Reference

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PySUca^oRs

NAT L INST. OF STAND & TECH R.LC.

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IMBSIR 79-1612

ISOBUTANE: PROVISIONAL THERMODYNAMIC FUNCTIONS

FROM 114 TO 700 K AT PRESSURES TO 700 BAR

Robert D. Goodwin

Thermophysical Properties Division

National Engineering Laboratory

National Bureau of Standards

Boulder, Colorado 80303

Prepared for:

Gas Research Institute

10 West 35th Street

Chicago, Illinois 60616

QC100

.056

79-1612

July 1979

1 7 1979

NBSIR 79-1612

« \

’

ISOBUTANE: PROVISIONAL THERMODYNAMIC FUNCTIONS

FROM 114 TO 700 K AT PRESSURES TO 700 BAR

Robert D. Goodwin

Thermophysical Properties Division

National Engineering Laboratory

National Bureau of Standards

Boulder, Colorado 80303

July 1979

Prepared for:

Gas Research Institute

IOl West 35th Street

Chicago, Illinois 60616

U.S. DEPARTMENT OF COMMERCE, Juanita M. Kreps, Secretary

Sidney Harman, Under Secretary

Jordan J. Baruch, Assistant Secretary for Science and Technology

NATIONAL BUREAU OF STANDARDS, Ernest Ambler, Director

CONTENTS

Page

1. INTRODUCTION 1 2. PHYSICAL PROPERTIES . 1 2.1 Fixed-Point Values 2

2.2 Melting Line and Vapor Pressures 2

2.3 The Orthobaric Densities 4

2.4 The Virial Equation 5

2.5 The Equation of State 6

2.6 The Ideal Gas Functions 8

2.7 Thermal oop Computations 8

2.8 The Heats of Vaporization 9

2.9 Saturated Liquid Specific Heats 9

3. COMPUTATIONAL METHODS 10

3.1 The Homogeneous Domain 10

3.2 The Saturated Liquid 11 3.3 The Compressed Liquid 12

4. TESTS AND COMMENTS 12

5. TABLES OF PHYSICAL AND THERMODYNAMIC PROPERTIES 14

5.1 Calculated P-p-T Isochores and Isotherms 14

5.2 The Joule-Thomson Inversion Locus ' 14

5.3 Thermophysical Properties of the Saturated Liquid 14

5.4 Thermophysical Properties Along Selected Isobars 15

6. ACKNOWLEDGMENTS 15

7. REFERENCES 16

APPENDIX A. Symbols and Units 20

APPENDIX B. Fixed-Point Values for Isobutane 21

APPENDIX C. Computer Programs 163

iii
LIST OF FIGURES

Page

Figure 1. The densi ty-temperature diagram of isobutane 22

Figure 2. The P-T locus of P-p-T data for isobutane 23

Figure 3. Comparison of enthalpies at T = 250 F 24

Figure 4. Comparison of enthalpies for saturated liquid 25

Figure 5. Calculated enthalpy at P = 50 bar 26

LIST OF TABLES

Table 1. Vapor pressures of isobutane 27

Table 2. Densities of saturated liquid 29

Table 3. Densities of saturated vapor 33

Table 4, Second virial coefficients 35

Table 5. Coefficients of the equation of state 36

Table 6, Calculated P(p) critical isotherm . . . . 37

Table 7. Summary of P-p-T data 39

Table 8. Comparisons with P-p-T data 40

Table 9. Comparisons with data for ideal gas functions 49

Table 10. Interpolated ideal gas functions 50

Table 11. Specific heats for saturated liquid at T < T^ 51

Table 12. Estimated coexistence data at T < Tj^ 52

Table 13. The heats of vaporization 53

Table 14. Comparisons with data for Cp(p,T) 56

Table 15. Comparisons of functions at T = 250 F 58

Table 16 Comparisons of functions at T = 440 K 59

Table 17. Comparisons with Starling, et al . on isotherms 60

Table 18. Calculated P(T) isochores 66

Table 19. Calculated P(p) isotherms 82

Table 20. The Joule-Thomson inversion locus 101

Table 21. Thermophysical properties of saturated liquid 102

Table 22. Thermophysical properties along isobars 105

IV
ISOBUTANE: PROVISIONAL THERMODYNAMIC FUNCTIONS

FROM 114 to 700 K AT PRESSURES TO 700 BAR

Robert D. Goodwin

Thermophysical properties of isobutane are tabulated at integral temperatures along isobars over the entire range of fluid

states. Results for the compressed liquid, from the triple- to

the boiling-point, have been estimated by use of the highly con- strained, nonanalytic equation of state, because experimental

P-p-T data are lacking in this region.

Key words: Densities; enthalpies; entropies; equation of state;

internal energies; isobars; isobutane; isochores; isotherms;

Joule-Thomson inversion; latent heats of vaporization; melting

line; orthobaric densities; specific heats; speeds of sound;

vapor pressures.

V

1. INTRODUCTION

Isobutane not only is a component of liquefied natural gas (LNG), but also

may become an important heat-exchange fluid for geothermal cycles [37]. The

present report is fifth in a series on the pure component of LNG, namely methane,

ethane, propane, n-butane, and isobutane.

Earlier compendia on isobutane have been presented by Das, et al . [12], and

by Starling, et al . [37]. Functions for ideal gas states recently were computed

from spectroscopic data by Chen, et al . [6]. A survey of available data quite

recently has been prepared by Kestin, et al . [25], and thermodynamic properties

have been tabulated by Mil ora and Combs [28a]. Our objective in this report is

to provide additional background and provisional derived properties on isobutane.

At present, serious deficiencies exist in accurate experimental P-p-T data for

the single phase, and for the coexistence boundary: vapor-pressures;

orthobaric densities; and heats of vaporization.

Whereas no P-p-T compressibility data exist for compressed liquid isobutane

at temperatures roughly below 300 K, there are accurate data for the saturated

liquid densities. By use of these data in the present, highly constrained

equation of state, we have estimated thermophysical properties for the compressed

liquid at low temperatures. Also presented here are formulations of the vapor

pressures, the orthobaric densities, the virial equation, the equation of state,

the ideal gas thermofunctions, the heats of vaporization, specific heats for the

saturated liquid, thermophysical properties on the liquid-vapor coexistence

boundary from the triple- to the critical-point, and thermophysical properties at

integral temperatures along isobars from 0 .1 through 700 bar.

To validate present work, some comparisons are made with results of Sage and

Lacey [34], of Das, et al . [12], and of Starling, et al . [37].

2. PHYSICAL PROPERTIES

Symbols and units appear in Appendix A. The density-temperatures diagram of

isobutane is presented by fig. 1. The upper, left corner gives the freezing

liquid line.
2.1 Fixed-Point Values

These values are listed in Appendix B.

(a) The Triple Point . The temperature is adopted from Das, et al . [12].

The pressure is obtained from our vapor-pressure eq. (2). The liquid density is

assigned for consistency with data in eq. (3). The vapor density is obtained

from our saturated-vapor densities eq. (4).

(b) The Boiling Point . The temperature is from our vapor-pressure eq. (2)

at a pressure of 1 atm = 1.01325 bar. Liquid and vapor densities are from

eqs. (3) and (4).

(c) The Critical Point . The temperature of 408.0 K is adopted in present

work on the basis of fitting orthobaric densities, P-p-T data, and examining

behavior of the calculated critical isotherm. Beattie, et al . [2] derived the

experimental value 134.98 + 0.05°C (Int.). The present critical density of

3.86 mol/L is adopted on the same basis as Tq, above. Beattie, et al . found

3.80 + 2 percent mol/L. The critical pressure from our vapor-pressure eq. (2) i 36 .549 bar, as compared with 36.477 + 0.05 bar found by Beattie, et al .

(a) The Melting Line . Measurements were described by Reeves, Scott, and

Babb [32]. We are grateful for a private communication from Professor Stanley E Babb, Jr., October 2, 1978, giving these, lower-pressure data for isobutane.

2.2 Melting Line and Vapor Pressures

140 .6 160.3

164.7

P,bar

”1140

3047

3720

By graphical approximations (for T-^ = 113.55 K) , we have estimated the

constants Pq = 430 bar, and e = 6.08 for the Simon equation.

P = P, - P„ [(T/T^f - 1], (

1 )

These constants differ greatly from those for other substances, e.g..

2
P^, bar e

Methane 1909 1 .85

Ethane 2560 2.179

Propane 7180 1 .283

n-butane 3634 2.210

Isobutane 430 6.08

(b) The Vapor Pressures . Data used for adjusting eq. (2) appear in

table 1. Values at ID = 40 have been derived via thermal loops, as described in

[17], by use of the saturated liquid specific heat data of Aston [1] from the

triple- to the boiling-point; the heat of vaporization at the normal boiling

point [1]; the ideal gas thermofunctions formulated here in section 2.6; the

virial equation formulated here in section 2.4; and, for the minor contribution

of V*dP to AH on the saturated liquid path, we also used preliminary

vapor-pressure and saturated liquid densities equations. Equation (2) is similar

to previous forms [17,18,19].

The arguments for eq. (2) are

x(T) E T/T^, u(T) E (1 - 1/x),

£n(P) = a + b*u + c*x + d*x^ + e*x^ + f*x*(l - x)^ , (2)

where P is in bar, e = 1.95, and -

a = 13.8083 5297 d = 112.7583 3458

b = 9 .3726 9200 e

= - 52.4214 0768

c = -70.5466 3008 f = 47 .8112 2198

Exponent c was selected for a best "fit" of P-p-T data under the constraint that,

at the critical point, the slope of the critical isochore, from the equation of

state, be equal to the slope of the vapor-pressure equation, 3P/3T = dP^/dT.

The fit of present vapor-pressure data is totally insensitive to values

3
1.1 j< e <. 1.95, but the critical-point slope is dependent on the value of e. The

present slope at the critical point is dPo/dT = 0.6341 bar/K.

The last column of table 1 gives the experimental difference,

^n(P/P^)/£n(P^/P^) - (1 - T^/T)/(l - T^/T^) ,

which would be zero for the elementary vapor-pressure equation, £n(P) = a - b/T,

when a and b are eliminated by constraint to the end-points.

2.3 The Orthobaric Densities

(a) Saturated Liquid Densities . Data in table 2 have been selected for

consistency. The variables for eq. (3) are -

x(T) = (T^ - T)/(T^ - T^), y(p) = (p - P^)/(p^ - P^) ,

(3)

c 2 3

y

= X + (x - x)*[a + b«x + c*x ] ,

where e = 0.35, and

a = 0.7869 1345 c = 0.0576 9816

b

= -0.1427 5354

The experimental residual in the last column of table 2 is -

(y - x)/(x^ - x) .

A plot of this residual shows the form of polynomial needed for (3).

(b) Saturated Vapor Densities . The following new type of formulation for

saturated vapor densities has been developed for consistency with the equation of

state (6), below, to yield a compressibility factor approaching unity in the

limit of low densities, as described earlier [17a, 18]. Data in table 3 have been

selected for consistency. Values at ID = 40 are derived from our vapor-pressure

and virial equations. We formulate the compressibility-factor for saturated

vapor, by use of our vapor- pressure equation, such that Iq{J) approaches unity

as p

->• 0, (hence Tq(p) -*• 0). Subscripts are omitted because we refer always to

saturated vapor and to the vapor pressure. Let Aq = (Z^ - 1 ) where Zq is

4
value of the compressibility-factor at the critical point, and define the

arguments

n(T) = Po(T)/P^, x(T) E T/T^, u(T) = (1 - x) .

The saturated vapor densities, dg = P/(Z"R"T), then are given by

z = 1 + A^'n«x"^‘f(x) , (4)

0

f(x) s 1 + a*u + b*u + c*exp[n*(l - 1/u)] ,

where e = 0.35, n = 3.6, and

a = -0.7640 5184 c = 30.7506 6326

b = 0.6505 0118

The next-to-last column in table 3 gives the experimental values

F(Z) E (Z^^p - l).x2/[Ap-n] .

used to develop a functional form for f(x).

2.4 The Vi rial Equation

For the truncated virial equation,

Pv/RT = 1 + B*(x)«p + . . . (5a)

we use reduced variables, p = d/d^, x = T/T^, where, for (5b) only,

dc = 3.80 mol/L and T^ = 408.13 K,

B*(x) = + B^/x + B

3

/x^ , (5b)

5
B2

0.500 8472

-1 .100 3932

83 = -0.647 8123

The first part of table 4 gives data used for adjusting (5b). Excluded data

weighted zero appear at the end of table 4.

Figure 2 shows the P-T regions covered by P-p-T data of Beattie, et al

.

(1950) [3]; of Morris, et al . (1939), [29]; and of Sage and Lacey

(1938), [34]. The data of Sage and Lacey were omitted from least-squares fitting

because they are superseded by Morris.

The nonanalytic equation of state used here has only three least-squares

coefficients for each isochore, as described in detail elsewhere [18]. Because

it is constrained to the liquid-vapor coexistence boundary, we have extrapolated

the equation to cover the entire compressed liquid region down to the

triple-point temperature (114 K) : compare fig, 1.

For any density (isochore) the coexistence temperature, Tq(p), is obtained

by iteration from equations for the orthobaric densities. The vapor pressure,

Po[T0 (p)] thus is a function of density, and the equation of state has the

form

2.5 The Equation of State

P - P^(p) = pR*-[T - Tg(p)] + pVt^-F(p,T) , ( 6 )

F(p,T) i B(p)-t(p,T) + C(p)-y(p,T) . ( 6 a)

The temperature-dependent functions in ( 6 a) are

»(p,T) F [T/T^(p)] , ( 6 b)

'f(p,T) = t(P>T) -

'l^o(p) > ( 6 c)

where 'l'o(p) is obtained from 4»(p,T) merely by replacing T with T0 (p),

6
4j(p,T) = 6 *exp[e ‘(1-x)] + (1 -6) ‘[I-go + w5,n(o))] . (6d)

The parameter, 0 _< 6 _< 1 , in (6d) is for relative weighting of the analytic and

nonanalytic parts, and

o)(p,T) = [1 - e(p)/T] , (6e)

where e(p) is a locus of temperatures inside the coexistence envelope

e(p) E T^(p) .exp[-a.f(p)] , (6f)

f(p) E IP - lT/(p^ -1)^

and pt is reduced density at the liquid triple point

The density-dependent coefficients in (6a) are

B(p) = + B2*exp(3*p) (6g)

C(p) = C^‘(p - 1 )*exp[-yp^] . (6h)

Parameters and coefficients of (6) for isobutane are

a = l, 3=0.5, y = 0.3, 6 = 2/3, e = 3,

B] = -0 .0516 5511 088 C] = 0.4208 3144 154

B2 = 0.6231 5236 106

Table 5 gives behavior of coefficients B(p), C(p) as a function of density,

and Table 6 gives behavior along the critical isotherm. These tables show that

the equation is smooth and well-behaved. Table 7 summarizes data and deviations

of the three authors, and table 8 gives deviations for each of the 246 P-p-T data

used. Whereas the deviations in general are greater than for methane, ethane,

propane, or n-butane, we nevertheless have a smooth and consistent representation

by means of the present, highly-constrained equation of state, which, in

addition, yields a maximum in the specific heats, Cv(p,T), at the critical

point.

7
2.6 The Ideal Gas Functions

We have developed a formulation of the spectroscopic specific heats.

C°(T), of Chen, et al . [6], using x = T/lOO,

C°/R - 4 = exp(-e/x) • E A.-xl-’ . i=l

^

where.

e = 6.40 A4 = -3137.57293

Al = 43.59076 A5 = 7742.58382

A2 = - 40.54350 A6 = -7583.91994

A3 = 739.72837 A7 = 3251 .25208

Table 9 shows the "fit" of data used. In this table, the values for

and for S° are obtained by numerical integration, starting

at T = 300 K. Table 10 gives interpolated values at integral temperatures.

2.7 Thermal OOP Computations

At temperatures from the triple- to the boiling-point, we have derived data

for vapor pressures, saturated vapor densities, and for heats of vaporization by

thermal loop computations for AH and for AS of saturated vapor and saturated

liquid. Our procedure was given in [17], and more generally by Yarbrough and

Tsai [43]. We use our virial eq. (5a), our ideal gas functions eq. (7), the heat

of vaporization of Aston, et al . at the normal boiling point [1], and the

following formulation of Aston's specific heats of the saturated liquid from the

triple- to the boiling-point, as seen in table 11. Define x(T) = (T - Tq)/ 300,

when,

CqCT) = a + b*x^ + c*x^ + d*x^ (8)

in J/mol/K, where Tq = 95.00 K is a fitting parameter, and

a = 98.508 712 c

= -700.483 251

b = 298.653 283 d = 635.097 472

8
The irregular behavior of the data makes it difficult to develop a simple

representati on. Computed results are given in table 12. The column headed P,EQM is vapor

pressure via a preliminary equation; derived results are in column P,BAR.

Heading Q,EQN gives formulated heats of vaporization via eq. (9); column Q,VAP

gives derived results in kJ/mol

.

2.8 The Heats of Vaporization

Table 13 shows the "fit" of our selected data. Those at ID = 40 we derived

via thermal loops (section 2.7). Those at ID = 41 are from the Clapeyron

equation. The formulation of these data in kilojoules/mol uses argument

x(T) = (Tc - T)/(Tc - Tt).

Qvap/Qt

^ X + (x^ - x)«[a + b«x^ + c*x^], kJ/mol , (9)

where e = 0.45, and,

Qt = 28.208 b = -0.239 2491

a = 1 .172 6829 c = -0.026 5020

The uncertainty of at least one percent in Qygp at the higher temperatures

will affect compressed liquid thermofunctions at these temperatures, because we

use Qvap to compute across the "dome."

2.9 Saturated Liquid Specific Heats

Specific heats Cg(T), along the saturated liquid path, are needed as a base to compute specific heats, Cv(p,T) Cp(p,T), in compressed liquid

states

.

We have used the ideal gas function S°(T), the equation of state, and the

heats of vaporization to compute Sg{T) along the saturated liquid path at

integral temperatures from the triple- to the critical -point. These are represented in J/mol/K by use of x = T/T^,

S„(T)-S. = A, •(! - x)^ + A.-<ln(x) + E A.-(l-x)’'^

o c I z i=3

( 10 )

9
where e = 0 .45 , and

Sc = 278.4457 6 A3

= -45.8024 5863

Ai = - 35.9738 7860 A4

= 0.1943 2181

A2

= 87.7051 4205 A5 = 15.9816 4931

The rms deviation is 0.003 percent for 31 points.

The specific heats follow from the relation Cg(T) = T*dSg/dT, in

J/mol /K,

C (T) = -e*A *x/(l-x)^‘^ + A.

o 1 c

5 i-3

X* Z) (i-2)*A.*(l-x) ( 11 ) i=3

3. COMPUTATIONAL METHODS

The numerical values for E and H in this report are based on the assigned

value, E = 0 at the liquid triple-point, obtained by use of the arbitrary value.

Eg = 23838.616 J/mol. Specific heats of Aston, et al . [1] could be

integrated to give the solid at T = 0 as reference state.

The homogeneous domain of fig. 1 includes all regions which can be attained

along isotherms starting at zero density without crossing the vapor-liquid

"dome," and without passing very close to the critical point at T Tq.

We start our computations*wi th ideal gas thermodynamic functions at zero

density, and then integrate along isotherms by use of the equation of state in

the following relations.

3.1 The Homogeneous Domain

AE = y'CP - T‘(3P/3T)]‘dp/p^ ( 12 )

AC

V (13)

10
AS R'Jln[P°/(pRT) + /"[R - (3P/3T)/p]-dp/p . (14)

Equation (14) is for use with initial entropies in hypothetical ideal gas states

at P° = 1 atm. For all other initial states we use

AS =

- y'(3P/9T)-dp/p^ . (14a)

In each (p,T) state, reached by above integrations, we compute

H = E + P-v , (15)

C = Cy + T*(3P/3T)^/(3P/3p)/p^ , (16)

= Cp‘(aP/3p)/C^ . (17)

3,2 The Saturated Liquid

At temperatures from the triple point up to the critical point, we first

obtain thermofunctions for the saturated vapor via eqs. (12) through (15). We

then use eq. (9) for the heat of vaporization, Qvap> compute

AH = - Q, AS = AH/T , (18)

such that the free energy of vaporization, AF = AH - T*AS, is zero. Having

obtained H and S for the saturated liquid, we compute E = H - P*v.

The single-phase specific heat, Cv(p,T), at the saturated liquid boundary

is obtained via eq. (11) for Cq(T) and the thermodynamic relation,

C^(p,T) = C^(T) + T-(3P/3T)-(dp^/dT)/p^ . (19)

where Pjj, is density of the saturated liquid. Values for Cp(p,T) and W(p,T)

on this boundary follow from eqs. (16) and (17). For liquid at the boiling point

we have obtained

11
Tb

Eb

261.3587 K,

16 784.1 J/mol,

Hb = 16 794.0 J/mol,

$b = 200.999 J/mol /K.

Equation (19) approches the difference of two infinities as T In

present work, Cy(p,T)g from eq. (19) becomes irregular at temperatures

roughly above 370 K. We therefore use the following formulation for CyCp,!)^,

J/mol /K, at the saturated liquid boundary, at temperatures from 340 K to the

critical, wherein x = (T - To)/(Tc - Tq), Tq = 340 K,

(Cv)o = a + b-x + c*x^/(l - x)^ , (20)

where,

£ = 0.1 b = 13.480

a = 111 .870 c = 5.380

3.3 The Compressed Liquid

Starting with above values for E, S, and Cy on the saturated liquid

boundary, we use eqs. (12), (13), and (14a) to integrate along isotherms, and

then obtain H, Cp, and W via eqs. (15), (16), and (17).

4. TESTS AND COMMENTS

Experimental data for isobutane from different laboratories, for the

coexistence boundary and for the single-phase P(p,T) surface, are of much lower

precision than desired for thermal computations, tables 1, 2, 3, and 8. By use

of the present, highly-constrained equation of state (6), however, we have

developed a smooth and consistent P(p,T) surface, as shown by derivatives given

in tables 6, 19, and 20. The poor representation of some P-p-T data in table 8

must arise in part from an inaccurate coexistence boundary, because our equation

of state is constrained to this boundary.

A condition for a well-behaved critical isotherm, table 6, is that, at the

critical point, the slope of the critical isochore from the equation of state be

equal to the slope of the vapor-pressure equation, 9P/3T = dPg/dT. By trial in

present work it became necessary to dimish dP^/dT at the critical point by

raising the exponent in eq. (2) to e = 1.95, and then also to increase 9P/9T at

the c.p. by raising the assigned critical density from 3.80 mol/L (Beattie) to

12
3.86 mol/L. Following the above investigation, these two slopes at the c.p, were constrained to equality via the least-squares program [27],

To validate or orient present derived results relative to earlier work, we present some comparisons.

Table 14 compares specific heats, Cp(T), from Sage and Lacey [34] with our results along isobars. Differences mostly are less than 10 percent. Table 15

compares densities, and differerrces of enthalpy and of entropy of [34] from our results along the subcritical isotherm at T = 250 F, 394.26 K. Enthalpy

differences for the gas are quite large, as illustrated in fig. 3. Enthalpy

differences from [34] along the saturated liquid path are compared with our

results in fig. 4. Approaching the critical temperature, our differences become

larger by 2 percent or more. Table 16 compares densities, and differences of enthalpy and of entropy of

Das, et al. [12] from our results along the supercritical isotherm at T = 440 K.

Enthalpy differences are a few percent. Table 17 compares properties of the

P(p,T) surface, and of enthalpy differences from Starling, et al . [37] with our

results along six isotherms (200 K through 500 K), at given densities. Partial

derivatives from the equations of state, 3P/3p, 9P/3T, B^p/BT^, are given

under the table 17 headings DP/DD, DP/DT, D2P/DT2 respectively. As no P-p-T data

exist for compressed liquid states below about 300 K, comparisons on the 200 K

isotherm result from extrapolations of the MBWR equation of Starling, et al., and

of our present equation of state. Density differences may be obtained from

table 17 as, Ap = AP/(3P/3p). In many regions they are as large as 2 percent.

Enthalpy differences, H(p,T) - HO(T), differ by only a few percent which,

however, may be a large absolute quantity: at T = 300 K and p = 10.40 mol/L, the

disagreement is (17,726 J/mol)*(2.63 percent) = 466 J/mol

.

Figure 5 shows that our enthalpies extrapolate smoothly (along the isobar at

P = 50 bar) at temperatures down to the triple point. The "jog" near

Tc = 408 K is due to the large values of Cp(p,T) in the critical region.

In conclusion, more accurate experimental data are needed for all P-p-T

states, including vapor-pressures and orthobaric densities. Experimental

specific heats for the saturated liquid from the triple-point to the highest

practical temperature are needed (data of Aston, et al . to the boiling-point have

a low precision). Experimental heats of vaporization over the widest practical

temperature range are sorely needed, as well as specific-heat measurements in

13
single-phase domains. All of these deficiencies already have been recognized by

Das, et al. [12], and by Starling, et al . [37].

During preparation of the present manuscript on isobutane in relation to

LNG, new computational and experimental work for the U.S. Department of Energy

was in progress at the National Bureau of Standards in Gai thersburg, Maryland.

The scaling laws have been applied to the critical -region data of Beattie,

et al . [2,3] by J. M. H. Levelt Sengers [35]. She thus has derived new critical-point constants, concluding, however, that an appreciable impurity of

n-butane would have only a very small effect on the dew- and bubble-point vapor

pressures, and that these results might be altered by new data.

Experimental work at NBS, Gaithersburg, also is in progress on accurate

vapor-pressure and single-phase P-p-T measurements. It is planned that following

completion of these measurements a collaborative analysis and correlation effort,

involving the work presented here and that at NBS-Gai thersburg, will be

undertaken. The collaborative effort will produce an equation of state and

tables that will supersede the provisional work provided here.

5. TABLES OF PHYSICAL AND THERMODYNAMIC PROPERTIES

5.1

Calculated P-p-T Isochores and Isotherms

Tables 18 and 19 give a selection of isochores and isotherms computed by

equation of state (6). These are essential to examine behavior of the P(p,T)

surface. They are a useful supplement to the isobars of table 22 for

interpolating P-p-T values and their derivatives.

5.2

The Joule-Thomson Inversion Locus

Table 20 gives the P-p-T locus of the J.-T. inversion, (3T/3P)|-i = 0,

obtained from equation of state (6) under the condition T*(9P/3T) = p*(9P/9p).

This table has been computed to temperatures well above those of P-p-T data, to

show approach to a maximum in P-T coordinates.

5.3

Thermophysical Properties of the Saturated Liquid

Table 21 gives physical and thermodynamic properties of saturated liquid

isobutane computed by methods of section 3. Column headings are interpreted on the first page of this table.

14
5,4 Thermophyslcal Properties Along Selected Isobars

Table 22 gives physical and thermodynamic properties on isobars, computed by

methods of section 3. Explanations for this table are given on the first page.

This table is extrapolated below the minimum temperature (300 K), and above the

maximum pressure (x 400 bar) of most of the P-p-T data used for adjusting the

equation of state.

6. ACKNOWLEDGMENTS

The author is indebted to many staff members of this research group for

valuable suggestions, for references and documents. Robert D. McCarty

contributed the essential least-squares program, providing for constraints.

Finally, we express grateful appreciation for support of this work by the Gas

Research Institute.

15
7. REFERENCES

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entropy, heats of fusion and vaporization and the vapor pressure of

isobutane, J. Am. Chem. Soc. 2059 (Aug 1940).

[2] Beattie, J. A., Edwards, D. G., and Marple, S., Jr., The vapor pressure,

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[3] Beattie, J. A., Marple, S. Jr., and Edwards, D. G., The compressibility of,

and an equation of state for gaseous isobutane, J. Chem. Phys. 1^, No. 1,

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[4] Benoliel, R. W. , Some physical constants of seven four-carbon-atom

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[5] Carney, B. R., Density of liquefied petroleum gas hydrocarbons. Petroleum

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[6] Chen, S. S., Wilhoit, R. C., and Zwol inski, B. J., Ideal gas thermodynamic

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[7] Coffin, C. C., and Maass, 0., The preparation and physical properties of

a-, 3- and Y-butylene and normal and isobutane, J. Am. Chem. Soc. 1427

(May 1928).

[8] Connolly, J. F., Ideality of n-butane: isobutane solutions, J. Phys. Chem.

1082 (1962).

[9] Cragoe, C. S., Private NBS Letter Circular, Dec. 1943, quoted by G. H. Hanson.

[10] Dana, L. I., Jenkins, A. C., Burdick, J. N., and Timm, R. L., Thermodynamic

properties of butane, isobutane, and propane. Refrigeration Engineering 12,

No. 12, 387 (Jun 1926).

[11] Das, T. R., and Kuloor, N. R. , Thermodynamic properties of hydrocarbons:

Part II - Isobutane, Indian J. Technol . 40 (1967).

[12] Das, T. R., Reed, C. 0., Jr., and Eubank, P. T., PVT surface and

thermodynamic properties of isobutane, J. Chem. and Eng. Data j^. No. 3,

253 (1973).

[13] Dymond, J. H., and Smith, E. B., The Virial Coefficients of Gases , Oxford

Science Research Papers 2, Clarendon Press, Oxford (1969).

16
[14] Foehr, E. G., and Fenske, M. R., Magneto-optic rotation of hydrocarbons,

Ind. Eng. Chem. No. 9, 1956-66 (1949).

[15] Gilliland, E. R., and Scheeline, H. W. , High-pressure vapor-liquid

equilibrium, Ind. Eng. Chem. No. 1, 48 (Jan 1940).

[16] Gilmour, J. B., Zwicker, J. 0., et al.. Fluorocarbon solutions at low

temperatures, J. Phys. Chem. 71^, No. 10, 3259 (Sep 1967).

f^,.^7] Goodwin, R. D., Provisional Thermodynamic Functions of Propane, from 85 to

700 K at Pressures to 700 Bar, Nat. Bur. Stand. (U.S.), Interagency Report

NBSIR 77-860 (Jul 1977).

[17a] Goodwin, R. D., Modification of the nonanalytic equation of state for the

limit of low densities, J. Res. Nat. Bur. Stand. (U.S.), 83 No. 4, 325

(1978).

[18]

K9]

[ 20 ]

[ 21 ]

[ 22 ]

[23]

Goodwin, R. D., The nonanalytic equation of state for pure fluids applied

to propane. Symposium on Equations of State in Engineering and Research,

176th National Meeting of the American Chemical Society, Miami Beach, Fla.,

Sept. 10-15, 1978. To be published in Advances in Chemistry Series . Goodwin, R. D., Normal Butane: Provisional Thermodynamic Functions from

135 to 700 K at Pressures to 700 Bar, Nat. Bur. Stand. (U.S.), Interagency

Report (under review, Nov. 13, 1978).

Gunn, R. D., M.S. Thesis, Univ. Calif., Berkeley (1958), quoted by J. A.

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

Hanson, G. H., Thermodynamic properties of saturated propylene, propane,

isobutane, isobutylene and normal butane, Chem. Eng. Progr. (Am. Inst.

Chem. Engrs.) 959 (1946).

Haynes, W. M., and Hiza, M. J., Jr., Measurements of the orthobaric liquid

densities of methane, ethane, propane, isobutane, and normal butane, J.

Chem. Thermodynamics^, 179 (1977).

Jessen, F. W., and Lightfoot, J. H., Ind. Eng. Chem. (ind. Edn.) 30, 312

(1933).

[24] Kahre, L. C., Liquid density of light hydrocarbon mixtures, J. Chem. Eng.

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[25] Kestin, J., Khalifa, H. E., and Kumar, B., Thermodynamic and Transport

Properties of Isobutane: A Survey of Available Data, Division of

Engineering, Brown University, Providence, R.I. 02912. Report No.

COO/4051-35 for Department of Energy, Division of Geothermal Energy,

November, 1978.

17
[26] Kretschner, C. B., and Wiebe, R. , J. Am. Chem. Soc. 73^, 3778 (1951).

[27] McCarty, R. D., Least-squares computer subroutine, unpublished report, this

laboratory, Jan. 3, 1972.

[28] McClune, C. R., Measurement of the densities of liquefied hydrocarbons from

93 to 173 K, Cryogenics, 289 (May 1976).

[28a] Milora, S. L., and Combs, S. K., Thermodynamic Representations of Ammonia

and Isobutane, ORNL/TM-5847, prepared for Energy Research and Development

Administration by Engineering Technology Division, Oak Ridge National

Laboratory, Oak Ridge, Tenn. 37830, May, 1977.

[29] Morris, W. M. , Sage, B. H., and Lacey, W. N., Volumetric behavior of

isobutane. Tech. Pub. No. 1128, Petroleum Technology (Am. Inst. Mining and

Metallurgical Engineers, preprint) November, 1939.

[30] Orrit, J. E., and Laupretre, J. M., Density of liquefied natural gas

components. Advances in Cryogenic Engineering , 23 , 573-579 (1978).

[31] Pompe, A., and Spurling, T. H., Virial Coefficients for Gaseous

Hydrocarbons , Tech. Paper No. 1, Commonwealth Scientific and Industrial

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[32] Reeves, L. E., Scott, G. J., and Babb, S. E., Jr., Melting curves of

pressure-transmitting fluids, J. Chem. Phys. No. 12, 3662 (Jun 1964).

Also, private communication on isobutane from Prof. S. E. Babb, Jr.,

October 2, 1978.

[33] Rodosevich, J. B., and Miller, R. C., Experimental liquid mixture densities

for testing and improving correl ations” for liquefied natural gas, AIChE J.

1^, No. 4, 729 (Jul 1973).

[34] Sage, B. H., and Lacey, W. N., Phase equilibrium in hydrocarbon systems.

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(1938).

[35] Sengers, J. M. H. Level t, private communication, Dec. 5, 1978. See, for

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18
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[38] Strein, Von K., Lichtenthal er, R. N., Schramm, B., und Schafer, K1 .

,

Messwerte ]es zweiten Virialkoeffizienten einiger gesattigter

Kohl enwasserstoffe von 300-500 K, Ber. Bunsenges Phys. Chem. 7^, No. 12,

1308 (1971).

[39] Tech. Committee, Natural Gasoline Assoc. Am., Densities of liquefied

petroleum gases, Ind. Eng. Chem. No. 10, 1240 (Oct 1942).

[40] Thompson, P. A., An explicit formula for the liquid-vapor saturation

densities as a function of pressure. Symposium on EQUATIONS OF STATE IN

ENGINEERING AND RESEARCH, 176th National Meeting of the American Chemical

Society, Miami Beach, Fla., Sept 10-15, 1978.

[41] Van der Vet, A. P., (Dutch-Shell Labs., Amsterdam), Density,

compressibility, expansion of light hydrocarbons and of light hydrocarbon

blends. Congress Modial du Petrol II, 515, Paris, 1937.

[42] Wackher, R. C., Linn, C. B., and Grosse, A. Y., Physical properties of

butanes and butenes, Ind. Eng. Chem. No. 5, 464 (May 1945).

[43] Yarbrough, D. W., and Tsai, C.-H., Vapor pressures and heats of

vapo»^i zation for propane and propene from 50 K to the normal boiling point.

Paper M-7, pp. 602-610, Vol . 23, Advances in Cryogenic Engineering (1978).

19
APPENDIX A. Symbols and Units

Subscripts c and t refer to critical and liquid triple points.

Subscripts g and £ refer to saturated vapor and liquid.

Subscript a refers to liquid-vapor coexistence (usually the liquid).

Superscript o refers to ideal gas states.

a, S, y, 6, E B{p), C{p)

B*(x)

Cv(p,T)

Cp(p.T)

Co(T)

d

non-linear parameters in the equation of state

density-dependent coefficients in the equation of state

second virial coefficient

molal heat capacity at constant volume, (J/mol)/K

molal heat capacity at constant pressure, (J/mol )/K

molal heat capacity for saturated liquid, (J/mol )/K

density, mol/L

E(P,T)

E°

f(p)

F(P,T)

H°

H(P,T)

the internal energy, J/mol

23,838.616 J/mol (arbitrary)

used in the definition of e(p)

definition in the equation of state

enthalpy for ideal gas state at T = 0

the enthalpy, J/mol

J the joule, 1 N-m

L the liter, 10"^ m^

mol 58.1243 grams of isobutane (C^2 = ]2 scale)

P pressure in bars, 1 bar = lO^N/m^, (1 atm = 1.01325 bar)

Po(T)

Pa(p)

(p,T)

''(P.T)

Qvap

R *

R

the vapor pressure, bar

PatTo(p)^» vapor pressure as function of density

function in the equation of state

function in the equation of state

AHvap» the heat of vaporization, J/mol

the gas constant, 8.3145 (J/mol )/K, 0.083145 (bar-L/mol )/K

(0.083145) *dc, bar/K

PS(P,T)

d/dc, density reduced at the critical point

the entropy, (J/mol )/K

T temperature, K To(p)

0(P)

liquid-vapor coexistence temperature, K

defined locus of temperatures

V 1/d, molal volume, L/mol

oo(p,T) [1 - 0(p)/T] for the equation of state

20
APPENDIX A. (Continued)

W(p,T) the speed of sound, meters/second

x(T) J/Jq for the equation of state

x(T) variously defined for other equations

Xq(p) Ta(p)/Tc» reduced temperature at coexistence, for the

equation of state.

APPENDIX B. Fixed-Point Values for Isobutane

Triple Point Boiling Point Critical Point

Temperature, K 113.55 261 .359 408.00

Pressure, bar 1.8893«10'^ 1 .01325 36 .5489

Density, mol/L

Vapor 2.001 •10‘® 0.04840 3.86

Liquid 12.755 10.2163 3.86

21
o

1/LOUJ ‘A1ISN3Q

Figure 1. The density-temperature diagram of isobutane

22

TEMPERATURE
ueq ‘d

Figure 2. The P-T locus of P-p-T data for isobutane

23

200

300

400

500

600
• •

' • CO CVJ 1-H

LOUJ/p>| ‘(IH-H)-

Figure 3. Comparison of enthalpies at T =

24

250 F

bar
o00

CO

o

ro

o

ro

oCVJ n

OoCO

L0iu/f>| ‘^HV

Figure 4. Comparison of enthalpies for saturated liquid

25
00 UD C\J

L0UJ/p>| ‘H

Figure 5. Calculated enthalpy at P = 50 bar

26

200

300

400

500

600
Table 1. Vapor pressures of isobutane

I-BUTANE VAPOR PRESSURES, EPP = 1.950

(1) ASTON, (2) BEATTIE, (3) CONNOLLY, (4) DANA, (5) MORRIS,

(6) S AGE/ LACEY, (7» MACKHER, ( 8 ) G I LL IL AND , (9 )GILMOUR, ( 40 » T HERMAL OOPS

.

TTRP =113.550, TCRT = 408.000

PTRP = .18893E-06, PCRT = 36.548852, OPSDT = .63410

13. 80835297 9.37269200 -70.'54663008 112. 75833458 -52. 42140768 47. 81122198

ID HT T,K U X P,BAR CALCD PCNT DPS/DT RFSID.

40 1.000 113.550 -2.59313 .27831 . 18892E-06 .18893E-06 -.01 .497E-07 -.00000

40 1.000 115.000 -2.54783 . 28186 . 27523E-06 . 27521E-06 .01 . 7 04E-07 .00225

40 1.000 120.000 -2.40000 .29412 .93316E-06 .93301E-06 .02 . 2 17E-06 . 00923

40 1.000 125.000 -2.26400 .30637 .28423E-05 .28421E-05 .01 .6 C5E-06 .01516

40 1.000 130.000 -2.13846 .31863 .78778E-05 .78785E-05 -.01 .154E-05 . 02017

40 1.000 135.000 -2.02222 . 33088 . 20085E-04 .20091E-04 -.03 . 361E-05 .02440

40 1.000 140.000 -1.91429 . 34314 .47552E-04 .47569E-04 -.04 .787E-05 . 02794

40 1.000 145.000 -1.81379 .35539 .10538E-03 .10541E-03 -. 03 .161E-04 .03089

40 1.000 150.000 -1.72000 .36765 . 220 07E-03 .22013E-03 -.03 .312E-04 . 03332

40 1.000 155.000 -1.63226 .37990 .43578E-03 . 43583E-03 -.01 .574E-04 .03529

40 1.000 160.000 -1.55000 . 39216 . 82241E-03 .82237E-03 . 00 . 1 ClE-03 .03685

40 1.000 165.000 -1.47273 .40441 .14861E-02 . 14357E-02 . 02 . 170E-03 . 03806

40 1.000 170.000 -1.40000 .41667 .258 15E-02 . 258 03E-02 . 04 .275E-03 .03896

40 1.000 175.000 -1.33143 .42892 .43261E-02 .43236E-02 . 06 .432E-03 .03957

40 1.000 180.000 -1.26667 .44118 .70164E-02 . 70117E-02 . 07 .656E-03 .03994

40 1.000 185.000 -1.20541 .45343 .11044E-01 .11037E-01 .07 . 970 E-03 . 040 09 40 1.000 190.000 -1.14737 .46569 . 16915E-01 . 16904E-01 . 07 . 140E-02 .04005

40 1.000 195.000 -1.09231 .47794 . 25263E-01 .25249E-01 . 06 .197E-02 .03984

40 1.000 200.000 -1.04000 .49020 . 36870E-01 . 36854E-01 . 04 . 271E-02 .03949

40 1.000 205.000 -.99024 . 5 0 2 45 . 52675E-01 .52665E-01 . 02 . 365E-02 .03900

40 1.000 210.000 -.94286 .51471 .73795E-01 . 73799E-01 -.00 . 484E-02 .03839

40 1.000 215. 000 -.89767 .52696 . 10153E+00 .10156E*00 -.03 .631E-02 .03769

40 1.000 220.000 -.85455 .53922 .13736E+00 .13744E+00 -.06 .810E-02 . 03690

40 1.000 225.000 -.81333 .55147 . 18297£*00 . 183 13E + 00 -. 09 . 1 02E- 01 . 03603

40 1.000 230.000 -.77391 .56373 . 24025E*00 .24053E+00 -.12 .128E-01 .03510

40 1.000 235.0 00 -.73617 .5 75 98 .31127E4-Q0 . 311 70E+00 -.14 .158E-01 . 03412

40 1.000 240 .000 - . 70000 .58824 . 39831E+00 .39393E+00 -.15 . 192E-01 .03310

40 1.000 245.000 -.66531 .60049 .50383E+00 .50466E+00 -. 16 . 232E- 01 .03203

1 1.000 245.584 -.66135 .60192 .52132E+00 .518 34E+ 00 .58 .237E-01 .03230

40 1.000 250.000 -.63200 .612 75 .63044E+00 .63153E-t-00 -.17 .277E-01 .03094

1 1.000 251.089 -.62492 .61541 . 66405Et00 .66223E+ 00 . 27 . 287E-01 .03093

1 1.000 254.399 -.60378 .62353 .76350E+00 . 76283E+00 .09 .321E-01 . 03009

40 1.000 255. 000 -.60000 .62500 .78097E+00 .78231E+00 -. 17 . 327E-01 . 02982

7 1.000 253.150 -.58048 .632 72 .88886E+00 .89090E+00 -.23 .362E-01 . 02907

1 1.000 259.922 -.56970 .63706 .95476E+00 .95695E+00 -.23 . 383E-01 . 02667

40 1.000 260.000 -.56923 .63725 .95834E+00 .95995E+00 -. 17 . 384E-01 .02868

7 1.000 261.250 -.56172 .64032 . 1 01 06E+01 . 10089E + 01 .17 . 399E-01 .02857

9 1.000 261.400 -.56083 .64069 . 1 0133E+01 .10149E+01 -.16 .4 OlE-01 . 02836

1 1.000 261.551 -.55993 .64106 . 101 78E^01 .10210E+01 -.31 . 4 03E-01 .02825

7 1.000 262. 750 -.55281 . 64400 . 10654E+01 .10702E+01 -.45 . 4 18E- 01 .02790

4 1.000 279.810 -.45813 .68581 .19993E*01 .19892E*01 .51 .672E-01 . 02438

4 1.000 287. 780 -.41775 .70534 .25905E+01 .25821E+01 . 33 .8 19E-01 .02238

4 1.000 295.230 -.38197 .72360 .32531E4-01 .32479E+01 . 16 .972E-01 . 02052

27
Table 1. Continued

I-BUTANE VAPOR PRESSURES, EPP = 1.950

ID NT T,K U X P,BAR CALCD PC NT OPS/OT RESIO.

4 1.000 299.480 -.36236 .73402 .36877E+01 .36807E+01 .19 .1 07E+00 .01953

4 1.000 304.130 -.34153 .74542 . 42143E*01 . 42016E+01 .30 .118E+00 .01849

4 1.000 309.030 -.32026 .75743 .48268E+01 .48073E»01 .41 .130E+00 .01740

4 1.000 313.070 -.30322 .76733 .53782E+01 .535 29E+01 .47 .140E«00 .01650

4 1.000 317.730 -.28411 .77875 .60502E+01 .60369E4-01 .22 .153E+00 .01530

4 1.000 317.730 -.28411 .77875 .60462E+01 .60369E+01 .15 .153E+00 .01527

4 1.000 323.660 -.24140 .80554 .79167E+01 .73878E+01 .37 .186E+00 . 01292

4 1.000 335. 320 -.21675 .82186 .91526E+01 .91990E+01 -.50 .208E>00 .01102

3 1.000 344.260 -.18515 .84377 .11146E+02 .11198E+02 -.46 .240E+00 .00916

5 1.000 344.261 -.18515 .84378 .11128E«-02 .11198E+02 -.62 .240E+00 .00908

6 1.000 344.261 -.18515 .84378 . 11107E+02 .11198E*02 -.81 .240E4^00 .00896

2 1.000 348.150 -.17191 .85331 .12090E+02 .12159E+02 -.57 .254E+00 . 00631

4 1.000 352.640 -.15699 .86431 . 13310E+02 ..13341E+02 -.23 .272E+00 .00760

4 1.000 352.640 -.15699 .86431 .13395E+02 .13341E+02 .41 .272E+00 .00793

4 1.000 345.070 -.18237 . 84576 . 11364E+02 .11393E+02 -.26 .243E^00 .00910

6 1.000 360.928 -.13042 .88463 .15810E»02 .15740E+02 .44 .307E+00 .00637

3 1.000 360.930 -.13041 .88463 .15726E*02 •15741E+02 -.09 .307E<-00 .00609

2 1.000 373.150 -.09339 .91458 .19832E+02 .19846E*02 -.07 .366E+00 . 00398

3 1.000 377.590 -.08054 .92547 .21572E+02 .21523E+02 .23 .390E«00 . 00342

5 1.000 377.594 -.08053 .92548 . 21567E*02 .21525E+02 .19 .390E+00 .00341

6 1.000 377.594 -.08053 .92548 .21629E*02 .21525E+02 .48 . 390E4-00 .00356

3 1.000 394.260 -.03485 .96632 .28936E+02 .28872E+02 .23 .498E+00 .00120

6 1.000 394.261 -.03485 .96633 .28937E*02 .28873E+02 .22 .498E+00 .00120

2 1.000 398.150 -.02474 .97586 . 30843E4-02 .30868E+02 -. 08 .529E+00 .00064

3 1.000 406.870 -.00278 .99723 .35788E4-02 • 35842E+ 02 -.15 .618E4-00 -.00003

3 1.000 407.770 -.00056 . 99944 .36325E*02 .364 03E+02 -. 22 .630E^00 -.00010

1 0.000 188.070 -1.16941 .46096 .15159E-01 .14383E-01 5. 39 .122E-02 .04281

1 0.000 201.456 -1.02526 .49376 .42610E-01 .40978E-01 3.98 .296E-02 .04138

7 0.000 206.450 -.97627 .50600 . 643S5E-01 .58191E-01 10.66 .397E-02 . 04413

7 0.000 215.150 -.89635 .52733 .11172E+00 .10251E+00 8.99 .636E-02 . 04219

1 0.000 216.729 -.88254 .53120 .11579E+00 .11297E+00 2.50 .689E-02 .03874

7 0.000 228. 750 -.78361 .56066 .23851E4-00 .22497E+00 6. 02 .121E-01 .03846

1 0.000 229.053 -.78125 .56140 .23233E+00 .22866E+00 1.60 .123E-01 .03618

7 0.000 237.350 -.71898 .58174 .36170E+00 . 35055E*00 3.18 .173E-01 .03536

7 0.000 242.150 -.68491 .59350 .45596E+00 .44198E*00 3.16 .208E-01 .03436

4 0.000 249.140 -.63763 .610 64 .62090E+00 .60808E+00 2.11 .269E-01 .03231

7 0.000 250.450 -.62907 .61385 .65488E+00 . 64408E^OO 1.68 .281E-01 .03180

4 0.000 255.090 -.59944 .62522 . 79740E+00 .78526E+00 1.55 .328E-01 .03069

4 0.000 259.310 -.57341 .63556 .94580E+00 .93372E4-00 1.29 .376E-01 .02960

4 0.000 261.0 00 -.56322 .63971 .1 0121E+01 .99896E+00 1.32 .396E-01 .02922

4 0.000 263.240 -.54992 .64520 .11430E+01 . 10908E+01 4. 78 .424E-01 .03047

4 0.000 270.910 -.50604 . 664 0 0 .14736E+01 .14558E+01 1.23 .530E-01 .02686

6 0.000 290.372 -.40509 .71170 .27579E+01 .28009E+01 -1.53 .870E-01 .02078

6 0.000 294.261 -.38652 .72123 . 31006E+01 .31548E+01 -1.72 .951E-01 .01976

2 0.000 303.150 -.34587 .74301 . 39932E+01 .40876E+01 -2.31 .1 15E+00 . 01734

6 0.000 310.928 -.31220 . 76208 .495B0E+01 .50583E+01 -1.98 .135E+00 .01570

2 0.000 323.150 -.26257 .79203 .67898E+01 .69099E+01 -1.74 . 169E+00 .01304

6 0.000 327.594 -.24544 .80293 . 75704E+01 .76913E+01 -1.57 .183E*00 .01214

e 0.000 352.039 -.15896 .862 84 .13652E+02 .13178E+02 3.60 . 270E4-00 .00969

8 0.000 372.594 -.09503 .91322 .19995E+02 .19643E+02 1.79 .363E+00 .00503

8 0.000 389.261 -.04814 .95407 .27234E+02 .26477E+02 2.86 .461E+00 . 0 0315

e 0.000 403.150 -.01203 .98811 . 33991E+02 .33626E+02 1.09 .576E+00 .00084

8 0.000 407.594 -.00100 .99900 .368 87E+02 .36293E+02 1.64 .628E+00 .00087

NP = 69 RMSPCT 270

28
Table 2. Densities of saturated liquid

I-9UTANE SATURATED LIQUID DENSITIES, EL = .350

«1) BEATTIE, (2) CARNEY, (3) COFFIN, ( 4 ) CR AGOE , ( 5 ) 0 ANA

,

(6» FOEHR, C7)GILM0UR, ( 3 » HAY NES, I 9» MCCLUNE, ( 10 » MORRIS,

(11) ORRIT, (12)SAGE/L, ( 13) SLIHINSK I , ( 14) T . C. N AT . G ASO . A . A ,

,

(15) VANOERVET, (16) HACKHER, ( 17 ) PENN. ST A TE

,

(18) KAHRE, (19) ROOOSEVICH.

TTRP =113.550, TCRT = 408.000, OTRP = 12.755, DCRT = 3.860

.786913448 -.142753535 .057698164

ID MT T,K X MOL/L CALCD PCNT ODS/DT RESID.

19 1.000 114. 000 .99847 12.754 12.748 . 05 -.01643 1.36907

19 1.000 115.000 .99508 12.741 12.731 .07 -.01643 1.03008

8 5.000 115.075 .99482 12. 731 12.730 .00 -.01643 .72094

19 1.000 120.000 .97809 12.665 12.649 .12 -.01644 .82790

8 5.000 120.075 .97784 12.649 12.648 . 01 -.01644 .71315

9 1.000 123.150 .96740 12.583 12.597 -.11 -.01644 .62967

8 5.000 125.075 .96086 12.569 12.566 .02 -.01645 .72027

9 1.000 128.150 .95042 12.501 12.515 -.11 -.01646 .65834

11 1. 000 129.478 .94591 12.483 12.493 -.08 -.01646 .67440

8 5.000 130.075 .94388 12.485 12.483 .01 -.01646 .71360

11 1.000 133.032 .93384 12.428 12.435 -.05 -.01647 .69145

9 1.000 133.150 . 93344 12.420 12.433 -.10 -.01647 .67620

8 5.000 135. 075 .92690 12.402 12.401 .00 -.01648 .71158

11 1.000 135.728 .92468 12.379 12.390 -.09 -.01648 .68447

9 1.000 138.150 .91645 12.341 12.350 -.07 -.01649 .69200

11 1.000 138.596 ,91494 12. 335 12.343 -.07 -.01649 .69490

8 5.000 140.075 .90992 12.322 12. 318 .02 -.01650 .718 07

11 1.000 141.445 .90526 12. 294 12.296 -.02 -.01650 .70830

9 1.000 143.150 .89947 12.260 12.268 -.06 -.01651 .69984

11 1.000 144.033 .89647 12.247 12.253 -.05 -.01652 .70327

8 5.000 145. 0 75 . 89294 12.235 12.236 -.01 -.01652 .71311

11 1.000 146.745 .88726 12.202 12.208 -. 06 -.01653 .70427

9 1.000 148.130 .88256 12.178 12.185 -. 06 -.01654 .70417

8 5.000 150.075 .87596 12.153 12.153 . 00 -.01655 .71635

11 1. 000 150.360 .87499 12.162 12.149 .11 -.01655 .73518

11 1.000 152.693 . 86706 12.1 06 12.110 -. 03 -.01656 .71170

9 1.000 153.150 .86551 12. 095 12.102 -.06 -.01657 .70768

11 1.000 155.443 .85772 12.058 12.064 -.05 -.01658 .71049

11 1.000 158.124 .84862 12.016 12.020 -.03 -.01660 .71458

9 1.000 158,150 . 84853 12,013 12.019 -.05 -.01660 .71181

11 1.000 160.760 .83967 11.973 11.976 -. 03 -.01662 .71654

9 1.000 163.150 . 83155 11.930 11.936 -.05 -.01664 .71465

11 1.000 163.448 .83054 11.928 11.931 -. 03 -.01664 .71814

11 1.000 166.140 . 82140 11.884 11.887 -. 02 -.01666 .71981

9 1.000 168.150 .81457 11. 848 11.853 -. 04 -.01668 .71850

11 1.000 171.559 .80299 11.793 11.796 -.03 -.01672 .72162

9 1.000 173.150 .79759 11.766 11.770 -. 03 -.01673 .72225

11 1.000 174.459 .79314 11.745 11.748 -.03 -.01675 .72320

11 1.000 177.042 . 78437 11.703 11.704 -.01 -.01677 .72575

11 1.000 179.875 .77475 11.656 11.657 -.01 -.01681 .72706

11 1.000 182.638 ,76537 11.609 11.610 -.01 -.01684 .72787

11 1.000 185.429 .75589 11.560 11.563 -.02 -.01688 .72818

11 1.000 188.223 .74640 11.512 11.516 -. 04 -.01692 .72814

11 1.000 194.542 . 72494 11.407 11.409 -.01 -.01701 .73287

11 1.000 199.435 .70815 11.325 11.325 .00 -.01710 .73606

11 1.000 205.110 .68905 11.225 11.228 -.02 -.01720 .73643

11 1.000 210.673 .67015 11.132 11.132 . 00 -.01732 . 74025

29
Table 2. Continued

I-BUTflNE SATURSTEO LIQUID DENSITIES, EL = .350

ID WT T,K X MOL/L CALCO PCNT DDS/OT RESIO.

11 1.000 216. 223 .65131 11.0 33 11.036 - .0 2 -.01744 .74112

11 1.000 221.684 .63276 10.937 10.940 -.02 -.01758 .74306

16 1.000 223.650 .62608 10.923 10.905 .16 -.01763 .75378

11 1.000 227.155 .61418 10.842 10.043 -.01 -.01773 .74567

2 1.000 227.594 .61269 10.841 10.836 .05 -.01775 .74906

8 5.000 228.000 .61131 10.827 10. 828 -.01 -.01776 .74623

14 1.000 228.428 .60986 10.827 10.821 .06 -.01777 .74994

11 1.000 229.970 .60462 10.790 10.793 -.03 -.01782 .74569

14 1.000 232.261 .59684 10.756 10.752 .03 -.01789 .75002

11 1.000 232.686 .59539 10.741 10.745 -.04 -.01790 .74659

2 1 . 000 233.150 .59382 10.743 10.737 . 06 -.01792 .75147

17 1.000 233.150 .59382 10.732 10.737 -. 04 -.01792 .74654

16 1.000 233.650 .59212 10.748 10.728 .19 -.01793 .75832

11 1.000 235.557 .58564 10.688 10.693 -. 05 -.01799 .74714

2 1.000 238. 706 .57495 10.643 10.636 . 06 -.01810 .75351

11 1.000 238.707 .57495 10.633 10.636 -.04 -.01810 .74900

14 1.000 238. 983 .57401 10.636 10.631 .04 -.01811 .75284

11 1.000 241.431 .56570 10.583 10.587 -.04 -.01820 .74981

17 1.000 243.150 .55986 10.553 10.556 -.03 -.01826 .75112

16 1.000 243.650 .55816 10.566 10.547 .19 -.01828 .76102

11 1.000 244.259 .55609 10.531 10.535 -.05 -.01830 .75056

2 1.000 244.261 .55608 10.541 10.535 . 06 -.01830 .75523

3 0.000 245.350 .55239 10.548 10.515 .31 -.01835 .76717

14 1.000 246. 150 .54967 10.503 10.501 .02 -.01838 .75435

11 1.000 246.962 .54691 10.479 10.486 -.06 -.01841 .75079

11 1.000 249.415 .53858 10.439 10.440 -.02 -.01851 .75368

2 1.000 249.817 .53722 10.438 10.433 .05 -.01853 .75674

14 1.000 249.817 .53722 10.438 10.433 . 05 -.01853 .75674

3 0.000 252.450 .52827 10.417 10.384 .32 -.01864 .76919

17 1.000 253.150 .52590 10.367 10.371 -. 04 -.01867 .75415

16 1.000 253.650 .52420 10.382 10.362 .19 -.01669 .76429

2 1.000 255.372 .51835 10. 337 10.329 . 07 -.01877 .75945

14 1.000 255. 372 .51835 10.336 10. 329 .06 -.01877 .75925

14 1.000 255.483 .51797 10.335 10.327 .07 -.01877 .75972

3 0.000 257.350 .51163 10.331 10.292 .38 -.01886 .77286

3 0.000 259.550 .50416 10.288 10.251 .36 -.01897 .77287

7 1.000 261.000 .49924 10.225 10.223 .02 -.0 1904 .75926

3 0.000 261.950 .49601 10.249 10.205 .43 -.01908 .77611

17 1.000 263.150 .49193 10.176 10.182 -.06 -.01915 .75687

16 1.000 263.650 .49024 10.185 10.172 .12 -.01917 .76423

3 0.000 264.650 .48684 10.192 10.153 . 38 -.01922 ,77472

2 1.000 266.483 .48061 10.127 10.116 .09 -.01932 .76366

14 1.000 266.483 .46061 10.127 10.118 .09 -.01932 .76381

3 0.000 266.950 .47903 10.149 10.109 .40 -.01935 .77583

3 0.000 267.650 .47665 10.139 10.095 .43 -.01939 . 77736

3 0.000 270.450 ,46714 10.077 10.041 . 36 -.01954 .77523

3 0.000 271.850 .46239 10.056 10.013 .42 -.01963 .77799

5 1.000 273. 150 .45797 10.013 9.988 .25 -.01970 .77184

16 1.000 273.150 .45797 9.995 9.988 .07 -.01970 .76519

17 1.000 273.150 .45797 9.982 9.988 -.06 -.01970 .76033

3 0.000 273.850 .45560 10.015 9.974 .41 -.01975 .77788

2 1.000 277. 150 .44439 9.913 9.909 . 05 -.01995 .76547

14 1.000 277.150 .44439 9.913 9.909 .04 -.01995 ,76540

3 0.000 277.450 .44337 9.956 9.903 .54 -.01997 .78332

18 1.000 277.550 .44303 9.901 9.901 . 01 -.01998 .76413

30
Table 2. Continued

I -8 UTANE SATURATED LIQUID DENSITIES , EL = .350

ID HT T,K X MOL/L CALCD PCNT DDS/DT RESIO . 5 1.000 281.150 .43080 9.856 9.828 .30 -.02022 .77569

3 0.000 281.650 .42911 9. 856 9.818 .39 -.02025 .77872

15 1.000 283.150 .42401 9.798 9.788 .11 -.02036 .76932

17 1.000 283.150 .42401 9.786 9.788 -.02 -.02036 .76506

13 5.000 233.200 .42384 9.782 9.787 -. 05 -.02036 .76387

3 0.000 284.850 .41824 9.791 9.753 . 39 -.02048 .77958

3 0.000 285.650 .41552 9.776 9.737 .41 -.02054 .78027

8 5.000 283.706 .40514 9.668 9.673 -.06 -.02077 .76530

2 1.000 288.706 .40514 9.679 9.673 . 06 -.02077 .76936

14 1.000 283.706 .40514 9.679 9.673 . 06 -.02077 .76926

15 1.000 238.710 .40513 9.686 9.673 .13 -.02077 .77175

18 1.000 288.750 .40499 9.680 9.673 .08 -.02078 .76997

5 1.000 289.150 .40363 9.686 9.664 .23 -.02081 .77501

6 5.000 290.000 .40075 9.641 9.646 -. 06 -.02087 .76584

15 1.000 293.150 .39005 9.592 9.580 .12 -.02113 .77244

17 1.000 293.150 .39005 9.586 9.580 . 06 -.02113 .77056

13 5.000 293.190 .38991 9.578 9.579 -.01 -.02113 .76816

3 0.000 293.350 .38937 9.619 9.576 . 45 -. 0 2115 .78332

12 1.000 294.261 .36628 9.626 9.557 .72 -.02122 .79248

5 1.000 297. 150 .37646 9.514 9.495 .20 -.02148 .77612

15 1.000 298.150 .37307 9.485 9.474 .12 -.02157 .77380

3 0.000 298.450 .37205 9.514 9.467 .50 -.02159 .78584

2 1.000 299.817 .36741 9.438 9.438 .01 -.02172 .77080

14 1.000 299.817 .36741 9.438 9.438 .01 -.02172 .77067

16 1.000 299.850 .36729 9.438 9.437 . 02 -.02172 .771 05

8 5.000 300.000 .36679 9.430 9.434 -.04 -.02174 .76937

1 1.000 303.150 .35609 9.445 9. 365 . 86 -. 0 2204 .79796

13 5.000 303.150 .35609 9.363 9.365 -.01 -.02204 .77096

15 1.000 303.150 .35609 9.377 9.365 .13 -.02204 .77535

5 1.000 305.150 .34930 9.342 9.320 .23 -.02225 .77907

15 1.000 308.150 .33911 9.266 9.253 .14 -.02256 .77704

2 1.000 310.928 .32967 9.196 9.190 . 06 -.02237 .77534

10 0.000 310.928 .32967 9.245 9.190 .60 -.02287 .79118

12 1.000 310.928 .32967 9.245 9.190 .60 -.02287 .79121

14 1.000 310.928 .32967 9.196 9.190 . 07 -.02287 .77541

18 1.000 310.950 .32960 9.194 9.189 .05 -.02288 .77496

13 5.000 313.120 .32223 9.136 9.140 -.02 -.02313 .77345

5 1.000 313.150 .32213 9.170 9.139 .34 -.02313 .78401

15 1.000 313.150 .32213 9.155 9.139 .17 -.02313 .77904

15 1.000 318.150 .30515 9.038 9.022 .18 -.02376 .78027

5 1.000 321.150 .29496 8.981 8.950 .35 -.02416 .78579

2 1.000 322.039 .29194 6.945 8.928 .18 -.02429 .78131

14 1.000 322.039 .29194 8.945 8.928 .19 -.02429 .78144

13 5.000 323.120 .28827 8.899 8.902 -.03 -.02444 .77552

1 1.000 323. 150 .28816 8.912 8.901 .12 -.02445 .77983

15 1.000 323.150 .28616 6.917 8.901 .18 -.02445 .78143

18 1.000 327.550 .27322 8.776 8.792 -. 18 -. 0 2512 .77241

12 1.000 327.594 .27307 8.839 8.791 .55 -.02512 .79234

5 1.000 329.150 .26779 8. 792 8. 75 2 .46 -.02538 .79025

13 5.000 333.110 .25434 8.649 8.650 -.02 -.02606 .77318

2 1.000 333.150 .25420 8.663 8.649 .16 -.02606 .78282

14 1.000 333.150 .25420 8.662 8.649 .15 -.02606 .78267

13 5.000 343.080 .22048 8.380 8.381 -.01 -.02807 .78043

10 0.000 344. 261 . 21647 8.392 8.347 .54 -.02835 .79443

12 1.000 344.261 .21647 8.389 8.347 .50 -.02835 .79354

31
Table 2. Continued

I-3UTANE SATURATED LIQUID DENSITIES, EL = .350

ID NT T,K X MOL/L CALCD PCNT OOS/DT RESIO.

1 1.000 348.150 .20326 8.258 8.235 .28 -.02931 .78846

13 5.000 353.090 .18648 8.087 8.087 -.01 -.03069 .78216

12 1.000 360.928 .15986 7.861 7.836 . 31 -.03336 .79103

13 5.000 363.110 .15245 7.761 7.763 -.02 -.03424 .78328

13 5.000 368.100 .13551 7.582 7.586 -.05 -.03653 .78316

1 1.000 373.150 .11836 7.364 7.395 -.42 -.03939 .77524

10 0.000 377.594 .10326 7.254 7.213 .57 -.04252 .79873

12 1.000 377.594 .10326 7.254 7.213 .57 -.04252 .79863

1 1.000 398.150 .03345 6.073 6.054 .31 -.08208 .79455

NP = 146, RMSPCT = .139

32
Table 3. Densities of saturated vapor

I-8UTANE SATURATED VAPOR DENSITIES, NF = 3, E = .35, EGX = 3.60

(l)DANA, «2)HANS0N/CRAG0E, ( 3) S AGE/L ACE Y

,

(4)SLIWINSKI, (40 )THERMALOOPS, (50 ) THOMPSON.

TTRP = 113.550, TCRT = 408.000, DGAT = . 20 01 147E-0 7, DCRT = 3.8600

-.764051 8360E + 00 . 6505011822E4-00 . 30 75 066326E+ 02

0 • 0 . 0 .

ID HT T,K MOL/L CALCC PCNT Z,XPT Z,CALC F(Z) OOS/DT

40 1.000 165.000 .10836E-03 . 10836E-0 3 -.00 . 99942 . 99939 3.23837 . 117E-04

40 1.000 170.000 .18273E-03 . 18272E-03 .01 .99902 .99909 3.34509 .184E-04

40 1.000 175.000 .29756E-03 .29753E-03 .01 . 99861 . 99870 2.99665 . 280E-04

40 1.000 160.000 .46938E-03 .46935E-03 .01 .99815 .99820 2.61038 . 414E-04

40 1.000 185.000 .71922E-03 .71925E-03 -.00 .99762 . 99758 2.24437 .594E-04

40 1.000 190.000 .10733E-02 . 10734E-0 2 -.02 .99699 . 99682 1. 95572 . 833E-04

40 1.000 195.000 .15632E-02 .15637E-02 -.03 .99625 . 99592 1.71954 . 114E-03

40 1.000 200. 000 .22267E-02 . 22277E-02 -.05 .99534 .99488 1.54094 . 153E-03

40 1.000 205.000 .31077E-02 . 31095E-02 -.06 .99425 .99368 1 . 39835 .201E-03

40 1.000 210.000 .42569E-02 . 42593E-02 -.06 . 99289 . 99232 1,29471 . 260E-03

40 1.000 215. 000 .57314E-02 . 57341E-02 -.05 .99125 .99079 1.21323 .332E-03

40 1.000 220.000 .75954E-02 . 75968E-02 -.02 .98925 . 98907 1. 15293 .416E-03

40 1.000 225.000 .99193E-02 . 99168E-0 2 .03 .98689 .98714 1.10396 .515E-03

40 1.000 230.000 •12781E-01 . 12769E-01 .09 .98409 . 98498 1.06575 .629E-03

40 1.000 235. 000 .16265E-01 . 16236E-01 .18 . 98079 . 98256 1. 03646 .760E-03

40 1.000 240.000 .20463E-01 .20403E-01 .29 .97697 . 97982 1.01270 .910E-03

2 1.000 244. 261 .24630E-01 . 24577E-01 .21 .97512 . 97721 .92683 .1056-02

40 1.000 245.000 .25472E-01 . 25364E-0

1

.43 .97259 . 97673 .99282 . 108E-02

1 1.000 249. 817 .309306-01 . 30987E-01 -.18 . 97515 .97336 . 75412 . 126E-02

40 1.000 250.000 . 31397E-01 . 31218E-01 .57 .96767 .97323 .97436 .1276-02

40 1.000 255.000 .38350E-01 .38068E-01 .74 . 96213 . 96926 . 95865 .148E-02

1 1.000 255. 372 .38440E-01 . 38621E-0

1

-.47 . 97350 .96895 .66237 . 1496-02

2 1.000 255.372 .38540E-01 .38621E-01 -.21 .97098 . 96895 . 72551 .149E-02

40 1.000 260.000 .46451E-01 . 46026E-0

1

.92 .95597 . 96478 . 94427 .171E-02

1 1.000 260.928 .47930E-01 . 47635E-01 .62 .95795 . 96389 .87528 .1766-02

2 1.000 266. 483 .57900E-01 . 58188E-0

1

-.50 .96290 .95313 .64967 .205E-02

2 1.000 277.594 .84280E-01 .84630E-01 -.41 .94814 . 94422 .65997 .273E-02

1 1.000 283.150 .10170E^00 . 10091E4-0 0 .79 . 92867 . 93599 . 78333 . 313E-02

4 5.000 283. 200 . 10065E«00 . 10106E + 0 0 -.41 .93974 . 93591 .66094 .314E-02

4 5.000 293. 190 .13678E+00 . 13636E+00 .31 .91598 .91881 .72028 . 395E-02

4 5.000 303. 150 .18065E+00 . 18 044E+0 0 .12 . 89771 .89377 .70042 .4926-02

2 1.000 310. 928 .22130E+00 . 2221 0E<-00 -.36 . 88415 . 88098 .67436 .5816-02

3 1.000 310.928 . 22113E1-00 . 2221QE+00 -.44 .88483 . 88098 .67040 .5816-02

4 5.000 313.120 .23484E+-00 . 23 512E+00 -.12 . 87668 .87563 .68705 .6086-02

1 1.000 316. 483 .25770E+00 . 25630E + 0 0 .55 . 86239 .36711 .71786 .6526-02

2 1.000 322. 039 .29600E+-00 . 29466F+00 .46 .84838 . 85225 .71227 . 7306-02

4 5.000 323. 120 . 30280E+00 . 30264E+ 00 . 05 . 84879 . 34923 .69638 . 7<47E-02

1 1.000 327.594 .33980E+00 . 33763E*0 0 .64 .83101 . 83635 . 71818 . 8186-02

3 1.000 327.594 .33927E*00 . 33763E<-00 .49 .83230 .83635 .71266 .8186-02

4 5.000 333. 110 . 38469E^00 . 38540E+00 -.18 .82103 .81952 .69142 .9166-02

1 1.000 333.150 . 38490E4-00 . 38577E*00 -.23 . 82124 .81939 .69016 .9176-02

4 5.000 343. 080 .48603E+00 . 48680E^0 0 -. 16 . 78746 .78622 .69790 .1136-01

4 5.00 0 353.090 .61214Et00 .612576*00 -.07 . 74919 . 74 866 . 70737 .1406-01

4 5.000 363.110 .77162E4-00 .770326*00 .17 . 70492 .70611 , 72159 .1776-01

4 5.000 368.100 .86590E+00 . 864476*00 .17 .68157 .68269 .72755 . 2016-01

33
Table 3. Continued

I-BUTANE SATURATED VAPOR DENSITIES, NF = 3, E = .35, EGX = 3.60

(l)OANA, (2)HANS0N/CRAG0E, ( 3) SAGE/LACEY,

(4) SLIWINSKI, (40 )THERMALOOPS, (50 ) THOMPSON.

TTRP = 113.550, TCRT = 408.000, OGAT = . 2001147E-0 7, OCRT = 3.8600

-.7640518360E+00 . 6505011622E+00 . 3 0 75 0663 26 E+ 02

0 . 0 . 0 .

ID WT T,K MOL/L CALCO PCNT Z,XPT Z,CALC F(Z> ODS/DT

40 0.000 113.550 .20010E-07 .20011E-07 -.01 1.00006 1. 00 000******»*** .509E-08

40 0.000 115.000 .28784E-07 . 28782E-07 .01 .99994 1.00000 875. 39293 . 711E-06

40 0.000 120.000 .93527E-07 .93512E-07 .02 .99984 1.00000 753. 65940 . 210E-07

40 0.000 125. 000 .27348E-06 . 27346E-06 .01 .99992 1.00000 136.09652 .560E-07

40 0.000 130.000 .72884E-06 .72890E-0 6 -.01 1.00008 . 99999 -54.09937 .137E-06

40 0.000 135. 000 .17894E-05 . 17899E-05 -.03 1.00026 . 99998 -72. 81902 . 308E-06

40 0.000 140.000 . 40852E-05 .40868E-05 -.04 1.00033 .99996 -41.80036 .647E-06

40 0.000 145.000 .67409E-05 . 87442E-05 -.04 1.00029 . 99992 -17. 70619 .128E-05

40 0.000 150.000 .17647E-04 .17653E-04 -.03 1.00020 .99985 -6.30081 .238E-05

40 0.000 155.000 .33818E-04 .33826E-04 -.02 1.00000 . 99975 . 06221 . 424E-05

40 0.000 160.000 .61834E-04 . 61842E- 04 -.01 . 99974 . 99960 2. 48627 .719E-05

1 0.000 266.483 .58690E-01 .58188E-01 1.21 .94671 . 95813 . 93310 .205E-02

1 0.000 272. 039 .71400E-01 . 70459E-0 1 1.34 .93905 .95 159 .90594 .237E-02

1 0.000 277.594 .85590E-01 .84630E-01 1.13 .93363 .94422 .84464 .273E-02

1 0.000 288.706 .12100E+00 . 11950E + 0 0 1.26 .91537 . 92685 . 80813 . 357E-02

2 0.000 288. 706 .11820E+00 .11950E+00 -1.09 .93705 .92685 . 60108 .357E-02

1 0.00 0 294. 261 .14190E+00 . 14064E+00 .89 . 90869 .91680 . 76330 .405E-02

3 0.000 294.261 .13954E4-00 . 14064E+00 -.79 .92406 .91680 .63483 .405E-02

1 0.000 299. 817 .16590E+00 .16460E+00 .79 . 89873 .90581 . 74598 .458E-02

2 0.000 299. 817 .16310E+00 . 16460E+00 -.91 .91416 .90581 .63233 .458E-02

1 0.000 305.372 .1940QE>00 .19165E+00 1.23 .88303 . 89338 . 76381 .516E-02

1 0.000 310.928 .22410E+00 . 22210E + 0 0 .90 .87311 .88098 .73867 .561E-02

1 0.00 0 322. 039 .29760E+00 .29466E4-00 1.00 .84382 . 85225 .73370 . 730E-02

2 0.000 333.150 . 39000E+00 . 38577E+00 1.10 . 81050 . 81939 . 73162 .917E-02

2 0.000 344.261 .50740E+00 .50027E + 0 0 1.43 . 77102 . 78202 . 73810 . 115E-01

3 0.000 344.261 .50688E>00 . 50027E+00 1.32 . 77181 .78202 . 73555 .115E-01

2 0.000 355. 372 .65370E+00 .64534E+00 1.30 . 72998 .73 944 . 73662 .147E-01

3 0.000 360.928 . 74746E + 0 0 . 73271E+00 2.01 . 70173 . 71585 . 75185 .168E-01

2 0.000 366.483 .64610E+00 . 83263E+00 1.62 .67947 .69046 .74849 .193E-01

2 0.00 0 377.594 .llllOE+01 . 10833E+01 2.56 .61712 .63 291 . 77243 .265E-01

3 0.000 377.594 .11130E+01 . 10833E+0

1

2.74 .61601 .63291 . 77467 .265E-01

2 0.000 388. 706 .14880E+01 . 14429E+01 3.13 .54525 .56230 .79808 . 399E-01

2 0.000 394. 261 .17560E+01 . 16971E+01 3.47 , 50158 .51899 . 81727 .527E-01

3 0.000 394.261 .17895E+01 . 16971E+01 5 .44 .49219 .51899 . 83267 .527E-01

2 0.000 399. 817 .21280E+01 . 20503E+ 01 3.79 .44899 .46600 .84463 .777E-01

2 0.000 405. 372 . 27830E«-01 .26549E+01 4.82 .37240 .39036 .89924 .165E4-00

NP = 45, RMSPCT = .30

34
Table 4. Second virial coefficients

I-BUTANE SECOND VIRIAL COEFFICIENTS, EV = 3.00

(nSEATTIE, (2)GUNN, (3)JESSEN, (4) KRETSCHNER,

<5) MORRIS/S/L, (6) SAGE/LACEY, C7)STREIN, Cd)CONNOLLY.

.50094721 -1.10039322 -.64781233

10 HT T,K X 8(T) 8* CALC OIF PCT

3 1.000 273. 16 .669 -889.00 -3.378 -3.304 -.074 -2.25

7 1.000 296.10 . 726 -691.00 -2.626 -2. 712 .086 3.19

3 1.000 303.16 .743 -699.00 -2.656 -2.561 -. 095 -3.71

4 1.000 303.16 .743 -644.00 -2.447 -2.561 . 114 4.45

7 1.000 308.10 .755 -634.00 -2.409 -2. 463 .053 2.17

6 1.000 327.60 .803 -541.34 -2.057 -2.123 . 066 3. 09

7 1. 000 333.90 .918 -532.50 -2.024 -2.027 .004 . 18

6 1.000 344.27 .844 -524.24 -1.992 -1.883 -.109 -5. 80

7 1.000 353.90 .867 -476.70 -1. 811 -1. 762 -. 050 -2.82

7 1.000 373.90 .916 -427.60 -1.625 -1.543 -. 082 -5.32

2 1.000 410.90 1.0 07 -310.60 -1.180 -1.227 . 047 3.80

5 1.000 410.94 1.007 -329. 72 -1.253 -1.227 -.026 -2.14

1 1.000 423.16 1.037 -289. 38 -1.100 -1.142 . 042 3.68

5 1.000 444.27 1.089 -256.50 -.975 -1.012 . 036 3. 71

2 1.000 444.30 1.089 -267.80 -1.018 -1.012 -. 006 -.55

1 1.000 448.16 1.098 -253.65 -.964 -.99 1 . 027 2.69

1 1.000 473.16 1.159 -223.20 -.848 -.8 64 .016 1 .84

2 1.000 477.60 1.170 -230.20 -.875 -. 844 -.031 -3.68

5 1.000 477.60 1.170 -223.06 -.848 -.844 -.004 -.46

1 1.000 498.16 1.221 -197. 06 -.749 -.757 .008 1.07

2 1.000 510.90 1.252 -191.60 -.728 -.708 -. 020 -2.77

5 1.000 510.94 1.252 -191.28 -.727 -.70 8 -. 019 -2.62

1 1. 000 523.16 1.282 -174. 14 -.662 -. 665 .003 .52

1 1.000 548.16 1.343 -153.27 -.582 -.536 . 003 .58

1 1.000 573.16 1.404 -133.76 -.508 -.517 .006 1.61

6 0.000 294.27 .721 -620 .77 -2.359 -2. 754 . 395 14.33

6 0.000 310.94 .762 -585.29 -2.224 -2.408 .184 7.65

8 0.000 344.26 . 944 -457.20 -1.737 -1.883 . 146 7. 74

2 0.000 344.30 .944 -414.00 -1.573 -1.883 . 309 16.43

8 0.000 360.93 .884 -412.70 -1.568 -1.680 .112 6.66

6 0.000 360.94 .884 -502.65 -1.910 -1.680 -. 230 -13.70

8 0.000 377.59 .925 -374.00 -1.421 -1.507 . 085 5.67

2 0.000 377.60 .9 25 -358.00 -1.360 -1.507 . 146 9.70

6 0.000 377.60 .925 -488.54 -1.856 -1.507 -.350 -23.23

8 0.000 394.26 .966 -341.10 -1.296 -1. 357 . 061 4.47

6 0.000 394.27 .966 -466.83 -1.774 -1.357 -.417 -30.75

7 0.000 394.60 .967 -384.00 -1.459 -1. 354 -.105 -7.77

8 0.000 406.87 .997 -318 . 30 -1.210 -1.25 7 . 047 3.76

8 0.000 410.93 1.007 -311.50 -1.184 -1.227 .043 3.51

7 0.000 413.80 1.014 -349.90 -1.330 -1.206 -.124 -10.25

7 0. 000 433.60 1.063 -320. 00 -1.216 -1.074 -. 142 -13.23

8 0.000 444.26 1.089 -259.60 -.986 -1.012 .026 2.55

7 0.000 453.60 1.111 -291.80 -1.109 -.961 -. 148 -15. 37

10 WT T,K X 8(T) 8* CALC DIF PCT

7 0.000 470.20 1.152 -267. 20 -1.015 -.878 -.137 -15.65

7 0.000 494. 00 1.210 -243.40 -.925 -. 774 -. 151 -1 9.56

NP = 25, RMSPCT = 2.99

35
Table 5. Coefficients of the equation of state EQNSTATE COEFFICIENTS, ISOBUTANE

DGAT = .200114700E-07

OTRP = 12.7550, TTRP = 113.550, PTRP = . 188930508E-06

DCRT = 3.8600, TCRT = 408.000, PCRT = 36.548852487

AL = 1.000, BE = .500, GA = .300

OE = .667, EP = 3.000, ER = 0.000, IX = 4 05165511088

.42083144154

MOL/L TSAT

.5 344.238

1.0 374.282

1.5 390.092

2.0 399.151

2.5 404.322

3.0 406.982

3.5 407.920

4.0 407.996

4.5 407.686

5.0 406.394

5.5 403.568

6.0 398.797

6.5 391.795

7.0 382.375

7.5 370.424

8.0 355.886

8.5 338.751

9.0 319.060

9.5 296.923

10.0 272.535

10.5 246.189

11.0 213.260

11.5 189. 168

12.0 159.321

12.5 129.059

.62315236106

THETA

326. 175

362.046

382. 874

395.513

402.880

406.614

407.893

407.994

407.534

405.539

401.046

393.282

381.685

365.919

345.890

321.754

293.924

263.072

230.109

196. 147

162.410

130.124

100.384

74.036

51.616

0.00000000000

B .6132

.6577

.7051

.7558

.8098

.8674

.9289

.9946

1. 0646

1.1392

1.2189

1. 3039

1.3946

1.4914

1.5947

1. 7048

1.8223

1.9477

2.0815

2. 2242

2. 3765

2.5390

2. 7123

2.8973

3. 0946

0.00000000000

C -.36629

-.31139

-.25554

-.19845

-.14065

-.08404

-.03204

.01080

.04009

.05341

.05192

.04049

.02579

.01335

.00552

.00178

.00044

.00008

.00001

.00000

.00000

.00000

.00000

.00000

.00000

PSAT

11.193

20.264

26. 862

31.4 C2 34.3 08 35.911

36.498

36.546

36.351

35.549

33.867

31.212

27.668

23.454

18.867

14.246

9.933

6.243

3.415

1.544

.533

.124

.016

.0 01 .0 00

36
TABLE 6. Calculated P(p) critical isotherm

The following page gives a high-resolution examination of the critical

isotherm as computed by equation of state (6). Column headings have the

following interpretations —

D/DC

TS/TC

PS/PC

P/PC

DP/DR

d/dc, dens.ity reduced at the critical point.

To(p)/Tc, reduced coexistence temperature.

Pq(p)/Pc> t^educed coexistence pressure.

P/Pc> pressure reduced at the critical point.

3P/3p slope of the critical isotherm, bar.

The last five columns give the density-dependence of functions used in the

equation of state, where R e p e d/d^ is density reduced at the liquid triple

poi nt--

DTS/DR E dTo(p)/dp, K.

DTH/DR E de(p)/dp, K.

DPS/DR E dPo(p)/dp, bar.

DXB/DR E 9$(p,T)/9p.

DXC/DR E 9 4'(p,T)/9p.

Mote: p = d/d-f-, density reduced at the liquid triple-point.

37
THE

CRITICAL

ISOTHERM,

ISOBUTANE

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39
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Table 8. Comparisons with P-p-T data

I-BUTANE PVT DATA VS. EQUATION OF STATE.

IDVIRIAL, (2)BEATTIE. (3)M0RRIS, (4) SAGE/LACEY,

10

22

2

22

22

222

2

2

22

222

2

2

22

2

2

2

2

2

2

2

2

22

2

2

2

22

2

2

2

22

22

PN WT T,K MOL/L CALCD O.PCT PtBAR CALCO P.PCT

1 .990 423. 150 .9992 1.0017 -.25 26. 041 25.995 .17

2 .994 448. 15 0 .9992 1.0008 -.17 28.827 28.792 .12

3 .998 473.150 .9992 1.0000 -.08 31.542 31.524 .06

4 .997 498.150 .9992 1.0000 -.08 34.228 34.204 .07

5 .997 523.150 .9992 1. 0001 -.09 36.872 36.843 .08

6 .992 548.150 .9992 1.0009 -.17 39.507 39.448 .15

7 .997 573. 150 .9992 1.0002 -.10 42. 060 42.023 .09

8 .946 423. 150 1.4988 1.5115 -. 85 33.488 33.337 .45

9 .970 448.150 1.4988 1.5063 -.50 38.129 38.009 .31

10 .990 473. 150 1.4988 1.5022 -.23 42.617 42.550 .16

11 .992 498.150 1.4988 1.5016 -.19 47.055 46.989 .14

12 .991 523.150 1.4988 1.5016 -.19 51.422 51.346 .15

13 .986 548. 150 1.4988 1.5024 -.24 55.749 55.637 .20

14 .980 573. 150 1.4988 1.5032 -.30 60.025 59.872 .25

15 .966 423.150 1.9984 2.0155 -.86 38.341 38.208 .35

16 .987 448. 150 1.9984 2.0054 -.35 45.079 44.993 .19

17 .993 473. 150 1.9984 2.0024 -.20 51. 645 51.580 .13

18 .999 498.150 1.9984 1.9989 -.03 58.029 58.017 .02

19 1.000 523.150 1.9984 1.9978 .03 64.321 64.336 -.02

20 .999 548. 150 1.9964 1.9992 -.04 70.583 70.559 .03

21 .996 573. 150 1.9984 2.0005 -.11 76.774 76.702 .09

22 .997 423.150 2.4980 2.5054 -.30 41.432 41.394 .09

23 .999 448. 150 2.4980 2.4939 . 16 50.409 50.449 -.08

24 .991 473.150 2.4980 2.4887 . 37 59.133 59.267 -.23

25 .989 498. 150 2.4980 2.4892 . 35 67.746 67.913 -.25

26 .988 523.150 2.4980 2.4897 . 33 76.227 76.421 -.26

27 .996 548.150 2.4980 2.4933 . 19 84.687 84.819 -.16

28 1.000 573.150 2.4980 2.4965 . 06 93.077 93.124 -.05

29 .990 423. 150 2.9976 2.9717 .86 43.418 43.5 09 -.21

30 .978 448.150 2.9976 2.9765 .70 54.756 54.933 -.32

31 .967 473.150 2.9976 2.9781 .65 65.882 66. 141 -.39

32 .977 498.150 2.9976 2. 9835 .47 76.936 77.193 -.33

33 .984 523. 150 2.9976 2. 9872 .35 87.879 88.122 -.28

34 .996 548.150 2.9976 2.9928 . 16 98.812 98.949 -.14

35 1.000 573.150 2.9976 2.9973 .01 109.684 109.692 -.01

36 .954 423. 150 3.4972 3.4289 1.95 44.877 45.077 -.45

37 .943 448.150 3.4972 3.4607 1.04 58.687 58.981 -.50

38 .958 473. 150 3.4972 3.4742 .66 72.458 72.767 -.43

39 .986 498.150 3.4972 3.4859 .32 86.248 86.463 -.25

40 .997 523.150 3.4972 3. 4924 .14 99.967 100.086 -.12

41 .997 548. 150 3.4972 3.5008 -.10 113. 758 113.645 .10

42 .984 573. 15 0 3.4972 3.5059 -.25 127.467 127. 149 .25

43 .654 423.150 3.9967 3.8759 3. 02 46.204 46.535 -.82

44 .887 448.150 3.9967 3.9472 1.24 62.771 63.216 -.71

45 .960 473. 150 3.9967 3. 9755 .53 79.560 79.884 -.41

46 .998 498. 150 3.9967 3.9926 .10 96.482 96.571 -.09

47 .995 523. 150 3.9967 4.0024 -.14 113.423 113.263 .14

48 .960 548.150 3.9967 4.0119 -.38 130.486 129.953 .41

49 .914 573. 150 3.9967 4.0182 -.54 147.539 146.635 .61

50 .717 423. 150 4.4963 4.3512 3.23 47.825 43.422 -1.25

51 .818 448. 150 4.4963 4.4409 1.23 67.655 68.285 -.93

52 .954 473.150 4.4963 4.4763 .44 87.980 38.361 -.43

53 1.000 498. 150 4.4963 4.4981 -.04 108.620 108.574 .04

54 .970 523. 150 4.4963 4.5095 -.29 129,341 128.882 .35

55 .889 548.150 4.4963 4.5209 -.55 150.316 149.257 .70

40
Xable 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

<l»VIRIAL, (2)BEATTIE, (3)M0RRIS» (4) SAGE/L ACEY.

10 PN HT T,K MOL/L CALCO 0,PCT P,BAR CALCO P,PCT

2 56 .626 573.150 4.4963 4.5267 -.68 171.239 169.676 .91

2 57 .562 423.150 4.9959 4.8662 2.60 50 . 359 51.246 -1.76

2 58 .729 448. 150 4.9959 4.9406 1.11 74.312 75.217 -1.22

2 59 .926 473.150 4.9959 4.9742 . 44 98.964 99.532 -.57

2 60 1.000 498.150 4.9959 4.9950 .02 124. 042 124.077 -.03

2 61 .967 523.150 4.9959 5.0074 -.23 149 . 31

3

148.787 .35

2 62 .878 548.150 4.9959 5.0185 -.45 174. 877 173.614 .72

2 63 .800 573.150 4.9959 5.0255 -.59 200.472 198.524 .97

2 64 .312 423.150 5.9951 5.9150 1.34 63.916 65.853 -3.03

2 65 .453 448.15 0 5.9951 5.9374 .96 99.714 101.991 -2.28

2 66 .653 473.150 5.9951 5.9563 .65 136. 323 138.444 -1.56

2 67 .859 498.150 5.9951 5.9723 . 38 173.519 175.111 -.92

2 68 .959 523.150 5.9951 5.9819 . 22 210.807 211.922 -.53

2 69 .998 548. 15 0 5.9951 5.9944 .01 248.763 248.830 -.03

2 70 .324 423. 150 6.9943 6.9469 .68 106.073 111.413 -3.09

2 71 .585 448. 150 6.9943 6.9606 .48 162.566 165.664 -1.91

2 72 .764 473.150 6.9943 6.9686 . 37 217.058 219.970 -1.34

2 73 .966 498. 150 6.9943 6.9819 . 18 272.615 274.281 -.61

2 74 .842 423.150 7.9935 8.0007 -.09 227.687 226.464 .54

2 75 .761 440.150 7.9935 8.0057 -.15 307. 815 305.394 . 79

NP = 75» ONRMSPCT = .835, PMEANOIF = .459, PMEANPCT = .408

41
Table 8. Continued

I-0UTANE PVT DATA VS. EQUATION OF STATE.

(DVIRIAL, (2)BEATTIE, (3) MORRIS, ( 4) SAGE/L ACEY .

ID PN WT T,K MOL/L CALCO D.PCT P,8AR CALCD P,PCT

3 76 .000 310.928 9.2542 9.1987 .60 6.095 18.949- 174.04

3 77 .826 410.928 .2167 .2145 1.00 6.895 6.959 -.94

3 78 .926 444. 261 .1964 .1952 .61 6.095 6.935 -.58

3 79 .866 477.594 .1611 .1796 . 83 6.895 6.950 -.80

3 80 .872 510. 928 .1678 .1665 . 80 6.095 6.949 -.78

3 81 .001 310.928 9.2822 9.2308 .55 13.790 25.3 03 -83.49

3 82 .003 344.261 8.4098 8.3688 .49 13.79 0 18.901 -37. 07

3 83 .869 410.928 .4705 .4661 .94 13.790 13.900 -.80

3 84 .982 444.261 .4154 .4140 . 33 13.790 13.830 -.30

3 85 .916 477.594 .3776 .3750 .68 13.790 13.876 -.63

3 86 .902 510.928 .3466 .3441 . 72 13.790 13.083 -.68

3 87 .002 310.928 9.3420 9.2921 .53 27.579 39.437 -43.00

3 88 .010 344.261 8.5164 8.4756 . 48 27.579 33.279 -20.67

3 89 .159 377.594 7.3569 7.3336 .32 27.579 28.872 -4.69

3 90 .962 410.928 1.1951 1.2028 -.65 27.579 27.476 .37

3 91 .983 444. 261 .9589 .9619 -.31 27.579 27.516 .23

3 92 .998 477.594 .8296 .8301 -. 06 27.579 27.565 . 05

3 93 .999 510.928 . 7412 .7405 .10 27.579 27.603 -.09

3 94 .931 410.928 1.5570 1.5750 -1.16 31.716 31.550 .52

3 95 .945 410.928 1.7203 1.7402 -1.16 33.095 32.942 .46

3 96 .947 410.928 1.9178 1.9436 -1.35 34.474 34.317 .46

3 97 .970 444. 261 1.3180 1.3243 -.48 34.474 34.366 .31

3 98 .983 477.594 1.0962 1.0994 -.29 34.474 34.397 .22

3 99 .996 510.928 .9616 .9627 -.11 34.474 34.442 .09

3 100 .985 410.920 2.1959 2.2155 -.89 35.053 35.769 .23

3 101 .998 410.928 2.3923 2.4006 -.35 36.542 36.515 .07

3 102 .990 410.928 2.6939 2.6565 1.39 37.232 37.311 -.21

3 103 .959 410.928 3.2965 3. 1098 5. 66 37.921 38.080 -.42

3 104 .791 410.928 4.6318 4.2078 9.15 30.611 39.0 06 -1.02

3 105 .751 410.928 5.0016 4.8134 3.76 39.300 39.752 -1.15

3 106 .356 410.928 5.3203 5.0770 4.57 39.990 41.065 -2.69

3 107 .0 05 310.928 9.3994 9.3499 .53 41.369 53.702 -30.01

3 108 .024 344.261 8.6068 8.5714 .41 41.369 46.011 -13.16

3 109 .294 377.594 7.5711 7.5524 .25 41.369 42.729 -3.29

3 110 .149 410. 928 5.6243 5.3720 4.49 41.369 43.352 -4. 79

3 111 .987 444. 261 1.7814 1.7676 -.34 41.369 41.289 .19

3 112 .972 477.594 1.3982 1.4041 -.42 41.369 41.244 .30

3 113 .987 510.928 1.1990 1.2027 -.24 41.369 41.289 .19

3 114 .060 410.928 6.1791 5.9900 3. 06 40.263 52.111 -7.97

3 115 .986 444. 261 2.4260 2.4119 .58 48.263 48.396 -.27

3 116 .956 477.594 1.7396 1.7499 -.58 40.263 48.075 .39

3 117 .990 510. 928 1.4581 1.4612 -.21 48.263 40.104 .16

3 118 .009 310.928 9.4510 9.4047 .49 55.150 67.364 -22.13

3 119 .037 344. 261 8.6937 8.6587 .40 55.158 61.039 -10.66

3 120 .366 377.594 7.7435 7.7256 .23 55. 158 56.743 -2.87

3 121 .034 410.928 6.4921 6. 2999 2.96 55.158 61.122 -10.81

3 122 .955 444.261 3.3005 3.2663 1.04 55.158 55.406 -.45

3 123 .991 477.594 2.1364 2.1415 -.24 55.158 55.073 .15

3 124 .989 510.928 1.7344 1, 7383 -.23 55.158 55.062 .17

3 125 .765 444. 261 4.2438 4. 1666 1.02 62, 053 62. 736 -1.10

3 126 1.000 477.594 2.5828 2.5799 .11 62.053 6 2.0 97 -.07

3 127 .996 510.928 2.0309 2.0331 -.11 62.053 62.002 .08

3 128 .012 310.920 9.5031 9.4568 .49 68.948 81.777 -13.61

3 129 .049 344.261 8.7740 6.7369 .40 68.946 75.315 -9.24

3 130 .526 377.594 7.8853 7. 8707 GO • 68.948 70.447 -2.18

42
Table 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

(DVIRIAL, (2)BEATTIE, (3)M0RRIS, < 4 ) S AGE/L ACEY .

ID PN WT T,K MOL/L CALCD D.PCT P,BAR CALCO P.PCT

3 131 .182 410.928 6.7563 6.6904 .97 68.948 71.973 -4.39

3 132 .720 444.261 4.8820 4. 8187 1. 30 6 8.94 8 69.804 -1.24

3 133 .995 477.594 3.0642 3.0563 .26 68.948 69.059 -.16

3 134 1.000 510.928 2.3435 2.3435 -.00 68.948 68.947 .00

3 135 .016 310.928 9.5658 9.5186 .49 86.184 100.038 -16.07

3 136 .061 344. 261 8.8671 8.8311 . 41 86.184 93.331 -8.29

3 137 .714 377.594 8.0370 8.0258 .14 86.184 87.538 -1.57

3 138 .101 410.928 7.0955 7. 0145 1.14 86.184 91.505 -6.17

3 139 .377 444. 261 5.7655 5.6895 1.32 86.184 88.448 -2.63

3 140 1.000 477.594 4.1921 4.1928 -.02 86.184 86.172 .01

3 141 .998 510.928 3.1565 3. 1592 -. 09 86.184 86.127 .07

3 142 .023 310.928 9.6225 9.5770 .47 103.421 117.501 -13.61

3 143 .080 344.261 8.9506 8.9159 . 39 103.421 110.880 -7.21

3 144 .884 377.594 8.1680 8.1601 .10 103.421 104.512 -1.05

3 145 .364 410.928 7.2927 7.2562 .50 103.421 106.398 -2.88

3 146 .245 444. 261 6.2478 6.1666 1.30 103.421 107.171 -3.63

3 147 .962 477.594 4.9647 4.9794 -.30 103.421 103.016 .39

3 148 .961 510.928 3.9118 3.9290 -.44 103.421 103.002 .41

3 149 .030 310.928 9.6766 9.6325 . 46 120 .658 134.971 -11.86

3 150 .108 344. 261 9.0269 8.9945 . 36 120.658 1 26. 118 -6.18

3 151 .989 377.594 8.2834 8.2791 . 05 120 .658 121.328 -.56

3 152 .664 410. 928 7.4726 7.4518 . 28 120.658 122.690 -1.66

3 153 .277 444.261 6.5664 6.4996 1.02 120.658 124.755 -3.40

3 154 .992 477.594 5.4909 5.4949 -.07 120.658 120.499 .13

3 155 .928 510.928 4.5297 4.5510 -.47 120.658 119.985 .56

3 156 . 039 310.928 9.7278 9.6854 . 44 137. 895 152.314 -10.46

3 157 .115 344. 261 9.1014 9.0679 . 37 137. 895 146.156 -5.99

3 158 .980 377.594 8.3868 8.3862 .01 137. 895 137.997 -.07

3 159 . 924 410.928 7.6277 7.6172 . 14 137.895 139.076 -.86

3 160 .280 444.261 6.8198 6.7581 . 90 137.895 142.589 -3.40

3 161 .994 477.594 5.8661 5.8679 -.03 137.895 137.802 .07

3 162 .885 510.928 5.0016 5.0251 -.47 137. 895 136.923 .71

3 163 .051 310.928 9.7762 9.7360 .41 155.132 169.391 -9. 19

3 164 .147 344. 261 9.1680 9.1367 . 34 155.132 163.323 -5.28

3 165 .929 377.594 8.4823 8.4838 -.02 155.132 154.850 . 1 8 3 166 .994 410.928 7.7631 7.7614 .02 155.132 155.352 -.14

3 167 .276 444.261 7.0304 6.9709 . 85 155.132 160.510 -3.47

3 168 1.000 477.594 6.1639 6. 1602 . 06 155.132 155.381 -.16

3 169 .838 510.928 5.3679 5.3928 -.46 155.132 153.836 . 84

3 170 . 083 310.928 9.8179 9.7844 . 34 172.369 184.750 -7. 18

3 171 .201 344.261 9.2294 9.2016 .30 172. 369 180.056 -4.46

3 172 .836 37 7. 594 8.5693 8.5737 -.05 172.369 171.499 .50

3 173 .850 410.928 7.8830 7.8894 -. 08 172.369 171 .460 .53

3 174 .301 444.261 7.2068 7.1523 . 76 172.369 178.057 -3.30

3 175 .996 477.594 6.4076 6.4012 . 10 172.369 172.863 -.29

3 176 .915 510.928 5.6752 5.6898 -.26 172.369 1 71 . 445 .54

3 177 . 097 310.928 9.8636 9. 8309 . 33 189.606 202. 176 -6.63

3 178 .206 344.261 9.2916 9.2630 .31 189.606 197.943 -4.40

3 179 .741 377.594 8.6500 8.6571 -.08 189.606 188.102 .79

3 18 0 .637 410.928 7.9904 8.0049 -. 18 189.606 187.355 1.19

3 181 . 332 444.261 7.3608 7.3109 .68 189.606 195.493 -3.10

3 182 .995 477.594 6.6136 6.6070 .10 189.606 19 0.2 C8 -.32

3 183 .935 510.923 5.9279 5.9387 -. 18 189.606 138.800 .42

3 184 .123 310.928 9.9062 9.8756 .31 206. 943 219.023 -5.89

3 185 .245 344.261 9.3484 9.3214 . 29 206.843 215.095 -3.99

3 186 .610 377.594 8 . 7240 8. 7349 -.13 206.843 204.353 1.20

43
Table 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

(l)VIRIAL, (2)BEATTIEt (3)HORRIS, (4) SAGE/LACEY.

ID PN WT T,K MOL/L CALCO D.PCT P.BAR CALCO P.PCT

3 187 .530 410. 928 8.0913 6.1102 -.23 206.843 203.640 1.55

3 188 .557 444.261 7.4848 7.4520 . 44 206.843 211.122 -2.07

3 189 .995 477.594 6.7879 6.7867 .02 206.843 206.971 -.06

3 190 .984 510. 928 6.1502 6.1532 -.05 206.843 206.581 .13

3 191 .171 310. 928 9.9455 9.9187 .27 224.080 235.139 -4,94

3 192 .35 2 344. 261 9.3994 9.3770 .24 224.080 231.233 -3.19

3 193 .594 377.594 8.7964 8.8079 -.13 224.080 221.279 1.25

3 194 .421 410.928 8.1826 8.2071 -.30 224.080 219.589 2.00

3 195 .867 444.261 7.5962 7.5793 . 22 224.080 226.495 -1.08

3 196 .721 477.594 6.9261 6.9464 -.29 224.080 221.780 1.03

3 197 1.000 510.928 6.3456 6.3420 .06 224.080 224.431 -.16

3 198 .212 310.928 9.9851 9.9602 .25 241.316 251.926 -4.40

3 199 .514 344.261 9.4477 9.4302 .19 241.316 247.169 -2.43

3 200 .569 377.594 6.8643 8.8766 -.14 241,316 238.108 1.33

3 201 .396 410.928 8.2710 8.2970 -.31 241.316 236.203 2.12

3 202 .980 444.261 7.7045 7.6953 .12 241.316 242.741 -.59

3 203 .542 477. 594 7.0592 7.0903 -.44 241,316 237.438 1.61

3 204 .987 510.928 6.5197 6,5107 . 14 241.316 242.295 -.41

3 205 .230 310.928 10.0251 10.0004 .25 258.553 269.413 -4.20

3 206 .75 0 344.261 9.4933 9.4811 .13 258.553 262.785 -1.64

3 207 .517 377.594 8.9274 8.9420 -.16 258.553 254.632 1.52

3 208 .378 410.928 8.3537 8.3808 -.32 258.553 252.355 2.20

3 209 .958 444. 261 7.8004 7.8021 -.02 258.553 258.282 .10

3 210 .343 477.594 7.1731 7.2213 -.67 258.553 252.027 2.52

3 211 .993 510.928 6.6713 6.6633 .12 258.553 259.497 -.36

3 212 .288 310.928 10.0617 10. 0393 .22 275.790 285.943 -3.68

3 213 .881 344.261 9.5393 9.5300 .10 275.790 279.155 -1.22

3 214 .501 377.594 8.9886 9.0039 -.17 275.790 271.455 1.57

3 215 .350 410. 928 8.4304 8.4595 -.35 275.790 269.290 2.36

3 216 .915 444. 261 7.8966 7.9009 -. 06 275.790 275.007 .28

3 217 .313 477.594 7.2907 7.3415 -.70 275.790 263.336 2.70

3 218 .997 510. 928 6.8097 6. 8027 .10 275.790 276.695 -.33

3 219 .323 310.928 10.0966 10.0771 .21 293.027 303.100 -3.44

3 220 .989 344. 261 9,5824 9.5770 . 06 293. 027 295.063 -.69

3 221 .588 377.594 9.0506 9.0628 -.14 293.027 289.377 1.25

3 222 .369 410.928 8.5059 8.5336 -.33 293.027 286.462 2.24

3 223 .903 444.261 7.9881 7.9930 -.06 293.027 292.086 .32

3 224 .310 477.594 7.4024 7.4527 -.68 293.027 285.064 2.72

3 225 .997 510.928 6.9383 6.9311 . 10 293.027 294.038 -.34

3 226 .429 310.928 10.1320 10.1136 .18 310.264 319.098 -2.85

3 227 1.000 344.261 9.6259 9.6223 .04 310.264 311.685 -.46

3 228 .605 377.594 9.1074 9.1191 -.13 310.264 306.603 1.18

3 229 . 389 410.928 8.5773 8.6036 -.31 310.264 303.684 2.12

3 230 .764 444.261 8.0676 8.0792 -.14 310.264 307.880 .77

3 231 .315 477.594 7.5072 7.5560 -.65 310.264 301.977 2.67

3 232 .990 510.928 7.0592 7.0500 .13 310.264 311.641 -.44

3 233 .514 310.928 10.1656 10.1492 .16 327.501 335.643 -2.49

3 234 .849 344. 261 9.6630 9.6659 -.03 327.501 326.334 .36

3 235 .624 377.594 9.1619 9. 1731 -.12 327.501 323.867 1.11

3 236 .401 410.928 8.6446 8.6701 -.30 327.501 320.780 2.05

3 237 .658 444. 261 8.1439 8.1603 -.20 327.501 323.925 1.09

3 238 .270 477.594 7.5983 7.6526 -.71 327.501 317.673 3.00

3 239 1.000 510.928 7.1656 7.1608 . 07 327.501 328,273 -.24

3 240 .727 310.928 10.1957 10.1837 . 12 344.738 350.825 -1.77

3 241 .666 344.261 9.7004 9.7082 -.08 344.738 341.540 .93

3 242 .6 36 377.594 9.2140 9.2248 -.12 344.738 341,065 1.07

44
Table 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

(l)VIRIAL, (2>BEATTIE, (3)MORRIS, < 4) S AG E/L A CEY

.

10 PN MT T,K MOL/L CALCO 0,PCT P,BAR CALCO P.PCT

3 243 .439 410.929 8.7102 8.7334 -.27 344.738 3 38. 313 1.86

3 244 .628 444.261 8.2192 8.2370 -.22 344.738 340.657 1.18

3 245 .200 477.594 7.6766 7.7432 -.87 344.738 331.965 3. 71

3 246 .962 510.928 7.2619 7.2645 -. 04 344. 738 344.288 .13

NP = 171, DNRMSPCT = 1. 485, PMEANOIF = 1.667, PMEANPCT = .934

45
Table 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

(l)VIRIAL, <2)BEATTIE, (3)M0RRIS, (i* ) SAGE/L ACEY .

ID PN HT t.k MOL/L CALCD DtPCT P.BAR CALCD P.PCT

k 247 1.000 294.261 .0287 . 0287 .03 .689 .690 -. 03

4 248 .999 310.928 .0271 .0271 .07 .689 .690 -.07

4 249 .992 327.594 .0257 . 0256 .18 .689 .691 -.18

4 250 .985 344. 261 .0244 . 0243 . 25 .689 .691 -.25

4 251 .984 360.928 .0232 .0232 .26 .689 .691 -.26

4 252 .977 377.594 .0222 . 0221 .31 .689 .692 -.31

4 253 .970 394.261 .0213 .0212 .36 .689 .692 -.36

4 254 .996 294.261 .0425 .0425 .13 1.013 1.015 -.13

4 255 .989 310.928 .0401 . 0400 .22 1.013 1.015 -.21

4 256 .976 327.594 .0380 . 0379 .32 1.013 1.016 -.32

4 257 .965 344. 261 .0361 .0359 .39 1.013 1.017 -.39

4 258 .952 360.928 .0343 .0 342 .46 1.013 1.018 -.45

4 259 .939 377. 594 .0328 . 0326 .52 1.013 1.018 -.52

4 260 .929 394.261 .0314 .0312 .56 1.013 1.019 -.56

4 261 .987 294.261 .0584 .0583 .24 1.379 1.382 -.23

4 262 .978 310.928 .0550 .0549 .31 1.379 1.383 -.30

4 263 .956 327.594 .0521 . 0518 .44 1.379 1.385 -.44

4 264 .933 344.261 .0494 .0491 .55 1.379 1.386 -.54

4 265 .909 360.928 .0470 .0467 .64 1.379 1.388 -.64

4 266 .889 377.594 .0449 .0446 .72 1.379 1.389 -.71

4 267 .876 394.261 .0429 .0426 . 76 1.379 1.389 -.76

4 268 .936 294. 261 .0896 . 0891 .56 2.068 2.079 -.53

4 269 .924 310.928 .0840 .0835 .60 2.068 2.080 -.58

4 270 .890 327.594 .0793 .0787 .73 2.068 2.083 -.71

4 271 .848 344.261 .0751 . 0745 .88 2.068 2.086 -.86

4 272 .817 360.928 .0714 . 0707 .97 2.068 2.088 -.96

4 273 .786 377.594 .068 0 .0673 1.06 2.068 2.090 -1.05

4 274 .762 394. 261 .0650 . 0643 1.13 2.068 2.092 -1.13

4 275 .833 294.261 .1225 .1214 .97 2.758 2.783 -.90

4 276 .847 310.928 .1143 .1133 .91 2.75 8 2.782 -.86

4 277 .817 327.594 .1074 . 1064 1.00 2.75 8 2.784 -.95

4 278 .782 344.261 .1015 .1004 1.10 2.758 2.787 -1.07

4 279 .732 360.928 .0963 .0951 1.25 2.758 2.792 -1.22

4 280 .698 377.594 .0917 . 0904 1.35 2.758 2.794 -1.33

4 281 .672 394. 261 .0875 . 0862 1.42 2.75 8 2.797 -1.41

4 282 .760 310.928 .1460 .1442 1.22 3.44 7 3.486 -1.13

4 283 .746 327.594 .1366 .1349 1.25 3.447 3.488 -1.17

4 284 .699 344.261 .1288 .1270 1.39 3.447 3.493 -1.32

4 285 .653 360 . 928 .1219 .1201 1.52 3.44 7 3.498 -1.47

4 286 .627 377.594 .1158 .1140 1.60 3.447 3.501 -1.55

4 287 .611 394.261 .1104 .1086 1.64 3.44 7 3.503 -1.61

4 288 .664 310.928 .1793 .1765 1.58 4.137 4.196 -1.43

4 289 .684 327.594 .1669 .1645 1.48 4.137 4.193 -1.37

4 290 .651 344.261 .1568 .1543 1.57 4.137 4.198 -1.47

4 291 .603 360.928 .1482 .1456 1.71 4.137 4.2 04 -1.63

4 292 .585 377.594 .1405 .1380 1.76 4.137 4.207 -1.70

4 29 3 .555 394. 261 .1337 .1312 1.85 4.137 4.211 -1.80

4 294 .576 327.594 .2315 .2270 1.94 5.516 5.611 -1.72

4 295 .580 344.261 .2156 .2116 1.88 5.516 5.610 -1.71

4 296 .55 0 360.928 .2026 .1986 1.96 5.516 5.616 -1.82

4 297 .530 377.594 .1913 .1875 2.01 5.516 5.621 -1.90

4 298 .502 394.261 .1816 .1778 2.10 5.516 5.626 -2.01

4 299 .510 327. 594 . 3021 . 2951 2.33 6. 895 7.030 -1.96

4 300 .530 344.261 .2787 .2727 2.16 6.895 7.025 -1.89

4 301 .524 360 .928 .2600 .2545 2.12 6.895 7.027 -1.92

46
Table 8. Continued

I-BUTANE PVT DATA VS. EQUATION OF STATE.

<UVIRIAL» I2IBEATTIE, <3»HORRIS, U ) SAGE/LACEY.

10 PN HT T,K MOL/L CALCD 0,PCT P.8AR CALCC P,PCT

k 302 .512 377.594 .2444 .2392 2.13 6.895 7.030 -1.97

4 303 .486 394. 261 .2311 . 2260 2.21 6.895 7.038 -2.0 7 4 304 .508 344.261 .3646 .3559 2.39 8.618 8.789 -1.96

4 305 .507 360. 928 .3368 .3291 2.29 8.618 8.789 -1.98

4 306 .510 377.594 .3142 .3072 2.22 8.618 8.789 -1.98

4 307 .488 394.261 .2956 .2889 2.26 8.618 8. 796 -2.07

4 308 .522 344. 261 .4606 .4491 2.50 10.342 10.540 -1.92

4 309 .506 360.928 .4203 .4101 2.42 10.342 10.548 -1.99

4 310 .521 377.594 .3886 .3799 2.26 10.342 10.542 -1.93

4 311 .513 394.261 .3633 .3553 2.22 10 . 342 10.546 -1.97

4 312 .563 360.928 .5112 .4994 2. 30 12.066 12.279 -1.77

4 313 .567 377.594 .4681 .4580 2.15 12.066 12.279 -1.76

4 314 .609 394.261 .4337 .4254 1.90 12.066 12.261 -1.62

4 315 .678 360.928 .6117 .5998 1.96 13. 790 13.980 -1.38

4 316 .632 377.594 .5537 .5427 1.99 13. 790 14.002 -1.54

4 317 .564 394. 261 .5111 .5001 2.16 13.790 14.035 -1.78

4 318 .826 360.928 .7264 .7158 1.45 15.513 15.656 -.92

4 319 .682 377.594 .6481 .6359 1.89 15.513 15.727 -1.38

4 320 .601 394.261 .5924 .5800 2. 09 15.51

3

15.769 -1.65

4 321 .000 294. 261 9.6766 9.6092 . 70 17.237 36.412- 111.24

4 322 .001 310.928 9.2916 9.2465 . 49 17.237 27.468 -59.36

4 323 .002 327.594 8.8900 8.8483 .47 17.237 24.560 -42.49

4 324 .004 344.261 8.4407 8.3967 .52 17.237 22.9 04 -32.88

4 325 .0 37 360.928 7.8762 7. 8549 .27 17.237 19. 013 -10.30

4 326 .686 377.594 .7552 .7400 2.02 17.237 17.472 -1.36

4 327 .616 394. 261 .6808 .6663 2.13 17.237 17.513 -1.60

4 328 .705 377.594 .8780 .8593 2. 13 18.961 19.207 -1.30

4 329 .605 394.261 .7783 . 7604 2.30 18.961 19.271 -1.64

4 330 .773 377.594 1.0222 1. 0013 2. 05 20 . 684 20.909 -1.09

4 331 .609 394.261 .8859 . 8643 2.44 20.684 21.020 -1.62

4 332 .730 394.261 1.1407 1.1152 2.23 24.132 24.429 -1.23

4 333 .989 394.261 1.4737 1.4815 -.53 27.579 27.523 .20

4 334 .001 294.261 9.7347 9.6700 . 66 34.474 53.952 -56.50

4 335 .004 310.928 9.3674 9.3214 .49 34.474 45.694 -32.55

4 336 .007 327.594 8.9886 8.9438 . 50 34.474 43.147 -25.16

4 337 .010 344.261 8.5720 8.5247 .55 34.474 41.453 -20.25

4 338 .219 360.928 8.0558 8.0424 .17 34.474 35.854 -4.00

4 339 . 061 377.594 7.4929 7.4505 .57 34.474 37.238 -8.02

4 340 .051 394.261 6.7021 6.5999 1.53 34.474 37.458 -8.66

4 341 .003 294.261 9.7935 9.7275 .67 51.71

1

72.692 -40.57

4 342 .008 310.928 9.4380 9.3913 .50 51.711 63.893 -23.56

4 343 .012 327.594 9.0774 9.0309 .51 51.711 61.513 -18.96

4 344 .020 344.261 8.6827 8.6376 .52 51. 711 59.176 -14.44

4 345 .118 360.926 8.2217 8. 1972 .30 51.711 54.702 -5.79

4 346 .078 377.594 7.7283 7.6854 .55 51. 711 55.394 -7.12

4 347 .101 394. 261 7.1120 7.0520 . 84 51. 711 54.874 -6.12

4 348 .004 294. 261 9.8460 9. 7820 .65 68.948 90.287 -30.95

4 349 .012 310. 928 9.5031 9.4568 . 49 68.948 81.777 -18.61

4 35 0 .017 327.594 9.1588 9.1113 .52 68.948 79.791 -15.73

4 351 .036 344.261 8.7795 8.7389 .46 68.948 76.352 -10.74

4 352 .206 360.928 8.3512 8.3302 . 25 68.948 71. 885 -4.26

4 353 .110 377.594 7.9102 7.8707 .50 68.946 73.073 -5.98

4 354 .129 394. 261 7.3885 7.3371 . 69 68.948 72.686 -5.42

4 355 .007 294.261 9.8955 9.8340 .62 86.184 107.660 -24.92

4 356 .016 310. 928 9.5658 9.5186 .49 86.184 100.038 -16.07

4 357 .028 327.594 9.2294 9.1859 .47 86.184 96.792 -12.31

47
Table 8. Continued

i-butane pvt data vs. equation of state.

(1)VIRIAL» (2IBEATTIE, (3»MORRIS, («) SAGE/LACEY.

ID PN HT t,k MOL/L CALCO D,PCT P,BAR CALCO P,PCT

4 358 .052 344.261 8.8700 8.8311 .44 86.184 93.908 -8.96

4 359 .136 360.928 8.4771 8.4475 .35 86.184 90.853 -5.42

4 360 .319 377.594 8.0488 8.0258 .29 86.184 88.971 -3.23

4 361 .182 394. 261 7.5962 7,5535 .56 86.184 90.070 -4.51

4 362 .008 294.261 9.9491 9.8836 .66 103.421 127.350 -23.14

4 363 .023 310.928 9.6225 9.5770 .47 103.421 117.501 -13.61

4 364 .052 327.594 9.2916 9.2557 . 39 103.421 112.735 -9.01

4 365 .080 344. 261 8.9506 8.9159 . 39 103.421 110.880 -7.21

4 366 .185 360.928 8.5800 8.5528 .32 103.421 108.168 -4.59

4 367 .495 377.594 8 .1777 8.1601 .22 103.421 105.355 -2.35

4 368 .264 394.261 7.7653 7.7305 .45 103.421 107.177 -3.63

4 369 .009 294.261 9.9996 9.9312 .68 120 .658 146.791 -21.66

4 370 .026 310.928 9.6800 9.6325 .49 120.658 136.097 -12.80

4 371 .061 327. 594 9.3579 9.3213 . 39 120.658 130.725 -8.34

4 372 .078 344.261 9.0328 8.9945 .42 120.658 129.507 -7.33

4 373 .226 360. 928 8.6745 8.6485 . 30 120.65 8 125.609 -4.10

4 374 .256 377.594 8.3084 8.2791 . 35 120.658 125.212 -3.77

4 375 .517 394.261 7.9033 7.8815 .28 120.658 123.364 -2.24

4 3 76 .009 294. 261 10.0507 9.9768 .74 137.895 167.316 -21.34

4 377 .029 310.928 9.7347 9.6854 .51 137.895 154.700 -12.19

4 378 .076 327.594 9.4187 9.3832 . 38 137. 895 148.186 -7.46

4 379 .096 344. 261 9.1044 9.0679 .40 137.895 146.911 -6.54

4 380 .245 360.928 8.7628 8.7365 . 30 137.895 143.312 -3.93

4 381 .445 377.594 8.4073 8.3862 .25 137.895 141.488 -2.61

4 382 .626 394.261 8.0323 8.0138 .23 137. 895 140.479 -1.87

4 383 .011 294. 261 10.0949 10.0207 . 74 155.132 185.819 -19.78

4 384 .032 310.928 9.7866 9.7360 .52 155.132 173.167 -11.63

4 3 85 .069 327.594 9.4770 9.4419 .37 155.132 165.838 -6.90

4 386 .147 344.261 9.1680 9.1367 .34 155.132 163.323 -5,28

4 387 .387 360.928 8.8387 8.8181 .23 155.132 159.691 -2.94

4 388 .515 377.594 8.5032 8.4838 .23 155.132 158.739 -2.33

4 389 .773 394.261 8.1463 8. 1320 . 18 155.132 157.347 -1.43

4 390 .013 294. 261 10.1357 10.0629 .72 172.369 203.553 -18.09

4 391 .035 310.928 9.8355 9.7844 .52 172.369 191.353 -11.01

4 392 .100 327.594 9.5327 9.4978 . 37 172. 369 133.567 -6.50

4 393 .201 344.261 9.2294 9.2016 .30 172.369 180.056 -4.46

4 394 .360 360.928 8.9159 8.8941 .24 172.369 177,516 -2.99

4 395 .613 377.594 8.5907 8.5737 .20 172.369 175.784 -1.98

4 396 .968 394.261 8.2389 8.2390 -.00 172,369 172.345 .01

4 397 .016 294.261 10.1731 10.1037 .68 189.606 220 .346 -16.21

4 398 .047 310.928 9.8778 9. 8309 . 47 189.606 207.709 -9.55

4 399 .136 327.594 9.5824 9.5511 .33 189.606 200.116 -5.54

4 400 .206 344.261 9.2916 9,2630 . 31 189.606 197.943 -4.40

4 401 .443 360.928 8.9856 8.9654 . 22 189.606 194.682 -2.68

4 402 .526 377.594 8.6773 8.6571 .23 189.606 193.970 -2.30

4 403 .893 394. 261 8.3335 8.3370 -.04 189.606 188.977 .33

4 404 .019 294.261 10.2108 10.1431 .66 206. 843 237.804 -14.97

4 405 .042 310. 928 9.9276 9. 8756 .52 206.843 227.732 -10.10

4 406 .127 327.594 9.6360 9.6020 . 35 206.843 218.759 -5.76

4 407 .120 344.261 9.3611 9.3214 .42 206.343 219.049 -5.90

4 408 .443 360.928 9.0535 9.0327 . 23 206.843 212.395 -2.68

4 409 .934 377.594 8.7433 8. 7349 .10 206. 843 208.782 -.94

4 410 .779 394.261 8.4201 8.4274 -.09 206. 843 205.400 .70

NP = 164, DNRMSPCT = 1. 727, PMEANOIF = .873, PMEANPCT = 1.461

NP = 246, ONRMSPCT = 1. 268, PHEANOIF = 1.189, PMEANPCT = .726

48
Table 9. Comparisons with data for ideal gas functions

I-BUTANE IDEAL GAS FUNCTIONSt JOULES , MOL ES, KELVINS

t,k HZ-HZZ CALCO PCNT sz CALCD PCNT CPZ CALCO PCNT

50.00 1674.4 1660.5 . 63 194.012 193.76 2 . 12 34.81 34 . 80 .04

100. 00 3699.1 3704.2 -.14 221.585 221.608 -.01 47.28 47.28 -.01

150.00 6398.4 6399.3 -.01 243.258 243.283 -.01 60.29 60 . 30 -.01

200.00 9702.7 9704.5 -.02 262.211 262.221 -.00 71.84 71 . 82 .0 3 273,15 15603,5 15603.7 -.00 287.190 287.212 -.01 89.91 89 . 93 -.02

298.15 17936,0 17935.7 . 00 295.390 295.377 . 00 96.65 96.67 -.02

300.00 18115.0 18115.0 -.00 295.976 295.976 -.00 97.15 97.17 -.02

400.00 29201.0 29201.8 -.00 327.691 327.683 . 00 124.43 124. 40 .02

500,00 42913.2 42909.0 .01 358.192 358.166 . 01 149. 24 149.17 .05

600.00 58924.1 58916.2 .01 387.313 387.292 . 01 170.37 170. 39 -.01

700.00 76681,0 76879.4 .00 414.927 414.947 -.00 188.28 188. 38 -.05

600.00 96496.4 96503.6 -.01 441.119 441.129 -. 00 203.64 203. 71 -.0 4 900.00 117539.4 117549,7 -.01 465.888 465.902 -.00 216.94 216. 89 .02

1000.00 139825.1 139824.3 .00 489.361 489.360 .00 228.45 228.34 .04

1100.00 163182.

7

163171,7 .01 511.620 511.605 . 00 238.49 238. 39 .04

1200.00 187476,7 187463.9 .01 532.749 532.736 . 00 247.15 247. 28 -.05

49
Table 10. Interpolated ideal gas functions

I-BUTANE ideal GAS FUNCTIONS. JOULE S , MOLES , KEL VI NS

T.K EZ-EZZ HZ-HZZ SZ CVZ CPZ

110.0 3275.8 4190.4 226.239 41.64 49,95

120.0 3705.6 4703.

3

230 .700 44. 32 52.63

130.0 4162.0 5242.9 235.018 46.96 55.27

140.0 4644.5 5808.5 239.208 49.52 57.83

150.0 5152.1 6399.3 243.283 51.98 60.30

160.0 5683.8 7014.2 247.251 54. 36 62.67

170.0 6239.0 7652.5 251.120 56.67 64.99

180.0 6817.2 8313.8 254. 899 58.95 67.26

190.0 7418.0 8997.7 258.596 61.22 69.53

200.0 8041.6 9704.5 262. 221 63.50 71.82

210.0 8688.1 10434.

2

265. 780 65.82 74.13

220.0 9358.1 11187.3 269.283 68.18 76.50

230.0 10051.9 11964.2 272.737 7 0.59 78.91

240.0 10770.2 12765.6 276.147 73. 06 81.38

250.0 11513.4 13592.

0

279.520 75.59 83.90

260.0 12282.1 14443.3 282.861 78. 16 86.48

270.0 13076.8 15321.7 286.173 80.78 89.10

280.0 13397.9 16225.9 289.462 83.44 91.76

290.0 14745.8 17157.0 292. 728 86. 14 94.45

300.0 15620.7 18115.

0

295.976 88.86 97.17

310.0 16522.9 19100.4 299. 2 07 91.59 99.91

320.0 17452.6 20113.2 302.422 94. 34 102.66

330.0 18409.8 21153.6 305,623 97.10 105.41

340.0 19394.5 22221.

4

308. 811 99.85 108.16

350.0 20406.3 23316.6 311.936 102. 60 110. 91 360.0 21446.4 24439.6 315.149 105.33 113.65

370.0 22513.4 25589.7 316.300 108. 05 116.37

380.0 23607.4 26766.

9

321.439 110. 75 119.07

390.0 24728.4 27971.0 324.567 113.43 121.75

400.0 25876.0 29201.8 327,683 116. 09 124.40

410.0 27050.0 30459.

0

330.737 118.71 127.03

420.0 28250.2 31742.3 333.879 121.31 129.62

430.0 29476.

1

33051.4 336.959 123. 87 132.19

440 .

0

30727.5 34335.9 340. 027 126.40 134.72

45 0.0 32004.1 35745.6 343.033 128.90 137.22

460.0 333 05.5 37130.1 346.126 131.36 139.66

470.0 34631.3 38539.1 349.156 133.79 142.11

480.0 35981.2 39972,1 352.173 136. 18 144.50

490.0 37354.8 41428.9 355.176 138. 54 146. 85 500.0 38751.8 42909.0 358.166 140.85 149.17

510.0 40171.7 44412.1 361.143 14 3. 14 151.45

520.0 41614.4 45937.

9

364. 106 145. 38 153.70

530.0 43079.3 47485.9 367. 054 147.59 155.91

540.0 44566 • 1 49055.9 369.989 149.76 158.08

550.0 46074.4 50647.4 372.909 151.90 160.22

560.0 47604.0 52260.1 375.815 154. 01 162.32

570 .0 49154.4 53893.

7

373.706 156.07 164.39

580.0 50725.4 55547.

8

381.583 158. 11 166.42

590.0 52316.5 57222.1 384.445 160.11 168.42

600.0 53927.5 58916.2 387,292 162. 08 170.39

610.0 55557.9 60629.6 390.125 164. 01 172. 33 620.0 57207.6 62362.6 392.942 165. 92 174.23

630.0 58876.2 64114.3 395. 745 167. 79 176.10

640.0 60563.3 65884.6 398.533 169.63 177.94

650.0 62268.7 67673.1 401. 3 06 171.44 179.76

660.0 63992.0 69479.6 4 0 4.0 64 173.22 181.54

670.0 65733.0 71303.7 406.8 07 174.98 183.29

630.0 67491.4 73145.3 409.5 35 176.70 165.01

690.0 69266.9 75004.0 412.248 178.40 18 6, 71 700.0 71059.

3

76879.4 414.947 180.07 188.36

50
Table 11. Specific heats for saturated liquid at

I-gUTa^f: C2AT, J/'^OL/^

.qSCSOlOO&LfOS .?^'5Geril7E + G2 .29 365 32?7-:t03

-. 7 00483251 F-t-03 . 6 3S 09 74 7 2E G 3 0.

10 WT T,K J/90L/K CALCC PCNT

1 . 964 120.000 103.29 100.21 . 08

1 . 943 13C. OGG 1C1.59 101.58 .01

1 .920 1 4 0 . 0 G 3 103.09 103.19 -. 13

1 .395 150.000 104.81 104.95 -.13

1 .367 16G . 00 0 106.78 106.80 - . 03

1 .836 170. OGO 10 8.91 108.71 . 1

= 1 .801 1=0.300 110.85 110.64 .21

1 . 761 190. 000 112.72 112.60 .10

1 .717 200.000 114.35 114.59 -.21

1 .665 210. JOO 116.36 116.65 - . 25

1 .60-. 220 . OGO 113.70 118.53 - . 11

1 .538 230.300 121.29 121.20 . 08

1 . 499 240.000 124.31 123.84 . 37

1 .3 68 250.000 127.11 126.88 . 18

1 .264 260. 30

J

129.70 130. 42 - . 55

NP = 15, R:iS=>CT = .18

51
Table 12. Estimated coexistence data at T<T

b I-3UTANE ESTIM AND QVAP, 1KJ/MOL.

TB = 261.40000 . PB = 1.01325, OB = .048942

EZB =12391.8. EGB =12136. 6, HZB = 14565.2, HGB = 14206.9

SZ8 = 283.3260 , SG3 = 282 .3403, QB = 21297.

0

T,K 100/T P,EQN P,BAR LN<P) MOL/L Q,EQN Q, VAP

113.55 .88067 .33889E-06 .18892E-06 -15.48194 . 20010E-07 28.208 28.208

115.00 .86957 .48127E-06 . 27523E-06 -15.10568 .28784E-07 28.139 28.138

120.00 .83333 .15070E-05 .93316E-06 -13. 88469 .93527E-07 27.901 27.898

125.00 .80000 .42873E-05 . 28423E-05 -12. 77089 .27348E-06 27.666 27.662

130.00 .76923 .11206E-04 .78778E-05 -11.75146 .72884E-06 27.434 27.429

135.00 .74074 .27169E-04 . 20085E-04 -10. 81552 .17894E-05 27.204 27.199

140.00 .71429 .61589E-04 .47552E-04 -9.95368 .40852E-05 26.976 26.971

145.00 .68966 .13147E-03 .10538E-03 -9.15 797 . 87409E-05 26.750 26.745

150.00 .66667 .26585E-03 . 22007E-03 -8. 42156 .17647E-04 26.526 26.521

155.00 .64516 .51201E-03 .43578E-03 -7.73838 . 33818E-04 26.303 26.298

160.00 .62500 .94348E-03 .82241E-03 -7.10327 .61834E-04 26.081 26.076

165.00 .60606 .16702E-02 . 14861E-02 -6.51163 . 10836E-03 25.859 25.855

170.00 .58824 .28507E-02 .25815E-02 -5.95939 .18273E-03 25.638 25.634

175.00 .57143 .47061E-02 .43261E-02 -5. 44309 .29756E-03 25.418 25.414

180.00 .55556 .75357E-02 .70164E-02 -4.95950 .46938E-03 25.197 25.194

185.00 .54054 . 11734E-01 .11044E-01 -4.50504 . 71922E-03 24.976 24.974

190.00 .52632 .17806E-01 .16915E-01 -4. 07955 . 10732E-02 24. 755 24.754

195.00 .51282 .26339E-01 .25263E-01 -3.67841 .15632E-02 24.532 24.532

200.00 .50000 . 38263E-01 .36870E-01 -3. 30036 . 22267E-02 24.308 24.310

205.00 .48780 .54369E-01 .52675E-01 -2.94362 .31077E-02 24.083 24.086

210.00 .47619 .75822E-01 .73795E-01 -2. 60646 . 42569E-02 23.856 23.861

215.00 .46512 . 10392E+00 . 10153E+00 -2. 28745 .57314E-02 23.627 23.633

220.00 .45455 .14015E4-00 .13736E+00 -1.98517 .75 954E-02 23.395 23.402

225.00 . 44444 .18620E+00 .18297E<-00 -1. 69043 .99193E-02 23.160 23.168

230.00 .43478 .24394E+00 .24025E+00 -1.42609 . 12781E-01 22.923 22.931

235.00 .42553 .31545E+00 . 31127E+00 -1. 16 709 . 16265E-01 22.681 22.688

240.00 .41667 .40299E+00 .39831E+00 -.92052 .20463E-01 22.436 22.440

245.00 .40816 .5 0899E + 00 .50383E*00 -.68551 .25472E-01 22.187 22.186

250.00 .40000 .63607E+00 .63044E+00 -.46134 .31397E-01 21.933 21.925

255.00 .39216 .78699E+00 .78097E+00 -.24722 . 38350E-01 21.673 21.656

260.00 . 38462 .96467E+00 . 95834E+00 -.04255 .46451E-01 21.408 21.377

52
Table 13. The heats of vaporization

I-3UTANE QVAP, E = .A'JO, ')T<?o = 2b. 20^

(l)ASTON,(2)OANA,(3) DAS/KULCOR , ( 4) OAS/REtO/E UEA NK

,

(5) HANSON, (6) SAGE/LACEY, (40 ) ThERMALOOPS , ( 4 1 > CL AFEYRON

.

.11726829E+01 - . 2 39 249 06E + 0 0 265 0 199 7E- C

1

0 . 0 . 0 .

ID WT T,K K J/HOL CALC °CNT PESIO

.

40 1.000 113.550 26. 208 28.208 0. oc I 40 1.000 115.000 28 . 1 38 28.139 -.00 .9030E+30

40 .998 120.003 27.8 98 27. 9Cl - . 01 .91 Q5c + 0 3 40 .996 125.000 27. 662 27.666 -.01 .9214E+00

40 .995 130.000 27.429 27.434 -. 02 .93158+03

40 . 993 135.000 27.199 27.204 -.0 2 .9415E+00

40 .991 140. COO 26. 971 26.976 -.02 .95076+00

40 .989 145. COO 26.745 26.750 -.02 .9597-7+00

40 .987 150.000 26.521 26.526 -.02 .9686E+0

0

40 . 985 155. 000 26.2 98 26.3C3 -. 02 .9771E+00

40 .983 160.000 26. 076 26.081 -.02 .9»52E+00

40 .981 165.000 25.855 25 . 859 -.02 .9932E+0

0

40 .979 170. 003 25.634 25.636 - . 02 . lCOlE+01

40 .977 175.000 25.414 25.415 -.01 .1009E+01

40 .974 180.003 25.194 25.197 -.0 1 .1016E+01

40 .97 2 185.000 24.974 24.976 -.01 .1023E+C1

40 .969 190.000 24.754 24.755 -. 00 .10 31- + 01 40 . 966 195. 000 24.532 24.532 -.00 .1037E+01

40 . 963 200.030 24.310 24.303 .01 .1044E+01

40 .960 205.000 24.056 24.083 . 01 . 1C51E+01

40 .95 7 210.000 23.361 23.856 . 02 .1058^+31

40 . 954 215. COO 23.633 23.627 .03 . IG 64E + 0 1 40 .95 0 220 . COO 23.432 23.395 . 03 . 1070E+01

40 . 947 225.000 23.166 23.160 .03 .1075E+01

40 .943 230.000 22 .931 22.923 . 04 . 1C81E+ 01 40 .939 235.030 22.688 22.681 . 03 • 1086t+01

40 .935 240.000 22.440 22.436 .02 .1091F+01

5 . 931 244 . 261 22.157 22.224 - . 3C . 1 0 8 3 E + 0 1 40 .930 245.000 22.186 22.187 -.00 .1095F+01

40 .926 250.000 21 . 925 21 . 933 -.0 3 .1398E+01

40 . 921 255.000 21.656 21.673 -.0“ .11 02F+01

5 .920 255.372 21 .5 90 21.654 -.29 .1C95E+01

40 .915 260.000 21.377 21.408 -.15 .11 04E+01

3 .914 261.323 21.297 21 .337 -.19 .1104E+01

4 .914 261 . 320 21.297 21. 337 - . 1 = . 11 C4E + 0 1 1 . 914 261.440 21.295 21.331 - . 17 .1105E+01

5 . 903 266.433 20. 996 21. 055 -.28 .11 06E+01

2 .904 27C.000 20.232 20 .859 -.13 .11 136+01

3 .904 270 . 030 20 . 820 20 . 859 -.19 .Ill2t+Jl

4 . 90 4 270.000 20. 769 20. 359 -.4 3 .11 04E+01

5 . 394 277.594 20 .347 20.424 - . 33 . 1113E + 01

2 . 390 280.030 20.246 2C.282 -.18 .1120F+01

3 .890 260.000 20.251 20.282 - . 15 .11216+01

4 . 890 280. OOC 20 . 1 54 20.282 -.6 3 . 1107E+ 01

5 . 877 2 3 « . 7 0 6 l9.6o5 19.75^ -. 34 .11226+01

53
Table 13. Continued

I-BUTflNE QVAP, E = .450, QTRP = 28.208

ID WT t,k K J/MOL CALC PCNT REDID.

2 .875 290.000 19.627 19. 672 -.23 . 1127E+01

3 .375 290.000 19.627 19.672 -.23 .1127E+01

4 .875 290.000 19.535 19.672 -.69 .1114E+01

6 . 875 290.000 19.573 19.672 -.50 . 1119E+01

5 . 85 3 299.617 18.996 19.034 -.20 .1134E+01

2 . 85 7 300.000 18.970 19.022 -.27 .1132E+01

3 .857 300.000 18.970 19.022 -.27 .1132E+01

4 . 85 7 300.000 18.916 19. 022 -.56 . 1125E + 01

6 . 857 300.000 19.029 19.022 .04 .1140E+01

4 .837 310.000 18.292 18. 327 -.19 . 1141E+01

2 . 837 310.000 18.234 18.327 -.5 1 .1133E+01

3 .837 310.000 18.292 18. 327 -.19 .1141t+01

6 .837 310.000 16.350 18.327 . 29 .1152E+01

5 . 834 310.928 18.226 16.260 -.19 .1141E+01

2 .812 320.000 17.405 17.578 -.99 .1129E+01

3 .812 320.000 17.502 17.578 -.43 .1141E+01

4 . 81 2 320. 000 17.619 17.578 .23 . 11 56E + 01

6 .312 320.000 17.631 17.578 .30 .1157E+01

5 .806 322.039 17.361 17.418 -.33 .1144E+01

2 .782 330.000 16.535 16.765 -1.37 .1127E+01

3 . 782 330.003 16.698 16.765 -.40 .1147E+01

4 . 782 330.000 16.657 16. 765 .55 .11 67E+ 01

6 .782 330.000 16.315 16.765 . 30 .1162E+01

5 .771 333.150 16.415 16.494 -.45 .1147E+31

3 . 745 340.000 15.8 07 15.675 -.43 .1151E+01

4 . 745 340.000 16.008 15.875 . 64 .1176E+01

6 . 745 340.000 15.933 15.375 .37 .1167E+01

5 . 727 344.261 15.402 15.467 -.42 .1153E+01

3 .699 350. 030 14. S57 14. 3S8 -.21 .1159E+01

4 .699 350.000 15.046 14.888 1.06 .1183E+01

6 .699 350.000 14.954 14.,388 .44 .1171E+01

5 .66 8 355.372 14.294 14.309 -.11 .1163E+01

3 .639 360.000 13.782 13.779 .0? .1167E+01

4 .639 360.000 13.929 13.779 1. 09 .1185E+01

6 .639 360.000 13.811 13.779 . 23 .1170E+01

5 .539 366.483 12.934 12. 975 .07 . 1169E+01

3 .558 370.030 12.514 12.505 . 07 . 1170E+ 0

1

4 .558 370.000 12.615 12.505 . 88 .1163E+01

6 . 558 370.000 12.539 12.505 .27 .1173E+01

5 .47 8 377.594 11.335 11,386 -.45 .1163E+01

3 . 44 3 380.000 10.950 10.995 -.41 .1164E4-01

4 .44 i 380.000 10.979 10.995 -.15 . 1163E+- 0 1 6 .44 3 380.000 10.908 10.995 -.79 .1158E+01

4 . 376 385.000 10. C67 10.112 -.44 .11 65E+-01

6 .376 385.000 9.391 10.112 -2.18 . 11 39E+3

1

5 .316 388.706 9.255 9.378 -1.31 .1153E+01

3 . 294 390.033 8.970 9.102 -1.45 . 1151c-t-01

4 . 294 390 . 000 9.017 9.10 2 -.9 3 . 1158E+ 01

6 .294 390.000 8.778 9.102 -3.56 .1120E+01

4 . 2Q3 395.000 7.807 7. 906 -1.26 .1155E+01

5 .127 399.617 6.377 6.460 -1.29 .1155E+01

3 .125 430.000 6.2 76 6.396 -1.83 .1147E+01

4 . 125 4 0 C . 0 0 0 6.397 6.396 .01 .1173E+01

5 . 100 405.372 3.591 3.913 -.57 . 1166E + C1
Table 13. Continued

I-3UTANE QVAP, £ = .<«50, QTRP = 28.208

10 WT T,K kj/hol CALC PCNT PESI9.

41 1.000 115.000 28.131 28.139 -.02 .3175E+00

41 .996 125.000 27.666 27.666 .00 .9264E+00

41 .992 135.000 27.202 27.204 -.01 .9443E+00

41 . 98? 145.000 26.742 26.750 -.03 .9581E4-00

41 . 934 155. 000 26.288 26.303 -. 06 . 9723E+00

41 .979 165.000 25.839 25.359 -.08 .9372E+00

41 .974 175. 000 25.396 25.418 - . 09 . 1 0 32E4-01 41 . 968 185. 000 24. 956 24.976 -. 08 . 1013E4-31

41 . 962 195.000 24,519 24.532 -. 05 .1034E+01

41 . 95 6 205.000 24.084 24 . 083 . 0 1 . 1051E+0

1

41 .949 215.000 23.651 23.627 . 1 0 .1068E+01

41 .941 225.000 23.218 23. 160 . 25 . 1085E+01

41 .932 235.000 22.778 22.681 .43 .11 02E+01

41 .923 245.000 22.326 22.187 . 63 . 11 18E + 01 41 .912 255.000 21.351 21.673 .82 .1132F+01

41 .900 265.000 21 . 544 21.137 .98 .1144E+01

41 .886 275.000 20. 796 20. 575 1.07 . 11 53E + 0 1 41 . 370 255.000 20.199 19.981 1.09 . 1159E+01

41 . 852 295.000 19.550 19.352 1.02 . 11 62F+ 0 1 41 . 330 305.000 18.846 18.681 .89 .1164E+01

41 .805 315. 000 1 8. 0 86 17.960 .70 . 1164E+01

41 . 775 325.000 17.268 17.180 .51 . 11 64E+ 0 1 41 . 73 8 335. 000 16.387 16.331 . 34 .1165E+01

41 .69 3 345.000 15.433 15.395 .25 . 1166E+0 1 41 . 634 355.000 14.393 14.351 .29 .1170E+0

1

41 . 557 365. 0 0 0 13.240 13. 166 .56 .1177E+01

41 . 453 375.000 11.926 11 . 786 1.13 . 1189E+0

1

41 .307 385.000 10.353 10.112 2.3 8 .1207E+01

41 .115 395.000 6.287 7.906 4.81 .1239£t01

41 .00 0 405.000 4. 724 4.150 1 3. 85 . 1347E+ 01

NP = 129, PMSPCT =
Table 14. Comparisons with data for C (p,T)

P

COMPARISON WITH ISOBUTANE CP OF SAGE/LACEY

T.K P,BAR MOL/L J/MOL/K CALC PC NT 294.261 0.000 0. 0 000 93.58 95.61 -2. 12 310.920 0.000 0.0000 95.96 100.16 -4. 19

327.594 0.000 0.0000 90.69 104.75 -5.79

344.261 0.000 0.0000 101.41 109.34 -7.25

360.928 0.000 0.0000 104.40 113.90 -0. 34

377.594 0.000 0.0000 107. 47 118.42 -9.25

394.261 0.000 0.0000 110. 77 122.88 -9. 85

294.261 1.013 .0425 94.75 97.05 -2.37

310.928 1.013 .0400 97.16 101.37 -4. 16 327.594 1.013 .0379 99.61 105. 70 -5. 83

344.261 1.013 .0359 102.43 110.22 -7. 06 360.928 1.013 .0342 105. 35 114.66 -8.12

377.594 1.013 .0326 108.41 119.08 -8.96

394.261 1.013 .0312 111. 72 123.46 -9.51

294.261 1. 379 .0583 95. 84 97.65 -1.85

310.928 1.379 .0549 97.54 101.86 -4.24

327.594 1.379 .0518 100.02 106.18 -5.80

344.261 1.379 .0491 102.80 110.56 -7. 02 360.928 1.379 .0467 105. 72 114.95 -8. 04

377.594 1.379 .0446 108.78 119.33 -8.84

394.261 1.379 .0426 112. 09 123.68 -9.37

294.261 2.758 . 1214 101.95 100.43 1.51

310.928 2.758 .1133 100. 75 104.01 - 3. 13

327.594 2.758 .1064 102.04 107.92 -5.44

344.261 2.758 .1004 104. 38 112.00 -6. 60 360.928 2.758 .0951 107.15 116.16 -7.76

377.594 2.758 .0904 110.14 120.36 -8.49

394. 261 2.758 . 0862 113.45 124.56 -8, 92

310.928 4.137 .1765 106.10 106.80 -.65

327.594 4. 137 .1645 104. 89 110.04 -4.68

344.261 4.137 .1543 106.30 113.68 -6.49

360.920 4.137 .1456 108. 73 117.54 - 7. 50

377.594 4.137 .1380 111. 63 121.51 -8. 14

56
Table 14. Continued

COMPARISON WITH ISOBUTANE CP OF SAGE/LACEY

T,K P,BAR MOL/L J/MOL/K CALC PCNT

394.261 4.137 .1312 114.91 125.54 -8.47

327.594 5.516 .2270 108.71 112.67 -3.51

344.261 5.516 .2116 108.66 115.67 -6. 06 360.928 5.516 .1986 110. 46 119.12 -7.27

377.594 5.516 .1875 113. 18 122.80 -7. 83 394.261 5.516 .1778 116.42 126.61 -8. 05 327.594 6.895 .2951 114. 11 116.06 -1. 69 344.261 6.895 .2727 111.50 116.06 -5.55

360.928 6.895 .2545 112.40 120.93 -7. 05 377.594 6.895 .2392 114.64 124.24 -7.57

394.261 6.895 .2260 118.02 127.78 -7.64

344.261 8.618 . 3559 115.93 121.86 -4. 87 360.928 8.613 .3291 115.15 123.64 -6.87

377.594 3.618 .3072 117. 05 126.30 -7.33

394.261 3.613 .2889 120.09 129. 42 -7.21

344.261 10.342 .4491 121. 52 127.13 -4.41

360.928 10. 342 .4101 118. 41 127. 03 -6. 78 377.594 10.342 .3799 119.46 128.74 -7. 21 394.261 10.342 .3553 122.28 131.29 -6 . 86 360.928 12.066 .4994 122.06 131.44 -7.14

377.594 12.066 .4580 122. 08 131.68 -7.29

394.261 12.066 .4254 124.59 133.44 -6.63

360.928 13.790 .5993 126. 46 137.53 -8.05

377.594 13.790 .5427 125.00 135.33 -7.63

394.261 13.790 .5001 126.99 135.95 -6. 59

360.928 15.513 .7153 132. 08 146.79 -10.02

377.594 15.513 .6359 128.28 140.00 -8. 37

394.261 15.513 .5600 129.52 138.94 -6.78

377.594 17.237 .7400 132.00 146. 28 -9.76

394.261 17. 237 .6663 132. 22 142.57 -7. 26

377.594 20.684 1.0013 142. 02 170.06 -16. 49

394.261 20.684 .8643 138. 36 152.89 -9.49

394.261 24.132 1.1152 146.40 171.98 -14. 87

NP = 66» RMSPCT = 7.41

57
Table

15.

Comparisons

of

functions

at T=

250

a.ocsjforofoPO<MCsj^T-«^fvj^ororofo^>ro I I I I I I I I I I I • I I • I I

OooOlfNW-J-(M-^’f0^rjvDoKiX>r^\I5CT'(\J

<OU?vDro«H«^N>N.^O(^CJvC^CTh..^(VJCSj

oCJoO^Jh-^J’N.orON.aCvIroiAKcOCT I |^^<\J<M(\irorOK>t£^vC«^vDvDad I I I I I « I I I I I I I I •

^O-J'OCVJN.vDOOCT«P0C3r^fVJTH-i’<a3Lr'^ ^c3 tf^(T'(r'ro^o^LfNtroK-ocoirii^'»Hj'

(/5 oifNro®Lf''C^^»^oo^vroo^ifNforwO'cr* I •••••«••••••••••••

t/)0(VJGO^vCO«^»*^OfMvDoOCD^fO^UNvD W I |^^r\jCVJf^l*OfOroif^vDvDv£)vCvDvO I I • I I I I I I I I I I I I o K

1^ • Z

fSJ oa M H

\0• >- o

ct o>

fO <x > o

IJ tl O< h*

N.

lU 9> O 00 «il» <3 z

C/0 I

:> 1 u. X o UJ w

t/i zo 00 M UJ th- z o D o z o a 3

u.

»> UJ </5 z o: o

<I UJ -j - »- <r 3 i-i o

CDO

{/> M 00UJ X o _j M £ V Z o

(/^ (/> £ z a: o <. 00 m

H4

00

a <I £ CD O z o 3 CL

.» J- K1 fvj ^ I i I ) • I (•III

OO.J'OO(TilflU'v0f'5(M(\Jlf\M<0f0^a3v0 I t I I I I ) I • t I I

.^oo'S-O'rovoro^HifitviiCi'oifvioJ’Cnj’a' I »H(vjinO'J’»-<<'OvDiOMf^a'fui»5fofo I I I IrHMMfOJ-tOtOfOJ'J-.J-J- I t I I I I I I I I I

^»-IPJ(\)C\J(\J(\J(VJ I

TH^\Cf*^N.N.a0 flD 0O

r0«^fl0f0f0v0TH<0<0*J'N-O»H<«\£)f0f0CM

V^^^jQKfs.fs.C0 «)«O

*-<ir'^N.<T'-5’aDfOaO ^^CVI^vDofOKO JT ^

«-lvHT4 (SJCsJ<MfoU>s,OorON>0 ^ tH CSJ 58
Table

16.

Comparisons

of

functions

at T=

A40 K

zorw®o>co<T'cy'«><ON.\r)\DU>if>u>4‘J“ro o****************** Q_ tH

Vo

J*

If

UJ- • 3 (/) cn z o »-* to >

UJ

a: ^ o

u. •> to ^ UJ

po j

1^ 3

(T>

O o O «? vD vD N. CD vD vD o (SJ IJV « \D

«J fVI fvj UD 00 N- PO iTi \D PO o o PO t— UV vD o

<x fO on (SJ IT PO PO (VJ o PO <r O' 1 ao ro OO o (VJ PO ir vD ^D P^ s. <D 00 o

fvj ro IT IT U) iD \D sD \D \D iD N. I I I I f 1 I I I I I I I I I I I

\£> <r (M If' irv O' o IT o l^ o N- pw UV PO

hsi PO sD O; O' UV «* CJ UV (\i

N O' 00 OV CO CO IT vC p^ P- O' CD p<. vH p^ rvj CVJ PO PO

to 1 CO o PO <D tH (VJ ro IT vD P^

K (C 00 <r o

ro u> \D s£> s£> s£> \£> kD \D vD ^£| >£> <X) p«- p^ t I I I I I I I I I I I I I I I I

H* IT* IC PO OD p^ PO fvj <r vD cr PO Z s. LC o <C IfV UV J- (VJ o O' CO P^ u> UV o

0. CJ P^ J* fVi (VJ CVJ (Vj rvj (VJ (VJ (VJ I u p^ o p^ PO cr « o O' s£> CO UV PO

u (VI o cr 4^ < CO PO PO PO (VJ cD (VJ CO (VJ 00 ^D (VJ o J- vD PO P- o <J* (VJ O' PO (T* \D PO (VJ PO (JV PO UV UV PO o cr PO • o PO CO CVJ vD P^ p- <o 00 CO ® CO u> u

(VJ UV o (VJ (VJ PO PO PO PO PO PO PO PO PO PO PO 1 1 H• 1 1 1 1 1 1 1 1 1 tH1 w1 1 1 1 a flO CP <p O' UV o p^ PO <X) U) cr <x> p*^ 00 UV (VJ

PSJ X U) UV (VJ o <c PO o CO

O O' o J* p*^ oO PO p- 1 <T* K. o PO CO cr p^ <T (VJ <D o o (TV \D PO o PO X 1 4* MJ tH UV p- O' o o o o o (T p^ w (VI UV o (VJ PO PO PO PO •t J- 4* 4" PO PO f 1 1 tH1 1 1 1 1 1 1 1 1 1 1 w1 1

r-i1

f— o UV (VJ IT* ^ PO PO CO UV vD (VJ (jv POK (T z o p^ CD pw u> (VJ o o O ^ (VJ o

Q. ^ I I I • I I

to

Ofu

(/) « •• o to

0'®ooirs^o^T-iooa>vDroifvif'Lf'vO<NJirN

_|(\J\IJOaOCDh-^fSJ.^rOOLr'®CD-^,~l-J’K) <tcD\X>co^N.fVj^c7'T4f^Lr\>^N.cr‘o^Mirt o******************

X -I P— o «j <ty PO (VJ PO (VJ (VJ o CO o p^ p^ PO <o (Vi 4- (T hH r V (VJ u> o PO 4* (VJ <r u> p^ UP UV 00 O' o o (VI X o U) flC 4* P^ PO (T PO u vD P^ CO o PO UV » o

to to

r 4- UV \D \D vD p^ p^ p^ K. P. P^ OO OO CO <o Z 0^ o <

to CD

q:< (O O’ PO UV o UV CD

U o U o UV o u o UV o u CD

a p— < H U> PO cr vD (VJ O'

u (VJ <o UV CO 4 p»- PO o X l—t CD O (VJ u p- o fO UV CO ro vD cr 4 p- cr u> PO o z o 3 a o o o tH (VJ (VJ (VJ (VJ PO ro PO PO 4 UV

(VJ 4- U> o (VJ 4- sD OO o (VJ 4 U> <o o UV o

(VJ (VJ (VJ (VI (VJ PO PO 4

59
Table

17.

Comparisons

with

Starling,

et

al.

on

isotherms o

UJoo• (A o UJ o -J

CJ Z>o

II ")

I0^

I- UJ

<r »- •

»-< (/)

h- 4- o% 4 O' in r^ 4 T-f CO \D 4 (VJ iH o O' <T* O'

O iH (VJ -S vO O' Z rH C\J 4 in cn o (VJ 4 in r^ O' iH ro in U) CO O ro in r^ O' T-l to o

Q. 1 .41 41 41 4• 41 in• in1 in1 in1 in1 in1 vO ^£»1 vO• vO1sX> K. 9 9 K1 h-9 K1 N- CO 9 9 1 O in O' nj (NJ o in (n o CO in <y> 1-4 o N. (VJ 4 4 1-4 \D CO CO 1-4 90

-J o CO r^ in ro o r^ in tH OO 4 iH K. (VJ <D ro eo roK 1-4 in O' ro «o

<r ro ra (5> COK in 4 ro iH o O' N. vJ3 4 ro 1-4 o CO rw in ro (VJ o o ro ro ro (NJ (Vi CVI (VI (VJ (VI (VJ (VI iH iH iH 1-4 1-4 o o a o o o

tvj• M• nj•

<VJ1

(VJ1

(VI•

(VJ1(VJ1

(VJ1

(VJ1

(VJ9(VI1

(VJ1

(VI1

(VJ1

(VJ9

(VJ (Vi 9 9(VJ9

(VI1(VJ9

(VJ (VJ (VJ 9 9 9 M T-i 00 ro \0 OO in tH in 00 4 o ro in in CVJ N- o iH O' in (7> o X <M 4 in v£> n- <o (n O' O' (n (T O' CO N. \D in ro CVJ o r^ in (VI o 1 ro nj o <n CO r^ ^X) in 4 ro (VJ iH o O' eo \0 in 4 (VJ 1-4 0 0' X 4* 4 4 ro ro ro ro ro ro ro ro to ro (VJ (VI (VI (VI (VI (VJ (VJ (VI (VJ 1-4

fVJ1(VJ1 rj•

(Vi1CVJ (VIl

(VJ1

(VJ1(VJ1(VJ1

(VJ1

CVJ•

(VJ«

(VJ1

(VJ9CVJ9

(Vi (VJ 9 9(VI9

(VJ9(VJ9 CM

M CM ) • 1 o <n in tH N. (Vi K tH in OO H ro in u> r^ vj3 in ro 1-4 CO .S' o tC

4* QO 4 r«^ -S' o sD ro O' in r^ ro O' in t-9 ro eo .S'

a if\ 0> O o (VJ (VI ro 4 4 in in sD N. N. eo 00 O' o o *r4 »4 (VJ ro ro o o w tH •H rH iH iH tH i-t iH 1-4 iH (VJ (VI (VJ (VJ (VJ (VJ (VJ 1 1 1

*H1tH1 1 1 1iH1

tH tH1 1

t41 9

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1-1 rA 1 1

1*41

1-49

1-41

1-4 ^4 i4 1 1 1

OJ (VJ o> r^ in ro (NJ

O cn CD r^ \D in in in 4 4 in in vD r^ « cn o CVJ

K o o nj ro 4 in in vO r^ CO O' o iH (VJ ro 4 in \0 N- CO O' ^ CM o o o o o o O o o o a o o 1-4 i4 W ^4 iH 1-4 (VI (VJ V o o o o o O o o o o o o O o o C3 o o O o o O O O a

fVl o o1 o1 01 o• 01 o1 01 01 o• 01 01 01 o1 01 o9 O 0 o1 1 o9 o9 o9 O

OO 9 9 9

1- ro O' in o in O' ro r^ o ro in n- O' o (VJ (VJ (VJ (VI (VJ ^4 o eo vO zo

Q.

(M ^X> tH \S> o 4 O' ro CO (VJ \C o 4 <T' ro

K

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K -c J- OO

O' OO <£) r^ r^ vO in in 4 4 ro ro (VJ iH o o O' CO CO r^

K \0 in

<M (Vi (VI (VJ (VJ (VI (VJ (VJ (VJ (VJ (VI (VJ (VJ (VJ CVJ 4M 1-4 1-4 i4 1-4 ^ 1-4 1^

O oo fVJ sD <n ^ 4 in r^ eo O' O' O' O' CO vO in ro o N. 4 o mom w eo 4 o ro O' in n- ro O' in H N. ro O' in O sC (VI N- ro eo <o K r^ a? <n O' o o tH (VJ (VJ ro ro 4 in in v£) SJD K CO «) cn O' o o

4- 4- 4 4 ^ IT in in in in in in in in in in If' Ifl in in in

m iO

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K o K in 4 -S' r*^ o 4 O' in (VJ

O o o iH 4 K (VJ CO in ro (VJ ro

O a> OO OO cO 00 CO CO cn O' O' o (VJ ro 4 in \0 rw O' o (VJ vO <0 V ro 4" in vO N «o O' o (VJ -S tfi s£> K O' O iH (VI 4 in vO s. CO o H (VI (VJ (VI CM f\j (VJ (VJ (VJ (Vi ro ro ro ro ro to to to W tH iH H iH 1-4 1-4 1-4 iH iH W 1*4 1*4 t4 ^ iH 1-4 K 00 4 O' 4 O) (VI in r^- (TN O o O O cn r^ 4 (VJ A -S O' 4 O' ro zo

Q.

O' \£> CSJ O'

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in in in 4 J- ro ro ro (VJ (VJ iH iH o o O' O' OO CD eo t'- vO

ro ro ro ro ro ro ro fO ro ro ro ro ro ro ro ro (VI (VI (VI (VI (VI CM CM tM

O

K rj CO lO \C CO CVJ CO \D \D <o ro O' CO O' ro eo f««- CO 4 N. <0 N* iH

-1 o 4 OO 4 H O' O' O' 4 a> 4 o CD r^ <o O' (VI u> (VJ eo vO IT) vD o in o in O' 4 O' in O in r^- (VI eo 4 O N. ro o \n ro o K o nj ro in N- O' O (VJ 4 in r^ OO o tH ro in \D CO o 1^ ro m ^

O' O' O' O' 0> ©N O' o O

O o o o 1^ 1^ iH iH ^ i4 (VJ (VJ (M (VI (VJ

1-4 iH i4 1*4 t4 iH i4 4 1*4 iH i4 o 00 ro in vO vO in ro ^ (n <C OO o 4 O ro o O in \D 1-4 ro 1-4 Q o ro ro ro r^ (VI o o (VJ r^ fO (VJ ro vO (VI o o ro O' K 00

o. o> 4 r^ o ro u> o j-® (VJ vD 1-4 u> t4 sC (VI CO 4 o vD ro

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vn v£) vO N.

K n- r^ r<. r^ <o 00 CO eo <o CD O' O' (n O' O' O'

O • _J « 9- u> 4 r'- O O' r'- <D ro m eo ro ro OO 4 m ro (M sO m CO O' m

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1-4 iH

W 1-4 4 iH 1*4 iH t4 4 i*H iH ^ i4 v4 iH i4 iH 1-4 t4 iH 60
ISOBUTANE,

R.O.G.

VS.

K.E.S.

ATT

=

300.

UNITS

KELVINS,

BARS,

G-MOL/LITER,

JOULES

DATA

=

R.O.G.

,

CALC.

=

K.E.S.

Table 17. Continued

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X O' O' O' CT O' CT* O' O' CT CT CA <A O' CA 0 o o O O o O O o o O

y4 w y4 61
ISOBUTANE

Table 17 Continued

8- O' o 40 Ul 40 4* 4- <t> K fO <T <o vO ro o CO UN fO tH O' CO 40 4 N. fO CO tH 4 Ul Z 4* OJ 40 ro 00 (\J Ul N- OT' (U Ul Ul Ul Ul UN 4 4 4 4 fO fO ro ro ro CM CM o ON

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8 8 8 8 8 8 1 8 8 8 8

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CM CM CM ro ro o o o o O O O o o o o o o o o o o o o o o o o o o o o o o o o o

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62

14564
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VS,

K.E.S.

AT

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=

410.00

OEG

UNITS

KELVINS,

BARS,

G-MOL/LITER,

JOULES.

DATA

=

R.O.G.,

CALC.

=

K.E.S.

Table 17. Continued

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1 P^• 1 CO

1 (T1 er

1 o *9 O' K O' O' o eg o \D O' eg PO PO sX3 9 O' 9 eg PO eg o O' eg PO eg 9 U) eg o UN 9 PO p^ CD eg UN u> UN u> o o eg -i -9 -9 9 9 eg s£> o N UN O UN CO o eg eg PO 9 U' p^ O PO O' \D UN sD o \0 u> CD CD o « eg PO O' sD 9 U' o W O CO O' 9 \D o M « eo CD PO N* UN O' PO u> O' PO ^ O' eg UN O •H 9 « 9 « eg U> UN o sD oO 9 eg o O' oc O' 9 O' UN PO eg 9 O' U) ^ eg eg PO PO 9 9 9 UN UN UN sD \C K Pw CO CO o O' O' O' o o eg eg PO PO 9 UN \£> U3 p^ CO o yA (g 9 \D CO o eg UN w tH •H W w eg eg eg eg eg eg PO PO PO

QC K \D O' O' O' eg eg O O PO eg O' 9 9 O' o o PO eg o w 00 9 9 PO P- 9 CD 9 PO CO CO eg v£) er PO (D eg UN CD \D eg

<xCD.9 ITN eg IT UN eg O' O' N. PO CO 9 P^ CO CD CD OO O' 9 o UN 9 t~4 lD U) PO P«. o PO sD o p« O' u> O eg vO eg 9 9

f\J ro PO UN O' PO U) o PO U> O' eg u CO 9 h- 9 p^ U' O' 9 O' 9 o p>- 9 PO eg eg 9 o U) 9 PO 9 CO 9 PO U' a eg eg PO PO 9 9 9 O' UN u> u> U> L0 pw K P«- CO (D CO O' O' O' o o o eg PO PO 9 UN U) p- CO O' eg 9 u> CO o PO \D ep w w eg eg eg eg eg PO PO PO PO e O o o o o o o o O o o o o o o o o o o o o o o o O O o o O o o CD o O o o O o o o CD o o o o o CD V (NJ o 9 o eg CO 9 o sD eg 9 o \£> eg CO 9 o sC eg CO 9 o eg €D 9 o u> eg CD 9 O U) eg 9 o vD eg <D 9 \D eg

fO 9- CO O' H eg 9 U) P^ O' o eg 9 UN h- <D o eg PO UN sD O o PO 9 lD O' eg 9 U> p^ O' CD eg 9 UN p- (D eg PO UN u> z eg eg eg eg eg eg PO PO fO PO PO PO 9 9 9 9 9 9 9 IT UN UN UN UN UN u> U) u> ^£> sD U> p^ P. p*. 65
TABLE 18. Calculated P(T) isochores

The following pages give P(T) along isochores, as computed by the equation

of state. The third column DP/DD is the isotherm slope (3P/9p) in units of the

bar and mol/L. The last two columns give the isochore slopes and curvatures

3P/3T, 32p/3t2, in units of the bar and K.

These tables show that the isochore curvatures are qualitatively consistent

with a maximum in the specific heat Cy(p,T) at the critical point.

66
Table 18. Calculated P(T) isochores

344

346

354

362

370

378

386

394

402

410

418

426

434

442

450

458

466

474

482

490

498

506

514

522

530

538

546

554

562

570

578

586

594

602

610

618

626

634

642

650

658

666

674

682

690

698

ISOBUTANE ISOCHORE AT .500 MOL/L

T,K P , BAR OP/OD DP/OT 02P /0 T 2 238 11.193 16 . Ill .05 36 -.00010

0 00 11.287 16.345 . 05 35 -. 00009

000 11.712 17.390 .0528 -.00008

000 12.132 18.410 .0522 -. 00007

000 12.548 19.409 .0517 -. C 0006

000 12.960 20.391 .0513 -. 00005

000 13.369 21.358 .0509 -.00005

000 13.775 22.313 . 0505 -.00004

000 14.177 23.256 .0502 -. 00004

000 14.578 24.187 . 0499 -.00004

000 14.975 25. 110 . 0496 -. 00004

000 15.371 26.023 . 0493 -. 00003

000 15.764 26.928 . 0491 -. 00 0 0 3 000 16.156 27. 825 .0488 -. 0000 3 000 16.545 28. 715 . 0486 - . 00003

000 16.933 29.598 . 0434 -.00003

000 17.320 30.475 . 0482 -.00002

000 17.704 31.346 .0480 -. 00 0 02

000 18.088 32.211 .0478 -. 00002

000 18.470 33. 072 .0477 -. 00002

000 13. 851 33.927 . 0475 -. 00002

000 19.230 34.779 .0474 -.00002

000 19.609 35.625 . 0472 -.00002

000 19.986 36.468 . 0471 -. C 0002

000 20.363 37.307 .04 70 -. 00001

000 20.738 38.143 .0469 -. 00001

000 21.113 38.975 .0468 -.00001

000 21.487 39.804 . 0 467 -.00001

000 21.860 40.630 .0466 -. 00001

000 22.232 41.453 . 04 65 -.00001

000 22.604 42.274 . 04 64 -.00001

000 22.975 43.092 . 0463 -. 00001

000 23.345 43.908 . 04 63 -.00001

000 23.715 44.721 . 0462 -.00001

000 24.084 45.533 . 04 61 -. COOOl

000 24.453 46.342 . 04 61 -.00001

000 24.821 47.149 . 04 60 -. 000 01 000 25.189 47.955 .04 59 -.00001

000 25.556 48.759 . 04 59 -. 00001

000 25.923 49.561 . 04 58 -.00001

000 26.289 50.362 .04 58 -.00001

000 26.655 51. 162 . 04 57 -.00001

000 27.021 51.960 . 0457 -.00001

000 27.386 52.756 .04 56 -.00001

000 27.751 53.552 .0456 -. 00000

000 28.116 54 . 346 . 04 56 -.00000

67
Table 18. Continued

IS03UTANE ISOCHORE AT 1.000 MOL/L

T,K P,BAR OP/00 OP/OT D2P/DT2

374.282 20.264 10.405 . 1232 -. 00036

378.000 20.720 11.016 .1220 -. 00030

386.000 21.687 12.286 .1199 -. 00023

394.000 22.638 13.515 .1181 -. C0020

402.000 23.573 14.714 .1167 -. 00017

410.000 24.506 15. 888 .1154 -.00015

418.000 25.424 17.042 .1142 -.00014

426.000 26.333 18.178 .1131 -. 00013

434.000 27.234 19.298 .1121 -.00012

442.000 28.127 20.404 .1112 -. 00011

450.000 29.013 21.497 .1104 -.00010

458.000 29.893 22.578 .1096 -. 00009

466.000 30. 767 23.649 .1089 -. 00009

474.000 31.636 24.709 .10 82 -.00008

482.000 32.499 25.760 .10 76 -.00008

490.000 33.357 26.802 .10 70 -. C0007

498.000 34.211 27. 836 .10 64 -.00007

506.000 35.061 28. 863 .1059 -. 00006

514.000 35.906 29.882 .10 54 -. 00006

522.000 36.748 30.895 .10 50 -. 00006

530.000 37.586 31.902 .1046 -.00005

538.000 38.421 32.903 .1042 -. G0005

546.000 39.252 33.898 .1038 -. 00005

554.000 40. 081 34.888 .1034 -. 00004

562.000 40.907 35.874 .1031 -.00004

570.000 41. 730 36.854 .1028 -. 00004

578.000 42.551 37.831 .1024 -.00004

586.000 43.370 38.803 . 1022 -. C0003

594.000 44.136 39.771 .1019 -. 00003

602.000 45.000 40.736 . 1016 -. 00003

610.000 45.812 41.698 .1014 -. 00003

618.000 46.622 42.656 .1012 -. C0003

626.000 47.431 43.611 .1010 -. 00003

634.000 43.238 44.563 .1007 -. 00003

642.000 49.043 45.512 .1006 -. C0002

650.000 49.846 46.459 .1004 -. 00002

658.000 50. 649 47.403 .1002 -. 00002

666.000 51.449 48.344 .1000 -.00002

674.000 52.249 49.284 .0999 -.00002

682.000 53.047 50.221 .0997 -. 00002

690.000 53.844 51.157 .0996 -. 00002

698.000 54.641 52.090 .0994 -.00002

68
Table 18. Continued

ISOBUTANE ISOCHORE AT 2.000 MOL/L

T,K P,SAR DP/00 DP/ CT D2P/0T2

399.151 31.402 3.293 .2957 -. C0198

402.000 32.238 3. 881 .2914 -. C0124

410.000 34.537 5.417 .2841 -. 00070

416.000 36. 789 6. 891 . 2793 -. C0053

426.000 39.006 8.334 .2754 -.00044

434.000 41.198 9.757 .2721 -. 00038

442.000 43. 363 11.164 .2693 -. C0034

450.000 45.507 12.558 .2667 -.00030

456.000 47.631 13.941 .2644 -.00028

466.000 49.738 15.314 .2623 -. 00025

474.000 51.828 16.678 . 2603 00023

462.000 53.903 18.035 .2585 -.00022

490.000 55.964 19.385 .2568 -. 00020

496.000 56.012 20.728 .2553 -. 00019

506.000 60.049 22.065 .2538 -. 00018

514. 000 62.073 23.396 . 2524 -. 00016

522.000 64.088 24.723 . 2512 -. 00015

530.000 66.092 26.044 .2500 -. 00015

538.000 68.087 27.360 .2488 -.00014

546.000 70.074 28.672 .2478 - . 00 0 1 3 554.000 72.052 29.980 .2468 -. C0012

562.000 74. 022 31.284 .2458 -.coon

570.000 75.985 32.585 .2449 -.00011

578.000 77.941 33.882 .2441 -. 00010

566.000 79.891 35.175 .2433 -. COOlO

594.000 81. 834 36.466 . 2426 -. 00009

602.000 83.772 37.753 .2418 -.00009

610.000 85.704 39. 038 .2412 -.00008

618.000 87. 631 40.320 . 2405 -. C0 0 08

626.000 89.552 41.599 .2399 -.00007

634.000 91.469 42. 876 .2393 -.00007

642.000 93.382 44.150 .2388 -.00007

650.000 95.290 45.422 .2383 -.00006

658.000 97. 194 46. 692 . 2378 -.00006

666.000 99.095 47. 959 .23 73 -. C0006

674.000 100.991 49.225 .2369 -. 00005

662.000 102.884 50.488 .2364 -.00005

690.000 104. 774 51.750 .2360 - . 00005

696.000 106.660 53.010 .2356 -.00005

69
Table 18. Continued

ISOBUTANt ISOCHORE AT 3.000 HOL/L

T,K P.BAR DP/00 OP/CT 02P/0T2

406.982 35.911 .439 .4888 -. 01521

410.000 37.360 1.033 .4756 -.00193

418.000 41.124 2.536 .4666 -. 00075

426.000 44 .836 4. 055 .4616 -. 00053

434.000 48.513 5.591 .4579 -. 00043

442.000 52. 163 7. 142 .4547 -. 00037

450.000 55.790 8.706 .4519 -. 000 32 458.000 59.395 10.281 .4495 00029

466.000 62.982 11.867 .4473 -. 00027

474.000 66.552 13.462 .4452 -.00024

482.000 70.106 15.066 .4433 -. 00023

490.000 73.646 16.677 .4416 -.00021

498.000 77.172 18.296 .4400 -. 00020

506.000 80.685 19.921 .43 85 -. 00018

514.000 84.187 21.552 .4370 -.00017

522.000 87.678 23.188 .4357 -. 00016

530.000 91.159 24.829 .4344 -. 00015

538.000 94.629 26.475 .4332 -. 00015

546.000 98.090 28.125 .4321 -. 00014

554.000 101.543 29.779 .4310 -. 00013

562.000 104.987 31.436 .4300 -.00012

570.000 108.423 33.097 .4290 -.00012

578.000 111.852 34.760 .4281 -.00011

586.000 115.273 36.426 .4272 -.00011

594.000 118.688 38. 094 .4264 -.00010

602.000 122.096 39. 764 .4256 -. COOlO

610.000 125.497 41.437 .4248 -.00009

618.000 128.893 43.111 .4241 -. 00009

626.000 132.283 44.786 .4234 -. 00 0 09 634.000 135.667 46. 463 . 4227 -.00008

642.000 139.047 48.141 .4221 -.00008

650.000 142. 421 49. 821 .4214 -. 00008

658.000 145.790 51.501 .4208 -.00007

666.000 149.154 53.182 .4203 -. 00007

6 74 . 0 0 0 152.514 54. 863 .4197 -. 00007

682.000 155.870 56.545 .4192 -.00007

690.000 159.221 58.228 .4187 -. 00006

698.000 162.568 59.911 .4182 -.00006

70
Table 18. Continued

ISOBUTANE ISOCHORE AT 3.860 MOL/L

T,K P.BAR DP/DD OP/OT 02P/0T2

408.000 36.549 0. 000 .6341 0. 00000

410.000 37.817 . 365 . 6341 -. 00000

418.000 42.890 1.982 .6341 -.00000

426.000 47.962 3.691 . 6340 -.00001

434.000 53.034 5.458 . 6340 -. COOOl

442.000 58.105 7. 268 .6339 -.00001

450.000 63.176 9.115 .6337 -. 00002

458.000 68.245 10.994 .6336 -. 00 0 02 466.000 73. 313 12.901 . 6334 -.00002

474.000 73.380 14. 833 .6333 -.00002

482.000 83.445 16.789 .6331 -.00002

490.000 88.509 18.765 .6329 -. 00003

498.000 93.571 20.760 .6326 -. 0000 3 506.000 98.631 22.772 .6324 -. 00003

514.000 103.689 24.800 .6322 -. 00003

522.000 108. 746 26.843 .6319 -.00003

530.000 113.800 28.900 .6316 -. 00003

538.000 118.852 30.969 . 6314 - . 00 0 04

546.000 123.902 33.049 .6311 -.00004

554.000 128.949 35.140 .6308 -. 00004

562.000 133.994 37.240 .63 05 -.00004

570.000 139.037 39.350 .6302 -.00004

578.000 144.077 41.468 . 6299 -. C0004

586.000 149.115 43.593 .6295 -. 00004

594.000 154. 150 45.726 . 6292 -. 00004

602.000 159.182 47.865 .62 99 -.00004

610.000 164.212 50.010 .62 86 -.00004

618.000 169.239 52. 160 . 62 82 -. 00004

626.000 174.263 54.316 .6279 -. 00004

634.000 179.285 56.476 .6275 -. 00004

642.000 184.304 58.640 .6272 -.00004

650.000 189.320 60.808 . 6268 -. C0004

658.000 194.333 62.980 .6265 -. 00004

666. 000 199.343 65.154 .6261 -.00005

674.000 204.350 67.332 .6257 -. 00005

682.000 239.355 69.512 . 6254 -. 00 0 05

690 .000 214. 356 71.695 .6250 -.00005

693.000 219.355 73.879 . 6246 -. C0005

71
Table 18. Continued

ISOBUTANE ISOCHORE AT 4.000 MOL/L

TtK P,BAR OP/00 DP/OT 02P/0T2

407.996 36.546 .002 .6524 .78005

410.000 37.869 .384 .6615 . 00069

418.000 43.173 2.075 .6640 . 00018

426.000 48.490 3.661 .6651 . 00012

434.000 53.815 5.707 .6660 . 00009

442.000 59.145 7.598 . 6666 . 00007

450.000 64.480 9.529 .66 71 . 00006

458.000 69.818 11.493 .6675 . 00004

466.000 75.159 13.486 .6678 . 00004

474.000 80.502 15.506 .6680 . 00003

432.000 85.847 17.550 .66 32 . 00002

490.000 91.194 19.615 .6684 . 00002

498.000 96.541 21.701 .6685 . 00001

506.000 101.889 23.604 .66 86 . 00001

514.000 107.238 25.924 .6666 . 00000

522.000 112.587 28.060 .66 86 -. 00000

530.000 117.935 30. 209 .6685 -. 00001

538.000 123.233 32.372 .66 85 -. 00001

546.000 128.631 34.546 .6684 -. COOOl

554.000 133.977 36.732 .6683 -.00002

562.000 139. 323 38.927 .6681 -. 00002

570.000 144.668 41.133 .6680 -.00002

578.000 150.011 43.346 .6678 -. 00002

586.000 155.353 45.568 .6676 -.00002

594.000 160.693 47.797 .6674 -. 00003

602.000 166.032 50.033 .6672 -. 00003

610.000 171.368 52.275 .6670 -. 00003

618.000 176.703 54.523 .6667 -.00003

626.000 182.036 56.776 .6665 -.00003

634.000 187. 367 59. 034 .6662 -. 00003

642.000 192.695 61.296 .6659 -. 00004

650.000 198.022 63.562 .6656 -.00004

658.000 203. 346 65.832 .6653 -.00004

666.000 208.667 68.105 .6650 -.00004

674.000 213.986 70.381 .6647 -. 00004

682.000 219.303 72.660 .6644 -.00004

690.000 224.617 74.941 .6641 -. 00004

698.000 229.928 77.224 . 6637 -. 00004

72
Table 18. Continued

ISOBUTANE ISOCHOiRE AT 5.000 MOL/L

T,K

406.394

410.000

418.000

426.000

434.000

442.000

450.000

458.000

466.000

474.000

482.000

490.000

498.000

506.000

514.000

522.000

530.000

538.000

546.000

554.000

562.000

570.000

578.000

586.000

594.000

602.000

610.000

618.000

626.000

634.000

642.000

650.000

658.000

666.000

674.000

682.000

690.000

698.000

P.BAR

35.549

38.882

46.394

53.989

61.642

69.340

77.077

84.847

92.646

100.471

108.319

116.188

124.076

131.980

139.899

147.832

155.777

163. 732

171.698

179.672

187.654

195.643

203. 638

211.638

219.643

227.652

235.664

243.678

251.695

259.713

267. 732

275.752

283.772

291.793

299.812

307. 831

315.849

323.866

OP/DO

1.193

2.561

5.506

8.468

11.455

14. 464

17.493

20.539

23.602

26.679

29. 768

32.870

35.982

39. 104

42.234

45.373

48.518

51.670

54.628

57.991

61.158

64.330

67.505

70.683

73.865

77.048

80.234

83.421

86.610

89.800

92.991

96.183

99.374

102.566

105.758

108. 950

112.141

115. 332

DP/OT

.9130

.9311

.9450

.9533

.9596

. 9648

.9693

.9732

. 9766

.9796

.9824

.9848

.9870

.9890

.9906

.9924

.9938

.9951

.9963

.9973

.9982

.9990

.9997

1.0003

1.0008

1.0013

1.0017

1.0020

1.0022

1.0024

1. 0025

1.0025

1.0025

1.0025

1.0024

1.0023

1. 0022

1.0020

D2P/0T2

. 01193

.00271

. 00124

.00089

. 00071

. 00060

.00052

. 00045

. 00040

.00036

. 00032

.00029

.00026

.00024

. 00021

.00019

. 00017

.00015

. C0014

. 00012

. 00 011

. 00009

. 00008

. 000 07

.00006

. 00 0 05

. 00004

. C0003

. 00003

. 00 0 02

. COOOl

. 00000

-. 00000

-. 00001

-.00001

-.00002

-. C0002

-. 00003

73
Table 18. Continued

398

402

410

416

426

434

442

450

458

466

474

432

490

498

506

514

522

530

538

546

554

562

570

578

586

594

602

610

618

626

634

642

650

658

666

6 74 682

690

698

ISOBUTANE ISOCHORE AT 6.000 MOL/L

T,K P,9AR DP/00 OP/OT 02P/DT2

797 31.212 10.228 1.4092 . 00261

000 35.737 12.302 1.4162 . 00184

000 47.116 17.348 1.4277 .00117

000 58.571 22.307 1.4358 . 00090

000 70.085 27.218 1.4423 .00074

000 81.645 32. 095 1.4477 . 00063

000 93.247 36.944 1.4524 . 00055

000 104.883 41.770 1.4565 . 00048

000 116.550 46.576 1.4601 . 00042

000 128.244 51.363 1.4633 . 000 37

000 139.961 56. 133 1.4661 . 00033

000 151.701 60.688 1.4636 .00029

000 163.459 65.629 1.4706 . 00026

000 175.233 70.355 1.4728 . 00023

000 187,023 75. 069 1.4745 . 00020

000 198.825 79.769 1.4760 .00016

000 210.638 84,458 1.4773 . 00015

000 222.462 69.136 1 .4785 . 00 0 1 3 000 234.294 93.802 1.4795 . 00 0 11 000 246. 133 98.458 1.4603 .00009

000 257.978 103.104 1.4810 .00008

000 269.828 107.739 1.4815 . 00 006

000 281.682 112.365 1.4820 . 00005

000 293.539 116.981 1.4823 .00003

000 305.399 121.588 1.4825 . 00002

000 317.260 126.186 1.4827 .00001

000 329.121 130.776 1.4827 -.00000

000 340.982 1 35.357 1.4826 -.00001

000 352.843 139. 929 1.4625 -.00002

000 364.703 144.493 1. 4823 -. 00 0 03 000 376.560 149.050 1.4821 -.00004

000 388.415 153.598 1.4817 -.00004

000 400.268 158.138 1.4813 -. C0005

000 412.117 162.671 1.4809 -.00006

000 423.962 167.197 1.4804 -.00006

000 435.803 171.715 1.4799 -. 00007

000 447.640 176.226 1.4793 -.00008

000 459.472 180. 730 1.4737 -.00008

000 471.293 185.227 1.4780 -. C0009

74
.Table 18. Continued

ISOBUTANE ISOCHORE AT 7.000 MOL/L

T,K

382.375

386.000

39‘*. 000

402.000

410.000

418.000

426.000

434.000

442.000

450.000

458.000

466.000

474.000

482.000

490.000

498.000

506.000

514.000

522.000

530.000

538.000

546.000

554.000

562.000

570.000

578.000

586.000

594.000

602.000

610.000

618.000

626.000

634.000

642.000

650.000

658.000

666.000

674.000

682.000

690.000

698.000

P.BAR

23.454

31.284

48.588

65.917

83.268

100.637

118.019

135.412

152.814

170.223

187.636

205.053

222.472

239. 891

257.308

274.724

292. 136

309.544

326.947

344.344

361.734

379.116

396.490

413.855

431 . 211

448.557

465.893

483.217

500.533

517.832

535.121

552.398

569.662

586.913

604.151

621.375

638.586

655.782

672. 964

690. 132

707.285

DP/00

37.171

40.368

47.368

54.311

61.209

68.068

74.892

81.685

88.449

95. 186

101.897

108.584

115.249

121.891

128.513

135.114

141.696

148.259

154.805

161. 332

167. 843

174.337

180.815

187.277

193,724

200.157

206.575

212.978

219.368

225. 744

232.107

238.457

244. 795

251.119

257.432

263. 732

270.020

276.297

282.562

288.816

295.059

OP/ CT 2.1589

2.1610

2.1647

2 . 1 6 76 2.1700

2.1719

2.1735

2.1748

2.1757

2.17 64

2 . 1 7 69 2.17 72 2.1774

2.17 73 2.17 71 2.1768

2.17 63

2. 1757

2.1750

2.17 42

2. 1733

2.1723

2.1712

2.1701

2. 1689

2.16 76 2.1663

2.1649

2.1634

2.1619

2. 1604

2.1588

2.15 72 2.1556

2.1539

2.1522

2.1504

2.1487

2.1469

2.1451

2.1432

02P/0T2

. 00061

. 00053

, 00041

,00033

. 00027

. 00022

.00017

.00014

.00010

. 00 0 08

. 00 0 05

. 00003

.00000

-.00002

-. 000 03 -.00005

-. 00007

-.00008

-. 00009

-.00011

-.00012

-.00013

-.00014

-.00015

-. C0016

-.00016

-. 00017

-. 00018

-. 0001 8 -.00019

-. 00019

-.00020

-. 00020

-.00021

-.00021

-. 00022

-. 00022

-.00022

-.00022

-. 00023

-.00023

75
Table 18. Continued

ISOBUTANE IS0CH0<?E AT 6.000 MOL/L

T,K

355.886

358.000

362.000

366.000

370.000

374.000

378.000

382.000

336.000

390.000

394.000

398.000

402.000

406.000

410.000

414.000

413. 000

422.000

426.000

430.000

434.000

438.000

442.000

446.000

450.000

454.000

458.000

462.000

466.000

470.000

474.000

478.000

482.000

486.000

490.000

494.000

498.000

502.000

506.000

510.000

514.000

518.000

522.000

526.000

530.000

534.000

538.000

542.000

546.000

550.000

554.000

558.000

562.000

566.000

570.000

574.000

578.000

P.BAR

14.246

20.952

33.643

46.334

59.026

71.718

84.410

97.101

109.792

122.401

135.169

147.855

160.540

173.222

185.902

198.580

211.255

223.927

236.596

249.262

261.924

274.583

287.238

299.089

312.536

325.179

337.818

350.452

363.082

375.707

388.327

400.943

413.554

426.159

438. 760

451.355

463.945

476.529

489.108

501.632

514.250

526.812

539.368

551.919

564.464

577.003

589.536

602.063

614.583

627.098

639.607

652.109

664.605

677.095

689.578

702.055

714.526

DP/DD

91.446

93.945

98.669

103.307

108.099

112.805

117.506

122.201

126.890

131.574

136. 253

140.927

145.595

150.258

154.917

159.570

164.218

168.861

173.499

178.132

182.760

187. 383

192.002

196.615

201.224

205.828

210.427

215. 021

219.611

224. 196

228.776

233.352

237.923

242.489

247. 051

251.608

256. 160

260.708

265.252

269.791

274.325

278. 855

283. 331

287.902

292.418

296.931

301.433

305.942

310.441

314.936

319. 426

323.912

328.394

332.872

337. 345

341. 814

346.279

OP/OT

3.1724

3.1725

3.1728

3.1729

3.1730

3.1730

3.1729

3.1727

3.1725

3.1722

3.1718

3.1714

3.1709

3.1703

3.1697

3.1691

3. 1684

3.16 76 3.1668

3.1660

3.1651

3.1642

3.1633

3.1623

3.1613

3. 1602

3.1591

3.1580

3.1569

3.1557

3.1545

3.1533

3.1520

3.1508

3.1495

3.1481

3.1468

3.1455

3.1441

3.1427

3.1413

3.1398

3.1384

3.13 69 3.1355

3.1340

3.1325

3.1310

3.1294

3.1279

3.1264

3.1248

3.1232

3. 1216

3. 1201

3.1185

3.1169

02P/0T2

.00009

.00007

. 00005

. C0003

. 00001

-. COOOl

-. 00003

-. 00005

-. 00007

-. 00008

-. COOIQ

-. 00012

-. 00013

-. 00014

-. 00016

-. 00017

-.00018

-. 00019

-.00020

-. 00021

-. 00022

-.00023

-.00024

-. C0025

-. 00026

-. 00027

-. 00028

-. 00028

00029

-. 00030

-.00030

-. 00031

-.00032

-. 00032

-.00033

-. 00033

-. 00034

-. 00034

-.00035

-.00035

-. 000 35

-. 00036

-. 00036

-. 00037

-. 00037

-. 00037

-. 00038

-. 00038

-.00038

-.00039

-. 00039

-. 00039

-. 000 39 -. 000 40

-. 00040

-. 00040

-. 00040

76
Table 18. Continued

isobutane isochore at 9.000 MOL/L

T,K P,BAR OP/DO DP/OT 02P/0T2

319.060 6.243 185.667 4.5906 .00001

323.000 19.740 190.670 4.5905 -. 00002

326.000 38.101 197.472 4.5904 -. C0006

330.000 56.462 204.267 4.5901 -.00009

334.000 74. 822 211.056 4.5896 -.00012

338.000 93.179 217.837 4.5891 -. C0016

342.000 111.534 224.611 4.5884 -. 00 018

346.000 129.886 231.379 4.5876 -. 00021

350.000 148.235 238.139 4.5867 -. 00024

354.000 166.580 244.692 4.5857 -.00026

358.000 184.921 251.639 4.5346 -. 00 0 29

362.000 203.257 258. 377 4.5834 -. 000 31 366.000 221.588 265.109 4.5821 -. 00033

370.000 239. 913 271.834 4.5807 -. 00035

374.000 258.234 278.551 4.5793 -.00037

378.000 276.548 285. 261 4.5777 -. C00 39

362.000 294.855 291.963 4.5761 -. 00041

366.000 313.157 298.658 4.5745 -. C00 43

390.000 331.451 305.346 4.5727 -. 00044

394.000 349.738 312.027 4.5709 -.00046

398.000 363.013 318.700 4.5690 -. 00048

402.000 386.290 325. 366 4.5671 -. 00049

406.000 404.555 332.024 4.5651 -.00050

410.000 422.811 338.675 4.5631 -.00052

414.000 441.059 345. 318 4.5610 -. C0053

418.000 459.299 351.954 4.5589 -. 00054

422.000 477.530 358.583 4.5567 -. 00055

426.000 495.752 365.204 4.5544 -.00056

430.000 513.966 371. 818 4.5522 -. 00057

434.000 532.170 378.424 4.5499 -.00058

438.000 550.364 385.023 4. 54 75 -.00059

442.000 563.550 391.614 4.5451 -. 00060

446.000 586.725 398.198 4.5427 -. 00061

450.000 604.891 404. 775 4.5403 -. 00062

454.000 623.048 411.345 4.5378 -. 00062

456.000 641.194 417.907 4.5353 -.00063

462.000 659.330 424.461 4.5327 -. 00064

466.000 677.456 431.008 4.5302 -.00064

470.000 695.571 437.548 4.5276 -.00065

474.000 713.676 444. 081 4.5250 -. 00066

77
Table 18. Continued

272

2 74 276

278

280

282

284

286

288

290

292

294

296

298

300

302

304

306

308

310

312

314

316

318

320

322

324

326

328

330

332

3 34 336

338

340

342

344

346

348

350

352

354

356

358

360

362

364

366

368

370

372

374

3 76

378

380

IS09UTANE ISOCHORE AT 10.000 MOL/L

T,K P,BAR OP/DD OP/CT 02P/0T2

535 1.544 337.524 6.6935 .00000

000 11 . 351 341.303 6.6935 -. 000 0 3 000 24.738 346.457 6.6934 -. 00007

000 38.124 351.606 6.6932 -.00010

000 51.511 356.752 6.6930 -. 00014

000 64.896 361.894 6.6926 -.00017

000 78.281 367. 032 6.6923 -. 00021

000 91.665 372.165 6.6918 -. 00024

000 105. 048 377.295 6.6913 -.00027

000 118.430 382.421 6.6907 -.00030

000 131.811 387.542 6.6901 -. 000 33

000 145.191 392.660 6.6894 -. 00036

000 158.569 397.773 6.6886 -.00039

000 171.945 402.882 6.6878 -.00042

000 185.320 407.968 6.6869 -. 00045

000 198.693 413.089 6. 6860 -. 00047

000 212.064 418.186 6.6851 -.00050

000 225.433 423.279 6.6840 -. 00052

000 238.800 428.363 6.6830 -.00055

000 252.165 433.453 6.6818 -. 00057

000 265.527 438.533 6.6807 -. 00059

000 273.887 443.610 6.6795 -.00062

000 292.245 446.683 6.6782 -.00064

000 305.600 453.752 6.6769 -.00066

000 318.953 458.816 6.6756 -. C0C68

000 332.302 463.877 6.6742 -. 00070

000 345.649 468.933 6.6728 -. 00072

000 358.994 473.985 6.6713 -.00074

000 372.335 479.034 6. 6698 -. 00 0 75 000 385.673 434.078 6.6683 -.00077

000 399. 008 489.118 6. 6668 -. 00079

000 412.340 494.155 6.6652 -.00081

000 425.669 499.187 6.6635 -.00082

000 438.994 504.215 6.6619 -. 000 84

000 452.316 509.239 6.6602 -. 00085

000 465.635 514.259 6.65 85 -.00087

000 478.950 519.275 6.6567 -.00088

000 492.262 524.287 6. 6549 -. 00090

000 505.570 529.296 6.6531 -. 00091

000 518.874 534.300 6.6513 -. 00092

000 532.175 539.300 6.6494 -.00094

000 545.472 544.296 6.6475 -.00095

000 558. 765 549.286 6 .6456 -.00096

000 572. 054 554.276 6.6437 -. 00097

000 585.339 559.261 6.6417 -. 00099

000 598.621 564.241 6.6397 -.00100

000 611.898 569. 217 6.6377 -. 00101

000 625.172 574. 190 6.6357 -.00102

000 638.441 579.158 6.6337 -.00103

000 651.707 584.123 6.6316 -. 00104

000 664.968 589. 083 6.6295 -.00105

000 678.225 594.040 6.6274 -.00106

000 691.477 598.993 6.6253 -. 00107

000 704.726 603.942 6.6231 -.00108

000 717.970 608.887 6.621

0

- . 00109

78
Table 18. Continued

210

220

222

224

226

228

230

232

234

236

238

240

242

244

246

248

250

252

254

256

258

260

262

264

266

260

270

272

274

276

278

280

282

204

206

208

290

ISOBUTANE ISOCHORE AT 11.000 MOL/L

T,K P. B AR OP/Ou DP/CT 02P/0T2

260 .124 569. 041 9.9623 .00000

000 17. 456 576.185 9.9622 -.00008

000 37.300 584.388 9.9620 -.00017

000 57.304 592.580 9.9615 -. 00026

000 77.226 600.761 9.9609 - . 00034

000 97.147 608. 931 9.9602 - . 00042

000 117.067 617.091 9.9592 -. 00050

000 136.984 625.240 9.9502 -. 00058

000 156.899 633.378 9.9569 -. 00065

000 176. 012 641.506 9.9556 -. 00072

000 196.721 649.624 9.9540 -. 00079

000 216.628 657.730 9.9524 -. 00005

000 236.531 665.827 9.9506 -. 00092

000 256.430 673.912 9. 9487 -. 00090

000 276.326 601.988 9.9467 -.00104

000 296. 217 690. 053 9. 9446 -.00109

000 316.104 698.108 9.9424 -.00115

000 335.987 706.152 9.9400 -. 00120

000 355.864 714. 186 9.9376 -. 00125

000 375.737 722.210 9.9350 -. 00130

000 395.604 730.224 9.9324 -.00135

000 415.466 730.227 9.9296 -.00139

000 435.322 746.221 9.9268 -. 00144

000 455.173 754.204 9.9239 -.00148

000 475. 018 762.178 9.9206 -. 00152

000 494.856 770. 141 9.9178 -. 00156

000 514.609 778.095 9.91 46 -. 00160

000 534.515 786.038 9.9113 - . C0164

000 554.334 793.972 9. 9080 -. 00160

000 574.147 601.896 9.9046 -. 00171

000 593.953 009.010 9.9012 -.00174

000 613. 751 817.714 9. 8977 CO170

000 633.543 825.609 9.8941 - . 00181

000 653.320 833.494 9.8904 -. 00184

000 673.105 641.370 9.8867 -. 00187

000 692.875 849.235 9.8830 -. 00190

000 712. 637 357. 0 92 9.0792 - . 00192

79
Table 18. Continued

ISOBUTANE ISOCHORE AT 12.000 MOL/L

T,K

159.321

160.000

161.000

162.000

163.000

164.000

165.000

166.000

167.000

165.000

169.000

170.000

171.000

172.000

173.000

174.000

175.000

176.000

177.000

178.000

179.000

180.000

181.000

182.000

183.000

184.000

185.000

186.000

187.000

188.000

189.000

190.000

191.000

192.000

193.000

194.000

195.000

196.000

197.000

198.000

199.000

200.000

201.000

202.000

203.000

204.000

205.000

206.000

P.BAR

.001

10.449

25.827

41.206

56.584

71.962

37.339

102.715

118.091

133.465

148.839

164.211

179.582

194.951

210.319

225.685

241.049

256.412

271.773

287.131

302.488

317.842

333.194

348.544

363.891

379.236

394.578

409.917

425.254

440.587

455.918

471.246

486.571

501.893

517.211

532.526

547.838

563.147

578.452

593.754

609.052

624.346

639.637

654.924

670.208

685.487

700.763

716.035

OP/00

925.928

930.745

937.829

944.904

951.970

959.028

966.078

973.119

980.153

987.178

994. 194

1001.203

1008.203

1015.195

1022.180

1029.156

1036.124

1043.084

1050.037

1056.981

1063.918

1070.847

1077.768

1084.681

1091.586

1098.484

1105.375

1112.257

1119.132

1126.000

1132.859

1139.712

1146.557

1153.394

1160.224

1167.047

1173.863

1180.671

1187.472

1194.265

1201.052

1207.831

1214.603

1221.368

1228.126

1234.877

1241.620

1248.357

OP/OT

15.3789

15.3789

15,3787

15.3784

15.3780

15.3774

15.3767

15.3759

15.3750

15.3739

15.3728

15.3715

15, 3701

15.3686

15.36 70 15.3653

15.3636

15.3617

15.3597

15.35 76 15.3554

15.3532

15.3509

15.3484

15.3459

15.3434

15.3407

15.3380

15.3352

15.3323

15.3293

15.3263

15.3232

15. 3201

15.3169

15.3136

15.3103

15.3069

15.3034

15.2999

15.2963

15.2927

15.2890

15.2853

15.2815

15.2777

15.2738

15.2699

02P/0T2

.00000

-. 00010

-. 00023

-. 00037

-. 00050

-. 00063

-.00075

-. 00087

-. 00099

-.00111

-. 00122

-.00133

-.00144

-. 00154

-. 00164

-.00174

-. 00184

-.00194

-.00203

-. 00212

-. 00221

-.00229

-. 00238

-.00246

-.00254

-. 00262

-.00270

-.00277

-.00284

-. 00291

-. 00298

-.00305

-.00312

-. 00318

-. 00325

-.00331

-.00337

-. 00343

-. 00348

-. 00 354

-.00359

-.00365

-. 00370

-.00375

-. 00330

-.00385

-. 00390

-.00394

80
Table 18. Continued

isobutane isochore at 12.755 MOL/L

T,K

113.550

114.000

115.000

116.000

117.000

116.000

119.000

120.000

121.000

122.000

123.000

124.000

125.000

126.000

127.000

126.000

129.000

130.000

131.000

132.000

133.000

134.000

135.000

136.000

137.000

136.000

139.000

140.000

141.000

142.000

143.000

144.000

145.000

P,8AR

.000

10.043

32.362

54.680

76.997

99.313

121.627

143. 939

166.249

186.556

210.659

233.160

255.457

277.750

300.039

322.323

344.603

366.878

369.148

411.412

433.671

455.924

473.170

500.411

522.645

544.873

567.093

589.307

611.514

633. 713

655.904

678. 089

700.265

OP/DD

1358.639

1363.997

1375. 886

1387. 750

1399.590

1411.406

1423.197

1434.964

1446.707

1458.427

1470. 124

1481.797

1493.447

1505.075

1516.679

1528.262

1539. 822

1551.359

1562. 875

1574.369

1585. 841

1597.292

1606.722

1620.130

1631.518

1642. 884

1654.230

1665.555

1676.860

1688.145

1699.409

1710.654

1721.879

DP/ DT 22 .31 88 22 .31 38 22 .31 84 22 . 31 76 22 .31 65

22 .31 49

22 .31 31 22 .31 09

22 .30 83

22 .3055

22 .30 23 22 .2988

22 .29 51 22 .29 10 22 .28 67 22 .2822

22 .27 74 22 .2723

22 .26 70 22 .26 15 22 .2558

22 .2499

22 . 2437

22 .23 74 22 .23 08 22 .22 41 22 .21 72 22 . 21 01 22 .20 29

22 .19 55 22 .18 79 22 . 18 02

22 .17 24

02P/0T2

.00000

-.00018

-. 00058

-, C0097

-. 00134

-.00170

-. 00205

-. C0238

-. 00270

-.00302

-. 00332

-.00361

-.00389

-.00417

-. 00443

-. 00468

-. C0493

-.00517

-. 00540

-. 00562

-.00584

-. 00605

-. 00625

-. 00644

-. 00663

-. 00681

-. 00699

-. 00716

-.00732

-. C0748

-.00764

00779

-.00793

ai
TABLE 19. Calculated P(p) isotherms

The following pages give P(p) isotherms, as computed by the equation of

state (6). The third column DP/DD is the isotherm slope (3P/9p) in units of the

bar and mol/L. The last two columns give the isochore slopes and curvatures,

DP/DT = (3P/9T), D2P/DT2 = (92p/3T^) in units of the bar and kelvins.

These tables show that 9P/9p is non-negative, and that it increases

monotonical ly with density.

82
Table 19. Calculated P(p) isotherms

ISOBUTANE ISOTHERfi AT 120.00 DEG. K MOL/L P, BAR DP/00 OP/OT D2P/DT2

.000 .000 9.977 . 0000 -.000000

12. 649 -.000 1284. 023 21.1068 .000000

12.650 1.270 1285.354 21.1176 -.000021

12.660 14.191 1298.888 21.2278 -.000234

12.670 27. 249 1312.567 21.3388 -.0 0C450

12.630 40.443 1326.391 21.4504 -.000668

12.690 53.777 1340.365 21.5627 -.000888

12.700 67. 251 1354.489 21.6758 -.001111

12. 710 80.867 1 368. 765 21.7896 -.001336

12. 720 94.627 1383.197 21.9041 -. 001564

12. 730 108.532 1397. 787 22.0194 -. 001794

12.740 122.563 1412.536 22.1354 -.002026

12.750 136. 783 1427.447 22.2522 -. 0 02262

12. 760 151.133 1442. 523 22.3697 -.002499

12.770 165. 634 1457.766 22.4881 -. 002740

83
Table 19. Continued

ISOBUTANE isotherm AT 140.00 DEG.

MOL/L

.000

12. 320

12.320

12.330

12.340

12.350

12.360

12.370

12.380

12.390

12.400

12.410

12.420

12.430

12.440

12.450

12.460

12.470

12.480

12.490

12.500

12.510

12.520

12.530

12.540

12.550

12.560

12.570

12.580

12.590

12.600

12.610

12.620

12.630

12.640

12.650

12.660

12.670

12.680

12.690

12. 700

12.710

12.720

12. 730

12. 740

12. 750

12. 760

12. 770

12. 780

12.790

12. 800

12.810

12.820

12.830

P.BAR

.000

.000

.296

11.197

22. 205

33.323

44.551

55.890

67.341

78.906

90.585

102.379

114. 290

126. 319

138.467

150. 735

163.124

175.636

188. 271

201.031

213.917

226.930

240.072

253.344

266. 746

280. 280

293. 950

307. 754

321. 695

335. 774

349.992

364. 351

378. 652

393.496

408.286

423. 222

438.307

453.541

468.927

484. 465

500.158

516.008

532.015

548.181

564.509

581.000

597.656

614.478

631.468

648.629

665.962

683.469

701.152

719.013

DP/OD

11.639

1084.373

1084. 665

1095.427

1106.289

1117.254

1128.323

1139.497

1150. 777

1162.165

1173.662

1135,269

1196.988

1208. 820

1220.767

1232, 331

1245.011

1257.312

1269.732

1282.276

1294.943

1307.735

1320.655

1333,704

1346. 884

1360.195

1373.642

1387.225

1400. 945

1414.306

1428. 80 8 1442. 954

1457.246

1471, 685

1486.275

1501.017

1515.912

1530. 965

1546.176

1561. 547

1577.083

1592. 784

1608.653

1624.692

1640.905

1657.294

1673.861

1690.610

1707.542

1724.661

1741. 969

1759.470

1777.167

1795.062

OP/OT

.0000

17.8901

17.8925

17.9797

18.0674

18.1556

18.2443

18.3336

18.4234

18.5137

18.6045

18.6959

18.7878

18.8802

18.9732

19.0668

19.1609

19.2555

19.3507

19.4465

19.5429

19.6398

19.7374

19.8355

19.9342

20.0335

20.1334

20.2339

20.3351

20.4368

20,5392

20.6422

20.7459

20.8501

20.9551

21.0607

21.1669

21.2738

21.3814

21.4896

21.5986

21.7082

21.8185

21.9295

22. 0412

22.1536

22.2668

22.3807

22.4953

22.6106

22. 7267

22.8436

22.9612

23.0796

K D2P/DT2

-.000000

.000000

-.000004

-.000135

-.000267

-.00040

1

-.000536

-.000673

-.000811

-.000950

-.001091

-.001234

-.001378

-.001523

-.001670

-.001818

-.001968

-.002120

-.002273

-.002427

-.002583

-.002741

-.002901

-.003062

-.003225

-.003389

-.003555

-. 003 723 -.003892

-.004064

-.004237

-.004412

-. 00458 e -.004767

-.004947

-.005129

-.005313

-.005499

-.005687

-.005877

-.006068

-.006262

-.006458

-.006656

-.006855

-.007057

-.007261

-.007467

-.007675

-.007836

-.008098

-.008313

-.008530

-.008749

84
Table 19. Continued

ISOBUTANE isotherm AT 160.00 DEG. K MOL/L P.BAR OP/DO OP/DT 02P/0T2

.000 .001 13.293 . 0 0 00 -.000000

11.989 .001 920. 843 15.2991 .000000

12.000 10.449 930.745 15.3789 -.000095

12.020 29.241 948.530 15.5214 -. 000267

12.040 48. 392 966.619 15.6654 -.000442

12. 060 67.908 985.021 15.8111 -.000621

12.080 87. 795 1003.742 15.9582 -.000803

12.100 108.060 1022. 789 16.1070 -. 000989

12. 120 128.709 1042.169 16.2575 -.0 01179

12.140 149. 749 1061. 890 16.4095 -.001372

12.160 171.187 1081. 959 16.5633 -. 0 01570

12.180 193.029 1102. 385 16. 7187 -.001771

12. 200 215.284 1123.175 16. 6759 -.001976

12.220 237.959 1144.338 17.0348 -.002135

12.240 261.060 1165.883 17.1955 -.002399

12.260 284.597 1187. 819 17.3580 -.002616

12.280 308.576 1210.155 17.5223 -. 002838

12.300 333.006 1232.900 17.6884 -.003064

12.320 357. 995 1256.066 17.8564 -.003295

12.340 383. 251 1279.661 18 .0264 -.003530

12.360 409.084 1303.696 18.1983 -.003770

12.380 435. 402 1328. 163 13.3721 -. 004014

12.400 462.214 1353.132 18 .5480 -. 004263

12.420 489.531 1378.556 18.7258 -.00451

e

12.440 517. 360 1404.466 18.9058 -.004777

12.460 545.713 1430.876 19.0878 -.005041

12.480 574.598 1457. 797 19.2719 -. 0 05310

12.500 604. 028 1435.244 19.4583 -.005535

12.520 634.012 1513.230 19.6468 -.005865

12.540 664 . 561 1541. 769 19.6375 -. 0 06150

12.560 695.685 1570. 877 20.0306 -. 0 06441

85
Table 19. Continued

IS03UTANE ISOTHERM AT 180.00 DEG. K

MOL/L P,BAR DP/DO OP/OT 02P/0T2

.000 .007 14.918 . 0000 -.000000

11.655 .007 783.101 13.1630 .000000

11. 660 4.213 786.986 13. 1941 -.000030

11.680 20.099 801. 636 13.3110 -. 000144

11.700 36.280 816.517 13.4291 -.000260

11. 720 52. 761 83 1. 634 13.5484 -.000378

11. 740 69.547 846.992 13.6689 -. 0 00 498

11. 760 86. 642 862.595 13.7906 -.000621

11. 780 104.052 878.448 13.9136 -. 000746

11.800 121.782 394.556 14.0378 -.000874

11.820 139.836 910.924 14.1634 -. 0 01 0 04

11. 840 153. 221 927,557 14.2902 -.001137

11.860 176. 940 944.461 14.4183 -.001272

11.880 196. 001 961 . 641 14.5477 -.001410

11.900 215.408 979.103 14.6785 -. 0 01550

11 . 920 235.167 996. 852 14.8106 -, 001693

11. 940 255. 284 1014. 895 14.9442 -.001839

11.960 275. 765 1033.238 15.0791 -. 0 01988

11.980 296,615 1051. 386 15.2154 -. 002139

12.000 317.842 1070.847 15.3532 -.002293

12.020 339. 451 1090.126 15.4924 -. 002450

12.040 361.449 1109. 732 15.6331 -. 0 02611

12.060 383. 843 1129.671 15.7753 -. 0 02774

12.080 406.639 1149.949 15.9190 -.002940

12.100 429. 843 1170. 576 16.0643 -, 003109

12.120 453 .464 1191. 558 16.2111 -.003282

12.140 477,508 1212. 903 16.3595 -.003458

12.160 501.983 1234.620 16.5095 -.003637

12.180 526.895 1256.71 7 16.6611 -.003819

12.200 552.254 1279. 202 16. 8143 -.004005

12.220 578.066 1302.085 16.9693 -.004194

12.240 604. 340 1325.375 17.1259 -.004387

12.260 631.084 1349.082 17.2842 -.004583

12.280 658. 306 1373.215 17 . 4443 -. 0 04783

12.300 686.015 1397.784 17.6062 -. 0 04987

12.320 714. 220 1422. 801 17.7698 -.005195

86
Table 19. Continued

MOL/L

.002

11.316

11.320

11.340

11.360

11. 380

11.400

11.420

11.440

11.460

11.480

11.500

11.520

11.540

11. 560

11.580

11.600

11.620

11.640

11.660

11.680

11.700

11. 720

11.740

11.760

11.780

11.800

11 . 820

11.840

11.860

11.880

11.900

11.920

11.940

11.960

11.980

12.000

12.020

12. 040

12.060

ISOBUTANE ISOTHERM AT 200.00 DEG. K P,BAR

.037

.037

2.897

16. 360

30.071

44.032

58.247

72. 719

87.454

102.454

117. 723

133.267

149.088

165.191

181.580

198. 260

215.236

232.510

250.089

267.977

286. 179

304.699

323. 543

342. 715

362.221

362. 066

402. 255

422. 794

443.689

464.945

486.567

508. 562

530.936

553.696

576.846

600.394

624. 346

648.709

673.490

698.696

DP/00

16.480

664.476

667. 082

679.326

691.751

704. 360

717.158

730.146

743.328

756.708

770.290

784. 376

798. 07 0 812.277

826.700

841.343

856.210

371.305

886.632

902.197

918.002

934.054

950.356

966. 913

933.731

1000.813

1018. 167

1035.796

1053.707

1071. 904

1090.395

1109.184

1128. 278

1147.663

1167.406

1187.453

1207. 831

1226.547

1249.609

1271.023

OP/DT

. 0 0 02 11.3689

11.3896

11.4868

11.5850

11.6841

11.7841

11.8852

11.9872

12.0901

12.1941

12.2992

12.4052

12.5123

12.6204

12.7296

12.8398

12.9512

13. 0637

13.1772

13.2919

13.4078

13.5248

13.6429

13. 7623

13.8829

14.0046

14.1276

14.2519

14.3774

14.5042

14.6323

14.7617

14.8924

15.0245

15.1579

15.2927

15.4289

15 .5666

15.7056

D2P/DT2

-.000000

.000000

-. 000016

-.000094

-.000172

-.000253

-.000335

-.000418

-.000503

-.000590

-.000676

-.000768

-.000860

-.000953

-.001043

-. 001145

-.001244

-.001345

-.001447

-.001552

-. 001658

-.001766

-.001 877

-.001989

-.002103

-. 002220

-.002338

-.002459

-.002582

-.002707

-.002834

-. 002964

-.003096

-. 003231

-.003367

-. 0 03507

-.003648

-. 0 03 79 3 -. 0 0 3940

-. 004089

87
Table 19. Continued

ISOBUTANE ISOTHERM AT 220.00 DEG. K MOL/L

. 008

10.970

10.980

11.000

11.020

11.040

11.060

11.080

11. 100

11.120

11.140

11.160

11.180

11.200

11.220

11.240

11.260

11.280

11. 300

11.320

11.340

11.360

11.380

11.400

11.420

11.440

11.460

11.480

11.500

11.520

11.540

11.560

11.580

11.600

11.620

11. 640

11.660

11.680

11.700

11 . 720

11. 740

11.760

11.780

11.800

11.820

P.BAR

.137

. 137

6.036

17.456

29.084

40.924

52.977

65.248

77.739

90.453

103.394

116.565

129.969

143.609

157.489

171.612

185.981

200.601

215.475

230.607

246.000

261.658

277.585

293. 784

310.261

327. 019

344.062

361.394

379.020

396.944

415.170

433.703

452.548

471.709

491.191

510.999

531.138

551.613

572.429

593.591

615. 105

636.976

659.209

681. 811

704. 786

OP/OD

17.940

560. 491

565.847

576.185

586.668

597.299

606.081

619.015

630.105

641.352

652.760

664.330

676. 065

687.969

700. 043

712.291

724.715

737.319

750.105

763. 077

776.237

789.588

803. 135

816. 881

830.828

844.980

859.342

873.915

888.706

903. 716

918.951

934.414

950.109

966.041

982.214

998.632

1015.300

1032.222

1049.405

1066. 051

1034.567

1102.557

1120.328

1139. 384

1158.231

OP/DT

. 0006

9.8380

9.8805

9.9622

10.0447

10.1279

10.2119

10.2967

10. 3822

10 .4686

10.5557

10.6437

10.7325

10.8221

10.9126

11.0039

11.0961

11.1891

11.2830

11.3778

11.4735

11.5701

11.6677

11. 7661

11.8655

11.9659

12.0672

12.1695

12.2727

12.3770

12.4822

12.5885

12.6958

12.8042

12.9136

13.0240

13.1356

13.2482

13.3620

13.4769

13.5929

13.7100

13.8233

13.9478

14.0685

D2P/0T2

-.000000

.000000

-.000028

-.000081

-.000136

-.000192

-.000249

-.000306

-.000365

-.000426

-.000487

-.000545

-.000613

-.000670

-.000744

-.000811

-.000875

-.000949

-.001020

-.001093

-.001166

-. 001241

-.001318

-.001395

-.001474

-.001555

-.001637

-. 001720

-.001805

-.001892

-.001980

-.002069

-.002161

-.002253

-.002348

-.002444

-.002542

-.002641

-.002742

-.002045

-. 0 02950

-.003056

-.003165

-.003275

-.003387

88
TaBle 19. Continued

ISOBUTANE ISOTHERM AT 250.00 OEG. K MOL/L P,8AR DP/00 OP/OT 02P/0T2

.0 J1 .632 19.728 .0 027 -.000001

10.430 .632 425.563 7.9149 .000000

10.440 5.052 429.631 7.9473 -.000016

10.480 22.556 445.642 8. 0741 -.000078

10.520 40.709 462.086 8.2031 -.000144

10.560 59.528 478. 976 8.3344 -.000211

10.600 79.033 496.325 8 .4680 -. 0 00282

10.640 99. 241 514.146 8.6039 -.000355

10.680 120.171 532.451 8.7423 -.000431

10.720 141.843 551.254 8.6832 -.000509

10.760 164.278 5 7 0 . 57 0 9.0265 -.000591

10.000 187.496 590. 414 9.1724 -. 000676

10.840 211.519 610. 80 0 9.3210 -.000764

10.880 236.368 631. 746 9.4722 -.000855

10.920 262.065 653.267 9.6261 -. 000949

10.960 288.636 675.382 9.7828 -.001047

11.000 316.104 698.108 9.9424 -.001148

11. 040 344.494 721.464 10.1048 -.001253

11.060 373. 830 745.469 10.2702 -.001361

11.120 404. 140 770.145 10.4387 -.001473

11.160 435. 451 795.512 10.6102 -.001590

11.200 467. 791 321. 593 10.7849 -.001710

11.240 501.188 848.410 10.9628 -. 001834

11.280 535. 674 875.989 11.1440 -.001963

11.320 571.278 904.354 11.3286 -.002096

11.360 608. 033 933.532 11.5166 -.002233

11.400 645.972 963.550 11.7081 -.002375

11.440 685.128 994.438 11.9033 -.002522

S3
Table 19. Continued

ISOBUTANE ISOTHERM AT 300.00 DEG.

MOL/L P.BAR

. 040 .975

. 080 1.908

.120 2.792

. 160 3.627

.165 3.736

9.434 3, 736

9.440 5.313

9.480 15. 301

9.520 25. 685

9.560 36.475

9.600 47. 683

9.640 59.320

9.630 71.397

9.720 83.925

9. 760 96.917

9.800 110.386

9. 840 124. 343

9.880 138.801

9.920 153. 774

9.96 0 169.276

10.000 185. 320

10.040 201.920

10.080 219. 091

10,120 236. 848

10 . 160 255.205

10.200 274. 180

10.240 293.787

10 . 280 314. 044

10.320 334.967

10.360 356. 573

10.400 378.881

10.440 401. 908

10.480 425. 674

10.520 450.197

10. 560 475.497

10.600 501.595

10 . 640 528. 512

10.680 556.268

10.720 584. 886

10.760 614.389

10.800 644.799

10. 840 676.141

10.380 708.440

DP/00 OP/OT

2 2.876 .0034

2 2. 718 . 0070

21.491 .0109

20.242 .0149

20.072 .0155

243.289 5.3965

244.841 5.4096

254.607 5.4916

264.636 5.5748

274.935 5.6595

285.509 5.7455

296. 367 5.8329

307.514 5.9217

318.958 6.0120

330. 705 6.1038

342.763 6.1970

355.140 6.2918

367.842 6.3832

380.879 6.4861

394.258 6.5857

407. 988 6.6869

422.076 6.7899

436.534 6.8945

451.368 7.0009

466.589 7.1090

432.207 7.2190

498.232 7.3308

514.674 7.4445

531.543 7.6601

548. 352 7.6777

566.611 7.7973

584.832 7.9189

603. 528 8.0426

622. 711 8.1634

642.394 8.2964

662.592 8.4266

683.317 8.5590

704.586 8.6937

726.413 8.6307

748.313 8.9701

771. 804 9.1120

795.402 9.2563

819.625 9.4031

K 02P/0T2

-. 000001

-.000003

-.000006

-.000013

-.000014

.000001

-.000003

-.000027

-.000053

-.000079

-.000106

-.000135

-.000165

-.000196

-.000228

-.000261

-.000295

-.000331

-.000366

-.000407

-.000447

-.000488

-.000531

-.000576

-.000622

-. 000670

-.000719

-. 0 00 77 0 -.000823

-.000878

-.000934

-.000993

-.001053

-.001116

-. 001180

-.001247

-. 001316

-.001387

-.001461

-.001537

-.001615

-.001696

-. 001779

90
Table 19. Continued

ISOBUTANE ISOTHERM AT 350.00 DEG. K MOL/L P.BAR OP/00 OP/OT 02P/0T2

. 060 2. 257 27.298 .0069 -.0 C0 0 02 .160 4. 36 0 25.261 .0145 -. 000006

. 240 6.299 23.219 . 0226 -.000015

.320 8.076 21.214 .0313 -.000028

.400 9. 694 19. 254 .0 406 -.000047

.480 11.158 17.342 .0 505 -.000075

.560 12.470 15.477 .0612 -.000116

.571 12.636 15.229 .0627 -.000124

8.180 12.636 105.031 3.3919 .000056

6.240 19.106 112.395 3.4675 .000035

8. 320 28.510 122. 782 3.5715 .000009

8.400 36.767 133. 757 3.6784 -.000018

8.430 49.927 145.352 3.7883 -.000044

8.560 62.041 15 7.599 3.9015 -.000071

8.640 75. 161 170.530 4.0179 -.000098

8.72 0 89.345 134.180 4.1378 -.000126

8.600 104. 650 198.584 4.2613 -.000156

8.880 121.139 213.779 4.3885 -.000188

8.960 138.877 229.804 4.5197 -.000221

9. 040 157.931 246.697 4.6548 -. 000257

9.120 176.373 264.501 4.7941 -. 000295

9.200 200.277 23 3.259 4.9376 -.000335

9.280 223.721 303.015 5.0859 -.000378

9. 360 248.787 323. 816 5.2388 -.000424

9 . 440 275.561 345.712 5.3964 -. 000474

9.520 304.131 368.754 5.5591 -.000526

9.600 334. 593 392.996 5.7270 -.000582

9.680 367. 044 418.494 5.9002 -. 000642

9.760 401. 587 445. 309 6.0791 -. 000706

9. 84 0 438.331 473.504 6.2637 -.000774

9.920 477.387 503.144 6.4544 -.000847

10.000 516.874 534.300 6.6513 -.000924

10.080 562.917 567.046 6.8546 -.001007

10.160 609.646 601.462 7.0647 -.001094

10.240 659.193 637.631 7.2817 -.0 01137

10.320 711. 716 675.642 7.5060 -. 001286

91
Table 19. Continued

ISOBUTANE ISOTHERM AT 400.00 DEG. K

MOL/L P,8AR OP/OD DP/OT D2P/0T2

.160 5.076 30.059 .0142 >.000004

. 320 9.611 26.645 . 0302 -.000017

.48 0 13. 613 23.411 .0479 -.000038

.640 17.114 20.388 . 0674 -.000069

. 800 20.149 17.591 . 0864 -.000111

.960 22.755 15.023 .1111 -. 000163

1.120 24. 968 12.681 .1353 -.000231

1.260 26.825 1 0 . 56 0 .1610 -.000317

1.440 28.359 8.652 .1881 -. 0 00430

1.600 29.604 6. 945 .2166 -.000588

1.760 30. 592 5.427 .2464 -.000829

1.920 31. 350 4.084 .2778 -.001265

2.065 31.862 3.004 .3080 -.002206

5.893 31.862 6.577 1.3435 .003022

5.920 32.103 9.165 1.3608 .002779

6.060 33.870 13.047 1.4646 .001860

6.240 36. 319 17.707 1.5736 .001356

6. 400 39.581 23.214 1.6880 .001023

6.560 43.797 29.635 1.6079 .000780

6.720 49.117 37. 037 1.9335 . 0 00 593

6.880 55. 705 45.495 2.0647 .000442

7.040 63. 736 55.091 2.2016 .000318

7.200 73. 400 65.923 2.3451 .000214

7.360 84. 903 78.106 2.4949 .000127

7.520 98.473 91.771 2.6518 .000053

7.680 114. 357 107.069 2.8163 -.000012

7. 640 132.831 124.170 2.9892 -.000069

6. 000 154.198 143. 262 3 .1711 -. 0 00123

6. 160 178.792 164.550 3.3629 -.000174

8.320 206. 983 188.260 3.5655 -.000225

8.480 239. 177 214.633 3.7797 -.000278

6.640 275.821 243. 929 4.0065 -.000334

6.800 317.405 276.431 4.2469 -.000396

6.960 364.467 312.444 4.5019 -.000464

9.120 417.592 352.297 4.7726 -. 0 00540

9.280 477.426 396.351 5.0602 -.000626

9.440 544, 67U 445. 000 5.3659 -.000722

9.600 620.094 496.677 5.6910 -.000830

9. 76 0 704. 540 557. 858 6,0370 -.000951

92
Table 19. Continued

IS08UTANE ISOTHERH AT «408.00 OEG. K MOL/L P, BAR OP/OD OP/OT D2P/DT2

. 160 5. 190 30. 812 .0142 -.000004

. 320 9.852 27.485 . 0301 -. 0 00016

.490 13.995 24.335 .0476 -.000036

.640 17.650 21.395 .0668 -. 000064

. 800 20.853 18.677 .0876 -.000100

.960 23.639 16.185 .1099 -.000146

1.120 26.044 13.915 .1336 -.000202

1.28 0 28.103 11.863 .1587 -.000268

1.440 29. 851 10.019 .1850 -.000347

1.600 31.320 8.372 .2126 -.000442

1. 760 32.540 6.911 .2411 -.000556

1.920 33.541 5.623 .2706 -.000694

2.080 34.348 4.498 . 3008 -.000867

2.240 34. 989 3.523 .3316 -.001088

2.400 35.483 2. 68 8 .3628 -. 001380

2.560 35.855 1.984 .3944 -.001782

2. 720 36.125 1.401 .4260 -.002362

2.880 36. 310 .932 .4576 -.003253

3. 040 36.429 .570 .4890 -.004734

3.200 36.498 .308 .5200 -.007475

3. 36 0 36. 532 .136 .5504 -.013393

3.520 36.545 .042 .5799 -.029910

3.680 36.549 . 006 .6080 -.109439

3.840 36.549 .000 .6324 -13.908881

4. 000 36.549 .002 .6540 .217478

4.160 36.551 . 024 .6842 . 052444

4.320 36.559 . 093 .7192 .023759

4.480 36.585 .241 .7589 .013714

4.640 36. 643 .510 . 8036 . 009007

4.800 36.757 .947 .8536 .006409

4.96 0 36. 958 1.60 9 .9093 .004813

5.120 37.287 2.559 . 9711 .003754

5.280 37. 796 3. 865 1.0390 .003007

5. 440 38.547 5.600 1.1135 . 00245 3 5.600 39.614 7. 83 6 1.1944 .002025

5.760 41.085 10. 648 1.2819 . 001681

5.920 43. 056 14.105 1.3759 .001397

6. 090 45. 637 18.277 1.4761 .001157

6.240 48.946 23.228 1.5826 .000951

6.400 53.115 29.026 1.6951 .000772

6. 560 58. 283 35.734 1.8135 .000616

6.720 64.602 43.425 1.9377 . 000480

6. 680 72.236 52.176 2.0679 .000360

7.040 81. 360 62.076 2.2041 .000257

7.200 92.167 73.229 2.3466 .000166

7. 360 104. 966 85.754 2.4958 .000068

7.520 119.689 99.788 2.6521 .000019

7.680 136.887 115.486 2.8161 -.000042

7.840 156.742 133.022 2.9885 -.000098

8.000 179. 563 152.588 3.1700 -.000150

8.160 205.690 174. 392 3.3614 -.000200

8.320 235.500 198.661 3 .5636 -.00025

1

8.480 269.406 225.639 3.7774 -.000304

8.640 307. 863 255.589 4.0037 -.000361

9.900 351. 368 28 8. 794 4.2436 -.000423

8.960 400.467 325.563 4.4981 -. 000491

9. 120 455. 756 366. 226 4.7682 -.000568

9.280 517. 887 411.154 5 .0551 -. 0 00 65 3 9.440 587. 573 460. 739 5.3600 -.000749

9.600 665.595 515.4l9g3 5.6843 -. 000656
Table 19. Continued

ISOaUTflNE ISOTHERM AT 410.00 OEG. K MOL/L P.SAR OP/00 DP/OT 02P/0T2

. 160 5.213 31.000 .0142 -.000004

. 320 9.912 27.694 .0300 -.000015

.480 14.090 24.564 .0476 -.000035

. 640 17. 784 21. 644 . 0667 -.000062

. 300 21.028 18. 945 .0874 -.000098

.960 23.858 16.472 .1096 -.000142

1.120 26.311 14.220 .1332 -.000196

1.280 28. 420 12.184 .1582 -. 000259

1.440 30.221 10.355 .1844 -.000333

1.600 31. 744 8.722 .2117 -. 000419

1. 760 33.021 7.272 .2400 -.000519

1.920 34.081 5.995 .2692 -.000637

2.080 34.948 4. 377 . 2991 -. 000774

2.240 35.649 3.908 .3296 -.000934

2.400 36.206 3.077 .3604 -.0 01120

2.560 36.641 2.374 .3913 -.001331

2. 720 36.973 1. 791 .4222 -. 001562

2. 680 37. 220 1.318 .4529 -.001790

3 . 040 37.400 .95 0 .4831 -.001968

3.200 37.529 .679 .5129 -.002019

3.360 37.622 .498 .5421 -.001858

3.520 37. 693 . 397 .5711 -.001448

3.680 37. 752 .359 .6003 -.000833

3.840 37.810 .363 .6303 -.000098

4.000 37.869 .384 .6615 .000694

4.160 37. 934 .438 .6945 .001488

4. 320 38.013 .552 .7303 . 0 02184

4.480 38. 116 .756 .7695 . 002676

4.640 38. 261 1.088 .6132 . 0 02913

4.800 38.473 1.596 .8620 .002921

4.960 38. 784 2.333 .9165 . 002768

5.120 39.236 3.362 .9772 . 002530

5.280 39.879 4.749 1.0442 . 002258

5.440 40.773 6.566 1.1179 .001986

5.600 42.007 8. 885 1.1982 . 001727

5.760 43.652 11.778 1.2851 . 001437

5.920 45.811 15.316 1.3785 . 001269

6.080 48.591 19.566 1.4784 . 001070

6.240 52.113 24.595 1.5844 . 000891

6.400 56.507 30. 467 1.6966 . 000730

6. 560 61. 911 37.249 1.8147 . 000586

6.720 68.479 45.014 1.9387 . 000457

6.880 76.372 53.339 2.0686 .000343

7. 040 65. 769 63. 816 2.2046 . 000243

7.200 96.861 75.050 2.3469 . 000156

7. 360 109.858 87.661 2.4959 .000079

7.520 124.993 101. 788 2.6521 .000011

7. 680 142.519 117.586 2.8160 -. 000049

7. 840 162. 719 135.232 2.9883 -.000104

a. 000 185.902 154. 917 3.1697 -.000156

8.160 212. 412 176. 850 3.3610 -.000207

8.320 242.626 201.258 3.5631 -.000258

8.480 276.960 223.337 3. 7768 -.000311

3.640 315.869 258.500 4.0030 -.000367

8.800 359. 854 291.881 4.2428 -. 000429

3.960 409. 462 328.338 4.4971 -.000498

9.120 465. 291 369.706 4.7670 -.000574

9.280 527.996 414. 849 5.0538 -.000659

9.440 598.292 464.667 5.3585 -.000755

9.600 676.962 519.597 , 5.6325 -.000862

94
Table 19. Continued

ISOBUTANE ISOTHERM AT 420.00 DEG. K MOL/L P,BAR DP/DO DP/DT D2P/0T2

. 160 5. 360 31.937 .0141 -.000004

. 320 10.212 28.733 , 0299 -.000014

.480 14.564 25.703 .0472 -.000032

. 640 18.448 22,880 .0661 -.000057

.800 21.897 20.274 . 0865 -.000086

. 960 24.947 17. 89 0 .1082 -. 000126

1.120 27,633 15. 722 .1314 -.000171

1.280 29.990 13. 764 .1558 -.000222

1.440 32. 049 12.007 .1813 -. 0 0027 e 1.600 33.842 10. 438 .2079 -.000339

1. 760 35.398 9. 044 .2355 -.000404

1.920 36. 745 7. 812 .2638 -.000470

2.060 37. 906 6. 731 .2928 -.000536

2.240 38.906 5.788 .3223 -.000597

2.400 39. 765 4. 972 .3521 -.000650

2.560 40.503 4.275 . 3821 -.000689

2.720 41.139 3.688 .4123 -.000708

2.880 41.669 3.207 .4425 -.000701

3. 040 42.171 2.829 .4726 -. 000663

3.200 42. 600 2.553 .5032 -.000593

3.360 42.993 2.379 .5338 -.000490

3.520 43.366 2.302 .5650 -.000358

3.680 43. 734 2.313 .5968 -.000202

3 . 840 44. 110 2.390 .6298 -.000028

4.000 44. 502 2.514 .6643 . 0 00 15 9 4. 160 44. 913 2. 706 . 7008 .000353

4.320 45.373 2.999 .7397 . 000545

4.480 45.885 3.426 .7818 .000726

4.640 46.479 4. 027 . 6275 .000885

4.800 47.185 4.844 .8777 .001013

4.960 48. 043 5. 926 .9328 . 001104

5.120 49.098 7.328 .9933 .001153

5. 280 50.408 9.10 9 1.0598 . 0 01163

5.440 52.037 11.332 1.1325 .001136

5.600 54.061 14.062 1.2116 . 001079

5.760 56.567 17.365 1.2971 . 000999

5.920 59.652 21.308 1.3891 .000903

6. 080 63. 423 25.954 1.4875 .000796

6.240 67. 993 31.369 1 .5922 .000686

6.400 73.506 37.620 1.7030 . 000575

6.560 60. 065 44. 776 1.8199 .000467

6.720 87.887 52.913 1.9427 .000365

6.830 97.074 62.116 2.0716 .000271

7.040 107. 826 72.483 2.2067 .000185

7.200 120.337 34.126 2.3482 .000107

7.360 134. 821 97.171 2.4965 .000038

7.520 151.514 111. 764 2.6520 -.000025

7.680 170.677 128.068 2.8154 -. 000083

7.840 192.596 146.261 2.9671 -. 0001 36 6.000 217.591 166.540 3.1680 -.000186

8.160 246.012 189.118 3.3588 -. 000236

8.320 273.244 214.225 3.5604 -.000287

6.460 314.712 242. 108 3.7735 -.000340

8.640 355.881 273.034 3 .9992 -.000397

8.800 402. 260 30 7.290 4.2383 -.000459

8.960 454, 407 345. 137 4.4920 -.000528

9.120 512.932 337. 064 4.7612 - . 000604

9.280 578.500 433. 29 1 5.0470 -.000639

9.440 651. 839 484.270 5.3508 -.000784

95
Table 19. Continued

ISOBUTANE ISOTHERM AT 450.00 OEG. K MOL/L PtBAR OP/00 OP/OT 02P/0T2

.160 5. 782 34.722 .0140 -.000003

.320 11.103 31.801 .0295 -.000011

.460 15.968 29. 045 .0 464 -.000025

.640 20.406 26.468 .0646 -.000043

.600 24. 455 24.139 .0842 -.000066

.960 28.143 22. 000 .1050 -.000093

1.120 31.506 20.064 .1270 -.000124

1.260 34.574 18.324 .1502 -.000156

1.440 37.379 16.766 .1745 -.000191

1.600 39.949 15.378 .1997 -.000225

1. 760 42.309 14.145 .2259 -.000259

1.920 44.463 13.054 .2529 -.000290

2.060 46.493 12.092 .2807 -.000318

2.240 48.358 11.249 .3091 -.000340

2.400 50.096 10. 516 .3382 -.000354

2.560 51. 729 9.888 .3678 -.000361

2.720 53.266 9.364 .3979 -.000357

2.660 54.731 8.946 .4286 -.000342

3.040 56.136 8.640 .4598 -.000316

3.200 57.502 8.456 .4917 -.000279

3.360 58.849 8.403 .5244 -.000230

3.520 60.199 8.489 .5580 -.000170

3.660 61.573 8.713 .5928 -.000102

3. 640 62.994 9.063 .6291 -.000026

4.000 64.480 9.529 .6671 .000055

4.160 66.051 10.144 .7071 .000140

4.320 67. 736 10.951 .7497 .000225

4.480 69.566 11.993 .7952 .000307

4.640 71.583 13.309 .8442 .000383

4.600 73.844 14.942 .8970 .000450

4.96 0 76.389 16.934 .9542 .000505

5.120 79.284 19.329 1.0163 .000546

5.280 62.598 22. 171 1.0834 .000570

5. 440 86.405 25.507 1.1561 .000577

5.600 90.769 29.383 1.2345 .000567

5.76 0 95.839 33. 850 1.3188 .000542

5.920 101. 655 38.958 1.4091 .000503

6.060 108.343 44. 763 1.5054 .000452

6.240 116.019 51.326 1.6078 .000393

6.400 124. 811 58.712 1.7161 .000328

6.560 134.855 66. 999 1.8305 .000260

6.720 146.303 76.273 1.9508 .000192

6.680 159. 321 86.633 2.0774 .000124

7.040 174.090 98.196 2.2103 .000060

7.200 190. 814 111.090 2.3497 -.000001

7.360 209.718 125.463 2.4961 -.000058

7.520 231.050 141.477 2.6499 -.000112

7.660 255.087 159.310 2.8116 -.000162

7.640 282.137 179.157 2.9819 -.000211

8.000 312.536 201.224 3.1613 -.000259

6.160 346.659 225.735 3.3506 -.000308

6.320 384.914 252.930 3.5506 -.000358

8.480 427.753 283.064 3.7622 -.000411

8.640 475.666 316.412 3.9862 -.000468

6.600 529.192 353.271 4.2234 -.000530

8.960 588.918 393.963 4.4750 -. 000598

9. 120 655. 483 438.838 4.7419 -.000674

96
Table 19. Continued

ISOBUTANE ISOTHERH AT 500.00 OEG. K MOL/L P.BAR OP/00 DP/DT 02P/0T2

. 160 6. 481 39.297 .0139 -.000002

. 320 12.566 36.781 . 0291 -.000008

.480 18. 260 34.422 . 0 454 -.000017

.640 23. 591 32.253 .0628 -.000029

.800 28.591 30.281 .0815 -.000044

.960 33.292 28.507 .1012 -. 0 00061

1.120 37. 724 26. 923 .1220 -. 0 0008 0 1.280 41.917 25.520 .1440 -.000100

1.440 45.899 24.283 .1669 -.000121

1.600 49.696 23.199 .1908 -.000141

1. 760 53. 330 22.252 .2158 -. 000160

1.920 56.823 21.430 .2416 -.000178

2. 080 60.194 20.722 .2684 -.000192

2.240 63.460 20.120 .2960 -.000204

2.400 66.637 19.61

8

.3246 -.000211

2.560 69. 743 19. 218 . 3540 -.000214

2. 720 72. 793 18.925 .3843 -. 000211

2.880 75.805 18.748 .4155 -.000203

3.040 78.799 18.704 .4477 -.000189

3.200 81. 799 18. 813 .4810 -.000169

3.360 84. 829 19. 097 .5155 -.000142

3.520 87.920 19.574 .5513 -.000111

3.680 91.103 20.255 .5836 -.000074

3.840 94. 412 21.137 .6276 -.000034

4.000 97. 878 22.225 .6685 .000009

4. 160 101.538 23.568 .7116 . 000054

4.320 105.436 25.219 .7573 . 000099

4.430 109.627 27.229 .8058 .000143

4.640 114.171 29.644 .8575 .000183

4.800 119.137 32.503 .9128 .000219

4.960 124.598 35. 846 .9721 .000248

5.120 130.635 39.706 1.0356 .000270

5. 280 137.333 44.114 1 .1036 .000282

5.440 144.782 49.098 1.1766 .000285

5.600 153.077 54.689 1.2547 . 000278

5.76 0 162. 317 60.917 1.3380 .000262

5.920 172.606 67. 818 1.4268 . 000238

6.080 184.057 75.437 1.5211 . 000205

6.240 196.787 93. 327 1 .6211 .000167

6.400 210. 926 93. 056 1 .7268 .000124

6.560 226.614 103.208 1.8384 .000078

6. 720 244. 00 7 114. 381 1.9560 . 000030

6. 880 263.277 126.696 2.0797 -.000019

7.040 284.616 140.287 2.2098 -.000067

7.200 308.246 155.312 2.3466 -.000115

7.360 334.403 171. <=40 2.4904 -.000161

7.520 363.362 190. 359 2.6418 -.000206

7,680 395.424 210. 77 0 2.8011 -.000250

7. 840 430.926 233.386 2 .9690 -.000294

8.000 470.238 258.435 3.1461 -.000339

8.160 513. 768 286.155 3. 3331 -.000386

8. 320 561.963 316. 800 3 .530 7 -.000434

8.430 615. 314 350. 642 3.7396 -. 0 00486

8.640 674.354 38 7. 969 3.9607 -. 0 00542

97
Table 19. Continued

ISO0UTANE ISOTHERM AT 550.00 DEG. K MOL/L P.BAR DP/00 DP/OT D2P/0T2

.160 7.175 43.812 .0138 -.000001

. 320 14. 010 41. 644 .0287 -. 000005

.<«ao 20. 510 39.629 .0447 -.000012

.6<*0 26. 701 37.800 . 0616 -. 000020

.800 32.616 36.166 .0796 -.000030

.960 38.285 34.725 .0987 -. 000042

1.120 43. 738 33.470 .1187 -. 000055

1.280 49.004 32.390 .1398 -.000068

1.440 54.111 31.471 .1619 -. 000082

1.600 59.083 30.700 .1850 -.000095

1. 760 63.942 30.061 .2092 -.000108

1.920 68. 709 29.544 .2343 -.000120

2.060 73.402 29.137 .2605 -.000130

2. 240 78.038 28.335 .2877 -.000138

2.400 82.635 28.636 .3159 -. 0 00143

2.560 87. 208 28.545 . 3452 -.000145

2.720 91. 775 28.571 .3756 -.000144

2.880 96.358 28.731 .4071 -.000140

3.040 100.978 29.047 .4399 -.000132

3.200 105. 662 29.546 .4739 -.000120

3. 36 0 110.444 30.258 .5094 -.000104

3.520 115.358 31.210 .5464 -.000086

3.630 120.445 32.419 .5852 -.000064

3. 84 0 125. 746 33.891 .6257 -. 000040

4. 000 131. 304 35.638 .6683 -.000014

4. 160 137. 168 37.723 .7132 . 000013

4.320 143.397 40.209 .7606 . 000040

4.480 150.059 43.151 .8108 .000065

4.64 0 157.232 46.598 .8641 .000089

4. 800 165.000 50.592 .9208 .000109

4.960 173. 453 55.170 .9811 . 000125

5.120 182.687 6 0. 35 9 1.0454 .000136

5.280 192.801 66.182 1.1139 . 000141

5.440 203. 900 72, 660 1.1869 . 000140

5.600 216.088 79. 310 1.2646 . 000132

5.760 229.476 87,654 1.3472 .000118

5.920 244.176 96,218 1.4349 .000098

6.080 260 .306 105.541 1. 5278 . 000073

6. 240 277.992 115.673 1.6261 . 000043

6.400 297. 369 126.684 1. 7299 .000009

6.560 318.583 138.663 1 .8395 -.000027

6.720 341. 798 151. 721 1.9549 -.000065

6. 880 367. 198 165. 939 2.0764 -.000104

7.040 394. 983 181. 624 2.2044 -. 0 00143

7.200 425.400 198.797 2.3390 -. 0 0018 3 7.360 458. 695 217.700 2.4807 -.000223

7.520 495.167 238.541 2.6300 -.000262

7.680 535.143 261.53 7 2.7872 -.000303

7.840 578.986 286.921 2.9530 -. 0 00343

8.000 627.098 314. 936 3.1279 -.000386

8.160 679.920 345.335 3. 3126 -.000430

98
Table 19. Continued

ISOBUTANE ISOTHERH AT 600.00 OEG. K MOL/L P,BAR OP/00 DP/OT 02P/DT2

. 160 7.866 98.289 .0138 -.000001

. 320 15. 991 96.925 . 0285 -.000009

.980 22.730 99.719 .0992 -.000008

. 690 29.761 93.199 .0608 -.000019

.800 36. 569 91. 876 . 0789 -. 000021

.960 93.172 90.798 .0969 -.000029

1. 120 99.619 39.807 .1169 -. 000038

1.280 55.919 39.093 .1370 -. 000098

1. 990 62.116 38.992 .1 585 -.000057

1.600 68.229 37.991 .1810 -.000067

1.760 79.280 37.675 .2096 -.000076

1.920 80.292 37.989 .2293 -.000089

2.080 86.281 37.908 .2550 -.000091

2.290 92.268 37.999 . 2819 -.000097

2.900 98.269 37.593 .3099 -. 000101

2.560 109. 309 37. 860 .3390 -.000109

2. 720 110. 392 38.261 .3699 -.000109

2.880 116. 556 38. 819 .9011 -.000102

3. 090 122.822 39. 599 .9392 -. 0 0 0 098

3.200 129.223 90.997 .9687 -.000091

3.360 135. 799 91.693 .5098 -.000082

3.520 192.579 93.171 .5926 -.000071

3.680 199. 625 99.951 .5821 -. 000058

3.990 156.981 97. 096 .6236 -.000093

9.000 169.697 99.973 .6673 -.000028

9.160 172.839 52.309 .7132 -.000012

9.320 181. 962 55.621 . 7617 .000009

9.980 190. 661 59. 469 .8129 .000019

9.693 200. 523 63.905 .8670 .000032

9.800 211. 195 68.979 .9295 .000093

9.960 222.630 79.710 .9859 .000051

5.120 235.389 81. 191 1.0500 . 0O0C56

5.280 298.633 88.283 1.1187 .000056

5.990 263.378 96. 152 1.1915 .000052

5.600 279.991 109.760 1.2688 .000093

5. 760 296. 992 119.121 1.3507 .000030

5.920 316.002 129. 259 1 .9375 .000012

6.080 336.798 135.207 1.5292 -.000009

6.290 359. 319 197.017 1 .6261 -.000039

6.900 383.893 159. 761 1.7285 -.000062

6.560 910. 992 173.532 1.8369 -.000092

6.720 939.935 188.952 1.9501 -.000129

6.880 970.866 209.669 2.0698 -.000157

7.090 505.005 222.337 2.1959 -.000191

7.200 592.101 291. 659 2.3237 -.000225

7.360 582.935 262. 839 2.9636 -. 0 0 026 0 7.520 626. 321 286. 098 2.6159 -. 000296

7.680 679.110 311. 672 2.7712 -.000333

99
Table 19. Continued

IS08UTANE isotherm AT 700.00 DEG. K HOL/L P.BAR OP/DO OP/OT D2P/DT2

. 160 9. 240 57.147 .0137 -.000000

. 320 18.277 55.831 . 0282 -.000002

.4S0 27.115 54.675 .0436 -. 0 00004

.6<»0 35.784 53.717 .0596 -.000007

• aoo 44.316 52.968 .0768 -.000011

.960 52. 744 52.426 .0948 -.000015

1.120 61.103 52.067 .1136 -.000020

1.26 0 69.423 51.940 .1335 -.000025

1.44 0 77.733 51. 972 .1543 -.000030

1.600 66.062 52.171 .1762 -.000035

1. 760 94.436 52.524 .1991 -.000040

1.920 102.876 53.023 .2231 -.000045

2. 060 111.411 53.660 .2483 -.000049

2.24 0 120.057 54.435 .2746 -.000053

2.400 128.838 55.352 . 3023 -.000057

2.960 137.777 56.421 .3312 -.000059

2. 720 146.902 57.663 .3615 -.000061

2.660 156. 240 59.102 .3932 -.000061

3.040 165.827 60.773 .4265 -.000061

3. 200 175.702 62. 717 .4614 -.000060

3.360 185.913 64.975 .4980 -.000057

3.520 196.513 67.587 .5364 -.000055

3.680 207.561 70.581 .5767 -.000051

3. 640 219. 120 73.973 .6191 -. 000047

4.000 231.255 77.795 .6637 -.000042

4.160 244. 042 82.137 .7105 -. 000038

4.320 257.571 87. 077 .7599 -.000033

4.480 271.942 92. 681 .8120 -. 0000 30 4.640 287.268 99.011 .8669 -.000027

4.600 303.667 106.112 .9248 -.000026

4.960 321.267 114.022 .9861 -.000027

5.120 340.198 122. 766 1.&508 -.000029

5.280 360.597 132.361 1.1191 -.000034

5.440 382. 600 142.817 1.1914 -. 000041

5.600 406.345 154. 141 1.2677 -.000051

5.760 431.972 166.346 1.3484 -.000064

5.920 459r624 179.450 1.4335 -.000078

6.080 489.446 193.489 1.5233 -. 000096

6. 240 521.593 208.516 1.6131 -.000115

6.400 556.223 224.610 1.7180 -.000136

6.560 593.530 241. 877 1.8233 -.000159

6. 720 633.698 260. 454 1.9342 -.000184

6.880 676. 954 280. 50 2 2.0511 -.000210

10 0
THE

T,K

350

360

370

380

390

400

410

420

430

440

450

460

470

480

490

500

510

520

530

540

550

560

570

580

590

600

Table 20. The Joule-Thomson inversion locus

JCULE-THCHSON INVERSION LOCUS FOR I-BUTANE

P,BAR MOL/L T.K P.BAR MOL /L

64.6 8.58 610 395.5 6.37

89.9 8.49 620 399. 0 6. 28

114.0 8.41 630 402.4 6.21

136.9 8.33 640 405.7 6. 13 158.7 8.25 650 408.8 6. 05 179.3 8.16 660 411.7 5.98

198.8 8. 08 670 414.6 5. 91 217.2 6.00 680 417.4 5. 84

234.5 7.91 690 420.1 5.77

250.3 7.63 700 422.7 5.70

266.1 7. 75 710 425.2 5 . 64

280.3 7.66 720 427.5 5.57

293.6 7.58 730 429.8 5.51

305.9 7.49 740 431.9 5.45

317.2 7.41 750 433.9 5. 39

327.6 7.32 760 435.

8

5. 33 337.1 7.23 770 437.5 5.27

345.3 7.14 780 439.1 5.21

353.6 7.06 790 440 .

5

5.16

360.3 6.97 300 441.7 5.10

367.2 6.68 310 442.8 5. 04

373.0 6.79 820 443.6 4.99

373.3 6.70 830 444.3 4.93

383.2 6.62 840 444. 8 4. 88 337.6 6.53 850 445.0 4.82

391.7 6.45 860 445.1 4. 76

1 0 1
TABLE 21, Thermophysical properties of the saturated liquid

This table was computed along paths described in section 3.0. Column

headings have the following i nterpretations--

OPS/DT = dPg/dT, vapor pressure.

ODL/DT E dpj^/dT, saturated liquid.

DP/DT E (3P/3T), single phase.

DP/DD E (9P/3p), single phase.

Q,VAP E AHvapj heat of vaporization.

CV E Cy (P jT ) j CS E Co(T),

CP E Cp (p ,T)

,

W E speed of sound.

102
Table 21. Thermophysical properties of saturated liquid

PROPERTIES OF SATURATED LIQUID I-BUTANE

T P r H

c CV CS CP W DEG K BAR J/MOL J/MOL J/MOL/

K

J/MOL/K J/MOL/K J/MOL/K M/SEC

113. 5S0 .1889E-06 . 0 . 0 108.255 73.23 99.82 99.32 1776

120.000 .9330E-06 641.1 641.1 113.748 73.81 99.84 99.84 1728

130.000 . 7879E-05 1647. 7 1647. 7 121. 805 74.85 101.49 101.49 1658

140.000 .4757E-04 2670.9 2670.9 129.398 76.01 103.24 103.24 1591

150.000 .2201E-Q3 3711.7 3711.

7

136. 571 77.29 1 05. 06 105.06 1528

160.000 .6224E-03 4771.0 4771.0 143. 413 78.68 106.98 106.98 1467

170.000 .2580E-32 5849.5 5849.5 149. 958 80.16 108.97 108.97 1409

leo. 000 .7012E-02 6948.1 6948.

2

156. 244 81.73 111.05 111.05 1353

190.000 .1690E-01 8067.9 8068.1 162. 304 83.37 113.21 113.21 1298

200.000 .3685E-01 9210.1 9210.4 168.165 85.07 115.45 115.45 1245

210. 000 .7380E-01 10375.9 10376.6 173. 852 86.83 117.77 117.79 1194

220.000 .1374E+00 11566.9 11568.

1

179. 386 98.64 120.18 120.21 1143

230.000 .2405E+00 12734.3 12786.6 184. 785 90.49 122 .69 122.73 10 94 240. 000 .3989E+00 14029.4 14033.

1

190.065 92.37 125.28 125.36 1045

250.000 .6315E+00 15302.8 15308.8 195.238 94.27 127.99 128.10 997

261.359 .1013E+01 16784.1 16794.0 200.999 96.46 131.19 131.39 943

270.000 .1408E+01 17936.1 17950.1 205. 30 9 98.14 133.74 134.02 902

280.000 .2002E*01 19297.0 19317.3 210.227 100.10 136. 83 137.23 855

290 .000 .2769E+01 20688.0 20716.7 215. 081 102.05 140.10 140.66 809

300.000 .3736E+01 22111.0 22150.6 219.882 104.02 143.56 144.3 7 762

310.000 .4934E+01 23568.2 23621.

8

224. 644 105.98 147.29 148.42 715

320 .000 .6392E+01 25062.9 25134.1 229.378 107.94 151.33 152.91 667

330. 000 .8140E+Q1 26598.8 26692.1 234.101 109.90 155.80 158.01 6 19 340. 000 .1021E»02 2813 1.6 28302.2 238.828 111.87 160.85 163.95 571

350.000 .1264E+02 2981 8.3 29972.7 243.580 113.85 1 66. 72 171.15 521

360 .000 . 1546E + 02 31518.

1

31714.6 248.383 115.38 173.94 190.31 469

370.000 .1872E+02 33295.4 33544.5 253.273 118.03 183.00 192.94 414

380.000 .2248E+02 35174.5 35490.8 258.314 120.50 195.93 212.51 355

390.000 .2682E+02 37204.6 37610.6 263.637 123.58 217.49 249.86 287

400. 000 . 3186E + 02 39541.

3

40081.9 269. 662 127.90 270.55 370 . 22 206

408. 000 .3655E+02 42792.3 43739.2 278.446 0.00 0.00 0.00 0

1 0 3
Table 21. Continued

PROPERTIES OF SftTURATEO LIQUID I-BUTANE

T P DEN V.LIQ V.GAS DPS/OT ooL/rr OP/OT DP/OD Q, VAP

DEG K BAR MCL/L L/MOL L/MOL BAR/K MOL/L/K BAR/K BAR-L/MOL J/MOL

113. 550 . 1889E-06 12.755 .07840 .4997E+03 .4970E-07 -.01643 22.319 .1359E+04 28206

120.000 . 9330E-06 12.649 .07906 .1069E*08 .2174E-06 -.01644 21.107 .1284E+04 27901

130.000 .7879E-05 12.485 .08010 .1372E+07 . 1536E-05 -.01646 19.406 .1179E+-04 27434

140.000 .4757E-04 12.320 . 08117 .2447E*06 . 7673E-05 -. 01650 17. 890 .1084E+04 26976

150. 000 . 2201E-03 12.155 .08227 .5665E+05 . 3120E-04 -.01655 16.529 .9988E+03 26526

160.000 .8224E-03 11.989 .08341 .1617E+05 . 1007E-03 -. 01661 15.299 .9208E+03 26081

170.000 .2580E-02 11.822 .08459 .5473E+04 •2753E-03 -.01670 14. 182 .8492E+03 25638

180.000 .7012E-02 11.655 .08560 .2131E+04 .6565E-03 -.01681 13.163 .7831E+03 25197

190.000 . 1690E-01 11.486 .08706 .9316E+03 . 1398E-02 -.01694 12.229 . 721 7E + 03 24755

200.000 .3685E-01 11.316 .08837 .4489E+03 .2707E-02 -.01711 11.369 .6645E+03 24308

210.000 . 7380E-01 11.144 .08974 .2348E+03 .4843E-02 -.01730 10.574 .6109E+03 23856

220.000 .1374E+00 10.970 . 09116 .1316E+03 .8098E-02 -.01754 9.838 .5605E+03 23395

230.000 .2405E+00 10.793 .09265 . 7831E+02 . 1278E-01 -. 01782 9.153 .5130E+03 22923

240.000 . 3989E+00 10.613 . 09422 .4901E+02 . 1921E-01 -.01815 8.514 .4681E+03 22436

250 .000 .6315E+00 10.430 .09588 .3203E+02 .2767E-01 -. 01853 7.915 .4256E + 03 21933

261.359 .1013E+01 10.216 .09768 .2066E+02 •4006E-01 -.01905 7.279 .3799E+03 21335

270.000 .1408E+01 10.050 .09951 .1521E+02 . 5166E-01 -.01952 6.823 .3469E+03 20 859

280.000 . 2002E4-01 9.851 .10151 .1094E+02 .6756E-01 -. 02014 6. 322 . 3106E+03 20282

290.000 .2769E+01 9.646 .10366 .8052E+01 .8625E-01 -.02087 5.848 .2760E+03 19672

300.000 .3736E*01 9.434 .10600 .6044E + 01 .1078E4-00 -. 02174 5.396 .2433E+03 19022

310.000 .4934E«-01 9.211 .10856 .4613E+0

1

.1323E+00 -.02277 4.966 .2123E+03 18327

320. 000 .6392E+01 8.977 .11139 .3571E+01 . 1598E+00 -.02401 4.552 .1830E+03 17578

330 . 000 .8140E+01 3.730 .11455 .2795E+01 . 1903E+00 -. 02552 4.155 .1554E+03 16765

340.000 . 1021E+02 3.466 .11812 .220 7E4-01 .2242E+ 00 -. 02740 3. 769 . 1294E+03 15875

350.000 . 1264E + 02 3.180 .12224 .1752E+01 .2617E>00 -.02980 3.392 .1 05 OE+03 14838

360.000 .1546E+02 7.867 .12711 .1394E+01 .3033£<-00 -.03301 3. 019 . 8228E+02 13779

370.000 .1872E+02 7.516 . 13305 .1107E+01 . 3500E+00 -. 03753 2.644 .6111E+02 12505

380 .000 .2248E+02 7.108 .14068 .8700E+00 .4035E+00 - . 04455 2.255 .4156E+02 10995

390.000 .2682E+02 6.6 06 . 15137 .6684E+00 .4666E+00 -. 05743 1.8 35 .2382E+02 9102

400.000 . 3186E«-02 5.893 .16970 .4843E+00 .5453E+00 -.09306 1.344 .8577E+01 6396

408.000 . 3655E*02 3.860 . 25907 .2591E+00 .6341E+00 0.00000 .634 0. 0

10 4
TABLE 22. Thermophysical properties along isobars*

The following pages give physical and thermodynamic properties along

selected isobars, as computed by methods of section 3 of the text.

The first line of each table refers to freezing liquid on the P(T) melting

line.

Each table at P < contains a blank line for the transition from

saturated liquid to vapor, as seen by the abrupt decrease of density.

Table headings for partial derivatives have the following interpretations--

DP/DT E 3P/9T,

DP/DD = 3P/3p.

The specific heat interpretations are--

CV i Cv(p,T),

CP 5 Cp{p,T).

*These tables are extrapolated beyond the range of some of the P-p-T data used

for adjusting the equation of state. Small discontinuities may be detected at

T = 408.0 K along isobars at P > Pc = 36.55 bar, due to change in the paths of

computation, section 3.

105
Table 22. Thermophysical properties along isobars

I-BUTANE ISCB4R AT P = .10000 BAR

T OEN VOL DP/DT OP/CO E H S CV CP M OEG K MOL/L L/MOL BAR/K 8AR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.554 12. 755 .07840 22.3189 1358.6=4 . 3 1.1 108. 262 73.23 96.82 1776

120.000 12.649 .07906 21.1077 1264.130 640.9 641.7 113, 745 73.81 99,84 1720

130.000 12.485 .08010 19.4071 1178.930 1647.6 1648.4 121.801 74.85 101.49 1658

140.000 12. 320 .08117 17.8909 1084.471 2670.8 2671.6 129, 386 76.01 103.23 1591

150.000 12.155 .08227 16.5296 998.945 3711.6 3712.5 136.570 77.29 105, 06 1528

160.000 11.989 .08341 15.2999 920 .938 4770.9 4771.8 143. 411 70.68 106.97 1467

170.000 11.822 .08459 14.1831 849. 324 5849. 7 5850.6 149. 956 80.16 108.97 1409

180.000 11.655 .08580 13.1637 763. 186 6949.

0

6949.9 156. 243 01.73 111.05 1353

190.000 11.486 .08706 12.2294 721. 795 8069.

8

8070.7 162. 304 83.37 113.21 1298

200.000 11.316 . 0 8837 11.3693 664.534 9213.

0

9213.9 168. 168 85.07 115. 45 1245

210.000 11.144 .08974 10.5747 610.8% 10379.8 10380.7 173. 857 86.83 117.79 1194

214. 751 11. 061 .09041 10.2178 586.554 10938.6 10939.5 176. 499 87.68 118.93 1169

214.751 .00565 176.924 .000473 17.570 32808.

4

34577.6 286. 571 67.03 75.60 184

220.000 . 00551 131.348 .000462 18. 0 18 33164.1 34977.6 288. 412 68.27 76.82 186

230.000 .00527 109.766 .000441 18.369 33860.

0

35757.7 291.879 70.67 79.20 190

240.000 .00505 198.171 . 000422 19.7 17 34530.1 36561.8 295. 300 73.13 8 1.64 194

250.000 . 00484 206.567 .000404 2 0.564 35324.

9

37390.6 298. 683 75.65 84.13 198

260.000 .00465 214.954 .000388 21.4 09 36095.0 38244.6 302. 033 78.22 06. 69 202

270.000 .00448 223.334 . 000374 22.253 36891.1 39124.4 305. 353 8 0. 83 89. 29 205

280.000 . 00432 231.708 .000360 23. 095 37713.4 40030.4 308. 640 83.49 91.93 209

290.000 .00417 240.076 .000347 23.937 38562.3 40963.1 311.920 86.18 94.61 212

300.000 .00403 248.439 . 000336 24.777 39438.

3

41922.7 315.173 88.90 97. 31 216

310.000 . 00389 256.798 .000325 25.617 40341.5 42909.4 318.409 91.63 100.04 219

320.000 .00377 265.153 .00 0314 26. 456 41272.

0

43923.5 321. 620 94.38 102.78 222

330.000 .00366 273.505 .000305 27. 294 42230.

0

44965.0 324.832 97.13 105.52 225

340.000 .00355 281.854 .000296 28.132 43215.4 46034.0 328. 023 99.88 108.27 229

350.000 .00345 290.201 . 000287 28.969 44228.

3

47130.

3

331. 201 102.62 111.01 232

360.000 .00335 298.545 .000279 29. 8 05 45268.6 48254.1 334. 367 105.36 113.74 235

370.000 .00326 306.886 . 000271 3 0. 642 46336.2 49405.0 337.520 108.00 116.45 238

380.000 .00317 315.226 . 000264 31.478 47430.0 50583.0 340. 662 11 C.78 119.15 241

390.000 .00309 323.565 .000257 32.313 48552.

3

51707.9 343. 791 113.45 121.82 244

400.000 .00301 331.901 .000251 33.149 49700.4 53019.4 346.909 116.11 124. 47 247

410.000 .00294 340.237 . 000245 33.984 50874.

8

54277.2 350.015 110.73 127. 09 250

420.000 .00287 348 .570 .000239 34. 8 19 52075.4 55561.1 353.108 12 1.32 129.68 253

430.000 . 00 280 356.903 .000233 35.653 53301.

7

56870 .

0

356. 190 123.89 132.24 255

440.000 .00274 365.235 . 000223 36.488 54553.5 53205.9 359. 259 126.42 134. 77 258

450.000 .00268 373.566 .000223 37. 322 55830.

4

59566.1 362. 316 128 .91 137.27 261

460.000 .00262 381.896 .000218 38. 156 57132.1 60951.1 365.360 131.38 139.73 264

470.000 .00256 390.225 .000213 36. 990 58458.2 62360.5 368. 391 133.80 142.15 266

480.000 .00251 398.553 .000209 39. 8 24 59809.

4

63794.

0

371.409 136.19 144.54 269

490 .000 .00246 406.880 . 000205 40. 658 61182.3 65251.

1

374.413 138.55 146.89 272

500. 000 .00241 415.207 .000200 41.491 62579.6 66731.6 377.404 140.86 149.21 274

520.000 .00232 431.859 .000193 43. 158 65442.

7

69761.3 383,345 145.39 153. 73 280

540.000 .00223 448.510 .000185 44. 825 68394.8 72879.9 389. 229 149.77 158. 11 285

560.000 .00215 465.158 .000179 46.491 71433.1 76084.7 395. 056 154.01 162,35 290

580.000 .00203 481.805 .000173 48.157 74554.

9

79372.9 400. 825 158.11 166.45 295

600.000 .00201 498.450 .000167 49.822 77757.

3

82741.8 406.535 162,08 170.42 300

620.000 .00194 515.094 .000161 51.488 81037.

7

06188.7 412. 186 165.92 174.25 305

640 .000 .00188 531.737 . 000156 53. 153 84393.

7

89711.

0

417. 777 169,63 177.96 309

660 .0 00 .00162 548.330 .000152 54.818 37822.6 93306.4 423. 309 173.23 181.56 314

680.000 .00177 565.021 .000147 56.483 91322.3 96972.5 428 . 781 176.70 185.03 318

700.000 .00172 581.662 .000143 58.148 94890.4 100707.0 434. 193 180.07 188.40 323

1 06
Table 22. Continued

I-BUTANE ISOBAR AT P = .50000 BAR

T DEN VOL DP/OT DP/OD E H S CV CP

DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.572 12. 755 . 07840 22.3190 1358.9 15 1.6 5.5 103.273 73.23 98.82 1776

120.000 12.649 .07906 21.1111 1284.549 640.

4

644. 3 113. 741 73.81 99.83 1728

130.000 12.485 .08010 19.4104 1179.336 1647.0 1651.0 121. 797 74.85 101.49 1658

140.000 12.320 .08117 17.8941 1084. 866 2670.2 2674.3 129. 381 76.01 103.23 1592

150.000 12.155 .08227 16.5327 999.331 3711.0 3715.

1

136. 565 77.29 105.06 1528

160.000 11.989 .08341 15.3030 921 . 3 17 4770.2 4774.4 143. 406 78.68 106.97 1468

170.000 11.323 .08458 14.1861 849.698 5848.9 5853.1 149. 951 8 0. 16 108.97 1409

180.000 11.655 .08580 13.1667 783.556 6948.1 6952.4 156.238 81.73 111.04 1353

190.000 11.487 .08706 12.2323 722,161 8068.8 8073.2 162. 299 83. 37 113.20 1298

200.000 11.316 .08837 11.3722 664.398 9212.

0

9216.4 168.162 85.07 115.45 1245

210.000 11.144 . 08973 10. 5776 611.259 10378.6 10383.

1

173. 851 86.83 117.78 1194

220.000 10.970 .09116 9.8406 560.821 11569.8 11574.3 179.336 88.64 120.20 1143

230.000 10.793 .09265 9.1548 513.228 12786.

5

12791 .

2

184. 785 9 0.49 122.73 1094

240.000 10. 613 .09422 8.5142 468. 185 14029.9 14034,7 190.063 92.37 125.36 1045

244.798 10.526 .09501 8.2215 447. 403 14636.

8

14641 .

5

192. 559 93.28 126. 66 1022

244.798 . 02515 39.766 .002146 19.473 34850.1 36838.4 283. 234 74 .66 83.81 193

250.000 . 02459 40 .671 .002095 19. 947 35244.0 37277.6 285. 009 75.94 85. 04 196

260.000 . 02358 42.403 .002004 20 . 849 36019.9 33140.1 288. 391 78.47 87.48 199

270.000 . 02266 44.128 .001921 21.743 36620.9 39027.3 291. 740 8 1. 06 89.99 203

230.000 .02181 45.845 .001846 22.630 37647.7 39939.9 295. 059 83 .69 92.55 207

290.000 .02103 47.557 .001776 23.510 38500.6 40878 .

4

298. 352 86.36 95.17 211

300.000 .02030 49.263 . 001712 24. 385 39380.

2

41843.3 30 1. 62 3 89.06 97.82 214

310.000 .01962 50.965 .001653 25.256 40286.6 42834.9 304. 874 91.78 100.50 213

320.000 . 01899 52.664 . 001598 26.123 41220.1 43853.3 308. 107 94.52 103.19 221.

330. 000 .01840 54.359 .001547 26.987 42180.8 44898.7 311.324 97.26 105.90 224

340.000 . 01 784 56.051 .001499 27. 847 43168.

7

45971.2 314.526 100.00 108.61 228

350.000 .01732 57.741 . 001454 28.705 44183.9 47070.9 317. 713 102.73 111.32 231

360.000 .01633 59.428 . 001411 29.561 45226. 3 48197.7 320. 887 105.46 114. 03 234

370.000 .01636 61.113 . 001372 30 . 4 14 46295.7 49351.4 324.043 108.17 116.72 237

380.000 .01592 62.797 .001334 31.266 47392.

1

50532.0 327, 196 110.86 119.39 240

390.000 . 01551 64.479 .001299 32. 1 16 48515.

2

51739.

2

330. 332 113.53 122. 05 243

400.000 .01512 66.159 .001265 32.964 49664.9 52972.8 333. 455 116.16 124.68 246

410.000 .01474 67.838 . 001233 33.812 50840.8 54232.7 336.566 118.80 127. 29 249

420.000 .01439 69.516 .001203 34.658 52042.6 55518.4 339. 664 121.39 129.86 252

430.000 .01405 71 .193 .001174 35.502 53 270.2 56829.

3

342. 750 123.95 132. 41 255

440.000 .01372 72 .869 .001147 36.346 54523.

1

58166.6 345. 823 126.47 134.93 258

450.000 . 01 341 74.544 . 001121 37. 1 90 55801.1 59528.3 348.883 1 28 .97 137.41 261

460.000 .01312 76.213 .001096 38.032 57103.8 60914.7 351.930 131.42 139.86 263

470.000 .01284 77.891 .001072 38.873 58430.8 62325.4 354. 964 133.85 142.28 266

480.000 .01257 79.564 .001049 39. 7 14 59731.9 63760.

1

357. 984 136.23 144.66 269

490.000 .01231 31.236 .001027 40.555 61156.

6

65218.4 360. 991 138.58 147. 00 272

500.000 .01206 82.906 .001007 41.394 62554.6 66700.0 363. 984 14 0.90 149.31 274

520.000 .01159 86.250 .000967 43. 072 65419.1 69731.5 369.929 145.42 153.82 279

540 .000 .01116 89.590 .000931 44. 749 68372.

4

72851.

9

375. 817 149.80 158. 19 285

560 .000 .01076 52.929 .000897 46.424 71411.8 76058.3 331. 647 154.04 162. 42 290

580.000 .01039 96.266 . 000866 48. 0 97 74534.5 79347.8 387.413 158.14 166.51 295

600.000 .01004 99.602 .000837 49.770 77737.3 82717.9 393. 130 162.10 170.47 300

620.000 . 00971 102.938 .000810 51 . 442 81019.

1

86165.9 398. 783 165.94 174.31 304

640 .000 .00941 106.272 . 000764 53.112 84375.7 89639.3 404. 376 169.65 178.01 309

660.000 .00912 109.606 .000760 54. 7 83 87805.3 93285.6 409. 909 173.24 181.60 314

680.000 .00885 112.940 .000738 56.452 91 305.6 96952.5 415. 332 176.71 185.07 318

700.0 00 .00860 116.272 . 000716 58. 1 21 94874.

2

100687.8 420 . 795 180.08 188.43 323

107
Table 22 Continued

I-BUTANE ISCBAR AT P = 1.01325 BAR

T DEN VOL OP/DT OP/CD E H S CV CP W DEG K NOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.594 12. 755 . 0 7840 22.3191 1359. 198 3. 2 11.1 108.287 73.23 98.82 1776

120 .000 12.650 .07905 21.1155 1285.086 639.7 647.8 113. 736 73.81 99.63 1729

130.000 12.485 .08009 19.4146 11 79. 857 1646.

3

1654.4 121. 791 74,85 101.49 1659

140.000 12. 321 ,08116 17. 6982 1085. 373 2669.

4

2677.7 129. 376 76,01 103.23 1592

150.000 12.156 .08227 16.5367 999. 827 3710.1 3718.4 136. 560 77.29 105.06 1529

160.000 11.990 .08340 15.3069 921.804 4769.2 4777.7 143. 400 78.68 106.97 1468

170.000 11. 823 .08458 14.1899 850. 178 5847.9 5856.4 149.945 60.16 108.96 1410

180.000 11.656 .08579 13. 1705 784.030 6947. 0 6955.7 156. 231 81.73 111.04 1353

190.000 11.487 .08705 12.2360 722.632 8067.6 8076.4 162.293 83.37 113.20 1299

200.000 11.317 .08636 11.3760 665.366 9210.6 9219.6 168. 156 85.07 115.44 1246

210.000 11.145 .08972 10.5813 6 1 1 , 7 26 1037 7. 1 10386.2 173.844 86.83 117.77 1194

220.000 10.971 . 09115 9.8443 561. 287 11568.1 11577.4 179. 379 88.64 120.20 1144

230.000 10.794 .09264 9. 1585 513.696 12784.

7

12794.1 184. 777 90.49 122.72 1094

240.000 10.614 .09421 8.5180 468.654 14028.0 14037.5 190. 055 92.37 125.35 1046

250.000 10.431 .09587 7.9177 425.916 15299.1 15308.8 195. 227 94.27 128.09 997

260.000 10.242 .09763 7,3531 385.273 16599.3 16609.2 200. 307 96.20 130.98 949

261.359 10.216 .09788 7.2789 379.9 01 16784.

1

16794.0 200.999 96.46 131. 39 943

261.359 . 04340 20.663 .004209 20.169 36035.

5

38129.2 282. 631 79.21 89.02 197

270.000 . 04666 21.430 .004041 21. 0 C9 36735.6 38907.0 285.559 81.39 91.03 201

280.000 . 04482 22.309 .003865 21.964 37568,8 39829.3 288. 913 83.98 93.46 205

290.000 .04314 23.182 . 003706 22. 9 C5 38427.4 40776.3 292. 236 86.62 95.97 208

300.000 .04158 24.048 .003562 23.833 39312.

0

41748.7 295. 532 89.29 98.53 212

310.000 . 04014 24.910 .003429 24.751 40222.8 42746.9 298.805 9 1.99 101.13 216

320.000 .03381 25.768 .003307 25.660 41160.

3

43771.3 302. 058 94.71 103.76 219

330 .000 .03756 26.622 .003195 26.561 42124.6 44822.

1

305. 291 97.43 106.42 223

340.000 .03640 27.473 .003090 27.456 43115.8 45899.6 308.508 100.16 109.08 226

350.000 . 03531 28.321 .002993 28.345 44134.

0

47003.7 311.708 102.88 111.75 230

360.000 .03429 29.167 .002902 29.229 45179.1 48134.5 314.894 105.59 114.42 233

370.000 .03332 30.010 .002816 30. 1 08 46251.1 49291.9 318.065 108.30 117.07 236

380.000 .03241 30 . 852 . 002736 30. 983 47349.8 50475.

8

321.222 110.98 119.72 239

390.000 .03155 31.692 .002661 31. 854 48475.

0

51636.2 324. 366 113.64 122.35 242

400.000 . 03074 32.530 .002590 32.722 49626.6 52922.7 327.496 116.28 124.96 245

410.000 . 02997 33.367 .002523 33,588 50804.2 54185.2 33 0. 614 118.89 127.54 248

420.000 .02924 34.203 .002459 34.450 5200 7.8 55473.4 333. 718 121.47 130.10 251

430.000 . 02854 35.037 .002399 35.311 53236.9 56787.0 336. 809 124.03 132.63 254

440.000 .02783 35.871 . 002342 36. 169 54491.

2

58125.8 339. 837 126.55 135.13 257

450.000 .02725 36.703 .002287 37.025 55770.5 59489.5 342.951 129.03 137.60 260

460.000 .02664 37.535 .002235 37.880 57074.

4

60877.6 346. 002 131.49 140. 04 263

470.000 .02606 38.366 .002186 38, 733 58402.

6

62290.0 349.040 133.91 142.44 266

460.000 . 02551 39.196 . 002139 39.585 59754.

7

63726.3 352. 063 136.29 144. 81 268

490.000 . 02498 40.026 .002093 4 0.4 35 61130.4 65186.0 355. 073 138.64 147.14 271

500.000 .02448 40.855 .002050 41.284 62529.3 66669.0 358. 069 140.95 149.44 274

520.000 .02352 42.512 .001969 42.979 65395.5 69703.0 364. 018 145.46 153.94 279

540.000 . 02264 44.167 .001894 44.670 68350.3 72825.5 369. 910 149.83 158.29 284

560.000 . 02182 45.821 .001825 46.358 71 391.0 76033.8 375. 744 154.07 162.51 290

560.000 . 02106 47.473 .001760 48.043 74514.

8

79325.0 381.518 158.16 166.59 295

600.000 .32036 49.124 .001701 49. 726 77719.1 82696.6 387. 233 162.12 170.55 299

620.000 .01970 50.774 . 001645 51.407 81001.

3

86145.9 392. 888 165.96 174.37 304

640.000 .01903 52.423 .001593 53.087 84358.7 89670.5 398. 482 169.67 178.07 309

660.000 .01849 54.072 . 001544 54. 765 87789.

0

93267.9 404.017 173.25 181.65 314

680.000 .01795 55.720 .001498 56.441 91289.9 96935.8 409. 492 176.73 185.12 318

700.000 . 01743 57.368 .001454 58.117 94859. 1 100671.9 414. 906 180.09 188.48 323
Table 22. Continued

I-BUTANE ISOBAR AT P = 1.50000 BAR

T DEN VOL OP/OT DP/DD E H S CV CP H DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.615 13. 755 .07040 22.3192 1359.465 4. 7 16.5 108.300 73.23 96.02 1776

130.000 13.650 .07905 21.1196 1205.596 639.1 651.0 113.731 73.01 99.83 1729

130.000 13.406 .00009 19.4106 1100. 351 1645.

7

1657.7 121. 786 74.05 101.49 1659

140.000 13. 331 .00116 17.9021 1005.054 3660. 7 2600.9 129.370 76.01 103.23 1592

150.000 13.156 .00336 16.5405 1000.297 3709.

3

3721.6 136. 554 77.29 105.06 1529

160.000 11.990 .00340 15.3106 922. 265 4768.3 4700.9 143. 395 70.60 106.97 1460

170.000 11.034 .00457 14.1936 050.632 5046.9 5059.6 149. 939 80.16 100.96 1410

100.000 11.657 .00579 13.1741 704. 400 6945.9 6950.0 156. 225 81.73 111.04 1354

190.000 11.400 .00705 12.2396 723.070 0066.4 0079.4 162.206 83.37 113.19 1299

300.000 11.310 .00036 11.3795 665. 010 9209.

3

9223.6 160. 149 85.07 115.44 1246

310.000 11.146 .00973 10.5040 612.160 10375.7 10309.2 173.037 06.03 117.77 1195

330.000 10.973 .09114 9.0479 561. 730 11566.

6

11500 .2 179. 371 80.64 120.19 1144

330.000 10.795 .09363 9. 1620 514.139 12703.

0

12796.9 184. 769 90 .49 122.71 1095

340.000 10.615 .09430 0.5215 469. 1 CO 14026.

1

14040.2 190. 047 92.37 125.34 1046

350.000 10.433 .09506 7.9213 4 26. 36 4 15297.0 15311.4 195. 219 94.27 128.00 990

360.000 10.344 .09763 7.3567 305. 725 16597.

0

16611.6 200. 298 96.20 130.97 950

370.000 10.050 .09950 6.0237 347. 009 17927.6 17942.5 205. 297 90.14 134.01 902

371.735 10.016 .09904 6.7341 340.475 10170.1 10105.1 206. 167 90.40 134.56 094

371.735 . 06974 14.339 . 006161 20.405 36795.0 30946.6 202.571 02.21 92.60 198

300.000 .06735 14.049 . 005915 21.255 37492.1 39719.4 285.372 84.29 94.46 202

390.000 . 06469 15.459 .005650 32.261 30356.0 40675.6 200. 728 86.89 96.62 206

300.000 .06336 16.063 .005411 23.246 39246.

6

41656.

0

292. 052 09.53 99. 20 210

310.000 .06003 16.660 . 005196 24.213 40162.2 42661.2 295. 340 92.20 101.79 214

330.000 .05796 17.354 .004999 25. 166 41103.0 43691.0 290.620 94.09 104.35 210

330 .000 . 05604 17.043 .004019 26. 1 07 42071.0 44740.3 301. 071 97.60 106.95 221

340.000 . 05436 10.439 . 004653 27.030 43066.3 45030.7 305. 102 100.31 109.56 225

350.000 . 05360 19.013 . 004499 27.950 44007.

5

46939.4 300. 316 103.02 112.16 220

360.000 .05104 19.593 . 004356 20.071 45 135.4 40074.3 311.513 105.72 114.81 232

370.000 .04950 20.171 . 004223 29.777 46210.

0

49235.6 314. 694 100.42 117.43 235

300 .000 . 04030 20 . 747 . 004099 30.676 47310.9 50422.9 317. 861 111.09 120.05 238

390.000 .04690 21.321 .003902 31.570 40430.2 51636.4 321. 013 113.74 122.65 242

400.000 . 04560 21.094 .003673 32.450 49591.7 5 20 75.0 324. 150 116.37 125.23 245

410.000 . 04451 22.465 .003769 33.342 50771.

1

54140.9 32 7. 274 110.90 127.79 240

430.000 . 04341 23.035 .003672 34. 222 51976.

3

55431.5 330. 304 121.55 130. 33 251

430.000 . 04337 23.604 .003579 35.0 99 53206.9 56747.4 333.401 124.10 132.05 254

440.000 .04137 24.171 .003492 35.972 54462.6 50000.3 336. 563 126.62 135.33 257

450.000 .04043 24.730 .003409 36.043 55743.2 59453.0 339.632 129.10 137.79 260

460.000 .03953 25.304 . 003330 3 7. 7 C9 57040. 2 60 043.0 342.687 131.55 140.21 262

470.000 .03066 25.069 . 003255 30.574 50377.5 62257.0 345. 728 133.96 142.60 265

400.000 .03703 26.433 .003103 39.437 59730.7 63695.6 340. 755 136.34 144.96 260

490.000 .03704 26.997 .003115 40. 290 61107.3 65156.0 351.76 0 130 .60 147.20 271

500.000 . 03630 27.56 0 .003050 41.157 62507.1 66641 .

1

354. 767 140.99 149.57 274

530.000 . 03406 20.604 .002927 42.069 65374.9 69677.5 360.721 145 .50 154.05 279

540.000 .03355 39.007 .003014 44.576 60331.1 72802.2 366. 616 149.07 150.39 204

560.000 . 03333 30.920 .00271

0

46. 2 70 71373.

0

76012.3 372. 453 154.10 162.60 209

500.000 .03130 32.040 .002614 47. 976 74490.

0

79305.2 370. 231 150.19 166.67 294

600.000 .03015 33.167 .002525 49. 670 77703.

2

02678.

2

303. 940 162.15 170.62 299

630 . 0 00 .03917 34.205 .002441 51.362 00906.2 06120.9 369.605 165.90 174.43 304

640.000 .03335 35.402 . 002363 53.050 04344.

4

09654.

6

395. 201 169.60 170.13 309

660.000 .03730 36.510 .002290 54.737 07775.4 93253.1 400. 736 173.27 101.70 314

600.000 .03657 37.633 . 003221 56. 4 21 91276.9 96921.9 406. 214 176.74 185.16 310

700.000 . 03501 30.740 .002157 50. 1 03 94046.6 100650.9 411.630 100.10 108.52 323
Table 22. Continued

I-BUTANE ISOBAR AT P = 2 BAR

T DEN VOL OP/OT OP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.637 12.755 . 07840 22.3194 1359.741 6.3 22.0 108. 314 73.23 98.82 1776

120.000 12.651 .07905 21.1239 1286.119 638.5 654.3 113. 725 73.81 99.83 1729

130.000 12.486 .08009 19. 4228 1180.858 1645.0 16 61 .

0

121. 781 74.85 101.48 1659

140.000 12. 322 .08116 17.9061 1086.347 2667.9 2684.2 129.365 76.01 103.23 1593

150.000 12.157 . 08226 16. 5444 1000.780 3708.4 3724.9 136.549 77.29 105.05 1529

160.000 11.991 .06340 15. 3144 9 22.7 39 4767.4 4784.

1

143.389 78.68 106.96 1469

170.000 11.825 .08457 14.1973 851. 1 00 5845.9 5862.8 149. 933 80.16 108.96 1410

180.000 11.657 .08578 13. 1776 784.942 6944.

8

6962.

0

156. 219 81.73 111.03 1354

190.000 11.489 .08704 12.2433 723. 536 8065.2 8082.6 162. 280 83.37 113.19 1300

200.000 11. 319 .08835 11.3831 666. 265 9208.

0

9225.6 168.142 85.07 115.43 1247

210.000 11.147 .08971 10.5884 612.6 <3 10374.2 1 0392.2 173.830 86.83 117.76 1195

220.000 10.973 .09113 9.8515 562.184 11565.

0

11583.2 179. 364 88.64 120.18 1145

230.000 10. 796 .09263 9.1656 514.594 12781.2 12799.8 184. 762 90.49 122.70 1095

240.000 10.616 .09419 8.5252 469.557 14024.

1

14043.0 190. 039 92.37 125.33 1046

250.000 10.433 .09585 7.9249 426.3 24 15294.9 15314.0 195. 210 94.27 128.07 998

260.000 10.245 .09761 7.3604 386.190 16594.6 16614.2 200.289 96.20 130.95 951

270.000 10.051 .09949 6.8275 347. 479 17925.0 17944.9 205. 287 98.14 133.99 903

279.971 9.852 .10150 6.3239 310.656 19293.0 19313.3 210. 213 100.09 137.22 856

279.971 .09132 10.950 .008184 20.463 37407.2 39597.2 282. 663 84.65 95.64 199

280 .000 .09131 10.952 .008183 20.467 37409.

7

39600.0 282. 673 84.66 95.65 199

290.000 .08751 11.427 . 007778 21.547 38281.7 40567.1 286. 067 87.19 97.82 203

300.000 .08407 11.895 .007421 22.595 39177. 7 41556.6 289.421 89.78 100.13 208

310.000 .08093 12.357 .007103 23.618 40098.5 42569.8 292. 744 92.43 102.54 212

320.000 .07804 12.813 .006817 24.620 41044. 7 4 36 0 7.4 296. 038 95.10 105. 01 216

330.000 .07538 13.266 .006556 25.6 04 42016.

8

44670.0 299.308 97.78 107.53 220

340.000 .07291 13.715 .006318 26.573 43015.

0

45758.

0

302. 556 100.48 110.08 223

350.000 .07062 14.161 .006099 27.529 44039.5 46871.6 305. 784 103.17 112.65 227

360.000 .06848 14.603 .005896 28.473 45090.3 48011.0 308.994 105.86 115.24 230

370.000 . 06647 15.044 .005709 29. 407 46167.4 49176.2 312. 136 108.54 117. 82 234

380.000 . 06459 15.482 .005534 30.3 32 47270.8 50367.2 315.363 111.20 120.40 237

390.000 . 06282 15.919 .005371 31.250 48400.3 51584.1 318.523 113.85 122.97 240

400.000 .06115 16.353 .005218 32. 160 49555.9 52826,5 321.669 116.47 125.53 244

410.000 . 05957 16.786 .005075 33.065 50 737. 2 54094.5 324. 800 119.07 128.07 247

420.000 . 05803 17.218 .004940 33.963 51944.

0

55387.

7

327. 916 121.64 130.58 250

430.000 . 05666 17.649 .004812 34.857 53176.

2

56706.0 331. 010 124.18 133.08 253

440.000 . 05531 18.078 .004692 35.746 54433.

4

58049.1 334.106 126.69 135.54 256

450.000 .05403 18 .507 .004578 36.631 55715.3 59416.7 337. 179 129.17 137.98 259

460.000 .05281 18.935 .004470 37. 512 57021.7 60808.6 340.239 131.61 140. 39 262

470.000 .05165 19.361 .004367 38.3 90 58352.1 62224.4 343.284 134.02 142.77 265

480.000 . 05054 19.787 .004269 39. 265 59706.

3

63663.8 346.314 136.39 145.12 268

490.000 .04947 20.213 .004176 40. 136 61084.

2

65126.7 349.330 138.73 147.43 270

500.000 .04846 20.638 .004087 41.006 62484.9 66612.4 352. 332 141.04 149. 71 273

520.000 . 04654 21.485 .003920 42.738 65354.

3

69651.4 358. 291 145.54 154.17 279

540.000 .04478 22.331 .003768 44.462 68312.

0

72776.3 364. 191 149.90 158.50 284

560.000 .04315 23 . 176 .003627 46.179 71355.2 75990.4 370. 031 154.13 162.69 289

580.000 .04163 24.019 .003497 47.891 74481.3 79285.1 375.812 158.21 166.76 294

600.000 . 04022 24.861 .003376 49. 597 77687.6 82659.7 381. 532 162.17 170.69 299

620.000 .03891 25.702 .003263 51.3 CO 80971.4 86111.7 387. 191 166.00 174. 50 304

640.000 . 03768 26.542 .003158 52.999 84330.

4

89638.7 392.790 169.70 178.19 309

660.000 .03652 27.361 .003060 54.694 87762.1 93238.3 398.328 173.29 181.76 314

680.000 .03544 23.219 .002968 56. 387 91264.

3

96908.1 403.805 176.76 185.21 318

700.000 .03441 29.057 . 002881 58. 0 77 94834.6 10 0646.0 409. 223 180.12 188.56 323

1 1 0
Table 22. Continued

I-gUTANE ISOBAR AT P = 3 BAR

T DEN VOL OP/DT DP/ CD E H S CV CP H OEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.660 12.755 .07840 22. 3197 1360.295 9. 4 32.9 108. 342 73.24 98.83 1777

120.000 12. 651 . 0 7904 21.1324 1287.167 637.3 661.0 113. 715 73.81 99. 83 1730

130.000 12.487 .08008 19.4310 1181 . 872 1 643.

6

1667.6 121.770 74.85 101.48 1660

140.000 12. 322 . 0 8115 17.9141 1087.335 2666.4 2690.8 129.354 76.01 103.22 1593

150.000 12.158 .08225 16. 5523 1001. 746 3706.

8

3731.4 136. 537 77.29 105.05 15 30 160.000 11.992 .08339 15.3221 923.688 4765.6 4790.6 143. 378 78.68 106.96 1469

170.000 11.826 .08456 14.2048 852. 0 34 5843.8 5869.2 149. 921 80.16 108.95 1411

180.000 11.658 .08577 13. 1852 785.866 6942.

6

6968.

3

156. 207 81.73 111.02 1355

190.000 11.490 .08703 12.2506 724. 452 8062.7 8088.8 162. 267 83.37 113.18 1300

200.000 11. 320 .08834 11.3904 667. 176 9205.3 9231.8 168. 129 35.07 115.42 1247

210.000 11.148 .08970 10.5956 613.531 10371.3 10398.2 173. 816 36.83 11 7. 75 1196

220.000 10 . 975 .09112 9.8587 563. 092 11561.

8

11589.1 179. 350 88.64 120.17 1146

230.000 10.793 .09261 9.1729 515.5 04 12777.7 12305.5 184. 746 9 C.49 122.68 1096

240.000 10.619 . 09417 8.5324 470.471 14020.

3

14048.5 190.023 92.37 125.30 1047

250.000 10.435 .09583 7.9323 427.745 15290.6 15319.3 195.193 94.27 128.04 999

260.000 10.247 .09759 7.3679 387.119 16569.9 16619.2 200. 270 96.20 130.92 952

270.000 10.054 .09946 6.8351 348. 422 17919.7 17949.5 205.268 98.14 133.96 904

280.000 9.355 .10147 6.3302 311.504 19231.6 19312.1 210. 197 100.10 137. 18 857

290.000 9. 647 .10366 5.8498 276.254 20677.6 20708.7 215.071 102.05 140.65 809

292.603 9.592 .10425 5.7283 267. 339 21055.

3

21086.6 216.335 102.56 141.60 796

292.603 .13405 7.460 . 012326 20 . 3 C8 38355.2 40593.2 283.001 86.54 100.72 199

300.000 .12974 7.707 . 011830 21.188 39031.

1

41343.3 285.533 90.37 102.14 202

310.000 .12445 8.036 .011241 22. 335 39964.

3

42375.0 288.916 92.92 104.25 207

320.000 .11965 8.358 . 010723 23.445 40921.

1

43428.4 292. 261 95.53 106.49 212

330.000 .11527 8.675 .010261 24.523 41902.4 4 45 0 4 .

8

295. 573 98.17 10 8. 83 216

340.000 .11126 8.938 .009846 25.575 42908.7 45605.0 298. 858 100.82 111.23 220- 350.000 .13756 9.297 . 009470 26. 605 43940.3 46729.5 302. 117 103.48 113.68 224

360.000 .10413 9.603 .009126 27.6 16 44997.6 47878.6 305. 355 106.15 116.16 228

370.000 .10094 9.907 .008811 28. 610 46080.5 49052.5 30 8. 571 108.80 118. 65 231

380.000 .09796 10.203 . 008520 29.590 47189.4 50251.7 311 . 769 111.44 121.16 235

390.000 .09517 10.507 . 008251 30.557 48323.7 51475.8 314.948 114.07 123. 66 238

400.000 .09256 10.304 .008001 31.513 49483.5 52724.8 318.111 116.67 126.16 242

410.000 .09009 11.100 .007768 32.459 50668.8 53998 .

7

321. 256 119.25 128. 64 245

420 .000 .08777 11 . 394 . 007549 33. 396 51879.

3

55297.

5

324. 386 12 1.81 131.11 248

430.000 .03557 11 .687 .007344 34. 3 25 53114.8 56620.3 327. 500 124.34 133.57 251

440.000 . 03348 11.978 .007152 35.248 54375.0 57968 .6 330.593 126.83 135.99 254

450.000 . 03 15 1 12.269 .006970 36.163 55659.8 59340.5 333.662 129.30 138.40 258

460.000 . 07963 12.559 .006798 37.073 56968.

8

60 736.4 336. 750 131.73 140.78 261

470.000 .07784 12.347 . 006636 37.977 58301.6 62155.9 339. 302 134.13 143.13 264

430.000 .07613 13.136 . 006481 38.877 5965 8.

1

63598.7 342. 840 136.50 145.45 266

490.000 .07450 13.423 .006335 39.772 61037.8 65064.7 345 . 863 138.83 147.74 269

500.000 . 0 7294 13.709 .006195 40.663 62440.

5

66553.4 348. 870 141.13 150.00 272

520.000 .07002 14.281 . 005935 42. 4 35 65313.4 69597.8 354.840 145.62 154.43 278

540.000 .06734 14.851 .005698 44.195 68274.2 72729.4 360. 749 149.97 158.72 283

560.000 . 06486 15.419 .005480 45.944 71320.0 75945.6 366.597 154.19 162.89 288

580.000 . 06256 15 .985 .005280 47. 684 74 44 8.4 79244.0 372. 384 158.27 166.93 294

600.000 .06042 16.550 .005094 49. 4 17 77656.

3

82621.

8

378.110 162.22 170. 84 299

620.000 . 05343 17.114 .004921 51 . 1 42 80942.5 86076.8 383. 774 166.04 174.64 304

640.000 . 05657 17.678 . 004761 52. 862 84303.1 89606.4 389. 377 169.74 178.31 309

660.000 . 05482 13 . 240 .004610 54.578 37736.3 93208.3 394. 918 173.32 181.87 313

680.000 . 05319 18.802 .004470 56.288 91239.

7

96880.3 400. 399 176.78 185. 32 318

700.000 . 05164 19. 363 . 004338 57.995 94811.2 100620.1 405. 819 180.14 168.65 323

1 1 1
Table 22 Continued

I-BUTANE ISCBAR AT P = « BAR

T DEN VOL OP/OT DP/ DO E H S CV CP W OEG K NOL/L L/MOL 3AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.723 12. 755 .07840 22. 3200 1360.849 12.5 43.9 108. 369 73.24 98.83 1777

120.000 12.652 .07904 21.1410 1288.2 14 636.1 667.7 113. 705 73.81 99.82 1731

130.000 12.488 .08008 19.4393 1182. 886 1642.2 1674.3 121.760 74.85 101.48 1661

140.000 12.323 .08115 17.9221 1088.322 2664.9 2697.4 129. 343 76.01 103.22 1594

150.000 12. 159 . 08225 16.5601 1002. 711 3705.

1

3738.0 136.526 77.29 105.04 1531

160.000 11.993 .08338 15.3297 924.636 4763.7 4797.1 143. 366 78.68 106.95 1470

170.000 11.827 .08455 14.2123 852.968 5841.8 5875.6 149. 909 8 0.16 108.94 1412

180.000 11.660 .08577 13.1926 786. 789 6940.4 6974.

7

156. 195 81.73 111.02 1355

190.000 11.491 . 08702 12.2579 725.368 8060.

3

8095.

1

162. 254 83.37 113.17 1301

200.000 11.322 .08833 11.3976 668.087 9202.6 9238.0 168. 116 85.07 115.41 1243

210.000 11. 150 .08969 10.6028 614.439 10368.4 10404.3 173. 803 66.83 117.74 1197

220.000 10.976 .09110 9.8659 564.000 11558.6 11595.0 179. 335 88.64 120.15 1146

230.000 10.800 .09259 9.1801 516.414 12 774.2 12811.3 184.731 9 C.49 122.66 1097

240.000 10.621 .09416 8.5397 471.385 14016.4 14054.1 190.007 92.37 125.28 1048

250.000 10.438 .09581 7.9396 428.665 15286.4 15324.7 195. 176 94.27 128.02 1000

260.000 10.250 .09756 7.3753 388.047 16585.2 16624.3 200.252 96.20 130.89 953

270.000 10.057 .09943 6.6427 349. 360 17914.5 17954.3 205.248 98.14 133.92 905

280.000 9.858 .10144 6.3360 312.456 19275.8 19316.4 210. 176 100.10 137. 14 858

290.000 9.651 .10362 5.8578 277. 221 20671.1 20712.5 215. 048 102.05 140.59 810

300.000 9.435 .10599 5.3987 243.549 22102.8 22145.2 219.877 104.02 144.35 762

302.383 9.381 .10659 5.2920 235. 743 22455.

2

22497.8 221.020 104.48 145.30 751

302.383 .17669 5.659 . 016626 19.972 39094.

9

41358.7 283. 394 91.65 105.05 198

310.000 . 17064 5.86 0 .015888 20.954 39819.4 42163.4 286.023 93.49 106.32 202

320.000 .16348 6.117 .015047 22.187 40789.

0

43235.8 289.428 96.01 108.23 207

330.000 . 15703 6.368 .014317 23.371 41781.1 44328.3 292.790 96.59 110.32 212

340.000 .15119 6.614 . 013671 24.514 42796.7 45442.4 296. 116 10 1.19 112.53 216

350.000 .14585 6.856 .013095 25.625 43836.8 46579.3 299.411 103.82 114.83 220

360.000 .14095 7.095 .012576 26.7 07 44901.

2

47739.1 302. 679 106.44 117.18 224

370.000 .13642 7.330 . 012105 27. 765 45990.5 48922.7 305. 922 109.07 119.56 228

380.000 .13221 7.564 .011675 28.803 47104.8 50130.3 309. 142 111.69 121.98 232

390.000 . 12830 7.794 .011280 29.822 48244.

3

51362.0 312. 342 114.29 124.40 236

400.000 .12464 8.023 .010915 30.825 49408.8 52618.1 315. 522 116.88 126.83 239

410.000 .12121 8.25 0 .010577 31. 815 50598.

3

53898.5 318. 684 119.44 129.26 243

420.000 .11799 8.476 .010263 32.792 51812.

7

55203.1 321.828 121.98 131.68 246

430.000 .11494 8.700 . 009970 33. 757 53051.

8

56531.8 324.954 124.50 134. 06 250

440.000 .11207 8.923 .009696 34.7 13 54315.3 57884.5 32 8. 064 126.98 136.47 253

450.000 .10935 9.145 .009438 35.660 55603.

0

59261.0 331.157 129.44 138.84 256

460.000 .10677 9.366 .009196 36.599 56914.

7

60661.0 334. 235 131.86 141.18 259

470.000 .10432 9.586 .008967 37.531 58250.

1

62034.

4

337. 296 134.25 143.50 262

480.000 .10199 9.805 .008751 38.456 59608.9 63530.9 340. 341 136.61 145.60 265

490.000 .09977 10.023 . 008546 39. 375 60991.1 65000.4 343. 371 138.93 148.06 268

500.000 .09765 10.241 .008352 40. 288 62395.

8

66492.2 346. 385 141.22 150.30 271

520. 000 .09368 10.675 .007991 42. 1 G1 65272.4 69542.2 352.366 145.70 154.69 277

540.000 .09004 11.106 .007663 43. 896 68236.

3

72 6 78.7 358.284 150.04 158.95 282

560.000 .03668 11.536 .007363 45.678 71284.9 75899.3 364. 140 154.25 163.09 288

580.000 .03358 11.964 . 007088 47.447 74415.7 79201.5 369. 933 158.32 167.11 293

600.000 .08070 12.391 . 006834 49. 206 77626.

2

82582.3 375. 665 162.26 171.01 298

620.000 .07802 12.817 .006599 50. 955 80913.

8

86040.7 381.334 166.08 174.78 303

640.000 .07551 13.243 .006360 52.697 84276.1 39573.1 386.941 169.77 178.44 308

660.000 .07317 13.667 . 006176 54.432 87710.7 93177.4 392.486 173.35 181.99 313

680.000 .07097 14.090 .005985 56.161 91215.

5

96851.6 397. 971 176.81 185.42 318

700.000 .06890 14.513 .005807 57.885 94788.2 100593.4 403.394 180.16 188.75 323
Table 22. Continued

I-BUTANE ISOBAR AT P = 5 BAR

T DEN VOL DP/DT OP/OD p H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.766 12.755 .07840 22. 3204 1361.405 15.6 54.8 108. 396 73.24 98.83 1777

120.000 12.653 .07903 21.1495 1289.262 634.8 674.4 113. 695 73. 81 99. 82 1731

130.000 12.489 .08007 19.4475 1183. 9C1 1640.9 1680.9 121. 749 74.85 101.47 1661

140.000 12.324 .08114 17.9301 1089.309 2663.4 2704.0 129. 332 76.01 103.21 1595

150.000 12. 160 .08224 16.5679 1003.677 3703.4 3744.5 136.515 77.29 105.04 1531

160.000 11.994 .08337 15.3373 925.5 83 4761.9 4803.6 143.354 78.68 106.95 1471

170.000 11.828 .08454 14.2198 853.9 C2 5839. 8 5882.1 149. 897 80.16 108.94 1412

ISO. 000 11. 661 .08576 13.2000 787.713 6938.1 6981.0 156. 182 81.73 111.01 1356

190.000 11.493 .08701 12.2652 726. 284 8057.9 8101.4 162. 241 83.37 113.16 1302

200.000 11.323 .08831 11.4049 668.998 9200.0 9244.2 168 . 102 85.07 115.40 1249

210.000 11.152 .08967 10.6100 615. 347 10365.5 10410.3 173.789 86.83 117.72 1198

220.000 10.978 .09109 9.8731 564. 908 11555.4 11600.9 179. 321 88.64 120.14 1147

230.000 10.302 .09258 9.1873 517. 324 12770.7 12817.0 184. 716 90.49 122. 65 1098

240.000 10. 623 .09414 8.5469 472.299 14012.

6

14059.7 189.991 92.37 125.26 1049

250.000 10.440 .09579 7.9469 429.585 15282.1 15330.0 195.159 94.27 127.99 1001

260.000 10.253 .09754 7. 3827 388.975 16580.5 16629.3 200. 234 96.20 130. 86 954

270.000 10.060 .09940 6. 8502 350.298 17909.3 17959.0 205.229 98.14 133.88 906

2S0. 000 9.861 .10141 6.3457 313.407 19270.

0

19320.7 210.155 100.10 137.09 859

290.000 9.655 .10358 5.8658 278.187 20664.5 20716.3 215.026 102.05 140.54 811

300.000 9.439 .10595 5.4070 244.534 22095.

3

22148.3 219. 852 104.02 144.28 763

310 .000 9. 211 .10856 4. 9661 212.351 23565.

6

23619.8 224.649 105.98 148.41 715

310.493 3.200 .10870 4.9447 210. 8 00 23641.1 23695.4 224. 878 106.08 148.63 712

310.493 . 21958 4.554 .021105 19.542 39709.9 41986.9 283. 789 94.29 108.97 197

320.000 .20995 4.763 . 019875 20. 854 40647.1 43028.7 287. 094 96.56 110.31 202

330.000 .20096 4.976 .018781 22.159 41652.

0

44140.1 290. 514 99.04 112.05 207

340.000 . 19293 5.183 . 017837 23. 4 C5 42678.

7

45270.4 293.888 101.59 114.01 212

350.000 .18567 5.386 .017008 24.6 03 43727.7 46420.7 297. 223 104.17 116.10 217

360.000 .17906 5.5 85 .016271 25.762 44800.2 47592.5 300. 524 106.76 11 8. 30 221

370.000 .17301 5.780 .015610 26.889 45896.5 48786.5 30 3. 796 109.35 120.55 225

380.000 .16 743 5.973 . 015013 27.987 47017.

2

50003.5 30 7. 041 111.94 122.86 229

390.000 .16226 6.163 .014469 29.061 48162.2 51243.6 3 1 0 . 26 3 114.52 125.19 233

400.000 .15746 6.351 . 013971 30.114 49331.7 52507.2 313.462 117.09 127.55 237

410.000 .15297 6.537 .013512 31.148 50525.8 53794.4 316. 641 119.64 129.91 241

420.000 . 14877 6.722 .013089 32.166 51744.6 55105.4 319.799 122.16 132.27 244

430.000 .14482 6.905 .012695 33. 169 52987.

3

56439.8 322.939 124.66 134.62 248

440.000 .14111 7.087 .012329 34. 160 54254.3 57797.

7

326.061 127.13 136.97 251

450.000 . 13760 7.267 .011987 35 . 1 39 55545.2 59178.9 329. 165 1 29.58 139.29 254

460.000 .13428 7.447 . 011666 36. 1 07 56859. 8 60583.

3

332. 252 131.99 141.60 258

470.000 .13113 7.626 .011364 37.066 58197.

8

62010.8 335.322 134.37 143.89 261

480.000 . 12814 7.804 .011080 38.017 59559.1 63461.0 338. 375 1 36 .72 146.16 264

490.000 .12530 7.981 . 010812 38.960 60943.3 64933.7 341.412 139.04 148.40 267

500.000 .12259 8.157 .010558 39. 896 62350.1 66428.

7

344.433 141.32 150.62 270

520.000 . 11 753 8.508 .010089 41.749 65230.4 69434.6 350.425 145.78 154.96 276

540.000 .11290 8.857 . 009664 43.581 68197. 6 72626.2 356. 353 150.11 159.19 281

560.000 .10965 9.204 .009277 45.394 71249.

1

75851.2 362. 217 154.31 163.30 287

580.000 .10471 9.550 .008923 47. 192 74382.4 79157.3 368. 017 158.37 167.30 292

600.000 .10107 9.894 . 006597 48.977 77595.

1

82542.1 3 7 3. 755 162.31 171.17 298

620.000 .09769 10.237 .008296 50.751 80884.3 36003.5 379. 429 166.12 174.93 303

640.000 .09452 10 .579 .008017 52.5 15 84248.9 89538.6 385. 041 169.81 178.57 308

660.000 . 09157 10.921 .007757 54.270 87685.1 93145.5 390. 590 173.38 182.11 31 3 680.000 .08880 11.261 .007515 56. 017 91 191.

3

96821.9 396. 077 1 76.84 185.53 317

700.000 .08620 11.601 .007288 57.758 94765.2 100565.8 40 1. 504 180.19 188.85 322

1 13
Table 22. Continued

I-BUTftNE ISOBAR AT P = 6 BAR

T DEN VOL DP/DT DP DEG K MOL/L L/MOL BAR/K BAR-L/

113.809 12. 755 .07840 22.3207 1361.

120.000 12. 654 .07903 21.1560 1290 . 130.000 12.490 .08007 19.4558 1184.

140.000 12.325 .08113 17.9381 1090 . 150.000 12. 160 .08223 16.5757 1004.

160.000 11.995 .08337 15.3450 926.

170.000 11.829 .08454 14.2273 854.

180.000 11.662 .08575 13.2073 788.

190.000 11.494 . 08700 12.2725 727.

200.000 11.325 .08830 11.4121 669.

210.000 11.153 .08966 10.6172 616.

220.000 10.980 .09108 9.8802 565.

230.000 10.804 .09256 9.1945 516.

240.000 10.625 .09412 8.5542 473.

250.000 10.442 .09577 7.9542 430.

260.000 10.255 .09751 7.3901 389.

270.000 10. 063 .09936 6.8578 351.

280.000 9. 864 .10138 6.3535 314.

290.000 9.658 .10354 5.8737 279.

300.000 9.443 .10590 5.4153 245.

310.000 9.216 . 10850 4.9748 213.

317.489 9.037 .11065 4. 6546 190.

317.489 .26292 3.603 .025777 19.

320.000 .25959 3.852 . 025323 19.

330.000 .24743 4.042 . 023731 20.

340.000 .23674 4.224 .022394 22.

350.000 .22721 4.401 .021245 23.

360.000 . 21863 4.5 74 . 020239 24.

370.000 . 21084 4.743 .019346 25.

330.000 .20370 4.909 .018550 27. 390.000 .19714 5.072 .017831 28.

400.000 .19107 5.234 . 017178 29.

410.000 .18543 5.393 . 016581 30. 420.000 .13017 5.550 .016032 31.

430.000 .17525 5.706 . 015526 32.

440.000 .17063 5.861 .015056 33.

450.000 .16628 6.014 . 014620 34.

460.000 .16217 6.166 .014212 35.

470.000 .15829 6.318 . 013831 36.

480.000 .15460 6.466 .013472 37.

490.000 .15111 6.618 .013135 38.

500.000 .14778 6. 767 . 012817 39.

520.000 .14159 7.063 . 012230 41.

540.000 . 13593 7.356 . 011702 43.

560.000 .13075 7.648 . 011223 45.

580.000 .12596 7.939 .010786 46.

600.000 .12154 8.228 . 010384 48.

620.000 .11743 8 .516 .010015 50.

640.000 .11360 8.803 .009673 52.

660.000 .11002 9.089 .009355 54.

680.000 .10668 9.374 .009059 55.

700.000 .10353 9.659 .008782 57.

E H S CV CP W J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

18.7 65.8 108. 424 73.25 96.84 1778

633.6 681.0 113. 684 73.81 99.82 1732

1639.

5

1687.5 121. 739 74.85 101.47 1662

2661.9 2710.6 129. 321 76.01 103.21 1595

3701.7 3751.1 136.504 77.29 105.03 1532

4760.1 4810.1 143.343 78.68 106.94 1471

5837. 8 5888.5 149. 885 80.16 108.93 1413

6935.9 6987.4 156.170 81.73 111.00 1357

8055.5 8107.7 162. 229 83.37 113.15 1303

9197.3 9250.3 168.089 85.07 115.39 1250

10362.6 10416.4 173. 775 86.83 117.71 1198

11552.

2

11606.9 179. 306 88.64 120.12 1148

12767.

3

12822.8 184. 701 90.49 122.63 1099

14008.8 14065.2 189.975 92.37 125.24 1050

15277.9 15335.3 195. 142 94.27 127.97 100 2 16575.

9

1 6634.4 200. 216 96. 20 130.83 955

17904.1 17963.7 205.210 98.14 133.84 907

19264,2 19325.0 210. 135 100.10 137.05 860

20658.0 20720.1 215. 003 102.05 140.48 813

22087.9 22151.5 219. 827 104.02 144.20 765

23557.

1

23622.

2

224.621 105.98 148.31 716

24683.

8

24750.2 228. 191 107.45 151.73 679

40239.9 42522.0 284.167 96.63 112.64 195

40493. 7 42805.0 285.055 97.19 112.86 197

41514.5 43939.5 288.546 99.56 114.09 202

42553.5 45088.0 291. 975 102. 02 115.70 208

43613.1 46253.8 295.355 104.54 117.54 213

44694.

5

47438.9 298. 694 107.09 119.53 218

45798.7 48644.5 301.997 109.65 121.64 222

46926.2 49871.6 305. 270 112.21 123.82 227

48077.6 51121.0 308.515 114.76 126.05 231

49252.5 52392.7 311. 734 117.31 128.31 235

50451.4 53687.1 314. 931 119.84 130.60 239

51674.2 55004.4 318.105 122.34 132.89 242

52921.0 56344.7 321. 259 124.83 135.19 246

54191.5 57708.0 324.394 127.29 137.48 249

55485.

7

59094.1 327. 509 129.72 139. 77 253

56803.3 60503.1 330.606 132.12 142.04 256

58144.

1

61934.8 333. 685 134.49 144.30 259

59508.0 63388.8 336. 746 136.83 146.53 263

60894.5 64865.2 339. 790 139.14 148.75 266

62303.8 66363.

8

342. 817 141.41 150.94 269

65186.0 69425.6 348. 822 145.87 155.24 275

68158.5 72572.4 354.759 150.18 159.44 281

71213.

0

75802.0 360.632 154.37 163.52 286

74348.

8

79112.2 366. 439 158. 43 167. 49 292

77563.8 82500.5 372.183 162.35 171.34 297

80855.

3

85964.8 377. 862 166.16 175. 08 302

84221.1 89502.8 383.478 169.84 178.71 307

87658.

9

93112.

3

389.032 173.41 182.23 312

91166.5 96791.0 394. 523 176.86 185.64 317

94741.7 100537.

1

399. 952 180.21 188.95 322

14

'/CD

MOL

961

3 09 915

297

642

531

8 36 636

199

9 C8 255

8 15 233

212

5 C3 902

236

357

153

5 17 357

183

056

437

885

247

543

787

987

150

281

385

466

5 26 568

594

6 C6 6 04 591

568

535

493

3 87 255

1 01

9 29 740

5 37 323

097

863

621

1
Table 22. Continued

I-BUTANE ISOBAR AT P = 7 BAR

T OEN VOL DP/DT OP/CO E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.352 12. 755 . 07840 22. 3211 1362.5 19 21.8 76.7 108. 451 73.25 98.84 1778

120.000 12.654 .07902 21.1666 1291.356 632.4 687.7 113. 674 73.81 99.81 1733

130.000 12.490 .06006 19.4640 1185. 929 1638.1 1694.2 121.728 74.85 101.47 1663

lAO.OOO 12.326 .08113 17.9461 1091.284 2660.4 2717.2 129. 311 76.01 103.20 1596

150.000 12.161 . 08223 16.5835 10 05.6 07 3700.1 3757.6 136.493 77.29 105.03 1533

160.000 11.996 .08336 15.3526 927.479 4758. 2 4816.6 143. 331 78.68 106.93 1472

170.000 11. 830 .08453 14.2348 855.769 5835.8 5894.9 149.873 80.16 108.92 1414

180.000 11. 664 .08574 13.2147 789.559 6933.7 6993.7 156. 153 81.73 11 0. 99 1358

190.000 11.496 .08699 12.2798 728. 1 14 8053.0 8113.9 162. 216 83.37 113.14 1303

200.000 11.326 .08829 11.4193 67 0. 8 18 9194.7 9256.5 168.076 85.07 115.38 1251

210.000 11.155 .08965 10.6244 617.162 10359.

7

10422.4 173. 761 86.83 11 7. 70 1199

220.000 10.982 . 09106 9.8374 566. 722 11549.

0

11612.

3

179.292 88.64 120.11 1149

230.000 10.806 .09254 9.2017 519.141 12763.8 12828.5 134. 685 90.49 122.61 1100

240.000 10.627 .09410 8.5614 474. 1 24 14004.9 14070.3 189.959 92.37 125.22 105 1 250.000 10.445 .09574 7.9615 431.422 15273.7 15340.7 195. 125 94.27 127.94 1003

260.000 10.258 .09749 7. 3975 390. 828 16571.

2

16639.4 200. 198 96.20 130.80 956

270.000 10. 066 .09935 6.8653 352.172 17898.9 17968.4 205.190 98.14 133.81 906

280.000 9.867 .10134 6.3612 315. 3 C6 19258.4 19329.3 210.114 100.10 137.00 861

290.000 9. 66 2 .10350 5.8817 280.117 20651.5 20723.9 214.980 102.05 140.42 814

300.000 9.447 .10586 5. 4236 246.5 00 22080.5 22154.6 219. 803 104.02 144.13 766

310.000 9. 221 . 10845 4.9835 214. 362 23548.6 23624.5 224. 594 105.98 148.22 718

320.000 3.931 .11135 4.5580 183.611 25059.8 25137.7 229. 371 107.94 152.83 668

323.680 8.888 .11251 4.4044 172.623 25623.0 25701.8 231. 117 108.66 154.70 650

323.680 . 30685 3.259 .030655 18.532 40 70 7. 5 42988.8 284. 525 98.74 116. 17 193

330.000 . 29691 3.368 . 029267 19.540 41366.5 43724.1 286. 774 100.14 116.55 197

340.000 .28295 3.534 . 027410 21.038 42420.6 44 8 94 .

5

290. 269 102.49 117.66 203

350.000 .27070 3.694 . 025851 22.444 43492.

3

46078.2 293. 700 104.94 119.16 209

360.000 .25981 3.849 . 024511 23.781 44584.0 47278.2 297. 081 107.44 120.91 214

370.000 .25002 4.000 . 023341 25. 060 45696.

8

48496.6 300. 420 109.96 122.62 219

380.000 .24113 4.147 . 022306 26.292 46832.

1

49735.1 303. 722 112.48 124.65 224

390 .000 .23301 4.292 .021381 27.435 47989.7 50993.9 306.992 115.01 126.96 228

400.000 .22554 4.434 .020547 28.643 49170.5 5 22 74.

1

310. 234 117.53 129.12 232

410.000 .21863 4.574 .019791 29.773 50374.

5

53576.2 313. 449 120.04 131.32 236

420.000 .21222 4.712 .019101 30.877 51602.

0

54900.4 316. 640 122.53 133.55 240

430.000 .20624 4.849 .018467 31.959 52852.9 56247.

0

319. 809 125.00 135.78 244

440.000 .20065 4.984 .017862 33.0 21 54127.

3

57615 .9 322.956 127.44 138.03 248

450.000 .19540 5.118 .017341 34. 066 55425.2 59007.6 326. 083 129.86 140.26 251

460.000 . 19046 5.250 . 016838 35. 095 56745.9 60421.

3

329. 191 132.25 142.50 255

470.000 .18580 5.382 .016368 36.110 58089.

7

61857.2 332. 279 134.61 144.71 258

480.000 . 18138 5.513 .015929 37.113 59456. 1 63315.3 335. 349 1 36.94 146.92 261

490.000 .17720 5.643 . 015517 38. 1 C4 60845.1 64795.3 333.401 139.24 149.10 264

500.000 .17323 5 . 773 . 015129 39. 0 85 62256.

3

66297.

1

341.435 141.51 151.27 268

520.000 . 16586 6.029 . 014417 41. 021 65 144 .

6

69365.0 347.451 145.95 155.53 274

540.000 . 15914 6.284 .013778 4 2.9 25 68118.6 72517.2 353 . 399 150.25 159.68 260

560.000 . 15299 6.536 .013201 44. 803 71178.

0

75751.4 359. 280 154.43 163.74 285

580.000 . 14733 6.787 .012676 46.659 74314.

8

79066.0 365. 094 158.48 167.68 291

600.000 .14211 7.037 .012196 48.457 77532.

0

82458.0 370.844 162.40 171.51 296

620.000 .13726 7.286 .011754 50.318 80825.

6

85925.5 376. 529 166.20 175.23 302

640.000 .13275 7.533 .011347 5 2.125 84193.3 89466.4 3« 2. 150 169.88 178.85 307

660.000 .12854 7.780 . 010969 53.919 87632.

7

930 78.4 337.707 173.44 182.35 312

680.000 .12460 8.026 . 010617 55.703 91141.

7

96759.6 393. 202 1 76.89 185.75 31 7 700.000 .12091 8.271 .010269 57.478 94718.2 100507.3 393. 634 180.24 189.05 322
Table 22. Continued

I-BUTANE ISOBAR AT P = 8 BAR

T DEN VOL OP/OT DP/CO E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.895 12.755 .07840 22.3215 1363. 078 24.9 87.6 108.478 73.26 98.84 1778

120.000 12.655 .07902 21.1751 1292. 4C4 631.2 694.4 113. 664 73.81 99. 81 1733

130.000 12.491 .08006 19.4722 1186. 943 1636.

8

1700.8 121. 718 74.85 101.46 1663

140.000 12.327 .08112 17.9541 1092.271 2658.

9

2723.

8

129. 300 76.01 103.20 1597

150.000 12.162 .08222 16.5913 1006.572 3698.4 3764.2 136. 482 77.29 105.02 1533

160.000 11.997 .08335 15.3602 928.426 4756.4 4823.1 143.320 78.68 106.93 1473

170.000 11.832 .08452 14.2423 856.7 03 5833.8 5901.4 149. 862 80.16 108.92 1415

180.000 11.665 .08573 13.2221 790.482 6931.5 7000.1 156. 145 81.73 110.98 1358

190.000 11.497 .08698 12.2871 729. 0 29 8050.6 8120.2 162. 203 83.37 113.13 1304

200.000 11.328 .08828 11.4266 671.728 9192.1 9262.7 168.063 85.07 115.37 1251

210.000 11.157 .08963 10.6316 618. 069 10356.8 10428.5 173. 747 86. 83 117.69 1200

220.000 10. 983 .09105 9.8946 567.6 28 11545,9 11618.7 179.277 88.64 120.09 1150

230.000 10.808 .09253 9.2089 520. 050 12760.3 12834.3 184. 670 90.49 122.59 1101

240.000 10.629 . 09408 8.5686 475.036 14001.1 14076.4 189.943 92.37 125.20 1052

250.000 10.447 .09572 7.9688 432.340 15269.5 15346.0 195.108 94.27 127.92 1004

260.000 10.260 .09746 7. 4049 391. 754 16566.5 16644.5 200. 180 96.20 130. 77 957

270.000 10.069 .09932 6.8729 353.1 08 17893.7 17973.2 205.171 98.14 133.77 909

280.000 9.871 . 10131 6.3689 316. 254 19252.6 19333.7 210. 093 100.10 136.96 862

290.000 9.665 .10346 5.8897 281. 080 20645.0 20727.8 214. 958 102.05 140.37 815

300.000 9.451 .10581 5.4318 247.481 22073.

2

22157.8 219. 778 104.02 1 44. 06 767

310.000 9.226 .10840 4.9922 215. 364 23540.2 23626.9 224.567 105.98 148.13 719

320.000 3.986 .11128 4.5672 184.641 25050.

0

25139.0 229. 340 107.94 152.71 670

329.260 8.749 .11430 4.1835 157.346 26483.5 26575.0 233. 751 109.76 157.60 623

329.260 .35149 2.845 .035752 17.982 41126.

8

43402.8 284. 859 100.67 119.61 191

330.000 . 35003 2.857 . 035536 18.111 41205.8 43491.3 285.128 100.82 119.60 192

340.000 .33196 3.012 .032970 19.770 42278.

7

44688.6 288. 702 103.02 119.99 199

350.000 . 31642 3.160 .030884 21.303 43364.

7

45893.0 292.194 105.38 121.03 205

360.000 .30280 3.302 . 029128 22.742 44468.0 47110.0 295. 623 107,81 122.46 210

370.000 .29070 3.440 . 027618 24. 1 08 45590.8 48342.9 299. 000 110.28 124.13 216

380.000 .27981 3.574 . 026300 25.415 46 734. 1 49593.1 302. 335 112.77 125.98 221

390.000 .26994 3.705 . 025133 26.672 47898.9 50862.5 305.633 115.27 127.94 225

400.000 .26092 3.833 . 024091 27.888 49085.9 52152.0 308. 898 117.76 129.99 230

410.000 .25262 3.958 . 023153 29. 069 50295.

5

53462.

2

312.133 120.25 132.10 234

420.000 .24496 4.082 .022302 3 0.218 51528. 2 54794.1 315. 342 122.72 134.24 238

430.000 .23784 4.205 .021525 31.341 52783.5 56147.1 318.526 125.17 136.41 242

440.000 .23120 4.325 . 020812 32.441 54061.8 57522.

0

321. 687 127.60 138.59 246

450.000 .22499 4 . 445 . 020155 33.520 55363.

1

58918.7 324. 826 130.01 140. 78 249

460.000 .21916 4.563 .019546 34.580 56687.1 60337.3 327. 944 132.38 142.97 253

470.000 .21368 4.680 . 018980 35. 625 58033.8 61777.8 331. 042 134.74 145. 15 256

480.000 .20850 4.796 .018453 36.654 59403.0 63240.0 334. 121 137.06 147.31 260

490.000 .20360 4.912 .017959 37.670 60794.5 64723.8 337. 180 139.35 149. 47 263

500.000 .19895 5.026 . 017496 38. 674 6220 8. 4 66229.4 340.222 141.61 151.61 266

520.000 .19035 5.254 . 016650 40.651 65100.8 69303.6 346. 250 146. 03 155.82 273

540.000 .18253 5.479 .015894 42.592 68078.3 72461.2 352. 208 150.33 159.94 279

560.000 .17539 5.702 .015213 44.5 03 71138.8 75700.2 358. 098 154.49 163.96 285

580.000 .16883 5.923 . 014595 46. 388 74280.

0

79018.6 363. 920 158.53 167.88 290

600.000 .16278 6.143 . 014032 48.251 77499.

6

82414.3 369.676 162.45 171.69 296

620.000 . 15718 6.362 .013516 5 0. 0 95 80795.3 85885.1 375. 366 166.24 175.39 301

640.000 .15197 6.580 .013040 51.9 24 84164.

3

89429.0 380. 992 169.91 178.99 306

660.000 .14712 6.797 . 012600 53. 738 87606.1 93044.0 386. 553 173.47 182. 48 311

680.000 .14258 7.014 . 012191 55. 540 91116.6 96727.5 392. 051 176.92 135.67 316

700.000 .13833 7.229 . 011810 57. 331 94694.5 100477.8 397. 487 180. 26 189.16 321

1 16
Table 22. Continued

I-BUTANE ISOBAR AT P = 10 BAR

T OEN VOL OP/DT OP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

113.980 12. 755 .07840 22.3224 1364.200 31.1 109.5 108.532 73.26 98.85 1779

120.000 12.657 .07901 21.1922 1294.498 628.7 707.7 113. 644 73.81 99.60 1735

130.000 12.493 .08005 19.4887 1168.972 1634.

0

1714.1 121.697 74.85 101.45 1665

140.000 12.329 .08111 17. 9701 1094.245 2655.8 2737.0 129. 278 76.01 103.19 1598

150.000 12.164 .08221 16.6068 10 06.5 03 3695.1 3777.3 136.459 77.29 105.01 1535

160.000 12.000 .08334 15.3755 930. 321 4752.

7

4836.1 143.297 78.68 106.92 1474

170.000 11.834 .08450 14. 2573 858.570 5829.7 5914.

2

149. 838 80 .16 108.90 1416

180.000 11.667 .08571 13.2368 792.328 6927.

1

7012.8 156. 121 81.73 110.97 1360

190.000 11.500 .08696 12.3016 730. 859 8045.

8

8132.8 162.178 03.37 113.12 1306

200.000 11.331 .08826 11.4410 673.547 9186.8 9275.0 168. 036 85.07 115.35 1253

210.000 11.160 . 0 8961 10.6460 619. 883 10351.

0

10440.6 173. 720 06.83 117.66 1202

220.000 10.987 .09102 9.9090 569.441 11539.6 11630.6 179.248 88 .64 120.06 1151

230.000 10.812 .09249 9. 2232 521.865 12753.

4

12845.8 184.640 90.49 122.56 1102

240.000 10.633 .09404 8.5831 476.859 13993.5 14087.5 189.911 92.37 125.16 1054

250.000 10.451 .09568 7. 9834 434.174 15261.1 15356.7 195. 074 94.27 127.87 1006

260.000 10.265 .09742 7.4197 393. 6C4 16557. 3 16654.

7

200. 144 96.2 0 130.71 959

270.000 10.074 .09926 6.8879 354.978 17883.4 17982.

7

205.133 98.14 133.70 912

280.000 9. 877 .10125 6.3643 318.148 19241.1 19342.4 210.052 10 C.IO 136.87 865

290.000 9. 672 .10339 5.9055 283. 0 03 20632.1 20735.5 214.913 102.05 140.25 018

300.000 9.459 .10572 5.4483 249. 439 22058.

6

22164.

3

219. 729 104.02 143.92 770

310.000 9.235 .10829 5.0094 217.366 23523.5 23631.8 224.512 105.98 147. 94 722

320.000 8.997 .11115 4.5855 186. 695 25030.6 25141.7 229.279 107.94 152.46 673

330.000 8.742 .11439 4.1728 157.331 26585.3 26699.7 234.049 109.90 157.69 623

339.057 8. 492 .11776 3.8046 131.763 28030.

4

28148.1 238. 382 111.60 163.34 575

339.057 .44334 2.256 . 046655 16. 825 41854.9 44110.5 285.461 104.15 126.47 187

340.000 .44075 2.269 . 046249 17.012 41960.9 44229.7 285.812 104.32 126.33 188

350.000 .41603 2.404 . 042538 18.867 43085.

1

45488.8 289.462 106.30 125.77 195

360.000 .39521 2.530 .039595 20.555 44 217.9 46748.1 293. 010 108.63 126.21 202

370.000 . 37723 2.651 .037163 22.123 45363.8 48014.7 296.481 110.99 127.22 200

380.000 .36144 2.767 . 035101 23.598 46526.

4

49293.2 299. 891 113.39 128.57 214

390.000 .34736 2.879 . 033318 24.999 47708.0 50536.8 303. 251 115.01 130.16 219

400.000 .33469 2.988 .031756 26. 340 48909.

1

51896.9 306. 568 118.25 131.92 224

410.000 .32318 3.094 .030372 27. 630 50130.9 53225.2 309. 843 12 C.68 133. 79 229

420.000 .31265 3.196 . 029133 28.877 51374.2 54572.6 313. 096 123.11 135.74 234

430.000 .30296 3.301 . 028015 30.087 52639.

1

55939.9 316. 313 125.53 137.75 230

440.000 .29399 3.401 .027001 31.266 53926.3 57327.8 319.503 127.93 139.80 242

450.000 .28566 3 .501 .026074 32. 416 55235.

3

58735.9 322. 668 130. 30 141.87 246

460.000 . 27788 3.599 . 025223 33.541 56566.3 60164.9 325.809 132 .66 143.96 250

470.000 .27060 3.695 . 024436 34.645 57919.4 61614.8 328. 927 134.99 146.05 253

480.000 .26376 3.791 .023711 35. 729 59294.4 63085.7 332.024 137.29 148.14 257

490.000 .25732 3.866 . 023034 36.796 60691.2 64577.4 335. 100 139.56 150.23 261

500.000 .25123 3.980 . 022403 37. 847 62109.6 66090.0 338. 156 14 1. 80 152.31 264

520.000 .24000 4.167 .021258 39.908 65010.9 69177.6 344. 210 146.20 156.42 271

540.000 .22986 4.351 . 020244 41.923 67995.8 72346.3 350. 190 150.47 160.46 277

560.000 .22064 4.532 . 019338 43.898 71062.7 75595.1 356. 097 154.62 164.42 283

580.000 .21 220 4.713 . 018522 45. 841 74209. 5 78922.1 361 . 934 158.64 168.28 209

600.000 .20444 4.891 .017781 47.757 77433.9 82325.3 367. 703 162.54 172.04 294

620.000 .19726 5.069 .017105 49.648 80734.2 85803.1 373. 404 166.32 175.71 300

640.000 . 19064 5.246 .016485 51 .5 19 84107.4 89352.9 379. 039 169.90 179.27 305

660.000 .18446 5.421 .015913 53.372 87551.9 92973.0 384. 609 173.53 182. 73 310

680.000 .17870 5.596 .015383 55. 210 91065.

4

96661.4 390. 114 176.97 106.10 316

700.000 .17330 5.770 .014691 57.034 94645.9 100416.

1

395. 556 180.31 109.37 321

1 17
Table 22. Continued

I-BUTANE ISOBAR AT P = 12 BAR

T DEN VOL DP/DT DP/CO E H S CV CP M DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.065 12.755 .07840 22.3233 1365. 326 37.2 13 1.3 108.585 73.27 98.86 1780

120.000 12.658 .07900 21.2092 1296.593 626. 3 721.1 113. 623 73.81 99. 80 1736

130.000 12. 495 .08003 19.5052 1191. 0 00 1631.

3

1727.4 121. 676 74.85 101.45 1666

140.000 12.331 .08110 17.9861 1096.2 19 2652.3 2750.2 129. 257 76. 01 103.18 1600

150.000 12. 166 . 06219 16.6224 1010.433 3691.8 3790.4 136.437 77.29 105.00 1536

160.000 12.002 .08332 15.3907 932.216 4749.1 4849.1 143.274 78.68 106.90 1476

170.000 11.836 .08449 14.2722 860.436 5825.

7

5927.1 149. 814 80.16 108.89 1418

180.000 11.670 .08569 13.2516 794.172 6922.7 7025,5 156. 096 81.73 110.95 1361

190.000 11. 502 .06694 12.3162 732.6 f8 8041.

0

8145.3 162. 152 83.37 113.10 1307

200.000 11.334 .08823 11.4554 675. 365 9181.5 9237.4 168.010 85.07 115.33 1255

210.000 11.163 .08956 10.6604 621.695 10345.

3

10452.8 173.692 86.83 117.64 120 3 220.000 10.990 .09099 9.9233 571. 251 11533.

2

11642.4 179. 219 88.64 120.03 1153

230.000 10.815 .09246 9.2376 523.679 12746. 4 12857.4 184.610 90.49 122.53 1104

240.000 10.638 .09401 8.5975 478.680 13985.9 14098.7 189.879 92.37 125.12 1056

250.000 10.456 .09564 7.9979 436.0 06 15252.7 15367.5 195.041 94.27 127.82 1008

260.000 10.270 .09737 7.4344 395. 451 16546.

0

16664.9 200. 109 96.20 130.65 961

270.000 10.080 .09921 6.9029 356. 844 17873.2 17992.2 205. 095 98.14 133.63 914

260.000 9.883 . 10118 6.3996 3 20. 039 19229.7 19351.1 210.011 10 C.IO 136.78 867

290.000 9.679 .10331 5.9213 264.923 20619.3 2 0743.2 214. 869 102.05 140.14 820

300.000 9.467 .10563 5.4647 251. 393 22044.

1

22170.8 219.680 104.02 143. 78 773

310.000 9.244 .10818 5.0265 219.361 23506.9 23636.7 224.459 105.98 147.77 725

320.000 9.008 .11102 4.6036 186.741 25011.

4

25144.6 229.219 107.94 152.23 676

330.000 3.755 .11422 4.1923 159.442 26562.8 26699.8 233.980 109.90 157.36 626

340.000 8.480 .11793 3.7880 131.350 28168.6 28310.1 238. 766 11 1.87 163.52 574

347.524 8.253 .12116 3.4847 110.9 11 29407.

6

29553.0 242.400 113.36 169.22 533

347.524 .53929 1.854 . 058611 15.620 42470.4 44695.5 285.973 107.26 133.54 182

350.000 .53026 1.386 .057132 16.165 42762.2 45025.2 286.918 107.67 132.80 185

360.000 .49849 2.006 . 052186 18. 191 43936.

8

46344.1 290. 634 109.61 131.30 193

370.000 .47219 2.118 .046335 20. 0 13 45114.

0

47655.3 294,227 111.78 131.16 200

380.000 .44978 2.223 . 045194 21.690 46301.

4

48969.4 297. 732 114.06 131. 75 207

390.000 .43026 2.324 . 042557 23.258 47502.6 50291.6 301. 167 116.40 132.80 213

400.000 .41301 2.421 .040297 24. 740 48720.5 51626.0 304.546 118.76 134.16 219

410.000 . 39756 2.515 .038330 26. 152 49956.9 52975.

3

307. 877 121. 14 135. 72 224

420.000 .38360 2.607 . 036597 27.5 06 51212.5 54340.7 311.168 123.53 137.42 229

430.000 .37088 2.696 .035053 28.810 52488.2 5 5723.8 314.423 125.90 139.23 234

440.000 .35921 2.784 .033667 30.072 53784.6 57125.3 317.645 128.26 141.12 238

450.000 . 34845 2.870 .032413 31.297 55102.

4

58546.2 320.833 130.61 143.05 242

460.000 . 33846 2.955 .031271 32.491 56441 •

0

59986.4 324.003 132.94 145.02 246

470.000 .32917 3.038 . 030226 33.657 57800.9 6 14 46 .

5

327. 144 135.24 147.02 25 0 480.000 .32043 3.120 .029264 34.798 59182.2 62926.6 33 0. 26 0 137.52 149.02 254

490.000 .31233 3.202 .028375 35.917 60584.

6

64426.7 333. 353 139.78 151. 04 258

500.000 . 30466 3.282 . 027551 37. 0 17 62008.2 65947.0 336.425 142.00 153.05 261

520.000 .29059 3.441 .026065 39.164 64918. 6 69048.

2

342. 506 146.37 157. 05 268

540.000 .27795 3.598 .024761 41.253 67911.3 72228.6 343.507 150.62 161.00 275

560.000 .26651 3.752 .023604 43.295 70984.8 75487.5 354.433 154.74 164.89 281

580.000 .25609 3.905 . 022568 45. 296 74137.

3

78823.2 360. 286 158.75 168.69 287

600.000 .24654 4.056 . 021633 47.263 77367.1 82234.5 366. 067 162.63 172.41 293

620.000 .23775 4.206 . 020784 49.201 80671.5 85718.9 371.780 166.40 176.03 299

640.000 .22961 4.355 .020008 51.115 84048.6 89274.8 377.425 170.05 179.56 304

660.000 .22206 4 .503 . 019296 53. 0 07 87496.5 92900.4 383. 003 173.59 182.99 310

680.000 .21503 4.65 0 . 018638 54. 880 91013.

1

96593.7 388.516 177.03 186.33 315

700.000 .20846 4.797 . 018028 56. 736 94596.5 100352.9 393. 964 180.35 189.58 320

118
Table 22. Continued

I-8UTANE ISOBAR AT P = 14 BAR

T OEN VOL OP/DT OP/CD c H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.150 12. 755 .07840 22.3241 1366.434 43.3 153.1 108. 639 73.28 98.87 1780

IZO.OOO 12.660 .07899 21.2262 1298.688 623. 8 734. 4 11 3. 60 3 73. 81 99.79 1737

130.000 12.496 .08002 19.5216 1193. 0 28 1628.6 1740.7 121. 655 74.85 101.44 1667

140.000 12.333 .08109 18.0020 1098.193 2649.

8

2763.4 129. 235 76. 01 103.17 1601

150.000 12.168 .08218 16.6379 1012. 362 3688.

4

3603.5 136.415 77.29 104.99 1538

160.000 12.004 .08331 15.4059 934.1 10 4745.4 4862.1 143. 251 78.68 106.89 1477

170 . 000 11.839 .08447 14.2871 862. 3 02 5821.

7

5940.0 149. 791 80.16 108. 88 1419

180.000 11.672 .08567 13.2663 796.0 16 6918.

3

7038.3 156. 072 81.73 11 0.94 1363

190.000 11.505 .08692 12. 3307 734.5 16 8036.2 8157.9 162. 127 83.37 113.08 1309

200.000 11.337 .08821 11.4699 677.182 9176.3 9299.8 167.983 35 . 07 115.30 1256

210.000 11.166 .08956 10.6747 623.5 06 10339.

5

10464.9 173. 665 86.83 117.61 1205

220.000 10.994 .09096 9.9376 573. 061 11527. 0 11654.3 179. 191 38.64 120.01 1155

230.000 10.819 .09243 9.2519 525.491 12739.6 12869.0 184.580 90.49 122.49 1106

240.000 10.642 .09397 8.6118 480.499 13978.

3

14109.9 189.847 92.37 125.08 1058

250.000 10.461 .09560 8.0124 437.836 15244.4 15378.2 195. 007 94.27 127. 77 1010

260.000 10.275 .09732 7. 4491 397.296 16538.9 16675.1 200. 073 96.20 130. 59 963

270.000 10.085 .09915 6.9178 358.708 17863.0 18001.8 205. 057 98.14 133.56 916

280.000 9.889 . 10112 6.4149 321.926 19218.

3

19359.9 209.970 100.10 136.69 869

290.000 9.686 .10324 5.9371 286.838 20606.5 2 0751 .

1

214. 824 102.05 140.04 822

300.000 9.475 .10554 5.4810 253.342 22029.

7

22177.4 219.632 104.02 143.64 775

310.000 9.253 .10807 5.0436 221.350 23490.5 23641.8 224.405 105.98 147.59 728

320.000 9. 018 .11089 4. 6217 190. 780 24992.

4

25147.7 229. 159 107.94 151.99 679

330.000 9.767 .11406 4.2116 161.543 26540.5 26700.1 233.912 109.90 157.04 630

340.000 8.495 .11772 3.8091 1 33.534 28141.8 28306.6 238.686 11 1. 87 163.07 578

350.000 8.193 .12205 3.4082 10 6. 6 00 2980 7.

9

29978.7 243.518 113.85 170.67 524

355.019 9.027 .12458 3.2047 93.4 12 30662.9 30837.3 245. 983 114.86 175. 43 495

355.019 .64016 1.562 . 071769 14.383 42999.

0

45186.0 286.399 110.10 141.12 178

360.000 .61698 1.621 .067843 15.586 43613.

2

45882.3 288. 348 110.85 138.77 183

370.000 .57817 1.730 . 061672 17.747 44834.9 47256.3 292.113 112.72 136.44 192

380.000 .54651 1.830 . 056920 19. 676 46054.

7

48616.4 295. 740 114.82 135.77 200

390.000 .51977 1.924 .053078 2 1.442 47280.9 49974.4 299. 268 1 17.04 136.01 207

400.000 .49666 2.013 .049874 23. 086 48519.

3

51338.1 302. 721 119.32 136.79 213

410.000 .47634 2.099 . 047144 24.634 49772.

2

52711.

3

306.112 121 .63 137.94 219

420.000 .45823 2.182 . 044779 26.1 (4 51041.9 54097.2 309. 452 123.96 139.32 224

430 .000 . 44191 2.263 . 042702 27.5 10 52330.2 55498.2 312. 748 126.29 140.88 229

440.000 .42709 2.341 . 040860 28.862 53637.2 56915.2 316.006 128.61 142.57 234

450 .000 .41353 2.418 .039210 30. 167 54 964 .

0

58349.5 319. 230 130.93 144.34 239

460.000 .40104 2.493 .037721 31.433 56310.9 59801.8 322. 422 133.23 146.17 243

470.000 . 39949 2.567 . 036369 32.663 5767 8.6 61273.1 325.586 135.50 148.05 247

480.000 . 37874 2.640 .035133 33.863 59066.5 62763.0 328.723 137.76 149.96 251

490.000 .36871 2.712 .033998 35. 0 36 60475.

0

64272.0 331 . 835 140.00 151.89 255

500.000 .35931 2.793 . 032951 36. 185 61904.

1

65900.5 334.923 142.20 153.83 259

520.000 .34215 2.923 .031080 38. 421 64624.

1

68915.9 34 1 . 032 146.54 157.71 266

540.000 .32683 3.060 .029450 40.586 67824.8 72108.4 34 7. 056 150.76 161 .57 273

560.000 .31303 3.195 . 028015 42.694 70905.3 75377.7 353.001 154.87 165.37 280

580.000 .30051 3.329 . 026738 44. 754 74063.

8

78722.5 358. 869 158.86 169. 12 286

600.000 .29909 3.459 . 025592 46.774 77298.9 82141.8 364.665 162.73 172. 78 292

620.000 .27859 3.590 . 024556 48. 759 80607.

6

85633.2 370.389 166.48 176.36 298

640.000 .26890 3.719 .023612 50.715 83988.8 89195.3 376.043 170.12 179.86 303

660.000 .25992 3.847 . 022749 52.645 87440.

3

92826.4 381. 630 1 73.66 183.26 309

680.000 . 25158 3.975 . 021955 54. 553 90960.

0

96524.8 337.150 177.08 186.57 314

700.000 .24391 4.102 .021221 56. 442 94546.5 100288.3 392. 605 180.40 189. 80 319

1 19
Table 22. Continued

I-BUTANE ISCBAR AT P = 16 BAR

T DEN VOL OP/OT DP/DD E H S CV CP M DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.234 12. 756 .07840 22.3250 1367.562 49.4 174.8 108.692 73.28 98.87 1781

120.000 12.661 .07898 21.2432 1300.783 621. 4 747.8 113.582 73.81 99.78 1739

130.000 12.498 .08001 19.5380 1195.056 1625.9 1753.9 121. 634 74.85 101.43 1669

140.000 12. 334 .08107 18. 0180 1100.167 2646.8 2776.6 129.214 76.01 103.16 1602

150.000 12. 170 .08217 16.6535 1014.292 3685.1 3816.6 136.393 77.29 104.98 1539

160.000 12.006 .08329 15.4211 936. 0 03 4741.8 4875.1 143. 228 78.68 106.88 1479

170.000 11.841 .08445 14.3021 864. 167 5817.7 5952.9 149.767 80.16 106.86 1420

180.000 11.675 .08565 13.2810 797. 860 6914.

0

7051.0 156. 047 81.73 110.92 1364

190.000 11.508 .08690 12.3452 736.343 8031.4 8170.4 162. 102 83.37 113.06 1310

200.000 11.339 .08819 11.4842 678.999 9171.0 9312.1 167.957 85.07 115.28 1258

210.000 11.169 .08953 10.6890 625. 316 10 333.8 10477.1 173. 637 86.83 117.59 1207

220 .000 10.997 .09093 9.9518 574.869 11520.7 11666.2 179. 162 88.64 119.98 1157

230.000 10.823 .09240 9.2662 527. 302 12732.7 12880.5 184.550 90.49 122.46 1108

240.000 10.646 .09393 8.6262 482. 316 13970.8 14121.1 189.816 92.37 125.04 1059

250.000 10.465 .09555 8.0269 439.664 15236.1 15389.0 194.974 94.2 7 127.72 1012

260.000 10. 280 .09727 7.4637 399. 1 39 16529.

7

16685.3 200. 038 96.20 130.54 965

270.000 10.091 .09910 6.9327 360.569 17852.

9

18011.4 205. 019 98,14 133.49 918

280.000 9.896 .10106 6.4302 323.310 19207. 1 19368.7 209.929 100.10 136.61 871

290.000 9.693 .10316 5.9527 288.749 20593.9 20758.9 214. 780 102.05 139.93 825

300.000 9.483 .10545 5.4972 255. 286 22015.

4

22184.1 219. 584 104.02 143.51 778

310.000 9.262 .10797 5.0606 223.334 23474.2 23646.9 224.352 105.98 147.42 731

320.000 9.029 .11076 4.6396 192.811 24973.6 25150.9 229. 100 107.94 151.77 682

330.000 3.779 .11390 4.2308 163.6 35 26518.4 26700.7 233.844 109.90 156.74 633

340.000 3.510 .11751 3.8301 1 35. 706 28115. 4 28303.4 238.608 111.87 162.62 582

350.000 3.212 .12177 3. 4317 108.884 29775.3 29970.1 243.423 113.85 169.99 528

360.000 7.874 .12700 3. 0266 32.942 31516.

6

31719.

8

248. 344 115.88 180. 01 470

361.768 7.808 .12807 2.9532 78.421 31826.

3

32031.2 249. 240 116.24 182.23 459

361.768 . 74695 1.339 .086319 13.126 43456.

1

45598.

2

286. 741 112.76 149.56 173

370.000 .69939 1 .430 . 078077 15.276 44515.9 46803.7 290.037 113.86 144.05 182

380.000 .65406 1.529 .070784 17.532 45780.5 48226.8 293.833 115.70 141.08 191

390.000 .61741 1.620 . 065193 19.539 47039.6 49631.0 297.481 117.76 140.01 199

400.000 .58666 1.705 . 060694 21. 371 48302.9 51030.2 301. 024 119.92 139.96 207

410.000 .56020 1.785 . 056956 23. 073 49575.

8

52431.9 304.486 122.15 140.52 213

420.000 .53702 1.862 .053782 24.673 50862.3 53841.8 307. 883 124.42 141.49 219

430.000 .51641 1.936 .051039 26. 1 89 52164.2 55262.5 311.226 126.69 142.73 225

440.000 .49790 2.008 .048636 27.637 53483.4 56696.9 314. 524 128.98 144.17 230

450.000 .48111 2.079 . 046509 29. 027 54820.6 58146.2 317. 781 131.25 145.74 235

460.000 .46577 2.147 . 044607 30.368 56176.6 59611.7 321.002 133.52 147.41 240

470.000 .45167 2.214 . 042893 31.666 57552.0 61094.4 324. 191 135.77 149.16 244

430.000 .43863 2.230 .041339 32.927 58947.4 62595.1 327.350 138.01 150.96 248

490.000' .42652 2.345 .039921 34. 156 60362.

3

64113.6 330.482 140.22 152. 79 253

500.000 .41522 2.408 . 038620 35. 356 61797.2 65650.6 333.587 142.41 154.64 257

520.000 .39471 2.534 . 036311 37.681 64727.4 68781.0 339. 725 146,71 158.39 264

540.000 .37651 2.656 .034319 39.924 67736.6 71986.1 345. 774 150 .91 162.15 271

560.000 .36020 2.776 .032576 42.099 70824.3 75266.2 351. 738 154.99 165.87 278

580.000 . 34547 2.895 .031035 44. 2 18 73989.

3

78620.7 357. 623 158.96 169.55 284

600.000 .33206 3.012 . 029659 46.290 77229.

3

82047.7 363. 432 162.82 173.16 291

620.000 .31978 3.127 . 028421 4 8. 3 22 80542.8 85546.2 369. 168 166.56 176.70 296

640.000 .30849 3.242 .027299 50.320 83928.1 89114.7 374. 833 170.19 180.15 302

660.000 .29804 3.355 .026275 52.289 87383.

5

92751.

8

380.428 173.72 183.53 308

680.000 .28836 3.468 .025336 54.232 90906.5 96455.2 385.956 177.13 186.81 313

700.000 .27933 3.580 . 024470 56. 152 94495.6 100223.5 391.418 180.45 190.02 318

120
Table 22. Continued

I-BUTftNE IS0B4R AT P = 18 BAR

T OEN VOL DP/OT OP/CD E H S CV CP W OEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.318 12.756 . 0 7840 22.3261 1368.694 55.4 196.5 108.744 73.29 98. 88 1782

120.000 12.663 .07897 21.2602 1302. 878 619.0 761.1 113.562 73.81 99. 78 1740

130.000 12,. 50 0 .08000 19.5545 1197.084 1623.2 1767.2 121. 613 74.85 101. 42 1670

140. 000 12.336 .08106 18. 0339 1102. 140 2643.8 2789.8 129.192 76.01 103.16 1604

150.000 12.172 .08215 16.6690 1016. 221 3681.8 3829.7 136.370 77.29 104.97 1540

160.000 12.008 .08328 15.4363 937. 897 4738.2 4888.1 143. 205 78.68 106.87 1480

170.000 11.843 .08444 14. 3170 666. 032 5813. 8 5965.7 149. 743 80.16 108.85 1422

180.000 11.677 .03564 13.2957 799.711 6909.6 7063.7 156.023 81.73 110.91 1366

190.000 11.511 . 08688 12.3598 738.169 8026.6 8183.0 162. 076 83.37 113.04 1312

200.000 11.342 .08816 11.4986 680. 814 9165.8 9324.5 167.931 85.07 115.26 1259

210.000 11.173 .08950 10.7033 627. 125 10328.

1

10489.

2

173. 610 86.83 117.56 1208

220.000 11.001 .09090 9.9661 576.676 11514.5 11678.1 179. 133 88.64 119.95 1158

230.000 10. 827 . 09236 9.2804 529.111 12725.

9

12892.1 184.520 90.49 122.42 1109

240.000 10.650 . 09390 8.6405 484.132 13963.3 14132.3 189. 784 92.37 125.00 1061

250.000 10.470 .09551 8.0413 441. 490 15227.9 15399.8 194.941 94.27 127.68 1014

260.000 10.285 .09722 7.4763 400. 979 16520.6 166 95.6 200. 002 96.20 130.48 967

270.000 10.096 . 09904 6. 9476 362. 428 17842.8 18021.1 204.981 98.14 133.42 920

280.000 9.902 . 10099 6.4453 325.691 19195.8 19377.6 209.889 100.10 136.52 674

290.000 9.700 .10309 5.9683 290.657 20581.3 2 0766 .9 214. 737 102.05 139.83 827

300.000 9.491 .10537 5. 5134 257. 2 25 22001.2 22190.9 219. 536 104.02 143. 38 781

310.000 9.271 .10786 5.0774 225.3 11 23456.1 23652.2 224. 300 105.98 147. 25 733

320.000 9.039 .11063 4.6574 194.836 24955.0 25154.2 229.041 107.94 151.55 686

330.000 8 . 702 .11375 4.2498 165.7 18 26496.7 26701.4 233.777 109.90 156. 43 637

340.000 8.524 .11731 3.8508 1 37. 865 28089.

4

28300.6 238.530 111.87 162.20 586

350 .000 8. 230 . 12151 3.4548 111.150 29743.3 29962.0 243. 331 113.85 169.34 533

360.000 7.898 .12662 3. 0537 85. 371 31475.

5

3 1703.4 248. 223 115.87 178.92 476

367.916 7.593 .13170 2.7225 65.389 32917.

8

33154.3 252.244 117.57 189.90 426

367.916 . 86079 1.162 .102502 11.854 43850.

6

45941 .

7

286. 999 115.28 159.29 167

370.000 .84353 1.185 . 099295 12.5 C2 44136.7 46270.6 287.890 115.41 156. 42 170

380.000 . 77627 1.288 .087596 15. 2 22 4547 0.4 47789.1 291.941 116.74 148.53 182

390.000 .72536 1.379 .079355 17.533 46773.7 49255.2 295.750 118.56 145.18 192

400.000 . 6843 4 1 .461 . 073034 19.590 48068.9 50699.

1

299. 406 120.59 143.84 200

410.000 . 65003 1.536 . 067950 21 . 468 49366.1 52135.2 302.953 122.71 143.58 207

420.000 .62057 1.611 . 063732 23.211 50672.

1

535 72.

6

306.417 124.90 143.99 214

430.000 .59480 1.681 . 060152 24.848 51990.2 55016.4 309.814 127.12 144.82 220

440.000 .57193 1.748 . 057063 26.399 53322.6 56469.8 313.155 129.35 145.95 226

450.000 .55141 1.814 .054359 27.879 54671.

2

57935.6 316.450 131.59 147.28 231

460.000 .53282 1 .877 .051966 29.298 56037.5 59415.7 319.703 133.83 148. 76 236

470.000 .51585 1.939 . 049829 30.667 57421.6 60911.0 322.919 136.05 150.35 241

480.000 .50025 1.999 .047906 31.992 58624.5 62422.

7

326.102 138.26 152.02 246

490 .000 .48584 2.058 .046162 33. 278 60246. 6 63951 .

5

329. 254 140.45 153.74 250

500.000 . 47246 2. 117 .044571 34.530 61687.8 65497.6 332.378 142.62 155.51 254

520.000 . 4433 1 2.231 . 041770 36. 947 6462 8.6 68643.6 338. 547 146.89 159.11 262

540.000 .42702 2.342 .039373 39. 268 67646.7 71861.9 344. 620 151.06 162.75 269

560.000 .40805 2.451 .037292 41.510 70 741.9 75153.1 350. 604 155.12 166.39 276

580.000 . 39097 2.558 . 035463 43.6 69 73913.2 78517.1 356. 506 159.07 170.00 283

600.000 .37549 2.663 . 033838 45.813 77158.

8

81952.5 362.329 162.92 173.55 289

620.000 .36136 2.767 . 032382 47.892 80477.

1

85458.3 363. 077 166.65 177.04 295

640.000 .34839 2.870 .031068 49.932 83866.

9

89033.6 373 . 752 1 70.27 180.46 301

660 .000 .33642 2.972 . 029873 51 . 939 87325.

7

92676.

1

379. 357 173.76 183.80 307

680.000 . 32534 3.074 . 028781 53.917 90852.0 96384.7 384. 892 177.19 187.06 312

700.000 .31504 3.174 . 027777 55. 869 94444.

0

100157.6 390.361 180.50 190.24 318

121
Table 22. Continued

I-BUTANE ISOBAR AT P = 20 BAR

T OEN \iOL OP/DT DP/CO E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.402 12.756 .07840 22.3272 1369. 8 29 61.4 218.2 108. 797 73.30 98.89 1783

120.000 12.664 .07896 21.2772 1304. 973 616.6 774.5 113.542 73.81 99.77 1742

130.000 12.501 .07999 19.5709 1199. 112 1620.5 1780.5 121. 592 74.85 101.42 1671

140.000 12.338 .08105 18.0498 1104. 1 13 2640.9 2803.0 129.171 76.01 103.15 1605

150.000 12.174 .08214 16.6845 1018. 149 3678.5 3842.8 136.348 77.29 104.96 1542

160.000 12.010 .08326 15.4515 939. 789 4734.5 4901.1 143. 183 78.68 106.86 1481

170.000 11.845 .08442 14.3319 367.896 5809.8 5978 .6 149.720 80.16 108.84 1423

130.000 11.630 .08562 13.3104 801.553 6905.

2

7076.5 155.998 81.73 110.89 1367

190.000 11.513 . 08686 12.3742 739.995 8021.9 8195.6 162. 051 83.37 113.03 1313

200.000 11.345 .08814 11.5130 682.628 9160.6 9336.9 167.904 85.07 115.24 1261

210.000 11.176 .08943 10.7176 628.9 33 10 322.

4

10501.4 173.582 86.83 117.54 1210

220.000 11.004 .09087 9.9803 578. 482 11508.2 11690.0 179. 105 88.64 119,92 1160

230.000 10.831 .09233 9.2946 5 3 0.919 12719.1 12903.7 184.490 9 C.49 122.39 1111

240.000 10. 654 .09386 6.6548 485.946 13955.8 14143.6 189. 753 92.37 124.96 1063

250.000 10.474 .09547 8.0557 443. 3 14 15219.6 15410.6 194. 907 94.27 127.63 1016

260 .000 10. 290 .09718 7.4929 402.8 17 16511.5 16705.9 199. 967 96.2 0 130.42 969

270.000 10.102 .09899 6. 9624 364. 283 17832.8 18030.7 204.944 98.14 133.35 922

280.000 9.908 .10093 6. 4605 327.568 19134.7 19336.5 209.849 100.10 136.44 876

290.000 9.707 .10302 5.9839 292.561 20568.8 20774.9 214. 693 102.05 139.72 830

300.000 9.493 .10528 5.5295 259. 160 21937.

2

22197.7 219.489 104.02 143.25 783

310.000 9.280 .10776 5.0942 227.284 23442. 1 23657.6 224. 247 105.98 147. 08 736

320.000 9.049 .11051 4.6750 196.853 24936.6 25157.7 228.983 107.94 151.33 689

330.000 8.804 .11359 4.2687 167.792 26475.2 26702.4 233. 711 109.90 156.14 640

340.000 8.539 .11711 3.8713 140.012 28063.

8

28298.1 238. 454 111. 87 161.78 590

350.000 8.243 .12124 3.4777 113.398 29712.0 29954.4 243. 240 113.85 168.73 537

360.000 7. 921 .12625 3. 0802 87.770 31435.4 31687.9 248.114 115.87 177.90 481

370.000 7.537 .13268 2.6648 6 2.8C6 33264.

3

33529.7 253.161 118.03 191.68 418

373.569 7.378 .13553 2.5071 53.942 33952.

8

34223.9 255.050 118.87 198.83 393

373.569 .93313 1.017 .120631 10.574 44188.1 46222.5 287. 169 117.71 170.90 162

380.000 .91979 1.087 .108812 12.680 45107.6 47282.0 289.982 118.07 160.01 171

390.000 .84690 1.181 .096254 15.401 46476.

0

48837.6 294.023 119.50 152.21 183

400.000 . 79156 1.263 .087280 17. 733 47813.

3

50339.9 297. 827 121.32 148.74 193

410. 000 . 74695 1.339 .080361 19.8 15 49141.1 51818.7 301.479 123.32 147.27 201

420.000 .70962 1.409 .074783 21. 719 50470.

1

53288.5 305. 022 125.42 146.89 209

430.000 .67757 1.476 . 070149 23.467 51806.8 54758.5 308.481 127.57 147.19 215

440.000 .64954 1.540 . 066214 25.149 53154.

7

56233.8 311.872 129.75 147.93 222

450.000 . 62468 1.601 . 062816 26.7 24 54516.

2

57717.

9

315. 208 131.94 148.97 227

460.000 .60236 1.66 0 .059841 28.227 55893.2 59213.5 318. 496 134.14 150.22 233

470.000 .53215 1.718 .057209 29.669 57287.1 60722.7 321. 741 136. 3 3 151.63 238

480.000 .56370 1.774 .054857 31. 059 58698.3 62246.3 324.949 138.51 153.15 243

490.000 .54675 1.829 . 052740 32.403 60127.9 63785.9 328. 123 140.68 154.75 247

500.000 .53108 1.883 .050321 33.708 61575.6 65341.5 331.266 142.83 156.41 252

520.000 .50299 1.988 . 047466 36.219 64527.4 68503.

7

337.468 147.07 159.85 260

540.000 .47838 2.090 .044620 38.619 67555.2 71735.9 343.567 151.21 163.38 267

560.000 .45657 2.190 . 042167 40. 929 70658.1 75038.6 349.572 155.25 166.92 275

580 .000 .43703 2.288 . 040024 43. 167 73836.

1

78412.5 355.491 159.18 170.45 282

600.000 .41937 2.385 . 038131 45.344 77087.

3

81856.3 361.329 163.01 173.95 288

620.000 .40330 2 .480 . 036442 47.470 80410.6 85369.6 367. 039 166.73 177.39 294

640.000 .33359 2.573 . 034922 49.552 83804.7 88951.4 372. 775 170. 34 180. 77 300

660 .000 .37506 2.666 .033546 51.596 87267. 3 92599.8 378. 383 173.84 184. 07 306

680.000 . 36254 2.758 . 032291 53.6 09 90 797.

0

96313.6 383.931 177.24 187.31 312

700.000 . 35093 2.850 . 031141 55.593 94392.

0

100091.2 389.406 180.54 190.46 3 '.7 122
Table 22. Continued

I-SUTANE ISOBAR AT P = 22 BAR

T OEN VOL OP/OT OP/CO E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/< J/MOL/K M/SEC

114.486 12.756 .07840 22.3283 1370 . 968 67.4 239.8 108. 849 73.31 98.89 1783

120.000 12.666 .07895 21.2942 1307. 068 614.1 787.8 113. 521 73.81 99.76 1743

130.000 12.503 .07998 19.5873 1201. 140 1617.

8

17 93.

3

121.571 74.85 101.41 1673

140.000 12. 340 .08104 18.0658 1106.087 2637.9 2816.2 129. 149 76.01 103. 14 1606

150.000 12. 176 .08213 16.7000 1020.078 3675.3 3855 .9 136.326 77.29 104. 95 1543

160.000 12.012 .08325 15.4666 941.6 82 4730.9 4914.1 143. 160 78.68 106.85 1483

170.000 11.848 . 08440 14.3467 369.760 5805.3 5991.5 149.696 8 0.16 108.82 1425

180.000 11.682 .08560 13.3250 803.3=4 6900.9 7089.2 155. 974 81.73 110.88 1369

190.000 11.516 .08684 12.3887 741. 8 20 8017.1 0208.2 162.026 83.37 113.01 1315

200.000 11.348 .08812 11.5273 684. 442 9155.4 9349.3 167. 878 85.07 115.22 1262

210.000 11.179 . 0 8945 10.7318 6 3 0. 7 39 1C 316.

7

10513.

5

173.555 86.83 117.52 1211

220.000 11.008 .09084 9.9945 580.286 11502.

0

11701.9 179. 076 08.64 119.89 1162

230.000 10.334 .09230 9.3089 532.725 12712.3 12915.3 184. 460 9 C.49 122. 36 1113

240.000 10.653 .09382 8.6691 487. 758 13948.4 14154.8 189. 721 92.37 124.92 1065

250.000 10.479 .09543 8.0701 445.136 15211.5 15421.4 194. 074 94.27 127.58 1018

260.000 10.295 .09713 7.5074 404.652 16502.5 16716.2 199.932 96.20 130.37 971

270.000 10.107 .09694 6.9772 366.136 17822.

8

18040.4 204. 906 98.14 133.28 924

280.000 9.914 .10087 6.4756 329.443 19173.6 19395.5 209.839 100.10 136.36 878

290.000 9.714 .10295 5.9994 294.460 20556.

4

20782.9 214. 650 102.05 139.62 832

300.000 9.506 .10520 5.5455 261.091 21973.

2

22204.6 219. 442 104.02 143.12 786

310.000 9.238 .10766 5.1109 229. 250 2342 6. 2 23663.

0

224. 195 105.96 146.92 739

320.000 9. 059 .11036 4.6926 198.864 24918.4 25161.3 223.925 107.94 151.12 692

330.000 3.815 .11344 4.2674 169.857 26454.

0

26703.5 233. 646 109.90 155.86 643

340.000 8. 553 .11692 3.8915 142. 148 28038.6 28295.8 238. 379 111.67 161. 39 593

350.000 8.265 .12099 3.5002 115.629 29681.2 29947.4 243. 150 113.85 168 . 14 542

360.000 7. 943 .12589 3. 1062 90.142 31396.3 31673.3 248.004 115.67 176.94 486

370.000 7.568 .13214 2.6969 65.413 33211.2 33501.9 253.014 1 18 .03 189.66 429

378.802 7.161 .13964 2. 3027 43.814 34942.

7

35249.9 257. 698 120.18 209.58 362

378.802 1.11585 .896 .141122 9.289 44470.

7

46442.3 287.245 120.09 165.32 157

380.000 1. 09833 .910 .137615 9. 768 44 65 8.3 46661.8 237.824 120.00 181.08 159

390.000 .98737 1.013 .117035 13. 103 46134.2 48362.3 292.242 120.63 162.45 174

400 .000 .91098 1.098 .103992 15. 786 47530 .

3

49945.

3

296. 251 122.15 155. 17 185

410.000 . 85247 1.173 . 094506 18. 1 C9 48897.2 51477.

9

300. 036 123.98 151.81 195

420.000 .30503 1.242 . 087132 20. 195 50254.

7

52987.4 303. 674 125.97 150.33 203

430 .000 .76532 1 .307 .031159 22. 1 08 51613.2 54437.9 307.205 128.04 149.91 211

440.000 .73113 1 .368 .0761 81 23.889 52978.

7

55907.7 310. 65 3 13 C.16 150.16 217

450.000 .70119 1.426 . 071943 25.565 54354. 6 57492.

1

314.035 132.31 150.64 223

460.000 .67460 1.482 . 063278 27.155 55 744 . 0 59005.2 317.360 134.46 151.82 229

470.000 . 65072 1 .537 .065066 28.673 57148.

1

60529.0 320. 637 1 36.62 153.01 235

480.000 . 62 90 8 1 .590 . 062220 30. 130 58568.6 62065.8 323.873 138.78 154.36 240

490.000 .60931 1 .641 . 059677 31 . 535 60005.

8

63616.4 327. 070 140.92 155.82 244

500.000 .59115 1.692 . 057385 32.894 61460.9 65132.4 330.234 143.05 157.37 249

520.000 .55376 1.790 . 053410 35.4=9 64424.6 68361.8 336.469 147.25 160.63 253

540.000 .53061 1.385 . 050068 37.979 67462.0 71608.2 342.595 151.36 164.02 266

560.000 .50578 1 .977 . 047208 40 . 358 70573.

1

74922.8 348. 622 155.38 167.47 273

580.000 .48364 2.063 . 044724 42.655 73757.

9

70306.7 354.559 159.29 170.92 280

600.000 .46370 2.157 . 042540 44. 384 77014.9 81759.3 360. 411 163.10 174.36 287

620.000 .44562 2.244 . 040601 47.056 80343.6 05280.5 366. 184 166.81 177.75 293

640.000 .42911 2.330 .038863 49. 180 83 741.

8

88068.7 371 . 880 170.41 181.08 299

660 .000 .41395 2.416 . 037294 • 51.262 07208.

3

92523.0 377. 502 173.90 184. 35 305

680.000 .39996 2.500 . 035867 53.3 C9 90741.7 96242.3 303. 054 177.30 187.56 3 1

1

700.000 . 33699 2.584 . 034563 55.324 94339.

7

100024.6 38 3.536 180.59 19 0.68 317

123
Table 22. Continued

I-BUTANE ISCBAR AT P = 24 BAR

T DEN VOL OP/OT DP/CO E H S CV CP M DEG K MOL/L L/MOL 3AR/K 8AR-L/M0L J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.569 12. 756 .07839 22.3295 1372.1 10 73. 3 261.4 108. 901 73. 31 98.90 1784

120.000 12.668 .07894 21. 3112 1309. 164 611.7 801.2 113.501 73.81 99.76 1744

130.000 12.505 .07997 19.6037 1203. 168 1615.

1

1807.1 121. 550 74.85 101.40 1674

140.000 12. 342 .08103 18.0817 1108.060 2634.9 2829.4 129. 128 76.01 103.13 1608

150.000 12.178 .06211 16.7155 1022.006 3672.0 3869.0 136. 304 77.29 104.94 1545

160.000 12.014 .08323 15.4818 943.574 4727. 3 4927.1 143. 137 78.68 106.84 1484

170.000 11.850 .08439 14.3616 871.623 5801.9 6004.4 149. 673 8 0.16 108.81 1426

180.000 11.685 .08558 13.3397 805.235 6896.6 7102.0 155.950 81.73 110.86 1370

190.000 11.519 .08682 12.4032 743.644 8012.4 3220.8 162.001 83.37 112.99 1316

200.000 11.351 .08810 11.5416 686.254 9150.

3

9361.7 167. 852 85.07 115.20 1264

210.000 11.182 .03943 10. 7460 632. 545 10311.

1

10525.7 173. 528 86.83 117.49 1213

220.000 11.011 . 09082 10.0087 582.090 11495.9 11713.

8

179. 048 88.64 119.86 1163

230.000 10.838 .09227 9.3230 534.530 12705.5 12926.9 184. 430 90.49 122.33 1114

240.000 10.662 ,09379 8.6833 489.569 13941.0 14166.1 189.690 92.37 124. 88 1067

250.000 10.483 .09539 8.0844 446. 956 15203.

3

15432.2 194. 841 94.27 127.54 1019

260.000 10. 300 .09708 7.5220 406.465 16493.5 16726.5 199.897 96.20 130.31 973

270.000 10.113 .09888 6.9919 367.986 17812.

9

18050.2 204.869 98.14 133.22 927

280.000 9.920 .10081 6.4906 331. 314 19162.5 19404.5 209. 769 100.10 136.28 880

290.000 9.721 .10287 6.0148 296. 357 20544.1 20791.0 214.607 102. 05 139.52 834

300.000 9.514 .10511 5.5615 263. 0 17 21959.

3

22211.6 219.395 104.02 143.00 788

310.000 9.297 .10756 5.1275 231.212 23410.5 23668.6 224. 144 105.98 146.76 742

320.000 9.069 .11026 4.7101 200.868 24900.4 25165.0 228.868 107.94 150.91 695

330.000 8.827 .11329 4.3060 171, 914 26433.0 26704.9 233.581 109.90 155.58 647

340.000 8.567 .11673 3.9116 144. 271 28013. 8 28293.9 238. 304 111.87 161.00 597

350.000 8.283 .12074 3.5224 117.844 29651.0 29940.8 243,063 113.85 167.57 546

360.000 7.965 .12555 3. 1316 92. 489 31358.3 31659.6 247. 896 115.87 176.04 491

370.000 7.598 .13162 2.7280 67.974 33160.

1

33476. 0 252.873 118.02 188.19 431

380.000 7.144 .13998 2.2875 43. 815 35111.1 35447.

1

258. 139 120.49 209.41 361

383.671 6.938 .14413 2.1057 34. 819 35897.9 36243.8 260.224 121.54 223.03 331

383.671 1.26152 .793 . 164544 8.0(3 44 69 6.

4

46600.9 287. 218 122.48 204.03 151

390.000 1.15666 .865 .143862 10.566 45726. 0 47800.9 290.322 122.11 179.20 163

400.000 1.04663 .955 .124028 13.727 47212.

0

49505.1 294.637 123.12 164. 04 177

410.000 .96863 1.032 .110821 16.344 48631.0 51108.7 298.598 124.72 157.55 188

420.000 .90812 1.101 .101030 18.639 50023.

8

52666.7 3 0 2. 35 3 126.56 154.45 197

430.000 .85876 1.164 . 093338 20. 712 51408.4 54203.1 305.968 128.54 153.07 205

440.000 .31715 1.224 . 08 7065 22. 621 52 794.0 55731.1 309. 481 130.59 152.67 213

450.000 . 78125 1.280 . 081814 24. 4 C4 54186.5 57258.5 312.914 132.68 152.90 219

460.000 .74974 1.334 .077329 26. 084 55589.4 58790.5 316. 281 134.80 153.56 226

470.000 . 72171 1.386 ,073440 27.681 57004.9 60330.3 319.593 136.92 154.50 231

480.000 .69649 1.436 .070024 29.2 08 58435.

2

61881.0 322. 858 139.04 155.65 237

490.000 .67362 1.485 .066994 30.674 59880.9 63443.7 326. 080 141.16 156. 96 242

500.000 .65270 1.532 .064281 32.089 61343.1 65020.1 329. 265 143.26 158.38 247

520.000 .61567 1.624 . 059612 34.789 64319.

7

68217.9 335.536 147.43 161.44 256

540.000 .58371 1.713 . 055723 37.349 67367.3 71478.9 341.689 151.51 164.69 264

560.000 .55569 1.800 .052417 39. 796 70486.

8

74805.8 347. 739 155.51 168.03 271

560.000 .53080 1.884 .049564 42.153 73678.7 78200.1 353. 694 159.41 171.40 279

600.000 .50849 1.967 . 04 7068 44. 434 76941.

7

81661.6 359. 562 163.20 174.77 286

620.000 .43831 2.048 .044861 46.652 80275.6 85190.5 365.347 166.89 178.11 292

640.000 .46993 2.128 . 042890 4 6. 817 83678.3 88785.4 371. 054 170.48 181.40 298

660.000 .45309 2.207 . 041117 50.937 87148.

7

92445.7 376.685 173.96 184.64 304

680.000 .43 758 2.285 . 039510 53. 0 17 90685.

6

96170.

4

382.245 177.35 187.81 310

700.000 .42323 2.363 .038044 55. 064 94286.7 99957.5 387. 734 180.64 190.91 316

124
Table 22. Continued

I-BUTANE ISCBAR AT P = 26 BAR

T DEN VOL DP/DT OP/CO E H S CV CP W DEG K MOL/L L/MOL 0AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.652 12. 756 .07839 22.3308 137 3. 256 79.2 283.0 108. 952 73.32 98.91 1785

120.000 12.669 .07893 21.3282 1311. 259 609. 3 614.6 113. 481 73.81 99.75 1746

130.000 12.506 .07996 19.6200 1205.196 1612.5 1820.3 121.529 74.85 101.39 1675

140.000 12. 343 .08101 18.0975 1110.032 2631.9 2642.6 129.106 76.01 103.12 1609

150.000 12.180 .08210 16.7310 1023.934 3668.

7

3882.2 136.282 77.29 104.93 154 6 160.000 12.017 . 0 8322 15.4969 945. 466 4723.

7

4940.1 143. 114 78.68 106.83 1486

170.000 11.852 .03437 14.3764 873.486 5797.9 6017.3 149. 649 8 C.16 108.80 1428

180.000 11.687 .08556 13.3543 807. 075 6892.2 7114.7 155. 926 81.73 110.85 1372

190.000 11.521 .08680 12.4176 745.468 8007.7 8233.3 161.975 83.37 112.97 1318

200.000 11.354 .08807 11.5559 688.066 9145.1 9374.1 167. 826 85.0 7 115.18 1266

210.000 11.185 .08940 10.7602 634. 350 10305.5 10537.9 173.501 86.83 117.47 1215

220.000 11.015 .09079 10. 0229 583.891 11489.

7

11725.7 179. 020 88.64 119. 64 1165

230.000 10.842 . 09223 9.3372 536. 334 12698.8 12938.6 184.401 90.49 122.29 1116

240.000 10.666 .09375 8.6975 491.378 13933.

6

14177.3 189.659 92.37 124. 64 1068

250.000 10.488 .09535 8.0987 448.774 15195.

2

15443.

1

194. 809 94.27 127.49 1021

260.000 10.305 .09704 7.5364 408. 3 16 16484.6 16736.9 199. 862 96.20 130.26 975

270.000 10.118 .09883 7. 0066 369.834 17803.

0

18059.9 204.832 98.14 133.15 929

280.000 9.926 .10075 6.5056 333.182 19151.6 19413.5 209. 729 100.10 136.20 883

290.000 9.727 .10280 6.0302 298. 249 20531.8 20799.1 214. 564 102. 06 139.42 837

300.000 9.521 . 1050 3 5.5773 264.938 21945.6 22218.6 219.348 104.02 142.87 791

310.000 9.306 .10746 5.1441 233.168 23394.9 23674.2 224. 093 105.98 146.61 744

320.000 9.079 .11014 4.7274 202.865 24882.5 25168.9 228.811 107.94 150.71 698

330.000 8.839 .11314 4.3244 173.962 26412.2 26706.4 233. 517 109.90 155.31 650

340.000 8.581 .11654 3.9315 146. 3 £4 27989.3 28292.3 238. 231 11 1.87 160.63 601

350.000 8.299 .12049 3.5443 120. 043 29621.4 29934.7 242. 976 113.85 167.03 550

360.000 7.966 .12521 3. 1567 94.813 31321.1 31646.7 247. 790 115.87 175.19 496

370.000 7.627 .13112 2.7582 70.493 33110.7 33451.6 252. 736 118.02 186.67 437

380.000 7.188 .13912 2.3283 46.6 «7 35037. 8 35399.5 2 5 7. 94 0 120.48 205.85 370

388.220 6. 706 . 14913 1.9131 26.828 36828.1 37215.8 262. 658 122.97 240.75 300

388.220 1.42371 .702 .191696 6.721 44868.2 46694.5 287. 073 124.91 229.64 145

390.000 1.37737 .726 .181928 7.6 24 45200.2 47087.9 288. 085 124.38 213.62 150

400.000 1.20527 .830 .148829 11.524 46843.6 49000 .

8

292. 930 124.29 177.21 168

410.000 1. 09837 .910 .129925 14.512 48336.5 50703.7 297. 136 125.54 165.08 181

420.000 1.02027 .980 .116801 17.048 49774.6 52323.0 331. 039 127.21 159.50 191

430.000 .95377 1.043 .106878 19.298 51190.6 53902.4 304. 756 129.07 156.76 200

440.000 .90815 1.101 . 098990 21. 346 52599. 9 55462.8 308. 344 131.04 155.53 208

450.000 . 86522 1.156 . 092508 23.2 42 54010.

8

5 7015.8 311.834 133.07 155.20 215

460.000 .82803 1.208 .087051 25.013 55428.

7

58568.

7

315.247 135.14 155.46 222

470.000 .79528 1.257 .082371 26.696 56857.0 60126.3 318. 597 137.22 156. 11 228

480.000 .76607 1.305 .078300 28.294 58297.6 61691.6 321 . 893 139.31 157.04 234

490.000 .73974 1.352 .074715 29. 8 23 59752.

8

63267.5 325. 142 141.40 158.16 239

500.000 .71582 1.397 .071526 31.294 61223.0 64855.2 328. 350 143.49 159.44 244

520.000 .67375 1.484 . 066085 34. 090 64212.9 68071.9 334.658 147.61 162.29 253

540.000 .63771 1.566 .061592 36.7 30 67271.1 71348.2 340.840 151.67 165.38 262

560.000 .60629 1.649 . 057801 39.246 70399.

3

74687.7 346. 913 155.64 168.61 270

580.000 .57853 1.729 . 054548 41.661 73598.5 78092.6 352.886 159.52 171.89 277

600.000 .55372 1.606 .051717 43.994 76867.

7

81563.2 358. 769 163.29 1 75.19 284

620.000 .53136 1.882 .049224 46.259 80206.9 85100.0 364.568 166.97 178.47 291

&40.000 .51105 1.957 .047007 48 . 465 83614.

2

88701.8 370 . 285 170.55 181.72 298

660.000 .49247 2.031 . 045018 50.621 87088.9 92368.4 375. 926 171.. 03 184.92 304

630.000 .47540 2.103 . 043220 52. 735 90629.

1

96098.1 381.494 177.40 188.06 310

700.000 .45963 2.176 .041584 54.812 94233.4 99890.1 386.98 9 180.69 19 1. 14 315

125
Table 22 Continued

I-BUTANE ISCBAR AT P = 28 BAR

T OEN VOL OP/OT OP/00 E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.734 12. 756 .07839 22. 3321 1374. 405 85.1 304.6 10 9. 004 73.33 93.91 1785

120.000 12.671 .07892 21.3451 1313. 354 606.9 627.9 113. 460 73.81 99.74 1747

130.000 12.508 .07995 19.6364 1207. 2 24 1609.

8

1833.6 121. 509 74,85 101.39 1677

140.000 12.345 .08100 18.1134 1112. 0 05 2629. 0 2855.3 129.085 76.01 103.11 1611

150.000 12.182 .08209 16.7464 1025.862 3665.4 3695.3 136. 260 77.29 104.92 1547

160.000 12.019 .08320 15.5120 947. 357 4720.1 4953.1 143. 092 78.68 106. 81 1487

170.000 11.855 .08436 14.3913 875.348 5794. 0 6030.2 149. 626 30.16 108.78 1429

180.000 11.690 .08554 13.3689 808.9 14 6887.9 7127.5 155.901 81.73 110.83 1373

190.000 11.524 .03678 12.4320 747.290 8003.0 8245.9 161.950 83.37 112.96 1319

200.000 11.357 .08805 11. 5702 689. 877 9139.

9

9386.5 167. 800 85.07 115.16 1267

210.000 11.188 .08938 10.7744 636. 153 10299.8 10550.1 173.474 86.83 117.44 1216

220.000 11.018 . 09076 10.0370 585.692 11483.

6

11737.7 178. 992 88.64 119.81 1167

230.000 10.846 .09220 9.3513 538. 136 12692.

0

12950.

2

184. 371 90.49 122.26 1118

240.000 10.670 .09372 8.7117 493.185 13926.

2

14188.6 189. 628 92.37 124.80 1070

250. 000 10.492 ,09531 3.1130 450. 5S0 15187.1 15454.0 194. 776 94.27 127.45 1023

260.000 10.310 .09699 7.5509 410.145 16475.

7

16747.3 199. 828 96.20 130.20 977

270.000 10.124 .09878 7.0212 371.679 17793.1 18069.7 204.795 98.14 133.09 931

280.000 9.932 .10068 6.5206 335, 047 19140.

7

19422.6 209.689 100.10 136.12 885

290.000 9.734 .10273 6.0455 300.1 38 20519.7 20807.3 214. 521 102. 06 139. 33 839

300.000 9.529 .10495 5.5932 266.856 21931.9 22225.7 219.302 104.02 142.75 793

310.000 9.314 .10736 5. 1605 2 35. 1 19 23379.

4

23680.0 224. 042 105.98 146.45 747

320.000 9.089 .11002 4.7447 204. 856 24864.6 25172.9 228. 755 107.94 150.51 701

330.000 8.850 .11299 4.3427 176.0 02 26391.

7

26708.1 233.454 109.90 155.05 653

340.000 8. 594 .11636 3. 9512 148.487 27965.1 28290.9 233. 153 111.87 160.27 604

350.000 8.316 .12025 3.5660 122.228 29592.3 29929.0 242, 891 113.85 166.51 554

360.000 8. 007 . 12489 3.1813 97.114 31284.8 31634.5 247.687 115.87 174. 38 501

370.000 7.655 .13064 2.7876 72.974 33063.

0

33428.8 252.604 116.02 185.26 443

380.000 7.230 .13831 2.3671 49. 497 34968.6 35355.9 257. 752 120.46 202. 76 378

390.000 6.654 . 15029 1.8728 25.9 04 37117.8 37538.7 263. 437 123.53 242.81 295

392.483 6.457 .15486 1.7220 19. 757 37744.

5

38178.1 265. 036 124.49 265.76 269

392.483 1.60784 .622 .223771 5.444 44973.3 46714.8 286. 786 127.48 267.13 140

400.000 1.39956 .715 . 1811 34 9, 1 15 46399.2 48399.9 291. 041 125.80 199. 31 157

410.000 1.24608 .803 .152759 12.598 48 005.

0

50252.1 295.617 126.49 175.40 173

420.000 1.14354 .874 .134885 15.421 49503.3 51951.9 299. 714 127.92 165.81 185

430.000 1.06644 .933 .122020 17.370 50958.2 53583.7 303.554 129.64 161.14 195

440.000 1.00476 .995 .112102 20.068 52395.

2

55181.9 30 7. 229 131.51 158.81 204

450 .000 . 95349 1 . 049 .104121 22. 0 83 53827.

3

56763.9 310.784 133.48 157.78 211

460.000 .9097? 1.099 . 097508 23.957 55262.0 58339.9 314. 248 135.49 157. 55 218

470.000 .87160 1.147 .091906 25.720 56704.

0

59916,5 317. 639 137.53 157.85 225

480.000 .83791 1.193 . 087079 27.390 58156.4 61498.1 320.969 139.59 158.52 231

490.000 .80777 1.238 .082864 28.983 59621.2 6 3037.5 324. 246 141.65 159. 44 236

500.000 .78054 1.281 .079141 30.5 10 61100.2 64687.4 327. 479 143.71 160.56 242

520.000 .73302 1.364 . 072839 33. 4 04 64104.

0

67923.9 333. 825 147.80 163.17 251

540.000 .69262 1.444 . 067682 36.124 67173.4 71216.1 340.038 15 1.82 166.10 260

560.000 .65761 1.521 . 063364 38.708 70310.

7

74568.5 346. 134 155.77 169. 20 268

580.000 .6268? 1.595 . 059679 41. 1 82 73517.4 77984.4 352.127 159.63 172.39 276

600.000 .59941 1.668 . 056489 43.566 76793.

3

81464.5 358. 026 163.39 175.62 283

620.000 .57478 1.740 . 053692 45.876 80137.6 35009.0 363.837 167.05 178.85 290

640.000 .55246 1.810 . 051213 48. 123 83549.

6

88617 .

6

369. 566 170.62 182. 05 297

660.000 . 53 210 1.379 . 048996 50.315 87028.

4

92290 .

5

375. 216 174.09 185. 21 30 3 680.000 .51343 1.948 . 046998 52.462 90572.

2

96025.7 380.792 177.46 186. 32 309

700.000 .49620 2.015 . 045185 54.569 94 180.

0

99822.6 386. 295 180.73 191.37 315

126
Table 22. Continued

I-BUTANE ISOBAR AT P = 30 BAR

T DEN VOL OP/OT DP/CO E H S CV CP W DEG K MOL/L L/MOL 9AR/K 8AR-L/M0L J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.617 12. 756 . 07839 22.3335 1375.557 90.9 326.1 109. 054 73. 34 98.92 1786

120.000 12. 672 . 07891 21.3621 1315.449 604.5 341.3 113. 440 73.81 99.74 1748

130.000 12.510 .07994 19.6528 1209.251 1607.1 1846.9 121.488 74.85 101.38 1678

140.000 12.347 .08099 18.1293 1113. 977 2626.0 2869.0 129.063 76.01 103.11 1612

150.000 12.184 .06207 16.7619 1027.789 3662.

2

3908.4 136.238 77.29 104.91 1549

160.000 12.021 .08319 15.5271 949. 2 48 4716.

5

4966.1 143. 069 78.68 106.80 1488

170.000 11.357 .08434 14.4061 877.2 JO 5790.1 6043.

1

149.603 80.16 108.77 1431

130.000 11. 692 .08553 13. 3835 810.753 6883.6 7140.2 155.877 81.73 110.82 1375

190.000 11.527 .08676 12.4464 749.1 12 7998.3 8258.5 161.925 83.37 112.94 1321

200.000 11. 360 .06803 11.5845 691.687 9134.

8

9398.9 167. 774 85.07 115.14 1269

210.000 11.192 .06935 10.7886 637.956 10294.2 10562.3 173. 447 86.63 117.42 1218

220.000 11.022 . 09073 10.0511 587. 492 11477. 4 11749.6 178. 963 88.64 119.78 1168

230.000 10.849 . 09217 9.3655 5 39.9 36 12685.

3

12961.9 184. 342 90.49 122.23 1120

240.000 10.674 .09368 8.7259 494.990 13918.9 14199.9 189.597 92.37 124. 77 1072

250.000 10.497 .09527 8.1273 452. 4C4 15179.1 15464.9 194. 743 94.27 127.40 1025

260.000 10.315 .09695 7.5653 411.972 16466.9 16757.7 199. 793 96.20 130.15 979

270.000 10.129 .09873 7.0359 373.521 17783.

4

18079.5 204. 758 98.14 133.02 933

260.000 9.933 .10062 6.5355 336.9 C9 19129.8 19431.7 209.650 100.10 1 36. 04 887

290.000 9.741 . 1 0266 6.0608 3 0 2. 0 24 20507.6 20815.6 214.479 102.06 139.23 841

300.000 9.536 .10486 5 .6089 268.769 21918.3 22232.9 219. 256 104.02 142. 63 796

310.000 9.323 .10726 5.1769 237. 064 23364.

0

23635.8 223. 992 105.98 146.30 750

320.000 9.099 . 10991 4.7618 206.841 24847.

3

25177.0 228.699 107.94 150.32 703

330.000 8.861 .11285 4. 3609 178. 0 34 26371.5 26710.0 233. 391 109.90 154.79 656

340.000 8.607 .11616 3.9707 150.579 27941.3 28289.8 238. 087 111.67 159.92 608

350.000 3.332 .12002 3.5874 124.398 29563.6 29923.7 242.807 113.85 166. 01 558

360.000 8.028 .12457 3.2054 99. 393 31249.

3

31623.0 247.586 115.67 173.62 506

370.000 7.662 .13018 2.8163 75. 420 33016.8 33407.4 252.475 118.01 183.95 449

360 .000 7. 269 .1 3757 2.4041 52. 226 34902.

9

35315.6 257. 574 120.45 200.04 386

390.000 6. 726 .14867 1.9316 29.254 37002.3 37448.3 263.129 123.48 233.42 308

396.466 6.184 .16170 1.5290 13. 561 38662.6 39147.7 267.403 126.13 304.85 237

396.466 1.823 .54862 .2627 4.176 45001.1 46646 .

9

286. 31 8 130.31 327.50 134

400.000 1.660 .60259 .2275 6. 359 45816.

4

47624.

2

288. 772 128.09 246.34 145

410.000 1.419 .70476 .1808 10.585 47622.9 49737.2 293.993 127.61 190.53 164

420.000 1.281 .78079 .1559 13.756 49204.8 51547.2 298. 356 126.70 173.93 178

430.000 1.183 .84522 .1391 16.4 27 50708.7 53244.4 302.350 130.24 166.41 190

440.000 1.108 .90273 .1266 18. 787 52178.

8

54887.

0

306. 127 132.01 162.59 199

450 .000 1.047 .95555 .1168 2 0. 9 28 53635.5 56502.1 309. 757 133.90 160.66 207

460.000 . 995 1. 00494 .1086 22.9 06 55089.

1

58103.9 313.277 135.85 159.85 215

470.000 .951 1.05168 .1021 24.754 56546.

0

59701.1 316.713 137.85 159.74 222

480.000 .912 1.09631 . 0964 26.498 58011.0 61299.9 320. 079 139.87 160.11 228

490.000 .878 1. 13923 . 0915 28. 156 59486.

5

6 29 0 4.

2

323. 387 141.91 160.80 234

500.000 . 847 1.18072 . 0871 29. 740 60974.6 64516.7 326. 645 143.94 161.74 239

520.000 . 794 1.26023 .0799 32. 731 63993.3 67773.9 333.032 147.98 164.09 249

540.000 .743 1.33610 . 0740 35.531 67074.3 71082.6 339. 276 151.98 166.84 259

560 .000 . 710 1.40918 . 0691 38.163 70 220.9 74448.5 345. 396 155. 90 169. 61 267

580.000 .676 1.48004 .0650 4 0. 7 15 73435.4 77675 .5 351.409 159.74 172.91 275

600.000 .646 1.54910 . 0614 43. 150 76717.8 81365 .1 357. 324 163.49 176.06 232

620.000 .619 1.61666 . 056 3 45.5 C5 80067.6 84917.7 363. 149 167.14 179.23 289

640.000 . 594 1.68303 .0555 47.791 83484.

7

88533.8 368. 889 170.69 182. 38 296

660.000 . 572 1.74834 . 0531 50. 0 20 86967.5 92212.5 374.549 174.15 185.50 302

680.000 .552 1.81276 . 0508 52. 199 90514.

9

95953.2 380.132 177.51 188.58 308

700.000 .533 1.8 7641 . 0468 5 4. 3 36 P4125.9 99755.1 385. 642 180.78 191.60 314

127
Table 22. Continued

I-BUTANE ISCBAR AT P = 32 BAR

T OEN VOL OP/OT OP/CD E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MCL J/MOL J/MOL J/MOL/< J/MOL/K J/MOL/K M/SEC

114.899 12. 756 .07839 22.3349 1376.713 96.8 347.6 109.105 73. 34 98.93 1767

120.000 12.674 .07890 21.3790 1317. 545 602.1 854.6 113.420 73.81 99.73 1750

130.000 12.511 .07993 19.6691 1211.279 1604.4 1860.2 121.467 74.85 101.37 1680

140.000 12.349 .03098 18.1451 1115.950 2623.

1

2882.2 129.042 76.01 103.10 1613

150.000 12.186 .08206 16.7773 1029.716 3658.9 3921.5 136. 216 77.29 104.90 1550

160.000 12.023 .08317 15.5422 951.139 4713.0 4979.1 143. 046 78.68 106.79 1490

170.000 11.859 .08432 14.4209 379. 071 5786.1 6056.0 149.579 80.16 108.76 1432

180.000 11.695 . 08551 13.3980 812.591 6879.4 7153.0 155.853 81.73 110.80 1376

190.000 11.529 .08674 12.4608 750. 933 7993.6 8271.1 161.900 83.37 112.92 1322

200.000 11.363 .08801 11.5987 693. 496 9129.7 9411.3 167. 748 85.07 115.12 1270

210.000 11.195 .08933 10.8028 639.757 10288.6 10574.5 173. 420 86.83 117.40 1219

220.000 11.025 .09070 10.0652 589. 290 11471.

3

11761.6 178.935 88.64 119.76 1170

230.000 10.853 .09214 9.3796 541.735 12678.

7

12973.5 184. 312 90.49 122.20 1121

240.000 10.679 .09365 8 . 74 0 0 496.794 13911.6 14211 .

3

189.566 92.37 124.73 1074

250.000 10.501 .09523 8.1415 454. 217 15171.0 15475.8 194. 711 94.27 127.36 1027

260.000 10.320 .09690 7.5796 413.796 16456.

0

16768.1 199. 759 96.20 130.10 981

270.000 10.134 . 09867 7.0504 375.361 17773.6 18089.4 204. 722 98.14 132.96 935

280.000 9.944 .10056 6.5503 338.771 19119.0 19440.8 209. 611 100.10 135.96 889

290.000 9. 747 .10259 6.0760 303. 905 20495.6 20823.9 214.437 102.06 139. 13 844

300.000 9.544 .10478 5.6246 270.678 21904.

3

22240.1 219. 210 104.02 142.51 798

310.000 9. 331 .10717 5. 1931 239. 0 05 23348.8 23691.7 223.942 105.98 146.15 753

320.000 9.106 .10979 4.7789 208.8 20 24829.9 25181.2 228.643 107.94 150.13 706

330.000 8.873 .11271 4.3789 180.059 26351.4 26712.1 233. 329 109.90 154.54 66 0 340.000 8.621 .11600 3.9901 152.661 27917.

8

28289.0 238.016 111.87 159.58 612

350.000 8.348 .11979 3.6086 126.555 29535.

5

29918.8 242. 725 113.85 165.53 562

360.000 8.048 .12426 3.2292 101.653 31214.6 31612.2 247.487 115.87 172.89 510

370.000 7.708 .12974 2.8442 77.832 32972.0 33387.2 252. 350 118.01 182.74 455

380.000 7.307 .13686 2.4397 54. 392 34840.

4

35278.3 257. 404 120.45 197.63 393

390.000 6.791 .14725 1.9650 32. 430 36698.2 37369.

4

262. 851 123.43 226.18 319

400.000 5.909 .16924 1.3535 8.917 39503.3 40044.9 269.618 127.75 363. 15 208

400.253 5.869 .17039 1.3293 8.2 38 39608.6 40153.8 269. 835 127.94 377.21 204

400.253 2.085 .47964 . 3118 2. 9 17 44925.

8

46460.6 285. 592 133.68 440.62 128

410.000 1.630 .61357 .2169 8. 438 47165.

9

49129.4 292. 189 129.02 215.07 155

420.000 1.436 .69640 .1807 12.049 48872.1 51100.5 296.941 129.57 184.75 171

430.000 1.311 . 76301 .1584 14.973 50439.1 52880.7 301 . 131 130.90 172.85 184

440.000 1.218 .82102 . 1426 17.5 08 51949.

4

54576.6 305.030 132.54 166.98 194

450.000 1.145 .37351 .1305 19.782 53434.

2

56229.5 308. 744 134.34 163.92 203

460.000 1.084 .92212 .1209 21.866 54909.0 57859.8 312.328 136.23 162.38 211

470.000 1.033 .96781 .1130 23. 8 02 56383.

0

59480.0 315. 813 138.18 161.79 218

480.000 .969 1.01122 .1063 25.621 57861.6 61097.5 319.218 140.16 161.81 225

490.000 .950 1.05273 .1005 27.344 59348.5 62717.4 322. 558 142.16 162.24 231

500.000 .915 1.09282 . 0956 28.986 60846.

0

64343.0 325.843 144.17 162.98 237

520.000 .855 1.16927 . 0872 32.073 63880.3 67621.9 332.273 148.17 165.04 247

540.000 .805 1.24193 . 0806 34.953 66973.4 70947.6 338.549 152.14 167. 60 25 7 560.000 . 76 2 1. 31170 . 0750 37. 672 70130.1 74327.5 344. 695 156.03 170.44 266

580.000 . 725 1.37920 . 0704 40.262 73352.5 77765.9 350. 727 159.85 173. 43 274

600.000 .692 1.44487 .0664 42.747 76641.6 81265.2 356.659 163.58 176.50 281

620.000 . 66 3 1.50903 .0629 45. 145 79997.2 84826.1 36 2. 49 7 167.22 179.61 288

640.000 .636 1.57194 . 0599 47.471 83419.

1

88449.3 368. 248 170.76 182. 71 295

660.000 .612 1.63330 .0572 49.735 86906.1 92134.3 373. 918 174.21 185. 80 302

630.000 .590 1.69476 . 0548 51. 947 90457.5 95880.8 379.510 177.57 188.84 308

700.000 .570 1.75495 .0526 54.112 94071.5 99687.4 385. 027 180.83 191.83 314

128
Table 22. Continued

I-BUTANE ISCBAR AT P = 34 BAR

T DEN VOL OP/OT OP/CD E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

114.980 12.757 .07839 22.3364 1377. 872 102. 6 369.1 109. 155 73.35 98.94 1788

120.000 12.675 .07889 21.3959 1319.640 599.7 868.0 113. 400 73.81 99. 73 1751

130.000 12.513 . 07992 19. 6854 1213.306 1601.8 1873.5 121. 446 74.85 101.36 1681

140.000 12. 351 .08097 18.1610 1117.922 2620.1 2895.4 129.021 76.01 103.09 1615

150.000 12.188 .08205 16.7928 1031. 643 3655.

7

3934.6 136.194 77.29 104. 89 1552

160.000 12.025 .08316 15. 5573 953.029 4709.4 4992.1 143.024 78.68 106.78 1491

170.000 11.361 .08431 14.4357 880.932 5782.2 6068.9 149. 556 8 C.16 106.75 1433

180.000 11.697 .08549 13.4126 8 14. 429 6875.1 7165.7 155.829 81.73 110.79 1378

190.000 11.532 .08672 12.4752 752.754 7988.

9

8283.7 161 . 875 83.37 112.91 1324

200.000 11.366 . 0 8798 11.6130 695. 304 9124.

6

9423.7 167. 722 85.07 115.10 1272

210.000 11.193 .08930 10.8169 641.558 10283.1 10586.7 173.393 86.83 117.38 1221

220.000 11.028 .09068 10.0793 591.087 11465.2 11773.5 178.907 88.64 119.73 1172

230.000 10.857 .09211 9.3936 543.533 12672.0 12985.2 184.283 90.49 122.17 1123

240.000 10.683 .09361 8.7541 498.596 13904. 3 1 4222.

6

189. 535 92.37 124.69 1076

250.000 10.505 .09519 8. 1557 456.027 15163.1 15436.7 194.678 94.27 127.31 1029

260.000 10.325 .09686 7.5940 415.618 16449.

3

16778.6 199. 724 96.20 130.04 983

270.000 10. 140 .09862 7.0650 377.198 17763.9 18099.3 204.685 98.14 132.89 937

280.000 9.950 .10050 6.5651 340. 627 19108.

3

19450.0 209.572 100.10 135.88 891

290.000 9. 754 .10252 6.0912 305. 784 20483.

6

20832.2 214. 395 102.06 139.04 846

300.000 9.551 .10470 5.6402 272.583 21891.5 22247.4 219.164 104. 02 142.40 801

310 .000 9.340 . 10707 5.2094 240.941 23333.7 23697.7 223. 892 105.98 146.01 755

320.000 9.113 .10967 4.7958 210.793 24812.7 25185.6 228.588 107.94 149.94 709

330.000 8.884 .11257 4.3968 182. 076 26331.6 26714.

3

233. 268 109.90 154.30 663

340.000 8.634 .11583 4.0092 154.733 27894.6 28288.4 237.946 111.87 159.25 615

350.000 3.364 . 1 1956 3.6295 128.698 29507.

8

29914.3 242. 644 113.85 165.07 566

360.000 8.067 .12396 3.2526 103.894 31180.6 3 1602.

1

247. 390 115.87 172.20 515

370.000 7. 733 .12932 2.8715 80.215 32928.5 33368.2 252. 229 118.01 181.61 460

380.000 7. 342 .13620 2.4739 57. 502 34780.6 35243.7 257. 241 120.44 195.46 400

390.000 6.850 .14598 2.0343 35.468 36803.1 3 72 99.4 262.596 123.40 220.38 330

400.000 6.090 . 16421 1.4712 13. 311 39235.6 39793.9 268.907 127.29 302.67 233

403.797 5.469 .18285 1.1132 3.844 40643.3 41265.

0

272. 499 130.02 565.23 169

403.797 2.433 .41101 . 3790 1.664 44685.

7

46083.1 284.431 138.37 727.26 122

410.000 1.907 .52448 .2668 6. 0 95 46582.

3

48365.5 290. 048 130.92 262.61 145

420.000 1.615 .61910 .2105 10.297 48494.3 50599.3 295.434 130.58 199.67 164

430.000 1.451 .68911 .1805 13.5 11 50145.9 52488.9 299. 882 131.61 180.86 178

440 .000 1.337 . 74816 . 1604 16. 234 51705.

2

54249.0 303. 928 133.09 172. 14 190

450.000 1.249 .80069 .1456 18.647 53222.9 55945.3 307. 741 134.79 167.60 199

460.000 1.178 . 84879 .1340 20 . 840 54721.7 57607.7 311. 395 136.61 165. 18 208

470.000 1.119 .89367 .1246 22.866 56214.2 59252.7 314. 933 138.51 164.01 215

480.000 1.068 .93606 . 11 68 24. 761 5770 7.

7

60890 .

3

318.381 140.45 163. 63 222

490.000 1.024 .97647 .1101 26.548 59206.8 62526.6 321. 756 142.42 163.77 229

500.000 . 985 1. 01527 .1044 28.248 60 714.

9

64166.8 325. 069 144.40 164.28 235

520.000 .918 1.08905 .0949 31.432 63765.6 67 468 .

4

331.544 148.36 166.03 246

540.000 . 863 1.15890 . 0874 34. 390 66871 .

4

70811 .

7

3 3 7. 85 2 152.29 168.38 255

560.000 . 816 1.22577 .0812 37. 175 70038.

2

74205.

3

344. 024 156.16 171.08 264

580.000 . 775 1.29031 .0760 39.822 73268. a 77655.9 350. 077 159.96 173.96 272

600.000 . 739 1.35298 .0716 42.357 76564.8 81164.9 356. 025 163.68 176.96 280

620.000 .707 1.41413 .0677 44.799 79926.

1

84734.2 361.877 167.30 160.00 287

640.000 . 678 1.47400 . 0644 47. 163 83353.1 88364 .

7

367. 640 170.83 183. 05 294

660.000 . 652 1.53282 . 0614 49.462 86844.4 92056.0 373.320 174.27 186.09 301

680.000 .629 1.59072 . 0587 51. 7 05 90399.6 95808.0 378.920 177.62 189. 10 307

700.000 .607 1.64785 .0563 53.899 94016.

9

99619.6 384.444 180.87 192.07 313

129
Table 22. Continued

I-BUTANE ISOBAR AT P = 35 BAR

T DEN VOL OP/DT DP/CO E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.021 12.757 .07839 22. 3371 1376.452 105,4 379. 8 109. 181 73.35 98.94 3788

120.000 12.676 .07889 21.4044 132 0.688 598.5 87,4. 7 113. 390 73.81 99.72 1752

130 .000 12. 514 .07991 19.6936 1214.320 1600.5 1880.1 121.436 74.85 101.36 1682

140.000 12. 351 .08096 18.1689 1118.908 2616.6 2902.0 129.010 76.01 103.06 1615

150.000 12.189 .08204 16. 8005 1 032. 607 3654.1 3941.2 136. 183 77.29 104.89 1552

160.000 12.026 .08315 15.5648 953.974 4707.6 4998.7 143.012 78.68 106.76 1492

170.000 11.863 .08430 14.4431 881.862 5780.3 6075.3 149. 544 80.16 106.74 1434

180.000 11.698 .08548 13.4199 315. 348 6672.9 7172.1 155.817 81.73 110.78 1378

190.000 11.533 .08671 12.4824 753.664 7986.6 8290.0 161.863 83.37 112.90 1325

200.000 11.367 .08797 11.6201 696. 2 C8 9122.

0

9430.0 167. 709 85.07 115.09 1272

210.000 11.199 .08929 10.8239 642.458 10280.3 10592.3 173. 379 86.83 117.36 1222

220.000 11.030 .09066 10.0863 591.985 11462.2 11779.5 178.893 68.64 119.72 1172

230.000 10.859 .09209 9.4007 544.431 12668.7 12991.0 184.268 9 0.49 122.15 1124

240.000 10.685 .09359 8. 7611 499.497 13900.

7

14228.3 189. 520 92.37 124.67 1076

250.000 10.508 .09517 8.1628 456.932 15159.1 15492.2 194.662 94.27 127.29 1030

260.000 10.327 .09633 7.6011 416.528 16444.9 16783.

8

199. 707 96.20 130.02 964

270.000 10.142 .09860 7.0722 376.1 15 17759.

1

13104.2 204.667 98.14 132.86 938

280.000 9.953 .10048 6.5725 341.553 19102.9 19454.6 209.552 100.10 135.85 893

290.000 9.757 .10249 6.0968 306. 7 22 20477. 7 20836.4 214. 374 102.06 139.00 847

300.000 9.555 .10466 5.6480 273.533 21884.

8

22251.1 219. 142 104.02 142.34 802

310.000 9. 344 .10702 5.2174 241.907 23326.

2

23700.8 223. 867 105.98 145.94 757

320.000 9.123 .10962 4.8043 211.777 24804.2 25187.3 228.561 107,94 149.85 711

330.000 8.889 .11250 4.4057 183. 082 26321.

8

26715.5 233. 237 109.90 154.18 664

340.000 8.640 .11574 4.0188 155,766 27883.1 28288.2 237.911 11 1.87 159.09 617

350.000 3.371 .11945 3.6398 129. 765 29494.

1

29912.2 242.603 113.85 164.84 568

360.000 8.077 .12332 3.2642 105.008 31163.9 31597.2 247.342 115.87 171.87 517

370.000 7. 745 .12911 2.8850 81 . 395 32907.

2

33359.1 252.170 118.01 181.07 463

380.000 7.359 .13588 2.4905 58.787 34751. 7 35227.3 257. 162 120.43 194.46 404

390.000 6.878 .14540 2.0577 36. 943 36758.3 37267.2 262.476 123.38 217.88 335

400,000 6.160 .16234 1.5184 15.272 39130.4 39698.6 268.628 127.16 286.30 243

405.487 5.197 .19241 ,9904 2.046 41247,4 41920.8 274. 067 131.29 651.10 151

405.487 2. 674 . 37395 .4260 1.032 44447.9 45756.7 283. 527 142.11 1139.47 119

410.000 2.091 .47832 .3012 4.8 08 46205.5 47879.6 288. 740 132.25 309.18 139

420.000 1.717 .58247 .2280 9.403 48283.8 50322.5 294.631 131.14 209.89 160

430.000 1.527 .65477 .1928 12.778 49989.1 52280.8 299. 241 131.98 185.64 175

440.000 1.399 . 71457 . 1701 15.601 51577. 0 54076.0 303. 373 133.38 175.07 187

450.000 1.303 .76724 .1537 18.085 53113.0 55798.

4

307. 240 135.02 169.62 197

460.000 1.227 .81518 . 1410 20.333 54625.2 57478.4 310.933 136.61 166.69 206

470.000 1.163 .85972 . 1308 22.404 56127.

7

59136.7 314.500 138.68 165.19 214

480.000 1.109 .90167 .1223 24. 337 57629.1 60784.9 317. 970 140.60 164.59 221

490.000 1.062 .94158 .1151 26.158 59134.

7

62430.2 321.363 142.55 164.57 227

500.000 1. 021 .97983 .1090 27.685 60648,

1

64077.5 324. 691 144.52 164.96 234

520.000 .95 0 1.05241 .0989 31.117 63707.5 67390.9 331. 189 148.46 166.54 245

540.000 .892 1.12097 . 0908 34.1 15 66820.

0

70743.4 337.515 152.37 168. 79 254

560.000 . 843 1.18652 .0843 36. 933 69991.9 74144.8 343.699 156.23 171.40 264

580.000 . 800 1.24971 .0788 39. 607 73226.6 77600.5 349. 763 160,02 174.23 272

600.000 . 763 1.31101 .0742 42.167 76526.

0

81114.6 355.719 163.72 177.19 280

620.000 .730 1.37077 . 0702 44,6 30 79890.6 34688.3 361.578 167.34 180.20 287

640,000 . 700 1.42926 . 0667 47.014 83320.

1

88322.5 367, 347 170.87 183. 22 294

660.000 .67 3 1.48668 .0635 49.330 86813.5 92016.9 373.031 174.30 186.24 3 01 680.000 . 64 8 1.54319 . 0606 51.588 90370.

6

95771.8 378.636 177.64 189.23 307

700.000 .625 1.59892 .0583 53. 796 93939.

7

99585.9 334.164 180.90 192.19 313

130
Table 22. Continued

I-BUT4NE ISOBAR AT P =36.54885 BAR

T OEN VOL OP/OT DP/CO E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.084 12.757 . 0 7839 22.3383 1379. 353 109.9 396.4 109. 219 73.36 98.94 1789

leo.ooo 12.677 .07888 21.4175 1322. 3 11 596.7 885.0 113. 374 73.81 99.72 1753

130.000 12.515 .07990 19.7062 1215.890 1598.4 1890.4 121.420 74.85 101.36 1683

140.000 12.353 . 08095 18.1811 1120.435 2616.4 2912.2 128.994 76.01 103.08 1616

150.000 12.190 .08203 16.8124 1 0 34. 0 99 3651.6 3951.4 136. 166 77.29 104. 83 1553

160 .000 12.028 . 08314 15.5765 955.437 4704.9 5008.7 142. 995 78.68 106.77 1493

170.000 11. 364 .08429 14,4545 883. 3 02 5777,3 6085.3 149. 526 8 C. 16 108.73 1435

180.000 11.700 .08547 13.4311 816.770 6869.6 7182.0 155.798 81.73 110.77 1380

190.000 11.535 .08669 12.4935 755.073 7983.

0

8299.8 161. 844 83.37 112.88 1326

200.000 11.369 .08796 11.6311 697. 6 07 9118.

1

9439.6 167. 689 85.07 115.08 1274

210.000 11.202 .08927 10.8349 643.851 10276. 0 10602.3 173. 359 86.83 117.35 1223

220.000 11.033 .09064 10.0972 593. 376 11457.5 11738.8 178.871 88.64 119.70 1174

230.000 10.361 .09207 9.4115 545.822 12663.6 13000.1 184.245 9 0.49 122.13 1125

240.000 10.688 .09357 8.7720 500. 891 13895.1 14237.0 189. 496 92.37 124.65 1078

250.000 10.511 .09514 8.1737 458.332 15152.9 15500.7 194. 637 94.27 127.26 1031

260.000 10. 331 .09680 7.6122 417.937 16438.1 16791.9 199.681 96.20 129.98 985

270.000 10.146 .09856 7.0834 379. 536 17751.7 18111.9 204.639 98.14 132.82 940

260.000 9.957 .10043 6.5840 342.987 19094.

7

19461 .7 209. 522 100.10 135.79 894

290.000 9. 762 . 10244 6.1105 308. 173 20468. 5 20842.

9

214.342 102.06 138.92 349

300.000 9.560 .10460 5.6601 275.004 21874.5 22256.8 219.107 104.02 142.25 804

310.000 9. 350 .10695 5.2299 243. 4 01 23314.6 23705.5 223.829 105.98 145.83 759

320.000 9.130 .10953 4.8173 213.298 24791.0 25191 .

3

228. 519 107.94 149. 71 713

330.000 8.898 .11239 4. 4194 184.637 26306.

6

26717.4 233. 190 109.90 154.00 667

340.000 3.650 .11561 4.0334 157.360 27865.5 28288.0 237. 858 11 1.87 158.85 620

350.000 8.383 .11929 3.6558 131. 4 12 29473.2 29909.1 242.542 113.85 164.50 571

360.000 8.091 .12359 3.2820 106.724 31138.3 31590.0 247.269 115.87 171.37 521

370.000 7. 764 .12880 2.9055 83.210 32874.

8

33345.6 252.079 118.01 180.28 467

380.000 7.385 .13540 2.5157 60. 755 3470 8.

1

35202.9 257. 042 120.43 193.01 409

390.000 6.918 .14454 2.0924 39. 177 36692.2 37220.5 262. 299 123.37 214.42 342

400.000 6.25 3 .15993 1.5826 18. 1 16 38989.4 39574.0 268. 254 127.02 268.47 256

410.000 2.52? .39644 .3841 2.528 45358.0 46606.9 285. 957 135.61 511.51 128

420.000 1.895 .52764 .2594 7.993 47920.

4

49848.

8

293. 299 132.11 230.54 154

430.000 1.654 .60452 .2139 11.641 49730.2 51939.6 298. 221 132.60 194.34 171

440.000 1.502 . 66579 . 1863 14. 626 51369.4 53802.8 302.505 133.84 180.12 184

450.000 1.391 .71884 .1670 17.223 5293 7.6 55564.8 306.465 135.40 173.03 194

460.000 1.304 .76664 .1523 19.558 54471.

7

57273.

7

310. 222 137.12 169. 19 203

470,000 1.233 .31076 . 1407 21. 700 55991.0 58954.2 313.836 138.95 167.12 211

480.000 1.174 .35211 . 1311 23.691 57505.3 60619.7 317. 343 14 (.83 166.14 219

490.000 1.122 .89131 .1231 25.562 59021.4 62279.0 320. 764 142.76 165.85 226

500.000 1.077 .92877 .1163 27.334 60543.5 63936 .

1

324. 116 144.70 166. 04 232

520.000 1.000 . 99963 .1051 30.6 39 63616.

6

67270.1 330. 651 148.60 167. 35 243

540.000 . 933 1.06637 .0964 33.697 66739.5 70637.

0

337. 004 152.49 169.42 253

560.000 .885 1.13001 .0893 36.565 69919.

6

74049.7 343. 209 156.33 171.92 263

580.000 .839 1.19125 . 0833 39.283 73161.1 77515.0 349. 289 160.10 174.66 271

600.000 . 800 1.25058 , 0783 41. 879 76466.

1

81036.8 355.259 163.80 177.54 279

620.000 . 764 1.30835 . 0740 44.375 79835.0 84616.9 361.129 167.40 180.50 286

640.000 . 733 1.36484 . 0702 46. 7 88 83268.

4

88256.8 366.906 170.92 183.49 29 3 660.000 .704 1.42025 .0669 49. 130 86765.

3

91956.2 372.598 174.35 186.47 300

680.000 .678 1.47475 .0639 51. 4 12 90325.4 95715.4 378. 209 1 77.69 189.44 3 07

700.000 . 654 1.52846 . 0613 53. 642 93947.

0

99533.4 383. 74 3 180.93 192.37 313

131
Table 22. Continued

I-BUTANE ISOBAR AT P = 36 BAR

T DEN VOL DP/OT OP/ CO E H S CV CP M DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.143 12.757 .07839 22.3395 1380.199 114.1 412.0 109. 255 73.37 98.95 1789

120.000 12.678 .07886 21.4297 1323.831 595.0 894.7 113.360 73.81 99.71 1754

130.000 12.516 . 07990 19.7181 1217. 361 1596.5 1900.1 121 . 405 74.85 101.35 1684

140.000 12.354 .08094 18.1926 1121.866 2614.

2

2921.3 128.978 76.01 103.07 1617

150.000 12.192 .08202 16. 8236 1035.496 3649.2 3960.9 136. 150 77.29 104.88 1554

160.000 12.029 . 08313 15.5874 956.8 08 4702. 3 5018.2 142.979 78.68 106.76 1494

170.000 11.866 .08427 14.4652 884.652 5774.4 6094.

7

149. 509 80.16 108.72 1436

160.000 11.702 .08545 13.4417 818. 102 6866.6 7191.

3

155. 781 81.73 110.76 1381

190.000 11.537 .06668 12.5039 756.393 7979.6 8309.

0

161.326 83.37 112.87 1327

200.000 11.371 .08794 11.6414 698.918 9114.4 9448.6 167. 671 85.07 115.06 1275

210.000 11.204 .08925 10.8451 645.156 10272.

0

10611.1 173.339 86.83 117.33 1224

220.000 11.035 .09062 10.1074 594. 678 11453.

1

11797.5 178.851 88.64 119.68 1175

230.000 10.864 .09205 9.4217 547.124 12658.8 13008.6 184.224 90.49 122.10 1127

240.000 10.691 .09354 8.7822 502. 196 13889.

8

14245.3 139.474 92.37 124.62 1079

250.000 10.514 . 09511 8.1840 459.642 15147.2 15508.6 194. 613 94.27 127.23 1033

260.000 10.334 .09677 7.6225 419.256 16431.8 16799.5 199.656 96.20 129.94 987

270.000 10. 150 .09852 7.0939 380. 865 17744.

7

18119.1 204. 613 98.14 132.77 941

260.000 9.961 .10039 6.5946 344. 330 19087.

0

19468.5 209. 494 100.10 135.74 896

290.000 9.767 .10239 6.1214 3 09.530 20459.9 20849.0 214. 311 102.06 138.86 851

300.000 9.566 .10454 5.6713 276.360 21865.0 22262.2 219.074 104.02 142.17 806

310.000 9.356 .10688 5.2415 244. 799 23303.

8

23710.

0

223. 793 105.98 145.73 760

320.000 9. 137 .10945 4.8294 214.721 24778.8 25194.7 228.480 107.94 149.58 715

330.000 8.905 .11229 4. 4322 186. 089 26292.6 26719.3 233. 147 109.90 153.83 669

340.000 8.659 .11548 4.0471 158.850 27849.1 28287.9 237.309 111.87 158.62 622

350.000 8.394 .11913 3.6706 132.948 29453.

7

29906.4 242. 485 113.85 164.19 574

360.000 8.105 .12339 3.2984 108. 3 22 31114.

7

31583.

5

247. 201 115.87 170.91 524

370.000 7.781 .12851 2.9244 64. 896 32845.

1

33333.4 251.996 118.01 179.56 471

360.000 7.409 .13497 2.5388 62.575 34668.4 35181.3 256. 934 12C.43 191.73 414

390.000 6.955 .14379 2.1235 41.221 36633.3 37179.7 262. 140 123.35 211.56 348

400.000 6.328 .15803 1.6357 20.620 38874.5 39475.1 267. 949 126.93 256.55 267

410.000 4.297 . 23275 .7248 .530 42466.

0

43350.4 277.403 143.27 2344.08 122

420.000 2.094 .47755 .2954 6.643 47525.1 49339.7 291.913 133.16 258.95 149

430.000 1.785 .56025 .2361 10.578 49467.7 51596.7 297. 226 133.22 204.33 167

440.000 1.604 .62329 . 2028 13. 7 21 51164.

5

53532.9 301. 679 134.29 185.54 180

450.000 1.477 .67686 . 1803 16.427 52766.

4

55338.5 305.737 135.75 176.55 191

460.000 1.380 .72465 .1636 18.844 54323.

6

57077.3 309. 559 137.42 171.71 201

470.000 1. 301 .76846 .1505 21.052 55859.4 58779.5 313. 221 139.20 169.05 209

480.000 1.236 .80933 .1398 23.098 57386.8 6 0462.3 316.763 141.05 167.67 217

490.000 1.179 .84794 .1310 25.016 58913.

3

62135.4 320. 214 142.95 167.10 224

500. OOQ 1.130 .88474 .1234 26.828 60 444.

0

63806.0 323.539 144.87 167.09 230

520.000 1.048 .95413 .1112 30. 202 63530.6 67156.3 330. 159 148.74 168. 13 242

540.000 .981 1.01929 .1017 33. 315 66663.4 70536.7 336.538 152.61 170.03 252

560.000 .925 1.08129 .0940 36. 229 69851.

3

73960.2 342. 763 156.43 172.40 262

580.000 .877 1.14085 . 0877 38. 987 73099.

1

77434.4 348. 859 160.18 175.06 270

600.000 .834 1.19848 . 0323 41.617 76409. 3 80963.6 354. 841 163.87 177.88 278

620.000 . 797 1.25454 .0776 44. 144 79782.9 84550.2 360.721 167.46 180.79 286

640.000 . 764 1.30930 .0736 46.584 83219.

8

83195.1 366. 507 170.97 183.74 293

660.000 . 734 1.36297 . 0701 48.950 86720.2 91899.5 372. 206 174. 39 186.69 300

680 .000 .706 1.41572 . 0669 51.254 90282.3 95662.6 377. 823 177.72 189.63 306

700.000 . 681 1.46769 . 0641 53.503 93907.2 99484.4 383. 362 180.97 192.54 312

132
Table 22. Continued

I-BUTANE ISOBAR AT P = 40 BAR

T OEN VOL OP/DT DP/CO E H S CV CP H DEG K MOL/L L/MOL BAR/K BAR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.223 12.757 .07839 22.3411 1381. 368 119. 8 433.3 109. 305 73.37 98.96 1790

120.000 12.660 .07887 21.4466 1325.927 592.6 908. 0 113. 339 73.81 99.71 1755

130.000 12.518 .07989 19.7344 1219.3 {9 1593.8 1913.4 121. 384 74.85 101.34 1685

140.000 12.356 . 08093 16.2084 1123.8 37 2611.

3

2935.0 126.957 76.01 103.06 1619

150.000 12.194 .06201 16.6390 1037.422 3646.

0

3974.

0

136. 129 77.29 104.87 1556

160.000 12.031 .08312 15.6025 958.697 4698.

7

5031.

2

142. 956 78.68 106.75 1495

170.000 11.868 .08426 14.4600 686.5 11 5770.6 6107.6 149.486 8 C.16 108.71 1438

180.000 11.705 .08544 13.4562 819.938 6862.3 7204.1 155. 757 81.73 110.74 1382

190.000 11.540 .06666 12.5182 758. 211 7975.0 8321.6 161.801 83.37 112.86 1328

200.000 11.374 .08792 11.6555 700.723 9109.

4

9461.0 167. 645 05. 07 115.04 1276

210.000 11.207 .08923 10.8592 646.953 10266. 5 10623.

4

173. 312 86.83 117.31, 1226

220.000 11.038 .09059 10.1214 596. 471 11447. 1 11809.5 178. 823 88.64 119.65 1176

230.000 10.668 . 09202 9.4357 548.9 18 12652.2 13020.3 184. 195 9 C.49 122.07 1128

240.000 10.695 .09351 8.7963 503.993 13882.6 14256.7 189.443 92.37 124.58 1081

250.000 10.518 .09507 8.1981 461 . 447 15139.

3

15519.6 194.581 94.27 127.19 1034

260.000 10.339 .09672 7.6368 421.071 16423.1 16810.0 199.622 96.2 0 129.89 980

270.000 10. 156 . 09847 7.1084 382.694 17735.2 18129.0 204.577 98.14 132.71 943

260.000 9.967 .10033 6.6093 346.1 77 19076.4 19477.8 209.456 100.10 135.66 898

290.000 9. 773 .10232 6.1364 311. 399 20448.2 20857.5 214. 270 102.06 138, 77 853

300.000 9.573 . 10446 5.6867 278. 273 21851.

9

22269.7 219.030 104.02 142.06 808

310.000 9.364 .10679 5.2575 246.720 23289.

1

23716.

3

223. 745 105.98 145.59 763

320.000 9.146 .10934 4.8461 216.676 24762.0 25199.4 228.426 107.94 149.41 718

330.000 8.916 .11216 4.4498 188.085 26273.4 26722.0 233.087 109.90 153.61 672

340.000 8.672 .11532 4.0658 160. 895 27826.

8

28286.0 237. 741 111.87 158.32 625

350.000 8.409 .11892 3.6908 135.055 29427.

3

29903.0 242.407 113.85 163.78 578

360.000 8.123 .12311 3. 3208 110. 5 11 31082.7 31575.1 247.109 115.87 170.31 528

370.000 7.805 .12813 2.9501 87.199 32805.

3

3 3317.5 251.883 118.00 178.63 476

380.000 7.440 .13441 2.5697 65. 047 34615.

4

35153.0 256. 788 120.42 190. 11 420

390.000 7.002 .14283 2. 1643 43.968 36556.4 37127.7 261. 934 123.33 208.09 357

400.000 6.416 .15582 1.7010 23. 881 38 735.3 39358.6 267.580 126. 84 244.51 281

410.000 5.305 . 18851 1.0552 5. 0 CO 41076.8 41830.8 273. 603 138.44 462.85 169

420.000 2.448 .40844 .3612 4.749 46847.4 48481.1 289. 657 134.91 327.34 140

430.000 1.988 .50293 .2717 9. 1 24 49067.

5

51079.

2

295. 775 134.14 222.11 161

440.000 1.757 .56911 .2262 12.493 50863.2 53139.6 300.514 134.94 194.33 175

450.000 1.603 . 62370 . 2003 15. 351 52519.2 55014.0 304.727 136.26 182.00 187

460.000 1.489 .67162 .1602 17.881 54111.8 56798.3 30 8. 649 137.84 175.51 197

470.000 1.398 .71513 . 1648 20.179 55673.0 58533.5 312. 381 1 39.55 171.89 206

480.000 1. 324 .75545 . 1524 22. 300 57219.5 60241.3 315. 977 141.36 169.90 214

490.000 1.260 .79335 . 1422 24.281 58761.

1

61934.5 319.469 143.22 168.92 221

500.000 1.206 .82933 .1337 26. 149 60304.

2

63621.6 322. 877 145.1

1

168 .60 228

520.000 1.115 .89690 .1199 29.6 15 63410.1 66997.7 329. 498 148.94 169.24 240

540.000 1.042 .96008 .1093 32.8 C4 66557.

4

70397.7 335. 914 152.76 170.88 251

560.000 .980 1.02002 .1007 35. 7 ei 69756.4 73836.5 342. 167 156.56 173.09 260

580.000 . 928 1.07747 . 0937 38.5«2 73013.2 77323.1 348. 284 160.30 175.62 269

600.000 .883 1.13295 . 0878 41.269 76330.7 60662.6 354. 284 163 .96 178.35 277

620.000 .843 1 . 1 8684 . 0828 43.837 79710.

5

84457.8 360.178 167.54 181.19 285

640.000 . 807 1. 23942 . 0784 46.313 83152.6 88110.3 365.976 171.04 184.09 292

660.000 . 775 1.29091 . 0745 48. 7 12 86657.5 91821.1 371. 685 174.45 187.00 299

680.000 .745 1.34146 .0711 51. 045 90224.3 95590.2 377. 311 177.78 189.90 306

700.000 .719 1.39123 .0681 53. 322 93851.9 99416.8 382. 857 101.01 192.78 312

133
Table 22. Continued

I-BUTftNE ISOBAR AT P = 42 BAR

T DEN VOL OP/DT DP/DO E H S CV CP W OEG K (10L/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.304 12.757 .07839 22.3428 1382.539 125.5 454. 7 109.354 73.38 98.96 1791

120.000 12.681 .07886 21.4635 1328.023 590.2 921.4 113.319 73.81 99.70 1756

130.000 12.520 .07988 19.7508 1221. 431 1591.

2

1926.6 121.363 74.85 101,34 1686

140.000 12.358 .08092 18.2242 1125.8 09 2608,

4

2948.

3

128.936 76.01 103.06 1620

150.000 12.196 .08200 16.8544 1039. 348 3642.8 3987.1 136.107 77.29 104.86 1557

160.000 12. 033 .08310 15.6175 960.586 4695.2 5044.2 142. 934 78.68 106.74 1497

170.000 11.871 .06424 14.4947 888.370 5766.7 6120.5 149.463 80.16 108.70 1439

180.000 11.707 .08542 13.4707 821.774 6858.

1

7216.8 155. 733 81.73 110.73 1384

190.000 11.543 .08664 12.5325 760.029 7970.

3

8334.2 161.776 33.37 112.84 1330

200.000 11.377 .08790 11.6697 702.528 9104.

3

9473.5 167.619 85.07 115.02 1278

210.000 11.210 .08920 10.8732 648.750 10260.9 10635.6 173.286 86.83 117.29 1227

220.000 11.042 .09056 10,1354 598.264 11441.1 11821.5 17 8. 795 88.64 119.62 1178

230.000 10.871 .09199 9.4497 550.710 12645.6 13032.0 184. 166 90.49 122.04 1130

240.000 10.698 .09347 8.8103 505.789 13875.5 14268.0 189. 413 92.37 124.55 1083

250.000 10.523 . 09503 8.2122 463. 250 15131.4 15530.6 194.549 94.27 127.14 1036

260.000 10.344 .09668 7.6510 422.885 16414.5 16820.6 199.588 96.20 129.84 990

270.000 10.161 .09842 7.1227 384.522 17725.

7

18139.0 204. 541 98.14 132. 65 945

280.000 9.973 .10027 6.6239 3 4 8. 0 21 19065.9 19487.1 209. 417 10 C.IO 135.59 900

290.000 9. 780 .10225 6. 1514 313.264 20436.

5

20866.0 214. 229 102.06 138.68 855

300.000 9.580 .10439 5.7021 280.162 21838.3 22277.3 218.985 104.02 141.96 811

310.000 9.372 .10670 5.2734 248. 637 23274.5 23722.6 223.696 105.98 145.45 766

320.000 9,155 . 10923 4.8627 216.6 26 24745.4 25204.2 228.373 107.94 149.24 721

330.000 8. 92 7 .11202 4.4672 190. 074 26254.4 26724.9 233.028 109.90 153.39 675

340.000 8.684 .11515 4,0843 162. 931 27804.

7

28288.3 237.674 111.87 158.03 629

350.000 8.424 .11871 3.7109 137.150 29401.

3

29899.9 242. 330 113.85 163.37 581

360.000 8.141 .12284 3,3429 112.683 31051 .

3

31567.

2

247. 019 115.87 169.74 532

370.000 7.827 .12776 2.9752 89.478 32765.9 33302.5 251.774 118.00 177.75 481

330.000 7. 470 .13386 2.5997 67.481 34564.3 35126.5 256. 648 120.42 188.62 426

390.000 7.046 . 14193 2.2032 46 . 644 36483.9 37080.0 261. 738 123.32 205.07 365

400.000 6.496 .15393 1.7597 26.973 38612.

4

39258.9 267. 253 126.77 235.57 293

410.000 5.599 .17860 1.1978 8. 872 40660.9 41411.0 272.490 137.64 349.10 196

420.000 2.981 .33546 ,4616 2.957 45696. 2 47305.1 286. 679 137.04 477.66 133

430.000 2.227 .44906 .3146 7.698 48611.6 50497.7 294. 202 135.15 246 .64 155

440.000 1.925 .51936 .2570 11.295 50537.

4

52718.7 299. 310 135.62 205,00 171

450.000 1.738 .57527 . 2223 14. 304 52258. 3 54674,4 303. 706 136.78 188.24 184

460.000 1.604 .62351 .1982 16.946 53890.9 56509.6 307. 740 138.26 179.72 194

470.000 1.500 .66684 .1801 19, 333 55480.2 58280.9 311.550 139.91 174.97 203

480.000 1.415 .70671 .1658 21.527 57047.5 60015.7 315. 202 141.67 172.28 212

490.000 1.344 .74400 .1541 23.571 58605.6 61730.4 318. 738 143. 49 170.83 219

500.000 1.283 . 77927 . 1444 25.493 60161.9 63434.9 322. 182 145.35 170.19 226

520.000 1.183 . 84521 .1289 29.050 63288.

0

66837.8 328. 855 149.13 170.39 238

540.000 1.103 .90661 .1171 32. 3 11 66449.9 70257.6 335. 309 152.92 171.76 249

560.000 1.037 .96468 .1077 35.350 69660.6 73712.3 341.591 156.69 173.79 259

580.000 .980 1. 02022 .1000 38. 2 13 72926.6 77211.5 347. 730 160.41 176.20 266

600.000 .931 1.07376 .0935 40. 936 76251.6 80761.4 353. 747 164. 05 178.83 277

620.000 .888 1.12566 . 0880 43.544 79637.6 84365.5 359.656 167.62 181.60 264

640.000 .850 1.17629 . 0832 46.056 83085.1 88025.5 365.466 171.11 184.44 292

660.000 .816 1.22579 . 0791 48. 487 86594.6 91742.9 371. 186 174.51 187.30 299

680.000 . 785 1. 27435 . 0754 50.849 90165.

3

95517.6 376. 820 177.83 190.17 305

700.000 . 756 1.32213 . 0721 53.151 93796.4 99349.4 382. 373 181.06 193.02 312

134
Table 22. Continued

I-8UTANE ISOBAR AT P = 44 BAR

T OEN VOL OP/OT OP/CO E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.384 12.757 . 0 7839 22. 3445 1383. 714 131.1 476.0 109. 403 73.39 98.97 1791

120.000 12.683 .07885 21.4804 1330.1 18 587.8 934.8 113.299 73.81 99.69 1758

130.000 12. 521 .07986 19.7670 1223. 458 1588.5 1939.9 121. 343 74.85 101.33 1688

140.000 12. 360 .08091 18.2400 1127.780 2605.5 2961.5 128.915 76.01 103.05 1621

150.000 12.198 .08198 16.8697 1041.274 363 9.5 4000.3 1 36. 085 77.29 104. 85 1558

160.000 12.035 .08309 15.6325 962.474 4691.7 5057.3 142. 911 78.68 106.73 1498

170.000 11.873 .08423 14.5095 890. 228 5762.8 6133.4 149.440 8 0. 16 108.68 1441

180.000 11.709 .08540 13.4852 823.6 C8 6853.

8

7229.6 155.709 81.73 110.72 1385

190.000 11.545 .08662 12.5468 761.845 7965.7 8346.8 161. 751 83.37 112.82 1331

200.000 11. 380 .08787 11.6839 704, 3 32 9099.

3

9485.9 167. 594 85.07 115.01 1279

210.000 11.213 .08918 10.8873 650.545 10255.5 1 0647.8 173. 259 86.83 117.26 1229

220.000 11.045 . 09054 10. 1494 600. 055 11435.1 11833.5 178. 768 88.64 119.60 1180

230.000 10.875 .09195 9.4636 552.501 12639.1 13043.7 184. 137 9 0.49 122.01 1132

240.000 10.702 .09344 8.8242 507.584 13868.

3

14279.4 189. 382 92.37 124.51 1084

250.000 10.527 .09499 8.2262 465. 051 15123.6 15541.6 194.517 94.27 12 7.10 1038

260.000 10.348 . 09663 7.6651 424.696 16405.9 168 31 .

1

199.554 96.20 129.79 992

270.000 10.166 .09837 7.1371 386. 347 17716.2 18149.0 204.505 98.14 132.59 947

280.000 9.979 .10021 6.6385 349.863 19055.5 19496.4 209.379 100.10 135.52 902

290.000 9. 786 .10219 6.1663 315. 1 25 20425. 0 20874.6 214. 188 102. 06 138.59 858

300.000 9.587 .10431 5.7174 282.047 21 825.9 22284.9 21 8. 941 104.02 141.85 813

310.000 9.380 . 1 0661 5.2893 250.550 23259.9 23729.0 223. 648 105.98 145.32 763

320.000 9.164 .10912 4.8792 220.571 24729.

0

25209.1 228.320 107.94 149.07 723

330.000 8.937 .11189 4. 4845 192. 056 26235.5 26727.9 232.969 109.91 153.17 678

340.000 8.696 .11499 4. 1027 164.959 27782.9 28238.9 237. 608 111.87 157.75 632

350.000 8.438 .11851 3. 7307 139.235 29375.

7

29897.1 242. 254 113.85 162.99 585

360.000 3.158 .12257 3.3647 114.841 31020.5 31559.8 246.930 115.87 169.19 53 7 370.000 7.849 .12740 2.9999 91.735 32727. 7 33288.3 251.666 118.00 176.91 486

380.000 7.499 .13334 2.6290 69. 880 34514.9 35101.6 256. 512 120.41 187.24 432

390.000 7.087 .14110 2.2403 49. 257 36415.

1

37035.9 261. 55 3 123.30 202.42 372

400.000 6.567 .15228 1.8132 29.931 38501.7 39171.7 266. 959 126.71 228.60 304

410.000 5.789 .17275 1.3014 12.366 40386.6 41146.7 271.760 137.26 304.84 217

420 .000 3. 794 .26359 .6202 2. 36 2 44595.

3

45755.1 282. 846 138.44 613.56 134

430.000 2.513 .39794 .3675 6.340 48084.2 49835.1 292.463 136.22 281.24 150

440.000 2. 112 .47341 . 2898 10. 139 50183.

4

52266.5 298. 056 136.33 218.03 167

450.000 1.883 .53097 .2467 13.292 51982.1 54318.3 302.668 137.32 195.39 180

460.000 1. 725 .57967 .2177 16. 0 43 53660.

7

56211.2 306. 830 138.69 184.37 191

470.000 1.605 . 62293 . 1965 18. 5 16 55280.

7

58021 .

6

310. 724 140.27 178.31 201

430.000 1.510 .66244 . 1800 20. 781 56870.

8

59785.6 314.438 141.98 174.82 209

490.000 1.430 .69920 .1667 22.886 58446.

5

61522.9 318.020 143.76 172.85 217

500.000 1.363 .73383 .1557 24.861 60 016. 7 63245.6 321. 501 145.59 171.84 224

520.000 1.253 .79831 .1383 28. 505 63163.9 66676.5 328.229 149.32 171.57 237

540.000 1.165 . 85810 . 1252 31 .8 38 66341.4 70117.0 334. 722 153.08 172.66 248

560.000 1.094 .91448 .1148 34.9 36 69564.

0

73587.7 341. 032 156.82 174.50 258

580.000 1.033 .96827 .1064 37.851 72839.

3

77099.7 347. 194 160.52 176.78 267

600.000 .980 1.02003 . 0993 40.6 18 76172.

0

80660.2 353. 230 164.15 179. 32 276

620.000 .934 1.07017 . 0934 43.265 79564.4 84273.2 359. 153 167.70 182.01 284

640.000 .894 1.11897 . 0882 45.811 83017.5 87941.0 364.975 171.18 184.79 291

660.000 .857 1.16667 . 0837 48.273 86531.4 91664.7 370. 705 174.57 187.61 298

680.000 . 824 1.21342 . 0797 50.664 90106.

2

95445.2 376. 34 7 177.88 190 . 44 305

700.000 . 794 1.25938 . 0762 52.992 93741.0 99282.3 381.909 181.10 193.26 311

135
Table 22 Continued

I-BUTANE ISOBAR AT P = 46 BAR

T OEN VOL DP/DT DP/CD P H S CV CP W OEG K MOL/L L/MOL 8AR/< BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.464 12.757 .07839 22.3463 1384.892 136.3 497.3 109. 452 73.39 98.98 1792

120.000 12.684 .07884 21.4972 1332. 214 585.5 948.1 113. 279 73.82 99.69 1759

130.000 12. 523 . 0 7985 19.7833 1225. 484 1585.9 1953.2 121. 322 74.85 101. 32 1689

140.000 12.361 .08090 18.2558 1129.751 2602.

6

2974.7 128. 893 76.01 103.04 1623

150.000 12. 200 .08197 16.8851 1043.199 3636.

3

4013.4 136.063 77.29 104.84 1560

160.000 12.038 .08307 15.6475 964.362 4688.

2

5070.3 142.889 78.68 106.72 1500

170.000 11.875 .08421 14.5242 892.0 86 5759. 0 6146.3 149. 417 80.16 108.67 1442

180.000 11.712 .08538 13.4996 325.442 6849.6 7242.4 155. 685 81.73 110.70 1386

190.000 11.548 .08660 12.5611 763.662 7961.

1

8359.5 161. 727 83 .37 112.81 1333

200.000 11.383 .08785 11.6960 706.135 9094.3 9498.4 167.568 85.07 114.99 1281

210.000 11.216 .08915 10.9013 652. 339 10250.0 10660.1 173. 232 86.83 117.24 1230

220.000 11.048 .09051 10.1634 601. 845 1142 9.1 11345.5 173. 740 88.64 119.57 1181

230.000 10.879 .09192 9.4776 554.291 12632. 6 13055.4 184. 108 90.49 121.98 1133

240.000 10.706 .09340 8.8382 509.376 13861.2 14290.3 139. 352 92.37 124.48 1086

250.000 10. 531 .09495 8.2402 466.851 15115.8 15552.6 194.485 94.27 127. 06 1040

260.000 10.353 .09659 7.6793 426. 506 16397. 4 16841.7 199. 521 96.20 129. 74 994

270 .000 10.171 .09832 7.1514 388.169 17706.

3

18159.1 204.469 98.14 132.53 949

280.000 9. 984 .10016 6.6531 351. 7 02 19045.

1

19505.8 209. 341 100.10 135.45 904

290.000 9.79 2 .10212 6.1611 316.984 20413.4 20883.2 214.147 102.06 138.51 860

300.000 9.594 .10423 5.7327 28 3.9 29 21813.0 22292.5 218. 897 104.02 141.74 815

310.000 9. 388 .10652 5. 3050 252.458 23245.5 23735.5 223.600 105.98 145.19 771

320.000 9.173 .10901 4.8956 222.510 24712.7 25214.

1

228. 268 107.94 148.90 726

330.000 8.947 .11176 4.5018 194.032 26216.9 26731.0 232.911 109.91 152.96 681

340.000 8.708 .11483 4. 1210 166. 979 27761.

4

28289.6 237. 543 111.87 157.47 635

350.000 8. 45 3 .11831 3. 7503 141. 3 C9 29350.4 29694.6 242.180 113.85 162.61 589

360.000 3.176 .12231 3.3863 116.985 30990.

2

31552.8 246.843 115.87 168.66 541

370.000 7.871 .12705 3.0242 93.972 32690.

4

33274.3 251.561 118.00 176.13 491

330.000 7.528 .13284 2.6574 72. 246 34467.

0

35078.1 256. 380 120.41 185.96 438

390.000 7.127 .14031 2.2759 51. 814 36349.

6

36995.0 261. 376 123.29 200.05 380

400.000 6.631 .15082 1.8627 32.778 38400.6 39094.3 266.639 126.67 222.97 315

410 .000 5.932 .16857 1.3860 15. 615 40175.4 4 0950.9 271. 199 137.02 280.34 234

420.000 4.513 .22158 .7909 3.535 43555.1 44574.3 279.920 137.88 502.80 148

430.000 2.864 .34920 . 4336 5.148 47467.

4

49073.7 290. 519 137.29 328.77 145

440.000 2. 321 .43081 . 3275 9. 0 43 49797.9 51779.6 296. 744 137.05 233.93 162

450.000 2.040 .49028 .2736 12.323 51689.

7

53945.

0

301. 612 137.86 203.58 176

460.000 1.853 .53957 .2389 15. 176 53420.5 55902.5 305.915 139.13 189.52 188

470.000 1.716 .58285 .2141 17.730 55074.9 5 7756.0 309. 902 140.64 181.91 198

480.000 1.60 8 .62208 .1951 20. 064 56689.5 59551.1 313. 681 142. 29 177.52 207

490.000 1.519 .65338 .1799 22. 227 58233.8 61312.3 317.313 144.03 174.97 215

500.000 1.444 .69244 . 1675 24.253 59869.

0

63054.

2

320.832 145.83 173.56 222

520.000 1.323 .75559 .1481 27.982 63036.3 66514.0 327.618 149.51 172.79 235

540.000 1.229 .81391 .1336 31. 385 66231.8 69975.7 334. 150 153.24 173.58 247

560.000 1.151 .86873 .1222 34.541 69466.3 73462.5 340. 491 156.95 175.22 257

580.000 1.086 .92093 . 1130 37. 5 C5 72751.

4

76987.7 346.676 160.63 177.36 266

600.000 1.030 .97108 .1053 40.315 76091.9 30556.9 352.729 164.24 179.80 275

620.000 .981 1.01958 . 0988 43. 0 00 79490.8 84180.9 358. 667 167.78 182.42 283

640.000 .937 1.06673 . 0933 45.580 82949.

4

8 7856.

4

364. 502 171.25 185.15 291

660.000 .899 1.11277 .0884 48. 0 73 36468.

2

91586.9 370. 241 174.63 187.92 298

680.000 .864 1.15786 . 0841 50.490 90046.3 95373.0 375. 893 177.93 190.71 305

700.000 .832 1.20216 . 0803 52.843 93685.2 99215.1 381.461 181.15 193.50 311

136
Table 22. Continued

I-BUTANE ISOBAR AT P = 48 BAR

T OEN VOL OP/DT OP/CD E H S CV CP W OEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.544 12.758 .07839 22.3481 1386.073 142.4 516.6 109. 500 73.40 98.98 1793

1?0. 000 12.686 .07883 21.5141 1334.3 10 583.1 961.5 113.259 73.82 99.68 1760

130.000 12.524 .07984 19.7996 1227.511 1583.3 1966.5 121. 302 74.85 101.31 1690

140.000 12.363 .08089 18.2715 1131.722 2599.7 2987.9 128.872 76.01 103.03 1624

150.000 12.201 .08196 16. 9004 1045. 124 3633. 1 4026.5 136. 042 77.29 104.83 1561

160.000 12.040 .08306 15.6625 966.250 4684.

6

5083.3 142. 866 78.68 106.70 1501

170.000 11.877 .08419 14.5369 893.944 5 755.

1

6159.2 149. 394 8 0.16 108.66 1443

180.000 11.714 .08537 13.5141 827.276 6845.

4

7255.2 155.661 81.73 11 0.69 1388

190.000 11. 550 .08658 12. 5754 765.477 7956.

5

8372.1 161.702 83.37 112.79 1334

200.000 11.386 .08783 11.7121 7 07.9 37 9089. 3 9510.8 167. 542 85.07 114.97 1282

210. 000 11.219 . 08913 10.9153 654. 1 33 10244.5 10672.4 173. 206 86.83 117.22 1232

220.000 11.052 .09048 10.1773 603.634 11423.

2

11657.5 178. 712 88.64 119.55 1183

230.000 10.882 .09189 9.4915 556.079 12626.

1

13067.2 184. 079 90.49 121.95 1135

240.000 10.710 .09337 8.6521 511.168 13854.

1

14302.3 189. 322 92.37 124.44 1088

250.000 10.536 .09492 8.2542 468. 648 15108.1 15563.7 194.454 94.28 127.02 1042

260.000 10.358 .09655 7.6934 428.313 16386.9 16852.3 199.487 96.20 129.69 996

270.000 10.176 .09827 7.1657 389.989 17697.4 18169.1 204.434 98.14 132.47 951

280.000 9.990 .10010 6.6676 353.5 38 19034. 8 19515.2 209.303 100.10 135.38 906

290.000 9.799 .10205 6.1960 318.839 20402.

0

20691.8 214. 107 102. 06 138.42 862

300.000 9. 601 .10415 5.7479 285.8 C6 21800.3 22300.2 218.853 104.02 141.64 818

310.000 9.3 96 .10643 5.3207 254. 362 23231.2 23742.

0

223. 553 105.98 145.06 773

320.000 9.182 .10891 4.9119 224. 444 24696.

5

25219.2 223. 215 107.94 146.74 729

330.000 8.95 8 .11164 4.5189 196. 0 Cl 26198.5 26734.3 232. 853 109.91 152.75 684

340.000 3.720 .11468 4. 1391 168.991 27740.1 28290.6 237.478 111.87 157.20 639

350.000 0.467 .11811 3.7698 143. 373 29325.5 29892.4 242.106 113.85 162.25 592

360.000 8.193 .12206 3.4075 119. 1 15 30960.5 31546.4 246. 757 115.87 168.15 545

370.000 7.892 .12671 3.0460 96.189 32654.

0

33262.2 251. 458 118.00 175 .38 495

380.000 7.555 .13237 2.6852 74.5 83 34420.

6

35056.

0

256. 252 12 C.41 184,77 443

390.000 7.165 .13957 2.3102 54.322 36287.

0

36957.0 261. 20 6 123.28 197.93 387

400.000 6.689 .14949 1.9089 35.534 38307.1 39024.7 266. 440 126.63 218.30 324

410.000 6.049 .16531 1.4586 18.6 86 40000.9 40794.5 270. 736 136.87 264, 44 249

420.000 4.953 .20191 .9302 5.870 42940.6 43909.3 27 3. 237 137.10 389.45 169

430.000 3.289 .30406 .5158 4. 389 46762.4 48221.9 238 . 386 138.16 379.11 143

440.000 2.556 . 39124 .3709 8.0 36 49377.

3

51255.3 295.365 137.77 253.06 159

450.000 2.20 8 .45282 . 30 34 11.4 06 51380.2 53553.7 300. 533 138.41 212.90 173

460.000 1.989 .50260 . 2619 14.349 53170.4 55583.8 304.995 139.57 195.17 185

470.000 1.831 . 54615 .2329 1 6. 980 54862.

4

57483.9 309. 083 14 1. 00 185.79 196

480.000 1.709 .58515 .2111 19. 378 56503.5 59312.3 312.932 142.60 180.39 205

490.000 1.610 .62105 .1939 21.597 58117.7 61098.7 316. 616 144.30 177.20 21 3 500.000 1.528 .65461 .1799 23. 671 59718,4 62860.6 320 . 176 146.07 175.36 221

520.000 1.396 .71654 .1563 27.482 62911.0 66350.4 327.020 149.70 174. 05 234

540.000 1.293 .77351 .1423 30.951 66121.

0

696 33.8 3 3 3 . 59 3 153.39 174.52 246

560.000 1.209 .82691 .1298 34.163 69366.0 73337.2 339.964 157.08 175.96 256

580.000 1.139 . 8 7764 .1197 37. 175 72663.

0

76875.6 346. 172 160.74 177. 96 266

600.000 1.080 .92629 .1114 40. 028 76011.4 80457.6 352.244 164.33 180.30 274

620.000 1. 027 .97323 .1044 42. 749 79416. 9 84088.7 356. 197 167.86 182.84 283

640.000 .981 1.01892 .0964 45.362 82881.

0

87771.9 364. 044 171.32 185.50 290

660.000 .940 1 .06344 . 0932 47. 8 {4 66404.6 91509.1 369. 793 174.69 188.23 297

680 .000 .903 1. 10701 . 0866 50. 329 89987.

3

95300.9 375. 453 177.98 190.98 304

700.000 .870 1.14978 . 0845 62. 7 C6 93629.2 99148.

1

381. 029 181.19 193.74 311

137
Table 22. Continued

I-BUTANE ISCBAR AT P = 50 BAR

T DEN VOL OP/DT DP/OD E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.623 12.758 .07838 22.3499 1387.257 147.9 539.9 109.548 73.41 98.99 1793

120.000 12.687 .07882 21.5309 1336. 406 580.

7

974.8 113. 239 73.82 99.68 1762

130.000 12.526 .07983 19.8158 1229.537 1580.7 1979.8 121. 281 74.85 101.31 1692

140.000 12.365 .08087 18.2873 1133.693 2596.

8

3001.1 128.851 76.01 103.02 1625

150.000 12.203 .08194 16.9157 1047. 049 3629.9 4039.7 136.020 77.29 104.82 1562

160.000 12.042 .08305 15.6775 968. 137 4681.1 5096.4 142. 844 78.68 106.69 1502

170 .000 11.879 .08418 14.5536 895. 301 5751.

3

6172.2 149.371 80.16 108.65 1445

180.000 11.717 .06535 13.5285 829. 109 6841.

2

7268.0 155. 638 81.73 110.67 1389

190.000 11. 553 .08656 12.5896 767. 292 7951.9 8384.7 161.677 83.37 112.77 1336

200.000 11.338 .08761 11.7262 709.738 9084.3 9523.3 167.517 85.07 114.95 1284

210.000 11.223 .08911 10.9293 655. 925 10239.

1

10684.

6

173. 179 86.83 117.20 1234

220.000 11.055 .09046 10.1912 605.422 11417.2 11669.5 178.685 88.64 119.52 1185

230.000 10.886 .09186 9.5054 557. 866 12619.6 13078.

9

184.050 90.49 121.92 1137

240.000 10.714 .09333 8.8660 512.957 13847.

0

14313.7 189.292 92.37 124.41 1090

250.000 10.540 . 0 9488 8.2682 470. 444 15100.

3

15574.7 194.422 94,28 126.98 1044

260 .000 10.363 .09650 7. 7075 430.1 18 16380.

4

16862.9 199.454 96.20 129.64 998

270.000 10.181 .09822 7.1799 391.807 17688.

1

18179.2 204. 398 98.15 132.42 953

280.000 9.996 .10004 6.6821 355.371 19024.5 19524.7 209. 266 10 C. 10 135.31 909

290.000 9.805 .10199 6.2107 320.692 20390.6 2 09 0 0.5 214.066 102.06 138.34 864

300.000 9.608 .10408 5.7630 287. 681 21787.

6

22308.

0

218. 810 104.02 141.54 820

310.000 9.404 .10634 5.3363 256.261 23217.

0

23746.7 223.505 105.98 144.94 776

320.000 9.191 .10880 4. 9281 226. 373 24680.4 25224.5 228. 164 107.94 148.58 732

330.000 8.968 .11151 4.5358 197.965 26180.2 26737.7 232. 796 109.91 152.55 687

340.000 8.732 .11452 4.1571 170. 995 27719.1 28291.7 237. 414 111.87 156.94 642

350.000 3.430 .11792 3.7890 145. A27 29300.9 29890.5 242. 033 113.85 161.90 596

360.000 3.209 .12181 3.4285 121.231 30931.

2

31540.3 246.672 115,87 167.66 549

370.000 7.913 .12638 3.0715 98. 387 32618.

3

33250.2 251. 35 8 118.00 174.67 500

380.000 7.581 .13190 2.7124 76.892 34375.6 35035.1 256.128 120. 41 183.66 449

390.000 7. 201 .13888 2.3432 56.784 36227.

1

36921.5 261. 044 123.28 196.01 394

400.000 6. 743 .14829 1.9524 38.2 10 38220.2 38961.6 266.203 126.61 214.35 333

410.000 6.148 .16264 1.5230 21. 6 18 39850.8 40664.0 270.333 136.75 253.12 262

420.000 5.234 .19107 1.0400 8.552 42546.3 43501.6 277. 172 136.58 330.49 188

430.000 3.749 .26671 .6099 4. 442 46045.

9

47379.5 286. 294 138.56 394.74 147

440.000 2. 320 .35464 .4207 7. 175 48920.3 50694.0 293.920 138.44 274.96 156

450.000 2.391 .41829 . 3365 10.555 51053.1 53144.5 299.430 138.95 223.38 170

460.000 2.132 .46899 .2868 13.568 52909.9 55254.8 304. 069 14 C. 00 201.35 183

470.000 1.951 .51246 .2530 16.266 54643.2 57205.5 308. 265 141.37 189.94 193

480.000 1.814 .55128 .2280 18. 725 56312.

9

59069.4 312. 189 142.91 183.41 203

490.000 1.704 .58682 .2085 20. 995 57946.2 60882.3 315. 928 144.57 179.53 211

500.000 1.613 .61991 .1928 23.116 59565.4 62664.9 319. 530 146.30 177.22 219

520.000 1.469 .68073 .1639 27. 0 05 62782.0 66135.7 326.434 149.89 175.34 233

540.000 1.358 .73645 .1512 30.5 38 66009.0 69691 .

3

333.050 153.55 175.48 245

560.000 1.268 .78853 . 1376 33.804 69269.

0

73211.7 339.451 157.21 176.71 255

580.000 1.193 .33791 . 1266 36.863 72574.

0

76763.5 345, 683 160.84 178.56 265

600.000 1.130 .38513 .1177 39.756 75930.5 80356.5 351.773 164.43 160.80 274

620.000 1.074 .93078 .1101 42.513 79342.

7

83996.6 357. 741 167.94 183.26 282

640 .000 1.026 . 97502 .1036 45. 158 82312.

4

37687.5 363, 600 171. 39 185. 66 290

660.000 .932 1.01813 . 0981 47.7 C9 36340.7 91431.4 369. 360 174.75 188.54 297

680. 000 . 943 1.06029 . 0932 50.179 89927.8 95229.3 375. 029 178.04 191.26 304

700.000 .903 1.10165 .0888 52.581 93573.1 99081.4 380.612 181.24 193.98 311

138
Table 22. Continued

I-BUTANE ISCBAR AT P = 52 BAR

T DEN VOL OP/DT OP/ CO E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115. 702 12.758 .07838 22.3519 1388.444 153.5 561.1 109.596 73.42 99.00 1794

120.000 12.689 . 07881 21.5478 1338.5 02 578.

4

988.2 113. 219 73.82 99.67 1763

130 .000 12.528 .07982 19.8320 1231.564 1578.0 1993.1 121. 261 74.85 101.30 1693

140.000 12.367 .08086 18.3030 11 35. 664 2593.9 3014.4 128.830 76.01 103.01 1627

150.000 12.205 .08193 16.9311 1048.974 3626.

8

4052.3 135. 998 77.29 104.61 1564

160.000 12.044 .08303 15.6925 970. 0 24 4677.6 5109.4 142. 822 78.68 106.68 1504

170.000 11.882 . 08416 14.5682 897.657 5747.4 6185.1 149. 348 8 0.16 108.63 1446

160.000 11.719 .08533 13.5430 830.941 6837.

0

72 80 .

8

155. 614 81.73 110.66 1391

190.000 11.556 .08654 12.6038 769. 1 06 7947.4 8397.4 161. 653 83.37 112.76 1337

200.000 11.391 .08779 11.7403 711. 539 9079.3 9535.3 167.491 85.07 114.93 1285

210.000 11.226 .08908 10. 9432 657. 7 17 10233.7 1 0696.9 173. 153 36.83 117.18 1235

220.000 11.058 . 09043 10.2051 6 07.2 08 11411.3 11881.6 178. 657 88.64 119.50 1186

230.000 10.839 . 09183 9.5192 559. 652 12613.2 13090.

7

184.022 90.49 121.89 1138

240.000 10.718 .09330 8.8799 514. 745 13840.0 14325.1 189. 262 92.37 124.37 1091

250.000 10.544 .09484 8.2821 472. 238 15092.

6

15585.8 194.390 94.28 126.94 1045

260.300 10.367 .09646 7.7215 4 31.9 22 16371.9 16873.5 199.420 96.20 129.60 1000

270.000 10.186 .09817 7.1941 393. 623 17678.

8

18189.3 204, 363 98.15 132.36 955

280.000 10.001 .09999 6.6965 357.2 C2 19014. 3 19534.

2

209. 228 10 C. 10 135.24 911

290.000 9.311 .10192 6.2254 322.541 20379.2 2 0909.3 214. 026 1 02. 06 136.26 667

300.000 9.615 .10400 5.7781 289.551 21 775.

0

22315.8 218. 766 104.02 141.44 823

310.000 9.412 .10625 5.3519 258.157 23202.9 23755.4 223.458 105.98 144.81 779

320.000 9.200 .10870 4.9442 228.297 24664.5 25229.8 228.112 107.94 148.43 734

330.000 8.973 .11138 4.5527 199.922 26162.1 26741.3 232.739 109.91 152.35 690

340.000 3 . 744 .11437 4. 1749 172.991 27698.

3

23293.0 237. 350 111.87 156.68 645

350.000 8.494 .11773 3.8081 147.471 29276.7 29888 .9 241.961 113.85 161.56 600

360.000 3.226 .12157 3.4493 123.335 30902.5 31534.6 246.589 115.87 167.19 553

370.000 7.933 .12606 3. 0946 100.568 32583.

4

33238.9 251. 259 118.00 173.99 505

360.000 7.607 .13146 2. 7389 79.174 34331.9 35015.4 256. 007 120.40 182.62 454

390.000 7.235 .13821 2.3752 59.206 36169.6 36888.3 260. 888 123.27 194.26 400

400.000 6. 794 .14719 1.9935 40.818 38138.6 38904.0 265.990 126.58 210.95 342

410.000 6.235 .16038 1.5813 24. A38 39718.1 40552.0 269.986 136.66 244,56 274

420.000 5.437 .18393 1.1309 11.282 42257.9 43214.4 276.399 136.23 297.32 205

430.000 4.172 .23972 . 7064 5. 1 37 45422.

8

46669.4 284. 525 138.48 378.50 155

440.000 3.112 .32131 .4774 6.562 48433.3 50104.6 292.427 139.01 296.76 155

450.000 2 .588 .38647 . 3729 9. 750 50 708.

3

52717.9 298. 30 3 139,46 234.92 168

460 .000 2.284 .43787 . 3138 12. 8 39 52639.

2

54916.

1

303. 135 140.43 208.06 180

470.000 2.077 .48147 .2745 15.593 54417.

6

56921 .

3

307.449 141.73 194.37 191

460.000 1.923 .52013 .2459 18. 1 05 56117.9 58822.6 31 1. 452 143.22 186.60 201

490.000 1.801 .55534 .2240 20.424 57775.5 60663 .

2

31 5. 248 144.84 181.95 210

500.000 1.701 .58800 . 2064 22.588 59409.

9

62467.5 318. 893 146.54 179. 15 217

520.000 1.544 .64779 .1798 26.551 62651.7 66020 .2 325.860 150.08 176. 66 231

540.000 1.424 .70235 . 1605 30.146 65896.2 69548.5 332.519 153.70 176.45 244

560.000 1.323 .75321 . 1456 33.464 69169.3 73086.0 338.951 157.34 177.46 254

580.000 1.248 .80133 .1337 36. 568 72484.

5

76651.4 345. 207 160.95 1 79. 17 264

600.000 1. 180 .84733 . 1240 39. 5 00 75849.3 30255.4 351.316 164 .52 181.30 2 73 620.000 1.122 .89164 .1159 42.292 79268.

2

83904.

7

357. 299 168.02 183.68 282

640.000 1.070 .93458 .1090 44.963 82743.6 87603.4 363. 170 17 1.45 186.22 289

660.000 1 . 024 .97639 .1030 47.546 86276.8 91354.0 368.941 174.81 188.85 297

660 .000 . 983 1.01724 . 0978 50.042 89868.0 95157.7 374. 613 178.09 191.53 304

700.000 .946 1.05730 .0931 52.466 93517.2 99015.2 380 . 209 181.28 194.22 310

139
Table 22. Continued

I-BUTftNE ISOBAR AT P = 55 BAR

T OEN VOL OP/OT DP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

115.920 12.758 .07838 22.3548 1390.231 161.8 592.9 109. 663 73.43 99.00 1795

120.000 12.691 .07880 21.5730 1341.647 574.9 1008.3 113.189 73.82 99. 66 1765

130,000 12.530 .07981 19.8564 1234.6 C3 1574.1 2013.1 121. 230 74.85 101.29 1695

140.000 12.369 .08085 18. 3266 1138.620 2589.5 3034.2 128. 799 76.01 103.00 1629

150.000 12.208 .08191 16.9540 1051.860 3622.

0

4072.5 135. 966 77.29 104.80 1566

160.000 12.047 . 08301 15.7149 972.854 4672.4 5129.

0

142. 788 78.68 106,67 1506

170,000 11.885 . 0 8414 14.5902 900.442 5741.

7

6204.5 149. 313 80.16 108.62 1448

180.000 11.723 .08530 13.5646 833.689 6830.3 7300.0 155.578 81.73 110.64 1393

190.000 11.560 .08651 12.6251 771.826 7940.5 8416.3 161. 616 83.37 112.73 1340

200.000 11.395 .08775 11.7614 714.238 9071.8 9554.5 167.453 85.07 114.90 1288

210.000 11.230 .08905 10.9642 660.4 03 10225,

5

10715.

3

173.113 86.83 117.14 1238

220.000 11.063 .09039 10,2259 609. 886 11402.5 11899.6 178.616 88.64 119.46 1139

230.000 10.395 .09179 9.5400 562.328 12603.5 13108.4 183.979 9 C.49 121.85 1141

240.000 10.724 .09325 3.9007 517.425 13829.5 14342.3 189. 217 92.37 124.32 1094

250.000 10.551 .09478 8.3030 474.926 15081.1 15602.4 194. 343 94.28 126. 86 1048

260 .000 10.374 .09639 7.7425 434.623 16359. 3 16889.5 199. 371 96.20 129.52 1003

270.000 10.194 .09810 7.2154 396.342 17665.

0

18204.5 204. 310 98.15 132.27 958

280.000 10. 010 .09990 6.7181 359.943 18999.0 19548 .5 209.172 100.10 135.14 914

290.000 9.820 .10183 6.2474 325.3 09 20362.4 20922.4 213.966 102.06 138. 14 870

300.000 9.625 .10389 5.8007 292. 350 21 756.

2

22327.

6

21 8. 702 104.02 141.29 826

310.000 9. 423 .10612 5.3751 260.992 23131.9 23765.6 223.389 105.98 144.63 782

320.000 9.213 . 10854 4. 9683 231.173 24640.

9

25237.9 228. 036 107.95 148.20 738

330.000 8.993 .11120 4.5779 202.646 26135.

3

26746.9 232.655 109.91 152.07 694

340.000 8.761 .11414 4.2014 175.972 27667.5 28295.3 237. 256 111.87 156.31 650

350.000 8. 514 .11745 3.8364 150.520 29240.9 29886.9 241. 854 113.85 161.06 605

360.000 8. 25 0 .12122 3.4800 126. 468 30860.

2

31526.9 246.466 115.87 166.52 559

370.000 7. 962 . 12560 3.1285 103.8 07 32532.4 33223.1 251.114 118.00 173.03 511

330.000 7.644 .13082 2.7776 82.552 34268.4 34987.9 255.831 120.40 181.18 462

390.000 7.284 .13728 2.4213 62.768 36087. 3 36842.3 260, 664 123.26 191.91 410

400.000 6,864 .14568 2.0516 44.619 38024.8 38826.0 265. 685 126.55 206.63 354

410.000 6.349 . 15751 1.6601 28. 495 39542.9 40409.2 269. 521 136.57 234.94 290

420.000 5.664 .17655 1.2450 15. 310 41929.7 42900.8 275.524 135.89 268.43 228

430.000 4.669 .21418 .8437 7. 2 38 44713. 7 45891.

7

282. 559 138.01 332,01 173

440.000 3.581 . 27925 .5727 6. 416 47692.

2

49228.0 290. 230 139.52 314.93 157

450.000 2.910 .34362 .4344 8.380 50161.

3

52051.7 296.579 140.14 253.06 166

460.000 2.527 .39572 .3582 11.868 52214.

9

54391.4 301.723 141.03 218.93 178

470.000 2.275 .43948 .3 094 14.668 54067.

3

5 64 84 .

5

306. 225 142.25 201.48 189

480.000 2.092 .47791 .2747 17.244 55817.

2

58445.7 310. 355 143. 67 191.66 198

490.000 1.951 .51267 .2485 19.6 26 57510.6 60330.3 314. 241 145.23 185.77 207

500.000 1.836 . 544 7 4 .2279 21.848 59172.

4

62168.5 317. 955 146.89 182.15 215

520.000 1.658 .60311 .1970 25.915 62453.3 65770.4 325. 019 150.36 178.69 230

540.000 1.524 .65607 .1749 29. 597 65725.

3

69333.6 331. 744 153,93 177.95 242

560.000 1.418 .70525 . 1580 32.989 69018.5 72897.4 338. 224 157.53 178.62 253

590.000 1.330 . 75163 .1447 36.157 72349.

4

76433.4 344.516 161.11 180.09 263

600.000 1.256 .79587 .1339 39.145 75726.7 80104.0 35 0.65 3 164.65 182.05 272

620.000 1.193 .63841 .1248 41.987 79156.1 83767.4 356. 659 168.14 184.32 281

640 .000 1.137 . 8 795 7 .1172 44. 707 82640.2 87477.8 362. 549 171.55 186. 76 289

660 .000 1.087 .91960 . 1106 47.326 86180.6 91238.4 363.335 174.90 169.32 296

630. 000 1. 043 .95867 . 1048 49, 858 89778.

2

95050.9 374.025 178.16 191.94 303

700.000 1.003 .99694 .0998 5 2. 316 93432.7 98915.8 379.627 181.35 194.58 310

140
Table 22. Continued

I-BUTANE ISOBAR AT P = 60 BAR

T DEN VOL OP/OT DP/DD E H S CV CP M OEG K MOL/L L/HOL BAR/K BAR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

116.016 12.759 .07838 22. 3600 1393.222 175. 4 645.7 109. 785 73.44 99.02 1797

120.000 12.695 .07677 21.6150 1346. 887 569. 0 1041.7 113. 139 73.82 99.65 1768

130.000 12.534 .07978 19.8968 1239.669 1567.6 2046.

3

121.179 74.85 101.27 1698

140.000 12.374 .06082 18.3659 1143.546 2582.

4

3067.3 128.746 76.01 102.98 1632

150.000 12.213 .08188 16.9922 1056.670 3614.

1

4105.4 135. 912 77.29 104.77 1569

160.000 12.052 .08297 15.7522 977.569 4663.

7

5161.6 142. 733 76.68 106.64 1509

170.000 11.891 .06410 14.6268 905.080 5732.2 6236.3 149. 256 80.16 108.59 1452

180.000 11.729 .08526 13.6005 838.266 6820.4 7332.0 155.519 81.73 110.60 1397

190.000 11.566 .08646 12.6606 776. 356 7929.2 8448.

0

161. 555 83.37 112.69 1343

200.000 11.402 .08770 11.7964 718.733 9059.5 9585.7 167.390 85.07 114. 86 1292

210.000 11.238 .08899 10.9989 664.874 10212.1 10746.0 173. 048 66.63 117.09 1241

220.000 11.071 . 09032 10 .2605 614.344 11387.8 11929.8 178.548 88.64 119.40 1193

230.000 10.904 . 09171 9.5745 566.781 12587.

6

13137.8 183. 907 90.49 121.78 1145

240.000 10. 734 .09317 8.9352 521. 883 13812.1 14371.0 189. 142 92 .37 124.24 1098

250.000 10.561 .09469 8.3376 479. 398 15062.

1

15630.2 194. 265 94.28 126. 78 1053

260.000 10.386 .09629 7.7774 439. 115 16338.5 16916.

3

199. 288 96.20 129.41 1008

270.000 10.207 .09798 7.2506 40 0.662 17642.1 18230.0 204. 223 98.15 132.14 963

280.000 10.024 .09977 6.7538 364.499 18973.

8

19572.

4

209. 079 10 C. 10 134. 97 919

290.000 9.836 .10167 6.2839 329.910 20334.6 20944.6 213. 867 102.06 137.94 875

300.000 9. 642 .10371 5. 6379 296.998 21725.4 22347.6 218.595 104.02 141.05 832

310.000 9.442 .10591 5.4135 265 .696 23147.4 23782.9 223.273 105.98 144.34 789

320.000 9.234 .10829 5.0081 235.943 24602.2 25252.0 227. 911 107.95 147.84 745

330.000 9.017 .11090 4.6193 207.692 26091.4 26756.8 232.517 109.91 151.61 702

340.000 8.739 .11378 4.2450 180. 906 27617. 3 28300.0 237. 103 11 1.87 155.72 658

350.000 8.547 .11700 3.8828 155. 558 29182.8 29884.9 241.681 113.86 160.29 613

360.000 8.286 .12065 3.5300 131.632 30792.

0

31515.9 246. 268 115.87 165.48 568

370 .000 8.009 .12486 3. 1836 109.1 28 32450.

6

33199.8 250. 882 118.00 171.57 522

380.000 7. 703 .12983 2.8398 88.074 34167.8 34946.8 255. 551 120.40 179.04 474

390.000 7. 361 .13586 2.4939 68.544 35959.

3

36774.4 260. 315 123.25 186.57 424

400.000 6.969 .14349 2.1405 5 0.7 C7 37853.4 38714.3 265.225 126.52 200.93 372

410.000 6.507 .15368 1.7749 34.898 39295.5 40217.6 268. 864 136.45 223.87 313

420.000 5.936 .16846 1.3988 21.744 41527.7 42538.4 274.456 135.56 242.81 258

430.000 5.198 .19239 1.0347 12.296 43 966.

1

45120 .

4

280. 530 137.31 275.88 206

440.000 4.289 .23314 .7390 8.094 46642.2 48041.0 287.244 139.47 300.63 173

450.000 3.497 .28600 .5530 6.468 49224.

1

50940.0 293. 760 140.86 273.80 168

460.000 2.973 .33641 . 4435 10. 7 19 51469.

3

53487.8 299. 362 141.68 237.40 175

470.000 2.633 .37984 .3750 13.4 C5 53456.

0

55735.

0

304. 196 143.03 214.18 185

480.000 2. 394 .41777 .3281 16. 0 12 55296.

7

57603.3 308. 551 144.37 200.68 195

490.000 2.213 .45178 .2935 18.462 57055.2 59765.9 312.598 145.86 192.52 204

500.000 2.071 .48294 .2668 20.761 58766.0 61663.7 316. 432 147.45 187.43 213

520.000 1.855 .53917 .2278 24.974 62116.7 65351.7 323.666 150.81 182.22 227

540.000 1.696 .56976 . 2004 28.785 65436.

4

68974.9 330. 503 154.30 180.50 240

560.000 1.571 .63646 .1799 32.289 68764.6 72583.3 337.065 157.84 180 .57 252

580.000 1.470 .68031 .1639 35. 556 72122.

3

76204.2 343. 418 161.37 181.65 262

600.000 1.385 .72198 . 1510 38.6 21 75521.

3

79853.

2

349. 603 164.87 183.33 271

620.000 1.312 .76193 . 1403 41.550 78968.

0

83539.

6

355. 647 168.33 185.38 260

640.000 1.249 .60049 .1313 44. 340 82466.9 87269.9 361.568 17 1.72 187.67 288

660.000 1.193 .83792 .1236 47.0 22 86019.

8

91047.3 367.380 175.04 190.10 296

680.000 1.144 .87439 .1170 49.611 8962 8. 1 94874.4 373. 093 178.29 192.62 303

700.000 1.099 .91006 .1111 52.121 93292.

0

98752.3 378. 713 16 1.46 195.19 310

141
Table 22. Continued

I-3UTANE ISOBAR AT P = 65 BAR

T DEN VOL OP/OT OP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

116.210 12.759 .07338 22.3654 1396.232 188.9 698.4 109.901 73.46 99.04 1799

120.000 12.698 .07875 21.6570 1352. 139 563.2 1075.1 11 3. 089 73.82 99.63 1771

130. 000 12.538 .07976 19.9373 1244.737 1561.2 2079.6 121, 128 74.85 101.26 1702

140.000 12.378 .08079 18.4051 1148.471 2575.

2

3100.3 128.694 76. 01 102.96 1635

150.000 12.218 .08185 17.0304 1061.478 3606.

2

4138.2 135.858 77.29 104.75 1573

160.000 12. 057 .08294 15.7894 982.282 4655.

1

5194.2 142.677 78.68 106.62 1513

170.000 11.896 .08406 14.6633 909.715 5722.7 6269.

1

149. 199 80.16 108.56 1455

180.000 11.735 .08522 13.6364 842.839 6810.1 7364.0 155.460 81.73 110.57 1400

190.000 11.572 .06641 12.6960 780. 882 7918.

0

8479.

6

161.494 83.37 112.66 1347

200.000 11.409 .08765 11.8314 723. 223 9047.2 9616.9 167.327 85.07 114.81 1295

210.000 11.245 .08893 11.0336 669. 339 10198,7 10776.

8

172. 982 86.83 117.04 1245

220.000 11.080 .09026 10.2950 618. 795 11373.

3

11960.0 178. 480 83.64 119.34 1197

230.000 10.912 .09164 9.6088 571.227 12571.

7

13167.4 183. 837 90.49 121.71 1149

240.000 10. 743 .09308 8.9696 526.333 13794.3 14399.8 189.068 92.37 124.16 1103

250.000 10.571 .09460 8.3721 483. 859 15043.3 15658.1 194. 187 94.2 8 126.68 1057

260.000 10.397 .09618 7. 8121 443.595 16317.9 16943.1 199. 206 96,20 129.30 1012

270.000 10.219 .09786 7.2856 405.369 17619.6 18255.6 204. 136 98.15 132.00 968

260.000 10. 037 .09963 6.7893 369. 039 18949.

0

19596.6 208. 988 10 0.10 134.81 924

290.000 9.851 .10151 6.3200 334.489 20307.1 20967.0 213.769 102.06 137.75 861

300.000 9.659 .10353 5.8749 301.625 21695. 0 22367.9 218.490 104.02 140.82 838

310.000 9. 461 .10570 5.4515 270. 377 23113.6 23800.6 223. 160 105.98 144.05 795

320.000 9.255 .10805 5.0473 240.685 24564.3 25266.

6

227. 787 107.95 147.49 752

330.000 9. 041 .11061 4.6602 212.5 03 26048.6 26767.5 232. 381 109.91 151.17 709

340.000 8.816 .11343 4.2879 185.797 27568.5 28305.8 236. 952 111.87 155.16 665

350.000 8.579 .11657 3.9282 160.543 29126.6 29884.

3

241. 513 113.86 159.57 622

360.000 8.326 .12011 3.5788 136.729 30726.2 31507.0 246.076 115.87 164.52 577

370.000 8. 054 .12417 3,2368 114.362 32372.

5

33179.6 250.659 118.00 170.26 532

360.000 7.75 8 .12890 2.8992 93.475 34073.1 34911.0 255.286 120.40 177.17 486

390.000 7. 431 .13458 2.5621 74.1 *9 35840.9 36715.7 259. 991 123.24 185.77 438

400 . 000 7.063 .14159 2.2217 5 6.5 46 37699.9 38620.2 264. 812 126.49 196.49 388

410.000 6.639 .15062 1.8752 40.957 39086.

0

40065.1 268. 307 136. 38 216.24 334

420.000 6.139 .16290 1.5252 27.846 41221.5 42280.4 273.644 135.37 228.47 284

430.000 5.534 .18071 1.1876 17.829 43482.7 44657.3 279. 237 136.89 247.97 235

440.000 4.809 ,20795 .8951 11.612 45900.4 47252.0 285. 201 139.02 270,30 197

450.000 4. 054 .24666 .6804 9.718 48386.2 49989.5 291.353 140.96 271.38 179

460.000 3.447 .29009 .5407 10.555 50716.4 52602.0 297. 096 142.39 249.62 178

470.000 3.018 .33132 .4499 12.643 52823.

0

54976.6 302. 204 143.65 226.24 165

480.000 2.716 .36821 .3881 15.096 54757.9 57151.2 306. 784 144,98 209.92 193

490.000 2. 492 .40134 .3435 17.534 56586.

0

59194.7 310.997 146.42 199.55 202

500.000 2.317 .43158 .3097 19.866 58349.

1

61154.4 314. 957 147.96 192.92 211

520.000 2.058 .48585 .2612 24.183 61773.8 64931.8 322. 366 151.23 185.85 226

540.000 1.871 .53434 .2278 28.101 65143.3 68616.5 329. 320 154. 65 183.12 239

560.000 1.728 .57887 .2032 31.704 68508.

0

72270.7 335. 964 158.13 182.56 250

560.000 1.612 .62051 .1842 35. 056 71893.5 75926.8 342. 380 16 1.62 183.22 261

600.000 1.515 .65996 .1690 38.212 75314.5 79604.2 348.613 165.09 184.61 271

620.000 1.433 .69768 .1565 41.202 78779.

3

83314.2 354. 695 168.51 186.45 280

640.000 1.362 .73401 .1461 44. 056 82292.9 87064.0 360. 648 171.88 188.58 268

660.000 1.300 .76921 .1372 46. 795 85858. 4 90858.3 366.486 175.18 190.88 296

680.000 1.245 .80345 . 1295 49.437 89477.

6

94700.1 372. 220 178.41 193.30 303

700.000 1.195 .83690 .1228 51.995 93150.9 98590.8 377.859 181.56 195.78 310

142
Table 22. Continued

I-BUTANE ISOBAR AT P = 70 BAR

T OEN VOL DP/DT DP/CO E H S CV CP H DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

116.402 12.760 .07837 22. 3711 1399.259 202. 3 750.9 110. 016 73.48 99.05 1801

120.000 12. 702 .07873 21.6988 1357.371 557.4 1108.5 113.040 73.82 99.62 1775

130.000 12. 542 .07973 19.9776 1249.8 02 1554.

7

2112.8 121.077 74.85 101.24 1705

140.000 12. 382 .08076 18.4442 1153.396 2568.1 3133.4 128. 641 76.01 102.94 1639

150.000 12.222 .08182 17.0684 1066. 285 3598.

4

4171.1 135.804 77.29 104. 73 1576

160.000 12.062 .06290 15. 8266 986.993 4646.5 5226.8 142.622 78.68 106.59 1516

170.000 11.902 .08402 14.6997 914. 347 5713.3 6301.5 149. 142 8 0.16 108.53 1459

180.000 11.741 .08517 13.6722 847. 4C9 6799.8 7396.0 155.402 81.73 110.54 1404

190.000 11.579 .08636 12.7312 7 85.4 03 7906.8 8511.3 161.434 83.37 11 2.62 1351

200.000 11.416 .08759 11.8662 727. 7 C8 9035.1 9648.2 167. 264 85.07 114.77 1299

210.000 11.253 .06887 11.0681 673.799 10185.5 1 0807.6 172. 917 86.83 116.99 1249

220.000 11.088 .09019 10.3293 623.239 11358.9 11990.2 178. 412 88.64 119.28 1201

230.000 10.921 .09157 9.6431 575.665 12556.

0

13197.0 183.766 90.49 121.64 1153

240.000 10.753 .09300 9.0038 530.773 13777.

7

14428.

7

188.994 92.37 124.08 1107

250.000 10.582 .09450 8.4064 488.310 15024.

6

15686.1 194. 110 94,28 126.59 1062

260.000 10. 408 .09608 7.8466 448 . 064 16297.5 16970.1 199. 125 96.20 129.19 1017

270.000 10.231 .09774 7.3205 409. 863 17597.2 18281.4 204. 051 98.15 131.87 973

280.000 10.051 .09950 6.8246 373. 564 18924.5 19620.9 208. 897 100.10 134. 66 929

290.000 9.866 .10136 6.3559 339.052 20280.1 20989.6 213.672 102.06 137.56 886

300.000 9.675 .10335 5.9115 306. 231 21665.

0

22388.5 218. 387 104.02 140.59 843

310.000 9.479 .10549 5.4891 275.033 23080.3 23618.7 223.048 105.99 143.78 801

320.000 9.276 .10781 5.0861 245.398 24527.

0

25281.

7

227. 666 107.95 147.15 758

330.000 9. 064 .11032 4.7005 217. 281 26006.6 26778.9 232.248 109.91 150.75 716

340.000 8.843 .11309 4.3301 190.649 27520.9 28312.5 236.806 111.88 154.64 673

350.000 8.609 .11615 3.9728 165.481 29071.9 29885.0 241. 349 113.86 158.90 630

360.000 8.362 .11959 3.6264 141.766 30662.8 31500.0 245.890 115.87 163.63 586

370.000 8.096 .12351 3.2884 119.517 32297. 8 33162.

4

250. 445 118.00 169.07 542

380.000 7.810 .12805 2.9562 98.770 33983.3 34879.7 255. 035 12 C.39 175.52 497

390.000 7. 496 .13341 2.6267 79.608 35730.

6

36664.5 259. 688 123.23 183.39 451

400.000 7.147 .13992 2.2969 62. 185 37560.3 38539.7 264.435 126.47 192.91 403

410.000 6.753 .14808 1.9651 46. 753 38902.

8

39939.4 267. 818 1 36.33 210.59 352

420.000 6.302 .15869 1.6341 33.672 40970.6 420 81.4 272.980 135.24 219.12 306

430.000 5.778 .17307 1.3158 23.347 43123.7 44335.2 278, 282 136.62 232.14 261

440.000 5.174 .19327 1.0323 16. 1 02 45379.

3

46732.2 283.792 138.62 247.40 222

450.000 4.516 .22145 .8058 12.260 47717.7 49267.9 289. 490 140.74 257.62 196

460.000 3.902 .25626 .6437 11.613 50027.

7

51821.5 295. 104 142.54 250.31 187

470.000 3.416 .29276 .5323 12.667 52197.

0

54246.3 300.319 144. 05 234. 14 188

480.000 3. 053 .32751 . 4546 14.628 54212.4 56505.0 305. 075 145 . 45 218.18 194

490.000 2.783 . 35938 .3986 16.898 56108.6 58624.2 309.446 146.90 206.40 202

500.000 2.573 .38859 .3565 19. 190 57925.

4

60645.5 313. 530 148.42 198.42 210

520.000 2.268 . 44094 . 2972 23.546 61426.5 64513 .

0

321.115 151 .62 189.54 225

540.000 2.051 .48751 .2570 27.544 64847. 6 68260.1 328. 187 154.98 185.76 238

560.000 1.886 .53010 .2278 31.229 68249.7 71960.3 334.915 158.41 184.57 250

580.000 1. 755 .56979 .2055 34.661 71663.

6

75652.1 341. 393 161.86 184.81 260

600.000 1.647 .60728 . 1878 37.885 75107.1 79358.1 347. 675 165.30 165.90 270

620.000 1.555 .64305 .1734 40.939 78590.0 83091. 4 353. 796 168.69 187.52 279

640.000 1.476 .67744 .1614 43.851 82118.9 86860.9 359. 780 172.03 189.48 288

660.000 1.407 .7 1069 .1512 46.644 85697.

1

90671.9 365. 643 175.31 191.66 296

680.000 1.346 . 74300 .1425 49. 334 89327. 2 94528.2 371. 399 178.52 193.98 303

700 .000 1. 291 .77452 .1349 51.936 93009.9 98431.6 377.056 181 .67 196.38 310

143
Table 22. Continued

I-3UTANE ISC8AR AT P = 75 BAR

T DEN VOL DP/DT DP/CD E H S CV CP H DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

116.593 12.760 .07837 22.3771 1402. 3 C4 215.5 803.3 110.129 73.50 99.07 1803

120.000 12.706 .07870 21.7407 1362.623 551.6 1141.9 112.990 73.82 99.60 1778

130.000 12.546 .07971 20.0179 1254. 868 1548.3 2146.1 121.026 74.85 101.22 1708

140.000 12.387 .08073 18.4832 1158. 319 2561.

0

3166.5 128.589 76.01 102.92 1642

150.000 12.227 . 0 8179 17.1064 1071.091 3590.6 4204.0 135.751 77.29 104.71 1579

160.000 12.067 .08287 15.8637 991.701 4637.9 5259.5 142.567 78.68 106,57 1520

170,000 11.907 .08398 14. 7360 918,977 5704. 0 6333.9 149. 085 80.16 108.50 1462

180.000 11.746 .08513 13.7079 851.976 6789.6 7428.1 155.343 81.73 110.50 1407

190.000 11.585 .08632 12. 7665 789.929 7895.6 8543.

0

161. 373 83.37 112.58 1354

200.000 11.423 .08754 11.9010 732. 189 9022.9 %79.5 167.202 85.07 114.72 1303

210.000 11. 260 .08881 11.1026 678.253 10172.

3

10838.4 172. 853 86.83 116.94 1253

220.000 11.096 .09013 10. 3635 627.677 11344.6 12020.5 178. 345 88.64 119.22 1205

230.000 10.930 .09149 9.6772 580.096 12540.

4

13226.7 183.696 90.49 121.57 1157

240.000 10. 762 . 09292 9.0378 5 35.2 05 13760.7 14457.6 188.921 92,37 124.00 1111

250.000 10.592 .09441 8.4405 492.751 15006.1 15714.2 194. 033 94.28 126.50 1066

260.000 10.419 .09598 7.8809 452.521 16277.

3

16997.2 199. 045 96.21 129. 08 1022

270.000 10.243 .09762 7.3551 414.343 17575.1 18307.3 203. 966 98.15 131.74 978

280.000 10. 064 .09936 6.8596 3 78. 0 73 18900.2 19645.5 208. 807 10 0.10 134.51 934

290.000 9.880 .10121 6.3915 343.597 20253.4 21012.5 213.577 102.06 137.38 892

300.000 9.692 .10318 5.9479 310,818 21635. 6 22409.4 218. 284 104.02 140.38 849

310.000 9.497 .10529 5.5263 279.667 23047.5 23837.2 222.938 105.99 143.52 807

320.000 9.296 .10757 5.1245 250.085 24490.5 25297.3 227. 546 107.95 146.83 765

330.000 9.087 .11005 4,7403 222. 028 25965.6 26790.9 232. 118 109.91 150.36 722

340.000 8.869 .11276 4.3716 195.464 27474.4 28320.1 236.662 111.88 154.14 680

350.000 8.639 .11575 4.0165 170. 373 29018.

9

29887.

0

241. 189 113.86 158.26 638

360. OQO 3.396 .11910 3.6729 146. 747 30601.5 31494.8 245. 710 115.87 162.81 595

370.000 8.137 .12289 3.3365 124,600 32226.1 33147.7 250. 239 118.00 167.98 552

380.000 7.859 .12724 3.0111 103.971 33898.0 34852.4 254. 795 120.39 174.04 508

390.000 7.557 .13234 2.6881 84.943 35627. 2 36619.7 259.403 123.23 181.33 463

400.000 7.224 .13843 2.3671 67. 658 37431.9 38470.1 264. 087 126.46 189.94 418

410.000 6.854 .14590 2.0472 52.338 38 739.

2

39833.4 267. 380 136.30 206.18 369

420.000 6.439 .15531 1.7309 39. 272 40756. 2 41921.0 272.410 135.16 212.44 325

430.000 5.971 .16749 1.4273 28.746 42835.2 44091,4 277. 517 136.45 221 .93 283

440.000 5.446 .18362 1.1527 20.909 44936.

3

46363.5 282. 740 138.33 232.61 245

450.000 4.875 .20512 .9233 15.830 47202.9 48741.3 288.084 14 0.44 242.41 216

460.000 4.302 .23244 .7468 13. 604 49441.5 51184.8 293.454 142.45 244.34 200

470.000 3.798 .26327 .6186 13.626 51616.2 53590.7 298.629 144.20 235.68 195

480.000 3.395 .29459 .5260 14. 799 53678.

8

55888.2 303. 467 145. 76 223.65 197

490 .000 3.081 .32454 .4581 16.660 55631.

9

58066.0 307.958 147.27 212.29 203

500.000 2. 837 .35247 .4071 18, 783 57499.

5

60143.0 312. 154 148.80 203.59 210

520.000 2.483 .40281 .3357 23.074 61076.9 64098.0 319.912 151.98 193.19 224

540.000 2.234 .44757 .2881 27.113 64550.

4

67907.2 327.101 155.29 168.41 237

560.000 2.048 .48839 .2539 30. 862 67990.5 71653.4 333.913 158.68 186.57 249

580.000 1.900 .52633 .2279 34. 359 71433.3 75380.8 34 0. 45 3 162. 09 186.38 260

600.000 1.779 ,56208 .2075 37.646 74899.4 79115.0 346.783 165.49 187.18 270

620.000 1.678 ,59612 .1910 40.758 78400.

8

82871.7 352. 942 168.86 188.58 279

640.000 1.590 .62879 .1773 43. 723 81944.9 86660.8 358. 957 172.18 190. 36 288

660.000 1.514 .66034 .1658 46.564 85535.9 90488.4 364. 846 175.44 192.43 296

680.000 1.447 .69095 .1559 49.299 89176.9 94359.0 370.623 178.64 194.65 304

700.000 1.387 .72078 .1473 51.942 92869.1 98274.9 376.299 18 1.77 196.97 311

144
Table 22. Continued

I-BUTftNE ISOBAR AT P = 80 BAR

T OEN VOL DP/DT OP/CO E H S CV CP M DEG K MOL/L L/MOL BAR/K BAR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

116.782 12.761 .07837 22.3834 1405. 366 228.6 855 .5 110. 241 73.52 99.08 1805

120.000 12.709 .07868 21.7823 1367. 856 545.9 1175.3 112. 941 73.82 99.59 1781

130.000 12.550 .07968 20.0582 1259.9 25 1541.9 2179.4 120.976 74.85 101.21 1711

140.000 12.391 .08070 18.5222 1163. 242 2553.9 3199.6 128.537 76. 01 102.91 1646

150.000 12.232 .0 8176 17.1443 1075.895 3582.

8

4236.8 135. 697 77.29 104. 68 1583

160.000 12.072 .08263 15.9007 996.408 4629.4 5292.1 142. 512 78.68 106.54 1523

170.000 11.912 .08395 14.7723 923.605 5694.7 6366.3 149. 029 80.17 108.47 1466

180.000 11.752 .08509 13.7435 856.539 6779.5 7460.2 155.285 81.73 110.47 1411

190.000 11.592 .08627 12.8016 794. 442 7884.6 8574.7 161. 313 83.37 112.54 1358

200.000 11.430 . 0 8749 11.9357 736. 664 9010.9 9710.8 167. 140 85.08 114.68 1307

210.000 11.267 .08875 11.1369 682. 7 Cl 10159.

2

10869.3 172.788 86.84 116.89 1257

220.000 11.104 .09006 10.3976 632. 108 11330.4 12050.8 173.278 88.64 119.16 1209

230.000 10.938 .09142 9.7111 584.519 12525.

0

13256.4 183. 627 90.49 121.51 1162

240.000 10.771 .09284 9.0718 539.6 c8 13743.9 14486.6 188. 849 92.37 123.92 1116

250.000 10.602 .09432 8.4745 497.182 14987.

8

15742.4 193. 957 94.28 126.41 1070

260.000 10. 430 .09588 7.9151 456.967 16257.3 17024.

3

198.965 96.21 128.97 1026

270.000 10.255 .09751 7.3895 418.811 17553.3 18333.3 203.862 98.15 131.62 982

280.000 10.077 .09923 6.8945 382.568 18876.

3

19670.1 208. 718 10 0. 10 134. 36 939

290.000 9.895 .10106 6.4268 348. 125 20227.1 21035.6 213.482 102.06 137.21 897

300.000 9.70 8 .10301 5.9839 315. 385 21606.5 22430.6 218. 183 104.02 140.17 855

310.000 9.515 .10510 5.5632 284.279 23015.3 23856.1 222.829 105.99 143.27 813

320.000 9.316 .10734 5.1625 254. 747 24454.6 25313.

3

227.429 107.95 146.53 771

330.000 9.109 .10978 4.7796 226. 746 25925.

4

26803.6 231.990 109.91 149.98 729

340.000 8.894 .11244 4.4125 200.244 27429. 0 28328.

5

236. 521 111.88 153.67 687

350.000 8.668 .11537 4. 0595 175.222 28967.3 29890.2 241. 033 113.86 157.67 646

360.000 8.430 .11863 3.7184 151.675 30542.2 31491.2 245.535 115.87 162.05 604

370.000 8.177 .12230 3.3873 129.618 32157.1 33135.5 250. 040 118.00 166.99 561

380.000 7.906 .12649 3. 0641 109.089 33816.7 34828.6 254.566 120.39 172 .72 518

390.000 7. 614 .13134 2.7468 90. 170 35529.

7

36580.4 259. 133 123.23 179.52 475

400.000 7.295 .13708 2.4333 72.992 37312.8 38409.5 263. 763 126.45 187.42 431

410.000 6.945 .14399 2.1231 57. 750 38590.9 39742.8 266.982 136.27 202.62 384

420.000 6.558 .15248 1.8185 44.686 40567.6 41787.5 271. 909 135.10 207.36 343

430.000 6.130 .16313 1.5266 34.0 C7 42592.

2

43697.2 276. 873 136.32 214.74 303

440.000 5.661 .17665 1.2599 25.781 44670.7 46083.8 28 1.900 138.13 222.66 267

450.000 5.156 .19393 1.0311 19.936 46798.5 48350.0 286.993 140.18 230.44 237

460.000 4.637 .21565 . 8468 16. 475 48958.1 50683.3 292. 121 142.26 235. 36 216

470.000 4.146 . 24121 .7057 15.3 C7 51102.6 53032.3 297. 173 144.18 233.14 206

480.000 3.724 .26855 .6004 15.7 C7 53178.5 55326.9 302.004 145.91 225.35 204

490.000 3. 380 .29589 .5213 16.950 55168.1 57535.2 306.558 147.52 216.29 206

500.000 3.104 .32215 .4610 18.728 57077.8 59655.0 31 0. 841 149.09 207.96 211

520 .000 2.701 .37027 . 3767 22. 791 60727.

3

63689.5 318. 755 152.28 196.67 225

540.000 2.420 .41326 .3209 26.813 64253.0 67559.0 326. 058 155.57 191.00 23 7 560.000 2.210 .45243 .2812 30.6 CO 67731 .

0

71350.5 332.952 158.93 188.55 249

580.000 2.046 .48877 .2514 34.150 71203.0 75113.1 339. 554 162. 31 187.95 260

600.000 1.912 .52295 .2281 37. 490 74691.9 78875.5 345.932 165.68 188.45 270

620.000 1.800 . 55544 .2093 40 .654 78211.7 82655-3 352. 129 169.03 189.64 200

640.000 1. 705 .58658 . 1938 43. 667 81771.

0

86463.7 358.175 172.32 191.27 268

660.000 1.622 .61660 .1808 46.552 85375.1 90307.9 364. 089 175.57 193.19 296

680.000 1.549 .64571 .1697 49.328 89027.

1

94192.7 369.888 178.75 195.31 304

700.000 1.484 .67404 . 1602 52. 0 10 92728.

7

98121.0 375. 581 181.86 197.55 311

145
Table 22. Continued

I-BUTANE ISC8AR AT P = 90 BAR

T DEN VOL OP/DT DP/DD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/HOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

117.155 12. 762 .07836 22.3966 1411.538 254.3 959.5 110.460 73.55 99.11 1809

120.000 12.717 .07864 21.8656 1378.344 534.5 1242.2 112.843 73.82 99.56 1788

130.000 12.558 .07963 20.1385 1270.068 1529.2 2245.9 120. 875 74.85 101.17 1718

140.000 12.400 .08065 16.6000 1173.086 2539.9 3265.8 128.434 76.01 102.87 1652

150.000 12.241 .08169 17.2199 1085.500 3567.4 4302,6 135.591 77.30 104.64 1590

160.000 12.082 .08277 15.9745 1 0 05 . 8 16 4612.5 5357.4 142.403 78.68 106.49 1530

170.000 11.923 .08387 14.8445 932. 852 5676.

2

6431.1 148.917 80.17 108.41 1473

180.000 11. 764 .08501 13.8145 865.657 6759.3 75 24.4 155. 169 81.73 110.41 1413

190.000 11.604 .08618 12.8714 803.457 7862.7 8638.3 161.194 83.37 112.47 1365

200.000 11.443 .08739 12.0047 745.602 8987.1 9773.6 167. 016 85.08 114.60 1314

210.000 11.282 .08864 11.2053 691.582 10133.4 10931.1 172.660 86,84 116.79 1265

220.000 11.119 .08993 10.4655 640. 952 11302.2 12111.6 178. 145 88.64 119.05 1216

230.000 10.955 .09128 9.7787 593.343 12494.

4

13316.0 183.488 90.49 121.38 1170

240.000 10.790 .09268 9.1392 548.450 13710.7 14544.

8

188. 705 92.37 123.77 1124

250.000 10.622 .09415 8.5421 506.0 16 14951.6 15796.9 193. 807 94.28 126.23 1079

260.000 1 0 . 45 2 .09568 7.9829 465.827 16217.9 17079.0 198.807 96.21 128.77 1035

270.000 10.279 .09729 7.4578 427. 709 17510.

2

18385.8 203. 715 98.15 131.38 992

280.000 10.103 .09898 6.9635 391.516 18829.2 19720.0 208.542 100.10 134.08 949

290.000 9.923 .10077 6.4968 357.134 20175.4 21082.4 213. 295 102. 06 136.87 907

300.000 9.739 .10268 6.0552 324.467 21549.6 22473.7 217.984 104.03 139.77 866

310.000 9.55 0 .10472 5.6360 293.439 22952.

4

23894.

9

222.616 105.99 142.79 824

320.000 9.354 .10690 5.2372 263.997 24384.7 25346.8 227,198 107.95 145.95 783

330.000 9.15 3 .10926 4. 8567 236.095 25847.

4

26830.

7

231. 740 109.91 149.27 742

340.000 8.943 .11182 4.4927 209.703 27341.4 28347.8 236, 248 111.88 152.80 701

350.000 8.724 .11463 4.1432 184. 8 03 28868.

0

29899.7 240. 731 113.86 156.59 661

360.000 8.494 .11773 3.8067 161. 390 30428. 9 31488.5 245. 199 115.88 160.68 620

370.000 8.251 .12120 3.4613 139.478 32026. 4 33117.2 249.662 118.00 165.23 579

380.000 7.994 .12510 3.1654 119.1 07 33664.3 34790.2 254. 134 120.40 170.42 538

390.000 7.719 .12956 2.8574 100.349 35349.5 36515.5 258.632 123.22 176.48 497

400.000 7.423 .13471 2.5560 83. 315 37097. 0 38309.4 263. 173 126.44 183.36 455

410.000 7.104 . 14076 2.2609 68.162 36328.5 39595.4 266.276 136.24 197.16 411

420.000 6.759 .14795 1.9737 55. 063 40245.

2

41576.7 271. 050 135.02 200.06 374

430.000 6.387 .15656 1.6993 44.147 42193.

1

43602,2 275.816 136.17 205.11 338

440.000 5.990 .16693 1.4455 35,4 09 44176.

5

45679.0 280. 590 137.86 210.22 304

450.000 5.573 .17944 1.2208 28.685 46190.7 47805.6 285. 369 139.81 215.09 275

460.000 5.142 .19446 1,0304 23.787 48229.

1

49979.

3

290. 147 141.86 219.51 251

470.000 4. 712 .21221 .8746 20.660 50280,4 52190.3 294.902 143.91 222.28 234

480.000 4.304 .23235 .7503 19.255 52321.9 54413.1 299.582 145.87 221.63 224

490.000 3.939 .25390 .6526 19. 222 54326.5 56611.6 304. 115 147.69 217.68 220

500.000 3. 625 .27585 .5756 19.998 56279.

9

58762.5 308.461 149.42 212.46 221

520.000 3.140 .31850 .4651 22.954 60041.1 62907.6 316.591 152.74 202.45 228

540.000 2.795 .35783 .3916 26.661 63663.3 66883.8 324. 095 156.04 195.81 239

560.000 2.539 .39393 .3398 30.406 67215.

7

70761.0 331.146 159.36 192.35 251

580.000 2.340 .42741 .3013 34.0 02 70745.

0

74591.6 337. 867 162.70 190.99 262

600.000 2.179 .45884 .2716 37.417 74279.

3

78408.

9

344. 338 166.03 190.92 272

620.000 2.046 ,48865 .2479 40.663 77836.

1

82233.9 350.609 169.33 191.69 281

640.000 1.934 .51715 .2285 43.758 81425,8 86080.2 356. 715 172.59 193.01 290

660.000 1.836 .54457 .2123 46. 721 85055.4 89956.6 362.679 175. 81 194,69 298

680.000 1.751 .5711

0

.1986 49.569 68729.

1

93869.0 368.519 178.96 196.61 306

700.000 1.675 .59688 . 1868 52. 319 92449.8 97821.7 374.248 182.05 198.68 313

146
Table 22. Continued

I-BUTANE ISOBAR AT P = 100 BAR

T OEN VOL DP/OT DP/CO E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/HOL J/MOL/K J/MOL/K J/MOL/K M/SEC

117.523 12.763 .07835 22.4108 1417. 774 279. 4 1062.9 110. 673 73.59 99.14 1812

120.000 12. 724 .07859 21.9487 1388. 8 34 523. 1 1309.1 112. 745 73.82 99.53 1794

130.000 12.566 .07958 20.2185 128 0. 2 Cl 1516.7 2312.5 120. 774 74.85 101.14 1725

lt*0. 000 12.408 .08059 18.6775 1182.9 28 2526.

1

3332.0 128.331 76.01 102.83 1659

150.000 12.250 .08163 17.2953 1095.100 3552.2 4368.5 135.486 77.30 104.60 1596

160.000 12.092 . 0 8270 16.0480 1015. 217 4595.8 5422.8 142. 295 78.68 106.44 1537

170.000 11.934 .08379 14.9165 942.090 5658.

0

6495.9 148.805 8 C.17 108.36 1480

180.000 11.775 .08492 13. 8851 874.763 6739.4 7588.

7

155. 055 81.73 110.34 1425

190.000 11.616 .08609 12.9410 812.457 7841.0 8701.9 161.075 83.37 112.40 1372

200.000 11.457 .08728 12.0734 754.522 8963.6 9836.4 166. 894 85.08 114.51 1321

210.000 11.296 .08852 11.2733 70 0. 442 10107.8 10993.

1

172. 534 86.84 116.70 1272

220.000 11.135 .08981 10.5329 649.771 11274.

5

12172.6 178. 014 88.65 118.94 _224

230.000 10.972 .09114 9.8458 602. 140 12464.

3

13375.8 183. 352 9 0.49 12 1.25 1178

240.000 10.308 .09253 9.2062 557.239 13678.

0

14603.3 188.562 92.37 123.62 1132

250.000 10.641 .09397 8.6090 514. 812 14916.1 15855.8 193. 658 94.28 126.06 1088

260.000 10.473 .09548 8.050 0 474.645 16179.3 17134.1 198. 651 96.21 12 6.57 1044

270.000 10.302 .09707 7.5253 436.559 17468.1 18438.8 203. 552 98.15 131.15 1001

230.000 10.123 .09873 7.0316 400.4 11 18783. 2 19770.5 208.369 100.11 133.81 959

290.000 9.951 .10049 6.5658 366.081 20125.

0

21130.0 213.112 102.07 1 36.55 917

300.000 9.769 .10236 6.1253 333.477 21494.

2

22517.9 217.789 104.03 139.39 876

310.000 9.583 .10435 5.7076 302.520 22891.4 23934.9 222.408 105.99 142.34 836

320.000 9.392 .10648 5.3105 273. 156 24317.2 25382.0 226.975 107.95 145.41 795

330.000 9.194 .10877 4.9321 245.340 25772.

3

26860.

0

231. 493 109.92 148.63 755

340.000 8.989 .11124 4.5707 219. 041 27257.5 28369.9 235.985 111.88 152.01 715

350.000 9. 776 .11394 4.2244 194.240 28773.6 29913.1 240. 443 113.87 155.61 675

360.000 8.554 .11691 3. 8917 170.934 30322.

0

31491.1 244. 88 0 115.88 159.47 636

370.000 8.320 .12019 3.5711 149. 1 34 31904.

3

33106.2 249. 306 118.01 163.71 596

380.000 8.074 .12385 3.2612 126.876 33523.5 34762.0 253. 732 120.40 168.50 557

390.000 7. 814 .12798 2.9606 110. 223 35185.

8

36465.6 258. 174 123.22 174.02 517

400.000 7.537 .13269 2.6684 93.271 36904.

5

38231.4 262. 644 126.43 180.20 478

410.000 7.241 . 13810 2.3845 78.144 36 100.5 39481.5 265.658 136.22 193.11 436

420.000 6.926 .14438 2.1099 64.976 39973.4 41417.2 270. 323 134.98 194.96 401

430.000 6. 592 .15170 1.8480 53. 855 41868.

9

43385.9 274.955 136.08 198.83 367

440.000 6.241 . 16023 1.6040 44.756 43791.2 45393.6 279. 570 137.71 202.65 336

450.000 5. 877 .17016 1.3841 37. 5 10 45736.1 47437.7 284. 164 139.58 206.13 308

460.000 5.505 .18166 1.1924 31 . 868 47696.4 49515.0 288. 730 141.58 209.31 284

470.000 5.131 .19491 1.0300 27.650 49673. 6 51622.7 293. 262 143.62 212. 12 265

480.000 4. 76 3 . 20995 . 8949 24. 8 C9 51654.6 53754.1 297. 750 145.65 213.94 250

490 .000 4.414 .22653 .7839 23. 3 15 53629.

3

55895.1 302.164 147.60 213.91 241

500.000 4.094 .24426 .6935 22.978 55582.9 58025.6 306.469 149.47 211.92 236

520.000 3.564 .28056 .5595 24. 400 59395.5 62201.1 314. 658 152.99 205.51 237

540 .000 3.166 .31581 .4679 27. 275 63091.

3

66249.

4

322. 298 156. 36 199.60 244

560.000 2.866 .34889 .4030 30.716 66710.2 70199.1 329.481 159.70 195. 74 254

580.000 2.633 .37978 .3550 34.2 32 70294.0 74091.8 336. 311 163.02 193.81 264

600.000 2.446 .40833 .3181 37.657 73872.4 77960.7 342.869 166.32 193 .*2 7 274

620 .000 2.292 .43636 .2889 40.947 77465.1 81828.8 349. 211 169.60 193. 67 283

640.000 2.161 .46266 . 2652 44.098 81084.7 85711.3 355.375 172.83 194.68 292

660.000 2.050 .48792 . 2456 47. 122 84 73 9.7 89618.9 361. 387 1 76.02 196. 13 300

680.000 1.952 .51233 .2290 5 0.031 88434.8 93558.1 367. 267 1 79. 15 197.86 308

700.000 1.866 .53601 .2148 52.838 92174.1 97534.3 373. 029 182.22 199.78 315

147
Table 22. Continued

I-BUTANE ISOBAR AT P = 110 BAR

T DEN VOL DP/DT DP/00 E H S CV CP W OEG K MOL/L L/MOL 3AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

117.885 12.764 .07834 22.4260 1424.071 304.0 1165.7 110. 881 73.62 99. 17 1816

120.000 12.731 .07855 22.0315 1399. 3 19 511.9 1376.0 112.647 73.82 99.50 1801

130.000 12.574 .07953 20.2983 1290.335 1504.2 2379.1 120.675 74.85 101.11 1731

140.000 12.416 .08054 18. 7547 1192. 767 2512.

3

3398.2 128.229 76.02 102.79 1665

150.000 12.259 .08157 17.3704 1104.695 3537.0 4434.3 135. 381 77.30 104.56 1603

160.000 12.102 .08263 16.1212 1024.611 4579.3 5488.2 142. 187 78.69 106.40 1543

170.000 11.944 .08372 14.9881 951.319 5639.9 6560.9 148.694 80.17 100.31 1486

180.000 11.787 .08484 13.9554 883.857 6719.8 7653.0 154. 940 81.73 110.28 1432

190.000 11.629 .08599 13. 0102 821. 443 7819.

7

8765.6 160. 958 83. 37 112.33 1379

200.000 11.470 . 08718 12.1416 763.425 8940.4 9899.4 166.773 85.08 114.43 1329

210.000 11.310 .08841 11.3408 709.282 10082.6 11055.2 172. 408 86.84 116.61 1230

220.000 11.150 .08969 10.5999 656.568 11247. 2 12233.7 177.884 88.65 118.84 1232

230.000 10.988 .09100 9.9124 610.909 12434. 7 13435.8 183.217 90.49 121.13 1186

240.000 10.825 .09237 9. 2726 565.998 13645.9 14662.0 188.422 92.38 123.49 1140

250.000 10.661 .09330 8.6754 523.574 14881.2 15913.0 193.511 94.28 125.90 1096

260.000 10.494 .09529 8.1165 403.422 16141.4 17189.6 198.497 96.21 128.38 1053

270.000 10.325 .09685 7.5922 445. 364 17426.

8

18492.

2

203. 390 98. 15 130.93 1011

280.000 10.153 .09849 7.0990 409.253 18738.2 19821.6 208. 199 10 0.11 133.56 969

290.000 9.97 8 .10022 6.6340 374. 970 20075.8 21178.3 212.933 102.07 136.26 928

300.000 9.799 .10205 6.1944 342. 421 21440.4 22562.9 217.599 104.03 139.04 807

310.000 9.616 .10400 5.7779 311.528 22832.2 23976.2 222. 205 105.99 141.92 847

320.000 9.428 .10607 5.3824 282. 230 24251.9 25418.7 226. 757 107.96 144.91 007

330.000 9.234 .10829 5.0059 254.487 25700. 0 26891.

2

231. 264 109.92 148.03 767

340.000 9.034 .11069 4 . 6467 228. 266 27177.

0

28394.6 235. 731 111.89 151.29 728

350.000 8.827 .11329 4.3032 203.548 28683.6 29929.8 240. 166 113.87 154,74 609

360.000 8.611 .11613 3. 9739 180.327 30220.

7

31498.1 244. 576 115.88 158.40 651

370.000 8. 385 .11925 3.6573 158.612 31789.5 3 3101.3 248. 969 118.01 162.39 612

380.000 8. 149 . 12271 3.3523 138.435 33392.6 34742.4 253.356 120.40 166.85 574

390.000 7.901 .12657 3.0578 119.849 35035.2 36427.5 257. 750 123.23 171 .97 536

400.000 7.638 .13092 2.7729 102.935 36730.

3

38170.4 262.162 126. 43 177,64 498

410.000 7. 362 .13584 2.4975 87. 796 37897.

8

39392.0 265. 106 136.21 189.96 458

420.000 7.070 .14145 2.2324 74.536 39737.

0

41292.9 269.686 134.95 191.14 426

430.000 6.763 . 14786 1.9799 63. 221 41593.

4

43219.9 274. 221 136.03 194.32 394

440.000 6.444 .15516 1.7437 53.8 24 43472.1 45179.

1

278. 725 137.61 197.47 364

450.000 6.116 .16349 • 1.5282 46. 189 45369.

5

47168.0 293. 194 139. 43 200.25 337

460.000 5.784 .17289 1.3369 40.070 47281.2 49133.0 287. 623 14 1.38 202.71 314

470.000 5.450 .18347 1.1710 35.228 49203. 4 51221.6 292. 007 143.40 204.98 294

480.000 5.121 .19529 1.0296 31.523 51133.5 53281.7 296.344 145.42 206.99 277

490 .000 4.799 .20836 .9102 28.927 53067.

2

55359.2 30 0. 628 147.42 208.36 265

500.000 4.494 . 22254 .8101 27.419 54997.2 57445.1 304. 842 149.37 208.64 256

520.000 3.954 .25269 .6564 27. 112 58814.

4

61596.2 312. 983 153.07 205.92 250

540.000 3.524 .28378 .5462 20. 875 62551.7 65673.3 320.677 156.56 201.82 253

560.000 3.188 .31372 .4700 31.669 66222.

6

69673.5 327.952 159.94 198.40 259

580.000 2.923 .34215 .4120 34. 9 05 69854.4 73618.0 334. 873 163.27 196.29 266

600.000 2.710 .36904 .3674 30.231 73473.

8

77533.2 341. 510 166.57 195.43 277

620.000 2.534 .39457 .3323 41.5 05 77101.0 81441.3 347.917 169.83 195.51 236

640.000 2.387 .41897 .3039 44.678 80749.5 85358.2 354. 135 173.05 196.27 295

660.000 2.260 .44239 .2805 47. 739 84428.

8

89295.2 36 0. 19 2 176.21 197.50 303

680 .000 2.151 .46501 .2608 50.693 88145.1 93260.2 366. Ill 179.33 199.06 311

700.000 2.054 .43693 .2440 53.546 91902.6 97258.0 371.906 102.38 200.84 318

148
Table 22. Continued

I-BUTANE ISOBAR AT P = 120 BAR

T DEN VOL DP/OT OP/CO E H S CV CP M DEG K MOL/L L/MOL 3AR/K BAR-L/MCL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

118.241 12.766 . 07833 22.4420 1430.4 26 328. 0 1268.0 111.084 73.65 99.20 1820

120.000 12.733 .07850 22.1141 1409.824 500.8 1442.9 112.551 73.82 99.47 1807

130.000 12.531 .07948 20.3778 130C. 470 1491.9 2445.7 120.575 74.85 101.08 1738

140.000 12.425 .08040 18.8317 1202.604 2498.

7

3464.5 128.127 76.02 102.76 1672

150.000 12.268 .08151 17.4452 1114.286 3522.1 4500.2 135.276 77.30 104.52 1610

160.000 12.112 . 0 8257 16.1942 1033.999 4562.

9

5553.7 142. 080 76.69 106. 35 1550

170.000 11.955 .08365 15.0595 960.5 39 5622.1 6625.8 148. 584 80.17 108.25 1493

180.000 11.798 .08476 14.0254 892.940 6700.3 7717.4 154.327 01.74 110.22 1439

190.000 11.641 .03591 13.0791 8 30.415 7798.5 0829.4 160.341 83.30 112.26 1386

200.000 11.483 .08709 12.2096 772. 311 8917. 4 9962.4 166. 652 85.00 114.36 1336

210.000 11. 324 .08830 11.4080 718.103 10057.8 11117.4 172.284 86.04 116.52 1287

220.000 11.165 .03956 10.6665 667. 341 11220.

2

12295.0 177. 755 80.65 110.74 1240

230.000 11.005 . 09007 9.9786 619.653 12405.5 13496.0 183.083 90.50 121.01 1193

240.000 10.843 .09223 9.3385 574. 727 13614.

2

14720 .9 188. 283 92.3 8 123.35 1149

250.000 10.680 .09364 0.7412 532. 3 02 14846.

9

15970.5 193. 366 94.20 125.75 1105

260.000 10.514 .09511 8.1024 492.161 16104.1 17245.4 198. 346 96.21 128.21 1062

270.000 10.347 .09665 7.6584 454.125 17386.4 18546.1 203.232 98.16 130.73 1020

280.000 10.177 .09826 7.1656 418.047 18694.1 19873.3 200.032 10 0.11 133.31 978

290.000 10.004 .09996 6.7012 383. 0 04 20027.

8

21227.

3

212. 757 102. 07 135.97 937

30C . 000 9.828 . 10175 6.2625 351.3 C2 21387.9 22608.9 217. 412 104.03 130.71 097

310 .000 9.647 .10365 5.0472 320.463 22774.7 24018.5 222. 006 106.00 141.53 358

320.000 9.463 .10568 5.4530 291.224 24188.6 25456.8 226.546 107.96 144.45 818

330.000 9.273 .10784 5.0782 263.545 25630.1 26924.

3

231.037 109.92 147.48 779

340.000 9.077 .11017 4.7210 237. 390 27099.

6

20421.6 235.486 111.09 150.64 741

350.000 8.875 .11268 4.3799 212.739 28597.

4

29949.6 239. 900 113.87 153.95 703

360.000 8.665 .11541 4.0535 189.585 30124.3 31509.2 244. 285 115.09 157.44 665

370.000 3.447 .11839 3.7404 167.935 31681.

1

33101.7 248. 649 118.02 161.22 628

380.000 8.219 .12167 3. 4396 147. 0 13 33269.9 34729.9 253. 002 120.41 165.43 591

390.000 7.981 .12530 3.1500 129. 266 34895.7 36399.3 257. 355 123.23 170.23 554

400.000 7.731 .12934 2.8710 112.362 36570.

8

38122.9 261. 718 126.43 175.52 513

410.000 7.470 .13387 2.6023 97.184 37714.8 39321.3 264.604 136.21 107.41 479

420.000 7.196 .13897 2.3446 83. 017 39526. 8 41194.4 269. 118 134.94 188.13 448

430 .000 6.911 .14470 2.0994 72. 314 41 352.6 43089.0 273.576 136.00 190.87 417

440.000 6.616 . 15114 1 . 8694 62.648 43 198. 0 45011 .

7

277. 996 137.56 193.63 389

450.000 6.315 .15335 1.6579 54.687 45060.2 46960.4 282.376 139.34 196.05 363

460.000 6.011 .16636 1.4676 40.202 46935.

2

48931 .6 286. 708 141.25 198.14 341

470.000 5. 707 .17522 1.2999 42. 940 40319.8 50922.4 290.939 143.23 200.01 321

480.000 5.406 .18496 1.1544 38.7 C6 50711.9 52931.4 295. 219 145.24 201.78 304

490.000 5.112 .19563 1.0293 35.405 52609.8 54957.3 299. 396 147.25 203.36 290

500.000 4.826 .20720 .9223 33.020 54510.9 56997.2 303.517 149.23 204.53 279

520.000 4.301 .23252 . 7532 30. 8 f9 58304.1 61094.4 311. 552 153.04 204.68 266

540.000 3. 856 .25931 .6303 31.453 62056.5 65168.3 319.240 156.64 202.51 264

560.000 3.496 .28608 .5398 33. 4 C3 65760.

7

69193.6 326.560 160.10 200.08 267

580.000 3.205 .31204 .4717 36.123 69430.8 73175.3 333.547 163.46 198.24 274

600.000 2. 96 8 .33689 .4192 39.195 73086.5 77129.2 340.249 166.77 197.30 282

620.000 2. 773 . 36062 . 3778 42. 362 76745.4 81072.8 346. 715 170.02 197.19 290

640.000 2.609 .33333 .3445 45. 502 00421.

3

85021.2 352. 933 173.23 197.75 298

660. 000 2.463 .40516 .3170 48.568 84124.

1

38936.0 359.033 176.39 198.80 306

630.000 2.346 .42622 .2940 51.545 87860.

0

929 75.5 365.038 179.48 200.20 314

700.000 2.239 .44664 . 2745 54.430 91635.9 96995.6 370. 864 182.52 201.85 321

149
Table 22. Continued

^ I-BUTANE ISCBAR AT P = 130 BAR

T DEN VOL DP/DT DP/DD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

118.592 12.767 . 07833 22.4588 1436. 838 351. 6 1 369.8 111.282 73.69 99.23 1824

120.000 12.745 .07846 22.1965 1420. 324 489.8 1509.8 112.454 73.82 99.45 1814

130.000 12.589 .07943 20.4572 1310.606 1479. 7 2512.3 120.477 74.85 101.05 1744

140.000 12.433 .08043 18.9064 1212.440 2485.2 3530.8 128. 026 76.02 102.72 1678

150.000 12.277 .08145 17.5197 1123. 874 3507.3 4566.1 135. 173 77.30 104.48 1616

160.000 12.121 . 08250 16.2668 1043. 3P0 4546.

7

5619.2 141.974 78.69 106.31 1557

170.000 11.965 .08358 15.1305 969.750 5604.

4

6690.9 148. 475 8 0.17 10 8.20 1500

180.000 11.809 .08468 14.0951 902. 0 12 6681.1 7781.

9

154. 715 81.74 110.17 1446

190.000 11.653 .08582 13.1476 839.374 7777.6 8693.2 160. 725 83.38 112.19 1393

200.000 11.496 .08699 12.2772 781.189 8894.7 10025.6 166.533 85.08 114.28 1343

210.000 11.339 .08820 11.4748 7 26.9 C5 10033.2 11179.8 172. 160 86.84 116. 43 1294

220.000 11.180 .08945 10. 7327 676.0 93 11193.

6

12356.4 177. 627 88.65 118.64 1247

230. 000 11.021 .09074 10.0443 628.371 12376.7 13556.3 182. 951 9 C.50 120.90 1201

240.000 10.860 .09208 9.4039 583. 426 13583. 1 14780.1 188.145 92.38 123.22 1157

250.000 10.698 .09347 8.8065 540.997 14813.2 16026.3 193. 223 94.29 125.60 1113

260.000 10.535 .09493 8.2478 500.863 16067.6 17301.6 198.197 96.21 128. 03 1070

270 .000 10.369 .09644 7.7239 462. 845 17346.

7

18600.5 203. 075 98.16 130.53 1029

280.000 10.201 .09803 7.2315 426. 793 18651.0 19925.4 207.868 100.11 133.08 987

290.000 10.030 .09970 6.7677 392.566 19980.9 21277.0 212. 584 102.07 135.70 947

300.000 9.856 .10146 6.3298 360.1 24 21336.7 22655.7 217. 230 104. 04 138.40 907

310.000 9.678 .10333 5.9154 329. 332 22718.

7

24061.9 221.813 106.00 141.16 863

320.000 9.496 .10530 5.5225 300.146 24127.2 25496.2 226. 339 107.96 144. 02 829

330.000 9.310 .10741 5. 1491 272.5 18 25562.6 26959.0 230.816 109.93 146.97 791

340.000 9.118 .10967 4.7937 246.418 27 025.

0

28450.7 235.243 111.89 150.03 753

350.000 8.921 .11210 4. 454 7 221. 823 28514.

8

29972.1 239. 643 113.88 153.23 716

360.000 8.716 .11473 4.1308 196.721 30032.3 31523.8 244. 006 115.89 156.58 679

370.000 3.505 .11758 3.6207 177. 119 31578.3 33106.9 248. 344 118.02 160.18 643

380.000 8.285 .12070 3.5234 157.034 33154.5 34723.6 252.666 120.41 164.18 606

390.000 8.056 .12414 3.2380 13 8.5 C6 34 765. 5 36379 .2 256.984 123.23 168.73 571

400.000 7, 817 .12793 2.9638 121.5 69 36423.4 38086.

4

261. 305 126.43 173.73 536

410.000 7.563 .13213 2.7006 106.356 37547.5 39265.2 264. 143 136.20 185.29 498

420.000 7.309 .13681 2.4487 92. 874 39336.9 41115.5 268.602 134.93 185.69 468

430.000 7.041 .14202 2.2094 81.185 41138.0 42984.2 272.999 135.98 188.13 439

440.000 6. 766 .14780 1.9844 71.269 42 956. 7 44878.1 277.353 137.52 190.63 412

450.000 6.465 . 15420 1.7763 63. 0 12 44 791.

3

46795.8 281.663 139.28 192.85 367

460.000 6.203 .16121 1. 5673 56. 212 46638.

2

48734.

0

285. 923 141.16 194.75 365

470.000 5.921 . 16888 1.4166 50.6 23 48494.5 50639.9 290.129 143.12 196.40 345

480.000 5.643 .17721 1.2703 46. 0 24 50358. 0 52661.7 294. 280 145.10 197.95 328

490.000 5. 370 .18622 1.1410 42.268 52227.

8

54648.

7

298.377 147.10 199.44 313

500.000 5.104 .19593 1.0290 39.294 54103.0 56650.0 302.420 149.09 200.81 301

520.000 4,602 .21728 .8481 35.660 57861.2 60685.9 310. 335 152.96 202.48 284

540.000 4.159 .24045 .7128 34.837 61609.6 64735.4 317.976 156.65 202.18 278

560.000 3. 785 .26422 .6110 35.914 65331,

0

68765.

9

325. 306 160.18 200.82 278

580.000 3.475 .28776 .5333 37.975 69028.1 72769.0 332.330 163.59 199.57 282

600.000 3.219 .31064 . 4730 40. 626 72713. 3 76751.6 339.081 166.92 198.80 288

620.000 3.006 .33267 .4252 43.565 76400.2 80725.0 345.595 170.18 198.65 295

640.000 2.826 .35386 . 3866 46.596 80101.3 84701 .

5

351. 908 173.39 199,09 303

660.000 2. 672 .37426 .3549 49.6 19 83826.

3

88691.6 358.047 176.53 200.00 310

680.000 2.538 .39396 . 3264 52.587 87582.

3

92703.8 364. 035 179.62 201.27 318

700.000 2.421 .41306 .3060 55.4 83 91374.4 96744.1 369. 391 182.65 202.81 325

150
Table 22. Continued

I-3UTANE ISOBAR AT P = 140 BAR

T OEN VOL OP/DT OP/CO E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

118.938 12. 769 .07832 22.4764 1443. 3 C4 374.7 1471.

1

111. 475 73.72 99.26 1828

120.000 12. 752 .07842 22.2786 1430.827 478.8 1576.7 112. 358 73.82 99.42 1820

130.000 12.597 .07939 20. 5362 1320.743 1467.5 25 78 .9 120.378 74.85 101.02 1751

140.000 12.441 .08038 18.9850 1222.286 2471.8 3597.1 127.925 76.02 102.69 1685

150.000 12.286 . 0 8139 17.5940 1133. 457 3492.6 4632.1 135. 070 77.30 104. 44 1623

160.000 12.131 .08243 16.3392 1052.755 4530.7 5634.8 141.868 78.69 106.26 1563

170.000 11.976 .08350 15.2013 978.953 5586.9 6755.9 148. 366 80.17 106.15 1507

180.000 11.820 .08460 14.1645 911.073 6662.

1

7846.5 154.603 81.74 110.11 1453

190.000 11.665 .08573 13.2158 848. 320 7757. 0 8957.2 160 . 61 0 83.38 112.13 1400

200.000 11.509 . 0 8689 12.3444 790. 042 8872.3 10038.8 166.414 85.08 114.21 1350

210.000 11.352 .08809 11.5412 735.688 10009.

0

11242.2 172.038 86.84 116.35 1302

220.000 11.195 .08933 10.7985 684. 823 11167. 4 12418.0 177.501 88.65 118.54 1255

230.000 11.037 .09061 10.1096 6 37. 0 65 12348.

4

13616.9 182.820 90.50 120.79 1209

240.000 10.877 .09193 9.4689 592. 099 13552.4 14839.5 188. 009 92.38 123.10 1165

250 .000 10.717 .09331 8.8713 549.660 14780.

0

16086.4 193.082 94.29 125.46 1121

260.000 10. 554 .09475 8.3125 509.530 16031.6 1 7358.1 198.049 96.22 127.87 1079

270.000 10.390 .09624 7.7888 471.525 17307.8 18655.2 202.921 98.16 130.34 1037

280.000 10.224 .09781 7.2967 435.495 18608.8 19978.1 207. 707 100.11 132. 86 997

290.000 10. 055 .09945 6.8334 4C1. 317 19935.

0

21327.3 212. 414 1 02 . 07 135.45 957

300.000 9.383 .10118 6.3961 368.891 21286. 7 22703.2 217. 050 104.04 138.10 917

310.000 9.708 . 10301 5.9826 338.138 22664.2 24106.3 221.623 106.00 140.82 879

320.000 9.529 .10494 5.5908 308.996 24067.6 25536.

8

226.138 107.97 143.61 640

330.000 9.346 .10700 5. 2187 281.4 15 25497.

2

26995.2 230.601 109.93 146.49 803

340.000 9.158 .10919 4.6649 255.359 26953.1 28481.8 235.018 111.90 149.47 766. 350.000 3.965 .11155 4.5278 230. 808 28435.4 29997.1 239. 395 113.88 152.56 729

360.000 8. 766 .11408 4.2060 207.748 29944.

4

31541.5 243.738 115.90 155.79 693

370.000 8.560 .11683 3.8985 186.179 31480.

5

33116.0 248.052 118.03 159.25 657

380 .000 3.347 .11931 3. 6042 166. 1 16 33045.

3

34722.6 252. 347 120.42 163.07 622

390.000 8. 126 .12307 3.3223 147.5 90 34643.

3

36366.2 256. 633 123.24 167.41 587

400.000 7.896 .12664 3.0521 130.6 48 36286.

1

38059.1 260.919 126.44 172.18 553

410.000 7.658 .13058 2.7934 115.347 37393.

2

39221.2 263. 716 136.21 183.50 517

420 .000 7. 412 . 1 3491 2.5463 101.744 39163.

5

41052.

3

268. 128 134.93 183.64 488

430.000 7.158 .13970 2.3117 89.874 40943.6 42899.4 272. 474 135.97 185.86 459

440 .000 6.893 .14496 2.0909 79.7 21 42740.4 44769.9 276. 774 137.50 188. 20 433

450.000 6.634 . 15073 1.8857 71.187 44552.5 46662.7 281. 028 139.24 190.31 409

460.000 6.369 .15700 1.6980 64. 098 46376.

9

48575.0 285. 231 141.10 192.11 387

470.000 6.105 .16379 1.5289 58.224 48210.8 50503.9 289.379 143.03 193.65 368

430 .000 5.845 .17109 1.3785 53.337 50 052. 3 52447.6 293.471 145.00 195.06 351

490.000 5.589 .17892 1.2461 49.261 51900.1 5 44 05.0 297.507 146.99 196.43 336

500.000 5.339 .18729 1.1301 45.891 53754.

0

56376.1 301 . 490 148.97 197.78 323

520.000 4.864 .20561 .9399 41. 154 57477. 2 60355.8 309.294 152.87 200.06 304

540.000 4.430 .22571 .7944 39. 025 61209.

8

64369.8 316.868 156.62 201. 10 293

560.000 4.052 .24679 .6826 39.062 64936.

0

68391.

1

324. 181 160.21 200.89 290

530.000 3.731 .26806 .5961 4 0. 455 68649.8 72402.

7

331. 219 163.67 200.27 291

600.000 3.460 .28903 .5282 42. 580 72357.

0

76403.4 338. 001 167.03 199.86 296

620.000 3.232 .30945 . 4740 45.170 76067.4 30399.7 344. 553 170.30 199.83 301

640.000 3. 033 . 32921 . 4302 47. 998 79790.

8

84399.8 350.903 173.51 200. 25 308

660.000 2.371 . 34831 .3941 50.9 13 83536.

1

88412.4 357.077 1 76.66 201.09 315

680.000 2.726 . 36679 . 3640 53. 831 87310.

3

92445 .

4

363.097 1 79. 75 202.26 322

700.000 2.599 .38472 . 3385 56. 7C9 91118.6 96504.6 368.980 182.77 203. 70 329
Table 22. Continued

I-3UTANE ISOBAR AT P = 160 BAR

T DEN VOL OP/DT DP /CO E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

119.614 12.772 .07830 22.5140 1456. 390 419.5 1672.2 111.843 73.79 99.31 1836

120.000 12.766 .07833 22.4422 1451.846 457.2 1710.6 112. 168 73.83 99.37 1833

130.000 12.612 . 0 7929 20.6937 1341.020 1443.6 2712.

3

120. 183 74. 86 100.96 1763

140.000 12.457 .08027 19.1372 1241.945 2445.4 3729.8 127. 726 76.02 102.62 1698

150.000 12. 303 .08128 17.7418 1152. 614 3463.

7

4764.1 134. 865 77.30 104.36 1636

160.000 12. 15 0 .03231 16.4832 1071.490 4499.

0

5815.9 141.658 78.69 106.18 1577

170.000 11.996 .08336 15.3420 997.3 36 5552.4 6886.2 148.151 80.17 10 8. 06 1520

180.000 11.842 . 08445 14.3024 929. 166 6624.

6

7975.7 154.382 81.74 110.00 1466

190.000 11.688 .08556 13.3513 366. 175 7716.3 9085.3 160.383 83.38 112.00 1414

200.000 11.534 .03670 12.4779 8 07. 7 06 8828.4 10215.6 166. 180 85.09 114.07 1364

210.000 11.379 .08788 11.6730 753.2 G3 9961.4 11367.5 171.797 86.85 116.19 1316

220.000 11.224 . 08910 10.9289 7 0 2. 2 24 11116.0 12541.6 177. 252 88.65 118.36 1270

230.000 11.063 .09035 10.2389 654. 384 12292.

3

13738.5 182.562 9 0.50 120.58 1224

240.000 10.911 .09165 9.5974 609. 364 13492.4 14958.9 187.742 92.38 122.86 1180

250.000 10.752 .09300 8.9994 566.898 14715.2 16203.2 192.804 94.29 125.18 1137

260.000 10. 593 .09440 8.4404 526. 762 15961.

6

17472.1 197. 760 96.22 127.56 1096

270.000 10.432 .09586 7.9168 486.771 17232.1 18765.8 202. 619 96.16 129.98 1055

230.000 10.269 .09738 7.4252 452.771 18526. 8 20084.9 207. 391 100.12 132.45 1015

290.000 10.104 .09897 6.9625 418.637 19646.1 21429.7 212.083 102.08 134.97 975

300.000 9.93 6 .10064 6.5263 386.266 21190.2 22800.5 216. 702 104.04 137.55 937

310.000 9. 766 .10240 6.1143 355.576 22559.

3

24197.6 221. 255 106.01 140.18 899

320.000 9.592 .10425 5.7242 326.501 23953.3 25621.3 225. 748 107.97 142.88 862

330. 000 9.415 . 10621 5. 3544 298. 989 25372.3 27071.7 230. 186 109.94 145.64 825

340.000 9.234 . 10830 5.0032 273.0 03 26816.

3

28549.0 234.576 11 1.91 148.47 789

350.000 9.048 .11052 4.6691 248. 513 28285.

2

30053.5 238.922 113.89 151.39 753

360.000 3.353 .11239 4. 3510 225. 5 C6 29779.

0

31585.3 243. 229 115.91 154.42 718

370.000 8.662 . 1 1544 4.0477 203.973 3129 7.9 33145.0 247. 503 118.04 157.64 684

380.000 8.461 .11819 3.7583 183.921 32843.

1

34734.2 251. 751 120.43 161.19 650

390.000 8.254 .12116 3.4619 165.368 34418.8 36357.4 255.985 123.25 165.22 617

400.000 8.040 .12438 3. 2179 148. 344 36036.

6

38026.7 260. 210 126.45 169.64 585

410.000 7.820 .12788 2.9660 132. 886 37115.5 39161.6 262. 940 136.21 180.60 550

420.000 7. 594 .13169 2.7261 119.036 38855.

0

40962.0 267. 279 134.93 160.40 523

430.000 7.36 2 .13583 2.4986 106.817 40601.9 42775.2 271.545 135.96 182.33 496

440.000 7.126 .14033 2.2841 96. 217 42363.9 44609.2 275.761 137.47 184.45 471

450.000 6.888 . 14516 2.0837 87.169 44140.9 46463.8 279. 929 139.20 186. 44 448

460.000 6.649 .15040 1.6985 79.542 45930. 7 48337.

2

284. 046 141.03 188.18 427

470.000 6.411 .15598 1.7293 7 3. 148 47730.9 5 C226.6 288. 110 142.93 189.68 408

480.000 6.176 . 16190 1.5764 67.778 49539.6 52130.1 292. 117 144.87 191.00 392

490.000 5. 946 .16817 1.4394 63. 233 51355. 6 54C46.

3

296. 063 146.83 192.23 377

500. OOP 5.721 .17478 1.3174 59.357 53178.2 55974.7 299. 964 146.79 193.46 364

520.000 5.290 .18903 1.1131 53.271 56843.9 59868.4 307. 600 152.69 195.91 342

540.000 4.837 .20461 .9520 49.243 60535.6 63809.3 315. 036 156.50 198.10 327

560 .000 4.519 .22128 .8242 47.230 64247. 2 67787. 8 322. 270 160.18 199.62 318

580.000 4.191 .23863 .7224 46.971 67971.0 71789.0 329. 291 163.72 200.41 314

600.000 3.904 .25613 .6407 47. 966 71702.

8

75801.6 336. 093 167.14 200.84 314

620.000 3.655 . 27361 .5746 49. 693 75444.9 79822.7 342. 685 170.46 201.30 317

640.000 3.439 .29076 .5204 51.873 79202. 7 83854.8 349. 086 173.70 201.95 322

660.000 3. 252 .30752 .4756 54. 355 82981.

7

87902.0 355. 313 176.85 202. 83 327

680.000 3.088 .32385 .4380 57.0 C7 86787.

7

91969.3 361. 384 179.94 203.94 333

700.000 2. 94 3 . 33976 .4062 59.733 90625.1 96061.2 367. 314 182.96 205.28 339

152
Table 22. Continued

I-eUTANE ISOBAR AT P = 190 BAR

T OEN VOL OP/OT DP/CO E H S CV CP W DEG K MOL/L L/MOL 8AR/K 0AR-L/MOL J/MOL J/MOL J/HOL/K J/MOL/K J/MOL/K M/SEC

120.272 12.776 . 0 7827 22.5543 1469.670 462. 6 1871.5 112.204 73.85 99.36 1844

130.000 12.626 .07920 20.8502 1361.303 1420.1 2845.7 119. 990 74.86 100.90 1776

140.000 12.473 . 08017 19.2665 1261. 604 2419.

5

3862.6 127. 528 76.02 102.56 1711

150.000 12.321 .06116 17.8886 1171. 759 3435.

2

4896.2 134.663 77.31 104.29 1649

160.000 12.168 .08218 16.6261 1090. 203 4468.0 5947 .

3

141 . 451 78.70 106.10 1590

170.000 12.016 .08322 15.4816 1015.690 5518.6 7016.7 147.939 8 0. 16 107.96 1533

180.000 11.863 .03429 14.4391 947.2 21 6587.9 8105.2 154. 164 81.74 109.90 1490

190.000 11.711 .08539 13.4855 883.984 7676.6 9213.7 160. 159 83.39 111.89 1428

200.000 11.559 .08652 12.6100 825.314 8785.4 10342.7 165.950 85.09 113.93 1378

210.000 11.405 .08768 11 . 8034 770.659 9914.

9

11493.2 171. 559 86. 65 116.04 1330

220.000 11.252 .08888 11.0578 719.548 11065.9 12665.7 177.007 88.66 118.19 1284

230.000 11.098 .09011 10.3667 671. 615 12238. 8 13860.

8

182. 309 90.51 120.39 1239

240.000 10.943 .09138 9.7243 626.530 13434.2 15079.1 187.480 92.39 122.64 1196

250.000 10.787 .09270 9.1256 584. 023 14652.

4

1 6321.0 192.533 94.30 124.93 1153

260.000 10.630 .09407 8.5663 543. 868 15893.

9

17587.2 197. 478 96.23 127.27 1112

270.000 10.472 .09549 8.0426 505. 876 17159. 0 18877.8 202.326 98.17 129.65 1072

280.000 10. 312 .09697 7.5512 469.890 18447.9 20193.4 207. 084 10 C. 12 132.07 1032

290.000 10.151 .09852 7.0890 435.783 19760.9 21534.2 211. 762 102.09 134.54 994

300.000 9.937 .10013 6.6536 403.448 21096.

0

22900 .

4

216. 365 104.05 137.06 956

310.000 9.821 .10193 6.2425 372. 8 00 22459.3 24292.2 220. 901 106. 02 139.61 919

320.000 9.652 .10361 5.8539 343.770 23844.8 25709.7 225.375 107.98 142.22 882

330.000 9.430 .10548 5.4858 316.3 04 25254.4 27153.1 229.792 109.95 144,68 846

340.000 9.305 .10747 5.1366 290. 360 26687. 9 28622.

3

234. 157 111.91 147.60 611

350.000 9.126 .10958 4.8050 265.9 06 26145. 1 30117.4 238.476 113.90 150.39 777

360.000 8.943 .11181 4.4897 242. 922 29625.

7

31638.4 242. 752 115.92 153.26 743

370.000 8. 756 .11420 4.1896 221.394 31130.

0

33135.6 246.992 118.05 156.30 710

380.000 8.565 .11676 3.9038 201. 321 32658.

8

34760.4 251.202 120.44 159. 65 677

390.000 8.369 .11950 3.6314 182. 7 11 34216.

2

36367.1 255.393 123.26 163.45 645

400.000 9.167 .12244 3.3720 165.580 35813.7 38017.6 259. 571 126.46 167.64 614

410.000 7.961 .12561 3. 1249 149.955 36870. 3 39131.3 262.248 136.23 178.35 581

420.000 7.751 .12902 2.8901 135.859 38585.6 4 09 0 8.

0

266. 529 134.94 177.92 555

430.000 7.536 .13270 2.6676 1 23. 3 09 40 306.

9

42695.4 270. 735 135.96 179.66 529

440.000 7.319 .13664 2.4576 112.297 42042.4 44501.9 274.333 137.47 181.66 505

450.000 7. 099 .14087 2.2608 102. 7 74 43792.7 46328.3 278.992 1 39.18 193.59 U82

460.000 6.879 .14537 2.0776 94.643 45556.3 48173.0 283.047 141.00 185.33 462

470.000 6.660 .15014 1. 9087 87. 756 47331.6 50034.

2

287. 050 142.88 186.97 444

480.000 6. 444 .15517 1.7544 81.934 49116.6 51909.7 290.998 144.80 188.21 426

490.000 6.232 .16045 1.6144 76.987 50909.

9

53798.1 294. 892 146.74 189.44 413

500.000 6.025 .16597 1.4882 72. 745 52710.9 55698.4 298.731 148.69 190.62 400

520.000 5.627 .17771 1.2733 65.863 56335.

4

59534.1 306. 253 152.57 192.98 378

540.000 5.25 3 . 19038 1.1004 60 . 774 59990.

8

63417.

6

313. 581 156. 36 195.38 361

560.000 4.904 .20392 .9606 57.303 63677.

2

67347.

9

320. 727 160. 10 197.59 34 8 580.000 4.583 .21819 . 8467 55.450 67391.2 71318.5 327.694 163.69 199.39 340

600.000 4.294 .23291 .7535 55.039 71 128.

1

75320.4 334.477 167.17 200. 74 337

620 . 000 4.035 .24780 .6767 55. 741 74885.

7

79346.2 341 . 078 170.53 201.61 336

640 .000 3. 907 . 26267 .6131 57.183 78664.

3

83392.3 34 7. 501 173.80 202.62 33 9 660.000 3. 605 .27736 .5598 59. 060 82467.

0

87459.5 353. 758 176.98 203.92 342

630.000 3.427 .29182 .5149 61. 244 36297.

3

91550.0 359.864 190.08 205.15 346

700.000 3.268 .3 0599 .4767 63.636 90158.5 95666.4 365.830 163.10 206.51 351

153
Table 22. Continued

I-BUTANE ISCBAR AT P = 200 BAP

T DEN VOL DP/OT DP/DO E H S CV CP M OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

120.912 12.779 . 07825 22.5972 1483. 132 504. . 2069.1 112.544 73.92 99.41 1852

130.000 12.641 .07911 21.0058 1381.593 1397.

0

2979.1 119.799 74.86 100.85 1789

140.000 12.489 .08007 19.4388 1281.263 2394.

1

3995.5 127. 333 76.03 102.50 1723

150.000 12. 338 .08105 18.0344 1190.894 3407.4 5028.4 134. 463 77.31 104.22 1661

160.000 12.186 . 08206 16.7681 1108. 899 4437.6 6078.8 141. 246 78.70 106.02 1603

170.000 12.035 .08309 15.6202 1034.0 18 5485.5 7147.3 147.729 8 0. 18 107.88 1547

160.000 11.884 . 08415 14.5747 965.242 6552.

0

8234.9 153. 949 81.75 109.80 1493

190.000 11.733 .08523 13.6186 901. 750 7637.

7

9342.3 159. 938 83.39 111.77 1442

200.000 11. 582 .08634 12.7409 842.870 9743.4 10470.2 165.723 85.09 113.81 1392

210.000 11.431 .08746 11.9324 788. 045 9869.6 11619.3 171. 326 86.85 115.89 1345

220.000 11.279 .08866 11.1853 736.8 01 11017.1 12790.2 176.766 86.66 118.03 1299

230.000 11.127 .08987 10.4929 688.764 12186.

2

13983.

6

182. 061 90.51 120.21 1254

240.000 10.974 .09112 9. 8495 643.6 02 13377.5 15200.0 187. 223 92.39 122.43 1211

250.000 10.621 .09241 9.2500 601. 043 14591.5 16439.7 192. 267 94.3 0 124.70 1169

260.000 10.667 .09375 8.6903 560.856 15828 .3 17703.

3

197. 202 96.23 127.00 1128

270.000 10.511 .09514 8.1663 522. 849 17088.4 18991 .2 202. 039 98.18 129.35 1088

280.000 10.354 .09658 7.6749 486. 864 18371.

9

20303.5 206. 786 10 C.13 131. 73 1049

290.000 10.196 .09808 7.2130 452.768 19678.9 21640.5 211.451 102.09 134.15 1011

300.000 10.035 .09965 6.7780 420. 453 21009.6 23002.5 216. 040 104.06 136.61 974

310.000 9.873 . 10128 6.3678 389.830 22363.8 24389.5 220.560 106.02 139.10 938

320.000 9.709 .10300 5.9801 360. 827 23741.6 25801.6 225. 016 107.99 141.64 902

330.000 9. 542 .10430 5.6133 333.387 25142.6 27236.7 229.414 109.95 144.21 867

340.000 9.372 .10670 5.2657 307.464 26566.

8

28700.8 2 3 3 . 75 8 111.92 146.83 833

350.000 9.19' .10871 4.9360 283. 0 24 28013.6 30187.7 238. 053 113.91 149.52 799

360.000 9.023 .11083 4.6229 260.040 29482.8 31699.3 242. 303 115.93 152.27 766

370.000 8.843 .11308 4. 3252 238. 495 30974.

3

33235.9 246.514 118.06 155.17 734

380.000 3.660 .11547 4.0422 218. 380 32489.2 34798.6 250.692 120.45 158.36 702

390.000 8. 473 .11802 3. 7729 199.695 34031.2 36391.5 254.846 123.27 162. 00 671

400.000 8.282 .12074 3.5168 182.446 35611.7 38026.5 258.985 126.47 166.00 641

410.000 8.088 .12364 3.2733 166.648 36650.1 39123.0 261.620 136.24 176.54 609

420.000 7.890 .12675 3.0422 152.314 38345.8 40880.3 265. 856 134.95 175.95 584

430.000 7.688 .13007 2.8232 139. 454 40046.

4

42647.7 270. 013 135.97 177.55 559

440.000 7.485 .13360 2.6165 128.061 41760.7 44432.7 274. 117 137.48 179.46 536

450.000 7.280 .13736 2.4222 118.098 43489.

7

46236.9 278. 171 139.18 181.36 514

460.000 7. 075 . 14134 2.2407 109.493 45232.

6

48059.4 282. 177 140.99 183.13 494

470.000 6,371 .14553 2.0722 102 .130 46988.

1

49898.7 286. 133 142.86 184.71 476

480.000 6.670 .14993 1.9170 95.861 48754 .5 51753.0 290. 037 144.76 186.13 460

490.000 6.472 . 15452 1.7749 9 0.5 16 50530.

4

53620.8 293.888 146.69 187.41 44 6 500.000 6.278 .15929 1 « 64 56 85.932 52315.1 55500.9 297. 686 148.62 188.60 433

520.000 5.905 .16935 1.4223 78.484 55909.1 59296.1 305. 128 15 2.48 190.92 411

540.000 5. 553 .18008 1.2399 72.7 29 59536.

7

63138.2 312.378 156.29 193.31 393

560.000 5.223 .19145 1.0904 68. 363 63199.4 67028.5 319. 452 160.02 195.72 379

580.000 4.916 .20343 .9669 65. 346 66897.

1

70965.8 326. 360 163.64 197.98 368

600.000 4,632 .21590 . 8642 63.663 70627, 7 74945.7 333. 106 167.15 199.96 361

620.000 4.373 .22868 . 7783 63. 186 74388.4 78962.0 339. 691 170.55 201.64 358

'640.000 4. 139 .24161 . 7062 63.686 78177.

5

83009.7 346.116 173.85 203.11 357

660.000 3.929 .25453 .6453 64.893 81994.9 87085.6 352. 387 177.05 204.49 359

680.000 3.740 ,26735 .5935 66.555 85342. 2 91189.2 358. 512 180.17 205.89 361

700.000 3. 571 .23001 .5491 6 8.5 C4 89721.3 95321.6 364. 502 1 83.21 207.36 36 5 154
Table 22. Continued

I-BUTftNE ISOBAR AT P = 220 BAR

T DEN VOL OP/OT DP/CD E H S CV CP H OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

121.535 12.783 . 07823 22.6424 1496.763 544.0 2265.0 112.869 73.98 99.46 1660

130.000 12.655 . 07902 21.1606 1401. 892 1 374.

2

3112.6 119. 610 74.87 10 0.79 1801

140 .000 12.505 .07997 19.5883 1300. 923 2369.1 4128.4 127. 139 76.03 102.44 1736

150.000 12.354 .08094 18.1794 1210.0 32 3379.

9

5160.7 134. 265 77.31 104.16 1674

160.000 12.204 .08194 16.9090 1127.578 4407.7 6210.4 141.044 78.70 105.94 1615

170.000 12.054 .08296 15. 7577 1052.322 5453.1 7278.1 147. 521 80.19 107.79 1560

180.000 11.905 .08400 14.7093 9 8 3. 2 31 6516.8 8364.8 153. 736 81.75 109. 70 1506

190.000 11.755 .08507 13.7506 919.476 7599.7 9471.2 159. 720 83.39 111.67 1455

200.000 11.606 .03617 12.8707 860. 373 8702. 3 10597.9 165.499 85.10 113.69 1406

210.000 11.456 .08729 12.0602 805 . 3 73 9825.4 11745.8 171. 096 86.86 115.76 1358

220 .000 11.306 .08845 11.3115 753. 994 10969.

4

12915.

3

176. 529 88.67 117.87 1313

230.000 11.156 .08964 10.6177 705.337 12135.0 14107.

0

181. 817 90.52 120.03 1269

240 .000 11.005 .09087 9. 9732 660.588 13322.5 15321.5 186.972 92.40 122.24 1226

250.000 10.854 .09213 9.3728 617.965 14532.3 16559.2 192.007 94.31 124.48 1184

260.000 10.702 . 0 9344 8.8124 577. 735 15764.

8

17820.5 196.933 96.24 126.75 1144

270.000 10.549 .09480 8.2881 539.7 02 17020.1 19105.7 201. 760 98.18 129.06 1104

280.000 10.395 .09620 7.7965 5 0 3. 7 04 18298.5 20415.0 206. 496 10 0.14 131.41 1066

290.000 10.239 .09767 7.3346 469.6 06 19600.0 21748.7 211.149 102.10 133.79 1028

300.000 10.382 .09919 6.9000 437.296 20924.

7

23106.8 215. 725 104.06 136.20 992

310.000 9.923 .10077 6.4902 406.683 22272.

4

24489.4 220. 230 106.03 138.64 956

320.000 9.763 .10243 6.1033 377.692 23643.1 25896.5 224. 671 108. 00 141. 11 921

330.000 9.600 .10417 5.7375 35 0. 261 25036.4 27328.0 229.051 109.96 143.61 667

340.000 9.435 .10599 5.3911 324.344 26452.1 28783.8 233.376 111.93 146.16 856

350 .000 9.268 .10790 5.0628 299.900 27889.

6

30263 .

4

2 3 7. 65 0 113.92 148.75 820

360. 000 9. 097 .10992 4.7513 276. 9C0 29348.7 31766.9 241.878 115.94 151 . 40 788

370.000 8.924 .11205 4 . 4556 255.321 30829.

1

33294.

3

246.063 118.07 154.19 757

380.000 8.748 .11431 4.1746 235. 149 32331.3 34846.6 250.213 120.46 157.26 726

390.000 3.569 .11669 3. 9077 216.377 33860.6 36427.9 254. 338 123.29 160.77 696

400 . COO 8. 387 .11923 3.6541 199. 0 C4 35426.

9

38049.9 258. 444 126.49 164 . 64 667

410.000 8.202 .12192 3.4132 133.033 36449.3 39132.0 261. 043 136.25 175. 04 636

420.000 8.014 .12478 3.1847 168.472 38 129 .2 40874.

2

265. 241 134.96 174.33 611

430.000 7. 824 .12781 2.9664 155.323 39812.7 42624.5 269.360 135.99 175.83 587

440.000 7.632 .13102 2.7640 143.577 41509.

5

44392.0 273. 423 137.49 177.68 564

450.000 7. 44 0 .13442 2.5716 1 33.2 06 43221.0 46178.2 277. 437 139.19 179. 55 543

460.000 7.247 .13800 2. 3913 124. 156 44 946.

8

47982.7 281.403 140.99 181.34 524

470.000 7.055 . 14175 2.2232 116. 335 46685.9 49804.4 285.321 142.85 182.98 506

480.000 6.865 .14567 2.0674 109.622 48436.

9

51641 .

7

289. 189 144.75 184.47 490

490.000 6.673 .14975 1.9238 103. 874 50 193. 7 53493.2 293. 007 146.67 185.82 475

500.000 6.495 .15398 1 . 7920 98.938 51970.

3

55357.7 296. 773 148.59 187. 07 462

520.000 6.141 . 16283 1.5620 90.936 55540.5 59122.7 304. 156 152.43 189.42 440

540.000 5.303 .17218 1.3716 84. 714 59146.5 62934.6 31 1. 349 156.23 191.78 422

560.000 5.494 .18202 1.2137 79. 791 62789.

8

66794.4 31 B. 368 159.95 194.21 408

590.000 5.199 .19233 1.0821 76.0 15 66471.6 70703.0 325.225 163.59 196. 64 396

600.000 4.924 . 20307 .9715 73.378 70191.

5

74659.0 331.931 167.12 198.94 387

620.000 4.670 .21414 .8780 71.862 73948.2 78659.3 338.489 170.54 201.04 381

640.000 4.436 .22544 . 7965 71. 371 77739. 7 82699.3 344.902 173.87 202.93 378

660 .000 4.222 .23635 . 730 7 71. 737 81564.6 86775.2 351.173 177.09 204.65 377

660.000 4.026 .24326 .6725 72. 758 8‘!422. 7 90384.5 357. 307 180.23 206. 28 378

700.000 3.852 .25961 .6223 74. 241 39 314 .

6

95026.1 363. 310 183.28 207.69 360

155
Table 22. Continued

I-BUT4NE ISOBAR AT P = 250 BAR

T DEN VOL DP/DT DP/CD E H S CV CP W OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

122.440 12.790 .07819 22. 7139 1517. 473 601.3 2556.

0

113, 331 74.08 99.53 1872

130.000 12.677 .07889 21.3911 1432.362 1340.8 3313.

0

119. 329 74. 87 100.72 1820

140.000 12.527 .07982 19.8108 1330.4 17 2332.3 4328.0 126. 852 76.04 102.35 1755

150.000 12.379 .08078 18.3950 1238.703 3339.8 5359.4 133.972 77.32 104.06 1693

160.000 12.230 .08176 17.1187 1155.570 4363.9 6408.0 140.744 78.71 105. 83 163 5 170.000 12.082 .08276 15.9622 1079.736 5405.5 7474.6 147. 215 80.19 107.67 1579

160.000 11.935 .08379 14.9092 1010. 159 6465.3 8560.0 153. 423 81.76 109.57 1526

190.000 11.787 .08484 13.9465 945.996 7544.

0

9665.0 159. 399 83.40 111.52 1475

200.000 11.640 .08591 13.0631 886.555 8642. 3 10790.1 165. 169 85.10 113.52 1426

210.000 11.493 .08701 12.2496 831. 267 9760.

8

11936.

1

170. 757 66.87 115.57 1379

220.000 11.345 .08814 11.4983 779.655 10900.

0

13103.6 176. 182 88.68 117.66 1334

230.000 11.198 .08931 10.8023 731. 313 12060.5 14293.1 181. 459 9 0.52 119.79 1290

240.000 11.050 .09050 10.1559 685.917 13242.6 15505.1 186. 603 92.41 121.97 1248

250 .000 10.901 .09173 9.5541 643. 130 14446.

6

16739.9 191.626 94.32 124.17 1206

260.000 10. 753 ,09300 8.9925 602. 864 15672.

9

17997.

9

196.540 96.25 126.41 1167

270.000 10.603 .09431 8.4673 564.771 16921.6 19279.5 201. 353 98.19 128.68 1128

280.000 10.453 .09567 7.9752 528.733 18193.0 20584.7 206. 074 100.15 130.98 1090

290.000 10. 301 .09708 7.5131 494.609 19486.9 21913.7 210. 711 102.11 133. 30 1053

300.000 10.149 .09853 7.0785 462.285 20803.3 23266.7 215. 269 104.08 135.64 1018

310.000 9.995 .10005 6.6691 431.663 22142.2 24643.4 219. 756 106.04 138.02 983

320.000 9.840 . 10163 6.2829 402.665 23503.2 26044.0 224. 175 108.01 140 .41 948

330.000 9.683 .10328 5.9160 375. 225 24886.

2

27468.1 228. 533 109.98 142.83 915

340.000 9.524 .10500 5.5728 349. 289 26290.6 28915.4 232.833 111.95 145.27 883

350.000 9.364 .10679 5.2460 324. 3 15 27715.

9

30385.8 237. 030 1 13.94 147.76 851

360.000 9. 201 .10868 4.9363 301. 766 29161.7 31878 .7 241. 277 115.95 150.29 820

370.000 9.037 .11066 4.6426 280.115 30627.8 33394.

3

245.431 118.09 152.95 790

380.000 8.870 .11274 4. 3639 259. 840 32115.

0

34933.

6

249.546 120.48 155.68 760

390.000 3.701 .11493 4.0994 240.924 33627. 0 36500.4 253.633 123.31 159.24 731

400.000 8. 529 .11724 3.8484 223. 358 35175.4 38106.4 257.699 126.51 162.97 703

410.000 8.356 .11967 3.6103 207.135 36179.3 39171.1 260.255 136.28 173.22 673

420.000 8.181 .12224 3.3846 192. 252 37838.5 40894.4 264. 407 134.99 172.38 649

430.000 8. 004 .12494 3.1708 178.7 C2 39501.2 42624.6 268.479 136.01 173.77 626

440.000 7.826 .12778 2.9688 166.478 41176.6 44371.0 272. 493 137.51 175.54 604

450.000 7.648 .13076 2.7783 155.553 42866.

7

46135.7 276. 459 139.21 177.39 583

460.000 7.469 .13388 2.5992 145. SEO 44571,5 47918.6 280. 378 141.01 179.19 564

470.000 7.292 .13714 2.4315 137. 424 46290.5 49719.1 284. 250 142.86 180.89 547

480.000 7.116 .14054 2.2750 130.066 48022 .6 51536.0 288. 075 144.75 182.48 531

490.000 6. 94 2 .14405 2. 1296 123.7 C6 49767.0 53368.2 291.85 3 146.66 183.94 516

500.000 6.772 .14763 1.9951 116.217 51522.5 55214.4 295. 583 148.57 185.29 503

520.000 6.442 .15524 1. 7571 109. 334 55064.5 58945.4 302. 899 152.39 187.78 481

540.000 6.129 .16315 1. 5567 102. 479 58645.9 62724.8 310. 030 156.17 190.16 463

560.000 5.834 .17140 1.3382 96.996 62267. 0 66552.

0

316. 990 159.89 192.58 448

580.000 5.556 .17997 1.2461 92.544 65928.9 70428.

2

323. 790 163.53 195.05 435

600.000 5.295 . 18884 1.1255 89.0 10 69632.9 74354.0 330.445 167.07 197.52 425

620.000 5.051 .19800 1.0224 86. 383 73378.7 78328.6 336. 961 170.52 199.93 417

640.000 4.822 .20738 .9337 84.662 77165.6 82350.2 343.345 173. 87 202.21 411

660.000 4.609 .21694 . 8569 83.805 80992.2 86415.8 349.600 177.12 204.34 407

630.000 4.413 .22661 .7903 83. 7 16 84857.4 90522.7 355. 730 180.28 206.33 406

700.000 4.232 .23632 . 7323 84. 270 88760.

4

94668.3 361.738 183.34 208.22 405

156
Table 22. Continued

I-BUTANE ISCBAR AT P = 300 BAR

T OEN VOL DP/DT DP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

123.877 12.801 . 07812 22.8426 1552.721 690.

5

3034.1 114.040 74.23 99.64 1893

130.000 12.711 .07867 21.7714 1483. 217 1286.9 3647.1 118.870 74.68 100.60 1851

140.000 12.564 .07959 20.1775 1379.595 2273.2 4660.9 126. 384 76.05 102.22 1 786

150.000 12.418 .08053 18. 7500 1286. 478 3275.1 5690.9 133.493 77.33 1 03.91 1724

160.000 12.273 .08148 17.4637 1202. 178 4293.5 6737.9 140. 255 78.72 105.67 1666

170.000 12.128 .08245 16.2982 1125.335 5329.1 7602.8 146. 716 8 0.20 107.49 1610

180.000 11.983 .08345 15.2375 1054.911 6382.

7

8886.2 152. 912 81.77 109.36 1557

190.000 11.839 . 0 8447 14.2679 990. 0 30 7455.

0

9989.0 158. 876 83.41 11 1. 29 1507

200.000 11.695 .08551 13.3785 929.984 8546.5 11111.7 164. 635 85.12 113.26 1459

210.000 11. 551 .08657 12.5597 874. 186 9657.9 12255.0 170. 209 86.88 115.28 1412

220.000 11.403 .08766 11.8037 822.147 10789.6 13419.5 175.619 88.69 117.34 1367

230.000 11.264 .08878 11.1037 773.459 11942.2 14605.6 180. 881 90.54 119. 44 1324

240 .000 11. 120 .08992 10.4539 727. 776 13116.0 15813.7 186.009 92.42 121.56 1283

250.000 10.977 .09110 9.8491 684.8 00 14311.2 17044.

3

191. 016 94.3 3 123.72 1243

260.000 10.833 .09231 9.2851 644. 297 15528.2 18297.6 195.911 96.26 125.91 1204

270.000 10.688 .09356 8.7579 606.056 16767.1 19573.8 200. 704 98.21 128.12 1166

280.000 10.544 . 0 9484 8.2642 569. 9 Cl 18027.

8

20873.

1

20 5. 404 10 0. 16 130.35 1129

290.000 10.393 .09617 7.8011 535.686 19310.5 22195.6 210. 017 102.13 132.60 1093

300.000 10.252 . 09754 7.3659 503.286 20614.9 23541.1 214.550 104.10 134.86 1059

310.000 10.106 .09895 6.9562 472.599 21941.

0

24909.6 219.010 106. 06 137.14 1025

320.000 9. 95 8 .10042 6.5701 443. 5 38 23288.

3

26300.9 223.400 108.03 139. 44 992

330.000 9.809 .10194 6.2053 416.0 30 24656.4 27714.9 227. 726 110.00 141.75 96 0 340.000 9.660 .10352 5.8615 390. 0 14 26045.

0

29150.7 231.992 111.97 144.07 929

350.000 9.509 .10517 5.5359 365.441 27453.4 30608.4 236.202 113.96 146.42 898

360.000 9.357 .10688 5.2277 342.267 28881.1 32087.

3

240. 360 115.98 148.82 869

370.000 9.203 . 10866 4.9358 320.455 30327.7 33597.5 244.471 118.12 151.33 840

380.000 9.049 .11051 4.6591 299. 975 31 794.

2

35109.7 248.541 12 C.51 154.10 812

390.000 8.893 .11245 4.3969 28 0.8 02 33284.3 36657.9 252. 590 123.34 157.30 784

400.000 8.735 .11448 4.1482 262.915 34809.3 38243.6 256. 594 126.55 160 . 86 758

410.000 8.577 .11659 3.9i25 246. 291 35788.

7

39286.

4

259. 096 136. 31 170.95 728

420.000 8.413 .11880 3.6892 230.920 37422.3 40986.2 263. 192 135. 03 169.96 707

430.000 8.258 .12110 3.4777 216.784 39058.6 42691.6 267. 205 136.05 171.23 635

440.000 3.097 .12350 3.2777 203.869 40707.1 44412.2 2 71. 16 0 137.55 172.92 664

450.000 7.936 .12600 3.0886 192. 152 42 370.2 46150.

3

275. 066 139.25 174.72 644

460.000 7. 776 .12861 2.9104 181.606 44048.4 47906.6 278. 926 141.05 176.53 625

470.000 7.616 .13130 2. 7426 172. 186 45 741.

7

49680.

9

282. 742 142.90 178.30 607

480.000 7.457 .13410 2.5850 163.841 47449.

4

51472.3 286.514 144.78 179.99 591

490.000 7.301 .13698 2.4375 156.498 49170.9 53280.2 290. 241 146.68 1 81 .59 577

500.000 7. 146 .13994 2.2996 150. 070 50905.5 55103.

7

293.925 148.59 183.09 564

520 .000 6.846 .14608 2.0519 139.566 54411.

2

58793.7 301.161 152.39 185.86 541

540.000 6. 559 .15247 1.8386 131.5 15 57962.

5

6 25 36.7 308. 224 156.15 188.42 522

560.000 6.286 .15907 1.6559 125.185 61557. 7 66329.8 315. 121 159.85 190.89 507

580.000 6.029 .16586 1.4994 120.038 65196.

7

70172.3 321. 863 163.48 193. 36 494

600.000 5.787 .17281 1.3648 115.753 68880.1 74064.5 328.460 167.03 195. 86 483

620.000 5.557 .17994 1.2485 112. 1 79 72608. 7 78006.8 334.923 170.49 198.33 473

640.000 5. 341 . 18722 1.1473 109.270 76382.7 81999.4 341. 261 1 73.85 200.87 466

660.000 5.137 .19465 1 . 0587 107. 0 24 80201.

8

86041.4 347.480 177.13 203.31 459

680.000 4.945 .20221 . 9808 105.440 84065.

2

90131.4 353.565 180.31 205.67 454

700.000 4.765 .20986 .9120 104.499 87971.9 94267.6 359. 579 183.40 207.93 45 1 157
Table 22. Continued

I-BUTANE ISOBAR AT P = 350 BAR

T OEN VOL OP/OT OP/CO E H S CV CP M OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

125.235 12.813 .07605 22.9809 1588.742 772.9 3504.5 114.632 74.39 99. 74 1914

130.000 12. 744 .07847 22. 1467 15 34. 140 1235.2 3981.6 118, 420 74.90 100.49 1881

140.000 12.600 .07937 20.5393 1428.8 19 2216. 4 4994.

1

125. 926 76. 06 102.10 1816

150.000 12.457 .08028 19.1000 1334. 255 3213.

1

6022.8 133. 026 77.34 103.73 1754

160.000 12.314 .03121 17.8033 1248.720 4226.1 7068.4 139.779 78.73 105.52 1696

170.000 12.1 71 .08216 16.6288 1170.843 5256.1 8131.7 146. 230 80.22 107.32 1641

130.000 12,030 .08313 15.5600 1099.530 6303.9 9213.4 152. 416 81.78 109.17 1589

190.000 11.888 .08412 14.5834 1033. 891 7370.

2

10314.2 158.370 83.43 111.08 1538

200.000 11.748 . 03512 13.6876 973.197 8455.4 11434.8 164.117 85.13 113.03 1490

210.000 11.607 .08615 12.8633 916.847 9560.2 125 75.7 169. 680 86.89 115.03 1445

220.000 11.467 ,08721 12.1023 864. 339 10685.

2

13737.4 175.073 88.70 117.06 1400

230.000 11.327 .08823 11.3979 815.252 11830.6 14920.5 180. 326 90.55 119.12 1358

240.000 11.187 .06939 10.7442 769. 233 12996.

8

16125.4 185. 440 92.44 12 1.22 1317

250.000 11.043 .09052 10.1361 725.983 14184.2 1 7352.3 190.431 94.35 123.34 1277

260,000 10.908 .09168 9.5691 685. 241 15392.9 18601.5 195. 311 96.28 125.48 1239

270.000 10.768 .09287 9.0394 646. 8 03 16622.9 19873.2 200.087 98,23 127.64 1202

280.000 10.626 .09409 8.5436 610. 482 17874.5 21167.5 204. 768 100.18 129.62 1166

290.000 10.486 .09534 8.0787 576.123 19147.

3

22484.4 209. 362 102.15 132.01 1131

300.000 10.348 .09664 7.6421 543.597 20441.4 23823.7 213.874 104,12 134.22 1098

310.000 10.207 .09797 7. 2315 512.794 21756.5 25185.5 218. 311 106.09 136.43 1065

320.000 10. 066 .09935 6.8447 483.620 23092.

2

26569.3 222. 678 108,06 138.65 1033

330.000 9.924 .10076 6.4799 455.996 24448.1 27974.3 226.979 110.02 140.88 1002

340.000 9. 782 .10223 6.1354 429.855 25823.6 29401.7 231. 217 112.00 143.12 972

350.000 9.639 .1 0375 5.8099 405. 141 27218.1 30649.4 235. 399 113.99 145.38 942

360.000 9.495 .10532 5.5020 3 81.8 C4 28631.2 32317,

4

239. 526 116.01 147.67 914

370.000 9. 350 .10695 5, 2106 359. 801 30062.4 338 05.5 243.604 118. 15 15 0.08 886

330.000 9.205 .10863 4.9345 339.096 31512.

6

35314.8 247.640 1 2 C.55 152.75 859

390,000 9.059 .11038 4.6730 319.656 32985.5 36848,9 251. 641 123.38 155.84 633

400.000 8.913 .11220 4.4252 301.451 34492.

7

38419.6 255.618 126.58 159.29 807

410.000 3. 766 .11408 4.1904 284.456 35453.4 39446.2 258. 080 136.35 169.29 779

420.000 3.618 .11603 3.9678 268.648 37067.9 41129.0 262. 135 135.07 168.21 758

430.000 8.470 .11306 3.7570 254.0 04 38684. 4 42816.4 266.105 136. 09 169.40 737

440.000 8.323 . 12016 3.5574 240.5 C3 40 312.

9

44518.3 270. 018 137.60 171.02 717

450.000 8.175 .12233 3.3666 228.122 41955.

8

46237.3 273. 831 139.29 172.79 697

460,000 8.027 .12457 3.1901 216.8 35 43614.

1

47974.2 277. 698 141.09 174,60 679

470.000 7.681 .12639 3.0216 206.6 10 45287.9 49729.2 281.473 142.95 176.39 662

480.000 7.735 .12928 2.8628 197. 406 46976.

9

51501.9 285. 205 144. 83 178.14 646

490.000 7. 591 . 13174 2.7133 189,176 48680.8 53291.7 288.895 146.73 179.82 631

500.000 7.448 .13426 2.5729 181. 858 50399.

0

55098.

1

292. 544 148,63 181.44 618

520.000 7.170 .13947 2.3179 169.679 53875.

8

58757.3 299. 720 152.42 184.45 594

540.000 6.902 .14488 2.0950 160.234 57403.6 62474.

3

30 6. 734 156.17 1 87.22 574

560 .000 6.647 . 15044 1.9011 152.863 60979.6 66244.9 313. 590 159.86 189.83 558

580.000 6.405 . 15613 1.7328 146.983 64602.4 70066 .

9

320.295 163.48 192.36 545

600.000 6. 176 .16193 1.5865 142.155 68271.9 73939.

3

326.859 167.03 194.88 534

620.000 5. 95 8 .16783 1.4589 138.088 71988.0 77862.1 333. 290 170.48 197.40 524

640.000 5. 75 3 .17383 1.3471 134. 6 24 75 751.2 81835.

3

339. 597 173,85 199.92 516

660.000 5.558 .17992 1.2486 131.692 79561.5 85658.8 345. 788 177.13 202.43 508

680.000 5.373 . 18611 1.1614 129. 271 83418.

5

89932.2 351.868 180.33 204.90 502

700.000 5.198 .19237 1.0338 127. 360 37321.

3

94054.6 357.842 183.43 207.32 497
Table 22. Continued

I-BUTAME ISCBAR AT P = 400 BAR

T OEN VOL OP/DT DP/OD E H S CV CP H OEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

126.521 12. 826 .07797 23. 1271 1625. 437 849. 2 3968.0 1 15.265 74.53 99.84 1935

130.000 12.776 .07827 22.5175 1585.190 1 185. 4 4316.2 117. 981 74.91 100.38 1911

140.000 12.634 . 07915 20.8965 1476.117 2161.8 5327.7 125.478 76.07 101.98 1846

150.000 12.493 .03004 19.4451 1382. 047 3153.5 6355.2 132. 571 77.36 103.65 1 784

160.000 12.353 .08095 18.1380 1295. 244 4161.5 7399.5 139. 315 78.75 105. 38 1726

170.000 12.213 .08188 16.9543 1216.289 5186.2 8461.4 145. 757 80.23 107.17 1671

ISO. 000 12.074 .08282 15. 8773 1144. 045 6228.6 9541.5 151.934 81.80 109.01 1619

190.000 11.936 .08378 14.8934 1077.6 09 7289.

2

10640.5 157. 873 83.44 110.89 1569

200.000 11.798 . 0 8476 13.9911 1016. 2 20 8368.6 11759.1 163. 615 85.15 112. 63 1522

210.000 11.660 .03576 13.1609 959.289 9467.4 12897.

3

169. 167 86.91 114.80 1476

220.000 11.523 .08678 12.3947 906. 273 10586.

0

14057.

2

174.554 88.72 116.61 1432

230.000 11.387 .03732 11.6856 856.750 11724.8 15237.7 179.791 90.57 118.85 1390

240.000 11.251 .08888 11.0277 810 . 356 12884.

2

16439.6 184. 893 92.46 120.91 1350

250.000 11.115 .08997 10.4158 766.783 14064.5 17663.3 189.871 94.37 123.00 1311

260.000 10.979 .09108 9.3455 725.770 15265.6 18909.0 194. 736 96.30 125. 11 1273

270.000 10.843 .09222 9.3129 637.094 16487.9 20176.3 199. 497 98.25 127.23 1237

260.000 10.708 .09339 8.8145 650.561 17731.

2

21466.8 204.163 100.21 129.37 1202

290.000 10.572 .09459 8. 3474 616. 0 18 18995.5 22779.0 208. 741 102.17 131.52 1168

300 . 000 10.437 .09532 7.9089 583.3 26 20280.5 24113.1 213.235 104.14 133.67 1134

310.000 10.301 .09708 7.4966 552.367 21586.1 25469.2 217. 654 106.11 135.83 1102

320.000 10.165 .09337 7.1064 523.042 22911.8 26846.7 222.001 108.08 138.00 1071

330 .000 10.029 .09971 6.7425 495. 267 24257.1 28245.5 226. 280 110.05 140.17 1041

340 .000 9. 893 .10108 6. 3972 468. 968 25621.6 29664.9 230.497 112.03 142.34 1012

350.000 9. 75 6 .10250 6.0710 444. 084 27004.

6

31104.5 234. 654 114.02 144.54 9tf4 360.000 9.620 . 10395 5.7626 420.559 28405.5 32563.7 233.757 116.04 146.76 956

370.000 9.482 .10546 5.4707 398.347 29624.1 340 42.4 242. 809 118.18 149.10 929

380.000 9.345 .10701 5.1944 377. 4 07 31261.0 35541.4 246. 318 120.58 151.69 903

390.000 9.207 .10861 4.9327 357.696 32720. 1 3 7064.6 250. 791 123.41 154.71 878

400.000 9. 069 .11026 4.6848 339. 184 34213.0 33623.6 254. 738 126.62 158.09 853

410.000 8.931 .11197 4.4497 321.839 35159.1 39637.9 257.169 136.39 168.02 825

420.000 8. 793 .11373 4. 2270 305.635 3675 8. 3 41307.

6

261. 193 135.11 166.87 805

430. 000 5.654 .11555 4.0159 290.533 38359.3 42981.3 265. 131 136.14 168.01 785

440.000 8.516 .11742 3.8159 276.528 39972.

1

44669.1 269.01

1

137.64 169.59 765

450.000 3.378 .11935 3.6265 263.578 41599.4 46373.5 272.841 139.34 171.33 746

460.000 3.241 .12134 3.4472 251.662 43242.1 43095.8 276. 627 141.14 173.12 728

470.000 8.105 .12339 3.2776 240. 749 44900.

5

49836.0 280. 369 142.99 174.92 711

430.000 7.969 .12549 3.1173 230. 3 09 46574.

7

51594.2 284. 071 144.88 176.70 695

490.000 7.835 .12764 2.9660 221.8 02 48264.

3

53369.9 287.732 146.78 178.44 681

500.000 7.702 .12984 2.8232 213.684 49969.0 55162.7 291. 354 148.68 180.12 667

520.000 7.441 .13439 2.5622 199. 908 53421.9 58797.4 293. 431 152.47 183. 31 643

540.000 7.139 .13909 2.3317 188.998 56929.

8

62493.5 305. 455 156.21 186.26 622

560.000 6. 948 .14393 2. 1288 180 . A 11 60489.7 66246.7 31 2. 280 159.90 189.04 605

530.000 6.718 .14386 1.9506 173.6 08 64099.5 70054.0 318.960 163.51 191.68 591

600.000 6.499 .15388 1 . 7943 168. 1 17 6775 8. 3 73913.5 325. 502 167.05 194.26 579

620 .000 6.291 .15897 1.6568 163.573 71465.3 77324.0 331.913 170.50 196.80 569

640.000 6.093 .16412 1.5356 159. 723 75220.

6

81785.3 338. 201 173.87 199. 32 561

660.000 5.906 .16932 1.4283 156. 411 79023.9 35796.9 344.373 177.16 201.84 553

660.000 5.723 .17459 1.3328 153.553 82875.

1

89358.7 350. 436 180.36 204.33 54 7 700.000 5.558 . 1 7991 1.2475 151. 1 15 86773.

8

93970.1 356. 394 183.47 206. 60 541

159
Table 22. Continued

I-BUTANE ISC8AR AT P = 500 BAR

T DEN VOL DP/DT OP/CO E H S CV CP W DEG K MOL/L L/MOL 8AR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

128.910 12. 852 .07781 23.4378 1700.555 986.8 4877.1 116. 285 74.82 100.03 1977

130.000 12.837 .07790 23.2463 1687.689 1091.3 4986.2 117.128 74.94 100.20 1970

140.000 12.700 .07874 21.5975 1576.926 2058.

7

5995.8 124. 611 76.11 101.78 1904

150.000 12. 563 .07960 20.1221 1477. 760 3041.3 7021.1 131.689 77,39 103.43 1843

160.000 12.428 .08047 18. 7937 1388. 3 04 4039.

8

8063.1 138. 418 78.78 105.14 1785

170.000 12.293 .08135 17.5912 1307. 074 5054.9 9122.4 144.845 80.26 106.90 1730

160.000 12.158 .08225 16.4974 1232.861 6037.

3

10199.7 151.006 81.83 108.71 1678

190.000 12.025 .08316 15. 4984 1164.732 7137.6 11295.7 156. 933 83.48 11 0.57 1629

200 .0 00 11.892 .08409 14.5825 1101.872 8206.5 12410.9 162. 653 85.18 112,48 1582

210.000 11.760 .08503 13.7401 1043.650 9294.4 13546 .0 168.188 86.95 114.41 1537

220.000 11.629 .08599 12.9628 989.5 18 10401.7 14701.3 173.556 88,76 116.38 1494

230.000 11.498 .08697 12.2437 939.0 21 11528.9 15877,4 178. 773 90.61 118.38 1452

240.000 11.368 .08797 11.5766 891.776 12676.2 17074.5 133. 854 92,50 120.40 1413

250.000 11.239 .08898 10.9565 847.458 13843.9 18292.9 188.811 94.41 122.45 1375

260.000 11.110 . 09001 10.3787 805.790 15032.1 19532.8 193.653 96.34 124.50 1338

270.000 10.981 .09107 9.8393 766.534 16240.9 20794.2 198. 390 98.29 126.57 1303

280.000 10. 853 .09214 9. 3348 729.489 17470.2 22077.3 203.031 100.25 128.65 1269

290.000 10. 725 .09324 8.8622 694.481 18719.9 23381.9 207.582 102.22 130.73 1236

300.000 10.598 .09436 8.4187 661.361 19989.8 24707.6 212. 049 104.19 132,81 1204

310.000 10.470 .09551 8.0019 630.001 21279.5 26054,9 216.438 106.16 134.90 1173

320.000 10.344 .09668 7.6097 600. 290 22588.

8

27422.7 220. 754 108.13 136.98 1143

330.000 10.217 .09788 7.2401 572.134 23917.1 28810.9 225. 001 110.11 139.07 1115

340.000 10. 090 .09910 6.8915 545.450 25263.8 30219.0 229. 183 112.08 141.16 1087

350.000 9.964 .10036 6.5624 520.166 26628.3 31646.3 233.306 114.08 143.26 1060

360.000 9.638 .10165 6.2513 496. 220 28010.1 33092.

3

237. 371 116,10 145.39 1033

370.000 9.712 .10296 5. 9571 473.555 29408.8 34556.9 241. 385 118.25 147.64 1008

380.000 9.537 .10431 5.6785 452. 1 22 30625.

2

36040.9 245. 353 12 C.65 150.14 983

390.000 9.461 .10570 5.4147 431.876 32263.2 37548.1 249.285 123.48 153.06 959

400.000 9.336 .10711 5.1647 412.776 33734.4 39090.1 253.188 126.69 156.35 936

410.000 9.211 .10857 4.9277 394.785 34 65 8.

2

40086.6 255. 576 136.47 166.19 909

420.000 9.036 .11006 4.7029 377,865 36234.

8

41737.7 259. 555 135.19 164.97 890

430.000 8. 962 .11158 4.4697 361.984 37812.9 43392.0 263.447 136.22 166.03 871

440.000 8.838 .11315 4.2875 347.114 39402.5 45059.8 267. 281 137.73 167.56 852

450.000 8.715 .11475 4.0956 333. 218 41006.

4

46743.7 271. 066 139.43 169.26 834

460.000 3.592 .11638 3.9136 320.272 42 62 6. 0 48445.1 274, 805 141.23 171. 03 816

470.000 3.471 .11806 3.7409 308.246 44261.6 5 C164.4 278.503 143.09 172.83 800

480.000 8. 35 0 .11976 3.5772 297.111 45913.5 51901.7 282. 160 144.98 174.63 784

490.000 8.230 .12151 3.4220 286. 837 47581.5 53656.9 285. 779 146.88 176.41 769

500.000 8.111 .12329 3.2749 277, 391 49265.5 55429.8 289.361 148.78 178.16 755

520.000 7.878 .12694 3.0037 260,848 52680.

3

59027.2 296. 415 152.57 181.55 730

540.000 7.651 .13070 2.7609 247.179 56155.5 62690.6 303. 328 156.31 184.76 708

560.000 7.431 .13456 2.5439 236. 030 59688.

3

66416.5 310.102 160.00 187.80 690

580.000 7. 220 .13850 2.3503 2 27. 0 15 63276.

3

70201.5 316. 743 163.61 190.68 674

600.000 7.017 .14250 2.1777 219. 740 66917.

7

74042.9 323.254 167.14 193.43 661

620.000 6. 824 .14655 2.0239 213.836 70610.8 77938.3 329. 640 170.59 196.09 650

640.000 6.639 . 15063 1.8866 208.979 74354.6 81886.2 335.907 173.96 198.69 640

660.000 6. 462 .15474 1.7638 204.912 78148.4 85885.4 342.060 177.24 201.23 632

680 .000 6.294 .15687 1.6537 201.441 81991.5 89935.2 348.105 180.44 203.74 625

700.000 6.134 .16303 1.5547 198. 433 85883.

3

94034.8 354. 047 183.55 206.21 619

160
Table 22. Continued

I-BUTANE ISOBAR AT P = 600 BAR

T OEN VOL OP/DT OP/ CO E H S CV CP M DEG K MOL/L L/MOL BAR/K BAR-L/HOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

131.094 12.880 .07764 23. 7664 1777.6 C9 1108.0 5766.

4

11 7. 147 75.10 100.21 2020

140.000 12.761 .07836 22. 2827 1676. 195 1963. 0 6664.

7

123.778 76.14 101.61 1961

150.000 12.629 .07918 20. 7829 1573.750 2937.3 7688.3 130. 844 77.43 103.24 1900

160.000 12.497 .08002 19.4328 1481.486 3927.2 8726.2 137. 560 78.82 104.93 1842

170.000 12.367 .08086 18.2111 1397.835 4933.6 9785.4 143.974 60.30 106.67 1787

180.000 12.237 .08172 17.1001 1321. 529 5957.1 10860 .

3

150. 122 81.67 108.47 1735

190.000 12.108 .08259 16.0856 1251.567 6998.3 11953.8 156. 035 83.51 110.31 1686

200.000 11.980 .08347 15.1557 1187. 1 18 8057.

8

13066.2 161. 741 85.22 112. 19 1639

210.000 11.852 .08437 14.3005 1127.5 01 9136.

0

14198.3 167. 261 86.99 114.10 1595

220.000 11.726 .08528 13.5115 1072.1 31 10233.

6

15350.4 172. 614 86.80 116.04 1552

230.000 11.600 .08620 12.7617 1020.546 11350.

7

16522.9 177.815 90.65 118.01 1511

240.000 11.475 .08714 12.1049 972.338 12487.6 17716.2 182. 880 92.54 120.00 1472

250.000 11. 351 .08810 11.4757 927. 163 13644.

7

18930.4 187.819 94.45 122.01 1435

260.000 11.228 .08906 10.6696 884.730 14821.9 20165.7 192. 644 96.39 124.03 1399

270.000 11.105 .09005 10.3426 844.788 16019.4 21422.3 197. 363 98.34 126.06 1364

280.000 10.983 .09105 9.6311 807.122 17237.

1

22700.0 201.984 10 C.30 128.09 1331

290.000 10.862 .09207 9. 3519 771. 546 18474.

8

23998.9 206.515 102.27 130.13 1299

300.000 10.741 .09310 6.9024 737.9 Cl 19732.

4

25318.6 210. 961 104.24 132.17 1268

310.000 10.620 .09416 8.4800 706. 048 21009.

4

26659.

0

215. 328 106.21 134. 21 1238

320.000 10.500 .09523 8.0626 675.867 22305.6 28019.6 219. 621 108.19 136.24 1210

330.000 10. 381 .09633 7.7082 647. 255 23620.

4

29400.1 223. 844 110.16 138. 27 1182

340.000 10.262 .09744 7.3551 620.121 24953.

2

30799.9 228. 002 112.14 140.31 1155

350.000 10.144 .09858 7.0218 594. 384 26303.5 32218.4 232. 099 114.14 142.35 1129

360.000 10.026 .09974 6. 7067 569. 974 27670,

6

33655.1 236.138 116.17 144.43 1104

370.000 9.909 .10092 6.4087 546.830 29054.

3

35109.7 240. 125 118.31 146.62 1079

380.000 9. 792 .10213 6.1266 524.896 30455.5 365 83.2 244. 065 12 0.72 149.06 1055

390.000 9.675 .10336 5.8594 504. 121 31877.8 38079.3 247. 968 123.55 151.93 1032

400.000 9.559 .10461 5.6060 484.459 33333.

0

39609.7 251. 842 126.77 155.16 1010

410 .000 9. 444 .10589 5.3657 465.868 34240.7 40594.1 254. 200 136.54 164.96 984

420.000 9.329 .10720 5. 1377 448. 311 35800.

9

42232.6 258.148 135 .27 163.68 966

430.000 9.214 .10852 4.9212 431.746 37362.4 43873.9 262. 010 136.30 164.71 947

440.000 9.101 .10988 4. 7156 416.143 38935.

4

45528.2 265. 813 137.81 166. 20 929

450.000 8.988 .11126 4.5204 401.467 40522.

8

47198.5 269.567 139.52 167.87 911

460.000 8.876 .11267 4.3349 387.688 42125.

8

48885.9 273.275 141,32 169.63 894

470.000 8.764 .11410 4.1586 374.775 43745.1 50591.1 276. 942 143.18 171.42 878

480.000 8 . 654 .11556 3.9911 362.698 45380.9 52314.3 280. 570 145.07 1 73.22 863

490.000 8. 544 .11704 3.6319 351.4 28 47033.

2

54055.5 284. 160 146.97 175.02 848

500.000 8.436 .11854 3.6806 340 .938 48701.9 55814.5 28 7. 714 148.88 176.80 834

520.000 8.222 . 12162 3.4003 322.1 78 52088.1 59385.5 294. 716 152.67 180.28 809

540.000 8.014 .12479 3.1473 306.181 55537.6 63024.

7

301.583 156.42 183.62 786

560.000 7.811 .12802 2.9191 292.691 59048.1 66729.4 308. 320 160.11 186.63 766

580.000 7. 615 .13132 2.7134 281.435 62617.5 70496.7 314. 929 163.72 189.88 749

600.000 7.426 .13467 2.5281 272. 1 21 66243.7 74323.8 321. 416 167.25 192.80 734

620.000 7.243 .13806 2.3612 264.451 69924.

8

78208.1 327. 784 170.70 195.61 722

640.000 7. 069 .14147 2.2107 258.138 73659.

1

82147.4 334. 037 174.06 198.31 711

660.000 6.901 . 14491 2. 0750 252. 916 77445.

4

86140.

0

340. 180 177.34 200.94 702

680.000 6.740 .14836 1.9524 246. 556 81282.7 90184.4 346. 217 180.54 203.49 694

700.000 6.587 .15182 1.8413 244.869 85169.9 94279.

3

352. 152 183.66 206.00 687

161
Table 22. Continued

I-BUTANE ISCBAR AT P = 700 BAR

T OEN VOL DP/OT DP/CD E H S CV CP W DEG K MOL/L L/MOL BAR/K BAR-L/MOL J/MOL J/MOL J/MOL/K J/MOL/K J/MOL/K M/SEC

133.107 12.909 .07747 24.1075 1856.286 1216. 3 6639.1 11 7. 883 7 5.36 100,37 2062

140.000 12.819 .07801 22.9536 1776.014 1873.9 7334.4 122.977 76.18 101.45 2017

160.000 12.691 .07880 21.4290 1670. 131 2840.4 8356.

3

130. 032 77,46 103.07 1955

160.000 12.563 .07960 20.0572 1574.9 15 3822.6 9394.6 136.737 78.86 104.75 1897

170.000 12.436 .08041 18.8160 1488. 708 4821.

0

10449.9 143. 140 80.34 106.48 1842

180.000 12.310 .08123 17.6875 1410.201 5836.4 11522.9 149.276 81.91 108.26 1790

190.000 12.185 .08207 16.6571 1336.287 6869.

4

12614.2 155. 178 83.56 11 0. 09 1741

200.000 12.061 .08291 15. 7128 1272. 130 7920.5 13724.4 160.872 85.27 111.95 1695

210.000 11.938 .08377 14.8444 1211. 003 8990.3 14853.9 166. 380 87.03 113.84 1650

220.000 11.816 .08463 14.0434 1154. 306 10079.

1

16003.

3

171. 720 68.84 115. 77 1608

230.000 11.695 .08551 13.3025 1101.538 11 187.

3

17173.0 176. 909 90.70 117.71 1568

240.000 11. 574 .08640 12.6154 1052.276 12315.2 18363.1 181.960 92.59 119.68 1529

260.000 11.455 .08730 11.9766 1006.146 13463.1 19574.0 186.886 94,50 121.66 1492

260 .000 11.336 .08821 11.3819 962.859 14630.9 20805.

7

191. 697 96.44 123.66 1457

270.000 11.218 .08914 10.8266 922.143 15818.7 22058.4 196,401 98.39 125.66 1423

280.000 11.101 .09008 10.3074 883.772 17026.5 23332.

0

201. 007 10 0.35 127.66 1390

290.000 10.985 .09103 9.8211 847.550 18254.

1

24626.3 205.522 102.32 129.67 1359

300.000 10.870 .09200 9.3649 813.305 19501.

4

25941.3 209. 952 104.29 131.67 1329

310.000 10. 755 .09298 8.9363 780.890 20767,9 27276.6 214. 302 106.27 133,68 1299

320.000 10.641 .09398 8.5330 750.177 22053.

3

28631.7 218, 573 108.24 135.68 1271

330.000 10.527 .09499 8.1531 721. 052 23357. 1 30006.4 222.783 11 C.22 137.67 1244

340.000 10.415 .09602 7.7948 693.419 24678.7 31400.0 226.923 112.20 139.67 1218

360.000 10.30 3 .09706 7.4564 667.189 26017.5 32811.9 231. 000 114.20 141.68 1193

360 .000 10.191 .09812 7.1367 642.292 27372.9 34241.6 235. 020 116.23 143.72 1168

370.000 10.080 .09920 6.8341 618.646 28 744. 8 35689.0 238.986 118.38 145.87 1145

380.000 9.970 .10030 6.5477 596.2 02 30133.8 37154.8 242.906 120.78 148.27 1122

390.000 9.861 .10141 6.2762 574. 903 31 543.

9

38642.8 246. 788 123.62 151.11 1099

400.000 9. 752 . 10254 6.0188 554.698 32986.8 40164.9 250.641 126.84 154.31 1077

410.000 9.644 .10369 5.7745 535.541 33881.9 41140.6 252.977 136.62 164.07 1051

420.000 9.536 .10436 5.5426 517.391 35429.6 42770.0 256.904 135.34 162.77 1034

430.000 9.429 .10605 5.3222 5 0 0.2 08 36978.

5

44402.0 260. 744 136.38 163.77 1016

440.000 9.323 .10726 5.1128 483.956 38538.8 46046.8 264. 525 137. 89 165.23 998

460.000 9.218 .10848 4.9137 468.600 40113.6 47707.3 268. 257 139.60 166,89 981

460.000 9. 114 .10972 4.7243 454.1 06 41704.

0

49384.8 271.944 141.41 168.63 965

470.000 9.010 .11099 4.5441 440.440 43310.9 51080.0 275.539 143 .27 170.41 949

480.000 8.907 .11227 4.3726 427.577 44934.

4

52793.1 279. 196 145. 16 172.21 934

490.000 8.806 .11356 4. 2093 415.486 46574,7 54524.3 262. 765 147.07 174.02 919

600.000 3. 705 .11488 4.0539 404.139 48231.

8

56273.4 286. 299 148.97 175.81 905

620.000 8.506 .11756 3.7649 383.566 51595.6 59824.9 293. 263 152.77 179.33 880

540.000 8.312 .12030 3.5028 365 • 644 55024.

6

63445.9 300. 096 156.52 182.75 857

560.000 8.123 .12310 3.2650 350. 159 58516.8 67134.0 306. 802 160. 21 186.05 836

680.000 7.939 .12595 3.0492 336. 895 62070.

1

70886.

9

313. 386 163.82 189.22 818

600.000 7.761 .12884 2.8533 325.626 65682.7 74701.9 319.852 167.36 192.26 802

620.000 7.589 .13177 2.6755 316.122 69352.6 78576.5 326.205 170.81 195.18 788

640.000 7.423 .1 3472 2.5141 308.150 73078.

0

82508.5 332. 446 174. 17 198.00 776

660.000 7. 263 .13769 2.3674 301.463 76857.3 86495.7 333. 581 177.45 200.71 765

680.000 7.109 .14067 2.2339 295.9 05 80689.

2

90536.3 344. 612 180.65 203.34 75 6 700.000 6.961 .14367 2.1123 291.222 84572.3 94626.9 350.543 183.76 205,90 749

162
o

o

oo

o

PROGRAt' IBUTHRMdNPUT, OUTPUT)

C I-BUTANE THERMOFUNCTIONS ON ISOBARS, START OCT. ?3, 1978.

NEW XEF, OENGASF, EOELF, FOR LOW DENSITIES.

FREEZING LIQUID DEN., (D/DT) = (T/T T

) *• ( 0 . 2 35 ) , GRAPH., PROPANE.

CCMMCN GK,GKK, B1,B2,B3,B4, E1,ER, IX COMMON/1/AL,B£,GA,OE,EP, OCRT, TCRT ,PCRT, OG A T, OTRP , T TRP , PTRP

COMMCN/3/CPDT,02PDT2,OPSDT,DPMDT,OPDO,OPDR,OTSDR,OTHOR

C0MMCN/4/XB1 ,XB2 , XCl,XC2, XE1,XE2, OXBDR, DXC OR, OXEDR

COMHON/5/ OOSOT

COMMCN/6/ TSAT, THETA, PSAT

COMMON/8/ IN, IK, P,T,DEN, E,H,S, CV,CP,CSAT, H,HK

COMMCN/9/ ONG,EG,HG,SG, CVG,CPG,WG, DPGOT,OPGDO

COMMCN/12/ DELS, OELCV

COMMCN/13/ ZCRT,ZSAT,DZSDT,ZFX, FRT,OFRTDT

COMMON/99/ TI,EZZ, EZ,SZ,CVZ, HZ,CPZ

DIMENSION PP(99)

1 FORMATdS, 2F10.0)

2 F0RMAT(I5, 3F10.0)

3 FORMAT(8I10)

5 FORMAT(IX)

9 FORMAT (8F10.0)

14 FORMATdHl 18X *I-3UTANE ISOBAR AT P =* F8.5, 4H BAR /)

15 FORMATdHl 18X *I-BUTANE ISOBAR AT P =* 14, 4H BAR /)

16 F0RMAT(19X IHT 6X3HDEN 6X3HV0L 5X5H0P/0T 5X5HDP/00

2 8X1HE 8X1HH 8X1HS 6X2HCV 6X2HCP 5X1HW /

3 15X 5HDEG K 4X5HM0L/L 4X5HL/M0L 5X5HBAR/K 1X9HBAR-L/M0L 4X5HJ/M0L

4 4X5MJ/M0L 2X7HJ/M0L/K 1X7HJ/M0L/K 1X7HJ/M0L/K 1X5HM/SEC ) 17 FORMATdOX F10.3, F9.3, F9.5, F10.4, F10.3, 2F9. 1, F9.3 , 2F8 .2 , 16)

18 FORMATdOX FlO.3, F9.5, F9.3, F10.6, FlO.3, 2 F9 . 1 , F9 . 3 , 2F8 . 2 , 16 ) 30 CALL PVTDATA

COMPUTE thermofunctions ON ISOBARS. START ON THE MELTING LINE.

ISOBARS AT P UNDER PCRT TRAVERSE THE DOME.

NOTE USE OF QVAP ,OATA, TO CROSS THE ,DOME,.

NOTE USE OF CSAT ,OATA, FOR SPECIFIC HEATS IN COMPRESSED LIQUID.

90 IN = 1 $ NI = 57 S READ 9, ( PP < I ) , 1= 1 , NI

)

91 DO 300 I=IN,NI 5 IP = P = PP(I) I IK = I S LS = 0 92 IF(P-IP) 93,94

93 PRINT 14, P i GO TO 95

94 PRINT 15, IP

95 PRINT 16 96 IF(I.E0.26) P = PCRT

100 T = FINDTMF(P) 5 CALL COMPRLO f V=l/OEN S IH=W

101 PRINT 17, T,DEN,V,OPOT,OPDD, E , H , S , C V , CP , I

W

102 IT = T/10 $ IF(P.LT.PCRT) 110,180

C

C CASES FOR P LESS THAN PCRT.

110 TS = FINOTSF(P) B K = L = 0 111 DO 150 J=l,99 t T = JT = 10*(IT+J)

112 IF(T.LT.TS) 115,117

115 CALL COMPRLQ $ V=l/OEN B IW=W

116 PRINT 17, T,OEN,V,OPDT,DPOD, E , H , S , C V , CP , I W B GO TO 150

117 LS = LS + 1 fi IF(LS.EQ.1I 120,130

CASE FOR SATURATED LIQUID AND VAPOR.

120 T = TS ? CALL COEXIST

123 V=1/CEN B VG=1/DNG B IW=H B IWG=HG

124 PRINT 17, T,OEN,V,OPDT,OPOO, E , H , S , C V , CP , I W t PRINT 5 125 IF(P.LT.30) 126,127

163
126 PRINT 18, T,ONG,VG,DPGOT,OPGOO, EG , HG , SG , C VG ,CPG , I WG S GOTO 128

127 PRINT 17, T,ONG,VG,OPGOT,OPGDO, EG , HG, SG , C VG , CPG , I WG 128 T = JT

_ CASES FOR THE HOMOGENEOUS DOMAIN.

130 IF ( JT.GT .500) 131,132

131 K = K+1 $ T = JT = JT 10*K $ IFCJT.GT.700) 300,132

132 CALL GENEOUS « V = 1/DEN t IW = W 133 IF(P.LT.30) 134,135

134 PRINT 18, T,OEN,V,OPOT ,OPOO, E,H,S, CV,CP,IW $ GO TO 150

135 PRINT 17, T,OEN,V,OPOT,OPOO, E,H,S, CV,CP,IW

150 CONTINUE

C

C FCR P ABOVE PCRT, CASES FOR T . LT . OR . T . GT . TC RT

.

180 K=L=0 I DO 250 J=l,99 S T = JT = 10»(IT+J)

181 IF{T,lT.TCRT) 192,210

C CASE A FOR T LESS THAN TCRT.

192 CALL COMPRLQ $ V=l/OEN S IW=W

193 PRINT 17, T,D£N,V,OPOT,OPOD, E , H , S, C V, CP , I W $ GO TO 250

C CASE FOR T ABOVE TCRT, HOMOGENEOUS DOMAIN.

210 IF( JT.GT. 500) 211,220

211 K = K+1 $ T = JT = JT + 10»K S IF (JT.GT. 700) 300,220

220 CALL GENEOUS $ V = 1/OEN $ IW = W 221 PRINT 17, T,OEN,V,OPOT,DPOD, E , H, S , C V , CP , I

W

250 CONTINUE

300 CONTINUE

999 STOP $ END

SUBRCUTINE COMPRLQ

C GIVEN P,T FOR COMPR.LIQ. AT T.LT.TC, GET OEN AND FUNCTIONS.

REVISED TO USE HSATF, SSATF, CSATXF, BUT NOT COEXIST. TIMESAVER.

^ INTEGRATE ALONG ISOTHERM T FROM SATLIQ UP TO POINT (P,T).

COMMON/3/OPOT,D2PDT2,OPSOT,DPMOT,DPOD,OPOR,DTSOR,DTHOR

COMMCN/5/ OOSOT

COMMON/8/ IN, IK, P,T,OEN, E,H,S, CV,CP,CSAT, W,WK

COMMON/12/ DELS, DELCV

DATA (TCRT=408.00)

1 FORMATdHO 9X »T NOT UNDER TCRT IN COMPRLQ.*/)

2 IF(T.GE.TCRT) 3,4

3 PRINT 1 S STOP

C GET PSAT, OENLIQ, AND SATLIQ FUNCTIONS FOR START.

4 PS = PSATF(T) $ OL = OENLIQF(T) S ODLDT = DOSDT

6 HS = HSATF(T) $ ES = HS - 100*PS/OL $ SS = SSATF(T)

7 IF(T.GT.340) 8,9

3 CVS = CVSATF(T) S GO TO 10

9

PX=PVTF(T,DL,0) $ CVS = CSATXF(T) + 10 0*T*DPDT*DOLOT/DL/DL

C INTEGRATE UP TO POINT (P,T).

10 DB = FINOENF(T,P) $ DX = DB - OL S IF(OX.GT.O) 11,20

11 N = DX*10 +5 $ E = ES EOELF(0,N,T,DL,OB)

12 H = E + 100*P/OB f S = SS DELS S CV = CVS DELCV

13 PX = PVTF(T,OB,l) f CP = CV + 10 0* T/DPOO* ( OPOT/03) **2

14 W = SORT (HK*CP*DPOO/CV) S DEN =03 $ RETURN

20 OEN=OL S E=ES S H=HS S S=SS S CV=CVS I PX = PVTF(T,OL,l)

21 CP = CV 100*T/DPDD* (0PDT/0L)**2 ? W = SORT (WK*CP*0PD0/CV

)

30 RETURN $ END 164
SUBROUTINE COEXIST

GIVEN T AT COEXISTENCE* GET BOTH VAPOR AND LIQUID FUNCTIONS.

FOR VAPOR, GET ONG , EG ,HG , SG , CVG,CPG,HG, OPGDT,OPGOO, - FOR LIQUID, GET OEN,E,H,S, CV , CP ,CSA T , M. OPOT.DPOO.

COEXIST CALLED BY COMPRLQ. P NOT USED, MUST NOT CHANGE.

COMMON/l/AL,BE,GA,DE,EP, OCRT, TCRT,PCRT, DG A T, OT RP , TTRP , PTRP C0MM0N/3/0PDT,D2P0T2,DPSDT,DPMDT ,OPOO,DPOR,OTSDR,DTHDR

COMMON/5/ DDSDT

COMMON/8/ IN, IK, P,T,OEN, E,h,S, CV,CP,CSAT, W,WK

C0MMCN/9/0NG,EG,HG,SG, CVG,CPG,MG, OPGOT.OPGOO

COMMCN/12/ DELS, OELCV

COMMON/99/ TI,EZZ, EZ,SZ,CVZ, HZ,CPZ

DATA (Q=l. 01325) , (G=0. 083145)

1 FORMATdHO 9X *T EXCEEDS TCRT IN COEXIST. / ) 2 IF(T.GT.TCRT) 3,4

3 PRINT 1 S STOP

4 PS = PSATF(T) t ONG = D8 = OENGASF(T)

5 TI = T $ CALL IDEAL $ N = DB*20 + 10

6 EG = EZZ * EZ * EOELF(1,N,T,0,OB) t HG = EG + 100*PS/OB

7 SG = SZ DELS - 10 0*G*ALOG ( G* T»DB/Q)

8 IF(T.EQ.TCRT) 9,11

9 PX = PVTF(T,OB,l) S OPGOT = OPOT $ DPGOO = DPOO

10 CPG = CVG = HG = 0 f GO TO 15

11 CVG = CVZ DELCV S PX = PVTF(T,OB,l)

12 CPG = CVG 100»T/OPOO*(OPOT/OB) **2 $ HG = SORT ( HK*CPG *080 O/CVG

)

13 OPGOT = DPDT S DPGDO = DPOD

NOH TRAVERSE THE ,OOME, USING QVAP ,OATA,.

15 DEN = CL = OENLIQF(T) $ DDLOT = DDSDT $ QV = QVAPXF(T)

16 H = HG - QV i S = SG - QV/T t E = H - 100»PS/DL

17 IF(T.EQ. TCRT) 18,19

18 PX = PVTF(T,OL,l) $ CP=CV=CSAT=H=0 f RETURN

19 CSAT = CSATXF(T) $ PX = PVTF(T,OL,l)

20 IFCT.GT.340) 21,22

21 CV = CVSATF(T) I GO TO 23

22 CV = CSAT 100*T*OPDT*ODLDT/OL/OL

23 CP = CV 100*T/DPOO* (OPOT/DL) **2

30 H = SQRT (HK*CP*OPOO/CV) S RETURN $ END

FUNCTION CSATXF(T)

THIS CSATXF(T) VIA IBUTHRM, NOV. 1, 1978. R.O.G.

SSAT = SCRT A*U**ES B*LN(X) C*U «• 0*U**2 E*U**3,

HHERE X E T/TCRT, U E (1-X).

CSAT = -ES*A*X/U** (1-ES) B - C* X - 2*0*X*U - 3*E*X»U**2.

DATA (ES=0.45) ,<TCRT = 408.0 ),(A = - 35. 97387860) ,(8 = 87.70514 205) , 1 <C=-45.80245863) , (0=0 .19432181) ,( E= 15.98164931

)

1 FORMATdHO 9X 3HT =F10.5, • IN CSATXF(T). • / ) 2 IF(TCRT-T) 3,4,5

3 PRINT 1, T S STOP

4 CSATXF =0 S RETURN

5 X = T/TCRT $ U = 1.0 - X f XE = U**(1-ES)

6 CSATXF = -ES*A*X/XE B - C*X - 2*0*X*U - 3*E*X*U*U

9 RETURN t END
SUBROUTINE DASTHRM

COMPARE OAS/REEO/£UBANK« 1973) ON T = 4AQ K ISOTHERM - ISOBUTANE

GIVEN P,ATM, Z, -(H-HZ) CAL/MOL. - ( S-S Z) C A L/ MOL/K.

COMMON/8/ iNtIK, P,T,DEN, E,H,S, CV»CP,CSAT, W,WK

COMMON/99/ TI,EZZ, EZ»SZ,CVZ, hZtCPZ

DATA (CK=4. 184) ,(R=0. 083145)

1 FORMAT(4F10.0)

2 FORMATdHl 9X ’COMPARISONS WITH DAS ET AL (1973) FOR ISOBUTANE AT

IT = 440 K,*/10X’UNITSt BARS, MOLES, LITERS, JOULES, KELVINS. ’ //

2 10X5HP,BAR 5X5HM0L/L 6X4HCALC 4X4HPCNT

3 4X6H(H-HZ) 6X4HCALC 4X4HPCNT 4X6H(S-SZ) 6X4HCALC 4X4HPCNT ) 3 FCRMAT(5X 3F10.3,F8.2, 2F10.1,F8.2, 2F10.3,F8.2)

10 T = 440 $ PRINT 2 $ 00 20 J=l,30

11 REAO 1, PA, Z, HX, SX t IF(PA) 12,30

12 P = 1.01325*PA $ HX = -CK’HX S SX = -CK’SX 5 DX = P/I/R/J

13 CALL GENEOUS S DPCT = 10 0 * ( DX/DEN- 1

)

14 H = H - EZZ - HZ J S = S - sz

15 HPCT = 100 (HX/H-1) $ SPCT = 100’(SX/S-1)

20 PRINT 3, P, OX,OEN,OPCT, HX,H,HPCT, SX,S,SPCT

30 RETURN S ENO
OO

O

O

f

function CVSATF(T)

C ISOBUTANE CV ON SATLIQ BOUNDARY NEAR THE C.P. NOV. 5,

VALID ONLY FOR T NOT LESS THAN TZ = 340 K. CV = CVZ A*X B*X4/(1-X) **0. 1, X = ( T- T Z ) / ( TC -T Z )

.

DATA (TZ=340.0», (TC=408.0) ,(TN=68.0)

DATA (CVZ=111.87),(A=13.48),(B=5.38),(E=0.1)

1 FORMATdHO 9X 3HT =F10.5, * IN CVSATF(T). / ) 2 IF (T.LT. TZ.OR. T.GE.TC) 3,4

3 PRINT 1, T S STOP

4 X = (T-TZ>/TN $ X2 = X’X $ XE = (1-X)*»E

5 CVSATF = CVZ A»X B»X2*X2/XE S RETURN « END

FUNCTION OENGASF(T)

C FOR I-BUTANE, R.O.G., OCT. 23, 1978.

VALID FOR TC=408.00, DC=3.86, PC= 36. 5468523 ONLY.

DESIGNED FOR ZSAT = 1 AT LOW DENSITIES, 5/29/77.

USE ZSAT E PS/DS/GK/TS WITH VAPOR PRESSURES, ANO ZCRT.

Z = 1 + (ZCRT-1)*PI*F(X)/X/X.

F(X) = 1 Al*VE + A2*V A3*EXP(EGX* (1-1/V) )

.

NOTE ZSMl FOR FUGACTY, NOT IN COMMON HERE.

C0MMCN/3/DPDT,D2PDT2,0PSDT,0PMD'^,DP0D,DP0R,0TSDR,0TH0R

COMMON/5/ DDSOT

COMMCN/13/ ZCRT, ZSAT ,DZSDT ,ZFX , FRT,OFRTOT

DIMENSION AV(3)

DATA (OCRT=3.86),(TCRT=408.00),(PCRT=36.548852467)

DATA (EG=0.35) ,(EGX = 3.60), (GKK=0. 083145)

OATA(AV = -0.764051836, 0.6?0501182, 30.75066326)

1 FORMATdHO 9X 3HT =F12.5, • IN DENGASF. * / ) 2 IF(TCRT-T) 3,4,5

3 PRINT 1, T S STOP

4 DENGASF = OCRT S DDSOT = 1.0E*10 S RETURN

5 ZN = ZCRT-1 1 FC = PCRT t P = PSATF(T)

6 PI = P/PC S PIT = OPSDT/PC

7 TC = TCRT S X = T/TC $ X2 = X*X 1 V - 1-X t 8 VE = V**EG S V£1 = -£G*VE/V

9 EGXV = EGX*d- 1/V) I IF(EGXV.LT.-290) 10 11 10 XP = XPl = 0 S GO TO 12

11 XP = EXP (EGXV) S XPl = -EGX*XP/V/V

12 F = 1 .0 * AVd) *VE AV(2)*V AV(3) •XP

13 FI = AV( 1) »VE1 - AV(2) AV(3)*XP1 t ZFX = F 15 ZSMl = ZN*PI*F/X2 f ZSAT = Z = 1 + ZSMl

16 DZSOT = DZDT = (PI* (FI -2*F/X) /TC F •PIT )

ZN/X2

17 DENGASF = P/T/Z/GKK

18 DOSDT = (DPSOT - P/T - P*D ZDT/Z) /T/Z/GKK S RETURN

19 78.

= -1

END

167
FUNCTION OENLIQF(T)

C FOR I-BUTANE, ROG, OCT. 23, 1978.

QEN = OCRT + YNL*(X (XE-X)*Y), YNL = OTRP - OCRT.

Y = A1 A2*X2 A3*X3.

CONHON/5/ OOSOT

DIMENSION AW(3)

OATA (EL = 0.35)

DATA (0CRT = 3.86) , (DTRP = 12 . 755) , ( TTRP = 113 . 55) , ( TC RT=4 0 8 . 0 0

)

OATA(AW = 0.786913448, -0.142753535, 0.057698164)

1 FORMATdHO 9X OENLIQF = 0, T EXCEEDS TCRT. * / ) 2 IF(TCRT-T) 3,4,5

3 PRINT 1 I STOP

4 DENLIQF = OCRT I DDSDT = -l.OE+10 5 RETURN

5 XN=TCRT-TTRP 5 X= ( TCRT -T) /XN S X2 = X*X i OXDT = -1.0/XN

6 XE = X**EL S V=XE-X S VI = EL*XE/X - 1 8 Y = AW(1) + AW(2)*X2 AW(3)*X*X2 S YNL = OTRP - OCRT

9 Y1 = 2*AW(2)*X 3*AW(3)*X2

11 DENLIQF = OCRT YNL*(X V*Y)

12 OOSOT = YNL*(1 + V*Y1 V1*Y)*0X0T S RETURN S END

FUNCTION EDELF (L,N,T,0A,DB)

C SPECIAL REVISION FOR VERY LOW DENSITIES.

GET CHANGE OF £, S, CV WITH DENSITY ALONG ISOTHERMS.

GET EDELF, DELS, OELCV FROM DA TO OB ON ISOTHERM T. COMMON/1 /AL, BE ,GA,OE,EP, OCR T , TCRT , PCRT , OGA T,OTRP,TTRP, PTRP

COMMCN/3/DPOT,D2POT2,DPSDT, DPMOT, OPD 0, DPOR ,OTS DR , OTHOR

COMMCN/12/ DELS, OELCV

COMMON/13/ ZCRT,ZSAT ,OZSOT,ZFX, FRT,OFRTDT

OATA (G = 0.083145)

1 ZK = 1.0 - 1/ZCRT S RK = G*TCRT/DCRT « E=S=CV=0

2 OX = (OB-OA)/N $ IF(OX) 3,30

3 DO 15 J=1,N 3 ON = DA {J-0.5)*DX

4 OXN = DX/ON/ON $ P = PVTF(T,ON,0) B CV = CV - D2P0T2*0XN

5 IF (ON. LT. OCRT) 7,9

7

E = E (ZK*ZSAT»ZFX + FRT - T*OFRTOT) *RK*OX B GO TO 10

9 E = E (P - T*OPOT)*OXN

10 IF(L.EQ.O) 11,12

11 S = S - OPOT*DXN S GO TO 15

12 S = S (G - OPOT/ON)»OX/DN

15 CONTINUE

16 EDELF = 100*E $ DELS = 10Q*S I OELCV = 1Q0*T»CV B RETURN

30 EOELF = DELS = OELCV =0 $ RETURN B END

168
FUNCTION FINDENF(T,P)

C ON ISOTHERM T» FIND DEN, MOL/L, TO MINIMIZE (P-PC) VIA EQNSTATE.

COHMCN/1 /AL,BE ,GA,OE ,EP, OCR T , TC RT , PCRT , DGA T, DT RP , T TRP , PT RP C0MMCN/3/0PDT,D2P0T2,DPS0T,0PM0T,DP00,0P0R,0TS0R,0TH0R

DATA (DM = 13. 5) , (GKK=0. 083145)

41 FORMATdHO 9X FINDENF = 0, FAILS TO CONVERGE. • / ) 42 FORMATdHO 9X *FINOENF = DCRT, OP/DR ZERO OR NEG. • / ) 43 FORMATdHO 9X *FINOENF = 0, DOUBLE- VALU ED AT P = PSAT. * / ) IF(P.GT.O) 1,35

1 IF(T-TCRT) 2,5,8

2 DG=OENGASF(T ) S OL=OENLIQF ( T ) S PS=PSATF(T) £ IF(P-pS) 3,32,4 30= OG/2 $ GO TO 11

4 D = (DL+0TRP)/2 $ GO TO 11

5 OG=OL=OCRT £ PS=PCRT $ IF(P-PS) 6,33,7 60= OCRT/2 £ GO TO 11 70= 2*0CRT £ GO TO 11

3 IF (T .LT. 450. 0) 9,10

9

PC = PVTF (T,OCRT, 0) £ IF(P-PC) 6,33,7

10 0 = CCRT

11 00 30 J=l,50 £ DP=P-PVTF(T,0,1) S IF(ABS ( OP/P ) - 1 . 0 E- 6 ) 31,31,12

12 IF (OFOD. GT. 0 ) 13,34

13 DO = DP/OPOD $ IF(ABS ( 00/0 ) -1 . 0 E-6 ) 31,31,14

14 0 = C + 00 £ IF(D.GT.O.O) 16,15

15 0 = P/GKK/T £ GO TO 30 16 IF(O.GT.OM) 17,18

17 0 = DM £ GO TO 30 18 IF(T-TCRT) 19,24,30

19 IF(P.LT.PS) 20,22

20 IF(O.GT.OG) 21,30

21 0 = OG £ GO TO 30 22 IF(O.LT.OL) 23,30

23 D = OL £ GO TO 30 24 IF (P .LT. PCRT) 25,27

25 IF(O.LT.DCRT) 30,26

26 0 = OCRT - 0.02 £ GO TO 30 27 IF (O.GT. DCRT) 30,28

28 D = OCRT + 0.02

30 CONTINUE £ PRINT 41 $ STOP

31 FINOENF =0 £ RETURN

32 PRINT 43 £ STOP

33 FINOENF = OCRT £ RETURN

34 FINOENF = OCRT £ PRINT 42 £ RETURN

35 FINOENF=OPOT=02POT2=0 £ OPDO=GKK*T £ OPDR=OPOO*DTRP

36 RETURN £ END

function FINOTMF(P)

C GIVEN P ON THE MELTING LINE, FIND T FOR I-9UTANE.

COMMON/l/AL, BE, GA,OE,EP, OCRT , T C RT , PCRT , OGA T, OTRP, TTRP, PTRP data (A = 430. 0) , (E=6. 08)

1 X = (P-PTRP)/A + 1 £ FINOTMF = T T RP • X * • ( 1 . 0 /E ) £ RETURN £ END

169
o

o

FUNCTION FINDTSF(P»

C GIVEN VAPOR PRESSURE P, ITERATE T TO MINIMIZE (P-PC).

COMMCN/l/AL ,3E,GA,DE,EPt OCRT , TCRT , PCRT , 0GAT,0TRP, TTRP, PTRP C0MMCN/3/DP0T»D2PDT2,0PS0T,0PMDT,0PD0,0PDR,0TS0R,DTH0R

1 FORMATdHO 9X FINDTSF = 0, FAILS TO CONVERGE. * / ) 2 FORMATdHO 9X *FINOTSF = 0, P EXCEEDS PCRT. » / ) 3 IF(P-PCRT) 4,11,12

4 T = 30Q S DO 9 J=l,50 S DP = P - PSATF(T) $ ADP = A9S <DP)

5 IF (AOP/P-1. OE-6) 10,6,6

6 IF(ADP/DPSOT/T-1.0E-6) 10,7,7

7 T = T OP/OPSDT S IF(T-TCRT) 9,9,8

8 T = TCRT

9 CONTINUE $ PRINT 1 S STOP

10 FINOTSF = T S RETURN

11 FINOTSF = TCRT S RETURN

12 PRINT 2 ? STOP $ END

SU9RGUTINE GENEOUS

C GIVEN P,T FOR THE HOMOGENEOUS DOMAIN - GET DEN AND FUNCTIONS AT ANY TEMPERATURE.

C0MMCN/3/DPDT, 02PDT2,0PSDT, DPMDT, OPOO,OPOR, 0TSDR,0THDR

COMMCN/8/ IN, IK, P,T,DEN, E,H,S, CV,CP,CSAT, W,WK

COMMCN/12/ DELS, OELCV

COMMCN/99/ TI,EZZ, EZ,SZ,CVZ, FZ,CPZ

DATA (0=1.01325) , (G=0. 083145)

3 TI = T $ CALL IDEAL S IF(P.GT.O) 4,10

4 DEN = 08 = FINOENF(T,P) S N = 08*20 10

5 E = EZZ + EZ + EOELF(1,N,T,0,OB) $ H = E 100*P/D8

6 S = SZ * DELS - 100*G*ALOG (G*T*D8/Q)

7 CV = CVZ DELCV S PX = PVTF(T,DB,1)

3

CP = CV * 100*T/OPOO*(OPOT/OB)**2

9 W = SORT (WK*CP*DPDD/CV) $ RETURN

10 OEN=S=0 $ £ = EZZ + EZ 5 H = E + 100*G*T t CV=CVZ $ CP=CPZ

12 W = SORT (WK*CP*G*T/CV) $ RETURN $ END

FUNCTION HSATF(T)

C I-BUTANE SATLIQ ENTHALPY, J/MOL.

THIS HSATF(T) VIA IBUTHRM, NOV. 1, 1978. R.O.G.

FOR 30 POINTS, 120 THRU 408 K, RMSPCT = 0.027,

DEFINE YH i ( H-HC ) / ( HT - HC ) , X E ( TC-T ) / < TC-T T ) , WHEN - YH = X + (XE-X)*(A1 + A2*X + A3*X2 + . . .) DIMENSION AH (3)

DATA (TTRP=113.55), (TCRT=408.00)

DATA (NFH = 3) , (EH=0.5) , (HTRP=0, 0 ) , ( HCRT = 43 739 . 1 8 2

)

OATA(AH = 0.4016094798, 0.4044226707, -0.1374834999)

1 FORMATdHO 9X 3HT =F10.5, * IN HSATF(T).*/)

2 IF(T .GT.TCRT) 3,4

3 PRINT 1, T S STOP

4 X = (TCRT-T) / (TCRT-TTRP) t IF(X.LE.O) 5,6

5 HSATF = HCRT S RETURN

6 V = X**EH -X $ FX=X I DO 7 K=1,NFH

7 PX = FX * V*AH(K)*X**(K-1)

8 HSATF = HCRT - (HCRT-HTRP) *FX $ RETURN ? END 170
SU3R0UTINE IDEAL

C I-BUTANE, VIA DATA OF CHEN ET AL (1975).

CPZ/R = 4 (A1 A2/X A3/X2 . . )*EXP(-E/X), X = T/100.

COMMON/99/ TI,EZZ, EZ,SZ,CVZ, FZ,CPZ

DIMENSION A(7)

DATA (E=6.40),(R=d.3145),(HI=7.26243166) ,(51=35.59759)

OATA(A = 43.59076, -40.54350, 739.72837, -3137.57293,

1

7742.53382, -7583.91994, 3251.25208)

1 NK = 7 $ XI = Tl/lOO S XP = EXP(-E/XI)

2 CP = 4.0 S DO 3 K=1,NK

3 CP = CP + A (K) *XP*XI** (1-K)

C NUMERICAL INTEGRATION FOR HZ/R, SZ/R - 5H=S=0 B N= ABS(TI-300)/4 +4 S OX = (XI-3)/N

6 DO 10 J=1,N B X = 3.0 + (J-0.5)*DX B XP = EXP(-E/X)

7 CPX = 4.0 B DO 8 K = 1 ,NK

8 CPX = CPX + A(K) XP*X'»»(1-K)

9 H = H CPX*OX B S = S CPX*OX/X

10 CONTINUE B H = (HI*3 + H)/XI B S = SI + S C CONVERT TO .OULES, MOLES, KELVINS.

11 HZ = R*TI*H S EZ = HZ - R*TI $ SZ = R*

S

12 CPZ = R*CP S CVZ = CPZ - R f RETURN B END

SUBROUTINE ISOTHRM

C PRINTOUT THE CRITICAL ISOTHERM.

COMMON/l/AL,BE,GA,DE,EP, DCRT , TCRT , PCRT , OGAT , DTRP , T TRP , PT RP COMMCN/3/OPOT,02POT2, OPSOT,DPMDT,OPOO,OF05,DTSOR,OTHOR

C0MMCN/4/XBl,XB2, XCl,XC2, XE1,XE2, DX8DR, DXCDR, OXEOR

COMMON/6/ TSAT, THETA, PSAT

1 FORMATdHl 14X *THE CRITICAL ISOTHERM, IS09UTANE * //

1 6X4HTC =F7.2, 6H, DC =F5.2, 6H, PC =Fll,7,

2 . AT THE C.P., OPS/DT =* F8.5, 9H, OP/OT =F6.5//

3 6X4HD/0C 9X5HTS/TC 9X5HPS/PC 10X4HP/PC 9X5HDP/0R 4X6H0TS/DR

4 4X6HDTH/DR 4X6H0PS/DR 4X6HDXB/0R 4X6HDXC/DR ) 2 F0RMAT(2X F8.2, 3F14.10, F14.9, 5F10.5)

3 PC = PVTF(TCRT,DCRT,0)

4 PRINT 1, TCRT, DCRT, PCRT, 9PS0T,0P0T S DO 8 J=l,31

5 DR = 0.84 0.01*J $ ON = OR*OCRT

6 PR = PVTF(TCRT,ON,l)/PCRT $ DPSOR = OPSOT’DTSDR

7 TSN = TSAT/TCRT B PSN = PSAT/PCRT

8 PRINT 2, OR, TSN, PSN, PR.DPDR, OTSOR ,OTHOR, DPSOR, OXBOR,OXEDR

9 RETURN B END

FUNCTION PMELTF(T)

C I-BUTANE melt-line. REEVES, SCOTT, AND BA93(JP),

J. CHEM. PHYS. 40(12), 3662 (1964).

V. PRIVATE COM. VIA S . E . BA 3B , JR . , OCT. 2, 1978 . C0MM0N/1/AL,BE,GA,DE,EP, DCRT, TCRT, PCRT, 0 GA T , DTRP , T TRP , PTRP

CO MMON/3/OPDT, D2P0T2, OPSOT ,DPMOT,OPOO,DPDR , OTSOR, D THOR

DATA (A=430. 0) , (E=6. 08)

1 X = T/TTRP B XE = X**E B PMELTF = PTRP A*(XE-l)

2 OPMOT = A*E*XE/X/TTRP B RETURN B END

171
SUBROUTINE JTLOCUS

C DERIVE THE J-T INVERSIO^ CURVE. USE ROUTINE DEL T AF ( T , 01 »

.

COMMCN/l/AL,BE,GA,OEfEP. OCRT , TC RT , PORT , DGAT,DTRP,TTRP, PTRP DIMENSION TT(99) ,PP(99) »DN<99)

DATA (A = 2.60) ,(B=O.50) ,(TZ=500.0)

1

FORMATdHl 16X *TH£ JOULE-THOMSON INVERSION LOCUS FOR T-BUTANE*//

1 17X3HT,K 5X5HP,BAR 5X5HM0L/L 7X3HT.K 5X5HP,BAR 5X5HM0L/L)

2 FORMATd OX 110, FIO. 1, F 10 .2, 110, FIO. 1 , F 10..2) 5 TA = 340 B NP = 52

6 PRINT 1 f 00 25 1 = 1, NP B OX = 1 .6

7 T = TA 10*1 S U = T/TZ B 01 = EXP( A -3*U)

10 IF(T-TCR T) 11,12,12

11 OL = OENLIQFJTI S IF (DI- DL) 25,12 ,12

12 SS = DEL TAF (T,DI) $ DO 20 IT = 1, 20

14 D=OI-DX S SL=0ELTAF( T, 01 B 0 = 01 + 0X B SP= OELTAF (T,D)

15 IF(SS-SL ) 18,16 ,16

16 IF(SP-SL ) 19,17 ,17

17 SS s SL $ 01 = 01 - OX B GO TO 20

13 IF(3S-SP ) 20,20 ,19

19 SS = SP $ 01 = 01 ox

20 OX = ox/ 2 23 TT < ]J = T S ON(I) = 01 B PP(I) = PVTF (T, 01,> 0) 25 CONTINUE B N = NP/ 2 s DO 29 J=1 ,N

26 IT = TT( J) 2 ITT = T T ( J + N)

29 PRINT 2, IT, FP(J) ,ONl( J ), I TT, PP( J+N ) ,0N(

J

+ N) 30 RETURN S END

FUNCTION OELTAF(T,D)

C GET (T*DP/DT - D*OP/DD) FOR THE J-T INVERSION CURVE.

C0MMCN/1/AL,8E,GA,D£,EP, OCRT , TCRT , PCRT , 0 GAT , OT RP , TTRP , PT RP CO MM ON/ 3 /OP OT , DEPOT? , D^SOT , OPMOT , OPOD, DP OR , 0 TSOR , DTHOR

1 IF(T-TCRT) 2,4,4

2 DL = DENLIQF(T) B IF{D-OL) 3,3,4

3 OELTAF = I.QE+100 $ RETURN

4 P = PVTF(T,0,1)

5 DELTAF = ABS ( T DP0T-0*0PDD ) B RETURN B END

172
SUBROUTINE PEEK

C EXAMINE BEHAVIOR OF THE COEFFICIENTS.

3(S) = 91 02*EXP(0E*S) t E(S) E El* ( S-1 ) * ( S-ER) *EXP ( -G A*S** IX)

WHERE, R = DEN/OTRP, S E DEN/DCRT.

COMMON GK,GKK, B1,B2, 83,84, E1,ER, IX COMMON/l/AL ,8E,GA,0E,EP, OCRT, TCRT ,PCRT, OGA T , OTRP , TTRP , PTRP

COMMON/6/ TSAT, THETA, PSAT

4 FORMATdHl 14X *EQNSTATE COEFFICIENTS, ISOBUTANE * //

1 15X 6HOGAT =E15.9/

2 15X 6H0TRP =F8.4, 8H, TTRP =F8.3, 8H, PTRP =E16.9/

3 IBX 6H0CRT =F8.4, 8H, TCRT =F8.3, 8H, PCRT =F13.9//

4 15X 4HAL =F6.3, 6H, BE =F&.3, 6H, GA =F6.3/

5 15X 4H0E =F6.3, 6H, EP =F6.3, 6H, ER =F6.3, 6H, IX =13//

6 13X 4F16.11/ 13X Fl6.ll/)

5 F0RMAT(15X 5HM0U/L 6X4HTSAT 5X5HTHETA 6X4HPSAT 9X1HB 9X1HC ) 6 FORMATdOX F 10 . 1 , 3F10.3, F10.4, F10.5)

10 PRINT 4, OGAT, OTRP, TTRP , PTRP, OCRT, TCRT , PCRT,

1

AL,BE,GA,DE,EP, ER,IX, B1,B2,03,B4, El

11 PRINT 5 ? DO 20 J=l,25 S ON = 0.5*J

12 R = ON/OTRP S S = ON/DCRT S SN = S-1 S IF(ER) 13,14

13 SR = S - ER t GO TO 15 14

15

SR = 1 S2 = S*S $ S3 = S*S2 $ SX = S**IX

16 B = 01 B2*EXP(BE*S)

18 E = E1*SN*SR*EXP(-GA*SX)

19 TSAT=TS=TSATF (ON) $ TH=THETAF ( ON ) S PS=PSATF(TS)

20 PRINT 6, ON, TS,TH,FS, B,E f RETURN I END

FUNCTION PSATF(T)

I-BUTANE VAPOR PRESSURES, BAR. RDG, OCT. 23, 1978.

LN(P) = A B*U C*X + 0*X2 * E*X3 F*X* ( 1-X ) •* EPP. WHERE, X E T/TCRT, U E (1-1/X).

COMMCN/3/OPOT,02POT2 ,DPSOT,OPMDT,OPOO,DPDR,OTSOR,OTHDR

DATA (EPP = 1.95) , (TCRT = 408.0 ) , ( A= 13. 808 35297), (B = 9. 3726920 0) , 1 (C=-70. 546630 08 ), (0=1 12. 75833 45 8 ),(E=-5 2. 42 140 76 3),

2 (F=47. 81122198)

1 FORMATdHO 9X *T ABOVE TCRT IN PSATF(T). * / ) 2 X = T/TCRT S X2 = X*X « XIT = 1.0/TCRT

3 U = 1.0 - 1/X S UlT = 1.0/X/T

4 V = 1.0 - X J IF(V) 7,8,9

7 PRINT 1 { STOP

8 Z = Z1 = 0 S GO TO 10

9 Z = V**EPP $ Z1 = -EPP*Z/V

10

CONTINUE

12 PL = A B*U C*X 0*X2 E*X*X2 F*X*7

13 PLIT = B*U1T (C 2*0*X 3*E*X2 F*(X*Zl Z))*XlT

15 PSATF = EXP(PL) $ OPSOT = PL1T*PSATF $ RETURN 8 END

173
SU8R0UTINE PRINTIT

C PRINTOUT ISOCHORES AND ISOTHERMS.

COMMCN/l/AL,B£,GA,D£,EP, DCRT ,TCRT ,PCRT , 0 GAT , OT RP , T TRP , PT RP COMMCN/3/OPOT, 02P0T2,0PSDT, 0PMDT,0P00,0F0R,0TS0R,0TH0R

1 FORMATdS, 2F10.0)

5 FORMAT (IX)

6 FORMATdHl 16X *ISOBUTANE TSOCHORE AT* F7. 3, * MOL/L* //

1 17X 3HT»K 5X5HP,0AR 5X5H0P/00 5X5H0P/0T 4X7H02P/DT2)

7 FORMATdOX F10.3, 2F10.3, F10.4, F11.5)

8 FORMATdHl 14X *ISOBUTANE ISOTHERM AT* F7.2, * OEG. K* //

1 lOX 5HM0L/L 5X5HP,BAR 5X5H0P/C0 5X5HDP/0T 5X7H02P/DT2 ) 9 F0RMAT(5X F10.3, 2F10.3. F10.4, F12.6)

C PRINTOUT THE ISOCHORES.

20 00 60 1=1,15 $ IF(I.EQ.l) 21,22

21 ON = 0,5 $ GO TO 30

22 IF(I.EQ.5) 23,24

23 ON = DCRT $ GO TO 30

24 IF(I.EQ.15) 25,26

25 ON = DTRP I GO TO 30

26 IFd.LT.5) 27,28

27 ON = I - 1 $ GO TO 30

28 ON = I - 2 30 PRIM 6, ON $ TS = TSATF(DN) S PS = PVTF ( TS, ON, 1

)

31 PRINT 7, TS, PS, DPDO, OPOT, D2P0T2

40 IF(I.LT.IO) 41,42

41 IT = 8 $ GO TO 50

42 IEd.LT.12) 43,44

43 IT = 4 $ GO TO 50

44 IF(I.LT.14) 45,46

45 IT = 2 B GO TO 50

46 IT = 1 50 00 59 J=114,700,IT $ TT = J $ IF(TT-TS) 59,59,52

52 PP = P\/TF(TT,ON,l ) B IF ( PP. GT . 72 0 ) €0,58

53 PRINT 7, TT,PP, OPOD, OPOT, 02PDT2

59 CONTINUE

60 CONTINUE

C PRINTOUT THE ISOTHERMS.

100 DO 130 1=1,99 $ READ 1, IDO, TT,OX S IF(IOO) 101,999

101 PRINT 8, TT B PM = PMELTF(TT)

102 IF(TT-TCRT) 103,103,104

103 DG = OENGASF(TT) S DL = DENLIQE(TT)

104 L = 0 B OS = OX

110 00 120 N=1,15Q0 B ON = N*OS S IF(TT-TCRT) 111,111,117

111 IF(9N.GE.0G. ANO.ON.LE.OL) 112,117

112 L = L 1 B IF(L.EQ.l) 113,120

113 PG=PVTF (TT, CG,1) B PRINT 9, OG , PG, OPDO , OPO T , 02 PDT2

114 PRINT 5 115 PL=PVTF(TT,OL,l) $ PRINT 9, OL , PL , OPOD , DPOT , 02P0T2

116 GO TO 120

117 PP = PVTF (TT,DN, 1) B IF ( PP .GT . PM. OR.PP. GT . 72 0 ) 130,119

119 PRINT 9, ON,PP, DPDO, OPDT, 02PDT2

120 CONTINUE

130 CONTINUE

999 RETURN $ END

174
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o

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subroutine PVTDATA

I-8UTANE EQNSIATE, OCT. 23, 1978, AT 10.29.

NEW XEF, OENGASF, EDELF, FOR LOW DENSITIES.

P - PSAT = S*GK* (T-TSAT ) S*S* GK*T CRT* F ( S , T ) , F(S,T) = B(S) *X8F(S,T) E ( S

) *X EF (S ,T ) W H (1-TH/T),

X8F(S,T) = SORT (X)*LN(T/TSAT) , XEF(S,T) = PSI - PSISAT, WHERE - PSI(S,T) i OE*EXP(EP* (1-X) ) (1-0E)*(1 - W W*LN(W)),

B(S) = ei B2*EXP (BE*S ) , R = OEN/DTRP, S = DEN/OCRT.

EIS) = E1*(S-1) *EXP(-GA*S**IX»

.

COMMON GK,GKK, B1,B2,B3,B4, E1,ER, IX COMMON/l/AL,BE,GA,OE,EP, OCR T , TCRT , PCR T , D GA T , DTRP , TTRP , PT RP COMMCN/3/ IN, IK, P,T,OEN, E,H,S, CV,CP,CSAT, W,WK

COMMON/13/ ZCRT,ZSAT,DZSDT,ZFX, FRT,DFRTOT

COMMCN/99/ TI,EZZ, EZ,SZ,CVZ, HZ,CPZ

17 WM = 58.1243 $ Q = 1.01325 * QP = Q/14. 69595 t EPP = 1.95

18 TTRP=113.55 $ 0TRP=12.755 f PTRP=PSATF (TT RP

)

19 TCRT=408.00 £ 0CRT=3.86 T PCRT=PS AT F ( T CRT

)

20 GKK = 0.083145 $ GK = GKK*DCRT £ ZCRT = PCRT/OCRT/GKK/TCRT

21 IX=4 $ AL=1 $ BE=0.50 S GA=0.30 £ DE=2./3. £ EP=3 £ ER=0

22 Bl=-0. 05165511088 £ 62=0.62315236106 £ B3=B4=0 S E 1= 0 . 42 08 3 1 44 15

4

23 OGAT = OENGASF (TTRP) £ CALL PEEK £ CALL ISOTHRM

24 WK = 100000/WM $ EZZ = 23838.616

GET BOILING POINT TEMP., VAP. ANO LIQ. DENSITIES.

50 FORMATdHl 9X ’BOILING POINT, I-BUTANE * //

1

10X4HTB =F10.5/ 10X4HOG =F10.7/ 10X4HDL =F10.5)

51 TBP = FINDTSF ( 1. 01325) £ OGB=OENGASF (TBP ) £ DLB= OENL IQ F ( TBP

)

52 PRINT 50 , TBP, DG8, DLB

99 RETURN £ END

FUNCTION QVAPXF(T)

I-BUTANE, OCT. 27, 1978. R.D.G.

FOR 129 WEIGHTED DATA (INCL. CLAOEYRON), RMS = 0.54 PCNT.

QVAP/QTRP = X (XE-X)*(A B*X2 C*X3), WHERE -

X E (TC-T) / (TC-TT ) , XE i X**E.

DATA (E=0. 45) , (QT = 2 8.208) , ( T T RP= 1 1 3 .55 ) , (TCRT =408.0), (XN=294. 45)

DATA (A=1.1726829),(B=-0.23924905),(C=-0.0265020)

1 FORMATdHO 9X *T EXCEEDS TCRT IN QVAPXF(T). * / ) 2 IF(TCRT-T) 3,4,5

3 PRINT 1 £ STOP

4 QVAPXF = 0 £ RETURN

5 X = (TCRT-T)/XN £ X2 = X*X £ XE = X**E

6 Q = CT*(X (XE-X)*(A B*X? C*X*X2))

7 QVAPXF = Q*1000 £ RETURN £ END
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FUNCTION PVTF(T,0,M)

I-BUTANE EQNSTATE, PVTF = P,BAR.

NOTE, M=0 RETURNS DP/OT, D?P/DT2. M=1 RETURNS ALSO OP/OO.

P-PSAT = S*GK* (T-TSAT) S*S*GK*TCRT*F ( S , T ) , WHERE - F(S,T) E B(S)*XBF (S,T ) E ( S ) EF (S, T )

,

AND - 3<S> =31+ B2*EXP«BE*S) , E(S) E El* (S-1 » (S-ER » *EXP ( -G A *S** IX )

.

WHERE, R E DEN/OTRP, S E OEN/OCRT.

COHMCN GK,GKK, B1,B2,B3,B4, E1,ER, IX COMMON/1/AL,0E,GA,OE,EP, 0CRT,TCRT,PCRT, 0GAT,0TRP,TTRP,PTRP

COMMON/3/OPDT,02POT2,DPSOT ,DPMOT ,0PD0,0P0R,0 TSOR,DTHOR

COMMON/4/X81 ,XB2, XC1,XC2, X£1,XE2, OXBDR, OXCOR, OXEOR

COMHON/b/ TSAT, THETA, PSAT

COMMON/13/ ZCRT,ZSAT,OZSOT,ZFX, FRT,OFRTOT

1 R = O/OTRP $ S = D/DCRT $ SN = S-1 S IF(ER) 2,3

2 SR = S - ER $ SRI =1 S GO TO 4

3 SR = 1 $ SRI = 0 4 S2 = S*S $ S3 = S*S2 $ SX = S**IX

5 GK = OCRT*GKK f TC = TCRT $ OSOR = DTRP/OCRT

6 RG = S*GK S GKT = GK*TC

7 TSAT=TS=TSATF(0) $ PSAT=PS=PSATF (TS) 8 THETA=THET AF ( 0)

8 XB = X3F(T,D) $ XE = XEF(T,D»

9 XP3 = £XP(BE*S) $ B = B1*S2 B2*S2*XPB

10

XP = EXP(-GA*SX) $ SM = SN*SR*S2 $ E = E1*SM*XP

12 F = B*XB £*XE $ FI = 8*XB1 E*XE1 $ F2 = B*XB2 E*XE2

13 PVTF = PS + RG*(T-TS) GKT*F % FRT=F/S2 t DFRT0T=F1 /S2/TC

14 OPOT = RG GK*F1 S D2P0T2 = GK*F2/TC I IF(M) 15,30

15 30 = <2*B1*S + B2*(3E*S2 + 2 *S ) *XPB) * OSOR

16 SMI = SR*S2 + SN*SR1*S2 SN*SR*2*S $ XPl = -IX*GA»SX/S

17 EO = El*(SM*XPl SMl»*XP*OSOR

20 FI = B*DXBOR BO*XB E*OXEDR ED*XE

26 OPOR = (OPSOT-RG)*OTSOR ( T -TS > *GK* OSOR GKT’Fl

27 OPOO = OPDR/OTRP

30 RETURN 8 END

FUNCTION SSATF(T)

I-BUTANE SATLIQ ENTROPY, J/MOL/K.

THIS SSATF(T) VIA I8UTHRM, NOV. 1, 1978. R.O.G.

FOR 31 POINTS, TTRP THRU TCRT, RMSPCT = 0.003.

SSAT - SCRT = A1*U**ES A2*LN(X) A3*U A4*U2 + A5*U3, WHERE

X E T/TCRT, U E (1-X).

COMMON/l/AL,BE,GA,DE,EP, DCRT , TCRT ,PCRT , DGAT,OTRP,TTRP, PTRP

DIMENSION AS<5)

DATA (NFS = 5> , (ES = 0.45) , ( T CRT = 4 0 0 . 0 ) , (SCRT = 270 . 44 576)

OATAJAS = -35.97387860, 87.70514205,

1

-45.80245863, 0.19432181, 15.98164931)

1 FOPMATdHO 9X 3HT =F10.5, * IN SSATF(T). * / ) 2 IF(T.GT.TCRT) 3,4

3 PRINT 1, T S STOP

4 X = T/TCRT $ U = 1.0 - X 8 IF(U.LE.O) 5,6

5 SSATF = SCRT 8 RETURN

6 SSATF = SCRT AS(1)*U**ES * AS ( 2

) * ALOG ( X ) 8 DO 7 K=3,NFS

7 SSATF = SSATF AS ( K) U** ( K- 2 ) 8 RETURN $ END 176
O

O

O

o

oo SUBROUTINE SAGECP

COMPARE CP ISOBUTANE , SAGE/LACEY WITH OUR CALCO. RESULTS.

THEIR DATA FOR HOMOGENEOUS DOMAIN IN BTU/LB/F, PSI, T,F.

CPK = 1054. 35/453. 5924*MH*1. 8. COMFON/8/ IN, IK, P,T,OEN, E,H,S, CV,CP,CSAT, W,WK

DIMENSION TB(7),CB<7), TK ( 99 ) , P A ( 99) , CP J ( 99)

DATA (PK = 14.503775) , (CPK = 243.192)

1 FORMATdOX 7F10.0)

2 FORMAT( 8F10.0 ) 3 FORMAT (1H116X*C0MPARISCN WITH ISOBUTANE CP OF SAGE/LACEY » //

1

17X 3HT,K 5X5HP,BAR 5X5HM0L/L 3X7HJ/MOL/K 6X4HCALC 6X4HPCNT ) 4 FORMATdOX 2F10.3, F10.4, 3F10.2)

5 FORMATdHO 12X 4HNP =13, lOH, RMSPCT =F6.2)

10 REAO 1, (T8( J) ,J = 1,7) $ 00 11 J=l,7

11 TB(J) = (TB(J) 459.67)/!, 8 B N = 0 12 DO 19 1=1,20 I READ 2, PSI, (CB( J) , J = 1 , 7

)

13 IF (PSI .LT. 400) 14,20

14 DO 19 J=l,7 I IF(CB(J)) 15,19

15 N = N 1 S TK(N) = TB(J) B PA(N) = PSI/PK

16 CPJ(N) = CB(J)*CPK

19 CONTINUE

20 NP = N S PRINT 3 8 SS = 0 22 00 30 J=1,NP B T=TK(J) S P=PA(J) B CALL GENEOUS

24 OIF = CPJ(J)-CP f PCT = 100*OIF/CP B SS = SS PCT’PCT

25 IF(J.EQ.34) PRINT 3 30 PRINT 4, T,P,OEN, CPJ(J),CP, PCT

31 SS = SQRT(SS/NP) $ PRINT 5, NP, SS B RETURN B END

SUBROUTINE SAGTHRM

COMPARE SAGE/LACEY ISOBUTANE DEN, DEL-H, OEL-S AT T = 250 F. PK E 14.69595/1.01325, OK = 453.5924/28.31685/58.1243,

HK = 1054. 35*58. 1243/453. 5924, SK E 1.8*HK

COMMON/8/ IN, IK, P,T,DEN, E,H,S, CV,CP,CSAT, W,WK

DIMENSION PX(30), OX(30), HX(30), SX(30)

DATA (PK=14. 50 3775) , (DK=0 .275590 ), (HK= 135. 1067) , (SK = 243. 1920)

1 FORMAT (4F10. 0)

2 FORMATdHl 9X *COMPARISONS WITH ISOBUTANE FUNCTIONS OF SAGE/LACEY

lAT T = 250 F,*/10X*UNITS, BARS, MOLES, LITERS, JOULES, KELVINS, T

1 = 394.261 K. * //

2 lOX 5HP,BAR 5X5HM0L/L 6X4HCALC 4X4HPCNT

3 4X(H(H-H1) 6X4HCALC 4X4HPCNT 4X6H(S-Sl) 6X4HCALC 4X4HPCNT ) 3 F0RMAK5X 3F10.3,F8.2, 2F10.1,F8.2, 2F10.3,F8.2)

9

T = (25C^459.67)/1.8 B DO 14 J=l,30

10 READ 1, PSI, V, HA, SA $ IF(FSI) 11,15

11 PX(J) = PSI/PK B OX(J) = DK/V

12 HX(J) = HK*HA S SX(J) = SK*SA

14 CONTINUE

15 NP = J-1 B HXl = HXd) B SXl = SX(1) B PS = PSATF(T)

16 P = PX(l) B CALL GENEOUS B H1=H B Sl=S B PRINT 2 20 00 40 J=1,NF $ P = PX(J)

21 HX(J) = HX(J) - HXl $ SX(J) = SX(J) - SXl

22 IF(P.LT.PS) 23,24

23 call GENEOUS B GO TO 25

24 CALL COMPRLQ

25H = H-H1 S S = S-S1 B OPCT = 1 0 0

* ( OX ( J ) / OEN- 1

)

26 IF(J.EQ.l) 27,28

27 HPCT = SPCT =0 B GO TO 40

28 HPCT = 100* ( HX ( J) /H-1 ) B SPCT = 1 0 0* ( SX ( J) /S-1

)

40 PRINT 3, P, OX (J) , DEN, OPCT, HX ( J ) , H, HPCT , SX(J),S.SPCT

90 RETURN B END 177
c

ccc

c

c

c

c

c

c

c

c

SU9R0UTI

STARLING

DATA FOR

BRITISH U MY (G-MOL

HENCE, ( PSI = (P,

(100*DK/P

COMMCN/3

COMMON/9

DATA (GK

DATA (3Z

1 (GA»9.2

2 (C=328.

3 (EZ=896

CONVERT M 19 DB = DK*

20 TR = 1.8

21 FI = 03*

22 F2 = BZ*

23 F3 = (9*

24 F4 = AL*

25 F5 = C*D

29 PSI = FI GET OP/OT

31 FIT = OB

32 F2T = (8

33 F3T = (B

34 F4T = -A 35 F5T = -2 36 DPDT = ( GET O2P/0

42 F2T2 = ( 43 F3T2 = - 44 F4T2 = 2 45 F5T2 = 6 46 02P0T2 = GET OP/DD

51 FIO = GK 52 F20 = 2* 54 F5A = (C

55 F50 = -2

56 OPOO = ( ENTHALPY

62 H2 = (BZ

63 H3 = (2*

64 H4 = (6*

65 H5 = (3

66 H = (H2

99 RETURN

NE STAREQN

ISOBUTANE EQNSTATE, RPT. ORO-5249-2, DEC. 31, 1977.

EQNSTATE IN BRITISH UNITS - NITS, PSI, T,OEG.R, LB-MOL/CUFT. MW = 58.12, GK = 10.7315

/L)*(28. 31685/453. 5924)*(58. 1243/58. 12) = LB-MOL/CUFT.

G-MOL/L) *( 0. 062432583) = LB-MOL/CUFT.

BAR)* (14.69595/1.01325) = ( P , BAR ) * 14. 5 03 775

.

K) • (PSI-CUFT/LBMOL) = JOULE/G-MOL.

/DP0T,D2P0T2,DPS0T ,OPMOT,DPOD,OPDR,DTSDR,OTHOR

/ IN, IK, P,T,DEN, E,H,S, CV,CP,CSAT, W,WK

=10. 7315), (DK= 0.06 24 32 58 3) ,( PK=1 4. 503775)

=2.026152731) , ( AZ= 389 80 . 20 15 ) , ( CZ=1 0 6. 5 81 450 88E+ 8)

,

13784536), ( B=6 . 707625 90 8 ) , ( A=3 8 864 . 3 892 ) , ( AL=6 . 8 7726560 5 )

,

21967 D1E+ 8) , (DZ=147. 0459327E+10) , ( 0=6 18 . 3 0 34445E +4)

,

1.524117E+10)

Y (T,DEN) INTO RANKINE, AND LB-MOL/CUFT.

DEN t 0B2=DB*DB $ DB3=DB*DB2

*T S TR2=TR*TR $ TR3=TR*TR2 $ TR4=TR2*TR2

GK*TR

GK*TR - AZ - CZ/TR2 DZ/TR3 - EZ/TR4 S F2 = F2*0B2

GK*TR - A - D/TR)*0B3

(A + 0/TR)*DB3*DB3 % XP = EXP(-GA*OB2)

B3/TR2*(1 GA*082)*XP

+ F2 + F3 + F4 4- F5 $ P = PSI/PK

, then CONVERT TO SI UNITS.

*GK

Z*GK + 2*CZ/TR3 - 3*DZ/TR4 + 4*E Z/ TR/TR4 ) * 062

*GK D/TR2)*DB3

L*D*DB3*DB3/TR2

C*OB3/TR3* (1+GA*0B2) *XP

1.8/PK)*(F1T F2T + F3T + F4T F5T)

T2, THEN CONVERT TO SI UNITS.

-6*CZ/TR4 + 12*0Z/TR/TR4 - 20*EZ/TR3/TR3)*OB2

2*0*OB3/TR3

•AL*0*0B3*0B3/TR3

*C*DB3/TR4* (1+GA*DB2)*XP

(1.8*1.8/PK)*(F2T2 + F3T2 + F4T2 + F5T2)

, THEN CONVERT TO SI UNITS.

*TR

F2/0B S F30 = 3*F3/0B S F4D = 6*F4/0B

/TR2)*(3*0B2 5*GA*DB*D83)

GA*0B*F5 F5A*XP

DK/PK)*(F10 F20 + F3D F4D + F50)

(H-HZ) VIA STARLING REPORT.

GK*TR - 2*AZ - 4*CZ/TR2 5*DZ/TR3 - 6*EZ/TR4)*0B

B*GK*TR - 3*A - 4*0/ TR) *0B2/2

A 7*D/TR) *AL*DB2*DB3/5

- (3 GA*DB2/2 - GA*G A*DB*0B3 ) *XP ) *C/GA/TR2

* H3 H4 H5) *OK*100/PK

$ END

178
SUBROUTINE STARTIT

C COMPARE ISOBUTANE PROPERTIES WITH STARLING ON ISOTHERMS.

COMMON/3/OPOT,02POT2,OPSOT,OPMOT,OPOO,DPOR,OTSOR,OTHOP

COMMON/8/ IN, IK, P,T,OEN, E,H,S, CV,CP,CSAT, H,WK

COMMON/99/ TI,EZZ, EZ,SZ,CVZ, HZ,CPZ

DIMENSION TT (6) , OX (6)

DATA (TCRT = 408.0)

OATA(TT = 200.0, 300.0, 400.0, 410.0, 450.0, 500.0)

DATA(OX = 0.02, 0.04, 0.16, 0.16, 0.16, 0.16)

1 FORMATdHl 2X»ISOBUTANE, R.D.G. VS. K.E.S. AT T =*F7.2,* DEG. K*/

1 3X 'UNITS KELVINS, BARS, G-MOL/LITER, JOULES. • /

1 3X "DATA = R.D.G. , CALC. = K.E.S. //

1 3X5HM0L/L 3X5HP,BAR 4X4HCALC 3X4HPCNT

2 3X5HDP/DD 4X4HCALC 3X4HPCNT

3 3X5HDP/0T 4X4HCALC 3X4HPCNT

4 2X7HD2P/0T2 5X4HCALC

5 5X4HH-HZ 5X4HCALC 3X4HPCNT ) 2 FORMAT (2XF6. 3, 2F8.2, F7.2, 2F8.2, F7.2, 2F8.3, F7.2,

1 2F9.5, 219, F7.2)

5 FORMAT(IX)

C PRINT SIX COMPARISON ISOTHERMS. OMIT COEXIST.

10 DO 99 1=1,6 S L = 0 S T = TT(I) S OS = DX(I)

11 PRINT 1, T $ PM = PMELTF(T) S IF(T-TCRT) 12,12,15

12 DG = DENGASF<T) S OL = DENLIQF(T)

15 DO 90 J=l,900 S ON = J*OS S IF(T-TCRT) 16,16,20

16 IF(ON.GE.DG.AND.ON.LE.OL) 17,20

17 L = L 1 S IF(L.EQ.l) 18,90

18 PRINT 5 $ GO TO 90

20 PGOO = P = PVTF(T,ON,l) S I F (P . GT . PM . OR. P. GT . 4 0 0 ) 99,21

21 OPOOG=OPOO S OPOTG=OPOT S 02P0T2 G= D2PDT2

22 IF (ON.LT.DG. (R.T.GT.TCRT) 23,24

23 CALL GENEOUS S GO TO 25

24 CALL COMPRLQ t TI = T $ CALL IDEAL

25 HGOO = H - tZZ - HZ

30 DEN = ON $ CALL STAREQN S PSTR = P B OPOOS=OPOD

31 OPOTS=OPDT $ D2P0T2S=02P0T2 S HSTR = H 35 PCTP = 100* ( FSTR/PGOO-1)

36 PCTD = 100* (OPDOS/OPDOG-1)

37 PCTT = 100’ (DPDTS/OPDTG-1)

39 PCTH = 100’ (HSTR/HGOD-1)

40 IHG = HGOD $ IHS = HSTR

50 PRINT 2, DEN, PGO 0, PS TR , PC TP , DPOOG , OPOOS , PCTD , OPOTG, OPOTS, PCTT

,

1 D2PDT2G, D2P0T2S, IHG, IHS, PCTH

90 CONTINUE

99 CONTINUE S RETURN B END

179
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SUBROUTINE TA8LIQ

C TABULATE THE I-BUTANE SATURATED LIQUID FUNCTIONS.

C0MM0N/1/AL,8E,GA,0E,EP. OCR T , TORT , PORT , D GAT , OT RP , TTRP, PTRP

COMMCN/3/OPOT,02POT2,OPSOT,DPMCT,OPOD,OPOR,DTSDR,OTHOR

COMMON/5/ OOSDT

COMMON/6/ TSAT, THETA, PSAT

COMMON/8/ IN, IK, P,T,DEN, E,H,S, CV,CP,CSAT, W,HK

COMMON/9/ONG,EG,HG,SG, CVG,CPG,WG, OPGO ,OPGOO

DIMENSION TSA(65), PSA(65)

4 FORMATdHl 13X ’PROPERTIES OF SATURATED LIQUID I-BUTANE’ //

1 14X1HT lOXlHP 5X3HDEN 3X5HV,LIQ 6X5HV,GAS 5 )6HDPS/DT 3X6H0DL/DT

2 4X5HDP/0T 6X5H0P/D0 2X5HQ,VAP /

3 lOX 5H0EG K 8X3HBAR 3X5HM0L/L 3X5HL/M0L 6X5HL/M0L 6X5HBAR/K

4 2X7HMOL/L/K 4X5H9AR/K 2X9HBAR-L/MOL 2X5HJ/M0L ) 5 FORMAT (5XF10. 3, Ell. 4, F8.3, F8.5, 2E11.4, F9.5, F9.3, Ell. 4, 17)

11 FORMATdHl 13X ’PROPERTIES OF SATURATED LIQUID I-BUTANE’ //

1 14X1HT IIXIHP 9X1HE 9X1HH 9X1HS

2 6X2HCV 6X 2HCS 6X2HCP 6X1HW /

3 10X5HDEG K 9X3HBAR 5X5HJ/M0L 5X5HJ/M0L 3X7HJ/M0L/K

4 1X7HJ/M0L/K 1X7HJ/M0L/K 1X7HJ/M0L/K 2X5HM/SEC ) 12 F0RMAT(5X F10.3, E12.4, 2F10.1, F10.3, 3F8.2, 17)

FOR PAGE ONE OF TABLIQ.

REPLACE T = 260 BY BOILING-POINT AT J = 31.

130 PR INT 4 S NP = 3 1 131 DO 150 J = 1, NP S IF (J. EQ. 1) 132, 133

132 T = TTRP s GO TO 1 39

133 IF ( J.EQ. 16) 134,135

134 T = FIND TSF ( 1.01325) £ GO TO 139

135 IF ( J.EOiP) 136,138

136 T = TCRT S OG = OL = OCRT £ DDLDT = 0 137 VG = VL = 1 . O/OCRT S GO TO 141 133 T = 100 + 1 O’J

139 DL = OENLIQF(T) I DDLDT = DDSDT

140 DG = DEN GAS F(T) £ VG = 1/DG £ VL = 1/DL

141 TS A(J) = T £ PX = PVTF (T.C)L,1)

147 PS A(J) = PS = PSAT $ IQX :: QX = QVA PXF«T) S DQ = 143 IF (DQ.GT .0. 4999) IQ X = IQX + 1 150 PR INT 5, T, PS,OL,VL, VG, OPSOT,DOLOT, DPOT,DPDD, IQX

1FOR PAGE TWO OF TABLI Q.

USE COEXI ST AT ALL TEMPS « 160 PR INT 11 £ DO 170 J=1 ,NP $ P = PSA(J) £ T = TS 164 CALL COE XIST £ IW = w 170 PR INT 12 , T ,P, E,H,S , CV,CSAT,CP, IW 999 RE TURN £ END

180
o

o

o FUNCTION THETAF(DEN)

theta = TSAT*£XP (U(S) )

.

LET Q = ( S-1) /(ST-1) , WHERE ST = OTRP/OCRT, THEN - IF S < 1, U = AL*Q**3, if S > 1, U = -AL*Q**3,

C0MMCN/1/AL,8E,GA,0E,EP» DCRT ,TCRT ,PCRT, DGAT,0TRP,TTRP,PTRP

COMMON/3/OPOT,D2POT2,OPSOT,DPMCT,OPOO,DPCR,0 TSDR,DTHDR

common/6/ tsat, theta, PSAT

1 S = OEN/OCRT $ OSOR = DTRP/OCRT « C = OSDR-1

2 Q = (S-D/C $ Q2 = Q*Q « U = AL*Q*Q2

3 U1 = AL*3*Q2*0S0R/C S IF(Q)

(* U = -U S U1 = -U1

5 XP = £XP(U) $ THETAF = TSAT’XP

6 OTHOR = (TSAT’Ul * OTSOR)*XP £ RETURN

9 THETAF = TCRT S OTHOR =0 £ RETURN £ END

FUNCTION TSATF(OEN)

C ITERATE T TO MINIMIZE (OEN-OCALC) VIA OENGASF(T), DENLIQF(T).

C0MMCN/1/AL,9E ,GA,DE ,EP, DCP T , TCRT ,PCR T , 0 GA T , OT RP , TTRP , PTRP C0MM0N/3/0P0T, D2P0T2,0PSDT,0PM0T,r)P0D, OP OR , 0 TSOR , OTHOR

COMMCN/5/ DDSDT

CATA (Q=2.0> , (FN=6. 3890561)

C NOTE, FN = EXP(Q) - 1.0.

1 FORMATdHO 9X *TSATF FAILS TO CONVERGE. * / ) 2 0=OEN £ S=0/DCRT £ YN=TCRT/TTRP-1 £ IF(OEN-CCRT) 3,30,4

3 ST = OGAT/OCRT £ F = ALOG ( S) / A L 0 G ( ST )

( ( 1 -S ) / (1 - ST )

) *• 2 £ GO TO 5

4 ST=OTRP/OCRT £ U= ( ( S- 1 ) / (ST - 1 )

) **3 £ F= ( EX P ( Q*U) -1 ) /FN

5 T = TCRT/d YN*F)

6 00 15 J=l,50 £ IF(OEN-DCRT) 7,30,8

7 DO = D - DENGASF(T) £ GO TO 9

8 00 = 0 - OENLIQF(T)

9 IF(A9S(D0/D) .LT.l.OE-7) 16,10

10 OT = OD/DDSOT £ I F ( ABS ( D T/T ) .L T . 1 . OE- 7 ) 16,11

11 T = T DT f IF(T) 12,12,13

12 T = TTRP i GO TO 15

13 IF (T ,LT. TCRT ) 15,14

14 T = TCRT - 0.10

15 CONTINUE £ PRINT 1 £ STOP

16 TSATF = T £ OTSDR = DTRP/OOSOT £ RETURN

30 TSATF = TCRT £ OTSOR =0 £ RETURN S END

181
o

o

FUNCTION XBF(T,0)

C X0F = SQRT(T/TC) *LN{T/TS) = Q(T)*Z(R,T),

COM^ON/l/AL,BE,GA,OE,EP, OCRT ,TCRT ,PCRT , OGA T , OT RP , T TRP , PTRP

C0MM0N/3/0P0T,02P0T2 tOPSOT ,DPMOT ,DPOD,DPDR,OTSDR,DTHDR

COMMON/4/XBl,XB2, XC1,XC2, XE1,XE2, DXBOR, DXCOR, OXEOR

COMMON/6/ TSAT, THETA, PSAT

1 TC = TCRT S TS = TSAT f X = T/TC

2 U = T/TS B UIX = TC/TS $ UlR = -U*OTSOR/TS

3 Z = ALOG(U) S Z1R=U1R/U $ Z1X=U1X/U B Z2X=-Z1X*Z1X 40= SQRT(X> $ 01 = 0.5/0 $ 02 = -01/2/X

5 X8F = Q*Z B OXBOR = Q*Z1P B XBl = Q*Z1X + Ol*Z

6 X82 = Q*Z2X * 01’2’ZIX 02*Z $ RETURN S END

FUNCTION XEF(T,D)

XEF E PSI - PSISAT, PSI = A*F(T) B*H(R,T), W E (1-TH/T),

F(T) E EXP(C* (1-X ) ) , H(R,T) E (1 - W W*LN(W)).

COMMON/l/AL ,BE,GA,DE,EP, D CRT , TCRT , PCRT, OGA T, OT RP , T TRP, PTRP COMMON/3/OPOT,0 2POT2 .OPSCT ,DPMDT ,0P0 0 , OP DR , 0 TSOR , OT HDR COMMON/4/XB1 ,XB2, XC1,XC2, XE1.XE2, DXBDR, DXCOR, OXEDR

COMMCN/6/ TSAT, THETA, PSAT

1 A=DE S B=l-A S C=EP $ TC=TCRT $ TS=TSAT S TH=THETA

2 X = T/TC B XS = TS/TC B XSl = DTSDR/TC

3 W = 1.0 - TH/T $ IF(W) 30,30,4

4 F = EXP(C*(1-X)) $ Fl = -C*F B F2 = -C»F1

5 WIR = -OTHDR/T B WIX = TH/T/X B W2X = -2*W1X/X

6 G = ALOG(W) B H = H*G - W + 1 B HIR = G’WIR

7 HIX = G*W1X B H2X = G*W2X + W1X*W1X/W

10 P = A*F + 8»H $ PIR = B*H1R

11 XEl = A*F1 t B*H1X S XE2 = A*F2 B*H2X

15 WS = 1.0 - TH/TS B IF(WS) 16,16,17

16 FS = HS = 1 B FSl = HSl =0 B GO TO 21 17 WSl = (TH*OTSOR/TS - DTHORI/TS B GS = ALOG(WSJ

18 HS = WS*GS - WS + 1 B HSl = GS’WSl

20 FS = EXP (C* (1-XS) ) $ FSl = -C*XS1*FS

21 PS = A*FS B*HS S PSI = A*FS1 B*HSl

25 XEF = P - PS B OXEDR = PIR - PSl S RETURN

30 XEF = XEl = XE2 = OXEDR =0 B RETURN B END

AND

182
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o

o

o

o

o

ooo

PROGRAM ZIEGLER(OUTPUT)

PROGRAM ZIEGLER(OUTPUT, PUNCH)

I-8UTANE, ESTIM. V.P. AND QVAP FROM TRIPLE- TO BOILING-POINTS,

USING ENTHALPY AND ENTROPY CLOSED LOOPS.

COMMON/1/ TA,T3,P8,QB, OELH.DELS

COMMON/2/ EZA,HZA,SZA, HGB,SGB, OHLAB,OSLA0

COMMON/3/OPDT,D2PDT2,OPSDT,DPMOT,OPOO,OPOR,OTSDR,OTHOR

COMMON/9/ PZIP, BZ, OBZDT, DPZOT, DZDD

COMMON/99/ TI.EZZ, EZ,SZ,CVZ, HZ,CPZ

DIMENSION QK(2) ,TK ( 150 ) ,OK (150 ),PIK (150) ,PK( 150) ,OJ( 19 0)

1 F0RMAT(I5, no. 3, E15.6)

2 F0RMAT(I5, F10.3, FIO.O)

3 FORMATdHl IIX »I-BUTANE ESTIM. V.P. , BAR, AND QVAP, KJ/MOL. • //

1 12X 4HTB =Flfl,5, 6H, PB =F8.5, 6H, DB =F9.6/

2 12X5HEZB =F7.1, 7H, EGB =F7.1, 7H, HZB =F8.1, 7H, HGB =F8.1/

3 12X 5HSZ3 =F9.4, 7H, SGB =F9.4, 6H, QB =F8.1/ ) 4 F0RMAT(7X 3HT,K 8X2HPI 6X5HP,BAR 5X5HMOL/L 6X3HHZA 6X3HHGA

1 6X3HSZA 6X3HSGA 4X5H0HGA9 4X5H0HLAB 4X5HDSGAB 4X5H0SLAB

2 5X3HQAH 5X3HQAS ) 5 FORMAT (2XF8. 2, El 0 . 4, E 11 . 5 , E 1 0 . 4 , 2F9.1,2F9.3, 2F9.1,2FP.3, 2F8.3)

6 F0RMAT(12X 3HT,K 4X5H100/T 7X5HP,EQN 7X5HP,SAR 6X5HLN(P)

1 7X5HM0L/L 3X5HQ,EQN 3X5HQ,VAP ) 7 F0RMAT(5X FlO.2, F9.5, 2E12.5, FU.5, £12.5, 2F8.3)

8 TTRP = 113.55 B PB = 1.01325 B TB = 261.4

ISOBUTANE QVAP,J/MOL VIA ASTON(1940) AT BP, 261.44 K.

9 QK(1) = QK(2) = 21297.0

GET HGB, SGB FOR SATVAPOR AT THE BOILING POINT.

13 TI = TB B call ideal S EZB=EZ f HZB=HZ S SZB=SZ

11 DN3 = FINDENF (TB,PB) B EGB = EZ < EOELF ( T3,0N3)

12 SGB = SZ + DELS B HGB = EGB + 100*P3/DNB

14 I = 1 B QB = QK(I)

15 PRINT 3, T8,PB,DN8, EZ3,EGB, HZB, HGB, SZB.SGB, QB S PRINT 4 DO temperatures from TRIPLE- TO BOILING-POINTS - 20 DO 50 J=l,149 B IF(J.EQ.l) 21,22

21 TA = T = TTRP B GO TO 23

22 TA = T = 112 J GET EZA, HZA, SZA AT T = TA.

23 TI = TA B CALL IDEAL B EZA=EZ B HZA=HZ S SZA=SZ

GET DHLAB, DSLAB FOR THE SATDLIQUIO FROM TA TO TB.

24 CALL CSATSUM B DHLAB = OELH B DSLAB = DELS

NOW ITERATE P (T=TA) TO MINIMIZE (QAH - QAS).

30 P = PI = PSATF(T) B OP = P/2 B SS = OELTAF(T,P)

31 DO 40 IT=1,15 B PL = P-DP B SL = OELTAF(T,PD

32 PP = P4-DP B SP = OELTAF(T,PP)

35 IF(SL-SS) 36,36,38

36 IF(SL-SP) 37,37,39

37 SS : SL B P = P - OP S GO TO 40 38 IF(SP-SS) 39,40,40

39 SS = SP B P = P DP

40 OP = OP/2 B DNA = FINDENF(T,P)

USE FINAL P TC GET DNA, HGA.SGA, 0HGA3,DSGAB,

AND THEN, VIA LOOP, GET QAH, QAS.

42 EGA = EZA + £0£LF(T,0NA) B SGA = SZA DELS

43 HGA = EGA lOO*P/ONA B DHGAB= HGB- HG A S 0SGA9=SGB-SG

A

44 QAH = QB + DHLAB - OHGAB B QAS = TA*(QB/TB DSLAB - OSGAB)

45 QAH = QAH/1000 B QAS = QAS/1000 ? FIK(J) = PI 46 TK(J)=TA B OK(J)=ONA B PK(J)=P B QJ(J) = (QAH*QAS)/2

50 PRINT 5, TA,PI,P,ONA, HZA, HGA, SZA, SGA, OHGAB, DHLAB,

1 83
o

o

o

1

DSGAB, OSLAB, QAH,QAS

C PRINT T,l/T, FEQN,P,LN(P> t DNA, QEQNtQt FOR PUBLICATION.

61 PRINT 3, TBtPB.DNB. EZB.EGB, HZB.HGB, SZB.SGB, QB « PRINT 6 62 00 99 J=l,149

C 63 IF(J.EQ.50.0R.J.EQ.99) 67,70

C 67 PRINT 3, TB,PB,ONB, E ZB, EGB , H ZB ,HGB, SZB , SG 9 , 03 S PRINT 6 70 T = TK(J) $ AT = 100/T S P = PK(J) S GP = ALOG(P)

71 QE = QVAPXF (T)/1000

C 75 PRINT 7, T,AT, PIK(J),P,GP, DK(J), QE,QJ(J)

80 lOX = «»0 S IF(J.EQ.l) 90,81

81 IT = T/5 $ IF(T-5*IT) 99,90

90 QCALC = 100D»QJCJ)

91 PRINT 7, T,AT, PIK(J),P,GP, DK(J), OE,QJ(J)

C 92 PUNCH 1, I0X,T,P $ PUNCH 1, IDX,T,DK(J) S PUNCH 2, IDX,T, QCALC

99 CONTINUE f STOP t END

SUBROUTINE CSATSUM

C GET OELH, DELS ALONG SATDLIQ FROM TA TO TB. COMMON/1/ TA,TB,PB,QB, OELH, DELS

COMMON/3/DPDT,D2PDT2,OPSOT,DPFDT,OPOD,OPDP,OTSOR,OTHOR

1E = H= S = 0 2 TR = TB - TA $ N = ABS(TP)/2 2 $ OT = TR/N

3 DO 6 J=1,N S TJ = TA + (J-0.5)*DT

4 CS = CSATXF(TJ) $ PS = PSATFJTJ) S OS = OENLIQF(TJ)

5 H = H CS’OT + 100*OPSOT»OT/OS S S = S CS*DT/TJ

8 CONTINUE

9 DELL = H S DELS = S $ RETURN t END

FUNCTION CSATXF(T)

I-BUTANE CSAT TO B.P. VIA ASTON <1940).

VIA PROGRAM CSATFIT, 9/20/79 AT 12.27.

CS(T) = A B*X2 C*X3 0*X4, X E (T-TZ)/300.

DATA (TZ = 95.0)

DATA ( A= 98. 5087), ( B= 298. 6533), (C=- 70 0.4833), (0=653. 09 75)

1 FORMATCIHO 9X *T EXCEEDS 265 IN CSATXF(T). * / ) 2 IF(T.GT.265) 3,4

3 PRINT 1 £ STOP

4 X = (T-TZ)/300 $ X2 = X*X

5 CSATXF = A B*X2 C»X»X2 0*X2*X2 £ RETURN £ END

FUNCTION DELTAF(T,P)

C GET ONA ,£GA,HGA,SGA FOR SATDVAPOR AT T,P, (T=TA),

C GET 0HGA8 E HGB-HGA, DSGAB E SGB-SGA,

C GET QAH, QAS VIA CLOSED LOOPS, THEN, OELTAF E ABS <0 AH-Q AS )

.

COMMON/1/ TA,TB,PB,QB, OELH, DELS

COMMON/2/ EZA,HZA,SZA, HG8,SGB, OHLAB,OSLAB

COMMON/99/ TI,EZZ, EZ,SZ,CV7, HZ,CPZ

1 IF(P.GT.O) 2,9

2 ONA = FINOENF(T,P) £ EGA = EZA EOELF(T,ONA)

3 SGA = SZA DELS £ HGA = EGA 100*P/DNA

5 0HGA8 = HGB - HGA £ DSGAB = SGB - SGA

6 QAH = OB OHLAB - DHGAB £ QAS = T*(QB/TB 0SLA8 - DSGAB)

8 OELTAF = ABS(QAH-QAS) £ RETURN

9 OELTAF = l.OE+100 £ RETURN £ END

184
OOO

OOO

^

FUNCTION E0ELF(T,0)

CHANGE OF E,S ON ISOTHERM T FROM OEN = 0 TO OEN = 0. USE VIRIAL EQNSTATE. NOTE OCZ = 3.8 MOL/L.

OELE = EOELF = -R* ( D/OC Z) *T »T»o 3 ( T ) /O T , DELS = -R»LN (0*R*T/P1) - R* (0 /OCZ ) * (B ( T ) T*03(T)/0T).

COMMON/1/ TA,TB,P3,03, OELH.DELS

COMMON/9/ PZIP, BZ, OBZOT, OPZOT, OZOO

DATA (Q=1.0132 5),(R= 0.08 31450),(OCZ=3.80)

1 Z = ZIPF(T,0) $ EOELF = - 1 0 0 * R* ( 0/ DC Z) * T T^O 3Z0

T

2 DELS = ALOG (0*R»T/Q) + (D/0CZ)*<8Z T*03Z0T)

9 DELS = -100*R*DELS S RETURN 5 END

FUNCTION FINOENF (T,P)

GIVEN P,T IN VIRIAL EQN., SOLVE QUADRATIC FOR OEN, MOL/L.

DATA (DCRT=3.30),(TCRT=408.13),(R=0.083145)

DATA <01=0.50084721) ,( 32 =-l. 100 39 3 22), (3 3= -0.64781233)

1 X = T/TCRT I B = 81 + B2/X B3/X/X/X

2 Q = SQRTd.O + 4*P*B/R/T/OCRT)

3 FINOENF = OCRT* (Q-1) /2/B S RETURN $ END

FUNCTION PSATF(T)

I-BU1ANE VAPOR PRESSURE, BAR. R.O.G., (SEPT, 1978).

LN(P) = A B*U C*X 0*X2 E*X3 F*X* ( 1-X) **EPP.

WHERE, X E T/TCRT, U E (1-1/X).

C0MM0N/3/0PDT,02P0T2 ,OPSDT ,DPMDT ,OPDO,OPOR, DTSOR, OTHOR

0ATA(EPP = 1. 30), (TCRT = 408. 10), (A=7. 70053220), (8 = 8.136 64 265),

1

(C= -6. 734 86 177), (0=2. 13 85 70 39), ( E= 0 . 4 946 9 225 ) ,(F=1. 13184170)

1 FORMATdHO 9X *T ABOVE TCRT IN PSATF(T). * / ) 2 X = T/TCRT S X2 = X*X B XIT = 1.0/TCRT

3 U = 1.0 - 1/X S UlT = 1.0/X/T

4V=1.0-X $ IF(V) 7,8,9

7 PRINT 1 B STOP

8 Z = Z1 = 0 B GO TO 10

9 Z = V**EPP B Z1 = -EPP*Z/V

10 CONTINUE

12 PL = A 4- 8*U C*X 0*X2 E*X*X2 F*X*Z

13 PLIT = B*U1T (C 2*0*X 3*E*X2 F*(X*Zl + Z))*XlT

15 PSATF = EXP(PL) B OPSOT = PL1T*PSATF B RETURN B END

FUNCTION ZIPF(T,0)

ISOOUTANE VIRIAL EQN., R.O.G., SEPT., 1978.

Z(T,0) = 1 * B(X)»S, X E T/TCRT, S E OEN/OCRT.

3(X) = 31 B2/X B3/X3. OEN IN MOL/L.

COMMCN/9/ PZIP, BZ, OBZOT, OPZOT, OZOO

DATA (DCRT = 3 .80) , (TCRT=408.1 3) , ( R= 0. 0 8 31 45

)

DATA (31=0.50064721) ,(32 =-1.10039322) ,(33=-0. 64781233)

1 S = O/OCRT B X = T/TCRT B X2 = X*X B X3 = X*X2

2 BZ = B = B1 B2/X B3/X3

3 ZIPF = 1.0 B*S B PZIP = D»R*T*ZIPF

4 03ZOT = -(32/X2 3* 93 /X/ X 3 ) / TCRT f OZOO = B/DCRT

5 OPZOT = 0*R* ( S*T*08Z0T ZIPF) B RETURN B END 185
NBS-114A (REV. 9-78)

U.S. DEPT. OF COMM.

BIBLIOGRAPHIC DATA

SHEET

1. PUBLICATION OR REPORT NO. NBSIR 79-1612

2.Gov't. Accession No, 3. Recipient’s Accession No,

4. TITLE AND SUBTITLE

ISOBUTANE; PROVISIONAL THERMODYNAMIC FUNCTIONS

FROM 114 to 700 K AT PRESSURES TO 700 BAR

5. Publication Date July 1979

7. AUTHOR(S)

Robert D. Goodwin

8, Performing Organ. Report No.

9. PERFORMING ORGANIZATION NAME AND ADDRESS

NATIONAL BUREAU OF STANDARDS

DEPARTMENT OF COMMERCE

WASHINGTON, DC 20234

10, project/ Task 'Work Unit No.

; 11. Contract/Grant No.

12. SPONSORING ORGANIZATION NAME AND COMPLETE ADDRESS rsrreer, City, State, ZIP)

Gas Research Institute

10 West 35th Street

Chicago, Illinois 60616

13. Type of Report & PerioiJ Covered

15. SUPPLEMENTARY NOTES

I I Document describes a computer program; SF-185, FIPS Software Summary, is attached.

16. ABSTRACT (A 200-woTd or less factual summary of most significant information. If document includes a significant bibliography or

literature survey, mention it here,)

Thermophysical properties of isobutane are tabulated at integral temperatures along

isobars over the entire range of fluid states. Results for the compressed liquid,

from the triple- to the boiling-point, have been estimated by use of the highly

constrained, nonanalytic equation of state, because experimental P-p-T data are lacking in this region.

17. KEY WORDS (six to twelve entries; alphabetical order; capitalize only the first letter of the first key word unless a proper name;

separated by semicolons) Densitios; efithalpies; entropies; equation of state; internal

energies; isobars; isobutane; isochores; isotherms; Joul e-Thomson inversion;

latent heats of vaporization; melting line; orthobaric densities; specific heats;

speeds of sound; vapor pressures.

18. AVAILABILITY [X^ Unlimited

I I For Official Distribution. Do Not Release to NTIS

I I Order From Sup. of Doc., U.S. Government Printing Office, Washington, DC

20402, SD Stock No. SN003-003-

PCX Order From National Technical Information Service (NTIS), Springfield, VA. 22161

19. SECURITY CLASS

(THIS REPORT)

UNCLASSIFIED

20. SECURITY CLASS

(THIS PAGE)

UNCLASSIFIED

21. NO. OF

PRINTED PAGES

191

22. Price

$ 8.00

USCOMM-DC

U. S. GOVERNMENT PRINTING OFFICE 1979-677-072/1293 Reg. 8