.643 265.53 80.340 57.59

525. -117.128 27.046 266.30 80.920 58.55

530. -118.503 27.452 267.07 81.496 59.51

535. -119.882 27.861 267.84 82.070 60.48

540. -121.264 28.273 268.61 82.639 61.45

545. -122.651 28.687 269.37 83.206 62.43

550. -124.041 29.105 270.13 83.769 63.41

555. -125.435 29.525 270.89 84.329 64.39

560. -126.833 29.948 271.65 84.885 65.37

565. -128.235 30.374 272.41 85.438 66.36

570. -129.641 30.802 273.16 85.988 67.35

575. -131.050 31.234 273.92 86.535 68.34

580. -132.463 31.668 274.67 87.078 69.34

585. -133.880 32.104 275.42 87.618 70.34

590. -135.300 32.544 276.17 88.155 71.34

595. -136.724 32.986 276.91 88.689 72.34

600. -138.152 33.431 277.66 89.220 73.35

605. -139.584 33.878 278.40 89.747

610. -141.020 34.328 279.14 90.272

615. -142.459 34.781 279.88 90.793

620. -143.902 35.236 280.62 91.311

625. -145.348 35.694 281.35 91.827

120
Table B2 . Properties along saturation boundary

T Pa

P oL pav

C

aL

W T "vL

A

T crL K MPa mol'dm 3 -3 mol'dm J«mol »K

1 -1 m»s ^Pa»s mW • m •

90.352 0.11E-05 21.67 0.150E-05 66.86 1995.9 1280.09 255.6

91. 0.13E-05 21.64 0.177E-05 67.23 1992.6 1244.72 255.1

92. 0.17E-05 21.61 0.227E-05 67.74 1987.2 1193.00 254.4

93. 0.22E-05 21.57 0.288E-05 68.19 1981.6 1144.52 253.6

94. 0.28E-05 21.54 0.364E-05 68.59 1975.7 1099.02 252.8

95. 0.36E-05 21.50 0.458E-05 68.94 1969.7 1056.26 252.1

96. 0.46E-05 21.47 0.573E-05 69.24 1963.5 1016.05 251.3

97. 0.58E-05 21.43 0.713E-05 69.50 1957.2 978.18 250.5

98. 0.72E-05 21.39 0.883E-05 69.73 1950.8 942.43 249.7

99. 0.90E-05 21.36 0.109E-04 69.92 1944.3 908.79 248.9

100. 0.11E-04 21.32 0.133E-04 70.09 1937.6 876.96 248.1

101. 0.14E-04 21.29 0.163E-04 70.23 1930.9 846.87 247.3

102. 0.17E-04 21.25 0.198E-04 70.34 1924.2 818.40 246.4

103. 0.21E-04 21.22 0.240E-04 70.43 1917.3 791.42 245.6

104. 0.25E-04 21.18 0.289E-04 70.51 1910.4 765.84 244.7

105. 0.30E-04 21.14 0.347E-04 70.57 1903.5 741.57 243.9

106. 0.37E-04 21.11 0.415E-04 70.61 1896.5 718.52 243.0

107. 0.44E-04 21.07 0.494E-04 70.64 1889.5 696.60 242.2

108. 0.53E-04 21.03 0.586E-04 70.66 1882.4 675.76 241.3

109. 0.63E-04 21.00 0.693E-04 70.68 1875.3 655.91 240.4

110. 0.75E-04 20.96 0.817E-04 70.68 1868.2 637.00 239.5

111. 0.89E-04 20.93 0.959E-04 70.67 1861.1 618.96 238.6

112. 0.10E-03 20.89 0.112E-03 70.66 1853.9 601.75 237.7

113. 0.12E-03 20.85 0.131E-03 70.65 1846.7 585.32 236.8

114. 0.14E-03 20.82 0.152E-03 70.63 1839.5 569.61 235.9

115. 0.17E-03 20.78 0.177E-03 70.60 1832.3 554.60 235.0

116. 0.20E-03 20.74 0.204E-03 70.58 1825.1 540.22 234.1

117. 0.23E-03 20.71 0.236E-03 70.55 1817.8 526.46 233.2

118. 0.27E-03 20.67 0.271E-03 70.52 1810.6 513.27 232.2

119. 0.31E-03 20.63 0.311E-03 70.49 1803.3 500.63 231.3

120. 0.35E-03 20.60 0.356E-03 70.46 1796.0 488.50 230.4

121. 0.41E-03 20.56 0.406E-03 70.42 1788.7 476.85 229.4

122. 0.47E-03 20.52 0.462E-03 70.39 1781.3 465.67 228.5

123. 0.54E-03 20.49 0.524E-03 70.36 1774.0 454.91 227.5

124. 0.61E-03 20.45 0.594E-03 70.33 1766.7 444.57 226.6

125. 0.70E-03 20.41 0.671E-03 70.30 1759.3 434.62 225.6

126. 0.79E-03 20.38 0.756E-03 70.27 1752.0 425.04 224.6

127. 0.90E-03 20.34 0.851E-03 70.25 1744.6 415.81 223.7

128. 0.10E-02 20.30 0.955E-03 70.22 1737.2 406.92 222.7

129. 0.11E-02 20.26 0.107E-02 70.20 1729.8 398.34 221.7

121-
Table B2 . Properties along saturation boundary (continued)

T P

a

p oL p av

C

oL

W T "aL

A aL

K MPa mol'dm 3 -3 mol»dm J»mol »K

1 -1 m»s /iPa«s mW • m •

K

130. 0.13E-02 20.23 0.120E-02 70.18 1722.4 390.06 220.8

131. 0.15E-02 20.19 0.134E-02 70.16 1715.0 382.07 219.8

132. 0.16E-02 20.15 0.149E-02 70.14 1707.6 374.36 218.8

133. 0.18E-02 20.12 0.165E-02 70.13 1700.2 366.90 217.8

134. 0.20E-02 20.08 0.183E-02 70.12 1692.8 359.69 216.9

135. 0.23E-02 20.04 0.203E-02 70.11 1685.3 352.72 215.9

136. 0.25E-02 20.00 0.225E-02 70.10 1677.9 345.98 214.9

137. 0.28E-02 19.96 0.248E-02 70.09 1670.5 339.44 213.9

138. 0.31E-02 19.93 0.273E-02 70.09 1663.0 333.12 212.9

139. 0.35E-02 19.89 0.301E-02 70.09 1655.5 326.99 211.9

140. 0.38E-02 19.85 0.330E-02 70.10 1648.1 321.05 210.9

141. 0.42E-02 19.81 0.362E-02 70.10 1640.6 315.29 209.9

142. 0.47E-02 19.78 0.397E-02 70.11 1633.2 309.70 209.0

143. 0.51E-02 19.74 0.434E-02 70.12 1625.7 304.27 208.0

144. 0.56E-02 19.70 0.474E-02 70.14 1618.2 299.00 207.0

145. 0.62E-02 19.66 0.516E-02 70.15 1610.7 293.88 206.0

146. 0.68E-02 19.62 0.562E-02 70.17 1603.2 288.91 205.0

147. 0.74E-02 19.59 0.611E-02 70.19 1595.7 284.08 204.0

148. 0.81E-02 19.55 0.664E-02 70.22 1588.2 279.38 203.0

149. 0.89E-02 19.51 0.720E-02 70.24 1580.7 274.80 202.0

150. 0.97E-02 19.47 0.780E-02 70.27 1573.2 270.35 201.0

151. 0.11E-01 19.43 0.844E-02 70.31 1565.7 266.02 200.0

152. 0.11E-01 19.39 0.912E-02 70.34 1558.2 261.80 199.0

153. 0.12E-01 19.35 0.985E-02 70.38 1550.7 257.69 198.0

154. 0.13E-01 19.32 0.011 70.42 1543.2 253.68 197.0

155. 0.15E-01 19.28 0.011 70.46 1535.7 249.77 196.0

156. 0.16E-01 19.24 0.012 70.51 1528.2 245.96 195.0

157. 0.17E-01 19.20 0.013 70.55 1520.6 242.25 194.0

158. 0.18E-01 19.16 0.014 70.60 1513.1 238.62 193.0

159. 0.20E-01 19.12 0.015 70.66 1505.6 235.08 192.0

160. 0.21E-01 19.08 0.016 70.71 1498.1 231.63 191.0

161. 0.23E-01 19.04 0.017 70.77 1490.5 228.25 190.0

162. 0.25E-01 19.00 0.019 70.83 1483.0 224.95 189.0

163. 0.27E-01 18.96 0.020 70.89 1475.5 221.73 188.1

164. 0.29E-01 18.92 0.021 70.95 1467.9 218.58 187.1

165. 0.31E-01 18.88 0.023 71.02 1460.4 215.50 186.1

166. 0.33E-01 18.84 0.024 71.09 1452.8 212.48 185.1

167. 0.35E-01 18.80 0.026 71.16 1445.3 209.53 184.1

168. 0.38E-01 18.76 0.027 71.24 1437.7 206.65 183.1

169. 0.40E-01 18.72 0.029 71.31 1430.2 203.82 182.1

122-
Table B2

Properties along sia titration boundary (continued)

T Pa

PaL 'av

C

aL

W T ctL %L A

T ctL K MPa mol'dm mol»dm J«mol »K

1 -1 m» s /iPa* s mW • m •

170. 0.43E-•01 18.68 0.031 71.39 1422.6 201.06 181.2

171. 0.46E-01 18.64 0.033 71.47 1415.1 198.35 180.2

172. 0.49E-01 18.60 0.035 71.56 1407.5 195.70 179.2

173. 0.52E-01 18.56 0.037 71.64 1399.9 193.09 178.2

174. 0.55E-01 18.52 0.039 71.73 1392.4 190.55 177.3

175. 0.59E-01 18.48 0.041 71.82 1384.8 188.05 176.3

176. 0.62E-01 18.44 0.044 71.91 1377.2 185.60 175.3

177. 0.66E-01 18.40 0.046 72.01 1369.7 183.19 174.3

178. 0.70E-01 18.36 0.049 72.11 1362.1 180.84 173.4

179. 0.74E-01 18.32 0.051 72.21 1354.5 178.52 172.4

180. 0.79E-01 18.28 0.054 72.31 1346.9 176.25 171.4

181. 0.83E-01 18.24 0.057 72.41 1339.3 174.02 170.5

182. 0.88E-01 18.19 0.060 72.52 1331.7 171.83 169.5

183. 0.93E-01 18.15 0.063 72.63 1324.2 169.68 168.5

184. 0.98E-01 18.11 0.066 72.74 1316.6 167.57 167.6

184.309 0.10 18.10 0.068 72.78 1314.2 166.93 167.3

184.552 0.101352 18.09 0.068 72.80 1312.4 166.42 167.1

185. 0.10 18.07 0.070 72.85 1309.0 165.50 166.6

186. 0.11 18.03 0.073 72.97 1301.4 163.46 165.7

187. 0.12 17.98 0.077 73.09 1293.7 161.45 164.7

188. 0.12 17.94 0.081 73.21 1286.1 159.48 163.8

189. 0.13 17.90 0.085 73.33 1278.5 157.55 162.8

190. 0.13 17.86 0.089 73.46 1270.9 155.64 161.9

191. 0.14 17.81 0.093 73.59 1263.3 153.77 160.9

192. 0.15 17.77 0.098 73.72 1255.6 151.92 160.0

193. 0.16 17.73 0.102 73.85 1248.0 150.11 159.0

194. 0.16 17.69 0.107 73.99 1240.4 148.32 158.1

195. 0.17 17.64 0.112 74.13 1232.7 146.56 157.2

196. 0.18 17.60 0.117 74.27 1225.1 144.83 156.2

197. 0.19 17.55 0.122 74.41 1217.4 143.13 155.3

198. 0.20 17.51 0.127 74.56 1209.7 141.45 154.4

199. 0.21 17.47 0.133 74.71 1202.1 139.80 153.4

200. 0.22 17.42 0.139 74.86 1194.4 138.17 152.5

201. 0.23 17.38 0.145 75.02 1186.7 136.56 151.6

202. 0.24 17.33 0.151 75.17 1179.0 134.98 150.7

203. 0.25 17.29 0.157 75.33 1171.3 133.42 149.8

204. 0.26 17.24 0.164 75.50 1163.6 131.89 148.8

205. 0.27 17.20 0.170 75.66 1155.9 130.37 147.9

206. 0.28 17.15 0.177 75.83 1148.2 128.88 147.0

207. 0.29 17.11 0.185 76.00 1140.4 127.40 146.1

-123
Table B2 . Properties along saturation boundary (continued)

T Pa

PeL p ov

C

aL

W

aLT "aL

x

T ctL K MPa mol»dm mol»dm J»mol «K

•1 -1 m» s /xPa»s raW • m • K

208. 0.31 17.06 0.192 76.18 1132.7 125.95 145.2

209. 0.32 17.02 0.200 76.35 1125.0 124.51 144.3

210. 0.33 16.97 0.208 76.53 1117.2 123.10 143.4

211. 0.35 16.93 0.216 76.72 1109.4 121.70 142.5

212. 0.36 16.88 0.224 76.90 1101.7 120.32 141.6

213. 0.38 16.83 0.233 77.09 1093.9 118.96 140.7

214. 0.39 16.78 0.241 77.29 1086.1 117.62 139.8

215. 0.41 16.74 0.251 77.49 1078.3 116.29 138.9

216. 0.42 16.69 0.260 77.69 1070.4 114.99 138.0

217. 0.44 16.64 0.270 77.89 1062.6 113.69 137.1

218. 0.46 16.59 0.279 78.10 1054.8 112.41 136.2

219. 0.47 16.55 0.290 78.31 1046.9 111.15 135.4

220. 0.49 16.50 0.300 78.52 1039.0 109.90 134.5

221. 0.51 16.45 0.311 78.74 1031.2 108.67 133.6

222. 0.53 16.40 0.322 78.96 1023.3 107.45 132.7

223. 0.55 16.35 0.333 79.19 1015.4 106.25 131.9

224. 0.57 16.30 0.345 79.42 1007.4 105.06 131.0

225. 0.59 16.25 0.357 79.66 999.5 103.88 130.1

226. 0.61 16.20 0.369 79.90 991.5 102.72 129.3

227. 0.63 16.15 0.382 80.14 983.6 101.57 128.4

228. 0.65 16.10 0.395 80.39 975.6 100.43 127.5

229. 0.68 16.05 0.408 80.64 967.6 99.30 126.7

230. 0.70 16.00 0.422 80.90 959.6 98.19 125.8

231. 0.72 15.95 0.436 81.16 951.5 97.09 125.0

232. 0.75 15.90 0.451 81.43 943.5 96.00 124.1

233. 0.77 15.84 0.465 81.70 935.4 94.92 123.3

234. 0.80 15.79 0.481 81.98 927.3 93.85 122.4

235. 0.83 15.74 0.496 82.26 919.2 92.79 121.6

236. 0.85 15.68 0.512 82.55 911.0 91.74 120.7

237. 0.88 15.63 0.529 82.84 902.9 90.71 119.9

238. 0.91 15.58 0.546 83.14 894.7 89.68 119.0

239. 0.94 15.52 0.563 83.45 886.5 88.66 118.2

240. 0.97 15.47 0.581 83.76 878.3 87.65 117.4

241. 1.00 15.41 0.599 84.08 870.0 86.66 116.5

242. 1.03 15.36 0.618 84.41 861.8 85.67 115.7

243. 1.06 15.30 0.637 84.74 853.5 84.69 114.9

244. 1.09 15.24 0.657 85.08 845.1 83.72 114.1

245. 1.13 15.19 0.677 85.43 836.8 82.75 113.2

246. 1.16 15.13 0.698 85.79 828.4 81.80 112.4

247. 1.19 15.07 0.719 86.15 820.0 80.85 111.6

124
Table B2

Properties along sa turation boundary (continued)

T Pa

poL 'ov

C

oL

W T "aLAohT K MPa mol'dm rnol'dm

3

T I' 1 J»mol »KV-

•1 -1 m» s /iPa» s mW»m «K

248. 1.23 15.01 0.741 86.52 811.6 79.91 110.8

249. 1.26 14.95 0.764 86.90 803.1 78.98 110.0

250. 1.30 14.89 0.787 87.29 794.6 78.06 109.1

251. 1.34 14.83 0.810 87.70 786.1 77.14 108.3

252. 1.38 14.77 0.835 88.11 777.5 76.23 107.5

253. 1.42 14.71 0.859 88.53 768.9 75.33 106.7

254. 1.46 14.65 0.885 88.96 760.3 74.43 105.9

255. 1.50 14.58 0.911 89.40 751.6 73.54 105.1

256. 1.54 14.52 0.938 89.86 742.9 72.66 104.3

257. 1.58 14.46 0.966 90.33 734.1 71.79 103.5

258. 1.62 14.39 0.994 90.81 725.4 70.91 102.7

259. 1.67 14.33 1.023 91.31 716.5 70.05 101.9

260. 1.71 14.26 1.053 91.82 707.7 69.19 101.1

261. 1.76 14.19 1.084 92.34 698.7 68.34 100.3

262. 1.80 14.13 1.116 92.89 689.8 67.49 99.5

263. 1.85 14.06 1.148 93.45 680.8 66.64 98.7

264. 1.90 13.99 1.182 94.03 671.7 65.80 97.9

265. 1.95 13.92 1.216 94.63 662.6 64.97 97.1

266. 2.00 13.85 1.252 95.25 653.4 64.14 96.3

267. 2.05 13.77 1.288 95.89 644.2 63.31 95.5

268. 2.10 13.70 1.325 96.55 634.9 62.48 94.8

269. 2.16 13.63 1.364 97.24 625.6 61.66 94.0

270. 2.21 13.55 1.404 97.96 616.2 60.85 93.2

271. 2.26 13.47 1.445 98.71 606.7 60.03 92.4

272. 2.32 13.40 1.487 99.49 597.2 59.22 91.6

273. 2.38 13.32 1.530 100.30 587.5 58.41 90.8

273. 2.39 13.31 1.537 100.30 587.5 58.41 90.8

274. 2.44 13.24 1.575 101.15 577.9 57.61 90.0

275. 2.49 13.16 1.622 102.04 568.1 56.80 89.3

276. 2.55 13.07 1.670 102.97 558.2 56.00 88.5

277. 2.62 12.99 1.719 103.95 548.3 55.19 87.7

278. 2.68 12.90 1.771 104.98 538.3 54.39 86.9

279. 2.74 12.81 1.824 106.07 528.1 53.59 86.1

280. 2.81 12.72 1.879 107.22 517.9 52.79 85.4

281. 2.87 12.63 1.936 108.44 507.5 51.98 84.6

282. 2.94 12.54 1.995 109.73 497.1 51.18 83.8

283. 3.01 12.44 2.057 111.11 486.5 50.37 83.0

284. 3.07 12.34 2.121 112.58 475.8 49.56 82.2

285. 3.14 12.24 2.187 114.17 465.0 48.75 81.5

286. 3.22 12.13 2.257 115.87 454.0 47.93 80.7

-125
Table B2 . Properties along saturation boundary (continued)

T Pa

PoL Pav

C

aL

W

aL "aL

X

T aL, K MPa mol'dm mol»dm J»mol »K

1 -1 m»s /xPa»s mW»m »K

287. 3.29 12.03 2.330 117.71 442.9 47.11 79.9

288. 3.36 11.92 2.406 119.72 431.6 46.28 79.1

289. 3.44 11.80 2.486 121.91 420.1 45.44 78.4

290. 3.51 11.68 2.570 124.32 408.5 44.60 77.6

291. 3.59 11.56 2.659 126.99 396.7 43.74 76.8

292. 3.67 11.43 2.753 129.97 384.7 42.87 76.1

293. 3.75 11.30 2.852 133.32 372.5 41.99 75.3

294. 3.83 11.16 2.959 137.15 360.1 41.09 74.6

295. 3.92 11.01 3.072 141.56 347.4 40.17 73.9

296. 4.00 10.85 3.195 146.73 334.4 39.22 73.2

297. 4.09 10.69 3.327 152.89 321.1 38.24 72.6

298. 4.18 10.51 3.472 160.40 307.4 37.22 72.0

298. 4.19 10.48 3.495 160.40 307.4 37.22 72.0

299. 4.27 10.31 3.633 169.81 293.2 36.15 71.6

300. 4.36 10.10 3.813 182.06 278.4 35.01 71.3

301. 4.45 9.86 4.019 198.85 262.9 33.79 71.4

302. 4.54 9.59 4.262 223.66 246.4 32.44 72.0

303. 4.64 9.25 4.562 265.26 228.7 30.89 73.8

304. 4.74 8.82 4.968 354.78 209.4 28.97 79.0

305. 4.84 8.05 5.703 803.05 188.0 25.91 109.2

305.33 4.8718 6.87 6.87

126
Table B3 . Properties in the single-phase region along isobars

ETHANE ISOBAR AT P = 1.13 •10" 6

MPa

T P Z H S C

V

C

P

W r\ A

K mol'dm kJ/mol J/(mol'K) J/(mol«K)

-1 m« s jzPa»s niW/(m«K)

90.352 21.664 0.000 -14.887 76.65 47.02 66.18 1995.0 1277.81 255.5

90.352 0.15E-05 1.000 3.043 275.09 26.86 35.17 180.9 3.04 2.9

95. 0.14E-05 1.000 3.207 276.87 27.11 35.42 185.3 3.17 3.2

100. 0.14E-05 1.000 3.384 278.69 27.38 35.70 189.9 3.32 3.5

105. 0.13E-05 1.000 3.564 280.44 27.66 35.97 194.3 3.46 3.7

110. 0.12E-05 1.000 3.744 282.12 27.93 36.25 198.7 3.60 4.0

115. 0.12E-05 1.000 3.926 283.74 28.22 36.53 202.9 3.75 4.3

120. 0.11E-05 1.000 4.109 285.30 28.50 36.82 207.0 3.90 4.7

125. 0.11E-05 1.000 4.294 286.81 28.79 37.11 211.1 4.04 5.0

130. 0.10E-05 1.000 4.480 288.27 29.09 37.40 215.0 4.19 5.3

135. 0.10E-05 1.000 4.668 289.69 29.38 37.70 218.8 4.34 5.6

140. 0.97E-06 1.000 4.857 291.06 29.69 38.00 222.6 4.50 5.9

145. 0.94E-06 1.000 5.048 292.40 30.00 38.31 226.3 4.65 6.3

150. 0.91E-06 1.000 5.241 293.71 30.31 38.63 229.9 4.80 6.6

155. 0.88E-06 1.000 5.435 294.98 30.64 38.95 233.4 4.96 7.0

160. 0.85E-06 1.000 5.630 296.22 30.96 39.28 236.9 5.11 7.3

165. 0.82E-06 1.000 5.827 297.43 31.30 39.62 240.3 5.26 7.7

170. 0.80E-06 1.000 6.026 298.62 31.65 39.96 243.6 5.42 8.1

175. 0.78E-06 1.000 6.227 299.79 32.00 40.32 246.9 5.57 8.5

180. 0.76E-06 1.000 6.429 300.93 32.37 40.68 250.1 5.73 8.8

185. 0.73E-06 1.000 6.634 302.05 32.74 41.05 253.3 5.89 9.2

190. 0.72E-06 1.000 6.840 303.15 33.12 41.44 256.4 6.04 9.6

195. 0.70E-06 1.000 7.048 304.23 33.52 41.84 259.4 6.20 10.1

200. 0.68E-06 1.000 7.258 305.29 33.93 42.24 262.4 6.35 10.5

205. 0.66E-06 1.000 7.471 306.34 34.35 42.66 265.3 6.51 10.9

210. 0.65E-06 1.000 7.685 307.37 34.78 43.09 268.2 6.66 11.4

215. 0.63E-06 1.000 7.902 308.39 35.22 43.53 271.1 6.82 11.8

220. 0.62E-06 1.000 8.120 309.40 35.67 43.99 273.9 6.97 12.3

225. 0.60E-06 1.000 8.342 310.39 36.14 44.46 276.6 7.13 12.7

230. 0.59E-06 1.000 8.565 311.37 36.62 44.93 279.3 7.28 13.2

235. 0.58E-06 1.000 8.791 312.35 37.11 45.42 282.0 7.43 13.7

240. 0.57E-06 1.000 9.019 313.31 37.61 45.92 284.7 7.59 14.2

245. 0.55E-06 1.000 9.250 314.26 38.12 46.44 287.3 7.74 14.7

250. 0.54E-06 1.000 9.484 315.20 38.64 46.96 289.8 7.89 15.3

255. 0.53E-06 1.000 9.720 316.14 39.18 47.49 292.4 8.04 15.8

127
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 1.13.10" 6

MPa (continued)

T P Z H S C

V

C

P

W V A

K mol'dm kJ/mol J/(mol.K) J/(mol.K)

-1 m«s /iPa«.'; iriW/(m«K)

260. 0.52E-06 1.000 9.959 317.07 39.72 48.04 294.9 8 .20 16.3

265. 0.51E-06 1.000 10.200 317.99 40.27 48.59 297.3 8 .35 16.9

270. 0.50E-06 1.000 10.444 318.90 40.84 49.15 299.8 8 .50 17.5

275. 0.49E-06 1.000 10.692 319.81 41.41 49.72 302.2 8 .65 18.1

280. 0.49E-06 1.000 10.942 320.71 41.99 50.30 304.6 8 .80 18.6

285. 0.48E-06 1.000 11.195 321.60 42.57 50.89 306.9 8 .94 19.2

290. 0.47E-06 1.000 11.451 322.49 43.17 51.48 309.2 9 .09 19.9

295. 0.46E-06 1.000 11.710 323.38 43.77 52.09 311.6 9 .24 20.5

300. 0.45E-06 1.000 11.971 324.26 44.38 52.69 313.8 9 .39 21.1

310. 0.44E-06 1.000 12.505 326.01 45.61 53.93 318.3 9 .68 22.4

320. 0.42E-06 1.000 13.050 327.74 46.86 55.18 322.8 9 .97 23.8

330. 0.41E-06 1.000 13.608 329.46 48.13 56.45 327.1 10 .25 25.2

340. 0.40E-06 1.000 14.179 331.16 49.41 57.73 331.4 10 .54 26.6

350. 0.39E-06 1.000 14.763 332.85 50.70 59.02 335.6 10 .82 28.1

360. 0.38E-06 1.000 15.359 334.53 52.00 60.31 339.8 11 .10 29.6

370. 0.37E-06 1.000 15.969 336.20 53.30 61.61 343.9 11 .38 31.1

380. 0.36E-06 1.000 16.592 337.86 54.60 62.91 348.0 11,.65 32.7

390. 0.35E-06 1.000 17.227 339.51 55.90 64.21 352.0 11,,92 34.3

400. 0.34E-06 1.000 17.876 341.16 57.19 65.51 355.9 12,.19 36.0

410. 0.33E-06 1.000 18.537 342.79 58.48 66.80 359.8 12 ,46 37.6

420. 0.32E-06 1.000 19.212 344.41 59.77 68.08 363.7 12,,72 39.3

430. 0.32E-06 1.000 19.899 346.03 61.04 69.36 367.5 12, 99 41.1

440. 0.31E-06 1.000 20.599 347.64 62.31 70.62 371.3 13. 25 42.8

450. 0.30E-06 1.000 21.311 349.24 63.57 71.88 375.1 13. 50 44.6

460. 0.30E-06 1.000 22.036 350.84 64.81 73.13 378.8 13. 76 46.4

470. 0.29E-06 1.000 22.774 352.42 66.05 74.36 382.5 14. 01 48.2

480. 0.28E-06 1.000 23.524 354.00 67.27 75.58 386.2 14. 26 50.0

490. 0.28E-06 1.000 24.285 355.57 68.48 76.79 389.8 14. 51 51.9

500. 0.27E-06 1.000 25.059 357.13 69.67 77.99 393.4 14. 76 53.8

520. 0.26E-06 1.000 26.643 360.24 72.03 80.34 400.5 57.6

540. 0.25E-06 1.000 28.273 363.31 74.32 82.64 407.5 61.5

560. 0.24E-06 1.000 29.948 366.36 76.57 84.89 414.3 65.4

580. 0.23E-06 1.000 31.668 369.38 78.76 87.08 421.1 69.3

600. 0.23E-06 1.000 33.431 372.37 80.91 89.22 427.7 73.3

625. 0.22E-06 1.000 35.694 376.06 83.51 91.83 435.9

128
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0100 MPa

T P Z H S C

V

C

P

W V A

K mo 1 • dm kJ/mol J/(mol»K) J/(mol«K) m»s 1

/xPa»s ir W/(m- K

95. 20.503 0.001 -14.572 80.04 47.93 68.71 1970 2 1057 22 252 1

100. 21.325 0.001 -14.225 83.61 48.15 70.12 1938 3 878 06 248 2 105. 21.144 0.001 -13.873 87.04 47.89 70.70 1903 9 742 13 243 9 110. 20.963 0.001 -13.519 90.34 47.39 70.82 1868 3 637 08 239 5 115. 20.780 0.001 -13.165 93.48 46.78 70.72 1832 1 554 40 235

120. 20.596 0.000 -12.812 96.49 46.14 70.52 1795 5 488 19 230 3 125. 20.411 0.000 -12.460 99.36 45.53 70.32 1758 8 434 30 225 5 130. 20.225 0.000 -12.108 102.12 44.97 70.15 1721 9 389 79 220 7 135. 20.039 0.000 -11.758 104.76 44.47 70.05 1684 9 352 52 215 8

140. 19.851 0.000 -11.408 107.31 44.04 70.01 1647 8 320 93 210 9

145. 19.661 0.000 -11.058 109.77 43.68 70.06 1610 6 293 84 206

150. 19.470 0.000 -10.707 112.14 43.38 70.18 1573 3 270 37 201

150.393 19.455 0.000 -10.679 112.33 43.36 70.20 1570 4 268 66 200 6 150.393 0.0080 0.996 5.261 218.32 27.15 35.03 230 8 4 81 6 7 155. 0.0078 0.995 5.428 219.41 29.06 37.24 233 4 4 96 7

160. 0.0076 0.995 5.618 220.62 30.22 38.55 236 5 5 11 7 4

165. 0.0073 0.996 5.813 221.82 30.95 39.34 239 8 5 26 7 7 170. 0.0071 0.996 6.011 223.00 31.49 39.90 243 1 5 42 8 1

175. 0.0069 0.996 6.212 224.17 31.94 40.36 246 4 5 58 8 5 180. 0.0067 0.997 6.414 225.31 32.35 40.77 249 6 5 73 8 9

185. 0.0065 0.997 6.619 226.43 32.75 41.17 252 8 5 89 9 3 190. 0.0063 0.997 6.826 227.53 33.15 41.56 255 9 6 04 9 7 195. 0.0062 0.997 7.035 228.62 33.55 41.96 259 6 20 10 1 200. 0.0060 0.997 7.246 229.69 33.96 42.36 262 6 35 10 5 205. 0.0059 0.998 7.458 230.74 34.38 42.78 264 9 6 51 10 9

210. 0.0057 0.998 7.673 231.77 34.81 43.20 267 8 6 66 11 4

215. 0.0056 0.998 7.891 232.79 35.25 43.64 270 7 6 82 11 8

220. 0.0055 0.998 8.110 233.80 35.71 44.09 273 5 6 97 12 3 225. 0.0054 0.998 8.331 234.80 36.17 44.55 276 3 7 13 12 8 230. 0.0052 0.998 8.555 235.78 36.65 45.02 279 7 28 13 2

235. 0.0051 0.998 8.782 236.76 37.14 45.50 281 7 7 44 13 7 240. 0.0050 0.999 9.010 237.72 37.64 46.00 284 4 7 59 14 2 245. 0.0049 0.999 9.242 238.67 38.15 46.51 287 7 74 14 8 250. 0.0048 0.999 9.475 239.62 38.67 47.03 289 6 7 89 15 3 255. 0.0047 0.999 9.712 240.55 39.20 47.55 292 1 8 05 15 8

260. 0.0046 0.999 9.951 241.48 39.74 48.09 294 6 8 20 16 4

265. 0.0045 0.999 10.193 242.40 40.29 48.64 297 1 8 35 16 9

270. 0.0045 0.999 10.437 243.32 40.85 49.20 299 6 8 50 17 5 275. 0.0044 0.999 10.685 244.23 41.42 49.77 302 8 65 18 1

280. 0.0043 0.999 10.935 245.13 42.00 50.35 304 4 8 80 18 7

129
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0100 MPa (continued)

T P Z H S C

V

C

P

W n A

K mol'dm kJ/mol J/(mol»K) J/(mol«K) m« s -1 fi?a» i3 ITiW/(m.K)

285. 0.0042 0.999 11.188 246.02 42.59 50.93 306 .7 8 .95 19.3

290. 0.0042 0.999 11.445 246.92 43.18 51.52 309 .1 9 .09 19.9

295. 0.0041 0.999 11.704 247.80 43.78 52.12 311 .4 9 .24 20.5

300. 0.0040 0.999 11.966 248.68 44.39 52.73 313 .7 9 .39 21.1

310. 0.0039 0.999 12.499 250.43 45.62 53.96 318 .2 9 .68 22.4

320. 0.0038 0.999 13.045 252.16 46.87 55.21 322 .6 9 .97 23.8

330. 0.0036 0.999 13.603 253.88 48.14 56.47 327 .0 10 .26 25.2

340. 0.0035 0.000 14.175 255.59 49.42 57.75 331 .3 10 .54 26.6

350. 0.0034 0.000 14.758 257.28 50.71 59.04 335 .5 10 .82 28.1

360. 0.0033 0.000 15.355 258.96 52.00 60.33 339 .7 11 .10 29.6

370. 0.0033 0.000 15.965 260.63 53.30 61.63 343 .8 11 .38 31.1

380. 0.0032 0.000 16.588 262.29 54.60 62.93 347 .9 11 .65 32.7

390. 0.0031 1.000 17.224 263.94 55.90 64.23 351 .9 11,,92 34.3

400. 0.0030 1.000 17.873 265.59 57.20 65.52 355 .9 12 ,19 36.0

410. 0.0029 1.000 18.534 267.22 58.49 66.81 359 .8 12,,46 37.6

420. 0.0029 1.000 19.209 268.85 59.77 68.09 363 ,7 12,,73 39.3

430. 0.0028 1.000 19.896 270.46 61.05 69.37 367,,5 12,.99 41.1

440. 0.0027 1.000 20.596 272.07 62.31 70.64 371,,3 13,.25 42.8

450. 0.0027 1.000 21.309 273.67 63.57 71.89 375,.1 13,,51 44.6

460. 0.0026 1.000 22.034 275.27 64.81 73.14 378,,8 13, 76 46.4

470. 0.0026 1.000 22.771 276.85 66.05 74.37 382,,5 14. 01 48.2

480. 0.0025 1.000 23.521 278.43 67.27 75.59 386, 1 14, 27 50.0

490. 0.0025 1.000 24.283 280.00 68.48 76.80 389, 8 14, 51 51.9

500. 0.0024 1.000 25.057 281.57 69.67 78.00 393, 4 14. 76 53.8

520. 0.0023 1.000 26.641 284.67 72.03 80.35 400. 4 57.6

540. 0.0022 1.000 28.271 287.75 74.33 82.65 407. 4 61.5

560. 0.0021 1.000 29.946 290.79 76.57 84.89 414. 3 65.4

580. 0.0021 1.000 31.666 293.81 78.76 87.08 421. 1 69.3

600. 0.0020 1.000 33.429 296.80 80.91 89.23 427. 7 73.4

625. 0.0019 1.000 35.693 300.50 83.51 91.83 435. 9

130
Table B3. Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0250 MPa

T P Z H S C

V

C

P

W n A

K mol«dm kJ/mol J/(mol«K) J/(mol»K) m»s

-1 /xPa«s it W/(m -K

95. 21.503 0.001 -14.572 80.04 47.93 68.71 1970 3 1057 35 252 1

100. 21.325 0.001 -14.224 83.61 48.15 70.11 1938 4 878 16 248 2 105. 21.145 0.001 -13.872 87.04 47.89 70.70 1904 742 22 243 9

110. 20.963 0.001 -13.518 90.34 47.39 70.82 1868 4 637 15 239 5 115. 20.780 0.001 -13.164 93.48 46.78 70.72 1832 2 554 46 235

120. 20.596 0.001 -12.811 96.49 46.14 70.52 1795 6 488 24 230 3 125. 20.411 0.001 -12.459 99.36 45.53 70.32 1758 9 434 34 225 6

130. 20.226 0.001 -12.108 102.12 44.97 70.15 1722 389 83 220 7 135. 20.039 0.001 -11.757 104.76 44.47 70.05 1685 352 56 215 8

140. 19.851 0.001 -11.407 107.31 44.04 70.01 1647 9 320 96 210 9

145. 19.662 0.001 -11.057 109.77 43.68 70.06 1610 7 293 87 206

150. 19.471 0.001 -10.707 112.14 43.38 70.18 1573 4 270 40 201

155. 19.278 0.001 -10.355 114.45 43.14 70.38 1536 249 86 196

160. 19.083 0.001 -10.003 116.69 42.95 70.65 1498 5 231 74 191 1

162.094 19.001 0.001 -9.854 117.61 42.88 70.79 1482 8 224 77 189

162.094 0.0187 0.990 5.694 213.53 27.90 35.99 238 1 5 18 7 6 165. 0.0184 0.990 5.801 214.18 29.22 37.50 239 6 5 27 7 8

170. 0.0179 0.990 5.992 215.33 30.66 39.12 242 5 5 42 8 2 175. 0.0173 0.991 6.191 216.47 31.55 40.09 245 7 5 58 8 5 180. 0.0168 0.991 6.393 217.61 32.18 40.74 248 9 5 73 8 9

185. 0.0164 0.992 6.598 218.74 32.69 41.26 252 5 89 9 3 190. 0.0159 0.993 6.805 219.84 33.15 41.70 255 2 6 04 9 7 195. 0.0155 0.993 7.015 220.93 33.58 42.12 258 3 6 20 10 1 200. 0.0151 0.994 7.227 222.00 34.00 42.53 261 3 6 36 10 5 205. 0.0148 0.994 7.440 223.06 34.43 42.95 264 3 6 51 11

210. 0.0144 0.995 7.656 224.10 34.86 43.37 267 3 6 67 11 4

215. 0.0141 0.995 7.874 225.12 35.30 43.79 270 2 6 82 11 9 220. 0.0137 0.995 8.094 226.14 35.76 44.23 273 6 98 12 3 225. 0.0134 0.996 8.316 227.13 36.22 44.69 275 8 7 13 12 8

230. 0.0131 0.996 8.541 228.12 36.69 45.15 278 6 7 29 13 3

235. 0.0128 0.996 8.768 229.10 37.18 45.62 281 3 7 44 13 8

240. 0.0126 0.996 8.997 230.06 37.67 46.11 284 7 59 14 3 245. 0.0123 0.997 9.229 231.02 38.18 46.61 286 6 7 75 14 8 250. 0.0121 0.997 9.463 231.97 38.70 47.13 289 2 7 90 15 3

255. 0.0118 0.997 9.700 232.90 39.23 47.65 291 8 8 05 15 8

260. 0.0116 0.997 9.940 233.84 39.77 48.18 294 3 8 20 16 4

265. 0.0114 0.997 10.182 234.76 40.32 48.73 296 8 8 35 16 9 270. 0.0112 0.997 10.427 235.67 40.88 49.28 299 2 8 50 17 5 275. 0.0110 0.998 10.675 236.58 41.45 49.84 301 7 8 65 18 1 280. 0.0108 0.998 10.925 237.49 42.02 50.42 304 1 8 80 18 7

131
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0250 MPa (continued)

T P z H S C

V C

p W 1

A

K mol'dm kJ/mol J/(mol-K) J/(mol»K) m»s

l /iPa* ! 5 niW/(m >K

285. 0.0106 998 11.179 238.38 42.61 51.00 306 5 8 95 19 .3 290. 0.0104 .998 11.435 239.28 43.20 51.59 308 8 9 10 19 .9 295. 0.0102 .998 11.695 240.16 43.80 52.18 311 .1 9 24 20 .5 300. 0.0100 998 11.957 241.05 44.41 52.78 313 .4 9 39 21 .1

310. 0.0097 998 12.491 242.80 45.63 54.01 318 9 68 22 .5

320. 0.0094 998 13.037 244.53 46.88 55.25 322 4 9 97 23 .8 330. 0.0091 999 13.596 246.25 48.15 56.51 326 8 10 26 25 2 340. 0.0089 999 14.168 247.96 49.43 57.79 331 1 10 54 26 6 350. 0.0086 999 14.752 249.65 50.72 59.07 335 4 10 83 28 1 360. 0.0084 999 15.349 251.33 52.01 60.36 339 5 11 11 29 6

370. 0.0081 999 15.959 253.00 53.31 61.66 343 7 11 38 31 1 380. 0.0079 999 16.582 254.66 54.61 62.96 347 7 11 66 32 7 390. 0.0077 999 17.219 256.32 55.91 64.25 351 8 11 93 34 3 400. 0.0075 999 17.868 257.96 57.20 65.55 355 7 12 20 36

410. 0.0073 999 18.529 259.59 58.49 66.83 359 7 12 46 37 6

420. 0.0072 999 19.204 261.22 59.77 68.11 363 6 12 73 39 3 430. 0.0070 999 19.892 262.84 61.05 69.39 367 4 12 99 41 1 440. 0.0068 999 20.592 264.45 62.32 70.65 371 2 13 25 42 8 450. 0.0067 1 000 21.305 266.05 63.57 71.91 375 13 51 44 6 460. 0.0065 1 000 22.030 267.64 64.82 73.15 378 7 13 76 46 4

470. 0.0064 1 000 22.768 269.23 66.05 74.38 382 4 14 02 48 2 480. 0.0063 1 000 23.518 270.81 67.27 75.60 386 1 14 27 50 1 490. 0.0061 1 000 24.280 272.38 68.48 76.81 389 7 14 52 51 9

500. 0.0060 1 000 25.054 273.94 69.68 78.01 393 3 14 76 53 8

520. 0.0058 1 000 26.638 277.05 72.03 80.36 400 4 57 6

540. 0.0056 1 000 28.268 280.13 74.33 82.66 407 4 61 5 560. 0.0054 1 000 29.944 283.17 76.57 84.90 414 3 65 4

580. 0.0052 1 000 31.664 286.19 78.77 87.09 421 69. 3 600. 0.0050 1 000 33.427 289.18 80.91 89.23 427. 7 73. 4

625. 0.0048 1 000 35.690 292.87 83.51 91.84 435. 9

-132-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0500 MPa

T P z H

i C

V C

p W n A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol«K) m« s

-

^Pa«

3 ITiW/(m>»K

95. 21.503 .003 -14.571 80 .04 47.93 68.71 1970 .4 1057 .57 252 .1

100. 21.325 .003 -14.223 83 .60 48.15 70.11 1938 .5 878 .34 248 .2 105. 21.145 .003 -13.871 87 .04 47.89 70.70 1904 .1 742 .36 244 .0

110. 20.963 .003 -13.517 90 .33 47.39 70.82 1868 .5 637 .27 239 .6 115. 20.780 .003 -13.163 93 .48 46.78 70.72 1832 .3 554 .56 235 .0

120. 20.596 .002 -12.810 96 .49 46.14 70.52 1795 .7 488 .32 230 .3 125. 20.412 .002 -12.458 99 .36 45.53 70.32 1759 .0 434 .41 225 .6 130. 20.226 .002 -12.107 102 .11 44.97 70.15 1722 .1 389 .89 220 .7 135. 20.039 .002 -11.756 104 .76 44.48 70.04 1685 .1 352 .61 215 .8 140. 19.851 .002 -11.406 107 .31 44.05 70.01 1648 .0 321 .01 210 .9

145. 19.662 .002 -11.056 109 .76 43.68 70.06 1610 .8 293 .92 206 .0 150. 19.471 .002 -10.706 112 .14 43.38 70.18 1573 .5 270 .44 201 .0 155. 19.278 .002 -10.354 114 .45 43.14 70.38 1536 .2 249 .91 196 .1 160. 19.083 .002 -10.002 116 .68 42.95 70.65 1498 .7 231 .78 191 .1 165. 18.886 .002 -9.648 118 .86 42.81 70.99 1461 .1 215 .66 186 .1

170. 18.687 .002 -9.292 120 .99 42.71 71.40 1423 .3 201 .22 181 .2 172.410 18.589 .002 -9.119 121 .99 42.68 71.62 1405 .1 194,.77 178 .9 172.410 0.0355 ,981 6.063 210 .05 29.12 37.58 243 .5 5,,50 8 .4

175. 0.0350 0.,982 6.162 210 .62 30.17 38.77 244 ,8 5,,58 8 .6 180. 0.0340 ,983 6.360 211 .74 31.54 40.27 247 ,8 5 74 9 .0

185. 0.0330 .984 6.563 212 .85 32.41 41.19 250 ,9 5 89 9 .4 190. 0.0321 0,.985 6.771 213 .96 33.05 41.84 254 ,0 6,,05 9 .8 195. 0.0313 0.,986 6.982 215 .05 33.58 42.35 257 ,2 6 20 10 ,2

200. 0.0305 0. 987 7.194 216 .13 34.05 42.80 260 ,3 6,,36 10 .6 205. 0.0297 0, 988 7.410 217 ,19 34.50 43.22 263, 3 6, 52 11 ,0

210. 0.0290 0,,989 7.627 218,,24 34.94 43.64 266, 3 6, 67 11,,5

215. 0.0283 0, 990 7.846 219,,27 35.38 44.05 269, 3 6, 83 11, 9 220. 0.0276 0,,990 8.067 220,,29 35.84 44.48 272,,1 6, 98 12,,4

225. 0.0270 0. 991 8.291 221,,30 36.29 44.92 275. 7, 14 12, 8 230. 0.0264 0. 992 8.516 222. 29 36.76 45.37 277. 8 7, 29 13, 3

235. 0.0258 0. 992 8.744 223.,27 37.25 45.83 280. 6 7. 44 13, 8 240. 0.0252 0. 993 8.975 224. 24 37.74 46.31 283. 3 7. 60 14. 3 245. 0.0247 0. 993 9.208 225. 20 38.24 46.79 285. 9 7. 75 14. 8 250. 0.0242 0. 994 9.443 226. 15 38.76 47.29 288. 6 7. 90 15. 3 255. 0.0237 0. 994 9.680 227. 09 39.28 47.81 291. 1 8. 05 15. 9

260. 0.0233 0. 994 9.921 228. 02 39.82 48.33 293. 7 8. 21 16. 4

265. 0.0228 0. 995 10.164 228. 95 40.36 48.87 296. 2 8. 36 17.

270. 0.0224 0. 995 10.409 229. 87 40.92 49.41 298. 7 8. 51 17. 5 275. 0.0220 0. 995 10.658 230. 78 41.49 49.97 301. 2 8. 66 18. 1 280. 0.0216 0. 995 10.909 231. 68 42.06 50.53 303. 6 8. 81 18. 7

133
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0500 MPa (continued)

T P z H S C

V C

p W V A

K mo 1 • dm kJ/mol J/(mol.K) J/(mol«K) m»s

l ^Pa«s itiW/(m-•K

285. 0.0212 .996 11.163 232.58 42.64 51.11 306 .0 8 .95 19 .3 290. 0.0208 .996 11.420 233.48 43.23 51.69 308 .4 9 .10 19 .9 295. 0.0205 .996 11.680 234.37 43.83 52.28 310 .7 9 ,25 20 .5 300. 0.0201 .996 11.943 235.25 44.43 52.88 313 .0 9 .40 21 .2 310. 0.0195 .997 12.478 237.00 45.66 54.09 317 .6 9 .69 22 .5

320. 0.0188 .997 13.025 238.74 46.90 55.33 322 .1 9 .98 23 .8 330. 0.0183 .997 13.584 240.46 48.17 56.58 326 .5 10 .26 25 .2 340. 0.0177 .998 14.157 242.17 49.44 57.85 330 .8 10 ,55 26 .6 350. 0.0172 .998 14.741 243.86 50.73 59.13 335 ,1 10 .83 28 .1 360. 0.0167 .998 15.339 245.55 52.02 60.42 339 ,3 11 .11 29 .6

370. 0.0163 .998 15.950 247.22 53.32 61.71 343 ,4 11 ,39 31 .1 380. 0.0159 .998 16.573 248.88 54.62 63.00 347 .5 11 ,66 32 .7 390. 0.0154 .998 17.210 250.54 55.92 64.29 351 ,6 11 93 34 .3 400. 0.0151 .999 17.859 252.18 57.21 65.58 355 ,6 12 ,20 36 .0 410. 0.0147 .999 18.521 253.82 58.50 66.87 359 ,5 12 47 37 .6

420. 0.0143 .999 19.197 255.44 59.78 68.15 363 4 12, 73 39 .3 430. 0.0140 .999 19.884 257.06 61.06 69.42 367,,3 13, 00 41 .1 440. 0.0137 .999 20.585 258.67 62.32 70.68 371 1 13, 26 42 .8 450. 0.0134 .999 21.298 260.27 63.58 71.94 374 9 13, 51 44 ,6

460. 0.0131 .999 22.024 261.87 64.82 73.18 378, 6 13. 77 46 .4

470. 0.0128 .999 22.762 263.46 66.05 74.41 382, 3 14. 02 48 .2 480. 0.0125 ,999 23.512 265.04 67.28 75.63 386, 14. 27 50 ,1

490. 0.0123 .999 24.274 266.61 68.48 76.83 389, 6 14. 52 51, 9 500. 0.0120 ,999 25.048 268.17 69.68 78.03 393. 2 14. 77 53, 8 520. 0.0116 ,999 26.633 271.28 72.03 80.38 400. 3 57, 6

540. 0.0111 1.,000 28.263 274.36 74.33 82.67 407. 3 61. 5 560. 0.0107 1,,000 29.939 277.40 76.58 84.92 414. 2 65. 4

580. 0.0104 1. 000 31.659 280.42 78.77 87.11 421. 69. 4

600. 0.0100 1, 000 33.423 283.41 80.91 89.25 427. 7 73. 4

625. 0.0096 1.,000 35.687 287.11 83.52 91.85 435. 9

134
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0750 MPa

T P z H S C

V C

p W n

A

K mol'dm kJ/mol J/(mol-K) J/(mol«K) m« s

i /xPa* < 3 IT W/(m -K

95. 21.504 004 -14.570 80 04 47.93 68.71 1970 5 1057 80 252 1 100. 21.326 004 -14.222 83 60 48.15 70.11 1938 6 878 51 248 .2 105. 21.145 004 -13.870 87 04 47.89 70.69 1904 2 742 50 244

110. 20.963 004 -13.516 90 33 47.39 70.82 1868 6 637 38 239 .6 115. 20.780 004 -13.162 93 48 46.78 70.71 1832 4 554 65 235

120. 20.597 004 -12.809 96 48 46.15 70.52 1795 8 488 40 230 3 125. 20.412 004 -12.457 99 36 45.53 70.31 1759 1 434 49 225 6 130. 20.226 003 -12.106 102 11 44.97 70.15 1722 2 389 96 220 7 135. 20.040 003 -11.755 104 76 44.48 70.04 1685 2 352 67 215 9 140. 19.852 003 -11.405 107 30 44.05 70.01 1648 1 321 07 210 9

145. 19.663 003 -11.055 109 76 43.68 70.06 1611 293 97 206

150. 19.472 003 -10.705 112 14 43.38 70.18 1573 7 270 49 201

155. 19.279 003 -10.353 114 44 43.14 70.38 1536 3 249 95 196 1 160. 19.084 003 -10.001 116 68 42.95 70.65 1498 8 231 83 191 1 165. 18.887 003 -9.647 118 86 42.81 70.99 1461 2 215 70 186 2

170. 18.687 003 -9.291 120 99 42.72 71.40 1423 5 201 26 181 3 175. 18.485 003 -8.933 123 06 42.66 71.87 1385 7 188 22 176 4

179.155 18.314 003 -8.633 124 75 42.65 72.32 1354 1 178 31 172 3 179.155 0.0517 974 6.296 208 08 30.13 38.95 246 5 5 71 9 180. 0.0514 974 6.329 208 27 30.46 39.32 246 9 5 74 9 1

185. 0.0500 976 6.530 209 37 31.92 40.90 249 8 5 89 9 4

190. 0.0486 978 6.737 210 47 32.85 41.86 252 9 6 05 9 8 195. 0.0472 979 6.948 211 57 33.52 42.52 256 6 21 10 2 200. 0.0460 981 7.162 212 65 34.06 43.04 259 2 6 36 10 7 205. 0.0448 982 7.379 213 72 34.55 43.49 262 3 6 52 11 1

210. 0.0437 983 7.597 214 78 35.01 43.91 265 3 6 68 11 5 215. 0.0426 985 7.818 215 81 35.46 44.32 268 3 6 83 12

220. 0.0416 986 8.040 216 84 35.91 44.73 271 3 6 99 12 4

225. 0.0406 987 8.265 217 85 36.37 45.16 274 2 7 14 12 9 230. 0.0397 987 8.492 218 84 36.84 45.59 277 7 30 13 3

235. 0.0388 988 8.721 219 83 37.31 46.04 279 8 7 45 13 8 240. 0.0380 989 8.952 220 80 37.80 46.50 282 6 7 60 14 3 245. 0.0372 990 9.186 221 77 38.30 46.98 285 3 7 76 14 8 250. 0.0364 990 9.422 222 72 38.81 47.47 287 9 7 91 15 4

255. 0.0357 991 9.661 223 67 39.33 47.97 290 5 8 06 15 9

260. 0.0350 991 9.902 224 60 39.87 48.48 293 1 8 21 16 4

265. 0.0343 992 10.145 225 53 40.41 49.01 295 7 8 36 17

270. 0.0337 992 10.392 226 45 40.96 49.54 298 2 8 51 17 6 275. 0.0330 993 10.641 227 37 41.52 50.09 300 7 8 66 18 1 280. 0.0324 993 10.893 228 27 42.10 50.65 303 1 8 81 18 7

-135
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.0750 MPa (continued)

T P z H S C

V C

p W V A

K mol»dm kJ/mol J/(mol.K) J/(mol^K) m*s

• l /iPa* 53 niW/(m-•K

285. 0.0319 .994 11.147 229.17 42.68 51.22 305 .5 8 .96 19 .3 290. 0.0313 .994 11.405 230.07 43.26 51.79 307 .9 9 .11 19 .9 295. 0.0308 .994 11.665 230.96 43.86 52.38 310 .3 9 .26 20 .6 300. 0.0302 .994 11.929 231.85 44.46 52.97 312 .6 9 .40 21 .2 310. 0.0292 .995 12.464 233.60 45.68 54.17 317 .2 9 .69 22 .5

320. 0.0283 .995 13.012 235.34 46.93 55.40 321 .7 9 .98 23 .8 330. 0.0274 .996 13.573 237.07 48.19 56.65 326 .2 10 .27 25 .2 340. 0.0266 .996 14.145 238.78 49.46 57.91 330 .5 10 .55 26 .7 350. 0.0259 .997 14.731 240.47 50.74 59.19 334 .8 10 .84 28 .1 360. 0.0251 .997 15.329 242.16 52.04 60.47 339 .1 11 .12 29 .6

370. 0.0244 .997 15.940 243.83 53.33 61.76 343 .2 11 ,39 31 .2 380. 0.0238 .997 16.564 245.50 54.63 63.04 347 .3 11 ,67 32 .7 390. 0.0232 .998 17.201 247.15 55.92 64.33 351 ,4 11 ,94 34 .3 400. 0.0226 ,998 17.851 248.80 57.22 65.62 355 .4 12.,21 36 .0 410. 0.0220 ,998 18.514 250.43 58.51 66.90 359 ,3 12.,47 37 .7

420. 0.0215 0,,998 19.189 252.06 59.79 68.18 363 .2 12. 74 39 ,4

430. 0.0210 0,,998 19.877 253.68 61.06 69.45 367 1 13. 00 41 1 440. 0.0205 998 20.578 255.29 62.33 70.71 370,.9 13. 26 42 ,8

450. 0.0201 0.,999 21.291 256.89 63.58 71.96 374. 7 13. 52 44,.6 460. 0.0196 0. 999 22.017 258.49 64.83 73.20 378. 5 13. 77 46, 4

470. 0.0192 0. 999 22.755 260.08 66.06 74.43 382. 2 14. 03 48, 2 480. 0.0188 0, 999 23.506 261.66 67.28 75.65 385. 9 14. 28 50, 1 490. 0.0184 0, 999 24.268 263.23 68.49 76.86 389. 5 14. 53 51. 9

500. 0.0181 0. 999 25.043 264.79 69.68 78.05 393. 1 14. 77 53. 8 520. 0.0174 0. 999 26.627 267.90 72.04 80.40 400. 3 57. 6

540. 0.0167 0. 999 28.258 270.98 74.33 82.69 407. 3 61. 5 560. 0.0161 0. 999 29.935 274.02 76.58 84.93 414. 2 65. 4

580. 0.0156 1. 000 31.655 277.04 78.77 87.12 421. 69. 4

600. 0.0150 1. 000 33.419 280.03 80.91 89.26 427. 6 73. 4

625. 0.0144 1. 000 35.683 283.73 83.52 91.86 435. 9

-136-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.1000 MPa

T P z H

i C

V C

p W V

A

K mol«dm kJ/mol J/(mol'K) J/(mol-K) m« s

-

/iPa*3 iriW/(m •K

95. 21.504 .006 -14.569 80 .04 47.93 68.71 1970 .6 1058 .02 252 .2

100. 21.326 .006 -14.221 83 .60 48.15 70.11 1938 .7 878 .69 248 .2

105. 21.146 .005 -13.869 87 .04 47.90 70.69 1904 .3 742 .64 244 .0

110. 20.964 .005 -13.515 90 .33 47.39 70.82 1868 .7 637 .50 239 .6

115. 20.781 .005 -13.161 93 .48 46.78 70.71 1832 .5 554 .75 235 .0

120. 20.597 .005 -12.808 96 .48 46.15 70.52 1796 .0 488 .49 230 .4

125. 20.412 .005 -12.456 99 .36 45.54 70.31 1759 .2 434 .56 225 .6

130. 20.227 .005 -12.105 102 .11 44.98 70.15 1722 .3 390 .02 220 .8 135. 20.040 .004 -11.755 104 .76 44.48 70.04 1685 .4 352 .73 215 .9 140. 19.852 .004 -11.404 107 .30 44.05 70.01 1648 .3 321 .12 211 .0

145. 19.663 .004 -11.054 109 .76 43.68 70.05 1611 .1 294 .02 206 .0

150. 19.472 .004 -10.704 112 .14 43.38 70.18 1573 .8 270 .54 201 .1 155. 19.279 .004 -10.352 114 .44 43.14 70.37 1536 .5 250 .00 196 .1

160. 19.085 .004 -10.000 116 .68 42.95 70.65 1499 .0 231 .87 191 .1 165. 18.888 .004 -9.646 118 .86 42.81 70.99 1461 .4 215 .75 186 .2

170. 18.688 .004 -9.290 120 .98 42.72 71.40 1423 .7 201 .30 181 .3 175. 18.486 .004 -8.932 123 .06 42.67 71.87 1385 .9 188 .26 176 .4

180. 18.280 .004 -8.571 125 .09 42.65 72.41 1347 .8 176 .42 171 .5 184.309 18.100 ,004 -8.258 126 .81 42.67 72.93 1315 .0 167 ,06 167 .4 184.309 0.0675 .967 6.470 206 .72 30.99 40.15 248 .5 5 .88 9 .5

185. 0.0672 ,968 6.498 206 ,87 31.23 40.41 248 .8 5 .90 9 .5 190. 0.0653 .970 6.704 207 ,97 32.55 41.80 251 .8 6 .06 9 .9 195. 0.0634 .972 6.915 209 ,06 33.41 42.66 254 ,9 6 .21 10 ,3

200. 0.0617 0..974 7.130 210 ,15 34.06 43.27 258 .1 6 37 10 .7 205. 0.0601 0. 976 7.347 211 .23 34.59 43.75 261 .2 6 52 11 .1

210. 0.0586 0. 978 7.567 212,,29 35.08 44.18 264 ,3 6. 68 11.,6

215. 0.0571 0. 979 7.789 213..33 35.54 44.59 267. 4 6. 84 12,.0 220. 0.0557 0. 981 8.013 214. 36 35.99 44.99 270. 4 6. 99 12 .5 225. 0.0544 0. 982 8.239 215. 38 36.45 45.40 273,,3 7. 15 12, 9 230. 0.0532 0. 983 8.467 216, 38 36.91 45.82 276, 2 7. 30 13, 4

235. 0.0520 0. 984 8.697 217. 37 37.38 46.25 279. 1 7. 45 13, 9 240. 0.0509 0. 985 8.930 218. 35 37.87 46.70 281. 8 7. 61 14, 4

245. 0.0498 0. 986 9.164 219. 32 38.36 47.16 284. 6 7. 76 14. 9 250. 0.0487 0. 987 9.401 220. 27 38.87 47.64 287. 3 7. 91 15. 4

255. 0.0477 0. 988 9.641 221. 22 39.39 48.13 289. 9 8. 07 15. 9

260. 0.0468 0. 989 9.883 222. 16 39.92 48.63 292. 5 8. 22 16. 5 265. 0.0459 0. 989 10.127 223. 09 40.46 49.15 295. 1 8. 37 17.

270. 0.0450 0. 990 10.374 224. 02 41.00 49.68 297. 7 8. 52 17. 6 275. 0.0442 0. 990 10.624 224. 93 41.56 50.22 300. 2 8. 67 18. 2 280. 0.0434 0. 991 10.876 225. 84 42.13 50.77 302. 6 8. 82 18. 8

137-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.1000 MPa (continued)

T P z H S C

V C

p W r\ A

K mol»dm kJ/mol J/(mol»K) J/(mol»K) m»s

l ^Pa«

!

3 ITiW/(m-K)

285. 0.0426 991 11.132 226.75 42.71 51.33 305 1 8 97 19.3

290. 0.0418 992 11.390 227.64 43.29 51.90 307 5 9 11 20.0

295. 0.0411 992 11.651 228.53 43.89 52.48 309 9 9 26 20.6

300. 0.0404 993 11.914 229.42 44.49 53.06 312 2 9 41 21.2

310. 0.0391 993 12.451 231.18 45.71 54.26 316 9 9 70 22.5

320. 0.0378 994 13.000 232.92 46.95 55.48 321 4 9 99 23.9

330. 0.0366 995 13.561 234.65 48.20 56.72 325 9 10 28 25.2

340. 0.0356 995 14.134 236.36 49.48 57.97 330 3 10 56 26.7

350. 0.0345 995 14.720 238.06 50.76 59.24 334 6 10 84 28.1

360. 0.0335 996 15.319 239.75 52.05 60.52 338 8 11 12 29.6

370. 0.0326 996 15.931 241.42 53.34 61.80 343 11 40 31.2

380. 0.0318 997 16.555 243.09 54.64 63.09 347 1 11 67 32.8

390. 0.0309 997 17.192 244.74 55.93 64.38 351 2 11 94 34.4

400. 0.0302 997 17.843 246.39 57.23 65.66 355 2 12 21 36.0

410. 0.0294 997 18.506 248.03 58.51 66.94 359 2 12 48 37.7

420. 0.0287 998 19.181 249.65 59.79 68.21 363 1 12 74 39.4

430. 0.0280 998 19.870 251.27 61.07 69.48 367 13 01 41.1

440. 0.0274 998 20.571 252.89 62.33 70.74 370 8 13 27 42.8

450. 0.0268 998 21.285 254.49 63.59 71.99 374 6 13 52 44.6

460. 0.0262 998 22.011 256.09 64.83 73.23 378 4 13 78 46.4

470. 0.0256 998 22.749 257.67 66.06 74.46 382 1 14 03 48.2

480. 0.0251 999 23.500 259.25 67.28 75.67 385 8 14 28 50.1

490. 0.0246 999 24.263 260.83 68.49 76.88 389 4 14 53 51.9

500. 0.0241 999 25.037 262.39 69.69 78.07 393 1 14 78 53.8

520. 0.0232 999 26.622 265.50 72.04 80.41 400 2 57.6

540. 0.0223 999 28.254 268.58 74.34 82.71 407 2 61.5

560. 0.0215 999 29.930 271.63 76.58 84.95 414 1 65.4

580. 0.0207 999 31.651 274.65 78.77 87.14 420. 9 69.4

600. 0.0201 1 000 33.415 277.64 80.91 89.27 427. 6 73.4

625. 0.0193 1 000 35.680 281.33 83.52 91.87 435. 8

138
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.101 325 MPa

T P z H

< C

V C

p W n

A

K mol*dm kJ/mol J/(mol-K) J/(mol«K) m* s

l fj.Pa- : 3 IT W/(m K

95. 21.504 .006 -14.569 80 .03 47.93 68.71 1970 .6 1058 .03 252 .2

100. 21.326 006 -14.221 83 .60 48.15 70.11 1938 7 878 69 248 .2 105. 21.146 .005 -13.869 87 .04 47.90 70.69 1904 3 742 64 244 .0

110. 20.964 005 -13.515 90 .33 47.39 70.82 1868 7 637 .50 239 .6 115. 20.781 .005 -13.161 93 .48 46.78 70.71 1832 5 554 76 235 .0

120. 20.597 005 -12.808 96 48 46.15 70.52 1796 488 49 230 .4

125. 20.412 005 -12.456 99 36 45.54 70.31 1759 2 434 57 225 .6 130. 20.227 005 -12.105 102 11 44.98 70.15 1722 4 390 03 220 .8 135. 20.040 005 -11.755 104 76 44.48 70.04 1685 4 352 74 215 .9 140. 19.852 004 -11.404 107 30 44.05 70.01 1648 3 321 13 211 .0

145. 19.663 004 -11.054 109 76 43.68 70.05 1611 1 294 02 206 .0

150. 19.472 004 -10.704 112 14 43.38 70.18 1573 8 270 54 201 .1 155. 19.279 004 -10.352 114 44 43.14 70.37 1536 5 250 00 196 1 160. 19.085 004 -10.000 116 68 42.95 70.65 1499 231 87 191 1 165. 18.888 004 -9.646 118 86 42.81 70.99 1461 4 215 75 186 2

170. 18.688 004 -9.290 120 98 42.72 71.40 1423 7 201 30 181 3 175. 18.486 004 -8.932 123 06 42.67 71.87 1385 9 188 26 176 4 180. 18.280 004 -8.571 125 09 42.65 72.41 1347 9 176 43 171 5 184.552 18.090 004 -8.240 126 91 42.67 72.96 1313 1 166 55 167 1 184.552 0.0683 967 6.478 206 66 31.03 40.21 248 6 5 88 9 5

185. 0.0681 967 6.496 206 75 31.19 40.38 248 8 5 90 9 5 190. 0.0662 969 6.702 207 85 32.53 41.79 251 8 6 06 9 9 195. 0.0643 972 6.913 208 95 33.41 42.67 254 9 6 21 10 3 200. 0.0626 974 7.128 210 04 34.06 43.28 258 6 37 10 7 205. 0.0609 976 7.346 211 11 34.60 43.77 261 2 6 52 11 1

210. 0.0594 977 7.566 212 17 35.08 44.19 264 3 6 68 11 6 215. 0.0579 979 7.788 213 22 35.54 44.60 267 3 6 84 12

220. 0.0565 980 8.012 214 25 36.00 45.00 270 3 6 99 12 5 225. 0.0552 982 8.238 215 26 36.45 45.41 273 3 7 15 12 9 230. 0.0539 983 8.466 216 27 36.92 45.83 276 2 7 30 13 4

235. 0.0527 984 8.696 217 26 37.39 46.27 279 7 45 13 9 240. 0.0515 985 8.928 218 23 37.87 46.71 281 8 7 61 14 4

245. 0.0504 986 9.163 219 20 38.37 47.17 284 5 7 76 14 9 250. 0.0494 987 9.400 220 16 38.87 47.65 287 2 7 91 15 4

255. 0.0484 988 9.640 221 11 39.39 48.14 289 9 8 07 15 9

260. 0.0474 988 9.882 222 05 39.92 48.64 292 5 8 22 16 5 265. 0.0465 989 10.126 222 98 40.46 49.16 295 1 8 37 17

270. 0.0456 990 10.373 223 90 41.01 49.69 297 6 8 52 17 6 275. 0.0448 990 10.623 224 82 41.57 50.22 300 1 8 67 18 2 280. 0.0439 991 10.875 225 73 42.13 50.77 302. 6 8. 82 18 8

139
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.101 325 MPa (continued)

T P Z H S CV

C

P

W n A

K mol«dm kJ/mol J/(mol«K) J/(mol«K) m»s 1/iPa«s itiW/(m'•K

285. 0.0431 0.991 11.131 226.63 42.71 51.33 305 .0 8 ,97 19 .4

290. 0.0424 0.992 11.389 227.53 43.30 51.90 307 .5 9 .11 20 .0 295. 0.0416 0.992 11.650 228.42 43.89 52.48 309 .8 9 .26 20 .6 300. 0.0409 0.993 11.914 229.31 44.49 53.07 312 .2 9 .41 21 .2 310. 0.0396 0.993 12.450 231.07 45.71 54.26 316 .8 9 .70 22 .5

320. 0.0383 0.994 12.999 232.81 46.95 55.48 321 .4 9 .99 23 .9 330. 0.0371 0.994 13.560 234.54 48.21 56.72 325 .9 10 .28 25 .2 340. 0.0360 0.995 14.133 236.25 49.48 57.98 330 .2 10 .56 26 .7 350. 0.0350 0.995 14.720 237.95 50.76 59.25 334 .5 10 .84 28 .1

360. 0.0340 0.996 15.318 239.64 52.05 60.52 338 .8 11 .12 29 .6

370. 0.0331 0.996 15.930 241.31 53.34 61.81 343 .0 11 .40 31 .2 380. 0.0322 0.997 16.555 242.98 54.64 63.09 347 .1 11 .67 32 .8 390. 0.0313 0.997 17.192 244.63 55.93 64.38 351 .2 11 ,94 34 .4

400. 0.0306 0.997 17.842 246.28 57.23 65.66 355 .2 12,,21 36 .0

410. 0.0298 0.997 18.505 247.92 58.51 66.94 359 ,2 12,,48 37 .7

420. 0.0291 0.998 19.181 249.54 59.80 68.22 363.,1 12,,74 39 .4 430. 0.0284 0.998 19.869 251.16 61.07 69.48 367,,0 13, 01 41 .1 440. 0.0278 0.998 20.571 252.78 62.33 70.74 370,,8 13, 27 42 .8 450. 0.0271 0.998 21.284 254.38 63.59 71.99 374,,6 13. 52 44 ,6

460. 0.0265 0.998 22.010 255.98 64.83 73.23 378, 4 13. 78 46,.4

470. 0.0260 0.998 22.749 257.56 66.06 74.46 382, 1 14. 03 48,,2

480. 0.0254 0.999 23.499 259.14 67.28 75.68 385. 8 14. 28 50,,1

490. 0.0249 0.999 24.262 260.72 68.49 76.88 389. 4 14. 53 51. 9

500. 0.0244 0.999 25.037 262.28 69.69 78.07 393. 1 14. 78 53. 8

520. 0.0235 0.999 26.622 265.39 72.04 80.42 400. 2 57. 6

540. 0.0226 0.999 28.253 268.47 74.34 82.71 407. 2 61. 5 560. 0.0218 0.999 29.930 271.52 76.58 84.95 414. 1 65. 4

580. 0.0210 0.999 31.651 274.54 78.77 87.14 420. 9 69. 4

600. 0.0203 1.000 33.415 277.53 80.91 89.27 427. 6 73. 4

625. 0.0195 1.000 35.680 281.22 83.52 91.87 435. 8

140-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.1500 MPa

T P z H C

V C

p W n

A

K mol'dm kJ/mol J/(mol»K) J/(mol-K) m« s

i /iFa*

3 niW/(m •K

95. 21.505 .009 -14.567 80 .03 47.93 68.70 1970 .8 1058 .47 252 .2

100. 21.327 .008 -14.219 83 .60 48.15 70.11 1938 .9 879 .03 248 .2

105. 21.146 .008 -13.867 87 .03 47.90 70.69 1904 .5 742 .91 244 .0

110. 20.965 .008 -13.513 90 .33 47.39 70.82 1868 .9 637 .73 239 .6

115. 20.782 .008 -13.159 93 .47 46.78 70.71 1832 7 554 .95 235 .1

120. 20.598 .007 -12.806 96 .48 46.15 70.52 1796 2 488 .65 230 .4

125. 20.413 .007 -12.454 99 .35 45.54 70.31 1759 5 434 .71 225 .6 130. 20.228 .007 -12.103 102 .11 44.98 70.14 1722 6 390 .15 220 .8 135. 20.041 007 -11.753 104 .75 44.48 70.04 1685 6 352 .85 215 9 140. 19.853 006 -11.403 107 .30 44.05 70.00 1648 5 321 23 211 .0

145. 19.664 006 -11.053 109 .75 43.69 70.05 1611 4 294 .12 206 .0

150. 19.473 006 -10.702 112 13 43.38 70.17 1574 1 270 63 201 1 155. 19.281 006 -10.351 114 43 43.14 70.37 1536 8 250 09 196 1 160. 19.086 006 -9.998 116 67 42.95 70.64 1499 3 231 95 191 2 165. 18.889 006 -9.644 118 85 42.81 70.98 1461 7 215 83 186 2

170. 18.689 006 -9.288 120 98 42.72 71.39 1424 1 201 37 181 3 175. 18.487 006 -8.930 123 05 42.67 71.86 1386 2 188 33 176 4

180. 18.282 005 -8.570 125 08 42.65 72.40 1348 2 176 50 171 6 185. 18.073 005 -8.206 127 08 42.68 73.01 1310 1 165 69 166 7 190. 17.860 005 -7.839 129 03 42.73 73.68 1271 7 155 77 162

192.154 17.767 005 -7.680 129 86 42.77 74.00 1255 1 151 74 159 9 192.154 0.0983 956 6.726 204 83 32.41 42.20 251 6 13 10 2 195. 0.0966 957 6.847 205 46 33.11 42.89 252 8 6 22 10 4

200. 0.0939 961 7.063 206 56 34.00 43.73 255 9 6 38 10 8

205. 0.0913 964 7.284 207 65 34.66 44.30 259 2 6 53 11 2

210. 0.0889 966 7.506 208 72 35.20 44.75 262 3 6 69 11 7 215. 0.0866 969 7.731 209 78 35.69 45.15 265 5 6 85 12 1 220. 0.0845 971 7.958 210 82 36.15 45.53 268 6 7 00 12 5 225. 0.0824 973 8.186 211 85 36.60 45.91 271 6 7 16 13

230. 0.0805 975 8.417 212 86 37.06 46.30 274 6 7 31 13 5

235. 0.0786 976 8.649 213 86 37.53 46.70 277 5 7 46 14

240. 0.0769 978 8.884 214 85 38.00 47.12 280 4 7 62 14 4

245. 0.0752 979 9.120 215 82 38.49 47.55 283 2 7 77 14 9

250. 0.0736 980 9.359 216 79 38.99 48.00 286. 7 92 15 5 255. 0.0721 982 9.600 217 74 39.49 48.47 288. 7 8 08 16

260. 0.0706 983 9.844 218 69 40.02 48.95 291. 4 8 23 16. 5 265. 0.0692 984 10.090 219 63 40.55 49.44 294. 8. 38 17. 1 270. 0.0679 985 10.338 220. 55 41.09 49.95 296. 6 8. 53 17. 6

275. 0.0666 985 10.590 221 48 41.64 50.47 299. 1 8. 68 18. 2 280. 0.0653 986 10.843 222 39 42.21 51.01 301. 7 8. 83 18. 8

141
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.1500 MPa (continued)

T P z H S C

V C

p W 1 A

K mol«dm kJ/mol J/(mol«K) J/(mol-K) m«s

-

fiVa* i3 ITiW/(m<•K

285. 0.0641 .987 11.100 223.30 42.78 51.56 304 .1 8 .98 19 .4

290. 0.0630 .988 11.359 224.20 43.36 52.11 306 .6 9 .13 20 .0

295. 0.0619 .988 11.621 225.09 43.95 52.68 309 .0 9 .27 20 .6 300. 0.0608 .989 11.886 225.99 44.54 53.25 311 .4 9 .42 21 .3 310. 0.0588 .990 12.424 227.75 45.75 54.43 316 .1 9 .71 22 .6

320. 0.0569 .991 12.974 229.50 46.99 55.63 320 .7 10 ,00 23 .9 330. 0.0551 .992 13.537 231.23 48.24 56.86 325 .2 10 ,29 25 .3 340. 0.0535 .993 14.111 232.94 49.51 58.10 329 .7 10 .57 26 .7 350. 0.0519 .993 14.699 234.65 50.79 59.36 334 .0 10 .85 28 .2 360. 0.0504 .994 15.299 236.34 52.07 60.63 338 .3 11 .13 29 .7

370. 0.0490 ,994 15.911 238.01 53.37 61.90 342 .5 11 ,41 31 .2 380. 0.0477 ,995 16.537 239.68 54.66 63.18 346 ,7 11 ,68 32 .8 390. 0.0465 ,995 17.175 241.34 55.95 64.46 350 .8 11 ,95 34 .4

400. 0.0453 ,996 17.826 242.99 57.24 65.74 354 ,8 12 ,22 36 ,0

410. 0.0442 ,996 18.490 244.63 58.53 67.01 358 ,8 12,,49 37 ,7

420. 0.0431 ,996 19.166 246.26 59.81 68.28 362 ,8 12,.75 39 ,4

430. 0.0421 0.,997 19.855 247.88 61.08 69.54 366 7 13. 02 41 ,1

440. 0.0411 0.,997 20.557 249.49 62.34 70.80 370, 6 13, 28 42 ,9

450. 0.0402 0,,997 21.271 251.10 63.60 72.05 374, 4 13, 53 44,,6

460. 0.0393 0. 997 21.998 252.69 64.84 73.28 378, 2 13, 79 46. 4

470. 0.0385 0. 998 22.737 254.28 66.07 74.51 381, 9 14, 04 48. 3 480. 0.0377 0. 998 23.488 255.86 67.29 75.72 385. 6 14. 29 50. 1 490. 0.0369 0,,998 24.251 257.44 68.50 76.92 389, 3 14. 54 52.

500. 0.0361 0. 998 25.026 259.00 69.70 78.11 392. 9 14. 79 53. 8 520. 0.0347 0. 998 26.612 262.11 72.05 80.45 400. 1 57. 6

540. 0.0335 0. 999 28.244 265.19 74.34 82.74 407. 1 61. 5 560. 0.0323 0. 999 29.921 268.24 76.59 84.98 414. 65. 4

580. 0.0311 0. 999 31.643 271.26 78.78 87.16 420. 9 69. 4

600. 0.0301 0. 999 33.408 274.25 80.92 89.30 427. 6 73. 4

625. 0.0289 0. 999 35.673 277.95 83.52 91.90 435. 8

142-
Table B3. Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.2000 MPa

T P z H

< C

V C

p W V A

K mo'L* dm kJ/mol J/(mol«K) J/(mol'K) m« s

l /iPa*

3 ITtW/o•K

95. 21 .505 .012 -14.565 80 .03 47.93 68.70 1971 .0 1058 .91 252 .2 100. 21 .327 .011 -14.217 83 .59 48.15 70.11 1939 .2 879 .38 248 .2 105. 21 .147 .011 -13.865 87 .03 47.90 70.69 1904 .8 743 .19 244 .0 110. 20 .965 .010 -13.511 90 .32 47.40 70.81 1869 .2 637 .96 239 .6 115. 20 .782 .010 -13.157 93 .47 46.79 70.71 1833 .0 555 .14 235 .1

120. 20 .599 .010 -12.804 96 .47 46.15 70.51 1796 .4 488 .82 230 .4

125. 20 .414 .009 -12.452 99 .35 45.54 70.31 1759 .7 434 .86 225 .7 130. 20 ,229 .009 -12.101 102 .10 44.98 70.14 1722 .8 390 .29 220 .8 135. 20 .042 ,009 -11.751 104 .75 44.48 70.03 1685 .9 352 .97 215 ,9

140. 19 .854 .009 -11.401 107 .29 44.05 70.00 1648 .8 321 .34 211 ,0

145. 19..665 ,008 -11.051 109 ,75 43.69 70.05 1611 .7 294 ,22 206 ,1

150. 19 ,474 ,008 -10.700 112 .13 43.39 70.17 1574 .4 270 .73 201 .1 155. 19 .282 ,008 -10.349 114 .43 43.14 70.36 1537 .1 250 .17 196 ,2

160. 19 .087 .008 -9.996 116 .67 42.95 70.63 1499 .6 232 .04 191 ,2

165. 18 .890 .008 -9.642 118 .85 42.82 70.97 1462 ,1 215 .91 186 ,3

170. 18 .691 ,008 -9.287 120 .97 42.72 71.38 1424 .4 201 ,45 181 ,4

175. 18 ,488 0,,007 -8.928 123 .05 42.67 71.85 1386 .6 188 .41 176 ,5

180. 18 .283 ,007 -8.568 125 .08 42.66 72.39 1348 .6 176 .57 171 ,6

185. 18,,074 ,007 -8.204 127 ,07 42.68 73.00 1310 .5 165 .76 166 ,8

190. 17,,862 ,007 -7.838 129 .03 42.74 73.67 1272 .1 155 .84 162 ,0

195. 17,,645 0,,007 -7.468 130 .95 42.82 74.42 1233 ,5 146 .69 157 ,3

198.179 17,,505 0,,007 -7.230 132 .16 42.90 74.93 1208 .9 141 ,23 154 .3 198.179 0,,1284 0,,945 6.914 203,,53 33.56 43.93 252 ,6 6,,33 10,,8

200. 0, 1271 0, 947 6.994 203,,93 33.94 44.26 253 ,7 6 39 11,,0

205. 0, 1234 0. 951 7.218 205,,03 34.73 44.92 257 6. 54 11,.4

210. 0, 1200 0, 954 7.443 206,,12 35.34 45.39 260 3 6, 70 11, 8 215. 0,,1168 0, 958 7.671 207,,19 35.85 45.77 263,,6 6, 86 12, 2 220. 0, 1138 0, 961 7.901 208,,25 36.32 46.11 266,,8 7, 01 12, 6 225. 0,,1110 0, 963 8.132 209, 29 36.77 46.45 269, 9 7, 17 13. 1 230. 0.,1083 0. 966 8.366 210, 32 37.22 46.80 273,,0 7. 32 13. 6

235. 0, 1057 0. 968 8.600 211, 33 37.68 47.17 276, 7, 48 14.

240. 0, 1033 0, 970 8.837 212, 32 38.14 47.55 278. 9 7. 63 14. 5 245. 0. 1010 0, 972 9.076 213. 31 38.62 47.95 281, 8 7, 78 15.

250. 0, 0988 0, 974 9.317 214, 28 39.10 48.37 284. 7 7. 94 15. 5 255. 0, 0967 0, 975 9.560 215. 24 39.61 48.81 287. 4 8, 09 16. 1

260. 0. 0947 0. 977 9.805 216, 19 40.12 49.27 290. 2 8. 24 16. 6 265. 0, 0928 0. 978 10.052 217, 14 40.64 49.75 292. 9 8. 39 17. 1 270. 0, 0910 0. 979 10.302 218. 07 41.18 50.23 295. 5 8. 54 17. 7 275. 0, 0892 0. 981 10.555 219. 00 41.72 50.74 298. 1 8. 69 18. 3 280. 0, 0875 0, 982 10.810 219. 92 42.28 51.26 300. 7 8. 84 18. 9

143
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.2000 MPa (continued)

T P z H S C

V C

p W 1 A

K mol«dm kJ/mol J/(mol-K) J/(mol-K) m»s

l //Pa* i 5 iriW/(m •K

285. 0.0859 .983 11.067 220.83 42.85 51.79 303 .2 8 .99 19 .5 290. 0.0843 .983 11.328 221.73 43.42 52.33 305 .7 9 .14 20 .1

295. 0.0828 .984 11.591 222.63 44.01 52.88 308 .2 9 .28 20 .7 300. 0.0814 .985 11.857 223.53 44.60 53.45 310 .6 9 .43 21 .3

310. 0.0786 .987 12.397 225.30 45.80 54.60 315 .4 9 .72 22 .6

320. 0.0761 .988 12.949 227.05 47.03 55.79 320 .0 10 .01 23 .9

330. 0.0737 .989 13.513 228.79 48.28 57.00 324 .6 10 .30 25 .3

340. 0.0715 .990 14.089 230.51 49.54 58.23 329 .1 10 .58 26 .7 350. 0.0694 .991 14.677 232.21 50.82 59.47 333 .5 10 .86 28 .2 360. 0.0674 .992 15.278 233.90 52.10 60.73 337 .8 11 .14 29 .7

370. 0.0655 .992 15.892 235.59 53.39 62.00 342 .1 11 .42 31 .2 380. 0.0637 .993 16.518 237.26 54.68 63.27 346 .3 11 .69 32 .8 390. 0.0621 .994 17.157 238.92 55.97 64.54 350 .4 11 .96 34 .4 400. 0.0605 ,994 17.809 240.57 57.26 65.81 354 ,5 12 ,23 36 .1 410. 0.0590 ,995 18.474 242.21 58.54 67.08 358 ,5 12 ,50 37 .7

420. 0.0576 0.,995 19.151 243.84 59.82 68.35 362 ,5 12, 76 39 .4 430. 0.0562 0,,996 19.841 245.46 61.09 69.61 366,,4 13, 03 41 ,1

440. 0.0549 0.,996 20.543 247.08 62.36 70.86 370,,3 13. 29 42 ,9

450. 0.0537 0,,996 21.258 248.68 63.61 72.10 374, 1 13. 54 44 .7 460. 0.0525 0, 997 21.985 250.28 64.85 73.33 377.,9 13. 80 46 .5

470. 0.0513 0, 997 22.724 251.87 66.08 74.56 381, 7 14. 05 48, 3 480. 0.0503 0, 997 23.476 253.45 67.30 75.77 385. 4 14. 30 50, 1 490. 0.0492 0. 997 24.240 255.03 68.51 76.97 389. 1 14. 55 52.

500. 0.0482 0. 998 25.015 256.59 69.70 78.15 392. 7 14. 80 53. 8

520. 0.0464 0. 998 26.602 259.71 72.05 80.49 399. 9 57. 6

540. 0.0446 0. 998 28.235 262.79 74.35 82.78 407. 61. 5 560. 0.0430 0. 999 29.912 265.84 76.59 85.01 414. 65. 4

580. 0.0415 0. 999 31.635 268.86 78.78 87.19 420. 8 69. 4

600. 0.0401 0. 999 33.400 271.85 80.92 89.32 427. 5 73. 4

625. 0.0385 0. 999 35.666 275.55 83.53 91.92 435. 8

144
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.2500 MPa

T P z H S C

V C

p W r\ A

K mo!L«dm kJ/mol J/(mol«K) J/(mol»K) m»s

• l /iPa*

3 ITiW/o•K

95. 21 .506 .015 -14 .563 80 .02 47.93 68.70 1971 .2 1059 .36 252 .2 100. 21 .328 .014 -14 .216 83 .59 48.15 70.10 1939 .4 879 .73 248 .3 105. 21 .148 .014 -13 .863 87 .02 47.90 70.69 1905 .0 743 .47 244 .1 110. 20 .966 .013 -13 .509 90 .32 47.40 70.81 1869 .4 638 .19 239 .7 115. 20 .783 .013 -13 .156 93 .46 46.79 70.71 1833 .2 555 .34 235 .1

120. 20 .599 .012 -12 .802 96 .47 46.15 70.51 1796 .7 488 .99 230 .4

125. 20 .415 .012 -12 .450 99 .34 45.54 70.31 1759 .9 435 .00 225 .7 130. 20 .229 .011 -12 .099 102 .10 44.98 70.14 1723 .1 390 .42 220 .9 135. 20 .043 .011 -11 .749 104 .74 44.48 70.03 1686 .1 353 .09 216 .0 140. 19 .855 .011 -11 .399 107 .29 44.05 70.00 1649 .1 321 .45 211 .1

145. 19 .666 .011 -11 .049 109 .74 43.69 70.04 1611 .9 294 .32 206 .1 150. 19 .475 .010 -10 .698 112 .12 43.39 70.16 1574 .7 270 .82 201 .2 155. 19 .283 .010 -10 .347 114 .42 43.15 70.36 1537 .4 250 .26 196 .2 160. 19 .088 0..010 -9 .995 116 .66 42.96 70.63 1500 .0 232 .12 191 .2 165. 18,,891 ,010 -9 .641 118 .84 42.82 70.97 1462 .4 215 .99 186 .3

170. 18 ,692 0..009 -9 .285 120 .96 42.72 71.37 1424 .8 201 .53 181 .4 175. 18 ,490 0,,009 -8 .927 123 .04 42.67 71.85 1387 .0 188 .49 176 .5 180. 18,,285 0,,009 -8,.566 125 .07 42.66 72.39 1349 .0 176 .65 171 .7 185. 18,,076 0.,009 -8 ,203 127 .06 42.68 72.99 1310 ,9 165 .83 166 .8 190. 17,.864 0,.009 -7,,836 129 ,02 42.74 73.66 1272 ,6 155 .91 162 .0

195. 17,,647 0.,009 -7,,466 130 ,94 42.83 74.40 1234 ,0 146 .76 157 .3 200. 17,.426 0,,009 -7,,092 132 ,84 42.94 75.22 1195 .2 138 .28 152 .6 203.144 17,.285 0, 009 -6,,855 134 ,01 43.03 75.78 1170 ,6 133 .25 149 ,7

203.144 0,.1583 0, 935 7,,064 202,,53 34.54 45.46 253 ,6 6 .50 11 .3 205. 0,,1565 0. 937 7,,149 202,,95 34.85 45.68 254 ,8 6 .55 11,.5

210. 0, 1520 0. 942 7, 378 204, 05 35.51 46.12 258, 2 6 .71 11 ,9

215. 0. 1478 0. 946 7, 610 205, 14 36.03 46.46 261, 6 6,.87 12, 3 220. 0,,1438 0. 950 7, 843 206.,21 36.50 46.75 264, 9 7,,02 12, 7 225. 0, 1401 0. 954 8. 077 207, 27 36.95 47.04 268. 1 7,,18 13, 2 230. 0. 1366 0. 957 8. 313 208. 30 37.39 47.34 271, 3 7.,33 13.,6

235. 0, 1333 0. 960 8. 551 209. 33 37.83 47.66 274, 4 7.,49 14. 1 240. 0, 1302 0. 962 8. 790 210. 33 38.28 48.01 277. 4 7,,64 14. 6 245. 0. 1272 0. 965 9. 031 211. 33 38.75 48.37 280. 4 7. 79 15. 1 250. 0. 1244 0. 967 9. 274 212. 31 39.23 48.76 283. 3 7. 95 15. 6 255. 0. 1217 0. 969 9. 518 213. 28 39.72 49.18 286. 2 8. 10 16. 1

260. 0. 1191 0. 971 9. 765 214. 24 40.22 49.61 289. 8. 25 16. 7 265. 0. 1167 0. 973 10. 015 215. 18 40.74 50.06 291. 7 8. 40 17. 2 270. 0. 1143 0. 974 10. 266 216. 12 41.27 50.53 294. 4 8. 55 17. 8

275. 0, 1121 0. 976 10. 520 217. 06 41.81 51.01 297. 1 8. 70 18. 3 280. 0. 1099 0. 977 10. 776 217. 98 42.36 51.51 299. 7 8. 85 18. 9

145
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.2500 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol-K) J/(mol«K) m»s

l /iPa«s ir W/(m >K

285. 0.1079 978 11.035 218.90 42.92 52.03 302 3 9 00 19 5 290. 0.1059 979 11.296 219.81 43.49 52.56 304 8 9 15 20 1 295. 0.1040 980 11.561 220.71 44.07 53.10 307 3 9 30 20 7 300. 0.1021 981 11.827 221.61 44.65 53.65 309 8 9 44 21 4

310. 0.0986 983 12.370 223.38 45.85 54.78 314 6 9 73 22 6

320. 0.0954 985 12.923 225.14 47.07 55.95 319 3 10 02 24

330. 0.0924 986 13.489 226.88 48.32 57.14 324 10 31 25 4

340. 0.0896 988 14.066 228.60 49.57 58.36 328 5 10 59 26 8 350. 0.0869 989 14.656 230.31 50.85 59.59 332 9 10 87 28 2 360. 0.0844 990 15.258 232.01 52.13 60.84 337 3 11 15 29 7

370. 0.0820 991 15.873 233.69 53.41 62.10 341 6 11 43 31 3 380. 0.0798 991 16.500 235.37 54.70 63.36 345 8 11 70 32 8 390. 0.0777 992 17.140 237.03 55.99 64.63 350 11 98 34 4

400. 0.0757 993 17.792 238.68 57.28 65.89 354 1 12 24 36 1 410. 0.0738 993 18.458 240.32 58.56 67.16 358 2 12 51 37 7

420. 0.0720 994 19.136 241.96 59.84 68.42 362 2 12 77 39 4

430. 0.0703 994 19.826 243.58 61.11 69.67 366 1 13 04 41 2 440. 0.0687 995 20.529 245.20 62.37 70.92 370 13 30 42 9

450. 0.0671 995 21.244 246.81 63.62 72.16 373 9 13 55 44 7 460. 0.0657 996 21.972 248.40 64.86 73.39 377 7 13 81 46 5

470. 0.0642 996 22.712 250.00 66.09 74.61 381 5 14 06 48 3 480. 0.0629 996 23.464 251.58 67.31 75.81 385 2 14 31 50 1 490. 0.0616 997 24.228 253.15 68.52 77.01 388 9 14 56 52

500. 0.0603 997 25.004 254.72 69.71 78.20 392 6 14 81 53 9 520. 0.0580 997 26.592 257.84 72.06 80.53 399 8 57 7

540. 0.0558 998 28.225 260.92 74.35 82.81 406 9 61 5 560. 0.0538 998 29.904 263.97 76.60 85.04 413 9 65 4

580. 0.0519 998 31.626 266.99 78.79 87.22 420 7 69 4

600. 0.0502 999 33.392 269.98 80.93 89.35 427 5 73 4

625. 0.0482 999 35.658 273.69 83.53 91.95 435. 7

-146-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.3000 MPa

T P z H

(

-* C

V C

p W n

A

K mo!L»dm kJ/mol J/(mol.K) J/(mol«K) m« s

i H?a»

:

3 irtW/(m<>K

95. 21 .506 .018 -14.561 80 .02 47.93 68.70 1971 .5 1059 .81 252 .2 100. 21 .329 .017 -14.214 83 .58 48.15 70.10 1939 .6 880 .08 248 .3 105. 21 .148 .016 -13.861 87 .02 47.90 70.68 1905 .2 743 .75 244 .1

110. 20 .967 .016 -13.507 90 .31 47.40 70.81 1869 .6 638 .42 239 .7 115. 20 .784 .015 -13.154 93 .46 46.79 70.70 1833 .4 555 .53 235 .1

120. 20 .600 .015 -12.801 96 .46 46.15 70.51 1796 .9 489 .16 230 .5 125. 20 .416 .014 -12.449 99 .34 45.54 70.30 1760 .2 435 .15 225 .7 130. 20 .230 .014 -12.097 102 .09 44.98 70.13 1723 .3 390 .55 220 .9 135. 20 .044 .013 -11.747 104 .74 44.49 70.03 1686 .4 353 .21 216 .0 140. 19 .856 .013 -11.397 107 .28 44.06 69.99 1649 .4 321 .56 211 .1

145. 19 .667 .013 -11.047 109 .74 43.69 70.04 1612 .2 294 .43 206 .1 150. 19 .477 .012 -10.697 112 .12 43.39 70.16 1575 .0 270 .92 201 .2 155. 19 .284 .012 -10.345 114 .42 43.15 70.35 1537 .7 250 .35 196 .2 160. 19 .090 .012 -9.993 116 .66 42.96 70.62 1500 .3 232 .21 191 .3 165. 18 .893 .012 -9.639 118 .83 42.82 70.96 1462 ,8 216 .07 186 .3

170. 18 .693 .011 -9.283 120 .96 42.73 71.37 1425,.1 201 .61 181 .4 175. 18 .491 .011 -8.925 123 .03 42.68 71.84 1387 .3 188 .56 176 .6 180. 18 .286 ,011 -8.565 125 .07 42.66 72.38 1349 .4 176 .72 171 .7 185. 18 .078 .011 -8.201 127 .06 42.68 72.98 1311 .3 165 .91 166 .9 190. 17 .865 Oil -7.835 129 .01 42.74 73.65 1273 .0 155 .98 162 .1

195. 17 .649 ,010 -7.465 130,.93 42.83 74.39 1234 ,5 146 .83 157,.3 200. 17..428 0.,010 -7.091 132 .83 42.95 75.21 1195 ,7 138 .35 152 ,6

205. 17..202 0, 010 -6.712 134 .70 43.09 76.11 1156,,5 130 ,45 148 ,0

207.404 17.,092 0,,010 -6.529 135,.59 43.17 76.57 1137.,6 126 ,85 145,,8

207.404 0..1878 0.,926 7.188 201.,72 35.40 46.84 254,,2 6 ,64 11,,8

210. 0,.1849 0. 929 7.310 202..31 35.73 47.01 256, 6 ,72 12,.0 215. 0. 1795 0. 935 7.546 203,,42 36.26 47.25 259, 5 6, 88 12,.4 220. 0, 1745 0. 940 7.783 204,,51 36.71 47.47 262. 9 7, 04 12, 8 225. 0.,1699 0. 944 8.021 205, 58 37.14 47.69 266. 3 7,,19 13. 3 230. 0.,1655 0. 948 8.260 206. 63 37.57 47.93 269. 6 7, 35 13. 7

235. 0.,1614 0. 951 8.500 207. 66 38.00 48.19 272. 8 7. 50 14. 2 240. 0. 1575 0. 955 8.742 208. 68 38.44 48.49 275. 9 7. 65 14. 7 245. 0. 1538 0. 957 8.985 209. 68 38.89 48.82 279. 7. 81 15. 2 250. 0. 1503 0. 960 9.230 210. 67 39.35 49.17 282. 7. 96 15. 7 255. 0. 1470 0. 963 9.477 211. 65 39.83 49.55 284. 9 8. 11 16. 2

260. 0. 1438 0. 965 9.725 212. 61 40.33 49.95 287. 8 8. 26 16. 7 265. 0. 1408 0. 967 9.976 213. 57 40.84 50.38 290. 6 8. 41 17. 3 270. 0. 1379 0. 969 10.229 214. 52 41.36 50.83 293. 3 8. 56 17. 8 275. 0. 1352 0. 971 10.485 215. 45 41.89 51.29 296. 8. 71 18. 4

280. 0. 1326 0. 972 10.742 216. 38 42.43 51.77 298. 7 8. 86 19.

147
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.3000 MPa (continued)

T P z H S C

V C

p W 1

A

K mol«dm kJ/mol J/(mol-K) J/(mol«K) m»s

• l /^Pa«s iriW/(m<•K

285. 0.1300 .974 11.002 217.30 42.99 52.27 301 .3 9 .01 19 .6 290. 0.1276 .975 11.265 218.22 43.55 52.78 303 .9 9 .16 20 .2 295. 0.1253 .976 11.530 219.12 44.13 53.31 306 .4 9 .31 20 .8 300. 0.1230 .978 11.798 220.02 44.71 53.85 308 .9 9 .45 21 .4

310. 0.1188 .980 12.342 221.81 45.90 54.96 313 .9 9 .75 22 .7

320. 0.1148 .982 12.897 223.57 47.12 56.11 318 .7 10 .03 24 .0 330. 0.1112 .983 13.464 225.31 48.35 57.29 323 .3 10 .32 25 .4

340. 0.1077 .985 14.043 227.04 49.61 58.49 327 .9 10 .61 26 .8 350. 0.1045 .986 14.634 228.75 50.87 59.71 332 .4 10 .89 28 .3 360. 0.1015 .988 15.237 230.45 52.15 60.95 336 .8 11 .17 29 .8

370. 0.0986 .989 15.853 232.14 53.43 62.20 341 .2 11 .44 31 .3 380. 0.0959 .990 16.481 233.82 54.72 63.45 345 .4 11,.71 32 .9 390. 0.0934 .990 17.122 235.48 56.01 64.71 349 .6 11 ,99 34 .5 400. 0.0910 .991 17.776 237.14 57.29 65.97 353 ,8 12 ,25 36 .1 410. 0.0887 ,992 18.442 238.78 58.57 67.23 357 ,8 12 ,52 37 .8

420. 0.0865 .993 19.120 240.41 59.85 68.48 361 ,9 12,,79 39 .5 430. 0.0845 0,.993 19.811 242.04 61.12 69.73 365 .8 13 ,05 41 .2 440. 0.0825 .994 20.515 243.66 62.38 70.98 369 ,8 13,,31 42 .9 450. 0.0806 ,994 21.231 245.27 63.63 72.21 373,,6 13,,56 44 .7 460. 0.0788 ,995 21.959 246.87 64.87 73.44 377,,5 13, 82 46 ,5

470. 0.0771 ,995 22.700 248.46 66.10 74.65 381, 3 14. 07 48,.3 480. 0.0755 ,996 23.452 250.04 67.32 75.86 385, 14. 32 50 2 490. 0.0739 ,996 24.217 251.62 68.52. 77.05 388. 7 14. 57 52,

500. 0.0724 0.,996 24.993 253.19 69.72 78.24 392. 4 14. 81 53, 9 520. 0.0696 0,,997 26.581 256.30 72.07 80.57 399,,7 57, 7

540. 0.0670 0.,997 28.215 259.39 74.36 82.84 406. 8 61. 5 560. 0.0646 0,,998 29.895 262.44 76.60 85.07 413. 8 65. 5 580. 0.0623 0. 998 31.618 265.46 78.79 87.25 420. 7 69. 4

600. 0.0602 0. 999 33.384 268.46 80.93 89.38 427. 4 73. 4

625. 0.0578 0. 999 35.651 272.16 83.54 91.97 435. 7

148
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.3500 MPa

T P z H

i C

V C

p W V

A

K mo!L«dm kJ/mol J/(mol-K) J/(mol«K) m»s

i /iPa*

!

3 niW/(m •K

95. 21 .507 .021 -14.559 80 .02 47.93 68.69 1971 .7 1060 .26 252 .3

100. 21 .329 .020 -14.212 83 .58 48.15 70.10 1939 .8 880 .43 248 .3

105. 21 .149 .019 -13.859 87 .02 47.90 70.68 1905 .4 744 .03 244 .1

110. 20 .967 .018 -13.506 90 .31 47.40 70.81 1869 .8 638 .65 239 .7 115. 20 .785 .018 -13.152 93 .45 46.79 70.70 1833 .6 555 .72 235 .2

120. 20 .601 .017 -12.799 96 .46 46.16 70.51 1797 .1 489 .33 230 .5 125. 20 .417 .016 -12.447 99 .33 45.55 70.30 1760 .4 435 .30 225 .7 130. 20 .231 .016 -12.096 102 .09 44.99 70.13 1723 .6 390 .68 220 .9

135. 20 .045 .016 -11.745 104 .73 44.49 70.02 1686 .7 353 .33 216 .0

140. 19 .857 .015 -11.395 107 .28 44.06 69.99 1649 .6 321 .67 211 .1

145. 19 .668 .015 -11.045 109 .73 43.69 70.03 1612 .5 294 .53 206 .2 150. 19 .478 .014 -10.695 112 .11 43.39 70.15 1575 .3 271 .01 201 .2 155. 19 .285 .014 -10.344 114 .41 43.15 70.35 1538 .0 250 .44 196 .3 160. 19 .091 .014 -9.991 116 .65 42.96 70.62 1500 .6 232 .29 191 .3 165. 18 .894 .014 -9.637 118 .83 42.82 70.96 1463 .1 216 .15 186 .4

170. 18..695 .013 -9.281 120 .95 42.73 71.36 1425 .5 201 .69 181 .5 175. 18,.493 .013 -8.924 123 .03 42.68 71.83 1387 .7 188 .64 176 .6 180. 18,.288 .013 -8.563 125 .06 42.66 72.37 1349 .8 176 .79 171 .7 185. 18,.079 .013 -8.200 127 .05 42.69 72.97 1311 .7 165 .98 166 .9 190. 17,,867 0,.012 -7.833 129 .01 42.74 73.64 1273 .4 156 .05 162 .1

195. 17.,651 .012 -7.463 130 .93 42.83 74.38 1234 .9 146 .90 157 .4 200. 17,,430 .012 -7.089 132 ,82 42.95 75.19 1196 .1 138 ,42 152 ,7

205. 17,,204 .012 -6.711 134 .69 43.10 76.09 1157 ,0 130,.52 148 ,0

210. 16,.973 0,.012 -6.328 136 .53 43.27 77.08 1117 ,6 123, 14 143 ,4

211.158 16,,918 ,012 -6.239 136,.96 43.32 77.32 1108 ,4 121, 50 142.,4

211.158 0, 2172 0,.918 7.294 201.,05 36.16 48.12 254,,6 6..77 12,.2 215. 0. 2122 0,.923 7.479 201,.92 36.54 48.19 257, 4 6, 89 12,,5

220. 0.,2060 0..929 7.721 203.,03 36.96 48.28 261.,0 7. 05 13,

225. 0. 2003 0,.934 7.962 204,,11 37.37 48.40 264. 4 7. 20 13,,4

230. 0. 1950 0.,939 8.205 205. 18 37.77 48.56 267. 8 7. 36 13,,8

235. 0. 1900 0.,943 8.448 206. 23 38.17 48.76 271. 1 7. 51 14, 3 240. 0. 1853 0. 947 8.692 207. 25 38.60 49.01 274. 4 7. 67 14, 8 245. 0. 1809 0. 950 8.938 208. 27 39.03 49.29 277. 5 7. 82 15. 3 250. 0. 1767 0. 953 9.185 209. 27 39.49 49.60 280. 6 7. 97 15. 8

255. 0. 1727 0. 956 9.434 210. 25 39.95 49.94 283. 6 8. 12 16. 3

260. 0. 1689 0. 959 9.685 211. 23 40.44 50.32 286. 5 8. 28 16. 8

265. 0. 1653 0. 961 9.937 212. 19 40.94 50.71 289. 4 8. 43 17. 3 270. 0. 1618 0. 963 10.192 213. 14 41.45 51.14 292. 2 8. 58 17. 9

275. 0. 1585 0. 965 10.449 214. 08 41.98 51.58 295. 8. 73 18. 5 280. 0. 1554 0. 967 10.708 215. 02 42.51 52.04 297. 7 8. 88 19.

149
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.3500 MPa (continued)

T P z H S C

V C

p W r\ A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol-K) m» s

• l /xPa«s iriW/(m<>K

285. 0.1524 0. 969 10.969 215.94 43.06 52.52 300 .4 9. 02 19 .6 290. 0.1495 0. 971 11.233 216.86 43.62 53.02 303 .0 9.,17 20 .2 295. 0.1467 0. 972 11.499 217.77 44.19 53.53 305 .6 9 ,32 20 ,8

300. 0.1441 0. 974 11.768 218.67 44.77 54.06 308 ,1 9 ,47 21 ,5

310. 0.1391 0..976 12.314 220.46 45.95 55.14 313 .1 9 .76 22 .7

320. 0.1344 .979 12.871 222.23 47.16 56.27 318 .0 10,.05 24 ,1

330. 0.1301 ,981 13.440 223.98 48.39 57.43 322 .7 10 .33 25 .4

340. 0.1260 .982 14.020 225.71 49.64 58.62 327 .3 10 .62 26 .8 350. 0.1222 ,984 14.612 227.43 50.90 59.83 331 .9 10 .90 28 .3 360. 0.1187 .985 15.217 229.13 52.18 61.06 336 .3 11 .18 29 .8

370. 0.1153 .987 15.834 230.82 53.46 62.30 340 ,7 11 ,45 31 .3 380. 0.1121 .988 16.463 232.50 54.74 63.54 345 ,0 11 .73 32 .9 390. 0.1091 ,989 17.105 234.17 56.03 64.80 349 .2 12 ,00 34 .5 400. 0.1063 .990 17.759 235.82 57.31 66.05 353 .4 12 ,27 36 ,1

410. 0.1036 .991 18.426 237.47 58.59 67.30 357 .5 12 ,53 37 ,8

420. 0.1011 .991 19.105 239.11 59.86 68.55 361 .6 12, 80 39 ,5

430. 0.0987 .992 19.797 240.73 61.13 69.80 365 .6 13, 06 41 .2 440. 0.0964 .993 20.501 242.35 62.39 71.04 369 .5 13, 32 43 .0 450. 0.0942 .993 21.217 243.96 63.64 72.27 373 .4 13, 57 44 ,7

460. 0.0921 .994 21.946 245.57 64.88 73.49 377 ,3 13. 83 46 ,5

470. 0.0901 .994 22.687 247.16 66.11 74.70 381 ,1 14. 08 48. 3

480. 0.0882 .995 23.440 248.74 67.33 75.91 384 ,8 14. 33 50 2 490. 0.0863 .995 24.205 250.32 68.53 77.10 388 ,6 14. 58 52.

500. 0.0846 .996 24.982 251.89 69.73 78.28 392 3 14. 82 53. 9 520. 0.0812 ,996 26.571 255.01 72.07 80.60 399,,5 57. 7

540. 0.0782 ,997 28.206 258.09 74.37 82.88 406.,7 61. 6

560. 0.0754 ,997 29.886 261.15 76.61 85.10 413.,7 65. 5 580. 0.0727 ,998 31.610 264.17 78.80 87.28 420. 6 69. 4

600. 0.0703 ,998 33.377 267.17 80.94 89.40 427. 4 73, 4

625. 0.0674 ,999 35.644 270.87 83.54 91.99 435, 7

-150
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.4000 MPa

T P z H S C

V C

p W 1

A

K mo]L* dm kJ/mol J/(mol«K) J/(mol-K) m« s

l //Pa*

:

3 ITiW/(m<•K

95. 21 ,508 .024 -14 .557 80 .01 47.93 68.69 1971 .9 1060 .70 252 .3 100. 21 .330 .023 -14 .210 83 .58 48.15 70.10 1940 .0 880 .77 248 .3 105. 21 .150 .022 -13 .857 87 .01 47.90 70.68 1905 .6 744 .31 244 ,1

110. 20 .968 .021 -13 .504 90 .30 47.40 70.81 1870 .1 638 .88 239 .7 115. 20 .785 .020 -13 .150 93 .45 46.79 70.70 1833 ,9 555 .92 235 ,2

120. 20 .602 .019 -12 .797 96 .46 46.16 70.50 1797 .4 489 .49 230 ,5

125. 20 ,417 .019 -12 ,445 99 .33 45.55 70.30 1760 .7 435 .45 225 ,8

130. 20 ,232 .018 -12 ,094 102 .08 44.99 70.13 1723 .9 390 .81 220 ,9

135. 20 ,046 .018 -11 .743 104 .73 44.49 70.02 1686 .9 353 .45 216 ,1

140. 19 ,858 .017 -11 ,393 107 .27 44.06 69.99 1649 .9 321 ,78 211 ,2

145. 19 ,669 .017 -11 .043 109 .73 43.70 70.03 1612 .8 294 .63 206 ,2

150. 19 ,479 ,016 -10 .693 112 .11 43.40 70.15 1575 .6 271 .11 201 ,3

155. 19 ,286 ,016 -10 .342 114 .41 43.15 70.34 1538 ,3 250 .53 196 .3 160. 19,,092 .016 -9 ,989 116 ,65 42.96 70.61 1500 .9 232 .38 191 .4 165. 18 ,895 .015 -9 .635 118 ,82 42.83 70.95 1463 .4 216 .23 186 .4

170. 18,,696 .015 -9 .280 120 ,95 42.73 71.35 1425 ,8 201 ,76 181 .5 175. 18,.494 .015 -8 ,922 123 ,02 42.68 71.82 1388 ,1 188 ,71 176 .6 180. 18 ,289 .015 -8 ,561 125 .05 42.67 72.36 1350 .2 176 ,87 171 ,8

185. 18,,081 .014 -8 ,198 127 .04 42.69 72.96 1312 .1 166 .05 167 ,0

190. 17,,869 .014 -7 ,832 129 ,00 42.75 73.63 1273 ,9 156 .12 162 .2

195. 17,,653 .014 -7 ,462 130 ,92 42.83 74.37 1235 ,4 146 .97 157 ,4

200. 17,,432 .014 -7,,088 132 .81 42.95 75.18 1196 .6 138 .48 152 .7 205. 17.,207 ,014 -6 ,710 134 ,68 43.10 76.08 1157 6 130 .59 148 ,1

210. 16,,975 ,013 -6 ,327 136,,53 43.27 77.06 1118 ,1 123 .21 143 ,5

214.528 16,,760 ,013 -5 .976 138 ,18 43.46 78.04 1082,.0 116 .93 139 .3

214.528 0,.2465 ,910 7, 387 200 ,47 36.85 49.33 254 8 6 .89 12 .6 215. 0,,2458 ,910 7..410 200, 58 36.89 49.31 255 .2 6 .91 12 .7 220. 0,,2384 ,917 7,.656 201, 71 37.26 49.22 258, 9 7,.06 13 .1 225. 0, 2315 ,924 7,,902 202. 82 37.62 49.20 262, 5 7.,22 13,,5

230. 0, 2251 0,,929 8. 148 203. 90 37.99 49.26 266, 7.,37 13, 9

235. 0, 2192 ,934 8. 395 204, 96 38.37 49.38 269.,5 7 ,53 14 4

240. 0, 2136 0,,938 8. 642 206, 00 38.77 49.56 272. 8 7 .68 14, 9

245. 0. 2083 ,942 8.,891 207, 02 39.19 49.78 276, 7.,83 15, 3 250. 0, 2034 0.,946 9,.140 208, 03 39.62 50.05 279. 2 7, 99 15. 8

255. 0, 1987 ,949 9. 391 209, 03 40.08 50.35 282. 3 8, 14 16. 3

260. 0,.1942 ,953 9,.644 210. 01 40.55 50.69 285. 3 8, 29 16. 9 265. 0,,1900 ,955 9.,898 210. 98 41.04 51.06 288, 2 8, 44 17. 4

270. 0, 1860 ,958 10, 154 211, 93 41.54 51.46 291. 1 8, 59 18..0 275. 0.,1822 ,960 10,,413 212, 88 42.06 51.88 293. 9 8, 74 18. 5 280. 0,,1785 ,963 10 .673 213, 82 42.59 52.32 296. 7 8, 89 19. 1

151
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.4000 MPa (continued)

T P z H S C

V C

p W n

A

K mol«dm kJ/mol J/(mol«K) J/(mol«K) m»s

l ^iPa«s itiW/(m<-K

285. 0.1750 .965 10.936 214.75 43.14 52.78 299 .4 9 .04 19 .7 290. 0.1716 .967 11.201 215.67 43.69 53.26 302 .1 9 .19 20 .3 295. 0.1684 .968 11.469 216.59 44.25 53.76 304 .7 9 .33 20 .9 300. 0.1653 .970 11.739 217.50 44.83 54.27 307 .3 9 .48 21 .5 310. 0.1595 .973 12.287 219.29 46.00 55.33 312 .3 9 .77 22 .8

320. 0.1541 .976 12.845 221.07 47.20 56.44 317 .3 10 .06 24 .1 330. 0.1491 .978 13.415 222.82 48.43 57.58 322 .1 10 .35 25 .5 340. . 1444 .980 13.997 224.56 49.67 58.76 326 .7 10 .63 26 .9 350. 0.1400 .982 14.591 226.28 50.93 59.95 331 ,3 10 ,91 28 .3 360. 0.1359 .983 15.196 227.98 52.20 61.17 335 ,8 11 ,19 29 .8

370. 0.1320 .985 15.814 229.68 53.48 62.40 340 .2 11 ,46 31 .4 380. 0.1284 .986 16.444 231.36 54.76 63.64 344 ,6 11 ,74 32 .9 390. 0.1249 .987 17.087 233.03 56.05 64.88 348 .8 12.,01 34 .5 400. 0.1217 .988 17.742 234.68 57.33 66.13 353 .0 12 .28 36 .2 410. 0.1186 .989 18.410 236.33 58.61 67.38 357 .2 12,,54 37 .8

420. 0.1157 .990 19.090 237.97 59.88 68.62 361,,2 12,.81 39 .5 430. 0.1129 .991 19.782 239.60 61.14 69.86 365 .3 13, 07 41 .2 440. 0.1102 0,.992 20.487 241.22 62.40 71.10 369,,2 13, 33 43 .0 450. 0.1077 0,.992 21.204 242.83 63.65 72.32 373,.2 13. 58 44 ,7

460. 0.1053 0,,993 21.933 244.43 64.89 73.54 377,.0 13. 84 46 ,5

470. 0.1030 0. 994 22.675 246.03 66.12 74.75 380, 9 14. 09 48,,4

480. 0.1008 0,,994 23.428 247.62 67.34 75.95 384,.7 14. 34 50, 2 490. 0.0987 0.,995 24.194 249.19 68.54 77.14 388. 4 14. 59 52,.0 500. 0.0967 0,,995 24.971 250.76 69.73 78.32 392. 1 14. 83 53. 9

520. 0.0929 0.,996 26.561 253.88 72.08 80.64 399. 4 57. 7

540. 0.0894 0,,997 28.196 256.97 74.37 82.91 406. 6 61. 6 560. 0.0862 0,,997 29.877 260.02 76.61 85.13 413. 6 65. 5 580. 0.0831 0, 998 31.601 263.05 78.80 87.31 420. 5 69. 4

600. 0.0803 0. 998 33.369 266.04 80.94 89.43 427. 3 73. 4

625. 0.0771 0.,999 35.637 269.75 83.54 92.02 435. 6

152
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.4500 MPa

T P z H

( C

V C

p W n

A

K mo"L»dm kJ/mol J/(mol-K) J/(mol«K) m»s

l /iPa*

3 ITiW/(m •K

95. 21 .508 .026 -14.555 80 .01 47.93 68.69 1972 .1 1061 .15 252 .3 100. 21 .331 .025 -14.208 83 .57 48.15 70.09 1940 .2 881 .12 248 .4

105. 21 .150 .024 -13.856 87 .01 47.90 70.68 1905 .9 744 .59 244 .2 110. 20 .969 .023 -13.502 90 .30 47.40 70.80 1870 .3 639 .11 239 .8 115. 20 .786 .023 -13.148 93 .45 46.79 70.70 1834 .1 556 .11 235 .2

120. 20 .603 .022 -12.795 96 .45 46.16 70.50 1797 .6 489 .66 230 .5 125. 20 .418 .021 -12.443 99 .32 45.55 70.30 1760 .9 435 .59 225 .8 130. 20 .233 .021 -12.092 102 .08 44.99 70.13 1724 .1 390 .95 221 .0

135. 20 .047 .020 -11.741 104 .72 44.49 70.02 1687 .2 353 .57 216 .1

140. 19 .859 .019 -11.392 107 .27 44.06 69.98 1650 .2 321 .89 211 .2

145. 19 .670 .019 -11.042 109 .72 43.70 70.03 1613 .1 294 .73 206 .2 150. 19 .480 .019 -10.691 112 .10 43.40 70.15 1575 .9 271 .20 201 .3 155. 19 .287 .018 -10.340 114 .40 43.16 70.34 1538 .6 250 .62 196 .3 160. 19 .093 .018 -9.988 116 .64 42.97 70.61 1501 .2 232 .46 191 .4

165. 18 ,897 .017 -9.634 118 .82 42.83 70.94 1463 ,8 216 .31 186 .5

170. 18 ,698 .017 -9.278 120 .94 42.73 71.35 1426 ,2 201 .84 181 .6 175. 18,,496 .017 -8.920 123 .02 42.68 71.82 1388 .4 188 .79 176 .7 180. 18 ,291 ,016 -8.560 125 .05 42.67 72.35 1350 .6 176 .94 171 .8 185. 18 ,083 ,016 -8.197 127 .04 42.69 72.95 1312 .5 166 .12 167 .0 190. 17,,871 0,,016 -7.830 128 .99 42.75 73.62 1274 .3 156 .19 162 .2

195. 17,.655 0,,016 -7.460 130 .91 42.84 74.35 1235,,8 147 .04 157 .5 200. 17,,434 0,,016 -7.087 132 .81 42.95 75.17 1197,,1 138 ,55 152 .8 205. 17,,209 0,,015 -6.708 134 ,67 43.10 76.06 1158,,1 130 .66 148 .1 210. 16, 978 0, 015 -6.326 136 ,52 43.28 77.04 1118,.7 123, 28 143 ,5

215. 16, 740 0, 015 -5.938 138.,34 43.48 78.13 1078. 8 116, 36 139 ,0

217.598 16, 614 0, 015 -5.734 139,,28 43.59 78.74 1057. 9 112, 93 136 6 217.598 0, 2758 0, 902 7.468 199,,96 37.49 50.46 254. 9 7, 00 13,

220. 0,,2716 0, 906 7.589 200.,51 37.62 50.31 256. 8 7, 08 13, 2 225. 0. 2635 0, 913 7.840 201. 64 37.92 50.11 260. 6 7. 23 13. 6

230. 0, 2559 0. 919 8.091 202. 74 38.23 50.03 264. 2 7. 39 14.

235. 0. 2490 0. 925 8.341 203. 82 38.58 50.05 267. 8 7. 54 14. 5 240. 0, 2424 0. 930 8.591 204. 87 38.95 50.15 271. 2 7. 69 15..0 245. 0. 2363 0. 935 8.842 205. 91 39.35 50.31 274. 5 7. 85 15. 4

250. 0. 2305 0. 939 9.094 206. 93 39.77 50.52 277. 8 8. 00 15. 9

255. 0. 2251 0. 943 9.348 207. 93 40.21 50.78 280. 9 8. 15 16. 4

260. 0. 2200 0. 946 9.602 208. 92 40.67 51.08 284. 8. 30 16. 9 265. 0. 2151 0. 950 9.858 209. 89 41.15 51.42 287. 8. 45 17. 5 270. 0. 2104 0. 953 10.116 210. 86 41.64 51.79 290. 8. 60 18.

275. 0. 2060 0. 955 10.376 211. 81 42.15 52.18 292. 8 8. 75 18. 6 280. 0. 2018 0. 958 10.638 212. 76 42.67 52.60 295. 7 8. 90 19. 1

153-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.4500 MPa (continued)

T P z H S C

V C

p W 1

A

K mo 1 • dm kJ/mol J/(mol'K) J/(mol«K) m» s

l ^Pa«s itiW/(m-K

285. 0.1978 .960 10.902 213.69 43.21 53.04 298 .4 9 .05 19 .7 290. 0.1939 ,962 11.169 214.62 43.76 53.50 301 .1 9 .20 20 .3 295. 0.1903 .964 11.438 215.54 44.32 53.99 303 .8 9 .35 20 .9 300. 0.1867 ,966 11.709 216.45 44.89 54.48 306 .4 9 .49 21 .6 310. 0.1801 .970 12.259 218.25 46.05 55.52 311 .6 9 .78 22 .8

320. 0.1739 0,,972 12.819 220.03 47.25 56.61 316 .6 10 .07 24 .1 330. 0.1682 0,,975 13.391 221.79 48.47 57.73 321 .4 10 .36 25 .5 340. 0.1629 0,,977 13.974 223.53 49.71 58.89 326 .2 10 .64 26 .9 350. 0.1579 0,,979 14.569 225.25 50.96 60.08 330 .8 10 .92 28 .4 360. 0.1532 0,,981 15.176 226.96 52.23 61.28 335 .3 11 .20 29 .9

370. 0.1488 0, 983 15.795 228.66 53.50 62.50 339 .8 11 .48 31 .4 380. 0.1447 0, 984 16.426 230.34 54.78 63.73 344 .1 11 .75 33 .0 390. 0.1408 0. 986 17.069 232.01 56.06 64.97 348 .4 12 .02 34 .6 400. 0.1371 0, 987 17.725 233.67 57.34 66.21 352 .7 12 .29 36 .2 410. 0.1336 0,,988 18.393 235.32 58.62 67.45 356 .8 12 ,55 37 .8

420. 0.1303 0,,989 19.074 236.96 59.89 68.69 360 ,9 12 ,82 39 .5 430. 0.1271 0,.990 19.767 238.60 61.16 69.93 365 .0 13 ,08 41 .3 440. 0.1242 0,,991 20.473 240.22 62.42 71.16 369 ,0 13,,34 43,,0

450. 0.1213 0,,991 21.190 241.83 63.66 72.38 372 ,9 13,,59 44..8 460. 0.1186 0, 992 21.920 243.43 64.90 73.60 376 ,8 13. 85 46,.6

470. 0.1160 0. 993 22.662 245.03 66.13 74.80 380.,7 14, 10 48.,4

480. 0.1135 0. 993 23.416 246.62 67.35 76.00 384, 5 14, 35 50. 2 490. 0.1111 0, 994 24.182 248.20 68.55 77.19 388, 2 14, 60 52. 1 500. 0.1089 0, 994 24.960 249.77 69.74 78.36 392, 14. 84 53. 9

520. 0.1046 0. 995 26.551 252.89 72.09 80.68 399. 3 57. 7

540. 0.1006 0. 996 28.187 255.97 74.38 82.95 406. 5 61. 6

560. 0.0970 0. 997 29.868 259.03 76.62 85.17 413. 5 65. 5 580. 0.0936 0. 997 31.593 262.06 78.81 87.34 420. 4 69. 5 600. 0.0904 0. 998 33.361 265.05 80.94 89.46 427. 3 73. 5 625. 0.0867 0. 998 35.630 268.76 83.55 92.04 435. 6

154-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.5000 MPa

T P z H

< ( V C

p W n

A

K mo!L«dm kJ/mol J/(mol»K) J/(mol-K) m« s

i /iPa*

:

5 niW/(m •K

95. 21 .509 .029 -14 .553 80 .00 47 .93 68.68 1972 .3 1061 .60 252 .3

100. 21 .331 .028 -14 .206 83 .57 48 .15 70.09 1940 .5 881 .47 248 .4

105. 21 .151 .027 -13 .854 87 .00 47 .91 70.68 1906 .1 744 .87 244 .2

110. 20 .970 .026 -13 .500 90 .30 47 .41 70.80 1870 .5 639 .34 239 .8

115. 20 .787 .025 -13 .146 93 .44 46 .80 70.70 1834 .3 556 .31 235 .2

120. 20 .603 .024 -12 .793 96 .45 46 .16 70.50 1797 .8 489 .83 230 .6

125. 20 .419 .024 -12 .441 99 .32 45 .55 70.29 1761 .2 435 .74 225 .8

130. 20 .234 .023 -12 .090 102 .07 44 .99 70.12 1724 .4 391 .08 221 .0

135. 20 .048 .022 -11 .740 104 .72 44 .50 70.01 1687 .4 353 .69 216 .1

140. 19 .860 .022 -11 .390 107 .26 44 .07 69.98 1650 .4 322 .00 211 .2

145. 19 .671 .021 -11 .040 109 .72 43 .70 70.02 1613 .4 294 .83 206 .3 150. 19 .481 .021 -10 .689 112 .10 43 .40 70.14 1576 .2 271 .30 201 .3 155. 19 .289 .020 -10 .338 114 .40 43 .16 70.34 1538 .9 250 .71 196 .4

160. 19 .094 .020 -9 .986 116 .64 42 .97 70.60 1501 .6 232 .55 191 .4

165. 18 .898 0,.019 -9 .632 118 .81 42 .83 70.94 1464 .1 216 .39 186 .5

170. 18 ,699 .019 -9 .276 120 .94 42 .74 71.34 1426 .5 201 .92 181 .6 175. 18 .497 0,.019 -8 .919 123 .01 42 .69 71.81 1388 ,8 188 .86 176 .7 180. 18 .292 0,,018 -8 .558 125 .04 42 .67 72.34 1351 ,0 177 .01 171 .9 185. 18 ,084 0,,018 -8 .195 127 .03 42 .69 72.94 1312 ,9 166 .19 167 .0 190. 17 ,873 0,,018 -7 .829 128 .99 42 .75 73.61 1274 ,7 156 ,26 162 .3

195. 17,,657 0,,017 -7 .459 130 .91 42 .84 74.34 1236,,3 147 ,11 157 .5 200. 17.,436 0,,017 -7 ,085 132 .80 42 .96 75.15 1197, 6 138 ,62 152 .8 205. 17,,211 0, 017 -6 ,707 134 ,67 43 .10 76.04 1158, 6 130 ,73 148 .2 210. 16, 980 0. 017 -6,,325 136 ,51 43 .28 77.02 1119, 2 123 ,35 143 .6 215. 16, 743 0. 017 -5,,937 138, 33 43 ,48 78.11 1079, 4 116, 43 139 .0

220. 16. 499 0. 017 -5, 543 140, 14 43,,71 79.31 1039. 1 109, 91 134,,5

220.423 16. 478 0. 017 -5, 510 140, 30 43,,73 79.42 1035. 6 109, 37 134, 1 220.423 0. 3050 0. 895 7. 541 199. 50 38, 08 51.55 254. 9 7, 10 13, 4

225. 0. 2963 0. 902 7. 776 200, 56 38, 26 51.15 258. 5 7, 25 13,.7 230. 0. 2875 0. 909 8. 031 201. 68 38, 51 50.89 262. 3 7. 40 14, 2

235. 0. 2794 0. 916 8. 285 202. 77 38. 81 50.78 266. 7. 55 14. 6 240. 0. 2718 0. 922 8. 539 203. 84 39. 15 50.78 269. 5 7. 71 15.

245. 0. 2648 0. 927 8. 793 204. 89 39. 52 50.87 273. 7. 86 15. 5 250. 0. 2582 0. 932 9. 048 205. 92 39. 92 51.02 276. 3 8. 01 16.

255. 0. 2519 0. 936 9. 303 206. 93 40. 34 51.23 279. 6 8. 17 16. 5

260. 0. 2460 0. 940 9. 560 207. 93 40. 79 51.49 282. 7 8. 32 17.

265. 0. 2405 0. 944 9. 818 208. 91 41. 26 51.79 285. 8 8. 47 17. 5 270. 0. 2352 0. 947 10. 078 209. 88 41. 74 52.13 288. 8 8. 62 18. 1 275. 0. 2302 0. 950 10. 340 210. 84 42. 24 52.50 291. 7 8. 77 18. 6 280. 0. 2254 0. 953 10. 603 211. 79 42. 76 52.89 294. 6 8. 92 19. 2

155-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.5000 MPa (continued)

T P z H S C

V C

p W n

A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol«K)

-

1

m« s ^Pa« <; niW/(m»K

285. 0.2208 .956 10.869 212.73 43.29 53.31 297.4 9 .06 19.8

290. 0.2165 .958 11.136 213.66 43.83 53.76 300.2 9 .21 20.4

295. 0.2123 .960 11.406 214.59 44.38 54.22 302.9 9 .36 21.0

300. 0.2083 .962 11.678 215.50 44.95 54.70 305.6 9 .50 21.6

310. 0.2008 .966 12.231 217.31 46.10 55.71 310.8 9 .80 22.9

320. 0.1939 .969 12.793 219.10 47.29 56.78 315.9 10 .08 24.2

330. 0.1874 .972 13.366 220.86 48.51 57.89 320.8 10 .37 25.6

340. 0.1814 .975 13.951 222.61 49.74 59.03 325.6 10 .65 27.0

350. 0.1758 ,977 14.547 224.33 50.99 60.20 330.2 10 .93 28.4

360. 0.1706 .979 15.155 226.05 52.26 61.40 334.8 11,,21 29.9

370. 0.1657 ,981 15.775 227.75 53.53 62.61 339.3 11 ,49 31.4

380. 0.1610 .983 16.407 229.43 54.80 63.83 343.7 11.,76 33.0

390. 0.1567 0,,984 17.051 231.11 56.08 65.06 348.1 12..03 34.6

400. 0.1526 0..985 17.708 232.77 57.36 66.29 352.3 12. 30 36.2

410. 0.1487 0,,987 18.377 234.42 58.64 67.53 356.5 12..56 37.9

420. 0.1450 0,,988 19.059 236.06 59.91 68.76 360.6 12. 83 39.6

430. 0.1414 0,,989 19.752 237.69 61.17 69.99 364.7 13. 09 41.3

440. 0.1381 0, 990 20.459 239.32 62.43 71.22 368.7 13. 35 43.0

450. 0.1349 0. 991 21.177 240.93 63.67 72.44 372.7 13. 60 44.8

460. 0.1319 0. 991 21.907 242.54 64.91 73.65 376.6 13. 86 46.6

470. 0.1290 0. 992 22.650 244.13 66.14 74.85 380.5 14. 11 48.4

480. 0.1262 0. 993 23.404 245.72 67.35 76.05 384.3 14. 36 50.2

490. 0.1236 0. 993 24.171 247.30 68.56 77.23 388.1 14. 61 52.1

500. 0.1210 0. 994 24.949 248.87 69.75 78.41 391.8 14. 85 54.0

520. 0.1163 0. 995 26.540 252.00 72.09 80.72 399.2 57.7

540. 0.1118 0. 996 28.177 255.08 74.38 82.98 406.4 61.6

560. 0.1078 0. 996 29.859 258.14 76.62 85.20 413.4 65.5

580. 0.1040 0. 997 31.585 261.17 78.81 87.36 420.4 69.5

600. 0.1005 0. 998 33.353 264.17 80.95 89.48 427.2 73.5

625. 0.0964 0. 998 35.623 267.87 83.55 92.06 435.6

156-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.5500 MPa

T P z H

< C

V C

p W V A

K mo!L«dm kJ/mol J/(mol»K) J/(mol.K) m« s

• i /iPa«

3 rriw/o•K

95. 21 .510 .032 -14 .551 80 .00 47 .93 68.68 1972 .6 1062 .05 252 .4

100. 21 .332 .031 -14 .204 83 .56 48 .15 70.09 1940 .7 881 .82 248 .4

105. 21 .152 .030 -13 .852 87 .00 47 .91 70.67 1906 .3 745 .15 244 .2 110. 20 .970 .029 -13 .498 90 .29 47 .41 70.80 1870 .7 639 .57 239 .8 115. 20 .788 .028 -13 .144 93 .44 46 .80 70.69 1834 .6 556 .50 235 .3

120. 20 .604 .027 -12 .791 96 .44 46 .16 70.50 1798 .1 490 .00 230 .6 125. 20 .420 .026 -12 .439 99 .32 45 .55 70.29 1761 .4 435 .89 225 .9 130. 20 .235 .025 -12 .088 102 .07 45 .00 70.12 1724 .6 391 .21 221 .0 135. 20 .048 .024 -11 .738 104 .71 44 .50 70.01 1687 .7 353 .81 216 .2 140. 19 .861 .024 -11 .388 107 .26 44 .07 69.98 1650 .7 322 .11 211 .3

145. 19 .672 .023 -11 .038 109 .71 43 .70 70.02 1613 .6 294 .93 206 .3 150. 19 .482 ,023 -10 .688 112 .09 43 .40 70.14 1576 .5 271 .39 201 .4 155. 19 ,290 .022 -10 .336 114 .39 43 .16 70.33 1539 ,2 250 .80 196 .4 160. 19 ,096 .022 -9 .984 116 .63 42 .97 70.60 1501 ,9 232 .63 191 .5 165. 18 ,899 ,021 -9 .630 118 .81 42 .83 70.93 1464 ,4 216 .48 186 .5

170. 18 .700 .021 -9 .275 120 .93 42 .74 71.33 1426 .9 202 .00 181 .6 175. 18 .499 .020 -8 .917 123 ,00 42 .69 71.80 1389 .2 188 .94 176 .8 180. 18 .294 .020 -8 .557 125 ,03 42 .67 72.33 1351 .4 177 .09 171 .9 185. 18 .086 .020 -8 .193 127 ,02 42 .70 72.93 1313 ,4 166 .27 167 .1 190. 17 .874 ,019 -7 .827 128 ,98 42 .75 73.59 1275 ,2 156 .33 162 .3

195. 17 ,659 ,019 -7,.457 130,,90 42 .84 74.33 1236 ,8 147 .18 157 ,6

200. 17 ,438 ,019 -7 .084 132, 79 42 ,96 75.14 1198 ,1 138 .69 152 ,9

205. 17,,213 ,019 -6 ,706 134, 66 43 ,11 76.03 1159 ,1 130 .79 148 ,2

210. 16,,982 0,,019 -6 ,323 136, 50 43 ,28 77.01 1119 7 123 ,42 143 ,6

215. 16.,745 0,,018 -5 ,936 138, 33 43,,48 78.09 1080 ,0 116 ,50 139 ,1

220. 16,,501 0,,018 -5,,542 140,,13 43,,71 79.29 1039 ,7 109 ,98 134 ,5

223.045 16,,349 0,,018 -5,,300 141, 23 43,,87 80.08 1014, 9 106 ,18 131 8 223.045 0,,3343 0,,887 7,,606 199, 09 38,,62 52.60 254, 8 7 ,20 13,,7

225. 0,,3300 0, 891 7,,709 199. 55 38,,66 52.34 256, 4 7 ,26 13 9

230. 0,,3198 0, 899 7,,969 200. 70 38,,83 51.85 260. 4 7, 42 14,,3

235. 0, 3105 0, 907 8.,228 201. 81 39, 07 51.58 264. 2 7, 57 14,,7

240. 3018 0, 913 8 ,485 202. 89 39, 36 51.47 267, 9 7, 72 15, 1 245. 0,,2938 0, 919 8, 743 203. 95 39, 70 51.46 271, 4 7, 88 15. 6

250. 0,,2862 0, 924 9,,000 204. 99 40, 08 51.55 274. 9 8, 03 16. 1 255. 0,,2792 0, 929 9,,258 206. 02 40, 48 51.71 278. 2 8, 18 16. 6

260. 0,,2725 0, 934 9,,517 207. 02 40. 91 51.92 281. 4 8. 33 17. 1 265. 0, 2662 0, 938 9,,778 208. 01 41. 37 52.18 284. 6 8, 48 17. 6

270. 0, 2602 0, 941 10,,039 208. 99 41. 84 52.48 287. 6 8. 63 18. 2 275. 0,,2546 0, 945 10,.302 209. 96 42. 33 52.82 290. 6 8. 78 18. 7 280. 0,,2492 0, 948 10 .567 210. 91 42. 84 53.19 293. 6 8, 93 19. 3

157
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.5500 MPa (continued)

T P z H S C

V C

p W o

A

K mol»dm kJ/mol J/(mol'K) J/(mol»K) m»s

l /iiPa«s iriW/(m<•K

285. 0.2441 .951 10.834 211.86 43.36 53.59 296 .5 9 .08 19 .8 290. 0.2392 .954 11.103 212.79 43.90 54.02 299 .3 9 .23 20 .4

295. 0.2345 .956 11.375 213.72 44.45 54.46 302 .0 9 .37 21 .0

300. 0.2301 .958 11.648 214.64 45.01 54.93 304 .7 9 .52 21 .7 310. 0.2217 .963 12.202 216.46 46.15 55.91 310 .0 9 .81 22 .9

320. 0.2139 ,966 12.766 218.25 47.34 56.95 315 .1 10 .10 24 .2 330. 0.2068 .969 13.341 220.02 48.55 58.04 320 .1 10 .38 25 .6 340. 0.2001 .972 13.927 221.77 49.78 59.17 325 .0 10 .67 27 .0

350. 0.1939 ,975 14.525 223.50 51.02 60.33 329 .7 10 .95 28 .4

360. 0.1881 .977 15.134 225.21 52.28 61.51 334 .3 11 .22 29 .9

370. 0.1826 0.,979 15.755 226.92 53.55 62.71 338 .9 11 .50 31 .5 380. 0.1775 ,981 16.388 228.60 54.83 63.92 343 ,3 11 .77 33 .0

390. 0.1726 0.,983 17.034 230.28 56.10 65.14 347 .7 12 ,04 34 .6 400. 0.1681 0, 984 17.691 231.95 57.38 66.37 352 .0 12 ,31 36 .2 410. 0.1637 0,,985 18.361 233.60 58.65 67.60 356 ,2 12 ,58 37 .9

420. 0.1596 0,,987 19.043 235.24 59.92 68.83 360 ,3 12 ,84 39 .6 430. 0.1558 0,,988 19.738 236.88 61.18 70.06 364 ,4 13,,10 41 .3 440. 0.1521 0, 989 20.444 238.50 62.44 71.28 368,,5 13, 36 43 .0 450. 0.1485 0. 990 21.163 240.12 63.69 72.50 372, 4 13, 61 44 .8 460. 0.1452 0. 990 21.894 241.72 64.92 73.70 376, 4 13, 87 46 .6

470. 0.1420 0, 991 22.637 243.32 66.15 74.91 380. 3 14. 12 48 ,4

480. 0.1389 0. 992 23.392 244.91 67.36 76.10 384. 1 14. 37 50..2 490. 0.1360 0. 993 24.159 246.49 68.57 77.28 387. 9 14. 62 52, 1 500. 0.1332 0. 993 24.938 248.07 69.76 78.45 391. 6 14. 86 54,

520. 0.1279 0. 994 26.530 251.19 72.10 80.76 399. 57. 8

540. 0.1231 0. 995 28.168 254.28 74.39 83.02 406. 3 61. 6

560. 0.1186 0. 996 29.850 257.34 76.63 85.23 413. 4 65. 5 580. 0.1144 0. 997 31.577 260.37 78.82 87.39 420. 3 69. 5 600. 0.1105 0. 997 33.346 263.36 80.95 89.51 427. 2 73. 5 625. 0.1061 0. 998 35.616 267.07 83.56 92.09 435. 5

158
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.6000 MPa

T P z H

i ( V C

p W V

A

K mo L • dm"

3 kJ/mol J/(mol-K) J/(mol-K) m» s

• i /iPa*

.

3 IT W/(m K

95. 21 .510 .035 -14.549 80 .00 47 .93 68.68 1972 .8 1062 .50 252 .4

100. 21 .333 .034 -14.202 83 .56 48 .16 70.09 1940 9 882 .17 248 .4

105. 21 .152 .032 -13.850 87 .00 47 .91 70.67 1906 5 745 .43 244 2 110. 20 .971 .031 -13.496 90 .29 47 .41 70.80 1870 9 639 .80 239 .8 115. 20 .788 .030 -13.142 93 .43 46 .80 70.69 1834 8 556 .70 235 .3

120. 20 .605 .029 -12.789 96 .44 46 .17 70.49 1798 3 490 .17 230 .6 125. 20 .421 .028 -12.437 99 31 45 .56 70.29 1761 6 436 .04 225 9 130. 20 236 .027 -12.086 102 06 45 .00 70.12 1724 9 391 34 221 1 135. 20 049 027 -11.736 104 71 44 .50 70.01 1688 353 93 216 2 140. 19 862 026 -11.386 107 25 44 .07 69.97 1651 322 22 211 3

145. 19 673 025 -11.036 109 71 43 71 70.01 1613 9 295 03 206 3 150. 19 483 025 -10.686 112 09 43 41 70.13 1576 8 271 49 201 4

155. 19 291 024 -10.335 114 39 43 16 70.33 1539 5 250 89 196 5 160. 19 097 024 -9.982 116 62 42 97 70.59 1502 2 232 72 191 5 165. 18 900 023 -9.629 118 80 42 84 70.93 1464 8 216 56 186 6

170. 18 702 023 -9.273 120 92 42 74 71.33 1427 2 202 08 181 7 175. 18 500 022 -8.915 123 00 42 69 71.79 1389 6 189 02 176 8 180. 18 296 022 -8.555 125 03 42 68 72.32 1351 7 177 16 171 9 185. 18 088 022 -8.192 127 02 42 70 72.92 1313 8 166 34 167 1 190. 17 876 021 -7.826 128 97 42 76 73.58 1275 6 156 40 162 4

195. 17 660 021 -7.456 130 89 42 84 74.32 1237 2 147 25 157 6 200. 17 440 021 -7.082 132 78 42 96 75.12 1198 6 138 76 152 9

205. 17 215 020 -6.705 134 65 43 11 76.01 1159 6 130 86 148 3 210. 16 985 020 -6.322 136 49 43 28 76.99 1120 3 123 48 143 7 215. 16 748 020 -5.934 138 32 43 49 78.07 1080 6 116 56 139 1

220. 16 504 020 -5.541 140 13 43 72 79.26 1040 3 110 05 134 6 225. 16 252 020 -5.142 141 92 43 97 80.59 999 5 103 88 130 1 225.497 16 227 020 -5.102 142 10 44 00 80.74 995 4 103 29 129 7 225.497 3636 880 7.666 198 72 39 14 53.62 254 7 7 29 14

230. 3530 889 7.905 199 77 39 19 52.94 258 4 7 43 14 4

235. 3423 897 8.169 200 90 39 35 52.47 262 4 7 59 14 8

240. 3324 904 8.431 202 01 39 59 52.21 266. 2 7 74 15 2 245. 3233 911 8.691 203 08 39 90 52.10 269. 8 7 89 15 7 250. 3148 917 8.952 204 13 40 24 52.11 273. 4 8 04 16 2 255. 3068 922 9.213 205 17 40 63 52.20 276. 8 8 20 16 7

260. 2993 927 9.474 206 18 41 04 52.36 280. 1 8 35 17 2 265. 2923 932 9.736 207. 18 41 48 52.58 283. 3 8. 50 17. 7 270. 2856 936 10.000 208. 17 41 95 52.85 286. 5 8. 65 18. 2 275. 2793 940 10.265 209. 14 42 43 53.16 289. 5 8. 80 18. 8

280. 2733 943 10.531 210. 10 42 93 53.50 292. 5 8 94 19. 3

159
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.6000 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol-K) J/(mol«K) m« s

l /iPa«:3 niW/(m-•K

285. 0.2676 .946 10.800 211.05 43.44 53.88 295 .5 9 .09 19 .9

290. 0.2622 .949 11.070 211.99 43.97 54.28 298 .3 9 .24 20 .5 295. 0.2570 .952 11.343 212.92 44.51 54.71 301 .1 9 .39 21 .1

300. 0.2520 .954 11.617 213.85 45.07 55.16 303 .9 9 .53 21 .7 310. 0.2427 .959 12.174 215.67 46.21 56.11 309 .2 9 .82 23 .0

320. 0.2341 .963 12.740 217.47 47.38 57.13 314 .4 10 .11 24 .3 330. 0.2262 .967 13.316 219.24 48.58 58.20 319 .5 10 .40 25 .6 340. 0.2189 .970 13.904 220.99 49.81 59.31 324 .4 10 .68 27 .0

350. 0.2120 .973 14.503 222.73 51.05 60.46 329 .2 10 .96 28 .5 360. 0.2056 .975 15.113 224.45 52.31 61.63 333 .8 11 .24 30 .0

370. 0.1996 .977 15.735 226.15 53.58 62.82 338 .4 11,.51 31 .5 380. 0.1939 .979 16.370 227.85 54.85 64.02 342 .9 11 .78 33 .0 390. 0.1886 .981 17.016 229.52 56.12 65.23 347 .3 12 ,05 34 .6 400. 0.1836 0,.983 17.674 231.19 57.40 66.45 351 .6 12 .32 36 .3 410. 0.1789 0,,984 18.345 232.85 58.67 67.68 355 .8 12,,59 37 .9

420. 0.1744 0, 985 19.028 234.49 59.93 68.90 360 .0 12. 85 39 .6 430. 0.1701 0. 987 19.723 236.13 61.20 70.12 364 ,1 13. 11 41 .3 440. 0.1661 0. 988 20.430 237.75 62.45 71.34 368 ,2 13. 37 43 .1 450. 0.1622 0, 989 21.150 239.37 63.70 72.55 372 .2 13, 63 44,,8

460. 0.1585 0. 990 21.881 240.98 64.93 73.76 376. 2 13, 88 46 .6

470. 0.1550 0. 990 22.625 242.58 66.16 74.96 380. 1 14. 13 48. 4

480. 0.1517 0. 991 23.380 244.17 67.37 76.14 383. 9 14. 38 50. 3

490. 0.1485 0. 992 24.148 245.75 68.57 77.32 387. 7 14. 63 52. 1 500. 0.1454 0. 993 24.927 247.32 69.76 78.49 391. 5 14. 87 54.

520. 0.1396 0. 994 26.520 250.45 72.11 80.79 398. 9 57. 8

540. 0.1343 0. 995 28.158 253.54 74.40 83.05 406. 2 61. 6

560. 0.1294 0. 996 29.842 256.60 76.63 85.26 413. 3 65. 5 580. 0.1249 0. 996 31.568 259.63 78.82 87.42 420. 2 69. 5 600. 0.1206 0. 997 33.338 262.63 80.96 89.53 427. 1 73. 5 625. 0.1157 0. 998 35.609 266.34 83.56 92.11 435. 5

160
Table B3 . Properties in the single -phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.6500 MPa

T P z H

i C

V C

p W n

A

K mo L*dm kJ/mol J/(mol«K) J/(mol-K) m* s

i fi?a* i 3 IT W/(m K

95. 21 .511 .038 -14 .547 79 .99 47.93 68.67 1973 1062 .95 252 4

100. 21 .333 .037 -14 .200 83 .56 48.16 70.09 1941 1 882 52 248 5 105. 21 .153 .035 -13 .848 86 99 47.91 70.67 1906 7 745 71 244 3 110. 20 .972 034 -13 .494 90 28 47.41 70.80 1871 2 640 04 239 9 115. 20 .789 033 -13 .140 93 43 46.80 70.69 1835 556 89 235 3

120. 20 606 032 -12 787 96 43 46.17 70.49 1798 5 490 34 230 7 125. 20 422 031 -12 435 99 31 45.56 70.29 1761 9 436 19 225 9

130. 20 236 030 -12 084 102 06 45.00 70.11 1725 1 391 47 221 1 135. 20 050 029 -11 734 104 70 44.50 70.01 1688 2 354 05 216 2 140. 19 863 028 -11 384 107 25 44.07 69.97 1651 3 322 33 211 3

145. 19 674 027 -11 034 109 70 43.71 70.01 1614 2 295 14 206 4

150. 19 484 027 -10 684 112 08 43.41 70.13 1577 1 271 58 201 4

155. 19 292 026 -10 333 114 38 43.16 70.32 1539 8 250 98 196 5 160. 19 098 026 -9 981 116 62 42.98 70.59 1502 5 232 80 191 5 165. 18 902 025 -9 627 118 80 42.84 70.92 1465 1 216 64 186 6

170. 18 703 025 -9 271 120 92 42.74 71.32 1427 6 202 16 181 7 175. 18 502 024 -8 914 122 99 42.69 71.79 1389 9 189 09 176 8 180. 18 297 024 -8 553 125 02 42.68 72.32 1352 1 177 23 172

185. 18 089 023 -8 190 127 01 42.70 72.91 1314 2 166 41 167 2 190. 17 878 023 -7 824 128 97 42.76 73.57 1276 156 48 162 4

195. 17 662 023 -7 454 130 89 42.85 74.30 1237 7 147 31 157 7 200. 17 442 022 -7 081 132 78 42.96 75.11 1199 138 83 153

205. 17 217 022 -6 703 134 64 43.11 75.99 1160 1 130 93 148 3 210. 16 987 022 -6 321 136 48 43.29 76.97 1120 8 123 55 143 7 215. 16 750 022 -5 933 138 31 43.49 78.05 1081 1 116 63 139 2

220. 16 507 022 -5 540 140 12 43.72 79.24 1041 110 11 134 7 225. 16 255 021 -5 141 141 91 43.97 80.57 1000 2 103 95 130 2 227.802 16 111 021 -4 914 142 91 44.13 81.38 977 100 64 127 7 227.802 3930 873 7 720 198 37 39.63 54.62 254 4 7 38 14 3 230. 3871 878 7 839 198 90 39.61 54.17 256 3 7 45 14 5

235. 3749 887 8 108 200 05 39.67 53.45 260 5 7 60 14 9

240. 3637 896 8 374 201 17 39.85 53.02 264 4 7 76 15 4

245. 3534 903 8 639 202 26 40.11 52.79 268 2 7 91 15 8 250. 3439 909 8 902 203 33 40.42 52.71 271 8 8 06 16 3 255. 3349 915 9 166 204 37 40.78 52.73 275 4 8 21 16 8

260. 3266 921 9 430 205 40 41.18 52.83 278 8 8 36 17 3 265. 3187 926 9 694 206 41 41.60 53.00 282. 1 8 51 17. 8 270. 3113 930 9 960 207 40 42.05 53.23 285 3 8 66 18. 3 275. 3043 934 10 227 208 38 42.52 53.51 288 4 8 81 18 8 280. 2977 938 10 495 209 34 43.01 53.82 291 5 8 96 19 4

161
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.6500 MPa (continued)

T P z H S C

V C

p W V

X

K mol«dm kJ/mol J/(mol«K) J/(mol»K) m» s

l /itPa«s niW/(m-•K

285. 0.2913 .942 10.765 210.30 43.52 54.17 294 .5 9 .11 20 .0

290. 0.2853 .945 11.037 211.25 44.04 54.55 297 .4 9 .25 20 .6 295. 0.2796 .948 11.311 212.18 44.58 54.96 300 .2 9 .40 21 .2 300. 0.2741 .951 11.587 213.11 45.13 55.39 303 .0 9 .55 21 .8 310. 0.2639 .956 12.145 214.94 46.26 56.32 308 .5 9 .84 23 .0

320. 0.2545 .960 12.713 216.74 47.43 57.31 313 .7 10 .12 24 .3 330. 0.2458 .964 13.291 218.52 48.62 58.36 318 .8 10 .41 25 .7 340. 0.2377 .967 13.881 220.28 49.84 59.46 323 .8 10 .69 27 .1 350. 0.2302 .970 14.481 222.02 51.08 60.59 328 .6 10 .97 28 .5 360. 0.2232 .973 15.092 223.74 52.34 61.74 333 .3 11 ,25 30 .0

370. 0.2167 .975 15.716 225.45 53.60 62.92 337 .9 11 ,52 31 ,5

380. 0.2105 .977 16.351 227.15 54.87 64.12 342 .5 11 .80 33 .1 390. 0.2047 .979 16.998 228.83 56.14 65.32 346 .9 12 .07 34 .7 400. 0.1992 ,981 17.657 230.50 57.41 66.54 351 .2 12 ,33 36 .3 410. 0.1940 ,983 18.329 232.15 58.68 67.75 355 ,5 12 ,60 38 .0

420. 0.1891 ,984 19.012 233.80 59.95 68.97 359 ,7 12. 86 39 .6 430. 0.1845 0.,985 19.708 235.44 61.21 70.19 363 ,9 13 12 41 ,3

440. 0.1801 ,987 20.416 237.07 62.46 71.40 367 .9 13, 38 43,,1

450. 0.1759 ,988 21.136 238.68 63.71 72.61 372 13. 64 44, 9

460. 0.1719 ,989 21.868 240.29 64.94 73.81 375 9 13, 89 46,.6

470. 0.1681 0,,990 22.612 241.89 66.17 75.01 379, 9 14. 14 48,,5

480. 0.1644 ,990 23.368 243.48 67.38 76.19 383, 7 14. 39 50. 3

490. 0.1610 0. 991 24.136 245.07 68.58 77.37 387, 5 14. 64 52. 1 500. 0.1576 0. 992 24.916 246.64 69.77 78.53 391. 3 14. 88 54.

520. 0.1514 0. 993 26.510 249.77 72.11 80.83 398. 8 57. 8

540. 0.1456 0, 994 28.149 252.86 74.40 83.09 406. 61. 6

560. 0.1403 0. 995 29.833 255.92 76.64 85.29 413. 2 65. 6 580. 0.1353 0. 996 31.560 258.95 78.83 87.45 420. 2 69. 5 600. 0.1307 0. 997 33.330 261.95 80.96 89.56 427. 1 73. 5 625. 0.1254 0. 998 35.602 265.66 83.56 92.14 435. 5

-162-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.7000 MPa

T P z H

i C

V C

p W V

A

K mo" .•dm kJ/mol J/(mol«K) J/(mol«K) m« s

l ^Pa«

;

3 IT W/(m •K

95. 21 511 041 -14.545 79 99 47.93 68.67 1973 2 1063 40 252 4

100. 21 334 039 -14.198 83 55 48.16 70.08 1941 3 882 87 248 5 105. 21 154 038 -13.846 86 99 47.91 70.67 1907 745 99 244 3 110. 20 972 036 -13.492 90 28 47.41 70.79 1871 4 640 27 239 9

115. 20 790 035 -13.138 93 42 46.80 70.69 1835 2 557 09 235 3

120. 20 606 034 -12.785 96 43 46.17 70.49 1798 8 490 50 230 7 125. 20 422 033 -12.433 99 30 45.56 70.28 1762 1 436 33 225 9 130. 20 237 032 -12.082 102 06 45.00 70.11 1725 4 391 61 221 1 135. 20 051 031 -11.732 104 70 44.51 70.00 1688 5 354 17 216 3 140. 19 864 030 -11.382 107 24 44.08 69.97 1651 5 322 44 211 3

145. 19 675 030 -11.032 109 70 43.71 70.01 1614 5 295 24 206 4

150. 19 485 029 -10.682 112 08 43.41 70.12 1577 4 271 68 201 5 155. 19 293 028 -10.331 114 38 43.17 70.32 1540 1 251 07 196 5 160. 19 099 028 -9.979 116 61 42.98 70.58 1502 8 232 89 191 6 165. 18 903 027 -9.625 118 79 42.84 70.91 1465 4 216 72 186 6

170. 18 704 026 -9.270 120 91 42.75 71.31 1427 9 202 23 181 7 175. 18 503 026 -8.912 122 99 42.69 71.78 1390 3 189 17 176 9 180. 18 299 026 -8.552 125 02 42.68 72.31 1352 5 177 31 172

185. 18 091 025 -8.189 127 01 42.70 72.90 1314 6 166 48 167 2 190. 17 880 025 -7.823 128 96 42.76 73.56 1276 5 156 55 162 4

195. 17 664 024 -7.453 130 88 42.85 74.29 1238 1 147 38 157 7 200. 17 444 024 -7.080 132 77 42.97 75.10 1199 5 138 90 153

205. 17 220 024 -6.702 134 63 43.11 75.98 1160 6 131 00 148 4

210. 16 989 024 -6.320 136 48 43.29 76.95 1121 4 123 62 143 8 215. 16 753 023 -5.932 138 30 43.49 78.02 1081 7 116 70 139 2

220. 16 510 023 -5.539 140 11 43.72 79.21 1041 6 110 18 134 7 225. 16 258 023 -5.140 141 90 43.98 80.54 1000 8 104 02 130 2 229.980 15 999 023 -4.735 143 68 44.26 82.02 959 5 98 20 125 8 229.980 4224 867 7.769 198 05 40.09 55.59 254 1 7 47 14 7 230. 4223 867 7.770 198 06 40.09 55.58 254 2 7 47 14 7

235. 4084 877 8.045 199 24 40.03 54.55 258 5 7 62 15

240. 3958 886 8.316 200 38 40.13 53.91 262 6 7 77 15 5 245. 3842 894 8.585 201 49 40.33 53.54 266 5 7 92 15 9 250. 3735 902 8.852 202 57 40.61 53.34 270 3 8 08 16 4

255. 3635 908 9.119 203 62 40.94 53.28 273 9 8 23 16 8

260. 3542 914 9.385 204 66 41.32 53.32 277 4 8 38 17 3 265. 3455 919 9.652 205 68 41.73 53.44 280 8 8 53 17 8 270. 3373 924 9.920 206 68 42.16 53.63 284. 1 8 68 18 4

275. 3296 929 10.188 207 66 42.62 53.87 287 3 8 83 18 9

280. 3223 933 10.458 208 64 43.10 54.15 290 4 8 97 19 5

163
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.7000 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol»K) J/(mol»K) m» s

• l /LiPa*

3 ITiW/(m<•K

285. 0.3153 .937 10.730 209.60 43.60 54.47 293 .4 9 .12 20 .0

290. 0.3087 .940 11.003 210.55 44.12 54.83 296 .4 9 .27 20 .6 295. 0.3025 .944 11.278 211.49 44.65 55.22 299 .3 9 .41 21 .2 300. 0.2965 .947 11.555 212.42 45.19 55.63 302 .2 9 .56 21 .8 310. 0.2853 .952 12.116 214.26 46.31 56.53 307 .7 9 .85 23 .1

320. 0.2750 .957 12.686 216.07 47.47 57.50 313 .0 10 .14 24 .4

330. 0.2655 .961 13.266 217.85 48.66 58.53 318 .2 10 .42 25 .7 340. 0.2567 .965 13.857 219.62 49.88 59.60 323 .2 10 ,70 27 .1 350. 0.2485 .968 14.458 221.36 51.11 60.72 328 .1 10 .98 28 .6 360. 0.2409 .971 15.071 223.09 52.36 61.86 332 .8 11 .26 30 .0

370. 0.2338 .973 15.696 224.80 53.62 63.03 337 .5 11,.54 31 .6 380. 0.2271 .976 16.332 226.49 54.89 64.22 342 .0 11..81 33 .1 390. 0.2208 .978 16.980 228.18 56.16 65.41 346 .5 12, 08 34 .7 400. 0.2149 .980 17.640 229.85 57.43 66.62 350 .9 12. 34 36 .3 410. 0.2092 ,981 18.313 231.51 58.70 67.83 355 .2 12. 61 38 .0

420. 0.2039 ,983 18.997 233.16 59.96 69.04 359 ,4 12, 87 39 ,7

430. 0.1989 ,984 19.693 234.80 61.22 70.25 363 .6 13,.13 41 .4 440. 0.1941 ,986 20.402 236.43 62.47 71.46 367 ,7 13, 39 43.,1

450. 0.1896 ,987 21.123 238.05 63.72 72.67 371 ,7 13. 65 44.,9

460. 0.1853 0.,988 21.855 239.66 64.95 73.87 375 ,7 13. 90 46.,7

470. 0.1812 0. 989 22.600 241.26 66.18 75.06 379, 6 14. 15 48. 5 480. 0.1772 0. 990 23.356 242.85 67.39 76.24 383, 5 14. 40 50. 3 490. 0.1734 0. 991 24.125 244.43 68.59 77.41 387, 4 14. 65 52. 2 500. 0.1698 0. 991 24.905 246.01 69.78 78.58 391. 2 14. 89 54.

520. 0.1631 0. 993 26.499 249.14 72.12 80.87 398. 6 57. 8

540. 0.1569 0. 994 28.139 252.23 74.41 83.12 405. 9 61. 7 560. 0.1511 0. 995 29.824 255.29 76.65 85.32 413. 1 65. 6 580. 0.1458 0. 996 31.552 258.33 78.83 87.48 420. 1 69. 5 600. 0.1408 0. 997 33.323 261.33 80.97 89.59 427. 73. 5 625. 0.1350 0. 997 35.595 265.04 83.57 92.16 435. 5

164-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.7500 MPa

T P z H

i C

V C

p W n

A

K mo" .•dm kJ/mol J/(mol'K) J/(mol-K) m»s

l /iPa* i 3 IT W/(m •K

95. 21 512 044 -14 543 79 99 47.93 68.67 1973 4 1063 85 252 4

100. 21 334 042 -14 196 83 55 48.16 70.08 1941 5 883 22 248 5 105. 21 154 041 -13 844 86 98 47.91 70.67 1907 2 746 27 244 3 110. 20 973 039 -13 490 90 28 47.41 70.79 1871 6 640 50 239 9

115. 20 791 038 -13 136 93 42 46.81 70.69 1835 5 557 29 235 4

120. 20 607 036 -12 783 96 43 46.17 70.49 1799 490 67 230 7 125. 20 423 035 -12 431 99 30 45.56 70.28 1762 4 436 48 226

130. 20 238 034 -12 081 102 05 45.00 70.11 1725 6 391 74 221 2 135. 20 052 033 -11 730 104 69 44.51 70.00 1688 7 354 29 216 3

140. 19 865 032 -11 380 107 24 44.08 69.96 1651 8 322 55 211 4

145. 19 676 032 -11 031 109 70 43.71 70.00 1614 8 295 34 206 4

150. 19 486 031 -10 680 112 07 43.41 70.12 1577 6 271 77 201 5 155. 19 294 030 -10 329 114 37 43.17 70.31 1540 5 251 16 196 6 160. 19 100 030 -9 977 116 61 42.98 70.57 1503 2 232 97 191 6

165. 18 904 029 -9 623 118 79 42.84 70.91 1465 8 216 80 186 7

170. 18 706 028 -9 268 120 91 42.75 71.31 1428 3 202 31 181 8 175. 18 504 028 -8 910 122 98 42.70 71.77 1390 7 189 24 176 9 180. 18 300 027 -8 550 125 01 42.68 72.30 1352 9 177 38 172 1

185. 18 093 027 -8 187 127 00 42.71 72.89 1315 166 55 167 3 190. 17 881 027 -7 821 128 95 42.76 73.55 1276 9 156 62 162 5

195. 17 666 026 -7 451 130 87 42.85 74.28 1238 6 147 45 157 8 200. 17 446 026 -7 078 132 76 42.97 75.08 1200 138 96 153 1

205. 17 222 026 -6 701 134 63 43.12 75.96 1161 1 131 07 148 4

210. 16 992 025 -6 318 136 47 43.29 76.93 1121 9 123 69 143 8

215. 16 756 025 -5 931 138 29 43.49 78.00 1082 3 116 77 139 3

220. 16 512 025 -5 538 140 10 43.72 79.19 1042 2 110 25 134 8 225. 16 262 025 -5 139 141 89 43.98 80.51 1001 5 104 09 130 3 230. 16 002 025 -4 733 143 68 44.26 81.99 960 1 98 24 125 9 232.046 15 892 024 -4 564 144 41 44.39 82.65 942 9 95 93 124 1 232.046 4520 860 7 814 197 75 40.53 56.55 253 8 7 55 14 9

235. 4428 867 7 980 198 46 40.44 55.78 256 5 7 64 15 2 240. 4286 877 8 257 199 63 40.44 54.89 260 8 7 79 15 6 245. 4156 886 8 530 200 75 40.58 54.34 264 8 7 94 16

250. 4037 894 8 801 201 85 40.81 54.02 268 7 8 09 16 5 255. 3926 901 9 070 202 92 41.11 53.87 272 4 8 24 16 9

260. 3824 907 9 340 203 96 41.46 53.84 276 8 39 17 4

265. 3727 913 9 609 204 99 41.85 53.90 279 5 8 54 17 9

270. 3637 919 9 879 206 00 42.28 54.04 282 9 8 69 18 4

275. 3552 923 10 150 206 99 42.72 54.24 286 1 8 84 19

280. 3472 928 10 421 207 97 43.20 54.49 289 3 8 99 19 5

-165
Table B3. Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.7500 MPa (continued)

T P z H S C

V C

p W V A

K mol'dm kJ/mol J/(mol-K) J/(mol-K) m«s

• l /^Pa»s itW/(m<•K

285. 0.3396 .932 10.694 208.94 43.69 54.79 292 .4 9 .14 20 .1 290. 0.3324 .936 10.969 209.89 44.19 55.12 295 .4 9 .28 20 .7 295. 0.3255 .939 11.246 210.84 44.72 55.48 298 .4 9 .43 21 .3 300. 0.3190 .943 11.524 211.77 45.26 55.88 301 .3 9 .57 21 .9 310. 0.3068 .948 12.087 213.62 46.37 56.74 306 .9 9 .86 23 .1

320. 0.2956 .954 12.659 215.44 47.52 57.68 312 .3 10 .15 24 .4

330. 0.2853 .958 13.241 217.23 48.70 58.69 317 .5 10 .43 25 .8 340. 0.2758 ,962 13.833 218.99 49.91 59.75 322 .6 10 .72 27 .2 350. 0.2669 0.,966 14.436 220.74 51.14 60.85 327 .5 11,.00 28 .6 360. 0.2587 .969 15.050 222.47 52.39 61.98 332 .3 11 .27 30 .1

370. 0.2510 0,,971 15.676 224.19 53.65 63.14 337 .0 11 .55 31 .6 380. 0.2437 0,,974 16.313 225.89 54.91 64.31 341 .6 11 .82 33 .1 390. 0.2369 0.,976 16.962 227.57 56.18 65.50 346 .1 12 .09 34 .7 400. 0.2305 0,,978 17.623 229.24 57.45 66.70 350 .5 12 ,36 36 .4 410. 0.2245 0.,980 18.296 230.91 58.71 67.91 354 .8 12 ,62 38 .0

420. 0.2188 0. 982 18.981 232.56 59.98 69.11 359 .1 12. 88 39 .7 430. 0.2134 0, 983 19.679 234.20 61.24 70.32 363 .3 13, 14 41 .4 440. 0.2082 0. 985 20.388 235.83 62.49 71.53 367 ,4 13, 40 43 .1 450. 0.2033 0. 986 21.109 237.45 63.73 72.73 371 .5 13, 66 44 .9 460. 0.1987 0,,987 21.842 239.06 64.96 73.92 375 .5 13, 91 46 ,7

470. 0.1942 0. 988 22.587 240.66 66.19 75.11 379,,4 14. 16 48,,5

480. 0.1900 0.,989 23.344 242.26 67.40 76.29 383 ,4 14. 41 50, 3 490. 0.1860 0. 990 24.113 243.84 68.60 77.46 387, 2 14. 66 52,,2

500. 0.1821 0. 991 24.894 245.42 69.79 78.62 391, 14. 90 54..0 520. 0.1748 0. 992 26.489 248.55 72.13 80.91 398, 5 57. 8

540. 0.1681 0. 994 28.130 251.64 74.41 83.16 405. 8 61. 7 560. 0.1620 0. 995 29.815 254.71 76.65 85.36 413. 65. 6 580. 0.1562 0. 996 31.544 257.74 78.84 87.51 420. 1 69. 5 600. 0.1509 0. 996 33.315 260.74 80.97 89.61 427. 73. 5 625. 0.1447 0. 997 35.588 264.45 83.57 92.18 435. 4

166-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.8000 MPa

T P z H

i C

V C

p W V

A

K mo" L«dm kJ/mol J/(mol.K) J/(mol-K) m» s

l yuPa*

3 IT W/(m •K

95. 21 .513 .047 -14.541 79 .98 47.93 68.67 1973 7 1064 .30 252 .5 100. 21 .335 .045 -14.194 83 .54 48.16 70.08 1941 8 883 .57 248 .5 105. 21 .155 .043 -13.842 86 .98 47.91 70.66 1907 4 746 .55 244 .3

110. 20 .974 .042 -13.488 90 .27 47.42 70.79 1871 8 640 .73 239 .9

115. 20 .791 .040 -13.134 93 42 46.81 70.68 1835 7 557 .48 235 .4

120. 20 .608 039 -12.781 96 42 46.17 70.49 1799 2 490 84 230 .7 125. 20 424 038 -12.430 99 29 45.57 70.28 1762 6 436 63 226 .0

130. 20 239 037 -12.079 102 05 45.01 70.11 1725 9 391 87 221 .2 135. 20 053 036 -11.728 104 69 44.51 70.00 1689 354 41 216 .3 140. 19 866 035 -11.379 107 23 44.08 69.96 1652 1 322 66 211 .4

145. 19 677 034 -11.029 109 69 43.72 70.00 1615 295 44 206 .5 150. 19 487 033 -10.678 112 07 43.41 70.11 1577 9 271 87 201 .5 155. 19 295 032 -10.327 114 37 43.17 70.31 1540 8 251 25 196 .6 160. 19 102 031 -9.975 116 60 42.98 70.57 1503 5 233 06 191 7 165. 18 906 031 -9.622 118 78 42.84 70.90 1466 1 216 88 186 7

170. 18 707 030 -9.266 120 90 42.75 71.30 1428 6 202 39 181 8 175. 18 506 030 -8.909 122 98 42.70 71.76 1391 189 32 177

180. 18 302 029 -8.548 125 00 42.69 72.29 1353 3 177 45 172 1 185. 18 094 029 -8.186 126 99 42.71 72.88 1315 4 166 62 167 3 190. 17 883 028 -7.819 128 94 42.77 73.54 1277 3 156 69 162 5

195. 17 668 028 -7.450 130 86 42.85 74.27 1239 147 52 157 8 200. 17 448 028 -7.077 132 75 42.97 75.07 1200 5 139 03 153 1 205. 17 224 027 -6.699 134 62 43.12 75.95 1161 7 131 13 148 5 210. 16 994 027 -6.317 136 46 43.29 76.91 1122 5 123 76 143 9 215. 16 758 027 -5.930 138 28 43.49 77.98 1082 9 116 84 139 3

220. 16 515 026 -5.537 140 09 43.72 79.16 1042 8 110 32 134 8 225. 16 265 026 -5.138 141 88 43.98 80.48 1002 2 104 16 130 4

230. 16 005 026 -4.732 143 67 44.26 81.96 960 8 98 31 125 9 234.014 15 789 026 -4.400 145 10 44.51 83.28 927 93 82 122 4

234.014 4816 854 7.856 197 47 40.95 57.49 253 5 7 63 15 2

235. 4782 856 7.913 197 71 40.90 57.18 254 4 7 66 15 3 240. 4622 867 8.196 198 91 40.78 55.98 258 8 7 81 15 7 245. 4477 877 8.473 200 05 40.85 55.22 263 1 7 96 16 1 250. 4345 886 8.748 201 16 41.03 54.76 267 1 8 11 16 6 255. 4223 894 9.021 202 24 41.29 54.49 270. 9 8 26 17

260. 4109 901 9.293 203 30 41.62 54.38 274. 6 8 41 17 5 265. 4004 907 9.565 204 34 41.99 54.38 278. 2 8. 56 18

270. 3905 913 9.837 205. 35 42.39 54.47 281. 6 8. 71 18 5 275. 3812 918 10.110 206. 35 42.83 54.63 285. 8. 86 19. 1 280. 3724 923 10.384 207. 34 43.29 54.84 288. 2 9. 00 19. 6

-167-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P - 0.8000 MPa (continued)

T P z H S C

V C

p W V A

K mo 1 • dm kJ/mol J/(mol»K) J/(mol«K) m» s

l fiFa* i5 ITiW/ ( m

-K

285. 0.3641 .927 10.659 208.31 43.77 55.11 291 .4 9 .15 20 .2 290. 0.3563 .931 10.935 209.27 44.27 55.41 294 .5 9 .30 20 .7 295. 0.3488 .935 11.213 210.22 44.79 55.76 297 .5 9 .44 21 .3 300. 0.3417 .939 11.493 211.16 45.32 56.13 300 .4 9 .59 21 .9 310. 0.3285 .945 12.058 213.02 46.42 56.96 306 .1 9 .88 23 .2

320. 0.3164 .950 12.632 214.84 47.57 57.87 311 .6 10 .16 24 .5 330. 0.3052 .955 13.216 216.64 48.74 58.86 316 .9 10 .45 25 .8 340. 0.2950 .959 13.809 218.41 49.95 59.90 322 .0 10 .73 27 .2 350. 0.2854 .963 14.414 220.16 51.18 60.98 327 .0 11 .01 28 .6 360. 0.2765 .966 15.029 221.89 52.42 62.10 331 .8 11 .29 30 .1

370. 0.2682 .969 15.656 223.61 53.67 63.25 336 .6 11 .56 31 .6 380. 0.2605 .972 16.294 225.31 54.93 64.41 341 .2 11 .83 33 .2 390. 0.2532 .975 16.944 227.00 56.20 65.60 345 .7 12 .10 34 .8 400. 0.2463 .977 17.606 228.68 57.46 66.79 350 .2 12 .37 36 .4

410. 0.2398 .979 18.280 230.34 58.73 67.99 354 .5 12 .63 38 .0

420. 0.2337 .980 18.966 231.99 59.99 69.19 358 .8 12..90 39 .7 430. 0.2279 0.,982 19.664 233.64 61.25 70.39 363 ,0 13 ,16 41 .4 440. 0.2223 .984 20.374 235.27 62.50 71.59 367 .2 13 ,41 43 .2 450. 0.2171 .985 21.095 236.89 63.74 72.78 371 .2 13,,67 44 .9 460. 0.2121 ,986 21.829 238.50 64.97 73.98 375 .3 13, 92 46.,7

470. 0.2074 0.,987 22.575 240.11 66.19 75.16 379,,2 14, 17 48,,5

480. 0.2028 0.,988 23.332 241.70 67.41 76.34 383,,2 14. 42 50,,3

490. 0.1985 0,,989 24.102 243.29 68.61 77.50 387,,0 14. 67 52. 2 500. 0.1944 0,,990 24.883 244.86 69.79 78.66 390. 9 14. 91 54. 1 520. 0.1866 0, 992 26.479 247.99 72.13 80.95 398. 4 57. 8

540. 0.1794 0. 993 28.120 251.09 74.42 83.19 405. 7 61. 7 560. 0.1728 0, 994 29.806 254.16 76.66 85.39 412. 9 65. 6

580. 0.1667 0.,995 31.535 257.19 78.84 87.54 420. 69. 5 600. 0.1610 0. 996 33.307 260.19 80.98 89.64 426. 9 73. 5 625. 0.1544 0. 997 35.580 263.91 83.58 92.21 435. 4

168
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.8500 MPa

T P z H

< ( V C

p W V

A

K mo l«dm kJ/mol J/(mol-K) J/(mol«K) m» s

-

/iPa«3 ITiW/(m K

95. 21 .513 .050 -14.539 79 .98 47 .93 68.66 1973 .9 1064 .75 252 .5 100. 21 .336 .048 -14.192 83 .54 48 .16 70.08 1942 .0 883 .92 248 .5

105. 21 .156 .046 -13.840 86 .98 47 .91 70.66 1907 .6 746 .83 244 .4

110. 20 .974 .044 -13.486 90 .27 47 .42 70.79 1872 .1 640 .96 240 .0

115. 20 .792 .043 -13.133 93 .41 46 .81 70.68 1835 .9 557 .68 235 .4

120. 20 .609 .041 -12.780 96 .42 46 .18 70.48 1799 .5 491 .01 230 .8

125. 20 .425 .040 -12.428 99 .29 45 .57 70.28 1762 .9 436 .78 226 .0

130. 20 .240 .039 -12.077 102 .04 45 .01 70.10 1726 .1 392 .00 221 .2 135. 20 .054 .038 -11.727 104 .69 44 .51 69.99 1689 .3 354 .53 216 .3 140. 19 .867 .037 -11.377 107 .23 44 .08 69.96 1652 .3 322 .77 211 .4

145. 19 .678 .036 -11.027 109 .69 43 .72 69.99 1615 .3 295 .54 206 .5 150. 19 .488 .035 -10.677 112 .06 43 .42 70.11 1578 .2 271 .96 201 .6 155. 19 .297 .034 -10.326 114 .36 43 .17 70.30 1541 .1 251 .34 196 .6 160. 19 .103 .033 -9.974 116 .60 42 .99 70.56 1503 .8 233 .14 191 .7 165. 18 .907 .033 -9.620 118 .77 42 .85 70.89 1466 .4 216 .96 186 .8

170. 18 .708 .032 -9.264 120 .90 42 .75 71.29 1429 .0 202 .47 181 .9 175. 18 .507 .032 -8.907 122 .97 42 .70 71.76 1391 .4 189 .39 177 .0 180. 18 .303 .031 -8.547 125 .00 42 .69 72.28 1353 .7 177 .53 172 .2 185. 18..096 ,031 -8.184 126 .99 42 .71 72.87 1315 .8 166 ,70 167 .4 190. 17 .885 ,030 -7.818 128 .94 42 .77 73.53 1277 .8 156 ,76 162 .6

195. 17.,670 ,030 -7.449 130 .86 42 .86 74.26 1239 ,5 147 .59 157 .9 200. 17 .450 ,029 -7.075 132 .75 42 .97 75.05 1201 ,0 139 .10 153 ,2

205. 17,,226 ,029 -6.698 134,.61 43 .12 75.93 1162 ,2 131..20 148 .5 210. 16 .996 ,029 -6.316 136,,45 43 .29 76.90 1123 ,0 123, 82 143 .9 215. 16,,761 0.,028 -5.929 138,,27 43 ,50 77.96 1083.,5 116, 90 139 ,4

220. 16,.518 0, 028 -5.536 140, 08 43,,73 79.14 1043, 4 110. 39 134, 9 225. 16,.268 0. 028 -5.137 141, 87 43,.98 80.45 1002. 8 104, 23 130, 4

230. 16.,008 0, 028 -4.731 143, 66 44,,27 81.92 961, 5 98. 38 126,.0 235. 15, 739 0,,028 -4.318 145. 44 44, 58 83.59 919. 4 92. 81 121. 6 235.894 15, 689 0, 028 -4.243 145. 75 44, 64 83.91 911. 8 91. 84 120. 8

235.894 0, 5114 0. 848 7.895 197. 21 41. 35 58.43 253. 1 7. 71 15. 5 240. 0. 4967 0. 858 8.132 198. 21 41. 16 57.18 256. 9 7. 83 15. 8 245. 0. 4806 0. 868 8.415 199. 37 41. 14 56.17 261. 3 7. 98 16. 2 250. 0. 4659 0. 878 8.695 200. 50 41. 26 55.54 265. 4 8. 13 16. 7 255. 0. 4524 0. 886 8.971 201. 60 41. 48 55.16 269. 4 8. 28 17. 1

260. 0. 4400 0. 894 9.246 202. 67 41. 78 54.96 273. 2 8. 43 17. 6 265. 0. 4284 0. 900 9.521 203. 71 42. 12 54.88 276. 9 8. 58 18. 1 270. 0. 4176 0. 907 9.796 204. 74 42. 51 54.92 280. 4 8. 73 18. 6

275. 0. 4075 0. 912 10.070 205. 75 42. 93 55.03 283. 8 8. 87 19. 1 280. 0. 3979 0. 918 10.346 206. 74 43. 38 55.20 287. 1 9. 02 19. 7

169
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.8500 MPa (continued)

T P z H S C

V C

p W *7 A

K mo 1 • dm kJ/mol J/(mol-K) J/(mol«K) m* s

i /zPa«

3 ITiW/(rrr•K

285. 0.3889 .922 10.622 207.72 43.86 55.44 290 .3 9 .17 20 .2 290. 0.3804 .927 10.900 208.69 44.35 55.72 293 .5 9 .31 20 .8 295. 0.3723 .931 11.180 209.64 44.86 56.03 296 .5 9 .46 21 .4

300. 0.3646 .935 11.461 210.59 45.39 56.39 299 .5 9 .60 22 .0

310. 0.3503 .941 12.028 212.45 46.48 57.18 305 .3 9 .89 23 .2

320. 0.3373 .947 12.605 214.28 47.61 58.07 310 .8 10 .18 24 .5 330. 0.3253 .952 13.190 216.08 48.78 59.03 316 .2 10 .46 25 .9 340. 0.3142 .957 13.785 217.86 49.98 60.05 321 .4 10 .74 27 .2 350. 0.3040 .961 14.391 219.61 51.21 61.12 326 .4 11 .02 28 .7 360. 0.2945 .964 15.008 221.35 52.44 62.23 331 .3 11 ,30 30 .1

370. 0.2856 .968 15.636 223.07 53.70 63.36 336 .1 11 ,57 31 .7 380. 0.2772 .970 16.275 224.77 54.95 64.52 340 .8 11 .84 33 .2 390. 0.2694 ,973 16.926 226.46 56.22 65.69 345 .3 12 ,11 34 .8 400. 0.2621 .975 17.589 228.14 57.48 66.87 349 .8 12,,38 36 .4 410. 0.2551 0.,977 18.264 229.81 58.75 68.06 354 .2 12, 64 38 .1

420. 0.2486 ,979 18.950 231.46 60.01 69.26 358 .5 12, 91 39 .7 430. 0.2424 ,981 19.649 233.11 61.26 70.46 362 .7 13,.17 41 .4 440. 0.2365 ,982 20.359 234.74 62.51 71.65 366 .9 13, 42 43 ,2

450. 0.2309 ,984 21.082 236.36 63.75 72.84 371 .0 13, 68 44 .9 460. 0.2256 0. 985 21.816 237.98 64.98 74.03 375 ,1 13, 93 46, 7

470. 0.2205 0. 986 22.562 239.58 66.20 75.21 379,.0 14. 18 48, 5 480. 0.2157 0,,988 23.320 241.18 67.41 76.39 383, 14. 43 50, 4

490. 0.2110 0. 989 24.090 242.77 68.61 77.55 386. 9 14. 68 52, 2 500. 0.2066 0. 990 24.871 244.34 69.80 78.71 390. 7 14. 92 54. 1 520. 0.1983 0, 991 26.468 247.48 72.14 80.99 398, 3 57. 9

540. 0.1907 0. 993 28.111 250.57 74.43 83.23 405. 6 61. 7 560. 0.1837 0. 994 29.797 253.64 76.66 85.42 412. 9 65. 6 580. 0.1772 0. 995 31.527 256.68 78.85 87.57 419. 9 69. 6

600. 0.1711 0. 996 33.300 259.68 80.98 89.67 426. 9 73. 6 625. 0.1641 0. 997 35.573 263.39 83.58 92.23 435. 4

170
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.9000 MPa

T P z H

i ( V C

p W n A

K mo _ • dm kJ/mol J/(mol-K) J/(mol»K) m* s

i /iPa*

3 IT W/(m •K

95. 21 .514 .053 -14 .537 79 97 47 .93 68.66 1974 1 1065 20 252 .5 100. 21 .336 051 -14 .190 83 54 48 .16 70.07 1942 2 884 27 248 6 105. 21 157 049 -13 .838 86 97 47 .92 70.66 1907 8 747 12 244 .4

110. 20 975 047 -13 484 90 26 47 .42 70.78 1872 3 641 19 240

115. 20 793 045 -13 131 93 41 46 .81 70.68 1836 2 557 87 235 5

120. 20 610 044 -12 778 96 41 46 18 70.48 1799 7 491 18 230 8 125. 20 426 042 -12 426 99 28 45 57 70.27 1763 1 436 93 226 1

130. 20 241 041 -12 075 102 04 45 .01 70.10 1726 4 392 13 221 2 135. 20 055 040 -11 725 104 68 44 .51 69.99 1689 5 354 65 216 4

140. 19 868 039 -11 375 107 23 44 08 69.95 1652 6 322 88 211 5

145. 19 679 038 -11 025 109 68 43 72 69.99 1615 6 295 64 206 5 150. 19 489 037 -10 675 112 06 43 42 70.11 1578 5 272 06 201 6 155. 19 298 036 -10 324 114 36 43 18 70.30 1541 4 251 43 196 7 160. 19 104 035 -9 972 116 59 42 99 70.56 1504 1 233 23 191 7 165. 18 908 035 -9 618 118 77 42 85 70.89 1466 8 217 04 186 8

170. 18 710 034 -9 263 120 89 42 76 71.29 1429 3 202 55 181 9 175. 18 509 033 -8 905 122 96 42 70 71.75 1391 8 189 47 177

180. 18 305 033 -8 545 124 99 42 69 72.27 1354 1 177 60 172 2 185. 18 097 032 -8 182 126 98 42 71 72.86 1316 2 166 77 167 4

190. 17 887 032 -7 816 128 93 42 77 73.52 1278 2 156 83 162 6

195. 17 672 031 -7 447 130 85 42 86 74.24 1239 9 147 66 157 9 200. 17 452 031 -7 074 132 74 42 98 75.04 1201 4 139 17 153 2 205. 17 228 031 -6 697 134 60 43 12 75.92 1162 7 131 27 148 6 210. 16 999 030 -6 315 136 44 43 30 76.88 1123 6 123 89 144

215. 16 763 030 -5 928 138 27 43 50 77.94 1084 116 97 139 4

220. 16 521 030 -5 535 140 07 43 73 79.11 1044 1 110 45 134 9 225. 16 271 030 -5 136 141 86 43 98 80.42 1003 5 104 30 130 5 230. 16 012 029 -4 731 143 65 44 27 81.89 962 3 98 45 126

235. 15 742 029 -4 317 145 42 44 58 83.55 920 2 92 88 121 6 237.694 15 592 029 -4 091 146 38 44 76 84.54 897 1 89 98 119 3

237.694 5413 841 7 931 196 96 41 74 59.35 252 6 7 78 15 8 240. 5322 847 8 067 197 53 41 59 58.52 254 9 7 85 16

245. 5142 859 8 356 198 72 41 46 57.22 259 4 8 00 16 4

250. 4980 869 8 640 199 87 41 51 56.39 263 8 8 15 16 8 255. 4832 879 8 920 200 98 41 68 55.87 267 9 8 30 17 2

260. 4695 887 9 199 202 06 41 94 55.56 271 8 8 45 17 7 265. 4569 894 9 476 203 12 42 27 55.41 275 5 8 60 18 2 270. 4451 901 9 753 204 15 42 64 55.38 279 1 8 74 18 7 275. 4341 907 10 030 205 17 43 04 55.44 282 6 8 89 19 2 280. 4237 912 10 308 206 17 43 48 55.58 286 9 04 19 8

171
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.9000 MPa (continued)

T P z H S C

V C

p W n

A

K mol'dm kJ/mol J/(mol-K) J/(mol-K) m» s

l /uPa»s rriW/(m-•K

285. 0.4140 .917 10.586 207.15 43.94 55.78 289 .3 9 .18 20 .3 290. 0.4048 .922 10.865 208.13 44.43 56.03 292 .5 9 .33 20 .9 295. 0.3961 .926 11.146 209.09 44.93 56.32 295 .6 9 .48 21 .5 300. 0.3878 .930 11.429 210.04 45.45 56.65 298 .6 9 .62 22 .1 310. 0.3724 .938 11.999 211.91 46.53 57.41 304 .5 9 .91 23 .3

320. 0.3584 .944 12.577 213.74 47.66 58.26 310 .1 10 .19 24 .6 330. 0.3455 0..949 13.164 215.55 48.83 59.20 315 .5 10 .48 25 .9 340. 0.3336 .954 13.761 217.33 50.02 60.21 320 .8 10 .76 27 .3 350. 0.3227 0..958 14.369 219.09 51.24 61.26 325 .9 11.,04 28 .7 360. 0.3125 ,962 14.987 220.83 52.47 62.35 330 .8 11 ,31 30 .2

370. 0.3030 ,966 15.616 222.56 53.72 63.47 335 .6 11 ,59 31 .7 380. 0.2941 .969 16.256 224.26 54.98 64.62 340 .3 11.,86 33 .2 390. 0.2857 .971 16.908 225.96 56.24 65.78 344 .9 12 ,13 34 .8 400. 0.2779 ,974 17.572 227.64 57.50 66.96 349 .4 12 ,39 36 .4 410. 0.2705 0,,976 18.247 229.30 58.76 68.14 353 .9 12 ,66 38 .1

420. 0.2635 0.,978 18.935 230.96 60.02 69.33 358 .2 12, 92 39 .8 430. 0.2569 0, 980 19.634 232.61 61.27 70.52 362 .5 13, 18 41 ,5

440. 0.2507 0. 981 20.345 234.24 62.52 71.71 366 ,6 13, 44 43 .2 450. 0.2447 0, 983 21.068 235.87 63.76 72.90 370 ,8 13, 69 45,.0 460. 0.2390 0,,984 21.803 237.48 64.99 74.09 374 8 13, 94 46,,7

470. 0.2337 0,,986 22.550 239.09 66.21 75.26 378, 9 14. 19 48, 6 480. 0.2285 0.,987 23.308 240.68 67.42 76.43 382. 8 14. 44 50, 4

490. 0.2236 0. 988 24.079 242.27 68.62 77.60 386..7 14. 69 52, 2 500. 0.2189 0. 989 24.860 243.85 69.81 78.75 390. 6 14. 93 54. 1 520. 0.2101 0. 991 26.458 246.98 72.15 81.03 398. 1 57. 9

540. 0.2020 0. 992 28.101 250.08 74.43 83.26 405. 5 61. 7 560. 0.1946 0. 994 29.788 253.15 76.67 85.45 412. 8 65. 6 580. 0.1876 0. 995 31.519 256.19 78.85 87.59 419. 9 69. 6 600. 0.1812 0. 996 33.292 259.19 80.98 89.69 426. 8 73. 6 625. 0.1738 0. 997 35.566 262.91 83.58 92.25 435. 3

172-
Table B3 . Properties in the single -phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.9500 MPa

T P z H

< C

V C

p W n

A

K mo' L»dm kJ/mol J/(mol-K) J/(mol«K) m« s

l /xPa«

3 rr W/(m »K

95. 21 .514 .056 -14.535 79 .97 47.93 68.66 1974 3 1065 .65 252 .5 100. 21 .337 .054 -14.188 83 .53 48.16 70.07 1942 4 884 .62 248 .6 105. 21 .157 .051 -13.836 86 .97 47.92 70.66 1908 1 747 .40 244 .4

110. 20 .976 .050 -13.482 90 .26 47.42 70.78 1872 5 641 42 240 .0

115. 20 .794 .048 -13.129 93 .40 46.81 70.68 1836 4 558 07 235 .5

120. 20 .610 .046 -12.776 96 .41 46.18 70.48 1799 9 491 35 230 8 125. 20 .426 .045 -12.424 99 28 45.57 70.27 1763 3 437 07 226 .1 130. 20 .242 .043 -12.073 102 03 45.01 70.10 1726 6 392 27 221 .3 135. 20 .056 .042 -11.723 104 68 44.52 69.99 1689 8 354 77 216 .4

140. 19 .869 .041 -11.373 107 .22 44.09 69.95 1652 9 322 99 211 .5

145. 19 .680 040 -11.023 109 68 43.72 69.99 1615 9 295 74 206 6 150. 19 491 039 -10.673 112 05 43.42 70.10 1578 8 272 15 201 6 155. 19 299 038 -10.322 114 35 43.18 70.29 1541 7 251 52 196 7 160. 19 105 037 -9.970 116 59 42.99 70.55 1504 4 233 31 191 8 165. 18 .909 037 -9.616 118 76 42.85 70.88 1467 1 217 13 186 8

170. 18 711 036 -9.261 120 88 42.76 71.28 1429 7 202 62 181 9

175. 18 510 035 -8.904 122 96 42.71 71.74 1392 1 189 54 177 1 180. 18 306 035 -8.544 124 99 42.69 72.27 1354 5 177 67 172 2 185. 18 099 034 -8.181 126 97 42.72 72.85 1316 6 166 84 167 4

190. 17 888 034 -7.815 128 93 42.77 73.51 1278 6 156 90 162 7

195. 17 674 033 -7.446 130 84 42.86 74.23 1240 4 147 73 157 9 200. 17 454 033 -7.072 132 73 42.98 75.03 1201 9 139 24 153 3 205. 17 230 032 -6.695 134 60 43.13 75.90 1163 2 131 34 148 6

210. 17 001 032 -6.313 136 44 43.30 76.86 1124 1 123 96 144

215. 16 766 032 -5.926 138 26 43.50 77.92 1084 6 117 04 139 5

220. 16 524 031 -5.534 140 06 43.73 79.09 1044 7 110 52 135

225. 16 274 031 -5.135 141 85 43.99 80.39 1004 2 104 37 130 5 230. 16 015 031 -4.730 143 64 44.27 81.85 963 98 52 126 1

235. 15 746 031 -4.316 145 41 44.58 83.51 921 92 95 121 7 239.423 15 498 031 -3.943 146 99 44.88 85.18 883 88 23 117 8

239.423 5714 835 7.964 196 72 42.11 60.28 252 2 7 86 16 1 240. 5688 837 7.999 196 87 42.06 60.03 252 8 7 87 16 1 245. 5488 850 8.294 198 08 41.80 58.37 257 6 8 02 16 5 250. 5309 861 8.583 199 25 41.78 57.31 262 8 17 16 9

255. 5146 871 8.868 200 38 41.90 56.63 266 3 8 32 17 3

260. 4996 880 9.150 201 48 42.12 56.20 270 3 8 47 17 8 265. 4858 887 9.430 202 54 42.42 55.97 274 2 8 61 18 3 270. 4730 895 9.710 203 59 42.77 55.87 277 9 8 76 18 8

275. 4611 901 9.989 204 61 43.16 55.88 281 4 8 91 19 3 280. 4499 907 10.269 205 62 43.58 55.97 284 9 9 05 19 8

173
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 0.9500 MPa (continued)

T P z H S C

V C

p W n A

K mol«dm kJ/mol J/(mol«K) J/(mol»K) m» s

l ^zPa* i3 rriW/(m<•K

285. 0.4394 .912 10.549 206.61 44.03 56.13 288 .2 9 .20 20 .4

290. 0.4294 .918 10.830 207.59 44.51 56.35 291 .5 9 .35 20 .9 295. 0.4200 .922 11.113 208.56 45.01 56.61 294 .6 9 .49 21 .5 300. 0.4111 .926 11.396 209.51 45.52 56.92 297 .7 9 .64 22 .1 310. 0.3946 0..934 11.969 211.39 46.59 57.64 303 .7 9 .92 23 .3

320. 0.3796 0..941 12.549 213.23 47.71 58.47 309 .4 10 .21 24 .6 330. 0.3658 .947 13.139 215.04 48.87 59.38 314 .9 10 .49 26 .0 340. 0.3531 ,952 13.737 216.83 50.06 60.36 320 .2 10 .77 27 .3 350. 0.3414 ,956 14.346 218.60 51.27 61.40 325 .3 11 .05 28 .8 360. 0.3306 ,960 14.965 220.34 52.50 62.47 330 .3 11 .33 30 .2

370. 0.3205 ,964 15.596 222.07 53.74 63.58 335 .2 11 .60 31 .7 380. 0.3110 ,967 16.237 223.78 55.00 64.72 339 .9 11 .87 33 .3 390. 0.3021 ,970 16.890 225.47 56.26 65.88 344 .5 12 .14 34 .9 400. 0.2938 ,972 17.555 227.16 57.52 67.04 349 .1 12 .40 36 .5 410. 0.2859 ,975 18.231 228.83 58.78 68.22 353 ,5 12 .67 38 .1

420. 0.2785 0.,977 18.919 230.48 60.03 69.41 357 .9 12 ,93 39 ,8

430. 0.2715 0, 979 19.619 232.13 61.29 70.59 362 ,2 13.,19 41,.5 440. 0.2649 0, 980 20.331 233.77 62.53 71.78 366,.4 13.,45 43, 2 450. 0.2585 0. 982 21.055 235.39 63.77 72.96 370. 5 13, 70 45,.0 460. 0.2525 0. 984 21.790 237.01 65.00 74.14 374,.6 13, 95 46. 8

470. 0.2468 0. 985 22.537 238.62 66.22 75.32 378.,7 14. 20 48..6 480. 0.2414 0. 986 23.296 240.22 67.43 76.48 382. 6 14. 45 50. 4

490. 0.2362 0. 987 24.067 241.80 68.63 77.64 386. 5 14. 70 52. 2 500. 0.2312 0. 988 24.849 243.38 69.82 78.79 390. 4 14. 94 54. 1 520. 0.2219 0, 990 26.448 246.52 72.15 81.07 398. 57. 9

540. 0.2133 0. 992 28.092 249.62 74.44 83.30 405. 4 61. 7 560. 0.2054 0. 993 29.779 252.69 76.67 85.48 412. 7 65. 6

580. 0.1981 0. 994 31.511 255.73 78.86 87.62 419. 8 69. 6 600. 0.1913 0. 995 33.284 258.73 80.99 89.72 426. 8 73. 6 625. 0.1834 0. 997 35.559 262.45 83.59 92.28 435. 3

174-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 1.0000 MPa

T P z H

< C

V C

p W r\ A

K mo'L*dm kJ/mol J/(mol-K) J/(mol«K) m« s

l /iPa*

3 ITiW/(m-•K

95. 21 .515 .059 -14 .533 79 .97 47 .93 68.65 1974 ,5 1066 .10 252 .5 100. 21 .338 .056 -14 .186 83 .53 48 .16 70.07 1942 ,6 884 .97 248 .6 105. 21 .158 .054 -13 .834 86 .96 47 .92 70.66 1908 ,3 747 .68 244 .4

110. 20 .977 .052 -13 .480 90 .26 47 .42 70.78 1872 ,7 641 .66 240 .0 115. 20 .794 .050 -13 .127 93 .40 46 .81 70.67 1836.,6 558 .26 235 .5

120. 20 .611 .049 -12 .774 96 .40 46 .18 70.48 1800..2 491 .52 230 .9 125. 20 .427 .047 -12 .422 99 .28 45 .57 70.27 1763 ,6 437 .22 226 .1 130. 20 .243 .046 -12 .071 102 .03 45 .01 70.10 1726 ,9 392 .40 221 .3 135. 20 .057 .044 -11 .721 104 .67 44 .52 69.98 1690,,0 354 .89 216 .4

140. 19 .870 .043 -11 .371 107 .22 44 .09 69.94 1653 ,1 323 .10 211 .5

145. 19 .681 .042 -11 .021 109 .67 43 .72 69.98 1616,,2 295 .85 206 .6 150. 19 .492 .041 -10 .671 112 .05 43 .42 70.10 1579 ,1 272 .25 201 .7 155. 19 .300 .040 -10 .320 114 .35 43 .18 70.29 1542 ,0 251 .61 196 .7 160. 19 .106 .039 -9 .968 116 .58 42 .99 70.55 1504 .8 233 .40 191 .8 165. 18 .911 .039 -9 .615 118 .76 42 .85 70.88 1467 .4 217 ,21 186 .9

170. 18 .713 .038 -9 .259 120 .88 42 .76 71.27 1430 ,0 202 .70 182 .0 175. 18 .512 .037 -8 ,902 122 .95 42 .71 71.73 1392 .5 189 .62 177 .1 180. 18 .308 .036 -8 .542 124 .98 42 .70 72.26 1354,.8 177 ,75 172 .3 185. 18 .101 .036 -8 .179 126 .97 42 .72 72.84 1317..0 166 ,91 167 .5 190. 17 .890 .035 -7 .813 128 .92 42 .78 73.50 1279..0 156 ,97 162 .7

195. 17 .675 .035 -7 .444 130 .84 42 .86 74.22 1240. 8 147 .80 158 .0 200. 17 .456 .034 -7..071 132 .73 42 .98 75.01 1202 4 139 .31 153 .3 205. 17 .233 .034 -6.,694 134 .59 43 .13 75.88 1163. 7 131 ,41 148 .7 210. 17 .003 .034 -6.,312 136 .43 43 .30 76.84 1124,.6 124 ,03 144 .1 215. 16 .768 .033 -5.,925 138 .25 43 .50 77.90 1085.,2 117..11 139 .5

220. 16..526 0.,033 -5.,533 140 .05 43 .73 79.07 1045, 3 110..59 135 .0 225. 16.,277 0,,033 -5,.134 141 ,84 43 .99 80.36 1004. 8 104 43 130 .6 230. 16..018 0,,033 -4..729 143 ,63 44,,27 81.82 963. 7 98 .59 126 .2 235. 15.,750 0,,032 -4. 316 145 .40 44 ,58 83.47 921. 7 93..03 121 .8 240. 15, 469 0..032 -3, 894 147 .18 44,,93 85.36 878. 8 87. 70 117 .4

241.086 15. 406 032 -3. 801 147. 57 45..01 85.81 869. 3 86. 57 116 ,5

241.086 0..6016 0. 829 7..994 196,,49 42. 48 61.20 251. 7 7, 93 16 .4 245. 0..5843 0. 840 8. 231 197.,47 42. 19 59.64 255. 6 8, 04 16.,6

250. 0..5645 0, 852 8. 525 198, 66 42. 07 58.31 260. 3 8. 19 17.

255. 0. 5466 0. 863 8..815 199, 80 42. 13 57.44 264. 6 8. 34 17.,5

260. 0. 5303 0..872 9. 100 200..91 42. 31 56.89 268. 8 8. 49 17. 9 265. 0. 5153 0. 881 9. 384 201. 99 42. 57 56.55 272. 8 8. 63 18. 4

270. 0..5014 0.,888 9. 666 203. 05 42. 90 56.38 276. 6 8. 78 18. 9 275. .4885 0. 895 9. 948 204. 08 43. 27 56.33 280. 2 8. 93 19. 4

280. 0,,4764 0..902 10. 230 205. 10 43. 68 56.37 283. 7 9. 07 19..9

-175-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 1.0000 MPa (continued)

T P z H S C

V C

p W f

A

K mol'dm kJ/mol J/(mol-K) J/(mol-K) m» s

l /^Pa«s itiW/(m«•K

285. 0.4650 .908 10.512 206.09 44.13 56.49 287 .2 9 ,22 20 .4

290. 0.4543 .913 10.795 207.08 44.59 56.68 290 .5 9 ,36 21 .0

295. 0.4442 .918 11.079 208.05 45.08 56.91 293 .7 9 ,51 21 .6 300. 0.4347 .922 11.364 209.01 45.59 57.20 296 .8 9 .65 22 .2 310. 0.4170 .930 11.939 210.89 46.65 57.87 302 .9 9 ,94 23 .4

320. 0.4009 .937 12.522 212.74 47.76 58.67 308 .7 10 .22 24 .7 330. 0.3863 ,944 13.113 214.56 48.91 59.56 314 ,2 10 ,51 26 .0 340. 0.3728 ,949 13.713 216.35 50.09 60.52 319 .6 10,,79 27 .4

350. 0.3603 ,954 14.323 218.12 51.30 61.54 324 .8 11 ,06 28 .8 360. 0.3488 ,958 14.944 219.87 52.53 62.60 329 ,8 11 ,34 30 .3

370. 0.3380 ,962 15.575 221.60 53.77 63.70 334 .7 11..61 31 .8 380. 0.3280 ,965 16.218 223.32 55.02 64.82 339 ,5 11, 88 33 .3 390. 0.3186 ,968 16.872 225.01 56.27 65.97 344 .2 12 ,15 34 .9 400. 0.3097 ,971 17.537 226.70 57.53 67.13 348 ,7 12, 42 36 .5 410. 0.3014 ,973 18.215 228.37 58.79 68.30 353 .2 12, 68 38 .1

420. 0.2935 ,976 18.904 230.03 60.05 69.48 357 ,6 12, 94 39 .8 430. 0.2861 ,978 19.604 231.68 61.30 70.66 361 ,9 13. 20 41 .5 440. 0.2791 ,979 20.317 233.32 62.55 71.84 366 ,1 13. 46 43 .3 450. 0.2724 ,981 21.041 234.95 63.78 73.02 370,,3 13..71 45 .0 460. 0.2661 ,983 21.777 236.56 65.01 74.20 374, 4 13, 96 46 .8

470. 0.2600 0. 984 22.525 238.17 66.23 75.37 378,,5 14. 22 48,,6

480. 0.2543 0, 985 23.284 239.77 67.44 76.53 382. 4 14. 46 50, 4

490. 0.2488 0. 987 24.056 241.36 68.64 77.69 386. 4 14. 71 52, 3 500. 0.2435 0. 988 24.838 242.94 69.82 78.84 390. 3 14. 95 54, 1

520. 0.2337 0, 990 26.438 246.08 72.16 81.10 397. 9 57. 9

540. 0.2247 0. 991 28.082 249.18 74.44 83.33 405. 3 61. 8 560. 0.2163 0. 993 29.771 252.25 76.68 85.51 412. 6 65. 7 580. 0.2086 0. 994 31.502 255.29 78.86 87.65 419. 7 69. 6 600. 0.2014 0. 995 33.276 258.30 80.99 89.75 426. 7 73. 6 625. 0.1931 0, 996 35.552 262.01 83.59 92.30 435. 3

-176-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 1.5000 MPa

T P z H

< C

V C

p W r\ A

K mo!L»dm kJ/mol J/(mol»K) J/(mol-K) m»s

-

^Pa«3 irtW/(m »K

95. 21 .521 .088 -14.514 79 .93 47.92 68.63 1976 .7 1070 .63 252 .8

100. 21 .344 .085 -14.167 83 .49 48.17 70.05 1944 .8 888 .49 248 .8

105. 21 .165 .081 -13.815 86 .92 47.93 70.63 1910 .4 750 .50 244 .7 110. 20 .984 .078 -13.461 90 .21 47.44 70.76 1874 .9 643 .98 240 .3 115. 20 .802 .075 -13.108 93 .36 46.83 70.65 1838 .9 560 .22 235 .8

120. 20 .619 .073 -12.755 96 .36 46.20 70.45 1802 .5 493 .21 231 .1

125. 20 .436 .071 -12.403 99 .23 45.59 70.24 1766 .0 438 .71 226 .4

130. 20 .251 .069 -12.052 101 .98 45.04 70.07 1729 .4 393 .72 221 .6 135. 20 .066 .067 -11.702 104 .63 44.54 69.95 1692 .6 356 .08 216 .8 140. 19 .879 .065 -11.353 107 .17 44.11 69.91 1655 .8 324 .19 211 .9

145. 19 .692 .063 -11.003 109 .62 43.75 69.94 1619 .0 296 .86 206 .9 150. 19 .502 .062 -10.653 111 .99 43.45 70.05 1582 .0 273 .20 202 .0

155. 19 .311 .060 -10.302 114 .29 43.20 70.24 1545 .0 252 .50 197 .1 160. 19 .118 .059 -9.951 116 .53 43.02 70.49 1507 .9 234 .25 192 .2 165. 18 .923 .058 -9.597 118 .70 42.88 70.82 1470 .8 218 .02 187 .3

170. 18 .726 .057 -9.242 120 .82 42.79 71.21 1433 .5 203 .48 182 .4

175. 18 .526 .056 -8.885 122 .89 42.73 71.66 1396 .2 190 .37 177 .5 180. 18.,323 .055 -8.526 124 .92 42.72 72.17 1358 .7 178 .48 172 .7 185. 18 ,117 .054 -8.163 126 .90 42.74 72.75 1321 .1 167 .63 167 .9 190. 17 ,907 0,,053 -7.798 128 .85 42.80 73.39 1283 .3 157 .67 163 .2

195. 17,,694 0.,052 -7.429 130 .77 42.89 74.10 1245 .3 148 .49 158 .5 200. 17,.476 0,,052 -7.057 132 .65 43.01 74.88 1207 ,2 139 .99 153 .8 205. 17,,254 ,051 -6.680 134 .51 43.15 75.73 1168 ,7 132 .08 149 .2 210. 17, 027 0.,050 -6.299 136 .35 43.33 76.67 1130 .0 124 ,70 144 .6 215. 16, 793 0,,050 -5.914 138 .16 43.53 77.69 1090..9 117 ,78 140 ,1

220. 16, 554 0. 050 -5.522 139,,96 43.75 78.83 1051, 4 111,,27 135, 6

225. 16. 306 0. 049 -5.125 141, 75 44.01 80.09 1011. 4 105.,12 131. 2 230. 16. 051 0. 049 -4.721 143, 52 44.29 81.49 970. 8 99, 29 126..8 235. 15. 786 0. 049 -4.310 145..29 44.60 83.07 929. 4 93, 74 122. 4

240. 15. 510 0. 048 -3.890 147. 06 44.94 84.88 887. 2 88. 43 118. 1

245. 15. 220 0. 048 -3.461 148. 83 45.31 86.97 843. 8 83. 33 113. 8 250. 14. 914 0. 048 -3.020 150. 61 45.72 89.43 799. 78. 40 109. 5 255. 14. 589 0. 048 -2.565 152. 41 46.16 92.43 752. 4 73. 61 105. 2 255.089 14. 583 0. 049 -2.557 152. 44 46.17 92.49 751. 6 73. 52 105. 1 255.089 0. 9144 0. 774 8.199 194. 61 45.63 70.71 246. 8. 61 19.

260. 0. 8761 0. 792 8.537 195. 93 44.94 67.13 252. 8. 73 19. 2 265. 0. 8426 0. 808 8.866 197. 18 44.64 64.78 257. 4 8. 87 19. 6

270. 0. 8131 0. 822 9.186 198. 38 44.57 63.21 262. 5 9. 00 19. 9 275. 0. 7865 0. 834 9.499 199. 52 44.67 62.14 267. 2 9. 14 20. 4

280. 0. 7625 0. 845 9.808 200. 64 44.88 61.40 271. 6 9. 28 20. 8

-177
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 1.5000 MPa (continued)

T P z H S C

V C

p W V A

K mol'dm kJ/mol J/(mol-K) J/(mol-K) m»s

l ^Pa« i; rriW/(m •K

285. 0.7404 .855 10.114 201.72 45.17 60.92 275 .8 9 .42 21 .3 290. 0.7201 .864 10.418 202.78 45.51 60.61 279 .9 9 .56 21 .8 295. 0.7013 .872 10.720 203.81 45.90 60.45 283 .7 9 .70 22 .3 300. 0.6837 .880 11.022 204.83 46.32 60.40 287 .5 9 .84 22 .9 310. 0.6519 .893 11.627 206.81 47.25 60.54 294 .5 10 .11 24 .0

320. 0.6236 ,904 12.234 208.74 48.27 60.94 301 .2 10 .39 25 .2 330. 0.5983 .914 12.846 210.62 49.34 61.52 307 .4 10 .67 26 .5 340. 0.5753 .922 13.465 212.47 50.47 62.23 313 .4 10 .94 27 .9 350. 0.5544 .930 14.091 214.28 51.62 63.05 319 .2 11 .21 29 .2 360. 0.5352 ,936 14.726 216.07 52.81 63.95 324 .7 11 .48 30 .7

370. 0.5176 .942 15.370 217.84 54.02 64.91 330 .1 11 .75 32 .1 380. 0.5012 0..947 16.024 219.58 55.24 65.91 335 .2 12 ,02 33 .7 390. 0.4860 .952 16.689 221.31 56.47 66.96 340 .3 12 .28 35 .2 400. 0.4717 0..956 17.364 223.01 57.71 68.03 345 .2 12 .55 36 .8 410. 0.4584 ,960 18.049 224.71 58.95 69.13 349 .9 12 81 38 .4

420. 0.4459 ,963 18.746 226.39 60.19 70.24 354 .6 13, 07 40 .1 430. 0.4342 0.,966 19.454 228.05 61.43 71.36 359 .1 13, 32 41 .8 440. 0.4231 ,969 20.174 229.71 62.67 72.49 363 .6 13, 58 43 .5 450. 0.4126 0. 972 20.904 231.35 63.89 73.63 368 13. 83 45 .3 460. 0.4026 0, 974 21.646 232.98 65.11 74.76 372. 3 14. 08 47.

470. 0.3932 0,,976 22.399 234.60 66.33 75.90 376, 5 14. 33 48. 8 480. 0.3842 0, 978 23.164 236.21 67.53 77.03 380. 7 14. 57 50. 6 490. 0.3757 0, 980 23.940 237.81 68.72 78.16 384. 8 14. 82 52. 5 500. 0.3676 0. 982 24.727 239.40 69.90 79.28 388. 8 15. 06 54. 3 520. 0.3524 0. 985 26.335 242.55 72.23 81.50 396. 7 58. 1

540. 0.3384 0. 987 27.987 245.67 74.50 83.69 404. 4 61. 9 560. 0.3256 0, 989 29.682 248.75 76.73 85.84 411. 8 65. 8 580. 0.3138 0. 991 31.420 251.80 78.91 87.95 419. 2 69. 7 600. 0.3028 0. 993 33.200 254.82 81.04 90.01 426. 3 73. 7 625. 0.2902 0. 995 35.482 258.54 83.63 92.54 435.

178
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 2.0000 MPa

T P z H

( C

V C

p W n

A

K mo! [•dm kJ/mol J/(mol-K) J/(mol«K) m* s

l /iPa*

3 IT W/(m •K

95. 21 .527 .118 -14.494 79 .89 47.92 68.60 1978 9 1075 18 253 .0

100. 21 .350 .113 -14.147 83 .45 48.17 70.02 1947 892 03 249 .1

105. 21 .171 .108 -13.795 86 .88 47.94 70.61 1912 .6 753 33 244 .9 110. 20 .991 104 -13.442 90 .17 47.45 70.74 1877 2 646 31 240 .5 115. 20 .809 101 -13.088 93 .32 46.85 70.63 1841 1 562 19 236 .0

120. 20 .627 .097 -12.736 96 .32 46.22 70.43 1804 8 494 90 231 .4

125. 20 444 094 -12.384 99 19 45.62 70.22 1768 4 440 20 226 .7 130. 20 .260 091 -12.033 101 94 45.06 70.04 1731 8 395 05 221 .9 135. 20 075 089 -11.684 104 58 44.56 69.92 1695 2 357 29 217 .1

140. 19 889 086 -11.334 107 12 44.13 69.88 1658 5 325 29 212 .2

145. 19 702 084 -10.985 109 57 43.77 69.91 1621 8 297 88 207 3 150. 19 513 082 -10.635 111 95 43.47 70.01 1584 9 274 15 202 4

155. 19 323 080 -10.284 114 24 43.23 70.19 1548 1 253 40 197 4

160. 19 130 079 -9.933 116 48 43.04 70.44 1511 1 235 10 192 5 165. 18 936 077 -9.580 118 65 42.90 70.76 1474 1 218 83 187 6

170. 18 739 076 -9.225 120 77 42.81 71.14 1437 204 27 182 8 175. 18 540 074 -8.868 122 83 42.76 71.58 1399 8 191 13 177 9 180. 18 338 073 -8.509 124 86 42.74 72.09 1362 5 179 21 173 1 185. 18 133 072 -8.147 126 84 42.77 72.66 1325 1 168 34 168 3

190. 17 925 071 -7.783 128 79 42.82 73.29 1287 5 158 37 163 6

195. 17 713 070 -7.414 130 70 42.91 73.98 1249 8 149 18 158 9 200. 17 496 069 -7.043 132 58 43.03 74.75 1211 9 140 67 154 3 205. 17 275 068 -6.667 134 44 43.18 75.58 1173 7 132 76 149 7 210. 17 050 067 -6.287 136 27 43.35 76.49 1135 3 125 37 145 1 215. 16 818 067 -5.902 138 08 43.55 77.50 1096 6 118 45 140 6

220. 16 580 066 -5.512 139 88 43.78 78.60 1057 4 111 95 136 1 225. 16 336 065 -5.116 141 65 44.03 79.82 1017 9 105 80 131 7 230. 16 083 065 -4.713 143 42 44.31 81.18 977 7 99 98 127 4

235. 15 821 065 -4.304 145 19 44.62 82.70 936 9 94 44 123

240. 15 549 064 -3.886 146 94 44.95 84.42 895 4 89 15 118 8

245. 15 264 064 -3.459 148 70 45.32 86.40 852 8 84 08 114 5 250. 14 964 064 -3.021 150 47 45.72 88.72 808 9 79 18 110 2 255. 14 646 064 -2.571 152 26 46.16 91.50 763 5 74 43 106

260. 14 306 065 -2.105 154 07 46.64 94.93 716 69 78 101 7 265. 13 935 065 -1.620 155 91 47.18 99.36 665 7 65 17 97 3

266.011 13 856 065 -1.519 156 29 47.29 100.42 655 1 64 25 96 5 266.011 1 253 722 8.273 193 10 48.28 81.83 239 3 9. 25 21 6

270. 1 201 742 8.589 194 29 47.40 76.57 245 2 9. 33 21 6

275. 1 147 763 8.961 195 65 46.81 72.33 251 8 9. 45 21 8 280. 1 101 780 9.315 196 93 46.57 69.55 257 7 9. 56 22 1

179-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P= 2.0000 MPa (continued)

T P z H S C

V C

p W n A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol«K) m«s

• l /iPa«s irtW/(m<K

285. 1.060 .796 9.658 198.14 46.55 67.64 263 .1 9 .69 22 .4

290. 1.024 .810 9.992 199.30 46.67 66.30 268 .1 9 ,81 22 .8 295. 0.9918 .822 10.321 200.43 46.90 65.35 272 .8 9 .94 23 .3 300. 0.9622 .833 10.646 201.52 47.20 64.69 277 .3 10 .07 23 .8 310. 0.9100 .853 11.289 203.63 47.94 63.94 285 .6 10 .33 24 .8

320. 0.8651 .869 11.927 205.65 48.83 63.72 293 .3 10 .59 25 .9 330. 0.8257 ,883 12.564 207.62 49.81 63.85 300 .5 10 .86 27 .1

340. 0.7908 .895 13.205 209.53 50.86 64.22 307 .2 11 .12 28 .4

350. 0.7594 .905 13.849 211.40 51.97 64.77 313 .5 11 ,39 29 .7 360. 0.7310 .914 14.500 213.23 53.11 65.46 319 .6 11 ,65 31 .1

370. 0.7050 ,922 15.159 215.03 54.28 66.24 325 .4 11 ,91 32 ,6

380. 0.6812 .929 15.826 216.81 55.47 67.11 331 .0 12 ,17 34 .1 390. 0.6592 ,936 16.501 218.57 56.68 68.03 336 .4 12.,43 35 .6 400. 0.6389 ,941 17.186 220.30 57.89 69.00 341 ,6 12.,69 37 .2 410. 0.6199 ,946 17.881 222.02 59.11 70.01 346 .7 12.,95 38 .8

420. 0.6022 .951 18.587 223.72 60.34 71.05 351 .6 13,,20 40 .4

430. 0.5857 ,955 19.302 225.40 61.56 72.11 356 ,5 13, 46 42 .1 440. 0.5701 ,959 20.029 227.07 62.79 73.18 361 ,2 13. 71 43 ,8

450. 0.5554 ,962 20.766 228.73 64.00 74.26 365 ,7 13. 96 45 .5 460. 0.5416 0.,966 21.514 230.37 65.22 75.35 370 ,2 14. 20 47.,3

470. 0.5285 0. 968 22.273 232.00 66.42 76.45 374, 6 14. 45 49..0 480. 0.5161 0, 971 23.043 233.63 67.62 77.54 379, 14. 69 50.,9

490. 0.5043 0. 973 23.824 235.24 68.80 78.64 383, 2 14. 93 52. 7 500. 0.4931 0. 976 24.616 236.84 69.98 79.73 387. 4 15. 17 54.,5

520. 0.4722 0.,980 26.232 240.00 72.29 81.90 395, 5 58. 3

540. 0.4531 0. 983 27.892 243.14 74.56 84.05 403. 4 62. 1 560. 0.4357 0. 986 29.594 246.23 76.78 86.16 411. 1 66.

580. 0.4196 0. 988 31.338 249.29 78.96 88.24 418. 6 69. 9

600. 0.4047 0. 991 33.123 252.32 81.08 90.28 425. 9 73. 9

625. 0.3876 0. 993 35.412 256.05 83.67 92.78 434. 8

180-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 2.5000 MPa

T P z H

<

( V C

p W n A

K mo! .•dm kJ/mol J/(mol«K) J/(mol«K) m* s

l yuPa*

3 IT W/(m •K

95. 21 .533 147 -14 475 79 .85 47 .92 68.57 1981 1 1079 77 253 .2 100. 21 .357 141 -14 128 83 41 48 .18 70.00 1949 1 895 59 249 .3 105. 21 178 135 -13 776 86 84 47 .95 70.59 1914 8 756 18 245 .2 110. 20 .998 130 -13 423 90 13 47 .47 70.72 1879 4 648 66 240 .8 115. 20 817 126 -13 069 93 27 46 .87 70.61 1843 4 564 17 236 .3

120. 20 635 121 -12 717 96 27 46 .24 70.41 1807 2 496 61 231 7 125. 20 452 118 -12 365 99 14 45 .64 70.19 1770 8 441 69 227 .0

130. 20 268 114 -12 015 101 89 45 .08 70.01 1734 3 396 38 222 2 135. 20 084 111 -11 665 104 53 44 59 69.89 1697 8 358 49 217 4

140. 19 899 108 -11 316 107 07 44 16 69.84 1661 2 326 40 212 5

145. 19 712 105 -10 966 109 53 43 79 69.87 1624 5 298 90 207 6 150. 19 524 103 -10 617 111 90 43 49 69.97 1587 8 275 10 202 7 155. 19 334 100 -10 267 114 19 43 25 70.14 1551 1 254 30 197 8

160. 19 142 098 -9 915 116 42 43 06 70.39 1514 3 235 95 192 9 165. 18 949 096 -9 563 118 59 42 93 70.70 1477 4 219 65 188

170. 18 753 094 -9 208 120 71 42 83 71.08 1440 4 205 05 183 1

175. 18 554 093 -8 852 122 78 42 78 71.51 1403 4 191 89 178 3 180. 18 353 091 -8 493 124 80 42 77 72.01 1366 3 179 95 173 5 185. 18 149 090 -8 131 126 78 42 79 72.57 1329 1 169 06 168 8 190. 17 942 088 -7 767 128 72 42 85 73.19 1291 7 159 07 164

195. 17 731 087 -7 399 130 63 42 94 73.87 1254 2 149 87 159 4

200. 17 516 086 -7 028 132 51 43 05 74.62 1216 5 141 35 154 7 205. 17 296 085 -6 653 134 36 43 20 75.43 1178 7 133 43 150 1 210. 17 072 084 -6 274 136 19 43 37 76.33 1140 5 126 04 145 6

215. 16 843 083 -5 890 138 00 43 57 77.31 1102 1 119 12 141 1

220. 16 607 082 -5 501 139 79 43 80 78.38 1063 4 112 62 136 7 225. 16 365 082 -5 106 141 56 44 05 79.56 1024 2 106 48 132 3 230. 16 115 081 -4 705 143 33 44 33 80.87 984 6 100 66 128

235. 15 856 081 -4 297 145 08 44 64 82.34 944 3 95 14 123 7 240. 15 587 080 -3 881 146 83 44 97 83.99 903 3 89 86 119 4

245. 15 307 080 -3 457 148 58 45 33 85.87 861 5 84 81 115 2 250. 15 013 080 -3 022 150 34 45 72 88.06 818 5 79 94 111

255. 14 702 080 -2 575 152 11 46 15 90.65 774 2 75 23 106 8 260. 14 370 080 -2 114 153 90 46 62 93.80 728 1 70 63 102 5 265. 14 012 081 -1 636 155 72 47 15 97.77 679 6 66 10 98 3

270. 13 618 082 -1 135 157 59 47 73 103.06 627 8 61 58 93 9 275. 13 173 083 -0 601 159 55 48 43 110.70 571 56 98 89 4

275.090 13 165 083 -0 592 159 58 48 44 110.86 569 9 56 89 89 4

275.090 1 628 672 8 251 191 73 50 74 96.46 231 9 9 93 24 4

280. 1 529 702 8 697 193 34 49 30 85.69 240. 6 9 98 24 1

181
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 2.5000 MPa (continued)

T P z H S C

V C

p W n A

K mol»dm kJ/mol J/(mol»K) J/(mol-K) m*s

• l /iPa*

3 nriW/(m<»K

285. 1.451 .727 9.109 194.80 48.58 79.42 248 .1 10 .06 24 .1

290. 1.386 .748 9.495 196.14 48.26 75.43 254 .7 10 .16 24 .3 295. 1.330 .766 9.865 197.41 48.18 72.71 260 .7 10 .26 24 .6 300. 1.281 .782 10.224 198.61 48.27 70.80 266 .2 10 .37 24 .9 310. 1.198 .810 10.919 200.89 48.74 68.43 276 .2 10 .60 25 .7

320. 1.130 .832 11.596 203.04 49.46 67.21 285 .1 10 .84 26 .7 330. 1.072 .850 12.265 205.10 50.33 66.67 293 .2 11 .08 27 .8 340. 1.021 .866 12.931 207.09 51.29 66.56 300 .8 11 .33 29 .0

350. 0.9766 .880 13.597 209.02 52.33 66.75 307 .8 11 .58 30 .3 360. 0.9369 .892 14.267 210.90 53.42 67.16 314 .5 11 .84 31 .6

370. 0.9011 .902 14.941 212.75 54.55 67.73 320 .8 12 .09 33 .0 380. 0.8686 .911 15.622 214.57 55.71 68.41 326 ,8 12 .35 34 .5 390. 0.8388 .919 16.310 216.35 56.88 69.19 332 ,6 12 .60 36 .0

400. 0.8114 .926 17.006 218.12 58.08 70.05 338 .2 12 .85 37 .5 410. 0.7861 .933 17.711 219.86 59.28 70.95 343 ,6 13 ,10 39 .1

420. 0.7626 ,939 18.425 221.58 60.49 71.90 348 8 13 35 40 .7 430. 0.7407 0..944 19.149 223.28 61.70 72.89 353, 8 13, 60 42,.4 440. 0.7203 0,,949 19.883 224.97 62.91 73.90 358. 8 13, 85 44,.1 450. 0.7010 0.,953 20.627 226.64 64.12 74.93 363, 6 14, 09 45, 8

460. 0.6830 0, 957 21.381 228.30 65.32 75.97 368. 3 14. 33 47,.5

470. 0.6659 0.,961 22.146 229.94 66.51 77.02 372. 9 14. 58 49. 3 480. 0.6498 0. 964 22.922 231.58 67.70 78.07 377. 3 14. 82 51. 1 490. 0.6345 0. 967 23.708 233.20 68.88 79.13 381. 7 15. 06 52. 9 500. 0.6200 0. 970 24.504 234.81 70.05 80.20 386. 1 15. 29 54. 7 520. 0.5932 0. 975 26.130 237.99 72.36 82.31 394. 5 58. 5

540. 0.5687 0. 979 27.797 241.14 74.62 84.41 402. 6 62. 3 560. 0.5464 0. 983 29.506 244.25 76.84 86.49 410. 5 66. 1 580. 0.5259 0. 986 31.256 247.32 79.00 88.54 418. 1 70. 1 600. 0.5069 0. 989 33.047 250.35 81.12 90.55 425. 6 74.

625. 0.4852 0. 991 35.342 254.10 83.71 93.03 434. 7

182
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 3.0000 MPa

T P z H

< C

V C

p W V

A

K mo".L«dm kJ/mol J/(mol-K) J/(mol-K) m» s

l /iPa*

3 rriW/(m'>K

95. 21 .539 .176 -14.455 79 .82 47.92 68.54 1983 .3 1084 .38 253 .4

100. 21 .363 .169 -14.108 83 .37 48.19 69.98 1951 .3 899 .17 249 .5 105. 21 .185 .162 -13.757 86 .80 47.97 70.57 1917 .0 759 .04 245 .4

110. 21 .005 .156 -13.403 90 .09 47.49 70.70 1881 .6 651 .01 241 .1

115. 20 .824 .151 -13.050 93 .23 46.89 70.59 1845 .7 566 .15 236 .6

120. 20 .642 .146 -12.698 96 .23 46.26 70.39 1809 .5 498 .32 232 .0 125. 20 .460 .141 -12.346 99 .10 45.66 70.17 1773 .2 443 .19 227 .3 130. 20 .277 .137 -11.996 101 .85 45.10 69.99 1736 .8 397 .72 222 .5 135. 20 .093 .133 -11.646 104 .49 44.61 69.86 1700 .3 359 .70 217 .7 140. 19 .908 .129 -11.297 107 .03 44.18 69.81 1663 .8 327 .50 212 .8

145. 19 .722 .126 -10.948 109 .48 43.82 69.83 1627 .3 299 .93 207 .9 150. 19 .534 .123 -10.599 111 .85 43.52 69.93 1590 .7 276 .06 203 .0 155. 19 .345 .120 -10.249 114 .14 43.28 70.10 1554 .1 255 .20 198 .1 160. 19 .154 .118 -9.897 116 .37 43.09 70.34 1517 .4 236 .81 193 .3 165. 18 .961 .115 -9.545 118 .54 42.95 70.64 1480 .7 220 .46 188 .4

170. 18 .766 .113 -9.191 120 .65 42.86 71.01 1443 .9 205 .83 183 .5 175. 18 .568 0..111 -8.835 122 .72 42.81 71.44 1407 .0 192 .64 178 .7 180. 18 .368 ,109 -8.476 124 .74 42.79 71.93 1370 .1 180 .68 173 .9 185. 18 .165 0.,107 -8.115 126 .72 42.82 72.48 1333 .0 169 .77 169 .2 190. 17 .959 ,106 -7.752 128,.66 42.87 73.09 1295 .9 159 ,77 164 .5

195. 17 .749 0,,104 -7.384 130,,56 42.96 73.76 1258 .6 150 .55 159 .8 200. 17 .535 0..103 -7.014 132,,44 43.08 74.49 1221 ,2 142 ,03 155 .2 205. 17 .317 0.,102 -6.639 134,.29 43.22 75.29 1183 .6 134 ,10 150 .6 210. 17 .095 0,,101 -6.261 136 ,11 43.40 76.17 1145 ,7 126 ,71 146 .1 215. 16 .867 0..099 -5.878 137 ,92 43.60 77.12 1107 .6 119,,79 141 .7

220. 16..633 0. 099 -5.489 139, 70 43.82 78.17 1069 2 113. 28 137 ,2

225. 16 .393 0. 098 -5.096 141, 47 44.07 79.32 1030 .5 107..15 132. 9 230. 16 .146 0,,097 -4.696 143, 23 44.35 80.58 991, 3 101. 34 128..6 235. 15.,890 0..097 -4.290 144. 98 44.65 82.00 951, 5 95. 83 124. 3 240. 15.,625 0. 096 -3.876 146. 72 44.98 83.58 911, 1 90. 57 120, 1

245. 15,,349 0. 096 -3.454 148. 46 45.34 85.37 870. 85. 53 115, 9

250. 15,,060 0. 096 -3.022 150. 21 45.73 87.44 827. 9 80. 70 111..7 255. 14.,755 0. 096 -2.579 151. 96 46.15 89.86 784. 5 76. 02 107. 5 260. 14,,432 0. 096 -2.122 153. 73 46.61 92.77 739. 6 71. 46 103. 4

265. 14,,085 0. 097 -1.650 155. 53 47.12 96.37 692. 7 67. 00 99. 2

270. 13,,706 0. 098 -1.157 157. 37 47.69 101.03 643. 1 62. 57 95.

275. 13. 284 0. 099 -0.636 159. 28 48.33 107.47 589. 5 58. 10 90. 6 280. 12, 798 0. 101 -0.077 161. 30 49.12 117.31 529. 7 53. 47 86. 1 282.915 12, 468 0. 102 0.277 162. 56 49.69 126.19 490. 4 50. 61 83. 2 282.915 2,,055 0. 621 8.140 190. 35 53.17 117.99 224. 1 10. 69 27. 8

-183-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 3.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol»dm kJ/mol J/(mol»K) J/(mol-K) m«s

l /xPa« <s rriW/(m<•K

285. 1.980 ,639 8.378 191.19 52.14 107.55 229 .0 10 .66 27 .3 290. 1.846 .674 8.876 192.92 50.69 93.22 238 .6 10 .66 26 .7 295. 1.743 .702 9.320 194.44 49.98 85.33 246 .7 10 .71 26 .5 300. 1.659 .725 9.734 195.83 49.67 80.39 253 .8 10 .77 26 .5 310. 1.526 .763 10.506 198.37 49.70 74.70 266 .0 10 .94 27 .0

320. 1.424 .792 11.237 200.69 50.17 71.74 276 .5 11 .14 27 .7 330. 1.340 .816 11.945 202.87 50.89 70.14 285 .8 11 .35 28 .7 340. 1.269 .836 12.642 204.95 51.75 69.34 294 .2 11 .58 29 .8 350. 1.208 .854 13.334 206.95 52.71 69.04 302 .0 11 .81 31 .0 360. 1.154 .868 14.024 208.90 53.75 69.09 309 .3 12 .05 32 .2

370. 1.107 .881 14.716 210.79 54.83 69.38 316 ,2 12 .29 33 .6 380. 1.064 ,893 15.412 212.65 55.95 69.85 322 ,7 12 .54 35 .0 390. 1.025 ,903 16.114 214.47 57.10 70.46 328 ,9 12 .78 36 .4 400. 0.9897 ,911 16.822 216.26 58.27 71.17 334 ,8 13 .02 37 .9 410. 0.9572 .919 17.537 218.03 59.45 71.96 340 ,5 13 ,27 39 .5

420. 0.9273 ,926 18.261 219.77 60.64 72.81 346 13 ,51 41 ,1

430. 0.8995 0, 933 18.994 221.50 61.84 73.71 351 ,3 13, 75 42 .7 440. 0.8736 ,939 19.736 223.20 63.03 74.65 356, 5 14. 00 44,.4 450. 0.8494 0.,944 20.487 224.89 64.23 75.61 361, 5 14. 24 46, 1 460. 0.8268 0,,949 21.248 226.56 65.42 76.60 366. 4 14. 48 47, 8

470. 0.8055 0, 953 22.019 228.22 66.61 77.61 371. 1 14. 71 49, 6 480. 0.7854 0, 957 22.800 229.87 67.79 78.62 375. 8 14. 95 51. 3 490. 0.7665 0. 961 23.591 231.50 68.96 79.64 380. 3 15. 19 53. 1 500. 0.7485 0, 964 24.393 233.12 70.13 80.67 384. 8 15. 42 55.

520. 0.7153 0. 970 26.027 236.32 72.42 82.73 393. 5 58. 7

540. 0.6852 0. 975 27.702 239.48 74.68 84.79 401. 8 62. 5 560. 0.6578 0. 979 29.418 242.60 76.89 86.82 409. 9 66. 3 580. 0.6327 0. 983 31.175 245.69 79.05 88.84 417. 7 70. 2 600. 0.6096 0. 986 32.972 248.73 81.16 90.83 425. 3 74. 2 625. 0.5832 0. 990 35.273 252.49 83.74 93.27 434. 6

-184
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 4.0000 MPa

T P z H

< C

V C

p W V

A

K mo!L»dm kJ/mol J/(mol«K) J/(mol-K) m« s

l /iPa«

3 rriW/(m'•K

95. 21 .551 .235 -14.416 79 .74 47.91 68.49 1987 .6 1093 .70 253 .9 100. 21 .376 .225 -14.069 83 .29 48.20 69.93 1955 .6 906 .38 250 .0

105. 21 .198 0..216 -13.718 86 .72 47.99 70.53 1921 .3 764 .81 245 .9 110. 21 .019 .208 -13.365 90 .01 47.52 70.66 1886 .0 655 .75 241 .6 115. 20 .839 .201 -13.012 93 .15 46.92 70.55 1850 .1 570 .15 237 .1

120. 20 .658 .194 -12.659 96 .15 46.30 70.34 1814 .1 501 .75 232 .5 125. 20 .476 0,.188 -12.308 99 .01 45.70 70.12 1777 .9 446 .20 227 .8 130. 20 .294 0,.182 -11.958 101 .76 45.14 69.93 1741 .7 400 .40 223 .1 135. 20 .111 0,,177 -11.609 104 .40 44.65 69.80 1705 .4 362 .12 218 .3 140. 19 .927 0.,172 -11.260 106 .93 44.22 69.74 1669 .1 329 .72 213 .5

145. 19 .742 0,,168 -10.911 109 .38 43.86 69.76 1632 .8 301 .98 208 .6 150. 19 .555 0,.164 -10.562 111 .75 43.56 69.85 1596 .4 277 .97 203 .7 155. 19 .367 0,,160 -10.213 114 .04 43.32 70.01 1560 .0 257 .00 198 .9 160. 19 .178 0,,157 -9.862 116 .27 43.13 70.24 1523 .6 238 .51 194 .0 165. 18 .986 0,,154 -9.510 118 .43 43.00 70.53 1487 .2 222 .09 189 .1

170. 18,.792 0, 151 -9.157 120 .54 42.90 70.89 1450 .7 207 .39 184 .3 175. 18,,596 0,,148 -8.801 122 .60 42.85 71.30 1414 ,1 194 .15 179 .5 180. 18,.398 0, 145 -8.443 124 .62 42.84 71.78 1377 .5 182 .14 174 .8 185. 18,.197 0, 143 -8.083 126 .59 42.86 72.31 1340 ,8 171 .20 170 .0 190. 17,,992 0, 141 -7.720 128 .53 42.92 72.90 1304 .1 161 .16 165 ,4

195. 17,,785 0.,139 -7.354 130,,43 43.01 73.54 1267 .2 151 .92 160 .7 200. 17,.573 0. 137 -6.985 132,.30 43.13 74.25 1230,.3 143 .38 156 ,1

205. 17,.358 0,,135 -6.612 134,.14 43.27 75.02 1193 ,2 135 .44 151 .6 210. 17,,138 0. 134 -6.234 135,,96 43.44 75.86 1155,,9 128 .04 147,,1

215. 16,,914 0. 132 -5.853 137,,76 43.64 76.77 1118, 4 121 .11 142,.7

220. 16,,684 0. 131 -5.467 139..53 43.87 77.76 1080..7 114..61 138, 3 225. 16 ,449 0. 130 -5.075 141,.29 44.12 78.85 1042..7 108..48 134,

230. 16,,206 0. 129 -4.678 143. 04 44.39 80.04 1004, 3 102, 68 129, 7 235. 15,,956 0. 128 -4.275 144. 77 44.69 81.36 965. 5 97,,19 125. 5 240. 15,,698 0. 128 -3.864 146. 50 45.02 82.82 926. 3 91. 96 121. 3

245. 15, 430 0. 127 -3.446 148. 23 45.37 84.46 886. 4 86. 96 117. 2 250. 15. 150 0. 127 -3.019 149. 95 45.75 86.32 845. 7 82. 16 113. 1 255. 14.,857 0. 127 -2.582 151. 68 46.16 88.47 804. 1 77. 54 109.

260. 14. 548 0. 127 -2.134 153. 42 46.60 90.98 761. 4 73. 07 105.

265. 14. 220 0. 128 -1.672 155. 18 47.09 94.00 717. 2 68. 71 100. 9

270. 13.,867 0. 128 -1.193 156. 97 47.61 97.74 671. 1 64. 43 96. 9 275. 13. 481 0. 130 -0.693 158. 81 48.20 102.57 622. 4 60. 17 92. 8 280. 13. 051 0. 132 -0.164 160. 71 48.88 109.23 569. 9 55. 86 88. 5 285. 12. 555 0. 134 0.405 162. 73 49.70 119.29 512. 51. 40 84. 1 290. 11.,946 0. 139 1.041 164. 94 50.81 137.19 444. 6 46. 55 79. 4

185-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 4.0000 MPa (continued)

T P z H S C

V

C

p W i A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol»K) m«s

l /^Pa« <; iriW/(m<•K

295. 11.087 0,,147 1.820 167.60 52.86 183.68 356 .7 40 .66 74 .2 295.981 10.852 0..150 2.009 168.24 53.60 205.14 334 .1 39 .21 73 .2 295.981 3.196 .509 7.580 187.06 58.83 233.23 207 .1 12 .80 38 .8 300. 2.824 0,.568 8.300 189.48 55.20 145.57 221 .1 12 .33 34 .0 310. 2.387 ,650 9.471 193.32 52.47 100.11 242 .5 12 .01 31 .1

320. 2.139 0..703 10.394 196.26 51.98 86.56 257 .8 11 .99 30 .7 330. 1.965 0,,742 11.225 198.81 52.21 80.24 270 .2 12 .08 31 .0 340. 1.830 .773 12.008 201.15 52.78 76.82 280 ,9 12 .22 31 .7 350. 1.720 .799 12.766 203.35 53.55 74.88 290 ,4 12 .39 32 .6 360. 1.628 .821 13.509 205.44 54.44 73.81 299 ,1 12 .58 33 .7

370. 1.549 ,839 14.244 207.46 55.42 73.30 307 ,1 12 .78 34 .8 380. 1.480 ,855 14.976 209.41 56.46 73.18 314 .6 12 .99 36 .1 390. 1.419 ,869 15.709 211.31 57.54 73.33 321 ,7 13 .20 37 .5 400. 1.364 ,881 16.443 213.17 58.65 73.67 328 .3 13 .43 38 .9 410. 1.315 0.,892 17.183 215.00 59.79 74.17 334,.7 13 .65 40 .4

420. 1.270 0. 902 17.927 216.79 60.95 74.78 340 7 13 .87 41 .9 430. 1.228 0. 911 18.678 218.56 62.11 75.48 346 .6 14 .10 43 .5 440. 1.190 0.,919 19.437 220.30 63.28 76.25 352, 2 14 .33 45 .1 450. 1.155 0,,926 20.204 222.03 64.46 77.08 357. 6 14 .56 46 .7 460. 1.122 0.,932 20.979 223.73 65.63 77.94 362, 9 14..79 48.,4

470. 1.091 0, 938 21.763 225.41 66.80 78.84 368. 15. 01 50, 1 480. 1.062 0, 944 22.556 227.08 67.96 79.76 373. 15. 24 51. 9 490. 1.035 0. 948 23.358 228.74 69.12 80.70 377. 8 15. 47 53. 7 500. 1.010 0. 953 24.170 230.38 70.28 81.65 382. 5 15. 69 55. 5 520. 0.9629 0. 961 25.822 233.62 72.56 83.59 391. 7 59. 1

540. 0.9208 0, 968 27.513 236.81 74.79 85.54 400. 4 62. 9 560. 0.8826 0. 973 29.244 239.96 76.99 87.50 408. 9 66. 7 580. 0.8479 0. 978 31.013 243.06 79.14 89.45 417. 70. 6 600. 0.8160 0. 983 32.821 246.13 81.25 91.38 424. 9 74. 5 625. 0.7798 0. 987 35.136 249.90 83.82 93.76 434. 5

186
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 5.0000 MPa

T P z H

< C

V C

p W 1 A

K mo! .•dm kJ/mol J/(mol«K) J/(mol-K) m« s

l /iPa*

3 IT W/(m •K

95. 21 563 294 -14.376 79 .67 47.91 68.43 1991 9 1103 13 254 .3 100. 21 388 281 -14.030 83 .22 48.22 69.89 1959 8 913 68 250 .5 105. 21 211 270 -13.679 86 64 48.02 70.49 1925 6 770 64 246 4

110. 21 033 260 -13.326 89 93 47.55 70.62 1890 3 660 54 242 .1

115. 20 853 251 -12.973 93 07 46.96 70.51 1854 6 574 17 237 6

120. 20 673 242 -12.621 96 06 46.34 70.30 1818 7 505 21 233 .1

125. 20 492 235 -12.270 98 93 45.74 70.08 1782 7 449 23 228 4

130. 20 311 228 -11.920 101 67 45.19 69.88 1746 6 403 10 223 7 135. 20 129 221 -11.571 104 31 44.70 69.75 1710 5 364 56 218 9 140. 19 946 215 -11.223 106 84 44.27 69.68 1674 4 331 95 214 1

145. 19 762 210 -10.874 109 29 43.91 69.69 1638 3 304 03 209 3 150. 19 576 205 -10.526 111 65 43.61 69.77 1602 1 279 89 204 4

155. 19 389 200 -10.176 113 94 43.37 69.92 1565 9 258 80 199 5 160. 19 201 196 -9.826 116 16 43.18 70.14 1529 8 240 22 194 7 165. 19 011 192 -9.475 118 33 43.04 70.42 1493 6 223 72 189 9

170. 18 818 188 -9.122 120 43 42.95 70.77 1457 4 208 96 185 1 175. 18 624 185 -8.767 122 49 42.90 71.17 1421 1 195 66 180 3 180. 18 427 181 -8.410 124 50 42.89 71.63 1384 9 183 61 175 6 185. 18 228 178 -8.051 126 47 42.91 72.14 1348 5 172 62 170 9 190. 18 025 176 -7.689 128 40 42.97 72.71 1312 2 162 56 166 2

195. 17 820 173 -7.324 130 30 43.06 73.34 1275 7 153 29 161 6 200. 17 611 171 -6.955 132 16 43.17 74.02 1239 2 144 72 157

205. 17 398 169 -6.583 134 00 43.32 74.76 1202 6 136 77 152 5 210. 17 181 167 -6.208 135 81 43.49 75.56 1165 8 129 36 148 1 215. 16 960 165 -5.828 137 60 43.69 76.43 1128 9 122 43 143 7

220. 16 734 163 -5.443 139 37 43.91 77.38 1091 8 115 92 139 4

225. 16 502 162 -5.054 141 12 44.16 78.41 1054 5 109 79 135 1 230. 16 265 161 -4.659 142 85 44.43 79.54 1017 104 01 130 8 235. 16 020 160 -4.258 144 58 44.73 80.77 979 1 98 53 126 7 240. 15 768 159 -3.851 146 29 45.05 82.13 940 8 93 32 122 6

245. 15 507 158 -3.437 148 00 45.40 83.64 902 88 35 118 5 250. 15 236 158 -3.014 149 71 45.77 85.33 862 7 83 59 114 5 255. 14 953 158 -2.583 151 41 46.17 87.25 822 6 79 02 110 5 260. 14 656 158 -2.141 153 13 46.60 89.46 781 7 74 61 106 5 265. 14 344 158 -1.688 154 86 47.07 92.05 739 7 70 33 102 6

270. 14 011 159 -1.220 156 61 47.57 95.16 696 3 66 16 98 7 275. 13 653 160 -0.735 158 39 48.12 98.99 651 2 62 05 94 7 280. 13 262 162 -0.228 160 21 48.73 103.93 603 7 57 96 90 7 285. 12 826 165 0.307 162 11 49.43 110.65 553 53 83 86 6 290. 12 325 168 0.884 164 11 50.26 120.55 497 6 49 56 82 4

187
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P= 5.0000 MPa (continued)

T P Z H S C

V C

p W 1 A

K mol»dm kJ/mol J/(mol-K) J/(mol-K)

-

1

m« s fj.Pa* «3 rr W/(m«K

295. 11.718 0.174 1.524 166.30 51.37 137.09 435.1 44 97 77.9

300. 10.906 0.184 2.283 168.85 53.19 172.16 360.6 39 64 73.1

310. 4.127 0.470 7.602 186.23 59.31 263.20 210.7 14 98 45.4

320. 3.181 0.591 9.258 191.50 54.72 123.27 236.9 13 55 36.4

330. 2.774 0.657 10.347 194.85 53.90 98.73 253.9 13 22 34.7

340. 2.512 0.704 11.277 197.63 53.99 88.51 267.5 13 14 34.5

350. 2.319 0.741 12.133 200.11 54.49 83.15 279.1 13 17 34.8

360. 2.167 0.771 12.948 202.40 55.20 80.07 289.4 13 26 35.5

370. 2.042 0.796 13.739 204.57 56.05 78.26 298.6 13 39 36.4

380. 1.937 0.817 14.515 206.64 56.99 77.23 307.1 13 55 37.5

390. 1.846 0.836 15.285 208.64 58.00 76.72 315.0 13 72 38.7

400. 1.766 0.852 16.051 210.58 59.05 76.57 322.4 13 91 40.0

410. 1.694 0.866 16.817 212.47 60.14 76.68 329.4 14 10 41.4

420. 1.630 0.878 17.585 214.32 61.26 76.98 336.0 14 30 42.8

430. 1.573 0.889 18.357 216.14 62.39 77.43 342.3 14 50 44.3

440. 1.520 0.899 19.134 217.93 63.53 78.00 348.4 14 71 45.9

450. 1.471 0.908 19.917 219.69 64.68 78.65 354.2 14 92 47.5

460. 1.427 0.916 20.707 221.42 65.83 79.37 359.8 15 14 49.1

470. 1.385 0.924 21.505 223.14 66.99 80.14 365.3 15 35 50.8

480. 1.346 0.930 22.310 224.83 68.14 80.95 370.6 15 56 52.5

490. 1.310 0.937 23.124 226.51 69.28 81.80 375.7 15 78 54.3

500. 1.276 0.942 23.946 228.17 70.43 82.67 380.7 15. 99 56.0

520. 1.215 0.952 25.618 231.45 72.68 84.47 390.2 59.6

540. 1.160 0.960 27.326 234.67 74.91 86.32 399.4 63.3

560. 1.110 0.968 29.071 237.85 77.09 88.19 408.2 67.1

580. 1.065 0.974 30.853 240.97 79.23 90.06 416.6 70.9

600. 1.024 0.979 32.673 244.06 81.33 91.93 424.8 74.8

625. 0.9772 0.985 35.000 247.86 83.89 94.25 434.6
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 6.0000 MPa

T P z H C

V C

p W V A

K mo L«dm kJ/mol J/(mol-K) J/(mol«K) m« s

l /LtPa* i 3 IT W/(m •K

95. 21 .575 .352 -14.337 79 .59 47.91 68.38 1996 2 1112 .69 254 .7 100. 21 .401 .337 -13.991 83 .14 48.23 69.84 1964 1 921 .07 250 .9 105. 21 .224 .324 -13.640 86 .57 48.04 70.45 1929 8 776 .53 246 .8 110. 21 .046 312 -13.287 89 .85 47.58 70.58 1894 7 665 .37 242 .6 115. 20 .868 301 -12.935 92 .98 47.00 70.47 1859 1 578 .23 238 .1

120. 20 .688 291 -12.583 95 .98 46.38 70.26 1823 3 508 70 233 6 125. 20 .508 281 -12.232 98 .84 45.78 70.03 1787 4 452 28 229

130. 20 .328 273 -11.882 101 .58 45.23 69.83 1751 5 405 82 224 3 135. 20 .146 265 -11.534 104 .22 44.74 69.69 1715 5 367 01 219 5 140. 19 .964 258 -11.185 106 .75 44.31 69.62 1679 6 334 19 214 7

145. 19 781 252 -10.837 109 19 43.95 69.62 1643 7 306 10 209 9 150. 19 597 245 -10.489 111 55 43.65 69.69 1607 7 281 82 205 1 155. 19 411 240 -10.140 113 84 43.41 69.84 1571 8 260 61 200 2 160. 19 224 235 -9.791 116 06 43.23 70.05 1535 9 241 94 195 4

165. 19 035 230 -9.440 118 22 43.09 70.32 1499 9 225 36 190 6

170. 18 844 225 -9.087 120 32 43.00 70.65 1464 210 53 185 8 175. 18 651 221 -8.733 122 38 42.95 71.04 1428 1 197 17 181 1 180. 18 456 217 -8.377 124 39 42.94 71.49 1392 1 185 07 176 4

185. 18 258 214 -8.018 126 35 42.96 71.98 1356 1 174 04 171 7 190. 18 058 210 -7.657 128 28 43.02 72.53 1320 1 163 95 167 1

195. 17 854 207 -7.293 130 17 43.10 73.14 1284 1 154 65 162 5 200. 17 648 204 -6.926 132 03 43.22 73.80 1248 146 06 158

205. 17 437 202 -6.555 133 86 43.36 74.51 1211 8 138 09 153 5 210. 17 224 200 -6.180 135 66 43.54 75.28 1175 6 130 67 149 1

215. 17 005 197 -5.802 137 45 43.73 76.12 1139 2 123 73 144 7

220. 16 783 195 -5.419 139 21 43.96 77.02 1102 7 117 22 140 4

225. 16 555 194 -5.031 140 95 44.20 78.00 1066 1 111 10 136 1 230. 16 321 192 -4.639 142 67 44.47 79.07 1029 2 105 32 132

235. 16 082 191 -4.241 144 39 44.77 80.23 992 1 99 85 127 8

240. 15 835 190 -3.836 146 09 45.09 81.50 954 7 94 65 123 8

245. 15 580 189 -3.425 147 78 45.43 82.90 917 89 70 119 8 250. 15 317 188 -3.007 149 47 45.80 84.45 878 8 84 98 115 8 255. 15 043 188 -2.581 151 16 46.19 86.19 840 1 80 45 111 9 260. 14 758 188 -2.145 152 85 46.61 88.16 800. 7 76 09 108

265. 14 458 188 -1.699 154. 55 47.06 90.42 760. 6 71 88 104 2

270. 14 142 0. 189 -1.240 156. 27 47.54 93.07 719. 5 67 79 100 3 275. 13 806 0. 190 -0.767 158. 00 48.07 96.22 677. 1 63. 79 96 5 280. 13 444 0. 192 -0.277 159. 77 48.63 100.11 633. 2 59. 86 92 7 285. 13 049 0. 194 0.236 161. 59 49.26 105.05 587. 2 55. 95 88 9

290. 12 611 0. 197 0.777 163. 47 49.97 111.65 538. 6 52. 00 84. 9

-189-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 6.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol«dm kJ/mol J/(mol.K) J/(mol»K) m* s

l /iPa«s itiW/(m'•K

295. 12.111 .202 1.357 165.45 50.81 121.02 486 .5 47 .95 80 .9 300. 11.516 .209 1.995 167.60 51.88 135.51 429 .9 43 .65 76 .7 310. 9.684 .240 3.662 173.05 56.14 222.98 296 .8 33 ,14 67 .8 320. 5.268 .428 7.314 184.64 59.68 284.90 217 .8 17 .85 51 .8 330. 3.937 .555 9.199 190.45 56.13 139.15 239 .0 15 ,25 41 .3

340. 3.382 .628 10.408 194.06 55.40 108.15 255 .4 14 .54 38 .6 350. 3.036 .679 11.418 196.99 55.52 95.25 268 .9 14,,26 37 .9 360. 2.787 .719 12.333 199.57 56.01 88.48 280 .6 14 ,17 37 .9 370. 2.594 .752 13.197 201.93 56.71 84.53 291 .0 14,,18 38 .4 380. 2.438 .779 14.029 204.15 57.54 82.15 300 .5 14,,24 39 .2

390. 2.307 .802 14.843 206.27 58.47 80.71 309 .1 14,,35 40 .2 400. 2.195 .822 15.645 208.30 59.46 79.89 317 .2 14, 48 41 .3 410. 2.097 .839 16.442 210.27 60.50 79.50 324 ,8 14, 63 42 .6 420. 2.010 ,855 17.236 212.18 61.57 79.41 331 ,9 14. 79 43,.9 430. 1.933 .868 18.031 214.05 62.67 79.56 338 ,7 14. 96 45 .3

440. 1.863 .880 18.828 215.88 63.78 79.88 345 ,2 15. 15 46 8

450. 1.799 0.,891 19.629 217.68 64.91 80.33 351, 4 15. 33 48, 3 460. 1.741 0.,901 20.435 219.45 66.04 80.88 357, 3 15. 53 49, 9 470. 1.687 0. 910 21.247 221.20 67.17 81.51 363, 15. 72 51. 5 480. 1.638 0, 918 22.065 222.92 68.31 82.20 368. 6 15. 92 53. 2

490. 1.591 0. 925 22.891 224.62 69.44 82.94 374. 16. 12 54. 9 500. 1.548 0. 932 23.724 226.31 70.57 83.73 379. 2 16. 33 56. 6 520. 1.470 0. 944 25.415 229.62 72.81 85.38 389. 2 60. 2 540. 1.401 0. 954 27.140 232.88 75.02 87.11 398. 7 63. 8 560. 1.339 0. 962 28.900 236.08 77.19 88.88 407. 8 67. 5

580. 1.283 0. 970 30.695 239.23 79.32 90.68 416. 5 71. 3 600. 1.233 0. 976 32.527 242.33 81.41 92.48 424. 9 75. 2 625. 1.175 0. 982 34.867 246.15 83.96 94.74 435.

-190
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 7.0000 MPa

T P z H C

V C

p W V A

K mo L»dm kJ/mol J/(mol«K) J/(mol«K) m« s

-

/iPa»3 iriW/(m •K

95. 21 .587 .411 -14.298 79 .52 47.90 68.32 2000 4 1122 .37 255 .2

100. 21 .413 .393 -13.952 83 .06 48.24 69.80 1968 3 928 .54 251 .4

105. 21 .237 .378 -13.601 86 .49 48.07 70.41 1934 1 782 .48 247 .3 110. 21 .060 363 -13.249 89 .77 47.61 70.55 1899 670 .24 243 .1

115. 20 .882 351 -12.896 92 .90 47.03 70.43 1863 5 582 .32 238 .7

120. 20 .703 339 -12.545 95 .89 46.42 70.22 1827 8 512 .21 234 .1

125. 20 .524 .328 -12.194 98 .76 45.82 69.98 1792 455 .35 229 .5 130. 20 344 .318 -11.845 101 .50 45.27 69.78 1756 3 408 55 224 .9 135. 20 164 309 -11.496 104 .13 44.78 69.64 1720 5 369 47 220 .1

140. 19 983 301 -11.148 106 .66 44.36 69.56 1684 8 336 43 215 .3

145. 19 801 293 -10.800 109 10 44.00 69.55 1649 308 18 210 .6 150. 19 617 286 -10.453 111 46 43.70 69.62 1613 3 283 75 205 7 155. 19 433 280 -10.104 113 74 43.46 69.75 1577 6 262 43 200 9 160. 19 246 273 -9.755 115 96 43.27 69.95 1541 9 243 66 196 1 165. 19 059 268 -9.404 118 12 43.14 70.22 1506 2 226 99 191 3

170. 18 869 262 -9.053 120 22 43.04 70.54 1470 6 212 09 186 6 175. 18 678 258 -8.699 122 27 42.99 70.92 1434 9 198 68 181 9 180. 18 484 253 -8.343 124 27 42.98 71.35 1399 3 186 53 177 2 185. 18 288 249 -7.985 126 23 43.01 71.83 1363 6 175 46 172 5 190. 18 090 245 -7.625 128 15 43.06 72.36 1328 165 33 167 9

195. 17 888 241 -7.262 130 04 43.15 72.95 1292 3 156 01 163 4

200. 17 684 238 -6.895 131 90 43.27 73.58 1256 6 147 40 158 9 205. 17 476 235 -6.526 133 72 43.41 74.27 1220 9 139 41 154 4

210. 17 265 232 -6.153 135 52 43.58 75.02 1185 1 131 97 150

215. 17 049 230 -5.776 137 29 43.78 75.82 1149 3 125 02 145 7

220. 16 830 227 -5.394 139 05 44.00 76.69 1113 3 118 51 141 4

225. 16 606 225 -5.009 140 78 44.25 77.62 1077 3 112 38 137 2 230. 16 376 224 -4.618 142 50 44.52 78.63 1041 1 106 61 133 1 235. 16 141 222 -4.222 144 20 44.81 79.73 1004 7 101 15 129

240. 15 900 221 -3.821 145 89 45.12 80.92 968 2 95 96 124 9

245. 15 651 220 -3.413 147 57 45.46 82.22 931 3 91 04 121

250. 15 395 219 -2.998 149 25 45.83 83.66 894 2 86 34 117 1 255. 15 129 218 -2.576 150 92 46.21 85.24 856 7 81 84 113 2 260. 14 853 218 -2.145 152 59 46.63 87.02 818 7 77 52 109 4

265. 14 565 218 -1.705 154 27 47.06 89.03 780 1 73 36 105 7

270. 14 263 219 -1.255 155 95 47.53 91.32 740. 9 69. 34 101 9

275. 13 944 220 -0.792 157 65 48.03 94.00 700. 8 65. 44 98 2 280. 13 605 0. 221 -0.314 159 37 48.57 97.18 659. 6 61. 62 94. 6 285. 13 241 0. 223 0.181 161. 13 49.15 101.04 617. 1 57. 86 90. 9 290. 12 846 0. 226 0.698 162. 93 49.79 105.89 573. 54. 12 87. 2

191
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 7.0000 MPa (continued)

T P Z H S C

V C

p W n A

K mo 1 • dm kJ/mol J/(mol-K) J/(mol«K)

-

1

m» s /iPa«;3 niW/(m«K

295. 12.408 0.230 1.243 164.79 50.51 112.19 527.0 50 37 83.4

300. 11.914 0.236 1.824 166.74 51.34 120.74 478.6 46 55 79.6

310. 10.646 0.255 3.164 171.13 53.63 151.66 375.5 38 33 71.6

320. 8.552 0.308 5.050 177.11 57.57 243.11 270.7 28 34 63.7

330. 5.793 0.440 7.634 185.07 58.30 217.92 235.5 19 51 52.3

340. 4.542 0.545 9.359 190.22 56.88 140.79 247.8 16 82 44.8

350. 3.912 0.615 10.606 193.84 56.57 112.72 261.5 15 84 42.0

360. 3.508 0.667 11.661 196.81 56.82 99.58 273.9 15 39 41.1

370. 3.216 0.708 12.617 199.43 57.37 92.35 285.1 15 18 40.9

380. 2.990 0.741 13.517 201.83 58.09 88.02 295.2 15 10 41.3

390. 2.807 0.769 14.383 204.08 58.93 85.32 304.5 15 10 42.0

400. 2.654 0.793 15.227 206.22 59.86 83.64 313.1 15 16 42.9

410. 2.523 0.814 16.058 208.27 60.85 82.62 321.1 15 24 43.9

420. 2.409 0.832 16.881 210.25 61.88 82.07 328.7 15 36 45.1

430. 2.309 0.848 17.700 212.18 62.94 81.85 335.8 15 49 46.4

440. 2.219 0.862 18.519 214.06 64.03 81.88 342.6 15 64 47.8

450. 2.138 0.875 19.339 215.91 65.13 82.10 349.1 15 80 49.3

460. 2.064 0.887 20.161 217.71 66.24 82.46 355.4 15 96 50.8

470. 1.997 0.897 20.988 219.49 67.36 82.93 361.4 16 14 52.3

480. 1.935 0.906 21.820 221.24 68.48 83.49 367.1 16 32 53.9

490. 1.878 0.915 22.658 222.97 69.60 84.12 372.7 16 50 55.6

500. 1.825 0.923 23.503 224.68 70.71 84.81 378.1 16. 69 57.3

520. 1.729 0.936 25.214 228.03 72.94 86.30 388.5 60.8

540. 1.645 0.948 26.956 231.32 75.13 87.90 398.3 64.3

560. 1.570 0.957 28.730 234.55 77.29 89.58 407.7 68.0

580. 1.503 0.966 30.539 237.72 79.41 91.30 416.6 71.8

600. 1.442 0.973 32.383 240.84 81.49 93.04 425.2 75.6

625. 1.374 0.981 34.736 244.69 84.03 95.22 435.6

-192-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 8.0000 MPa

T P z H

< C

V C

p W n A

K mo"L« dm kJ/mol J/(mol«K) J/(mol«K) m* s

l /iPa«

3 ITiW/(m<•K

95. 21 .599 .469 -14 .258 79 .44 47.90 68.27 2004 .7 1132 .19 255 .6 100. 21 .426 .449 -13 .913 82 .99 48.26 69.75 1972 .5 936 .09 251 .8 105. 21 .250 .431 -13 .562 86 .41 48.09 70.37 1938 .3 788 .48 247 .8 110. 21 .074 .415 -13 .210 89 .69 47.64 70.51 1903 .3 675 .15 243 .6 115. 20 .896 .400 -12 .858 92 .82 47.07 70.39 1867 .9 586 .45 239 .2

120. 20 .718 .387 -12 .506 95 .81 46.46 70.18 1832 .3 515 .75 234 .7 125. 20 .540 .375 -12 .156 98 .67 45.86 69.94 1796 .7 458 .45 230 .1

130. 20 .361 .364 -11 .807 101 .41 45.31 69.73 1761 .1 411 .29 225 .4

135. 20 .181 .353 -11 .459 104 .04 44.82 69.58 1725 .5 371 .95 220 .7 140. 20 .001 .344 -11 .111 106 .57 44.40 69.50 1689 .9 338 .69 216 .0

145. 19 .820 .335 -10 .763 109 .01 44.04 69.49 1654 .4 310 .26 211 .2 150. 19 .637 .327 -10 .416 111 .36 43.74 69.54 1618 .9 285 .69 206 .4

155. 19 .454 .319 -10 .068 113 .64 43.50 69.67 1583 .4 264 .25 201 .6 160. 19 .269 .312 -9 ,719 115 .86 43.32 69.86 1547 .9 245 .38 196 .8 165. 19 .083 .306 -9 .369 118 .01 43.18 70.12 1512 ,5 228 .63 192 .1

170. 18 .894 .300 -9.,018 120 .11 43.09 70.43 1477 .1 213 .66 187 .3 175. 18 .704 .294 -8 .665 122 .16 43.04 70.79 1441 .7 200 .19 182 .6 180. 18 .512 ,289 -8 ,310 124 ,16 43.03 71.21 1406 .4 187 .99 178 .0 185. 18 .318 ,284 -7 ,953 126 .11 43.05 71.68 1371 .0 176 ,88 173 .3 190. 18 .121 ,279 -7,,593 128 ,03 43.11 72.20 1335 ,7 166 ,72 168 .8

195. 17 .922 0,,275 -7,,230 129 ,92 43.20 72.77 1300 .4 157 ,37 164 .2 200. 17 .719 0.,272 -6,.865 131.,77 43.31 73.38 1265 .1 148 ,73 159 .7 205. 17 ,514 ,268 -6, 497 133,,59 43.46 74.05 1229 .8 140 .72 155 ,3

210. 17 .305 0.,265 -6, 125 135,,38 43.63 74.76 1194 ,5 133 .27 151 .0 215. 17 .093 262 -5,.749 137,,15 43.82 75.54 1159 .1 126.,31 146 ,7

220. 16..876 0,,259 -5. 369 138.,89 44.05 76.37 1123,.7 119, 79 142 ,4

225. 16, 655 0, 257 -4. 985 140. 62 44.29 77.26 1088, 2 113. 66 138.,2

230. 16..430 0, 255 -4. 596 142. 33 44.56 78.22 1052,,7 107. 89 134.,1

235. 16. 199 0,.253 -4. 203 144, 02 44.85 79.26 1017. 102. 43 130, 1 240. 15,.962 0, 251 -3. 804 145. 70 45.16 80.38 981. 2 97. 26 126. 1

245. 15. 719 0. 250 -3. 399 147. 37 45.50 81.60 945. 2 92. 35 122, 2 250. 15. 469 0,.249 -2. 987 149. 03 45.86 82.94 909. 87. 67 118, 3 255. 15. 211 0, 248 -2. 569 150. 69 46.24 84.40 872. 5 83. 20 114, 5 260. 14. 943 0, 248 -2. 143 152. 34 46.64 86.01 835. 7 78. 91 110. 8 265. 14. 665 0. 248 -1. 709 154. 00 47.07 87.82 798. 5 74. 80 107. 1

270. 14. 375 0. 248 -1. 265 155. 66 47.53 89.85 760. 8 70. 83 103. 5 275. 14. 071 0. 249 -0. 810 157. 33 48.01 92.16 722. 6 66. 99 99. 9 280. 13. 751 0. 250 -0. 342 159. 01 48.53 94.84 683. 6 63. 26 96. 3 285. 13. 411 0. 252 0. 139 160. 72 49.08 97.99 643. 8 59. 62 92. 8 290. 13. 046 0. 254 0. 639 162. 45 49.67 101.78 603. 56. 03 89. 2

-193-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 8.0000 MPa (continued)

T P z H S C

V C

p W V A

K mol'dm kJ/mol J/(mol«K) J/(mol-K)

- l m* s /iPa*

:

5 IT W/(m K

295. 12.651 258 1.159 164.23 50.32 106.43 561.0 52 48 85 .7 300. 12.218 262 1.705 166.07 51.04 112.29 517.8 48 93 82 1 310. 11.186 277 2.908 170.01 52.77 129.90 428.5 41 68 74 9 320. 9.793 307 4.353 174.60 55.09 162.85 341.0 33 97 67 5 330. 7.849 371 6.223 180.34 57.38 206.54 272.3 25 92 60 2

340. 6.029 469 8.185 186.21 57.69 174.83 253.9 20 46 52 3 350. 4.974 553 9.712 190.63 57.43 134.32 260.5 18 10 47 3 360. 4.342 616 10.937 194.09 57.55 113.12 271.1 17 02 44 9 370. 3.913 665 12.006 197.02 57.98 101.59 281.8 16 46 43 9 380. 3.595 704 12.985 199.63 58.61 94.77 292.0 16 16 43 7

390. 3.346 737 13.909 202.03 59.38 90.51 301.4 16 01 44

400. 3.143 765 14.800 204.28 60.25 87.77 310.3 15 95 44 6 410. 2.972 790 15.668 206.43 61.19 86.01 318.6 15 96 45 5 420. 2.827 810 16.522 208.49 62.18 84.92 326.4 16 01 46 5 430. 2.699 829 17.368 210.48 63.21 84.29 333.9 16 09 47 7

440. 2.587 845 18.209 212.41 64.27 83.99 340.9 16 19 48 9

450. 2.487 860 19.049 214.30 65.34 83.95 347.6 16 31 50 3 460. 2.396 873 19.889 216.14 66.44 84.10 354.1 16 45 51 7 470. 2.314 885 20.731 217.96 67.54 84.40 360.3 16 59 53 2 480. 2.239 895 21.577 219.74 68.64 84.82 366.3 16 75 54 8

490. 2.170 905 22.428 221.49 69.75 85.33 372.0 16 91 56 4

500. 2.106 914 23.284 223.22 70.85 85.91 377.6 17 08 58

520. 1.992 929 25.015 226.61 73.06 87.23 388.2 61 4

540. 1.891 942 26.774 229.93 75.23 88.71 398.3 64 9 560. 1.803 953 28.564 233.19 77.38 90.28 407.9 68 5

580. 1.724 962 30.386 236.38 79.49 91.92 417.1 72 2 600. 1.652 970 32.241 239.53 81.57 93.59 425.9 76

625. 1.572 979 34.607 243.39 84.10 95.71 436.4

-194
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 9.0000 MPa

T P z H S C

V C

p W V A

K mo!_«dm kJ/mol J/(mol-K) J/(mol-K) m* s

i H?a'S mW/(m •K

95. 21 611 527 -14 219 79 37 47 90 68.21 2008 9 1142 13 256

100. 21 438 505 -13 874 82 91 48 27 69.71 1976 7 943 74 252 3 105. 21 263 485 -13 524 86 33 48 11 70.34 1942 5 794 56 248 3 110. 21 087 467 -13 171 89 61 47 67 70.47 1907 6 680 12 244 1

115. 20 910 450 -12 819 92 74 47 10 70.36 1872 2 590 61 239 7

120. 20 733 435 -12 468 95 73 46 50 70.14 1836 8 519 31 235 2 125. 20 556 421 -12 118 98 59 45 90 69.90 1801 3 461 56 230 7 130. 20 377 409 -11 769 101 32 45 36 69.69 1765 9 414 05 226

135. 20 199 397 -11 421 103 95 44 87 69.53 1730 4 374 43 221 3 140. 20 019 386 -11 073 106 48 44 44 69.44 1695 340 96 216 6

145. 19 839 376 -10 726 108 91 44 08 69.42 1659 7 312 35 211 8 150. 19 658 367 -10 379 111 27 43 79 69.47 1624 3 287 63 207 1 155. 19 475 359 -10 032 113 55 43 55 69.59 1589 1 266 08 202 3 160. 19 291 351 -9 683 115 76 43 36 69.78 1553 8 247 11 197 5 165. 19 106 343 -9 334 117 91 43 23 70.02 1518 7 230 28 192 8

170. 18 919 337 -8 983 120 01 43 13 70.32 1483 5 215 24 188 1 175. 18 730 330 -8 630 122 05 43 09 70.68 1448 4 201 71 183 4

180. 18 540 324 -8 276 124 05 43 07 71.08 1413 4 189 46 178 7 185. 18 347 319 -7 919 126 00 43 10 71.54 1378 3 178 30 174 1 190. 18 152 314 -7 560 127 91 43 15 72.04 1343 4 168 10 169 6

195. 17 954 309 -7 199 129 79 43 24 72.59 1308 4 158 72 165 1

200. 17 754 305 -6 835 131 64 43 36 73.19 1273 5 150 06 160 6

205. 17 551 301 -6 467 133 45 43 50 73.83 1238 6 142 03 156 2 210. 17 345 297 -6 096 135 24 43 67 74.52 1203 6 134 56 151 9 215. 17 135 294 -5 722 137 00 43 87 75.27 1168 7 127 59 147 6

220. 16 921 291 -5 343 138 74 44 09 76.07 1133 8 121 06 143 4

225. 16 704 288 -4 961 140 46 44 33 76.92 1098 9 114 93 139 3 230. 16 482 286 -4 574 142 16 44 60 77.84 1063 9 109 15 135 2 235. 16 255 283 -4 182 143 84 44 89 78.83 1028 9 103 70 131 2 240. 16 023 281 -3 786 145 52 45 20 79.89 993 8 98 53 127 2

245. 15 785 280 -3 383 147 17 45 53 81.04 958 5 93 63 123 4

250. 15 540 279 -2 975 148 82 45 89 82.28 923 2 88 97 119 5 255. 15 289 278 -2 560 150 47 46 27 83.64 887 7 84 52 115 8 260. 15 029 277 -2 139 152 10 46 67 85.12 851 9 80 27 112 1 265. 14 760 277 -1 709 153 74 47 09 86.75 815 9 76 19 108 5

270. 14 481 277 -1 271 155 38 47 54 88.57 779 6 72 27 104 9 275. 14 189 277 -0 823 157 02 48 01 90.61 742 9 68 48 101 4

280. 13 884 278 -0 364 158 68 48 51 92.92 705 8 64 82 97 9

285. 13 563 280 107 160 34 49 04 95.57 668 1 61 26 94 5 290. 13 223 282 592 162 03 49 60 98.65 629 8 57 78 91 1

-195-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 9.0000 MPa (continued)

T P z H S C

V C

p W n A

K mo 1 • dm kJ/mol J/(mol'K) J/(mol«K)

-

m* s ^Pa»s ntW/(m<K

295. 12.859 .285 1.094 163.75 50.20 102.30 590.9 54 .37 87 .7 300. 12.468 .289 1.616 165.50 50.85 106.67 551.2 51 .01 84 .4

310. 11.573 .302 2.738 169.18 52.33 118.55 470.6 44 .32 77 .6 320. 10.466 .323 4.008 173.21 54.11 136.78 392.3 37 .58 70 .9 330. 9.064 .362 5.501 177.80 55.98 162.27 324.7 30 .81 64 .4

340. 7.469 .426 7.201 182.88 57.27 171.68 282.3 24 .89 58 .2 350. 6.153 .503 8.822 187.58 57.77 149.72 271.0 21 .12 52 .7 360. 5.272 .570 10.195 191.45 58.06 126.36 274.6 19 .13 49 .2 370. 4.678 .625 11.378 194.69 58.48 111.28 282.6 18 .06 47 .3 380. 4.249 .670 12.440 197.52 59.07 101.96 291.6 17 .44 46 .5

390. 3.921 .708 13.428 200.09 59.79 96.03 300.6 17,,08 46 .3 400. 3.659 ,740 14.368 202.47 60.61 92.15 309.3 16, 88 46 .6 410. 3.443 ,767 15.275 204.71 61.51 89.59 317.6 16, 78 47 ,2

420. 3.261 ,790 16.162 206.85 62.46 87.89 325.4 16, 74 48 ,0

430. 3.104 0..811 17.035 208.90 63.46 86.81 333.0 16. 75 49,.0

440. 2.966 0,,829 17.900 210.89 64.49 86.17 340.1 16. 80 50 ,1

450. 2.844 0.,846 18.760 212.82 65.55 85.85 347.0 16. 88 51,,4

460. 2.736 0. 860 19.618 214.71 66.62 85.78 353.6 16. 98 52, 7 470. 2.637 0. 873 20.476 216.55 67.71 85.90 359.9 17. 09 54, 1 480. 2.548 0, 885 21.336 218.36 68.80 86.16 366.0 17. 22 55. 6

490. 2.466 0. 896 22.200 220.14 69.89 86.54 371.9 17. 35 57. 2 500. 2.391 0. 906 23.067 221.90 70.99 87.02 377.5 17. 50 58. 8

520. 2.256 0. 923 24.819 225.33 73.17 88.17 388.4 62. 1 540. 2.139 0. 937 26.595 228.68 75.34 89.51 398.7 65. 5 560. 2.037 0. 949 28.400 231.96 77.47 90.98 408.5 69. 1

580. 1.945 0. 959 30.235 235.18 79.58 92.53 417.8 72. 7 600. 1.863 0. 968 32.102 238.35 81.64 94.14 426.7 76. 5 625. 1.771 0. 978 34.481 242.23 84.17 96.19 437.4

196
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 10.0000 MPa

T P z H

4 ( V C

p W n

A

K mo L • dm kJ /mo

1

J/(mol-K) J/(mol»K) m« s

-

1

/iPa* 3 ITiW/(m •K

95. 21 .623 .586 -14.180 79 .30 47 .89 68.16 2013 .1 1152 .21 256 .4

100. 21 .450 .561 -13.835 82 .84 48 .28 69.67 1980 .8 951 .48 252 .7 105. 21 .276 .538 -13.485 86 .25 48 .14 70.30 1946 .7 800 .69 248 .7 110. 21 .101 518 -13.133 89 .53 47 .71 70.44 1911 .8 685 .13 244 .6

115. 20 .925 .500 -12.781 92 .66 47 .14 70.32 1876 .6 594 .80 240 .2

120. 20 .748 483 -12.430 95 .65 46 .53 70.10 1841 .3 522 .90 235 .8

125. 20 571 468 -12.080 98 .50 45 .94 69.86 1805 .9 464 .69 231 .2 130. 20 394 454 -11.731 101 .24 45 .40 69.64 1770 6 416 .83 226 .6 135. 20 216 441 -11.383 103 .86 44 .91 69.48 1735 3 376 .93 221 .9 140. 20 037 429 -11.036 106 .39 44 .49 69.38 1700 1 343 .24 217 .2

145. 19 858 418 -10.689 108 82 44 .13 69.36 1664 9 314 .45 212 5 150. 19 677 407 -10.342 111 17 43 .83 69.40 1629 8 289 .59 207 7 155. 19 496 398 -9.995 113 45 43 .59 69.52 1594 7 267 91 203

160. 19 313 389 -9.647 115 66 43 .41 69.69 1559 7 248 .84 198 .2 165. 19 129 381 -9.298 117 81 43 .27 69.93 1524 8 231 .92 193 .5

170. 18 944 373 -8.948 119 90 43 18 70.22 1489 9 216 81 188 8 175. 18 756 366 -8.596 121 94 43 13 70.56 1455 203 22 184 1 180. 18 567 360 -8.242 123 93 43 12 70.96 1420 3 190 92 179 5 185. 18 376 354 -7.886 125 88 43 14 71.40 1385 5 179 72 174 9 190. 18 183 348 -7.528 127 79 43 20 71.89 1350 9 169 48 170 4

195. 17 987 343 -7.167 129 67 43 29 72.42 1316 3 160 07 165 9 200. 17 788 338 -6.804 131 51 43 41 73.00 1281 7 151 38 161 5 205. 17 587 334 -6.437 133 32 43 55 73.62 1247 2 143 33 157 1 210. 17 383 329 -6.067 135 10 43 72 74.29 1212 7 135 85 152 8 215. 17 176 326 -5.694 136 86 43 92 75.01 1178 2 128 86 148 6

220. 16 965 322 -5.317 138 59 44 13 75.78 1143 7 122 32 144 4

225. 16 751 319 -4.936 140 30 44 38 76.60 1109 3 116 18 140 3 230. 16 532 316 -4.551 142 00 44 64 77.48 1074 9 110 41 136 2 235. 16 309 314 -4.161 143 67 44 93 78.42 1040 4 104 95 132 2 240. 16 081 312 -3.767 145 33 45 24 79.43 1006 99 79 128 3

245. 15 848 310 -3.367 146 98 45 57 80.51 971 5 94 90 124 5 250. 15 609 308 -2.961 148 62 45 93 81.68 936 9 90 25 120 7 255. 15 363 307 -2.550 150 25 46 30 82.94 902. 2 85 82 117

260. 15 110 306 -2.132 151 87 46 69 84.31 867. 4 81 59 113. 4

265. 14 850 306 -1.707 153 49 47 11 85.81 832. 5 77. 54 109. 8

270. 14 580 306 -1.273 155. 11 47. 55 87.46 797. 4 73. 66 106. 3 275. 14 299 306 -0.832 156. 74 48. 01 89.27 762. 69. 92 102. 9 280. 14 007 307 -0.380 158. 36 48. 50 91.30 726. 4 66. 31 99. 5 285. 13 702 308 0.082 160. 00 49. 01 93.58 690. 5 62. 82 96. 2 290. 13 381 310 0.556 161. 65 49. 55 96.18 654. 2 59. 42 92. 9

197
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 10.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol»dm kJ/raol J/(mol-K) J/(mol«K) m»s

• l /iPa»

3 ITiW/(m •K

295. 13.042 .313 1.044 163.32 50.12 99.15 617 .6 56 .12 89 .6 300. 12.682 .316 1.548 165.01 50.73 102.60 580 .6 52 .88 86 .4

310. 11.880 .327 2.616 168.51 52.07 111.37 506 .3 46 .56 80 .0

320. 10.936 .344 3.787 172.23 53.59 123.47 434 .1 40 .37 73 .8 330. 9.808 .372 5.098 176.26 55.21 139.15 369 .9 34 .34 67 .8

340. 8.515 .415 6.562 180.63 56.59 151.90 321 .0 28 .79 62 .2 350. 7.248 .474 8.080 185.03 57.58 148.87 294 .3 24 .46 57 .3 360. 6.227 .536 9.499 189.03 58.24 134.09 286 .6 21 .65 53 .4

370. 5.483 .593 10.763 192.49 58.80 119.38 288 .9 19 .97 50 .9 380. 4.938 .641 11.901 195.53 59.42 108.70 295 .0 18 .96 49 .4

390. 4.524 .682 12.949 198.25 60.13 101.44 302 .5 18 .33 48 .8 400. 4.198 .716 13.937 200.75 60.92 96.53 310 .4 17 .94 48 .7 410. 3.931 .746 14.885 203.09 61.79 93.18 318 .2 17 .70 49 .0 420. 3.709 .772 15.804 205.31 62.72 90.90 325 .9 17 .56 49 .7 430. 3.519 795 16.705 207.43 63.70 89.37 333 3 17 .49 50 .5

440. 3.354 0. 815 17.594 209.47 64.71 88.37 340. 4 17 .48 51 .5 450. 3.210 0. 833 18.474 211.45 65.75 87.77 347. 2 17,,50 52 .6 460. 3.081 0. 849 19.350 213.38 66.80 87.47 353, 8 17, 55 53 .8 470. 2.965 0,,863 20.224 215.26 67.87 87.40 360, 2 17, 63 55,.2 480. 2.861 0. 876 21.099 217.10 68.95 87.51 366. 4 17, 72 56,.6

490. 2.765 0. 888 21.975 218.90 70.03 87.76 372. 3 17. 83 58.

500. 2.678 0. 898 22.854 220.68 71.12 88.12 378. 1 17. 95 59..6 520. 2.523 0. 917 24.626 224.15 73.29 89.10 389. 1 62. 8 540. 2.388 0. 933 26.420 227.54 75.44 90.31 399. 5 66. 1 560. 2.271 0. 946 28.239 230.85 77.56 91.67 409. 4 69. 6

580. 2.167 0. 957 30.087 234.09 79.66 93.14 418. 8 73. 2 600. 2.073 0. 967 31.966 237.27 81.71 94.68 427. 9 76. 9 625. 1.970 0. 977 34.357 241.18 84.23 96.66 438. 7

-198-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 11.0000 MPa

T P z H

< C

V C

p W 1

A

K mo' .•dm kJ/mol J/(mol»K) J/(mol«K) m« s

i //Pa»

:

3 IT W/(m •K

95. 21 634 644 -14.141 79 22 47 89 68.11 2017 3 1162 42 256 9 100. 21 463 616 -13.796 82 76 48 30 69.63 1985 959 31 253 2 105. 21 289 592 -13.446 86 18 48 16 70.26 1950 9 806 89 249 2 110. 21 114 570 -13.094 89 45 47 74 70.40 1916 1 690 18 245 1 115. 20 939 549 -12.742 92 58 47 17 70.29 1880 9 599 03 240 .7

120. 20 763 531 -12.391 95 56 46 57 70.06 1845 7 526 52 236 3 125. 20 587 514 -12.042 98 42 45 98 69.82 1810 5 467 84 231 8 130. 20 410 499 -11.693 101 15 45 44 69.60 1775 3 419 63 227 2 135. 20 233 484 -11.345 103 78 44 95 69.43 1740 2 379 45 222 5 140. 20 055 471 -10.999 106 30 44 53 69.33 1705 1 345 53 217 8

145. 19 877 459 -10.652 108 73 44 17 69.30 1670 1 316 56 213 1 150. 19 697 448 -10.306 111 08 43 87 69.34 1635 2 291 55 208 4

155. 19 517 437 -9.959 113 36 43 64 69.44 1600 4 269 75 203 7 160. 19 335 428 -9.611 115 56 43 45 69.61 1565 6 250 57 198 9 165. 19 152 419 -9.262 117 71 43 32 69.84 1530 8 233 57 194 2

170. 18 968 410 -8.913 119 80 43 22 70.12 1496 2 218 39 189 5 175. 18 782 403 -8.561 121 83 43 18 70.45 1461 6 204 73 184 9 180. 18 594 395 -8.208 123 82 43 16 70.84 1427 1 192 38 180 3 185. 18 404 389 -7.853 125 77 43 19 71.27 1392 7 181 14 175 7 190. 18 213 382 -7.495 127 68 43 25 71.74 1358 3 170 86 171 2

195. 18 019 377 -7.135 129 55 43 33 72.26 1324 161 42 166 8 200. 17 822 371 -6.773 131 38 43 45 72.82 1289 8 152 70 162 4

205. 17 623 366 -6.407 133 19 43 59 73.43 1255 6 144 63 158

210. 17 421 362 -6.038 134 97 43 76 74.07 1221 5 137 12 153 7 215. 17 217 357 -5.666 136 72 43 96 74.77 1187 5 130 12 149 5

220. 17 009 354 -5.290 138 45 44 18 75.51 1153 5 123 58 145 4

225. 16 797 350 -4.911 140 15 44 42 76.30 1119 5 117 43 141 3 230. 16 582 347 -4.527 141 84 44 69 77.14 1085 6 111 65 137 2 235. 16 362 344 -4.139 143 51 44 97 78.04 1051 7 106 20 133 3 240. 16 138 342 -3.747 145 16 45 28 79.00 1017 8 101 04 129 4

245. 15 909 339 -3.349 146 80 45 61 80.03 984 96 15 125 6 250. 15 675 338 -2.946 148 43 45 96 81.13 950 1 91 51 121 9 255. 15 435 336 -2.538 150 04 46 33 82.31 916 2 87 10 118 2 260. 15 189 335 -2.123 151 65 46 72 83.59 882 3 82 89 114 7 265. 14 935 334 -1.702 153 26 47 13 84.97 848 3 78 86 111 1

270. 14 673 334 -1.273 154 86 47 57 86.47 814 2 75 00 107 7 275. 14 403 334 -0.837 156 46 48 02 88.11 780 1 71 30 104 3 280. 14 122 335 -0.392 158 07 48 50 89.92 745. 8 67 74 101

285. 13 830 336 0.063 159 68 48 99 91.92 711 3 64 30 97 7 290. 13 525 337 0.528 161 29 49 52 94.15 676. 7 60 97 94 5

-199-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 11.0000 MPa (continued)

T P z H S C

V C

p W 1

A

K mo 1 • dm kJ/mol J/(mol»K) J/(mol-K) m« s

l //Pa*

5 ITiW/(m -K

295. 13.206 .340 1.005 162.92 50.07 96.66 642 .0 57 .74 91 .4

300. 12.870 .343 1.495 164.57 50.64 99.49 607 .1 54 .60 88 .3 310. 12.135 .352 2.523 167.94 51.89 106.36 537 .5 48 .54 82 .2

320. 11.298 .366 3.628 171.45 53.28 115.19 470 .0 42 .71 76 .3 330. 10.336 .388 4.833 175.16 54.74 125.99 408 .8 37 .14 70 .7

340. 9.252 .421 6.148 179.08 56.10 136.35 358 .6 31 .97 65 .5 350. 8.127 .465 7.536 183.11 57.24 139.76 324 .3 27 .58 60 .9 360. 7.106 .517 8.911 186.98 58.16 134.01 306 .6 24 .31 57 .1

370. 6.276 .570 10.201 190.51 58.92 123.71 301 .2 22 .10 54 .3 380. 5.636 .618 11.387 193.68 59.64 113.82 302 .8 20 .67 52 .5

390. 5.141 ,660 12.485 196.53 60.38 106.13 307 .7 19 .74 51 .4 400. 4.749 ,696 13.517 199.14 61.18 100.56 314 ,0 19 ,13 51 .0 410. 4.431 0.,728 14.502 201.58 62.04 96.60 320 ,9 18,,73 51 .0

420. 4.167 0,,756 15.453 203.87 62.96 93.81 327 ,9 18,,47 51 .4

430. 3.943 ,780 16.381 206.05 63.91 91.86 334 ,9 18, 31 52 .0

440. 3.749 0.,802 17.292 208.15 64.91 90.53 341. 8 18, 21 52 .9 450. 3.580 ,821 18.193 210.17 65.93 89.66 348, 5 18. 17 53 ,9

460. 3.431 0.,838 19.087 212.13 66.97 89.14 355, 18. 17 55 ,0

470. 3.297 0.,854 19.977 214.05 68.03 88.89 361, 3 18. 21 56..2 480. 3.176 0,,868 20.865 215.92 69.10 88.85 367. 4 18. 26 57,,5

490. 3.067 0, 880 21.754 217.75 70.17 88.97 373. 4 18. 34 58. 9 500. 2.967 0. 892 22.645 219.55 71.24 89.22 379. 1 18. 43 60. 4

520. 2.790 0, 912 24.437 223.07 73.40 90.02 390. 2 63. 5 540. 2.638 0. 929 26.248 226.48 75.53 91.09 400. 7 66. 8 560. 2.505 0. 943 28.082 229.82 77.65 92.36 410. 7 70. 2

580. 2.388 0. 955 29.943 233.08 79.73 93.74 420. 2 73. 8 600. 2.284 0. 966 31.832 236.29 81.79 95.21 429. 3 77. 4

625. 2.168 0. 977 34.236 240.21 84.30 97.12 440. 2

200
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 12.0000 MPa

T P z H

< C

V C

p W n

A

K mo!L«dm kJ/mol J/(mol«K) J/(mol«K) m»s

i /LiPa«S IT! :W/(m-•K

95. 21 .646 .702 -14.101 79 .15 47.89 68.06 2021 .5 1172 .78 257 .3 100. 21 .475 ,672 -13.757 82 .69 48.31 69.59 1989 .1 967 .23 253 .6 105. 21 .302 0..645 -13.407 86 .10 48.19 70.23 1955 .1 813 .16 249 .7 110. 21 .127 0,,621 -13.055 89 .37 47.77 70.37 1920,.3 695 .29 245 .6 115. 20 .953 ,599 -12.704 92 .50 47.21 70.25 1885 .2 603 .30 241 .3

120. 20 .777 ,579 -12.353 95 .48 46.61 70.03 1850 ,1 530 .16 236 .8 125. 20 .602 0,,560 -12.003 98 .34 46.02 69.78 1815,,0 471 .02 232 .3 130. 20 .426 .544 -11.655 101 ,07 45.48 69.55 1780 ,0 422 .44 227 .8 135. 20 .250 0,,528 -11.308 103 ,69 44.99 69.38 1745 .0 381 .98 223 .1 140. 20 .073 0,,514 -10.961 106 ,21 44.57 69.28 1710 ,2 347 .83 218 .4

145. 19 .895 ,500 -10.615 108 .64 44.21 69.24 1675 .3 318 .68 213 .8 150. 19 ,717 0,,488 -10.269 110 .99 43.92 69.27 1640 ,6 293 .52 209 .0 155. 19 .537 0,,477 -9.922 113 .26 43.68 69.37 1605 ,9 271 .59 204 .3 160. 19 ,357 0,,466 -9.575 115 .47 43.49 69.53 1571 ,3 252 ,31 199 ,6

165. 19 .175 0,.456 -9.227 117 .61 43.36 69.75 1536 ,8 235 .23 194 .9

170. 18 .992 0,.447 -8.877 119 .69 43.27 70.02 1502 ,4 219 .97 190 .3 175. 18 .807 0,,439 -8.526 121 .73 43.22 70.35 1468 ,1 206 .25 185 ,6

180. 18 .621 0,,431 -8.174 123 .72 43.21 70.72 1433 ,9 193 .84 181 ,1

185. 18 .432 0,,423 -7.819 125 ,66 43.23 71.14 1399 ,7 182 .56 176 ,5

190. 18 .242 0.,416 -7.462 127 .56 43.29 71.60 1365 ,6 172 .24 172 ,0

195. 18 ,050 0,,410 -7.103 129 ,43 43.38 72.10 1331 ,6 162 ,76 167 ,6

200. 17 ,855 0,,404 -6.741 131 .26 43.50 72.65 1297 ,7 154 .02 163 .2 205. 17 .658 0,,399 -6.377 133 .06 43.64 73.24 1263 .9 145 .92 158 ,9

210. 17 ,459 0. 394 -6.009 134 .83 43.81 73.86 1230.,2 138 .40 154 .6 215. 17 ,256 0,,389 -5.638 136 .58 44.00 74.54 1196, 6 131,.38 150 ,4

220. 17 ,051 0, 385 -5.263 138 ,30 44.22 75.25 1163,.0 124 .82 146 .3 225. 16 ,842 0, 381 -4.885 140 .00 44.47 76.01 1129, 5 118 .67 142 .2 230. 16 ,630 0, 377 -4.503 141 .68 44.73 76.82 1096, 112 .88 138 ,3

235. 16,,414 0, 374 -4.117 143,.34 45.02 77.68 1062,,7 107 .43 134 ,3

240. 16,,193 0, 371 -3.726 144,,99 45.32 78.60 1029. 4 102 ,27 130 ,5

245. 15 ,969 0. 369 -3.331 146,,62 45.65 79.58 996. 1 97,,39 126,,7

250. 15 ,739 0. 367 -2.930 148,,24 46.00 80.62 962. 9 92,,76 123,,0

255. 15,,504 0, 365 -2.525 149,,84 46.37 81.73 929. 7 88,,35 119,,4

260. 15 ,263 0, 364 -2.113 151,,44 46.75 82.92 896. 6 84,,16 115,,9

265. 15 .016 0, 363 -1.695 153,,03 47.16 84.21 863. 4 80, 15 112, 4

270. 14 ,762 0, 362 -1.271 154,,62 47.59 85.59 830. 3 76, 32 109,

275. 14 .500 0. 362 -0.839 156,,20 48.04 87.09 797. 2 72. 64 105, 7 280. 14 ,230 0, 362 -0.400 157,,79 48.50 88.72 764. 69. 11 102, 4

285. 13,,949 0, 363 0.048 159,,37 48.99 90.50 730. 8 65.,72 99. 2 290. 13 ,658 0, 364 0.506 160,,96 49.50 92.46 697. 6 62,,44 96. 1

201
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 12.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol«K) J/(mol«K)

- l m* s ^Pa«

5 ITiW/(m-K

295. 13.355 .366 0.973 162.56 50.03 94.62 664.4 59 .28 93.0

300. 13.038 .369 1.452 164.17 50.59 97.01 631.2 56 .21 90.0

310. 12.356 .377 2.449 167.44 51.77 102.62 565.4 50 .34 84.2

320. 11.596 .389 3.509 170.80 53.07 109.48 501.8 44 .77 78.6

330. 10.745 .407 4.643 174.29 54.43 117.52 443.1 39 .50 73.3

340. 9.803 .433 5.860 177.93 55.76 125.62 393.1 34 .62 68.4

350. 8.810 .468 7.145 181.65 56.94 130.48 355.3 30 .33 64.0

360. 7.851 .511 8.449 185.33 57.98 129.52 331.0 26 .87 60.3

370. 7.008 .557 9.719 188.81 58.90 123.93 318.8 24 .31 57.4

380. 6.312 .602 10.922 192.01 59.74 116.50 315.0 22 .51 55.4

390. 5.752 .643 12.051 194.95 60.55 109.52 316.2 21 ,28 54.0

400. 5.302 ,681 13.117 197.64 61.38 103.88 320.2 20 ,44 53.3

410. 4.934 .713 14.133 200.15 62.25 99.61 325.6 19,.86 53.1

420. 4.629 .742 15.113 202.52 63.15 96.47 331.7 19, 46 53.2

430. 4.370 0..768 16.066 204.76 64.10 94.20 338.0 19, 19 53.6

440. 4.148 0,,791 16.999 206.90 65.09 92.59 344.4 19, 01 54.3

450. 3.954 0,,811 17.919 208.97 66.10 91.48 350.8 18. 90 55.2

460. 3.783 0,,829 18.830 210.97 67.13 90.76 357.1 18. 84 56.2

470. 3.630 0, 846 19.735 212.92 68.17 90.34 363.2 18. 82 57.3

480. 3.494 0. 861 20.637 214.82 69.23 90.15 369.2 18. 84 58.6

490. 3.370 0. 874 21.539 216.68 70.29 90.14 375.1 18. 88 59.9

500. 3.257 0. 886 22.441 218.50 71.36 90.29 380.8 18. 94 61.3

520. 3.058 0. 908 24.252 222.05 73.50 90.92 391.8 64.3

540. 2.888 0. 925 26.080 225.50 75.63 91.86 402.3 67.5

560. 2.740 0. 941 27.928 228.86 77.73 93.02 412.3 70.8

580. 2.609 0. 954 29.802 232.15 79.81 94.33 421.9 74.3

600. 2.493 0. 965 31.702 235.37 81.85 95.73 431.0 77.9

625. 2.365 0. 976 34.118 239.32 84.36 97.58 442.0

202
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 13.0000 MPa

T P z H

< C

V C

p W V

A

K mo!L«dm kJ/mol J/(mol«K) J/(mol»K) m«s

l /^Pa» '. 3 ITiw/o•K

95. 21 .657 .760 -14.062 79 .08 47.89 68.01 2025 .6 1183 .27 257 .7 100. 21 .487 .728 -13.718 82 .61 48.33 69.55 1993 .2 975 .25 254 .1

105. 21 .314 .699 -13.368 86 .02 48.21 70.19 1959 .2 819 .50 250 .2 110. 21 .141 .672 -13.016 89 .29 47.80 70.33 1924 .5 700 .44 246 .0 115. 20 .966 .648 -12.665 92 .42 47.24 70.22 1889 .5 607 .60 241 .8

120. 20 .792 .627 -12.314 95 .40 46.65 69.99 1854 .5 533 .84 237 .4

125. 20 .617 .607 -11.965 98 .25 46.06 69.74 1819 .6 474 .22 232 .9 130. 20 .442 .588 -11.617 100 .98 45.52 69.51 1784 .7 425 .27 228 .3 135. 20 .267 .571 -11.270 103 .60 45.03 69.33 1749 .9 384 .52 223 .7 140. 20 .090 .556 -10.924 106 .12 44.61 69.22 1715 .1 350 .14 219 .1

145. 19 .914 .541 -10.578 108 .55 44.26 69.18 1680 .5 320 .80 214 .4

150. 19 .736 0,,528 -10.232 110 .90 43.96 69.21 1645 .9 295 .49 209 .7 155. 19 ,558 0,,516 -9.885 113 .17 43.72 69.30 1611 .5 273 .44 205 .0 160. 19 .378 ,504 -9.539 115 .37 43.54 69.45 1577 .1 254 .06 200 .3 165. 19 .198 .494 -9.191 117 .51 43.40 69.66 1542 .8 236 .88 195 .7

170. 19 .016 .484 -8.842 119 .59 43.31 69.93 1508 .6 221 .55 191 .0 175. 18 .832 .474 -8.492 121 .62 43.26 70.24 1474 .5 207 .77 186 .4

180. 18 ,647 .466 -8.139 123 .61 43.25 70.60 1440 .5 195 ,31 181 .8 185. 18 ,460 ,458 -7.785 125 .55 43.28 71.01 1406 .6 183 .98 177 .3 190. 18.,272 0,.450 -7.429 127 .45 43.34 71.46 1372 ,9 173 .62 172 .9

195. 18,,081 0,.443 -7.071 129 .31 43.42 71.95 1339 ,2 164 .11 168 .4 200. 17..888 0,.437 -6.710 131 ,14 43.54 72.48 1305 .6 155 .33 164 .1 205. 17.,693 0.,431 -6.346 132 ,94 43.68 73.05 1272 .1 147 ,21 159 .8 210. 17..496 0. 426 -5.979 134 ,70 43.85 73.66 1238 .8 139 ,67 155 ,5

215. 17..295 0..420 -5.609 136 ,44 44.05 74.31 1205 .5 132 64 151 ,4

220. 17,.092 0..416 -5.236 138,,16 44.27 75.01 1172 3 126, 06 147,,3

225. 16,,886 0.,412 -4.859 139,,85 44.51 75.74 1139.,2 119, 90 143, 2 230. 16, 677 0,,408 -4.478 141,,53 44.77 76.52 1106.,3 114, 10 139, 3 235. 16,.464 0. 404 -4.094 143,,18 45.06 77.35 1073. 4 108, 65 135. 4

240. 16,.247 0, 401 -3.705 144,,82 45.36 78.23 1040, 6 103, 49 131, 6

245. 16,,026 0. 398 -3.311 146,,44 45.69 79.16 1007, 9 98, 61 127, 8 250. 15, 801 0. 396 -2.913 148, 05 46.04 80.14 975, 3 93. 98 124, 2 255. 15,,571 0..394 -2.510 149, 65 46.40 81.20 942. 8 89. 59 120. 6

260. 15, 335 0. 392 -2.101 151. 24 46.79 82.32 910. 4 85. 40 117. 1 265. 15, 094 0. 391 -1.687 152. 81 47.19 83.52 878. 81. 41 113. 6

270. 14, 847 0, 390 -1.266 154. 39 47.61 84.80 845. 7 77. 60 110. 3 275. 14, 593 0,.390 -0.838 155. 96 48.05 86.18 813. 5 73. 95 107.

280. 14,.331 0,,390 -0.404 157, 52 48.51 87.66 781. 3 70. 45 103. 8 285. 14,,061 0, 390 0.038 159, 09 48.99 89.27 749. 2 67. 09 100. 7 290. 13,.781 0, 391 0.489 160. 66 49.49 91.01 717. 2 63. 86 97. 6

203
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 13.0000 MPa (continued)

T P Z H S C

V C

p W n A

K mol»dm kJ/mol J/(mol»K) J/(mol«K) m»s

l //Pa«s itiW/(m.K

295. 13.492 0.393 0.949 162.23 50.01 92.91 685 .3 60 .74 94.6

300. 13.191 0.395 1.419 163.81 50.55 94.98 653 .6 57 .73 91.7

310. 12.550 0.402 2.391 166.99 51.69 99.70 590 .8 52 .00 86.0

320. 11.849 0.412 3.415 170.25 52.92 105.27 530 .3 46 .61 80.7

330. 11.078 0.428 4.499 173.58 54.21 111.59 474 .0 41 .57 75.6

340. 10.239 0.449 5.648 177.01 55.50 118.03 424 .8 36 .91 70.9

350. 9.351 0.478 6.855 180.51 56.71 122.86 385 .2 32 .74 66.7

360. 8.468 0.513 8.093 183.99 57.81 124.06 356 .9 29 .23 63.2

370. 7.650 0.552 9.323 187.37 58.82 121.60 339 .5 26 .46 60.3

380. 6.937 0.593 10.517 190.55 59.75 116.83 330 .7 24 .39 58.0

390. 6.338 0.633 11.658 193.51 60.64 111.32 328 .0 22 ,90 56.5

400. 5.843 0.669 12.745 196.27 61.51 106.23 329 .1 21 ,83 55.6

410. 5.432 0.702 13.785 198.83 62.40 102.02 332 .6 21 ,06 55.1

420. 5.088 0.732 14.788 201.25 63.32 98.75 337 ,2 20 ,52 55.0

430. 4.796 0.758 15.763 203.55 64.27 96.28 342 ,6 20 ,13 55.3

440. 4.546 0.782 16.716 205.74 65.24 94.47 348 ,3 19, 86 55.8

450. 4.327 0.803 17.654 207.84 66.25 93.17 354 ,2 19. 67 56.6

460. 4.135 0.822 18.581 209.88 67.27 92.28 360 ,1 19. 55 57.5

470. 3.964 0.839 19.501 211.86 68.31 91.71 366. 19. 48 58.5

480. 3.811 0.855 20.416 213.79 69.36 91.39 371. 8 19. 45 59.6

490. 3.673 0.869 21.329 215.67 70.41 91.28 377. 5 19. 45 60.9

500. 3.547 0.882 22.242 217.51 71.47 91.32 383. 1 19. 48 62.2

520. 3.326 0.904 24.072 221.10 73.60 91.79 394. 65.1

540. 3.137 0.923 25.916 224.58 75.72 92.61 404. 3 68.2

560. 2.974 0.939 27.778 227.97 77.81 93.67 414. 3 71.5

580. 2.830 0.953 29.664 231.28 79.88 94.90 423. 8 74.9

600. 2.702 0.964 31.575 234.52 81.92 96.24 433. 78.4

625. 2.561 0.977 34.003 238.48 84.42 98.02 444.

204
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 14.0000 MPa

T P z H

<

( V C

p W V A

K mo"L«dm kJ/mol J/(mol'K) J/(mol-K) m« s

-

ptPa*

5 ITiW/(m •K

95. 21 .669 .818 -14.023 79 .01 47 .88 67.96 2029 .7 1193 .92 258 .2

100. 21 .499 .783 -13.678 82 .54 48 .34 69.51 1997 .3 983 .37 254 .5 105. 21 .327 .752 -13.329 85 .95 48 .24 70.16 1963 .3 825 .90 250 .6 110. 21 .154 .724 -12.978 89 .22 47 .83 70.30 1928 .7 705 .65 246 .5 115. 20 .980 .698 -12.626 92 .34 47 .28 70.18 1893 .8 611 .94 242 .3

120. 20 .806 .674 -12.276 95 .32 46 .68 69.95 1858 .9 537 .54 237 .9 125. 20 .632 .653 -11.927 98 .17 46 .10 69.70 1824 .1 477 .44 233 .4

130. 20 .458 .633 -11.579 100 .90 45 .56 69.47 1789 .3 428 .12 228 .9 135. 20 .283 .615 -11.232 103 .52 45 .08 69.29 1754 .6 387 .08 224 .3 140. 20 .108 .598 -10.886 106 .04 44 .66 69.17 1720 .1 352 .47 219 .7

145. 19 .932 .583 -10.540 108 .46 44 .30 69.12 1685 .6 322 .94 215 .0

150. 19 .755 .568 -10.195 110 .81 44 .00 69.14 1651 .2 297 .47 210 .3 155. 19 .578 .555 -9.849 113 .07 43 .77 69.23 1616 .9 275 .30 205 .7 160. 19 .399 .542 -9.502 115 .27 43 .58 69.37 1582 .8 255 .81 201 .0 165. 19 .220 .531 -9.155 117 .41 43 .45 69.58 1548 .7 238 .54 196 .4

170. 19 .039 .520 -8.806 119 .49 43 .36 69.83 1514 .7 223 .13 191 .7 175. 18 .857 .510 -8.457 121 .52 43 .31 70.14 1480 .9 209 .29 187 .1 180. 18 .673 .501 -8.105 123 .50 43 .30 70.49 1447 .1 196 .77 182 .6 185. 18 .488 ,492 -7.752 125 .44 43 .32 70.89 1413 .5 185 .39 178 .1 190. 18 .301 ,484 -7.396 127 .34 43 .38 71.33 1380 .0 174 .99 173 .7

195. 18 ,112 0,,477 -7.038 129 ,19 43 .47 71.81 1346 .6 165 .45 169 .3 200. 17 .920 0,,470 -6.678 131.,02 43 .58 72.32 1313 ,4 156 65 164 .9 205. 17 ,727 0,,463 -6.315 132.,81 43 ,73 72.88 1280 ,2 148,.50 160 ,6

210. 17 ,532 0, 457 -5.949 134,.57 43 ,90 73.47 1247 ,2 140, 94 156 ,4

215. 17.,334 0,.452 -5.580 136,,31 44.,09 74.10 1214, 3 133, 89 152 ,3

220. 17,,133 0, 447 -5.208 138,,02 44,,31 74.77 1181, 5 127. 30 148 ,2

225. 16.,929 0, 442 -4.832 139. 71 44,,55 75.48 1148, 8 121. 12 144. 2 230. 16. 723 0. 438 -4.453 141. 38 44,,82 76.24 1116, 3 115. 32 140. 2 235. 16. 513 0. 434 -4.070 143. 02 45, 10 77.03 1083. 9 109. 86 136. 4

240. 16. 299 0. 430 -3.683 144. 66 45, 40 77.87 1051. 6 104. 70 132. 6

245. 16. 082 0. 427 -3.291 146. 27 45. 73 78.76 1019. 4 99. 82 128. 9

250. 15. 861 0. 425 -2.895 147. 87 46. 07 79.70 987. 4 95. 19 125. 3 255. 15. 635 0. 422 -2.494 149. 46 46. 44 80.70 955. 5 90. 80 121. 7 260. 15. 405 0. 420 -2.088 151. 04 46. 82 81.76 923. 7 86. 63 118. 2 265. 15. 169 0. 419 -1.676 152. 60 47. 22 82.89 892. 82. 65 114. 8

270. 14. 928 0. 418 -1.259 154. 16 47. 64 84.08 860. 5 78. 85 111. 5 275. 14. 681 0. 417 -0.835 155. 72 48. 08 85.36 829. 75. 22 108. 3 280. 14. 427 0. 417 -0.405 157. 27 48. 53 86.73 797. 8 71. 75 105. 1 285. 14. 165 0. 417 0.032 158. 82 49. 00 88.19 766. 6 68. 42 102.

290. 13. 896 0. 418 0.477 160. 36 49. 50 89.76 735. 7 65. 21 99.

205
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 14.0000 MPa (continued)

T P z H S C

V C

p W 1

A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol«K) m» s

l /iPa»

; niW/(m<K

295. 13.619 .419 0.930 161.91 50.00 91.45 704 .9 62 .14 96 .1

300. 13.331 .421 1.392 163.46 50.53 93.27 674 .3 59 .17 93 .2

310. 12.725 .427 2.344 166.59 51.64 97.35 614 .2 53 .55 87 .7 320. 12.069 .436 3.341 169.75 52.82 102.02 556 .3 48 .31 82 .5 330. 11.360 .449 4.386 172.97 54.06 107.19 502 .1 43 .43 77 .7

340. 10.597 .467 5.485 176.25 55.31 112.46 453 .8 38 ,93 73 .2 350. 9.793 .491 6.633 179.57 56.52 116.86 413 .5 34 .88 69 .2 360. 8.980 .521 7.814 182.90 57.65 118.97 382 .8 31 .38 65 .7 370. 8.204 .555 9.003 186.16 58.72 118.33 361 .6 28 .50 62 .8 380. 7.499 .591 10.174 189.28 59.72 115.59 348 .8 26 .25 60 .5

390. 6.884 0..627 11.311 192.24 60.67 111.68 342 ,3 24 ,54 58 .9 400. 6.359 0..662 12.407 195.01 61.59 107.52 340 ,4 23 ,26 57 .8 410. 5.915 .694 13.462 197.62 62.51 103.72 341 6 22, 32 57 .1 420. 5.539 0.,724 14.483 200.08 63.45 100.55 344 ,6 21. 63 56 .9 430. 5.217 0.,751 15.476 202.41 64.40 98.04 348.,7 21..13 57 .0

440. 4.940 0,,775 16.446 204.64 65.38 96.12 353, 5 20. 76 57 ,4

450. 4.698 0,,796 17.400 206.79 66.38 94.69 358, 7 20. 49 58..0 460. 4.485 0, 816 18.341 208.86 67.40 93.67 364. 1 20. 30 58..7 470. 4.296 0. 834 19.274 210.86 68.43 92.98 369, 6 20. 17 59..7 480. 4.127 0, 850 20.202 212.82 69.47 92.56 375. 1 20. 09 60. 7

490. 3.974 0. 865 21.126 214.72 70.52 92.34 380. 6 20. 05 61. 9 500. 3.836 0. 878 22.049 216.59 71.58 92.31 386. 20. 04 63. 2 520. 3.592 0. 901 23.898 220.21 73.69 92.63 396. 6 65. 9 540. 3.385 0. 921 25.757 223.72 75.80 93.33 406. 8 69.

560. 3.206 0. 938 27.633 227.13 77.89 94.30 416. 7 72. 2

580. 3.049 0. 952 29.530 230.46 79.95 95.46 426. 1 75. 5 600. 2.910 0. 964 31.452 233.72 81.98 96.74 435. 3 78. 9 625. 2.757 0. 977 33.892 237.70 84.48 98.45 446. 2

206
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 15.0000 MPa

T P z H C

V

( p W *l A

K mo L«dm kJ/mol J/(mol«K) J/(mol»K) m« s

l jj-Fa* : 3 IT W/(m •K

95. 21 .680 .876 -13.983 78 .94 47.88 67 91 2033 8 1204 71 258 .6 100. 21 .511 .839 -13.639 82 .46 48.35 69 .47 2001 4 991 59 255

105. 21 .339 .805 -13.290 85 .87 48.26 70 12 1967 4 832 38 251 .1 110. 21 .167 775 -12.939 89 .14 47.86 70 27 1932 8 710 91 247

115. 20 .994 .747 -12.588 92 .26 47.31 70 15 1898 1 616 32 242 8

120. 20 .821 722 -12.238 95 .24 46.72 69 92 1863 3 541 27 238 4

125. 20 647 699 -11.889 98 .09 46.14 69 66 1828 6 480 68 234

130. 20 474 678 -11.541 100 .82 45.60 69 43 1793 9 430 99 229 .5 135. 20 300 658 -11.194 103 .43 45.12 69 24 1759 4 389 65 224 .9 140. 20 125 640 -10.848 105 95 44.70 69 12 1725 354 81 220 3

145. 19 950 624 -10.503 108 37 44.34 69 07 1690 7 325 09 215 6 150. 19 775 608 -10.158 110 72 44.05 69 08 1656 5 299 47 211

155. 19 598 594 -9.812 112 98 43.81 69 16 1622 4 277 16 206 3 160. 19 420 581 -9.466 115 18 43.62 69 30 1588 4 257 56 201 7 165. 19 242 568 -9.119 117 31 43.49 69 50 1554 5 240 21 197 1

170. 19 062 557 -8.771 119 39 43.40 69 75 1520 8 224 72 192 5 175. 18 881 546 -8.421 121 42 43.35 70 04 1487 2 210 81 187 9

180. 18 699 536 -8.070 123 40 43.34 70 39 1453 7 198 24 183 4

185. 18 515 527 -7.718 125 33 43.37 70 77 1420 3 186 81 178 9 190. 18 329 518 -7.363 127 22 43.42 71 20 1387 1 176 37 174 5

195. 18 142 510 -7.005 129 08 43.51 71 66 1354 166 79 170 1 200. 17 952 502 -6.646 130 90 43.63 72 17 1321 157 96 165 8 205. 17 761 495 -6.284 132 69 43.77 72 71 1288 2 149 79 161 5 210. 17 567 489 -5.919 134 45 43.94 73 29 1255 5 142 20 157 3 215. 17 371 483 -5.551 136 18 44.14 73 90 1222 9 135 13 153 2

220. 17 173 478 -5.180 137 88 44.35 74 55 1190 5 128 53 149 1 225. 16 972 472 -4.805 139 57 44.60 75 24 1158 2 122 34 145 1 230. 16 768 468 -4.427 141 23 44.86 75 96 1126 1 116 53 141 2 235. 16 561 464 -4.046 142 87 45.14 76 73 1094 1 111 06 137 4

240. 16 350 460 -3.660 144 49 45.45 77 54 1062 3 105 89 133 6

245. 16 137 456 -3.270 146 10 45.77 78 39 1030 6 101 01 129 9 250. 15 919 453 -2.876 147 70 46.11 79 29 999 1 96 39 126 3 255. 15 697 451 -2.477 149 27 46.47 80 24 967 7 92 01 122 8 260. 15 472 448 -2.073 150 84 46.85 81 25 936 5 87 84 119 4

265. 15 241 447 -1.665 152 40 47.25 82 31 905 5 83 87 116

270. 15 006 445 -1.250 153 95 47.67 83 43 874 7 80 08 112 7 275. 14 765 444 -0.830 155 49 48.10 84 62 844 76 47 109 5 280. 14 518 444 -0.404 157 03 48.55 85 89 813 5 73 01 106 4

285. 14 265 444 0.029 158 56 49.02 87 24 783 2 69. 70 103 4

290. 14 005 444 0.469 160 09 49.50 88. 67 753 2 66 53 100 4

207
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P= 15.0000 MPa (continued)

T P Z H S C

V C

p W 1

X

K mol«dm kJ/mol J/(mol«K) J/(mol-K) m« s

l fiFa»s it W/(m K

295. 13.737 0.445 0.916 161.62 50.00 90.19 723 4 63 48 97 5 300. 13.461 0.447 1.371 163.15 50.52 91.82 693 9 60 55 94 7 310. 12.884 0.452 2.307 166.21 51.61 95.40 636 55 02 89 4

320. 12.266 0.460 3.280 169.31 52.75 99.41 580 2 49 89 84 3 330. 11.605 0.471 4.296 172.43 53.95 103.77 528 45 14 79 6

340. 10.901 0.487 5.356 175.59 55.17 108.20 480 8 40 76 75 3 350. 10.163 0.507 6.458 178.79 56.37 112.11 440 3 36 81 71 4

360. 9.412 0.532 7.593 181.99 57.52 114.56 407 9 33 34 68

370. 8.680 0.562 8.743 185.14 58.62 114.98 384 1 30 41 65 1 380. 7.996 0.594 9.887 188.19 59.66 113.60 368 1 28 03 62 8

390. 7.382 0.627 11.011 191.11 60.67 111.03 358 5 26 16 61 1 400. 6.842 0.659 12.105 193.88 61.64 107.88 353 7 24 72 59 9 410. 6.376 0.690 13.168 196.50 62.59 104.69 352 4 23 62 59 1 420. 5.974 0.719 14.200 198.99 63.54 101.82 353 5 22 79 58 7 430. 5.628 0.746 15.206 201.36 64.51 99.41 356 2 22 16 58 7

440. 5.327 0.770 16.190 203.62 65.50 97.49 360 21 69 58 9 450. 5.064 0.792 17.158 205.79 66.50 96.01 364 3 21 34 59 4

460. 4.832 0.812 18.112 207.89 67.51 94.92 369 1 21 08 60 1 470. 4.625 0.830 19.057 209.92 68.54 94.14 374 1 20 89 60 9 480. 4.440 0.846 19.996 211.90 69.58 93.63 379 2 20 76 61 9

490. 4.273 0.862 20.930 213.83 70.63 93.34 384 3 20 67 63

500. 4.122 0.875 21.863 215.71 71.68 93.23 389 5 20 62 64 2 520. 3.857 0.900 23.729 219.37 73.78 93.42 399 7 66 8 540. 3.632 0.920 25.603 222.91 75.88 94.02 409 7 69 7 560. 3.437 0.937 27.492 226.34 77.96 94.91 419 4 72 8

580. 3.267 0.952 29.400 229.69 80.02 95.99 428 8 76 1 600. 3.116 0.965 31.332 232.96 82.05 97.21 437 8 79 5 625. 2.950 0.978 33.783 236.97 84.53 98.87 448 7

208
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 16.0000 MPa

T P z H

< C

V C

p W V A

K mo'[•dm kJ/mol J/(mol-K) J/(mol»K) m* s

-

^Pa«

3 IT W/(m •K

95. 21 .692 .934 -13.944 78 .86 47.88 67.86 2037 9 1215 .66 259 .0

100. 21 .523 .894 -13.600 82 .39 48.37 69.43 2005 .5 999 .92 255 .4

105. 21 .352 .858 -13.251 85 .80 48.28 70.09 1971 5 838 .93 251 .6

110. 21 .180 826 -12.900 89 06 47.89 70.24 1937 716 .21 247 .5 115. 21 .008 .797 -12.549 92 18 47.35 70.12 1902 3 620 .74 243 .3

120. 20 835 770 -12.199 95 16 46.76 69.88 1867 6 545 03 239 .0

125. 20 662 745 -11.850 98 01 46.18 69.62 1833 483 95 234 .5 130. 20 489 722 -11.503 100 73 45.64 69.39 1798 5 433 88 230 .0

135. 20 316 702 -11.156 103 35 45.16 69.20 1764 1 392 24 225 .5 140. 20 143 682 -10.811 105 86 44.74 69.07 1729 9 357 .15 220 .9

145. 19 968 665 -10.466 108 29 44.38 69.01 1695 7 327 24 216 3 150. 19 793 648 -10.121 110 63 44.09 69.02 1661 7 301 46 211 6

155. 19 618 633 -9.775 112 89 43.85 69.09 1627 8 279 03 207

160. 19 441 619 -9.430 115 09 43.67 69.23 1594 259 32 202 .4 165. 19 264 605 -9.083 117 22 43.53 69.42 1560 3 241 88 197 8

170. 19 085 593 -8.735 119 29 43.44 69.66 1526 8 226 31 193 2 175. 18 905 582 -8.386 121 32 43.39 69.95 1493 4 212 34 188 6 180. 18 724 571 -8.036 123 29 43.38 70.28 1460 2 199 71 184 1

185. 18 541 561 -7.683 125 22 43.41 70.66 1427 188 23 179 7 190. 18 357 552 -7.329 127 11 43.47 71.07 1394 1 177 75 175 2

195. 18 171 543 -6.973 128 96 43.55 71.53 1361 2 168 13 170 9 200. 17 984 535 -6.614 130 78 43.67 72.02 1328 5 159 27 166 6

205. 17 794 528 -6.252 132 57 43.82 72.55 1296 151 07 162 3 210. 17 602 521 -5.888 134 32 43.99 73.11 1263 6 143 46 158 2 215. 17 408 514 -5.521 136 05 44.18 73.70 1231 4 136 37 154 1

220. 17 212 508 -5.151 137 75 44.40 74.34 1199 3 129 75 150

225. 17 013 503 -4.778 139 43 44.64 75.00 1167 4 123 55 146 1 230. 16 812 498 -4.401 141 08 44.90 75.71 1135 7 117 73 142 2 235. 16 607 493 -4.021 142 72 45.18 76.45 1104 1 112 25 138 4

240. 16 400 489 -3.637 144 34 45.49 77.23 1072 7 107 08 134 6

245. 16 189 485 -3.248 145 94 45.81 78.05 1041 5 102 20 131

250. 15 975 482 -2.856 147 52 46.15 78.91 1010 5 97 58 127 4

255. 15 758 479 -2.459 149 10 46.51 79.82 979 7 93 19 123 9

260. 15 536 476 -2.058 150 65 46.89 80.77 949 89 03 120 5 265. 15 310 474 -1.651 152 20 47.29 81.78 918 6 85 06 117 2

270. 15 080 473 -1.240 153 74 47.70 82.84 888. 4 81 29 113 9

275. 14 845 471 -0.823 155 27 48.13 83.95 858. 4 77 69 110 8

280. 14 605 471 -0.400 156 79 48.58 85.13 828. 6 74 25 107 7 285. 14 359 470 0.029 158. 31 49.04 86.38 799 1 70 96 104 7 290. 14 107 470 0.464 159. 83 49.52 87.70 769 8 67 81 101 8

-209
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 16.0000 MPa (continued)

T P Z H S C

V C

p W V A

K mol«dm kJ/mol J/(mol»K) J/(mol«K) m«s

l /iPa* <5 IIiW/(m«K

295. 13.848 0.471 0.906 161.34 50.01 89.09 740 .9 64 .78 98.9

300. 13.583 0.472 1.355 162.85 50.52 90.57 712 .3 61 .88 96.2

310. 13.030 0.476 2.276 165.87 51.58 93.76 656 .3 56 .42 90.9

320. 12.443 0.483 3.231 168.90 52.70 97.28 602 .5 51 .38 86.0

330. 11.821 0.493 4.222 171.95 53.87 101.04 551 .9 46 .72 81.4

340. 11.165 0.507 5.252 175.02 55.07 104.85 505 .8 42 .45 77.2

350. 10.480 0.525 6.318 178.11 56.26 108.32 465 .5 38 .57 73.4

360. 9.782 0.546 7.415 181.20 57.41 110.82 432 .2 35 .14 70.1

370. 9.092 0.572 8.530 184.26 58.53 111.84 406 .4 32 .18 67.3

380. 8.436 0.600 9.647 187.24 59.60 111.37 388 .0 29 .73 65.0

390. 7.831 0.630 10.754 190.11 60.64 109.80 375 ,7 27 .74 63.2

400. 7.289 0.660 11.841 192.86 61.65 107.56 368 .3 26 .16 61.9

410. 6.810 0.689 12.904 195.49 62.64 105.04 364 .7 24 .92 61.0

420. 6.390 0.717 13.942 197.99 63.62 102.59 363 .9 23 .96 60.5

430. 6.024 0.743 14.956 200.38 64.60 100.40 365 .1 23 ,22 60.3

440. 5.703 0.767 15.951 202.66 65.59 98.57 367 6 22,,65 60.4

450. 5.421 0.789 16.929 204.86 66.60 97.11 371. 22,,22 60.8

460. 5.171 0.809 17.894 206.98 67.61 95.99 375. 21, 88 61.4

470. 4.949 0.827 18.850 209.04 68.64 95.17 379, 4 21, 63 62.1

480. 4.749 0.844 19.799 211.04 69.68 94.60 384. 21. 45 63.0

490. 4.569 0.860 20.743 212.98 70.72 94.25 388, 8 21. 32 64.0

500. 4.405 0.874 21.684 214.88 71.77 94.08 393, 6 21. 23 65.2

520. 4.119 0.898 23.566 218.57 73.87 94.17 403. 4 67.7

540. 3.876 0.919 25.454 222.14 75.96 94.68 413. 70.5

560. 3.666 0.937 27.355 225.59 78.03 95.49 422. 5 73.5

580. 3.483 0.953 29.274 228.96 80.08 96.50 431. 7 76.7

600. 3.321 0.966 31.216 232.25 82.11 97.67 440. 6 80.1

625. 3.143 0.980 33.678 236.27 84.59 99.27 451. 4

-210-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 17.0000 MPa

T P z H

< ( V C

p W V

A

K mo'L«dm kJ/mol J/(mol-K) J/(mol«K) m« s

l /iPa«

3 ITiW/(m<•K

95. 21 .703 .992 -13.905 78 .79 47 .88 67.81 2042 .0 1226 .77 259 .4

100. 21 .534 .949 -13.561 82 .32 48 .38 69.39 2009 .5 1008 .35 255 .9 105. 21 .364 .911 -13.212 85 .72 48 .31 70.05 1975 .6 845 .55 252 .0

110. 21 .193 .877 -12.861 88 .98 47 .92 70.20 1941 .1 721 .58 248 .0

115. 21 .021 .846 -12.511 92 .10 47 .38 70.09 1906 .5 625 .20 243 .8

120. 20 .849 .817 -12.161 95 .08 46 .80 69.85 1871 .9 548 .83 239 .5 125. 20 .677 .791 -11.812 97 .93 46 .22 69.59 1837 .4 487 .24 235 .1

130. 20 .505 .767 -11.465 100 .65 45 .68 69.35 1803 .1 436 .78 230 .6 135. 20 .332 .745 -11.119 103 .27 45 .20 69.15 1768 .8 394 .84 226 .1 140. 20 .160 ,724 -10.773 105 .78 44 .78 69.02 1734 .7 359 .52 221 .5

145. 19 .986 .706 -10.428 108 .20 44 .42 68.96 1700 .7 329 .41 216 .9 150. 19 .812 .688 -10.083 110 .54 44 .13 68.96 1666 .9 303 .47 212 .3 155. 19 .638 .672 -9.739 112 .80 43 .89 69.03 1633 .2 280 .90 207 .7 160. 19 .462 ,657 -9.393 114 .99 43 .71 69.16 1599 ,6 261 .09 203 .0 165. 19 .286 .643 -9.047 117 ,12 43 .57 69.34 1566 .1 243 .55 198 .5

170. 19 .108 .629 -8.700 119 .20 43 .48 69.57 1532 .8 227 .91 193 .9 175. 18 .929 0.,617 -8.351 121 ,22 43 .44 69.86 1499 ,6 213 .86 189 .3 180. 18 .749 ,606 -8.001 123 ,19 43 .43 70.18 1466 ,6 201 .18 184 ,9

185. 18 .568 0,,595 -7.649 125,,12 43 .45 70.55 1433 ,7 189 .65 180 ,4

190. 18 .385 0,,585 -7.295 127,,00 43 .51 70.95 1401 ,0 179 ,13 176 .0

195. 18 ,201 0,,576 -6.940 128 ,85 43 .60 71.40 1368, 4 169 .47 171 ,7

200. 18 .014 0, 567 -6.581 130,,67 43 .71 71.88 1336,.0 160 ,58 167 ,4

205. 17.,826 0,,559 -6.221 132,.45 43 .86 72.39 1303 7 152 ,35 163..2 210. 17 ,636 0, 552 -5.857 134, 20 44 ,03 72.94 1271 7 144.,72 159.,0

215. 17..444 0. 545 -5.491 135,.92 44 ,22 73.52 1239, 7 137 ,61 154 9

220. 17.,250 0, 539 -5.122 137. 62 44 ,44 74.13 1208 130 ,97 150 .9 225. 17.,054 0, 533 -4.750 139, 29 44 ,68 74.78 1176. 5 124 ,75 147.

230. 16.,855 0, 527 -4.374 140, 94 44.,94 75.46 1145. 1 118 ,92 143,.1 235. 16.,653 0. 522 -3.995 142, 57 45, 22 76.18 1113. 9 113. 43 139..3 240. 16,,448 0. 518 -3.613 144, 18 45, 53 76.93 1083, 108, 26 135..6

245. 16..241 0. 514 -3.226 145. 78 45, 85 77.72 1052. 2 103. 37 132.

250. 16, 030 0. 510 -2.835 147, 36 46, 19 78.55 1021. 6 98, 75 128. 4

255. 15, 816 0. 507 -2.440 148. 92 46, 55 79.42 991. 3 94, 36 125.

260. 15. 599 0. 504 -2.041 150. 47 46, 93 80.33 961. 2 90, 20 121. 6 265. 15. 377 0. 502 -1.637 152. 01 47. 32 81.28 931. 3 86. 25 118. 3

270. 15. 152 0. 500 -1.228 153. 54 47, 73 82.29 901. 6 82. 48 115. 1 275. 14. 922 0. 498 -0.814 155. 06 48. 16 83.34 872. 3 78. 89 112.

280. 14. 688 0. 497 -0.395 156. 57 48. 60 84.45 843. 1 75. 46 108. 9

285. 14. 448 0. 497 0.031 158. 08 49. 06 85.61 814. 3 72. 18 105. 9 290. 14. 203 0. 496 0.462 159. 57 49. 53 86.83 785. 8 69. 05 103. 1

-211-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 17.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol«dm kJ/mol J/(mol«K) J/(mol«K) m* s

l ^Pa«s it W/(m •K

295. 13.953 497 0.899 161.07 50.02 88.12 757 6 66 05 100 3 300. 13.697 498 1.343 162.56 50.53 89.46 729 8 63 17 97 6 310. 13.165 501 2.252 165.54 51.57 92.35 675 4 57 77 92 4

320. 12.605 507 3.191 168.52 52.67 95.49 623 3 52 79 87 6 330. 12.016 516 4.162 171.51 53.82 98.80 574 2 48 21 83 1

340. 11.399 528 5.167 174.51 54.99 102.14 529 2 44 01 79

350. 10.758 543 6.204 177.52 56.17 105.23 489 2 40 20 75 3 360. 10.103 562 7.269 180.52 57.32 107.67 455 4 36 81 72

370. 9.453 585 8.354 183.49 58.45 109.02 428 3 33 85 69 3 380. 8.825 610 9.446 186.40 59.55 109.16 407 9 31 33 66 9

390. 8.236 637 10.534 189.23 60.61 108.32 393 4 29 26 65 1 400. 7.698 664 11.610 191.95 61.65 106.80 383 8 27 57 63 7 410. 7.214 691 12.668 194.57 62.66 104.91 378 1 26 22 62 8 420. 6.783 718 13.708 197.07 63.67 102.91 375 5 25 14 62 2 430. 6.402 743 14.727 199.47 64.67 101.02 375 1 24 30 61 9

440. 6.066 766 15.729 201.77 65.67 99.36 376 3 23 64 61 9 450. 5.768 788 16.715 203.99 66.68 97.97 378 6 23 12 62 2 460. 5.502 808 17.689 206.13 67.70 96.88 381 8 22 71 62 7 470. 5.265 826 18.654 208.20 68.73 96.05 385 5 22 40 63 3 480. 5.052 843 19.611 210.22 69.77 95.45 389 5 22 16 64 2

490. 4.860 859 20.563 212.18 70.81 95.07 393 9 21 98 65 1 500. 4.684 873 21.513 214.10 71.85 94.85 398 3 21 85 66 2 520. 4.378 898 23.409 217.82 73.95 94.86 407 5 68 6

540. 4.118 920 25.310 221.41 76.03 95.29 416 8 71 3 560. 3.893 938 27.223 224.89 78.10 96.03 425 9 74 2

580. 3.697 954 29.153 228.27 80.15 96.99 434 9 77 4

600. 3.524 967 31.104 231.58 82.16 98.11 443 7 80 6

625. 3.333 981 33.576 235.61 84.64 99.66 454 4

212
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 18.0000 MPa

T P z H

< C

V C

p W n

A

K mo' .•dm kJ/mol J/(mol-K) J/(mol-K) m»s

l /iPa*

3 IT W/(m •K

95. 21 .714 10 049 -13.865 78 .72 47.88 67.76 2046 1 1238 .04 259 .8 100. 21 .546 10 005 -13.522 82 .24 48.40 69.35 2013 5 1016 .88 256 .3 105. 21 .376 965 -13.173 85 65 48.33 70.02 1979 6 852 .24 252 5 110. 21 .206 928 -12.823 88 .91 47.95 70.17 1945 2 726 .99 248 5 115. 21 .035 895 -12.472 92 03 47.42 70.06 1910 7 629 .70 244 3

120. 20 863 865 -12.122 95 00 46.83 69.82 1876 2 552 .65 240

125. 20 692 837 -11.774 97 85 46.26 69.55 1841 9 490 .55 235 6 130. 20 521 812 -11.427 100 57 45.72 69.31 1807 6 439 71 231 2 135. 20 349 788 -11.081 103 18 45.24 69.11 1773 5 397 46 226 6 140. 20 177 766 -10.735 105 69 44.82 68.98 1739 6 361 89 222 1

145. 20 004 746 -10.391 108 11 44.47 68.91 1705 7 331 59 217 5 150. 19 831 728 -10.046 110 45 44.17 68.91 1672 305 49 212 9

155. 19 657 711 -9.702 112 71 43.93 68.97 1638 5 282 79 208 3 160. 19 482 694 -9.357 114 90 43.75 69.09 1605 1 262 86 203 7 165. 19 307 680 -9.011 117 03 43.62 69.26 1571 8 245 23 199 1

170. 19 131 666 -8.664 119 10 43.53 69.49 1538 7 229 51 194 6

175. 18 953 653 -8.316 121 12 43.48 69.76 1505 7 215 39 190 1 180. 18 774 641 -7.966 123 09 43.47 70.08 1472 9 202 65 185 6 185. 18 594 629 -7.615 125 01 43.49 70.44 1440 3 191 07 181 2 190. 18 412 619 -7.262 126 90 43.55 70.84 1407 8 180 50 176 8

195. 18 229 609 -6.906 128 74 43.64 71.27 1375 5 170 81 172 5 200. 18 045 600 -6.549 130 55 43.76 71.74 1343 3 161 88 168 2 205. 17 858 591 -6.189 132 33 43.90 72.24 1311 4 153 63 164

210. 17 670 583 -5.826 134 08 44.07 72.77 1279 6 145 97 159 9

215. 17 480 576 -5.461 135 79 44.27 73.34 1248 138 84 155 8

220. 17 288 569 -5.093 137 49 44.48 73.94 1216 6 132 18 151 8

225. 17 093 563 -4.722 139 16 44.72 74.56 1185 4 125 95 147 9

230. 16 897 557 -4.347 140 80 44.98 75.23 1154 4 120 11 144 1 235. 16 698 552 -3.969 142 43 45.27 75.92 1123 6 114 61 140 3 240. 16 496 547 -3.588 144 03 45.57 76.65 1093 109 43 136 6

245. 16 291 542 -3.203 145 62 45.89 77.41 1062 6 104 54 133

250. 16 084 538 -2.814 147 19 46.23 78.21 1032 5 99 91 129 5 255. 15 873 535 -2.421 148 75 46.59 79.04 1002 6 95 52 126

260. 15 660 532 -2.023 150 29 46.96 79.92 973 91 36 122 7 265. 15 442 529 -1.622 151 82 47.36 80.83 943 6 87 41 119 4

270. 15 221 527 -1.215 153 34 47.76 81.78 914 5 83 65 116 2 275. 14 996 525 -0.804 154 85 48.19 82.78 885 7 80 06 113 1 280. 14 767 524 -0.387 156 35 48.63 83.82 857 1 76 64 110 1 285. 14 534 523 0.035 157 85 49.09 84.91 828 9 73 38 107 2 290. 14 296 522 0.462 159 33 49.56 86.06 801 70 26 104 3

213
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 18.0000 MPa (continued)

T P z H S C

V C

p W 1 A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol»K) m« s

l /iPa»;s niW/(m • K

295. 14.053 522 0.895 160.82 50.04 87.25 773 5 67 28 101 6 300. 13.804 523 1.335 162.29 50.54 88.49 746 4 64 42 98 9 310. 13.291 525 2.233 165.24 51.57 91.13 693 6 59 06 93 8

320. 12.754 530 3.158 168.17 52.65 93.96 642 9 54 14 89 1 330. 12.193 538 4.112 171.11 53.78 96.92 595 2 49 62 84 .7

340. 11.608 549 5.096 174.05 54.93 99.89 551 1 45 48 80 .7 350. 11.003 562 6.110 176.98 56.10 102.69 511 7 41 73 77 1 360. 10.387 579 7.149 179.91 57.25 105.00 477 6 38 36 73 9 370. 9.771 599 8.207 182.81 58.38 106.52 449 6 35 41 71 1 380. 9.171 621 9.276 185.66 59.49 107.07 427 6 32 86 68 8

390. 8.601 645 10.346 188.44 60.58 106.76 411 3 30 71 67

400. 8.072 671 11.409 191.13 61.64 105.80 399 9 28 94 65 5 410. 7.589 696 12.460 193.73 62.68 104.45 392 3 27 49 64 5 420. 7.152 721 13.497 196.23 63.70 102.89 387 9 26 32 63 8 430. 6.762 745 14.518 198.63 64.72 101.33 386 25 38 63 5

440. 6.413 767 15.524 200.94 65.73 99.87 385 9 24 63 63 4

450. 6.102 788 16.516 203.17 66.75 98.62 387 1 24 03 63 6 460. 5.824 808 17.497 205.33 67.78 97.58 389 3 23 56 64

470. 5.574 826 18.469 207.42 68.81 96.78 392 3 23 18 64 6

480. 5.348 843 19.433 209.45 69.85 96.19 395 7 22 89 65 3

490. 5.144 859 20.393 211.43 70.89 95.78 399 5 22 66 66 2 500. 4.958 873 21.350 213.36 71.93 95.55 403 6 22 49 67 2 520. 4.633 899 23.259 217.11 74.02 95.49 412 1 69 5 540. 4.356 920 25.172 220.71 76.10 95.86 420 9 72 1 560. 4.117 939 27.096 224.21 78.17 96.55 429 7 75

580. 3.909 955 29.035 227.62 80.21 97.46 438 5 78

600. 3.724 969 30.995 230.94 82.22 98.53 447 1 81. 2 625. 3.522 983 33.477 234.99 84.69 100.03 457 5

214
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 19.0000 MPa

H W

K mo!L«dm kJ/mol J/(mol.K) J/(mol.K) m« s

J. /^Pa« < 3 ITiW/(m<-K

21 .725 1 .107 -13 .826 78 .65 47 .87 67 .71 2050 .1 1249 .47 260 .3 21 .558 1 .060 -13 .483 82 .17 48 .41 69 .31 2017 .6 1025 .53 256 .8 21 .389 1 .018 -13 .134 85 .57 48 .36 69 .99 1983 .7 859 .02 253 .0

21 .219 .979 -12 .784 88 .83 47 .98 70 .14 1949 .3 732 .46 249 .0

21 .048 .944 -12 .433 91 .95 47 .45 70 .02 1914 .9 634 .23 244 .8

20 .878 .912 -12 .084 94 .92 46 .87 69 .79 1880 .5 556 .50 240 .5 20 .707 .883 -11 .736 97 .77 46 .29 69 .52 1846 .3 493 .89 236 .2 20 .536 .856 -11 .389 100 .49 45 .76 69 .27 1812 .1 442 .65 231 .7 20 .365 .831 -11 .043 103 .10 45 .28 69 .07 1778 .2 400 .09 227 .2 20 .193 .808 -10 .698 105 .61 44 .86 68 .93 1744 .4 364 .28 222 .7

20 .022 .787 -10 .353 108 .03 44 .51 68 .86 1710 .7 333 .78 218 .1 19 .849 .768 -10 .009 110 .36 44 .21 68 .85 1677 .1 307 .51 213 .5 19 .676 .749 -9 ,665 112 .62 43 .98 68 .91 1643 .8 284 .68 209 .0 19 .503 .732 -9 .320 114 .81 43 .79 69 .02 1610 .5 264 .64 204 .4

19 .328 0,.717 -8 .974 116 .93 43 .66 69 .19 1577 .5 246 .91 199 .8

19 .153 .702 -8 .628 119 .00 43 .57 69 .41 1544 .6 231 .11 195 .3 18 .976 ,688 -8 .280 121 .02 43 .52 69 .68 1511 .8 216 .93 190 .8 18 ,799 0,,675 -7,.931 122 .99 43 .51 69 .99 1479 .2 204 .12 186 .3 18 .620 ,663 -7..580 124 .91 43 .54 70 .34 1446 .8 192 .49 181 .9 18.,440 ,652 -7,.228 126 .79 43 .59 70 .72 1414 ,5 181 .88 177 .6

18.,258 0..642 -6..873 128 .63 43 .68 71 .15 1382 ,5 172.,15 173 ,3

18,.075 0,,632 -6,.516 130 ,44 43 .80 71 .60 1350 .6 163,,19 169 ,0

17,,890 0,,623 -6,.157 132,.21 43 .94 72 .09 1318 .9 154,,90 164 .8 17.,703 0,,615 -5,.795 133,.96 44 .11 72 .61 1287 ,4 147,,22 160 ,7

17.,515 0.,607 -5.,431 135,,67 44 .31 73 .17 1256 .1 140,,07 156,,7

17,,325 0. 600 -5,,063 137,,36 44 .52 73 .75 1225 133, 40 152, 7 17,,133 0, 593 -4,,693 139,,02 44,.76 74 .36 1194, 1 127. 15 148. 8 16,,938 0, 587 -4,,320 140, 66 45,,03 75,.00 1163, 4 121. 29 145.

16,,741 0. 581 -3,,943 142, 28 45,,31 75,.68 1133, 115. 78 141. 2 16,,542 0.,576 -3,,563 143,,89 45,,61 76,.38 1102, 8 110. 59 137. 6

16. 340 0. 571 -3.,179 145. 47 45,,93 77,,12 1072, 8 105. 69 134.

16. 136 0. 566 -2. 792 147. 03 46.,27 77,,89 1043. 1 101. 06 130. 5 15. 929 0. 563 -2. 400 148. 58 46. 63 78, 69 1013. 6 96. 67 127. 1 15. 718 0. 559 -2. 005 150. 12 47. 00 79. 53 984. 5 92. 51 123. 7 15. 505 0. 556 -1. 605 151. 64 47. 39 80. 40 955. 5 88. 56 120. 5

15. 288 0. 554 -1. 201 153. 15 47. 80 81. 31 926. 9 84. 80 117. 3 15. 068 0. 551 -0. 792 154. 66 48. 22 82. 26 898. 6 81. 22 114. 3 14. 844 0. 550 -0. 378 156. 15 48. 66 83. 25 870. 6 77. 81 111. 3 14. 616 0. 549 0. 041 157. 63 49. 11 84. 28 843. 74. 56 108. 4

14. 384 0. 548 0. 465 159. 10 49. 58 85. 35 815. 7 71. 45 105. 6

95

100

105

110

115

120

125

130

135

140

145

150,

155

160,

165.

170,

175,

180,

185,

190.

195.

200.

205.

210.

215.

220.

225.

230.

235.

240.

245.

250.

255,

260.

265.

270.

275.

280.

285.

290.

215-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 19.0000 MPa (continued)

T P z H S C

V C

p W V A

K mo 1 • dm kJ/mol J/(mol«K) J/(mol«K) m«s

l /xPa«s niW/(m •K

295. 14.147 548 0.894 160.57 50.06 86.46 788 .8 68 48 102 .8 300. 13.906 548 1.330 162.03 50.55 87.62 762 .3 65 63 100 .2 310. 13.410 550 2.218 164.95 51.58 90.06 710 .8 60 31 95 .2 320. 12.893 554 3.131 167.85 52.64 92.64 661 5 55 43 90 .5 330. 12.355 560 4.071 170.74 53.75 95.32 614 9 50 96 86 .2

340. 11.798 570 5.038 173.62 54.89 98.01 571 8 46 87 82 .3 350. 11.224 582 6.031 176.50 56.04 100.55 532 9 43 16 78 .7 360. 10.640 597 7.048 179.37 57.19 102.74 498 8 39 83 75 6

370. 10.055 614 8.083 182.21 58.33 104.33 470 1 36 87 72 9 380. 9.481 634 9.131 185.00 59.45 105.15 447 34 30 70 6

390. 8.931 656 10.184 187.73 60.55 105.22 429 2 32 11 68 7 400. 8.413 679 11.234 190.39 61.62 104.70 416 1 30 27 67 2 410. 7.935 702 12.277 192.97 62.68 103.78 407 28 74 66 2 420. 7.497 726 13.309 195.45 63.72 102.62 401 27 48 65 4

430. 7.101 748 14.329 197.85 64.76 101.37 397 6 26 46 65

440. 6.744 770 15.336 200.17 65.78 100.15 396 2 25 62 64 9

450. 6.423 791 16.332 202.41 66.81 99.05 396 3 24 95 65

460. 6.134 810 17.318 204.58 67.84 98.12 397 6 24 41 65 3 470. 5.873 828 18.295 206.68 68.88 97.37 399 8 23 98 65 8

480. 5.637 845 19.266 208.72 69.92 96.80 402 6 23 63 66 5

490. 5.422 860 20.232 210.71 70.96 96.40 405 8 23 36 67 3 500. 5.227 874 21.194 212.66 72.00 96.16 409 4 23 14 68 2 520. 4.883 900 23.116 216.43 74.09 96.06 417 2 70 4

540. 4.590 922 25.040 220.06 76.17 96.39 425 4 72 9

560. 4.338 941 26.974 223.57 78.23 97.03 433 9 75 7

580. 4.117 957 28.922 226.99 80.26 97.89 442 3 78. 7 600. 3.923 971 30.890 230.33 82.27 98.93 450 7 81. 8

625. 3.709 986 33.382 234.39 84.74 100.39 460. 9

216
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 20.0000 MPa

T P z H

< C

V C

p W n A

K mo! .•dm kJ/mol J/(mol«K) J/(mol«K) m« s

l /iPa»s it W/(m •K

95. 21 .737 1 165 -13.787 78 58 47.87 67.66 2054 1 1261 07 260 7 100. 21 570 1 115 -13.444 82 10 48.42 69.27 2021 6 1034 29 257 2 105. 21 401 1 070 -13.095 85 50 48.38 69.96 1987 7 865 87 253 4

110. 21 231 1 030 -12.745 88 76 48.01 70.11 1953 4 737 99 249 5 115. 21 062 993 -12.395 91 87 47.48 69.99 1919 638 82 245 3

120. 20 891 959 -12.045 94 85 46.91 69.75 1884 8 560 39 241 1 125. 20 721 929 -11.697 97 69 46.33 69.48 1850 6 497 26 236 7 130. 20 551 900 -11.350 100 41 45.80 69.23 1816 6 445 61 232 3 135. 20 381 874 -11.005 103 02 45.32 69.03 1782 8 402 74 227 8 140. 20 210 850 -10.660 105 52 44.90 68.89 1749 1 366 68 223 3

145. 20 039 828 -10.316 107 94 44.55 68.81 1715 6 335 97 218 7 150. 19 868 807 -9.972 110 27 44.25 68.80 1682 2 309 55 214 2 155. 19 696 788 -9.628 112 53 44.02 68.85 1649 286 57 209 6

160. 19 523 770 -9.283 114 72 43.83 68.95 1616 266 42 205 1

165. 19 349 753 -8.938 116 84 43.70 69.12 1583 1 248 60 200 5

170. 19 175 738 -8.592 118 91 43.61 69.33 1550 4 232 71 196

175. 19 000 723 -8.245 120 92 43.56 69.59 1517 8 218 46 191 5 180. 18 823 710 -7.896 122 89 43.55 69.89 1485 4 205 60 187 1 185. 18 645 697 -7.546 124 80 43.58 70.24 1453 2 193 92 182 7 190. 18 466 686 -7.194 126 68 43.64 70.62 1421 2 183 26 178 3

195. 18 286 675 -6.839 128 52 43.72 71.03 1389 4 173 49 174 1 200. 18 104 664 -6.483 130 33 43.84 71.48 1357 8 164 49 169 8

205. 17 921 655 -6.125 132 10 43.99 71.95 1326 3 156 18 165 7 210. 17 736 646 -5.764 133 84 44.16 72.46 1295 1 148 47 161 6

215. 17 550 638 -5.400 135 55 44.35 73.00 1264 1 141 30 157 5

220. 17 361 630 -5.034 137 23 44.57 73.57 1233 3 134 60 153 6 225. 17 171 623 -4.664 138 89 44.81 74.16 1202 7 128 34 149 7 230. 16 979 616 -4.292 140 53 45.07 74.79 1172 4 122 47 145 9 235. 16 784 610 -3.916 142 14 45.35 75.44 1142 3 116 95 142 2 240. 16 587 604 -3.537 143 74 45.65 76.13 1112 4 111 75 138 5

245. 16 388 599 -3.155 145 32 45.97 76.84 1082 8 106 84 135

250. 16 187 594 -2.769 146 88 46.31 77.59 1053 5 102 20 131 5 255. 15 983 590 -2.379 148 42 46.66 78.36 1024 4 97 81 128 1 260. 15 776 586 -1.985 149 95 47.04 79.17 995 7 93 65 124 8 265. 15 566 583 -1.587 151 47 47.43 80.01 967 2 89 70 121 6

270. 15 353 580 -1.185 152 97 47.83 80.88 939 85 94 118 4

275. 15 137 578 -0.779 154 46 48.25 81.78 911 2 82 36 115 4

280. 14 917 576 -0.367 155 94 48.69 82.72 883 7 78 96 112 4

285. 14 695 574 0.049 157 42 49.14 83.70 856 6 75 71 109 5 290. 14 468 573 0.470 158 88 49.60 84.71 829 9 72 61 106 8

-217-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 20.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol»K) J/(mol»K) m* s

• l /iPa«;s niW/(m<>K

295. 14.237 .573 0.896 160.34 50.08 85.75 803 .5 69 .65 104 .1

300. 14.003 .573 1.327 161.79 50.57 86.84 777 .6 66 .82 101 .4

310. 13.521 .574 2.207 164.67 51.59 89.10 727 .2 61 .52 96 .5 320. 13.022 .577 3.110 167.54 52.64 91.49 679 .1 56 .68 91 .9 330. 12.506 .583 4.037 170.39 53.74 93.95 633 .6 52 .24 87 .7

340. 11.972 .591 4.989 173.23 54.86 96.40 591 .4 48 .20 83 .8 350. 11.425 .602 5.965 176.06 56.00 98.73 553 .0 44 .52 80 .3 360. 10.869 .615 6.962 178.87 57.15 100.80 519 .1 41 .21 77 .2 370. 10.311 ,631 7.979 181.66 58.29 102.40 490 .0 38 .27 74 .5 380. 9.761 .648 9.008 184.40 59.41 103.39 466 .0 35 .68 72 .2

390. 9.230 ,668 10.045 187.09 60.52 103.75 447 .0 33 .45 70 .4 400. 8.726 ,689 11.082 189.72 61.61 103.57 432 .5 31 .55 68 .9 410. 8.254 0.,711 12.115 192.27 62.68 103.00 421 .9 29 .95 67 .7 420. 7.819 0,,732 13.141 194.74 63.74 102.18 414 .5 28,,62 67 ,0

430. 7.421 0, 754 14.158 197.14 64.79 101.22 409 .8 27,,52 66 ,5

440. 7.058 0. 775 15.165 199.45 65.83 100.24 407 ,1 26. 62 66 .3 450. 6.730 0. 794 16.163 201.69 66.86 99.31 406 ,2 25, 88 66, 3 460. 6.432 0. 813 17.152 203.87 67.90 98.50 406 ,5 25. 27 66, 5 470. 6.162 0. 831 18.133 205.98 68.94 97.82 407 9 24. 78 67.

480. 5.916 0. 847 19.109 208.03 69.98 97.30 409, 9 24. 38 67, 6

490. 5.693 0. 862 20.080 210.03 71.02 96.92 412. 6 24. 06 68. 3 500. 5.488 0. 877 21.048 211.99 72.07 96.68 415, 7 23. 80 69. 2 520. 5.128 0. 902 22.980 215.78 74.15 96.58 422. 7 71. 3 540. 4.821 0. 924 24.913 219.43 76.23 96.87 430. 3 73. 7 560. 4.555 0. 943 26.856 222.96 78.29 97.47 438. 3 76. 4

580. 4.323 0. 959 28.814 226.40 80.32 98.30 446. 4 79. 4

600. 4.118 0. 973 30.790 229.74 82.32 99.30 454. 5 82. 4

625. 3.893 0. 989 33.290 233.83 84.79 100.73 464. 5

-218-
Table B3. Properties in the single -phase region along isobars (continued)

ETHANE ISOBAR AT P = 25.0000 MPa

T P z H S C

V C

p W r\ A

K mol»dm kJ/mol J/(mol-K) J/(mol-K) m« s

1 /iPa* i 3 IT W/(m -K

95. 21 792 1 452 -13 .590 78 23 47.87 67.43 2074 1321 76 262 .8 100. 21 627 1 390 -13 248 81 74 48.49 69.09 2041 3 1079 85 259 .4

105. 21 461 1 334 -12 900 85 13 48.50 69.80 2007 6 901 35 255 .7 110. 21 294 1 284 -12 551 88 38 48.16 69.97 1973 5 766 50 251 .9 115. 21 127 1 238 -12 201 91 49 47.65 69.85 1939 6 662 37 247 .8

120. 20 960 1 195 -11 853 94 46 47.09 69.61 1905 8 580 32 243 .7 125. 20 793 1 157 -11 505 97 30 46.52 69.32 1872 2 514 47 239 .4

130. 20 626 1 121 -11 159 100 01 45.99 69.06 1838 8 460 74 235 .1

135. 20 459 1 089 -10 815 102 61 45.51 68.84 1805 6 416 24 230 .7 140. 20 292 1 058 -10 471 105 11 45.10 68.67 1772 6 378 88 226 2

145. 20 125 1 030 -10 128 107 52 44.75 68.57 1739 8 347 13 221 8 150. 19 957 1 004 -9 785 109 84 44.45 68.54 1707 2 319 85 217 3 155. 19 789 980 -9 442 112 09 44.22 68.57 1674 8 296 18 212 8 160. 19 621 958 -9 099 114 27 44.03 68.65 1642 6 275 43 208 3 165. 19 452 937 -8 756 116 38 43.90 68.78 1610 5 257 11 203 9

170. 19 282 917 -8 411 118 44 43.81 68.97 1578 7 240 80 199 5 175. 19 112 899 -8 066 120 44 43.76 69.20 1547 1 226 19 195 1 180. 18 941 882 -7 719 122 40 43.76 69.47 1515 8 213 01 190 7 185. 18 769 866 -7 371 124 30 43.78 69.77 1484 6 201 06 186 4

190. 18 596 851 -7 021 126 17 43.84 70.11 1453 6 190 17 182 1

195. 18 422 837 -6 670 127 99 43.93 70.49 1422 9 180 19 177 9 200. 18 247 824 -6 317 129 78 44.05 70.89 1392 4 171 01 173 8

205. 18 071 812 -5 961 131 54 44.19 71.32 1362 2 162 54 169 7 210. 17 893 800 -5 603 133 26 44.36 71.78 1332 2 154 69 165 7 215. 17 715 789 -5 243 134 96 44.55 72.26 1302 5 147 40 161 7

220. 17 535 779 -4 881 136 63 44.77 72.77 1273 140 59 157 9

225. 17 353 770 -4 516 138 27 45.01 73.30 1243 8 134 24 154 1 230. 17 171 761 -4 148 139 88 45.27 73.85 1214 9 128 28 150 4

235. 16 986 753 -3 777 141 48 45.55 74.43 1186 3 122 69 146 7 240. 16 801 746 -3 403 143 05 45.85 75.03 1158 117 43 143 2

245. 16 613 739 -3 027 144 60 46.17 75.65 1130 112 48 139 7 250. 16 424 732 -2 647 146 14 46.50 76.29 1102 3 107 80 136 3 255. 16 233 726 -2 264 147 66 46.86 76.96 1074 9 103 37 133

260. 16 041 721 -1 877 149 16 47.23 77.64 1048 99 18 129 8 265. 15 846 716 -1 487 150 64 47.61 78.35 1021 3 95 21 126 7

270. 15 650 712 -1 094 152 11 48.01 79.08 995 1 91 44 123 6

275. 15 451 708 -0 696 153 57 48.43 79.83 969 2 87 86 120 7 280. 15 251 704 -0 295 155 02 48.85 80.60 943 7 84 46 117 8 285. 15 048 701 110 156 45 49.30 81.38 918 7 81 22 115 1 290. 14 843 699 519 157 87 49.75 82.19 894 1 78 14 112 4

219-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 25.0000 MPa (continued)

T P z H S C

V C

P W n A

K mol«dm kJ/mol J/(mol-K) J/(mol»K) m» s

l H?a» <3 ITiW/(m •K

295. 14.637 696 0.932 159.29 50.22 83.01 869 9 75 20 109 8 300. 14.427 695 1.349 160.69 50.70 83.85 846 2 72 39 107 3 310. 14.003 693 2.196 163.47 51.68 85.57 800 3 67 17 102 6 320. 13.569 692 3.060 166.21 52.71 87.34 756 6 62 41 98 2 330. 13.127 694 3.943 168.92 53.76 89.13 715 2 58 07 94 2

340. 12.677 698 4.843 171.61 54.85 90.90 676 5 54 12 90 6 350. 12.222 703 5.760 174.27 55.95 92.61 640 7 50 54 87 3 360. 11.762 710 6.695 176.90 57.07 94.21 608 1 47 29 84 3 370. 11.302 719 7.644 179.50 58.19 95.65 578 7 44 36 81 8

380. 10.845 730 8.607 182.07 59.32 96.87 552 9 41 73 79 5

390. 10.394 742 9.581 184.60 60.44 97.83 530 6 39 40 77 6 400. 9.956 755 10.563 187.09 61.56 98.50 511 8 37 33 76 1 410. 9.533 769 11.550 189.53 62.67 98.92 496 4 35 52 74 8 420. 9.129 784 12.540 191.91 63.77 99.11 483 9 33 95 73 8 430. 8.747 799 13.532 194.24 64.87 99.14 474 1 32 58 73 2

440. 8.387 815 14.523 196.52 65.95 99.05 466 6 31 41 72 7 450. 8.050 830 15.512 198.75 67.03 98.89 461 30 40 72 5 460. 7.736 845 16.500 200.92 68.10 98.71 457 29 54 72 5 470. 7.443 859 17.487 203.04 69.16 98.52 454 5 28 80 72 7 480. 7.172 873 18.471 205.11 70.22 98.37 453 1 28 17 73

490. 6.920 887 19.454 207.14 71.28 98.26 452 6 27 64 73 5 500. 6.686 899 20.436 209.12 72.33 98.20 452 9 27 19 74 2 520. 6.266 923 22.401 212.98 74.42 98.28 455 4 75 8

540. 5.901 944 24.369 216.69 76.49 98.62 459 5 77 8

560. 5.582 962 26.347 220.29 78.54 99.18 464 8 80 2

580. 5.301 978 28.338 223.78 80.56 99.94 470. 7 82. 8 600. 5.051 992 30.345 227.18 82.55 100.85 477. 1 85. 5 625. 4.776 1 007 32.883 231.33 85.00 102.15 485. 4

220
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 30.0000 MPa

T P z H

< C

V C

p W 1 A

K mo!L«dm kJ/mol J/(mol»K) J/(mol»K) m« s

l /xPa«

3 ITiW/(m •K

100. 21 .683 1 .664 -13.052 81 .39 48.56 68.92 2060 .7 1128 .63 261 .6

105. 21 .520 1 .597 -12.705 84 .77 48.61 69.66 2027 .0 939 .02 258 .0

110. 21 .355 1 .536 -12.356 88 .02 48.30 69.84 1993 .3 796 .59 254 .2

115. 21 .191 1 .481 -12.007 91 .12 47.82 69.72 1959 .7 687 .09 250 .3

120. 21 .027 1 .430 -11.659 94 .09 47.26 69.47 1926 .3 601 .13 246 .2

125. 20 .863 1 .384 -11.313 96 .92 46.70 69.18 1893 .2 532 .37 242 .1

130. 20 .699 1 .341 -10.968 99 .62 46.18 68.90 1860 .4 476 .41 237 .8

135. 20 .535 1 .302 -10.624 102 .22 45.71 68.66 1827 .8 430 .18 233 .5 140. 20 .371 1 .265 -10.281 104 .71 45.29 68.48 1795 .4 391 .44 229 .1

145. 20 .208 1 .231 -9.939 107 .11 44.94 68.37 1763 .3 358 .59 224 .8

150. 20 .044 1 .200 -9.597 109 .43 44.65 68.31 1731 .4 330 .41 220 .4

155. 19 .880 1 .171 -9.256 111 .67 44.41 68.32 1699 .7 305 .98 216 .0

160. 19 .715 1 .144 -8.914 113 .84 44.23 68.38 1668 .3 284 .62 211 .6 165. 19 .550 1 .119 -8.572 115 .95 44.10 68.49 1637 ,0 265 .77 207 .2 170. 19 .385 1 .095 -8.229 117 .99 44.01 68.65 1606 .1 249 .01 202 .8

175. 19 .219 1 .073 -7.885 119 .98 43.96 68.85 1575 .3 234 .02 198 .5 180. 19 .053 1 .052 -7.540 121 .93 43.95 69.09 1544 .8 220 .50 194 .2 185. 18 .886 1 .033 -7.194 123 .82 43.98 69.37 1514 ,6 208 .26 190 .0 190. 18 .718 1,.015 -6.847 125 .68 44.03 69.68 1484 .6 197 .12 185 .8 195. 18 .550 .997 -6.497 127 .49 44.12 70.02 1454 ,8 186 .92 181 .7

200. 18 .381 0.,981 -6.146 129 .27 44.24 70.38 1425, 3 177,,54 177 .6 205. 18 ,211 0,.966 -5.793 131 .01 44.38 70.78 1396, 1 168..90 173 .6 210. 18 .040 0,,952 -5.439 132 .72 44.55 71.19 1367. 2 160,,89 169,.6 215. 17 ,868 0,,939 -5.082 134 .40 44.75 71.64 1338, 6 153,,46 165 .8 220. 17,,696 0,,927 -4.722 136 .06 44.96 72.10 1310. 2 146,,54 162,.0

225. 17,,522 0.,915 -4.360 137 ,68 45.20 72.58 1282. 2 140. 07 158, 3

230. 17,,347 0,,904 -3.996 139,.28 45.46 73.08 1254. 5 134. 02 154. 6 235. 17,,171 0. 894 -3.630 140,,86 45.74 73.60 1227. 128. 34 151. 1 240. 16,.995 0. 885 -3.260 142.,41 46.04 74.14 1200. 123. 01 147. 6

245. 16, 817 0. 876 -2.888 143. 95 46.36 74.70 1173. 3 117. 98 144. 2

250. 16, 638 0. 867 -2.513 145. 46 46.69 75.28 1146. 9 113. 24 140. 9 255. 16.,458 0. 860 -2.135 146. 96 47.04 75.87 1120. 9 108. 76 137. 6 260. 16,,276 0. 853 -1.755 148. 44 47.41 76.48 1095. 3 104. 53 134. 5 265. 16,,094 0. 846 -1.371 149. 90 47.79 77.10 1070. 1 100. 52 131. 5 270. 15, 910 0. 840 -0.983 151. 35 48.19 77.74 1045. 2 96. 72 128. 5

275. 15. 725 0. 834 -0.593 152. 78 48.60 78.39 1020. 8 93. 11 125. 6 280. 15. 539 0. 829 -0.200 154. 20 49.03 79.05 996. 8 89. 68 122. 8

285. 15. 351 0. 825 0.197 155. 61 49.46 79.73 973. 3 86. 42 120. 1 290. 15. 162 0. 821 0.598 157. 00 49.91 80.42 950. 2 83. 32 117. 5

295. 14. 972 0. 817 1.002 158. 38 50.38 81.12 927. 5 80. 37 115.

-221-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 30.0000 MPa (continued)

T p Z HSCCWr/A v p

- 3 -

i K mol«dm " kJ/mol J/(mol»K) J/(mol«K) m»s

' /iPa»s mW/(m«K)

300. 14.781 0.814 1.409 159.75 50.85 81.83 905.4 77.56 112.6

310. 14.395 0.809 2.234 162.45 51.82 83.27 862.5 72.33 108.0

320. 14.004 0.805 3.074 165.12 52.83 84.73 821.7 67.57 103.8

330. 13.609 0.803 3.929 167.75 53.87 86.20 783.1 63.25 99.9

340. 13.211 0.803 4.798 170.35 54.93 87.65 746.9 59.31 96.4

350. 12.810 0.805 5.682 172.91 56.02 89.07 713.1 55.73 93.2

360. 12.408 0.808 6.580 175.44 57.12 90.44 681.8 52.48 90.4

370. 12.007 0.812 7.490 177.93 58.23 91.72 653.2 49.53 87.8

380. 11.608 0.818 8.414 180.39 59.34 92.89 627.3 46.87 85.6

390. 11.214 0.825 9.348 182.82 60.47 93.94 604.2 44.47 83.7

400. 10.827 0.833 10.292 185.21 61.59 94.85 583.8 42.31 82.1

410. 10.450 0.842 11.244 187.56 62.71 95.60 566.0 40.39 80.8

420. 10.083 0.852 12.204 189.87 63.82 96.22 550.8 38.67 79.7

430. 9.730 0.862 13.168 192.14 64.93 96.71 537.9 37.15 78.9

440. 9.392 0.873 14.137 194.37 66.04 97.09 527.2 35.81 78.4

450. 9.069 0.884 15.110 196.56 67.13 97.40 518.5 34.62 78.0

460. 8.762 0.895 16.085 198.70 68.22 97.64 511.4 33.58 77.8

470. 8.471 0.906 17.063 200.80 69.31 97.86 505.8 32.67 77.8

480. 8.196 0.917 18.042 202.86 70.38 98.05 501.5 31.87 78.0

490. 7.936 0.928 19.024 204.89 71.45 98.23 498.4 31.17 78.4

500. 7.692 0.938 20.007 206.87 72.51 98.43 496.2 30.56 78.8

520. 7.245 0.958 21.980 210.74 74.61 98.88 494.1 80.1

540. 6.849 0.976 23.963 214.49 76.69 99.44 494.5 81.8

560. 6.496 0.992 25.958 218.11 78.74 100.13 496.6 83.9

580. 6.182 1.006 27.969 221.64 80.76 100.94 500.0 86.2

600. 5.900 1.019 29.996 225.08 82.74 101.86 504.3 88.7

625. 5.586 1.033 32.559 229.26 85.18 103.15 510.4

222-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 35.0000 MPa

T P z H

i C

V C

p W V A

K mo!.•dm kJ/mol J/(mol-K) J/(mol»K) m« s

l ^iPa*

.

3 IT W/(m •K

100. 21 .738 1 936 -12.856 81 05 48.63 68.76 2079 7 1180 .99 263 .7 105. 21 .577 1 858 -12.510 84 42 48.73 69.52 2046 .2 979 .13 260 .3

110. 21 .415 1 787 -12.162 87 66 48.44 69.72 2012 7 828 .40 256 .6 115. 21 253 1 722 -11.813 90 76 47.98 69.60 1979 4 713 .08 252 .7 120. 21 092 1 663 -11.466 93 72 47.43 69.35 1946 5 622 .91 248 .8

125. 20 931 1 609 -11.120 96 54 46.88 69.05 1913 8 551 .01 244 .7 130. 20 770 1 559 -10.776 99 25 46.36 68.76 1881 5 492 .68 240 .5 135. 20 609 1 513 -10.432 101 84 45.89 68.51 1849 5 444 59 236 .3 140. 20 448 1 470 -10.090 104 32 45.48 68.31 1817 7 404 40 232 .0

145. 20 288 1 431 -9.749 106 72 45.13 68.18 1786 2 370 38 227 .7

150. 20 127 1 394 -9.409 109 03 44.83 68.11 1754 9 341 24 223 4

155. 19 967 1 360 -9.068 111 26 44.60 68.09 1723 9 316 02 219 1 160. 19 806 1 328 -8.728 113 42 44.42 68.13 1693 2 294 00 214 7 165. 19 645 1 299 -8.387 115 52 44.28 68.22 1662 7 274 59 210 4

170. 19 484 1 271 -8.045 117 56 44.19 68.36 1632 4 257 36 206 1

175. 19 322 1 245 -7.703 119 54 44.15 68.54 1602 5 241 95 201 9 180. 19 160 1 221 -7.360 121 48 44.14 68.76 1572 8 228 09 197 7 185. 18 998 1 198 -7.015 123 36 44.16 69.01 1543 3 215 54 193 5 190. 18 835 1 176 -6.670 125 21 44.22 69.30 1514 2 204 13 189 4

195. 18 671 1 156 -6.322 127 01 44.31 69.61 1485 3 193 69 185 3

200. 18 508 1 137 -5.973 128 78 44.43 69.95 1456 7 184 10 181 3 205. 18 343 1 119 -5.623 130 51 44.57 70.31 1428 4 175 27 177 4

210. 18 178 1 103 -5.270 132 21 44.74 70.70 1400 4 167 10 173 5 215. 18 012 1 087 -4.916 133 88 44.93 71.10 1372 7 159 52 169 7 220. 17 846 1 072 -4.559 135 52 45.15 71.53 1345 3 152 46 165 9

225. 17 679 1 058 -4.200 137 13 45.39 71.98 1318 3 145 87 162 3 230. 17 511 1 045 -3.839 138 72 45.65 72.44 1291 6 139 71 158 7 235. 17 343 1 033 -3.476 140 28 45.92 72.92 1265 2 133 93 155 2 240. 17 173 1 021 -3.110 141 82 46.22 73.42 1239 2 128 51 151 8 245. 17 004 1 010 -2.742 143 34 46.54 73.93 1213 5 123 40 148 5

250. 16 833 1 000 -2.371 144 84 46.87 74.45 1188 2 118 59 145 2 255. 16 662 991 -1.997 146 32 47.22 74.99 1163 3 114 04 142

260. 16 489 982 -1.621 147 78 47.59 75.55 1138 8 109 75 139

265. 16 317 974 -1.242 149 22 47.97 76.11 1114 7 105 68 136

270. 16 143 966 -0.860 150 65 48.37 76.69 1091 101 83 133 1

275. 15 969 959 -0.475 152 06 48.78 77.28 1067. 7 98. 18 130 3 280. 15 793 952 -0.087 153 46 49.20 77.88 1044. 9 94. 71 127. 5 285. 15 618 946 0.304 154. 85 49.63 78.48 1022. 4 91. 41 124. 9

290. 15 441 940 0.698 156 22 50.08 79.10 1000. 5 88. 28 122. 3 295. 15 264 935 1.095 157. 57 50.54 79.72 979. 85. 30 119. 9

-223-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 35.0000 MPa (continued)

T P Z H S C

V C

p W V A

K mo 1 • dm kJ/mol J/(mol'K) J/(mol»K) m» s

l ^uPa«s itiW/(m<•K

300. 15.086 .930 1.495 158.92 51.01 80.35 958 .0 82 .46 117 .5 310. 14.728 .922 2.305 161.57 51.97 81.63 917 .3 77 .18 113 .0

320. 14.368 .916 3.128 164.19 52.97 82.92 878 .7 72 .39 108 .9 330. 14.007 .911 3.963 166.76 54.00 84.21 842 .1 68 .03 105 .1

340. 13.644 .907 4.812 169.29 55.05 85.49 807 .7 64 .06 101 .7

350. 13.280 .906 5.673 171.79 56.13 86.75 775 .4 60 .44 98 .5 360. 12.918 .905 6.547 174.25 57.22 87.98 745 .3 57,.15 95 .7 370. 12.556 .906 7.433 176.68 58.32 89.16 717 .5 54,.16 93 .2 380. 12.198 .908 8.330 179.07 59.43 90.28 692 .0 51,.45 91 .0

390. 11.843 ,911 9.238 181.43 60.55 91.32 668 .8 48,.99 89 .1

400. 11.493 .916 10.156 183.75 61.67 92.29 647 .8 46,.76 87 .5 410. 11.151 ,921 11.083 186.04 62.79 93.17 629 .1 44,,75 86 .1

420. 10.816 ,927 12.019 188.30 63.91 93.96 612 .5 42,,93 85 .0 430. 10.490 ,933 12.962 190.51 65.02 94.66 597 .9 41,,30 84 .1 440. 10.175 0,,940 13.912 192.70 66.13 95.29 585 .3 39,,84 83 .4

450. 9.871 0,,948 14.868 194.85 67.24 95.85 574 ,4 38,,53 82 .9 460. 9.579 0.,955 15.829 196.96 68.34 96.36 565 ,2 37. 36 82 .7 470. 9.298 0.,963 16.795 199.04 69.43 96.82 557 ,4 36. 32 82 .6 480. 9.030 0, 971 17.765 201.08 70.51 97.25 550,,9 35. 38 82, 6

490. 8.774 0, 979 18.740 203.09 71.59 97.66 545,,7 34. 56 82, 8

500. 8.530 0. 987 19.718 205.07 72.66 98.06 541, 4 33. 82 83. 2 520. 8.078 1. 002 21.687 208.93 74.77 98.85 535, 5 84. 2 540. 7.668 1. 017 23.672 212.67 76.85 99.66 532. 5 85. 7 560. 7.299 1. 030 25.674 216.31 78.90 100.53 531. 7 87. 5 580. 6.965 1. 042 27.694 219.86 80.92 101.46 532. 5 89. 6

600. 6.662 1. 053 29.733 223.31 82.91 102.46 534. 5 91. 8

625. 6.321 1. 065 32.311 227.52 85.34 103.80 538. 3

224-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 40.0000 MPa

T P Z H

4 C

V C

p W n A

K mo'L«dm kJ/mol J/(mol«K) J/(mol«K) m* s

- l //Pa*

5 ITiW/(m •K

100. 21 .792 2 .208 -12.660 80 .71 48.70 68.61 2098 .4 1237 .38 265 .8

105. 21 .633 2 .118 -12.315 84 .08 48.84 69.40 2065 .0 1021 .96 262 .5 110. 21 .474 2 .037 -11.967 87 .31 48.58 69.60 2031 .7 862 .12 258 .9 115. 21 .314 1 .963 -11.619 90 .41 48.13 69.49 1998 .8 740 .46 255 .1

120. 21 .155 1 .895 -11.272 93 .36 47.60 69.24 1966 .2 645 .73 251 .3

125. 20 .997 1 .833 -10.927 96 .18 47.06 68.93 1934 .0 570 .47 247 .3 130. 20 .838 1 .776 -10.583 98 .88 46.54 68.63 1902 .2 509 .58 243 .2 135. 20 .680 1 .723 -10.241 101 .46 46.07 68.37 1870 .7 459 .53 239 .0

140. 20 .523 1 .674 -9.899 103 .94 45.66 68.16 1839 .4 417 .79 234 .8 145. 20 .365 1 .629 -9.559 106 .33 45.31 68.01 1808 .5 382 .51 230 .6

150. 20 .208 1 .587 -9.219 108 .64 45.02 67.92 1777 .8 352 .36 226 .3 155. 20 .051 1 .548 -8.880 110 .86 44.78 67.89 1747 .4 326 .31 222 .1 160. 19 .893 1 .511 -8.540 113 .02 44.60 67.91 1717 .3 303 .59 217 .8 165. 19 .736 1 .477 -8.200 115 .11 44.46 67.99 1687 .5 283 .59 213 .6 170. 19 .578 1 .445 -7.860 117 .14 44.37 68.11 1658 .0 265 .86 209 .4

175. 19 .421 1 .416 -7.519 119 .12 44.33 68.27 1628 .7 250 .02 205 .2 180. 19 .263 1 .388 -7.178 121 .04 44.32 68.47 1599 .7 235 .79 201 .0 185. 19 .104 1,.361 -6.835 122 .92 44.34 68.70 1571 .1 222 .91 196 .9 190. 18 .946 1 ,336 -6.490 124 .76 44.40 68.96 1542 .7 211 .21 192 .9 195. 18 .787 1.,313 -6.145 126 .55 44.49 69.25 1514 .6 200 .52 188 .9

200. 18 .628 1.,291 -5.798 128 .31 44.60 69.57 1486 8 190 ,71 184 ,9

205. 18..468 1. 271 -5.449 130 .03 44.75 69.90 1459 3 181 ,68 181 ,0

210. 18 ,308 1. 251 -5.099 131 .72 44.92 70.26 1432. 1 173 ,32 177 2 215. 18..148 1, 233 -4.747 133 .38 45.11 70.65 1405, 2 165 ,58 173 ,5

220. 17..987 1. 216 -4.392 135 ,01 45.33 71.04 1378, 7 158,,37 169, 8

225. 17. 826 1. 199 -4.036 136.,61 45.56 71.46 1352. 5 151, 65 166, 2 230. 17. 664 1. 184 -3.678 138,,18 45.82 71.90 1326. 6 145, 37 162. 7 235. 17. 502 1. 170 -3.317 139,,74 46.10 72.34 1301. 1 139. 49 159. 2 240. 17. 339 1. 156 -2.954 141, 26 46.40 72.81 1276. 133. 96 155. 8

245. 17. 176 1. 143 -2.589 142. 77 46.71 73.28 1251. 2 128. 76 152. 6

250. 17. 013 1. 131 -2.221 144. 25 47.05 73.77 1226. 9 123. 86 149. 4

255. 16. 849 1. 120 -1.851 145. 72 47.40 74.28 1202. 9 119. 24 146. 3 260. 16. 685 1. 109 -1.479 147. 17 47.76 74.79 1179. 3 114. 88 143. 2 265. 16. 520 1. 099 -1.103 148. 60 48.14 75.31 1156. 1 110. 74 140. 3 270. 16. 355 1. 089 -0.725 150. 01 48.54 75.85 1133. 3 106. 83 137. 4

275. 16. 189 1. 081 -0.345 151. 41 48.94 76.39 1110. 9 103. 12 134. 7 280. 16. 023 1. 072 0.038 152. 79 49.36 76.94 1089. 99. 60 132.

285. 15. 856 1. 065 0.425 154. 15 49.80 77.50 1067. 5 96. 26 129. 4

290. 15. 690 1. 057 0.814 155. 51 50.24 78.07 1046. 5 93. 08 126. 9

295. 15. 523 1. 051 1.205 156. 85 50.70 78.64 1025. 9 90. 06 124. 5

225
Table B3. Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 40.0000 MPa (continued)

T P z H S C

V C

p W n A

K mol'dm kJ/mol J/(mol»K) J/(mol-K) m« s

l ^Pa«

:

3 IT W/(m •K

300. 15.355 1 044 1.600 158.17 51.17 79.22 1005 7 87 18 122 1 310. 15.020 1 033 2.398 160.79 52.13 80.39 966 8 81 83 117 .7 320. 14.683 1 024 3.208 163.36 53.12 81.57 929 9 76 97 113 6 330. 14.347 1 016 4.030 165.89 54.14 82.76 894 8 72 54 109 9 340. 14.010 1 010 4.863 168.38 55.19 83.94 861 7 68 52 106 5

350. 13.675 1 005 5.708 170.83 56.26 85.10 830 6 64 85 103 4

360. 13.340 1 002 6.565 173.24 57.34 86.25 801 5 61 50 100 6 370. 13.008 1 000 7.433 175.62 58.44 87.36 774 5 58 45 98 1 380. 12.678 999 8.312 177.96 59.55 88.44 749 4 55 68 95 9 390. 12.353 999 9.202 180.27 60.66 89.47 726 4 53 15 94

400. 12.031 1 000 10.101 182.55 61.78 90.45 705 3 50 85 92 3 410. 11.715 1 002 11.010 184.80 62.90 91.37 686 1 48 76 90 9 420. 11.406 1 004 11.928 187.01 64.01 92.24 668 8 46 86 89 7 430. 11.104 1 008 12.855 189.19 65.13 93.05 653 3 45 14 88 8 440. 10.809 1 012 13.789 191.34 66.24 93.80 639 5 43 58 88

450. 10.523 1 016 14.731 193.45 67.35 94.51 627 3 42 17 87 5 460. 10.246 1 021 15.679 195.54 68.45 95.17 616 6 40 90 87 1 470. 9.979 1 026 16.634 197.59 69.55 95.79 607 3 39 75 86 9 480. 9.721 1 031 17.595 199.61 70.63 96.37 599 2 38 72 86 9 490. 9.473 1 036 18.561 201.61 71.71 96.94 592 4 37 78 87

500. 9.234 1 042 19.533 203.57 72.79 97.48 586 5 36 95 87 2 520. 8.787 1 053 21.494 207.41 74.91 98.53 577 6 88

540. 8.376 1 064 23.475 211.15 77.00 99.56 571 7 89 3 560. 8.000 1 074 25.476 214.79 79.05 100.60 568 2 90 9 580. 7.656 1 083 27.499 218.34 81.06 101.67 566 6 92 8

600. 7.341 1 092 29.543 221.81 83.05 102.76 566 5 94 9 625. 6.984 1 102 32.130 226.03 85.48 104.18 568.

226
Table B3 . Properties in the single -phase region along isobars (continued)

ETHANE ISOBAR AT P = 45.0000 MPa

T P Z H

i C

V C

p W V A

K mo"L«dm kJ/mol J/(mol«K) J/(mol-K) m« s

l /iPa*

3 ITiW/(m •K

100. 21 .845 2 .478 -12.464 80 .38 48.77 68.46 2116 .8 1298 .34 267 .9 105. 21 .688 2 .377 -12.119 83 .74 48.95 69.28 2083 .5 1067 .81 264 .7 110. 21 .531 2 .285 -11.772 86 .97 48.72 69.50 2050 .4 897 .94 261 .2 115. 21 .374 2 .202 -11.425 90 .06 48.29 69.39 2017 .8 769 .36 257 .5 120. 21 .217 2 .126 -11.079 93 .01 47.76 69.13 1985 .6 669 .70 253 .7

125. 21 .061 2 .056 -10.734 95 .82 47.23 68.82 1953 .8 590 .81 249 .8 130. 20 .905 1 .991 -10.390 98 .52 46.71 68.51 1922 .4 527 .19 245 .8 135. 20 .750 1 .932 -10.049 101 .10 46.25 68.24 1891 .4 475 .03 241 .7 140. 20 .595 1 .877 -9.708 103 .57 45.84 68.02 1860 .7 431 .63 237 .6 145. 20 .440 1 .826 -9.368 105 .96 45.49 67.85 1830 .3 395 .03 233 .4

150. 20 .286 1 .779 -9.029 108 .26 45.19 67.75 1800 .2 363 .80 229 .3 155. 20 .132 1 .734 -8.691 110 .48 44.96 67.71 1770 .4 336 .87 225 .1 160. 19 .978 1 .693 -8.352 112 .63 44.77 67.72 1740 .9 313 .41 220 .9 165. 19 .824 1 .655 -8.013 114 .71 44.64 67.78 1711 .7 292 .79 216 .7 170. 19 .669 1 .619 -7.674 116 .74 44.55 67.88 1682 .8 274 .53 212 .6

175. 19 .515 1 .585 -7.335 118 .71 44.50 68.02 1654 ,1 258 .24 208 .4 180. 19 ,361 1 .553 -6.994 120 .63 44.49 68.20 1625.,8 243 .61 204 .3 185. 19 ,207 1 .523 -6.652 122 .50 44.51 68.42 1597 ,8 230 .39 200 .3 190. 19 ,052 1..495 -6.310 124 .32 44.57 68.66 1570 ,1 218 .38 196 .3 195. 18.,897 1..469 -5.966 126 .11 44.66 68.93 1542 .7 207.,42 192 ,3

200. 18,,742 1..444 -5.620 127 .86 44.77 69.23 1515. 6 197.,38 188.,4

205. 18.,587 1,,420 -5.273 129 .57 44.92 69.55 1488. 9 188,,13 184 ,6

210. 18,,432 1.,398 -4.925 131,.25 45.09 69.89 1462. 4 179,,59 180.,8

215. 18,,276 1,,377 -4.575 132,,90 45.28 70.25 1436. 3 171,,67 177.,2

220. 18,,120 1,,358 -4.222 134,,52 45.49 70.62 1410,.5 164, 31 173,,5

225. 17, 964 1,,339 -3.868 136 ,11 45.73 71.02 1385. 1 157,,44 170,

230. 17,,808 1,,321 -3.512 137,.68 45.99 71.43 1360. 151. 03 166. 5 235. 17, 651 1, 305 -3.154 139, 22 46.27 71.85 1335. 2 145. 03 163, 1 240. 17. 495 1..289 -2.794 140, 74 46.56 72.29 1310. 9 139. 39 159. 8 245. 17, 337 1. 274 -2.431 142, 23 46.88 72.74 1286. 9 134. 09 156. 5

250. 17. 180 1. 260 -2.066 143. 71 47.21 73.20 1263. 3 129. 10 153. 4

255. 17. 023 1. 247 -1.699 145. 16 47.56 73.68 1240. 1 124. 39 150. 3 260. 16. 865 1. 234 -1.329 146. 60 47.92 74.16 1217. 2 119. 94 147. 3 265. 16. 707 1. 222 -0.957 148. 01 48.30 74.65 1194. 8 115. 74 144. 4

270. 16. 549 1. 211 -0.583 149. 41 48.70 75.16 1172. 8 111. 76 141. 6

275. 16. 390 1. 201 -0.206 150. 80 49.10 75.67 1151. 2 107. 98 138. 9 280. 16. 232 1. 191 0.174 152. 16 49.52 76.19 1130. 1 104. 40 136. 2 285. 16. 073 1. 181 0.556 153. 52 49.96 76.72 1109. 3 101. 00 133. 7 290. 15. 915 1. 173 0.941 154. 86 50.40 77.25 1089. 97. 76 131. 2 295. 15. 756 1. 164 1.329 156. 18 50.86 77.79 1069. 2 94. 69 128. 8

227
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 45.0000 MPa (continued)

T P Z H S C

V C

p W 1 A

K mol'dm kJ/mol J/(mol»K) J/(mol»K) m* s

l /xPa«s itiW/(m<•K

300. 15.597 1 .157 1.719 157.49 51.32 78.33 1049 .8 91 .76 126 .5 310. 15.280 1 .143 2.508 160.08 52.28 79.43 1012 .3 86 .32 122 .1 320. 14.962 1 .130 3.307 162.62 53.27 80.54 976 .6 81 .38 118 .1

330. 14.645 1 .120 4.118 165.11 54.29 81.65 942 .8 76 .88 114 .4

340. 14.330 1 .111 4.940 167.57 55.33 82.76 910 .8 72 .78 111 .0

350. 14.015 1 .103 5.774 169.98 56.40 83.87 880 .6 69 .04 108 .0 360. 13.703 1 .097 6.618 172.36 57.48 84.96 852 .4 65 .63 105 .2 370. 13.393 1 .092 7.473 174.70 58.57 86.03 825 ,9 62 .51 102 .7 380. 13.085 1..088 8.338 177.01 59.67 87.07 801 .3 59 ,66 100 .5 390. 12.782 1 .086 9.214 179.29 60.78 88.09 778 .5 57 .06 98 .5

400. 12.483 1 .084 10.100 181.53 61.90 89.07 757 ,5 54,,69 96 .8 410. 12.188 1 .083 10.995 183.74 63.01 90.01 738 2 52,,53 95 .4 420. 11.899 1 .083 11.900 185.92 64.13 90.92 720,,5 50,,55 94 .1 430. 11.615 1.,084 12.813 188.07 65.24 91.78 704, 5 48..75 93 .1 440. 11.338 1..085 13.735 190.19 66.36 92.61 689, 9 47, 11 92 ,3

450. 11.069 1..087 14.665 192.28 67.46 93.39 676..9 45. 61 91 ,7

460. 10.806 1, 089 15.603 194.34 68.57 94.14 665, 2 44. 25 91 .2 470. 10.551 1..091 16.548 196.37 69.66 94.86 654, 8 43. 02 91,,0

480. 10.304 1..094 17.500 198.38 70.75 95.55 645. 6 41. 89 90, 8 490. 10.065 1..097 18.459 200.35 71.83 96.22 637, 6 40. 87 90, 9

500. 9.834 1,,101 19.424 202.30 72.91 96.86 630. 5 39. 94 91..0 520. 9.396 1. 108 21.374 206.13 75.03 98.10 619. 1 91. 7 540. 8.990 1,.115 23.348 209.85 77.12 99.31 610. 8 92. 8 560. 8.615 1..122 25.346 213.49 79.17 100.49 605. 1 94. 2 580. 8.268 1, 129 27.368 217.03 81.19 101.68 601. 4 95. 9

600. 7.947 1. 135 29.414 220.50 83.17 102.87 599. 4 97. 9

625. 7.580 1. 142 32.004 224.73 85.60 104.38 598. 8

228
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 50.0000 MPa

T P Z H

< C

V C

p W V A

K mo"L • dm kJ/mol J/(mol«K) J/(mol«K) m« s

i /xPa« • 3 ITiW/(m-•K

100. 21 .896 2 .746 -12.268 80 .05 48.84 68.32 2134 .9 1364 .46 270 .0

105. 21 .742 2 .634 -11.924 83 .41 49.06 69.17 2101 .7 1117 .04 266 .9 110. 21 .587 2 .533 -11.577 86 .64 48.86 69.40 2068 .8 936 .09 263 .5 115. 21 .432 2 .440 -11.230 89 .72 48.44 69.30 2036 .5 799 .94 259 .9 120. 21 .277 2 .355 -10.885 92 .66 47.92 69.04 2004 .7 694 .92 256 .2

125. 21 .124 2 .277 -10.540 95 .48 47.39 68.72 1973 .3 612 .11 252 .3 130. 20 .970 2 .206 -10.197 98 .17 46.88 68.40 1942 .3 545 .55 248 .4

135. 20 .818 2 .140 -9.856 100 .74 46.42 68.12 1911 .7 491 .14 244 .4 140. 20 .665 2 .079 -9.516 103 .21 46.01 67.89 1881 .4 445 .97 240 .3 145. 20 .513 2 .022 -9.177 105 .59 45.66 67.72 1851 .5 407 .96 236 .3

150. 20 .362 1 .969 -8.839 107 .89 45.36 67.60 1822 .0 375 .59 232 .1 155. 20 .210 1 ,920 -8.501 110 .10 45.13 67.54 1792 .7 347 .72 228 .0

160. 20 .059 1 ,874 -8.163 112 .25 44.94 67.54 1763 .8 323 .48 223 .9 165. 19 .908 1 ,831 -7.825 114 .33 44.81 67.58 1735 .1 302 .20 219 .8 170. 19 .757 1 .790 -7.487 116 .34 44.72 67.67 1706 .8 283 .38 215 .7

175. 19 .606 1 .753 -7.149 118 .31 44.67 67.80 1678 .8 266 .61 211 .6 180. 19 ,456 1 ,717 -6.809 120 .22 44.66 67.97 1651 ,1 251 ,56 207 .6 185. 19 ,305 1 ,684 -6.469 122 .08 44.68 68.17 1623 .7 237 ,98 203 .6 190. 19 .154 1.,652 -6.128 123 .91 44.74 68.39 1596 .6 225 .66 199 .6 195. 19 ,003 1.,623 -5.785 125 .69 44.82 68.65 1569 .9 214 ,41 195 .7

200. 18 ,852 1 ,595 -5.441 127,,43 44.94 68.93 1543 .4 204 ,12 191 .9 205. 18.,701 1, 569 -5.096 129 ,13 45.08 69.23 1517 .3 194 ,64 188 .1 210. 18 ,550 1,,544 -4.749 130,,80 45.25 69.55 1491 .5 185 ,90 184 .4

215. 18 ,398 1,,520 -4.400 132,,45 45.44 69.90 1466 .1 177,,79 180 ,7

220. 18 ,247 1,,498 -4.050 134,,06 45.66 70.26 1441 ,0 170,,27 177 .2

225. 18..095 1, 477 -3.697 135,,64 45.89 70.63 1416 .2 163,,25 173 .7 230. 17,.944 1. 457 -3.343 137, 20 46.15 71.02 1391 .8 156,,70 170 .2 235. 17,.792 1. 438 -2.987 138. 73 46.43 71.43 1367 ,8 150, 57 166 ,9

240. 17,.640 1,.420 -2.629 140, 24 46.72 71.84 1344 .1 144, 81 163,.6 245. 17,,488 1, 404 -2.269 141, 72 47.04 72.27 1320 ,8 139, 40 160 .4

250. 17, 337 1, 387 -1.906 143,,19 47.37 72.71 1297. 8 134. 31 157, 3 255. 17, 185 1, 372 -1.542 144, 63 47.72 73.17 1275, 3 129. 51 154. 2 260. 17,,033 1. 358 -1.175 146. 06 48.08 73.63 1253, 1 124. 97 151. 3 265. 16, 881 1.,344 -0.805 147. 46 48.46 74.10 1231, 4 120. 69 148. 4

270. 16,.728 1, 331 -0.434 148. 85 48.85 74.58 1210, 1 116. 63 145. 6

275. 16, 576 1, 319 -0.060 150. 23 49.26 75.07 1189, 1 112. 78 142. 9 280. 16, 424 1, 308 0.317 151. 58 49.68 75.56 1168. 6 109. 13 140. 3 285. 16,,273 1, 297 0.696 152. 92 50.11 76.06 1148, 5 105. 66 137. 8 290. 16,,121 1, 286 1.078 154. 25 50.55 76.57 1128. 8 102. 37 135. 3 295. 15,,969 1, 277 1.462 155. 56 51.01 77.09 1109. 6 99. 24 133.

-229-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 50.0000 MPa (continued)

T p Z H S C C W r? A

v p K mol-drn"

3 kJ/mol J/(mol-K) J/(mol«K) m-s"

1 /iPa-s mW/(m-K)

300. 15.817 1.267 1.849 156.86 51.47 77.60 1090.8 96.26 130.7

310. 15.515 1.250 2.630 159.43 52.42 78.65 1054.4 90.71 126.4

320. 15.213 1.235 3.422 161.94 53.41 79.71 1019.9 85.67 122.4

330. 14.912 1.222 4.224 164.41 54.43 80.77 987.0 81.09 118.7

340. 14.613 1.210 5.037 166.84 55.47 81.84 955.9 76.90 115.3

350. 14.316 1.200 5.861 169.22 56.53 82.90 926.6 73.08 112.3

360. 14.021 1.191 6.695 171.57 57.61 83.96 899.0 69.59 109.5

370. 13.729 1.184 7.540 173.89 58.70 85.00 873.1 66.40 107.0

380. 13.439 1.178 8.395 176.17 59.80 86.02 848.9 63.48 104.8

390. 13.153 1.172 9.260 178.42 60.91 87.02 826.4 60.80 102.8

400. 12.872 1.168 10.135 180.63 62.02 88.00 805.5 58.36 101.1

410. 12.594 1.165 11.020 182.82 63.13 88.96 786.1 56.12 99.6

420. 12.321 1.162 11.914 184.97 64.25 89.88 768.3 54.06 98.3

430. 12.054 1.160 12.818 187.10 65.36 90.78 751.9 52.19 97.2

440. 11.792 1.159 13.730 189.19 66.47 91.64 737.0 50.47 96.4

450. 11.536 1.158 14.651 191.26 67.58 92.48 723.4 48.89 95.7

460. 11.286 1.158 15.579 193.30 68.68 93.29 711.0 47.46 95.2

470. 11.042 1.159 16.516 195.32 69.78 94.07 699.9 46.14 94.8

480. 10.805 1.159 17.461 197.31 70.87 94.83 689.9 44.94 94.6

490. 10.575 1.160 18.413 199.27 71.95 95.56 680.9 43.84 94.6

500. 10.352 1.162 19.372 201.21 73.02 96.28 672.9 42.83 94.6

520. 9.927 1.165 21.311 205.01 75.15 97.66 659.6 95.2

540. 9.529 1.169 23.278 208.72 77.24 98.99 649.4 96.1

560. 9.157 1.173 25.271 212.35 79.29 100.30 641.8 97.4

580. 8.811 1.177 27.290 215.89 81.31 101.58 636.3 99.0

600. 8.489 1.181 29.334 219.35 83.29 102.86 632.6 100.8

625. 8.118 1.185 31.926 223.59 85.71 104.46 630.0

-230-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 55.0000 MPa

T P Z H

< C

V C

p W V A

K mo' .•dm kJ/mol J/(mol-K) J/(mol»K) m« s

l /liPa*

:

3 IT W/(m -K

100. 21 947 3 .014 -12 .072 79 74 48.90 68.19 2152 7 1436 49 272 .1

105. 21 794 2 .891 -11 .728 83 09 49.17 69.06 2119 6 1170 08 269 .0

110. 21 641 2 .779 -11 .382 86 31 48.99 69.31 2086 9 976 84 265 .7 115. 21 488 2 677 -11 036 89 39 48.58 69.22 2054 9 832 37 262 .2 120. 21 336 2 584 -10 690 92 33 48.08 68.95 2023 4 721 50 258 .6

125. 21 185 2 498 -10 346 95 14 47.56 68.63 1992 3 634 45 254 8

130. 21 034 2 419 -10 004 97 82 47.05 68.31 1961 7 564 73 251

135. 20 883 2 346 -9 663 100 39 46.59 68.02 1931 6 507 90 247

140. 20 734 2 279 -9 324 102 86 46.18 67.77 1901 8 460 84 243

145. 20 584 2 216 -8 985 105 24 45.82 67.59 1872 4 421 34 239

150. 20 435 2 158 -8 648 107 53 45.53 67.46 1843 3 387 76 235

155. 20 287 2 104 -8 311 109 74 45.29 67.39 1814 5 358 89 230 9

160. 20 138 2 053 -7 974 111 88 45.11 67.38 1786 1 333 82 226 9

165. 19 990 2 006 -7 637 113 95 44.97 67.41 1758 311 85 222 8

170. 19 842 1 961 -7 300 115 96 44.88 67.48 1730 2 292 44 218 8

175. 19 694 1 919 -6 962 117 92 44.83 67.60 1702 8 275 16 214 8

180. 19 547 1 880 -6 624 119 83 44.82 67.75 1675 7 259 67 210 8

185. 19 399 1 843 -6 284 121 69 44.84 67.94 1648 8 245 71 206 8

190. 19 252 1 808 -5 944 123 50 44.89 68.16 1622 3 233 05 202 9 195. 19 104 1 776 -5 603 125 27 44.98 68.40 1596 2 221 51 199 1

200. 18 957 1 745 -5 260 127 01 45.10 68.66 1570 3 210 94 195 3 205. 18 809 1 716 -4 916 128 71 45.24 68.95 1544 8 201 23 191 5 210. 18 662 1 688 -4 571 130 37 45.40 69.26 1519 6 192 27 187 8 215. 18 515 1 662 -4 223 132 01 45.60 69.59 1494 8 183 97 184 2 220. 18 367 1 637 -3 875 133 61 45.81 69.93 1470 3 176 27 180 7

225. 18 220 1 614 -3 524 135 19 46.05 70.29 1446 1 169 09 177 2 230. 18 072 1 591 -3 172 136 74 46.30 70.67 1422 3 162 39 173 8

235. 17 925 1 570 -2 817 138 26 46.58 71.05 1398 9 156 12 170 5 240. 17 778 1 550 -2 461 139 76 46.88 71.46 1375 8 150 24 167 3 245. 17 631 1 531 -2 103 141 24 47.19 71.87 1353 1 144 72 164 1

250. 17 484 1 513 -1 742 142 69 47.52 72.29 1330 8 139 52 161

255. 17 337 1 496 -1 380 144 13 47.87 72.73 1308 8 134 62 158

260. 17 190 1 480 -1 015 145 55 48.23 73.17 1287 3 129 99 155 1 265. 17 043 1 465 -0 648 146 94 48.61 73.63 1266 1 125 61 152 3 270. 16 896 1 450 -0 279 148 32 49.00 74.09 1245 3 121 47 149 5

275. 16 750 1 436 093 149 69 49.41 74.56 1225 117 54 146 8

280. 16 603 1 423 467 151 04 49.82 75.04 1205 113 82 144 2 285. 16 457 1 410 843 152 37 50.25 75.52 1185 5 110 28 141 7 290. 16 311 1 398 1 222 153 69 50.70 76.01 1166 3 106. 92 139 3

295. 16 165 1 387 1 603 154 99 51.15 76.50 1147 6 103. 73 136 9

231
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 55.0000 MPa (continued)

T P Z H S C

V C

p W n

A

K mol«dm kJ/mol J/(mol«K) J/(mol«K) m»s

l ^Pa»

«

3 IT W/(m K

300. 16.020 1 376 1.987 156.28 51.61 77.00 1129 3 100 69 134 7 310. 15.730 1 357 2.762 158.82 52.56 78.01 1094 95 03 130 4

320. 15.441 1 339 3.547 161.31 53.55 79.04 1060 3 89 88 126 4

330. 15.154 1 323 4.343 163.76 54.56 80.07 1028 3 85 20 122 8 340. 14.869 1 309 5.149 166.17 55.60 81.10 998 80 92 119 4

350. 14.586 1 296 5.965 168.53 56.66 82.13 969 3 77 01 116 4

360. 14.305 1 284 6.791 170.86 57.74 83.16 942 3 73 44 113 6 370. 14.027 1 275 7.628 173.15 58.83 84.18 916 9 70 17 111 1 380. 13.753 1 266 8.475 175.41 59.92 85.19 893 1 67 17 108 8 390. 13.481 1 258 9.332 177.64 61.03 86.18 870 8 64 41 106 8

400. 13.214 1 252 10.198 179.83 62.14 87.16 850 1 61 89 105 1 410. 12.951 1 246 11.075 182.00 63.25 88.12 830 7 59 57 103 5 420. 12.691 1 241 11.961 184.13 64.37 89.05 812 8 57 45 102 2 430. 12.437 1 237 12.856 186.24 65.48 89.97 796 3 55 49 101 1 440. 12.188 1 234 13.760 188.32 66.59 90.86 781 53 70 100 2

450. 11.943 1 231 14.673 190.37 67.69 91.72 767 52 05 99 4

460. 11.705 1 229 15.594 192.39 68.80 92.57 754 2 50 54 98 9

470. 11.471 1 227 16.524 194.39 69.89 93.39 742 5 49 15 98 5 480. 11.244 1 226 17.462 196.37 70.98 94.20 731 9 47 87 98 2 490. 11.023 1 225 18.408 198.32 72.06 94.98 722 3 46 70 98 1

500. 10.807 1 224 19.362 200.24 73.14 95.75 713 6 45 62 98 1 520. 10.394 1 224 21.292 204.03 75.26 97.23 698 8 98 5 540. 10.005 1 224 23.251 207.72 77.35 98.67 687 99 3 560. 9.640 1 225 25.238 211.34 79.40 100.06 677 8 100 5 580. 9.297 1 227 27.253 214.87 81.41 101.43 670 7 101 9

600. 8.976 1 228 29.295 218.34 83.39 102.79 665. 6 103. 6

625. 8.604 1 230 31.886 222.57 85.81 104.46 661. 3

-232-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 60.0000 MPa

T P Z H

< C

V C

p W n A

K mo!L«dm kJ/mol J/(mol«K) J/(mol«K) m* s

• l fj.Fa» •. 3 ITiW/(m<•K

100. 21 .996 3 .281 -11.876 79 .42 48.97 68.06 2170 .3 1515 .28 274 .1

105. 21 .846 3 .146 -11.533 82 .77 49.27 68.97 2137 .2 1227 .42 271 .2 110. 21 .695 3 .024 -11.187 85 .98 49.12 69.23 2104 .8 1020 .48 267 .9 115. 21 .544 2 .913 -10.841 89 .06 48.73 69.14 2073 .0 866 .85 264 .5 120. 21 .394 2 .811 -10.496 92 .00 48.24 68.88 2041 .7 749 .59 261 .0

125. 21 .244 2 .717 -10.152 94 .80 47.71 68.55 2011 .1 657 .93 257 .3 130. 21 .096 2 .631 -9.810 97 .48 47.21 68.22 1980 .9 584 .80 253 .5 135. 20 .948 2 .552 -9.470 100 .05 46.75 67.92 1951 .1 525 .37 249 .6 140. 20 .800 2 .478 -9.131 102 .52 46.34 67.67 1921 .7 476 .29 245 .7 145. 20 .653 2 .410 -8.793 104 .89 45.99 67.47 1892 .7 435 .19 241 .8

150. 20 .507 2 .346 -8.456 107 .17 45.69 67.34 1864 .1 400 .32 237 .8 155. 20 .361 2 .287 -8.120 109 .38 45.46 67.26 1835 .8 370 .39 233 .8 160. 20 .215 2 .231 -7.784 111 .52 45.27 67.23 1807 .9 344 .45 229 .8 165. 20 .070 2 .179 -7.447 113 .58 45.13 67.25 1780 .3 321 .75 225 .8 170. 19 .924 2 .130 -7.111 115 .59 45.04 67.32 1753 ,1 301 .71 221 .8

175. 19 .780 2 ,085 -6.774 117 .55 44.99 67.42 1726 ,1 283 .90 217 .8 180. 19 .635 2 ,042 -6.437 119 .45 44.97 67.56 1699,.5 267,.95 213 ,9

185. 19 ,490 2.,001 -6.099 121 .30 44.99 67.74 1673 .2 253,,58 210 .0 190. 19 .346 1 ,963 -5.759 123 .11 45.05 67.94 1647 ,3 240 ,56 206 .1 195. 19 .202 1.,927 -5.419 124 .88 45.13 68.17 1621 7 228,,71 202 .3

200. 19 .057 1,,893 -5.078 126 .61 45.25 68.42 1596, 4 217,,87 198 ,6

205. 18.,913 1.,861 -4.735 128 .30 45.39 68.70 1571,,4 207,,90 194, 9 210. 18 .769 1,,831 -4.391 129,.96 45.55 69.00 1546, 8 198,,72 191, 2 215. 18,.626 1.,802 -4.045 131,,59 45.74 69.31 1522, 5 190, 22 187 7 220. 18..482 1,.775 -3.698 133, 18 45.96 69.64 1498, 5 182, 33 184, 2

225. 18.,338 1,.749 -3.348 134,,75 46.19 69.99 1474. 9 174. 98 180, 7 230. 18,.195 1..724 -2.998 136,,29 46.45 70.35 1451. 7 168. 12 177, 4

235. 18,.052 1, 701 -2.645 137.,81 46.73 70.73 1428. 8 161. 71 174, 1 240. 17,,908 1. 679 -2.290 139. 30 47.02 71.12 1406. 2 155. 70 170, 9 245. 17.,765 1. 658 -1.934 140.,77 47.33 71.52 1384. 1 150. 05 167. 7

250. 17,,623 1. 638 -1.575 142. 22 47.66 71.93 1362. 3 144. 73 164. 7 255. 17,,480 1. 619 -1.214 143. 65 48.01 72.35 1340. 9 139. 72 161. 7 260. 17, 337 1. 601 -0.852 145. 06 48.37 72.78 1319. 8 134. 99 158. 8 265. 17,.195 1. 584 -0.487 146. 45 48.75 73.22 1299. 2 130. 52 156.

270. 17..053 1. 567 -0.119 147. 82 49.14 73.67 1278. 9 126. 29 153. 3

275. 16,.911 1. 552 0.250 149. 18 49.55 74.12 1259. 1 122. 28 150. 6 280. 16, 770 1. 537 0.622 150. 52 49.96 74.59 1239. 6 118. 48 148.

285. 16,,629 1. 523 0.996 151. 84 50.39 75.06 1220. 5 114. 87 145. 5 290. 16,.488 1. 509 1.372 153. 15 50.83 75.53 1201. 9 111. 44 143. 1 295. 16,.347 1. 496 1.751 154. 45 51.29 76.01 1183. 6 108. 17 140. 8

233
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 60.0000 MPa (continued)

T p Z HSCCW77A v p K mol-drn"

3 kJ/mol J/(mol«K) J/(mol-K) m«s

_1

/xPa«s mW/(m«K)

300. 16.207 1.484 2.133 155.73 51.75 76.50 1165.7 105.07 138.6

310. 15.928 1.461 2.902 158.25 52.70 77.48 1131.3 99.29 134.3

320. 15.651 1.441 3.682 160.73 53.68 78.48 1098.4 94.03 130.3

330. 15.375 1.422 4.472 163.16 54.70 79.48 1067.1 89.24 126.7

340. 15.102 1.405 5.272 165.55 55.73 80.49 1037.5 84.87 123.4

350. 14.831 1.390 6.082 167.90 56.79 81.50 1009.4 80.86 120.3

360. 14.562 1.377 6.902 170.21 57.86 82.51 982.9 77.20 117.5

370. 14.297 1.364 7.732 172.48 58.95 83.52 957.9 73.84 115.0

380. 14.034 1.353 8.572 174.72 60.05 84.51 934.4 70.76 112.7

390. 13.775 1.343 9.422 176.93 61.15 85.50 912.4 67.93 110.7

400. 13.520 1.334 10.282 179.11 62.26 86.47 891.8 65.33 108.9

410. 13.268 1.327 11.152 181.25 63.37 87.43 872.5 62.93 107.3

420. 13.021 1.320 12.031 183.37 64.48 88.38 854.6 60.73 106.0

430. 12.778 1.313 12.919 185.46 65.59 89.30 838.0 58.70 104.8

440. 12.539 1.308 13.817 187.53 66.70 90.21 822.5 56.84 103.9

450. 12.305 1.303 14.723 189.56 67.81 91.10 808.3 55.12 103.1

460. 12.076 1.299 15.639 191.57 68.91 91.97 795.1 53.53 102.4

470. 11.852 1.295 16.563 193.56 70.00 92.82 783.0 52.07 102.0

480. 11.633 1.292 17.495 195.52 71.09 93.66 771.9 50.73 101.7

490. 11.419 1.290 18.436 197.46 72.17 94.48 761.8 49.49 101.5

500. 11.211 1.287 19.385 199.38 73.24 95.28 752.5 48.34 101.4

520. 10.810 1.284 21.306 203.15 75.36 96.84 736.5 101.7

540. 10.431 1.281 23.258 206.83 77.45 98.35 723.4 102.4

560. 10.073 1.279 25.240 210.44 79.50 99.82 712.9 103.4

580. 9.735 1.278 27.251 213.96 81.51 101.26 704.6 104.8

600. 9.417 1.277 29.290 217.42 83.49 102.67 698.1 106.4

625. 9.046 1.276 31.879 221.65 85.90 104.41 692.3

234
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 65.0000 MPa

T P Z H

< ( V C

p W V

A

K mo" .•dm kJ/mol J/(mol-K) J/(mol«K) m« s

l ^Pa«

.

3 IT W/(m K

105. 21 .896 3 .400 -11.337 82 .45 49 .37 68.87 2154 6 1289 .63 273 .3 110. 21 .747 3 .268 -10.992 85 .67 49 .25 69.15 2122 3 1067 .36 270 .1 115. 21 .598 3 .147 -10.646 88 .74 48 .87 69.07 2090 7 903 .58 266 .8 120. 21 .450 3 .037 -10.301 91 67 48 .39 68.80 2059 8 779 .32 263 .3 125. 21 303 2 .936 -9.958 94 48 47 87 68.47 2029 5 682 .66 259 .7

130. 21 156 2 842 -9.617 97 15 47 37 68.14 1999 6 605 .83 256

135. 21 010 2 756 -9.277 99 72 46 91 67.83 1970 2 543 .60 252 2 140. 20 865 2 676 -8.938 102 18 46 50 67.57 1941 3 492 .37 248 4

145. 20 720 2 602 -8.601 104 55 46 15 67.37 1912 7 449 .55 244 5 150. 20 576 2 533 -8.264 106 83 45 85 67.22 1884 5 413 31 240 5

155. 20 433 2 468 -7.929 109 03 45 61 67.13 1856 7 382 27 236 6 160. 20 289 2 408 -7.593 111 16 45 42 67.09 1829 2 355 40 232 6 165. 20 147 2 352 -7.258 113 23 45 29 67.11 1802 1 331 92 228 7 170. 20 004 2 299 -6.922 115 23 45 19 67.16 1775 3 311 22 224 8 175. 19 862 2 249 -6.586 117 18 45 14 67.26 1748 9 292 84 220 9

180. 19 720 2 202 -6.249 119 08 45 12 67.39 1722 8 276 41 217

185. 19 578 2 158 -5.912 120 93 45 14 67.55 1697 261 61 213 1 190. 19 437 2 117 -5.574 122 73 45 20 67.74 1671 5 248 22 209 3 195. 19 295 2 078 -5.234 124 49 45 28 67.96 1646 4 236 04 205 5 200. 19 154 2 041 -4.894 126 22 45 39 68.21 1621 6 224 90 201 8

205. 19 013 2 006 -4.552 127 90 45 53 68.47 1597 2 214 67 198 2 210. 18 873 1 973 -4.209 129 56 45 70 68.76 1573 1 205 25 194 6 215. 18 732 1 941 -3.865 131 18 45 89 69.06 1549 3 196 53 191

220. 18 592 1 911 -3.519 132 77 46 10 69.38 1525 8 188 45 187 6 225. 18 452 1 883 -3.171 134 33 46 33 69.72 1502 7 180 92 184 2

230. 18 312 1 856 -2.821 135 87 46 59 70.07 1480 173 90 180 8 235. 18 172 1 831 -2.470 137 38 46 87 70.44 1457 6 167 34 177 6 240. 18 033 1 806 -2.117 138 87 47 16 70.82 1435 5 161 18 174 4

245. 17 893 1 783 -1.762 140 33 47 47 71.20 1413 9 155 40 171 3 250. 17 754 1 761 -1.405 141 77 47 80 71.61 1392 6 149 97 168 3

255. 17 616 1 740 -1.046 143 20 48 15 72.02 1371 6 144 84 165 3 260. 17 477 1 720 -0.685 144 60 48 51 72.44 1351 1 140 01 162 4

265. 17 339 1 701 -0.322 145 98 48 88 72.86 1330 9 135 44 159 6 270. 17 201 1 683 0.044 147 35 49 28 73.30 1311 1 131 11 156 9 275. 17 064 1 666 0.412 148 70 49 68 73.75 1291 7 127 02 154 3

280. 16 927 1 649 0.781 150 03 50 10 74.20 1272 6 123 13 151 7 285. 16 790 1 634 1.154 151 35 50 53 74.66 1254 119 44 149 3 290. 16 654 1 619 1.528 152 65 50 97 75.12 1235 7 115 93 146 9 295. 16 518 1 604 1.905 153 94 51 42 75.59 1217 9 112 59 144 5 300. 16 382 1 591 2.284 155 21 51 88 76.07 1200 4 109 42 142. 3

235-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 65.0000 MPa (continued)

H W

K mol'dm kJ/mol J/(mol-K) J/(mol«K) m«s /iPa«s mW/(m-K)

310. 16 .112 1 .565 3 .049 157 .72 52 .83 77 .03 1166 .7 103 .51 138 .1 320. 15 .845 1 .542 3 .825 160 .18 53 .81 78 .00 1134 .5 98 .13 134 .1

330. 15 .579 1 .521 4 .609 162 .60 54 .82 78 .99 1103 .9 93 .23 130 .5 340. 15 .316 1 .501 5 .404 164 .97 55 .86 79 .98 1074 .8 88 .75 127 .1 350. 15 .055 1 .484 6 .209 167 .30 56 .91 80 .98 1047 .3 84 .65 124 .1

360. 14 .797 1 .468 7 .024 169 .60 57 .98 81 .98 1021 .2 80 .90 121 .3 370. 14 .542 1 .453 7 .849 171 .86 59 .07 82 .97 996 .6 77 .45 118 .7 380. 14 .290 1 .440 8 .683 174 .08 60 .16 83 .96 973 .4 74 .28 116 .5 390. 14 .042 1 .428 9 .528 176 .28 61 .26 84 .94 951 .6 71 .37 114 .4 400. 13 .797 1 .417 10 .382 178 .44 62 .37 85 .91 931 .1 68 .68 112 .6

410. 13..555 1..407 11 ,246 180 ,57 63 .48 86 .87 912 .0 66 .21 111 .0 420. 13 .318 1 .398 12 ,119 182,,68 64 .59 87 .82 894 .1 63 .94 109 .6 430. 13 .084 1.,389 13,.002 184,,76 65 .70 88 .75 877 .3 61 .84 108 .4 440. 12 ,855 1 ,382 13 .894 186,,81 66 .81 89 .67 861 ,8 59 .90 107 .4 450. 12 ,630 1 ,375 14,,796 188,,83 67 .91 90 .58 847 ,3 58,.11 106 .5

460. 12,,409 1,.370 15,,706 190,,83 69,.01 91,.46 833 ,9 56,,45 105 ,9

470. 12,,194 1,,364 16, 625 192.,81 70,.10 92,.34 821 .5 54,,93 105,,4

480. 11,,982 1,,359 17, 553 194, 76 71,,19 93,,20 810, 1 53.,51 105.

490. 11,,776 1. 355 18,,489 196. 69 72,,27 94,,04 799, 6 52. 21 104, 8

500. 11,,574 1.,351 19, 433 198. 60 73.,34 94.,87 789, 9 51. 00 104. 7

520. 11, 185 1. 344 21. 347 202. 35 75. 46 96. 49 772. 9 104. 8

540. 10, 815 1. 339 23. 293 206. 02 77. 54 98. 06 758. 8 105. 4

560. 10, 464 1. 334 25. 269 209. 62 79. 59 99. 58 747. 1 106. 3 580. 10, 132 1. 330 27. 276 213. 14 81. 60 101. 08 737. 7 107. 6

600. 9. 818 1. 327 29. 312 216. 59 83. 58 102. 54 730. 1 109.

625. 9. 449 1. 324 31. 898 220. 81 85. 99 104. 34 722. 9

-236-
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 70.0000 MPa

T P Z H

i C

V C

p W V A

K mo L«dm kJ/mol J/(mol.K) J/(mol»K) m« s

i /iFa* : 3 U W/(m •K

105. 21 .945 3 .654 -11.141 82 15 49.48 68.78 2171 7 1357 .39 275 .4

110. 21 .798 3 .511 -10.796 85 35 49.37 69.08 2139 6 1117 .87 272 .3

115. 21 .651 3 .381 -10.451 88 42 49.01 69.00 2108 2 942 .83 269 .1

120. 21 .505 3 .262 -10.107 91 35 48.54 68.74 2077 6 810 .87 265 .7 125. 21 360 3 .153 -9.764 94 15 48.03 68.41 2047 6 708 .74 262 .1

130. 21 .215 3 053 -9.423 96 83 47.53 68.07 2018 627 .91 258 .5 135. 21 072 2 960 -9.083 99 39 47.07 67.75 1989 562 67 254 .7 140. 20 928 2 873 -8.745 101 85 46.66 67.48 1960 4 509 11 251 .0

145. 20 786 2 793 -8.408 104 22 46.30 67.27 1932 3 464 47 247 .1

150. 20 644 2 719 -8.072 106 49 46.01 67.12 1904 5 426 77 243 .3

155. 20 503 2 649 -7.737 108 69 45.77 67.02 1877 1 394 53 239 4

160. 20 362 2 584 -7.402 110 82 45.58 66.97 1850 1 366 68 235 5 165. 20 221 2 523 -7.067 112 88 45.44 66.97 1823 4 342 37 231 6

170. 20 081 2 466 -6.732 114 88 45.34 67.02 1797 1 320 98 227 7 175. 19 942 2 412 -6.397 116 83 45.28 67.11 1771 1 302 01 223 8

180. 19 802 2 362 -6.061 118 72 45.27 67.23 1745 4 285 06 220

185. 19 663 2 314 -5.725 120 56 45.29 67.38 1720 1 269 82 216 2 190. 19 524 2 270 -5.387 122 36 45.34 67.57 1695 1 256 03 212 4

195. 19 386 2 227 -5.049 124 12 45.42 67.78 1670 5 243 50 208 7 200. 19 247 2 187 -4.709 125 84 45.53 68.01 1646 2 232 05 205

205. 19 109 2 149 -4.369 127 52 45.67 68.27 1622 2 221 55 201 4

210. 18 972 2 113 -4.027 129 17 45.84 68.55 1598 5 211 88 197 8

215. 18 834 2 079 -3.683 130 78 46.03 68.84 1575 2 202 93 194 3 220. 18 697 2 047 -3.338 132 37 46.24 69.15 1552 3 194 64 190 9 225. 18 560 2 016 -2.992 133 93 46.47 69.48 1529 6 186 93 187 5

230. 18 423 1 987 -2.643 135 46 46.73 69.82 1507 3 179 73 184 2 235. 18 287 1 959 -2.293 136 96 47.00 70.18 1485 4 173 01 181

240. 18 151 1 933 -1.942 138 45 47.29 70.55 1463 8 166 71 177 8 245. 18 015 1 907 -1.588 139 90 47.60 70.93 1442 6 160 79 174 8 250. 17 880 1 883 -1.232 141 34 47.93 71.32 1421 7 155 23 171 8

255. 17 745 1 861 -0.875 142 76 48.28 71.72 1401 2 149 99 168 8 260. 17 610 1 839 -0.515 144 15 48.64 72.13 1381 1 145 04 166

265. 17 475 1 818 -0.153 145 53 49.01 72.55 1361 3 140 37 163 2 270. 17 341 1 798 0.211 146 89 49.40 72.98 1341 9 135 94 160 5 275. 17 208 1 779 0.577 148 24 49.81 73.42 1322 9 131. 75 157 9

280. 17 075 1 761 0.945 149 56 50.22 73.86 1304. 3 127. 78 155 3 285. 16 942 1 744 1.315 150 87 50.65 74.31 1286. 124. 00 152 9

290. 16 809 1 727 1.688 152 17 51.09 74.77 1268. 1 120. 41 150 5 295. 16 678 1 711 2.063 153 45 51.54 75.23 1250. 6 117. 00 148 2 300. 16 546 1 696 2.440 154. 72 52.00 75.70 1233. 5 113. 75 146

237
Table B3 . Properties in the single-phase region along isobars (continued)

ETHANE ISOBAR AT P = 70.0000 MPa (continued)

T P Z H S C

V C

p W n A

K mo"L»dm kJ/mol J/(mol^K) J/(mol«K) m* s

l /iPa« i3 ITiW/(m<•K

310. 16 .285 1 .668 3.202 157.22 52.95 76.64 1200 .5 107 .71 141 .7 320. 16 .026 1 .642 3.973 159.67 53.93 77.60 1168 .9 102 .21 137 .8 330. 15 .769 1 .618 4.754 162.07 54.94 78.57 1138 .8 97 .19 134 .2 340. 15 .515 1 .596 5.545 164.43 55.97 79.55 1110 .3 92 .60 130 .8 350. 15 .263 1 .576 6.345 166.75 57.03 80.54 1083 .2 88 .40 127 .7

360. 15..014 1 .558 7.155 169.03 58.10 81.52 1057 .5 84 .55 124 .9 370. 14 .768 1 .541 7.975 171.28 59.18 82.51 1033 .2 81 .00 122 .4 380. 14 .525 1 .525 8.806 173.49 60.27 83.49 1010 .3 77 .75 120 .1 390. 14..286 1 .511 9.645 175.67 61.37 84.47 988 .7 74 .75 118 .0 400. 14 .050 1 .498 10.495 177.82 62.48 85.44 968 .4 71 .99 116 .1

410. 13 .817 1 .486 11.354 179.95 63.59 86.40 949 .4 69 .44 114 .5 420. 13 .588 1 ,475 12.223 182.04 64.70 87.35 931 .5 67 .08 113 .1 430. 13.,363 1 ,465 13.101 184.11 65.80 88.29 914 .7 64 .91 111 .8 440. 13.,142 1,,456 13.989 186.15 66.91 89.22 899 ,1 62 .90 110 .8 450. 12,,925 1,,448 14.885 188.16 68.01 90.13 884 .5 61 ,04 109 .9

460. 12.,712 1,,440 15.791 190.15 69.11 91.04 870 .9 59,,32 109 ,2

470. 12,,503 1,,433 16.706 192.12 70.20 91.92 858 ,3 57,,72 108 ,6

480. 12.,299 1,,426 17.630 194.06 71.29 92.80 846,.6 56, 25 108, 2 490. 12.,098 1,,420 18.562 195.99 72.37 93.66 835,,7 54. 88 107. 9

500. 11. 903 1.,415 19.503 197.89 73.44 94.51 825. 7 53. 61 107. 8

520. 11. 524 1. 405 21.410 201.63 75.55 96.17 807. 9 107. 8

540. 11. 163 1. 397 23.349 205.29 77.64 97.79 792. 9 108. 3 560. 10. 820 1, 389 25.321 208.87 79.68 99.36 780. 4 109. 1 580. 10. 494 1. 383 27.323 212.39 81.69 100.90 770. 110. 3 600. 10. 184 1. 378 29.356 215.83 83.66 102.40 761. 4 111. 6

625. 9. 819 1. 372 31.940 220.05 86.07 104.25 753.

-238-
Table B4 . Properties in the single-phase region along isotherms

ETHANE ISOTHERM AT T = 95.00 K

P P ap/3T|

p 3P/3p|

T C

V W V A

mol»dm MPa MPa.K"

1 3 MPa • dm «mol

1 J/(mol-K) m« s

l fiPa-s mW/(m«K)

0.458E -05 0.362E- 05 0.3807E -07 0.790 27.08 185 3 3.17 3.2

21.503 0.362E- 05 2.870 81.417 47.93 1970 1 1057.13 252.1

21.55 3.883 2.891 83.060 47.91 1987 1 1092.60 253.8

21.60 8.079 2.913 84.823 47.90 2005 1132.97 255.6

21.65 12.365 2.935 86.611 47.89 2023 1176.59 257.5

21.70 16.741 2.956 88.425 47.88 2041 1223.88 259.3

21.75 21.208 2.978 90.266 47.87 2059 1275.32 261.2

21.80 25.768 3.000 92.133 47.86 2077 1 1331.50 263.1

ETHANE ISOTHERM AT T = 100.00 K

p P 3P/5T|

p d?/dp\

T C

V W V A

mol'dm MPa MPa«K

_1 3 MPa«dm «mol

1 J/(mol»K)

- l m« s /iPa*s niW/(m-K)

0.133E- 04 0.111E-04 0.1108E -06 0.832 27.30 189.9 3.32 3.5

21.325 0.111E-04 2.784 77.575 48.15 1938.3 877.99 248.2

21.35 1.964 2.794 78.406 48.17 1946.8 891.78 249.1

21.40 5.926 2.815 80.071 48.23 1963.8 920.52 250.9

21.45 9.972 2.836 81.760 48.28 1980.7 951.26 252.7

21.50 14.103 2.857 83.472 48.34 1997.8 984.21 254.6

21.55 18.320 2.878 85.210 48.40 2014.8 1019.63 256.5

21.60 22.624 2.899 86.972 48.46 2032.0 1057.82 258.3

21.65 27.017 2.921 88.761 48.52 2049.2 1099.13 260.3

21.70 31.501 2.942 90.576 48.58 2066.4 1143.94 262.2

21.75 36.075 2.963 92.418 48.65 2083.7 1192.76 264.2

21.80 40.743 2.984 94.287 48.71 2101.2 1246.14 266.2

21.85 45.504 3.005 96.185 48.78 2118.6 1304.76 268.2

21.90 50.362 3.027 98.111 48.84 2136.2 1369.47 270.2

21.95 55.316 3.048 100.065 48.91 2153.8 1441.26 272.2

22.00 60.369 3.070 102.049 48.97 2171.6 274.3

-239
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 105.00 K

p P 3P/3T|

p 3P/3H

T C

V W V A

mol'dm MPa MPa.K"

1 3 MPa* dm »mol1 J/(mol •K) m«s pPa»s mW/(m«K)

0.347E -04 0.303E-04 0.2876E -06 0.873 27.48 194.4 3.46 3.7

21.144 0.303E-04 2.678 73.838 47.89 1903.9 742.08 243.9

21.15 0.417 2.680 74.015 47.90 1905.7 744.41 244.1

21.20 4.157 2.700 75.593 48.00 1921.9 765.73 246.0

21.25 7.977 2.720 77.192 48.09 1938.2 788.34 247.8

21.30 11.877 2.740 78.814 48.18 1954.6 812.38 249.6

21.35 15.858 2.760 80.460 48.28 1970.9 838.00 251.5

21.40 19.923 2.780 82.128 48.38 1987.4 865.34 253.4

21.45 24.072 2.801 83.822 48.48 2003.9 894.60 255.3

21.50 28.306 2.821 85.539 48.57 2020.5 925.99 257.2

21.55 32.626 2.841 87.283 48.67 2037.1 959.77 259.2

21.60 37.034 2.862 89.051 48.77 2053.9 996.21 261.2

21.65 41.532 2.883 90.846 48.87 2070.7 1035.67 263.2

21.70 46.119 2.903 92.668 48.97 2087.6 1078.52 265.2

21.75 50.799 2.924 94.516 49.08 2104.5 1125.25 267.2

21.80 55.571 2.945 96.392 49.18 2121.6 1176.41 269.3

21.85 60.438 2.966 98.295 49.28 2138.7 271.4

21.90 65.401 2.986 100.227 49.38 2155.9 273.5

ETHANE : LSOTHERM AT T == 110.00 K

P P <9P/dT|

p d?/dp\

T C

V W 1 A

mol«dm MPa MPa.K"

1 3 MPa«dm «mol

1 J/(mol'•K) m»s /iPa«s m W/(m-K)

0.816E -04 0.747E-04 0.6763E 06 0.915 27.59 198.8 3.60 4.0

20.962 0.747E-04 2.564 70.231 47.39 1868.3 637.04 239.5

21.00 2.662 2.578 71.359 47.47 1880.1 649.42 240.9

21.05 6.268 2.598 72.878 47.59 1895.8 666.67 242.7

21.10 9.951 2.617 74.417 47.70 1911.6 684.88 244.5

21.15 13.710 2.636 75.979 47.82 1927.5 704.14 246.4

21.20 17.549 2.655 77.562 47.94 1943.4 724.54 248.3

21.25 21.467 2.675 79.168 48.05 1959.3 746.20 250.2

21.30 25.466 2.694 80.798 48.17 1975.4 769.24 252.1

21.35 29.547 2.714 82.450 48.29 1991.5 793.79 254.0

21.40 33.711 2.734 84.127 48.41 2007.7 820.03 256.0

21.45 37.960 2.754 85.829 48.53 2024.0 848.12 258.0

21.50 42.295 2.773 87.555 48.65 2040.3 878.28 260.0

21.55 46.716 2.793 89.306 48.77 2056.8 910.76 262.0

21.60 51.226 2.814 91.083 48.89 2073.3 945.83 264.0

21.65 55.825 2.834 92.886 49.01 2089.9 983.83 266.1

21.70 60.515 2.854 94.715 49.13 2106.6 268.2

21.75 65.297 2.874 96.571 49.25 2123.3 270.3

-240-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 115.00 K

p P 3P/3T|

p d?/dp\

r CV W 1

A

mol'dm MPa MPa-K'

1 3 MPa* dm «mol1 J/(mol«K)

- l m« s ^Pa»s niW/(m.K)

0.177E -03 0.169E-03 0.1460E -05 0.957 27.62 203.1 3.75 4.3

20.779 0.169E-03 2.450 66.761 46.78 1832.0 554.36 235.0

20.80 1.383 2.457 67.350 46.83 1838.3 559.76 235.7

20.85 4.787 2.476 68.794 46.95 1853.7 573.31 237.5

20.90 8.263 2.494 70.257 47.08 1869.0 587.54 239.3

20.95 11.813 2.512 71.741 47.20 1884.4 602.50 241.2

21.00 15.437 2.531 73.246 47.33 1899.9 618.25 243.0

21.05 19.138 2.550 74.771 47.46 1915.5 634.86 244.9

21.10 22.915 2.568 76.319 47.58 1931.1 652.41 246.8

21.15 26.770 2.587 77.889 47.71 1946.7 670.98 248.7

21.20 30.704 2.606 79.481 47.84 1962.5 690.67 250.6

21.25 34.718 2.625 81.096 47.97 1978.3 711.58 252.6

21.30 38.814 2.644 82.734 48.10 1994.2 733.83 254.6

21.35 42.992 2.664 84.396 48.22 2010.2 757.56 256.6

21.40 47.254 2.683 86.082 48.35 2026.3 782.93 258.6

21.45 51.601 2.702 87.792 48.48 2042.4 810.12 260.6

21.50 56.034 2.722 89.527 48.61 2058.6 839.33 262.7

21.55 60.554 2.741 91.287 48.75 2074.9 264.8

21.60 65.163 2.761 93.072 48.88 2091.3 266.9

21.65 69.861 2.781 94.883 49.01 2107.8 269.0

ETHANE

" LSOTHERM AT T == 120.00 1 <

P P 3P/3T|

p d?/dp\

T C

V W V

A

mol'dm MPa MPa.K"

1 3 MPa«dm 'mol1 J/(mol-K)

-

1

m» s fiFa'S rr W/(m-K)

0.355E -03 0.355E-03 0.2925E -05 0.999 27.57 207.4 3.90 4.7

20.595 0.355E-03 2.338 63.427 46.14 1795.5 488.15 230.3

20.60 0.286 2.340 63.550 46.15 1796.8 489.11 230.5

20.65 3.498 2.357 64.923 46.28 1811.8 500.02 232.2

20.70 6.779 2.375 66.316 46.41 1826.8 511.43 234.0

20.75 10.130 2.393 67.727 46.54 1841.8 523.37 235.8

20.80 13.552 2.410 69.159 46.67 1857.0 535.88 237.7

20.85 17.046 2.428 70.610 46.80 1872.1 549.00 239.5

20.90 20.613 2.446 72.081 46.93 1887.4 562.79 241. U 20.95 24.255 2.464 73.573 47.06 1902.7 577.29 243.3

21.00 27.971 2.483 75.087 47.19 1918.0 592.58 245.2

21.05 31.764 2.501 76.621 47.32 1933.5 608.70 247.1

21.10 35.634 2.519 78.178 47.45 1949.0 625.74 249.1

21.15 39.582 2.538 79.757 47.59 1964.6 643.78 251.0

-241
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 120.00 K (continued)

p P 5P/3T|

p d?/dp\

T C

V W n

A

mol*dm MPa MPa«K

_1 3 -

' MPa 'dm «mol

L J/(mol'•K) m» s

l /xPa«s mW/(m«K)

21.20 43.610 2.556 81.359 47.72 1980,.3 662.91 253.0

21.25 47.718 2.575 82.983 47.85 1996 ,0 683.25 255.0

21.30 51.908 2.594 84.630 47.98 2011. 8 704.89 257.1

21.35 56.182 2.612 86.301 48.12 2027, 7 728.00 259.1

21.40 60.539 2.631 87.996 48.25 2043,,7 261.2

21.45 64.982 2.650 89.715 48.39 2059,,7 263.3

21.50 69.511 2.669 91.458 48.52 2075, 9 265.4

ETHANE ISOTHERM AT T = 130.00 K

p P dP/3T|

p 3P/3p|

T C

V W V

A

mol'dm MPa MPa.K"

1 3 MPa«dm «mol J/(mol«K) ra«s liFa'S niW/(m-K)

0.120E-02 0.129E-02 0.9749E--05 1.082 27.30 215.7 4.19 5.3

20.225 0.129E-02 2.128 57.151 44.97 1721.8 389.76 220.7

20.25 1.431 2.136 57.773 45.03 1729.0 393.54 221.6

20.30 4.352 2.152 59.037 45.16 1743.4 401.35 223.3

20.35 7.335 2.169 60.317 45.29 1757.9 409.47 225.0

20.40 10.384 2.185 61.615 45.41 1772.4 417.90 226.8

20.45 13.497 2.202 62.930 45.54 1787.0 426.69 228.6

20.50 16.677 2.218 64.263 45.67 1801.6 435.84 230.4

20.55 19.924 2.235 65.615 45.80 1816.3 445.39 232.2

20.60 23.239 2.252 66.985 45.92 1831.0 455.35 234.1

20.65 26.623 2.269 68.375 46.05 1845.8 465.76 236.0

20.70 30.076 2.286 69.784 46.18 1860.7 476.65 237.8

20.75 33.601 2.303 71.212 46.31 1875.6 488.06 239.8

20.80 37.198 2.320 72.661 46.44 1890.7 500.03 241.7

20.85 40.868 2.337 74.130 46.57 1905.7 512.59 243.6

20.90 44.611 2.355 75.619 46.70 1920.9 525.80 245.6

20.95 48.430 2.372 77.130 46.83 1936.1 539.70 247.6

21.00 52.325 2.389 78.661 46.96 1951.4 554.36 249.6

21.05 56.296 2.407 80.214 47.09 1966.7 569.84 251.6

21.10 60.346 2.425 81.789 47.22 1982.2 253.7

21.15 64.476 2.443 83.386 47.35 1997.7 255.7

21.20 68.685 2.460 85.004 47.49 2013.2 257.8

242-
Table B4 . Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 140.00 K

p P 3P/3T|

p d?/dp\

T C

V W r) A

mo 1 • dm MPa MPa-Kf

1 MP;a • dm • mo1 J/(mol«K)

- i m* s fiYa'S niW/(m«K)

0.330E -02 0.383E-02 0.2667E-04 1.162 27.05 223.5 4.50 6.0

19.850 0.383E-02 1.938 51.358 44.04 1647.8 320.91 210.9

19.90 2.576 1.953 52.495 44.16 1661.6 326.56 212.5

19.95 5.229 1.968 53.658 44.28 1675.6 332.46 214.2

20.00 7.942 1.983 54.837 44.40 1689.6 338.56 215.9

20.05 10.713 1.999 56.031 44.52 1703.7 344.87 217.7

20.10 13.545 2.014 57.242 44.64 1717.8 351.41 219.4

20.15 16.438 2.030 58.468 44.76 1732.0 358.19 221.1

20.20 19.392 2.045 59.712 44.88 1746.2 365.22 222.9

20.25 22.409 2.061 60.972 45.00 1760.5 372.51 224.7

20.30 25.490 2.077 62.250 45.12 1774.8 380.09 226.5

20.35 28.634 2.093 63.546 45.24 1789.2 387.98 228.

20.40 31.845 2.108 64.859 45.36 1803.7 396.18 230.2

20.45 35.121 2.124 66.190 45.48 1818.2 404.72 232.1

20.50 38.464 2.140 67.540 45.60 1832.8 413.63 234.0

20.55 41.875 2.157 68.909 45.73 1847.4 422.92 235.9

20.60 45.355 2.173 70.296 45.85 1862.2 432.63 237.8

20.65 48.905 2.189 71.703 45.97 1876.9 442.78 239.7

20.70 52.526 2.206 73.129 46.09 1891.8 453.41 241.7

20.75 56.218 2.222 74.575 46.22 1906.7 464.55 243.7

20.80 59.984 2.239 76.041 46.34 1921.7 476.24 245.7

20.85 63.823 2.255 77.527 46.46 1936.7 247.7

20.90 67.737 2.272 79.034 46.59 1951.8 249.8

ETHANE ISOTHERM AT T == 150.00 K

Second virial c:oefficient :Ls -719.2

3 .. - 1 cm «mol

P P 3P/3T|

p 5P/3p|

x C

V W V

A

mol'dm MPa

- 1 3 - MPa«K MPa«dm «mol

1 J/(mol^K)

-

m* s /LtPa«S IT:W/(m«K)

0.779E -02 0.967E-02 0.6281E-04 1.239 27.13 230.6 4.80 6.7

19.470 0.967E-02 1.765 46.002 43.38 1573.3 270.37 201.0

19.50 1.389 1.774 46.626 43.44 1581.4 272.98 201.9

19.55 3.747 1.788 47.683 43.55 1595.0 277.48 203.6

19.60 6.158 1.802 48.755 43.66 1608.6 282.12 205.2

19.65 8.622 1.817 49.840 43.77 1622.3 286.90 206.8

19.70 11.142 1.831 50.940 43.88 1636.0 291.83 208.5

19.75 13.717 1.846 52.055 43.99 1649.7 296.91 210.2

19.80 16.348 1.860 53.184 44.10 1663.5 302.16 211.9

19.85 19.035 1.875 54.329 44.21 1677.3 307.58 213.6

-243-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 150.00 K (continued)

p P 9P/ST|

p

' T C

V W V A

mo 1 • dm MPa MPa.K"

1 3 MPa«dm «mol1 J/(mol«K)

- l m» s ptPa«s itiW/(m«K)

19.90 21.781 1.890 55.490 44.32 1691.2 313.19 215.3

19.95 24.585 1.904 56.666 44.44 1705.1 318.99 217.0

20.00 27.448 1.919 57.858 44.55 1719.1 324.99 218.8

20.05 30.371 1.934 59.067 44.66 1733.1 331.20 220.6

20.10 33.355 1.949 60.292 44.77 1747.2 337.64 222.4

20.15 36.400 1.964 61.534 44.89 1761.4 344.32 224.2

20.20 39.508 1.979 62.793 45.00 1775.6 351.25 226.1

20.25 42.680 1.995 64.069 45.11 1789.9 358.45 227.9

20.30 45.915 2.010 65.363 45.22 1804.2 365.94 229.8

20.35 49.216 2.025 66.675 45.34 1818.6 373.72 231.7

20.40 52.583 2.041 68.005 45.45 1833.0 381.83 233.6

20.45 56.017 2.056 69.353 45.57 1847.5 390.28 235.6

20.50 59.519 2.072 70.719 45.68 1862.1 399.09 237.5

20.55 63.089 2.088 72.104 45.79 1876.8 239.5

20.60 66.730 2.104 73.508 45.91 1891.5 241.5

ETHANE ISOTHERM AT T = 160.00 K

3 - 1 Second virial coefficient is -647.7 cm «mol

p P dP/ST|

p dP/dpl1 T C

V W V A

mol'dm MPa MPa.K"

1 3 MPa«dm 'mol1 J/(mol-K)

- l m* s ^iPa«s niW/(m-K)

0.163E-01 0.215E-01 0.1319E -03 1.308 27.72 236.9 5.11 7.4

19.083 0.215E-01 1.609 41.042 42.95 1498.5 231.74 191.1

19.10 0.732 1.613 41.370 42.98 1503.0 232.94 191.6

19.15 2.824 1.627 42.332 43.08 1516.3 236.51 193.1

19.20 4.965 1.640 43.306 43.18 1529.6 240.16 194.7

19.25 7.155 1.654 44.293 43.28 1542.8 243.92 196.2

19.30 9.395 1.667 45.293 43.38 1556.2 247.79 197.8

19.35 11.684 1.681 46.307 43.48 1569.5 251.76 199.4

19.40 14.025 1.695 47.333 43.58 1582.9 255.85 201.0

19.45 16.418 1.708 48.374 43.68 1596.3 260.06 202.7

19.50 18.863 1.722 49.429 43.79 1609.8 264.39 204.3

19.55 21.361 1.736 50.497 43.89 1623.3 268.86 206.0

19.60 23.913 1.750 51.581 43.99 1636.9 273.46 207.6

19.65 26.519 1.764 52.679 44.09 1650.5 278.20 209.3

19.70 29.181 1.778 53.792 44.20 1664.1 283.10 211.1

19.75 31.899 1.792 54.920 44.30 1677.8 288.16 212.8

19.80 34.673 1.806 56.063 44.40 1691.6 293.38 214.5

19.85 37.505 1.820 57.223 44.51 1705.4 298.77 216.3

-244-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 160.00 K (continued)

p P 3P/3T|

p 3P/3p|

T C

V W V A

mo 1 • dm MPa MPa.K"

1 MP a* dm 'mol

1 J/(mol'K)

-

m« s /j.~Pa*s niW/(m-K)

19.90 40.396 1.835 58.398 44.61 1719.2 304.36 218.1

19.95 43.346 1.849 59.589 44.72 1733.2 310.13 219.9

20.00 46.355 1.863 60.797 44.82 1747.1 316.11 221.7

20.05 49.425 1.878 62.021 44.92 1761.2 322.31 223.6

20.10 52.557 1.893 63.262 45.03 1775.3 328.73 225.4

20.15 55.752 1.907 64.519 45.13 1789.4 335.40 227.3

20.20 59.010 1.922 65.794 45.24 1803.6 342.32 229.2

20.25 62.332 1.937 67.087 45.34 1817.9 231.1

20.30 65.719 1.952 68.397 45.45 1832.2 233.1

20.35 69.172 1.967 69.724 45.55 1846.6 235.0

ETHANE ISOTHERM AT T = 170.00 K

Second virial coefficient is -580.1 3 -. - 1 cm »mol

P P 3P/3T|

p 3P/3p|

T CV W n A

mol«dm MPa MPa.K"

1 MP a • dm • mo1 J/(mol'K)

- l m* s /xPa«s rrtW/(m-K)

0.308E -01 0.429E-01 0.2530E-03 1.368 28.79 242.3 5.42 8.2

18.686 0.429E-01 1.465 36.440 42.71 1423.3 201.21 181.2

18.70 0.539 1.469 36.676 42.74 1426.8 201.98 181.6

18.75 2.395 1.481 37.550 42.83 1439.7 204.88 183.1

18.80 4.294 1.494 38.436 42.92 1452.6 207.85 184.5

18.85 6.238 1.507 39.333 43.01 1465.6 210.90 186.0

18.90 8.228 1.519 40.242 43.10 1478.5 214.02 187.5

18.95 10.263 1.532 41.164 43.19 1491.5 217.23 189.0

19.00 12.344 1.545 42.097 43.28 1504.6 220.51 190.5

19.05 14.473 1.558 43.043 43.38 1517.6 223.88 192.1

19.10 16.649 1.571 44.002 43.47 1530.7 227.35 193.6

19.15 18.873 1.584 44.973 43.56 1543.8 230.90 195.2

19.20 21.146 1.597 45.958 43.66 1557.0 234.56 196.8

19.25 23.469 1.610 46.956 43.75 1570.2 238.31 198.4

19.30 25.842 1.623 47.967 43.85 1583.4 242.18 200.0

19.35 28.266 1.636 48.993 43.94 1596.7 246.15 201.7

19.40 30.742 1.650 50.032 44.03 1610.0 250.24 203.3

19.45 33.269 1.663 51.086 44.13 1623.4 254.46 205.0

19.50 35.850 1.676 52.153 44.22 1636.8 258.80 206.7

19.55 38.485 1.690 53.236 44.32 1650.3 263.27 208.4

19.60 41.174 1.704 54.333 44.42 1663.9 267.88 210.1

-245-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 170.00 K (continued)

p P 5P/3T|

p 5P/3 P | t C

V W 1

A

mol«dm MPa MPa-K"

1 MP a • dm • mo

1

1 J/(mol«K)

- l m* s juPa-s mW/(m«K)

19.65 43.919 1.717 55.446 44.51 1677.5 272.64 211.9

19.70 46.719 1.731 56.573 44.61 1691.1 277.55 213.7

19.75 49.576 1.745 57.716 44.70 1704.8 282.63 215.4

19.80 52.491 1.759 58.875 44.80 1718.6 287.87 217.2

19.85 55.464 1.773 60.050 44.89 1732.4 293.29 219.1

19.90 58.496 1.787 61.240 44.99 1746.3 298.90 220.9

19.95 61.588 1.801 62.447 45.09 1760.2 222.7

20.00 64.741 1.815 63.670 45.18 1774.2 224.6

20.05 67.956 1.829 64.910 45.28 1788.2 226.5

ETHANE ISOTHERM AT T = 180.00 K

Second virial coefficient is -519.6

3 .. - 1 cm «mol

P P 5P/3T|

p d?/dp\

T C

V W n A

mo 1 • dm MPa MPa«K

_1

MP a* dm «mol

1 J/(mol«K)

-

1

m* s /iPa«s niW/(m-K)

0.541E -01 0.787E-01 0.4519E-03 1.416 30.26 246.8 5.74 9.1

18.279 0.787E-01 1.333 32.167 42.65 1347.7 176.39 171.5

18.30 0.745 1.338 32.492 42.68 1352.9 177.37 172.1

18.35 2.389 1.350 33.286 42.76 1365.5 179.78 173.4

18.40 4.074 1.362 34.091 42.84 1378.1 182.25 174.8

18.45 5.799 1.374 34.907 42.93 1390.7 184.78 176.2

18.50 7.565 1.386 35.733 43.01 1403.3 187.36 177.6

18.55 9.372 1.398 36.570 43.09 1415.9 190.00 179.0

18.60 11.222 1.410 37.419 43.17 1428.6 192.70 180.5

18.65 13.114 1.422 38.279 43.26 1441.3 195.47 181.9

18.70 15.050 1.434 39.150 43.34 1454.0 198.31 183.4

18.75 17.030 1.446 40.033 43.43 1466.8 201.22 184.9

18.80 19.054 1.458 40.928 43.51 1479.5 204.20 186.4

18.85 21.123 1.471 41.835 43.60 1492.4 207.26 187.9

18.90 23.237 1.483 42.755 43.68 1505.2 210.39 189.4

18.95 25.398 1.496 43.687 43.77 1518.1 213.61 191.0

19.00 27.606 1.508 44.631 43.86 1531.0 216.91 192.5

19.05 29.862 1.521 45.589 43.94 1544.0 220.30 194.1

19.10 32.165 1.533 46.560 44.03 1557.1 223.78 195.7

19.15 34.518 1.546 47.544 44.12 1570.1 227.35 197.3

19.20 36.920 1.559 48.541 44.21 1583.2 231.03 199.0

19.25 39.372 1.571 49.552 44.29 1596.4 234.81 200.6

19.30 41.875 1.584 50.578 44.38 1609.6 238.70 202.3

19.35 44.430 1.597 51.617 44.47 1622.9 242.71 204.0

19.40 47.037 1.610 52.670 44.56 1636.2 246.83 205.7
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 180.00 K (continued)

p P 3P/3T|

p 3P/3p|

T CV W n

A

mol«dm MPa MPa-K'

1 MP a* dm «mol

1 J/(mol«K)

-

m* s /j.Fa-s niW/(m»K)

19.45 49.697 1.623 53.738 44.65 1649.6 251.08 207.4

19.50 52.411 1.637 54.820 44.73 1663.0 255.45 209.1

19.55 55.180 1.650 55.918 44.82 1676.5 259.97 210.9

19.60 58.003 1.663 57.030 44.91 1690.1 264.62 212.7

19.65 60.883 1.677 58.158 45.00 1703.7 214.4

19.70 63.819 1.690 59.300 45.09 1717.3 216.3

19.75 66.813 1.704 60.459 45.18 1731.0 218.1

19.80 69.865 1.717 61.633 45.26 1744.8 219.9

ETHANE ISOTHERM AT T = 190.00 K

Second virial coefficient is -466.7

3 .. - 1 cm «mol

P P 3P/3T|

p ap/a P | T C

V W V A

mol'dm MPa MPa-K"

1 MP,a* dm «mol1 J/(mol-K)

- l m« s /iPa*s niW/(m-K)

0.889E -01 0.135 0.7611E-03 1.450 32.01 250.4 6.06 10.0

17.860 0.135 1.210 28.196 42.73 1271.6 155.75 161.9

17.90 1.285 1.219 28.772 42.79 1281.5 157.37 163.0

17.95 2.741 1.231 29.493 42.86 1293.7 159.41 164.3

18.00 4.234 1.242 30.224 42.93 1306.0 161.49 165.6

18.05 5.764 1.253 30.965 43.00 1318.3 163.62 166.9

18.10 7.331 1.264 31.715 43.08 1330.6 165.79 168.2

18.15 8.936 1.276 32.476 43.15 1342.9 168.01 169.5

18.20 10.579 1.287 33.247 43.23 1355.2 170.28 170.9

18.25 12.261 1.298 34.028 43.30 1367.5 172.60 172.3

18.30 13.982 1.310 34.820 43.38 1379.9 174.97 173.6

18.35 15.743 1.321 35.622 43.46 1392.3 177.39 175.0

18.40 17.544 1.333 36.435 43.53 1404.7 179.88 176.5

18.45 19.386 1.344 37.260 43.61 1417.1 182.41 177.9

18.50 21.270 1.356 38.095 43.69 1429.6 185.01 179.3

18.55 23.196 1.368 38.942 43.77 1442.1 187.67 180.8

18.60 25.165 1.379 39.801 43.85 1454.7 190.40 182.2

18.65 27.176 1.391 40.671 43.92 1467.3 193.19 183.7

18.70 29.232 1.403 41.553 44.00 1479.9 196.05 185.2

18.75 31.332 1.415 42.448 44.08 1492.6 198.98 186.7

18.80 33.477 1.427 43.355 44.16 1505.3 201.98 188.3

18.85 35.668 1.439 44.274 44.24 1518.0 205.07 189.8

18.90 37.905 1.451 45.206 44.32 1530.9 208.23 191.4

18.95 40.188 1.463 46.151 44.41 1543.7 211.48 193.0

19.00 42.520 1.475 47.109 44.49 1556.6 214.81 194.6

247
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 190.00 K (continued)

p P ap/aT|

p 3P/dp|

T CV W n A

mol»dm MPa MPa»K

_1 MP<a* dm «mol

1 J/(mol«K)

-

1

m* s /iPa«s niW/(m.K)

19.05 44.899 1.488 48.080 44.57 1569.6 218.24 196.2

19.10 47.328 1.500 49.064 44.65 1582.6 221.75 197.9

19.15 49.806 1.512 50.062 44.73 1595.6 225.37 199.5

19.20 52.334 1.525 51.074 44.81 1608.7 229.09 201.2

19.25 54.914 1.538 52.099 44.89 1621.9 232.92 202.9

19.30 57.545 1.550 53.139 44.97 1635.1 236.86 204.6

19.35 60.228 1.563 54.193 45.05 1648.4 206.3

19.40 62.964 1.576 55.261 45.14 1661.7 208.0

19.45 65.754 1.589 56.344 45.22 1675.1 209.8

19.50 68.599 1.602 57.442 45.30 1688.6 211.6

ETHANE ISOTHERM AT T = 200.00 K

Second virial coefficient Ls -420.8 3 .. - 1 cm »mol

P P dP/3T|

p d?/d P \'t C

V W 1

A

mol'dm MPa MPa-Kf

1 MP.a «dm «mol

1 J/(mol«K)

- l m* s /iPa«s itiW/ ( m • K

)

0.10 0.159 0.8651E-03 1.523 33.99 255.5 6.38 10.8

0.139 0.217 0.1222E-02 1.467 33.92 253.0 6.39 11.0

17.425 0.217 1.096 24.505 42.94 1194.8 138.23 152.6

17.45 0.839 1.101 24.827 42.97 1200.9 139.09 153.2

17.50 2.097 1.112 25.473 43.03 1212.8 140.80 154.4

17.55 3.386 1.122 26.127 43.10 1224.7 142.55 155.6

17.60 4.709 1.133 26.790 43.16 1236.6 144.33 156.8

17.65 6.066 1.143 27.462 43.22 1248.6 146.15 158.0

17.70 7.456 1.154 28.143 43.29 1260.5 148.01 159.3

17.75 8.880 1.165 28.833 43.35 1272.5 149.90 160.5

17.80 10.339 1.175 29.533 43.42 1284.4 151.83 161.8

17.85 11.834 1.186 30.242 43.49 1296.4 153.80 163.1

17.90 13.364 1.197 30.961 43.56 1308.4 155.81 164.4

17.95 14.930 1.207 31.689 43.63 1320.5 157.87 165.7

18.00 16.533 1.218 32.428 43.69 1332.5 159.96 167.0

18.05 18.173 1.229 33.177 43.76 1344.6 162.11 168.4

18.10 19.850 1.240 33.936 43.84 1356.7 164.30 169.7

18.15 21.566 1.251 34.705 43.91 1368.8 166.54 171.1

18.20 23.321 1.262 35.485 43.98 1381.0 168.82 172.5

18.25 25.115 1.273 36.276 44.05 1393.2 171.16 173.9

18.30 26.949 1.284 37.078 44.12 1405.5 173.56 175.3

18.35 28.823 1.295 37.891 44.19 1417.7 176.01 176.7

18.40 30.738 1.307 38.715 44.27 1430.1 178.51 178.2

18.45 32.695 1.318 39.550 44.34 1442.4 181.08 179.6

248
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 200.00 K (continued)

p P dP/3T|

p d?/dp\

T CV W V A

mo 1 • dm MPa MPa.K"

1 3 MPa «dm 'mol

1 J/(mol.K)

-

m» s /j.Fa»s niW/(m»K)

18.50 34.693 1.329 40.398 44.41 1454.8 183.70 181.1

18.55 36.735 1.341 41.256 44.49 1467.3 186.39 182.6

18.60 38.819 1.352 42.127 44.56 1479.8 189.14 184.1

18.65 40.948 1.364 43.010 44.64 1492.3 191.97 185.6

18.70 43.120 1.375 43.905 44.71 1504.9 194.86 187.1

18.75 45.338 1.387 44.813 44.79 1517.5 197.83 188.7

18.80 47.602 1.399 45.733 44.86 1530.2 200.87 190.2

18.85 49.912 1.411 46.666 44.94 1543.0 204.00 191.8

18.90 52.269 1.422 47.612 45.01 1555.8 207.20 193.4

18.95 54.673 1.434 48.570 45.09 1568.6 210.49 195.0

19.00 57.126 1.446 49.542 45.16 1581.5 213.87 196.7

19.05 59.628 1.459 50.528 45.24 1594.5 217.35 198.3

19.10 62.179 1.471 51.527 45.31 1607.5 200.0

19.15 64.781 1.483 52.540 45.39 1620.5 201.7

19.20 67.433 1.495 53.566 45.46 1633.7 203.4

ETHANE ISOTHERM AT T = 210.00 IC Second virial coefficient iLs -381.0 3 .. - 1 cm »mol

P P 3P/3TI

p ap/dpi1 T C

V W Q A

mol'dm MPa MPa.K"

1 3 MPa«dm »mol

1 J/(mol.K)

- l m» s /^Pa«s niW/(m«K)

0.10 0.168 0.8642E -03 1.613 35.25 261.6 6.69 11.7

0.15 0.247 0.1324E -02 1.546 35.49 258.3 6.71 11.9

0.20 0.323 0.1808E -02 1.477 35.85 255.0 6.73 12.1

0.208 0.334 0.1886E -02 1.466 35.93 254.5 6.73 12.1

16.972 0.334 0.9887 21.074 43.27 1117.4 123.12 143.4

17.00 0.926 0.9941 21.392 43.30 1123.8 123.93 144.0

17.05 2.010 1.004 21.969 43.35 1135.4 125.39 145.1

17.10 3.123 1.014 22.554 43.40 1147.0 126.88 146.2

17.15 4.265 1.024 23.146 43.46 1158.6 128.39 147.4

17.20 5.438 1.033 23.747 43.51 1170.1 129.93 148.5

17.25 6.640 1.043 24.356 43.57 1181.7 131.50 149.7

17.30 7.873 1.053 24.973 43.62 1193.3 133.11 150.8

17.35 9.138 1.063 25.599 43.68 1204.9 134.74 152.0

17.40 10.433 1.073 26.233 43.74 1216.5 136.40 153.2

17.45 11.761 1.083 26.876 43.80 1228.1 138.10 154.4

17.50 13.121 1.093 27.528 43.86 1239.8 139.82 155.6

17.55 14.514 1.104 28.189 43.92 1251.4 141.59 156.9

17.60 15.940 1.114 28.860 43.98 1263.1 143.38 158.1

17.65 17.400 1.124 29.539 44.05 1274.8 145.22 159.4

249
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 210.00 K (continued)

p P 5P/5T|

p d?/dp\

T C

V W 1

A

mol'dm MPa MPa»K

_1 3 MPa* dm 'mol

1 J/(mol'K)

- l m« s /iPa«s itiW/(m«K)

17.70 18.894 1.134 30.228 44.11 1286.6 147.09 160.6

17.75 20.423 1.144 30.927 44.17 1298.3 149.00 161.9

17.80 21.987 1.155 31.635 44.24 1310.1 150.95 163.2

17.85 23.587 1.165 32.353 44.30 1322.0 152.94 164.5

17.90 25.223 1.176 33.081 44.37 1333.8 154.97 165.9

17.95 26.895 1.186 33.820 44.43 1345.7 157.04 167.2

18.00 28.605 1.197 34.568 44.50 1357.6 159.16 168.6

18.05 30.352 1.207 35.328 44.57 1369.6 161.33 169.9

18.10 32.138 1.218 36.097 44.63 1381.6 163.55 171.3

18.15 33.962 1.229 36.878 44.70 1393.6 165.81 172.7

18.20 35.826 1.239 37.669 44.77 1405.7 168.13 174.1

18.25 37.729 1.250 38.472 44.84 1417.9 170.49 175.5

18.30 39.673 1.261 39.285 44.91 1430.0 172.92 177.0

18.35 41.658 1.272 40.110 44.97 1442.3 175.40 178.4

18.40 43.684 1.283 40.947 45.04 1454.5 177.93 179.9

18.45 45.753 1.294 41.795 45.11 1466.9 180.53 181.4

18.50 47.864 1.305 42.656 45.18 1479.2 183.19 182.9

18.55 50.019 1.317 43.528 45.25 1491.7 185.92 184.4

18.60 52.217 1.328 44.412 45.32 1504.1 188.71 185.9

18.65 54.460 1.339 45.309 45.39 1516.7 191.58 187.5

18.70 56.748 1.351 46.218 45.46 1529.2 194.52 189.0

18.75 59.082 1.362 47.139 45.53 1541.9 197.53 190.6

18.80 61.462 1.374 48.074 45.60 1554.5 192.2

18.85 63.890 1.385 49.021 45.67 1567.3 193.8

18.90 66.365 1.397 49.981 45.74 1580.1 195.5

18.95 68.888 1.409 50.955 45.81 1592.9 197.1

250-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 220.00 K

3 - 1 Second virial coefficient is -346.5 cm »mol

p P dP/3T|

p d?/dp\

T CV W >7 A

mol»dm MPa MPa«K

_1

MPaL'dm »mol

1 J/(mol.K)

-

m« s /LiPa*S rriW/(m-K)

0.10 0.177 0.8618E-•03 1.703 36.24 267.6 7.01 12.6

0.15 0.260 0.1317E-02 1.639 36.54 264.5 7.03 12.8

0.20 0.341 0.1792E--02 1.575 36.91 261.3 7.05 12.9

0.25 0.418 0.2289E-•02 1.511 37.38 258.2 7.07 13.1

0.30 0.492 0.2813E-•02 1.445 37.98 255.0 7.09 13.3

0.301 0.492 0.2819E-•02 1.445 37.99 254.9 7.09 13.3

16.498 0.492 0.8877 17.889 43.71 1039.0 109.90 134.5

16.50 0.526 0.8880 17.908 43.71 1039.4 109.94 134.5

16.55 1.434 0.8972 18.414 43.75 1050.6 111.18 135.5

16.60 2.368 0.9063 18.928 43.79 1061.8 112.44 136.6

16.65 3.327 0.9155 19.449 43.84 1073.0 113.72 137.6

16.70 4.313 0.9246 19.978 43.88 1084.2 115.02 138.6

16.75 5.325 0.9339 20.513 43.93 1095.4 116.34 139.7

16.80 6.364 0.9431 21.057 43.97 1106.6 117.69 140.8

16.85 7.431 0.9524 21.608 44.02 1117.8 119.06 141.8

16.90 8.525 0.9617 22.166 44.07 1129.0 120.46 142.9

16.95 9.647 0.9710 22.733 44.12 1140.3 121.88 144.0

17.00 10.798 0.9804 23.308 44.17 1151.5 123.32 145.2

17.05 11.978 0.9898 23.890 44.22 1162.8 124.80 146.3

17.10 13.188 0.9992 24.481 44.28 1174.0 126.30 147.4

17.15 14.427 1.009 25.080 44.33 1185.3 127.82 148.6

17.20 15.696 1.018 25.688 44.38 1196.6 129.38 149.7

17.25 16.996 1.028 26.304 44.44 1208.0 130.96 150.9

17.30 18.326 1.037 26.929 44.50 1219.3 132.58 152.1

17.35 19.689 1.047 27.562 44.55 1230.7 134.23 153.3

17.40 21.083 1.057 28.205 44.61 1242.1 135.91 154.5

17.45 22.509 1.066 28.857 44.67 1253.6 137.62 155.8

17.50 23.969 1.076 29.518 44.73 1265.0 139.36 157.0

17.55 25.461 1.086 30.188 44.79 1276.5 141.14 158.3

17.60 26.987 1.096 30.867 44.85 1288.1 142.96 159.5

17.65 28.548 1.106 31.557 44.91 1299.6 144.82 160.8

17.70 30.143 1.116 32.256 44.97 1311.2 146.71 162.1

17.75 31.774 1.126 32.965 45.03 1322.9 148.64 163.4

17.80 33.440 1.136 33.684 45.09 1334.6 150.61 164.7

17.85 35.142 1.146 34.413 45.15 1346.3 152.63 166.1

17.90 36.881 1.156 35.152 45.22 1358.1 154.68 167.4

17.95 38.658 1.167 35.902 45.28 1369.9 156.78 168.8

18.00 40.472 1.177 36.662 45.34 1381.7 158.93 170.1

18.05 42.324 1.187 37.433 45.41 1393.7 161.13 171.5

18.10 44.215 1.198 38.215 45.47 1405.6 163.37 172.9

251
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 220.00 K (continued)

p P dP/3T|

p dP/d P \ T C

V W 1

A

mol*dm MPa MPa«K

_1 3 MPa* dm *mol

1 J/(mol*K)

-

1

m* s /iPa*s mW/(m*K)

18.15 46.146 1.208 39.008 45.53 1417.6 165.67 174.4

18.20 48.116 1.219 39.812 45.60 1429.6 168.02 175.8

18.25 50.127 1.230 40.628 45.66 1441 .

7

170.42 177.3

18.30 52.179 1.240 41.454 45.72 1453.9 172.88 178.7

18.35 54.273 1.251 42.293 45.79 1466.1 175.39 180.2

18.40 56.409 1.262 43.143 45.85 1478.3 177.97 181.7

18.45 58.587 1.273 44.005 45.92 1490.7 180.61 183.2

18.50 60.809 1.284 44.879 45.98 1503.0 184.7

18.55 63.075 1.295 45.766 46.05 1515.4 186.3

18.60 65.386 1.306 46.664 46.11 1527.9 187.8

18.65 67.742 1.318 47.575 46.18 1540.4 189.4

ETHANE ISOTHERM AT T = 240.00 K

Second virial coefficient is -290.1 3 -- 1 cm *mol

P P 3P/3T|

p dP/dp\

T C

V W n

A

mol'dm MPa MPa^Kf 1 3 MPa* dm *mol

1 J/(mol*K)

-

1

m* s /^Pa*s niW/(m*K)

0.10 0.194 0.8569E--03 1.880 38.12 279.1 7.63 14.5

0.20 0.376 0.1767E--02 1.766 38.68 273.6 7.67 14.8

0.30 0.547 0.2735E--02 1.652 39.35 268.0 7.72 15.1

0.40 0.707 0.3772E--02 1.539 40.17 262.4 7.78 15.5

0.50 0.855 0.4888E--02 1.425 41.20 256.7 7.83 15.9

0.582 0.967 0.5870E--02 1.331 42.24 252.0 7.88 16.2

15.466 0.967 0.7015 12.202 44.93 878.2 87.65 117.4

15.50 1.381 0.7068 12.458 44.94 885.2 88.26 117.9

15.60 2.666 0.7224 13.237 44.97 906.0 90.10 119.6

15.70 4.029 0.7381 14.040 45.02 926.7 92.00 121.4

15.80 5.475 0.7539 14.867 45.07 947.4 93.95 123.1

15.90 7.004 0.7699 15.720 45.12 968.2 95.97 125.0

16.00 8.619 0.7859 16.598 45.19 989.0 98.05 126.8

16.10 10.324 0.8021 17.503 45.25 1009.9 100.20 128.7

16.20 12.121 0.8184 18.434 45.33 1030.7 102.42 130.6

16.30 14.012 0.8349 19.394 45.40 1051.7 104.71 132.6

16.40 16.001 0.8514 20.381 45.49 1072.7 107.08 134.6

16.50 18.089 0.8682 21.398 45.57 1093.9 109.53 136.7

16.60 20.281 0.8851 22.445 45.66 1115.1 112.07 138.8

16.70 22.579 0.9022 23.523 45.75 1136.4 114.70 141.0

16.80 24.987 0.9195 24.633 45.85 1157.8 117.42 143.2

16.90 27.507 0.9369 25.775 45.95 1179.4 120.24 145.4

252
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 240.00 K (continued)

p P 3P/aT|

p d?/dp\

T CV W 1

A

mol'dm MPa MPa«K~

3 MPa 'dm «mol

1 J/(mol«K)

- l m* s /zPa«s niW/(m-K)

17.00 30.143 0.9545 26.950 46.04 1201.1 123.16 147.7

17.10 32.898 0.9724 28.159 46.15 1223.0 126.20 150.0

17.20 35.776 0.9904 29.404 46.25 1245.0 129.35 152.4

17.30 38.780 1.009 30.685 46.36 1267.2 132.63 154.9

17.40 41.914 1.027 32.003 46.46 1289.6 136.04 157.4

17.50 45.182 1.046 33.360 46.57 1312.1 139.59 159.9

17.60 48.588 1.065 34.755 46.68 1334.9 143.28 162.5

17.70 52.134 1.084 36.191 46.79 1357.8 147.13 165.2

17.80 55.827 1.104 37.668 46.90 1380.9 151.14 167.9

17.90 59.669 1.123 39.187 47.01 1404.3 155.34 170.6

18.00 63.666 1.143 40.750 47.12 1427.8 173.5

18.10 67.821 1.164 42.357 47.24 1451.6 176.4

ETHANE ISOTHERM AT T = 260.00 K

Second virial coefficient is -246.2 3 , - 1 cm •mol

P P 3P/dT|

p 3P/3p|

T C

V W n A

mol'dm MPa MPa-Kf

1 MPsL«dm «mol1 J/(mol«K)

- l m* s /LlPa-S ITiW/(m-K)

0.10 0.211 0.8531E-03 2.056 40.14 289.9 8.24 16.6

0.20 0.411 0.1750E-02 1.952 40.58 285.0 8.29 16.9

0.30 0.601 0.2692E-02 1.848 41.05 280.1 8.35 17.2

0.40 0.781 0.3682E-02 1.747 41.56 275.2 8.40 17.5

0.50 0.951 0.4722E-02 1.646 42.12 270.3 8.47 17.8

0.60 1.110 0.5816E-02 1.547 42.75 265.4 8.53 18.1

0.70 1.260 0.6967E-02 1.448 43.46 260.5 8.60 18.5

0.80 1.400 0.8181E-02 1.351 44.26 255.7 8.68 18.9

0.90 1.530 0.9462E-02 1.255 45.17 250.8 8.75 19.3

1.00 1.651 0.1082E-01 1.160 46.18 245.9 8.83 19.8

1.054 1.713 0.1159E-01 1.108 46.79 243.3 8.88 20.1

14.267 1.713 0.5317 7.370 46.65 708.9 69.27 101.2

14.30 1.957 0.5358 7.544 46.64 715.0 69.70 101.6

14.40 2.738 0.5487 8.087 46.62 733.6 71.03 103.0

14.50 3.575 0.5617 8.651 46.61 752.4 72.40 104.3

14.60 4.469 0.5747 9.233 46.60 771.1 73.80 105.7

14.70 5.422 0.5879 9.836 46.61 789.9 75.24 107.2

14.80 6.437 0.6013 10.460 46.62 808.7 76.72 108.6

14.90 7.515 0.6147 11.104 46.63 827.5 78.24 110.1

15.00 8.658 0.6283 11.769 46.66 846.5 79.81 111.7

-253-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 260.00 K (continued)

p P 3P/3T|

p 8?/dp\

T C

V W n A

mo 1 • dm MPa MPa«K

_1 3 MPa • dm *mol

1 J/(mol«K)

-

m» s /iPa«s itiW/(m«K)

15.10 9.869 0.6420 12.457 46.69 865.4 81.42 113.2

15.20 11.150 0.6558 13.166 46.73 884.5 83.08 114.8

15.30 12.503 0.6697 13.899 46.77 903.6 84.79 116.5

15.40 13.931 0.6838 14.654 46.82 922.8 86.54 118.2

15.50 15.435 0.6980 15.434 46.87 942.0 88.36 119.9

15.60 17.019 0.7124 16.238 46.93 961.4 90.22 121.6

15.70 18.684 0.7269 17.067 46.99 980.8 92.15 123.4

15.80 20.433 0.7416 17.921 47.05 1000.4 94.14 125.2

15.90 22.269 0.7565 18.802 47.12 1020.1 96.19 127.1

16.00 24.194 0.7715 19.710 47.19 1039.9 98.31 129.0

16.10 26.212 0.7866 20.645 47.27 1059.8 100.49 131.0

16.20 28.324 0.8020 21.609 47.35 1079.9 102.75 133.0

16.30 30.534 0.8175 22.601 47.43 1100.1 105.09 135.0

16.40 32.845 0.8333 23.624 47.51 1120.5 107.51 137.1

16.50 35.260 0.8492 24.677 47.60 1141.0 110.02 139.2

16.60 37.782 0.8653 25.762 47.69 1161.6 112.61 141.4

16.70 40.414 0.8816 26.879 47.77 1182.5 115.30 143.6

16.80 43.159 0.8982 28.029 47.86 1203.5 118.08 145.8

16.90 46.020 0.9150 29.213 47.96 1224.7 120.97 148.1

17.00 49.002 0.9320 30.432 48.05 1246.1 123.97 150.5

17.10 52.108 0.9492 31.686 48.14 1267.7 127.09 152.9

17.20 55.341 0.9667 32.978 48.24 1289.5 130.33 155.4

17.30 58.705 0.9844 34.307 48.34 1311.5 133.70 157.9

17.40 62.203 1.002 35.674 48.43 1333.8 160.4

17.50 65.841 1.021 37.081 48.53 1356.2 163.0

17.60 69.621 1.039 38.529 48.63 1378.8 165.7

-254
Table B4

.

Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 273.15 K

3 - 1 Second virial coefficient is -222.5 cm «mol

p P 3P/STI 3P/3p| C W n X

p T v -3 -1 3-1 -1 mol«dm " MPa MPa«K MPa«dm »mol ' J/(mol«K) m»s ' p-Pa»s mW/(m«K)

0.10 0.222 0.8511E-03 2.171 41.56

0.20 0.434 0.1742E-02 2.072 41.93

0.30 0.637 0.2673E-02 1.974 42.32

0.40 0.829 0.3645E-02 1.879 42.73

0.50 1.012 0.4659E-02 1.784 43.16

0.60 1.186 0.5716E-02 1.691 43.62

0.70 1.351 0.6818E-02 1.600 44.11

0.80 1.506 0.7965E-02 1.510 44.64

0.90 1.653 0.9161E-02 1.421 45.22

1.00 1.790 0.1041E-01 1.334 45.83

1.10 1.919 0.1170E-01 1.248 46.50

1.20 2.040 0.1306E-01 1.164 47.23

1.30 2.152 0.1447E-01 1.081 48.02

1.40 2.256 0.1594E-01 1.000 48.87

1.50 2.352 0.1748E-01 0.920 49.80

1.539 2.387 0.1810E-01 0.889 50.18

13.321 2.387 0.4253 4.641 48.17

13.40 2.766 0.4339 4.946 48.11

13.50 3.280 0.4448 5.348 48.05

13.60 3.836 0.4559 5.766 47.99

13.70 4.434 0.4671 6.200 47.94

13.80 5.076 0.4784 6.651 47.91

13.90 5.765 0.4898 7.119 47.88

14.00 6.501 0.5014 7.605 47.85

14.10 7.286 0.5131 8.109 47.84

14.20 8.123 0.5249 8.632 47.83

14.30 9.013 0.5369 9.173 47.83

14.40 9.958 0.5490 9.733 47.84

14.50 10.960 0.5612 10.312 47.85

14.60 12.021 0.5736 10.911 47.87

4671

4784

4898

5014

5131

5249

5369

5490

5612

5736

5860

5987

6114

6243

6374

6506

6639

6774

6911

7050

14.70 13.143 0.5860 11.531 47.89

14.80 14.328 0.5987 12.172 47.92

14.90 15.578 0.6114 12.833 47.96

15.00 16.896 0.6243 13.516 48.00

15.10 18.282 0.6374 14.222 48.04

15.20 19.741 0.6506 14.950 48.09

15.30 21.273 0.6639 15.702 48.14

15.40 22.882 0.6774 16.477 48.20

15.50 24.569 0.6911 17.277 48.26

15.60 26.338 0.7050 18.101 48.32

255-

296 7 8.64 18 1 292 1 8.69 18 3 287 6 8.75 18 6

283 1 8.81 18 9

278 6 8.88 19 2

274 1 8.94 19 5 269 7 9.02 19 9 265 3 9.09 20 2 260 9 9.17 20 6 256 6 9.26 21

252 3 9.34 21 4

248 9.44 21 9

243 7 9.53 22 4

239 5 9.63 22 9 235 3 9.73 23 5

233 6 9.77 23 7 588 7 58.45 90 9 602 59.27 91 7 618 9 60.34 92 8 635 9 61.43 94

653 62.55 95 1 670 1 63.70 96 3 687 3 64.87 97 5 704 6 66.08 98 8 721 9 67.31 100 1

739 3 68.58 101 4

756 8 69.89 102 7 774 4 71.23 104 1 792 72.60 105 5 809 8 74.01 106 9

827 6 75.46 108 4

845 5 76.96 109 9 863 6 78.49 111 4

881 7 80.07 113

899 9 81.70 114 6

918 3 83.37 116 2 936 8 85.10 117 9 955 3 86.87 119 6 974 1 88.71 121 3 992 9 90.59 123 1
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 273.15 K (continued)

Second virial coefficient is -222.5 cm »mol

mol'•dm

15,,70

15.,80

15,.90

16,.00

16 .10

16 .20

16 .30

16,.40

16,.50

16,.60

16 .70

16 .80

16 .90

17,.00

17,,10

-3

MPa

dP/dT\

p

dP/dp\

T

CvW

-1 3 -1 -1

MPa»K MPa»dm »mol J/(mol»K) m»s

n a

^Pa«s mW/(m«K)

28.190

30.129

32.157

34.276

36.490

38.802

41.214

43.729

46.351

49.082

51.926

54.887

57.967

61.171

64.501

0.,7190

0..7331

0..7475

.7621

0..7768

.7917

.8069

.8222

0..8378

0,.8535

0,.8695

.8858

.9022

0,.9190

0,,9359

18 ,952 48 .38 1011 .9 92 ,54 124,,9

19 .828 48 ,45 1031 .0 94 .56 126 .8 20 .732 48 ,52 1050 .3 96 .63 128 .7 21 .663 48 ,60 1069 .8 98 .78 130,.6 22 .623 48 ,67 1089 .4 101 .00 132,.6

23 .611 48,.75 1109,.2 103,.29 134,.6 24,.630 48 .83 1129..1 105 .66 136,,7

25,.679 48,.91 1149,.2 108,.12 138,.8 26..760 48,.99 1169,,6 110,.66 141,,0

27,.873 49,.08 1190,,1 113 .30 143,,2

29,.019 49,.16 1210, 8 116,,03 145, 4

30,.199 49,,25 1231.,7 118,,86 147. 7 31,.413 49,,34 1252,,8 121.,80 150. 1 32,,664 49,,43 1274. 1 152. 5 33,,951 49,,52 1295. 6 154..9

17.20 67.962 0.9531 35.275 49.60 1317.4 157.4

ETHANE ISOTHERM AT T = 280.00 K

Second virial coefficient is -211.4 cm «mol

p P SP/3TI

P 3P/3p|

T

C

V

W V

A

mol -dm MPa MPa«K" MPa •dm «mol

' 1 J/(mol-K)

-1 m» s /iPa«s mW/(m«K)

0.10 0.228 0.8502E-03 2.230 42.32 300.1 8.85 18.9

0.20 0.446 0.1738E-02 2.134 42.67 295.7 8.90 19.1

0.30 0.655 0.2664E-02 2.039 43.02 291.4 8.96 19.4

0.40 0.854 0.3629E-02 1.946 43.39 287.0 9.02 19.7

0.50 1.044 0.4633E-02 1.855 43.78 282.7 9.09 20.0

0.60 1.225 0.5676E-02 1.765 44.18 278.5 9.16 20.3

0.70 1.397 0.6760E-02 1.676 44.60 274.2 9.23 20.6

0.80 1.560 0.7886E-02 1.589 45.05 270.0 9.31 20.9

0.90 1.715 0.9053E-02 1.504 45.53 265.9 9.39 21.3

1.00 1.861 0.1026E-01 1.420 46.03 261.8 9.47 21.7

1.10 1.999 0.1152E-01 1.337 46.57 257.7 9.56 22.1

1.20 2.129 0.1282E-01 1.257 47.14 253.7 9.66 22.5

1.30 2.250 0.1417E-01 1.178 47.74 249.7 9.75 23.0

1.40 2.364 0.1557E-01 1.100 48.39 245.7 9.85 23.5

1.50 2.470 0.1701E-01 1.024 49.09 241.8 9.95 24.0

-256-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 280.00 K (continued)

p P dP/3T|

p dF/dp\

T CV W 1

A

mol«dm MPa MPa^K"

1 MPs[•dm «mol

1 J/(mol«K)

-

m* s (j.Pa*s rr W/(m-K)

1.60 2.569 0.1852E-01 0.949 49.83 237.9 10.06 24.5

1.70 2.660 0.2007E-01 0.876 50.63 234.0 10.17 25.2

1.80 2.744 0.2169E-01 0.804 51.48 230.2 10.29 25.8

1.882 2.808 0.2305E-01 0.747 52.22 227.2 10.38 26.4

12.742 2.808 0.3699 3.361 49.18 520.9 52.96 85.5

12.80 3.008 0.3756 3.540 49.12 530.1 53.49 86.1

12.90 3.378 0.3855 3.860 49.01 545.9 54.42 87.0

13.00 3.781 0.3954 4.194 48.92 561.8 55.37 88.0

13.10 4.217 0.4055 4.543 48.84 577.7 56.34 89.0

13.20 4.690 0.4157 4.906 48.77 593.8 57.33 90.1

13.30 5.199 0.4261 5.285 48.71 609.9 58.35 91.1

13.40 5.747 0.4365 5.679 48.65 626.1 59.39 92.2

13.50 6.335 0.4471 6.089 48.61 642.3 60.46 93.4

13.60 6.965 0.4578 6.516 48.57 658.7 61.56 94.5

13.70 7.639 0.4686 6.959 48.54 675.2 62.68 95.7

13.80 8.358 0.4796 7.419 48.52 691.8 63.83 96.9

13.90 9.123 0.4907 7.896 48.51 708.4 65.01 98.1

14.00 9.938 0.5020 8.391 48.50 725.2 66.22 99.4

14.10 10.802 0.5133 8.904 48.50 742.0 67.46 100.7

14.20 11.719 0.5248 9.435 48.50 759.0 68.73 102.0

14.30 12.690 0.5365 9.985 48.51 776.0 70.04 103.4

14.40 13.717 0.5483 10.554 48.53 793.2 71.38 104.8

14.50 14.801 0.5602 11.143 48.55 810.4 72.76 106.2

14.60 15.946 0.5722 11.752 48.57 827.8 74.18 107.6

14.70 17.152 0.5844 12.381 48.61 845.3 75.64 109.1

14.80 18.423 0.5967 13.031 48.64 862.9 77.14 110.6

14.90 19.759 0.6092 13.703 48.68 880.6 78.68 112.1

15.00 21.164 0.6219 14.396 48.73 898.4 80.27 113.7

15.10 22.639 0.6347 15.112 48.78 916.4 81.91 115.3

15.20 24.187 0.6476 15.851 48.83 934.5 83.59 117.0

15.30 25.810 0.6607 16.613 48.88 952.7 85.32 118.7

15.40 27.511 0.6740 17.400 48.94 971.1 87.11 120.4

15.50 29.291 0.6874 18.211 49.00 989.6 88.95 122.2

15.60 31.154 0.7010 19.047 49.07 1008.3 90.86 123.9

15.70 33.101 0.7148 19.910 49.13 1027.1 92.82 125.8

15.80 35.136 0.7288 20.799 49.20 1046.1 94.84 127.7

15.90 37.262 0.7430 21.715 49.27 1065.3 96.94 129.6

16.00 39.480 0.7573 22.659 49.35 1084.6 99.10 131.5

16.10 41.795 0.7719 23.632 49.42 1104.1 101.33 133.5

16.20 44.208 0.7866 24.635 49.50 1123.7 103.64 135.6

-257-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 280.00 K (continued)

p P 5P/5T|

p 8F/d P \ T C

V W n A

mol«dm MPa MPa«K

_1 3 MPa* dm «mol

1 J/(mol»K)

-

1

m» s /xPa»s mW/(m»K)

16.30 46.723 0.8016 25.668 49.58 1143.6 106.04 137.6

16.40 49.342 0.8168 26.732 49.66 1163.7 108.51 139.8

16.50 52.070 0.8322 27.828 49.74 1183.9 111.08 141.9

16.60 54.909 0.8478 28.956 49.82 1204.4 113.73 144.2

16.70 57.862 0.8637 30.118 49.90 1225.0 116.49 146.4

16.80 60.934 0.8798 31.314 49.99 1245.9 148.7

16.90 64.126 0.8961 32.546 50.07 1267.0 151.1

17.00 67.444 0.9127 33.813 50.16 1288.3 153.5

ETHANE ISOTHERM AT T = 298.15 K

Second virial coefficient is -185.5 3

1 - 1 cm »mol

P P 3P/3T|

p d?/dp\

T C

V W n

A

mol«dm MPa MPa.K"

1 MPsfdm *mol1 J/(mol«K)

-

1

m* s jj.Fa>s itiW/(m-K)

0.10 0.243 0.8483E -03 2.388 44.43 309.0 9.39 21.1

0.20 0.478 0.1730E -02 2.298 44.71 305.0 9.44 21.4

0.30 0.703 0.2646E.-02 2.210 44.99 301.1 9.51 21.6

0.40 0.920 0.3596E--02 2.123 45.28 297.2 9.57 21.9

0.50 1.128 0.4579E -02 2.038 45.58 293.3 9.64 22.1

0.60 1.327 0.5596E--02 1.955 45.88 289.5 9.71 22.4

0.70 1.519 0.6647E--02 1.873 46.19 285.7 9.79 22.7

0.80 1.702 0.7732E--02 1.793 46.51 282.0 9.87 23.0

0.90 1.877 0.8850E--02 1.714 46.84 278.3 9.96 23.3

1.00 2.045 0.1000E--01 1.637 47.17 274.7 10.04 23.7

1.10 2.205 0.1119E--01 1.562 47.51 271.2 10.13 24.0

1.20 2.357 0.1241E--01 1.488 47.87 267.6 10.23 24.4

1.30 2.502 0.1366E--01 1.416 48.23 264.2 10.33 24.8

1.40 2.640 0.1495E--01 1.346 48.60 260.8 10.43 25.2

1.50 2.772 0.1627E--01 1.277 48.99 257.4 10.54 25.6

1.60 2.896 0.1762E-01 1.210 49.39 254.1 10.64 26.1

1.70 3.014 0.1901E-01 1.145 49.80 250.9 10.76 26.5

1.80 3.125 0.2043E-01 1.081 50.23 247.7 10.87 27.0

1.90 3.230 0.2188E-01 1.019 50.67 244.6 10.99 27.5

2.00 3.329 0.2337E-01 0.959 51.13 241.6 11.12 28.1

2.10 3.422 0.2489E-01 0.900 51.60 238.6 11.24 28.7

2.20 3.509 0.2645E-01 0.843 52.09 235.7 11.37 29.3

2.30 3.590 0.2803E-01 0.787 52.60 232.8 11.51 29.9

2.40 3.666 0.2965E-01 0.734 53.12 230.0 11.65 30.6

2.50 3.737 0.3131E- 01 0.682 53.67 227.3 11.79 31.4

258-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 298.15 K (continued)

p P 3P/3T|

p 't C

V W n

A

mol'dm MPa MPa-K"

1 MPsfdm «raol

1 J/(mol«K)

-

m« s /iPa«s niW/(m»K)

2.60 3.803 0.3299E-•01 0.631 54.23 224.6 11.93 32.2

2.70 3.863 0.3471E-•01 0.583 54.81 222.0 12.08 33.0

2.80 3.919 0.3646E-•01 0.536 55.42 219.5 12.23 33.9

2.90 3.971 0.3824E-•01 0.491 56.04 217.0 12.39 34.8

3.00 4.018 0.4006E-•01 0.447 56.69 214.6 12.55 35.9

3.10 4.060 0.4190E-•01 0.405 57.36 212.2 12.71 37.0

3.20 4.099 0.4377E-01 0.365 58.05 210.0 12.87 38.2

3.30 4.133 0.4567E-01 0.326 58.77 207.8 13.04 39.5

3.40 4.164 0.4759E-01 0.290 59.50 205.6 13.22 41.0

3.496 4.190 0.4946E-01 0.256 60.23 203.6 13.39 42.5

10.468 4.190 0.2084 0.626 54.94 303.9 36.98 71.9

10.50 4.211 0.2104 0.655 54.79 307.4 37.17 72.0

10.60 4.281 0.2167 0.750 54.36 318.1 37.75 72.1

10.70 4.361 0.2231 0.852 53.97 328.9 38.34 72.4

10.80 4.452 0.2296 0.962 53.62 339.9 38.94 72.7

10.90 4.554 0.2361 1.079 53.29 351.0 39.56 73.1

11.00 4.668 0.2428 1.205 52.99 362.3 40.18 73.6

11.10 4.795 0.2496 1.338 52.72 373.7 40.82 74.1

11.20 4.936 0.2565 1.481 52.47 385.2 41.47 74.6

11.30 5.091 0.2635 1.632 52.24 396.9 42.13 75.2

11.40 5.263 0.2706 1.794 52.04 408.7 42.80 75.8

11.50 5.450 0.2779 1.965 51.85 420.7 43.49 76.5

11.60 5.656 0.2852 2.146 51.68 432.8 44.20 77.2

11.70 5.880 0.2927 2.338 51.52 445.2 44.91 77.9

11.80 6.124 0.3003 2.540 51.38 457.7 45.65 78.6

11.90 6.388 0.3080 2.754 51.25 470.3 46.40 79.4

12.00 6.675 0.3158 2.980 51.13 483.2 47.16 80.2

12.10 6.985 0.3238 3.217 51.02 496.2 47.94 81.0

12.20 7.319 0.3319 3.467 50.92 509.3 48.74 81.8

12.30 7.679 0.3401 3.729 50.83 522.7 49.55 82.7

12.40 8.065 0.3485 4.004 50.75 536.2 50.38 83.6

12.50 8.480 0.3570 4.292 50.68 549.8 51.23 84.5

12.60 8.924 0.3657 4.593 50.61 563.7 52.10 85.5

12.70 9.399 0.3744 4.908 50.55 577.7 52.99 86.4

12.80 9.906 0.3833 5.237 50.50 591.8 53.91 87.4

12.90 10.447 0.3924 5.580 50.46 606.1 54.84 88.4

13.00 11.022 0.4016 5.937 50.42 620.5 55.79 89.4

13.10 11.635 0.4109 6.310 50.39 635.1 56.77 90.5

13.20 12.285 0.4203 6.697 50.37 649.9 57.77 91.6

13.30 12.975 0.4299 7.100 50.35 664.7 58.79 92.7

-259-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 298.15 K (continued)

p P dP/3T|

p 3P/dp|

x C

V W 1

A

mol'dm MPa MPa.K"

1 3 MPa 'dm »mol J/(mol«K) ra«s /iPa«s iriW/(m-K)

13.40 13.705 0.4397 7.518 50.34 679.8 59.84 93.8

13.50 14.479 0.4495 7.953 50.33 694.9 60.92 95.0

13.60 15.296 0.4595 8.403 50.33 710.2 62.02 96.2

13.70 16.160 0.4697 8.871 50.33 725.6 63.15 97.4

13.80 17.071 0.4800 9.356 50.34 741.2 64.31 98.6

13.90 18.032 0.4904 9.858 50.35 756.9 65.50 99.9

14.00 19.043 0.5009 10.377 50.37 772.7 66.72 101.2

14.10 20.108 0.5116 10.916 50.39 788.7 67.98 102.5

14.20 21.227 0.5225 11.472 50.42 804.9 69.26 103.9

14.30 22.403 0.5335 12.048 50.45 821.1 70.59 105.3

14.40 23.637 0.5446 12.643 50.48 837.5 71.95 106.7

14.50 24.932 0.5559 13.258 50.52 854.1 73.34 108.1

14.60 26.290 0.5674 13.894 50.56 870.8 74.78 109.6

14.70 27.712 0.5790 14.551 50.60 887.6 76.26 111.1

14.80 29.200 0.5907 15.229 50.65 904.6 77.78 112.7

14.90 30.758 0.6026 15.929 50.70 921.8 79.34 114.3

15.00 32.387 0.6147 16.651 50.75 939.1 80.96 115.9

15.10 34.089 0.6270 17.397 50.80 956.6 82.62 117.5

15.20 35.867 0.6394 18.166 50.86 974.2 84.33 119.2

15.30 37.723 0.6520 18.959 50.92 992.0 86.09 120.9

15.40 39.660 0.6648 19.777 50.98 1010.0 87.91 122.7

15.50 41.679 0.6778 20.621 51.04 1028.2 89.78 124.5

15.60 43.785 0.6909 21.491 51.11 1046.5 91.72 126.3

15.70 45.979 0.7043 22.388 51.18 1065.1 93.72 128.2

15.80 48.263 0.7178 23.312 51.24 1083.8 95.78 130.1

15.90 50.642 0.7316 24.264 51.31 1102.7 97.92 132.0

16.00 53.117 0.7456 25.246 51.39 1121.8 100.12 134.0

16.10 55.692 0.7597 26.257 51.46 1141.2 102.41 136.1

16.20 58.369 0.7741 27.298 51.53 1160.7 104.77 138.1

16.30 61.153 0.7887 28.371 51.61 1180.4 140.3

16.40 64.045 0.8036 29.476 51.68 1200.4 142.4

16.50 67.049 0.8187 30.613 51.76 1220.5 144.6

-260
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 300.00 K

3 - 1 Second virial coefficient is -183.1 cm «mol

p P aP/3T|

p d?/dp\

r C

V W r\ A

mol«dm MPa MPa-K"

1 MPa •dm «mol

1 J/(mol«K)

-

1

m« s /zPa»s mW/(m«K)

0.10 0.245 0.8481E-03 2.404 44.65 309.9 9.44 21.3

0.20 0.481 0.1730E-02 2.315 44.92 305.9 9.50 21.6

0.30 0.708 0.2645E-02 2.227 45.20 302.0 9.56 21.8

0.40 0.926 0.3593E-02 2.141 45.49 298.2 9.63 22.1

0.50 1.136 0.4575E-02 2.057 45.78 294.3 9.70 22.4

0.60 1.338 0.5589E-02 1.974 46.07 290.6 9.77 22.6

0.70 1.531 0.6638E-02 1.893 46.37 286.8 9.85 22.9

0.80 1.716 0.7719E-02 1.813 46.68 283.2 9.93 23.2

0.90 1.894 0.8834E-02 1.735 47.00 279.6 10.01 23.5

1.00 2.063 0.9981E-02 1.659 47.32 276.0 10.10 23.9

1.10 2.225 0.1116E-01 1.584 47.65 272.5 10.19 24.2

1.20 2.380 0.1238E-01 1.511 47.99 269.0 10.29 24.6

1.30 2.528 0.1362E-01 1.440 48.34 265.6 10.39 25.0

1.40 2.668 0.1490E-01 1.370 48.70 262.2 10.49 25.4

1.50 2.802 0.1621E-01 1.302 49.07 258.9 10.59 25.8

1.60 2.928 0.1756E-01 1.235 49.45 255.7 10.70 26.2

1.70 3.049 0.1893E-01 1.171 49.84 252.5 10.82 26.7

1.80 3.163 0.2034E-01 1.107 50.24 249.4 10.93 27.2

1.90 3.270 0.2178E-01 1.046 50.66 246.3 11.05 27.7

2.00 3.372 0.2326E-01 0.986 51.08 243.3 11.18 28.2

2.10 3.468 0.2476E-01 0.928 51.53 240.4 11.30 28.8

2.20 3.558 0.2630E-01 0.872 51.99 237.5 11.43 29.4

2.30 3.642 0.2787E-01 0.817 52.46 234.7 11.57 30.0

2.40 3.721 0.2947E-01 0.764 52.95 232.0 11.71 30.7

2.50 3.795 0.3110E-01 0.712 53.45 229.3 11.85 31.4

2.60 3.864 0.3276E-01 0.663 53.97 226.7 11.99 32.1

2.70 3.927 0.3446E-01 0.615 54.51 224.2 12.14 32.9

2.80 3.987 0.3618E-01 0.568 55.06 221.7 12.29 33.8

2.90 4.041 0.3793E-01 0.524 55.63 219.3 12.45 34.7

3.00 4.091 0.3971E-01 0.480 56.23 216.9 12.61 35.6

3.10 4.137 0.4151E-01 0.439 56.83 214.7 12.77 36.6

3.20 4.179 0.4334E-01 0.399 57.46 212.5 12.94 37.7

3.30 4.217 0.4520E-01 0.361 58.11 210.3 13.11 38.9

3.40 4.252 0.4708E-01 0.325 58.77 208.2 13.28 40.2

3.50 4.282 0.4899E-01 0.291 59.45 206.2 13.46 41.6

3.60 4.310 0.5091E-01 0.258 60.15 204.3 13.64 43.2

3.70 4.334 0.5286E-01 0.226 60.87 202.4 13.82 44.9

3.80 4.355 0.5482E-01 0.197 61.61 200.6 14.01 46.8

3.808 4.357 0.5497E-01 0.194 61.67 200.5 14.02 46.9

10.084 4.357 0.1892 0.433 56.47 276.8 34.92 71.4

-261
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 300.00 K (continued)

p P dP/3T|

p d?/dp\

't C

V W V A

mol'dm MPa MPa.K"

1 3 MPa* dm »mol

1 J/(mol«K)

- l m* s ^Pa«s rriW/(m«K)

10.10 4.364 0.1901 0.444 56.39 278.3 35.00 71.3

10.20 4.412 0.1957 0.516 55.87 287.9 35.54 71.2

10.30 4.467 0.2014 0.594 55.39 297.7 36.09 71.2

10.40 4.531 0.2073 0.678 54.95 307.7 36.65 71.3

10.50 4.603 0.2133 0.769 54.54 317.8 37.22 71.5

10.60 4.684 0.2194 0.866 54.16 328.1 37.80 71.8

10.70 4.776 0.2256 0.970 53.82 338.6 38.39 72.2

10.80 4.879 0.2319 1.081 53.50 349.2 38.99 72.6

10.90 4.993 0.2383 1.201 53.21 359.9 39.60 73.0

11.00 5.119 0.2448 1.328 52.94 370.9 40.23 73.5

11.10 5.259 0.2515 1.464 52.70 381.9 40.86 74.1

11.20 5.412 0.2583 1.608 52.47 393.2 41.51 74.6

11.30 5.581 0.2652 1.762 52.27 404.6 42.18 75.2

11.40 5.765 0.2722 1.925 52.08 416.2 42.85 75.9

11.50 5.966 0.2793 2.098 51.91 427.9 43.54 76.6

11.60 6.185 0.2865 2.282 51.75 439.9 44.24 77.3

11.70 6.423 0.2939 2.476 51.61 452.0 44.96 78.0

11.80 6.680 0.3014 2.681 51.47 464.3 45.69 78.7

11.90 6.959 0.3090 2.897 51.35 476.8 46.44 79.5

12.00 7.260 0.3168 3.125 51.24 489.5 47.21 80.3

12.10 7.585 0.3247 3.365 51.14 502.4 47.99 81.1

12.20 7.934 0.3327 3.617 51.05 515.4 48.78 82.0

12.30 8.309 0.3409 3.882 50.97 528.6 49.60 82.8

12.40 8.711 0.3492 4.159 50.89 542.0 50.43 83.7

12.50 9.141 0.3577 4.450 50.83 555.6 51.28 84.7

12.60 9.601 0.3662 4.754 50.77 569.3 52.15 85.6

12.70 10.092 0.3749 5.071 50.72 583.2 53.04 86.6

12.80 10.616 0.3838 5.402 50.67 597.2 53.96 87.6

12.90 11.173 0.3928 5.748 50.63 611.4 54.89 88.6

13.00 11.766 0.4019 6.108 50.60 625.8 55.84 89.6

13.10 12.395 0.4112 6.483 50.57 640.3 56.82 90.7

13.20 13.063 0.4206 6.873 50.55 654.9 57.82 91.8

13.30 13.770 0.4301 7.278 50.54 669.7 58.85 92.9

13.40 14.519 0.4398 7.699 50.53 684.6 59.90 94.0

13.50 15.310 0.4496 8.136 50.52 699.7 60.97 95.2

13.60 16.147 0.4595 8.589 50.52 714.9 62.08 96.4

13.70 17.029 0.4696 9.059 50.53 730.3 63.21 97.6

13.80 17.959 0.4798 9.547 50.54 745.8 64.37 98.8

13.90 18.939 0.4902 10.051 50.55 761.4 65.56 100.1

14.00 19.970 0.5007 10.574 50.57 777.2 66.78 101.4

262
Table B4 . Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 300.00 K (continued)

p P 5P/3T|

p dP/dp\

T CV W r] A

mol'dm MPa MPa«K

_1 3 MPa* dm »mol

1 J/(mol«K)

-

m« s /xPa«s rr W/(m«K)

14.10 21.054 0.5113 11.114 50.59 793.1 68.04 102.7

14.20 22.193 0.5221 11.674 50.62 809.1 69.33 104.1

14.30 23.389 0.5331 12.252 50.65 825.3 70.65 105.5

14.40 24.644 0.5442 12.850 50.69 841.7 72.01 106.9

14.50 25.960 0.5554 13.468 50.72 858.2 73.41 108.4

14.60 27.339 0.5668 14.107 50.76 874.8 74.85 109.8

14.70 28.782 0.5784 14.766 50.81 891.6 76.33 111.4

14.80 30.293 0.5901 15.447 50.86 908.6 77.85 112.9

14.90 31.872 0.6019 16.150 50.91 925.7 79.42 114.5

15.00 33.524 0.6140 16.876 50.96 943.0 81.04 116.1

15.10 35.248 0.6262 17.625 51.01 960.4 82.70 117.8

15.20 37.049 0.6386 18.397 51.07 978.1 84.41 119.4

15.30 38.929 0.6511 19.194 51.13 995.8 86.18 121.2

15.40 40.889 0.6639 20.015 51.19 1013.8 88.00 122.9

15.50 42.932 0.6768 20.862 51.26 1032.0 89.88 124.7

15.60 45.062 0.6899 21.736 51.32 1050.3 91.82 126.5

15.70 47.281 0.7033 22.636 51.39 1068.8 93.82 128.4

15.80 49.590 0.7168 23.564 51.46 1087.5 95.89 130.3

15.90 51.994 0.7305 24.520 51.53 1106.4 98.03 132.3

16.00 54.495 0.7444 25.506 51.60 1125.5 100.24 134.3

16.10 57.096 0.7586 26.521 51.67 1144.8 102.53 136.3

16.20 59.801 0.7729 27.566 51.74 1164.3 104.89 138.4

16.30 62.611 0.7875 28.643 51.82 1184.1 140.5

16.40 65.530 0.8023 29.752 51.89 1204.0 142.7

16.50 68.562 0.8174 30.894 51.97 1224.2 144.9

263
Table B4 . Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 305.33

3 - 1 Second virial coefficient is -176.5 cm »mol

p P 3P/3T|

p SP/dp|

T CV W V A

mol»dm MPa MPa.K"

1 MPa • dm • mo1 J/(mol«K)

- l m» s /xPa«s itiW/(m«K)

0.10 0.249 0.8477E-03 2.450 45.29 312.4 9.60 22.0

0.20 0.490 0.1728E-02 2.362 45.55 308.5 9.66 22.3

0.30 0.722 0.2640E-02 2.277 45.81 304.8 9.72 22.5

0.40 0.945 0.3585E-02 2.192 46.08 301.0 9.79 22.8

0.50 1.160 0.4562E-02 2.110 46.35 297.3 9.86 23.0

0.60 1.367 0.5571E-02 2.029 46.62 293.7 9.93 23.3

0.70 1.566 0.6612E-02 1.949 46.90 290.1 10.01 23.6

0.80 1.757 0.7685E-02 1.871 47.19 286.5 10.09 23.9

0.90 1.941 0.8790E-02 1.795 47.48 283.0 10.18 24.2

1.00 2.116 0.9926E-02 1.720 47.77 279.6 10.27 24.5

1.10 2.285 0.1109E-01 1.647 48.07 276.2 10.36 24.8

1.20 2.446 0.1229E-01 1.576 48.38 272.8 10.45 25.2

1.30 2.600 0.1352E-01 1.506 48.69 269.6 10.55 25.6

1.40 2.747 0.1478E-01 1.438 49.01 266.3 10.66 26.0

1.50 2.888 0.1607E-01 1.372 49.33 263.2 10.76 26.4

1.60 3.022 0.1739E-01 1.307 49.67 260.1 10.87 26.8

1.70 3.149 0.1875E-01 1.244 50.01 257.0 10.99 27.2

1.80 3.270 0.2013E-01 1.183 50.35 254.0 11.10 27.7

1.90 3.386 0.2154E-01 1.123 50.71 251.1 11.22 28.2

2.00 3.495 0.2298E-01 1.065 51.07 248.3 11.35 28.7

2.10 3.599 0.2444E-01 1.008 51.45 245.5 11.47 29.2

2.20 3.697 0.2594E-01 0.953 51.83 242.8 11.61 29.7

2.30 3.789 0.2746E-01 0.900 52.22 240.1 11.74 30.3

2.40 3.877 0.2902E-01 0.849 52.62 237.5 11.88 30.9

2.50 3.959 0.3059E-01 0.799 53.03 235.0 12.02 31.5

2.60 4.037 0.3220E-01 0.750 53.45 232.6 12.17 32.2

2.70 4.109 0.3383E-01 0.704 53.88 230.2 12.31 32.9

2.80 4.177 0.3548E-01 0.659 54.32 227.9 12.47 33.6

2.90 4.241 0.3716E-01 0.615 54.77 225.6 12.62 34.4

3.00 4.301 0.3887E-01 0.574 55.23 223.5 12.78 35.2

3.10 4.356 0.4059E-01 0.534 55.71 221.4 12.94 36.0

3.20 4.407 0.4234E-01 0.495 56.19 219.3 13.11 36.9

3.30 4.455 0.4411E-01 0.458 56.68 217.4 13.28 37.9

3.40 4.499 0.4589E-01 0.423 57.18 215.5 13.45 38.9

3.50 4.540 0.4770E-01 0.390 57.70 213.6 13.63 39.9

3.60 4.577 0.4952E-01 0.358 58.22 211.9 13.81 41.0

3.70 4.611 0.5135E-01 0.327 58.75 210.2 14.00 42.2

3.80 4.643 0.5320E-01 0.298 59.29 208.5 14.18 43.4

3.90 4.671 0.5506E-01 0.271 59.83 207.0 14.38 44.7

4.00 4.697 0.5693E-01 0.245 60.39 205.5 14.57 46.1

264
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 305.33 (continued)

p P 5P/aT|

p 3P/3p|

T CV W r\ A

mol«dm MPa MPa.Kf

1 MPa

3 •dm «mol1 J/(mol-K)

- l m* s /xPa«s it W/(m«K)

4.10 4.720 0.5880E-01 0.221 60.95 204.0 14.77 47.6

4.20 4.741 0.6068E-01 0.198 61.51 202.6 14.97 49.2

4.30 4.760 0.6257E-01 0.177 62.08 201.3 15.18 50.9

4.40 4.777 0.6445E-01 0.157 62.65 200.0 15.39 52.7

4.50 4.791 0.6633E-01 0.139 63.22 198.8 15.60 54.7

4.60 4.804 0.6820E-01 0.122 63.79 197.6 15.82 56.8

4.70 4.816 0.7007E-01 0.106 64.35 196.5 16.04 59.1

4.80 4.826 0.7192E-01 0.092 64.91 195.4 16.26 61.6

4.90 4.834 0.7376E-01 0.079 65.47 194.3 16.49 64.4

5.00 4.841 0.7557E-01 0.067 66.01 193.3 16.73 67.4

5.10 4.848 0.7737E-01 0.056 66.54 192.3 16.96 70.8

5.20 4.853 0.7914E-01 0.047 67.06 191.4 17.20 74.7

5.30 4.857 0.8089E-01 0.039 67.56 190.5 17.45 79.0

5.40 4.860 0.8260E-01 0.031 68.05 189.6 17.70 83.9

5.50 4.863 0.8429E-01 0.025 68.51 188.8 17.95 89.6

5.60 4.866 0.8594E-01 0.020 68.94 188.0 18.21 96.3

5.70 4.867 0.8755E-01 0.015 69.35 187.2 18.47 104.1

5.80 4.869 0.8912E-01 0.012 69.73 186.5 18.73 113.6

5.90 4.870 0.9066E-01 0.009 70.07 185.8 19.00 125.2

6.00 4.870 0.9216E-01 0.006 70.38 185.1 19.27 139.7

6.10 4.871 0.9363E-01 0.004 70.65 184.4 19.55 158.3

6.20 4.871 0.9505E-01 0.003 70.88 183.8 19.83 182.6

6.30 4.872 0.9645E-01 0.002 71.07 183.2 20.12 215.8

6.40 4.872 0.9782E-01 0.001 71.21 182.6 20.41 263.0

6.50 4.872 0.9916E-01 0.001 71.30 182.1 20.71 335.0

6.60 4.872 0.1005 0.000 71.35 181.6 21.01 457.6

6.70 4.872 0.1018 0.000 71.35 181.3 21.31 716.2

6.80 4.872 0.1031 0.000 71.30 180.9 21.62 1677.7

6.870 4.872 0.1040 0.000

6.90 4.872 0.1044 0.000 71.20 180.7 21.93 3794.3

7.00 4.872 0.1057 0.000 71.04 180.5 22.25 912.1

7.10 4.872 0.1070 0.000 70.84 180.5 22.58 520.4

7.20 4.872 0.1084 0.000 70.59 180.6 22.91 360.3

7.30 4.872 0.1098 0.001 70.30 180.9 23.24 272.5

7.40 4.872 0.1113 0.002 69.96 181.3 23.58 217.5

7.50 4.872 0.1128 0.003 69.57 181.9 23.93 180.4

7.60 4.873 0.1144 0.004 69.14 182.7 24.28 154.3

7.70 4.873 0.1161 0.006 68.68 183.8 24.63 135.3

7.80 4.874 0.1178 0.009 68.18 185.2 24.99 121.2

7.90 4.875 0.1197 0.013 67.65 186.8 25.36 110.5

265-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 305.33 (continued)

p P aP/3T|

p 3P/3p|

T C

V W *) A

mol»dm MPa MPa^K"

1 3 MPa 'dm 'mol1 J/(mol.K)

- l m* s /iPa«s niW/(m-K)

8.00 4.876 0.1217 0.017 67.09 188.7 25.73 102.2

8.10 4.878 0.1239 0.024 66.51 191.0 26.11 95.7

8.20 4.881 0.1261 0.031 65.90 193.6 26.50 90.6

8.30 4.885 0.1285 0.041 65.28 196.6 26.89 86.5

8.40 4.889 0.1311 0.052 64.65 199.9 27.28 83.2

8.50 4.895 0.1338 0.065 64.02 203.6 27.69 80.4

8.60 4.902 0.1366 0.081 63.37 207.7 28.10 78.2

8.70 4.911 0.1397 0.099 62.73 212.2 28.52 76.3

8.80 4.922 0.1428 0.121 62.10 217.0 28.94 74.7

8.90 4.936 0.1462 0.145 61.47 222.2 29.37 73.5

9.00 4.951 0.1497 0.172 60.85 227.8 29.81 72.4

9.10 4.970 0.1534 0.203 60.25 233.7 30.25 71.5

9.20 4.992 0.1572 0.237 59.66 239.9 30.71 70.8

9.30 5.018 0.1611 0.274 59.09 246.4 31.17 70.2

9.40 5.047 0.1653 0.316 58.54 253.2 31.63 69.8

9.50 5.081 0.1695 0.362 58.01 260.3 32.11 69.5

9.60 5.120 0.1740 0.411 57.51 267.7 32.59 69.3

9.70 5.163 0.1785 0.465 57.03 275.3 33.09 69.2

9.80 5.213 0.1832 0.524 56.58 283.1 33.59 69.2

9.90 5.268 0.1880 0.587 56.15 291.1 34.10 69.2

10.00 5.330 0.1930 0.655 55.75 299.4 34.62 69.4

10.10 5.399 0.1981 0.729 55.37 307.9 35.15 69.6

10.20 5.476 0.2033 0.807 55.01 316.5 35.68 69.9

10.30 5.561 0.2086 0.892 54.68 325.4 36.23 70.2

10.40 5.655 0.2141 0.982 54.37 334.4 36.79 70.5

10.50 5.758 0.2197 1.079 54.08 343.6 37.36 71.0

10.60 5.871 0.2254 1.183 53.81 353.1 37.94 71.4

10.70 5.995 0.2313 1.293 53.57 362.7 38.53 71.9

10.80 6.130 0.2372 1.411 53.34 372.5 39.13 72.4

10.90 6.277 0.2433 1.537 53.12 382.6 39.74 72.9

11.00 6.437 0.2496 1.671 52.92 392.8 40.37 73.5

11.10 6.611 0.2559 1.813 52.74 403.3 41.00 74.1

11.20 6.800 0.2624 1.964 52.57 413.9 41.65 74.8

11.30 7.005 0.2690 2.125 52.42 424.8 42.31 75.4

11.40 7.225 0.2758 2.295 52.27 435.9 42.99 76.1

11.50 7.464 0.2827 2.475 52.14 447.2 43.68 76.8

11.60 7.721 0.2897 2.666 52.02 458.7 44.38 77.5

11.70 7.997 0.2969 2.867 51.90 470.4 45.10 78.3

11.80 8.295 0.3042 3.079 51.80 482.3 45.83 79.1

11.90 8.614 0.3116 3.303 51.70 494.5 46.58 79.9

266
Table B4. Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 305.33 (continued)

p P 3P/dT|

p d?/3p\1 T C

V W n A

mol'dm MPa MPa-K"

1 3 MPa* dm «mol

1 J/(mol«K)

- l m* s /iPa»s iriW/(m«K)

12.00 8.955 0.3192 3.538 51.61 506.8 47.35 80.7

12.10 9.321 0.3269 3.785 51.53 519.3 48.13 81.5

12.20 9.713 0.3348 4.044 51.46 532.0 48.93 82.4

12.30 10.131 0.3428 4.316 51.40 544.9 49.74 83.3

12.40 10.577 0.3509 4.601 51.34 558.0 50.58 84.2

12.50 11.051 0.3592 4.899 51.29 571.3 51.43 85.1

12.60 11.557 0.3676 5.210 51.24 584.8 52.30 86.1

12.70 12.094 0.3762 5.535 51.20 598.4 53.19 87.0

12.80 12.664 0.3848 5.873 51.17 612.1 54.10 88.0

12.90 13.269 0.3937 6.226 51.14 626.1 55.04 89.1

13.00 13.910 0.4026 6.594 51.12 640.2 56.00 90.1

13.10 14.588 0.4117 6.976 51.10 654.4 56.97 91.2

13.20 15.306 0.4210 7.373 51.09 668.8 57.98 92.3

13.30 16.063 0.4304 7.785 51.08 683.4 59.01 93.4

13.40 16.863 0.4399 8.214 51.08 698.1 60.06 94.6

13.50 17.707 0.4495 8.658 51.08 713.0 61.14 95.7

13.60 18.595 0.4593 9.119 51.09 728.0 62.24 96.9

13.70 19.531 0.4692 9.596 51.10 743.1 63.38 98.2

13.80 20.515 0.4793 10.091 51.11 758.4 64.54 99.4

13.90 21.550 0.4895 10.603 51.13 773.9 65.74 100.7

14.00 22.636 0.4999 11.133 51.16 789.5 66.97 102.0

14.10 23.777 0.5104 11.682 51.19 805.2 68.23 103.3

14.20 24.973 0.5210 12.249 51.22 821.1 69.52 104.7

14.30 26.227 0.5318 12.836 51.25 837.2 70.85 106.1

14.40 27.541 0.5428 13.442 51.29 853.4 72.22 107.5

14.50 28.916 0.5539 14.068 51.33 869.8 73.62 109.0

14.60 30.355 0.5652 14.715 51.37 886.3 75.07 110.5

14.70 31.860 0.5766 15.383 51.42 903.0 76.55 112.0

14.80 33.433 0.5882 16.072 51.47 919.8 78.08 113.6

14.90 35.075 0.5999 16.784 51.52 936.8 79.66 115.2

15.00 36.790 0.6118 17.519 51.57 954.0 81.28 116.8

15.10 38.580 0.6239 18.277 51.63 971.4 82.95 118.4

15.20 40.447 0.6362 19.059 51.69 988.9 84.67 120.1

15.30 42.392 0.6486 19.865 51.75 1006.6 86.45 121.9

15.40 44.420 0.6613 20.697 51.81 1024.5 88.28 123.6

15.50 46.533 0.6741 21.554 51.87 1042.6 90.17 125.4

15.60 48.732 0.6871 22.438 51.94 1060.9 92.12 127.3

15.70 51.021 0.7003 23.349 52.00 1079.4 94.13 129.2

15.80 53.403 0.7138 24.287 52.07 1098.0 96.21 131.1

15.90 55.880 0.7274 25.255 52.14 1116.9 98.36 133.1

267
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 305.33 (continued)

p P 3P/3T|

p 5P/5 P | t C

V W n A

mol'dm MPa MPa.K"

1 MPci«dm «mol1 J/(mol«K)

- l m* s /xPa»s mW/(m«K)

16.00 58.455 0.7412 26.251 52.21 1136.0 100.59 135.1

16.10 61.131 0.7553 27.278 52.28 1155.2 137.1

16.20 63.911 0.7696 28.336 52.35 1174.7 139.2

16.30 66.799 0.7841 29.425 52.42 1194.4 141.3

16.40 69.797 0.7988 30.546 52.50 1214.4 143.5

ETHANE ISOTHERM AT T = 320.00 K

Second virial coefficient is -159.8 3 .. - 1 cm »mol

P P 3P/3T|

p 3P/dH

T C

V W *) A

mol»dm MPa MPa.K"

1 MPsi* dm »mol1 J/(mol»K)

-

m« s /xPa«s niW/(m«K)

0.10 0.262 0.8466E-03 2.576 47.08 319.2 10.03 24.0

0.20 0.515 0.1723E-02 2.494 47.31 315.6 10.09 24.2

0.40 0.998 0.3567E-02 2.333 47.76 308.7 10.22 24.7

0.60 1.449 0.5528E-02 2.178 48.21 301.9 10.37 25.2

0.80 1.869 0.7607E-02 2.029 48.68 295.4 10.54 25.7

1.00 2.261 0.9801E-02 1.887 49.15 289.1 10.71 26.3

1.20 2.625 0.1211E-01 1.752 49.63 283.0 10.91 27.0

1.40 2.962 0.1452E-01 1.622 50.12 277.1 11.11 27.7

1.60 3.274 0.1705E-01 1.499 50.61 271.5 11.33 28.4

1.80 3.562 0.1968E-01 1.383 51.11 266.2 11.56 29.2

2.00 3.828 0.2240E-01 1.273 51.62 261.1 11.81 30.1

2.20 4.072 0.2523E-01 1.169 52.13 256.3 12.07 31.0

2.40 4.296 0.2814E-01 1.071 52.65 251.8 12.35 32.0

2.60 4.501 0.3114E-01 0.980 53.18 247.6 12.64 •33.0

2.80 4.688 0.3422E-01 0.894 53.70 243.6 12.94 34.1

3.00 4.859 0.3738E-01 0.815 54.24 239.9 13.26 35.3

3.20 5.014 0.4060E-01 0.742 54.77 236.6 13.59 36.5

3.40 5.156 0.4389E-01 0.675 55.30 233.5 13.93 37.8

3.60 5.285 0.4724E-01 0.613 55.83 230.7 14.29 39.2

3.80 5.402 0.5063E-01 0.558 56.36 228.2 14.66 40.6

4.00 5.508 0.5406E-01 0.507 56.88 225.9 15.05 42.1

4.20 5.605 0.5753E-01 0.462 57.38 223.9 15.45 43.6

4.40 5.693 0.6103E-01 0.421 57.87 222.2 15.87 45.1

4.60 5.774 0.6455E-01 0.386 58.34 220.8 16.30 46.7

4.80 5.848 0.6808E-01 0.355 58.78 219.6 16.74 48.3

5.00 5.916 0.7163E-01 0.328 59.19 218.7 17.20 49.8

5.20 5.979 0.7519E-01 0.306 59.57 218.0 17.68 51.3

5.40 6.039 0.7875E-01 0.287 59.90 217.6 18.17 52.8

5.60 6.094 0.8233E-01 0.272 60.18 217.4 18.68 54.2

-268-
Table B4 . Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 320.00 K (continued)

p P dP/5T|

p dP/dp\

T CV W V

A

mo 1 • dm MPa MPa^K"

1 3 MPa • dm »mol

1 J/(mol-K)

-

m»s fj,Fa»s rriW/(m«K)

5.80 6.148 0.8593E--01 0.260 60.40 217.5 19.20 55.5

6.00 6.199 0.8956E--01 0.252 60.56 218.0 19.74 56.7

6.20 6.249 0.9323E--01 0.247 60.67 218.8 20.30 57.8

6.40 6.298 0.9697E--01 0.245 60.70 220.0 20.88 58.7

6.60 6.347 0.1008 0.247 60.67 221.6 21.47 59.6

6.80 6.397 0.1047 0.252 60.57 223.7 22.08 60.3

7.00 6.448 0.1088 0.260 60.40 226.3 22.71 61.0

7.20 6.501 0.1131 0.273 60.17 229.5 23.36 61.5

7.40 6.557 0.1175 0.290 59.89 233.4 24.03 61.9

7.60 6.617 0.1222 0.313 59.56 238.0 24.72 62.3

7.80 6.683 0.1272 0.342 59.18 243.3 25.44 62.6

8.00 6.755 0.1325 0.378 58.78 249.5 26.17 62.9

8.20 6.835 0.1381 0.422 58.35 256.4 26.94 63.2

8.40 6.924 0.1440 0.475 57.91 264.2 27.72 63.4

8.60 7.025 0.1503 0.538 57.47 272.8 28.53 63.8

8.80 7.140 0.1569 0.612 57.03 282.3 29.37 64.2

9.00 7.271 0.1639 0.698 56.60 292.5 30.23 64.7

9.20 7.420 0.1713 0.797 56.18 303.6 31.13 65.3

9.40 7.591 0.1790 0.911 55.79 315.4 32.05 65.9

9.60 7.785 0.1872 1.041 55.42 328.1 33.01 66.7

9.80 8.008 0.1958 1.188 55.08 341.5 34.00 67.5

10.00 8.262 0.2048 1.355 54.76 355.7 35.03 68.4

10.20 8.551 0.2142 1.543 54.47 370.8 36.10 69.4

10.40 8.881 0.2242 1.755 54.20 386.8 37.20 70.5

10.60 9.255 0.2347 1.993 53.95 403.7 38.35 71.7

10.80 9.680 0.2457 2.261 53.73 421.5 39.54 72.9

11.00 10.162 0.2572 2.560 53.53 440.3 40.77 74.3

11.20 10.706 0.2693 2.895 53.36 460.0 42.06 75.6

11.40 11.322 0.2820 3.266 53.20 480.7 43.40 77.1

11.60 12.016 0.2952 3.679 53.06 502.2 44.80 78.6

11.80 12.796 0.3090 4.134 52.95 524.7 46.25 80.2

12.00 13.672 0.3234 4.634 52.85 548.0 47.77 81.9

12.20 14.653 0.3383 5.181 52.77 572.1 49.35 83.7

12.40 15.748 0.3537 5.778 52.71 597.0 51.01 85.6

12.60 16.968 0.3697 6.428 52.67 622.7 52.74 87.5

12.80 18.323 0.3863 7.131 52.65 649.0 54.56 89.5

13.00 19.824 0.4034 7.891 52.64 676.1 56.46 91.7

13.20 21.483 0.4210 8.711 52.65 703.8 58.46 93.9

13.40 23.312 0.4392 9.592 52.68 732.1 60.55 96.2

13.60 25.324 0.4579 10.539 52.71 761.1 62.76 98.6

269
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 320.00 K (continued)

p P dP/3T|

p 3P/3p|

T C

V W n A

mo 1 • dm MPa

- 1 3 - MPa«K MPa* dm »mol

1 J/(mol»K)

- l m* s |iPa«s mW/(m«K)

13.80 27.532 0.4772 11.553 52.76 790.8 65.08 101.1

14.00 29.950 0.4971 12.638 52.83 821.1 67.53 103.8

14.20 32.592 0.5176 13.797 52.90 852.1 70.11 106.5

14.40 35.474 0.5387 15.035 52.99 883.8 72.83 109.4

14.60 38.612 0.5604 16.355 53.08 916.2 75.71 112.4

14.80 42.022 0.5829 17.762 53.18 949.2 78.77 115.5

15.00 45.723 0.6060 19.259 53.29 983.0 82.01 118.7

15.20 49.732 0.6298 20.852 53.40 1017.6 85.45 122.1

15.40 54.070 0.6544 22.545 53.53 1053.0 89.11 125.7

15.60 58.757 0.6797 24.344 53.65 1089.1 93.00 129.4

15.80 63.815 0.7059 26.255 53.78 1126.1 133.2

16.00 69.267 0.7330 28.282 53.91 1164.0 137.3

ETHANE ISOTHERM AT T = 340.00 K

Second virial coefficient is -140.1 3 , - 1 cm «mol

P P aP/3T|

p 3P/dp|

T C

V W T) A

mol'dm MPa MPa«K

_1

MPsi«dm •mol

1 J/(mol«K)

-

m* s /xPa«s niW/(m.K)

0.10 0.279 0.8453E-03 2.748 49.59 328.2 10.60 26.8

0.20 0.550 0.1718E-02 2.671 49.78 325.0 10.67 27.0

0.40 1.069 0.3547E-02 2.522 50.14 318.7 10.81 27.4

0.60 1.559 0.5483E-02 2.378 50.51 312.7 10.96 27.9

0.80 2.021 0.7527E-02 2.241 50.88 306.9 11.13 28.4

1.00 2.456 0.9674E-02 2.110 51.25 301.3 11.31 29.0

1.20 2.865 0.1192E-01 1.984 51.62 296.0 11.51 29.6

1.40 3.250 0.1427E-01 1.865 52.00 290.9 11.72 30.2

1.60 3.612 0.1672E-01 1.753 52.36 286.1 11.94 30.9

1.80 3.951 0.1926E-01 1.646 52.73 281.5 12.18 31.6

2.00 4.270 0.2189E-01 1.545 53.09 277.3 12.43 32.3

2.20 4.569 0.2460E-01 1.450 53.45 273.2 12.70 33.1

2.40 4.850 0.2740E-01 1.360 53.80 269.5 12.98 34.0

2.60 5.114 0.3028E-01 1.277 54.15 266.0 13.27 34.9

2.80 5.362 0.3323E-01 1.199 54.48 262.9 13.57 35.8

3.00 5.594 0.3626E-01 1.127 54.81 260.0 13.89 36.7

3.20 5.813 0.3935E-01 1.060 55.13 257.4 14.22 37.7

3.40 6.019 0.4251E-01 0.999 55.43 255.2 14.57 38.7

3.60 6.213 0.4572E-01 0.943 55.72 253.2 14.93 39.8

3.80 6.396 0.4900E-01 0.892 56.00 251.5 15.30 40.8

-270
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 340.00 K (continued)

p P dP/ST|

p dP/dp\

't C

V W n

A

mo 1 • dm MPa MPa-K"

1 MPa •dm *mol

1 J/(mol«K)

-

m* s /iPa«s it W/(m«K)

4.00 6.570 0.5233E 01 0.846 56.26 250.1 15.69 41.9

4.20 6.735 0.5572E •01 0.805 56.50 249.0 16.09 43.0

4.40 6.892 0.5916E -01 0.769 56.73 248.2 16.51 44.1

4.60 7.043 0.6265E •01 0.737 56.93 247.7 16.94 45.1

4.80 7.188 0.6620E 01 0.710 57.11 247.6 17.39 46.2

5.00 7.327 0.6981E-01 0.688 57.27 247.7 17.85 47.3

5.20 7.463 0.7348E-01 0.669 57.41 248.2 18.32 48.3

5.40 7.595 0.7722E 01 0.655 57.51 249.0 18.81 49.3

5.60 7.725 0.8104E-01 0.645 57.60 250.1 19.32 50.3

5.80 7.854 0.8494E-01 0.640 57.66 251.7 19.84 51.3

6.00 7.982 0.8893E-•01 0.640 57.69 253.6 20.38 52.2

6.20 8.110 0.9304E- 01 0.644 57.70 256.0 20.94 53.1

6.40 8.239 0.9726E- 01 0.653 57.68 258.8 21.51 54.0

6.60 8.371 0.1016 0.667 57.64 262.1 22.10 54.8

6.80 8.507 0.1061 0.687 57.59 265.9 22.71 55.6

7.00 8.647 0.1108 0.713 57.51 270.2 23.34 56.4

7.20 8.792 0.1157 0.745 57.42 275.0 23.99 57.1

7.40 8.945 0.1207 0.784 57.31 280.3 24.66 57.9

7.60 9.107 0.1260 0.831 57.20 286.3 25.35 58.6

7.80 9.278 0.1315 0.885 57.07 292.8 26.06 59.4

8.00 9.461 0.1372 0.948 56.94 299.9 26.79 60.2

8.20 9.658 0.1432 1.020 56.81 307.6 27.55 60.9

8.40 9.870 0.1494 1.102 56.67 315.9 28.33 61.7

8.60 10.099 0.1560 1.195 56.54 324.8 29.14 62.6

8.80 10.349 0.1628 1.301 56.40 334.4 29.97 63.4

9.00 10.621 0.1699 1.420 56.27 344.7 30.84 64.3

9.20 10.918 0.1773 1.553 56.14 355.6 31.73 65.3

9.40 11.243 0.1851 1.704 56.01 367.3 32.66 66.3

9.60 11.600 0.1932 1.872 55.88 379.7 33.61 67.3

9.80 11.993 0.2017 2.060 55.76 392.9 34.60 68.4

10.00 12.426 0.2106 2.269 55.64 406.9 35.63 69.5

10.20 12.902 0.2199 2.503 55.53 421.8 36.70 70.7

10.40 13.429 0.2297 2.763 55.42 437.5 37.80 71.9

10.60 14.009 0.2400 3.051 55.31 454.1 38.95 73.2

10.80 14.651 0.2507 3.370 55.22 471.6 40.14 74.6

11.00 15.360 0.2619 3.723 55.13 490.0 41.38 76.0

11.20 16.143 0.2736 4.111 55.05 509.2 42.68 77.5

11.40 17.007 0.2859 4.537 54.99 529.3 44.02 79.0

11.60 17.960 0.2986 5.003 54.93 550.3 45.42 80.6

11.80 19.011 0.3119 5.512 54.89 572.0 46.89 82.3

-271-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 340.00 K (continued)

p P 3P/3T|

p 3P/3p|

T C

V W n

A

mol»dm MPa MPa.K"

1 3 MPa* dm «mol1 J/(mol«K)

- l m« s j/Pa«s mW/(m«K)

12.00 20.167 0.3257 6.065 54.86 594.6 48.41 84.0

12.20 21.440 0.3400 6.666 54.84 617.9 50.01 85.9

12.40 22.837 0.3548 7.316 54.83 642.0 51.68 87.8

12.60 24.370 0.3701 8.019 54.84 666.8 53.43 89.8

12.80 26.048 0.3860 8.776 54.86 692.3 55.26 91.8

13.00 27.884 0.4024 9.590 54.89 718.5 57.18 94.0

13.20 29.888 0.4193 10.464 54.93 745.4 59.20 96.3

13.40 32.074 0.4367 11.401 54.98 773.0 61.32 98.6

13.60 34.453 0.4548 12.403 55.04 801.4 63.55 101.1

13.80 37.040 0.4734 13.476 55.11 830.4 65.90 103.7

14.00 39.848 0.4926 14.620 55.19 860.1 68.38 106.4

14.20 42.893 0.5124 15.842 55.27 890.6 71.00 109.2

14.40 46.190 0.5329 17.144 55.36 921.8 73.77 112.1

14.60 49.756 0.5540 18.530 55.46 953.8 76.70 115.1

14.80 53.608 0.5758 20.006 55.57 986.6 79.81 118.3

15.00 57.765 0.5983 21.575 55.68 1020.1 83.11 121.6

15.20 62.245 0.6216 23.243 55.79 1054.5 125. 1 15.40 67.069 0.6457 25.015 55.90 1089.7 128.7

ETHANE ISOTHERM AT T = 360.00 K

Second virial coefficient is -123.4 3

1 - 1 cm 'mol

P P 3P/3T|

p 3P/3 P | t C

V W 1

A

mol«dm MPa MPa-K*

1 MPcL«dm •mol

1 J/(mol-K)

- l m* s /iPa«s mW/(m»K)

0.10 0.296 0.8444E--03 2.920 52.15 336.9 11.16 29.8

0.20 0.584 0.1715E--02 2.848 52.30 334.0 11.23 30.0

0.40 1.140 0.3531E--02 2.709 52.61 328.4 11.38 30.4

0.60 1.668 0.5449E--02 2.576 52.91 323.0 11.54 30.8

0.80 2.171 0.7465E--02 2.449 53.21 317.9 11.71 31.3

1.00 2.648 0.9578E--02 2.328 53.51 312.9 11.90 31.8

1.20 3.102 0.1179E--01 2.212 53.81 308.3 12.10 32.4

1.40 3.533 0.1409E--01 2.103 54.11 303.8 12.31 32.9

1.60 3.943 0.1648E--01 1.999 54.40 299.7 12.54 33.6

1.80 4.333 0.1896E-01 1.901 54.69 295.8 12.78 34.2

2.00 4.704 0.2152E-•01 1.808 54.97 292.2 13.04 34.9

2.20 5.057 0.2417E--01 1.722 55.25 288.8 13.31 35.6

2.40 5.393 0.2690E-01 1.640 55.51 285.7 13.59 36.4

2.60 5.714 0.2971E-•01 1.565 55.77 283.0 13.88 37.2

2.80 6.019 0.3259E-01 1.494 56.02 280.5 14.19 38.0

-272
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 360.00 K (continued)

p P 3P/<9T|

p d?/dp\1 T C

V W n A

mo 1 • dm MPa MPa«K

_1

MPa

3 •dm «mol1 J/(mol-K)

- l m« s /xPa»s m W/(m-K)

3.00 6.312 0.3555E-01 1.429 56.26 278.2 14.51 38.8

3.20 6.591 0.3858E-01 1.370 56.49 276.3 14.85 39.7

3.40 6.860 0.4168E-01 1.315 56.71 274.7 15.20 40.6

3.60 7.118 0.4485E-01 1.265 56.91 273.4 15.56 41.5

3.80 7.366 0.4809E-01 1.221 57.11 272.3 15.93 42.4

4.00 7.606 0.5139E-01 1.181 57.28 271.6 16.32 43.3

4.20 7.839 0.5477E-01 1.146 57.45 271.2 16.72 44.2

4.40 8.065 0.5822E-01 1.117 57.60 271.1 17.14 45.2

4.60 8.286 0.6173E-01 1.091 57.73 271.4 17.57 46.1

4.80 8.502 0.6533E-01 1.071 57.85 271.9 18.02 47.0

5.00 8.715 0.6900E-01 1.055 57.95 272.8 18.48 47.9

5.20 8.925 0.7276E-01 1.045 58.03 274.1 18.95 48.9

5.40 9.133 0.7660E- 01 1.039 58.10 275.7 19.45 49.8

5.60 9.341 0.8055E- 01 1.039 58.16 277.7 19.95 50.7

5.80 9.549 0.8460E- 01 1.044 58.20 280.1 20.47 51.6

6.00 9.759 0.8876E- 01 1.054 58.22 282.9 21.01 52.4

6.20 9.971 0.9304E- 01 1.070 58.24 286.2 21.57 53.3

6.40 10.187 0.9745E- 01 1.093 58.24 289.8 22.14 54.2

6.60 10.408 0.1020 1.122 58.23 294.0 22.73 55.0

6.80 10.636 0.1067 1.158 58.20 298.6 23.34 55.9

7.00 10.872 0.1116 1.201 58.18 303.7 23.97 56.7

7.20 11.117 0.1166 1.251 58.14 309.3 24.61 57.5

7.40 11.373 0.1219 1.310 58.10 315.4 25.28 58.4

7.60 11.642 0.1273 1.378 58.05 322.0 25.97 59.2

7.80 11.925 0.1329 1.454 58.00 329.1 26.68 60.1

8.00 12.224 0.1388 1.540 57.94 336.8 27.42 61.0

8.20 12.542 0.1449 1.637 57.89 345.0 28.17 61.9

8.40 12.880 0.1513 1.746 57.83 353.8 28.95 62.8

8.60 13.241 0.1579 1.866 57.77 363.2 29.76 63.8

8.80 13.627 0.1648 2.001 57.71 373.2 30.60 64.8

9.00 14.042 0.1720 2.150 57.65 383.8 31.46 65.8

9.20 14.488 0.1795 2.316 57.59 395.2 32.36 66.8

9.40 14.970 0.1873 2.501 57.53 407.2 33.28 67.9

9.60 15.490 0.1955 2.705 57.47 419.9 34.24 69.0

9.80 16.053 0.2040 2.931 57.41 433.4 35.23 70.2

10.00 16.664 0.2129 3.181 57.35 447.7 36.26 71.4

10.20 17.327 0.2223 3.457 57.30 462.8 37.33 72.7

10.40 18.049 0.2320 3.761 57.25 478.7 38.44 74.0

10.60 18.834 0.2422 4.094 57.20 495.4 39.59 75.3

10.80 19.688 0.2527 4.460 57.16 512.9 40.79 76.7

-273-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 360.00 K (continued)

p P 3P/5TI d?/3p\

P T

- 3

- i 3-1

mol'dm " MPa MPa*K MPa«dm 'mol J/(mol»K) m»s

11.00 20.620 0.2638

11.20 21.635 0.2753

11.40 22.741 0.2872

11.60 23.945 0.2996

11.80 25.258 0.3125

12.00 26.686 0.3259

12.20 28.239 0.3398

12.40 29.928 0.3541

12.60 31.762 0.3689

12.80 33.753 0.3843

13.00 35.910 0.4002

13.20 38.248 0.4166

13.40 40.777 0.4335

13.60 43.512 0.4510

13.80 46.465 0.4691

14.00 49.652 0.4878 16.546 57.60 895.9 69.32 109.2

14.20 53.089 0.5072 17.830 57.69 926.1 71.98 112.0

74.79 115.0

118.1

121.3

15.00 69.660 0.5913 23.844 58.09 1055.1 124.7

ETHANE ISOTHERM AT T = 380.00 K

3 - 1 Second virial coefficient is -108.9 cm -mol

4 .860 57 .13

5 .296 57 ,10

5 .770 57 ,08

6 .285 57 .07

6 .843 57 .07

7 .447 57 .07

8 .097 57 .09

8 .798 57 ,11

9 .552 57,.15

10.,361 57,,19

11 .228 57,,24

12..156 57,,30

13 ,148 57,,36

14 ,208 57,,44

15 ,340 57.,51

W n

A

-

m» s /uPa«s iriW/(m-K)

531.2 42.04 78.2

550.2 43.33 79.7

570.1 44.69 81.3

590.8 46.10 82.9

612.2 hi .57 84.7

634.3 49.11 86.5

657.2 50.72 88.3

680.8 52.41 90,3

705.2 54.17 92.3

730.2 56.02 94.4

756.0 57.97 96.6

782.5 60.01 98.9

809.7 62.16 101.3

837.7 64.42 103.9

866.4 66.80 106.5

14.40 56.790 0.5272 19.198 57.78 957.1

14.60 60.774 0.5478 20.653 57.88 989.0

14.80 65.058 0.5692 22.200 57.98 1021.6

P P 3P/3T|

p 3P/3p|

T C

V W n

A

mo 1 • dm MPa MPa«K

_1

MPs

3

i • dm • mo

L J/(mol»K)

-

m« s /j,?a*s mW/(m«K)

0.10 0.313 0.8436E-03 3.091 54.73 345.3 11.72 32.9

0.20 0.618 0.1712E-02 3.025 54.85 342.7 11.79 33.1

0.40 1.210 0.3519E-02 2.895 55.11 337.7 11.94 33.5

0.60 1.777 0.5422E-02 2.772 55.37 332.9 12.10 33.9

0.80 2.319 0.7417E-02 2.654 55.62 328.3 12.28 34.3

1.00 2.839 0.9504E-02 2.542 55.87 324.0 12.47 34.8

1.20 3.337 0.1168E-01 2.436 56.12 319.9 12.68 35.3

1.40 3.814 0.1395E-01 2.335 56.36 316.1 12.90 35.9

1.60 4.271 0.1630E-01 2.240 56.60 312.5 13.13 36.5

1.80 4.710 0.1873E-01 2.151 56.83 309.2 13.37 37.1

2.00 5.132 0.2125E-01 2.067 57.06 306.2 13.63 37.7

2.20 5.537 0.2385E-01 1.988 57.29 303.4 13.90 38.4

274
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 380.00 K (continued)

p P 3P/5T|

p 3P/3p|

T CV W n

A

mo 1 • dm MPa MPa«K

_1

MPa • dm • mo

1

1 J/(mol«K)

- l m* s /^Pa«s ir W/(m-K)

2.40 5.927 0.2653E-01 1.915 57.50 300.9 14.19 39.1

2.60 6.303 0.2929E-01 1.847 57.71 298.7 14.48 39.8

2.80 6.666 0.3213E-01 1.784 57.91 296.8 14.79 40.6

3.00 7.017 0.3504E-01 1.727 58.10 295.1 15.12 41.3

3.20 7.357 0.3803E-01 1.674 58.28 293.8 15.46 42.1

3.40 7.687 0.4109E-01 1.627 58.45 292.7 15.81 42.9

3.60 8.008 0.4423E-01 1.584 58.62 292.0 16.17 43.7

3.80 8.321 0.4745E-01 1.547 58.77 291.5 16.55 44.6

4.00 8.627 0.5074E-01 1.515 58.91 291.4 16.94 45.4

4.20 8.928 0.5411E-01 1.487 59.04 291.5 17.34 46.3

4.40 9.223 0.5756E-01 1.465 59.16 292.0 17.76 47.1

4.60 9.514 0.6109E-01 1.448 59.26 292.9 18.19 48.0

4.80 9.802 0.6471E-01 1.436 59.36 294.0 18.64 48.8

5.00 10.089 0.6843E-01 1.429 59.44 295.5 19.10 49.7

5.20 10.374 0.7223E-01 1.428 59.52 297.4 19.58 50.6

5.40 10.660 0.7614E-01 1.432 59.58 299.7 20.07 51.4

5.60 10.948 0.8015E-01 1.442 59.63 302.3 20.58 52.3

5.80 11.238 0.8428E-01 1.458 59.67 305.3 21.10 53.2

6.00 11.531 0.8853E-01 1.481 59.71 308.7 21.64 54.0

6.20 11.830 0.9290E-01 1.510 59.73 312.6 22.19 54.9

6.40 12.136 0.9741E-01 1.546 59.75 316.9 22.77 55.7

6.60 12.450 0.1021 1.590 59.75 321.7 23.36 56.6

6.80 12.773 0.1069 1.642 59.76 326.9 23.97 57.5

7.00 13.107 0.1118 1.702 59.75 332.5 24.59 58.3

7.20 13.454 0.1170 1.770 59.74 338.7 25.24 59.2

7.40 13.816 0.1223 1.848 59.73 345.3 25.91 60.1

7.60 14.194 0.1278 1.936 59.71 352.5 26.60 61.0

7.80 14.590 0.1335 2.034 59.69 360.1 27.31 61.9

8.00 15.008 0.1395 2.143 59.66 368.3 28.04 62.8

8.20 15.448 0.1457 2.263 59.64 377.0 28.80 63.8

8.40 15.914 0.1521 2.397 59.61 386.3 29.58 64.8

8.60 16.408 0.1587 2.545 59.58 396.1 30.39 65.8

8.80 16.933 0.1657 2.708 59.55 406.6 31.23 66.8

9.00 17.492 0.1729 2.887 59.52 417.6 32.09 67.9

9.20 18.089 0.1805 3.085 59.49 429.4 32.99 69.0

9.40 18.728 0.1883 3.302 59.46 441.8 33.92 70.1

9.60 19.412 0.1965 3.542 59.43 454.9 34.88 71.3

9.80 20.146 0.2051 3.804 59.40 468.7 35.87 72.5

-275
Table B4 . Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 380.00 K (continued)

p P SP/3T|

p d?/8p\

't C

V W n A

mo 1 • dm MPa MPa«K

_1 MP;a • dm • mo

1 J/Onol-K)

- l m* s /iPa«s mW/(m«K)

10.00 20.935 0.2140 4.092 59.38 483.2 36.91 73.7

10.20 21.784 0.2233 4.406 59.36 498.5 37.98 75.0

10.40 22.699 0.2329 4.750 59.34 514.6 39.10 76.4

10.60 23.686 0.2430 5.125 59.33 531.4 40.25 77.7

10.80 24.752 0.2534 5.533 59.32 548.9 41.46 79.2

11.00 25.902 0.2643 5.976 59.32 567.2 42.71 80.7

11.20 27.145 0.2755 6.456 59.32 586.2 44.02 82.2

11.40 28.487 0.2872 6.975 59.33 606.0 45.38 83.9

11.60 29.937 0.2994 7.536 59.34 626.5 46.81 85.6

11.80 31.504 0.3120 8.140 59.37 647.7 48.29 87.3

12.00 33.196 0.3250 8.790 59.40 669.6 49.84 89.1

12.20 35.023 0.3385 9.489 59.43 692.3 51.47 91.0

12.40 36.995 0.3525 10.238 59.48 715.7 53.17 93.0

12.60 39.122 0.3670 11.041 59.53 739.8 54.95 95.1

12.80 41.416 0.3819 11.901 59.58 764.6 56.83 97.2

13.00 43.887 0.3974 12.821 59.64 790.2 58.79 99.5

13.20 46.548 0.4134 13.803 59.71 816.5 60.86 101.8

13.40 49.412 0.4300 14.851 59.78 843.5 63.04 104.3

13.60 52.493 0.4471 15.969 59.86 871.4 65.33 106.8

13.80 55.805 0.4649 17.160 59.94 899.9 67.75 109.5

14.00 59.362 0.4832 18.428 60.03 929.3 70.31 112.2

14.20 63.182 0.5022 19.778 60.12 959.5 115.1

14.40 67.279 0.5218 21.213 60.21 990.5 118.1

ETHANE ISOTHERM AT T = 400.00 K

Second virial coefficient is -96.3 3 - 1 cm •mol

P P 5P/5T|

p SP/dp|

T C

V W n

A

mo 1 • dm MPa MPa.K"

1 3 MPa* dm »mol

1 J/(mol«K)

-

m* s /iPa»s mW/(m-K)

0.10 0.329 0.8430E--03 3.262 57.30 353.5 12.26 36.1

0.20 0.653 0.1709E -02 3.200 57.41 351.2 12.33 36.3

0.40 1.281 0.3510E -02 3.080 57.63 346.7 12.49 36.7

0.60 1.885 0.5400E--02 2.966 57.85 342.4 12.66 37.1

0.80 2.467 0.7379E--02 2.857 58.06 338.4 12.84 37.5

1.00 3.028 0.9446E--02 2.754 58.28 334.6 13.03 38.0

1.20 3.569 0.1160E--01 2.657 58.49 331.0 13.24 38.5

1.40 4.091 0.1383E--01 2.564 58.69 327.7 13.47 39.0

1.60 4.596 0.1616E-01 2.478 58.89 324.7 13.70 39.5

1.80 5.083 0.1856E-01 2.397 59.09 321.9 13.95 40.1

276
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 400.00 K (continued)

p P dP/3T|

p d?/dp\

T CV W V

A

mol'dm MPa MPa«K

_1

MPa •dm «mol

1 J/(mol«K)

- l m« s //Pa«s niW/(m«K)

2.00 5.555 0.2104E-01 2.321 59.28 319.4 14.21 40.7

2.20 6.012 0.2361E-01 2.250 59.46 317.2 14.48 41.4

2.40 6.455 0.2625E-01 2.185 59.64 315.2 14.77 42.0

2.60 6.886 0.2897E-01 2.125 59.82 313.5 15.07 42.7

2.80 7.305 0.3177E-01 2.070 59.98 312.1 15.39 43.4

3.00 7.714 0.3465E-01 2.020 60.14 310.9 15.71 44.1

3.20 8.114 0.3761E-01 1.975 60.29 310.1 16.05 44.8

3.40 8.505 0.4064E-01 1.935 60.43 309.5 16.40 45.6

3.60 8.888 0.4376E-01 1.901 60.57 309.3 16.77 46.4

3.80 9.265 0.4695E-01 1.872 60.70 309.4 17.15 47.1

4.00 9.637 0.5023E-01 1.847 60.82 309.7 17.54 47.9

4.20 10.004 0.5359E-01 1.828 60.93 310.4 17.95 48.7

4.40 10.369 0.5704E-01 1.815 61.03 311.4 18.37 49.6

4.60 10.731 0.6058E-01 1.806 61.12 312.8 18.80 50.4

4.80 11.092 0.6421E-01 1.803 61.20 314.4 19.25 51.2

5.00 11.452 0.6794E-01 1.806 61.28 316.5 19.71 52.0

5.20 11.814 0.7178E-01 1.815 61.35 318.9 20.19 52.9

5.40 12.179 0.7572E-01 1.830 61.41 321.6 20.68 53.7

5.60 12.547 0.7977E-01 1.851 61.46 324.8 21.19 54.5

5.80 12.920 0.8394E-01 1.880 61.50 328.3 21.71 55.4

6.00 13.299 0.8823E-01 1.915 61.54 332.3 22.25 56.2

6.20 13.686 0.9266E-01 1.957 61.57 336.7 22.81 57.1

6.40 14.083 0.9723E-01 2.008 61.60 341.5 23.38 57.9

6.60 14.490 0.1019 2.066 61.62 346.7 23.97 58.8

6.80 14.910 0.1068 2.134 61.63 352.4 24.58 59.7

7.00 15.344 0.1118 2.210 61.64 358.6 25.21 60.6

7.20 15.794 0.1170 2.296 61.65 365.2 25.86 61.5

7.40 16.263 0.1224 2.393 61.65 372.3 26.53 62.4

7.60 16.752 0.1280 2.500 61.65 379.9 27.22 63.3

7.80 17.264 0.1338 2.619 61.65 388.0 27.93 64.2

8.00 17.801 0.1397 2.750 61.64 396.6 28.67 65.2

8.20 18.365 0.1460 2.895 61.63 405.8 29.43 66.2

8.40 18.960 0.1524 3.054 61.62 415.5 30.21 67.2

8.60 19.587 0.1591 3.228 61.61 425.7 31.02 68.2

8.80 20.252 0.1661 3.418 61.60 436.6 31.86 69.3

9.00 20.956 0.1734 3.627 61.59 448.1 32.73 70.4

9.20 21.704 0.1809 3.855 61.58 460.1 33.63 71.5

9.40 22.500 0.1888 4.105 61.57 472.9 34.56 72.6

9.60 23.347 0.1969 4.377 61.57 486.3 35.53 73.8

9.80 24.252 0.2054 4.673 61.56 500.4 36.53 75.1

277-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 400.00 K (continued)

p P 5P/5T|

p 3P/3p|

T C

V W n A

mol'dm MPa MPa«K

_1 3 MPa 'dm 'mol

1 J/(mol.K)

- l m« s ^Pa»s niW/(m-K)

10.00 25.218 0.2143 4.997 61.56 515.2 37.56 76.3

10.20 26.252 0.2235 5.348 61.56 530.6 38.64 77.7

10.40 27.360 0.2330 5.729 61.56 546.8 39.76 79.0

10.60 28.546 0.2429 6.143 61.57 563.7 40.93 80.4

10.80 29.819 0.2532 6.590 61.59 581.3 42.14 81.9

11.00 31.185 0.2639 7.073 61.60 599.6 43.41 83.4

11.20 32.651 0.2750 7.595 61.63 618.6 44.72 85.0

11.40 34.225 0.2865 8.156 61.65 638.4 46.10 86.7

11.60 35.916 0.2984 8.760 61.69 658.8 47.53 88.4

11.80 37.732 0.3107 9.408 61.73 679.9 49.03 90.2

12.00 39.682 0.3235 10.103 61.77 701.8 50.60 92.0

12.20 41.777 0.3368 10.848 61.82 724.4 52.24 94.0

12.40 44.025 0.3504 11.645 61.87 747.7 53.96 96.0

12.60 46.438 0.3646 12.498 61.93 771.7 55.76 98.1

12.80 49.028 0.3793 13.408 62.00 796.4 57.66 100.3

13.00 51.806 0.3945 14.380 62.06 821.9 59.65 102.5

13.20 54.784 0.4102 15.416 62.13 848.2 61.74 104.9

13.40 57.977 0.4265 16.521 62.21 875.2 63.95 107.4

13.60 61.397 0.4433 17.697 62.29 903.0 109.9

13.80 65.061 0.4608 18.948 62.37 931.6 112.6

14.00 68.982 0.4788 20.279 62.46 961.0 115.4

ETHANE ISOTHERM AT T = 420.00 K

Second virial coefficient is -85.2 3 .. - 1 cm •mol

P P 3P/3T|

p d?/dp\

T C

V W V A

mol'dra MPa MPa«Kf

X MPsi 'dm «mol

1 J/(mol«K)

-

m* s /iPa«s mW/(m«K)

0.10 0.346 0.8425E-•03 3.433 59.86 361.6 12.80 39.5

0.50 1.674 0.4431E-02 3.211 60.24 353.6 13.11 40.2

1.00 3.217 0.9398E-•02 2.964 60.71 344.8 13.59 41.3

1.50 4.644 0.1488E-•01 2.751 61.15 337.6 14.14 42.5

2.00 5.974 0.2087E-•01 2.572 61.56 332.0 14.78 43.9

2.50 7.221 0.2736E--01 2.425 61.95 328.1 15.49 45.4

3.00 8.404 0.3434E-01 2.310 62.29 325.9 16.29 47.1

3.50 9.537 0.4182E-01 2.228 62.61 325.5 17.17 48.9

4.00 10.637 0.4982E-•01 2.179 62.88 327.0 18.13 50.8

4.50 11.721 0.5837E-•01 2.164 63.10 330.4 19.18 52.7

278-
Table B4. Properties in the single -phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 420.00 K (continued)

p P dP/3T|

p 3P/3p|

T CV W V A

mol»dm MPa MPa-K"

1 MPsL»dm 'mol

1 J/(mol-K)

-

m»s /xPa»s rriW/(m.K)

5.00 12.807 0.6752E-01 2.185 63.29 336.0 20.31 54.7

5.50 13.913 0.7734E-01 2.246 63.44 343.9 21.54 56.7

6.00 15.061 0.8791E-01 2.352 63.55 354.1 22.86 58.8

6.50 16.274 0.9932E-01 2.509 63.63 367.0 24.29 60.9

7.00 17.579 0.1117 2.723 63.69 382.6 25.83 63.2

7.50 19.008 0.1251 3.004 63.72 401.1 27.49 65.4

8.00 20.596 0.1397 3.362 63.74 422.7 29.29 67.8

8.50 22.385 0.1558 3.810 63.76 447.6 31.24 70.4

9.00 24.424 0.1734 4.367 63.77 475.9 33.37 73.1

9.50 26.773 0.1928 5.053 63.79 508.1 35.69 76.0

10.00 29.503 0.2141 5.894 63.82 544.4 38.23 79.2

10.50 32.697 0.2375 6.918 63.86 584.7 41.02 82.6

11.00 36.456 0.2631 8.153 63.94 629.4 44.11 86.4

11.50 40.891 0.2911 9.633 64.03 678.3 47.53 90.5

12.00 46.135 0.3217 11.392 64.16 731.7 51.36 95.1

12.50 52.337 0.3551 13.470 64.30 789.5 55.66 100.1

13.00 59.666 0.3916 15.913 64.47 851.9 60.51 105.7

13.50 68.319 0.4313 18.772 64.66 919.1 111.9

ETHANE ISOTHERM AT T = 450.00 K

Second virial coefficient is -70.9

3

n - 1 cm «mol

P P d?/8T\

p dP/dp\

T C

V W V A

mol»dm MPa MPa»K

_1

MPa •dm «mol

1 J/(mol«K)

-

m»s fiFa'S itiW/(m»K)

0.10 0.372 0.8419E-03 3.689 63.65 373.3 13.58 44.7

0.50 1.807 0.4417E-02 3.492 63.96 366.6 13.91 45.4

1.00 3.498 0.9342E-02 3.276 64.34 359.5 14.39 46.4

1.50 5.089 0.1476E-01 3.093 64.70 353.9 14.96 47.6

2.00 6.597 0.2067E-01 2.943 65.04 349.9 15.60 48.9

2.50 8.038 0.2707E-01 2.826 65.35 347.6 16.33 50.3

3.00 9.428 0.3396E-01 2.741 65.64 347.0 17.14 51.9

3.50 10.785 0.4137E-01 2.690 65.89 348.1 18.02 53.6

4.00 12.124 0.4931E-01 2.673 66.12 351.2 18.99 55.4

4.50 13.464 0.5783E-01 2.694 66.31 356.2 20.05 57.2

5.00 14.824 0.6697E-01 2.754 66.48 363.3 21.19 59.1

5.50 16.225 0.7681E-01 2.858 66.62 372.6 22.42 61.1

6.00 17.690 0.8741E-01 3.012 66.73 384.4 23.75 63.2

6.50 19.246 0.9886E-01 3.222 66.83 398.7 25.18 65.3

7.00 20.923 0.1113 3.497 66.90 415.7 26.73 67.5

279-
Table B4. Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 450.00 K (continued)

mol»dm

5P/3T|

MPa MPa«K

8?/dp W

3-1 - 1 MPa»dm »mol J/(mol»K) m»s

r, X

|iPa»s mW/(m«K)

7.50

8.00

8.50

9.00

9.50

10.00

10.50

11.00

11.50

12.00

22.756

24.784

27.055

29.622

32.549

35.914

39.805

44.325

49.593

55.745

0.1248

0.1394

0.1555

0.1730

0.1922

0.2133

0.2363

0.2614

0.2889

0.3189

3.847

4.282

4.818

5.472

6.265

7.224

8.374

9.745

11.372

13.290

66.97

67.02

67.07

67.13

67.19

67.26

67.34

67.45

67.57

67.71

435.6 28 .40 69.8

458.5 30 .21 72.2

484.6 32 .18 74.8

514.1 34 .32 77.6

547.3 36 .65 80.6

584.3 39 .21 83.8

625.3 42 .04 87.3

670.4 45 .16 91.1

719.7 48 .63 95.4

773.3 52 .52 100.0

12.50 62.938 0.3516 15.541 67.87 831.5 105.1

ETHANE ISOTHERM AT T = 500.00 K 3

_ 1 Second virial coefficient is -51.7 cm «mol

p P 3P/3T| d?/dp\ C

mol«dm

- 3

" - 1 3-1

MPa MPa«K MPa«dm •mol J/(mol«•K)

W

- l m«s

V

/iPa»s

A

mW/(m«K)

0.10

0.50

1.00

1.50

2.00

2.50

3.00

3.50

4.00

4.50

00

50

00

50

00

7.50

8.00

8.50

00

50

10.00

10.50

11.00

11.50

0.414

2.027

3.963

5.823

7.624

9.382

11.114

12.839

14.573

16.337

18.153

20.045

22.040

24.169

26.466

28.972

31.733

34.802

38.241

42.122

46.528

51.556

57.318

63.941

0.8412E-03

0.4399E-02

0.9273E-02

0.1462E-01

0.2043E-01

0.2673E-01

0.3352E-01

0.4082E-01

0.4868E-01

0.5713E-01

0.6622E-01

0.7602E-01

0.8660E-01

0.9803E-01

0.1104

0.1239

0.1385

0.1544

0.1717

0.1906

0.2112

0.2337

0.2583

0.2851

4.115

3.958

3.790

3.655

3.553

3.485

3.450

3.452

492

573

700

877

113

414

789

5.250

5.811

6.486

7.294

8.257

9.399

10.750

12.339

14.203

69.74

69.98

70.27

70.55

70.80

71.04

71.26

71.46

71.64

71.80

71.94

72.07

72.19

72.29

72.39

72.48

72.56

72.65

72.74

72.84

72.94

73.06

73.19

73.32

392.1

387.3

382.6

379.4

377.7

377

379

382

387

395

404.4

416.0

429.8

446.2

465.2

487.0

511.8

539.6

570.8

605.4

643.6

685.8

731.8

782.1

14.84

15.18

15.68

16.27

16.93

17.67

18.49

19.39

20.37

21.44

22.59

23.83

25.17

26.62

28.18

29.87

31.71

33.69

35.86

38.23

40.84

43.71

46.89

53.9

54.5

55.5

56.5

57.7

59.1

60.5

62.1

63.7

65.5

67

69

71

73

75

77.9

80.4

83.0

85.8

92.1

95.7

99.7

104.0

-280
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 550.00 K

3 - 1 Second virial coefficient is -36.7 cm •mol

p P 3P/3T|

p 3P/3p|

T CV W r? A

mol • dm MPa MPa-K"

1 MPa •dm «mol

1 J/(mol«K) m* s ii? a • s mW/ ( m • K

)

0.10 0.456 0.8406E-03 4.540 75.51 410.0 63.5

0.50 2.247 0.4386E-02 4.420 75.71 406.9 64.1

1.00 4.426 0.9225E-02 4.299 75.94 404.3 65.0

1.50 6.551 0.1452E-01 4.210 76.17 403.1 65.9

2.00 8.641 0.2026E-01 4.155 76.38 403.4 67.1

2.50 10.712 0.2648E-01 4.134 76.57 405.3 68.3

3.00 12.782 0.3319E-01 4.151 76.75 408.9 69.7

3.50 14.869 0.4042E-01 4.205 76.92 414.2 71.2

4.00 16.994 0.4819E-01 4.302 77.07 421.3 72.7

4.50 19.179 0.5657E-01 4.446 77.21 430.4 74.4

5.00 21.448 0.6560E-01 4.640 77.34 441.6 76.2

5.50 23.829 0.7533E-01 4.892 77.46 454.9 78.1

6.00 26.351 0.8584E-01 5.209 77.58 470.6 80.0

6.50 29.050 0.9720E-01 5.599 77.68 488.7 82.1

7.00 31.964 0.1095 6.074 77.79 509.5 84.3

7.50 35.140 0.1228 6.645 77.89 532.9 86.6

8.00 38.628 0.1373 7.327 77.99 559.2 89.1

8.50 42.488 0.1530 8.135 78.09 588.6 91.8

9.00 46.788 0.1701 9.090 78.19 621.2 94.6

9.50 51.606 0.1888 10.214 78.30 657.2 97.7

10.00 57.034 0.2090 11.533 78.42 696.8 101.1

10.50 63.177 0.2311 13.077 78.54 740.1 104.7

281-
Table B4 . Properties in the single-phase region along isotherms (continued)

ETHANE ISOTHERM AT T = 600.00 K

3 - 1 Second virial coefficient is -24.6 cm •mol

/iPa«s mW/(m«K)

73.5

74.0

74.8

75.7

76.8

77.9

79.2

80.6

82.1

83.6

85.4

87.2

89.1

91.1

93.3

95.7

98.2

100.8

103.7

106.9

10.00 67.434 0.2070 13.635 83.62 745.4 110.3

p P 5P/3T|

p dP/d P \ T C

V W

mol* dm MPa MPa»K

_1

MPa. • dm • mo

1 J/(mol«K)

-

m« s

0.10 0.498 0.8402E-03 4.965 80.95 427.2

0.50 2.466 0.4376E-02 4.881 81.12 425.6

1.00 4.886 0.9188E-02 4.804 81.32 424.8

1.50 7.275 0.1444E-01 4.759 81.51 425.4

2.00 9.651 0.2013E-01 4.750 81.69 427.5

2.50 12.031 0.2629E-01 4.777 81.86 431.1

3.00 14.435 0.3294E-01 4.843 82.01 436.3

3.50 16.882 0.4010E-01 4.952 82.16 443.3

4.00 19.394 0.4781E-01 5.106 82.29 452.1

4.50 21.996 0.5611E-01 5.311 82.42 462.9

5.00 24.715 0.6507E-01 5.573 82.54 475.7

5.50 27.580 0.7473E-01 5.899 82.66 490.7

6.00 30.626 0.8515E-01 6.297 82.77 507.9

6.50 33.890 0.9643E-01 6.776 82.87 527.6

7.00 37.417 0.1086 7.349 82.98 549.8

7.50 41.257 0.1218 8.027 83.08 574.7

8.00 45.465 0.1362 8.826 83.18 602.5

8.50 50.106 0.1517 9.765 83.29 633.3

9.00 55.256 0.1686 10.862 83.39 667.2

9.50 60.999 0.1870 12.143 83.50 704.6

282
Appendix C: Listing of a FORTRAN 77 program to calculate the thermophysical

properties of ethane

In this Appendix, we give the complete listing for a FORTRAN 77

(FORTRAN V) program to calculate the thermophysical properties of ethane.

Several aspects of this code must be mentioned. The program was written

for a mainframe computer with very high precision; implementations for many

personal computers will need to convert constants, functions, etc. to

double precision. The program reflects the correlations as written in the

body of this text; no systematic attempt was made to optimize the code.

The comments interspersed throughout the code are meant to assist a programmer; however these are not complete. The program should be used in

conjunction with this manuscript and [1], to assist in judging the

uncertainties of the resulting properties and the applicable ranges of the

correlations

-283
PROGRAM C2PROPS

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32) , PTRP , DTRP , TTRP

'

, CMW

10

15

20

WRITE(*,5)

FORMAT

(

********THIS PROGRAM ALLOWS INTERACTIVE CALCULATION^

*********OF MANY ETHANE THERMOPHYSICAL PROPERTIES**-

******'/

*****'/

******'/

*IT IS BASED ON THE CORRELATIONS OF FRIEND, INGHAM, AND ELY*'/

*******AS SUBMITTED TO J. PHYS . CHEM. REF. DATA 1989********'/

*******************UNDER THE TITLE:*************************'/

***********THERMOPHYSICAL PROPERTIES OF ETHANE*************'/

: Vf *-k -Je -k -A- -A-

-j-j— /

k*** AND APPEARING IN THIS NBS TECHNICAL NOTE********'/)

WRITE(*,6)

FORMAT

(

**THIS IMPLEMENTATION WAS WRITTEN FOR A MAIN FRAME COMPUTER*'/

***************WITH 60 BIT WORD SIZE***********************'

/

******THE UNITS FOR INPUT AND OUTPUT ARE:******************'/

***PRESSURE-MEGAPASCALS, DENSITY-MOLES PER CUBIC DECIMETER,--'"'/

***********TEMPERAURE - KELVINS , ENERGY - JOULES , ************** '

/

*************VISCOSITY-MICROPASCAL SECONDS , **************** '

/

*****AND THERMAL CONDUCTIVITY-MILLIWATTS PER METER KELVIN '/

** ***ALL NOMINALLY EXTENSIVE QUANTITIES ARE EXPRESSED *******'/

**************ON A PER MOLE BASIS************************ ' //)

PAUSE '*****PRESS ANY KEY TO CONTINUE*****'

WRITE(*,7)

FORMAT

(

*PLEASE CONSULT THE PAPER AND TEXT OF THIS TECH NOTE*****'/

 FOR FURTHER DETAILS CONCERNING THE CORRELATIONS** ****'/

A:*****^********************************************* - ////

)

WRITE (*, 15)

FORMAT (' PLEASE ENTER CODE FOR THE FOLLOWING CATEGORIES'/

OF THERMOPHYSICAL PROPERTIES:'/

1 ALONG THE SATURATION BOUNDARY'/

2 IN THE SINGLE PHASE GIVEN TEMPERATURE AND DENSITY'/

3 IN THE SINGLE PHASE GIVEN TEMPERATURE AND PRESSURE'/

4 OTHER STATE FUNCTIONS IN THE SINGLE PHASE'/

5 TRANSPORT PROPERTIES IN THE SINGLE PHASE'/

6 DILUTE AND IDEAL GAS PROPERTIES'/

7 TERMINATE THIS PROGRAM'/' ')

READ(*,*) I CAT

IF(ICAT.EQ.1)THEN

WRITE (*, 20)

ENTER FUNCTION NUMBER AND STATE POINT'/

SATURATION BOUNDARY (PRESSURE AND DENSITIES)'/

FROM ANCILLARY EQUATIONS- -GIVE T'/

2 SATURATION BOUNDARY (PRESSURE AND DENSITIES)'/

FROM MAXWELL CONSTRUCTION- -GIVE T'/

3 SATURATION TEMPERATURE FROM PRESSURE- -GIVE P'/

4 LIQUID HEAT CAPACITY ALONG SATURATION- -GIVE T'/

5 LIQUID SOUND SPEED ALONG SATURATION- -GIVE T'//'

READ(* , *) IFUNC , PROP1

IF(IFUNC.EQ.1)THEN

ANS=PSATF(PROP1)/10.

ANS1=DSATL(PR0P1)

ANS2=DSATV(PR0P1)

END IF

IF(IFUNC.EQ.2)CALL SATF( PROPl , ANS , ANSI , ANS2

)

IF(IFUNC . EQ . 2) ANS=ANS/10

IF(IFUNC.EQ.3)ANS=TSAT(PROP1*10.)

IF( IFUNC. EQ. 4) ANS=CSAT( PROPl)

IF(IFUNC.EQ.5)THEN

CALL SATF(PROPl,PPP,PROP2,PPPP)

FORMAT

(

1

')

-284-
25

30

35

ANS=WSF(PROP2 , PROP1)

END IF

IF(IFUNC.LE.2)WRITE(*,80)PROP1,ANS,ANS1,ANS2

IF( IFUNC. GT. 2) WRITE (*, 81) PROPl, ANS

END IF

IF(ICAT.EQ.2)THEN

WRITE(*,25)

FORMAT (' ENTER FUNCTION NUMBER AND STATE POINT'/

1 PRESSURE- -GIVE T AND RHO'/

2 ISOCHORIC HEAT CAPACITY- -GIVE T AND RHO'/

3 ISOBARIC HEAT CAPACITY- -GIVE T AND RHO'/

4 SOUND SPEED- -GIVE T AND RHO'/

5 ISOTHERMAL DP/DRHO- -GIVE T AND RHO'/

6 ISOCHORIC DP/DT--GIVE T AND RHO'/)

READ(* , *) IFUNC , PROP1 , PROP2

IF(IFUNC . EQ . 1) CALL PRESS (ANS , PROP2 , PROPl ,1)

IF(IFUNC . EQ . 1) ANS=ANS/10

IF(IFUNC.EQ.2)ANS= CVF(PROP2 , PROPl)

IF(IFUNC.EQ.3)ANS=CPEE(PROP2, PROPl)

IF( IFUNC. EQ. 4) ANS=WSF(PROP2 , PROPl)

IF ( I FUNC . EQ . 5 ) CALL DPDD ( ANS , PROP2 , PROPl , 1

)

IF(IFUNC.EQ.5)ANS=ANS/10.

IF( IFUNC . EQ . 6 ) CALL DPDT (ANS , PROP2 , PROPl , 1

)

IF(IFUNC.EQ.6)ANS=ANS/10.

WRITE (* , 82 ) PROPl , PROP2 , ANS

END IF

IF(ICAT.EQ.3)THEN

WRITE (*

FORMAT

(

1

30)

ENTER FUNCTION NUMBER AND STATE POINT'/

DENSITY- -GIVE T AND P'/

2 ISOCHORIC HEAT CAPACITY- -GIVE T AND P'/

3 ISOBARIC HEAT CAPACITY- -GIVE T AND P'/

4 SOUND SPEED- -GIVE T AND P'/

5 ISOTHERMAL DP/DRHO- -GIVE T AND P'/

6 ISOCHORIC DP/DT--GIVE T AND P'/)

READ(* , *) IFUNC , PROPl , PROP2

RHO = RHOF(PROP2*10. , PROPl)

I F ( I FUNC . EQ . 1 ) ANS=RHO

IF(IFUNC.EQ.2)ANS= CVF (RHO , PROPl)

IF ( IFUNC. EQ. 3 )ANS=CPEE (RHO, PROPl)

IF(IFUNC.EQ.4)ANS=WSF(RH0,PR0P1)

IF( IFUNC . EQ . 5 ) CALL DPDD (ANS , RHO , PROPl , 1

)

IF(IFUNC.EQ.6)CALL DPDT (ANS , RHO , PROPl , 1)

IF(IFUNC.GE.5)ANS=ANS/10.

WRITE (*,82) PROPl , PROP2 , ANS

END IF

IF(ICAT.EQ.4)THEN

WRITE (*

FORMAT

(

1

2

34

5

35)

40

ENTER FUNCTION NUMBER AND STATE POINT'/

ENTROPY- -GIVE T AND RHO'/

HELMHOLTZ ENERGY- -GIVE T AND RHO'/

INTERNAL ENERGY- -GIVE T AND RHO'/

GIBBS ENERGY- -GIVE T AND RHO'/

ENTHALPY- -GIVE T AND RHO'/)

READ(* , *) IFUNC , PROPl , PROP2

IF ( IFUNC. EQ.l)ANS=ENTROPY(PROP2, PROPl)

IF( IFUNC. EQ. 2 )ANS=HELM(PROP2, PROPl)

IF( IFUNC. EQ. 3 )ANS=UNTERN(PROP2 , PROPl)

IF( IFUNC. GE. 4) CALL PRESS (PPP , PROP2 , PROPl , 1)

IF( IFUNC . EQ . 4) ANS=GIBBS (PROP2 , PROPl , PPP)

IF(IFUNC.EQ.5)ANS=ENTHALP(PROP2, PROPl, PPP)

WRITE (*, 82) PROPl, PROP2 , ANS

END IF

IF(ICAT.EQ.5)THEN

WRITE (*, 40)

FORMAT (' ENTER FUNCTION NUMBER AND STATE POINT'/

285
C ' 1 VISCOSITY- -GIVE T AND RHO'/

C ' 2 THERMAL CONDUCTIVITY- -GIVE T AND RHO'/

C ' 3 VISCOSITY- -GIVE T AND P'/

C ' 4 THERMAL CONDUCTIVITY- -GIVE T AND P'/)

READ (* , *) IFUNC , PROP1 , PROP2

IF(IFUNC.EQ.1)ANS=VSCTY(PR0P2,PR0P1)

IF ( IFUNC . EQ . 2 ) ANS=XLAMF ( PROP2 , PROP1

IF(IFUNC.GE.3) PROO=RHOF(PROP2*10 . ,PROPl)

IF(IFUNC.EQ.3)ANS=VSCTY(PR00,PR0P1)

IF(IFUNC.EQ.4)ANS=XLAMF(PR00,PR0P1)

WRITE (* , 82) PROP1 , PROP2 , ANS

END IF

IF(ICAT.EQ.6)THEN

WRITE (*, 45)

45 FORMAT (' ENTER FUNCTION NUMBER AND STATE POINT'/

1 SECOND VIRIAL COEFFICIENT- -GIVE T AND 0'/

2 IDEAL GAS ISCHORIC HEAT CAPACITY- -GIVE T AND 0'/

3 IDEAL GAS ISOBARIC HEAT CAPACITY- -GIVE T AND 0'/

4 IDEAL GAS ENTHALPY- -GIVE T AND 0'/

5 IDEAL GAS INTERNAL ENERGY- -GIVE T AND 0'/

6 IDEAL GAS ENTROPY- -GIVE T AND RHO'/

7 IDEAL GAS HELMHOLTZ ENGERGY- -GIVE T AND RHO'/

8 IDEAL GAS ENTROPY- -GIVE T AND P'/

9 IDEAL GAS HELMHOLTZ ENERGY- -GIVE T AND P'/

10 DILUTE GAS VISCOSTIY- -GIVE T AND 0'/

11 DILUTE GAS THERMAL CONDUCTIVITY- -GIVE T AND 0'/)

READ(* , *) IFUNC , PROP1 , PROP2

IF (PROP2.EQ.0.)PROP2=0. 000001

IF(IFUNC. EQ. 1)ANS=BVIR(PR0P1)

IF ( (IFUNC . EQ . 8 ) . OR . (IFUNC . EQ . 9 ) ) PROP2=10 . *PROP2/ ( R*PR0P1

IF( (IFUNC. GT.l) .AND. (IFUNC . LT. 10) ) CALL IDEAL1(

C PROP1 , PROP2 , EID , HID , HEL , SID , CVID , CPID , 3

IF(IFUNC.EQ.2)ANS=CVID

IF(IFUNC.EQ. 3)ANS=CPID

IF(IFUNC.GE.4)ANS=HID

IF(IFUNC.EQ.5)ANS=EID

IF(IFUNC.EQ.6)ANS=SID

IF(IFUNC.EQ.7)ANS=HEL

IF(IFUNC.EQ.8)ANS=SID

IF(IFUNC.EQ.9)ANS=HEL

IF(IFUNC.EQ.10)ANS=ETAO(PROP1)

IF( IFUNC . EQ . 11) ANS=TCOND0 ( PROP1

IF( IFUNC. LE. 5) WRITER, 81) PROP1, ANS

I F (( I FUNC . GT . 5 ) . AND . ( I FUNC . LT . 10 )

) WRI TE ( * , 8 2 ) PROP1 , PROP2 , ANS

IF(IFUNC.GE.10)WRITE(*,81)PROP1,ANS

END IF

IF(ICAT.EQ.7)STOP 'FINISH C2PROPS'

GO TO 10

80 FORMAT(1X,4G20.9)

81 FORMAT(1X,2G20.9)

82 FORMAT(1X,3G20.9)

END

C

C**

c**

C

FUNCTION CSAT(T)

«f******THIS FUNCTION CALCULATES THE HEAT CAPACITY OF THE LIQUID

sr******ALONG THE SATURATION BOUNDARY

COMMON /DERIV/ DPSDT, DDSDT

RHO=DSATL(T)

CALL DPDT(DPD,RHO,T,l)

CSAT=CVF(RHO , T) - 100 . *T/RHO**2*DPD*DDSDT

RETURN

END

286-
FUNCTION BVIR(T)

C

C*********THIS FUNCION CALCULATES THE SECOND VIRIAL COEFFICIENT

C*********USING THE SCHMIDT -WAGNER EQUATION OF STATE

C

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32) , PTRP , DTRP , TTRP

* , CMW

C

TA = TC / T

T15 = TA ** 1.5

T25 = TA ** 2.5

T5 = TA ** 5 T6 = TA ** 6 B = G(l) + G(2)*T15 + G(3)*T25 + G(14)*T5+ G(15)*T6

BVIR = B / DC

RETURN

END

C

SUBROUTINE SATF(TS , PS ,DSL,DSV)

C PURPOSE --- THIS ROUTINE CALCULATES THE SATURATION

C PRESSURE AND COEXISTING DENSITIES FROM

C AN EQUATION OF STATE.

C

C VERSION 2.0 5/20/82

C

C CODED BY -- J. F. ELY

C THERMOPHYSICAL PROPERTIES DIVISION

C NATIONAL BUREAU OF STANDARDS

C BOULDER, COLORADO 80303

C

C * * * * -k -k -k ~k -k -k -k -k -k -k -k ~k ~k -k -k -k -k -k -k * -k -k ~k -k COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32), PTRP, DTRP, TTRP

* , CMW

LOGICAL ENTER

DATA TOL, FTOL, ENTER / 1.0E-4, 1.0E-6, .FALSE. /

C

IF(TS.LT.TC) GO TO 005

PS = PC

DSL = DC

DSV = DC

RETURN

C

005 IF (ENTER) GO TO 010

ENTER = .TRUE.

BV = ALOG(PTRP/PC) / (1.0/TTRP - 1.0/TC)

AV = ALOG(PC) - BV / TC

C INITIAL GUESS AT THE VAPOR PRESSURE

010 PS = EXP(AV+BV/TS)

C

C INITAL GUESS AT THE VAPOR DENSITY

DV = PS / (R*TS)

C INITIAL GUESS AT LIQUID DENSITY

C

TR = TS /TC

EPS = (1.0-TR)**(2. 0/7.0)

DL = DC / ZC**EPS

IF (DL.GT.DTRP) DL = DTRP

C

C IMPROVE VAPOR GUESS NEAR CRITICAL

C

IF (TR.LT.0.85) GO TO 015

DV = DL - 3.75 * DC * (1 . 0-TR)**0 . 333

C NEWTON -RAPHSON ITERATION FOR DENSITIES

015 DO 100 J = 1, 25

020 CALL PVTF(PL,DL,TS,DPDL,D2PDD2,GL)

030 IF (DPDL.GT.O.O.AND.PL.GT.O.O) GO TO 040

-287-
DL = 1.02 * DL

GO TO 020

040 CALL PVTF(PV,DV,TS I DPDV,D2PDD2 ) GV)

IF (DPDV.GT.0.0) GO TO 060

DV = 0.98 * DV

GO TO 040

060 Fl = GL -GV

F2 = PL - PV

F2L = DPDL

F2V = - DPDV

F1L = F2L / DL

F1V = F2V / DV

DENOM = F1L * F2V - F2L * F1V

IF (ABS(DENOM) .LE.1.0E-10) GO TO 120

DDL = -(F1*F2V-F2*F1V) / DENOM

DDV = -(F1+DDL*F1L) / F1V

DL = DL + DDL

IF(DL.LT.DC) DL = DC

DVS = DV

DV = DV + DDV

IF(DV.GT.DC) DV = DC

IF(DV.LE.O.O) DV=DVS/2.0

IF (ABS(DDL/DL) .LT.TOL .AND. ABS(DDV/DV) . LE. TOL) GO TO 110

FNORM = F1*F1 + F2*F2

IF(TR.LT.0.99 .AND. FNORM. LE . FTOL) GO TO 110

100 CONTINUE

110 PS = PV

DSL = DL

DSV = DV

RETURN

120 WRITE(6,340) DENOM

GO TO 110

300 FORMAT(I3,8G10.4)

310 FORMAT(I3,2F12.8,G13.6)

330 F0RMAT(F8 . 2 , G13 . 6 , 2F10 . 6 , 2G13 .6)

340 FORMAT('DENOM IS TOO SMALL IN SATF',G13.6)

END

FUNCTION RH0F(P1,P2)

-k -k

PURPOSE -- THIS ROUTINE CALCULATES THE DENSITY OF A FLUID AT

T AND P GIVEN AN INITIAL GUESS IN FOP. ON EXIT,

IT RETURNS THE FUGACITY COEFFICIENT IN FOP. IT

REQUIRES A ROUTINE 'PVTF' WHICH CALCULATES P,

DPDD, AND GR = G(T , P) -G*(T , 1)

CODED BY- -J. F. ELY

THERMOPHYSICAL PROPERTIES DIVISION

NATIONAL ENGINEERING LABORATORY

NATIONAL BUREAU OF STANDARDS

BOULDER, COLORADO 80302

VERSION 2.0 5/23/82

-k -k ~k -k -k -k ~k -k ~k ~k •k 'k -k X -k -k -k -k -k

REVISED 3/12/85 TO CHANGE BOUNDS AND AVOID CRITICAL REGION IN N-R.

COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32) , PTRP , DTRP , TTRP

<

, CMW

DATA TOLERD, TOLERP / 1.0E-8, 1.0E-8/

ESTABLISH BOUNDS AND START NEWTON -RAPHSON

PI

-288
T = P2

D = P / (R*T)

IF (T.GT.TC) GO TO 019

CALL SATF(T,PS,DSL,DSV)

D = DSV

IF (P.GE.PS) D = DSL

IF ((P.GE.1.5*PS).AND.((TC-T).LE.7.)) D = 2.0 * DSL

GO TO 020

019 IF (P.GT.2.*PC) D = 1.5 * MAX(D,DC)

C

C ESTABLISH BOUNDS AND START NEWTON RAPHSON

020 DLO=0.0

DHI =1.50 * DTRP

DMAX = 1.2 * DHI

DO 100 IAP-1,20

CALL PVTF(PX,D,T,DPDD,D2PDD2,GR)

C

C IF DPDD IS ZERO OR NEGATIVE, TRY BISECTION

C IF(DPDD.LE.1.0E-3) GO TO 120

DP=P-PX

DD=DP/DPDD

C SAVE DENSITY FOR POSSIBLE BISECTION

IF (DP) 040,300,060

040 DHI=D

GO TO 080

060 DLO=D

080 DN=D+DD

C KEEP D WITHIN BOUNDS OR GO TO BISECTION

IF (DN.LT.0.0 .OR. DN.GT.DMAX) GO TO 120

D=DN

IF(LAP.EQ.l) GO TO 100

IF(ABS(DP/P) .LE.TOLERP) GO TO 300

IF(ABS(DD/D) .LE.TOLERD) GO TO 300

100 CONTINUE

C NEWTON -RAPHSON FAILURE. TRY BISECTION

120 IF(T.GT.TC) GO TO 160

C

C SUB -CRITICAL. MAKE SURE THAT WE HAVE THE

C PROPER BOUNDS ON THE DENSITY.

IF(P.LT.PS) GO TO 140

DLO = DSL

IF(DHI.LE.DSL) DHI=DMAX

GO TO 160

C 140 IF(DLO.GE.DSV) DLO=0 . DHI = DSV

C

C START THE BISECTION

160 D=0.50*(DLO+DHI)

CALL PVTF(PX,D,T,DPDD,D2PDD2,GR)

DP=PX-P

IF(DP) 200,300,220

200 DLO=D

GO TO 240

220 DHI=D

240 IF(ABS(DP/P) . LE . TOLERP) GO TO 300

IF(ABS(DLO/DHI-1.0) .GT.TOLERD) GO TO 160

C

C BISECTION FAILED. GIVE UP

260 WRITE (6, 400) T, P,D , DPDD , DLO , DHI , LAP , PX

C CONVERGENCE ! ! ! 300 RHOF=D

RETURN

400 FORMATC'RHOF FAILED AT T =',F9.3,' P =' ,G14 . 7 , 4G12 . 6 , 14 , G12 . 6)

END

-289-
SUBROUTINE PVTF( PO , DO , TO , DPDD , D2PD2 , GO

)

~k &&&•&•&•&•$:&&&&•& &•&&&&&&•&•&•&•&&•$:•&•&

PURPOSE --- THIS ROUTINE CALCULATES THE PRESSURE, ITS FIRST

TWO DENSITY DERIVATIVES AND THE GIBBS ENERGY

RELATIVE TO THE IDEAL GAS AT 1 BAR

THIS ROUTINE IS FOR THE WAGNER EQUATION OF STATE

VERSION 1.0 - 2/18/85

CODED BY -- J. F. ELY

CHEMICAL ENGINEERING SCIENCE DIVISION

NATIONAL BUREAU OF STANDARDS

BOULDER, COLORADO 80303

DIMENSION S(4), P(10,3), Q(3), DQDD(3) , D2QDD2(3), D3QDD3(3)

COMMON /REFDAT/ RG , PC, DC, TC , ZC , G(32) , PTRP , DTRP , TTRP

, CMW

DATA P / 30*0. /, TLAST / -1.0 /

T = TC / TO

D = DO / DC

IF(T.EQ. TLAST) GO TO 040

TLAST=T

RT = RG * TO

TS = SQRT(T)

TTS = T * TS

T2

T3

T4

T5

T6

T7

T8

Til = T17 = T18 =

T

T

T *

T * T *

T * T2

T8

* T

* T2

T3

T4

T5

T6

T6

* T3

T6 * Til

T * T17

P(1,D

P(2,l)

P(3,l)

P(6,l)

P(7,l)

P(8,l)

P(l,2)

P(2,2)

P(3,2)

P(5,2)

P(6,2)

P(7,2)

P(8,2)

P(10,2) =

P(2,3) = P(3,3)

P(4,3)

P(5,3)

G(l) + (G(2) + G(3)*T) * TTS

G(4)/TS + G(5)*TTS + G(6)*T2

G(7) + (G(8) + G(9)*TTS) * T

G(10)

G(11)*T2 + G(12)*T5

G(13)*T2

G(14)*T5

(G(16) + G(18)*T3

G(20)

G(21)

G(22)

G(23)

G(24)

+ G(15)*T6

G(17)*T2) - + G(19)*T7T2 * TTS

T6

T8

T4

T6

T5

TS

TS

TS

G(25) * Til * Til

G(26) * Til + G(27) * T18

(G(28) + G(29)*T11*T) * Til

(G(30) + T * (G(31) + G(32)*T5)) T17

290
060

070

10

* D + P(ll-I

* D + S(l)

GO TO 060

* D + S(2)

GO TO 060

* D + S(3)

040 DO 070 J = 1, 3 DO 050 K - 1, 4

050 S(K) = 0.

DO 060 1=1

S(l) = S(l) * D + P(11-I,J)

S(2) = S(2)

IF (I.EQ.10)

S(3) = S(3)

IF (I.EQ.9)

S(4) = S(4)

CONTINUE

Q(J) = S(l) * D

DQDD(J) = S(2)

D2QDD2(J) = S(3) * 2.0

D3QDD3(J) = S(4) * 6.0

D2 = D * D

D3 = D * D2

F2 = EXP(-D2)

F3 = EXP(-D*D3)

TWOD = 2.0 * D

FORD = 4.0 * D3

DRT = DO * RT

PHI = Q(l) + Q(2) * F2 + Q(3) * F3

TRM2 = DQDD(2) - TWOD * Q(2)

TRM3 = DQDD(3) - FORD * Q(3)

DPHDD = DQDD(l) + TRM2 * F2 + TRM3 * F3

PO = DRT * (1.0 + D * DPHDD)

TRM2P = D2QDD2(2) - 2.0 * Q(2) - TWOD * DQDD(2)

TRM3P = D2QDD2(3) - 12.0 * D2 * Q(3) - FORD * DQDD(3)

TRM22 = TRM2P - TWOD * TRM2

TRM33 = TRM3P - FORD * TRM3

D2PHD2 = D2QDD2(1) + TRM22 * F2 + TRM33 * F3

DPDD = RT * (1.0 + TWOD * DPHDD + D2 * D2PHD2)

TRM22P = D3QDD3(2) - 4.0 * DQDD(2) - TWOD * D2QDD2(2)

'< - 2.0 * TRM2 - TWOD * TRM2P

TRM33P = D3QDD3(3) - 24.0 * D * (Q(3) + D * DQDD(3))

'< - FORD * (D2QDD2(3) + TRM3P) - 12.0 * D2 * TRM3

D3PHD3 = D3QDD3(1) + (TRM22P - TWOD * TRM22) * F2

'< + (TRM33P - FORD * TRM33) * F3

D2PD2 = RT * (2.0*DPHDD + 4.0*D*D2PHD2 + D2*D3PHD3) / DC

ZO = PO / DRT

GO = RT * (PHI

RETURN

END

+ ZO - 1.0 + ALOG(DRT))

FUNCTION CVF(D,T)

:*******THIS FUNCTION CALCULATES THE ISOCHORIC HEAT CAPACITY

CALL CVR(CVD,D,T,1)

CALL IDEAL(T,CVI,SI)

CVF = CVI + 100.0 * CVD

RETURN

END

291
FUNCTION WSF(D,T)

C

C THIS ROUTINE CALCULATES THE SOUND VELOCITY

C GIVEN THE DENSITY AND TEMPERATURE

C

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32), PTRP, DTRP , TTRP

* , CMW

C

COMMON /DPDCAL/ CP, CV , DPD , DPT

C

CV = CVF(D.T)

CALL DPDT(DPT,D,T,1)

CALL DPDD(DPD,D,T,1)

DPT = DPT / D

CP = CV + 100.0 * T * DPT * DPT / DPD

WSS = CP * DPD / (CMW * CV)

IF(WSS.LT.O.)WSS=0.0

WSF = SQRT(1.0E5 * WSS)

RETURN

END

C

SUBROUTINE PROPSS (PP, DD,TT , IDD)

C*******'*****THIS SUBROUTINE CALCULATES MANY OF THE THERMODYNAMIC

C************PROPERTIES FROM THE SCHMIDT -WAGNER EQUATION OF STATE

DIMENSION X(33),B(33)

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32), PTRP, DTRP, TTRP

* , CMW

EQUIVALENCE (B,X)

1 CONTINUE

D = DD/DC

DEN = DD

T = TC/TT

TEMP = TT

RT = R * TEMP

DRT = DEN * RT

DDRT = D * DRT

RTD = RT / DC

RD - DEN * R

RTT = RD / TC

D2 = D * D

D3 = D2 * D

D4 = D3 * D

D5 = D4 * D

D6 = D5 * D

D7 = D6 * D

D8 = D7 * D

D9 = D8 * D

D10 = = D9 * D

Dll = D10 * D

D12 = = Dll * D

D13 = = D12 * D

D14 = D13 * D

D15 = D14 * D

D16 = D15 * D

TS = SQRT (T)

TMS - 1.0 / TS

T15 = T * TS

T2 = T * T

T25 = T2 * TS

T3 = T2 * T

T35 = T3 * TS

T4 = T3 * T

T45 = T4 * TS

T5 = T4 * T

T55 = T5 * TS

T6 = T5 * T

292-
T65 = T6 * TS

T7 = T6 * T

T75 = T7 * TS

T8 = T7 * T

T85 = T8 * TS

T9 = T8 * T

T95 = T9 * TS

Til = T8 * T3

T12 = Til * T

T17 = T12*T5

T18 = T17 * T

T19 = T18 * T

T22 = T18 * T4

T23 = T22 * T

T24 = T23 * T

Fl = EXP ( -D2)

F2 = EXP ( -D4)

GO TO (100,200, 300,400,500,600,700,800) ,K

ENTRY PRESS (PP, DD,TT,IDD)

C********ENTRY TO CALCULATE PRESSURE

K = 1 GO TO 1 100 CONTINUE

B( 1) = DDRT * 1.0

B( 2) = DDRT * T15

B( 3) = DDRT * T25

B( 4) = DDRT * 2 . *D*TMS

B( 5) = DDRT * 2.*D*T15

B( 6) = DDRT * 2 . *D*T2

B( 7) = DDRT * 3 . *D2

B( 8) = DDRT * 3.*D2*T

B( 9) = DDRT * 3.*D2*T25

B(10) = DDRT * 6 . *D5

B(ll) = DDRT * 7.*D6*T2

B(12) = DDRT * 7 . *D6*T5

B(13) = DDRT * 8.*D7*T2

B(14) = DDRT * (l.-2.*D2)*T5*Fl

B(15) = DDRT * (l.-2.*D2)*T6*Fl

B(16) = DDRT * (2.*D-2.*D3)*T35*F1

B(17) = DDRT * (2.*D-2.*D3)*T55*F1

B(18) = DDRT * (3.*D2-2.*D4)*T3*F1

B(19) = DDRT * (3.*D2-2.*D4)*T7*F1

B(20) = DDRT * (5.*D4-2.*D6)*T6'*F1

B(21) = DDRT * (6.*D5-2.*D7)*T85*F1

B(22) = DDRT * (7.*D6-2.*D8)*T4*F1

B(23) = DDRT * (8.*D7-2.*D9)*T65*F1

B(24) = DDRT * ( 10 . *D9 - 2 . *D11)*T55*F1

B(25) = DDRT * (2.*D-4.*D5)*T22*F2

B(26) = DDRT * (3.*D2-4.*D6)*T11*F2

B(27) = DDRT * ( 3 . *D2 - 4 . *D6 ) *T18*F2

B(28) = DDRT * (4 . *D3-4 . *D7) *T11*F2

B(29) = DDRT * (4 . *D3-4 . *D7)*T23*F2

B(30) = DDRT * (5.*D4-4.*D8)*T17*F2

B(31) = DDRT * (5.*D4-4.*D8)*T18*F2

B(32) = DDRT * ( 5 . *D4 - 4 . *D8 ) *T23*F2

IF(IDD.GT.0)GO TO 102

B(33) = PP-DRT

RETURN

102 P = M = 32

DO 101 I = 1,M

P = P+B(I) * G(I)

101 CONTINUE

P = P + DRT

PP = P RETURN

-293-
ENTRY DPDD(PP,DD,TT,IDD)

c****

c ******ENTRY TO CALCULATE ISOTHERMAL DENSITY DERIVATIVE OF PRES

K = 2 GO TO 1 200 CONTINUE

B( 1) = RT k 2.00 * D

B( 2) = RT * 2.00 * D * T15

B( 3) = RT * 2.00 * D * T25

B( 4) = RT •k 6.00 * D2 *TMS

B( 5) = RT -k 6.00 * D2 * T15

B( 6) = RT k 6.00 * D2 * T2

B( 7) = RT •k 12.00 * D3

B( 8) = RT k 12.00 * D3 * T

B( 9) = RT * 12.00 * D3 * T25

B(10) = RT •* 42.00 * D6

B(ll) = RT k 56.00 * D7 * T2

B(12) = RT * 56.00 * D7 * T5

B(13) = RT * 72.00 * D8 * T2

B(14) = RT k Fl * (2.00 * D - 10 *D3 + 4.*D5) * T5

B(15) = RT k Fl * (2.00 * D - 10 *D3 + 4.*D5) * T6

B(16) = RT k Fl * (6.00 * D2 - 14 *D4 + 4.*D6) * T35

B(17) = RT k Fl * (6.00 * D2 - 14 *D4 + 4.*D6) * T55

B(18) = RT k Fl * (12.0 * D3 - 18 *D5 + 4.*D7) * T3

B(19) = RT k Fl * (12.0 * D3 - 18 *D5 + 4.*D7) * T7

B(20) = RT k Fl * (30.00 *D5 - 26 *D7 + 4.*D9) * T6

B(21) = RT k Fl * (42.00 *D6 - 30 *D8 + 4.*D10) * T85

B(22) = RT k Fl * (56.00 *D7 - 34 *D9 + 4.*D11) k T4

B(23) = RT k Fl * (72.00 *D8 - 38 *D10 + 4.*D12) * T65

B(24) = RT k Fl * (110.00 *D10 -46 *D12 + 4.*D14) * T55

B(25) = RT k F2 * (6.00 * D2 - 36 * D6 + 16.0 k D10) * T22

B(26) = RT k F2 * (12.0 * D3 - 44 * D7 + 16.0 k Dll) * Til

B(27) = RT k F2 * (12.0 * D3 - 44 * D7 + 16.0 * Dll) * T18

B(28) = RT k F2 * (20.0 * D4 - 52 * D8 + 16.0 • * D12) * Til

B(29) = RT k F2 * (20.0 * D4 - 52 * D8 + 16.0 • * D12) * T23

B(30) = RT k F2 * (30.0 * D5 - 60 * D9 + 16.0 •k D13) * T17

B(31) = RT •k F2 * (30.0 * D5 - 60 * D9 + 16.0 ' * D13) * T18

B(32) = RT k F2 * (30.0 * D5 - 60.0 * D9 - 16.0 * D13) * T23

M = 32

IF(IDD.(3T.0)GO TO 202

B(33) = PP- RT

RETURN

202 P =

DO 201 [ = 1 M

P = P+B(I) * G(I)

201 CONTINUE

P = P+RT

PP = P

C

RETURN

ENTRY DPDT(PP,DD,TT,IDD)

c****

C

****ENTRY TC) CALCULATE ISOCHORIC TEMPERATURE DERIVATIVE OF PRE

K = 3 GO TO 1 300 CONTINUE

B( 1) = RD * D B( 2) = -RE) >t .5*D*T15

B( 3) = -RE) * 1.5*D*T25

B( 4) = RD * 3.*D2*TMS

B( 5) = -RE) * D2*T15

B( 6) = -RE) * 2.*D2*T2

B( 7) = RD k 3.*D3

B( 8) = O.C) B( 9) = -RE) k 4.5*D3*T25

294
302

301

B(10) = RD * 6.*D6

B(ll) = -RD * 7.*D7*T2

B(12) = -RD * 28.*D7*T5

B(13) = -RD * 8.*D8*T2

B(14) = -RD * (4.0*D-8.*D3)*T5*F1

B(15) = -RD * (5.0*D-10.*D3)*T6* Fl

B(16) = -RD * 5.0*(D2-D4)*T35*F1

B(17) = -RD * 9.0*(D2-D4)*T55*F1

B(18) = -RD * (6.*D3-4.*D5)*T3*F1

B(19) = -RD * (18.*D3-12.*D5)*T7*F1

B(20) = -RD * (25.*D5-10.*D7)*T6*F1

B(21) = -RD * (45.0*D6-15.*D8)*T85*F1

B(22) = -RD * (21.*D7-6.*D9)*T4*F1

B(23) = -RD * (44.*D8-11.*D10)*T65*F1

B(24) = -RD * (45.*D10-9.*D12)*T55*F1

B(25) = -RD * (42.*D2-84.*D6)*T22*F2

B(26) = -RD * (30.*D3-40.*D7)*T11*F2

B(27) = -RD * (51.*D3-68.*D7)*T18*F2

B(28) = -RD * 40.*(D4-D8)*T11*F2

B(29) = -RD * 88.*(D4-D8)*T23*F2

B(30) = -RD * (80.*D5-64.*D9)*T17*F2

B(31) = -RD * (85.*D5-68.*D9)*T18*F2

B(32) = -RD * (110.*D5-88.*D9)*T23*F2

IF(IDD.GT.0)GO TO 302

B(33) = PP- RETURN

P = DO 301 I =

P = P+G(I)

CONTINUE

PP = P+RD

RETURN

RD

32

B(I)

C****

c

400

ENTRY SR(PP,DD,TT,IDD)

r*****ENTRY TO CALCULATE RESIDUAL ENTROPY

K = 4

GO TO 1 CONTINUE

1) = -R

2) = R *

3) = R *

4) = -R

5) = R *

6) = R

7) = -R

8) = 0.0

9) = R *

10) = -R

11) = R *

12) = R * 13) = R * 14) = R *

15) = R *

16) = R *

17) = R *

18) = R *

19) = R *

20) = R *

21) = R *

22) = R * 23) = R *

24) = R *

25) = R * 26) = R *

27) = R *

D

0.50 * D * T15

1.50 * D * T25

* 1.50 * D2 * TMS

0.50 * D2 * T15

* D2 * T2

* D3

1.5 * D3 * T25

' D6

D7

4.00 * D7 * T5

D8 * 4.00

00

5500

00

00

5

5

5 21.0

10.0

17.0

T2

* D7

T2

* D - * D - * D2 - * D2 - * D3

* D3

* D5

D6 - D7 - D8 - D10

* D2

* D3

* D3

T5 * T6 * T35 * T55

* T3

* T7

* T6

T85 * T4 * T65

* T55

* T22

* Til

* T18

Fl

Fl

Fl

* Fl

* Fl

* Fl

* Fl

Fl

Fl

* Fl

* Fl

* F2

* F2

* F2

295
X(28) = R * 10.0 * D4 * Til * F2

X(29) = R * 22.0 * D4 * T23 * F2

X(30) = R * 16.0 * D5 * T17 >t F2

X(31) = R * 17.0 * D5 * T18 * F2

X(32) = R * 22.0 * D5 * T23 * F2

IF(IDD. GT.0)GO TO 402

RETURN

402 P =

DO 401 I = 1 ,32

P = P+G(I) * X(I)

401 CONTINUE

PP = P

RETURN

C

ENTRY AR(PP, DD,TT,IDD)

T*/"\ /^ A T PTTT AT1 !-* ni-** c tMNlKI TO CALCULATE RE:>UDU

K = 5 GO TO 1 500 CONTINUE

B( 1) = RT * D

B( 2) = RT •k D * T15

B( 3) = RT * D * T25

B( 4) = RT k D2 *TMS

B( 5) = RT •k D2 * T15

B( 6) = RT k D2 * T2

B( 7) = RT k D3

B( 8) = RT •k D3 * T

B( 9) = RT k D3 * T25

B(10) = RT •k D6

B(ll) = RT •k D7 * T2

B(12) = RT "k D7 * T5

B(13) = RT "a D8 * T2

B(14) = RT k D * T5 * Fl

B(15) = RT k D * T6 *F1

B(16) = RT * D2 * T35 * Fl

B(17) = RT * D2 *T55 * Fl

B(18) = RT * D3 * T3 * Fl

B(19) = RT * D3 * T7 * Fl

B(20) = RT * D5 * T6 * Fl

B(21) = RT * D6 * T85 * Fl

B(22) = RT * D7 * T4 * Fl

B(23) = RT * D8 * T65 * Fl

B(24) = RT * D10 * T55 * Fl

B(25) = RT * D2 * T22 * F2

B(26) = RT k D3 * Til * F2

B(27) = RT -k D3 * T18 * F2

B(28) = RT k D4 * Til * F2

B(29) = RT -k D4 * T23 * F2

B(30) = RT JL. D5 *T17 * F2

B(31) = RT -k D5 * T18 * F2

B(32) = RT k D5 * T23 * F2

IF(IDD. 2T.0)GO TO 502

RETURN

502 P = DO 501 I = 1 ,32

P = P+G(I) * B(I)

501 CONTINUE

PP = P

RETURN

-296
ENTRY CVR(PP,DD,TT,IDD)

(J "A" ~k -k -k ~k >r *• ~k &-k J c :ntry tiJ CALCULATE RES ID!JAL IS

K = 6 GO TO l 600 CONTINUE

X( 1) = 0.0

X( 2) = -R * 0.75 * D * T15

X( 3) = -R * 3.75 * D * T25

X( 4) = -R * 0.75 * D2 * TMS

X( 5) = -R * 0.75 * D2 * T15

X( 6) = -R * 2.00 * D2 * T2

X( 7) = 0.0

X( 8) = 0.0

X( 9) = -R * 3.75 * D3 * T25

X(10) = 0.0

X(ll) = -R * 2.00 * D7 * T2

X(12) = -R * 20.00 * D7 * T5

X(13) = -R * 2.00 * D8 * T2

X(14) = -R * 20.00 * D * T5 * Fl

X(15) = -R * 30.00 * d * T6 * Fl

X(16) = -R * 8.75 * D2 *T35 * Fl

X(17) = -R * 24.75 * D2 * T55 * Fl

X(18) = -R * 6.00 * D3 * T3 * Fl

X(19) = -R * 42.00 * D3 * T7 »' Fl

X(20) = -R * 30.00 * D5 * T6 >

< Fl

X(21) = -R * 63.75 * D6 *T85 >' Fl

X(22) = -R * 12.0 * D7 * T4 * Fl

X(23) = -R * 35.75 * D8 * T65 -k Fl

X(24) = -R * 24.75 * D10 * T55

X(25) = -R * 462.0 * D2 * T22 -k F2

X(26) = -R * 110.0 * D3 * Til * F2

X(27) = -R * 306.0 * D3 * T18 * F2

X(28) = -R * 110.0 * D4 * Til -k F2

X(29) = -R * 506.0 * D4 * T23 * F2

X(30) = -R * 272.0 * D5 * T17 * F2

X(31) = -R * 306.0 * D5 * T18 * F2

X(32) = -R * 506.0 * D5 * T23 * F2

IF(IDE>.GT.0)GO TO 602

RETURbf 602 P = DO 601 1 = 1 ,32

P = P+G(I) * X(I)

601 CONTINUE

PP = I

i RETUR^f C ENTRY DP2D2(PP,DD,TT,IDD)

C****-A-****ENTRY TO CALCULATE SECOND ISOTH

C K = 7

fKtbbUKt

GO TO 1 700 CONTINUE

B( 1) = RTD < < 2.0

B( 2) =RTD * 2.0 * T15

B( 3) =RTD * 2.0 * T25

B( 4) =RTD * 12.0 * D * TMS

B( 5) =RTD * 12.0 * D * T15

B( 6) =RTD * 12.0 * D * T2

B( 7) =RTD * 36.0 * D2

B( 8) =RTD * 36.0 * D2 * T

B( 9) =RTD * 36.0 * D2 * T25

B(10) =RTD * 252. * D5

B(ll) =RTD * 392. * D6 * T2

B(12) =RTD * 392 D6 T5

297
702

701

B(13) =RTD

B(14) =RTD

B(15) =RTD

B(16) =RTD

B(17) =RTD

B(18) -RTD*

B(19) -RTD*

B(20) =RTD*

B(21) -RTD*

B(22) -RTD*

B(23) -RTD*

B(24) -RTD*

B(25) -RTD*

B(26) -RTD*

B(27) -RTD*

B(28) -RTD*

B(29) -RTD*

B(30) =RTD*

B(31) -RTD*

B(32) -RTD*

M = 32

IF(IDD.GT.O

B(33) = PP

RETURN

PP =

DO 701 I = PP = PP + B

CONTINUE

PP = PP

RETURN

* 576

*( 2 *( 2 *(12.

*(12.

36.0

36.0

150.

252.

392.

576.

1100

12.0

36.0

36.0

80.0

80.0

150.

150.

150.

.0 - .0 - 0*D

0*D

*D2

*D2

0*D4

0*D5

D7 *

34.

34.

- 68.

- 68.

-114.

-114.

-242

-324

0*D6-418.

0*D7-524.

.0*D9-772

*D- 240.0

-356.

-356.

-496.

*D3 -496.

0*D4 -660

0*D4 -660

0*D4-660.

*D2

*D2

*D3

T2

* D2 + 40. * D2 + 40. * D3 + 52.0

* D3 + 52.0

* D4 + 64. * D4 + 64.

.0*D6 + 88.0

0*D7 +100.0

*D8 + 112.0

0*D9 + 124.0

.0*D11 +148.0

'< D5 +304.0

0*D6 +352.0 * 0*D6 +352.0 * 0*D7 +400.0 * 0*D7 +400.0 * .0*D8 +448.0

.0*D8 +448.0*

0*D8 +448.0 *

* D4 - * D4 - * D5 - l * D5 - ; * D6 - * D6 - * D8 - .

*• D9 - 8 * D10-

'< Dll- 8 *D13- 8

'< D9- 64

D10- 64

D10- 64

Dll- 64

Dll- 64

* D12-64

D12- 64

D12- 64

8.0 * D6

8.0 * D6

1.0 * D7)

J.O * D7)

8.0 * D8

8.0 * D8

1.0 * D10

* Dll)

i.O * D12

* D13)

* D15)

* D13)

* D14)

* D14)

* D15)

* D15)

* D16)

* D16)

* D16)

)G0 TO 702

1,M

(D*G(I)

)*T5*F1

) *T6*F1

*T35*F1

*T55*F1

)*T3*F1

)*T7*F1

)*T6*F1

*T85*F1

) *T4*F1

*T65*F1

*T55*F1

*T22*F2

*T11*F2

*T18*F2

*T11*F2

*T23*F2

*T17*F2

*T18*F2

*T23*F2

C*****

C

ENTRY DP2DT2(PP,DD,TT,IDD)

• ENTRY TO CALCULATE SECOND ISOCHORIC TEMPERATURE DERIVATIVE

•** **OF PRESSURE

800

K = 8 GO TO 1 CONTINUE

1) = 0.0

2) = RTT *

3) = RTT * 4) = RTT *

5) = RTT *

6) = RTT *

7) = 0.0

8) = 0.0

9) = RTT * 10) = 0.0

11) = RTT * 12) = RTT * 13) = RTT * 14) = RTT * 15) = RTT * 16) = RTT * 17) = RTT * 18) = RTT * 19) = RTT * 20) = RTT *

21) = RTT *

22) = RTT *

23) = RTT * 24) = RTT * 25) = RTT * 26) = RTT * 27) = RTT * 28) = RTT *

D * 0.75 * T25

D * 3.75 * T35

1.5 * D2 * TS

1.5 * D2 * T25

4 . 0*D2*T3

11.25*D3*T35

14.*D7 *T3

140. *D7* T6

16.*D8 *T3

(20.*D-40.*D3)*T6 * Fl

(30.*D-60.0*D3) *T7*F1

(D2-D4)*17.5*T45*F1

(D2-D4)*49.50*T65*F1

(18.0*D3-12.0*D5)* T4*F1

(126.0*D3-84.0*D5)* T8*F1

(150.0*D5-60.*D7) * T7*F1

(382.5*D6-127.5*D8) * T95

(84.0*D7-24.0*D9) * T5*F1

(286.0*D8-71.5*D10) * T75

(247.5*D10-49.5*D12) * T6

( 924. 0*D2- 1848. 0*D6)

(330.0*D3-440.0*D7)

(918.0*D3-1224.0*D7)

(D4-D8)*440.0*T12*F2

T2

T12

Tl

*F1

*F1

5*F1

3*F2

*F2

9*F2

298
B(29) = RTT * (D4-D8)* 2024 . 0*T24*F2

B(30) = RTT * (1360.0*D5-1088.0*D9) * T18*F2

B(31) = RTT * (1530.0*D5-1224.0*D9) * T19*F2

B(32) = RTT * (2530. 0*D5- 2024. 0*D9) * T24*F2

IF (IDD.GT.O) GO TO 801

B(33) = PP

RETURN

801 PP = 0.0

DO 802 I = 1,32

PP = PP + G(I) * B(I)

802 CONTINUE

PP=PP

RETURN

END

C

FUNCTION ENTROPY (DENS, TEMP)

C********FUNCTION TO CALCULATE ENTROPY FROM DENSITY AND TEMPERATURE

C

CALL SR (EN, DENS, TEMP ,1)

CALL IDEAL1 (TEMP , DENS , EID , HID , HEL , SID , CVID , CPID , 1

)

ENTROPY=100 . *EN+SID

RETURN

END

C

SUBROUTINE IDEAL1 (T , D , EID , HID , HEL , SID , CVID , CPID , IATM)

CC***********HAS EXPLICIT DENSITY DEPENDENCE; GOOD FOR ALL PROPERTIES

CC*******AT ANY PRESSURE (OR DENSITY RELATED TO P VIA IDEAL GAS EOS)*****

CC******THIS IS FOR ETHANE AT ANY DENSITY AND TEMPERATURE

CC

COMMON /REFDAT/ Rl , PC , DC, TC , ZC , G(32) , PTRP , DTRP , TTRP

* , CMW

DIMENSION QS(7)

DATA QS/- .285949905507E+02,

A .381594759913E+01,

B .860212992578E+01,

C - .330757346034E+01,

D -.559566778576E+00,

E .507222665072E+01,

F -.550748741700E+01/

DATA Q0/-23. 446765/

CC

CALL IDEAL2(T, EID, HID, HEL, SID, CVID, CPID)

IF ( IATM. NE.O) THEN

R = Rl*100.

TAU=TC/T

DEL=D/DC

ADD=R*(Q0-QS(1) + LOG(DEL/TAU)

)

HEL=HEL+T*ADD

SID=SID-ADD

END IF

RETURN

END

CC

SUBROUTINE IDEAL2 (T , EID , HID , HEL, SID , CVID , CPID)

CC**************NEW IDEAL SUBROUTINE FOR 1986 VALUE OF GAS CONSTANT********--

CC******FORM OF HELMHOLTZ FREE ENERGY FOLLOWS GOODWIN WITH WAGNER VARIABLES'-

CC**********GOOD ONLY AT 1 ATM; PROBLEM FOR HEL AND SID- -SEE I DEAL1********

CC

COMMON /REFDAT/ Rl , PC , DC, TC , ZC , G(32) , PTRP, DTRP, TTRP

* , CMW

DIMENSION QS(7)

C********COEFFICIENTS FOR ETHANE (C2 )***************

DATA QS/- .285949905507E+02,

A .381594759913E+01,

B .860212992578E+01,

C -.330757346034E+01,

-299-
D - .559566778576E+00,

E .507222665072E+01,

F -.550748741700E+01/

DATA P1.P2/- .33333333, - .66666667/

R = Rl*100.

TAU=TC/T

TAU3=TAU**P1

TAU23=TAU**P2

EXTAU=EXP(QS(7)*TAU ) PHID-QS(l)+(QS(2)+l.)*LOG(TAU)+QS(3)*TAU3+QS(4)*TAU23

1 +QS ( 5 ) /TAU+QS ( 6

) *LOG ( 1

. - EXTAU

)

PHIDD1=QS ( 2

) -QS ( 3 ) /3 . *TAU3 - 2 . *QS (4) /3 . *TAU23 -QS ( 5 ) /TAU

1 -QS ( 6

) *QS ( 7) *TAU/ ( 1 . /EXTAU - 1 .

)

PHIDD2=-QS ( 2 )+4 . *QS ( 3) /9 . *TAU3+10 . *QS (4) /9 . *TAU23

1 +2 . *QS ( 5 ) /TAU - QS ( 6

) *QS ( 7

) **2*TAU**2*EXTAU/ ( EXTAU - 1 . ) **2

HEL=R*T*PHID

CPID=R*(1. -PHIDD2)

EID=R*T*PHIDD1

HID=R*T+EID

CVID=-R*PHIDD2

SID=-R*(PHID-PHIDD1)

RETURN

END

C

FUNCTION HELM (DENS, TEMP)

C*********THIS FUNCTION IS FOR HELMHOLTZ FREE ENERGY

C

CALL AR(HE, DENS, TEMP, 1)

HE=100.*HE

CALL IDEAL1 (TEMP , DENS , EID , HID , HEL, SID , CVID , CPID , 1)

HELM=HE+HEL

RETURN

END

C

FUNCTION GIBBS (DENS, TEMP, PRES)

C**********THIS FUNCTION IS FOR GIBBS ENERGY

C

HEL=HELM(DENS , TEMP)

GIBBS=HEL+PRES*1 . E05/(DENS*1000 .

)

RETURN

END

C

FUNCTION UNTERN( DENS, TEMP)

C*********THIS FUNCTION IS FOR INTERNAL ENERGY

C

HEL=HELM ( DENS , TEMP)

SS=ENTROPY(DENS , TEMP)

UNTERN=HEL+SS*TEMP

RETURN

END

C

FUNCTION ENTHALP( DENS, TEMP, PRES)

C*********THIS FUNCTION IS FOR ENTHALPY

C

HEL=HELM ( DENS , TEMP

)

UNT=UNTERN ( DENS , TEMP)

GIB=GIBBS (DENS , TEMP , PRES

)

ENTHALP=G I B+UNT - HEL

RETURN

END

300-
FUNCTION CPEE(RHO,TEE)

C*********THIS FUNCTION IS FOR ISOBARIC HEAT CAPACITY

C D = RHO

CVCAL = CVF(D,TEE)

CALL DPDT(P1,D,TEE,1)

CALL DPDD(P2,D,TEE,1)

CPCAL = CVCAL + 100.0 * TEE * PI * PI / (D * D * P2)

CPEE=CPCAL

RETURN

END

C

FUNCTION OM22S(TS)

C**********THIS FUNCTION IS FOR THE 11-6-8 GAMMMA EQUALS 3 C**********OMEGA 22 COLLISION INTEGRAL

C

DIMENSION C0(9)

C

DATA C0/-3.0328138281E+00, 1 . 6918880086E+01 , - 3 . 7189364917E+01

,

* 4.1288861858E+01,-2.4615921140E+01, 8 . 9488430959E+00

,

* -1.8739245042E+00, 2 . 0966101390E-01 , -9 . 6570437074E-03/

TI = 1.0 / TS

T1=TS.**( 1.0/3.0)

ETA =0.0

DO 020 J-1,9

ETA =ETA +C0(J)*TI

020 TI-TI*T1

OM22S = 1.0 / ETA

RETURN

END

C

FUNCTION VSCTY(D,T)

C PURPOSE - - THIS ROUTINE CALCULATES THE VISCOSITY OF ETHANE

C

C VERSION 4.0 5/17/85 - - CODED BY J . F. ELY

C WITH SUBSEQUENT REVISIONS

C

COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32), PTRP , DTRP , TTRP

* , CMW

C

DIMENSION GV(ll) , F(ll)

C

C COEF FROM C2ETAWT TRANSFERRED 11/88 --CHANGED 12/88

C UNITS ARE IN MICRO PA SEC MUST BE *10

.

C

C*******THESE ARE TRUNCATED COEFFICIENTS AS IN PAPER************

DATA GV.ETAS

1/0.47177003,-0.23950311,0.39808301,-0.27343335,0.35192260,

2-0.21101308, -0.004785797,0.073781299, -0.030425255,

3 -0.30435286 , 0.001215675,15.977/

C

020 DELTA = D / DC

TAU = TC / T

F(l) = DELTA

F(2) = TAU*DELTA

C

C

F(3) = DELTA**2

F(4) = TAU*DELTA**2

F(5) = DELTA**2 * TAU * SQRT(TAU)

C

F(6) = DELTA**

3

F(7) = DELTA** 3 * TAU**

2

C

- 301-
F(8) = DELTA**4

F(9) = DELTA**4 * TAU

C

F(10)= DELTA

F(ll)= DELTA * TAU

C

ETA = 0.

DO 040 J =1, 9 040 ETA = ETA + F(J)*GV(J)

DENOM = 1.0 + F(10)*GV(10) + F(11)*GV(11)

ETAG = ETAO(T)

060 ETA = ETAG + ETAS * ETA / DENOM

VSCTY = ETA

RETURN

END

FUNCTION ETAO(T)

C******THIS FUNCTION EVALUATES THE ZERO DENSITY VISCOSITY

C******OF ETHANE (C2)

C

COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32), PTRP , DTRP , TTRP

* , CMW

DATA EOK/245 . 0/

TS = T / EOK

ETAO = 12.0085*SQRT(TS)/OM22S(TS)

RETURN

END

C

FUNCTION TCONDO(T)

C**********THIS FUNCTION EVALUATES THE ZERO DENSITY

C**********THERMAL CONDUCTIVITY OF ETHANE

C**********COEFFICIENTS FOR ETHANE FROM 12/88

C

COMMON /REFDAT/ RT , PC, DC, TC , ZC , A9(32), PTRP, DTRP, TTRP

* , CMW

DATA CON, EOK/0. 276505, 245.0/

C NEW COEFFICIENTS FROM FIT OF 12/20/88

DATA G1.G2/1. 710414723, -0.6936482165/

CALL IDEAL2(T,X1,X2,X3,X4,CV,X5)

CVDIM— CV/(100.*RT)

TS=T/EOK

TCC=- (G1+G2/(TS) )*(CVDIM+1 .5)

ETAO=ETA0(T)

TCOND0=CON*ETAO* (3.7 5+TCC

RETURN

END

C

FUNCTION XLAMF(D.T)

C

C*******THIS FUNCTION IS FOR THE THERMAL CONDUCTIVITY OF ETHANE

C********COEFFICIENTS ADDED 1/89 FROM HEP'S RUN OF 1/10/89

C

COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32), PTRP, DTRP, TTRP

* , CMW

C

c DIMENSION G(7) ,F(7)

C*****NEW COEFFICIENTS FROM 1/24/89 FIT

C

DATA G,ES /.960843217927E+00, . 275002352857E+01

1 -.266092886126E-01, - . 781467287125E-01 , . 218813393267E+00

2 .238495630673E+01, - . 751139710430E+00 ,4.41786/

C

C

020 DELTA = D / DC

TAU = TC / T

TCO = TCONDO(T)

-302-
TCCRIT = CRLAM(D,T)

C F(l) =DELTA

F(2) = DELTA**

2

F(3) = DELTA**

3

F(4) = DELTA**4

F(5) = DELTA**

5

F(6) = DELTA*TAU**1.5

F(7)= DELTA**3*TAU

C TCX = 0.

DO 040 J = 1, 7 040 TCX = TCX + F(J)*G(J)

060 TCX = TCO + ES * TCX + TCCRIT

XLAMF=TCX

RETURN

END

C FUNCTION CRLAM(D,T)

C DGF CODING OF OLCHOWY-SENGERS SIMPLE THEORY- -5/88

C CONSTANTS FOR ETHANE FLUID

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32) , PTRP , DTRP , TTRP

* , CMW

C THIS FUNCTION DOES CALL THE DAMPING FCT , DAMP AND

C THE XICALC FUNCTION TO EVALUATE XI.

DATA CON1 ,QDI/1 . 55E-09 , . 545E-09/

DEL=D/DC

TAU=TC/T

THI=2 . *TC

QD=1./QDI

VISBK=VSCTY(D,T)

CV = CVF(D,T)

CALL DPDT(P1,D,T,1)

CALL DPDD(P2,D,T,1)

CALL DPDD(P3,D,THI,1)

CP = CV + 100.0 * T * PI * PI / (D * D * P2)

XI=XICALC(T,D,P2,P3)

QDPSI=QD*XI

CRLAM=C0N1*DEL*CP/(TAU*VISBK*XI)

CRLAM=CRLAM*DAMP (DEL , QDPSI , CP , CV)

RETURN

END

C FUNCTION DAMP(DEL,QDPSI,CP,CV)

DATA PI/3.141592654/

FAC1=EXP ( -QDPS 1/ ( 1 . +QDPS 1**3/ ( 3 . *DEL**2 ) )

)

FAC2=(CP-CV)/CP*(ATAN(QDPSI)+CV*QDPSI/(CP-CV))

DAMP=2 . /PI* ( FAC1 - 1 . +FAC2

)

RETURN

END

C

FUNCTION XICALC (T,D,DPDD,HITDPDD)

C THIS FUNCTION CALCULATES CORRELATION LENGTH

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32) , PTRP, DTRP, TTRP

* , CMW

DATA CON2 , POWNG/4 . 28243E- 10 , . 50745E0/

DEL=D/DC

TAU=TC/T

THI=2.*TC

DIMINV=R*T/DPDD

DIMHINV=R*THI/HITDPDD

DELDER=DIMINV-DIMHINV

IF(DELDER. LT . 1 . E- 8) DELDER=1 . E8

XICALC=CON2*(DEL*TAU*DELDER)**POWNG

RETURN

END

-303-
c

c FUNCTION TSAT( PRESS)

C********THIS FUNCTION CALCULATES THE SATURATION TEMPERATURE

C********GIVEN A PRESSURE BELOW ITS CRITICAL VALUE

C

COMMON /DERIV/DF,DJUNK

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32), PTRP , DTRP , TTRP

* , CMW

IF(PRESS.GT.PC)THEN

PAUSE 'PRESSURE GREATER THAN CRITICAL IN TSAT'

RETURN

END IF

IF(PRESS . LT . PTRP)THEN

PAUSE 'PRESSURE LESS THAN TRIPLE POINT IN TSAT'

RETURN

END IF

XL=TTRP

XH=TC

TSAT=.5*(XL+XH)

DXOLD=ABS(XH-XL)

DX=DXOLD

F=PSATF(TSAT) -PRESS

DO 11 J-1,100

IF( ( (TSAT-XH)*DF-F)*( (TSAT-XL)*DF-F) . GE. . C .OR. ABS(2.*F).GT.ABS(DXOLD*DF))THEN

DXOLD=DX

DX=0.5*(XH-XL)

TSAT=XL+DX

IF(XL.EQ. TSAT) RETURN

ELSE

DXOLD=DX

DX=F/DF

TEMP=TSAT

TSAT=TSAT-DX

IF(TEMP . EQ . TSAT)RETURN

ENDIF

IF(ABS(DX) .LT. . 00005)RETURN

F=PSATF(TSAT) -PRESS

IF(F.LT.O.)THEN

XL=TSAT

ELSE

XH=TSAT

ENDIF

11 CONTINUE

PAUSE 'IN TSAT: EXCEEDES MAXIMUM ITERATIONS'

RETURN

END

304
BLOCK DATA C2INIT

C*******THIS BLOCK DATA SUBROUTINE SUPPLIES THE FUNDAMENTAL CONSTANTS

C*******AND PARAMETERS NECESSARY FOR THE ETHANE FLUID IN

C*******ACCORDANCE WITH THE CORRELATIONS OF

C*******FRIEND , ELY, AND INGHAM, ' THERMOPHYSICAL PROPERTIES OF ETHANE'

COMMON /REFDAT/ R, PC, DC, TC , ZC , G(32), PTRP , DTRP , TTRP

* , CMW

C

COMMON/SATBDY/TCC , PCC , DCC , ZCC , RC , EPP , BETA

C

DATA TC, PC, DC, PTRP, DTRP, TTRP, CMW

C/305.330, 48.7180, 06.870, 1.130E-05, 21.667, 90.352, 30.070/

DATA TCC, PCC, DCC

C/305.330, 48.7180, 06.870/

C********TRIPLE PT PRESSURE CHANGE TO 1.13 RATHER THAN 1 . 1308- -11/88

C COEFFICIENTS FROM FIT OF 9/26/88

DATA G/.462154305597E+00, - . 192369363873E+01 , . 398786040031E+00

,

1 .160545323723E-01, . 128952422187E+00 , . 354583204912E-01

,

2 .349278445395E-01, - . 113061833802E-01 , - . 398090327788E-01

,

3 .830319368340E-03, .459215751833E-03 , . 175302879173E-06

,

4 -.709195161256E-04, - . 234361622492E+00 , . 845746976449E-01

,

5 .148610520102E+00, - . 100168578674E+00 , - . 592648243875E-01

,

6 -.412635142172E-01, . 218551618688E-01 , - . 745527209579E-04

,

7 -.988590855721E-02, . 102084164987E-02 , - . 521896558472E-03

,

8 .985921620300E-04, . 468651408558E-01 , - . 195580116459E-01

,

9 - .465571616512E-01, . 328779053755E-02 , . 135720901854E+00

,

A - .108464714554E+00, - . 675028369034E-02/

DATA R, EPP, BETA, ZC/0 . 08314510, 1.9, 0.355,0.27934000/

DATA RC , ZCC/0 . 08314510 , . 27934000/

END

FUNCTION PSATF(T)

PURPOSE --- THIS ROUTINE CALCULATES THE SATURATION PRESSURE AND

ITS DERIVATIVE WITH RESPECT TO T, GIVEN T.

CODED BY- -J. F. ELY

CHEMICAL ENGINEERING SCIENCE DIVISION 773.20

NATIONAL BUREAU OF STANDARDS

BOULDER, COLORADO 80303

VERSION 1.0 -- 6/3/83

k-k-k'k-k^-k-k-k-k k ~k "k -k ~k ~k -k REVISED 2/27/85 TO REJECT CALLS IF T .GT. TC

:~kXX~k~k~k~k1<izi?i(~kX~ki<ic~k~k~k~kic~k~k~kX~k~k~k~k~k~k~k-k-k~k-k-k-k-k'k-k-k'k-k-k->

NEW COEFFICIENTS FROM HEP'S FIT OF ETHANE DATA FROM JIM ELY

9/10/86

CHANGED 2/06/86 TO RETURN TO EPP=1 .

CHANGED 6/03/86 TO EPP=1 . 9 AND USES TSTAR AS VARIABLE

AND IS FORCED TO PC AT T = TC

.- "k ~k "Sc ~k -k ~k ~k -k ~k -k -k -k ~k -k ~k -k i? ~k -k-k~k~k -k -k ~k ~k -k -k -k ~k ~k ~k -k k-k -k -k -k -k ~k ~k ~k -k -k k-k -k -k -A- -k -k -k -k -k -k ~k ~k ~k ~k ~k -k ~k -k -J COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32), PTRP, DTRP, TTRP

'

, CMW

DIMENSION G(5)

COMMON /DERIV/ DPSDT, DDSDT

EPP =1.9

-305-
C THE FOLLOWING FOR PC = 48.718 AND TC = 305.33 3-4-88

G( 1)= -.795531542571E+01

G( 2)= .147806828674E+02

G( 3)= .153282697603E+01

G( 4)= -.134317917619E+02

G( 5)= .470489080510E+01

X = 1. - T / TC

IF(X) 1,2,2

1 PRINT 4

4 FORMAT(10X, 'T ABOVE TCRT IN PSATF(T) .

' / ) STOP

2 PCAL = G ( 1

) *X/ ( 1

. -X) +G ( 2

) *X**EPP+G ( 3) *X+G ( 4

) *X*X+G ( 5) *X*X*X

PSATF= PC*EXP(PCAL)

DPSDT=-PSATF/TC*(G(1)/(1. -X)**2+EPP*G(2)*X**(EPP-1 . 0)+G(3)

* + 2.*G(4)*X+3.*G(5)*X**2)

RETURN

END

FUNCTION DSATL(T)

C

C THIS ROUTINE CALCULATES THE SATURATED LIQUID

C DENSITY OF ETHANE USING NEW CORRELATION

C

C REVISED 2/27/85 TO REJECT CALLS IF T . GT . TC

C

c

C NEW COEFFICIENTS FROM HEP'S FIT OF WAGNER AND ARMSTRONG DATA

C 1/31/86

C REVISED COEFFICIENTS FROM 3/13/88

COMMON /REFDAT/ R, PC, DC, TC , ZC , A (32), PTRP , DTRP , TTRP

* , CMW

COMMON /DERIV/ DPSDT, DDSDT

DIMENSION G(5)

BETA - .355

: TC = 305.33 AND DC = 6.870

G( 1)= .193074035545E+01

G( 2)= -.653985599985E+00

G( 3)= .814136166546E+00

G( 4)= -.383814110665E+00

G( 5)= - .339743046787E+00

X = 1.0 - T / TC

IF (X) 1,2,3

1 PRINT 4

4 FORMAT ( 10X, ' DSATL = 0, T EXCEEDS TCRT. ' / ) STOP

2 DSATL = DC

DDSDT = -1.0E+10

RETURN

3 DENOM = 1.0 + G(5) * X**(l . 0-BETA)

X4 = X*X*X*X

Y = (G(l) * X**BETA + G(2) * X*X + G(3) * X*X*X+G(4)*X4) / DENOM

DYDX = BETA*G(1)*X**( BETA- 1.0) + 2.0*G(2)*X + 3.0*G(3)*X*X

* + 4.0*G(4)*X*X*X

DYDX = (DYDX - Y * G(5) * (1.0 -BETA) / X**BETA) / DENOM

DSATL = DC * (Y + 1.0)

DDSDT = - DC * DYDX / TC

RETURN

END

306
FUNCTION DSATV(T)

Q -k ieieititic-kiiitic&ieitieie'k'kititieie-'kic-itie'kicieic i< ~k -k -k -k -k C

C PURPOSE --- THIS ROUTINE CALCULATES THE SATURATED VAPOR DENSITY,

C AND ITS DERIVATIVE WITH RESPECT TO T, GIVEN T. IT

C REQUIRES THE USE OF "PSATF" WHICH CALCULATES THE

C SATURATIION PRESSURE AND ITS DERIVATIVE WRT T.

C

C CODED BY--B. C. COOKE

C CHEMICAL ENGINEERING SCIENCE DIVISION 773.20

C NATIONAL BUREAU OF STANDARDS

C BOULDER, COLORADO 80303

C

C VERSION 1.0 -- 6/3/83

Q ~k ~k -k ~k -k -k -k -k ~k -k ~k -k -k ~k ~k ~k ~k ~k -k -k -k -k ~k ~k ~k -k -k -k ~k ~k ~k -k ~k -k -k c

C REVISED 2/27/85 TO REJECT CALLS IF T . GT . TC

C

C

C NEW COEFFICIENTS FROM HEP'S FIT OF ETHANE DATA FROM ELY

C 9/10/86

C

C REVISED 6/03/86. USES BETA =0.355 AND SCALING AMPLITUDE

C IS SAME IN VAPOR AND LIQUID TO LOWEST ORDER

COMMON /DERIV/ DPSDT, DDSDT

COMMON /REFDAT/ R, PC, DC, TC , ZC , A(32), PTRP , DTRP , TTRP

* , CMW

DIMENSION G(4)

C THE FOLLOWING ARE FROM VAPOR AND LIQUID FIT OF 3-13-88

BETA = .355

C*******CALCULATE GO FROM UNROUNDED G(l) AND ZC , (THEN ROUND)

GO = -0.7483719

C THESE COEFS FROM A FIT ON 9-21-88. ID 12 DATA OMITTED

G( 1)= -.137289517553E+01

G( 2)= - .119259688503E+01

G( 3)= .186150455934E+01

G( 4)= .131364937601E+01

C ZC = PC / (R * TC * DC)

X = T / TC

TAU = 1.0 - X

IF (TAU) 1,2,3

1 PRINT 4

4 FORMAT ( 10X, 'T EXCEEDS TC IN DSATV. ' / ) STOP

2 DSATV=DC

DDSDT=1 . OE+100

RETURN

3 F = GO*TAU**BETA + G(1)*TAU**(2 . *BETA)

F = F + G(2)*(TAU + TAU**4) + G(3)*TAU**2

Y = 1.0 + G(4)*TAU

PS = PSATF(T)

PRX = (ZC-1.0) * PS / (PC*X**8)

FOY = F / Y

Z = 1.0 + PRX * (i.o + FOY)

RTZ = 1.0 / (R * T * Z)

DSATV = PS * RTZ

DFDX= - BETA*GO*TAU** (BETA- 1 . 0) - G ( 1

) *2 . *BETA*TAU** ( 2 . *BETA- 1 .

)

DFDX=DFDX - G ( 2

) * ( 1 . +4 . *TAU**3 ) - 2 . *G ( 3

) *TAU

DYDX = -G(4)

DPDX = (ZC-1.0)*DPSDT*TC/(PC*X**8)- 8 . 0*PRX/X

DZDX = DPDX*(1.0+FOY) + PRX*(DFDX/Y - FOY*DYDX/Y)

DDSDT = DPSDT^RTZ - DSATV/T - DZDX*DSATV/(Z*TC)

RETURN

END

-307-
SUBROUTINE IDEAL(T , CVID , SID)

C********IDEAL GAS PROPERTIES FOR ETHANE AT 0.101325 MPA (1 ATM)

C**************NEW IDEAL SUBROUTINE FOR 1986 VALUE OF GAS CONSTANT**'

C******NEW R FORCES SLIGHT DEVIATIONS IN OTHER PROPERTIES, SINCE NOT*

C*******ALL EQS ARE DIRECTLY PROPORTIONAL TO R************.**********-J

C**************DATE OF CHANGE 4/14/87********************************

C******************EVALUATED AT 1 ATM (PROBLEM FOR ARGUMENT SID ONLY*

C***********HEP'S COEFFICIENTS FOR ETHANE ARE IN HERE 8/88***********

COMMON /REFDAT/ Rl , PC , DC, TC , ZC , G(32), PTRP , DTRP , TTRP

* , CMW

DIMENSION QS(7)

DATA QS/- .285949905507E+02,

A .381594759913E+01,

B .860212992578E+01,

C -.330757346034E+01,

D - .559566778576E+00,

E .507222665072E+01,

F -.550748741700E+01/

CC

DATA PI, P2/- .33333333, - .66666667/

R = Rl*100.

TAU=TC/T

TAU3=TAU**P1

TAU23=TAU**P2

EXTAU=EXP ( QS ( 7

) *TAU ) PHID=QS(l)+(QS(2)+l.)*LOG(TAU)+QS(3)*TAU3+QS(4)*TAU23

+QS ( 5 ) /TAU+QS ( 6

) *LOG ( 1

. - EXTAU)

PHIDD1=QS ( 2

) -QS ( 3 ) /3 . *TAU3 - 2 . *QS (4) /3 . *TAU2 3 - QS ( 5 ) /TAU

-QS ( 6

) *QS ( 7

) *TAU/ ( 1 . /EXTAU - 1 .

PHIDD2= -QS ( 2 ) +4 . *QS ( 3 ) /9 . *TAU3+10 . *QS (4 ) /9 . *TAU2 3 +2 . *QS ( 5 ) /TAU - QS ( 6

) *QS ( 7

) **2*TAU**2*EXTAU/ ( EXTAU - 1 . ) **2

CVID=-R*PHIDD2

SID=-R*(PHID-PHIDD1)

RETURN

END

-308-

--U.S. GOVERNMENT PRINTING OFFICE: 1993-774-025/69047
NISTTechnical Publications

Periodical

Journal of Research of the National Institute of Standards and Technology—Reports NIST research and

development in those disciplines of the physical and engineering sciences in which the Institute is active. These include physics, chemistry, engineering, mathematics, and computer sciences. Papers cover a broad

range of subjects, with major emphasis on measurement methodology and the basic technology underlying

standardization. Also included from time to time are survey articles on topics closely related to the

Institute's technical and scientific programs. Issued six times a year.

Nonperiodicals

Monographs—Major contributions to the technical literature on various subjects related to the Institute's scientific and technical activities. Handbooks—Recommended codes of engineering and industrial practice (including safety codes) developed

in cooperation with interested industries, professional organizations, and regulatory bodies.

Special Publications—Include proceedings of conferences sponsored by NIST, NIST annual reports, and

other special publications appropriate to this grouping such as wall charts, pocket cards, and bibliographies.

Applied Mathematics Series—Mathematical tables, manuals, and studies of special interest to physicists,

engineers, chemists, biologists, mathematicians, computer programmers, and others engaged in scientific and

technical work.

National Standard Reference Data Series—Provides quantitative data on the physical and chemical

properties of materials, compiled from the world's literature and critically evaluated. Developed under a worldwide program coordinated by NIST under the authority of the National Standard Data Act (Public Law

90-396). NOTE: The Journal of Physical and Chemical Reference Data (JPCRD) is published quarterly for NIST by the American Chemical Society (ACS) and the American Institute of Physics (AIP). Subscriptions,

reprints, and supplements are available from ACS, 1155 Sixteenth St., NW, Washington, DC 20056.

Building Science Series—Disseminates technical information developed at the Institute on building materials,

components, systems, and whole structures. The series presents research results, test methods, and

performance criteria related to the structural and environmental functions and the durability and safety characteristics of building elements and systems.

Technical Notes—Studies or reports which are complete in themselves but restrictive in their treatment of

a subject. Analogous to monographs but not so comprehensive in scope or definitive in treatment of the subject area. Often serve as a vehicle for final reports of work performed at NIST under the sponsorship

of other government agencies.

Voluntary Product Standards—Developed under procedures published by the Department of Commerce in Part 10, Title 15, of the Code of Federal Regulations. The standards establish nationally recognized

requirements for products, and provide all concerned interests with a basis for common understanding of the characteristics of the products. NIST administers this program as a supplement to the activities of the private sector standardizing organizations.

Consumer Information Series—Practical information, based on NIST research and experience, covering

areas of interest to the consumer. Easily understandable language and illustrations provide useful background

knowledge for shopping in today's technological marketplace.

Order the above NIST publications from: Superintendent of Documents, Government Printing Office,

Washington, DC 20402.

Order the following NISTpublications—F1PS and NISTlRs—from the National Technical Information Service,

Springfield, VA 22161.

Federal Information Processing Standards Publications (FTPS PUB)—Publications in this series collectively constitute the Federal Information Processing Standards Register. The Register serves as the

official source of information in the Federal Government regarding standards issued by NIST pursuant to the Federal Property and Administrative Services Act of 1949 as amended, Public Law 89-306 (79 Stat. 1127),

and as implemented by Executive Order 11717 (38 FR 12315, dated May 11, 1973) and Part 6 of Title 15 CFR (Code of Federal Regulations).

NIST Interagency Reports (NISTTR)—A special series of interim or final reports on work performed by

NIST for outside sponsors (both government and non-government). In general, initial distribution is handled

by the sponsor; public distribution is by the National Technical Information Service, Springfield, VA 22161,

in paper copy or microfiche form.