-AJJJJJ4—Sfe#44r5-

NASA

Reference

Publication

1102

NBSIR

82-1672

April 1983

NBS ii ....

1 tun

A 1110b cl7 cllEb

Transport

Properties

of Oxygen

H. M. Roder

25th

25

Anniversary

1958-1983

NATIONAL BUREAU OF STANDARDS

LIBRARY NASA

Reference

Publication

1102

NBSIR

82-1672

1983

(\JASA

National Aeronautics

and Space Administration

MAY 3 1 ncrVcuL-c.~

QC \oo

Transport

Properties

of Oxygen

H. M. Roder

Thermophysical Properties Division

National Engineering Laboratory

National Bureau of Standards

Boulder, Colorado

Prepared for NASA Lewis Research Center

1983

Scientific and Technical

Information Branch

Contents

Page

1. Introduction 1

2. Representation of the Viscosity 3

3. Representation of the Thermal Conductivity 4

3.1 Calculations for Region 1 7 3.2 Calculations for Region 2 8

3.3 Boundaries for Regions 1 and 2 9

4. Representation of the Thermal Diffusivity 9

5. Prandtl Number 11

6. Description of the Data Tables 13

7. Error Estimates 14

8. Summary 15

9. References 16

Appendix A. Program Listings for Viscosity 80

Appendix B. Program Listings for Thermal Conductivity 81

Appendix C. Conversion Factors, Oxygen 83

List of Figures

Figure 1. Region of the PVT surface covered by the new thermal

conductivity measurements [8] 6

List of Tables

Table 1. Overview of Previous Publications 2

Table 2. Thermal Conductivities near 162.9805 K 10

Table 3. Thermal Conductivities from Li ghtscatteri ng, Weber [9] . . 12

Table 4. Transport Properties of Oxygen for saturated Liquid

and Vapor, SI Units 17

Table 5. Transport Properties of Oxygen, Isobars, SI Units .... 18

Table 6. Transport properties of Oxygen for saturated Liquid

and Vapor, Engr. Units 50

Table 7. Transport Properties of Oxygen, Isobars, Engr. Units ... 52

i i i

TRANSPORT PROPERTIES OF OXYGEN

H. M. Roder

Thermophysical Properties Division

National Engineering Laboratory

National Bureau of Standards

Boulder, Colorado 80303

1. Introduction

An accurate thermophysical properties base for fluid oxygen has been

developed through a series of measurements and analyses. Table 1 presents a chronology of prior publications which contain equations of state, correlations

of the transport properties, data tables for the transport properties, or a combination of these items. Table 1 shows that the massive set of tables for

oxygen in NASA SP 3071 [2] has gradually been extended and superseded by new measurements and new correlations. Specifically there have been new experimental

measurements of viscosity [4], a new correlation of viscosity and thermal

conductivity [3], an extension of the PVT measurements from 34 MPa (5000 psia) to

80 MPa (12000 psia) [5], a new equation of state which includes the extension in

pressure [6], the development of an interactive package for the equation of

state [7], new experimental thermal conductivity measurements [8], and new experimental thermal diffusivity measurements near the critical point [9]. The

present tables were computed because previous tables of the transport properties

of oxygen extend to only 34 MPa (5000 psia), and because for thermal conductivity

the new measurements [8,9J show the previously best correlation l 3 J to be in error by up to 35 percent for nearly all temperatures at the highest pressures.

1
Table

1.

Overview

of

Previous

Publications

2
2 . Representation of the Viscosity

Values of the viscosity are calculated from the correlation of Hanley,

et al . [3_|. For the correlation the authors surveyed the literature and

systematically selected data which met particular criteria for accuracy. For

oxygen the experimental measurements of Haynes [4] with an accuracy of 2 percent

were selected. This set of data was measured with a torsionally oscillating

quartz crystal , and it comprises some 200 points at temperatures from 75 to 300 K with pressures to 34 MPa. The correlation expresses viscosity in terms of

density and temperature, and it requires an equation of state (EOS) to translate

pressures into equivalent densities. The EOS most commonly used is the

interactive package by McCarty [7]. The dependence of viscosity on temperature

and density is expressed in [3] as

n(p »T) = n

0

(T) + n-|(T)p + an(p,T) + an

c (p,T) , (1)

where

t- 1 x t -2/3 x t -1/3 x , t 1/3 , t 2/3 ^ T n

o

= g

l T + y2T 9 3

T +fM 9

5

T g 6 T 9

7 T

98

T

4/3

9gT

3 ^ 3

and

n

1 (T) = A + B [C - tn(T/F)] 2

,

and

an(p,T) = D exp[

i + k

2

/T] |exp[p 0,1

(k

3 + k 4

/T 3/2

)

+ ep

0,5

(k

5 + k6

/T + k

? /T2

)] - 1 .0

}

,

( 2 )

(3)

(4)

where 0 is a density dependent factor given by e = (p - p

c )/p . While there is evidence for an enhancement of viscosity near the critical

point, term 4 in eq (1), zati (p,T), is not considered in reference L 3 J . Program

listings to calculate the viscosity [ 7 J are given in appendix A. For completeness the values of the coefficients for eqs (2-4) are listed below. For these

* A full description of how to calculate An

c (p,T) is given in reference [10].

3
3 coefficients the units implied are temperature in K, density in g/cm , and

viscosity in pg/cm*s.

Equation (2) Equation (3) Equation (4)

g

1 = -9.7076378593E+1

g

2

= 8.2801254201 E+l

g

3 = -2.4668758803E+1

g4

= 2.1324360243

A

F

C

B

4.352652

2.036126

1.4

100.0

D -12.15239

2.434069 x 10

2

18.20116

- 2.749896 x 10

3

1 .0 pg/cm s

g

5 = 3.7851 049522 E

g 6

= -1 .0487216090E-1

g

? = 1.11 34441304E-2

g 8

= -5.3676093757E-4

g

g = 1 .0279379641 E-5

- 0.3142173

1.191150 x 10

2

2.739043 x 10

2

0.435 g/cm3

3. Representation of the Thermal Conductivity

Values of the thermal conductivity are calculated from the correlation of

Roder [8]. This new correlation is based on new experimental measurements of the

thermal conductivity [8 j and new experimental measurements of the thermal

diffusivity [9]. The new conductivity values [8] comprise 1126 points measured

on 13 isotherms from 78 to 310 K with pressures to 70 MPa. The measurements were

made with a new transient hot wire apparatus.

The new correlation expresses thermal conductivity as a function of density

and temperature rather than temperature and pressure because over a wide range of

experimental conditions the behavior of thermal conductivity is dominated by its

density dependence. The technique requires an equation of state [7] to translate

measured pressures into equivalent densities. The dependence of thermal

conductivity on temperature and density is normally expressed as

The first term on the right of eq (1) is the dilute gas term which is

independent of density. The second is the excess thermal conductivity. The

first two terms taken together are sometimes called the "background" thermal

conductivity. The final term is the critical point enhancement. The dilute gas

term is expressed as

A(P,T) = A

q

(T) + X excess(p»T) + AX critical (5)

4
( 6 )

A

o (T) = [A -|T ~ 1 + A

2

T"

2/3

+ A

3

T'

1/3

+ A

4 + A5T

1/3

+ A

6

T

2/3

+ A

? T + AgT4/3

+ A

g T

5/3 ]/1000 .

with A

q in W/m*K and T in kelvin.

The expression used for the excess thermal conductivity is as follows:

A

excess

(p « T > = “P + 5[e

BpY -1.0] (7)

where the parameters a, £, y, 6 are functions of temperature as follows:

a = B-jT y

= + B^T + B^T2

( 8 )

3

= B^ + B^T + B^T2

6 = Bg + B

g

T + B-jq/T

2

The coefficients for eqs (6) and (7) with T in kelvins and A in W/m*K are Equation (6) Equation (7)

A

1 = -2.0395052193E+5 Bi = .298644E-5

A

2

= 2 . 4088 141709E+5 B 2

= .59842E+00

A

3

= -1 .2014175 1 83E+5 B 3= .1 1 362E-01

A

4

= 3.295494919E+4 B

4

= - . 1 9520E-04

A

5

= -5.4244239598E+3 b

5

= .47624E+00

A

6

= 5.4734865540E+2 B,u

= - .64769E-03

A

7

= -3.2854821539E+1 B

7 = .83223E-06

A

8

= 1.0753572103 B

S

= - .278141 E-4

a

9

= -1.4610986820E-2 B

9

= .1 53705E-6

B 10

= .147176E+1

The calculation of the third term in eq (5) is split into two separate regions

which are shown in figure 1. The first region is called the critical region

proper, and it corresponds roughly to the range of conditions for which Sengers,

et al . [10] recommend the use of a scaled equation of state. The second region

is called the extended critical region. It is shown as a triangle in figure 1

5
DENSITY,

mol/L

TEMPERATURE, K

Figure 1. Region of the PVT surface covered by the new thermal conductivity

measurements [8]. Also shown are regions 1 and 2 for the

calculation of the critical point enhancement. The new thermal

diffusivity measurements [9] are nearly all located in region 1.

6
and covers those densities and temperatures for which the new measurements [8]

reveal an anomalous increase above the background conductivity.

3.1. Calculations for Region 1 We define the reduced variables T = T/T , p = p/p„, P = P/P _ and

AT = (T - T

c )/Tc and Ap (p - p c )/pc (9)

The scaling variables are defined by

x - at*/|ap*i 1/b

X + X. and y

=

( 10 )

The symmetrized compressibility is defined by

* _

I Ap y/b [(1 + E)/(l + Ey26

L

D[6 + (y - 1 ) (6 - B'

1 +u

(•Y - 1)/2B

Ey

26

)/(l + e/b

)] ]

for which a special case occurs at the critical isochore where Ap = 0

(ID

x; = r| AT*r . ( 12 )

The coefficient r in eq (12) is defined by

r ^1 +

(13)

Given the definitions above, Sengers, et al . [10] estimate the critical

enhancement from

This equation relates the thermal conductivity enhancement at a given temperature

and density to the pressure coefficient (3P/3T) , the symmetrized compressibility

P

X*|* and the (normal) shear viscosity n«

7
The values to be used with eqs (9-14) for oxygen are 154.581 K 13.63 mol/L

49.77054 atm

1.38054 * 10“23 J/K

n = 0

A = 1.04

A

x

= 39.8

B

a

= 5.45

5 = 5.9783 x 10

-10

8

Y

6

D

E

X,

0.355

1.190

4.352

2.36

0.287

0.183

The prescription given by Sengers, et al . [10] has been modified in two

minor ways. First, the value of a adopted to be 1.02 for CO^ in [10] is chosen

to be 1.04 for oxygen. This number is established as a best value for Weber's

new experimental diffusivity measurements [9], see section 4. The second

modification is to extend the calculation using the scaled equation out to a temperature of 162.9805 K or 1.054 T

c rather than 1.03 T .

3.2. Calculations for Region 2

The expressions used in this region are as follows [8].

AXcritical<p ' T > =

{ C

1 /(T + C 2> + C3 + C4

T

} "

-X

(15)

we define

^center pc + ^5^ " ^

1 .5

(16)

then the variable x in eq (15) is

x = C c (p - p . ) for p > p 4. , 6

X 'center 7 K ^center ’

X Cg(p - P cen ^- er

) + 6y(p - P cen-)- er)

The coefficients for eqs (15-18) are

for p ^ p center

T =

c 154.581 K C 4

- - .282950E-04

p

c

= 13.63 mol/L <5- - .71 599E-3

c, .219200E+0 C

f, .13804E+0

C

2

C

3

-145.55

. 7345 1 2E -02

O

i

II .1 2980E-5

(17)

(18)

8
3.3. Boundaries for Regions 1 and 2

The four boundaries defining the two different regions of computation are the saturated liquid and vapor at the lower temperature, 162.9805 K at the upper

temperature, densities between 8.5 and 7.5 mol/L at the lower density, and

densities between 18 and 13.6 mol/L at the upper density. The boundaries are shown in p-T coordinates in figure 1. For any given temperature between

saturation and 162.9805 K the switch between regions 1 and 2 is accomplished

without an abrupt change in the value of A. This is done by switching at those

densities where the calculated values of thermal conductivity from [8] and [10] are equal

The switch in calculation at the upper temperature boundary of 162.9805 K can not, unfortunately, be accomplished without an abrupt change in the value

of thermal conductivity. The reason for this is because in reference L10] the

centering density is p

c by definition, whereas in reference [8] the centering

density is less than p

c for all temperatures other than T

c

» The maximum "glitch"

along the 162.9805 K boundary is about 1.6 percent in the value of A. The local

change across this boundary is shown for densities from 0 to 30 mol/L in

table 2.

Programs to calculate the thermal conductivity are new. Listings are given

in appendix B. The changes required in the program set of reference [7] to

implement the new thermal conductivity calculation are indicated in appendix B by arrows.

4. Representation of the Thermal Diffusivity

The thermal diffusivity is defined by

a = A/p C

p

(19)

where C

p is the heat capacity at constant pressure. Both p and C

p are normally

obtained from an equation of state and the thermal diffusivity is then calculated

from the thermal conductivity. Occasionally the thermal diffusivity is measured

directly, as was done by Weber [9] who used a light scattering apparatus to

measure the thermal diffusivity, primarily in the critical region.

The experimental information to be considered are the 76 points presented in

three groups in table 3, where the values are taken from reference [9]. Weber

converted his experimental measurements of thermal diffusivity to values of

9
Table ?. Thermal Conductivities near 162*9805 K Temoer atur es Density Thermal Conductivities Dev I at I ons Inside outside Inside outs 1 de 1 n.-out.

K K mo 1 /L V/m.K W/m.K W/m.K percer

162.980 162 .<381 .5 .015578 .015579 -.000000 -.00 162.980 162 .<381 1.0 .016030 .016030 -.000000 -.00 162.980 162 .<381 1.5 .016539 .016539 -.000000 -.00 162.980 162.961 2.0 .017123 .017123 -.000000 -.00 162.980 162.981 2.5 .017795 .017795 -.000000 -.00 162.980 162.961 3.0 .018566 .018566 -.000000 -.00

16? • 9 8 0 162.961 3.5 .019636 .019636 -.000000 -.00

162. 98C 162.901 8 . 0 .020612 .020612 -.000000 -. 00 162.980 162.981 8.5 .021691 .021691 .000000 .00 162.980 162.961 5.0 .022668 .022668 .000000 .00 162.980 162.981 5.5 .023938 .023938 .000000 .00 162.980 162.981 6.0 .025296 .025296 .000000 .00 162.980 162.981 6.5 .026728 .026728 .000000 .00 162.980 162.961 7.0 .028231 .028231 .000000 .00 162.980 162.961 7.5 .029792 .029792 .000000 .00 162.980 162.981 8.0 .031602 .031601 .000000 .00 162.980 162.981 8.5 .033216 .033066 .000168 .50 162.980 162.981 9.0 .035036 .036713 .000321 .92 162.980 162.961 9.5 .036831 .036386 .000665 1.21 162.980 162.981 10.0 .038586 .038051 .000535 1.39 162.980 162.981 10.5 .060280 .039692 .000588 1.66 16?.9«0 162 .961 11.0 .061896 .061292 .000602 1.66 162.980 162.981 11.5 .063611 .062836 .000575 1.32 162.980 162.981 12.0 .066813 .066310 .000503 1.12 162.980 162.961 12.5 .066087 .065703 .000386 .83 162.980 162 .961 13.0 .067229 .067005 .000226 .67 162. 980 162.961 13.5 .068258 .06 8213 .000065 .09 162.980 162.981 16.0 .069325 .069326 .000001 .00 162.980 162.981 16.5 .050362 .050362 .000001 .00 162.980 162.961 15.0 .051276 .051276 .000001 .00 162.980 162.981 15.5 .052131 .052131 .000001 .00 162.980 162.981 16.0 .052928 .052928 .000001 .00 162.980 162.961 16.5 .053682 .053681 .000001 .00 162.980 162.981 17.0 .056613 .056612 .000000 .00 162.980 162.981 17.5 .055161 .055161 .000000 .00 162.980 162.981 18.0 .055890 .055889 .000000 .00 162.980 162.981 18.5 .056680 .056680 .000000 .00 162.980 162.961 19.0 .057533 .057533 .000000 .00 162.980 162.981 19.5 .058668 .058668 .000000 .00 162.980 162.981 20.0 .059506 .059506 .000000 .00 162.980 162.981 20.5 .060656 .060656 .000000 .00 162.980 162 .961 21.0 .061937 .061937 .000000 .00 162.980 162.961 21.5 .063358 .063358 .000000 .00

1 62.980 162.981 22.0 .066927 .066927 .000000 .00 162.980 162.981 22.5 .066651 .066551 .000000 .00 162.980 162.961 23.0 .068533 .068533 .000000 .00 162.980 162

9 el 23.5 .070576 .070576 -.000000 -.00 162.980 162.981 26.0 .072780 .072780 -.000000 -.00

162.980 162.961 26.5 .075165 .075165 -.000000 -.00 162.980 162.981 25.0 .077671 .077671 -.000000 -.00 162.980 162.981 25.5 .080356 .080356 -.000000 -.00 162.980 162.981 26.0 .083195 .083195 -.000000 -.00 162.980 162.981 26.5 .086190 .086190 -.000000 -.00 162.980 162 .981 27.0 .089339 .089360 -.000000 -.00 162.980 162.981 27.5 .092661 .092661 -.000000 -.00 162.980 162.981 28.0 .096095 .096095 -.000000 -.00 162.980 162.981 28.5 .099700 .099700 -.000000 -.00 162.980 162.981 29.0 .103658 .103658 -.000000 -.00 162.980 162.981 29.5 .107369 .107369 -.000000 -.00 162.980 162.981 30.0 .111636 . 111636 -.000000 -.00

10
thermal conductivity using eq (19). Thus the comparisons to be made are "experimental thermal conductivity" to calculated thermal conductivity, where the method

of calculation has been described in the previous section. In table 3 the first

group, 14 points, includes all of Weber's measurements with temperatures greater

than 158. K, i.e., these points represent an overlap of the experimental

measurements of references [8] and [9]. The second group, 33 points, includes

those measurements for which the experimental densities lie between 13.1 and

13.7 mol/L, or |Ap*| 0.04. In essence this group is quite close to critical

density. The remaining 29 points, i.e., the last group, are characterized by

experimental densities which are considerably different than critical density.

Differences between the calculation and Weber's "thermal conductivity" values [9] are given in table 3. The RMS deviation for the first grouping of 14 points is

5.3 percent. Well within the experimental uncertainty estimated by Weber, this

average deviation indicates agreement between the diffusivity experiment and the

hot wire thermal conductivity measurements. For the second grouping of 33 points

we find an RMS deviation of 7.5 percent, again within the expected uncertainty of

the experimental measurements. This average deviation indicates agreement

between the diffusivity measurements and the most current method of predicting

the anomalous thermal conductivity in the critical region for densities close to

critical, i.e., for AA

c

(p c ,T) . However, the deviation of the third grouping of

29 points is nearly 27 percent RMS, which exceeds experimental uncertainty by a considerable margin, and indicates a basic disagreement between these measurements and the prediction for densities which are substantially different from

critical density. Despite considerable effort, the cause of the disagreement

remains unresolved. The calculation values off the critical isochore may,

therefore, be uncertain by as much as 30 percent for both thermal diffusivity and

thermal conductivity.

5. Prandtl Number

The Prandtl number, Pr, is defined by the relation

Pr = C

p nM (20)

where C is the specific heat at constant pressure, n the viscosity and X the

r thermal conductivity. To conserve space the Prandtl number has not been

presented in the tables, it is however quite easy to calculate the Prandtl number

11
Table 3. Thermal Conductivities from 1 1 ghtscatter I ng» Weber [9].

T emper ature Dens 1 1 y Thermal

exp. Conductivity

calc. Deviationsexp.-ca 1 c* GroupRMS

K mo 1 /L W/m.K W/m.K W/m.K percent percent

158.519 13.1b .0556 .0562 -.0006 -1.16 161.8*7 13. 14 .0*80 .0*90 -.0010 -2.08

16*. *26 13.27 .0*82 .0*68 .0014 2.82

16* .*26 13.27 .0*70 .0*68 .0002 .34 16*. *26 13.27 .0*** .0*68 -.0024 -5.50 166.796 13. 08 .0*15 .0*53 -.0038 -0. 15 168.9*6 13.21 .0**0 .0**9 -.0000 -1.04

173.935 13.04 .0*1* .0*33 -.0010 -4.40

159.583 13 .40 .05*1 .0538 .0003 .57 159.890 13.44 .0525 .0530 -.0005 -.08 159.883 13.58 .0537 .0533 .0004 .80 159.878 13.50 .0527 .0531 -.0004 -. 84 158.133 15.30 .0693 .0589 .0104 15.03

160. *93 15.30 .0550 .05*2 .0008 1.44

5.23

15*. 619 13.13 .2507 .2855 -.0348 -13.00

155.173 13.18 .10*3 .0996 . 0047 4.51 155.6*9 13.10 .0875 .0812 .0063 7.16 155.651 13.20 .0871 .0812 .0050 6.74 156.6*2 13.10 .0715 .0665 .0050 7.03 157.580 13.18 .0627 .0601 .0026 4.12

15*. 717 13.33 .18*2 .1835 .0007 .35 15*. 7*6 13.37 . ] 758 .1697 .0061 3.47

15*. 771 13.40 .167* .1600 .0074 4.40

15*. 787 13.38 .1601 .15*3 .0058 3.64

15* . 795 13. 30 .1 578 .1520 .0058 3. 68 15*. 6*5 13.42 .2610 .2635 -.0025 -.05

15*. 690 13.44 .2109 .2063 .0046 2.17

1 5*. 801 13.44 .1627 .1507 .0120 7.36

15* . 8*1 13. 46 .1567 . 1*0* .0163 10. 37 15*. 872 13.43 .1*26 .1337 .0080 6.21 155.025 13.47 .1212 .1129 .0083 6.88 155.03* 13.53 .1230 .1121 .0100 8.87 155.271 13.56 .1100 .0956 .0144 13.00 155.52* 13.54 .0990 .0856 .0134 13. 52 155.5*6 13.57 .0970 .0850 .0120 12.40 155.769 13.57 .0891 .0793 .0008 10.08 156.003 13.58 .0855 .07*9 .0106 12.35 156.509 13.58 .0783 .0685 .0008 12.56

157. 000 13.58 .0731 .06*3 .0088 12.03

157. *68 13.58 .06*3 .061* .0020 4.40

15*. 595 13. 63 . 5600 . 5831 -.0231 -4.12

15*. 598 13.63 .5180 .5266 -.0086 -1.66

1 5* . 590 13.63 . 5230 .5111 .0110 2.27

1 5*. 603 13.63 • * 72 C .*605 .0115 2.44

15*. 617 13.63 . 3 550 . 3578 -.0028 -. 70 15*. 628 13.63 .3170 .3129 .0041 1.20

15*. 678 13.63 .2250 .2198 .0052 2.30

7.61

15*. 579 12.08 .7700 .*065 . 3635 47.21

15*. 560 12.51 . 2825 .1839 .0086 34.80

15*. 5*2 12.26 .2152 .1*32 .0720 33.47

1 5* .*97 11.87 .152* .1057 .0467 30.61

1 5* .**9 11.57 . 1 256 .0893 .0363 28.03

15*. *10 11.38 .1206 .0813 .0303 32.62

15* .388 11.20 .1058 .0779 .0270 26.41

15*. 361 11.18 .113* .07** .0300 34.44

15*. 267 10.86 .0906 .0659 .0247 27.31

15*. 169 10.50 .0687 .0602 .0085 12.40

1 5* . 131 10.40 .0870 .0585 .0285 32.78

15*. 007 10.22 .0723 .05*1 .01 82 25.22

15* .000 10.21 .0707 .0538 .0160 23. 83 153.792 0.83 .0565 .0*89 .0076 13.54 153.57* 0.40 .0517 .0*52 .0065 12.56 153.330 0.18 .0*76 .0*23 .0053 11.21 152.860 8.66 .0*05 .0380 .0025 6. 14 152.0*2 8.65 .0*57 .0379 .0078 17.11

15* . 808 15.28 .1295 .097* .0321 24.76 155.0*6 15.20 .1110 .0861 .0240 22.43 155.1*3 15. 20 .1213 .0832 .03 81 31.44

155. 28C 15.30 . 1 029 .0797 .0232 22.53 155.51* 15.30 .0950 .075* .0106 20.66 155.737 15.20 .08** .072* .0120 14.21 155.7*0 15.30 .0978 .0723 . 02 55 26. 07 155.752 15.30 .0922 .0721 .0201 21.76 156.221 15.31 .0851 .0676 .0175 20.55

15* .579 14.20 .6580 .3889 .2601 40. 80 15* .*09 15.00 .1265 .0828 .0437 34.57

26.88

12
from the variables tabulated. If we solve eq (19) for C

p and substitute into

eq (20) the relation for the Prandtl number becomes

Pr ( 21 )

As an example we use eq (21) to determine Pr for the saturated liquid at 100 K

p _ 1542.3 x 1(T

6

Kr 1.0907 x 0.000723

1 .956

Values for n, P, and a are taken from table 4. Because the viscosity is

tabulated in yg/cm s rather than Pa s, no unit conversions are required, and Pr

is dimensionless as expected.

6. Description of the Data Tables

The following tables of values for the transport properties are presented

in this report:

Table 4. Transport properties of oxygen for saturated liquid and vapor, SI

units.

Table 5. Transport properties of oxygen, isobars, SI units.

Table 6. Transport properties of oxygen for saturated liquid and vapor, Engr.

units.

Table 7. Transport properties of oxygen, isobars, Engr. units.

Table entries of temperature and pressure are chosen to correspond to the

values given in NASA RP 1011 [5] so that the present tables can be thought of as

an augmentation or extension of the earlier ones. Slight differences in the

vapor pressure and density entries may be evident; they occur because the

tables of NASA RP 1011 [5] were prepared using a polynomial PVT surface, while

the present tables utilize a modified Benedict-Webb-Rubin equation of state [7].

It was not possible to use the polynomial PVT surface because that program

specifically excludes a portion of the PVT surface close to the critical point.

Conversions to other SI units and to units normally used in applied problems are given in appendix C. The tables were calculated using the programs listed in

appendices A and B. The new programs given in appendix B for the thermal

conductivity were written to be compatible with the equation of state package of

reference [7]. The primary variables internal to the computer programs of refer- ence [7] are pressure in atmospheres, density in moles/liter, and temperature in

13
kelvins. The changes required in the program set of reference [7] to implement

the new thermal conductivity calculation are listed in appendix B. The changes

are minimal, and they are indicated in appendix B by arrows. Branching occurs on the value of the molecular weight. We note that the dilute gas value for thermal

conductivity, FUNCTION DILV(T), ENTRY DILT of reference [7] remains unchanged.

The number of digits given in tables 4-7 should not be construed to be indicative

of the accuracy of a quantity. Host of the properties in the tables range in

value over several orders of magnitude, making it necessary to print more digits

than is needed at one end of the range. If a given property is varying very

slowly it may require digits beyond those necessary for accuracy to show the

direction of the change. As an extreme case consider the triple point, the first

two lines in table 4. The triple point pressure is not known to be better than

about two digits, yet the saturated liquid density differs by five orders of

magnitude from that of the vapor.

7. Error Estimates

Vi scosi ty : The most recent experimental measurements published for a wide

range of the viscosity surface are those by Haynes [4]. These new measurements

cover temperatures from 75 to 300 K with pressures to 34 MPa. The correlation

[3] represents the 175 experimental points with a RMS deviation of 1 percent

(1 a) where the maximum and minimum deviations are + 3 and - 3 percent. Thus the

uncertainty in viscosity for the tables presented here is approximately 1 percent

for the dilute gas rising to 3 percent at pressures of 34 MPa. The uncertainty

is expected to increase to no more than 10 percent for pressures up to 100 MPa.

Thermal Conductivity : The uncertainty of the dilute gas values is

approximately 1 percent at room temperature and 1 atmosphere pressure, rising to

5 percent in going down to the triple point. The accuracy of the tables is

expected to be 1.5 percent (1 o) over much of the surface, as established by the

fit of the correlating surface [8]. This accuracy degrades to around 6 percent

at 77 K and zero density and to around 6 percent in the region covering the

critical enhancement at 159 K. For temperatures closer to critical the

calculated values may be in error by as much as 30 percent. Extrapolation of the

thermal conductivity surface of [8] for temperatures higher than about 340 K has

not been examined.

Thermal Diffusivity : The uncertainty is estimated to be 5 percent, except

for the critical region. At the critical point the thermal diffusivity is

14
expected to go to zero, even though both thermal conductivity and specific heat

at constant pressure diverge strongly. In the near critical region (T + 3

percent; p c + 30 percent) the uncertainties are as large as 30 percent when

compared to experiment.

8. Summary

This report presents tables of viscosity, thermal conductivity, and thermal

diffusivity of oxygen, as a function of temperature and pressure from the triple

point to 320 K with pressures to 100 MPa. Values of the viscosity are calculated

from a previous correlation. Values of the thermal conductivity are calculated

from a new correlation which combines new experimental measurements of the

thermal conductivity and new experimental measurements of the thermal

diffusivity in the critical region.

15
9. References

1. McCarty, R. D.; and Weber, L. A.: Thermophysi cal Properties of Oxygen from

the Freezing Liquid Line to 600 R for Pressures to 5000 psia. (NBS-TN-384,

National Bureau of Standards.) NASA CR-1 21 739, July 1971.

2. Roder, H. M.; and Weber, L. A.: ASRDI Oxygen Technology Survey. Volume I:

Thermophysical Properties. NASA SP-3071 , 1972.

3. Hanley, H. J. M.; McCarty, R. D.; and Haynes, W. M.: The Viscosity and

Thermal Conductivity Coefficients for Dense Gaseous and Liquid Argon, Krypton, Xenon,

Nitrogen and Oxygen. J. Phys. Chem. Ref. Data, vol . 3, no. 4, 1974, pp. 979-1017.

4. Haynes, W. M.: Measurements of the Viscosity of Compressed Gaseous and

Liquid Oxygen. Physica, vol. 89A, 1 977, pp. 569-582.

5. Weber, L. A.: Thermodynami c and Related Properties of Oxygen from the

Triple Point to 300 K at Pressures to 1000 bar. NASA RP-1011 , 1977.

6. Weber, L. A.: A Modified Benedi ct- Webb-Rubi n Equation of State for Gaseous

and Liquid Oxygen. (NBSIR-78-882, National Bureau of Standards.) NASA CR-157861 ,

April 1978.

7. McCarty, R. D.: Interactive FORTRAN IV Computer Programs for the

Thermodynamic and Transport Properties of Selected Cryogens (Fluids Pack).

(NBS-TN-1025, National Bureau of Standards.) NASA CR-164016, Oct. 1980.

8. Roder, H. M.: The Thermal Conductivity of Oxygen (Submitted to J. Res. Nat.

Bur. Stands.)

9. Weber, L. A.: Thermal Conductivity of Oxygen in the Critical Region.

(Submitted to Intern. J. Thermophysics .

)

10.

Sengers, J. V.; Basu, R. S.; and Level t Sengers, J. M. H.: Representative

Equations for the Thermodynami c and Transport Properties of Fluids Near the

Gas-Liquid Critical Point. NASA CR-3424, May 1981.

16
Table 4. Transport Properties of Oxygen for saturated Liquid and Vaporj SI Units

Temp* Pressure Density

K MPa g /cm**3

54.359 .00015 1.306190

54.359 .00015 .000010

56. .00024 1.299003

56. .00024 .000017

58. .00043 1.290220

58. .00043 .000028

60. .00073 1.281405

60. .00073 .000047

6 2. .00119 1.272552

63. .00119 .000074

64. .00188 1.263654

64. .00188 .000113

66. .00288 1.254707

66. .00288 .000168

68. .00429 1.245706

68. .00429 .000244

70. • 008 2 5 1.236647

70. .00625 .000345

72. .00889 1.227527

73. .C0PB9 .000478

74. .01240 1.218340

74. .01240 . 000650

76. .01695 1.209083

76. .01695 .000866

78. .02276 1.199753

78. .02276 .001137

80. .03009 1 .190345

80. .03009 . C01469

82. .03919 1.180854

82. .03919 .001872

84. .05035 1.171275

84. .05035 .002356

86. .06387 1.161604

86. .06387 .00’931

88. .08007 1.151835

88. .08007 .003607

90. .09931 1.141960

90. .09931 .004396

92. .12194 1.131973

92. .12194 .005308

94. .14833 1.121867

94. .14833 .006357

96. .17887 1.111632

96. .17887 .007555

98. .21395 1.101259

98. .21395 .008916

1H0. .25399 1.090736

100. .25399 .010452

102. .29940 1.080053

102. . 29940 .012180

104. .35061 1.069196

104. .35061 .014115

Thermal

Cond

.

W/m.K

Viscosity

ml crog/cm.

s

Thermal

Olffus Ivlty cm**2/s

.20356

.00408 4852.336.3 .0009374 .270533

.20050

.00436 4677.638.0 .000927 2.860294

.19693 .00467 4462.3

39.9 .000915 1.797919

.19353

.00495 4248.241.8 .000905 1.161530

.19026 .00520

4038.2

43.6

. 000896

.770926

.18710

.00543 3834.445.4 .000888.525087

.18404

.00565 3638.347.1 .000879

.366477

.18105 .00586

3450.

8

48.8 .000871

.261671

.17813 .006073272.3

50.5 .000863.190824

.17526

.00627

3103.0

52.1 .000855

.141898

.17243 .00647 2943.0

53.8 .000847

.107424

.16964 .00667 2791.9

55.4 .000839.082673

.16687

.00687 2649.5

87.0 .000831

.064591

.16411 .00708 2515.5

58.7 .000823

.051164

.16137

.00728 2389.560.3 .000814.041042

.15864 .00749 2271.0

61.9 .000806.033303

.15590

.00770

2159.5

63.5

. .000797

.027309

.15317

.00791 2054.765.2 .000787.022609

.15043 .008121956.1

66.8 .000778.018882

.14769

.00834

1863.3

68.5 .000768

.015896

.14494 .00856 1775.9

70.1 .000757 .013479

.14217

.00879

1693.5

71.8 .000746.011504

.13940

.00902 1615.7

73. 5 .000735

.009878

.13661

.00926 1542.375.2 .000723.008527

.13380

.00949

1472.

8

76.9

.000711 .007397

.13058 .00974 1407.1

78.

6

.000698 .006444

T emp

.

Pressure Dens 1 ty

K MPa g/cm**3

106. .4081 1.05815

106. .4081 .01627

108. .4722 1.04690

108. .4722 .01867

110. .5434 1.03543

110. . 5434 .02134

112. .6222 1.02371

112. .6222 .02428

114. .7090 1.01173

114. .7090 .02753

116. .8043 .99946

116. .8043 .03111

118. .9085 .98687

118. .9085 .03506

120. 1.0222 .97392

120. 1.0222 .03939

122. 1.1458 .96059

122. 1.1458 .04416

124. 1.2 79 7 .94683

124. 1.2797 .04940

126. 1.424 5 .93260

126. 1.4245 .05515

128. 1.5807 .91782

128. 1 .5807 .06149

130. 1.7488 .90245

130. 1.7488 .06847

132. 1.9294 .88640

132. 1.9294 .07618

134. 2.1229 .86957

134. 2.1229 .08472

136. 2.3301 .85185

136. 2.3301 .09421

138. 2.5514 .83309

138. 2.5514 . 10481

140. 2.7875 .81308

140. 2 .7 87 5 .11674

142. 3.0392 .79155

142. 3.0392 .13028

144. 3.3072 .76811

144. 3.3072 .14584

146. 3.5924 .74215

146. 3.5 92 4 .16405

148. 3.8958 .71262

148. 3.8958 .18598

150. 4.2186 .67747

150. 4.2186 .21370

152. 4.5625 .63157

152. 4.5625 .25242

154. 4.9305 . 54944

154. 4.9305 .32914

154.581 5 .0430 .54944 154.581 5.0430 .32914

Therma 1 Cond. W/m.KViscosity

microg / cm . s

Thermal Diffuslvlt cm**2/s

.12814 .00999 1344.8

80.4 .000685.005636

.12528

.01025 1285.682.2 .000671.004945

.12241 .01051 1229.4

84.0 .000657.004352

.11951 .01078 1175.9

85.8 .000642 .003840

.11659

.01106 1124.8

87.7 .000626.003395

.11365 .01135 1075.0

89.6 .000610 .003006

.11069

.01165 1029.491.6 .000593

.002665

. 10770

.01196 984.693.7

.000575

.002365

.10468

.01230 941.6

95.8

.000557 .002099

.10164

.01264 900.298.0

.000538

.001862 .09857

.01302 860.3100.3

.000518

.001651

,0954e

.01342 821.6 102.7

.000497 .001462

.09235 .01385784.1 105.2

.000475

.001292

.08920

.01433 747.6107.9

. 000453

.001138

.08602

.01487 712.0

110.8

.000429

. 000999

.08282 .01549 677.2

113.9

.000404

.000873

.07960

.01621 642.9117.3

. 000378 .000759

.07638

.01706 608.9121.1

.000350

.000654

.07317

.01811 575.1125.3 .000320 .000557

.07002

.01945 541.1130.1 .000289.000467

.06700

.02121 506.4 135.7

.000254

.000383

.06423 .02365 470.4

142.6

.000216

.000302

.06197 .02726 431.5

151.5

.000171 .000221

.06075

.03324 366.2 164.7

.000115

.000133

.06376

.05480 317.9

193.9

.000034 .000035
Table 5. Transport Properties of Oxygen* Isobars* SI Unit

.1 MPa Isobar #2 MPa Isobar

TempDensity Thermal V i sco s i t

y

Thermal Temp. Density Ther ma

Viscosity Therma

C ond • micro- Dlffuslvlty C on d

micro- Dlf fusiv

K g/cm**3 W/m.K g/cm.s cm**2/s K g / cm** 3 W/m.K g /cm.

cm**2

54.370 1.3063 .20358 4855.4 .000937 * 54.3 82 1.3063 .20361 4858.5 .000937

56. 1.2991 .20054 4681.7 .000927 56. 1.2992 .20059 4685.8 .000927

58. 1.2903 . 19698 4466.2 .000916 58. 1.2905 .19703 4470.0 .000916

6 C • 1.2815 .19358 4251.8 .000906 60. 1.2817 .19362 4255.4 .000906

62. 1.2727 .19031 4041 .6 .000896 62. 1.2728 .19036 4045.0 .000897

64. 1.2638 .18715 3837.6 .000888 64 . 1.2639 .18720 3840.9 .000888

66. 1.2548 .18409 3641.3 .000879 66. 1.2550 .18414 3644.5 .000880

68. 1.2458 .18110 3453 .6 .000871 68. 1.2460 .18116 3456.6 .000872

70. 1.2368 .17818 3275.0 .000863 70. 1.2369 .17824 3277.8 . 000864

72. 1 .2277 .17531 3105.5 .000855 72. 1.2278 .17537 3108.2 .000856

74. 1.2185 .17248 2945.2 .000847 74. 1.2186 .17254 2947.8 .000848

76. 1.2092 .16969 2793.9 .000840 76. 1.2094 .16975 2796.4 .000840

78. 1.1999 .16691 2651.4 .000831 78. 1.2001 .16698 2653.8 .000832

80. 1.1905 .16416 2517.1 .000823 80. 1 .1906 .16422 2519.5 .000823

82. 1.1810 .16141 2390.8 .000815 82. 1.1812 .16148 2393.1 .000815

84. 1.1714 .15867 2272.0 .000806 84 . 1.1716 .15874 2274.2 . 000806

86. 1.1617 .15593 2160.3 .000797 86. 1 . 1619 .15600 2162.3 .000797

88. 1.1519 .15318 2055.1 .000787 88. 1.1521 .15326 2057.1 .000788

<30. 1.1420 .15043 1956.1 .000778 90. 1.1422 .15051 1958.1 .000778 90.066 1.1416 .15034 1953.0 .000777 92. 1.1322 .14775 1864.8 .000768 90.066 .0044 .00813 66.9 .018773 94. 1 . 1220 .14498 1776.8 .000757

92. .0043 .00831 68.4 .019778 96 . 1.1117 . 14219 1693.8 .000747

94. .0042 .00851 69.9 .020837 97.237 1.1052 .14046 1644.8 .000739

96. .0041 .00870 71.5 .021917 * 97.237 .0084 .00893 72.8 .010463

98. .0040 .00889 73.0 .023018 98. . 0083 .00901 73.4 .010686

100. .0039 .00909 74.6 .024141 100. . 0081 .00920 75.0 .011276

102. .0039 .00929 76.1 .025286 102. .0079 .00939 76.5 .011876

104. .0038 .00948 77.7 .026452 104 . . 0077 .00959 78.0 .012484

106. .0037 .00968 79.2 .027640 106. .0076 .00978 79.6 .013102

108. . 0036 .00988 80.8 .028849 108. .0074 .00998 81.1 .013730

110. .0036 .01008 82.3 .030079 ' 110. .0073 .01018 82.6 .014366

112. .0035 .01028 83 .8 .031331 112 . . 0071 .01037 84.1 .015013

114. .0034 .01048 85.3 .032604 114. .0070 .01057 85.7 .015668

116. .0034 .01068 86.9 .033898 116. .0069 .01077 87.2 .016333

118. .0033 .01088 88.4 .035212 118. . 0067 .01097 88.7 .017008

120. .0033 .01108 89.9 .036547 120. . 0066 .01116 90.2 .017692

122. .0032 .01128 91 .4 .037902 122. .0065 .01136 91.7 .018385

124. .0031 .01147 92.9 .039278 124. .0064 .01156 93.2 .019088

126. .0031 .01167 94 .4 .040673 126. .0063 .01175 94.7 .019800

128. .0030 .01187 95.9 .042089 128. . 0062 .01195 96.2 .020522

130. .0030 .01207 97.4 .043523 130. .0061 .01215 97.7 .021252

132. .0029 .01226 98.9 .044978 132. . 0060 .01234 99.2 .021992

134. .0029 .01246 100.4 .046451 134. .0059 .01254 100.6 .022742

136. .0029 .01266 101.8 .047944 136. .0058 .01273 102.1 .023500

138. .0028 .01285 103.3 .049457 138. .0057 .01293 103.6 .024267

140. .0028 .01305 104.8 .050988 140. .0056 .01312 105.1 .025044

142. .0027 .01324 106.2 .052539 142. . 0055 .01332 106.5 .025831

144. .0027 .01343 107.7 .054110 144. .0054 .01351 108.0 .026626

146. .0027 .01363 109.2 .055700 146. .0054 .01370 109.4 .027432

148. .0026 .01382 110.6 .057312 148. .0053 .01389 110.9 .028248

150. .0026 .01401 112 .1 .058946 150. .0052 .01409 112.3 .029075

152. .0025 .01421 113.5 .060604 152. . 0051 .01428 113.7 .029915

154. .0025 .01440 114.9 .062292 154. . 0051 .01448 115.2 .030770

156. .0025 .01459 116.4 .063940 156. .0050 .01466 11.6.6 .031601

158. .0025 .01476 117.8 .065589 158. .0049 .01484 118.0 .032432

160. .0024 .01494 119.2 .067264 160. .0049 .01501 119.4 .033275

165. .0023 .01539 122.7 .071543 165. .0047 .01546 122.9 .035431

170. .0023 .01584 126.2 .075939 170. . 0046 .01590 126.4 .037645

175. .0022 .01628 129.7 .080442 175. . 0044 .01635 129.9 .039912

180. .0021 .01672 133.1 .085048 180. .0043 .01678 133.3 .042229

185. .0021 .01716 136.5 .089753 185. .0042 .01722 136.7 .044596

190. .0020 .01759 139.8 .094556 190. .0041 .01765 140.0 .047012

195. .0020 .01802 143.1 .099455 195. . 0040 .01807 143.3 .049475

200. .0019 .01844 146.4 . 104449 200. . 0039 .01850 146.6 .051985

210. .0018 .01927 152.9 .114718 210. .0037 .01933 153.1 .057143

220. .0018 .02009 159.3 .125354 220. .0035 .02015 159.4 .062485

230. .0017 .02090 165.5 .136351 230. .0034 .02096 165.7 .068006

240. .0016 .02170 171 .6 .147703 240. .0032 .02175 171.8 .073703

250. .0015 .02248 177.7 .159402 250. . 0031 .02254 177.8 .079573

260. .0015 .02326 183.6 .171442 260. . 0030 .02332 183.7 .085612

270. .0014 .02404 189.4 .183814 270. .0029 .02409 189.5 .091817

280. .0014 .02480 195.1 .196511 280. .0028 .02485 195.2 .098184

290. .0013 .02556 200.7 .209523 290. .0027 .02561 200.8 . 104708

300. .0013 .02631 206.3 .222843 300. .0026 .02637 206.4 . 111384

310. .0012 .02706 211.7 .236472 310. .0025 .02712 211.8 .118215

320. .0012 .02782 217.1 .250436 320. . 0024 .02787 217.2 .125214

Two Phase Boundary

18
Table 5. Transport Properties of fxvaen* Isobars* SI Units

.3 MPa Isobar .4 MPa Isobar

Temp. Den s i tv Thermal

C onrl

.

Viscosity

microThermal

01 f f us 1 v I tv Temp. Dens i t y Therms 1 C on d

.

Viscosity

microTherma

1

Diffusivity

K q / c m* * 3 W/m.K q / c m . s cm**2/s K g / cm** 3 W/m.K g / c m . s cm**?/

s

54.393 1 .3064 .20363 4861.6 . 000937 * 54 .405 1. 3064 •20365 4 86 4 . 7 . 000937

56 . 1 .2 994 .20064 4689.9 .000927 56 . 1. 2995 .20068 4694 .

1

. 000927

58 . 1.2906 .19708 4473 .9 .000916 58 . 1.2907 .10712 4477 .

8

.000916

60 . 1.2818 .19367 4259.1 .000906 60 . 1 . 2819 .10372 426 ? .7 . 000906

6 ?. 1 .2729 .10041 404 8 .5 .000897 62 . 1 . 2731 .10045 4051 .9 . 000897

64 . 1.2640 . 1 87?5 3844.2 . 000888 64 . 1 . 2642 .18730 3847.5 . C 00888

66 . 1.2551 .18410 3647.6 .000880 66 . 1.2552 .18424 3650.7 .000880

6 P • 1.2461 . 1 P 1 2-1 3459.6 .000872 68 . 1.2463 .1 8126 3462.5 . 000872

70 . 1 .2371 .17829 3280.6 . 0008*4 70 . 1 . 2372 .17835 3283.4 . C 00864

72 . 1.2280 .17543 3110.9 .000856 7 ? . 1 . 228 ] .17548 3113.6 . 000856

74 . 1.2198 .17260 2950.4 . C 00 e 4 P 74 . 1.2190 .] 7266 2953.0 . 000848

76 . 1 .2095 .16981 2798.9 .000840 76 . 1 . 2097 .16087 2801.4 .000840

78 . 1 .2002 .16704 2656.2 .000832 78 . 1 . 2004 .16710 2658.6 . 000832

8 C • 1 .1909 .16428 2521.8 .000824 30 . 1 . 1910 .16435 2524.1 .000824

8 2 . 1 .1 813 .16154 2395.3 .000815 82 . 1.1815 .16161 2397.5 .000816

84 . 1 . 1 718 .15981 2276.3 . 000807 84 . 1 .1720 .15807 2278.5 . 000807

86 . 1.1621 . 15607 2164.4 .000798 86 . 1 . 1623 .15614 2166.5 . 000798

PP. 1.1523 .15333 2059.2 . O 0078 P 88 . 1. 1525 .15340 2061.2 . 000789

90 . 1.1424 .15058 1960.0 .000779 90 . 1. 1426 .18066 1962.0 . 000779

92 . 1.1324 . 1 4793 1866.7 .000769 9 ? . 1.1326 .14701 1 868.6 . 0007*9

94 . 1 . 122 ? .14506 1 778.7 .000758 94 . 1 .1225 .14514 1780.6 . C 00759

96 . 1.1119 .14227 1 695 .7 .000747 96 . 1.1122 .14236 1697.5 . 000748

98 . 1.1015 .13947 1617.3 .000736 98 . 1.1018 .13056 1619.1 . 000736

100 . 1 .0909 .13668 1543.1 .000724 100 . 1.0912 .13674 1 544.9 .000724

102 . 1.0901 . 1 33*0 1472 .8 .000711 102 . 1 . 0804 .13380 1474.6 . 000712

* 102.025 1 .0799 . 1 3877 1 47 ?.o .000711 104 . 1 . 0694 .13103 1408.0 . 000699

* 102.025 .0122 .00950 76.9 .007384 * 105.733 1 .0596 .12352 1352.9 .000687

104 . .0119 .00969 78.4 .007803 * 105.733 . 0160 .00006 80.1 . 005736

106 . .0116 • 00 9 Q 8 79.9 .000233 106 . . 0159 .00008 80.3 . 005781

108 . .0114 .01007 81 .5 .008667 108 . . 0155 .01017 81 .

9

.006121

11 C . .0111 .01027 83.0 .009107 110 . .0152 .01036 83.4 . 006464

112 . .0109 .01046 84 .5 .009553 112 . . 0148 .01056 84 .

9

. 006810

114 . . 0107 .01066 qo

*c o .010004 114 . . 0145 .01075 86.4 . 007159

116 . .0105 .01085 87 .5 .010460 116 . . 0142 .01004 87.9 .007512

IIP . . 0103 .01105 89.0 .010923 IIP . . 0139 .01114 89.4 . C 07869

120 . .0101 .01125 90.5 .011391 120 . . 0136 .01133 90.9 . 008230

122 . .0099 .01144 92 .0 .011864 122 . .0134 .01153 92.4 . 008594

124 . .0097 .01164 93.5 .012343 124 . .0131 .01172 93.9 . 008962

126 . .0095 .01183 95.0 .012828 126 . .0129 .01101 95.4 . 009334

128 . . 009 ^ .01203 96.5 .013319 128 . . 0126 .01211 96 .

8

. 009710

130 . .0092 .01222 98.0 .013816 130 . .0124 .01230 98.3 .010090

132 . .0090 .01242 99.5 .014318 132 . . 0122 .01250 99.8 .010474

134 . .0089 .01261 100.9 . 01482 * 134 . . 0120 .01269 101.3 . 010862

136 . .0087 .01281 102 .4 .015340 136 . .0118 .01288 102.7 .011254

138 . .0086 .01300 103.9 .016860 1 38 . .0116 .01308 104.2 .011650

140 . .0085 .01319 105.3 .016386 140 . . 0114 .01327 105.6 .012051

142 . . 0083 .01339 106,8 .016918 142 . .0112 .01346 107.1 .012456

144 . .0082 .01358 108.2 .017456 144 . .0111 .01365 108.5 .012865

146 . .0081 .01377 109.7 .018000 146 . . 0109 .01384 110.0 .013279

148 . .0080 .01397 111.1 .016551 148 . . 0107 .01404 111.4 . 013698

150 . • 007 9 .01416 112.6 .019110 150 . . 0106 .01423 112.8 .014123

152 . .0078 .01436 114.0 .019677 152 . . 0104 .01443 114.3 .014554

154 . .0077 .01455 115.4 .020265 154 . . 0103 .01462 115.7 .014994

156 . .0075 .01473 116.8 .020814 156 . .0101 .01480 117.1 .015417

158 . .0074 . C 1

4

90 118.3 .021371 158 . .0100 .01407 118.5 .015838

160 . .0074 .oisce 119.7 .021938 160 . . 0099 .01515 119.9 .016266

165 . . 0071 .01552 123.2 .023386 165 . . 0095 .01550 123.4 .017361

170 . .0069 .01597 126.6 .024873 170 . . 0092 .01603 126.9 .018484

175 . .0067 .01641 130.1 .026395 175 . . 0090 .01647 130.3 . 019634

180 . .0065 .01684 133.5 .027950 180 . . 0087 .01600 133.7 . 020808

185 . .0063 .01 728 136.9 .029538 185 . . 0085 .01733 137.1 .022006

1 90 . .0061 .01771 140.2 .031158 190 . . 0082 .01776 140.4 .023228

195 . .0060 .01813 143.5 .032809 195 . . 0080 .01810 143.7 .024473

200 . . 0058 .01855 146.8 .034491 200 . . 0078 .01861 147.0 .025741

210 . .0055 .01938 153.2 .037946 210 . . 0074 .01044 153.4 .028346

220 . .0053 .02020 159.6 .041523 220 . . 0071 .02025 159.8 .031040

230 . .0050 .02101 165.8 .045218 230 . . 0067 .02106 166.0 .033822

240 . .0048 .02180 171.9 .049030 240 . .0065 .02186 172,1 .036692

250 . .0046 .02259 177.9 .052957 250 . . 0062 .02264 178.1 .039647

260 . .0045 .02337 183.8 .056996 260 . . 0059 .02342 184.0 . 042686

270 . .0043 .02414 189.6 .061145 270 . . 0057 .02410 189.8 .045807

280 . .0041 .02490 195.3 .065401 280 . . 0055 .02405 195.5 .049008

290 . .0040 .02566 201 .0 .069762 2 90 . . 0053 .02571 201.1 .052287

300 . .0039 .02642 206.5 .074224 300 . . 0051 .02646 206.6 . 055642

310 . .0037 .02717 211.9 .078789 310 . . 0050 .02721 212.0 .059074

320 . .0036 .02792 217.3 .083466 320 . . 0048 .02706 217.4 .062590

* Two Phase Boundary

19
Table 5 • Transport Properties of Oxygen* Isobars* SI Units.

,5 ^ P a Isobar .6 MPa Isobar

Temp, 0 pn s i t v Thermal Viscosity Thermal Temp . Density Thermal Viscosity T herma 1 C orwj , micro- Dlffusivlty C on d . micro- Dlffusivlty

K q / c m * * 3 W /t . K Q / C m , s cm **? /s X g / cm** 3 W/m.K g/cip.s c m**2 /

56.616 1 .3065 .20368 6 R 67 .8 .000937 * 56.628 1 . 3066 •20370 6870.9 .000937

5

A , 1 .

966 . 2007 ? 6698 .

.000928 56 . 1.2997 .20078 6702.3 . 000928

50 . 1 .2908 . 19717 6681.7 . 000917 58 . 1 .2909 .19722 6685.5 .000917

fcC . 1 .2820 .19377 6266.6 .000907 60 . 1 . 2 821 .1 9382 6270.1 .000907

62 . 1.2732 .19050 6 0

r 5 .6 .

00 P 97 62 . 1.2733 .19055 6058.9 . 000898

66 . 1 .2663 . 1«735 7050.7 .000089 66 . 1 . 2666 . 1 8740 3856.0 .000889

6 b . 1.2556 .18629 3 6 5 3 . P . 000880 66 . 1.2555 .18435 3656.9 .000881

bp . 1.2666 . 1813 ? 3665 .5 . 00087 ? 68 . 1 . 2665 .18137 3668.5 .000873

70 . 1 . 2376 . 17 P 60 3206.3 .000866 70 . 1 . 2375 .17846 3289.1 . 000865

7 ?. 1 .2283 . 17656 3116.3 .000857 72 . 1.2286 .17559 3119.0 .000057

7 A . 1.2191 . 1727 ? 2955.6 . O 00 P 6 ty 76 . 1.2193 .17277 2958.2 . 000869

76 . 1 .2099 . 16993 2003.9 .000061 76 . 1. 2100 .16999 2806.6 .000861

78 . 1. 2006 .16716 2660.9 .000833 78 . 1 . 2007 .16722 2663.3 .000833

8 C • 1.1912 .16661 2526.6 .000825 80 . 1 .1916 .16448 2528.7 .000825

82 . 1.1817 .16167 2 3 Q 9 ..000016 02 . 1.1819 .16174 2602.0 .000816

8 *». 1.1721 . 1 5896 2280.6 .000807 86 . 1 . 1723 . 1 5901 2282 .. 000806

86 . 1.1625 .15621 2168.6 • 00 C 79 P 86 . 1.1627 .15620 2170.7 .000799

PP . 1.1527 .15360 2063.2 .000799 80 . 1 .1529 .15355 2065.2 .000790

90. 1 . 16?9 . 1 5073 1 966.0 .000780 90 . 1 . 1631 .15081 1966.0 . 000780

92 . 1.1329 .16798 1870 .6 .000770 92 . 1. 1331 .14806 1872.5 .000770

04 , 1.1727 . 1652 ? 1702.5 .000769 96 . 1 . 123 C .14530 1706.6 . 000760

96 . 1.1125 .16266 1699.6 .000768 96 . 1.1127 .14252 1701.2 .000769

90 . 1 . 1020 .13966 1620.9 .000737 90 . 1 . 1023 .13973 1622.7 . 000737

100 . o o f- ' . 136 P 3 1566.7 .000725 100 . 1 . 0917 .13692 1568.6 . 000726

102 . 1.0807 .13399 1676.4 .000713 102 . 1.0810 .13408 1678.1 .000713

106 . 1 .0697 .13112 1609.7 . 000699 106 . 1 . 0700 .13122 1611.5 . 000700

106 . 1 .0585 .12023 1366.6 .000686 106 . 1. 0588 .12834 1360.1 .000687

10 P . 1.0670 .12531 1206.1 .000672 100 . 1. 0676 .12542 1207.8 .000672 108.806 1 .0623 .12613 1 ? 62 .6 .000666 110 . 1.0356 .12247 1230.6 . 000657 108.806 .0197 .01035 82.9 . 006695 * 111.657 1 . 0269 .12030 1190.2 . 000666

11 C . .0196 .01066 83.8 .006066 * 111.657 .0235 .01071 85.3 .003972

112 . .0190 .01065 85 .3 .005153 112 . . 0233 .01076 85.7 .006060

116 . .0185 .01086 86.8 .006663 116 . . 0227 .01094 87.2 . 006290

116 . .0181 .01 106 88.3 .005735 116 . . 022 ? .01113 80.7 . 006562

11 ft . .0177 . 0112 ? 89 .

.006029 118 . . 0216 .01132 90.2 . 006795

120 . .0173 .01162 91.3 .006325 120 . . 0212 .01151 91.7 . 005069

122 . .0170 .01161 92 .7 .006625 122 . . 0207 .01170 93.1 .005306

126 . .01 66 . 011 P 0 96 ,? .006926 126 . . 0203 . 01 ie 9 96.6 . 005566

1 ’ 6 . .0163 .01200 95 .7 .007231 126 . .0199 .01208 96.1 . 005826

120 . . 0160 .01219 57.2 .007539 128 . . 0195 .01227 97.5 . C 06086

130 . .0157 .01230 98.7 .007869 130 . . 0191 .01246 99.0 .006350

13 2 . .0156 .01257 100.1 .008162 132 . . 0187 .01266 100.5 .006617

136 . .0152 .01277 101.6 .008678 136 . . 0186 .01285 101.9 . 006886

136 . .0169 .01296 103.0 .008798 136 . .0181 .01304 103.6 . 007157 np. .0166 .Cl 315 106.5 .009120 138 . .0178 .01323 106.8 . 007630

1 6 C . .0166 .01336 105.9 .009666 160 . . 0175 .01342 106.3 .007706

162 . . 0162 .01353 107.6 .009775 162 . .0172 .01361 107.7 .007985

16 ^, .0160 .01373 108.0 .010107 166 . .0169 .01380 109.1 .008266

166 . .0137 .01392 110.3 .010666 166 . . 0166 .01399 110.6 .008551

168 . .0135 .01611 111.7 .010786 160 . .0166 .01419 112.0 . 000838

150 . .0133 .01630 113.1 .011128 150 . . 0161 .01438 113.6 .009130

152 . .0131 .01650 116.5 .011678 152 . . 0159 .01457 116.8 .009626

156 . .0129 .01670 116.0 .011835 156 . .0156 .01478 116.2 .009727

156 . . 0128 .01687 117.6 .012176 156 . . 0156 .01495 117.7 .010015

158 . .0126 .01506 IIP .8 .012516 158 . .0152 .01512 119.1 .010299

160 . .0176 .01522 120.2 .012861 160 . . 0150 .01529 120.5 .010589

165 . .0120 .01565 123.7 .013763 165 . . 0165 .01572 123.9 .011330

170 . .0116 .01609 127.1 .016669 170 . . 0160 .01615 127.6 .012091

175 . .0113 .01653 130.5 .015575 175 . . 0136 .01659 130.8 .012868

180 . .0109 .01696 133.9 .016521 180 . .0132 .01702 136.2 .013662

185 . .0106 .01739 137.3 .017686 185 . .0128 .01745 137.5 .016671

1 9 C , .0103 . 01

P 2 160.6 .018669 190 . . 0126 .01788 160.8 .015295

195 . .0100 .01826 163.9 .019671 195 . .0121 .01830 166.1 .016135

200 . . 0098 .01 866 167.2 .020690 200 . . 0118 .01872 167.6 .016989

210 . .0093 .01969 153.6 .022586 210 . .0112 .01954 153.8 .018762

220 . .0088 .02031 159.9 .026769 220 . . 0106 .02036 160.1 .020556

230 . .0086 .02111 166.1 .026986 230 . .0102 .02116 166.3 .022626

260 . .0081 .02191 172.2 02928 e 260 . . 0097 .02196 172.6 .026351

250 . • 007 R .02269 178.2 .031660 250 . . 0093 .02274 178.6 .026335

260 . .0076 .02367 186.1 .036099 260 . . 0089 .02352 186.2 .028373

270 . .0072 .02626 189.9 .036603 270 . . 0086 .02429 190.0 .030666

280 . .0069 .02500 195.6 .039171 280 . .0083 .02505 195.7 .032612

290 . .0067 .02576 201 .2 .061801 2 90 . . 0080 .02581 201.3 .036810

300 . .0066 .02651 206.7 .066691 300 . . 0077 .02656 206.8 .037057

310 . .0062 .02726 212.1 .067263 310 . .0075 .02731 212.2 .039355

320 . .0060 .02801 217.5 .050062 320 . . 0072 .02806 217.6 .061710

* Two Phase Boundary
Table 5 . Transport Properties of Oxygen* Isobars* SI Units

.7 MPa Isobar .8 MPa Isobar

Tew d • Oen s i t y Thermal Viscosity Thermal Temp. Density Thermal Viscosity Therma

1

C on d • micro- D 1 f f us I v 1 ty C ond • ulcro- D I f f us I v 1 ty

K g / cn'**3 W/m.K g / c m . s cm**2/s K g / cm** 3 W/m.K g /cm.

s

cm**2 /

s

* 5<* . 439 1.3066 .20373 4874 .0 .000937 * 54 .4 5 1 1.306? .20375 4877.1 .000938

56. 1 .2998 .200«2 4706.4 .000928 56. 1 . 2999 .20087 4710.5 .000928

58. 1.2911 .19726 4489.4 .000917 58. 1.2912 .19731 4493.3 . 000917

60. 1.2823 . 1 93 86 4?73.

7

.000907 60. 1 . 282<t .19391 4277.4 .000907

62. 1 .2734 .19060 4062 .3 .000898 62. 1.2736 .19065 4065.6 . 000898

64. 1 .2646 .18745 3857.3 .000889 64 . 1.2647 .18750 3860.6 . 000889

66. 1.2557 .18440 3660.0 .000881 66. 1 . 2588 .18445 3663.2 .000881

6 P • 1.2467 .18142 - 3471 .4 .000873 68. 1.2468 .18147 3474.4 .000873

70 . 1 .2377 .17851 3291 .9 .000865 70. 1.2378 .17856 3294.8 . 000865

72. 1.2286 .17565 3121.7 .000857 72. 1.2287 .17571 3124.4 .000857

74. 1 .2194 .17283 2960.8 .000849 74. 1.2196 .17289 2 96 3 .

4

.000850

76. 1.2102 .17005 280P .9 .000841 76. 1.2104 .17011 2811.4 .000842

78. 1 .2009 .16728 2665.7 .000833 78. 1.2011 .16735 2668.1 .000834

80. 1.1915 .16454 2531.0 .000825 80. 1.1917 .16460 2533.3 .000826

82. 1.1821 .16181 2404 .2 .000817 82 . 1 .1823 .16187 2406.4 .000817

84. 1 .1725 . 1 5908 2284.9 .000808 84. 1.1727 .15915 2287.1 .000809

86. 1 .1629 . 15635 2172.8 .000799 86. 1.1631 .15642 2174.9 .000800

RP. 1.1531 .1536? 2067 .2 .000790 88. 1. 1534 .15369 2069.3 .000791

90. 1.1433 .15089 1967. Q .000780 90. 1.1435 .15096 1969.9 . 000781

92. 1.1333 .14814 1874 .4 .000771 92. 1.1335 .14822 1876.3 . 000771

94. 1.1232 .14538 1786.2 .000760 94. 1.1235 .14546 1788.1 .000761

9* . 1 .1130 .14261 1703 .1 .000749 96 . 1.1132 .14269 1704.9 .000750

98. 1.1026 .13982 1624.5 .000738 98 . 1.1028 .13990 1626.3 . 000739

IOC. 1 .OQ?0 .13701 1550.2 .000726 100. 1.0923 .13710 1552.0 .000727

102. 1.0813 .13418 1479.9 .000714 102 . 1.0816 .13427 1481.6 .000715

104. 1 .0703 .13132 1413.2 .000701 104. 1.0706 .13142 1414.9 .000702

106. 1.0591 .12844 1349.8 .000687 106. 1.0595 .12854 1351.6 .000688

1CP. 1 .0477 .12552 1289 .6 .000673 108. 1. 04 81 .12563 1291.3 .000674

110. 1 .0360 .12258 1232.1 .000658 110. 1 . 0364 .12269 1233.8 . 000659

112. 1 .0240 .11960 1177.2 .000643 112. 1. 0244 .11972 1178.9 . 000644

* 113. PCI 1.012Q . 11688 1129.8 .000628 114. 1.0121 .11670 1126.4 .000627

* 113. P01 .0272 .01103 87.5 .003436 * 115.914 1.0000 .11378 1078.1 . 000611

114. .0271 .01105 87.7 .003458 * 115.914 .0310 .01134 89.6 . 003022

116. .0264 .01123 89.1 .00368? 116 . . 0309 .01134 89.6 .003031 UP. .02*° .01142 90.6 .003907 118. . 0301 .01153 91.1 . 003234

120. .026? .01161 92.1 .004132 120. . 0293 .01171 92.5 . 003438

122. .0246 .01179 93.6 .004358 122. . 0286 .01189 94.0 .003642

124. .0241 .011 9P 95.0 .004*86 124. .0280 .01208 95.4 .003847

126. .023 5 .01217 96.5 .004814 126. . 0273 .01227 96.9 . 004053

128. . 0231 .01236 97.9 .00504* 128. . 0268 .01245 90.3 . 004260

130. .0226 .01255 99.4 .005276 130. .0262 .01264 99.8 .004467

132. .02?? .01274 100.8 .005510 132 . . 0257 .01283 101.2 .004676

134. .0217 .01293 102.3 .005745 134. . 0252 .01302 102.7 . 004886

136. .0213 .01312 103 .7 .005982 136. . 0247 .01320 104.1 . 005098

1 3 P . .0210 .01331 105.2 .006220 138. .0242 .01339 105.5 . 005311

140. .0206 .01350 106.6 .006461 140 . . 0238 .01358 107.0 .005525

142. . 0202 .01369 108.0 .006704 142 . . 0234 .01377 108.4 . 005741

144. .0199 .013 8P 109.5 .006949 144. . 0230 .01396 109.8 .005959

14*. .0196 .01407 UO.Q .007197 146. . 0226 .01415 111.2 . 006180

148. .0193 .01426 112.3 .007447 148. . 0222 .01434 112.7 . 006402

150. .0190 .01446 113.7 .007701 150. . 0219 .01454 114.1 .006628

152. .0187 .0146* 115.1 . 00795P 152 . . 0215 .01473 115.5 . 006856

154. .01 R4 .01485 116.5 .008221 154. . 0212 .01494 116.9 . 007090

156. .01*1 .01503 117.9 .009469 156. . 0209 .01511 118.3 .007309

158. .0179 .01519 119.3 .008715 158. .0205 .01527 119.7 .007526

160. .0176 .01536 120.7 ,0089*5 160 . . 0202 .01543 12 1.0 .007747

165. . 0170 .01579 124.2 .009606 165. . 0195 .01585 124.5 .008312

1 7 C . .0164 .01622 127.6 .010263 170. .0189 .01628 127.9 .008891

1 7 5 . .0159 .01665 131.0 .0 10934 175 . . 0183 .01671 131.3 .009483

180. .0154 .01708 134.4 .011619 180. . 0177 .01714 134.7 . 010087

185. .0150 .01751 137.7 .012317 185. .0172 .01757 138.0 .010701

1 9 C • .0145 .01793 141.1 .013028 190. .0167 .01799 141.3 .011327

195. .0141 .01836 144 .3 .013752 195 . .0162 .01841 144.6 .011964

200. . 0138 .01 877 147.6 .014488 200. .0158 .01883 147.8 .01261

2

210. .0131 . 0 1 9 6 C 154.0 .01 5998 210. .0150 .01965 154.2 .013939

220. .0124 . 02 04 1 160.3 .017558 220. . 0142 .02047 160.5 .015310

230. .0119 .02122 166.5 .019167 230. . 0136 .02127 166.7 .016724

240. .0114 .02201 172.5 .020825 240. .0130 .02206 172.7 .018180

250. .0109 .02279 178.5 .022531 250. . 0125 .02284 178.7 . 019678

260. .0104 .02357 184.4 .024284 260. .0120 .02362 184.5 . 021216

270. .0100 .02434 190.2 .026083 270. .0115 .02438 190.3 . 022795

280. .0097 .02510 195.8 .027927 280. .0111 .02515 196.0 .024413

2 90. .0093 .02536 201 .4 .029815 2 90 . . 0107 .02590 201.6 .026070

300. . 0090 .02661 20 6.9 .031746 300. . 0103 .02665 207.1 .027763

310. .0087 .02735 7 1 2 .

4

.033731 310. .0100 .02740 212.5 . 029495

320. . 0084 . 0 2 p 1

0

217 .7 .035744 320 . . 0097 ,0?815 217.8 .031269

* Two Phase Roundly
Table 5. Transport Properties of Oxygen* Isobars* SI Units 9 MPa Isobar 1,0 MPa Isobar Temo, Oen s 1 t y Ther ma

V 1 sco s 1 1

y

Thermal Temp • Density Th e r m a 1 Viscosity Therma

C ond • micro- Oi ffuslvlty C ond * micro- D 1 f fus 1 v 1 ty

K g / c m* * 3 U/m.K g/ cm.s cm+*2/s K g / cm**

W/m.K g /cm,cm**2 /

5*.461.3068 .20377 4880.2 .000938 * 54.474 1.3068 .203 80 4883.4 .000938

56. 1.3001 .20091 4714.6 .000928 56. 1 . 3002 .20096 4718.8 . 000928

50. 1.2913 .19736 4497.2 .000917 58. 1.2914 .19740 4501.0 . 000918

6 C . 1.2825 .19396 4281.0 .000907 60. 1.2826 .19401 4284.7 .000908

62. 1.2737 .19070 4069,2 .000898 62. 1.2738 .19075 4072.7 . 000898

64. 1.2648 .18755 3863.0 . 000890 64 . 1.2650 .18760 3867.1 . 000390

66. 1 .2 559 .18450 3666.3 .000881 66. 1.2561 .18455 3669.4 .000882

68. 1.2470 .18153 3477 ,4 .000873 60. 1.2471 .18158 3480.3 .000874

70. 1.2379 . 17862 3297.6 .000866 70. 1.2381 .17867 3300.4 . 000866

72. 1.2289 .17576 3127.1 .000858 72 . 1. 2290 .17582 3129.8 . C 00658

74. 1.2197 .17295 2966.0 .000850 74. 1 . 21 99 .17301 2 96 8.5 . 000850

76. 1.2105 .17017 2813.8 .000842 76. 1.2107 .17023 2816.3 .000842

78. 1.2012 .16741 2670.5 .000834 78 . 1.2014 .16747 2672.9 . 000634

80. 1.1919 . 16467 2535.6 .000826 80. 1 .1921 .16473 2537.9 .000826

82. 1.1824 .16194 2408.6 .000818 82 . 1 .1826 .16200 2410.8 . 000918

84. 1.1729 .15921 2289.2 .000809 84 . 1 . 1731 .1 5928 2291.4 . 000909

86. 1.1633 .15649 2176.9 .000800 86. 1 . 1635 .15656 2179.0 .000801

ee . 1.1536 .15377 2071.3 .000791 88. 1. 1538 .15364 2073.3 .000791

90. 1.1437 .15103 1971.9 .000781 90. 1 . 1440 .15111 1973.8 . 000782

92. 1.1338 .14829 1878.2 .000772 92. 1 .1340 .14837 1880.2 . 000772

94. 1.1237 .14554 1790.0 .000761 94 . 1 .1239 .14562 1791.9 .000762

96. 1.1135 .14277 1706.7 .000750 96 . 1.1137 .14286 170 8.6 . 000751

98. 1.1031 .13999 1628.1 .000739 98. 1 . 1034 .14008 1629.9 . 000740

100. 1 .0926 .13719 1553.8 .000727 100. 1.0929 .13728 1555.6 . 00072 P

102. 1.0819 .13436 1483 .4 .000715 102. 1 .0822 .13446 1485.2 .000716

104. 1.0709 .13151 1416.7 .000702 104. 1.0713 .13161 1418.4 . 000703

106. 1.0598 .12064 1 353 .3 .000689 106. 1.0601 .12874 1355.0 . 000690

108. 1 .0484 .12574 1293.0 .000675 100. i .04 ee .12584 1294.7 . 000676

110. 1 .0368 .12280 1235.6 .000660 110. 1 .0372 .12291 1237.3 . 000661

112. 1.0248 .11983 1180.7 .000645 112. 1.0253 .11995 1102.4 .000645

114. 1.0126 . 11682 1128.1 .000628 114. 1.0130 .11694 1129.9 .000629

116. .9999 .11377 1077 .7 .000611 116. 1.0004 .11390 1079.5 .000612

117 ,

4 3 .9879 .11092 1033.0 .000594 118. . 9873 .11081 1031.0 . 000594 117.843 .034 7 .01163 91 .5 .002690 * 119.623 . 9764 .10826 992.9 .000579

118. .0347 .01164 91.6 .002705 * 119.623 . 03 85 .01190 93.3 . 002419

120. .0337 .01182 93.0 .002 893 120. . 0383 .01194 93.6 .002452

122. .0329 .01200 94 .5 .003081 122. . 0373 .01211 95.0 . 002627

124. .0320 .01210 95.9 .003269 124. .0363 .01229 96.4 . 002802

126. .0313 .01237 97 .3 .003457 126. . 0354 .01247 97.8 . 002976

128. . 0306 .01255 98.8 .003646 128 . . 0345 .01265 99.2 . 003151

130. .0299 .01273 100.2 • 003 83 ^

1 30. 0338 .01283 IOC .

.003326

132. .0293 .01292 101.7 .004025 132. . 0330 .01302 102.1 . 003501

134. .0287 .01311 103.1 .004216 134. . 0323 .01320 103.5 . 003677

136. .0281 .01329 104.5 .004408 136. . 0316 .01338 104.9 . 003 8 5 4 138. .0276 .01348 105.9 .004601 138. .0310 .01357 106.3 . 004031

140. .0271 .01367 107.4 .004795 140. . 0304 .01376 107.8 . 004209

142. . 0266 .01385 108.8 .004991 14? . . 0290 .01394 109.2 .004389

144 . .0261 .01404 110.2 .005108 144. .0293 .01413 110.6 .004570

146. .0256 .01423 111 .6 .005387 146 . . 0288 .01432 11?.

. 004752

148. .0252 .01443 113.0 .005588 148. . 0283 .01451 113.4 . 004936

150. .0248 .01462 114.4 .00579? 150. . 0270 .01471 114.8 .005122

152. .0244 .01402 115.8 .005999 152 . . 0273 .01491 116.2 .005311

154. .0240 .01502 117.2 .006210 154. . 0269 .01511 117.5 . 005505

156. .0236 .01519 118.6 .006407 156. . 0265 .01527 110.9 . 005684

158. .023 3 .01534 120.0 .006601 158. .0261 .01543 120.3 . 005860

1 6 C . .0229 .01551 121 .4 • 0 06 79 8 160 . . 02 57 .01559 121 .

. 006039

165. . 0221 .01593 124.8 .007305 165. . 0247 .01600 125.1 . 006498

170. .0214 .01635 128.2 .007824 170. . 0239 .01642 128.5 .006969

175. .0207 .01678 131.6 .008354 175 . . 0231 .01604 131.9 .007450

180. .0200 .01721 134.9 . 008894 180. . 0223 .01727 135.2 . 007940

185. .0194 .01763 138.2 .009444 185 . .0217 .01769 136.5 . 008438

190. .0188 .01805 141.5 .010004 190. . 0210 .01011 141.8 . 000945

195. .0103 .01847 144 .8 .010573 196. . 0204 .01853 145.0 . 009460

200. .0178 .01899 148 .0 .011152 200 . . 0198 .01894 148.3 . 009984

210. .0169 .0197] 154.4 . 0 1 ? 3 3 8 210. .01 88 .01976 154.6 .011057

220. .0161 .02052 160.7 .013562 2 20 . . 0179 .02057 160.9 .012163

230. .0153 .02132 166.8 .014824 230. . 0171 .02137 167.0 .013303

240. .0146 .0221 1 172.9 .016123 240. . 0163 .02216 173.1 .014477

250. .0140 .02209 178.8 .017458 250 . . 0156 .02294 179.0 .015683

260. .0135 .02367 184.7 .018830 260. . 0150 .02372 184.9 .016922

27 C . .0129 . 02 4 4 3 190.5 .020238 270. .0144 .02440 190.6 .018192

2 8 C . .0125 .02519 196.1 .021600 280. .0139 .02524 196.3 .019493

290. .0120 .02595 201 .7 .023156 2 90 . . 0134 .02600 201.8 .020825

300. .0116 .02670 207.2 .024665 300 . . 0129 .02675 207.3 .022166

310. .0112 .02745 212 .6 .026207 310. .0125 .02749 212.7 .023576

320. .0109 .02020 217.9 .027788 320. .0121 .02024 218.1 .025003

* Two Phase Poundary

22
Table 5,i Transport Properties of Oxygen. Isobar s, SI Units.

1.5 MPa Isobar 2.0 MPa Isobar

Temp • Density Therma

1

V 1 scos i ty Therma

1

Temp . De ns 1 ty Thermal1 Viscosity Therma

1

C ond

.

micro- Diffusivity Cond. m 1 cro- Diffusivity

K g/cm**3 W/m.K g/cm.s •cm**2/s K g/ cm**3 W/m.K g /cm. s cm*»2/s

* 54. 531 1.3072 .20392 4898.9 .000938 54.5 89 1.3075 .20404 4914.3 .000939

56 . 1.3008 .20119 4739.4 .000929 56 . 1.3013 .20142 4760.1 .000930

58 . 1.2920 .19764 4520.5 .000919 58 . 1.2926 .19787 4539.9 .000920

6 C • 1.2832 .19425 4303.0 .000909 60 . 1.2839 .19449 4321.3 .000910

62 , 1.2744 .19099 4090 .0 .000900 62 . 1.2751 .19124 4107.4 .000901

64 . 1.2656 .18785 3883.6 .000891 64 . 1.2663 .18810 3900.0 .000892

66 . 1 .2567 .18481 3685.0 .000883 66 . 1.2574 .18506 3700.6 .000884

68 . 1.2478 .18184 3495.2 .000875 68 . 1.2485 .18211 3510.0 .000876

70 . 1.2388 .17894 3314.6 .000867 70 . 1.2395 .17922 3328.8 .000869

72 . 1.2298 .17610 3143.4 .000859 72 . 1.2305 .17638 3156.9 .000861

74 . 1.2207 .17329 2981.5 .000852 74 . 1.2215 .17358 2994.5 .000853

76 . 1 .2115 .17052 2828.8 .000844 76 . 1. 2123 .17082 2841.2 .000846

78 . 1.2023 .16778 2684.8 .000836 78 . 1.2031 .16806 2696.8 .000838

80 . 1.1929 .16505 2549.4 .000828 80 . 1.1938 .16536 2560.9 .000830

82 . 1.1836 .16233 2421.9 .000820 82 . 1.1845 .16266 2433.0 .000822

84 . 1.1741 .15962 2302.1 .000811 84 . 1.1750 .15996 2312.8 .000813

86 . 1.1645 .15691 2189.4 .000803 86 . 1.1655 .15726 2199.8 .000805

88 . 1.1548 .1 5420 2083.4 .000794 88 . 1.1559 .15456 2093.5 .000796

90 . 1.1450 .15148 1983.7 .000784 90 . 1.1461 .15185 1993.5 .000786

92 . 1.1352 .14876 1889.7 .000774 92 . 1.1363 .14914 1899.3 .000777

94 . 1.1251 .14602 1801.2 .000764 94 . 1.1263 .14642 1810.5 .000767

96 . 1.1150 .14327 1717.7 .000754 96 . 1.1163 .14368 1726.9 .000756

98 . 1.1047 .14051 1638.9 .000743 98 . 1.1060 .14093 1647.9 . 000746

100 . 1 .0943 .13772 1564 .4 .000731 100 . 1.0956 .13816 1573.2 .000734

102 . 1.0836 .13492 1493.9 .000719 102 . 1.0851 .13538 1502.6 .000722

104 . 1.0728 .13209 1427.1 .000707 104 . 1.0744 .13257 1435.7 .000710

106 . 1.0618 .12924 1363 .6 .000693 106 . 1 . 0634 .12974 1372.2 .000697

108 . 1.0506 .12636 1303.3 .000680 108 . 1. 0523 .12688 1311.8 .000684

110 . 1 .0390 .12346 1245.8 .000665 110 . 1.0409 .12400 1254.3 .000670

112 . 1.0273 . 12052 1191 .0 .000650 112 . 1.0292 .12108 1199.4 .000655

114 . 1.0152 .11754 1138.5 .000634 114 . 1.0173 .11814 1147.0 .000639

116 . 1.0027 .11453 1088.2 .000618 116 . 1.0050 .11515 1096.8 .000623

118 . .9898 .11148 1039.8 .000600 lie . .9923 .11213 1048.5 . 000606

120 . .9765 .10837 993 .2 .000582 120 . . 9792 .10907 1002.1 .000588

122 . .9627 .10521 94 8.1 .000562 122 . . 9656 .10595 957.2 .000569

124 . . 9483 .10200 904.4 .000541 124 . . 9515 .10278 913.7 .000549

126 . .9331 .09870 861.7 .000519 126 . .9367 .09955 871.4 .000528

* 126.985 .9254 .09705 841.1 .000508 128 . .9211 .09624 830.

1

.000505

* 126.985 .0582 .01321 101 .5 .001555 130 . .9047 .09284 789.4 .000481

128 . .0572 .01329 102.1 .001626 132 . . 8871 .08935 749.2 . 000454

130 . .0555 .01344 103.4 .001763 132.746 . 8802 .08802 734.3 .000444

132 . .0539 .01360 104.7 .001898 * 132.746 .0793 .01453 109.0 .001085

134 . .0524 .01377 106.1 .002033 134 . .0773 .01460 109.7 .001162

136 . .0510 .01393 107.4 .002167 136 . . 0746 .01472 110.8 .001282

138 . .0498 .01411 108.7 .002300 138 . .0722 .01486 112.0 .001399

140 . .0486 .01428 110.1 .002433 140 . . 0700 .01500 113.2 .001514

142 . .0475 .01446 111 .4 .002566 142 . .0680 .01516 114.4 . 001628

144 . .0465 .01464 112.8 .002699 144 . .0662 .01532 115.6 .001742

146 . .0455 .01482 114.1 .002833 146 . . 0645 .01549 116.8 .001855

148 . .0446 .01501 115.5 .002968 148 . . 0629 .01567 118.1 . 001968

150 . .0437 .01521 116.8 .003104 150 . .0615 .01587 119.3 .002082

152 . .0429 .01541 118.1 .003242 152 . . 0601 .01608 120.6 .002198

154 . .0421 .01563 119.5 .003385 154 . .0588 .01631 121.9 .002318

156 . .0413 .01577 120.8 .003510 156 . .0576 .01641 123.2 .002417

158 . .0406 .01589 122 .2 .003631 158 . .0565 .01648 124.4 .002511

160 . .0399 .01603 123.5 .003755 160 . .0554 .01657 125.7 .002607

165 . . 0383 .01640 126.8 .004075 165 . . 0529 .01687 128.9 . 002858

170 . .0369 .01679 130.1 .004402 170 . .0507 .01723 132.1 .003114

175 . .0355 .01720 133.4 .004735 175 . . 0487 .01760 135.3 .003374

180 . .0343 .01761 136.7 .005074 180 . .0469 .01798 138.5 .003638

185 . .0332 .01 802 139.9 .005418 185 . . 04 52 .01837 141.6 .003905

190 . .0321 .01842 143.2 .005766 190 . .0437 .01877 144.8 .004176

195 . .0312 .01883 146.4 .006120 195 . . 0423 .01916 147.9 . 004449

200 . .0303 .01924 149.5 .006479 200 . . 0410 .01956 151.0 .004726

210 . .0286 .02005 155.8 .007213 210 . .0387 .02035 157.2 .005291

220 . .0271 .02085 162.0 .007967 220 . . 0366 .02114 163.2 .005869

230 . .0258 .02164 168.1 .008743 230 . . 0348 .02192 169.2 .006463

240 . .0246 .02242 174.0 .009539 240 . .0331 .02269 175.1 .007071

250 . .0236 .02320 179.9 .010357 250 . . 0316 .02346 180.9 .007694

260 . . 0226 .02397 185.7 .011195 260 . . 0303 .02422 186.7 .008333

270 . .0217 .02473 191.4 .012054 270 . .0291 .02498 192.3 .008986

280 . .0209 .02549 197 .0 .012934 280 . . 02 80 .02573 197.9 .009654

290 . .0201 .02624 202.6 .013832 290 . .0269 .02648 203.4 .010336

300 . .0194 .02698 208 .0 .014750 300 . .0260 .02722 20 8.8 .011033

310 . .0188 .02772 213.4 .015688 310 . .0251 .02796 214.1 .011743

320 . .0181 .02847 218.7 .016649 320 . . 0242 .02870 219.4 .012472

* Two Phase Boundary

23
Table 5. Transport Properties of Oxygen# Isobars* SI Units

2.5 MPa Isobar 3.0 MPa Isobar

Temp, Density Thermal Viscosity Thermal Temp . Dens 1 1 y Ther ma

Viscosity Thermal

C ond

micro- 0 1 f f us 1 v 1 ty Cond. mlcro- D 1 f fusl v 1 1

y

K g / c m**3 W/m.K g / c m . s cm** 2/K g/ cm** 3 W/m.K 9 /cn.s c m**2 /

54.646 1 .3078 .20416 4929.8 .000939 * 54.703 1.3081 . 20428 4945.2 • 00094 0 56. 1 . 3019 .20165 4780.8 .000931 56. 1.3025 .20188 4801.6 .000932

5 B

1.293? .19811 4559.4 .000921 58. 1.2938 .19034 4578.9 .000922

60. 1 . 2945 .1 947? 4339.7 .000911 60 . 1.2851 .19496 4358.1 .000912

62. 1 . 2757 .19148 4124.7 .000902 62. 1. 2763 .19172 4142.1 . 000903

64. 1.2669 .18835 3916.4 .000893 64 . 1.2676 .18860 3932.9 .000895

66. l.?581 .16532 3716.2 .000885 66. 1.2587 .18558 3731.9 . 000887

68 . 1 .2492 .18237 3524.9 .000878 68. 1 . 2499 .18263 3539.8 . 000879

70. 1 . 2403 .17949 3342.9 . 000870 70. 1.2410 .17976 3357.1 . 000871

72. 1.2313 .17666 3170.4 .000862 72. 1 . 2320 .17693 3184.0 .00086*

74 . 1 .2??? .17387 3007.4 .000855 74 . 1.2230 .17415 3020.4 .000856

76. 1 .2131 .17111 2853.6 .000847 76. 1.2139 .17141 2866.0 .0008*9

78. 1.2039 .16839 2708 .7 .000839 78. 1.2048 .16869 2720.7 .0008*1

8 C

1 .1 947 .16568 2572.4 .0008*2 80. 1.1956 .16599 2583.8 . 000833

82. 1.1854 .16298 2444 .

.000824 82. 1 .1863 .16330 2455.2 .000825

84. 1 .1760 .16029 2323.5 .000815 84 . 1.1769 .16062 2334.2 . 000817

86. 1.1665 .15760 2210.2 .000807 86. 1.1675 .15795 2220.5 .000809

88. 1.1569 .15492 2103.5 .000798 88. 1.1579 .15527 2113.6 . 000800

90. 1.1472 .15222 2003.

.000789 90. 1. 1483 .1 5259 2013.0 . 000791

9?. 1.1374 .14952 1908.8 .000779 92. 1.1385 .14990 1918.3 .000782

94 , 1 .1 27* .14681 1819.9 .000769 94 . 1.1287 .14721 1 829.1 .000772

96. 1.1175 .14409 1736.0 .000759 96. 1.1187 .14450 1745.1 .000762

98. 1.1073 .14136 1656.8 .000748 98 . 1. 1086 .14178 1665.7 .000751

ICC. 1 .0970 . 1 3 P 6 0 1582.0 .000737 100. 1 .0984 .13904 1590.8 .0007*0

102 . 1 .0865 .13583 1511.3 .000726 102. 1 . 0880 .13628 1519.9 . 000729

104. 1 . 0759 .13304 1444.2 .000714 104. 1.0774 .1 3351 1452.7 . 000717

106. 1 .0651 . 13023 1380.6 .000701 106. 1.0667 .13072 1389.1 .00070*

10P . 1 .0540 .12739 1320.2 . 000688 108. 1.0557 .12790 132 8.6 .000691

110. 1 .042 7 . 1 2453 1262.7 .0006 7 4 110. 1 . 0445 .12506 1271.0 . 000678

11?. 1.031? .12164 1207.9 .000659 112. 1.0331 .12219 1216.2 . 00066*

114. 1.0194 .11872 1155.5 .000644 114. 1.0214 .11930 1163.8 .0006*9

116. 1 .0072 .11577 1105.3 .000628 116 . 1 . 0094 .11637 1113.7 .000633

118. .9947 .11278 1057.1 .00061? 118. . 9971 .11341 106 5.6 .000617

120. .981 8 .10975 1010.8 .000594 120. . 9843 .11042 1019.4 .000600

12?. .9684 .10667 966.1 .000576 122 . . 9712 .10738 974.9 .000582

124. .9546 .10355 922 .9 .000556 124. . 9576 .10430 931.9 . 000563

1 ? 6 . . Q401 .10036 88C .9 .000536 126. . 9434 .10116 890.2 .0005**

1?P. .9249 .0 071? 839.9 .000514 128. . 9286 .09797 849.5 .000523

130 . , CO 8Q .09380 799.8 .000491 130. .9130 .09472 809.8 .000500

13?. .3919 .09039 760.2 .000466 132. . 8965 .09138 770.8 . 000*77

134. . 8738 .08686 720.9 .000439 134. . 8790 .08797 732.2 .000*51

136. .8540 .08324 681 .5 .000409 136. . 8602 .08445 693.7 . 000*23 137.547 . 8 374 .08033 650.6 .000384 138. . 8396 .08081 654.9 .000393

1 37. 547 .1023 .01603 116.5 .000784 140. . 8168 .07702 615.3 .000359

138. .101 ? .01604 116.7 .000811 * 141 .697 . 7949 .07365 580.2 . 000325

140. .0968 .01609 117.5 .000925 * 141.697 . 1281 .01794 124.6 .000571

14?. .0930 .01618 118.4 .001035 142. .1269 .01792 124.6 . 0005 9 0 14 4, .0897 .01630 119.4 .001142 144 . . 1201 .01786 124.9 . 000705

146. ,086« . 01 643 120 .4 .001247 146. .1146 .01788 125.4 . 00081*

148. .0842 .01659 121.5 .001351 148. . 1099 .01796 126.0 .000918

1 50. .081 8 . 01677 122.6 .001456 150. . 1059 .01810 126.8 .001021

152. .0796 .01699 123.7 .001562 152. . 1023 .01830 127.7 .001125

154. .0776 .01725 1?4.8 .001671 154. . 0992 .01858 128.6 .001231

156. .0757 .01727 126.0 .001756 156. . 0963 .01846 129.6 .001308

158. .0760 .0172* 127.2 .001833 158 . . 0937 .01828 130.6 .001376

160. • 0 7 ? 4 .01727 128.4 .001914 160. .0912 .01819 131.6 . 001**7

165. .0687 .01746 131.4 .002124 165. . 0860 .01820 134.3 .001631

1 7 C • .0655 .01774 134.4 .002338 170. .0815 .01837 137.1 .001819

175. .0627 .01807 137 .4 .002556 175. . 0776 .01862 139.9 .002009

180. . 0602 .01842 140.5 .002776 180. . 0742 .01891 142.8 .002200

135. • 0 5 7 Q .01878 143.5 .002997 185. .0711 .01924 145.7 .002392

1 90 . . 0558 .01915 146 .6 .003221 190. . 0684 .01958 148.6 . 00258*

195. .0539 .01953 149.6 .003447 195. . 0659 .01993 151.6 .002779

2 OC

.0521 .01Q91 152 .6 .003675 200. .0637 .02029 154.5 . 00297*

210. .0*90 .02068 158.7 .004138 210. .0596 .02103 160.3 . 003370

220. .0463 .02144 164 .6 .004611 220 . . 0562 .02177 166.1 .00377*

? 30. 0439 .02221 170.5 .005096 230. . 0532 .02252 171.9 . 00*185

2 40. .0417 .02297 176.3 .005591 240. .0505 .02327 177.6 .00*606

250. .0398 .02373 182 .0 .006098 250 . . 0481 .02402 183.3 .005035

260. . 0331 •02449 187.7 .006617 260. . 0460 .02476 188.8 . 005*73

270. .0365 .02524 193.3 .007146 270. . 0440 .02550 194.4 .005921

280 . .0351 .02598 198.8 .007688 280. . 0423 .02624 199.8 .006377

290. .033 8 .02672 204.2 .008240 290. . 0406 .02697 205.2 . 0068*3

300. . 0325 .02746 209.6 .008803 300. . 0392 .02770 210.5 .007317

310. .0314 .02819 214.9 .009377 310. .0378 .02843 215.7 .007801

320. .0304 .02893 220.1 ,009966 320 . . 0365 .02917 220.9 . 008297

* Two Phase Boundary

24
Table 5. Transport Properties of Oxygen* Isobars* SI Units

3.5 MPa Isobar

Temp

.

Dens i t

y

Thermal VI scos 1 ty Therma

1

C ond • micro- Dlffuslvlty

K g/cm*'*3 W/m.K g/cm.s cm**2 /s

54.760 1.3084 .20440 4960.6 .000941

56. 1.3031 .20211 4822.4 .000933

58. 1 .2944 .19857 4598.5 .000923

60. 1.2857 .19520 4376.5 .000913

62. 1.2769 .19196 4159.5 .000904

64. 1.2682 . 18885 3949.4 .000896

66. 1.2594 .18583 3747.5 .000888

68. 1.2506 .18289 3554 .7 .000880

70. 1.2417 .18002 3371.3 .000873

72. 1.2327 .17721 3197.5 .000865

74. 1.2238 .17444 3033 .3 .000858

76. 1.2147 .17170 2878.4 .000850

78. 1.2056 .16899 2732.6 .000843

80. 1.1964 .16630 2595.3 .000835

82. 1.1872 .16362 2466.3 .000827

84. 1.1778 .16096 2344.9 .000819

86. 1.1684 .15829 2230.9 .000811

88. 1.1589 .15562 2123 .6 .000802

90. 1.1494 .15296 2022.7 .000793

92. 1 .1397 .15028 1927.8 .000784

94. 1.1299 .14760 1838.4 .000774

96. 1.1199 .14490 1754.1 .000764

98. 1.1099 .14219 1674 .6 .000754

100. 1.0997 .13947 1599.5 .000743

102. 1.0894 .13673 1528.5 .000732

104. 1.0789 .13398 1461.2 .000720

106. 1 .0682 .13120 1397.5 .000708

108. 1.0574 .12840 1336.9 .000695

110. 1 .0463 .12558 1279.3 .00068?

112. 1.0350 .12274 1224 .5 .000668

114. 1.0234 .11987 1172.1 .000653

116. 1.0115 .11697 1122 .0 .000638

118. .9994 .11404 1074.0 .000622

120. .9868 .11107 1027.9 .000606

122. .9739 .10807 983.6 .000588

124. .9605 .10503 940.7 .000570

126. .9466 .10194 899.2 .000551

128. .9321 .09880 858.9 .000531

130. .9169 .09561 819.6 .000509

132. .9009 .09234 781.0 .000487

134. .8840 .08901 743.0 .000463

136. .8659 .08559 705.4 .000437

138. .8463 .08208 667.7 .000408

140. .8249 .07845 629.5 .000377

142. .8009 .07468 5 90.1 .000342

144 . .7731 .07075 548.5 .000300 145.365 .7507 .06794 517.5 .000266 145.365 .1579 .02059 133.8 .000409

146. .1540 .02045 133 .4 .000451

148. .1440 .02022 132.9 .000572

150. .1363 .02017 132.8 .000684

I 52. .1301 .02028 133.1 .000793

154. .1248 .02055 133.6 .000903

156. .1203 .02017 134 .2 .000978

158. .1162 .01971 134.9 .001041

160. .1126 .01943 135.6 .001107

165. .1050 .01913 137 .8 .001276

17C. .0988 .01913 140.3 .001447

175. .0936 .01927 142.8 .001618

180. .0391 .01949 145.5 .001788

185. .0851 .01976 148.2 .001959

190. .0816 .02006 150.9 .002130

195. .0785 .02038 153.7 .002302

200. .0756 .02071 156.5 .002475

210. .0706 .02140 162.2 .002823

220. .0663 .02212 167.8 .003177

230. .0626 .02285 173.4 .003537

240. .0594 .02358 179.0 .003903

250. .0565 .02431 184 .6 .004277

260. .0539 .02504 190.1 .004658

270. .0516 .02577 195.5 .005047

280. .0495 .02650 200.9 .005443

290. .0476 .02723 206 .2 .005846

300. .0458 .02795 211 .4 .006257

310. .0442 .02867 216.6 .006675

320. .0427 .02941 221.8 .007105

Two Phase Boundary

4.0 MPa Isobar

Temp • Density Thermal Viscosity Thermal

C ond

.

mlcro- D 1 f fusi v 1 K g/ cm**3 W/m.K g / c m . s cm**2/s

* 54.817 1.3088 .20452 4975.9 • 00094

1

56. 1.3036 .20234 4843.3 • 000934

58. 1.2950 .19880 4618.1 .000923

60. 1.2863 .19544 4395.0 . 000914

62. 1.2776 . 19221 4176.9 .000905

64 . 1.2688 .18910 3 96 5.9 . 000897

66. 1.2601 .18608 3763.2 .000889

68. 1.2512 .18315 3569.5 . 0C0881

70. 1.2424 .1 8029 3385.5 .000874

72. 1.2335 .17749 3211.1 .000867

74 . 1.2245 .17472 3046.3 .000859

76. 1.2155 .17199 2890.9 . 000852

78. 1.2064 .16929 2744.5 .000844

80. 1.1973 .16661 2606.8 . 000837

82. 1 .1881 .16395 2477.3 . 000829

84 . 1.1788 .16129 2355.6 . 000821

86. 1.1694 .15863 2241.2 .000813

88. 1.1600 .15598 2133.6 .000804

90. 1. 1504 .15332 2032.5 . 000795

92. 1.1408 .15066 1937.3 .000786

94 . 1.1310 .14798 1847.6 .000777

96. 1.1212 .14530 1763.1 .000767

98. 1.1112 .14261 1683.4 . 000757

100. 1.1011 .13990 1608.2 .000746

102 . 1.0908 .13718 1 537.0 .000735

104. 1. 0804 .13444 1469.6 . 000723

106. 1.0698 .13168 1405.8 .000711

108. 1. 0590 .12690 1345.2 .000699

110. 1.04 80 .12610 1287.5 . 000686

112 . 1.0368 .12328 1232.7 . 000672

114. 1.0254 .12043 1180.3 .000658

116. 1.0137 .11756 1130.3 .000643

118. 1.0016 .11465 1082.3 . 000628

120. . 9893 .11172 1036.3 .000611

122 . . 9765 .10875 992.

1

.000595

124. . 9633 .10575 949.4 .000577

126. . 9497 .10270 90 8.1 .000558

128. . 9355 .09961 868.1 .000539

130. . 9207 .09647 829.1 .000518

132. . 9051 .09327 791.0 .000497

134. . 8887 .09001 753.5 .000474

136. . 8712 .08668 716.5 . 000449

138. . 8525 .08327 679.7 .000423

140. . 8322 .07978 642.7 .000394

142. . 8099 .07618 605.0 .000362

144. . 7846 .07248 566.0 .000326

146. . 7550 .06866 524.1 . 000283

148. .7174 .06473 476.4 . 000226

* 148.659 . 7018 .06341 458.0 .000202

* 148.659 . 1943 .02467 145.3 .000275

150. .1810 .02398 143.0 .000376

152 . . 1674 .02358 141.4 .000507

154. . 1575 .02364 140.6 .000630

156. . 1496 .02271 140.4 .000712

158. . 1431 .02175 140.5 .000778

160. .1376 .02114 140.8 .000843

165. . 1264 .02035 142.2 .001005

170. .1178 .02009 144.0 .001165

175 . .1108 .02006 146.2 .001323

180. . 1049 .02017 148.5 .001480

185. . 0999 .02036 151.0 .001636

190. . 0954 .02060 153.5 .001791

195. .0915 .02088 156.2 .001946

200. .0880 .02117 158.8 . 002102

210. .0819 .02181 164.2 .002414

220 . .0767 .02249 169.7 .002731

230. . 0723 .02319 175.1 .003051

240. . 0684 .02390 180.6 .003378

250. .0650 .02461 186.0 .003710

260. . 0620 .02533 191.4 . 004048

270. .0593 .02605 196.7 .004392

280. . 0568 .02677 202.0 .004743

290. . 0546 .02749 207.3 . 005099

300. . 0525 .02820 212.5 .005462

310. .0506 .02891 217.6 .005832

320 . . 0488 .02965 222.7 .006211

25
Table 5. Transport Properties of Oxygen* Isobars* SI Units.

4 • 5 HPa Isobar 5.0 MPa Isobar

Temp . Den s 1 t y Thermal

C ond

V 1 scos 1 ty microThermal

D 1 f f us i v 1 ty TemD . Density Ther ma

Cond. ViscositymicroThermal0 1 f fus 1 v 1 ty

K g/cm**3 W/m.K g/cm .s cm + *2 /s K g/ cm**3 W/m.K g/cm.s cm**2/s

* 5^.875 1.3091 .20464 4991 .2 .000942 * 54.932 1 . 3094 .20476 5006.5 .000942

56. 1 . 304? .20257 4864.2 .000935 56. 1 . 3048 .20280 4885.1 . 000936

58. 1 .2956 .19904 4637.7 .000924 58. 1 . 2961 .19927 4657.3 .000925

6 C • 1.2869 .19567 4413.5 .000915 60. 1.2875 .19591 4432.0 . 000916

62. 1 .2782 .19245 4194.4 .000906 62. 1 . 2788 .19269 4211.9 . 000907

64. 1 .2695 .18934 3982.4 .000898 64 . 1.2701 .18959 3998.9 • 0Q0 8 9 9 66. 1.2607 .18634 3778.8 .000890 66. 1.2614 .18659 3794 .

.000891

68. 1.2519 .18341 3584 .4 .000883 68. 1. 2526 .18367 3599.3 .000884

70. 1.2431 .18056 3399.7 .000875 70. 1.2438 .1 8083 3413.9 . 000877

72. 1 .2342 .17776 3224.6 .000868 72. 1.2349 .17803 3238.2 .000869

74. 1.2253 .17501 3059.2 .000861 74 . 1.2260 .17529 3072.2 .000862

76. 1.2163 .17229 2903.3 .000853 76. 1. 2171 .17258 2915.7 .000855

78. 1.2072 .16959 2756.4 . 000846 78. 1.2081 .16989 2768.3 . 000848

8 C

1.1981 .16692 261 8.3 .000838 8 C

1 .1990 .16723 2629.7 . 000840

82. 1.1890 .16426 2488.3 .000831 82. 1.1898 .16458 2499.4 . 000833

84. 1.1797 .16162 2366.3 .000823 84 . 1. 1806 .16194 2376.9 . 000825

86. 1.1704 .15897 2251.5 .000015 86. 1.1713 .15931 2261.8 .000817

88. 1.1610 .15633 2143 .6 .000806 88. 1 . 1620 .15668 2153.6 .000808

90. 1.1515 .15368 2042.2 .000798 90. 1 . 1525 .15404 2051.9 . 000800

92. 1.1419 .15103 1946.7 .000789 92. 1.1430 .15140 1956.1 .000791

94. 1.1322 .14837 1856.8 .000779 94 . 1. 1333 .14875 1866.0 . 000782

96. 1 .1224 .14570 1772.1 .000770 96. 1 .1235 .14610 1781.1 .000772

98. 1.1124 .1430? 1692 .2 .000759 98 . 1.1137 .14343 1701.0 . 000762

ICC. 1.1024 .14033 1616.8 .000749 100. 1 . 1037 .14075 1625.4 .000752

102. 1.0922 .13762 1545.5 .000730 102 . 1 . 0936 .13806 1 554.0 .000741

104. 1.0918 .13489 1478.0 .000727 104 . 1.0833 .13535 1486.4 . 000730

1 06

1 .0713 .13215 1414.1 .000715 106. 1 . 0729 .13262 1422.3 .000718

ice. 1.0606 .12939 1353 .4 .000703 108. 1 . 0622 .12908 1361.6 . 000706 no. 1.0498 .12661 1295.7 .000690 no. 1.0515 .12712 1303.8 . 000694

112. 1.0387 .12381 1240.8 .000676 112 . 1.0405 .12434 1248.9 . 000680

114 . 1.0273 .12099 1188.4 . 00066? 114. 1.0292 .12153 1196.5 . 000667

116. 1 .0157 .11814 1138.4 .000648 116. 1 . 0178 .11871 1146.5 . 000653

118. 1.00*8 .11526 1090.

.000633 113 . 1.0060 .11586 1098.7 . 000638

1 20. .9916 .11236 1044.6 .000617 120. . 9940 .11298 1052.8 . 000622

122. .9791 • 1 C 9 4 2 1000.5 .000600 122. . 9016 .11008 1008.8 . 000606

124. .9661 .10645 958.0 .000583 124. . 9668 .10714 966.4 . 000589

126. .9527 .10345 916 .9 .000565 126. . 9556 .10418 92 5.4 .000572

128. .9388 .10040 877.1 .000546 128. . 9420 .10117 885 .

. 000554

130. .9243 .09731 838.4 .000527 130. . 9270 .09813 847.4 . 000535

132. .9091 . 09417 800 .6 .000506 132. .9130 .09505 010.0 . 000515

134. .893? .C9Q9e 763.6 .000484 134. . 8975 .09191 773.4 .000494

136. .8763 .08773 727 .2 .000461 136 . . 8811 .08873 737.5 . 000471

138. . 8583 .08441 691.1 .000436 138. . 8638 .08550 702.1 . 000448

140. .8390 .08103 655 .1 .000409 140. . 8453 .08221 666.9 .000423

14?. .0180 . 07757 618.8 .000380 142 . . 8254 .07807 631.7 .000396

144. . 7946 • 0740*' 581.7 .000348 144. . 8035 .07549 596.0 . 000367

146. .7681 .07046 54? .9 .000311 146. . 779? .07208 559.4 .000335

148. .7365 .066 87 500.8 .000267 148. .7513 .06871 520.8 . 000298

150. .6952 .06340 451 .6 .000208 150. . 7176 .06551 478.6 . 000254

* 151.646 .6410 .06085 39 5.0 .000126 152. . 6724 .06286 42 8. 1 . 000194 151.646 .2443 .03191 161.9 .000149 154. . 5822 .06213 344.1 .000075

152. ,2350 . 03109 159.4 .000189 154.361 .5151 .07770 293.5 .000017

154. . 2055 .02923 152.7 .000363 * 154.361 . 3666 .08153 210.1 . 000014

156. .1889 .02683 149.9 .000473 156. . 2561 .03528 169.4 .000213

158. .1771 .02484 148.5 .000552 158. . 2256 .03004 161.7 . 000336

160. .1679 .02358 147.8 .000624 160. . 2075 .02732 158.2 .000427

165. .1510 .02195 147.6 .000789 165. .1799 .02411 154.7 . 000603

1 7 C • .1389 .02128 148.6 .000944 170. .1626 .02278 154.2 .000764

175. .1295 .02102 150.1 .001093 175. . 1500 .02218 154.8 . 000909

180. .1219 .02097 152.0 .001240 180. . 1402 .02192 156.1 . 001040

185. .1155 .02106 154.2 .001384 185. . 1321 .02186 157.8 .001104

190. .1100 .02122 156.5 .001527 190. . 1252 .021 92 159.7 . 001318

195. .1051 .02143 1 58.9 .001670 195. .1193 .02206 161.9 . 001450

200. .1008 .02169 161.3 .00181? 200. . 1142 .02225 164.1 . 001582

210. .0935 .02226 166.4 .002097 210. . 1054 .02274 168.8 . 001845

220. .0873 .02289 171 .6 .002385 220 . . 0982 .02331 173.8 .002110

230. . 0821 .02355 176.9 .002675 230 . . 0921 .02394 178.8 . 002376

24 C.0776 .02424 182.2 .002970 2 40. .0869 .02459 104.0 .002645

25C. .0737 .02493 187 .5 .003270 250 . . 0824 .02526 189.1 . 002919

260. .0701 .02563 192.8 .003574 260. . 0784 .02594 194.3 . 00 31 97

2 70. .0670 .02634 198 .0 .003884 270 . . 0748 .02663 199.4 .003479

280. .0641 .02704 203.2 .004 1 90 280. . 0715 .02732 204.5 .003765

290. .0616 .02775 208.4 .004519 290. . 0686 .02802 209.6 . 004056

300. . 0592 .02845 213.5 .004845 300 . . 0659 .02871 214.7 .004352

310. .0570 .02916 218.6 .005177 310. .0635 .02941 219.7 . 004653

320. .0550 .02989 223 .6 .005517 320 . . 0612 .03013 224.6 . 004963

* Two Phase Roundary

26
Table 5. Transport Properties of Oxygen* Isobars* SI Units.

5.5 Isobar 6.0 MPa Isobar

Terr d . Oen s 1 t y Th p r rr a 1 V 1 s c os 1 1 v Thermal Temp. Oen s 1 t y Thermal V 1 sco s 1 ty T hernia 1 C ond . micro- 0 1 f f us 1 vl tv C on d

.

micro- Dlffusivlty

K g/cm**3 W/m.K g / c m . s cm**2/s « g / cm** 3 W /m .K a / cm ,

s

c / s

5 A .

<2 p Q 1.3097 .20488 5021.7 • 00094 3 * 55.066 1.3100 .20500 5037.0 .000963

5 6. 1.3054 .20303 4906.1 .000937 56. 1.3059 .20325 6927.1 . 000938

58. 1 .2967 .19950 4677 .0 .000926 5 9. 1. 2973 .1 9973 6696.7 .000927

6 C . 1.2881 .19614 4450.5 .000917 60. l .? e 87 .19638 6669.

1

.000918

6 2. 1.2794 .19293 6229.6 .000908 62. 1 . 2800 .19317 6266.9 . 000909

66 . 1.2707 .18983 4015.5 .000900 66 . 1.2716 .19008 6032.1 .000901

66. 1.2620 .18684 9810.? .000893 66. 1 . 2627 .18709 3825.9 . 000896

68. 1.2533 .18393 3614.3 .000885 69. 1.2560 .18619 3629.2 . 000886

70. 1.2445 .1810 9" 34?8 .

1

.000878 70. 1.2652 .18136 3662.3 .000879

7?. 1.2357 .17831 3251.7 • OOC 87

1

72. 1 . 2366 .17858 3265.3 .000872

74 . 1.2268 .17557 3085.1 .000864 76 . 1.2275 .17585 3098.1 .000865

76 . 1.2179 .17287 2928.1 .000856 76. 1. 2186 .17315 2960.5 . 000858

78. 1.2089 .17019 2780.2 .000849 78. 1.2097 .17069 2792.1 .000851

ec . 1 .1908 .16754 2441.2 .00084? 80. 1 . 2007 .16786 2652.6 .000863

B 2. 1 .1907 .16490 2510 .4 .000834 92. 1. 1916 .16521 2521.6 . 000836

84. 1.1815 .16227 2387.5 .000827 86 . 1.1826 .16259 2398.2 .000828

86. 1 • 1 7?3 .15965 2272.1 .000819 86. 1.1732 .15998 2282.6 .000821

PP . 1.1629 .15702 2163.4 .000810 88 . 1.1639 .15737 2173.5 .000812

90. 1.1535 .15440 2061.6 .00080? 90. l .1566 .15676 2071.2 . 000806

9?. 1.1440 .15177 1945.5 .000793 92. 1.1651 .15216 1976.9 .000795

94. 1.1346 .14914 1975.7 .000704 96 . 1.1356 .16951 1886.3 .000786

96. 1.1247 .14649 1790.1 .000775 96. 1.1259 .16688 1799.0 .000777

98. 1.1149 .14384 1709 .8 .000765 98 . 1.1161 .16626 1718.5 . 000767

100. 1.1050 .14117 1434.0 .000755 100. 1 . 1063 .16159 1662.6 .000757

10?. 1.0949 .13849 1562 .4 .000744 102 . 1.0963 .13892 1 570.8 .000767

104. 1 . 0847 •1^580 1494.7 .000733 106 . 1.0861 .13625 1503.0 .000736

106. 1 .0744 .13309 1430.5 .00072? 106. 1.0758 .13355 1638.7 .000725

10 P . 1 .063 R .13036 1369.7 .000710 108. 1. 0656 .13086 1377.8 .000713

110. 1.0531 .12762 1311.9 .000697 110. 1.0568 .12812 1319.9 .000701

11?. 1.04?? .12486 1256.9 .000684 112 . 1.0660 .12537 1266.9 .000688

114. 1.0311 .12208 1204.5 .000671 116. 1.0330 .12261 1212.6 .000675

116. 1 .0198 .11927 1154.5 .000657 116. 1.0217 .11983 1162.6 .000661

118. 1.0081 .11645 1106.7 .000643 118 . 1. 0102 .11703 1116.6 .000667

1?0. .9962 .11360 1060.9 .000627 120. . 9985 .11621 1068.9 .000633

12?. . 9 R 4 0 .11072 1016.9 .000612 122. . 9866 .11136 1025.0 .000617

124. .9714 .10782 974.7 .000595 126. . 9760 .10869 982.8 .000601

126. . 9585 .10409 933.9 .000578 126. .9613 .10559 962.2 .000585

128. .9451 .10193 894.5 .000561 128. . 9681 .10266 90 3.0 .000568

130. .931? .09 R 93 856.3 .000542 130. . 9366 .09971 865.0 .000550

132. .9167 .09589 819.2 .000523 132. . 9203 .09672 82 8.1 .000531

134. .9016 .09282 783.0 .000503 136. . 9055 .09370 792.2 .000512

136. .8857 . C 8 9 7 0 747.5 .000482 136. . 8901 .09066 757.2 .000691

138. .8690 .08654 712.6 .000459 138. . 8739 .08755 722.8 .000670

1 4 C • .8512 .08334 678.1 .000436 160. . 8567 .08662 688.9 .000668

14?. . R 322 .08010 643.8 .000411 162 . . 8385 .08127 655.3 .000626

144. .8116 .07683 609.3 .000384 166. .8189 .07810 621.8 .000399

146 . .7890 .07356 574 .3 .000355 166. . 7977 .07693 588.1 .000373

148. .7637 .07034 538.2 .000323 168. .7763 .07186 553.7 .000366

150. .7344 .06731 500.0 .000287 150. . 7681 .06891 518.2 .000316

15?. . 698 7 .0*476 457.7 .000244 152. . 7175 .06662 680.6 .000279

154. .6499 .06354 406.5 .000187 156. .6800 .06696 638.6 .000260

156. .5532 .06103 323.0 .000081 156. .6285 .06221 387.7 .000181

1 5 P . . 3267 .04513 196.7 .000117 158. . 5380 .05811 313.7 .000102

160. .2681 .03421 176.8 .000239 160. . 3930 .05000 228.0 .000107

16*. .2156 .02712 164 .5 .000451 165. . 2625 .03152 179.2 .000312

170. .1898 .02471 161.2 .000613 170. . 2217 .02721 170.3 . 000683

175. .1727 .02359 160.4 .000756 175. . 1979 .02532 167.2 . 000628

IRC . .1599 .02304 160.8 .000891 190. .1813 .02635 166.6 .000760

185. .1497 .02278 161.9 .001021 185. . 1686 .02385 166.6 . 000885

190. .1413 .02271 163.4 .001147 190. . 1583 .02361 167.5 . 001006

195. .1342 .02276 165.2 .00127? 195. . 1697 .02353 168.9 .001126

200. .1280 .02288 167.1 .001395 200. .1626 .02356 170.5 .001261

210. .1177 .02326 171.5 .001641 210. .1303 .02363 176.3 .001671

2?0. .1093 .02377 176 .1 .001886 220. . 1207 .02625 178.6 .001701

230. .1023 .02434 180.9 .002132 230. . 1127 .02677 183.1 .001930

240. • 0 96 4 .02496 185.8 .002381 260. . 1060 .02535 187.8 .002162

250. .0912 .02560 190.8 .002633 250 . .1001 .02596 192.6 .002396

?6 C . .0867 .02626 195.8 .002889 260. .0950 .02660 197.5 .002633

270. .0826 .02693 200.8 .003148 270 . . 0905 .02725 20 2.6 .002873

280. .0790 .02761 205.9 .003411 280. . 0865 .02791 207.3 .003117

290. .0757 .02829 210.9 .003678 290. .0828 .02857 212.2 .003366

300. .0727 .02897 215.8 .003949 300. . 0795 .02926 217.1 .003615

310. .0700 .02966 220.8 .004226 310. .0765 .02992 221.9 .003870

320. .0675 .03038 225 .7 .004510 320 . . 0737 .03063 226.8 .006133

* Two Phase Roundary

27
Table 5. Transport Properties of Oxygen* Isobars* SI Units.

6.5 MPa Isobar 7.0 MPa Isobar

TempHens 1 t y Thermal V 1 s c os 1 1 y Thermal Temp

Density Ther ma 0 Viscosity Therma

Cond. micro- n 1 f f us 1 v 1 ty Cond. m i c ro- Dlffuslvity

K a /cm**3 W/m.K g/cm.s cm*+2/s K g/em»*3 W/m.K g/cm.s cm**2 7s

55.103 1.3104 .20512 5052 .1 .000944 55.159 1.3107 .20525 5067.3 .000944

56. 1.3065 .20348 4948.2 .000939 56. 1.3071 .20371 6969.3 .000939

58. 1.2979 .19096 4716.5 .000928 58. 1.2985 .20019 6736.3 .000929

60. 1.2893 .19661 4487.7 .000919 60. 1.2899 .19686 6506.3 .000920

62. 1.2806 .19341 4264.4 .000910 62. 1.2812 .19366 6282.0 .000911

6* . 1.2720 . 19032 4048.6 .000902 68 . 1.2726 .19057 6065.2 .000904

66. 1 . 2633 .18734 3841.6 .000895 66. 1.2660 .18759 3857.6 .000896

68. 1.2546 . 18445 3644 .1 .000888 68. 1.2553 .18670 3659.1 .000889

70. 1.2459 .10162 3456.5 .000880 70. 1.2666 .18188 3670.7 . 000882

72. 1.2371 .17885 3278.8 .000873 72. 1.2378 .17912 3292.6 .000875

74, 1 .2283 .17613 3111.1 .000866 76 . 1.2290 .17661 3126.0 .000868

76. 1 .2194 .17344 2952.9 .000859 76. 1.2202 .17373 2965.3 .000861

70. 1.2105 .17079 2804.0 .000852 78. 1.2113 .17108 2815.9 .000854

80. 1.2015 .16815 2664.0 .000845 80. 1.2023 .16865 2675.6 .000847

82. 1.1925 .16553 2532.4 .000838 82. 1.1933 .16586 2 56 3.6 .000839

84. 1.1833 .16292 2408.8 .000830 86 . 1.1862 .16326 2619.6 .000832

86. 1 .1 *42 .16031 2292.6 .000822 86. 1.1751 . 16065 2302.9 . 000824

88. 1 .1649 .15771 2183 .4 .000814 88. 1. 1659 .15806 2193.6 .000816

90. 1 .1556 .15511 2080.8 .000806 90. 1.1566 .15566 2090.6 . 000808

92 . 1.1462 .15250 1984 .3 .000798 92 . 1.1672 .15287 1993.6 .000800

94. 1.1367 .14989 1893.4 .000789 96. 1.1378 .1 5027 1902.5 .000791

96. 1 .1771 .14727 1807.9 .000780 96. 1.1282 .16766 1816.7 .000782

90 . 1.1174 .14464 1727.2 .000770 98. 1. 1186 .16506 1735.9 .000773

100. 1.1075 .14200 1651.1 .000760 100. 1.1088 .16262 1659.6 .000763

in?. 1.0976 .13935 1579.2 .000750 102. 1.0989 .13978 1587.5 .000753

104. 1.0075 .13669 1511.2 .000739 106 . 1. 0889 .13713 1519.6 . 000742

106. 1 .0773 .13401 1446.8 .000728 106. 1.0788 .13667 1656.9 .000731

108. 1.0670 .13132 1385.8 .000717 108. 1.0685 .13179 1393.8 .000720

110. 1 .0564 .12861 1327.9 .000705 110. 1.0580 .12910 1335.8 .000708

112. 1.0457 .12589 1272.8 .000692 112. 1.0676 .12639 1280.6 .000696

114. 1.0348 .12314 1220.3 .000679 116. 1.0366 .12367 1228.1 .000683

116. 1 .0237 .12038 1170.3 .000666 116. 1.0256 .12093 1178.1 .000670

118. 1.0173 .11761 1122.5 .000652 118. 1. 0163 .11817 1130.3 .000656

120. 1 .0007 .11481 1076.8 .000638 120. 1.0028 .11560 1086.6 .000642

122. .9088 .11199 1033.0 .000623 122. . 9911 .11260 1060.9 . 000628

124. .9765 .10914 990.9 .000607 126. . 9790 .10979 998.8 .000613

126. .9640 .10628 950 .4 .000591 126. . 9666 .10695 958.6 .000597

128. .9510 .10339 911.3 .000574 128. . 9539 .10610 919.5 .000581

1 3 C

.9376 . 10047 873.5 .000557 130. . 9607 .10122 881.9 .000564

1 32. .9237 .09752 836.9 .000539 132 . .9271 .09831 865.6 .000546

134. .9093 .09455 001.3 .000520 136. . 9130 .09538 810.1 .000528

136. .8943 .09155 766.5 .000501 136. . 8983 .09263 775.7 . 000509

138. . 8785 .08851 732.6 .000480 138. . 8830 .08965 762.1 .000490

140. . 8619 .00546 699.2 .000459 160. . 8669 .08665 709.2 .000470

142. . 8444 .08238 666.3 .000437 162. . 8500 .08366 676.8 .000449

] 44 . .8 257 .07929 633.6 .000414 166. . 8321 .08063 666.7 .000427

146. .8056 .07622 600.9 .000309 166. . 8129 .07766 612.9 . 000404

148. .7838 .07322 567.9 .000363 168. . 7926 .07652 581.1 . 000380

150. .7597 .07039 534 .3 .000336 150. .7700 .07176 568.9 .000355

152. .7376 .06797 499.4 .000307 152 . . 7652 .06932 516.1 .000330

154. .7009 • 06 6 ? 9 462.2 .000277 156. . 7173 .06758 681.9 .000305

156 . .6619 .06357 421.0 .000234 156. . 6867 .06689 665.6 .000270

150. .6095 .05997 372.1 .000178 158 . . 6650 .06153 605.8 . 000228

160. .5297 .05668 309.8 .000126 160 . . 5935 .05809 360.1 . 000183

165. . 323 5 . C 3 8 06 203.8 .000205 165. .6127 .06563 262.8 . 000163

] 7 0

.2601 .03048 182.5 .000374 170. . 3069 .03670 199.5 .000288

175 . .2265 .02743 175.6 .000519 175 . . 2589 .03002 186.1 .000428

1 8 C. 2047 .02591 172.9 .000650 180. . 2303 .02773 180.6 . 000556

185. .1887 .02508 172 .0 .000771 185. . 2103 .02668 178.2 .000675

1 90

.1762 .02462 172.2 .000088 190. . 1951 .02576 177.6 . 000788

195. .1659 .02440 173.0 .001001 195. .1829 .02536 177.5 .000896

200. .1573 .02432 174.2 .001112 200. . 1728 .02515 178.2 . 001002

2 1 C

.1433 • 02 4 4 A 177.4 .001330 210. .1566 .02510 180.7 .001209

2 70

.1323 .02477 181.2 .001545 220. . 1661 .02532 186.1 .001414

230. .1233 .02523 185.5 .001761 230. .1360 .02570 187.9 . 001617

240. .115 7 . 07575 189.9 .001978 260. .1255 .02618 192.1 .001821

250 . .1092 .02633 194 .5 .002197 250 . .1183 .02672 196.5 .002027

2 6 C.1035 .02694 199.2 .002418 260. .1120 .02729 201.1 .002235

270. .0905 . 02787 204 .0 .002642 270 . . 1065 .02789 205.7 . 002445

200. .0940 .02821 208.0 .002869 280 . . 1016 .02851 210.3 .002657

29C . .0900 .02886 713 .6 .003099 290. . 0972 .02915 215.0 .002873

300. . 0863 .02981 218.4 .003332 300. . 0932 .02979 219.7 .003091

310. .0830 .03018 223.2 .003570 310. .0895 .03066 226.6 .003313

320. .0800 .03088 227.9 .003815 320 . . 0862 .03116 229.1 .003542

* Two Phaso Boundary

28
Table 5. Transoort Properties of Oxygen* Isobars* SI Units.

7.5 MPa Isobar 8.0 MPa Isobar

Temp • Density Thermal Viscosity Thermal Temp . Density Th e r m a 1 Viscosity Thermal

C ond . micro- D 1 f f us 1 v 1 ty C on d

.

micro- Dlffusiv Ity

K q/cm**3 W/m.K g / c m . s c m** 2 /

s

K g/ cm** 3 W/m.K g /cm.

s

cm**2/

s

55.216 1.3110 .20537 5082 .6 • D 00945 * 55 .273 1.3113 .20569 5097.6 . 00 094 5 56. 1.3076 .20393 6990.6 .000940 56. 1 . 3082 .20616 5011.6 . 000941

58. 1 .2990 .20062 6756.1 .000930 58. 1 . 2996 .20065 6776.0 .000931

60. 1 .2906 .19708 6526.9 •000931 60. 1.2910 .1 9731 6563.6 . 000^22

62. 1.2819 .19388 6299.5 .00091? 62. 1 . 28 2 5 .19612 6317.1 . 000914

66. 1.2733 .19081 6081 .9 .000905 66 . 1.2739 .19105 6098.5 . 000906

66. 1.2666 .1 8786 3873.1 .000897 66. 1 . 2653 .10809 3808.9 . 000898

68. 1.2560 .18696 3676.0 .000890 6P . 1. 2566 .18521 3589.0 . 000891

70. 1.267? .18 215' 3686.9 .000883 70. 1.2680 .18261 3699.2 .000884

72. 1 .2385 .17939 3306.0 .000876 72. 1 . 2393 .17966 3319.5 .000877

76. 1.2298 .17668 3137.0 .000869 76 . 1 . 2305 .17696 3169.9 . 000871

76. 1.2210 .17601 2977.7 .00086? 76. 1.2217 .17630 2990.1 . 000864

78. 1.2121 .17137 2827.8 .000855 70. 1 .2129 .17167 2 83 9.7 . 000857

80. 1.2032 .16876 2686.9 .000848 00. 1 . 2060 .16906 2698.3 . 000850

82. 1.1962 .16615 2556.6 .000841 02. 1.1950 .16666 2565.6 . 000843

86. 1.1851 . 16356 2630.0 .000834 86 . 1.1860 .16388 2660.6 .000836

86. 1.1760 .16098 2313.1 .000836 86. 1 .1770 .16131 2323.3 .000828

88. 1 .1669 .15860 2203 .3 .000818 80. 1.1678 .15876 2213.2 . 00C320

90. 1.1576 .1558] 2100.0 .000810 90. 1.1586 .15616 2109.6 . 000812

92. 1.1683 .15323 2003 .0 .00080? 92. 1 . 1693 .15359 2012.3 .000804

96. 1.1389 .15066 1911.6 .0 00793 96 . 1.1399 .15101 192 0.7 .000796

96. 1.1296 .16806 1825.6 .000784 96. 1.1305 .16863 1836.6 .000787

98. 1.1198 .16566 1766 .5 . 000775 98. 1 . 1209 .16586 1753.2 . 000778

ICO. 1.1100 .16283 1668.1 .000765 100. 1.1113 .16323 1676.5 .000768

102. 1 .1002 .16020 1595.8 .000755 102. 1.1015 .16062 1606.1 . 000758

106. 1.0903 .13757 1527.6 .000745 106. 1 . 0916 .13800 1535.7 .000748

106. 1.0802 .13692 1663.0 .000734 106. 1.0016 .13537 1671.0 .000737

108. 1.0700 .13226 1601.7 .000723 108. 1.0715 .13272 1609.6 .000726

110. 1.0 59 6 .12958 1363.6 .000712 110. 1 . 0612 .13006 1351.6 . 00071

5

112. 1.0691 .12689 1288.6 .000700 112. 1.0506 .12739 1296.2 .000703

116. 1.0386 .12619 1235.9 .000687 116 . 1. 0601 .12670 1263.6 . 000691

116. 1 .0275 .12167 1185.8 .000674 116. 1.0293 .12200 1193.5 . 000678

118. 1.0163 .11873 1138.1 .000661 118. 1. 0183 .11929 1165.7 . 000665

120. 1.0050 .11598 1092.6 .000647 120. 1 . 0070 .11656 1100.1 .000652

122. .9933 .11321 1068.7 .000633 122 . . 9955 .11381 1056.6 . 000638

126. .9316 .11062 1006.7 . 000618 126. . 9838 .11105 1016.5 . 000623

126. .9692 . 10762 966.6 .000603 126. . 9717 .10827 976.2 . 000608

128. .9566 .10679 927 .6 .000587 128. . 9593 .10567 935.5 . 000593

130. .9637 .10195 890.1 .000570 130. . 9666 .10266 898.2 . 000577

132. .9303 .09908 853 .9 .000553 132. . 9335 .09903 862.1 . 000560

136. .9165 .09619 818.7 .000536 136. . 9199 .09690 827.2 .000543

136. .9022 .09328 786 .6 .000518 136 . . 9059 .09612 793.3 . 000526

138. . 8872 .09036 751.3 .000499 138 . . 8913 .09126 760.

3

. 000508

160. .8716 .08761 718.8 .000480 160. . 8761 .08835 728.1 .000489

162. .8552 .08667 686.9 .000460 162 . . 8603 .08565 696.6 .000470

166. .8380 .08152 655.6 .000439 166. . 8636 .08257 665.7 . 000450

166. .8197 .07860 626.3 .000417 166. . 8260 .07971 635.2 .000430

168. .8002 .07575 593.6 .000395 168. . 8076 .07692 605.0 . 000409

150. .7791 .07305 562 .6 .000373 150. . 7875 .07627 576.9 .000383

152. . 7562 .07063 531.1 .000350 152 . . 7660 .07187 566.8 .000367

156. .7309 .06881 699.0 .000328 156. .7627 .07000 516.3 .000348

156. .7026 .06616 665.8 .000299 156. . 7169 .06738 683.3 .000322

158. . 6693 .06296 630.7 .000264 158. . 6880 .06631 651.2 . 000293

160. .6296 .05979 392 .7 .000228 160. . 6568 .06129 617.5 .000262

165. .6891 .05072 287 .2 .000170 165 . • 5 6 6 6 .05358 32 5.7 .000196

170. .3618 .03963 222.6 .000236 170. .6190 .06628 250.8 .000217

175. .2958 .03311 199.6 .000356 175. . 3367 .03660 215.9 . 000305

1 8 C . .2586 .02986 189.9 .000478 180. . 2890 .03229 200.9 .000416

185. .2335 .02808 185.6 .000593 185. . 2582 .02988 193.6 . 000525

190. . 2151 .02706 183.3 .000702 190. . 2361 .02865 190.0 . 000630

195. .2006 .02662 182.6 .000807 195. . 2192 .02758 188.2 .000731

200. .1888 .02606 182 .7 .000909 2 00. . 2055 .02706 187.5 .000028

210. .1703 .02580 186.3 .001107 210. .1866 .02656 188.2 .001018

220. .1562 .02591 187.1 .001301 220. . 1685 .02653 190.6 . 001203

230. .1669 .02620 190.6 .001494 230. .1559 .02673 193.6 .001387

260. .1355 .02662 196.5 .001687 260. . 1655 .02708 197.0 .001570

250. .1275 .02711 198.6 .001881 250. . 1368 .02753 200.9 .001754

260. .1206 .02766 203.0 .002077 260. .1292 .02803 205.0 .001939

270. .1165 .02823 207.6 .002274 270. . 1226 .02858 209.2 .002126

280. .1092 .02883 211.9 .002475 280. .1168 .02915 213.6 .002316

290. .1066 .02966 216.5 .002677 290. .1116 .02976 218.1 .002507

300. .1000 .03006 221.1 .002882 300. . 1069 .03035 222.6 .002701

310. .0961 .03071 225.7 .003091 310. . 1027 .03098 227.1 . 002898

320. .0925 .03160 230.3 .003307 320. . 0988 .03166 231.6 .003102

* Two Phase Boundary

29
Table 5. Transport Properties of Oxygen* Isobars* SI Units

8*5 MPa Isobar

Temp. Density Thermal V 1 s c os 1 1 y Thermal

C ond

micro- Dl f f us 1 v 1 ty

K g/cm**3 W/m.K g/cm.s cm**2/s

55.330 1.3116 .20561 5112.5 .000946

56 . 1.3087 .20439 5032.9 .000942

58 . 1.3002 .20088 4795.8 .000932

60 . 1.2916 .19754 4 5 6 2 •

.000923

62 . 1.2831 .19436 4334.7 .000915

6 A o 1.2745 .19130 4115.1 .000907

66 . 1.2659 .18834 3904.6 .000899

68 . 1.2573 .18547 3703.9 .000892

70 . 1.2486 .18267 3513.4 .000886

72 . 1 .2400 .17993 3333.1 .000879

74 . 1.2312 .17724 3162.9 .000872

76 . 1.2225 .17458 3002.5 .000865

78 . 1.2137 .17196 2851.6 .000858

80 . 1 . 2048 .16936 2709.7 .000852

82 . 1 .1959 .16677 2576 .4 .000844

84 . 1.1869 .16420 2451,1 .000837

86 . 1.1779 .16164 2333.5 .000830

88 . 1.1688 .15907 2223.0 .000822

90 . 1.1596 .15651 2119.2 .000814

92 . 1.1504 .15395 2021.6 .000806

94 . 1.1410 .15138 1929.7 .000798

96 . 1.1316 .14881 1 843.2 .000789

98 . 1.1221 .14623 1761.8 .000780

100 . 1.1125 .14364 1684.9 .000771

102 . 1.1028 .14104 1612 .4 .000761

104 . 1.0930 .13843 1543.8 .000751

106 . 1 .0830 .13581 1478.9 .000740

108 . 1.0730 .13318 1417.5 .000730

110 . 1 .0628 .13054 1359.2 .000718

112 . 1.0524 .12788 1303.9 .000707

114 . 1.0418 .12521 1251 .3 .000695

116 . 1.0311 .12253 1201.1 .000682

118 . 1.0202 • 1 1

84 1153.3 .000670

120 . 1 .0091 .11713 1107.7 .000656

122 . .9977 .11440 1064.0 .000643

124 . .9861 .13 167 1022.1 .000628

126 . .9742 .10891 982 .0 .000614

128 . .9620 .10615 943.3 .000599

130 . .9495 .10336 906.1 .000583

132 . .9366 .10057 870.2 .000567

134 . .9233 .09775 835.5 .000551

136 . .9095 . 09493 801.8 .000534

138 . .8953 .09209 769.0 .000516

140 . .8805 .08925 737.2 .000498

142 . .8650 .08640 706.0 .000480

144 . .8489 .08357 675.5 .000461

146 . .8319 .08077 645 .6 .000442

148 . .8141 .07804 616.0 .000422

150 . .7951 .07543 586.7 .000402

152 . .7749 .07305 557.5 .000383

154 . .7531 .07114 52 8.3 .000365

156 . .7294 .06856 498.8 .000342

158 . .7034 . 06559 468.8 .000316

160 . .6743 . 06269 43 8.0 .000289

165 . . 5831 .05557 356.3 .000227

170 . .4707 . 04785 280.4 . 0002ie

175 . .3797 .04017 23 5 .4 .000276

180 . .3219 .03496 213.8 .000368

195 . .2846 .03187 203.1 .000469

19 C . .2583 .03001 197.4 .00 568

195 . .2384 .02885 194 .3 .000665

200 . . 2227 .02811 192.8 .000759

210 . .1988 .02737 192.3 .000941

220 . .1810 .02718 193.8 .001118

230 . .1671 .02728 196.4 .001293

2 40 . .1557 .02756 199.5 .001468

250 . .1461 .02795 203.2 .001643

260 . .1379 .02842 207.1 .001819

270 . .1308 .02893 211.2 , 001997

280 . .1245 .02948 215.4 .002176

290 . .1189 . 03 C 05 219.7 .002357

300 . .1138 .03064 224.1 .002541

310 . .1092 .03125 228.5 .002727

320 . .1051 .03192 232.9 .002921

* Two Phase Boundary

9,0 MPa Isobar

Te hd . Density The r ma 1 Viscosity T her ma 1 C ond

m i c ro- D 1 f f u s 1 v 1 t y K g / cm**3 W /m .K g/cin.s c m**2 / s

55.386 1.3119 .20573 5127.5 .000946

56 . 1.3093 .20461 5054.1 .000943

58 . 1.3008 .20111 4815.8 . 000933

60 . 1.2922 .19778 4581.0 . 000924

62 . 1.2837 .19459 4352.4 .000916

64 . 1.2751 .19154 4131.8 . 000908

66 . 1.2665 .18859 3920.4 .000901

68 . 1.2579 .18572 3718.9 . 000894

70 . 1.2493 .1 8293 3527.6 . 000887

72 . 1.2407 .18020 3346.7 .000880

74 . 1.2320 .17751 3175.8 .000873

76 . 1.2232 .17487 3014.9 .000967

78 . 1.2144 .17225 2863.5 . 000860

80 . 1.2056 .16966 2721.1 .000853

82 . 1.1967 .16708 2587.3 . 0 C 0846

84 . 1. 1878 .16452 2461.7 . 000939

86 . 1.1788 .16196 2343.7 .000832

88 . 1.1697 .15941 2232.9 . 000924

90 . 1 .1606 .15686 2128.7 .000816

92 . 1.1514 .1 5431 2030.8 . 000808

94 . 1 . 1421 .15175 1938.7 . 000300

96 . 1 . 1327 .14919 1852.0 .000791

98 . 1.1233 .14662 1770.3 . 000783

100 . 1.1137 .14404 1693.3 . 000773

102 . 1. 1041 .14146 1620.6 . 000764

104 . 1.0943 .13006 1551.9 . 000754

106 . 1 . 0844 .13625 1486.9 . 000743

108 . 1. 0744 .1 3364 1425.3 .000733

110 . 1 . 0643 .13101 1367.0 .000722

11 ? . 1.0540 .12837 1311.5 .000710

114 . 1 . 0436 .12572 1258.9 . 000699

116 . 1.0329 .12305 1208.7 . 000686

lie . 1 . 0221 .12038 1160.9 . 000674

120 . 1.0111 .11769 1115.2 . 000661

122 . . 9999 . 11499 1071.6 .000647

124 . . 9884 .11227 1029.7 .000633

126 . . 9766 .10955 989.6 . 000619

128 . . 9646 .10681 95 1.1 . 000604

130 . .9522 .10405 914.0 . 000589

132 . . 9396 .10129 879.2 . 000574

134 . . 9265 .09851 843.6 . 000558

136 . . 9130 .09572 810.1 . 000541

138 . . 8991 .09292 777.6 .000524

140 . . 8846 .09012 746.0 .000507

142 . . 0696 .08733 715.2 . 0 C 0489

144 . . 0539 .08454 685.1 .000471

146 . . 8375 .08179 655.6 . 000453

148 . . 8203 .07911 626.5 . 000434

150 . . 0022 .07654 597.9 .000416

152 . . 7830 .07418 569.5 . 000397

154 . . 7625 .07224 541 .

. 000331

156 . . 7404 .06970 513.0 • 0 C 036 C 158 . .7165 .06602 48 *. . 5 .000336

160 . . 6904 .06401 455.6 .000312

165 . . 6118 .05723 381.0 . 000255

170 . . 5138 .05045 308.5 .000231

175 . .4218 .04342 256.8 . 000264

180 . . 3561 .03773 228.6 . 000335

188 . . 3122 .03402 213.8 . 000424

190 . .2814 .03170 205 .7 . 000517

195 . . 2584 .03022 201.1 . 000610

200 . . 2404 .02926 198.6 . 000700

210 . . 2135 .02823 196.8 . 000874

220 . . 1938 .02707 197.5 . 001044

230 . . 1784 .02786 199.5 . 001212

240 . . 1660 .02006 202.3 . 001378

250 . . 1555 .02840 205.6 . 001545

260 . . 1467 .02882 209.2 .001713

270 . . 1389 .02929 213.1 . 001382

290 . . 1322 .02981 217.2 .002053

2 90 . . 1261 .03036 221.4 . 00222 5 300 . . 1207 .03093 22 5.6 . 002399

310 . .1158 .03153 229.9 .002577

320 . . 1114 .03219 234.3 .002761

30
Table 5. Transoort Proper ties of Pxyqen. Isobars# SI Unitsr q,5MPaIsr. bar 10.0 MPa Isobar

T e m o , 0 p n s i f v T b p r m a 1 Viscosity T b e r ir a 1 Te^D. Oe ns 1 t y Therma

1

Viscosity T h e r ma 1 C on H , micro- n i f f us i v 1 ty C ond

.

micro- 0 1 f f us i v i ty

K 1 / c T * *3 W/m . K g/cT.s c m * * 2 / s K q / cm** 3 W / m . K g /cm .

s

cn**2/s

55 . 3 1 . 31?5 . 2 0

c P 5 514 ? .4 .000947 + 55.500 1. 3126 .20597 5157.6 . 000947

56 . 1 .3099 . 2 0 4 p 4 5075 . c .000944 56 . 1 . 3106 .20506 5096.8 . 000945

*> fl , 1.3013 .20133 4835 .7 .000934 58 . 1.3019 .20156 6855.7 .000935

6 C • 1 . 2920 .19801 4 5 Q 9 .7 .000925 60 . 1 . 2936 .19826 6618.5 . 000926

<>? . 1 .2 843 .19483 4370.0 .000917 62 . 1 . 2869 .19507 6387.7 . 000918

^4 . 1 .2757 .19178 4148 .

5

. 00^909 66 . 1.2763 .19202 6165.2 . 000910

6 ^. 1 . 267 ? . 188«3 3936.2 .000907 66 . 1 . 2678 . 1 8908 3952.0 .000903

68 . 1 .2586 . 1 8507 3733.9 .000895 68 . 1.2593 .18623 376 e . 9 . 000896

70 . 1.2500 . 183T9 3541.9 .000888 70 . 1.2507 .18365 3556.

1

. 000889

72 . 1 .2414 . 1 8046 3 3 6 0 .2 .000881 72 . 1.2621 .18073 3373.8 . 000883

74 . 1 . 2327 .1777q 3

1

P 8 .

8

.000875 76 . 1.2336 .17806 3201.8 . 000876

76 . 1 .2740 .17515 3027 .3 . 000 P 6 P 76 . 1.2267 .17563 3039.7 . 000870

7 p . 1.2152 .17254 2875 .3 .000861 78 . 1.2160 .17283 2887.2 . 000863

80 . 1 .2064 .16996 2732.5 .000855 80 . 1 . 2072 .17025 2763.9 .000856

82 . 1.1976 .16739 2598.3 .000848 82 . 1.1986 .16770 2609.3 .000849

84 . 1.1887 .16483 2472.3 .000841 86 . 1.1895 .16515 2682.8 . 000842

86 . 1.1797 .16229 2353.9 .000834 86 . 1 .1806 .16261 2366.1 .000835

P 8 . 1.1707 .15975 2242 .7 .000826 88 . 1 . 1716 .16008 2252.6 .000828

90 . I .1 616 .15770 2138.3 .000818 90 . 1.1625 .15755 2167.8 . 000820

92 . 1 .1524 . 15466 2040 .

1

.000810 92 . 1 .1536 .15501 2069.3 .000813

94 . 1 . 147 ? .15212 1947.7 •000802 96 . 1 . 1662 .15268 1956.7 . 000804

96 . 1.1338 .14956 1 860 .P .000794 96 . 1.1369 .16996 1869.5 . 000796

98 . 1.1244 .14701 1778.9 .000785 98 . 1.1256 .16739 1787.6 .000787

100 . 1.1140 .14444 1701.7 .000776 100 . 1.1161 .16686 1710.0 .000778

102 . 1.1053 .14187 1628.8 .000766 102 . 1.1066 .16228 1636.9 .000769

104 . 1 .0956 .13929 1559.9 . 000757 106 . 1.0970 .1 3971 1567.9 .000759

106 . 1.0858 .13669 1494 .8 .000746 106 . 1.0872 .13713 1502.7 .000749

108 . 1.0759 .13409 1433.1 .000736 108 . 1.0773 .1 3656 1660.9 .000739

11 C . 1 .0658 .13148 1374.6 .000725 110 . 1.0673 .13196 1382.3 . 000728

112 . 1.0556 .12885 1319 .? .000714 112 . 1.0572 .12933 1326.7 .000717

114 . 1.0452 .12622 1266.4 .000702 116 . 1.0669 .12671 1273.9 .000706

116 . 1.0347 .12357 1216.2 .000690 116 . 1.0365 .12608 1223.7 . 000694

118 . 1.0240 .12091 1168.4 .000678 118 . 1.0258 .12166 1175.8 .000682

12 C . 1 .0131 .11825 1122.7 .000665 120 . 1.0150 .11879 1130.1 • C 0066 9

122 . 1.0020 .11557 1079.0 .000652 122 . 1.0060 .11616 1086.6 . 000656

124 . .9906 .11287 1037.2 .000638 126 . . 9928 .11367 1066.7 . 000643

126 . .9700 .11017 997.2 .000624 126 . . 9813 .11079 1006.6 .000629

] 2 P . .0671 .10746 958.7 .000610 128 . . 9696 .10810 966.2 .000615

130 . .9550 .10473 921.7 .000595 130 . . 9576 .10560 929.3 .000601

132 . .9425 .10199 886.0 . 000580 132 . . 9653 .10269 893.7 .000586

1 34 . .9296 . 09925 851 .6 .000564 136 . . 9327 .09997 859.6 .000571

136 . .9164 .09650 818.2 .000548 136 . . 9197 .09725 826.2 .000555

138 . .9027 .09374 785.9 .000537 138 . . 9063 .09653 79 6.1 .000539

140 . .8886 .09098 754 .6 .000515 160 . . 8926 .09181 76 3.0 .000523

142 . .8739 .0 P P 22 724.1 .000498 162 . . 8781 .08909 732.7 .000507

144 . . 8587 .08548 694.3 .000481 166 . . 8633 .08660 703.2 .000490

146 . .842 8 .08278 665.2 .000463 166 . . 8679 .08373 676.5 . 000473

1 4 P . .8262 .08014 636.6 .000445 168 . .8318 .08113 66 6.3 .000456

150 . . 8088 .07760 608.5 .000428 150 . . 8150 .07863 618.7 . 000439

152 . .7905 .07527 580.8 .000411 152 . . 7976 .07631 591.5 .000423

154 . .7710 .07330 553 .3 .000395 156 . .7789 .07633 566.7 .000408

156 . .7503 .07079 526.0 .000376 156 . . 7592 .07185 538.2 .000390

158 . .7281 .06799 498.7 .000354 158 . .7386 .06912 511.8 .000370

160 . .704 1 . 06526 471.3 .000332 160 . . 7161 .06665 685.6 . 000350

165 . .6342 .05871 401 .9 .000280 165 . . 6527 .06009 620.0 .000302

170 . .5486 .05246 333 .6 .000248 170 . . 5766 .05616 355.6 .000267

175 . . 4606 .04615 278 .8 .000263 175 . . 6968 .06837 300.3 .000269

1

8

C . .3904 .04044 244.9 .000316 180 . .6236 .06291 262.0 .000306

185 . .3406 . 03626 225.7 .000391 185 . .3693 .03869 23 8.7 .000368

190 . . 3053 .03349 214.9 .000476 190 . . 3297 .03535 226.9 . 000443

195 . .2791 .03168 208.6 .000563 195 . . 3002 .03322 216.6 .000524

20 C . .2587 .03048 204.8 .000648 200 . . 2773 .03176 211.5 .000605

210 . .2285 .02914 201.5 .000816 210 . . 2637 .03010 206.6 .000765

220 . . 2067 .02859 201.3 .000979 220 . . 2198 .02935 205.6 .000922

230 . .1899 .02846 202.7 .001140 230 . . 2016 .02909 2 06.2 .001076

240 . .1763 .02858 205.1 .001299 260 . .1868 .02912 208.1 .001229

250 . .1650 .02885 208.1 .001459 250 . .1766 .02932 210.7 .001382

26 C • .1555 .02923 211.5 .001619 260 . .1663 .02966 213.8 .001535

270 . .1472 .02967 215.2 .001781 270 . .1556 .03005 217.3 .001690

280 . .1399 .03016 219.1 .001943 280 . . 1676 .03050 221.0 .001845

290 . .1334 .03068 223.1 .002108 290 . . 1607 .03100 226.9 .002002

3 CO * .1276 .03122 227.2 .002273 300 . . 1365 .03152 22 8.9 .002161

310 . .1224 .03181 231 .4 .002443 310 . . 1290 .03209 233.0 .002322

320 . .1177 .03246 235.7 . 002618 320 . .1239 .03273 237.1 .002490

* Two Phase Boundary

31
Table 5. Transport D roperties of Oxygen* Isobars* SI Units

11. C MPg Isobar 12.0 MPa Isobar

Tern p - Density T h e r m a 1 fond.

V 1 scos 1 ty microThermal Diffuslvlty

Temp

Density Thermal

C ond

Viscosity

microTherma 1 Diffusivity

K 0/Cni^*3 W/m .K g/cm.s cm**?/s K q / cm * + 3 W/m.K g /cm.

cm**2 /s

55.613 1 .3132 .20621 5187 .

. 000948 * 55.726 1. 3138 .20645 5216.7 . 000949

56. 1.3115 .20551 5139.7 .000946 56. 1.3126 .20596 5102.7 .000948

5P. 1.3030 .20201 4895.8 .000936 58. 1 . 3041 .20247 4936.0 . 000938

60. 1.2946 .19870 4656.1 .000927 60. 1 . 2957 .19916 4693.8 .000929

62. 1.2961 .19553 4423.1 .000919 62. 1.2872 .19600 4458.6 .000921

64 . 1.2776 .19260 4198.6 .000912 64 . 1.2788 .1 9298 4232.1 .000914

66. 1 .2691 .18957 3983.6 .000905 66. 1 . 2703 .19006 4015.3 . 000907

68. 1 .2606 .18673 3778.9 .000898 68. 1.2619 .18723 3808.9 .000901

7 C. 1 . 2520 .1 83 96 3584.7 .000892 70. 1 . 2534 .18448 3613.2 .000894

72. 1.2435 .18126 3401 .0 .000885 72. 1 . 2448 .18179 3428.1 . 000888

74. 1 .2249 .17861 3227.7 .000879 74. 1.2363 .17915 3253.6 . 000881

76. 1 .2262 .17599 3064 .4 .000872 76. 1.2277 .17655 3089.2 .000875

78. 1.2176 .17341 2910.9 .000866 78. 1.2191 .17398 2934.6 .000869

PC . 1 .20R8 .17085 2766.6 .000859 80. 1 . 2104 .17143 2789.4 . 000862

82. 1 .200] .16R30 2631 .1 .000853 82. 1.2017 .16891 2653.0 .000856

84. 1.1913 .16578 2503.9 .000846 84 . 1.1930 .16640 2524.9 . 000849

96 . 1 .1 824 .16326 2384 .4 .000839 86. 1.1842 .16390 2404.7 . 000842

88. 1.1735 .16074 2272.2 .000832 88 . 1.1753 .16140 2291.8 . 000835

90. 1 .1645 .15823 2166.8 .000824 90. 1 .1664 .1 5891 2185.8 .00082 8 92. 1.1554 .15572 2067 .7 .000817 92 . 1.1574 .15641 2086.1 . 000821

94. 1 . 1 463 .15320 1974.6 .000809 94. 1.1484 .15392 1992.4 . 000813

96. 1.1371 . 15068 1986.9 .000801 96 . 1.1393 .15142 1904.3 .000805

98. 1.1279 .14816 1804.4 .00079? 98 . 1. 1301 .14892 182 1.3 . 000797

100. 1.1185 .14563 1726.6 .000783 100. 1.1208 .14641 1 743.1 . 000788

102. 1.1091 .14309 1653.2 . C00774 102. 1.1115 .14389 1669.3 . 000779

1 C 4 . 1 .0995 .14054 1583.8 .000765 104. 1.1021 .14137 1599.6 .000770

106. 1 .0 890 .13799 1518.3 .000755 106 . 1 . 0925 .13884 1533.8 .000761

1 C 8

1.0801 .13543 1456.3 .000745 108. 1 . 0829 .13630 1471.5 . 000751

lie. 1 .0703 .13286 1397.5 .000735 110. 1.0732 .13376 1412.5 .000741

112. 1 .060* .1 302P 1341.7 .000724 112 . 1. 0633 .13121 1356.6 .000731

114. 1 .0502 .12769 1288.8 .000713 114. 1.0533 .12865 1303.5 . 000720

llh. 1 . 0399 . 1 2509 1238.4 .000702 116. 1.0432 .12608 1253.0 . 000709

IIP. 1.0294 .12249 1190.5 .000690 118. 1.0330 .12351 1204.9 . 000697

120. 1 . 01 RP .11908 1144 .7 .000678 120 . 1.0225 .12093 1159.1 . 000686

122. 1.0080 .11725 1101.1 .000665 12? . 1.0120 .11835 1115.4 . 000674

1 P 4 , .9971 .11463 1059.3 .000652 124. 1 . 0012 .11576 1073.7 .000661

126. .9959 .11199 1019.3 .000639 126. . 9902 .11316 1033.7 . 000649

128. .9744 .10935 981.0 .00^626 128. . 9790 .11056 995.5 . 000636

130. .962 7 .10670 944.2 .000612 130. . 9677 .10796 958.7 . 000623

132. .9508 .10404 908 .8 .000598 132. . 9560 .10535 92 3.5 . 0C0609

134. . 9385 .10138 874 .7 .000583 1 34. . 9441 .10274 889.5 .000595

136. .9260 .09872 841 .8 .000569 136. . 9319 .10014 856 .

. 000581

138. .9131 .09607 8 1 0 . C .000554 138. . 9195 .09754 825.3 .000567

1 4 C . .8998 .09341 77Q.2 . 0C053R 140 . . 9066 .09494 794.8 . 000552

142. .8861 .09077 749 .

.000523 147 . . 8935 .09236 765.

.000538

144.. .871 9 .08814 720.4 .000507 144 . . 8800 . C 89 80 736.7 .000523

14^. . 8573 .08555 692 .2 .000491 146. . 8660 .08728 709.0 .000508

1 4 P . . 8422 .0830? 664 .

.000476 148. .8516 .00480 682.0 . 000494

1 5 C.8264 .08058 637.8 . 000460 150. . 8367 .08242 655.7 . 000479

152. .8101 .07830 611.6 .000445 152. . 8214 .08016 630.1 . 000465

154 . .7930 .07629 585.8 .000432 154 . . 8054 .07815 60 5.1 . 00045 3 156. . 7751 .07388 560.5 .000416 156. . 7888 .07579 58C.7 . 000438

158. .7563 .07126 535.5 .000398 159. . 7716 .07326 556.7 .000422

1 6 C . .7365 .06871 510.9 .000381 160. . 7536 .07081 533.3 .000407

165. .6820 . 06263 4 5 0.6 .000339 165. . 7050 .06494 476.4 . 000369

170. .6192 .05791 39? .3 .000305 170. . 6507 .05953 422.2 .000337

175. . 5500 .05184 339.1 .000291 175 . . 5912 .05462 372.0 .000318

180. .4 922 .04700 296.6 .000306 190. . 5301 .05016 328.8 . 000319

18 5. .4 244. . 04263 266.7 . 000345 1 95 . . 4734 .04609 295.2 .000342

1 9 C • .3786 .03908 247.2 .000401 190. . 4250 .04251 271.1 .000382

195. .343 1 . 0364 1 234 .6 .000467 195 . . 3855 .03957 254.4 . 000433

200. . 31 c 4 .03449 2 2 6.5 .000537 200. . 3536 .03729 24 3.1 . 000492

21 C. .274 9 .03214 217.7 .00068? 210. . 3065 . C 34 3 0 229.9 .000620

22 0. . 2464 .03096 214.2 . r C0827 220 . . 2734 .03267 22 3.9 . 000752

230. . 2 249 . 0304 ] 213.6 .000969 230. . 2486 .03182 221.5 . 000884

240. .207p . 03024 214 .4 .001111 240 . . 2291 .03143 221.2 .001015

250. .1938 .03030 216.3 .001252 250. . 2132 .03133 222.2 . 001146

260 . . 1 8? 0 . 03052 71 8 . P .001393 260. .1999 .03143 224.0 . 001277

270. .1719 .03083 221 .8 .001535 270. .1985 .03165 226.5 . 001409

280. .1631 .03122 225 .1 .001678 280 . .1786 .03196 229.4 .001541

290. .1553 .03166 27 8 .6 .001 822 2 90 . .1700 .03234 232.5 . 001674

300. .1484 .03214 ? 37.3 .001968 300. . 1623 .03276 235.9 . 001809

310. .1422 .03266 236.2 .002116 310. . 1553 .03325 239.5 .001946

32 0. .1366 • 0 3 3

9 9 240.1 .002271 370 . . 1491 .03385 243.2 . 002090

Two Phase Poundar
Table 5 • Transport Properties of C x y g e n » Isobars* SI Units

13,0 MPa Iso tar

Temp. Den s i t y Th p r m a 1 Viscosity T h e r m a 1 C on d . micro- 0 i f Tus 1 v 1 ty

K q /cm**3 W/m.K a / c m . s cTM**2/s

55.838 1.3144 .2C669 52*6.1 .600950

5 6. 1 .3137 .206*0 5225 .P .0009*9

58. 1.3053 .20292 *976.3 .0009*0

6 0. 1 .2968 .19961 *731 .6 .000931

6?. 1.2884 .196*7 ** 94 .2 .00092?

68. 1.2800 .193*5 *265.6 .000916

6 6. 1 .7716 .1905* *0*7 .0 . 000909

68. 1.2631 .16773 r) P39.0 .000903

70. 1.2547 • IP *"9 9 36*1 .P .000896

72. 1.2462 .18231 3*55 .3 . 000890

74. 1.7377 .17968 3 2 79 .

5

.00088*

76. 1.2292 •17710 311* .0 .000878

78. 1.2206 .17*55 2968.3 .000872

80. 1.2170 .17202 2812 .1 .000865

8?

.

1 .2033 .16951 367* .8 .000859

84. 1.1946 .16702 25*5.9 .000853

86. 1.1859 .16*53 2*2* .9 .0008*6

ee. 1.1771 .16205 2311.3 .000839

90. 1.1683 .15958 220* .6 .000832

92. 1.1594 .15710 210*.* . 0C0825

94. 1 .1504 .15*63 2010.2 .000817

96 . 1.1414 . 15215 1921.6 .000809

98. 1.1323 .1*967 1838.1 .000801

100. 1.1231 .1*718 1759.5 .000793

102. 1 .1 139 .1**69 1685.3 .00078*

104 . 1.1046 . 1*219 161 5.* .000776

106. 1.0951 .13968 15*9.2 . 000766

1 C 8 . 1.0856 .13717 1*86.7 .000757

110. 1.0760 .13*65 1*27 .* .0007*7

112. 1.0663 .13213 1371.3 .000737

114. 1 .0564 .12959 1318.0 .000726

116. 1.0465 .12706 1267.* .000716

IIP. 1 .0364 .12*52 1219.2 .G00705

120. 1.0261 .12197 1173 .3 .000693

182. 1 .0157 .119*2 1129.6 .000682

124. 1 .0057 .11686 1087.8 .000670

126. .9944 .11*30 10*7.8 .000658

128. .9835 .1117* 1009.6 .0006*5

130. .9724 .10918 972.9 .000633

132. .9610 .10662 937.8 .000620

134. .9404 .10*06 903 .9 .000606

136. .9376 .10150 871 .* .000593

138. .9255 .09895 8*0 .1 .000579

140. .9131 .096*1 809.8 .000566

142. .9004 .09389 780.6 .00055?

144. . 8874 .09139 752 .3 .000538

146. .8741 .08892 72*.

9

.00052*

148. .8603 .08650 698.* .000510

150. .8462 .08*15 672 .6 .000*97

152. .8316 .08193 6*7.5 .000*8*

154. .8166 . 07992 623.1 .000*72

156. .8010 .07761 599.3 .000*58

158. .7850 .07516 576.1 .000**3

160. .7684 .07278 553.* .000*29

165. .7241 .06709 *99.0 .000395

170. .6756 .0618* **7.7 .000366

175. .6231 .05707 *00.1 .0003*5

180. .5685 .05279 357.7 .000338

185. . 5152 .o*e9* 322.5 .000350

190. .4669 .0*5*9 295.3 .000377

195. . 4254 .0*250 275.3 .000*16

200. .3908 .0*003 260.9 .000*6*

210. .3380 .03653 2*3.2 .000575

220. .3004 .03**6 23*.

3

.000695

230. .2724 .03330 230.1 .000816

240. .2504 .03268 228.5 .000938

250. .2326 .032*1 228.5 .001060

260. .2177 .03238 229.6 .001182

270. .2051 .03250 231.5 .001305

280. .1942 .03273 233.9 .001*28

290. .1846 .0330* 236.7 .001552

300. .1761 .033*1 239.8 .001676

310. .1685 .03385 2*3.0 .00180*

320. .1616 .03**2 2*6.5 .001938

14.0 MPa Isobar

T e n d . Density Thenra 1 Viscosity T he r m a I C on d

.

micro- Oiffusivity

< q / cm** 3 W/m.K 3 /c m . s c 71**2 / s

55.951 1.3150 .20694 5275.* . 000951

58 . 1.31*8 .20685 5269.1 . 000951

58 . 1 . 306* .20337 5016.7 . 000 v*

1

60. 1 . 2980 .20007 * 76Q ,

5

.000933

62 . 1 . 2 8 96 .19693 *529.8 . 0C0925

64 • 1 . 2812 .19392 *299.3 . 00091

p

66. 1 . 2729 .19103 *078.8 . C0091 1 68 . 1.26** .1 °822 3 86 9.

1

. 000905

70. 1 . 2560 .18550 3670.3 . 000899

72 . 1 . 2*76 .18283 3*82.5 . 000993

74. 1 . 2391 .1 8022 3305.* .0C0PP7

76 . 1.2306 .17765 3138.7 . 000881

78. 1. 2221 .17511 2982.0 . C00875

80. 1.2135 .17260 283*.

8

. CC0968

82 . 1 . 20*9 .17011 2696.6 .000862

84. 1. 1963 .16763 2566.9 . 000956

8* . 1.1876 .16516 2**5.

1

. 0009*9

«« . 1.1789 .16270 2330.8 . 0C08 * 2 00. 1 . 1701 .1602* 2223.

5

.000836

92 . 1 . 1613 .15779 2 12? .7 . 000828

64 . 1 .152* .15533 2027.9 .000821

66 . 1. 1*35 .15287 1 93 8.7 .000813

58. l .13*5 .150*1 135* .8 . 000806

100. 1.125* . 1*79* 1775 .

8

. 000798

102 . 1. 11 62 .1*5*7 1701.3 . 000789

104 . 1. 1070 . 1*299 1631.0 . 0007 8 C 106. 1 . 0977 .1*051 156*.

5

. CC0772

108. 1.0883 .13802 1501.7 . 000762

1 10 . 1.0788 .13553 1**2.

2

.000753

112. 1 . 0692 .13303 1385.8 .0007*3

114 . 1 . 0595 .13052 1332.* .000733

116. 1.0*97 .12802 1281.6 .000723

118. 1.0397 .12550 1233.3 .000712

1 20 . 1 . 0296 .12299 1187.3 . 000701

122. 1.019* .120*7 11*3.5 .000690

124. 1.0090 . 1 179* 1101.7 . 000678

126. . 9985 .115*2 1061.7 . 000666

128. . 9878 .11290 1023.5 .00065*

130. . 9769 .11037 986.8 . 0006*2

132. . 9658 .10785 951.7 . 000630

134 . .95*5 .1053* 918.0 .000617

136. . 9*30 .10282 885.6 . 00060*

138. . 9313 .10032 85* .* . 000591

140. . 9193 .09783 92*. 3 . 000578

142. . 9070 .09535 795.3 .000565

144 . . 89** .09290 767.3 .000552

146. . 8816 .090*8 7*0.2 . 000536

148. . 868* .08811 713.9 . 000525

150. . 85*9 .08581 688.5 . 000513

152. . 8*10 .08362 663.9 . 000500

154 . . 8267 .08160 639.9 . 000*89

156. . 8121 .0793* 616.6 .000*76

158. . 7970 .07696 59*.

0

. 000*63

160. .781* .07*6* 571.9 . 000**9

165. .7*0* .06911 519.3 .000*18

170. . 6962 .06398 *70.1 .000390

175. . 6*90 .05930 *2* . 5 . 000369

180. . 5996 .05512 383.3 . 000359

185. .5503 .05139 3*7.7 . 000362

190. . 5037 .0*807 318.8 . 000380

165 . . *620 .0*512 296.2 . 000*10

200. .*258 .0*258 279,3 .000**8

210. . 3688 .0387* 257.3 .0005*3

220. . 3273 .03630 2*5.5 . 000650

230. . 2961 .03*82 239.2 .000762

240. .2717 .03397 236.2 . 000875

250. .2519 .03353 235.2 . 000989

260. . 2356 .03336 235.5 . 001103

270. .2216 .03337 236.7 . 001217

2 80 . . 2096 .03352 238.6 .001332

260. . 1991 .03376 2*1.0 . 001**8

300. .1899 .03*07 2*3.7 .001565

310. . 1816 .03**6 2*6.7 .00168*

320. .17*1 .03501 2*9.9 . 001809

Tho Phase Boundary

33
Table 5. Transport Properties of Oxygen* Isobars* SI Units

15.0 MPa I soba r

Temp . Density Thermal Viscosity Thermal

Con d

micro- Dlffuslvlty

K g/cm**3 W/m .K g / cm •

cm**? /s

56.063 1.3157 .20710 5304 ..00095?

58. 1.3075 . 2 0 3 R 1 5057.3 .000943

60. 1 .2991 .20052 4R07.5 .00093*

6?. 1 .2907 .19739 45 6 5.. 6 .000927

6 4. 1.2824 . 19440 4332.9 .000920

66. 1.2740 .19151 4110.6 .000914

68. 1.2657 . 1 PP7? 3899.? .000907

70. 1.2573 .18600 3699.0 .000901

7?. 1.2489 . 1P335 3509.7 . C 00 R 95

7 4. 1 . ? 4 0 5 .1 8075 3331.3 .000889

76. 1.2321 .17819 3163.5 . C C C R R 3 78. 1.2236 .17567 3005.7 .000077

80. 1.2151 .17317 2857.5 .00087]

0?. 1 .2065 .17070 271 P.3 .000065

84. 1 .1900 .16824 25R7.8 .000859

06 . 1 .1893 .16679 2465.3 .C0CP53

PP . 1 . 1R07 .16334 ?350 .? .000846

90. 1.1720 . 1 6090 224 2 . 3 .000839

92. 1.163? .15846 2140.6 .00083?

94 . 1 . 1 5^4 .15403 ? 04 c .5 .OOO0?6

96. 1.1455 .15359 1955.9 .00CP1P

98. 1 .1366 .15114 1871.5 .000810

100. 1 .1274 .14070 1792.0 . C0C Q 0?

10? . 1.1185 .14624 1717.1 .000794

104. 1 .1094 .14379 1646.5 .000785

106. 1 .1002 .14133 1579.7 .000777

10P. 1 .0909 .13886 151 6 .6 . 000768

110. 1.0015 .13639 1456.Q .000759

11?. 1.0720 .13392 1400.3 .000749

114. 1 .06?5 .13144 1346.6 .000739

116. 1 .052 0 . 1 2096 1295 .6 .000729

IIP. 1 . 04?0 .12647 1 ?47.2 .000719

1?0. 1 .0331 . 1 239P 1201.1 . 0 0 0 7 0 R

12?. 1 .0230 . 12149 11*7.2 . 0 00697

1 ? 4 , 1.0123 .11900 1115.3 .000606

126. 1 . 0025 .11651 1 075.3 .000675

1?P. .9920 .1140? 1037.1 .000663

130. • 9 R 1 3 .11154 1000.5 .000651

132. .9706 . 1 0905 9 65.4 .000639

134. .9594 .10657 931.7 .000627

136. .340? .10410 899 .4 . 000615

138. .9368 .10164 R68.3 .000602

1 4 C

.925 1 . 09920 83 8 .4 .000590

142. .913? .09677 909 .

.000577

144. .9011 .09436 701 ..000565

146. . 8087 .09198 754.8 .00055?

140. .0760 .08965 728.9 .000540

150. .8430 .00739 7 0 3 .7 .000527

152. . 0497 .06522 679 .

.000516

154. . P 3 6.08322 655.8 .000505

156. .8221 .08099 632.9 .000497

1 5 P

• 807 R .07968 610.7 .000490

160. .793 1 . 0764? 5 8 9.2 .000469

165. .754« .07101 537.9 . 000438

170. .7139 .06598 4 9 0 .2 .000413

175. . 6705 .06139 446.1 .000392

180. .6254 .05726 406.1 .OC03R0

1P5. . 5793 .05359 370 .P .000378

1 90. . 5357 .05034 340.9 .000386

195. .494 e .04745 316.7 .000410

2 C C . .450? .04491 297.7 .000441

210. .3903 • 0 4 0 * 8 272 .0 .0005??

220. . 3536 .03814 ? 5 7 , ? .000617

2 3 C

. 3195 .03639 248.9 .00071

240. .292 8 .03531 ?4 4 .3 .000024

25 0 . .271? .03468 ?4? . ? .000930

260. . 253 3 .03437 24 1.7 .001037

270. . ? 3 8 1 .03427 24? .? .001144

? 8 C

.2251 .03433 243.6 .001252

290. .2136 .03449 245 .5 . 001360

3 C C . .2036 .03474 24 7.9 .001469

310. .1946 .03509 250 .5 .001581

320. .1865 .03560 2*3.5 .001700

16.0 MPa Isobar

Temp . Dens 1 t y Thermal Viscosity T her ma 1 C o nd . micro- Diffuslvity

K g / cm + * 3 W /m ,K g/cm.s c m**2 / s

56.176 1.3163 .20742 5333.4 .000953

58 . 1.3086 .20426 5098.0 . 000949

60. 1 . 3002 .20098 4 04 5.7 . 000936

62. 1 . 2919 .19785 4601 .

. 000929

64 . 1.2836 .1 9486 4366.7 . 000922

66 . l . 2752 .1 9199 4142.5 .00091-6 68 . 1 . 2669 .18921 3929.4 . 000909

70. 1.2586 . 1 06 50 3727.6 . 00090 3 7? . 1 .2502 .18387 3536.9 . 000898

74 . 1.2419 .18128 3357.3 . 00089?

76. 1 . ??35 .1 7374 3188.2 . 000086

78 . 1.2251 .17623 3029.3 . 000880

80. 1.2166 .

1 7375 2880.1 .000874

8 ? . 1.2081 .17129 2740.1 . 000060

84 . 1.1996 .1 6 Pp<* 2608.7 . 00086?

* 6 . 1 .1910 .16641 2485.4 .000056

88 . 1.1R24 .16398 2369.6 . 000849

90. 1.1736 .16156 2261.0 . 000043

92 . 1 . 1451 .1 5914 2159.0 . C COR 3

94 . 1.1564 .15672 2 063 .

. 000829

96 . 1. 1476 . 1 5429 1972.9 . 0C0322

98 . 1.1387 .15187 1888.1 . CCO01

100 . 1.1290 .14644 1808.2 .000*07

102 . L . 1208 .14701 1732.9 . 000799

104 . 1.1118 .14458 1661.9 . 000790

106 . 1 . 1027 .14214 1594.8 . CC07 * ? 108 . 1 . 0935 .13969 1531.4 . 000773

110 . 1 . 0842 .13725 1471.4 . 000764

112 . 1 . 0748 .13479 1414.6 . 000755

114. 1 .0654 .13234 1360.7 .000745

116 . 1.0558 .12988 1309.5 . 000736

110 . 1.0462 .12742 1261.0 . 000725

1 ? 0 . 1 . 0364 .12466 1214.7 . 000715

1 ?? . 1 . 0265 .12250 1170.7 .000705

124. 1.0165 .12004 1128.7 . 000694

126 . 1 . 0063 .11758 1088.7 . C0C683

128 . . 9960 .11512 105 0.4 . 000672

1 30 . . 9956 .11267 1013.8 . QOO 60 O 13? . . 9749 .11022 978.7 . 000649

134. . 9642 .10778 94 5.1 .000637

136. . 9532 .10535 912.9 . 000625

138 . . 9421 .10293 381.9 . 00061

140. . 9307 .10052 85 2.0 .000601

142 . . 9191 .09813 82 3.. 000589

144. . 9074 .09576 795.7 .000577

146 . . 8953 .09343 769.0 . 000565

148. . 8831 .09114 743.2 .000553

150 . . 8706 .08R91 718.3 . 000541

152. . 8578 .08677 694 .

. 000530

154. . 8447 .08477 671.0 .000520

156 . . 8314 .08258 648.4 . 000508

159. . 8178 .0803? 626.5 . 0004 9 6 160 . . 8038 .07811 60 5.3 . 000485

165 . . 7676 .072 82 55 5.1 . 000457

170. . 7293 .06789 508.6 . 000433

175. . 6891 .06335 465.7 . 000413

180. . 64 74 .05927 426.6 . 000399

105 . . 6050 .05563 391 .

. 000394

190. . 5634 .05241 361.6 . 000400

195 . . 5239 .04955 336.3 .000415

200 . . 4876 .04703 315.8 . 000440

210 . . 4264 .04291 286.8 . 000508

??0 . . 3791 .03995 269.2 . 000592

230. . 3425 .03795 258.6 . 000685

240 . . 3136 .03666 252.7 . 000763

250. . 2903 .03586 249.5 . 0003°?

260. . 2709 .03541 240.1 .000981

270 . . 2545 .03520 ? 4 7 ,

.001082

200 . . 2 404 .03516 248.7 .001183

290 . . 2280 .03524 250.2 .001265

300. .217? .03542 25?.

.001388

310 . . 2075 .03572 254.5 . 001493

320. . 1988 .03620 25 7.1 . 301605

* Two Phase Boundary
Table 5. Transport Properties of Oxyqen> Isobar s» SI Units

17.0 mp 3 I sobar 18.0 MPa Isobar

T P'T p . 0 an s I t y Thermal

C on d . Viscosity

microTh p r ma

1

Dl f fuslvlty

Temp . Density Th er ir a 1 C ond . Viscosity

microThermal0 1 f f us 1 y i ty

K q/ C n**3 W/m .K q/cti.s Cm**2 /s K g / cm**3 W / m • K q/cm.s cm**2 /

s

56.288 1.3169 .20766 5362.2 .000954 * 56. 399 1.3175 .20790 5390.9 . 000955

58. 1 .3097 . 20670 5138.9 • C 00946 58. 1.3108 .20515 5179.8 • 00094 8 60. 1.301* .20163 4*883 .9 . C 00 93 8 60. 1.3025 .20187 4 92 2 .

2

. 000940

^ 2 . 1 .?Q30 .19831 6637.3 .000931 62. 1.2942 .19877 4673.2 .000932

*4 . 1.2867 . 19533 4400.5 .000924 64 . 1.2859 .19580 4434.3 . 000926

66. 1 . 2

7 6 5 . 1 9267 4174.6 .COO 9 18 66. 1 . 2777 .19294 4206 .4 . 000920

68 . 1 .2682 .18970 3959.6 .000912 68. 1.2694 .19018 3989.8 . 000914

70. 1 .2599 . 1 8700 3756.2 .000906 70. 1.2611 .1 8750 3784.9 . 000908

72. 1.2616 .1863^ 3564.2 .000900 72. 1.2529 .18489 3591.4 .000902

7 4.. 1.2632 .181 °1 3383 .2 .000894 74

.

1.2446 .1 8233 3409.1 . 000897

76. 1 . 2369 .17928 7212.9 .000889 76. 1 . 2363 .17981 3237.7 . 000891

7P . 1 .2265 .17678 3053 .0 .000883 76. 1.2280 .17733 3076.6 . 000886

PC. 1 . 2 1 P 1 .17432 2902.8 .000877 80. 1.2196 .17488 2 92 5.4 .000880

8 2. 1.2097 .17187 2761 . 8 .000871 82. 1.2112 .17245 2783.5 . 000874

86. 1.2012 .16966 2629.5 .000865 84 . 1.2028 .17004 2650.4 . 000868

86 . 1.1927 .1670? 2505.4 .000859 86. 1 .1944 .16763 2525.5 .000862

88 . 1.1862 .16661 2389.0 .000853 88. 1. 1859 .16524 2408.3 . 000856

90. 1.1756 .16220 2279.7 .000846 90. 1.1774 .16285 2298.3 .000850

92. 1 .1 670 .159^0 2177 .0 .000840 92. 1.1688 .16046 2195.1 .000843

96. 1.1583 .1 5760 2080.6 .000833 94 . 1.1602 .15808 2098.1 . 000837

96. 1.1696 . 15500 1989.9 .000826 96. 1.1515 .15569 2006.9 .000830

98. 1.1608 .15259 1904 .6 .000819 98. 1. 1428 .15330 1921.1 . 000823

IOC. 1.1320 .i50ie 1 8 24 .

3

.000811 100. 1.1341 .15091 1840.3 . 000815

102. 1.1231 .16777 1748.6 .000803 102. 1 . 1253 .14852 1764.2 .000808

106. 1.1161 .16535 1677.2 .000795 104 . 1.1164 .14613 1692.4 . 000800

106. 1.1051 .16296 1609.8 .000787 106. 1.1075 .14373 1624.6 .000792

108. 1 .0960 .16051 1546.1 .000778 108. 1.0985 .14132 1560.6 .000783

110. 1 .08*8 .13809 1485.8 .000770 110. 1.0894 .13892 1500.

1

. 000775

112. 1.0776 .13566 1428.7 .000761 112. 1 . 0802 .13651 1442.8 .000766

116. 1.0682 .13323 1374.6 .000751 114 . 1.0710 .13410 1388.5 .000757

116. 1 .0588 .13079 1323.3 .000742 116. 1 . 0617 .13169 1336.9 . 000748

118. 1.0693 .12836 1274.6 .000732 118. 1 . 0523 .12928 1288.0 .000738

120. 1 .0396 .12593 1228 .2 .000722 120. 1.0428 .12687 1241.5 .000729

122. 1.0299 .12369 1184 .1 .000712 122 . 1.0332 .12446 1197.2 .000719

126. 1. 0200 .12106 1142.0 .000701 124. 1 . 0235 .1 2206 1155.1 .000709

126. 1 .0100 .11863 1101.9 .000691 126. 1.0137 .11966 1114.9 .000698

128. .9999 .11620 1063.6 .000680 128. 1.0037 .11726 1076.5 .000688

130. .9897 .11378 1026.9 .000669 130. . 9937 .11486 1039.8 .000677

132. .9793 .11136 991 .8 .000658 132. . 9834 .11248 1004.7 .000666

136. .9687 .1 0096 958.2 .000646 134. .9731 .11010 971.1 . 000655

136. .9580 .10656 926.0 .000635 136. . 9626 .10774 938.9 .000644

138. .9671 .10617 895.1 .000623 138. . 9520 .10538 90 8.0 . 000633

1 6 C • .9360 .10180 865.3 .00061? 140. .9412 .10305 878.3 .000622

162. .9268 .09965 836.7 .000600 142 . . 9302 .10073 849.8 .000611

166 . .9133 .09712 809.2 .000588 144. .9190 .09844 822.3 .000600

166. .9017 .09482 782.7 .000577 146. . 9077 .09617 795.9 .000588

168. .8898 .09257 757.1 .000566 148. . 8962 .09395 770.5 .000577

150. .8777 .09037 732.4 .000554 150. . 8845 .09178 745.9 .000567

152. .8656 .08825 708.5 . 000544 152. . 8725 .08969 72 2.2 . 000556

156. . 8528 .08626 685.4 .000534 154. . 8604 .08771 699.3 .000547

156. .8600 .08611 663 .1 .000523 156. . 8481 .08559 677.2 . 000536

158. .8270 .08189 641.5 .000511 158. . 8355 .08341 655.8 . 000525

160. .8136 .07973 620.6 .000500 160. . 8227 .08129 635.2 .000515

165. .7792 .07656 571 .2 .000474 165. . 7898 .07619 586.4 .000490

170. . 7631 .06969 525.6 .000451 170. . 7555 .07142 541.6 .000468

175. .7056 .06522 483.7 .000431 175. .7199 .06700 500.4 .000449

1 8 C

.

.6666 .06117 445.4 .000418 180. . 6833 .06298 462.8 .000435

185. .6269 .05756 411 .0 .000411 185. . 6460 .05936 428.8 .000427

190. . 6876 .05633 380.8 .000413 190. .6089 .05615 398.7 .000426

195. .5697 .05169 354.9 .000423 195. . 5727 .05331 372.5 .000433

200. .5162 .06898 333 .4 .000442 200. . 5382 .05079 350.2 . 000448

210. .6526 .06682 301.7 .000500 210. .4770 .04660 316.3 .000496

220. .6035 .06171 281 .6 .000574 220 . . 4268 .04340 294.0 .000562

230. .3669 .03951 269.1 .000659 230. . 3865 .04104 279.6 .000638

260. .3361 .03803 261.5 .000749 240. . 3540 .03939 270.4 .000721

250. .3090 .03706 257.0 .000841 250. . 3275 .03826 264.8 .000807

26C • .2882 .03666 254.7 .000935 260. .3054 .03753 261.5 .000895

270. .2706 .03616 253.8 .001029 270. . 2866 .03709 259.9 .000984

280. . 2555 .03600 254.0 .001125 280. . 2705 .03686 259.5 .001074

290. .2623 .03601 255.0 .001221 290. .2564 .03678 260.0 .001165

300. .2307 .03612 256.6 .001317 300. .2441 .03683 261.1 .001256

310. .2203 .03636 258.6 .001417 310. . 2330 .03701 262.8 .001350

320. .2110 .03681 260.9 .001523 320. . 2232 .03743 264.8 .001451

* Two Phase Boundary
Table 5. Transport Properties of Oxygen* Isobars* SI Units 19.0 MP a Isobar 20.0 MPa I soba r Temp

Density Thermal V I s c os 1 1 y Thermal Temp. Dens 1 1 y Thermal Viscosity Thermal

C ondmicro- 0 1 f f us 1 v 1 t y C on d

micro- D 1 f fusl v 1 ty

K W /m • k q/cm.S cm+*2/s K q / cm** 3 W/m.K g /cm.

cm**2 /

56,511 1.3181 .20814 5419.4 .000955 * 56.623 1.3187 .20838 5447.7 . 000956

5 8. 1.3119 .20559 5220.9 .000949 58. 1.3129 .20603 5262.1 . 000950

60. 1.3036 .20232 4960 .6 .000941 60. 1. 3047 .20277 4999.1 . 000943

62. 1 .2953 .19922 4709.3 .000934 62. 1.2964 .19967 4745.4 .000936

6*. 1.2871 .19626 4468.2 .000928 64. 1.2882 .19672 4502.2 .000930

66. 1.2788 .19341 423 8 .4 .000922 66 . 1.2800 .19388 4270.4 .000924

68. 1 . 2706 .19066 4020.1 .000916 68. 1.2719 .19115 4050.4 . 000918

7 C o 1.2624 .18800 3813.6 .000910 70. 1.2637 .18849 3842.3 .000912

72. 1.2542 .18540 3618.6 .000905 72 . 1.2555 .18590 3645.9 .000907

7 4, 1 .2459 .18285 3435.1 .000899 74. 1 . 2473 .18337 3461.0 . 000902

76. 1.2377 .18035 3262 .4 .000894 76 . 1.2391 .18088 3287.1 . 000896

78 . 1 .2394 .17788 3100.2 .000888 78. 1 . 2308 .17843 3123.8 .000891

80. 1.2211 .17544 2948 .0 .000883 80 . 1.2226 .17600 2970.6 .000885

82. 1.2128 .1 7303 2805.1 .000877 82. 1.2143 .17360 2 82 6.8 . 000880

84. 1 .2044 .17063 2671.2 .000871 84. 1 . 2060 .17121 2691.9 .000874

86 . 1.1960 .16824 254 5 .5 .000866 86 . 1. 1976 .16884 2565.5 .000869

ee . 1.1876 .16586 2427.6 .000860 88 . 1 .1893 .16648 2446.8 .000863

90. 1 .1 791 .16349 2316.9 .000853 90. 1 .1809 .16412 2335.5 .000857

9? . 1 .1 706 .16112 2213.0 .000847 92. 1.1724 .16177 2231.0 . 000851

94 . 1 .1621 • 1 58 7 5 2115 .5 .000840 94. 1.1639 .15942 2132.8 . 000844

96. 1.1535 .1 563 8 2023.7 .00083* 96. 1.1554 .1 5706 2040.5 . 000838

98 . 1.1449 .15401 1937.4 .000827 9« . 1.1469 .15471 1953.8 .000831

100. 1.1362 .15164 1856.2 .000820 100 . 1.1383 .15236 1872.1 .000824

102. 1 .1275 .14976 1779.7 .000812 102. 1. 1296 .15000 1795.1 .000816

104. 1.1187 . 14689 1707.5 .000804 104. 1.1209 .14764 1722.6 .000809

106. 1 .1098 .14451 1639 .4 .000797 106 . 1. 1121 .14528 1654.2 .000801

108. 1 .1009 .14213 1575.1 .000788 108 . 1.1033 .14292 1589.5 .000793

110. 1.0919 .13974 1514.3 . 000780 110. 1 . 0944 .14055 152 8.4 .000785

112. 1.0829 .13736 1456.7 .000772 112. 1.0855 .13819 1470.6 .000777

114. 1 .0738 .13497 1402.2 .000763 114 . 1 . 0765 .13582 1415.8 . 000768

116. 1 .0646 .13258 1350.4 .000754 116. 1.0674 .13345 1363.8 . 000760

118. 1 .0653 .13019 1301 .3 .000745 118. 1.0582 .13109 1314.5 .000751

120. 1.0459 .12781 1254 .7 .000735 120. 1. 0489 .12872 1267.7 .000741

122. 1.0364 .12542 1210.3 .000725 122. 1.0396 .12636 1223.1 . 000732

124. 1 .076 9 . 1 2304 1168.0 .000716 124 . 1 . 0302 .12401 1180.7 .000722

126. 1 .0172 .12066 1127.7 .000706 126. 1. 0206 .12165 1140.

.000713

128. 1 .0074 .11829 1089.2 .000695 128 . 1.0110 .11931 1101.8 . 000703

130. .9975 .11593 1052 .5 .000685 130. 1. 0013 .11697 1065.0 . 000693

132. .9875 .11357 1017.4 .000675 13?. . 9914 .11464 1029.8 .000683

134. .9774 .11122 983 .7 .000664 134 . . 9815 .11232 996.1 .000672

136. .9671 . 1 C 889 951.5 .000653 136. . 9714 o 11001 963.9 .000662

138. .9567 .10656 920.6 .000642 138. . 9612 .10772 933.0 .000651

140. .9461 .10426 891.0 .000632 140. . 9508 .10544 903.4 .000641

142 . .9354 .10197 862.5 .000621 142. . 9404 o 10319 874.9 .000631

144 . . 924 5 . 09971 83 5.1 .000610 144 . . 9297 .10095 847.6 .000620

146. .9135 .0974 8 808.8 .000599 146. . 9190 .09875 82 1.3 . 000610

148. .9023 .09529 783 .4 .000589 148. . 9080 .09659 796.0 .000600

150. . 8909 .09315 7*9.0 .000578 150. . 8970 .09447 771.7 . 000590

157. .8793 .0 9107 735.4 .000569 152. . 8857 .09242 74 8.2 .000580

154. . Q 67 6 .08911 712.7 .000559 154 . . 8744 .09046 725.6 .000571

156. . 8 557 .08701 690.7 .000549 156. . 8628 .08840 703.8 .000561

158. . 84 3 5 .08488 669.6 .000539 158. . 8511 .08630 682.8 .000551

1 6 C • .831 2 .08279 649.1 .000529 160. . 8392 .08424 662.4 . 000542

165. .7996 .07778 600.9 .000505 165. . 8088 .07930 614.6 .000519

170. .7669 .07307 556 .6 .000483 170. . 7773 .07466 570.8 . 000498

176. .7330 .06870 516.0 .000465 175 . . 7450 .07034 530.7 .000460

180. .6983 .06471 478.9 .000451 1 80 . . 7119 .06637 494.1 . 000466

185. . 6631 .06110 4 4 5.4 .000442 185. . 6784 .06277 460.9 . 000457

190. .6278 .05788 415.4 .000440 190. . 6448 .05955 431.0 . 000453

195. . 5932 .05503 389.0 .000444 195 . .6117 .05668 404.5 .000455

200. .5599 .05251 366.2 .000455 200. . 5796 .05414 381.4 . 000463

210. . 4995 .04829 330.7 .000495 210. . 5204 .04989 344.6 . 000497

220. . 4488 .0450] 306.3 .000553 220. . 4696 .04655 316.6 .000548

230. .4073 .04254 290.1 .000623 230. . 4272 .04398 300.8 . 000611

240. . 3734 .04074 279.5 . 000699 240. . 3922 .04206 288.8 . 000682

250. .3455 .03947 27? .7 .000779 250. . 3631 .04067 280.8 .000756

260 . .3222 .03861 268.5 .000862 260. . 3386 .03969 275.6 .000834

270. . 3073 .03806 266.2 .000946 270. .3178 .03903 272.5 .000913

280. .2853 .03773 265 .1 .001031 280. . 2998 .03861 270.9 . 000993

290. .2704 .03757 265.1 .001117 290. . 2842 .03837 270.3 . 001074

300. .2573 .03754 2 6 5.8 .001203 300. . 2704 .03827 270.6 . 001156

310. .24*6 .03767 267.1 .00129? 310. . 25 81 .03834 271.5 . 001241

320. .2352 .03805 268.8 .001 388 320. . ?4 70 .03868 272.9 .001332

* Two p hase Boundary
Table 5. Transport Properties of Oxygen* Isobars# SI Units

? 1 • 0 MPa Isobar 22.0 MPa Isobar

Temp. Oens 1 t y The r ma

1

C on d • Viscosity

m | c roTh e r m a 1 Diftusivltv

Temp. Density Thermal

C on d

.

Viscosity

microT he r m a 1 D i f fusi v i ty

K g/cm**3 W/m.K a/cm.s cm**2 /s K g / cm** 3 W/m.K g /c m .

s

cm**2 /

S

56.738 1.3193 •20863 5475.9 .000957 * 56.845 1.3199 .20007 5503.8 .000958

5 8. 1.3160 • 2 C6 4 6 5303 .5 .000952 58 . 1.3151 .20690 5344.9 . 000953

60. 1 . 3058 .20321 5037.7 .000944 60. 1 . 3068 .20365 5076.5 . 000946

6 2. 1 .2976 .20012 4781 .6 .000938 *2. 1 .2987 .20057 4817.0 .000939

66. 1.2896 .19718 4536.2 .000931 64 . 1.2905 .19763 4570.3 .000933

66. 1.281? .1 9435 4302.5 .000925 66. 1. 2824 .19482 4334.6 . 000927

68. 1.2731 .19162 4080 .7 .000920 68. 1 . 2743 .19210 4111.1 . 000922

70. 1.2669 .18898 3871.0 .000914 70. 1 . 2662 .1 8947 3 899.7 . 000917

72. 1.2568 . 1 P6<r0 3673.2 .000909 72 . 1.2580 .18690 3700.4 .000911

76. 1.2686 .18388 3486.9 .000904 74. 1.2499 .18439 3512.9 . 000906

76. 1 .2606 .1 8141 3311 .8 .000899 76. 1.2418 .18193 3336.5 .00090 I 7 P • 1 .2322 .17897 3147 .4 .000893 78. 1.2336 .17950 3171.0 .000896

80. 1.2260 .17656 2993.1 .000888 00. 1 . 2255 .17711 301 5.7 . 000891

82. 1.2158 .17417 2848.4 .000883 82. 1.2173 .17473 2870.0 .000086

86. 1.2075 .17180 2712.7 .000877 04 . 1.2091 .17238 2733.4 .000880

86 . 1 .1993 .16944 2585 .4 .000872 86. 1 . 2008 .17004 2 60 5.

3

. 000875

88. 1.1909 .16709 2466.0 .000866 88. 1 .1926 .1 6770 2485.2 . 000869

90. 1.1826 .16475 2354.0 .000860 90. 1.1843 .16538 2372.5 .00086 3 92. 1.1762 .16241 224 8.8 .000854 92 . 1 . 1760 .16305 2266.7 . 000857

96. 1.1658 .16008 2150.1 .000848 94. 1 . 1676 .16073 2167.3 . 000851

96. 1.1573 .15774 2057.3 .000841 96 . 1. 1592 .15041 2074.0 . 000845

98. 1.1688 .15541 ] 970.0 .000035 90. 1. 1508 .15609 1986.2 . 000839

100. 1 .1603 .15307 1887.9 .000828 100. 1 .1423 . 1 5377 1903.6 . 000032

102. 1.1317 .1507? 1810.5 .000821 102. 1.1338 .15145 1825.8 . 000025

1C6. 1.1231 .14839 1737.

6

.000813 104 . 1.1253 .14913 1752.5 .000818

106. 1.1166 .14605 1668.8 .000806 106 . 1 .1166 .14680 1683.3 . 000810

108. 1.1057 .14370 1603.8 .000798 108 . 1. 1080 .14448 1618.0 . 000803 no. 1 .0969 .14136 1542.4 .000790 110. 1 . 0993 .14215 1556.3 .000795

112. 1.0880 .13901 1484.3 .000782 112. 1.0905 .13902 1497.9 .000787

116. 1.0791 .13666 1429.3 .000774 114. 1.0817 .13749 1442.6 . 000779

116. 1.0701 .13432 1377.1 .000765 116. 1.0728 .13517 1390.3 . 000771

IIP. 1.0610 .13197 1327.6 .000756 110. 1 .0630 .13204 134C.6 . 000762

120. 1.0519 .12963 1280.6 .000747 120 . 1.0548 .13052 1293.3 . 000753

122. 1.0627 .12729 1235.9 .000738 1 22. 1.0457 .12820 1248.5 . 000745

126. 1.0336 .12495 1193.3 .000729 124. 1.0365 .12589 1205.8 .000735

126. 1.0260 .12263 1152.8 .000720 126. 1 . 0273 .12358 1165.1 .000726

12 P

.

1.0165 .12030 1114.2 .000710 128. 1.0179 .12128 1126.4 . 000717

130. 1.0069 .11799 1077.3 .000700 130. 1 . 0085 .11899 1089.4 .000707

132. .9953 .11568 1042.0 .000690 132 . . 9990 .11671 1054 .

1

. 000698

136. .9855 .11339 1008.3 .000680 134. . 9893 .11444 1020.3 . 000688

136. .9756 .11111 976.1 . 00067C 1 36 o . 9796 .11219 988.0 . 000678

138. .9656 .10884 945.2 .000660 138. . 9698 .10995 957.1 .000669

160. .9556 .10659 91 5.5 .000650 140 . . 9598 .10772 92 7.5 . 000659

162. .9652 .10437 88 7.1 .000640 142. . 9498 .10552 099.0 . 000649

166. .9368 .10216 859.8 .000630 144. . 9396 .10334 871.7 .000639

166. .9263 .09999 833 .6 .000620 146 . . 9293 .10119 845.5 .000629

16 8. .9136 .09785 808.3 .000610 148. . 9189 .09908 820.3 .000620

150. .9028 . 09575 784.1 . 000600 150. . 9084 .09700 796.1 .000611

152. .8919 .09372 760.7 .000591 152. . 8977 .09499 772.8 . 000601

156. .8808 .09170 738.1 .000582 154. . 8869 .09306 750.3 . 000593

156. .8696 .08974 716.4 .000573 156. . 8760 .09104 728.7 .000584

158. . 85 82 . 08767 695.5 .000563 158. . 8650 .08900 707.8 .000574

160. .8667 .08565 675.3 .000554 160 . . 8538 .08701 687.7 .000565

165. .8173 .08078 627.8 .000532 165. . 8254 .08220 640.5 . 000544

170. .7871 .07619 584.4 .000512 170. .7961 .07767 597.4 .000525

175. .7560 .07191 544 .6 .000495 175 . . 7663 .07343 557.9 .000508

180. .7266 .06797 508.4 .000481 180. . 7358 .06952 522.0 . 000495

185. .6923 .06439 475.4 .000471 195. . 7051 .06594 489.3 . 000485

190. .6602 .06115 445.8 .000466 190. . 6743 .06271 459.7 .000479

195. .6285 .05827 419.2 .000467 195. . 6438 .05981 433.2 .000478

200. .5975 .05571 395.9 .000472 200. . 6139 .05722 409.7 .000482

210. .5397 .0514] 358.1 .000500 210. . 5575 .05288 371.1 .000505

220. .6891 .04803 330.6 .000545 220. . 5074 .04945 342.4 . 000545

230. .6662 .04538 311.4 .000603 230. . 4642 .04674 321.8 . 000597

260. .6102 .04336 298 .0 .000668 240. . 4276 .04463 307.3 .000657

250. .3801 .04186 288.9 .000737 250. . 3966 .04303 297.1 . 000722

260. .3567 .04077 282.9 .000810 260. . 3703 .04184 290.2 .000790

270. . 3329 . 04000 279.0 .000885 270. . 3477 .04098 285.5 . 000861

28 C , .3161 .03949 276.7 .000961 280. . 3282 .04038 282.6 .000932

290. .2977 .03917 275 .6 .001038 2 90 . . 3110 .03998 281.0 . 001005

300. . 2832 .03900 275.4 .001115 300. . 2959 .03974 280.4 .001079

310. .2703 .03902 275.9 .001195 310. . 2824 .03970 280.5 .001155

320. .2588 .03931 277.0 .001283 320. . 2704 .03996 281.2 .001239

* Two Phase Boundary

37
Table 5. Transport Properties of Oxyq en» Isobars# SI Units. 23.0 MPa Isobar 24. 0 MPa Isobar

Temp. 0 en s 1 t y Therma

Viscosity Thermal Temp, Density Thermal Viscosity Therma

C ond . micro- Dlffuslvlty C on d

micro- D 1 f f us 1 v 1 ty

K a/cm’M‘3 W/m.K g/cu.s cip**2/s K g / cm* * 3 W/m.K g /cm .

cm**2 /

56.456 1.3205 .20411 5531.6 .000959 * 57.067 1.3211 .20935 5559.3 . 000960

5 P1.3161 .20734 5386.5 .000955 58 . 1.3172 .20777 5428.3 . 000956

60. 1.3074 .20404 5115.3 . 000947 60. 1 . 3090 .20453 5154.2 . 000949

62. 1.2448 .20102 4854.2 .000941 62. 1 . 3009 .20146 4 890.6 .000943

64. 1 .2416 .14804 4604 .5 .000935 64. 1 . 2928 .19864 4638.7 . 000937

66. 1.2835 .14528 ‘4 3 66.8 .000929 66. 1 . 2847 .19574 4399.0 . 000931

68. 1 .2755 .14258 4141.5 .000924 68. 1 . 2766 .19305 4171.9 .000926

70. 1.2674 . ie445 3428.5 .000914 70 . 1 . 2686 .1 9043 3957.3 .00092

72. 1 .2543 .18740 3727.7 .000914 72. 1 . 2606 .18789 3755.0 . 000916

74. 1.2512 .18440 3538.8 .000909 74 . 1 . 2525 .18541 3564.7 . 000911

76. 1.2431 .18245 3361.3 .000904 76. 1 . 2445 .1 8297 3386.0 . 000906

78. 1.2350 .18004 3144 .6 .000849 78. 1 . 2364 .10057 3218.1 .000901

00. 1.2264 .17766 3038.2 .000893 80 . 1.2283 .17820 3060.7 .000896

82. 1.2188 .17530 2841.6 .oooepp 82. 1 . 2202 .17585 2913 .

.000891

84 . 1.2106 .17245 2754.1 .000883 84 . 1.2121 .17353 2774.7 . 000086

86. 1 . 2024 .17063 2625.2 .000878 86. 1 .2040 .17121 2645.0 .000881

PP. 1 .1442 .16831 2504.3 .000872 88 . 1 .1958 .16891 2523.4 .000075

40. 1.1860 .1 6600 2340 .4 .000P67 90. 1. 1876 .16661 2409.3 . 000070

42. 1.1777 .16364 2284.4 .000861 92. 1 . 1794 .16432 2302.2 . 000864

44. 1.1644 .16138 2184.5 .000855 44 . 1 . 1712 .16203 2201.7 . 000858

46. 1.1611 .15408 2040.6 .000849 96. 1 . 1629 .1 5974 2107.2 . 000852

4P . 1.1527 .15678 2002 .3 .000842 98 . 1 . 1546 .15745 2018.4 . 000846

100. 1 .1443 .15447 1914.3 .000836 100. 1. 1463 .15517 1934.9 . 000840

102. 1.1354 .15217 1841.0 . 0 CC 82 9 102. 1.1379 .15288 1856.2 .000833

104. 1.1274 .14486 1767.3 .000822 104 . 1.1295 .15059 1782.1 .000826

106. 1.1184 .14755 1697.8 .000815 106. 1.1210 .14030 1712.2 .000819

108. 1.1103 .14524 1632.2 .000808 108. 1.1125 .14600 1646.2 . 000012

11C. 1.1017 .14243 1570.1 .000*00 110. 1. 1040 .14371 1583.9 . 0008 C 5 112. 1.0430 .14062 1 51 1 .5 .000792 112. 1 . 0954 .14142 1 524.9 . 000797

114. 1.0842 .13832 1455.4 .000784 114 . 1.0867 .13913 1469.1 . 000709

116. 1 .0754 .13601 1403.3 .000776 116. 1.0780 .13684 1416.3 .000781

IIP. 1.0666 .13370 1353.4 .000768 118. 1 . 0693 .13455 1366.1 .000773

120. 1 .0577 .13140 1306.0 .000759 120. o

vC o .13227 1318.5 . 000765

122. 1 .0487 .12410 1261.0 . 000751 122. 1.0516 .12999 1273.3 .000756

124. 1 .0346 .12681 1218.1 .000742 124 . 1. 0426 .12772 1230.3 . 000748

126. 1 .0305 .12452 1177.3 .000733 126. 1 . 0336 .12545 1189.4 . 000739

128. 1.0213 .12225 1138.5 .000724 128. 1.0245 .12319 1150.6 .000730

130. 1.0120 .11448 1101.4 .000714 130. 1.0154 .12095 1113.2 . 000721

132. 1.0026 .11772 1064 ,o .000705 132. 1 . 0061 .11871 1077.7 .000712

134. . 4431 .11547 1032.1 . 000696 134. . 9968 .11649 1043.8 .000703

136. .4836 .11324 444.8 .000686 136. . 9874 .11428 1011.4 . 000694

138. .4734 .11102 468.8 . 000677 138 . . 9779 • 1 1 2 0 P 9 Q 0 • 3 .000685

140 . .4641 .10fl«3 939.1 .000667 140. . 9683 .10990 950.6 . 000675

142. .4543 .10665 910.7 .000658 142 . . 95 86 .10775 92 2.2 .000666

144 . .44^3 .10444 883.4 .000648 144 . .0488 .10562 894 .

. 000657

146. .4342 .10237 857 .2 .000639 146. . 9390 .10351 860 .. 000640

148. .4240 .10027 832.0 . 000629 148 . . 9290 .10144 84 3.5 . 000639

15C. .4138 .04822 807.8 .000620 150. . 91 89 .09941 819.3 .000630

152. .4033 .04623 784 .5 .000612 152. . 9087 .09743 796.0 .000621

154. .8428 .04431 762.1 .000603 154. . 8985 .09552 77 3.6 .000613

156. . 8822 .04231 740.5 .000504 156. . 8881 .09355 752.1 • 0006 Oh 158. .8714 .04030 719.8 .000585 158 . . 8776 .09156 731.4 . 000596

160. .8606 .08833 699.7 .000577 160. . 8670 .00962 711.4 . 000587

165. . 8324 .08358 652 .7 .000556 165 . . P401 .08492 664.6 . 000567

17C. .8047 .07410 6CQ .8 .000537 170. . 81 2 7 .08040 62 1.

. 000549

175. .775 8 .07440 570.7 .000521 175 . . 7 3 4 0 .07633 58 2.9 . 000533

180. . 7465 .07102 534.9 .000508 180. . 7564 .07246 547.3 . 000520

185. .7164 .06745 502 .4 .000498 185. . 7279 .06891 514.9 . 000510

140. .6873 .06421 472 .9 .000491 190 . . 6993 .06567 485.6 . 000503

145 . . 6578 .061 30 4 4 6,8 .000489 195. . 6709 .06274 459.1 . 000500

200. .6240 .05864 422.8 .000492 200. . 6429 .06012 43 5.4 . 000502

2 1 C

. 5740 .05430 383.6 .000511 210. . 5894 .05568 395.6 . 000517

220. .5245 .05C«2 354 .0 .000546 220. . 5406 .05214 365.2 . 000548

230. .4813 . C48C5 332 .2 .000593 230. . 4975 .04932 34 2.4 .000591

2 4 C

.444 2 .04587 316.5 . 0 00 64 P 240. . 4602 .0*708 325.7 . 000642

250. .4126 . 0441305.4 .000709 250 . . 4280 .04531 313.6 . 000699

260. . 38 55 .04240 297.5 .000773 260. . 4003 .04395 304 .

. 000759

270. .3672 .04145 292.2 .000840 270. . 3763 .04292 298.0 . 000022

2 PC . .3414 .04127 288.6 .000908 2 80 . . 3553 .04216 294 .

.000087

240 . . 3241 .04080 286.5 .000977 290. . 3369 .04161 292.0 . 000952

300. .30«4 . C4044 285 .4 .001047 300. . 3207 .04124 290.5 . 00101

3 1 C . .2444 .04034 2P5 .1 .001120 310. . 3061 .04108 289.8 .001089

320. .2818 . 04 06 C 285.5 .001200 320 . . 2930 .04125 289.9 .001165

* Two Phase Boundary
Table 5. Transport Properties of Oxvgen* Isobars* SI Units.

25.0 M Pa Isobar 26.0 MPa Isobar

T em o • Dp o s I tv Thermal Viscosity Th e r m a 1 Temp , Oe ns 1 1 y Thermal Viscosity Therma

1

C on rl

.

micro- 0 1 f f us 1 v 1 t y C on d

.

micro- D 1 f fusl v Ity

K g/ C m**3 W-n.K o/cm ,s /

s

K g/ cm**3 W/m.K g/cm.s c w + + 2 / s

57.178 1.3218 .20959 5586 .8 .000060 * 57.2 88 1.3222 .20983 5614.1 .000961

5

0 • 1.3133 .20820 5470.1 .000057 58. 1.3193 .20863 5512 .

1

.000959

*0. 1.3101 . 20497 5103.7 .000050 60. 1.3111 .20540 5232.3 .000952

f- ?

.

1 .3020 •20191 4977.1 .000044 62 . 1.3030 .20235 4 96 3.7 .000946

64. 1 . 2939 . 19899 4677.9 .000038 64. 1 . 2950 . 19944 4707.3 .000940

6 fc

.

I .2888 .19620 4431.3 .000033 66 . 1.2870 .19666 4463.6 .000935

68. 1.2778 .1935? 4707.3 . 000O?fi 68 . 1.2790 .19398 4232.8 . 000930

70. 1 .2608 .19091 3986 .1 .000023 70. 1.2710 .19139 4014.9 . 000925

72. 1.2618 . 1 8 83 8 3787.4 . 000018 72 . 1.2631 .1 8887 3 80 9.7 .000920

74 . 1.2538 .18591 3590.7 .000013 74 . 1.2551 .1 8641 3616.7 .000915

76. 1.2458 .18349 3410.7 .000008 76 . 1.2471 .1 8400 3435.4 .000911

78. 1.2378 .18110 3241.7 .000004 78 . 1.2391 .18162 3265.2 .000906

80. 1 .2297 .17874 3083.2 .000800 80. 1.2311 .17928 3105.7 .000901

82. 1 .2217 .17641 7934.7 .000804 82 . 1.2231 .17696 2 95 6.2 .000896

84. 1.2136 .17409 7795.4 .000880 84. 1.2151 .17466 2816.0 .000892

86. 1.2055 .17180 7664.8 .000884 86 . 1.2071 .17237 2684.6 .000887

88. 1 .1976 .16951 2547.4 .000878 88. 1.1990 .17010 2561.4 .000881

90. 1.1893 .16722 2427 .6 .000873 90 . 1.1909 .16783 2445.9 . 000876

92. 1.1811 .16495 2319.9 .000867 92. 1.1828 .16557 2337.5 . 000871

94. 1.1730 .16267 271

8

. 7 .00086? 94. 1.1747 .16331 2235.8 .000865

96. 1.1647 .16040 2123.7 .000856 96 . 1.1665 .16105 2140.2 . 000859

98 . 1 .1565 .15813 2034.4 .000850 98. 1.1584 .15879 2050.4 . 000853

100. 1.148? .15585 1950.4 .000844 100. 1.1501 .15653 1965.9 . 000847

102. 1 .1 309 .15358 1871.3 .000837 102. 1.1419 .15428 1886.4 .000841

104 . 1 .1316 .15131 1796.8 .000830 104. 1 .1336 .15202 1811.4 .000835

106. 1.1232 .14903 1726.5 .000824 106. 1.1253 .14976 1740.8 . 000828

108. 1.1148 . 14675 1660.2 .000817 108. 1 .1169 .14750 1674.1 .000821

110. 1.1063 . 14448 1597 .5 • 000 809 110. 1 . 1086 .14524 1611.1 .000814

112. 1.0978 .14220 1538.3 .000802 112. 1.1001 .14298 1551.6 .000807

114. 1.0892 .13993 1482 .2 .000794 114 . 1 . 0916 .14072 1495.2 .000799

116. 1.0806 .13766 1429.1 .000787 116. 1.0831 .13647 1441.9 .000792

118. 1 .0719 .13539 1378.8 .000779 118. 1.0745 .13622 1391.3 .000784

120. 1.063? .13313 1331.0 .000771 120. 1.0659 .1 3397 1343.3 .000776

122. 1.0544 .13087 1285.6 .000762 122. 1.0572 .13173 1297.7 .000768

124. 1.0456 .12861 1242 .4 .000754 124 . 1.0485 .12949 1254.3 .000760

126. 1.0367 .12637 1201.3 .000745 126. 1.0397 .12727 1213.1 .000751

128. 1 .0277 .12413 1162.2 .000737 128. 1.0308 .12505 1173.8 .000743

130. 1.0187 .12190 1124.9 .000728 130. 1.0219 .12284 1136.4 .000734

132. 1 .0096 .11968 1089.3 .000719 132. 1.0129 .12064 1100.7 .000726

134. 1.0004 . 11748 1055.3 .000710 134 . 1.0039 .11846 1066.6 .000717

13^. .9911 .11529 1022.8 .000701 136. . 9947 .11629 1034.0 .000708

138. .981 8 .11312 991 .7 .000692 138. . 9855 .11414 1002.9 .000700

140. .97 2 3 .11096 961.9 .000683 140. . 9763 .11200 97 3.1 .000691

142. .9628 .10883 933.4 .000674 142. .9669 .10989 944.5 .000682

144 . .9532 .10672 906.1 .000665 144 . . 9575 .10780 917.1 .000673

146. .9435 .10464 879.9 .000656 146. . 9480 .10573 890.9 .000665

148. .9338 .10258 854 .7 .000647 148. . 9384 .10370 865.7 .000656

1 5 C

.

.9239 .10067 830.5 .000639 150. . 9287 .10170 841.5 .000648

152. .9139 .09861 807.3 .000630 152. . 9189 .09976 818.2 .000639

154. .9039 .09671 784.9 .000623 154. . 9091 .09787 795.9 .000632

156. .8937 . 09476 76 3.4 .000614 156. . 8992 .09594 774.4 .000624

158. . 8835 .09279 742.7 .000606 158. . 8891 .09400 753.7 .000615

160. . 8732 .09087 722.7 .000597 160. . 8791 .09209 733.8 .000607

165. .8470 .08623 676 .0 .000578 165. . 8535 .08750 687.2 .000588

170. .8203 .08184 633.5 .000560 170. . 8275 .08315 644.7 .000571

175. .7932 .07771 594.6 .000545 175. . 8012 .07905 606.0 .000556

180. .7657 .07387 559.2 .000532 180. .7745 .07524 570.7 . 000543

185. .7381 .07033 527.0 .000522 185. .7477 .07171 53 8.5 .000533

190. .7104 .06709 497 .7 .000515 190. . 7209 .06847 509.3 .000526

198 . .6829 .06415 471.2 .000511 195. . 6942 .06552 482.8 .000522

200. .6558 .06151 447.4 .000512 200. .6679 .06286 459.0 .000521

210. .6037 .05702 407.3 .000524 210. .6171 .05833 418.5 .000531

220. . 5558 .05343 376.1 .000551 220. . 5700 .05469 386.6 .000555

230. .5129 .05056 352 .4 .000590 230. .5275 .05176 362.2 .000590

240. .4754 .04826 334.7 .000637 240. . 4900 .04941 343.7 .000634

250. .4428 .04643 321.7 .000690 250. . 4571 .04752 329.9 .000684

260. .4146 .04499 312.3 .000747 260. .4284 .04601 319.6 .000737

270. .3900 .04388 305.5 .000807 270. .4033 .04484 312.2 .000794

280. .3685 .04305 300.8 .000868 2 80. . 3813 .04393 306.9 .000852

290. . 3495 .04243 297.6 .000931 290. . 3618 .04325 303.2 .000912

300. .3327 .04199 295 .6 .000994 300. .3445 .04274 300.7 .000972

310. .3176 .04177 294.5 .001061 310. . 3290 .04247 299.3 .001035

320. .3041 .04190 294.3 .001134 320. . 3150 .04255 298.7 .001106

* Two Phase Boundary
Table 5. Transport Properties of Oxygen# Isobars* SI Units

27 ,C ^Pa Isobar

Temp . Dens 1 ty The r maViscosity Thermal

C on rl

micro- Dlffuslvlty

K g / cm + « 3 W/m.K o/cm.s cm**2/s

57.390 1.3228 .21007 5641 .2 .000962

50. 1.3203 .20706 5554.2 .000960

6 C . 1.7122 .20583 5271.5 .000953

6?. 1.3041 .20277 5000.3 .000947

64. 1.2761 .17787 4 7 41 .6 .000942

6 6. 1.2801 .17712 4 4 Q 5 .9 .000936

68. 1.2802 .17445 4263 .3 .000932

70. 1.2722 .17187 4043.8 .000927

72. 1.2643 .18736 3837.0 .000922

74. 1.2564 .1 8671 3*42.6 .00091

76. 1 .24 04 .18451 3460 .0 .000913

78. 1.2405 .10215 3288.8 .000908

80. 1.2725 . 17781 3128.2 .000904

82. 1.2246 .17751 2977.7 .000899

84, 1.2166 .17522 2836.6 .000894

86. 1.2086 .17275 2704.4 .000889

88 . 1.2006 .17067 2580 .4 .000884

70. 1.1725 .16843 2464.2 .000879

72. 1.1845 .16618 2355 .2 .000874

74. 1.1764 .16374 2262.8 .000868

76. 1 .1683 .16170 2156.7 .000863

70. 1.1602 .15745 2066.3 .000857

100. 1.1520 .15721 1981 .3 .000851

102. 1.1437 .15477 1901.4 .000845

104. 1.1356 .15272 1826.0 .000839

106. 1.1274 . 15048 1755.0 .000832

108. 1.1171 .14824 1687.9 .000825

110. 1.1108 .14577 1 624 .6 .000818

112. 1.1024 .14375 1564.8 .000811

114. 1 .0740 .14151 1508.2 .000804

116. 1.0856 .13727 1454.5 .000797

118. 1.0771 .13704 1403.7 .000789

120. 1.0686 .13481 1355.5 .000781

122. 1.0600 .13258 1309.7 .000773

124. 1.0513 .13036 1266.2 .000765

126. 1.0426 .12015 1224.8 .000757

128. 1.0737 .12575 1185.4 .000749

130. 1.0251 .12376 1147.8 .000741

132. 1.0162 .12157 1112.0 .000732

134. 1 .0073 .11742 1077.8 .000724

136. .7783 .11727 1045.1 .000715

138. .7872 .11514 1013.9 .000707

140. .7801 .11302 984 .0 .000698

142. .7707 .11073 955.4 .000690

144. .7616 .10005 928.0 .000681

146. .7522 .10601 901.7 .000673

148. .7428 .10477 876.5 .000664

150. .7333 .10282 852 .3 .000656

152. .7238 .10080 829.0 .000648

154. .7141 .07701 806.6 .000641

156. .7044 .07707 785.2 .000633

158. .8746 .07517 764.5 .000625

160. . 8847 .07328 744.6 .000617

165. .8578 .0e873 698.0 .000598

170. .8344 .08442 655 .6 .000582

175. .8087 . 08036 617.0 .000567

180. .7828 .07657 581.7 .000554

185. .7568 .07305 54 9.6 .000544

170. . 7307 .06781 520.5 .000536

175. .7040 . 06686 494.0 .000532

200. .6772 .06417 470.1 .000531

210. .6277 .05761 429.3 .000539

220. . 5834 .05572 396.9 .000560

230. .5414 .05274 371.7 .000597

240. .5037 .05053 352 .5 .00063?

250. . 4708 .04858 337.9 .000679

260. .4418 .04702 377.0 .000779

270. .4163 .04078 318.9 .000783

280. .3730 .04481 313.0 .000838

270. .3738 . 04406 308.8 .000895

3CC. .3 R 60 .04350 305.9 .000953

310. .3401 .04317 304.1 .001013

320. . 3 257 .04321 303.7 .001081

28.0 MPa Isobar

Temp , Density Thermal V 1 sco s 1 ty Therma

C ond • micro- Dlffuslvlty

K q / cm **3 W/m.K g/cm.s cm**2/

57.509 1.3238 .21031 5668.2 • 000963

58. 1.3210 .20969 5596.0 .000961

60. 1.3133 .20627 5310.8 .000955

62. 1 . 3052 .20323 5037.1 . 000949

64 . 1.2972 .20030 0776.1 . 000943

66. 1.2892 .19757 0528.3 .000938

68 . 1.2813 .19091 0293.9 .000933

70. 1 . 2730 .19230 0072.7 .000929

72. 1.2655 .18980 3860.0 .000924

74 . 1.2576 .18701 3668.6 .000920

76. 1 . 2097 .18502 3080.7 .000915

78. 1.2018 .1 8267 3312.3 .000911

80. 1 . 2339 .18035 3150.6 .000906

82 . 1.2260 .17805 2999.1 .000902

84. 1.2180 .17578 2 857.2 .000097

86. 1.2101 .17352 2720.1 .000892

88. 1.2021 .17127 2599.0 .000887

90. 1.1901 . 16903 2082.0 .000882

92 . 1 . 1861 .16680 2372.7 .000877

94. 1 . 1781 .16057 2269.8 .000872

96 . 1.1701 .16230 2173.1 . 000866

98 . 1.1620 .16011 2082.2 .000861

100. 1.1539 .15788 1996.7 .000855

102 . 1.1058 .15565 1916.3 .000849

ltf4. 1.1376 .15302 1800.5 .000842

106. 1 . 1295 .15120 1769.1 .000836

108. 1.1212 .10897 1701.7 .000830

110. 1.1130 .10670 1638.1 . 000823

112. 1.1007 .10051 1577.9 .000816

114. 1.0960 .10229 1521.0 .000809

116. 1.0880 .10006 1067.1 .000801

118. 1.0796 .13785 1016.

.000794

120. 1.0712 .13563 1367.6 .000786

122. 1.0627 .13302 1321.6 .000779

124. 1.0561 .13122 1277.9 .000771

126. 1.0055 .12903 1236.0 . 000763

128. 1.0369 .12685 1196.8 .000755

130. 1.0282 .12067 1159.1 .000747

132. 1.0190 .12251 1123.2 .000739

134. 1.0106 .12037 1088.9 .000730

136. 1 . 0017 .11823 1056.1 .000722

138. . 9928 .11612 1020.8 .000714

140. . 9838 .11002 990.8 .000705

14 2. . 9797 .11195 966.1 . 000697

144 . . 9656 .10989 938.7 .000689

146. . 9560 .10786 912.3 .000680

148. .9071 .10587 887.1 .000672

150 . . 9378 .10390 862.8 .000664

152. . 9280 .10198 839.6 .000657

154. . 9190 .10012 817.2 .000649

156. . 9090 .09822 795.7 .000641

158. . 8998 .09632 775.0 .000634

160. . 8902 .09005 755.1 . 000626

165. . 0650 .08990 708.6 . 000608

170. . 8010 .08567 666.2 .000591

175. .8159 .08163 627.6 .000577

180. . 7907 .07786 592.0 .000564

185 . . 7653 .07036 560.0 .000554

190. . 7000 .07113 531.2 .000547

195. . 7108 .06817 500.8 . 000542

200. .6899 .06508 080.8 . 000540

210. .6015 .06086 039.7 . 000547

2 20. . 5961 .05712 006.9 .000565

230. . 5505 .05009 381.1 .000594

240 . . 5172 .05163 361.1 .000631

250. . 0800 .00960 305.8 . 000675

260. . 0507 .06802 330.2 .000723

270. . 0288 .00672 325.5 .000773

280. . 0059 .00568 319.1 . 000826

2 90 . . 3855 .000 87 310.0 .000880

300. . 3673 .00025 311.1 .000935

310. . 3510 .00387 30B.q . 000993

320. . 3362 .00387 307.7 .001058

+ Two Phase Boundary

40
Table 5. Transport Properties of Cxygen* Isobar s> ST Units

2 9.0 M Pa Isobar 30.0 MPa Isobar

Temp • Density Thp r i>a 1 C on d

.

Viscosity

microTh er ma 1 0 1 f f us 1 v 1 t y

T e n d . Dens 1 1 y THp r ma

1

C on d . ViscositymicroTherm?

1

Diffusivity

K g /cm** 3 W/m .K a / c m , s cm**? /s K g / cm * * 3 W/m.K g /cm .

s

c m**2 / s

57*619 1.3240 .21055 5695.0 .000963 * 57.729 1 . 3245 .21079 5721.6 . 000964

58 . 1.3224 .20991 563 8.7 .000962 58 . 1.3234 .21034 5681.2 .000963

6 r . 1.3143 .20670 5350.2 .000956 60 . 1.3153 .20713 5389.6 .000957

62 . 1.3063 .20366 5073.8 .000950 62 . 1 . 3073 .20410 5110.7 . 000952

6 A . 1 .2983 .20078 4810.6 .000945 64 . 1 . 2994 .20122 4845.1 . 000946

66 . 1 .2904 • 1

9

P 02 4560.7 .000940 66 . 1 . 2915 .19847 4593.2 . 000942

68 . 1 .2825 .19537 4324 .4 . 000935 68 . 1.2836 .19583 4355.0 . 000937

7 C . 1.2746 .19281 4101 .5 .000931 70 . 1.2758 .19328 4130.5 . 000933

72 . 1 .2667 . 1903-3 8391 . 7 .000926 77 . 1 . 2679 .19081 3919.1 .00092 8 76 . 1.2689 .18740 3694 .5 .000922 74 . 1.2601 .18839 3720.5 .000924

76 . 1 .2610 . 1855 ? 3509 .

4

.000918 76 . 1 . 2523 .18602 3534.1 .000920

78 . 1.2431 .18318 3335.8 .000913 78 . 1.2444 .18370 3359.3 . 000916

80 . I .2363 . 180 p P 3173.1 .000900 80 . 1 . 2366 .18140 3195.5 . 000911

82. 1 .2274 .17860 3020.6 .000904 82 . 1.2288 .17913 3042.0 . 000907

84 . 1.2195 .17633 2877.7 .000900 84 . 1 . 2209 .17689 2898.2 . 000902

86 . 1.2116 .17409 2743.8 .000895 86 . 1.2131 .17465 2763.5 . 0 C 0898

88 . 1 .2037 .17185 2618.3 .000890 80 . 1 . 2052 .17243 2637.2 .000893

<30 . 1 . 19*7 .16963 2500.6 .000885 90 . 1 . 1973 .17022 2518.8 . 000888

92 . 1 .1878 .16741 2390.3 .000880 92 . 1 . 1894 .16801 2407.8 . 000883

<34 . 1 .1790 . 1 651 C 2286.7 .000875 94 . 1 . 181 5 .16581 2303.6 . 000878

<36 . 1 .1718 .16297 2189.4 .000870 96 . 1 .1735 .16361 2205.

7

. 000873

<3 e . 1.1638 . 1607

6

7098 .0 .000864 98 . 1 . 1656 .16141 2113.8 . 000868

ICC. 1.1558 .15855 2012.1 .000858 100 . l .1576 .15921 2027.3 .000862

102 . 1.1477 .15633 1931 .2 .000852 102 . 1 . 1496 .15701 1946.0 . 000856

104 . 1 .1396 .15412 1855.0 .000846 104 . 1.1416 .15481 1 869.4 . 000850

106 . 1.1315 .15190 1783.2 .00 0 P 4 C 106 . 1.1335 .15261 1797.2 .000844

108 . 1.1233 .14969 171

5

.4 .000834 108 . 1 . 1254 .15041 1729.0 . 000838

110 . 1.1152 .14748 1651.4 .000027 no . 1 .1173 .14821 1664 .

7

.000331

112 . ] .1069 .14527 1591.0 .000820 112 . 1 . 1092 .14601 1604.0 . 000825

114 . 1 .0987 .14306 1533.8 .000813 114 . 1 .1010 .14382 1546.5 . 000818

116 . 1.0904 .14085 1479.6 .000806 116 . 1 . 0928 .14163 1492.1 .000811

118 . 1.0921 .13865 1428 .

3

. 000799 118 . 1. 0845 .13944 1440.5 .000804

1 20 . 1 .0787 .13645 1379.7 .000792 120 . 1.0762 .13726 1391.6 .000797

122 . 1 .0653 .13426 1333 .5 .000784 122 . 1 . 0679 .13508 1345.2 .000789

124 . 1.0569 .13207 1 289.6 .000776 124 . 1 . 0596 .13291 1301.1 . 000782

126 . 1 .0484 .12990 1247.8 .000769 126 . 1.0511 .13075 1259.2 .000774

128 . 1.0398 • 1 2 7 7 ? 1208.1 .000761 128 . 1.0427 .12860 1219.3 . 000766

130 . 1 .0312 .12557 1170.3 .000753 130 . 1.0342 .12646 1181.3 . 000759

132 . 1.0226 .12343 1134.2 .000745 132 . 1 . 0257 .12433 1145.1 .000751

134 . 1.0139 .12130 1099.8 .000737 134 . 1.0171 .12222 1110.6 .000743

136 . 1 . 005

1

.11918 1066.9 .000729 136 . 1 . 0084 .12012 1077.6 .000735

138 . .9963 .11709 1035.5 .000720 138 . . 9997 .11804 1046.1 . 000727

140 . .9874 .11501 1005.5 .000712 140 . , 9910 .11598 1016.0 .000719

142 . .9785 .11295 976.7 .000704 142 . . 9822 .11393 987.2 .000711

144 . .9695 .11091 949.2 .000696 144 . . 9733 .11191 959.6 . 000703

146 . .9605 .10890 922.8 .000688 146 . . 9644 .10992 933.1 . 000695

148 . .9513 . 1069 ? 897.5 .000680 148 . . 9554 .10795 907.8 . 000688

150 . .9422 .10497 873 .2 .000672 150 . . 9464 .10602 88 3.4 . 000680

152 . .9329 .10306 849.9 .000665 152 . . 9373 .10412 860.1 .000673

154 . .9237 .10121 827.5 .000657 154 . . 928 ? .10228 837.7 . 000665

156 . .9143 .09933 806.0 .000650 156 . . 9190 .10041 816.1 . 000658

158 . .9049 .09744 785.3 .000642 158 . . 9098 .09854 795.4 . 000651

160 . .8954 .09559 765.4 .000635 160 . . 9005 .09671 775.5 . 000643

16 K . .8715 .09112 718.9 .000617 165 . . 8770 .09228 729.0 . 000626

170 . .8473 .08688 676.5 .000601 170 . . 8533 .08807 686.6 . 000610

175 . .8228 .08288 638.0 .000587 175 . . 8294 .08409 648.1 . 000596

180 . . 798 ? .07912 602.8 .000574 180 . . 8053 .08036 612.9 .000584

185 . .7735 .07563 570.8 .000564 185 . . 7812 .07688 580.9 .000574

190 . .7488 .07241 541.7 .000557 190 . . 7571 .07366 551.8 . 000566

195 . . 724 ? .06945 515.2 .000552 195 . .7331 .07069 52 5.2 . 000561

200 . .6999 .06675 491.1 .000550 200 . . 7094 .06799 501.2 . 000559

210 . .6527 .06209 449.8 .000554 210 . . 6632 .06329 459.6 . 000562

220 . .6081 .05830 416.6 .000570 220 . .6195 .05946 426.0 .000576

230 . .5670 .05522 390.2 .000597 230 . . 5789 .05633 399.1 .000600

240 . .5299 .05272 369.6 .000632 240 . . 5420 .05378 377.9 .000632

250 . .4967 .05067 353.7 .000672 250 . . 5089 .05168 361.4 .000671

260 . .4672 .04900 341.4 .000717 260 . .4792 .04996 348.6 .000713

270 . .4410 .04764 332 .2 .000765 270 . . 4528 .04855 33 8.7 .000759

280 . .4177 .04655 325.2 .000816 280 . .4292 .04741 331.3 . 000807

290 . .3970 .04568 320.0 .000867 290 . .4082 .04649 325.7 . 000856

300 . .3784 .04500 316.3 .000920 300 . . 3892 .04576 321.6 . 000906

310 . .3617 .04457 313.8 .000975 310 . . 3722 .04527 318.6 . 000959

320 . . 3466 .04452 312.2 .001038 320 . . 3567 .04518 316.7 . 001019

* Two Phase Boundary

41
Table 5. Transport Properties of Oxygen* Isobars* SI Units. 35.0 HPa Isobar 40.0 MPa Isobar

Temp

Density Thermal V 1 scos 1 1 y Thermal Temp . Density Thermal Viscosity Thermal

C ond

micro- 0 1 f f i>s 1 v 1 t y C ond

micro- Dlffusivity

K g/cm*+3 W/m.K g/cm.s cm + *2 /s K g / cm* + 3 W/m.K g /cm.

c m**2 / s

58.276 1.3274 .21199 5852 .2 .000968 58.819 1.3302 .21318 5978.5 . 000971

60. 1.3205 .20925 5588.5 .000963 60. 1.3255 .21133 5789.8 .000969

62. 1.3126 .20625 5296.2 .000959 62. 1 . 3176 .20835 5483 .

.000965

64. 1. 3047 .20340 5018.7 .000954 64 . 1 . 3099 .20554 5193.7 .000961

66. 1.2969 .20069 4756.2 .000950 66. 1 . 3022 .20287 4920.3 .000957

68. 1.2892 .19810 4508.5 .000946 68. 1.2946 .20031 4662.7 .000954

70. 1.2815 .19559 4275.3 .000942 70. 1 . 2871 .19786 4420.7 . 000951

72. 1.2738 .19317 4056.1 .000938 72. 1 . 2795 .19548 4193.5 . 000947

74. 1 .2662 .19080 3850.4 .000934 74. 1.2720 .19316 398Q.5 . 000944

76. 1.2585 .18849 3657 .5 .000931 76. 1 . 2645 .19090 3780.9 . 00094 1 78. 1.2509 .18622 3476.8 .000927 78. 1.2570 .1 8869 3594.0 . 000938

80. 1.2432 .18399 3307.5 .000923 80. 1 . 2496 .18651 3419.2 . 000934

82. 1.2356 .18178 3148.9 .000919 82 . 1 . 2421 .1 8436 3255.5 .000931

84. 1.2279 .17959 3000.5 .000915 84. 1 . 2346 .18223 3102.3 .000927

86. 1.2203 .17742 2861.5 .000911 86. 1.2272 .18012 2958.9 .000924

88. 1.2126 .17527 2731 .2 .000907 88. 1.2197 .17802 2824.6 .000920

90. 1 .2049 .17312 2609.2 .000903 90. 1.2123 .17593 2698.8 . 000916

92. 1.1973 .17097 2494.7 .000898 92 . 1 . 2048 .17384 2580.9 .000912

94. 1.1896 .16883 2387.4 .000894 94 . 1.1973 .17177 2470.4 .000908

96. 1.1819 .16670 2286.6 .000889 96 . 1.1898 .16969 2366.6 . 000904

98. 1.1742 .16456 2192.0 .000884 98 . 1.1824 .16762 2269.2 . 000900

1 00. 1.1666 .16243 2103.0 .000879 100. 1 .1749 .16554 2177.6 .000895

10?. 1.1587 .16030 2019.3 .000874 102 . 1 . 1674 .16347 2091.6 .000891

104. 1.1510 .15817 1940.6 .000869 104. 1 . 1599 .16140 2010.5 . 000886

106. 1.1432 .15603 1 866.3 .000863 106. 1.1523 .15933 1934.2 . 000861

108. 1.1354 .15390 1796.3 .000857 108 . 1 . 1448 .15726 1862.3 . 000876

110. 1.1276 .15177 1730.3 .000852 110. 1.1373 .15519 1794.4 .000870

112. 1.1198 .14964 1667.9 .000846 112 . 1 . 1297 .15312 1730.4 .000865

114. 1.1119 .14752 1608.9 .000840 114. 1 .1222 .15106 1669.8 .000859

116. 1 .1041 . 14540 1553.1 .000833 116. 1.1146 .14900 1612.6 .000854

118. 1.0962 .14328 1500.3 . 000827 118. 1.1070 .14694 1558.4 . 000848

120. 1.0882 .14117 1450.2 .000820 120. 1 .0994 .14489 1507.0 .00084?

122. 1.0803 .13906 1402.7 .000814 122 . 1.0918 .14284 1458.3 .000836

124. 1.0723 .13696 1357.6 .000807 124. 1 . 0842 .14081 1412.1 . 000830

126. 1 .0643 .13487 1314.7 . 000800 126. 1.0765 .13878 1368.2 . 000824

128. 1.0563 .13279 1273.9 .000793 128. 1 . 0688 .13676 1326.5 .000816

1 30. 1.0483 .13073 1235.2 .000786 130. 1.0612 .13475 1286.8 . 000811

132. 1. 0402 .1 2867 1198.2 .000779 132. 1 . 0535 .13276 1249.1 . 000805

134. 1 .0321 . 1 2663 1163.0 .000772 134. 1.0457 .13078 1213.1 . 000798

136. 1 .0239 .12460 1129.4 .000765 136 . 1. 0380 .12861 1178.8 .000792

138. 1 .0157 .12260 1097.3 .000758 1 33. 1 .0302 .12696 1146.0 . 000785

1 4 C

1.0075 .12060 1066.7 .000751 140. 1.0224 .17493 1114.8 . GC07 7 9

14?. . 99Q3 .11863 1037.4 .000744 142. 1 . 0146 .12302 1084 .9 .000772

144. • 9 91 0 .11668 1009.4 .000736 144. 1 . 0068 . 12113 1056.4 . 000766

146. .9827 .11476 9 8 2.5 . CC072Q 146. . 9990 .11926 1029.1 . 000760

148. .97^3 . 11286 956.8 .000722 148. . 9911 .11741 1002 .

.000753

150. .9659 .11099 932 .2 . 0 C C 7 ] 5 150. . 9832 .11559 977.9 . 000747

152. .9575 .10915 908.6 .000709 152. . 9763 . 11381 953.9 . 000741

154. . 9 4 Q

.10736 885.9 .000702 154 . . 96 7 A .11205 930.9 . 000735

156. .9406 .10555 864.2 .000696 156 . . 9595 .11030 908.8 . 000729

158. .9321 .10375 843 .3 .000689 1 58 . . 9515 .10656 887.6 . 000723

160. .9235 .10199 823 .2 .000682 160. . 9436 .10684 36 7.. 000717

165. .9020 .09771 776.3 . 0 00 6

A 7 165. . 9236 .10269 819.8 . C0070 2 170. .8804 .09364 733.8 .000653 170 . . 9035 .09873 776.7 .000689

175. . 8 587 .08978 695.0 .000640 175. . 8835 .09496 73 7.5 . 0006 7 7 180. .8369 .08613 659.8 .000628 180. . 8634 .09136 701.8 . 000666

185. .8152 .08271 627.6 .000616 185 . . 8433 .08802 669.3 .000657

190. .7935 .07952 598.2 .000611 190. . 8234 .08486 639.6 .000649

195. .7719 .07656 571 .5 .000605 1 95 . . 8036 .08190 612.5 . 000643

2CC

.7505 .07382 547.1 .000601 200. . 7840 .07915 587.7 . 000638

210. .7087 .06899 504 .6 .000599 210. . 7455 .07424 544.2 . 000635

220. . 6687 .06496 469.5 .000607 220. . 7084 .07007 508.0 . 000637

230. .6308 .06162 440.7 .000622 230. . 6730 .06654 477.8 . 000647

240. .5956 .05884 4 3 7 .2 .000644 240 . . 6396 .06358 452.7 . 0006 6 3 250. . 563? .05653 398.2 .000672 250. . 6084 .06107 432.0 . 000693

260. .5335 .05459 3 82 .9 .000704 260. . 5794 .05895 414.9 . 0C0708

270. .5066 .05296 370.7 .000740 270. . 5526 .05714 400.9 . 000736

280. .4 821 .05159 361 .0 .000778 280. . 5780 .05558 389.4 . 000767

290. . 4599 .05044 353 .4 .000817 290 . . 5053 .05424 380.1 . 000799

300. .4397 .04948 347.4 .000858 300. . 4845 .05309 372.6 .000833

310. .4213 .04876 342.9 .000901 310. . 4653 .05218 366.6 .000868

320. . 4046 .04846 339 .

.000951 320. . 4477 .05167 361.8 . 000909

* Two Phase Boundary
Table 5. Transport Properties o f Oxygen* Isobars* SI Units* 45*0 MPa Isobar 50.0 MPa Isobar

Temp

.

Oen s 1 t y Thermal Cond

.

Viscosity

microThermal01 f f us 1 v 1 ty Temp . Oens 1 ty Ther ma

1

Cond. Viscosity microThermal Dlffuslvlty

K g/cm**3 W/m.K g/cm *s cm**? /s K g / cm**3 W/m.K q/cm.s cro**2 t s

59. 35* 1.3329 .21437 6100.4 .000975 * 59.894 1.3355 .21556 6218.1 . 000978

60. 1 .3303 .21338 5993 .5 .000974 60. 1.3351 .21550 6199.6 .000978

6? . 1.3226 .21043 5672.7 .000971 62 . 1 . 3374 .21256 5 86 3 .

7

.000976

64 . 1.3149 .20764 5370.2 .000967 64. 1.3199 .20970 5558.0 .000973

*6 # 1.3074 .20500 5085.4 .000964 66. 1.3125 .20709 5251.6 .000971

6 P

.

1 .2999 .20249 4817.7 .000962 68. 1.3050 .20561 5973.5 .000969

70. 1 .2 924 .20007 4566.6 .000959 70 . 1.2977 .20223 571 3.0 . 000967

12. 1.2850 .19773 4331.1 .000956 72. 1.2905 .19995 5569.2 . 000964

76 . 1.2777 .19547 4110.6 .000953 74. 1.2632 .19772 5251.0 .000962

7fc

.

1.2703 .19326 3904 .3 .000951 76 . 1.2759 .19556 5027.7 .000960

7P . 1.2630 .19109 3711.2 .000948 78. 1 . 2686 .19355 3828.3 .000957

PO . 1.2557 .18896 3530 .6 .000945 80. 1.2616 .19136 3651.8 . 000955

R? . 1 .2484 .1 8687 3361.7 .000942 82. 1.2555 .18931 3567.6 . 000952

8 4. 1.2411 .18479 3203.7 .000939 84. 1 . 2573 .18729 3305.6 .000950

86. 1.2338 .18273 3055.8 .000936 86. 1.2502 .18528 3152.3 . 000947

8 P . 1.2265 .18069 2917.4 .000933 88. 1 . 2331 .18329 3009.7 .000944

cr. 1.219? .17866 2787.8 .000929 90 . 1.2260 .18131 2876.2 .000941

92. 1.2120 .17663 2666.4 .000926 92. 1.2189 .17935 2751.2 . 000938

96. 1.2047 .17461 2552.5 .000922 94 . 1.2118 .17737 2635.0 .000935

96. 1.1974 .17259 2445.7 .000918 96 . 1.2057 .17550 2525.1 .000932

9«. 1 .1 901 .17057 2345.5 .000914 98 . 1 .1976 .17355 2521.0 .000928

100. 1.1829 .16855 2251 .3 .000910 100. 1. 1905 .17157 2325.1 .000925

10?. 1.1756 .16654 2162.8 .000906 102. 1.1835 .16951 2233.1 .000921

104. 1 .1683 .16452 2079.5 .000902 104 . 1 . 1763 .16755 2157.5 .000917

106. 1.1610 .16251 2001.0 .000897 106. 1. 1693 .16558 2066.9 .000913

10P. 1 .1537 .16049 1927.1 .000893 108. 1 . 1622 .16362 1990.9 .000909

110. 1.1464 .15848 1857.4 .000888 110. 1.1551 .16166 1919.3 .000905

11?. 1.1291 .15647 1791.6 .000883 112. 1.1560 .15970 1851.7 .000900

114. 1.1318 .15446 1729.4 .000878 114. 1 .1509 .15775 1787.9 . 000896

116 . 1.1245 .15245 1670.6 .000873 116. 1.1339 .15578 1727.6 .000891

IIP. 1.1172 .15045 1615.0 .000868 118. 1 .1268 .15383 1670.5 .000886

1?0. 1.1099 .1 4845 1562.3 .000862 120. 1.1197 .15188 1616.5 . 000881

1??. 1.1025 .14646 1512.4 .000857 122. 1.1126 .15995 1565.2 .000876

1 ? 4 . 1.0952 .14448 1465.1 .000851 124 . 1.1055 .15800 1516.7 .000871

126. 1 .0878 .14250 1420.1 .000846 126. 1.0985 .15607 1570.6 .000866

128. 1 .0805 . 14054 1377.4 .000840 128. 1.0913 .15515 1526.8 .000861

130. 1.0731 .1 3 85 8 1336.7 .000834 130 . 1 . 0852 .15225 1385.2 .000855

1 3?. 1 .0657 .13664 1298.1 .000828 132. 1.0771 .15035 1355.6 . 000850

134. 1.0583 .13471 1261.3 .000822 134. 1.0700 .13856 1307.9 . 000845

136. 1 .0509 . 1 32 °0 1 226.2 .000816 136. 1 .0629 .13659 1272.0 . 000839

13 8. 1.0435 . 1 3090 1192 .7 .000811 138. 1.0558 .13575 1237.8 . 000834

140. 1 .0361 .1290? 1160.8 .000805 140. 1 . 0587 .13290 1205.1 . 000828

147. 1 .0287 .12715 1130.

3

.000799 142. 1.0516 .13108 1173.9 .000823

144 . 1.0212 .12531 1101 .2 .000793 144 . 1.0355 .12927 1155.1 .000817

146. 1.0138 .12349 1073.3 .000787 146. 1.0275 . 12759 1115.7 . 000812

148. 1 .0063 .12169 1046.6 .000781 148. 1 . 0202 .12573 1088.5 .000806

15 0. .998 8 .11991 1021 .1 .000775 150. 1. 0131 .12399 1062.5 . 000801

152 . .9914 .11816 996.7 .000769 152. 1 . 0060 .12227 1037.5 . 000796

154. .9839 . 11644 973.2 . 000764 154 . . 9988 .12059 1013.5 .000790

156. .9764 .11473 950.7 . C 007 5 8 156. . OQ17 .11891 990.6 .000785

158. .96 89 .11303 929.2 .000753 158. . 9856 .11725 968.6 . 000780

160. .961 4 .11137 908 .

5

.000747 160. . 9775 .11562 957.5 .000775

165. .9426 .10731 860.2 .000734 165. . 9596 .11165 898.3 .000763

170. .9238 .10343 816.4 .000722 170. . 9518 .10785 853.7 .000751

175. .9050 .09974 776.7 .000710 175. . 9251 .10520 813.2 .000740

180. . 886? . 0962? 740.4 .000700 180. . 9065 .10075 776.5 . 000731

1P5. .8675 .09290 707.4 .000691 185. . seee .09756 752.8 .000722

1 9 C • . P4P9 .08977 677.2 .000684 190 . .8713 .09535 712.0 . 000714

195 . . 8305 .08603 649.6 .000677 195. . 8539 .09152 683.9 . 000708

? 00 . .8122 .08408 624 .4 .000672 200. . 8367 .08867 658.1 .000703

210. .7764 .0791

?

580.0 .000667 210. . 8030 .08367 612.8 .000696

2 20 . .7416 .07484, 542.7 .000667 220. . 7702 .07932 575.6 . 000695

230. .70R3 .07117 511 .4 .000673 230. . 73 87 .07555 552.2 . 000698

240

.

.6766 .06005 485.1 .0006P4 240. . 7085 .07228 515.8 . 000706

250 . .6467 .06537 463 .0 .000699 250. . 6798 .06956 591.6 . 000718

260. .6186 .06308 444,5 .000719 260. . 6526 .06702 572.0 .000733

270. .5923 .06110 429.1 .000741 270. .6271 .06589 555.5 .000751

280. .5679 .05939 416.2 .000766 2 80 . . 6031 .06303 551.5 .000771

2 90. . 5 453 .05789 405.6 .000793 290. . 5806 .06139 529.6 . 000793

300. .5242 .05658 396 .7 .000820 300. . 5596 .05995 519.7 .000816

310. .5047 .05551 3 8 9.4, .000850 310. . 5500 .05871 511.5 . 000841

320. .4 866 .05480 383 .5 .000885 320. . 5217 .05783 505.5 .000870

* Two Phase Boundary
Table 5. Transport Properties of Oxygen* Isobars* SI Units

55 *0 MPa Isobar 60.0 MPa Isobar

Tem o • Dens 1 1 y Ther maViscosity Thermal Temp • Density Thermal Viscosity Therma

C on d

w 1 c r o- Dlffuslvlty C ond

m 1 cr o- D 1 f f us 1 y 1 1 y

K g / cm* + 3 W/rr.K g/cm.s cm»«2/s K g/ cm**3 W/m.K g/cm.s cm**2/s

60.425 1.3381 .21675 6331.5 .000981 * 60.954 1. 3407 .21793 6440.8 • 00098 4 6?. 1.3321 .21446 6056.7 .000980 62. 1 . 3367 .21643 6251.5 • 000984

64. 1.3246 .21173 5727.3 .000979 64. 1.3793 .21372 5908.1 •000984

66. 1.3173 .20915 5418.0 .000977 66 . 1.3220 .21116 5587.2 .000983

68. 1 .3100 .70670 5130.1 .000975 68. 1.3148 .20875 5287.5 .000982

70. 1.3028 .20436 4860 .0 .000974 70. 1.3077 .20644 5007.6 .000981

7? . 1.2956 .20210 4607.5 .000972 72 . 1.3006 .20422 4746.3 .000979

74 . 1 .2 885 .19992 4371.6 .000970 74. 1.2936 .20208 4502.4 .000978

76. 1.2814 .19780 4151.2 .000968 76. 1.2867 .20000 4274.7 . 000977

78. 1.7743 .19573 3945.3 .000967 78. 1.2797 .19798 4062.2 .000975

00. 1.2673 .19370 3752.9 .000965 80 . 1.2728 .19599 3863.9 .000974

82. 1.2603 .19170 3573.2 .000963 82. 1.2660 .19404 3678.7 .000972

84. 1 .2533 .18973 3405.3 .000960 84. 1.2591 .19211 3505.7 .000970

86. 1.2463 .18777 3240.3 . 000958 86. 1.2523 .19020 3344.0 .000968

80. 1 .2394 .18583 3101.5 .000956 08. 1. 2455 .18830 3192.9 .000966

90. 1.2374 .18390 2964.1 .000953 90. 1.2387 .18642 3051.5 .000964

92. 1.2755 .18197 2835.4 .000950 92. 1.2319 .1 8454 2919.

.000962

94 . 1 .21«6 .18005 2714.9 .000948 94. 1. 2251 .18267 2795.2 .000960

96. 1.2116 .17814 2601.8 .000945 96. 1.2183 .1 8080 2679.0 .000957

go

1.2047 .17672 2495.8 .000942 98. 1.2116 .17894 2570.0 .000954

ICO. 1 .1 97 8 .17431 2396.2 . 000938 100. 1.2048 .17707 2467.6 .000951

102. 1.1909 .17240 2302.7 .000935 102. 1.1981 .17520 2371.5 .000949

104. 1.1840 . 1 7048 2214.7 .000932 104. 1.1914 .17333 2281.1 .000945

106. 1.1771 .16057 2131.8 .000928 106. 1.1847 .17146 2196.0 .000942

108. 1.1702 .16665 2053.8 .000924 108. 1.1779 .16959 2115.9 .000939

110. 1.1634 .16474 1980.3 .000920 110. 1.1712 .16772 2040.4 . 000935

117. 1.1565 .16282 1910.9 .000916 112. 1 . 1645 .16585 1969.2 .000931

114. 1.1496 .16091 1 845 .4 .000912 114 . 1.1579 .16398 1901.9 .000928

116. 1.1477 .15900 1783.4 .000908 116. 1.1512 .16211 1838.4 .000924

118. 1 .1359 .15709 1724.9 .000903 118. 1.1445 .16024 1778.3 .000920

120. 1 .12Q0 .15518 1669.4 .000899 120. 1.1378 .15838 172 1.4 .000916

172 . 1.1221 .15328 1616.9 .000894 122. 1.1312 .15652 1667.6 .000911

124. 1.1153 .15139 1567 .1 .000890 124. 1 . 1245 .15467 1616.5 .000907

126. 1.1084 .14951 1519.8 .000885 126. 1 .1178 .15282 156 8.1 . 000903

128. 1.1016 .14763 1475 .0 .000880 128. 1.1112 .15098 1522.1 . 000898

1 3 C . 1.0947 .14576 1432.3 .000875 130. 1.1046 .14915 1478.4 .000894

132. ] .0878 .14391 1391.8 .000870 132. 1 . 0979 .14733 1436.8 .000889

134. 1.0810 .14206 1353.2 .000865 134 . 1.0913 .14552 1397.3 .000884

136. 1 .0741 .14023 1316.4 .000860 136. 1.0847 .14372 1359.6 .000880

138. 1.0673 .13841 1281.4 .000855 138. 1.0781 .14194 1323.8 . 000875

1 4 C . 1.0604 .13661 1247.9 .000850 140. 1.0714 .14017 1289.6 . 000870

142. 1 .0536 .13482 1216.1 .000845 142. 1 . 0648 .13842 1256.9 . 000866

14 4, 1.0468 .13306 1185.6 . 000840 144 . 1.0582 .13668 1225.7 . 000861

146 . 1 .0399 .13131 1156.5 .000835 146. 1.0516 .13496 1196.0 .000856

148. 1.0331 .12958 1128.6 .000830 148. 1.0451 .13326 1167.5 .000851

1 50. 1.0763 .12787 1102.0 .000825 150. 1.0385 .13158 1140.3 .000847

157. 1 .0194 .17618 1076.5 .000820 152. 1.0319 .12992 1114.2 .000842

154. 1.01.26 .1 2453 1052.1 .000815 154 . 1.0253 .12829 1089.2 .000837

156. 1.0058 .12208 1028.7 .000810 156. 1.0188 .12666 1065.3 .000833

158. .9990 . 12125 1006.2 .000805 158. 1.0122 .12506 1042.4 .000828

160. .997] .11964 9 0 4,7 .000800 160. 1.0057 .12348 1020.4 .000824

165. .9751 .11574 934 .5 .000789 165. . 9894 .11963 969.1 . 000813

170. .9582 .11199 889.0 .000778 170. . 9732 .11593 92 2.7 . 000802

175. .9413 .10840 847.8 .000768 175. . 9570 .11239 880.6 .000793

180. .9245 .10498 810.2 .000758 180. . 9409 .10901 842.2 .000784

185. . 9078 .10173 775.9 .000750 185. . 9250 .10578 807.3 .000776

190. .8912 .09865 744.6 .000743 190. . 9091 .10272 775.3 .000769

195. .8747 .09574 715.9 .000736 195. . 8935 .09982 746.0 .000762

200. .8584 .09299 689.6 .000731 200. . 8779 .09707 719.2 .000757

210. . 8764 .08797 643.3 .000724 210. . 8474 .09203 671.8 . 000749

270, .7953 .08355 604.0 .000721 220. . 8177 .08756 631.6 .000745

230. .7653 .07968 570.7 .000722 230 . . 7889 .08362 597.4 . 000745

240. . 7364 .07631 542.4 .000728 240. . 7613 .08015 568.2 . 000749

250. .7088 .07336 518.2 .000736 250 . . 7347 .07709 543.1 .000755

260 . .6826 .07078 497.6 .000748 260. . 7093 .07439 52 1.7 .000764

270. .6578 .06852 480.1 .000763 270. . 6852 .07200 503.2 .000776

780. . 634 3 . 06652 465.1 .000779 280 . . 6623 .06987 487.4 . 000790

290. .6122 .06475 452.3 .000798 290. .6406 .06797 473.8 .000805

300. .5914 .06316 441 .5 .000817 300 . . 6201 .06627 462.2 .000821

310. . 5718 .06180 432.2 .000838 310. . 6007 .06477 452.1 .000839

320. .5535 .06075 424 .4 .000862 320. . 5824 .06356 443.6 .000859

* Two Phase Boundary

44
Table 5. Transport Properties of Oxygen* Isobars* SI Units 65.0 M°a I sobar 70.0 MPa Isobar

Temp

.

Oens 1 1 v Thermal V 1 scos i t y Th e r ma

1

Temp. Dens i t y Thermal Viscosity T he r ma 1 C on d . micro- Dlffuslvlt-y Cond. micro- 0 i f f us i v i t y K p /cm* + 3 W/rn.K g /cm .

s

cm**2/s K g / cm * * 3 W/m.K g /cm.

s

ct**2/s

61.478 1 .3-V32 .21911 6545.9 .000988 * 62.000 1.3456 .22028 6647.1 . 000991

62. 1.3412 .21837 6448.3 .000988 62 . 1.3456 .22028 6647.1 .000991

64. 1.3339 .21567 6090.3 .000988 64. 1. 33S3 .21760 6274.1 . 000992

66. 1.3266 .21315 5756.7 .000988 66. 1.3312 .21509 5927.3 . 000992

6 P • 1.3196 .21076 5445.7 .000987 68. 1 . 3241 .21273 5604.8 . 000993

70. 1.3125 .20848 5155.8 .000987 70. 1.3172 .21049 5304.6 . 000993

72. 1.3055 .20630 4885.4 .000986 72. 1.3103 .20834 5025.0 . 000993

74. 1.2966 .20420 4633.4 .000966 74 . 1.3035 .20627 4764.7 .000992

76. 1 .2918 .20216 4398 .4 .000985 76 . 1. 2968 .20427 4522.2 .000992

78. 1.2850 .20017 4179.2 .000984 78 . 1 . 2901 .20233 4296.2 . 000992

80. 1 .278? .19823 3974.7 .000983 80. 1 .2834 .20042 4085.5 .000991

82. 1.2714 .19632 3783 .9 .000981 82 . 1.2768 .19856 3889.0 . 000990

84. 1.2647 .19444 3605.8 .000980 84. 1 . 2702 .19671 3705.6 . 000989

86. 1.2580 . 19257 3439.4 .000978 86. 1 . 2636 .19489 3534.4 . 000988

88. 1.2513 . 1 9C 7 2 3283.9 .000977 88. 1 . 2570 .19309 3374.5 . 000967

9C. 1 .2447 .18888 3138.4 .000975 90 . 1 . 2505 .19129 3225.0 . 000985

92. 1.2380 .18705 3002.4 .000973 92. 1.2440 .18950 3085.2 . 000984

94 . 1 .2314 .18523 2874.9 .000971 94. 1 . 2375 .18772 2954.2 .000982

96. 1.2248 .18340 2755.5 .000969 96 . 1.2310 • 1 8 5 9 4 2831.6 .000980

98. 1.2182 .18158 2643.5 .000966 98. 1. 2245 .18416 2716.6 . 000978

100. 1.2116 .17976 2538.4 .000964 100 . 1.2181 .18238 260 8.6 . 000976

102. 1 . 2050 .17793 2439.7 .000961 102. 1.2117 .1 8060 2507.3 . 000974

104 . 1.1984 .17611 2346.9 .000959 104. 1 . 2052 .17881 2412.0 . 000971

106. 1.1919 .17428 2259.5 .000956 106. 1.1988 .17703 2322.4 . 000968

108. 1.1853 .17245 2177.3 .000953 108. 1 .1924 .17524 2238.0 .000966

110. 1.1788 .17062 2099.8 .000949 110. 1.1860 .17345 2158.5 .000963

112. 1.1723 .16879 2026.7 . 000946 112. 1.1797 .17165 2083.6 . 000960

114. 1.1657 .16696 1957.7 .000943 114 . 1.1733 .16986 2012.8 .000957

116. 1.1592 .16513 1892.5 .000939 116. 1.1669 .16807 1946.0 .000953

118. 1 .1527 .16330 1830.9 .000935 118. 1.1606 .16628 1882.8 . 000950

120. 1.1462 .16148 1772.6 .000932 120. 1.1543 .16449 1823.0 . 000947

122. 1.1397 .15966 1717.4 .000928 122. 1 . 1479 .16270 1766.4 .000943

124. 1.1333 .15784 1665 .0 .000924 124. 1.1416 .16092 1712.7 . 0009 3 9 126. 1.1268 .15603 1615.4 .000920 126. 1.1353 .15914 1661.8 . 000936

128. 1.1204 .15422 1568.2 .000915 128. 1 .1291 .15736 1613.6 .000932

130. 1.1139 .15243 1523.5 .000911 130. 1.1228 .15560 1567.7 .000928

132. 1.1075 .15064 1480.9 .000907 132. 1.1165 .15384 1524.1 . 000924

134 . 1.1010 .14886 1440.4 .000903 134 . 1.1103 .15209 1482.6 • 00092 C 136. 1.0946 .14710 1401.8 .000898 136. 1 .1040 .15036 1443.1 . 000916

138. 1.0882 .14534 1365.1 .000894 138. 1 . 0978 .14863 1405.5 . 000912

140. 1.0818 .14360 1330.1 .000889 140. 1 . 0916 .14692 1369.7 . 000907

142. 1.0754 .i4iee 1 296.7 .000885 142. 1.0854 .14522 1335.5 .000903

144. 1 .0690 .14017 1264.8 .000880 144 . 1.0792 .14354 1302 .

9

.000899

146. 1 .0626 .13848 1234.3 .000876 146. 1 . 0730 .14187 1271.7 .000895

148. 1 .0563 .13680 1205.2 .000872 148 . 1 . 0668 .14022 1241.9 .000891

1 5 C • 1.0499 .13514 1177.3 .000867 150. 1 . 0607 .13858 1213.4 . C00386

152. 1 .0436 .13351 1150.7 .000863 152. 1 . 0545 * 13697 1186.1 .000882

154. 1 .0372 .13190 1125.2 .000858 154 . 1.0484 .1 3537 1160.0 . 000878

156. 1.0309 .13030 1100.7 .00085* 156. 1.0423 .13379 1135.0 .000874

158. 1.0246 .12872 1077 .2 .000850 158. 1.0362 .13223 1111.0 .000370

1 6 C • 1.0183 .12716 1054.8 .000846 160. 1.0301 .13069 1088.0 . 000866

165. 1 .0026 .12336 1002.4 .000835 165. 1.0149 .12693 1034.5 . 000856

1 70 . .9870 .11970 955 .0 .000825 170. . 9999 .12332 986.1 .000847

175. .9715 .11619 912.0 .000816 175. . 9849 .11984 942.2 . 000838

180. .9560 .11284 872 .9 .000808 180. . 9700 .11651 90 2.2 . 0008 3 C 185. . 9 40 7 .10964 837.2 .000800 185. . 9553 .11333 865 .

8

.000822

190. .9256 .10659 804 .5 .000793 190. . 9407 .11030 832.4 .000815

195. .9105 .10370 774.6 .000786 195. . 9262 .10741 801.9 . 000809

200. .8956 .10095 747.2 .000781 200. .9119 .10467 773.9 .000804

210. .8664 .09590 698.8 .000773 210. . 8837 .09959 724.4 .000795

220. . 8379 .09139 657.6 .000768 220. . 8563 .09505 682.3 .000790

230. .8103 .08738 622 .5 .000767 230. . 8297 .09098 646.3 . 000786

240. .7836 .08382 592.4 .000769 240. . 8040 .08734 61$.

4

.000788

250. .75 80 .08066 566.6 .000773 250. . 7792 .08409 588.7 . 000791

260. .7334 .07785 544.3 .000781 260. . 7554 .08118 565.7 . 000797

270. .7100 .07534 525.1 .000790 270. .7325 .07856 545.8 .000804

280. .6876 .07310 508.5 .000801 280 . . 7107 .07620 528.6 . 0008 1

3

290. . 6664 .07108 494.2 .000813 290. . 6899 .07407 513.6 .000823

300. .6462 .06925 4 81.8 .000827 300. . 6701 .07213 500.5 . 000834

310. .6270 .06763 471.1 .000842 310. .6512 .07039 489.2 .000847

320. .6089 .06628 461 .9 .000859 320. . 6332 .06890 479.4 . 000861

* Two Phase Boundary

45
Table 5. Transport Properties of Oxygen# Isobars# SI Units. 75.0 MPa Isobar 80.0 MPa Isobar

Temp • Density Thermal

Con d

V 1 sco s 1 1

y

mlcroThermal Dlffuslvltv

T emp • Density Therma

C ond

V 1 s co s 1 t y microThermal

Di f fusl v Ity

K g/cm**3 W/m. K g /c m . s cm** 2/K g/ cm**3 W/m .K g /cm .

cm**2 /

62.510 1 . 3480 . 221^6 6744.5 .000994 63.032 1.3504 .22263 6838.0 . 000997

64. 1.3427 • 2 1 950 6459.4 .000995 64 . 1.3469 .22137 6646.3 . 000998

66. 1 .3356 .21701 6099.? .000997 66. 1 . 3399 .21890 6272.2 .001000

68. 1.3206 • 21 9 67 5764.8 .000998 68. 1.3330 .21659 5925.6 . 001002

70. 1.3217 .21296 5454.0 .000998 70. 1.3262 .21440 5604.1 .001004

72. 1 .3150 .21039 5165.1 .000999 72. 1.3195 .21231 5305.6 .001005

7 4. 1.3083 .20831 4096.3 .000999 74 . 1.3129 .21031 502 8.2 .001005

76. 1.3016 .20635 4646.1 .000999 76. 1.3063 .20838 4770.2 . 001006

78. 1.2950 .20999 4413.2 .000999 78. 1 . 2998 .20651 4530.3 .001006

80

1.2884 .20258 4196.2 .000999 00. 1 . 2934 .20468 4306.9 .001006

82. 1 .2819 .20075 3993.9 .000998 82. 1.2869 .20289 4098.8 .001006

84. 1.2754 .19899 3805.3 .000998 84 . 1.2806 .20113 3904.8 .001006

86. 1.2690 .19716 3629.2 .000997 86. 1.2742 .19939 3723.8 .001006

88. 1.2625 .19590 3464.9 .000996 88. 1.2679 .19767 3554.9 .001005

90. 1.2561 .19365 3311.2 .000995 90. 1. 2616 .19595 3397.1 .001004

92. 1.2497 .19190 3167 .6 .000994 92. 1 . 2553 .19425 3249.6 .001004

94 . 1.2434 .19016 3033.1 .000992 94 . 1.2491 .19254 3111.6 .001002

96. 1 .2 370 .18892 2907.2 .000991 96. 1 . 2428 .19084 2982.3 .001001

98. 1.2307 .18668 2789.1 .000989 98. 1. 2366 .18914 2861.2 . 001000

IOC. 1.2244 .18999 2678.3 .000987 100. 1 . 2304 .18744 2747.6 . 000998

102. 1.2181 .18320 2574.3 .000985 102. 1.2242 .18574 2640.9 .000997

104. 1.2118 .18195 2476.6 .000983 104. 1.2101 .18403 2540.7 . 000995

106. 1 .2055 .17970 2384.7 .00098] 106. 1.2119 .18232 2446.4 .000993

108. 1.1992 .17795 2298.2 .000978 108. 1.2058 .18061 2357.7 .000991

110. 1.1930 .17620 2216.6 .000976 110. 1.1997 .17889 2274.2 . 000988

112. 1 .1868 . 17995 2139.8 .000973 112. 1.1936 .17717 2195.4 .000986

114. 1.1805 .17269 2067.2 .000970 114. 1 . 1875 .17545 2 12 1.0 .000983

116. 1.1743 .17093 1998.7 .000967 116. 1.1814 .17372 2050.8 .000981

118. 1.1681 .16917 1933.9 .000964 118 . 1.1754 .17200 1984.5 . 000978

120. 1.1620 .16792 1872.7 .000961 120. 1.1693 .17027 1921.7 .000975

122. 1 .1558 .16566 1814.7 .000958 122. 1 . 1633 .16855 1062.3 . 000972

124. 1.1496 .16391 1759.7 . 000954 124. 1.1573 .16683 1806.0 .000969

126. 1.1435 .16216 1707.6 .000951 126. 1.1513 .16511 1752.7 .000965

128. 1.1374 .16092 1658.1 .000947 128. 1. 1453 .16339 1702.0 .000962

130. 1 .1313 .15868 1611.2 .000944 130. 1 .1394 .16168 1653.9 . 000959

132. 1.1252 .15695 1566.5 .000940 132. 1.1334 .15998 1608.2 .000955

134. 1.1191 .16523 1524.0 .000936 134. 1 . 1275 .15828 1564.0 .000952

136. 1.1130 .15352 1483 .6 .000932 136. 1.1216 .15660 1523.4 . 000948

138. 1.1069 .15182 1445.1 .000928 138. 1.1157 .15492 1484.0 . 000944

140. 1.1009 .15013 1408.4 .000924 140. 1.1098 .15326 1446.5 .00094 1

142. 1.0949 .19896 1373.5 .000921 142. 1 . 1039 .15160 1410.7 .000937

144. 1.0888 .19680 1340.1 .000917 144. 1 . 0980 .14996 1376.5 . 000933

146. 1 .0828 .19515 1308.2 .000913 146. 1.0922 .14833 1343.9 • 0 C 0 9 3 C 148. 1.07fc8 .19352 1277.7 .000900 140. 1 . 0863 .14672 1312.7 . CC0926

150. 1 .0709 .19190 124 8.5 .000905 150. 1 . 0805 .14513 1282.9 . 000922

152. 1.0649 .19031 1220.7 .000901 152. 1.0747 .14355 1254.4 . 000918

154. 1 .0590 . 13973 1194.0 .000897 154. 1 .0689 .14199 1227.1 .000915

156. 1.0530 .13717 1168.4 .000893 156. 1.0632 .1 4044 1200.9 .000911

158. 1.0471 .13563 1143.9 .000889 158 . 1.0574 .13891 1175.9 . 000907

160. 1 .0412 . 13910 1120.4 .000885 160. 1.0517 .13740 1151.9 .000904

1 6 * • 1.0265 .13038 1065.7 .000876 165. 1.0374 .13372 1096.0 .000995

170. 1 .0119 .12680 1016.2 .000867 170. 1 . 0233 .13016 1045.4 . 000306

175. .9974 .12335 971.3 .000858 175 . 1.0092 .12673 999.6 . 000879

180. .9831 .12009 930.5 .000850 180. . 9953 .12344 957.9 . 000870

185. .9688 .11688 893.3 .000843 185. .9815 .12029 919.8 . 000863

1 9 C • .9547 .11385 859.2 .000836 190. . 9678 .11728 885.1 . 000856

195. .9407 .11097 828 .0 .000830 195. . 9543 . 1144C 853.2 .000850

200. .9269 .10823 799.4 .000825 200. . 9409 .11166 824.0 . 000945

210. .8997 .10319 748.8 .000816 210. . 9146 .10656 772.3 . 000936

220. .8733 . 09856 705.8 .000810 220 . . 8890 .10194 728.3 .000830

2 3 C

.8475 .09999 668.9 .000807 230. . 8641 .09777 690.5 . 0008 2 6 240. .8226 .09073 637.2 .000807 240. . 8399 .09400 658.0 . 000825

250. .7986 .08790 609.0 .000809 250. . 8166 .09059 630.0 . 000825

260. .7755 .08939 506.1 .00081? 260. . 7940 .08750 605.6 .000828

270. .7532 .08167 565.5 .000818 270 . . 7724 .08468 504.4 . 000332

280. .7319 .07921 547.6 .00082* 280. . 7515 .00211 565.9 . 000837

290. .7115 .07696 532 .0 .000833 290 . . 7316 .07975 549.7 . 000844

3 CO

.6921 .07991 518.4 .00084? 300. . 7124 .07759 535.5 . 000851

310. .6735 .07305 506.5 .000852 310. . 6941 .07562 523.1 . 000359

320. . 6557 .07193 496.1 .000864 320 . . 6766 .07388 512.2 . 000869

* Two Phase Boundary

46
Table 5. Transoort Properties of Oxvqen» Isobar s» SI Units.

85. C MPa Isotar 90.0 MPa Isobar

Ten c . hen s 1 ty Thermal Viscosity Thermal Terno

.

Dens 1 1 y Ther rra 1 Viscosity T her ma 1 C ond . micro- Oiffusivitv C ond . micro- D I f f u s i v i t y

K q/ct1 **? W/IP.K p / c m • s cm**2 /S K g / cm**3 W/m.K q/cm.s c m**2 / s

63 . c <*4 1.3527 .27380 6 9? 7 .9 .001000

6 . 1.3511 .72321 *834.9 .001003 * 64.052 1.3550 .22497 7014.2 .001003

6 * • 1 .344 1 .22076 64 4 6 .5 .001004 66. 1.3483 .22260 6622.2 . 001007

68. 1.’373 .21867 608 t . 6 .001006 68. 1.3415 .22032 6250.3 .001010

70. 1 .3306 .71631 5755.0 .001008 70. 1 . 3348 .21818 5906.5 .001013

72. 1 . 3336 .21675 5446.6 .001010 77 . 1.3283 .21615 5588.2 .001015

7 4 . 1.3176 .71728 5160.4 .001011 74. 1.3218 .21422 5293.1 .001017

76. 1.3100 .21038 4894 .6 .00101? 76. 1.3154 .21235 5019.2 .001018

7 p . 1 .3066 .20885 4647.5 .00] C 1

3

78. 1 . 3091 .21055 4764.8 .001020

80. 1 .2901 .70676 4417 .6 .001014 80 . 1.3028 .20879 4528.3 .001021

82. 1.2910 . 20500 4?03 .5 .001014 82 . 1.2966 .20707 4308.3 .001021

84. 1 .7865 .20328 4004.1 .001014 84 . 1 . 2904 .20538 4103.4 .001022

86 . 1

. ’703 .20157 3818.? .001014 86 . 1.2842 .20372 3912.5 .001022

Rfi . 1 .2731 .109«0 3644.8 .001014 88. 1.2781 .20207 3734.4 .001022

90. 1 .2660 . 10071 3482 .8 .001013 00. 1 . 2720 .20043 3568.1 .001022

9? . 1.7607 .1 0656 3333 .3 .001013 92 . 1.2660 .19880 3412.8 .001022

9 4 . 1.2566 .10688 3189.7 .00101? 94. 1 . 2599 .19717 3267.5 .001021

96. 1.268 5 . 1°322 3057.1 . 0 0

1

C 1

1

96. 1.2539 .19555 3131.6 .001021

98. 1 .2626 .10156 2932.9 .001010 98. 1.2479 .19392 3004.2 .001020

100. 1.2363 .18080 2816.4 .001009 100 . 1.2420 .1 9229 2884.8 .001019

10?. 1.7302 .18073 2707.0 . 001007 102. 1.2360 .19066 2772.7 .001018

104 . 1 .2267 .18656 2604.3 .001006 104. 1 . 2301 .18903 2667.5 .001017

106. 1.2182 .1 86 00 2507 .7 .001004 106. 1.2242 .18739 2568.5 .001015

108. 1.2127 .18320 2416.8 .001002 108. 1.2183 .18574 2475.4 .001014

110. 1.2067 .18152 2331.2 .001000 110. 1 .2124 .18409 2387.7 .001012

11?. 1 .2002 .17083 2250.5 .000998 112. 1 . 2066 .1 8243 2305.1 .001010

114. 1.1062 .17816 2174 .3 .000996 114 . 1.2007 .18078 2227.1 . 001008

116. 1.1883 .17665 2102.4 .000993 116. 1.1949 .17911 2153.5 .001006

118. 1.1826 .17675 2034.5 .000991 118. 1.1091 .17745 2083.9 .001003

1?0. 1.1765 .17306 1970.2 .000988 120. 1. 1833 .17578 2018.2 .001001

1 ??. 1.1706 .17136 1909.4 . 000985 122. 1.1775 .17411 1955.9 .000998

124. 1.1667 .16067 1851 .8 .000982 124. 1.1718 .17245 1896.9 .000996

126. 1.1588 .16708 1797.1 .000979 126. 1.1660 .17078 1841.0 .000993

128 . 1.1530 .16620 1745.3 .000976 128. 1.1603 .16912 1788.0 .000990

130. 1.1671 . 16661 1696.1 .000973 130. 1 . 1546 .16746 1737.6 .000987

132. 1.1613 .16293 1649.3 .000970 132. 1.1489 .16580 1689.8 .000984

134. 1.1355 .16126 1604 .8 .000967 134 . 1.1433 .16416 1644.3 .000981

136. 1.1207 .15059 1562.5 .000963 136. 1.1376 .16251 1601.0 .000978

138. 1.1260 .15706 1522 .? .000960 138. 1.1320 .16088 1559.8 .000974

140. 1.1182 .15620 1483.8 .000956 140. 1.1263 .15926 1520.5 .000971

14?. 1.1125 .15666 14*7.2 .000953 142. 1 . 1207 .15764 1483.1 .000968

144 . 1.1068 .15306 1412.2 .000949 144 . 1.1152 .15604 1447.4 .000964

146. 1.1011 .15163 1378.9 .000946 146. 1 . 1096 .15445 1413.2 .000961

148. 1 .0056 .16086 1347 .0 .000942 148 . 1. 1040 .15287 1380.7 .000958

150. 1.0807 .16826 1316.5 . 000939 150. 1.0985 .15131 1349.5 .000954

152. 1.0861 .16660 1287.4 .000935 152. 1.0930 .14976 1319.7 .000951

154. 1.0786 .16515 1259.5 .000931 154 . 1.0875 .14822 1291.2 .000947

156. 1.0728 .16362 1232.7 .000928 156. 1.0820 .14671 1263.9 .000944

158. 1.0672 . 16210 1207.1 .000924 158. 1.0766 .14520 1237.7 .000941

160. 1.0616 .16061 1182.6 .000921 160. 1.0711 .14372 1212.6 .000937

165. 1 .0678 .13695 1125.5 .000912 165. 1.0576 .14009 1154.3 .000929

170. 1.0360 .13361 1073.8 .000904 170. 1.0442 .13658 1101.5 .000921

175. 1.0703 .13001 1027.0 .000896 175. 1.0309 .13319 1053.7 .000913

180. 1.0068 .12676 984 .4 .000888 1 80 . 1.0177 .12993 1010.2 .000906

185. .9036 .12360 945.6 .000881 185. 1.0047 .12680 970.6 .000899

190. .9802 .12050 910.1 .000875 190. . 99 ie .12380 934.3 .000893

195. .9670 .11772 877.5 .000869 195. . 9790 .12093 901.1 .000887

200. .9560 .11607 847.7 .000864 200. .9664 .11818 870.6 .000882

21 C • .9285 .10085 794.9 .000855 210. .94 16 .11305 816.7 . 000873

220. .9036 .10521 749.9 .000848 220. .9174 .10837 770.7 .000866

230. .8706 .10009 711.3 .000844 230. . 8938 .10411 731.3 .000861

240. . 8 560 .00716 678.0 .000842 240. . 8710 .10022 697.3 . 000858

250. .8332 .09368 649.2 .000841 250. . 8488 .09667 667.8 .000857

260. .8113 .00050 624 .2 .000843 260. . 8274 .09341 642.1 .000857

270. .7001 .08750 602.4 .000845 270. . 8067 .09041 619.7 .000859

280. .760 e .08602 583.3 .000849 280 . . 7868 .08765 600.1 .000861

290. .7502 .08266 566.6 .000854 2 90. . 7676 .08509 582.8 .000865

300. .7316 .08020 551.9 .000860 300. .7492 .08272 567.6 .000869

310. .7136 .07812 539.0 .000866 310. .7314 .08054 554.3 .000873

32 C • .6061 .07625 527.6 .000874 320. .7144 .07855 542.5 .000879

* Two Phase Boundary

47
Table 5. Transport °ropertles of Pxygen* Isobars* SI Units

95.0 ^P a Isobar 100.0 MPa Isobar

TempDensity Th e r m a 1 Viscosity Thermal Temp . Density Ther ma

Viscosity Thermal

C ond • micro- Diffuslvlty C ond • micro- Diffuslvlty

K a /cm**3 U/m.K q/ciP.S cm**? /s K g / cm** 3 W/m.K g /cm.

cm*»2/

64.558 1.3573 .22614 7097.1 . 0 C 1 006 * 65.060 1 .3595 .22730 7176.6 .001009

66 . 1 .3523 .22441 6799.1 .001009 66 . 1 . 3563 .22619 6977.4 .001012

68 . 1.3456 .22215 6414 .? .001013 68 . 1. 3496 .22396 6579.1 .001016

70 . 1.3390 .22003 6058.9 .001017 70 . 1.3430 .22186 6212.0 .001021

72 . 1 .3325 . 21 e 03 5730.3 .001020 72 . 1.3366 .21988 5873.0 .001024

74 . 1.3261 .21612 5426.1 .001022 74 . 1.3303 .21800 5559.5 .001027

76 . 1.3198 .21429 5144 .0 .001024 76 . 1 . 3240 .21619 5269.2 . 001029

78 . 1.3135 .21251 4 R 8 2 .3 .001026 78 . 1.3179 .21445 4999.9 .001032

80 . 1.3073 .21079 4639.1 .001027 80 . 1.3118 .21276 4750.0 .001033

82 . 1.3012 .20911 4413.0 .001028 82 . 1.3057 .21111 4517.7 .001035

84 . 1.2951 .20745 *• 202.6 .001029 84 . 1 . 2997 .20948 4301.7 .001036

86 . 1.2 890 .20582 4006.5 .001030 86 . 1.2937 .20789 4100.5 .001037

88 . 1.2830 .20421 3823.8 .001030 88 . 1 . 2878 .20631 3913.0 .001038

90 . 1.2770 .20260 3653.2 .001031 90 . 1.2819 .20474 3738.2 .001039

92 . 1 .2711 .20101 3493.9 .001031 92 . 1. 2760 .20318 3574.9 .001039

94 . 1 .2651 .19942 3345.0 .001030 94 . 1 . 2702 .20163 3422.2 .001039

96 . 1.2592 .19783 3205 .7 .001030 96 . 1.2644 .20007 3279.5 .001039

98 . 1.2533 .19624 3075 .2 .001030 98 . 1 . 2586 .19851 3145.8 .001039

10 O . 1.2475 .19465 2952 .8 .001029 100 . 1.2528 .19695 3020.5 .001038

102 . 1.2416 .19305 2838.0 .001028 102 . 1. 2471 .19539 2903.0 . 001038

104 . 1 .235 8 .19145 2730.2 .001027 104 . 1.2414 .19382 2792.6 .001037

106 . 1.2300 .18984 2628.9 .001026 106 . 1.2357 .19225 2688.9 .001036

108 . 1.2242 .18823 2533.6 .001024 108 . 1.2300 .19066 2591.3 .001035

110 . 1.2185 .18661 2443.8 .001023 110 . 1.2243 .18908 2499.5 . 001034

112 . 1.2127 .18498 2359.2 .001021 112 . 1.2187 .18748 2412.9 .001032

114 . 1.2070 .18336 2279.4 .001019 114 . 1.2131 .18588 2331.3 .001031

116 . 1.2013 .18172 2204.1 .001017 116 . 1.2074 .18428 2254.3 .001029

116 . 1.1956 .18009 2132.9 .001015 118 . 1.2019 .18267 2181.5 .001027

120 . 1.1899 .17845 2065.6 .001013 120 . 1.1963 .1 8106 2112.6 .001025

122 . 1.1843 .17681 2001.9 .001011 122 . 1.1907 .17944 2047.5 .001023

124 . 1.1786 .17517 1941.6 .001008 124 . 1. 1852 .17783 1985.8 .001021

126 . 1.1730 .17352 1884.4 .001006 126 . 1. 1797 .17621 1927.3 .001018

128 . 1 .1674 .17189 1830.2 .001003 128 . 1.1742 .17459 1871.9 .001016

130 . 1.1618 .17025 1778.7 .001000 130 . 1. 1687 .17298 1819.2 .001013

132 . 1.1562 .16862 1729.8 .000597 132 . 1 .1633 .17137 1769.2 .001010

134 . 1.1507 .16699 1683 .2 .000995 134 . 1.1578 .16976 1721.7 .001008

136 . 1.1451 .16537 1639.0 .000992 136 . 1. 1524 .16816 1676.4 .001005

138 . 1 .1396 .16375 1596.8 .000988 138 . 1.1470 .16656 1633.4 .001002

140 . 1.1341 .16215 1556.7 .000985 140 . 1. 1416 .16497 1592.4 .000999

142 . 1 .1287 .16055 1 518 .4 .000982 142 . 1.1363 . 16339 1553.2 .000996

144 . 1.1232 .15896 1481 .9 .000979 144 . 1.1309 .16182 1515.9 .000993

146 . 1 .1176 .15739 1447.0 .000976 146 . 1.1256 .16026 1480.3 .000990

148 . 1.1123 .15583 1413.7 .000973 148 . 1.1203 .15872 1446.3 .000987

150 . 1.1069 .15428 1381.9 .000969 150 . 1.1150 .15718 1413.8 .000984

152 . 1.1015 .15274 1351.5 .000966 152 . 1 . 1097 .15566 1382.7 .000981

154 . 1.0962 .15122 1322.3 .000963 154 . 1.1045 .15415 1352.9 .000978

156 . 1.0908 .14972 1294.4 .000960 156 . 1.0992 .15266 1324.4 .000975

158 . 1.0855 .14823 1267.7 .000956 158 . 1.0940 .15118 1297.1 .000971

160 . 1.0802 .14675 1242.1 .000953 160 . l.oese .14971 1271.0 .000968

165 . 1 .0670 .14315 1182.5 .000945 165 . 1 . 0759 .14613 1210.1 .000961

170 . 1.0539 .13966 1128 .6 .000937 170 . 1. 0631 .14265 1155.1 . 000953

175 . 1.0409 .13628 1079.8 .000930 175 . 1.0505 .13930 1105.3 .000946

180 . 1.0281 .13304 1035 .4 .000923 160 . 1.0379 .13606 1059.9 .000939

185 . 1.0154 .12991 994.9 .000916 185 . 1.0255 .13294 1018.6 .000932

190 . 1.0028 .12692 957.9 .000910 190 . 1.0132 .12995 980.8 .000926

195 . .9903 .12404 924.0 .000904 195 . 1.0011 .12708 94 6.2 .000921

200 . .9780 .12129 892 .9 .000899 200 . . 9891 .12432 914.5 .000915

210 . .9539 .11614 837.8 .000890 210 . . 9655 .11916 858.3 .000906

220 . .9303 .11144 790.9 .000883 220 . . 9425 .11442 810.4 .000899

230 . .9073 .10713 750.6 .000877 230 . . 9201 .11008 769.3 .000893

240 . . 8851 .10319 715.8 .000874 240 . . 8983 .10608 733.7 .000889

250 . .8634 .09957 685 .6 .000872 250 . . 8772 .10240 70 2.9 .000886

260 . .8425 .09624 659.3 .000871 260 . . 8568 .09899 676.0 .000885

270 . .8223 .09316 636.4 .000872 270 . . 8370 .09583 652.4 .000884

280 . .8028 .09030 616.2 .000873 2 80 . . 8178 .09289 631.8 . 000884

29 C . . 78 39 .08765 598.5 .000875 290 . .7993 .09014 613.5 .000885

3 C 0 . .7658 .08518 582.8 . 00087 e 300 . . 7815 .08757 597.5 .000387

310 . .7484 .08289 569.0 .000681 310 . . 7643 .08517 583.2 .000888

320 . .7316 .08079 556.8 .000885 320 . .7478 .08296 570.6 .000891

* Two Phase Boundary

48

Table ft • Transoort Properties of 0»vgen for saturated L i o u i <1 a n H Vapor t n g r . Units

Tptp , Pressure Den s 1 t y The r a- a 1 Viscosity T h e r m a 1 Temo, p ressur° P en s 1 t y T h e r t a 1 V 1 s co s i t y T h e r t a 1 C ond

rr 1 CTO- PI ffus Ivltv C on o . micro- Oiffusivitv

P p s i a 1 b/f t**3 RTU/f t .h ,,p 1 b/f t. s f t**2/h p o s i a 1 t /f t **3 RTU/f t .h,, P 1 b /f t . s ft **2 /h

<n .8<>6 .0?] 81.5428 .11769 326.06 .00363 190. 57.250 66.2125 .07485 91.2 8 .00267

'? 7 .8<i 6 .021 .0007 .00236 2.44 16.54835 190. 57 .2 50 . 9 P 4 7 • CC 5

7 4 5.37 .02249

100. .031 81.2157 .11639 317.52 . 00360 192 . 62.172 65.8256 .07354 8 9.02 . 00264

100 . .031 .0009 .00248 2.52 12.33342 192. 62.172 1.0642 .00582 5.44 .02090

10?. .043 80.9115 .11522 309.51 .00358 194. 67.399 65 .4346 . C 7 2 6 2 86.8? .00261

10? . • 04 3 .0013 .00258 2.60 9 , 4 f 5 7 R 194. 67.399 1 .1484 .00591 ^.51 .01944

108 . . 059 80.6068 .11409 301.46 .00355 196. 72.99? 65.0393 .07170 84.69 .00258

108. .0 59 .0017 .00268 2.67 7.32589 196. 72.94

1 .2376 .00599 5.57 .01810

106. .07 9 80.3015 .11298 293.43 .00353 198. 78.812 64.6396 .07077 82 .6 1 .00255

106. .079 .0022 .00277 2.74 5.71802 198. 78.81? 1 .3320 . 00608 5.64 .01686

108. • 1 0 ft 79.9955 .11189 285.46 .00351 200. 85.021 64.235? .06984 80.59 .00251

108. .105 .0029 • 002 86 2.81 4 . *0094 200. 85.021 1.4318 .00616 5.71 .01573

110. .139 79.6888 .11083 277.58 . OC 3 4 9 202. 91.580 63.8259 . 06891 78.63 . 00248 no. .139 .0038 .00294 2.88 3.57259 202 . 91.580 1.5374 .00625 5.78 .01468

11?. .181 79 .3812 .10980 269.81 .00347 204 . 98.501 63.411

.06797 76.71 .00245

11?. .181 .0048 .00302 2.94 2.85897 204. 98.501 1.6489 .00634 5.85 .01370

118 . .234 79.0728 .10878 262.17 .00345 206. 105.794 62.991.06703 74.04 .00241

118. .234 .0061 .00310 3.01 2.30614 206. 105 .794 1.7666 .00643 5.92 .01290

116. .300 78.7635 .10778 254. 68 .00343 208. 113.471 62 .5660 .06609 73.02 .00238

116. . 300 . 0077 . 00317 3.07 1 . 87458 208. 113.471 1.8908 .00652 5.99 .01197

118. .380 78.4532 .10680 247.96 .00341 210. 121.545 62.1344 .06514 71.25 . 00234

118. .380 .0096 .00324 3.14 1.53514 210. 121.545 2.0218 .00662 6.0 7 .01119

1?0. .478 78.1419 .10583 240.22 .00340 2 12. 130.025 61 .6964 .06419 69.51 .00231

1?0. .478 .0119 .00331 3.20 1 .26617 212. 130.025 2.1600 .00672 6.14 .01047

122. .597 77.8295 .10487 233.25 .00338 214. 138.926 61.251

.06323 67.62 . 00227

122. .597 . 0146 .00338 3.27 1.05152 214. 138.926 2.3056 .00682 6.22 .00979

128. .738 77.5160 .10393 226.48 .00336 216. 148.257 •c o o o .06227 66.16 .00223

128. .738 .0178 .00344 3.33 . 87901 216. 148.257 2.4592 .00692 6.30 . 00916

1?6. .907 77.2014 .10299 219.89 .00334 218. 153.031 60.3409 .06130 64.54 .00219

126. .907 .0216 .00351 3.39 .73945 218. 158 .031 2.6210 .00702 6.37 .00858

128. 1.106 76.8855 .10207 213.49 .00333 220. 168.260 59.8738 .06033 62.96 . 00215

128. 1.10 ft .0259 .00357 3.45 . 62579 220. 168.260 2.7915 .00713 6.45 .00802

130. 1.340 76.5685 .10115 207.29 .00331 222. 178.957 59.3984 .05936 61.41 .00211

130. 1.340 .0309 .00364 3.51 .53265 222 . 178.957 2.9712 .00724 6.54 .00751

132. 1.613 76.2501 .10024 201.27 .00329 224 . 190.133 58.9141 .05837 59.89 .00207

132. 1.613 .0367 .00370 3.58 .45587 224. 190.133 3.1-606 .00736 6.62 .00703

138 . 1.930 75.9305 .09934 195.45 .00328 226. 201.801 58.4203 .05739 58.40 . 00202

138. 1.930 .0433 .00377 3.64 . 39220 226. 201 .801 3.3602 .00748 6.70 .00657

136. 2.296 75.6094 .09844 189.81 .00326 228. 213.974 57.9165 .05640 56.93 .00198

136. 2.296 .0508 .00383 3.70 .33910 228. 213.974 3.5708 .00760 6.79 .00614

138. 2.717 75.2870 .09754 184. 35 .00324 230. 226.664 57.4021 .05540 55.49 .00193

138. 2.717 .0593 .00390 3.76 .29458 230. 226.664 3 .7928 .00773 6.88 .00574

180. 3.198 74.9631 .09666 179.07 .00322 232. 239.884 56.8763 .05440 54 .08 .00189

180. 3.198 .0689 .00396 3.82 .25707 232. 239.384 4.0271 . 00787 6.98 .00536

182. 3.745 74.6377 .09577 173.97 .00321 234. 253.648 56.3382 .05340 52.69 .00184

18?. 3.745 .0797 .00403 3.88 .22530 234 . 253.643 4.2745 .00801 7.07 .00501

188. 4.364 74.3108 .09499 169.04 .00319 236. 267.969 55.7871 .05239 51 .32 .00179

188 . 4.364 .0917 .00409 3.94 .19826 236. 267.969 4.5359 .00816 7.17 .00467

186. 5.063 73.9823 .09400 164.27 .00317 238. 282.860 55.2220 .05137 49.97 .00174

186. 5.063 .1051 .00416 4.00 .17515 238. 282.860 4.8124 .00832 7.27 .00435

188. 5.848 73.6521 .09312 159.66 .00315 240. 298.335 54.6417 .05035 48.64 .00169

188. 5.848 .1200 .00422 4.06 .15530 240. 298.335 5.1050 .00849 7.38 ,00405
Table 6. Transport Pro rtles of Oxygen for saturated Llauid and Vapor* Engr* Units

Temp. Pressure Density Ther ma 1 V 1 scos 1 t

y

Ther ma

1

T emp

.

Pressure Density Therma

1

Viscosity Thermal Cond • m i cr o- D 1 ffus Ivlty Cond. micro- Di f fusi vi

R psla 1 b / f t **3 BTU/ft.h,,R Ib/ft.s ft**2/h R psla 1 b / f t** 3 BTU/ft.h. R Ib/ft.s ft**2/h

150. 6.727 73. 3203 .09225 155.20 .00313 2*2. 31*. *10 5*. 0*51 .0*932 *7.32 .0016*

150. 6.727 .136* .00*29 * .12 .13819 2*2. 31*. *10 5. *150 .00867 7 .*9 .00376

152. 7.707 72.9867 .09137 150.90 .00311 2** . 331.098 53. *307 .0*830 *6.02 .00159

152. 7.707 .15*6 .00*35 *.18 .12337 2**. 331.098 5. 7**0 .00887 7.61 .003*9

15*. 8.795 72.6513 .090*9 1*6.7* .00309 2*6. 3*8. *1* 52.7969 .0*726 ** .73 .00153

15*. 8.795 .17*5 .00**2 *.25 .11050 2*6. 3*8. *1* 6.0937 .00909 7.73 .00323

156. 10.001 72.31*0 .08961 1*2.72 .00307 2*8. 366.375 52.1*19 .0*623 *3. *5 .001*8

156. 10.001 .1963 .00**9 *.31 .09926 2*8. 366.375 6. *659 .00932 7.86 .00299

158. 11.332 71.97*8 .08873 138.83 .00305 250. 38*. 997 51. *63* .0*519 *2.18 .001*2

158. 11.332 .2202 .00*56 *.37 .089*3 250. 38*. 997 6.8631 .00958 7.99 .00275

160. 12.797 71.6336 .08786 135.07 .00303 252. *0* . 2 97 50.7590 .0**16 *0.92 .00136

160. 12.797 .2*62 .00*63 * . *3 .08079 252. *0* . 2 97 7.2879 .00986 8.13 .00253

162. 1*.*0* 71.2902 .08698 131.** .00301 25*. *2*. 292 50.025* .0*313 39.65 .00129

162. 1*.*0* .27** .00*70 * .*9 .07317 25*. *2*. 292 7.7*36 .01019 8.29 .00232

16*. 16.163 70. 9**8 .08610 127.93 .00299 256. **5.001 *9.2589 .0*210 38.39 .00123

16*. 16.163 .3051 .00*77 *.55 .066*3 256. **5.001 8.23*1 .01055 8. *5 .00212

166. 18.083 70.5971 .08521 12*. 5* .00297 258. *66.*** *8. *5*8 .0*109 37.12 .00116

166. 18.083 . 3382 .00*8* *.61 .060*6 258. *66.*** 8.76*5 .01096 8.63 .00192

168. 20.173 70.2*71 .08*33 121.25 .00295 260. *88.6*2 *7.6069 .0*009 35.85 .00109

168. 20.173 .37*1 .00*91 *.67 .0551* 260. *88.6*2 9.3*10 .011*5 8.82 .0017*

170. 22 .**3 69.89*6 .083** 118.07 .00293 262. 511.619 *6.7073 .03912 3* .55 .00102

170. 2 2 . ** 3 .*127 .00*98 *.7* .050*0 262. 511.619 9.9717 .01201 9.03 .00156

172. 2*. 903 69.5396 .08256 115.00 .00290 26*. 535.399 *5.7*5* .03818 33.2* .0009*

172. 2*. 903 .*5*2 .00505 *.80 .0*615 26*. 535.399 10.6676 .01268 9.26 .00138

17*. 27.562 69.1821 .08167 112.02 .00288 266. 560.010 **.7061 .03730 31.88 .00085

17*. 27.562 .*988 .00513 *.86 .0*23* 266. 560.010 11. **39 .013*9 9.52 .00120

176. 30. *31 68.8217 .08077 109.1* .00285 268. 585. *83 *3.5671 .03651 30. *8 .00076

176. 30. *31 .5*66 .00520 *.92 .03892 268. 585 .* 83 12.3231 .01**9 9.83 .00103

178. 33.519 68. *586 .07988 106. 3* .00283 270. 611.855 *2.293* .03583 29.00 .00066

178. 33.519 .5978 .00528 *.99 .03583 270. 611.855 13.3*07 .01576 10.1 8 .00085

180. 36.838 68.0925 .07898 103.6* .00280 272. 639.170 *0.8236 .03533 27.39 .00055

180. 36.838 .6525 .00535 5.05 .0330* 272. 639.170 1* . 5 588 .017** 10.62 .00067

182. *0.397 67.7232 .07808 101.01 .00278 27*. 667 .* 86 39.0338 .03511 25.57 .000*2

187. *0.397 .7109 .005*3 5.11 .03052 27*. 667.* 86 16.10*0 .01975 11.20 .000*8

18*. **.207 67.3508 .07718 98. *7 .00275 276. 696.886 36.5919 .03533 23.29 .00025

18*. **.207 .7732 .00551 5.18 .02822 276. 696.886 18.3235 .02*38 12.08 .00027

186. *8.279 66.97*9 .07627 96.00 .00272 278. 727.5*3 31.3822 .051*5 19.16 .00005

186. *8.279 .839* .00558 5.2* .02613 278. 727.5*3 23.9567 .06158 1* . 6 5 .00003

188. 52.623 66.5956 .07536 93.60 .00270 278.2*6 731 .*26 27.2276

188. 52.623 .9099 .00566 5.31 .02*23 278.2*6 731. *26 27.2276

51
T ah I e 7. T r ans oor t Propprtles of Cxyopn, Isobars* Fnar., Units.

5 . p s 1 a I s o h a r 10. o s 1 3 Isobar

T p rr c . P pfl S i t y T h p r m a ! V i s c o s i t y Thpr fra 1 T e d . 0 p n s i t v Thermal Viscosity T her ma

C on d . micro- P i f f us i v i f V Cond. micro- D i f f us 1 v 1 ty

R 1 h / f h + * 3 B TU / f t . h • P • h / f t . s f t **2 /h 0 1 b / f t **3 BTU/ft.h.R Ib/f t.s f t**2/

Q7, p*} 81 .544 2 .11770 32* . 1 3 .003*3 4 97.860 81.5456 .11770 326.20 .00363

1 0 P • 8 1 . 2 1 P2 .11640 317 .62 .003*0 100 . 81 . 2207 .11641 317.71 . 00360

1 o

e

. 80.45*8 .11354 297. ^3 . "0354 105. 80. 4594 .11355 297.62 .00354 nr

79. *91

.11084 ?77 .6* .00349 110. 79.6941 .11085 277.74 .00349 n*. 7 P .Q?09 .10829 258.48 .00344 115 . 78. 9238 .10830 258.56 .00344

12 C. 78 .1446 .10534 240. 28 .00340 1 20. 78.1475 .10585 240.35 . 00340

125. 77.3*15 .10347 223 .21 .00335 125. 77. 3646 .10348 223.28 . 00335 nr. 7* . 5709 .10116 207. 33 .00331 130. 76.5742 .10117 207 .40 . 00331 ns 75.7721 .QCOfiQ 192.64 .00327 135 . 75 . 7756 .09891 192.70 .00327 nc. 74.9*44 .09**6 179 . 09 .00322 140. 74 . 9681 .09667 179.15 .00322

1 *

c

. 74 .1 470 .09445 166.63 . OC318 145. 74 .1609 .09446 166.69 .00318

1 45 . P? » 74 .010* . 09408 164 .*7 .00317 150 . 73.3230 .09225 155.23 . 00313

1 4 5.10*9 .00415 4. CO . 1 7700 155. 72.4834 .09005 144.72 .00308

1 5 r

.1009 .00426 4 .12 .18860 4 155.998 72.3143 .08961 142.72 .00308

15?

.0975 .0044? 4 . ? 7 • 2 0 2 94 4 155.998 . 1963 .00449 4.31 . 09927

160

.0943 .00458 4 . 41 .21778 160. . 1910 .00461 4.42 . 10540

165 . . 091 3 . 00474 4 . 56 .23316 165 . . 1848 .00477 4.57 . 11327

17C. .088* .00 4«9 4.71 .24901 17C. .1790 .00492 4.71 .12138

17*. .08*0 .00505 4 . 65 .26540 175. .1736 .00508 4 .86 . 12973

IBP. .0835 .00521 5. 00 .28231 180. . 1685 .00523 5.00 .13833

1 8S .081 2 . 00577 5.14 . 2Q973 185. . 1637 .00539 5.15 .14717

1 QO . .0790 .09553 5 .23 .31766 190. . 1592 .00555 5.29 . 15626

1*55. .07*70 .00569 5.43 .33610 195. . 1549 .00571 5.44 . 16559

200

.0750 . 00585 5 . 57 .35503 200. . 1509 .00587 5.58 . 17516

?C*. .0 7 M ,00601 5.71 .37465 205. . 1471 .00603 5 .72 . 18496

210. .9714 .00617 5 . P6 .39434 210 . . 1435 .00620 5.86 . 19500

215. . 0*97 . 00*34 6.00 .41471 215 . . 1401 .00636 6.01 .20527

220. .0681 . 00650 6.14 .43554 220. .1368 .00652 6.15 .21576

22 6 . .0665 .00666 6 .28 .45683 225 . . 1337 .00668 6.29 .22648

2 3 0. .0*51 .00682 6. 4? .4785* 230. . 1307 .00684 6.43 .23741

225. .0*37 . CC69P 6.56 .50073 2 35 . . 12 79 .00699 6.57 . 24857

240. .0623 .00713 6.70 .52334 240. .1251 .00715 6.71 .25993

?45 . .0*11 .00729 6 . 84 .54638 245 . . 1225 .00731 6.84 .27151

250. .0593 .00745 6.97 .56984 250 . .1200 .00747 6.98 . 28330

255 . .9586 .00761 7.11 .59373 2 5

c

. .1176 .00762 7.12 .29530

260. .0575 .CC776 7.25 .*1806 260 . .1153 .00778 7.25 . 30751

2 6

c

. . 0 564 .00792 7. 38 .64283 265. . 1131 .00793 7.39 . 31995

270 . .0554 .00807 7.52 .66807 270. .1110 .00809 7.52 . 33262

27*. .0543 .00823 7 . 65 .69384 275 . . 1089 .00825 7.66 . 34556

2 P 0

.0534 .00838 7. 79 .71975 280. .1070 .00840 7.79 . 35856

28*-

. 0524 .0085? 7.92 .74536 285 . . 1051 .00854 7.93 .37140

?9C . .0515 .00867 6 .05 .77151 290. . 1032 .00868 8.06 .38450

295 . .0506 .00881 P .18 .79811 2 95 . . 1015 .00883 8.19 . 39784

300. . 0498 .00696 8.31 .82512 300. . 0998 .00897 8.32 .41138

3 1 C

.0482 . 0092 6 8.57 . «eo30 310. .0965 .00926 8.58 .43903

320. .0467 .00953 8.83 . 93694 320 . . 0935 .00954 8.84 .46742

330. .0452 . OC 9 89 . 09 . 99499 330. . 0906 .00982 9.09 . 49650

340. .0439 .01009 9 . 34 1.05442 340. . 0879 .01010 9.34 .52627

350. .0426 .01036 9.59 1.11519 350 . . 0854 .01038 9.59 . 55672

360. .0415 .01064 9. 83 1.17728 360. . 0830 .01065 9.84 . 58782

370. . 0403 .01091 10. 08 1.24069 370. . 0807 .01092 10.08 . 61958

380 . .0393 .01117 10.32 1.30539 380. . 0786 .01118 10.32 .65198

390. .0383 .01144 10.55 1.37137 390 . . 0766 .01145 10 .56 . 68502

400. .0373 .01170 10.79 1 .43861 400. . 0747 .01171 10.79 .71869

410. .0364 .01196 11 .02 1 .50710 410. . 0728 .01197 11.03 .75298

4?P. .0355 .01222 11.25 1.57683 420 . . 0711 .01223 11 .26 . 78790

430. .0347 .01247 11 . 48 1 .64779 430. . 0694 .01248 11.49 . 82342

44 0. .0339 .01273 11.71 1.71996 440. .0678 .01274 11.71 .85955

450. .0331 . 0 1 2 9 P 11.93 1 .79332 450. .0663 .01299 11.94 . 89628

460. .0324 .01323 12 .16 1 . 86787 460 . . 0649 .01324 12.16 . 93360

470 . .0317 .01348 12. 37 1.94359 470. . 0635 .01349 12.38 . 97150

480. .0311 .01373 12.59 2 .02046 480. .0622 .01374 12.60 1.00998

490. .0304 .01397 12.81 2 .09847 4 90. . 0609 .01399 12.81 1.04903

500. .0298 .01422 13.02 2.17761 500. . 0597 .01423 13.02 1.08864

510. .0292 .01446 13.23 2.25784 510. . 0585 .01448 13.24 1.12880

520. .0^87 .01471 13.44 2.33917 520 . . 0574 .01472 13.45 1 . 16950

530. .0281 .01495 13.65 2.42157 530. .0563 .01496 13.65 1.21074

540. .0276 .01519 13 . 86 2.50501 540. . 0552 .01520 13.86 1.25250

* Two Phase Boundary

52
Table 7. Transpo t Properties of Oxygen* Isobars* Fngr. Units

15, psla Isobar

Tern d • Dens 1 t y Thermal V 1 scos 1 ty Thermal

Cond

.

micro- Olffusivit

R Ib/f t**3 BTUm.h.,R Ib/ft.s f t+*2/h

* <37.868 81.5870 .11771 326.27 .00363

100. 81.2232 .11682 317.81 .00360

105. 80.8620 .11356 297 .71 .00358

110. 79. 6968 .11086 277.82 .00389

115. 78.9266 .10831 258.63 .00388

120. 78.1505 .10586 280.82 .00380

125. 77.3677 .10389 223.35 .00335

130. 76.5778 .10118 207.86 .00331

135. 75.7791 .09892 192.76 .00327

180. 78.9718 .09668 179.21 .00323

185. 78.1587 .09887 166.78 .00318

150. 73.3271 .09227 155.29 .00313

155. 72.8878 .09007 188.76 .00309

160. 71.6356 .08786 135.09 .00303

* 162.698 71 .1700 .08667 130.20 .00301

* 162.698 .2888 .00872 8.51 .07073

165. .2808 .00879 8.58 .07322

170. .2713 .00895 8.72 .07875

175. .2628 .00510 8.87 .08882

180. .2589 .00526 5.01 .09026

185. .2875 .00582 5.16 .09628

190. .2806 .00557 5.30 .10239

195. . 2380 .00573 5.88 .10868

200. .2278 .00589 5.59 .11513

205. .2220 .00605 5.73 .12178

210. .2168 .00621 5.87 .12889

215. .2112 .00637 6.01 .13539

220. .2062 .00653 6.15 .18288

225. .2018 .00669 6.29 .18968

230. .1968 .00685 6.83 .15697

235. .1925 .00701 6.57 .16885

280. .1888 .00717 6.71 .17207

285. .1888 .00733 6.85 .17983

250. .1806 .00788 6.99 .18773

255. .1770 .00768 7.12 .19577

260. .1735 .00779 7.26 .20395

265. .1701 .00795 7.80 .21228

270. .1669 .00810 7.53 .22076

275. .1638 .00826 7.66 .22982

280. .1608 .00881 7.80 .23812

285. .1580 .00856 7.93 .28670

290. .1552 .00870 8.06 .25586

295. .1525 .00888 8 . 19 .26837

300. .1899 .00899 8.32 .27382

310. .1850 .00927 8.58 .29190

320. .1808 .00956 8.88 .31087

330. .1361 .00988 9.09 .33030

380. .1320 .01012 9.35 .35019

350. .1282 .01039 9.59 .37052

36C. .1286 .01066 9.88 .39129

370. .1212 .01093 10.08 .81250

380. .1180 .01120 10. 32 .83813

390. .1150 .01186 10.56 .85619

800. .1121 .01172 10.80 .87867

810. .1093 .01198 11.03 .50157

820. .1067 .01228 11.26 .52888

83 C. .1082 .01250 11.89 .58859

880. .1018 .01275 11 .72 .57271

850. .0995 .01300 11.98 .59722

860. .0978 .01325 12.16 .62213

870. .0953 .01350 12.38 .68783

880. .0933 .01375 12.60 .67311

890. .0918 .01800 12.81 .69917

500. .0895 .01828 13.03 .72560

510. .0878 .01889 13.28 .75280

520. .0861 .01873 13.85 .77956

530. .0885 .01897 13.66 .80708

580. .0829 .01522 13.86 .83898

* Two Phase Boundary

20* psla Isobar

Temp

.

Density Therma

1

Viscosity Therma

1

C ond

.

m I c ro- Dlffuslvity

R 1 b / f t

3

BTU/ft.h . R Ib/ft.s f t+*2/h

* 97.875 81.5888 .11771 326.38 .00363

100. 81.2257 .11683 317.91 .00360

105 . 80.8686 .11357 2 97.80 .00358

110. 79.6995 .11087 277.90 .00389

115. 78. 9298 .10832 258.71 .00388

120. 78.1538 .10587 280.89 .00380

125. 77.3708 .10350 223.81 .00335

130. 76.5807 .10119 207.52 . 00331

135. 75.7825 .09893 192.82 .00327

180. 78.9758 .09670 179.26 .00323

185. 78.1586 .09888 166.79 .00318

150. 73.3312 .09228 155.38 .00313

155. 72.8922 .09008 188.81 .00309

160. 71.6803 .08788 135.18 .00308

165. 70.7781 .08566 126.25 . 00298

* 167.880 70.2751 .08880 121.51 .00295

* 167.880 .3711 .00890 8.67 .05558

170. . 3657 .00897 8.73 .05738

175. .3539 .00512 8.88 .06173

180. . 3830 .00528 5.02 .06618

185. . 3328 .00588 5.17 .07078

190. .3232 .00559 5.31 .07581

195. .3182 .00575 5.85 .08019

200. . 3057 .00591 5.59 .08509

205. .2977 .00607 5.78 .09009

210. . 2901 .00623 5.88 .09520

215. . 2830 .00639 6.02 .10083

220. . 2762 .00655 6.16 .10575

225. .2697 .00671 6.30 .11119

230. . 2636 .00687 6.88 .11673

235. . 2577 .00703 6.58 .12237

280. . 2521 .00718 6.72 . 12812

285. .2867 .00738 6.86 .13397

250. . 2816 .00750 6.99 .13993

255 . . 2367 .00765 7.13 .18599

260. .2320 .00781 7.27 .15215

265 . . 2275 .00796 7 .80 .15882

270. . 2231 .00812 7.58 . 16881 275. .2190 .00828 7.67 .17133

280. .2189 .00883 7.80 . 17788

285. .2111 .00857 7.98 .18833

290. . 2073 .00871 8.07 . 19092

295. . 2037 .00886 8 .20 .19762

300. .2003 .00900 8.33 .20882

310. . 1937 .00929 8.59 .21832

320. .1875 .00957 8.85 .23258

330. . 1817 .00985 9.10 .28718

380. .1763 .01013 9.35 .26213

350. .1712 .01080 9.60 .27780

360. .1668 .01067 9.88 .29301

370. . 1618 .01098 10.09 . 30898

380. . 1575 .01121 10.33 . 32520

390. . 1538 .01187 10.57 .38177

800. . 1895 .01173 10.80 .35865

810. . 1858 .01199 11.03 . 37585

820. . 1823 .01225 11.26 .39335

830. . 1390 .01251 11.89 .81116

880. . 1358 .01276 11 .72 .82927

850. .1328 .01301 11.98 .88767

860. .1299 .01326 12.16 .86638

870. . 1271 .01351 12 .38 .88537

880. .1288 .01376 12.60 . 50865

8 90. .1219 .01801 12.82 .52822

500. .1198 .01825 13.03 . 58806

510. . 1171 .01850 13.28 .56818

520 . .1188 .01878 13.85 . 58857

530. .1126 .01898 13 .66 .60523

580. .1105 .01523 13.86 .62618

53
Table 7. Transport- Properties o f Oxvaen. Tsofcirs. Enqr . Units.

2 5. ps i a Isobar Temp, Dens i t

Thermal Viscosity Th e r m a 1 C o n d • micro- Dlffuslvity

P Ib/f t**3 RTU/ft.h,,p 1 b/f t .s f t**2/h

97.88? 81 .5498 .11772 326.42 .00363

100. 81 . 2282 .11644 318 . CO .00360

105. 80 .4672 .11358 ? 97. 8 9 . 008 54 110. 79.7027 .11088 277 , 99 .00349

115. 78.93?? .10833 258 . 78 .00344

120. 78.1564 . 1 0588 240.57 .00340

12 5. 77.3739 .1 0351 22^.48 .00335

130. 76.5340 .10120 207.58 .00331

13*. 75.7860 .09«94 192.88 .00327

140. 74.9791 .09*7] 179.32 .00323

14 5. 74.1625 .09450 166.85 . 00318

150. 73.3354 .09230 155.39 .00314

155. 72 .4966 .09010 144.86 .00309

360 . 71.6430 .08789 135.19 .00304

165. 70.7791 .08568 126.29 .00298

170. 69.8973 .08345 118.10 .00293 172.076 69.5241 .08252 114.88 .00290 172.076 .455 8 .00506 4 . 80 .04600

178. .4470 .00515 4.89 .04808

180. .4327 .00530 5.03 .05171

185. .4105 .00546 5 .17 .05541

190. .4071 .00561 5.32 .05920

195. .3955 . OC 5 77 5.46 .06308

2 CO. 3R46 .00593 5.60 .0 6704

205. .3744 .00609 5.74 .07109

210. . 3647 .00625 5.89 .07522

215. . 3556 .0064] 6.03 .07943

2 2 C

.3469 • OC 6 5 7 6 .17 .08373

225. . 3387 .00673 6.31 .08811

230. .3308 .00688 6.45 .09257

235 . . 3234 .00704 6. 5Q .09711

240. .3167 .00720 6.72 . 10174

245. . 3095 .00736 6 . 86 .10645

2 5 C . . 3030 .00751 7.00 .11123

256 . .2968 .00767 7.14 .11610

260. . 2908 .00782 7.27 . 17106

265. .2851 .00798 7.41 .12610

270. .2796 .00613 7.54 .13123

275 . . 2744 .00829 7. *8 . 13647

280. .2693 . 00844 7 . 81 .14173

285 . . 2644 .00858 7 . 94 .14690

290. .2 597 .00873 8 .07 .15219

295. . 255? .00887 8.20 . 1 5756

300. .2 508 .00901 8.33 .1630?

310. . 2425 .00930 8 .59 .17416

320. . 2347 .00958 8.85 .18559

330. .2275 .00986 9.10 .19730

340. .2206 .01014 9 . 35 .20928

350. .2142 .01041 9.60 .22153

360. . 2082 .01068 9 . 85 .23404

370. .2024 .01095 10.09 .24680

380. .1970 .01122 10.33 .25983

390. .1919 .01148 10.57 .27310

400. .1870 .01174 10.80 .28663

410. .1824 .01200 11.04 .30040

420. .1780 .01226 11 . 27 .31442

430. .1739 .01252 11.50 .32869

440. .1699 .01277 11.72 .34319

450. .1661 .01302 11 .95 .35794

460. .1624 .01327 12.17 .37292

470. .1589 .0135? 12.39 .38813

480

.1556 .01377 12.60 .40357

490. .1524 .01402 12.82 .41974

500. .1493 .01426 13.03 .43513

510. .146^ .01451 13.24 .45124

520. .1435 .01475 13.45 .46757

530. .1408 .01499 13.66 .48411

54 C • .1382 .01524 13. e7 .50086

30. ps ia Isobar

Temp. Density Th e r m a 1 Viscosity T ho r m a 1 C on (1 . micro- Dlffusivity

P 1 b/ f t** 3 BTU /f t .h

,R 1 b/f t .s f t**2 / h

97 . 883 81 . 5512 .11772 326.49 . 00363

100. 81. 2307 .1 1645 318.10 .00360

105. 80.4698 .11358 297.97 . 00354 no. 79. 7049 .11089 278.07 .00347

115. 78 . 9350 .10834 2 58 .86 .00344

120. 78. 1593 .10589 240.64 .00340

125. 77.3770 .10352 223.55 . 00336

130. 76.5873 .10121 207.65 .00331

135 . 75 . 7894 .09895 1 92 .93 . 00327

140. 74 . 9828 .0967? 179.37 .00323

145 . 74 . 1664 .09451 166.90 .00318

150. 73. 3395 .09231 155 .44 . 00314

155. 72.5010 .09011 144.91 . 00309

160. 71.6496 .08791 135.23 . 00304

165. 70. 7841 .08569 126.34 . 00298

17C. 69. 9027 .08347 118.14 . 00293

175. 69.0034 .08122 110.58 . 00297 175.709 6 8. 8743 .08090 109.55 . 00286

17*. 709 . 5395 .00519 4 .92 .03940

180. . c 2 4 ? . CC5 32 5.04 . C4204

185 . . 5077 .00546 5.18 . 04519

1 90 . . 4924 .00563 5.33 . 04838

195. . 478] .00579 5.47 .0*166

200. . 4646 .00595 5.61 .05499

205. . 4520 .00611 5.75 .05840

210. . 4401 .00627 5 .89 .06188

215. . 4289 .00643 6.03 .06542

220 . .4183 .00658 6.13 . 06903

22*. . 4082 .00674 6.32 .07271

230. . 3987 .00690 6.45 .07645

235 . . 3896 .00706 6.59 . Cfi 02 6 240. . 3809 .00721 6.73 . 08414

245 . . 3727 .00737 6.87 .08808

250. . 36 4 8. .00753 7.01 . 09210

255 . . 3572 .00768 7.14 .09617

2 6° . . 3500 .00784 7 .28 . 10032

265. . 3431 .00799 7.41 .10454

270 . . 3364 .00815 7.55 . 10884

275. . 3300 .00830 7.68 . 11322

280. . 3239 .00846 7.81 . 11762

285. .3180 .00860 7.95 . 12194

2 90 . . 3123 .00874 8 .09 . 12636

295 . . 3068 •008b8 8.21 .13085

300. . 3015 .00903 8.34 .13541

310. . 2915 .00931 8.60 . 14472

320. . 2821 .00959 8.85 . 15426

330. . 2733 .00987 9.11 . 16404

340. . 2651 .01015 9.36 .17405

350. . 2573 .01043 9.61 .18427

360 . . 2500 .01070 9.65 . 19471

370. . 2432 .01096 10.09 .20537

380 . . 2366 .01123 10.33 .21624

390. . 2305 .01149 10.57 . 22732

400. .2246 .01176 10.81 .23861

410 . .2191 .01201 11.04 .25010

420. . 2138 .01227 11.27 . 26130

430. . 2087 .01253 11.50 .27371

440. . 2039 .01278 11.72 . 28591

450. .1994 .01303 11.95 .29811

460 . . 1950 .01328 12.17 . 31061

470. .1908 .01353 12.39 . 32330

4R0. . 186e .01378 12 .61 .33618

490. . 1829 .01403 12.82 . 34925

500. .1792 .01427 13.03 .36250

510. . 1757 .01452 13.25 . 37594

520. . 1723 .01476 13.46 . 38956

530. . 1690 .01500 13.66 . 40336

540. . 1659 .01525 13.87 .41732

Two Phase Boundary
Tab I e 7 T r ans po t Properties of Oxygen* Isobars* Engr. Units

35. ps i a Isobar 40. psia Isobar Temp • Den s i t y Thermal V 1 scos i ty Thermal Temp • Dens 1 1 y Therma

1

Viscosity Therma 1 C on d • f 1 cr o- Diffusivi ty C on d

.

m 1 c ro- D If fusi vity

P 1 b/f t**3 BTU/f t .h

,

» R Ib/ft.s ft**2/h R 1 b/ ft**3 8TU/f t.h., R Ib/ft.s f t**2/h

* 97.896 81.5526 .11773 326.56 .00363 * 97.903 81 . 5580 .11773 326.63 .00363

100. 81.2333 .11686 318.20 .00360 100. 81.2358 .11687 318.29 .00360

105. 80.8723 .11359 298.06 .00358 105 . 80. 8789 .11360 298.15 .00358

110. 79.7076 .11090 278.15 .00389 110. 79.7103 .11091 278.23 .00389

115. 78.9379 .10835 258.98 .00388 115. 78.9807 .10836 259.01 .00388

120. 78.1623 .10590 280.71 .00380 120. 78.1653 .10591 280.78 .00380

125. 77.3801 .10353 223.61 .00336 125. 77.3832 .10358 223.68 .00336

13C. 76.5906 .10123 207.71 .00331 130. 76.5938 .10128 207.77 .00331

135. 75.7929 .09896 192.99 .00327 135. 75.7968 .09898 193.05 .00327

18 0. 78.9868 .09673 179.83 .00323 180. 78.9901 .09675 179.88 .00323

185. 78.1703 .09852 166.95 .00318 185. 78.1782 .09858 167.00 .00318

150. 73.3836 .09232 155.89 .00318 150. 73. 3877 .09238 155.58 . 00318

155. 72. 5053 .09012 188.96 .00309 155. 72.5097 .09018 185.00 .00309

160. 71 .6583 .08792 135.28 .00308 160. 71.6590 .08798 135.33 .00308

165. 70.7891 .08571 126.38 .00298 165 . 70. 7980 .08573 126.83 .00298

170. 69.9080 .08388 118.18 .00293 170. 69.9133 .08350 118.23 .00293

175. 69.0091 .08128 110.62 .00287 175. 69.0189 .08126 110.66 .00287

* 178.910 68.2928 .07987 105.10 .00282 180. 68.0963 .07899 103 .66 .00280 178.910 .6223 .00531 5.02 .03853 * 181.788 67.7633 .07818 101.29 .00278

180. .6177 .00538 5.05 .03512 * 131.788 . 7088 .00582 5.11 .03078

185. .5977 .00550 5.19 .03785 185. .6893 .00552 5.20 .03235

190. .5791 .00565 5.33 .08068 190. .6678 .00567 5.38 .03882

195. .5619 .00581 5.88 .08388 195. .6870 .00583 5.89 .03738

200. .5858 .00597 5.62 .08638 200. .6280 .00599 5.63 .03991

205. .5306 .00613 5.76 .08933 205 . .6103 .00618 5.77 .08252

210. .5165 .00628 5.90 .05238 210. . 5937 .00630 5.91 .08518

215. . 5031 .00688 6.08 .05580 215. . 5781 .00686 6.05 .08788

220. .8908 .00660 6.18 .05852 220. . 5633 .00662 6.19 .05068

225. .8785 .00676 6.32 .06170 225 . . 5898 .00677 6.33 .05388

230. .8671 .00692 6.86 .06893 230. . 5362 .00693 6.87 .05629

235. .8563 .00707 6.60 .06822 235. . 5237 .00709 6.61 .05918

280. .8861 .00723 6.78 .07156 280. .5118 .00725 6.78 .06213

285. .8363 .00739 6.88 .07896 285. . 5008 .00780 6.88 .06512

250. .8270 .00758 7.01 .07882 250. .8896 .00756 7.02 .06816

255. .8181 .00770 7.15 .08193 255. .8793 .00771 7.15 .07125

260. .8095 .00785 7.28 .0 8550 260. . 8698 .00787 7.29 .07839

265. .8018 .00801 7.82 .08918 265 . . 8600 .00802 7.83 .07758

270. .3935 .00816 7.55 .09288 270. .8509 .00818 7.56 .08083

275. .3860 .00832 7 .69 .09662 275 . .8822 .00833 7.69 .08815

280. . 3788 .00887 7.82 .10080 280. .8339 .00888 7.83 .08788

285. .3718 .00861 7.95 .10811 285 . .8258 .00862 7 .96 .09078

29C. .3651 .00875 8.08 .10791 290. .8181 .00877 8.09 .09806

295. .3586 .00890 8.21 .11176 295. . 8107 .00891 8.22 .09785

300. .3528 .00908 8.35 .11568 300. .8035 .00905 8.35 . 10089

310. .3806 .00932 8.60 .12368 310. . 3900 .00938 8.61 .10790

320. .3296 .00961 8.86 .13188 320. . 3773 .00962 8.86 . 11510

330. . 3193 .00989 9.11 .18028 330. . 3655 .00990 9.12 .12286

380. .3097 .01016 9.36 .18888 380. . 3588 .01017 9.37 . 13000

350. .3006 .01088 9.61 .15766 350. . 3839 .01085 9.62 .13769

360. .2920 .01071 9. 86 .16662 360. . 3381 .01072 9.86 .18555

370. . 2880 .01098 10.10 .17577 370. . 3288 .01099 10.10 .15357

380. .2763 .01128 10.38 .18511 380. .3161 .01125 10.38 .16175

390. .2691 .01151 10.58 .19862 3 90. . 3078 .01152 10,58 . 17009

800. .2623 .01177 10.81 .20831 800. . 2999 .01178 10.81 .17858

8 1 C . .2557 .01203 11. 08 .21817 810. . 2925 .01208 11.05 .18722

820. .2896 .01228 11.27 .22822 820. . 2858 .01229 11.28 .19602

830. . 2837 .01258 11.50 .23883 830. . 2786 .01255 11 .51 .20897

880. .2381 .01279 11.73 .28882 880. . 2722 .01280 11.73 .21807

850. .2327 .01308 11.95 .25537 850. .2661 .01305 11.95 .22332

860. .2276 .01329 12.17 .26610 860. . 2602 .01330 12.18 .23271

870. . 2227 .01358 12.39 .27698 870. .2586 .01355 12 .39 . 28225

880. .2180 .01379 12.61 .28808 880. .2892 .01380 12.61 .25193

890. .2135 .01808 12.82 .29925 890. .2881 .01805 12.83 .26175

500. . 2092 .01828 13. 08 .31062 500. . 2391 .01829 13.08 . 27171

510. .2050 .01853 13.25 .32215 510. .2388 .01858 13.25 .28181

520. .2011 .01877 13.86 .33388 520 . . 2298 .01878 13.86 .29208

530. .1972 .01501 13.67 .38567 530. . 2255 .01502 13.67 .30281

580. .1935 .01526 13.87 .35766 580. .2212 .01527 13.87 . 31290

* Two Phase Boundary

55
Tab I 7 Tr anspo t Properties of Oxygen* Isobars* Engr, Units

45 • psla I sobar

Temp • Oens 1 1 v Therma

Viscosity Thermal

Cond • micro- D 1 f f u s 1 v 1

R 1 b/f t**3 BTU/f t.h.R Ib/ft.s f t**2/h

* 97*910 81.5556 .11776 326.71 .00363

ICC. 81.2383 .11668 318.39 .00360

105. 80.6775 .11361 298 .26 .00356 no. 79.7130 .11092 278.31 .00369

115. 78.9635 .10837 259.09 .00366

120. 78.1682 .10592 260.85 ,00360

125. 77.3863 .10355 223. 76 .00336

130. 76.5971 .10125 207.83 .00331

135. 75.7998 .09899 193.11 .00327 no. 76.9937 .09676 179.56 .00323

155. 76.1780 .09655 167.06 .00318

150. 73.3518 .09235 155.59 .00316

155. 72.5161 .09015 165.05 .00309

160. 71.6636 .08795 135.37 .00306

165. 70.7990 .08576 126.67 .00298

170. 69.9187 .08352 118.27 .00293

175. 69.0206 .08128 110.70 .00287

180. 68.1025 .07901 103.70 .00280

* 185.500 67.2759 .07700 97.97 .00276

* 186.600 .7861 .00552 5.19 .02779

185. . 7829 .00556 5. 21 .02805

190. .7572 .00569 5.35 .03029

195. .7336 .00585 5.69 .03256

200. .7116 .00601 5. 66 .03687

205. .6911 .00616 5.78 -03721

210. .6719 .00632 5.92 .03960

215. .6539 .00668 6.06 .06203

220. .6370 .00663 6. 20 .06650

225. .6210 .00679 6.36 .06701

230. .6059 .00695 6.68 .06956

235. .5915 .00710 6.61 .05215

260. .5779 .00726 6.75 .05678

265. .5650 .00762 6.89 .05766

250. .5527 .00757 7.03 .06017

255. .5609 .00773 7.16 .06293

260. . 5297 .00788 7.30 .06576

265. .5189 .00806 7.63 .06859

270. .5086 .00819 7.57 .07150

275. .6987 .00835 7.70 .07666

280. .6893 .00850 7.83 .07763

285. .6801 .00866 7.96 .08033

290. .6716 .00878 8.10 .08330

295. .6630 .00892 8.23 .08631

300. .6568 .00906 8.36 .08938

310. .6395 .00935 8.61 .09563

320. .6251 .00963 8.87 .10206

330. .6117 .00991 9.12 .10860

360. .3992 .01019 9.37 .11531

350. .3876 .01066 9.62 .12217

360. .3763 .01073 9.86 .12917

370. .3658 .01100 10.11 .13631

380. .3559 .01126 10.35 .16359

390. .3665 .01153 10.58 .15101

600. .3377 .01179 10.82 .15857

610. . 3293 .01205 11.05 .16626

620. .3213 .01230 11 .28 .17609

630. .3136 .01256 11.51 .18206

660. .3066 .01281 11.73 .19015

650. .2995 .01306 11.96 .19838

660. .2928 .01331 12.18 .20676

670. .2865 .01356 12 .60 .21523

680. . 2805 .01381 12. 61 .22386

690. .2767 .01606 12 . 83 .23258

500. .2691 .01630 13.06 .26165

510. .2638 .01655 13.25 .25063

520. .2586 .01679 13.66 .25953

530. .2537 .01503 13.67 .26876

560. .2689 .01528 13.88 .27809

* Two Phase Boundary

50 • psla Isobar

Temp . Density Therma

Viscosity Thermal

Cond. m 1 c ro- Dlffusivlty

R 1 b/ft**3 BTU/f t.h •R Ib/ft.s f t+*2/h

97.918 81.5567 .11776 326.78 .00363

100. 81.2608 .11669 318.69 .00360

105. 80.6801 .11362 298.33 .00356

110. 79.7156 .11093 278.60 .00369

115. 78.9663 .10838 259.16 .00366

120. 78. 1712 .10593 260.92 .00360

125. 77. 3896 .10356 223.81 .00336

130. 76.6006 .10126 207.90 .00331

135. 75.8033 .09900 193.17 .00327

160. 76.9976 .09677 179.60 .00323

165. 76.1819 .09656 167.11 .00318

150. 73.3559 .09236 155.66 .00316

155 . 72.5185 .09017 165.10 .00309

160. 71.6683 .08797 135.62 .00306

165. 70.8060 .08576 126.51 .00299

170. 69. 9260 .08353 118.31 .00293

175. 69. 0263 .08129 110.76 .00287

180. 68.1087 .07903 103.76 .00281

185. 67.1683 .07676 97.25 .00276

* 186.808 66. 8221 .07591 95 .02 .00271 186.808 . 8676 .00562 5.27 .02536

190. . 8688 .00571 5.36 .02665

195 . . 8216 .00587 5.50 .02872

200. .7966 .00602 5.66 .03083

205. .7730 .00618 5.79 .03296

210. .7511 .00636 5.93 .03513

215. .7306 .00669 6.07 .03736

220. .7116 .00665 6.21 .03958

225. .6933 .00681 6.36 .06186

230. .6762 .00696 6.68 .06617

235. . 6600 .00712 6.62 .06652

260. . 6666 .00728 6.76 .06890

265. .6300 .00763 6 .90 .05132

250. .6162 .00759 7.03 .05378

255. .6029 .00776 7.17 .05628

260. .5903 .00790 7.30 .05882

265 . . 5782 .00805 7.66 .06160

270. . 5666 .00820 7.57 .06602

275. . 5555 .00836 7.70 .06670

280. . 5669 .00851 7.86 .06939

285. . 5367 .00865 7.97 .07200

290. . 5269 .00879 8.10 .07668

295. . 5156 .00893 8.23 .07760

300. . 5063 .00908 8.36 .08017

310. .6891 .00936 8.62 .08581

320. .6731 .00966 8.87 .09159

330. . 6581 .00992 9.13 .09751

360. . 6661 .01020 9.38 .10356

350 . .6309 .01067 9.62 . 10976

360. .6185 .01076 9.87 . 11605

370. .6068 .01101 10.11 . 12269

380. . 3958 .01127 10.35 .12905

390. . 3856 .01156 10.59 .13576

600. . 3755 .01180 10.82 . 16256

610. . 3661 .01206 11.05 .16969

620. . 3572 .01231 11.28 .15655

630. . 3687 .01257 11.51 .16372

660. . 3606 .01282 11.76 .17102

650. . 3329 .01307 11.96 . 17866

660. .3255 .01332 12.18 .18597

670. . 3185 .01357 12.60 .19361

680. . 3117 .01382 12.62 .20138

690. . 3053 .01607 12.83 .20925

500. . 2991 .01631 13.05 .21723

510. . 2931 .01656 13.26 .22533

520. . 2876 .01680 13.67 .23353

530. .2819 .01506 13 .67 .26183

560. . 2767 .01529 13.88 .25026

56
Table 7 Tr an soo t Properties of Oxygen. Isobars E ngr . Units

100 . psla I soba r

Temp . Dens 1 ty Therma

1

Viscosity Th er ma Cond. micro- 01 ffuslv

R Ib/f t**3 BTU/ft.h .R Ib/ft.s f t**2/l

* 97.089 81.5707 .11779 327.50 .00363

100. 81.2658 .11658 319.95 .00361

105. 80.5060 .11372 299.22 .00355

110. 79.7925 .11103 279.22 .00399

115. 78.9799 .10898 259.93 .00395

120. 78.2006 .10603 291 .63 .00390

125. 77.9209 .10367 229.98 .00336

130. 76.6331 .10137 208.52 .00332

135. 75.8378 .09912 193.76 .00328

190. 75.0339 .09689 180.15 .00323

195. 79.2206 .09969 167.69 .00319

150. 73.3970 .09250 156.19 .00319

155. 72.5621 .09031 195.58 .00310

160. 71.7197 .08811 135.88 .00309

165. 70.8536 .08591 126.96 .00299

170. 69.9770 .08370 118.75 .00299

175. 69.0832 .08196 111.17 .00288

180. 68.1699 .07921 109.16 .00281

185. 67.2395 .07603 97.66 .00275

190. 66.2739 .07962 91.62 .00268

195. 65.2892 .07229 85.99 .00260

200. 69. 2609 .06991 80.71 .00252 209.920 63.3238 .06778 76 .31 .00299

* 209.920 1.6730 .00636 5.87 .01351

205. 1.6659 .00638 5.88 .01365

210. 1.6075 .00652 6.02 .01987

215. 1.5593 .00667 6.16 .01609

220. 1.5055 .00683 6.29 .01732

225. 1.9605 .00698 6.93 .01857

230. 1 .9187 .00713 6.57 .01982

235. 1.3798 .00728 6.70 .02108

290. 1.3939 .00793 6.89 .02236

295. 1.3093 .00759 6.97 .02365

250. 1.2771 .00779 7.11 .02995

255. 1.2968 .00789 7.29 .02627

260. 1.2180 .00809 7. 38 .02761

265. 1 .1908 .00820 7.51 .02897

270. 1.1699 .00835 7.69 .03035

275. 1.1903 .00851 7.77 .03176

280. 1.1168 .00866 7.90 .03316

285. 1.0993 .00879 8.03 .03950

290. 1 .0729 .00893 8.16 .03587

295. 1.0523 .00907 8.29 .03727

300. 1.0326 .00921 8.92 .03869

310. .9955 .00998 8.68 .09158

320. .9612 .00976 8.93 .09955

330. .9299 .01009 9.18 .09757

390. .8997 .01031 9.93 .05066

350. .8720 .01058 9.67 .05382

360. .8960 .01085 9.92 .05703

370. .8216 .01112 10.16 .06030

380. .7986 .01138 10.39 .06369

390. .7770 .01169 10. 63 .06703

900. .7565 .01190 10.86 .07099

910. .7371 .01216 11.09 .07901

920. .7188 .01292 11.32 .07758

930. .7013 .01267 11.55 .08121

990. .6897 .01292 11.77 .08991

950. .6689 .01317 11.99 .08866

960. .6539 .01392 12.21 .09296

970. .6395 .01367 12.93 .09633

980. .6257 .01392 12.65 .10025

990. .6126 .01917 12.86 .10922

500. .6000 .01991 13.07 .10825

510. .5879 .01965 13.28 .11239

520. . 5763 .01990 13. 99 .11697

530. .5652 .01519 13.70 .12066

590. .5595 .01538 13.90 .12990

* Two Phase Bounda ry

ISO. psla Isobar

Temp • Dens 1 ty Thermal Viscosity Therma

1

Cond. m 1 c ro- Dlffuslvlty

R 1 b / f t. * * 3 BTU/ft.h..R Ib/ft.s f t**2/h

* 98.060 81.5896 .11784 328.22 .00363

100. 81.2908 .11667 320.42 .00361

105. 80.5318 .11381 300.11 .00355

110. 79. 7699 .11112 280 .04 .00350

115. 79.0025 .10858 260.69 .00345

120. 78.2301 .10614 242.34 .00341

125. 77.9519 .10378 225.14 .00336

130. 76. 6657 .10148 209 .14 .00332

135. 75.8722 .09923 194.35 .00328

190. 75.0703 .09702 180.71 .00324

195. 79.2591 .09482 168.17 .00319

150. 73.4379 .09263 156.64 .00315

155. 72.6055 .09045 146.06 .00310

160. 71.7610 .08826 136.35 .00305

165. 70.9029 .08606 127.41 .00300

170. 70.0298 .08386 119.18 .00294

175. 69.1398 .08163 111.59 .00288

180. 68.2308 .07939 104.57 .00282

185. 67. 3002 .07712 98.07 .00276

190. 66.3951 .07482 92 .02 .00269

195. 65.3618 .07250 86.39 .00261

200. 69.3959 .07014 81.11 .00253

205. 63.2921 .06774 76.16 .00244

210. 62.1936 .06529 71.48 .00235

215. 61.0919 .06279 67.04 .00225

* 216.369 60. 7172 .06209 65.87 .00222

* 216.369 2.9880 .00694 6.31 .00905

220. 2.9179 .00704 6.41 .00973

225. 2.3293 .00718 6.54 .01065

230. 2.2499 .00732 6.67 .01156

235. 2.1775 .00747 6.80 .01248

290. 2.1111 .00762 6.93 .01340

295. 2.0498 .00776 7.07 .01433

250. 1 . 9929 .00791 7.20 .01526

255 . 1.9399 .00806 7.33 .01620

260. 1.8903 .00821 7.46 .01714

265. 1 . 8438 .00837 7.59 .01810

270. 1.7999 .00852 7.72 .01908

275. 1.7585 .00868 7.85 .02007

280. 1.7193 .00883 7.98 .02105

285. 1.6821 .00895 8.11 .02196

290. 1.6467 .00908 8.24 .02290

295. 1.6130 .00921 8.36 .02386

300. 1 . 5808 .00935 8.49 .02484

310. 1.5207 .00962 8.74 .02682

320. 1.4656 .00989 8.99 .02884

330. 1.4147 .01016 9.24 .03091

390. 1.3675 .01043 9.48 .03301

350. 1.3237 .01070 9.73 .03516

360. 1. 2828 .01096 9.97 .03734

370. 1.2446 .01123 10.21 .03956

3 80. 1.2087 .01149 10.44 .04182

390. 1.1750 .01175 10.68 .04412

900. 1.1432 .01201 10.91 .04646

910 . 1.1132 .01226 11.14 .04884

920. 1.0849 .01252 11.36 .05125

930. 1.0580 .01277 11.59 .05370

990. 1. 0324 .01302 11.81 .05619

950. 1.0082 .01327 12.03 .05872

960. .9850 .01352 12.25 .06129

970. . 9630 .01377 12.47 .06389

9 80 . . 9420 .01402 12.68 .06653

990. .9219 .01426 12 .90 .06921

500. . 9027 .01451 13.11 .07192

510. . 8842 .01475 13.32 .07467

520. . 8666 .01499 13.52 .07745

530. . 8496 .01523 13.73 . 08026

590. . 8334 .01547 13.93 .08311

57
Table 7. Transport Properties of 0*yqen» Isobar s« Enar . Units.

200. ps I

Isobar 250 . os I a Isobar Temp. P en s i t y T h e r ma 1 Viscosity Ther Ta

Temp . Density Th er tr a 1 Viscosity Thermal

C on d . micro- Diffusivity C on d

micro- Diffusivity

P 1 h /f t**3 RTU/ft.h.R 1 h/f t.s ft **2 /h P 1 h / f t **3 RTU/f t .h,,p Ib/ft.s f t**2/h

* 9 P . 1 3 1 PI . 5906 .11788 ^2« . 94 .003*4 * 90.202 81.6126 .11793 329.65 . 00364

100. 81 .3157 .11676 321 .39 .00361 100. 8 1 . 3406 . 1 1*85 322.36 .00361

105. 80.5575 .1 1390 301 . 00 .00355 105 . 80. 5832 .11400 301 .89 . 00355

110. 79.79*2 . 11122 280.86 .00350 110. 79 . *229 .11132 281.68 .00350

115. 79.0304 . I 0868 261 .45 . 00345 115 . 70.0583 .10878 262.22 . 00346

120. 78 .2594 .10624 243.05 .00341 120. 73 . 2886 .10634 243.76 . 00341

1?5. 77.4822 .10389 225 . 80 .00337 125 . 77. 5130 .10399 226.47 .00337

1 3 C . 76.6982 .10160 209 .77 .09333 13*. 76.7305 .10171 2 10.39 .00333

135. 75 .9065 .09925 1 94 . 93 .00328 135. 76, 9407 .09947 195.52 . 00329

140. 75.1065 .09716 181.26 . 00324 140 . 75 . 1427 .09726 181.82 . 00325

145. 74 .

Q 75 .09494 168 . 69 .00320 145. 74 . 33 57 .09507 169.22 .00320

150. 73.4785 .09276 157.15 .00315 150 . 73.5191 .09290 157.65 .00316

155. 72. 6487 .09059 1 46. 5. 00311 155 . 72.6918 .09072 147 .03 • C 0311

160. 71.8070 .08841 136.81 .00306 160. 71 . 0527 .08855 137.27 .00306

165. 70.9519 .08622 127 . 85 .00301 165 . 71. 0007 .08637 128.30 . 00301

170. 70.0822 .08402 119. 61 . 0 0 2 9 5 170. 70.1343 .08610 120.04 • 002 36 175. 69.1960 • C 8 1 p 0 112.01 .00289 175. 69.2518 .08197 112.43 . 00290

1 8 C . 68.2912 .07957 104.90 .00283 180. 68.3511 .07974 105 .39 . 00284

185. 67.3654 .07731 98.47 .00277 1 85 . 67. 4300 .07749 X CD ->1 .00277

190. 66.4157 .07502 92.42 .00270 1 90 . 66.4856 .07522 92 .82 .00271

195. 65.4386 .07271 86.78 .00262 195. 65.5147 .07292 87.18 .00263

200. 64.4300 .07036 81 .51 . 00254 200 . 64.5131 .07058 81 .90 . 00255

205. 63.38*7 .06797 76.56 .00246 205. 63.4761 .06821 76.95 .00247

210. 62 .2963 .06554 71 . 88 .00237 210. 62.3976 .06580 ^2 .29 . CC 238

215. 61 .1570 .06306 67.46 .00227 215. 61.2702 .06334 67.87 . 00228

220. 59.9563 .06052 63.23 .00216 220. 60.0842 .06082 63.66 . 00218

225. 58.6805 • C 5 7 9 1 59.17 .00205 225 . 58. 8269 .05824 59.62 . 00207

* 225.697 5 P .4958 .05754 58.62 .00203 230. 57.4811 .05557 55.71 .00195

* 225.697 3.3293 .00746 6.69 .00664 + 233 .478 56. 4000 .05366 53.05 .

C 185 230. 3.2074 .00757 6.80 .00731 * 233.478 4. 2086 .00797 7.05 . 00510

235 . 3.0819 .00770 6.92 .00807 235. 4.1454 .00800 7.08 .00531

240. 2.9701 .00784 7.05 .00883 240. 3.9584 .00812 7.20 . 00600

245. 2.8694 .00798 7.18 .00959 245. 3.7962 .00824 7.31 . 00667

250. 2.7778 .00812 7.30 .01035 250 . 3.6532 .00837 7.43 .00734

255. 2.6939 .00826 7.43 .01110 255 . 3.5253 .00851 7.55 . C 0799

260. 2 .6165 .00841 7.56 .01186 260. 3.4098 .00865 7.68 .00865

265. 2. 5448 .00856 7.69 .01263 265 . 3. 3044 .00879 7.80 .00931

270. 2.4780 . 00872 7.81 .01341 270. 3.2076 .00895 7.92 .00998

275. 2.4155 . 00888 7 . 94 .01420 275 . 3.1182 .00912 8.04 . 01066

280. 2.3569 .00903 8 . 07 .01497 280. 3.0352 .00926 8.17 .01132

285. 2.3016 .00913 8.19 .01568 285 . 2.9577 .00934 0 .29 .01189

290. 2.2495 .00925 8.32 .01640 290. 2.8852 .00944 8.41 .01249

295. 2.2002 .00937 8 . 44 .01714 295. 7.8171 .00955 8 .53 .01310

300. 2.1533 .00950 8.57 .01789 300. 2.7520 .00967 8.66 .01372

310. 2.0665 .00976 8.82 .01942 310. 2.6346 .00992 8.90 . 01498

320. 1 .9874 .01002 9.06 .02098 320 . 2. '52 81 .01017 9.14 . 01626

330. 1.9150 .01029 9.31 .02257 330. 2.4313 .01043 9.38 .01756

340. 1.8483 .01055 9.55 .02418 340. 2.3428 .01069 9.62 . 01 88 p 350. 1.7867 .01002 9 . 79 .02582 350. 2.2615 .01095 9.86 .02022

360. 1.7295 .01108 10.03 .02749 360. 2. 1863 .01121 10.09 .02158

370. 1.6762 .01134 10.26 .02919 370. 2.1166 .01146 10.32 . 02296

380. 1.6264 .01 1 6 C 10.50 .30 91 380. 2.0518 .01172 10 .56 .02436

390. 1.5797 .01186 10.73 .03266 3 90 . 1.9912 .01197 10.78 .02579

400. 1.5358 .01212 10 .96 .03444 400. 1.9344 .01223 11.01 . 02723

410. 1 .4946 .01237 11.19 .03625 410. 1.8811 .01248 11.24 .02870

420. 1.4555 .01262 11 .41 . C 3 e 08 420 . 1. 8309 .01273 11.46 .03019

430. 1.4187 .01288 11.63 .03995 *30. 1.7835 .01298 11.68 .03169

440. 1 .3837 .01313 11 .06 .04184 440 . 1.7387 .01323 11.90 .03322

450. 1.3506 .01338 12.07 .04376 450. 1.6963 .01348 12 .12 .03478

460. 1 .3191 .01362 12.29 .04570 460. 1 . 6560 .01373 12.34 .03635

470. 1.2891 .01387 12.51 .04767 470 . 1.6177 .01397 12.55 .03794

480. 1.2605 .01412 12.72 .04967 480. 1 .5813 .01422 12.76 .03956

490. 1.2332 .01436 12.93 .05170 4 90 . 1.5465 .01446 12 .97 . 04120

500. 1.2071 .01460 13.14 .05375 500. 1.5134 .01470 13.18 . 04285

510. 1 .1822 .01485 13.35 .05583 510. 1.4817 .01494 13.39 .04453

520. 1.1583 .01509 13.56 .05793 520. 1.4514 .01518 13.59 . 04623

530. 1 .1354 .01533 13.76 .06006 530. 1.4224 .01542 13.80 .04794

540. 1.1134 • Cl 5 57 13.97 .06222 540. 1.3945 .01566 14.00 .04968

* Two Phase Boundary
Table 7. Transport Properties of Oxygen. Isobars* Fngr. Units.

300. psla Isobar 350. ps I a Isobar

Temp . Density Thermal V I s c os 1 1 y Thermal

C on -j • micro- 0 i f f us i v i ty

R Ib/f t**3 B T l' / f t . h ,,R Ih/ft.s f t**2/h

98.274 81.6263 .11798 330.37 .00364

100. 81.3654 .11695 323 . 33 .00362

105. 80.6089 .11409 302 .78 .00356

110. 79.8495 .11141 282.51 .00351

115. 79.0862 .10887 262.98 .00346

120. 78.3178 .10645 244 .47 .00342

125. 77.5436 .10410 227.13 .00337

130. 76.7628 .10182 211.01 .00333

135. 75.9747 .09958 196.11 .00329

140. 75.1786 .09738 182.38 .00325

145. 74.3738 .09520 169.75 .00321

150. 73.5504 .09303 158.15 .00316

155. 72.7346 .09086 147.51 .00312

160. 71 . 8983 .08870 137.73 .00307

165. 71 .0493 .08652 128.74 .00302

170. 70.1861 .08434 120.47 .00296

175. 69.3072 .08214 112.84 .00291

180. 68.4107 .07992 105 . 80 .00285

185. 67.4941 .07768 99.27 .00278

190. 66.5550 .07541 93.21 .00271

195. 65.5900 .07312 87. 57 .00264

200. 64.5953 .07080 82.29 .00257

205. 63.5663 .06845 77.35 .00248

210. 62.4974 .06605 72.68 .00240

215. 61.3815 .06361 68.27 .00230

220. 6C.2096 .06111 64.08 .00220

225. 58.9699 .05856 60.06 .00209

230. 57.6468 .05593 56 . 18 .00197

235. 56.2178 .05320 52.39 .001 84 240. 54 .6405 .05036 48.66 .00169 240.211 54. 5797 .05024 48 . 50 .00169 240.211 5.1368 .00851 7.39 • C 0 4 C 2 245 . 4.8799 .00859 7 .49 .00463

250. 4.6541 .00870 7. 59 .00526

255. 4 .4598 • 00 8

B 1 7.70 .00587

260. 4 .2891 .00894 7.82 .00647

265. 4.1371 .00908 7 .93 .00707

270. 4.0001 .00923 8 . 05 .00767

275 . 3 . 8756 . 00941 8.16 • 0 0 8 2 9 28C. 3.7614 .00954 8.2 8 .00887

285 . 3.6561 .00959 8 . 40 .00936

290. 8.5585 . 00966 8 .52 .00987

295 . 3.4676 .00976 8 . 64 .01039

300. 3.3825 • 00 9 P6 8.75 .0109?

310. 3.2275 .01009 8 . 99 .01200

3 2 C

.

3.0892 .01033 9.23 .01310

330. 2.9648 .01058 9.46 .014?i

340. 2.851

8

.01083 9 . 70 .01534

3 5 C

.

2 .7487 .01108 9.93 .01648

360. 2.6538 .01134 10.16 .01764

370. 2.5663 .01159 10.39 .01881

380. 2 .4 fi 5 1 .01134 10.62 .02000

3 9 C

.

2.4096 .01 2^9 10.85 .02121

400. 2.3390 .01235 11 .07 .02243

410. 2 • ? 7 3 0 .01260 11.29 .02367

4 20. 2 .2109 .01284 11.51 . 02492

430. 2 . 1525 .01309 11.73 .02619

4 40

.

2 . 097-a .01334 11.95 .02748

450. 2.045? .01359 12.17 • 0 2

0 79 460. 1.9958 .01 3

B 3 12.38 .0301?

670 . 1.9489 .01407 12.59 .03146

480. 1.9043 .01432 12.81 .03282

490. 1 .8619 .01456 13. Cl .03419

500. 1.8214 .01400 13.22 .03559

510. 1.7828 .0] 504 13.43 .03700

520. 1 .7459 .0152° 13.63 .03842

530. 1

.

7 106 .01552 13 . «3 .03986

560. 1 .6767 .01576 14.04 .04132

Te m p . Density Thermal Viscosity T he r m a 1 C ond

.

micro- Dlffusivity

R 1 b/ f t**3 BTU/ft.h.R Ib/ft.s f t**2 /h

98.345 81 . 6401 .11803 331.09 . 00364

100. 8 l . 3902 .11704 324.31 .00362

105. 80.6345 .11418 303.68 .00356

110. 79. 8761 .11151 2 83 . 33 . 00351

115. 79.1140 .10897 263.74 .00346

120. 78. 3469 .10655 245 .19 . 00342

125. 77. 6742 .10421 227.80 .00338

130. 76.7950 .10193 211.64 . C033 4 135. 76.0087 .09970 196.70 .00330

140. 75.2145 .09750 182.93 .00326

145 . 74.4118 .09532 170.28 . 00321

150. 73 . 5996 .09316 158.65 .00317

155 . 7? . 7773 .09100 147.99 .00312

160. 71 . 9436 .08884 138.19 . 00307

165. 71 . 0975 .08667 129.19 .00302

170. 70. 2376 .08450 120.90 .00297

175. 69.3624 .08230 113.26 . 00291

180 . 69. 4698 .08009 106.20 . C0286

185. 67.5578 .07786 99.67 .00279

1 90 . 66.6237 .07561 93.61 . 00272

195. 65.6645 .07333 87.96 .00265

200. 64 . 6766 .07102 8? .68 .00258

205 . 63.6555 .06868 77.74 .00250

210. 62. 5958 .06630 73.08 .00241

215 . 61 . 4910 .06388 68.68 .00232

220. 60. 3326 .06140 64.49 . 00222

225. 59. 1098 .05887 60.49 .00211

230. 57. 8081 .05627 56.63 . 00200

235 . 56 . 4075 .05359 52 .88 .00187

240 . 54. e784 • 050ei 49.19 .00173

245 . 53. 1743 .04788 45.50 .00157 246.180 52. 7390 .04717 44.62 .00153 246.180 6.1261 .00911 7.74 .00321

250. 5.8451 .00914 7.80 . 00369

255 . 5. 5400 .00922 7.89 . 00428

260. 5 .2845 .00932 7.99 . 00486

265 . 5 . 0645 .00945 3.09 .00543

270. 4. 8715 .00959 3.20 . 00599

275. 4 .6997 .00977 8 .30 .00657

2 80. 4.5449 .00989 8.41 . 00 7 L

1

29 5 . 4.4042 .00989 8 .5? .00754

290 . 4. 2763 .00993 8.64 . 00799

295 . 4 . 1664 .01000 8.75 . 00845

300. 4 . C 4 6 2 .01008 8.86 . 0089?

310. 3. 8476 .01029 9.09 . 00988

320. 3 . 6726 .01051 9.3? .01085

330 . 3.5167 .01074 9.55 .01183

340. 3. 3763 .01098 9.78 .01231

350. 3.2489 .01123 10.01 .01381

360 . 3.1325 .01147 10 .24 .01483

370. 3.0255 .01172 10.46 .01585

390 . 2. 9268 .01197 10.69 .01689

390. 2.8352 .01222 10.91 .01793

400. 2.7499 .01247 11.13 .01900

410 . 2 .6703 .01271 11.35 . 02007

420. 2. c 9 5 7 .01296 11 .57 .02116

430 . 2.5256 .01321 11.79 .02227

440. 2.4596 .01345 1? .01 .02339

450 . 2.3973 .01369 12.22 .C 2452

460. ? . 33 84 .01394 12 .43 .02567

470. 2.2826 .01418 12.64 . 02683

480 . 2.22 96 .01442 12.85 . 02801

490. 2 •

1

7 9? .01466 13.06 .02920

500 . 2.1312 .01490 13.27 .03040

510. 2 . 0854 .01514 13.47 . 03162

520. ? • C 4 1 7 .01538 13.67 .03285

530 . ? . 0000 .01562 13.87 .03410

540. 1 . 9600 .01585 14.07 .03535

Two Phase Poundarv
Table 7. Transport Properties o

f Oxygen# Isobars# Fngr. Units.

400. psia Isobar 450. osla Isobar

Temp. Density Thermal Viscosity Thermal Temp . Dens 1 1 y Thermal Viscosity Thermal

C on d

micro- Olffuslvlty C ond . micro- Dl f fusl v Ity

P 1 b/f t**3 BTU/f t .h

,P Ib/ft.s f t**2/h R lb/ f t +*3 BTU/ft.h.R Ib/ft.s f t**2 / h

* 98.416 81 .6540 .11808 331 . 60 .00364 * 98.487 81 . 6678 .11812 332.51 • 00364

100. 81.4150 .11713 325.28 .00362 100 . 81.4397 .11722 326 .26 . 00362

1 C 5

80 .6*00 .11428 304.57 .00356 105. 80.6855 .1 1437 305.47 .00357 no. 79.9027 .11161 284.16 .00351 110. 79. 9292 .11170 284 .98 .00351

115. 79,1417 .10907 264. 51 .00347 115. 79. 1693 .10117 265.27 .00347

1 70. 78.3760 .10665 245 . 90 .00342 120. 78 . 4049 .10675 246.61 .00343

126. 77.6067 .1 0431 228.46 .00338 125. 77.6351 .10442 229.13 .00339

130. 76.8271 .10204 212. 26 .00334 130. 76.8591 .10215 212.89 .00335

135 . 76.0425 . 09981 197.28 .00330 135. 76.0763 .09993 197.87 .00330

1 4 C • 75.250’ .0976? 183.49 .00326 140. 75.2859 .09774 184 .04 .00326

145. 7 4 .4495 .09545 170 . 80 .00322 145 . 74.4872 .09558 171.33 .00322

150. 73.6397 .09329 159. 16 .00317 150. 73.6795 .09342 159.66 .00318

155. 72 . 81 97 .09114 140.46 .00313 155. 72.8620 .09128 148.94 .00313

160. 71 .98P7 .08898 138.65 .00308 160 . 72.0336 .08913 139.11 .00309

165. 71.1455 .08682 129.63 .00303 165. 71. 1933 .08697 130.07 .00304

1 70 . 70.2889 .08465 121.33 .00298 1 70. 70.3398 .08481 121 .76 .00298

175. 69.4171 .06247 113.68 .00292 175. 69.4715 .08263 114.09 .00293

190. 68.5285 .06027 106.61 .00286 180. 68 . 5868 .08044 107.02 .00287

18 6. 67.6209 .07805 100.07 .00280 185. 67.6836 .07823 100.47 . 00281

19C. 66.6919 .07580 94 . no .00273 190. 66.7594 .07599 94.39 .00274

195. 65 .7384 .07353 88.35 .00266 195. 65. 8116 .07374 88.73 .00267

200 . 64.7570 .07124 83.07 .00259 200. 64. 8366 .07145 83.46 .00260

205. 63.7436 .06891 78.13 .00251 205 . 63. 8306 .06914 78.51 .00252

210. 62.6929 .06654 73 .47 .00242 210. 62 . 7886 .06679 73.86 .00244

215. 61 . 5988 .06414 69.08 .00233 215. 61 . 7049 .06440 69.47 .00235

220. 60.4534 .06169 64.90 .00224 220 . 60.5720 .06197 65.31 .00225

226. 59.2466 .05918 60.91 .00213 225. 59.3805 .05949 61.33 . 00215

230. 57.965? .05662 57.08 .00202 230. 58.1184 .05695 57.52 .00204

235. 56.5911 .05397 53.36 .00190 235 . 56.7692 .05434 53.82 .00192

2 4 C

55.0982 .05123 49.71 .00176 240. 55. 309P .05165 50.21 .00179

245 . 53.4464 .04838 46.08 .00161 245 . 53.7052 .04885 46.64 .00165

250. 51 .5673 .04537 42. 38 .00143 250. 51 . 8986 .04592 43.02 . 00148

* 251.561 50.9160 .04439 41.19 .00137 255 . 49.7834 .04282 39 .26 .00128

7 251.561 7.1921 .00980 8.10 .00256 + 256.473 49. 0725 .04186 38.09 .00121

255. 6.8492 .00979 8.14 .00301 * 256.473 8.3557 .01064 8.49 .00207

260. 6.4474 .00984 8.20 .00359 260. 7.8824 .01058 8.49 .00252

265. 6.1209 .00993 8.28 .00416 265. 7.3666 .01058 8.53 .00311

270. 5.8456 .01005 8.37 .00471 270 . 6.9605 .01067 8 .59 .00367

275. 5.6077 .01023 8 . 47 .00527 275. 6.6252 .01083 8.67 . 00423

280. 5.3984 .01033 8.57 .00578 280. 6.3396 .01089 8.75 .00472

2 85 . 5.2115 .01025 8.67 .00616 285 . 6.0909 .01070 8.84 .00508

290. 5 . 042 p .01024 8.77 .00657 290. 5. 8708 .01063 8.93 .00546

295. 4.8893 .01028 8.88 .00699 295 . 5.6735 .01061 9.03 . 00585

300. 4.7485 .01034 6.99 .00742 300. 5 .4948 .01064 9.13 . 00624

310. 4 .4979 .01051 9.21 .00828 310. 5.1817 .01076 9.34 .00703

320. 4.2802 .01071 9 .43 .00915 320. 4 . 9142 .01092 9.55 .00783

330. 4.0883 .01092 9.65 .01003 330. 4.6811 .01112 9.76 .00864

340. 3.9170 .01115 9.67 .01092 340 . 4,4751 .01133 9.97 .00945

350. 3.7628 .01 138 10. 10 .01181 350. 4.2910 .01155 10.19 .01026

360. 3.6227 .01162 10.32 .01272 360. 4.1249 .01178 10.41 .01108

370. 3.4946 .01 1 86 10.54 .01363 370. 3.9738 .01201 10.63 .01190

380. 3.3768 .01211 10 . 76 .01455 380. 3.8356 .01225 10.84 .01274

390. 3.2681 .01235 10.98 .01548 390 . 3.7084 .01248 11 .06 .01358

4 CC. 3.1671 .01259 11.20 .01643 400. 3.5908 .01272 11.27 .01443

410. 3.0732 .01284 11.42 .01738 410 . 3.4816 .01296 11.49 .01529

420. 2.9853 .01308 11.63 .01835 420. 3.3798 .01320 11.70 .01616

430. 2.9030 .01332 11.65 .01933 430. 3.2846 .01344 11.91 .01704

440. 2.8256 .01356 12.06 .02032 440. 3. 1954 .01368 12.12 .01793

450. 2.7528 .01381 12.27 .02132 450. 3.1114 .01392 12.33 .01883

460. 2 .6839 .01405 12.48 .02233 460. 3. 0323 .01416 12.54 .01974

4 7 C • 2.6188 .01429 12.69 .02336 470. 2 . 9576 .01440 12.75 .02066

480 . 2.5571 .01453 12 .90 .02440 4 80. 2. 8868 .01463 12.95 .02159

490. 2.4985 .01477 13.11 .02545 490. 2. 8197 .01487 13.16 .02254

5CC. 2.4427 .01500 13.31 .02651 500. 2.7560 .01511 13.36 .02349

510. 2.3896 .01524 13.51 .02759 510 . 2.6953 .01534 13.56 .02445

520. 2.3389 .01548 13. 72 .02867 520. 2.6375 .01558 13.76 .02543

530. 2.2905 .01571 13.92 .02977 530. 2.5823 .01581 13.96 .02641

540. 2.2443 .01595 14.11 .03088 540. 2.5296 .01605 14.16 .02740

* Two Phase Boundary

60
Table 7, Transoort Properties of Oxygen# Isobars# Engr* Units.

500. osla Isobar 600. psia Isobar

Temp. Density Thermal Viscosity Thermal

C ond • micro- Olffuslvlty

R Ib/f t**3 BTU/ft.h.P Ih/ft.s f t**2/h

* QP.55B PI .681

6

.11817 333.23 .00364

100. 81 .4644 .11731 327.24 .00363

105. 80.7110 . 11446 306.36 .00357

lie. 79.9556 .31180 285.81 .00352

115. 79.1969 .10927 266.04 .00347

120. 78.4338 .10686 247.32 .00343

125. 77.6654 .10453 229.80 .00339

130. 76.8910 .10226 213.51 .00335

135. 76.1099 .10005 198 . 46 .00331

140. 75.3214 .09786 184.60 .00327

145. 74.5747 .09570 171.85 .00323

150. 73.7192 .09355 160.16 .00318

155. 72.9041 .09141 149.42 .00314

160. 72.0783 .08927 139.57 .00309

165. 71.2408 .08712 130.51 .00304

170. 70. 3904 .08497 122.18 . 00299

175. 69.5266 .08280 114.51 .00294

1 8 C

.

68.6447 .08061 107.42 .00288

185. 67.7458 .07841 100 . 86 .00282

190. 66.8265 .07619 94.78 .00275

195. 6 5 .8841 .07394 89. 12 .00268

200. 64.9154 .07166 83 .84 .00261

20 F• 63.9166 .06936 78. 89 . 00253

210. 62 .8831 .06703 74.25 .00245

215. 61 .8094 .06466 69.86 .00236

220. 60.6885 .06225 65.71 .00227

225. 59.5118 .05979 61.75 .00217

2 3 C

.

58.7680 .05728 57.95 .00206

235 . 56.9422 .05470 54.28 .00195

240. 56.5138 .05205 50. 70 .00182

245. 53.9523 .04931 47.18 .00168

250. 52.2097 . 04645 43.64 .00152

255. 60.7008 .04345 40.00 .00134

260. 47.7433 .04027 3 6.06 .00111

* 260.997 47.1654 .03960 35.20 .00105

* 260.997 9.6481 .01171 8 .92 .00165

265. 8.9781 .01154 8 . 87 .00218

27C. 8.2842 .01151 8.88 .00278

275. 7 .7930 .01163 8.91 .00336

280. 7.3951 .01161 8.97 .00386

2« 5. 7.0604 .01126 9.04 .00420

2 90. 6.7718 .01109 9.12 .00456

795 . 6.5182 .01101 9.20 .00492

300. 6.2922 .01099 9.29 .00529

3 1 C

.

6.9033 .01 104 9 . 48 .00604

320. 5.5771 .01117 9.67 .00678

330. 5. 2967 .01134 9 . 88 .00752

340. 5.0516 .01153 10.08 .00827

350. 4 .8744 .01173 10.29 . 00902

360. 4.6397 .01195 10. 50 .00977

370. 4.4636 • Cl 217 10.72 .01052

380. 4.3033 .C124C 10.93 .01129

390. 4.1564 .01 263 11.14 .01206

400. 4.0210 .01286 11.35 .01283

410. 3.8956 .01309 11.56 .01362

420. 3 .7797 .01333 11.77 .01441

430. 3.6705 .01357 11.98 .01521

440. 3.5688 .01380 12.19 .01602

450. 3.4734 .0] 404 12 . ^9 .01684

460. 3.3835 .01427 12.60 .01767

470. 3.29^8 .01451 12.80 .01851

480. 3.2187 .01474 13. Cl .01935

490. 3.1429 .01498 13.21 .02021

500. 3.0709 .01521 13.41 .02107

5 1 C

.

3.0024 .01545 13.61 .02195

520. 2.9373 .01568 13 . 81 .02283

530. 2.8752 .01591 14.01 .02372

540. 2.8159 .01614 14.20 .02462

* Two Phase Boundary

Temo

.

Density Thermal Viscosity Therma

1

Cond. micro- D 1 f fus 1 v 1 ty

R 1 b/ f t**3 BTU/ft.h.R Ib/ft.s f t**2/h

98.700 81.7091 .11827 334.65 .00365

100. 81 . 5136 .11749 329.20 .00363

105. 80.7617 .11465 308.16 .00357 no. 80.0083 .11199 287.47 .00352

115 . 79.2519 .10947 267.57 .00348

120. 78.4913 .10706 248.75 .00344

125. 77.7258 .10474 231 .13 .00340 no. 76.9546 .10248 214.76 .00336

135. 76.1768 .10028 199.63 .00332

140. 75.3920 .09810 185 .71 .00328

145

.

74 .5993 .09595 172 .91 .00324

150. 73.7982 .09382 161.16 .00319

155. 72.9877 .09169 150.38 .00315

160. 72.1670 .08956 140.48 .00310

165. 71.3351 .08742 131.39 .00306

170. 70.4909 .08528 123.03 .00300

175. 69.6328 .08312 115.33 .00295

180. 68.7594 .08095 108.22 .00289

185. 67.8688 .07877 101.65 . 00283

190. 66.9589 .07656 95.55 .00277

195. 66.0271 .07434 89.88 .00270

200. 65.0706 .07209 84.60 .00263

205. 64.0857 .06981 79.65 .00256

210. 63.0685 .06750 75.01 .00248

215 . 62.0139 .06517 70 .64 .00239

220. 60.9158 .06279 66.50 .00230

225 . 59.7666 .06038 62.56 .00221

230. 58.5569 .05792 58.79 .00210

235 . 57.2741 .05540 55.17 .00199

240. 55.9016 .05283 51 .65 .00188

245. 54.4157 .05018 48.21 .00175

250 . 52.7814 .04745 44.79 .00160

255. 50.9415 .04462 41.34 . 00144

260. 48. 7905 .04169 37.74 .00125

265 . 46.0857 .03865 33 .76 .00101 269.110 42.8802 .03611 29.67 .00071 269.110 12. 8674 .01516 10.02 .00093

270. 12.4497 .01491 9.93 .00110

275 . 10.9554 .01435 9.67 .00186

280. 10.0494 .01386 9.59 .00244

285 . 9. 3905 .01291 9.57 .00281

290. 8.8712 .01238 9.59 .00316

295. 8.4425 .01208 9.63 .00351

300. 8.0777 .01190 9.68 . 00385

310. 7.4798 .01175 9.81 .00453

320 . 7.0014 .01176 9.97 .00519

330. 6.6037 .01184 10.15 .00585

340. 6.2644 .01197 10.33 .00650

350. 5.9692 .01214 10 .52 .00716

360. 5.7087 .01232 10.72 .00781

370. 5.4760 .01252 10.91 .00846

350 . 5.2662 .01272 11.11 .00912

3 90 . 5.0756 .01294 11.31 . 00978

400. 4.9012 .01315 11.52 .01045

410. 4 . 7409 .01337 11.72 .01112

420 . 4. 5926 .01360 11.92 . 01180

430. 4 . 4550 .01382 12.12 .01248

440 . 4.3268 .01405 12.32 .01317

450. 4. 2069 .01428 12.52 .01387

460. 4.0944 .01451 12.73 . 01457

470. 3.9887 .01474 12.92 .01528

480. 3. 8P90 .01497 13.12 .01600

4 90. 3.7948 .01520 13.32 .01672

500. 3.7057 .01543 13.52 .01746

510. 3.6211 .01566 13.71 .01819

520. 3.5407 .01589 13.91 .01894

530. 3.4642 .01612 14.10 .01969

540 . 3.3913 .01634 14.30 .02045

61
Table 7, Transport Properties of Oxvgen* Isobars* Enqr. Units*

700. psla Isobar 800. psia Isobar

Temp • Density Th e r t a 1 V 1 s c os 1 1 y Thermal Temo. Oe ns 1 1 y Thermal Viscosity Therma

Cord. micro- D 1 f f us 1 v i ty C on dmicro- 0 1 f fusi v I P 1 b/f t**3 PTU/ft.h.P Ib/ft.s f t**2/h R 1 b / ft * * 3 8TU/ft.h*R Ib/ft.s f t**2 /h

98. 841 81 .7366 .11836 336.07 .00365

100 . 81.5627 .11768 331 . 17 .00364 * 90,983 81 . 7640 .11846 337.48 . 00365

10 K

. 80.8123 .11404 300.96 .00350 100 . 81 . 61 16 .11786 333.14 .00364 no. 80.0608 .11218 789.13 .00353 105 . 80 . 8627 .11502 311.77 .00358

115 . 79.3066 . 1 0966 769.1

.00340 110 . 80.1130 .11237 290 .79 .00353

120 . 78.5486 .10726 230.19 .00344 115 . 79.3610 .10986 270 .65 .00349

12 5 . 77.7859 .10495 232. *6 .00340 120 . 78 . 6056 . 10747 251 .61 .00345

130 . 77.0177 .10270 216 .01 .00336 125 . 77. 0456 .10516 233.80 .00341

135 . 76 . 24*3 .10050 200.91 . 0033 ? 130 . 77 . 0005 .10292 2 17.26 .00337 no . 75.4621 .09834 1 86 . 91 .00329 135 . 76. 3094 .10073 201 .98 . 00333

14 5 . 74.6734 .09620 173.96 .00325 140 . 75.5317 .09858 187.92 . 00329

150 . 73. Q 765 .09407 162.16 .00320 145 . 74.7469 .09645 175.01 .00325

155 . 73.0706 .09196 151.33 .00316 150 . 73.9541 .09433 163.15 . 00321

160 . 72.2549 .08904 161 . 39 .00311 155 . 73.1528 .09223 152 .28 . 00317

165 . 71.4285 .08772 132.27 .00307 160 . 72.3470 .09012 142.31 . C0313

170 . 70.5902 .08559 123.88 .00302 165 . 71 . 5209 .08801 133.15 . 00308

175 . 69.7387 .08345 116.15 .00297 170 . 70. 6884 .08589 124.72 .00303

180 . 68 . 87?6 .08129 109.02 .00291 175 . 69. 8434 .08377 116.97 .00298

185 . 67.9901 .07912 102.43 .00205 180 . 48.9843 . oei63 109.82 . 00292

190 . 67.0892 .07694 96 . 3 ? .0 0279 185 . 68. 1096 .07948 103.21 . 00237

1 9

c

. 66.1676 .07473 90.64 .00272 190 . 67. ? 1 75 .07731 97.08 . 00281

200 . 65.2227 .07250 95.35 .00265 195 . 64.3057 .07512 91.39 .00274

205 . 64.2511 .07025 90.41 .00258 200 . 65.3719 .07291 86 .10 . 00267

210 . 63.2493 .06797 75.77 .00250 205 . 64.4130 . 07068 01.15 .00260

215 . 62.2126 .06566 31 . 4Q .00242 210 . 63.4258 .06843 76.51 .00253

220 , 61.1358 .06332 67. 27 .00233 215 . 67 .4060 .06615 72 .15 .00245

225 . 60.0121 .06095 63 .35 .00224 220 . 61 . 3491 .06384 68.0 3 .00236

230 . 58.8334 .05054 59.61 .00214 275 . 60.7490 .06151 64.13 .00228

235 . 57.5892 .05600 56.03 .00204 230 . 59.0988 .05914 60.41 .00218

240 . 56.2658 .05357 52 . c 6 .00193 235 . 57. 8895 .05673 56 . 86 .00208

245 . 54.8446 .05100 49 . 19 .00181 240 . 56.4097 .05428 53.44 . 00198

250 . 53.2990 .04837 45.97 .00168 245 . 55.2445 .05178 50.12 .00186

255 . 51.5887 .04567 42 .55 .00153 250 . 53.7733 .04924 46.88 .00174

260 . 49.6466 .04292 39.18 .00137 7 5 5 . 52.1667 .04665 43.67 .00161

265 . 47.3439 .04014 35 . 6 ? .00118 260 . 50. 3789 .04403 40.45 .00147

27. 44.3657 .03748 31 . 59 .00093 265 . 48.3327 .04141 37.15 . 0C130

275 . 39.2588 .03552 25.94 .00049 270 . 45 . 8756 .03895 33.64 .00112

276. 207 36.2669 .03538 23.01 .00023 275 . 42.6214 .03706 29.58 . 00088 276.207 18 . 629 ? .02519 12.20 .00025 280 . 36.7353 .03573 23.59 .00044

280 . 14.5246 .01083 10.87 .00109 285 . 19. 7566 .02479 12.96 .00052

2P5 . 12.7045 .01587 10.46 .00165 290 . 15.0101 .01837 11.62 .00112

290 . 11.6137 .01447 10.30 .00208 295 . 14.0453 .01628 11.18 .00157

295 . 10.8277 .01368 10.23 .00245 300 . 12.9002 .01514 10.97 . 00195

300 . 10.2126 .01320 10.21 .00279 310 . 11.3817 .01398 10.81 .00261

310 . 9.2795 .01270 10.24 .00344 320 . 10 . 3*46 .01346 10.80 .00321

320 . 8.5813 .01250 10.34 .00406 330 . 9.5818 .01323 10.86 .00377

330 . 8.0254 .01246 10.47 .00466 340 . 8. 9649 .01315 10.97 .00432

340 . 7. 5651 .01251 10.62 .00525 350 . 0.4535 .01317 11.09 . 00486

350 . 7.1734 .01261 10.79 .00584 360 . 8.0181 .01324 11.24 .00539

360 . 6.8336 .01275 10.96 .00642 370 . 7.6401 .01335 11.40 .00591

370 . 6.5341 .01291 11 .14 .00700 380 . 7.3071 .01349 11.56 . 00644

380 . 6.2671 .01308 11.32 .00758 3 90 . 7.0101 .01365 11.73 .00697

390 . 6.0266 .01327 11.51 .00817 400 . 4.7427 .01382 11.91 .00749

400 . 5.8084 .01347 11.70 .00875 410 . 6. 5000 .01401 12.09 . 00802

410 . 5.6090 .01368 11.89 .00934 420 . 6. 2703 .01420 12 .27 . 00855

420 . 5 .4257 .01389 12.09 .00994 430 . 6.0744 .01440 12.45 .00909

430 . 5.2564 . 0 1

1 C 12.28 .01054 440 . 5.8862 .01460 12 .64 .00963 440 . 5.0993 .01432 12.47 .01114 450 . 5.7115 .01481 12.83 .01017

450 . 4.9530 .01454 12.67 .01175 460 . 5. 5488 .01502 13.01 .01072

460 . 4.8163 .01476 12.86 .01236 470 . 5.3968 .01523 13 .20 . 01127

470 . 4.6881 .01498 13.06 .01298 4 80 . 5.2542 .01545 13.39 . 01183

480 . 4.5676 .01520 13.25 .01361 490 . 5.1202 .01567 13.57 .01239

490 . 4.4541 .01543 13.44 .01424 500 . 4. 9939 .01588 13.76 .01295

500 . 4.3468 .01565 13.64 .01488 510 . 4. 8747 .01610 13.95 .01352

510 . 4.2453 .01588 13.83 .01552 520 . 4.7617 .01632 14.13 .01410

520 . 4.1490 .01610 14.02 .01617 530 . 4.6546 .01654 14.32 .01468

530 . 4.0575 .01632 14.21 .01682 540 . 4.5528 .01676 14 .51 .01526

540 . 3.9704 .01655 14 .40 .01748 530 . 3.4642 .01612 14.10 .01969

* Two Phase Boundary

62
Table 7. Transport Properties of 0«ygen> Isobars* Engr. Units.

<>00. psla Isobar 1000. psia Isobar

Temp • Density Therma

1

Viscosity Therma

1

Temp • Density Thermal V 1 SCO s l ty Thermal

C ond

.

micro- D i ffuslvlty C on d

.

micro- Dlf fusivlty

R 1 b/f t**3 BTU/ft.h •R Ib/ft.s t t**2/h R 1 b/ f t**3 BTU/ft.h. R Ib/ft.s f t**2/h

99.124 81 *7913 .11856 338.89 •00366 * 99.265 81 . 8186 .11865 340.29 .00366

100 . 81.6603 • 1 1 80 4 335.12 • 00364 100 . 81 . 7089 .11822 337.10 . 00365

105 . 80.9128 .11520 313.58 .00359 105 . 30.9628 .11539 315.39 .00359

110 . 80.1650 .11256 292.45 .00354 110 . 80. 2168 .11274 2 94 .12 . 00355

115 . 79.4152 .11005 272.19 .00350 115 . 79.4692 .11025 273.73 . 003-50 120 . 78.6622 .10767 253.04 .00346 120 . 78.7186 .10787 254 . <,7 . CC 346

125 . 77.9050 .10537 235.13 .00342 125 . 77.9641 .10558 236.47 .00342

130 . 77.1429 .10314 218.51 . 0033 e 130 . 77.2049 .10336 219.76 .00339

135 . 76.3750 .10096 203.16 .00334 135 . 76.4403 .10118 204.33 .00335

140 . 75.6009 .09881 189.03 .00330 140 . 75.6696 .09905 190.14 .00331

145 . 74.8198 .09669 176. 05 .00326 145 . 74. 8923 .09694 177.10 .00327

150 . 74.0312 .09459 164.15 .00322 150 . 74.1077 .09484 165.14 . 00323

155 . 73.2343 .09249 153.23 .00318 155 . 73.3151 .09276 154 .18 .00319

lftO . 72.4283 .09040 143.21 .00314 160 . 72.5139 .09068 144.12 .00315

165 . 71 .6124 .08830 134.02 .00309 165 . 71 . 7031 .08859 1 34 .89 .00310

170 . 70.7856 .08620 125.57 .00304 170 . 70.8818 .08650 126.41 . 00306

175 . 69.9468 .08409 117.79 • 00 ? 99 175 . 70.0491 .08440 118.60 .00301

180 . 69.0946 .08196 110.61 .00294 1 80 . 69. 2035 .08229 111.40 . 0 C 2 9 5 185 . 68.2275 .07982 103.93 .00288 185 . 68.3438 .03017 104 .75 . 00?90

190 . 67.3438 .07767 97 . 84 .00282 190 . 67. *683 .07803 98.59 .00284

195 . 66.4415 .07550 92.14 .00276 195 . 66. 5751 .07588 92 .88 .00278

200 . 65.5184 .07331 86.83 .00270 200 . 65. 6622 .07371 97.57 .00271

205 . 64.5716 .07111 81 . 88 .00263 205 . 64. 7270 .07153 82 .61 • C 026 5 210 . 63.5982 .06888 77.24 .00255 210 . 63.7668 .06932 77.97 .00258

215 . 62 .5945 .06663 72 . 89 .00248 215 . 62.7782 .06710 73.61 .00250

220 . 61.5561 .06435 68.78 .00239 220 . 61.7574 .06485 69.51 . 00242

225 . 60.4780 .06205 64.89 .00231 225 . 60 . 699 e .06258 65.64 .00234

230 . 59.3540 .05972 61.20 .00222 230 . 59,6001 .06028 61.96 .00225

235 . 58.1764 .05736 57.67 .00212 235 . 58.4515 .05796 58.45 .00216

240 . 56.9358 .05496 54.28 .00202 240 . 57.2462 .05561 55.10 .00206

245 . 55.6198 .05252 51.01 .00191 245 . 55 . 9739 .05324 51.87 .00196

250 . 54.2123 .05006 47.83 .00180 250 . 54.6216 .05083 48.74 . 00186

255 . 52.6910 .04756 44.71 .00168 255 . 53.1722 .04841 45 .69 . 0017 4 260 . 51.0234 .04504 41.62 .00155 260 . 51 . 6018 .04598 42 .69 . 00162

265 . 49.1592 .04255 38.50 .00141 265 . 49. 8755 .04359 39.71 . 00150

270 . 47.0117 .04020 35 . 29 .00125 270 . 47.9392 .04133 36.69 . 00136

275 . 44 .4095 .03833 31 . 82 .00108 275 . 45 . 700 ? .03946 33.56 .00122

280 . 40.9258 .03677 27 . 82 .00085 280 . 4?. 9802 .03780 30.20 .00106

285 . 34.9783 .03361 22.25 .00049 285 . 39. 3766 .03506 26.35 . 00082

290 . 24 .6816 .02739 15.47 .00047 290 . 33.9861 .03206 21.60 .00058

295 . 19.1098 . 020°5 13. 03 .00085 295 . 26. 9862 .02757 16.95 .00058

300 . 16.5667 .01318 12.20 .00126 300 . 21.9062 .02290 14.43 .00060

310 . 13.9113 .01573 11.58 .00195 310 . 17.0491 .01816 12 .69 . 00143 320 . 12.3714 .01468 11 . 39 .00254 320 . 14.6948 .01625 12.13 .00201

330 . 11.2964 .01417 11 .34 .00308 330 . 13.1961 .01531 11 .92 .00254

340 . 10.4760 .01391 11.37 .00360 340 . 12.1109 .01482 11.85 .00303

350 . 9.8158 .01331 11.45 .00410 350 . 11. 2667 .01456 11.86 .00351

360 . 9 . 265 P .01380 11.56 .00459 360 . 10. 5796 .01444 11.92 .00397

370 . 8.7960 .01385 11.68 .00508 37C . 10.0029 .01441 12.01 . 00442

380 . 8.3872 .01394 11.82 .00556 380 . 9.5077 .01444 12.12 . 00467

39 C . 8.0263 .01406 11.98 .00604 390 . 9.0752 .01451 12.25 .00531

400 . 7.7041 .01420 12.14 .00652 400 . 8.6023 .01462 12.38 .00576

410 . 7.4137 .01436 12.30 .00700 410 . 8. 3495 .01474 12.53 .00620

4?c • 7.1499 .01453 12.47 • 0 07 4 Q 420 . 3 . 0401 .01489 12.69 .00664

430 . 6.9087 .01471 12.64 .00797 430 . 7.7585 .01505 12.85 .00709

440 . 6.6868 .01490 12.82 .00846 440 . 7. 5007 .01522 13.01 . 00753

450 . 6.4818 .01510 13.00 .00895 450 . 7,2633 .01540 13.18 . 00798 460 . 6.2915 .01530 13.17 .00945 460 . 7.0437 .01558 13 .35 . 00844

470 . 6.1142 .01550 13.35 .00994 470 . 6 . R 39 e .01577 13.52 .00899

480 . 5.9484 .01570 13.53 .01045 480 . 6.6496 .01597 13.69 .00935

490 . 5 .7929 .01591 13.72 .01095 49 C . 6.4716 .01617 13.87 .00961

500 . 5.6467 .01612 13.90 .01146 500 . 6. 3046 .01637 14.04 .01027

510 . 5.5089 .01633 14.08 .01197 510 . 6.1475 .01657 14.22 .01074

520 . 5.3786 .01654 14.26 .01249 520 . 5.0994 .01678 14.39 .01121

530 . 5.2553 .01676 14.44 .01301 530 . 5.8593 .01698 14 .57 .01169

540 . 5 . 13 fi 3 .01697 14.62 .01354 540 . 5.7266 .01719 14.74 .01216

Two Phase Boundary

63
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units HOC, osia Isobar 1200. psla Isobar

TempDens 1 tv T h e r m a 1 Viscosity Thermal Temp • Density Thermal Viscosity Thermal

C on d • micro- D 1 f f us 1 v 1 ty C on d • micro- D 1 f f us 1 v 1 1 y

P 1 b/f t**3 BTU/f t.h • R Ib/ft.s f t**2/h p 1 b/ f t **3 BTU/ft.h.R Ib/ft.s f t**2/h

99.406 81 . 8 4 5 P .11875 341 . 69 .00366 * 99.547 81.8729 .11885 343.09 .00366

100. 81.7573 .11840 339.09 .00365 100. 81.8055 .11858 341.09 .00366

106. 81 .0126 .11557 317.21 .00360 105. 81.0622 .11575 319.03 .00360

110. 80.2684 .11293 295.79 .00355 110 . 80.3198 .11312 297.47 .00356

116. 79 . 5 229 .11044 275. 27 .00351 115. 79.5763 .11064 276.82 .00351

12 C . 78.7747 .10807 255.90 .00347 120. 78. 8305 .10827 257.34 .00347

12 5. 78.0229 .10579 237.80 .00343 125 . 78.0814 .10599 239.14 .00344

130. 77.2666 .10357 221.01 .00339 130. 77.3279 .10379 222.26 .00340

135. 76. 5051 .10141 205.51 .00336 135. 76. 5696 .10163 206.68 .00336

140. 75.7379 .09928 191.25 .0033?. 140. 75. 8057 .09951 192.35 .00333

145 . 74.9642 .097 ie 178.15 .00328 145. 75.0357 .09742 179.19 .00329

150. 74. 1*36 .09510 166.15 .00324 150. 74.2589 .09535 167.13 .00325

155. 73 .3953 .09302 155.13 .00320 155. 73.4748 .09329 156.07 .00321

16 0. 72.5986 .09095 145.03 .00316 160. 72.6827 .09122 145 .93 .00317

165. 71.7928 .08888 135.76 .00311 165. 71.8818 .08916 136.62 .00313

170. 70.9770 .08680 127.24 .00307 170. 71.0713 .08710 128.08 .00308

175. 70.1502 .08471 119.41 .00302 175. 70.2502 .08503 120.21 .00303

1 B 0 • 69.3111 .08262 112.1 P .00297 180. 69.4174 .08294 112.96 .00298

1 B 5

68.458 5 .08051 105.51 .00291 185. 68.5718 .08085 106.27 .00293

190. 67.5909 . 07839 99.34 .00286 190. 67.7118 .07875 100.09 .00287

195. 66.7066 .07626 93.62 .00280 195. 66.8360 .07663 94.35 .00281

200. 65.8035 .07411 88.29 .00273 200. 65.9424 .07450 89.01 .00275

205. 64 . e 794 .07194 83.33 . 0 C 2 67 205. 65.0289 .07235 84.04 .00269

210. 63.9318 .06976 78.69 .00260 210. 64. 0933 .07019 79.39 .00262

215. 62.9576 .06756 74. 33 .00253 215. 63.1327 .06801 75.04 .00255

22 0. 61.9533 .06534 70.24 .00245 220 . 62.1441 .06582 70.95 .00248

225. 60.9149 .06310 66.37 .00237 225 . 61.1238 .06360 67.09 .00240

230. 59.8377 .06084 62.70 .00228 230 . 60.0675 .06138 63.44 .00232

235. 58.7159 .05855 59.22 .00220 235 . 58. 9704 .05913 59.97 .00223

240. 57.5426 • 0 5 6 ? 5 55.89 .00210 240. 57.8265 .05686 56.66 .00214

24*. 56.3094 .05392 52.70 .00201 245 . 56.6286 .05458 53 .50 .00205

250. 55.0058 .05158 49.61 .00191 250. 55.3682 .05229 50.45 .00195

255. 53.61*1 .04922 46.6? .00180 255. 54.0341 .04999 47.51 .00185

260. 52.1282 .046*6 43.70 .00169 260. 52.6126 .04769 44.64 .00175

265. 50.5113 .04455 40.81 .00157 265. 51.0851 .04544 41.84 .00164

270. 48.7310 .04236 37.94 .00145 270. 49.4261 .04331 39.07 .00153

275. 46.7313 .04050 35.02 .00133 275. 47.5994 .04146 36.31 .00143

280. 44.4195 .03*79 32.01 .00120 2 80 . 45.5501 .03973 33.51 .00132

286. 41.6287 .03623 28 . 79 .00102 285. 43. 1929 .03731 30.63 .00117

290. 38.0518 .03370 25.22 .00083 290. 40.3929 .03495 27.60 .00101

295. 33.3314 .03094 21.29 .00069 295. 36.9726 .03260 24.38 .00087

300. 28.1152 .02754 17.82 .00070 300. 32.9116 .03013 21.15 .00079

310. 20.9261 .02131 14.30 .00108 310. 25.2151 .02462 16.46 .00094

320. 17.3850 .01822 13.12 .00160 320. 20.4363 .02055 14.40 .00132

330. 15.3058 .01670 12.63 .00211 330. 17. 6349 .01834 13.51 .00177

340. 13.8805 .01588 12.41 .00258 340. 15.7898 .01711 13.09 .00222

350. 12.8108 .01542 12.33 .00303 350. 14.4500 .01639 12.68 .00265

360. 11.9615 .01516 12.33 .00347 360. 13.4116 .01597 12 .79 .00306

370. 11.2614 .01503 12.37 .00389 370. 12. 5708 .01572 12.77 .00346

380. 10.6684 .01499 12.44 .00431 380 . 11.8683 .01559 12.80 .00385

390. 10.1560 .01501 12.54 .00472 3 90. 11.2677 .01554 12.87 . 00424

400. 9.7063 .01507 12.66 .00514 400. 10.7450 .01555 12.95 .00463

410. 9.3066 .01516 12.78 .00555 410. 10.2837 .01560 13.06 .00502

420. 8.9478 .01527 12.92 .00596 420. 9.8721 .01568 13.17 .00540

430. 8.6230 .01541 13.07 .00637 430. 9. 5013 .01579 13.30 .00578

440. 8.3269 .01556 13.22 .00679 440. 9. 1646 .01591 13.44 .00617

450. 8.0553 .01572 13.37 .00720 450. 8.8569 .01605 13.58 .00655

460. 7.8049 .01589 13.53 .00762 460. 8.5742 .01620 13.73 .00694

470. 7. 5729 .01606 13.69 .00804 470. 8.3129 .01636 13.88 .00733

480. 7.3572 .01624 13 . 86 .00846 480. 8.0706 .01653 14.04 .00772

4 9 C « 7.1558 .01643 14.02 .00888 490. 7 . 8449 .01670 14 .19 .00811

500. 6.9673 .01662 14.19 .00931 500. 7.6340 .01688 14.35 .00851

510. 6.7902 .01682 14.36 .00974 510. 7.4363 .01707 14.52 .00891

52 C . 6.6234 .01701 14.53 .01017 520. 7.2504 .01726 14.68 .00931

530. 6.4660 .01721 14.70 .01061 530. 7. 0752 .01745 14.84 .00971

540. 6.3171 .01741 14.87 .01104 540. 6.9097 .01764 15.01 .01012

* Two Phase Boundary

64
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units.

1300. psla Isobar 1400. psla Isobar

Temp

.

Dens 1 1

y

Therma

1

Viscosity Therma

1

Temp o Density Thermal V 1 scos I ty Therma 1 Cond • micro- 01 f f us Iv 1 ty C ond • micro- 0 1 f f us 1 y 1 ty

R I b/f t**3 BTU/ft.h.R Ib/ft.s ft**2/h R 1 b/ f t**3 BTU/ft.h.R Ib/ft.s f t**2/h

99.668 81.9000 . 1180 * 344.48 .00367 00.820 81.9260 . 1190 * 3 * 5.86 .00367

100 . 81.8536 .11876 343.09 .00366 100 . 81.0015 . 1180 * 3 * 5.09 .00367

105 . 81.1116 . 1159 * 320.85 .00361 105 . 81.1609 .11612 322.68 .00361

110 . 80.3709 .11331 299.14 .00356 110 . 80.4210 . 113*9 300.82 .00357

115 . 79.6296 .11083 278.37 .00352 115 . 70.6825 .11102 279.92 .00352

120 . 76.8861 . 108*7 258.77 . 003*8 120 . 78 . 0 * 1 * .10867 260.21 . 003*9

125 . 78.1395 .10620 240.48 . 003 ** 125 . 78.1973 . 106*0 2 * 1.81 . 003*5

130 . 77.3989 . 10*00 223.51 . 003*1 130 . 77 . 4*05 . 10*21 224.76 . 003*1

135 . 76.6336 .10185 207 . 85 .00337 135 . 76.6073 .10208 200.03 .00338

1 <* 0 . 75.8730 .00075 193.46 .00333 1 * 0 . 75 . 9*00 .09098 194.56 . 0033 * 14 5 . 75.1066 .00766 190. 24 .00330 1 * 5 . 75.1770 .00790 181.28 .00331

150 . 74.3336 .00560 168.12 .00326 150 . 74.4078 .09585 160.11 .00327

155 . 73.5536 ,00355 157.01 .00322 155 . 73.6319 .00381 157.96 .00323

160 . 72.7660 .00150 146 . 83 .00318 160 . 72 . 8*85 .00177 1 * 7.73 .00319

165 . 71.9699 . 080*5 137.49 . 0031 * 165 . 72.0571 .08973 138.35 .00315

170 . 71.1645 .08730 128.91 .00300 170 . 71.2569 .08760 120.73 .00310

175 . 70.3491 .08533 121.01 .00305 175 . 70 . 4*70 . 0856 * 121.81 .00306

180 . 69.5225 .08326 113.74 .00300 180 . 69 . 626 * .08358 114.52 .00301

185 . 68.6836 .08110 107.03 . 0020 * 185 . 68 . 70*0 .08152 107.78 .00296

190 . 67.8311 .07010 100.82 .00280 190 . 67 . 0*87 . 070*4 101.56 .00290

195 . 66.9634 .07600 95.07 .00283 105 . 67.0300 .07736 95.70 .00285

200 . 66.0789 . 07*88 89.72 .00277 200 . 66.2133 .07526 00.4 3 .00270

2 C 5 . 65.1757 .07275 84.75 .00271 205 . 65.3100 .07315 85.45 .00273

210 . 64.2516 .07061 80.10 . 0026 * 210 . 64.4067 .07103 80.79 .00266

215 . 63.3040 . 060*5 75.74 .00257 215 . 63.4716 .06889 76.43 .00260

220 . 62.3302 .06628 71.65 .00250 220 . 62.5118 .06675 72 . 3 * .00253

225 . 61.3268 . 06*10 67 . PO . 002*3 225 . 61 . 52*5 . 06*59 68.40 . 002*5

230 . 60.2902 . 06

1

OC 64.15 .00235 230 . 60. 5063 . 062*2 64.86 .00238

235 . 59.2160 .05060 60.70 .00226 235 . 59 . 453 * .06023 61.42 .00230

2 A C . 58.0991 .05746 57.41 .00218 2 * 0 . 58 . 361 * . 0580 * 56.15 .00221

24 5 . 56.9333 .05522 54.27 .00200 2 * 5 . 57.2250 . 0558 * 55 .03 . 00213

250 . 55.7115 .05207 51.26 .00200 250 . 56.0381 .05363 52 . 0 * . 0020 *

2 5

c

. 54.4248 .05072 4 P . 36 .00100 255 . 54.7035 . 051*3 * 9.17 .00195

260 . 53 .0622 . 0 * 8*8 4 5.54 .00181 260 . 53 . 482 * . 0 * 92 * * 6.40 .00186

265 . 51.6096 . 0*620 42.81 .00171 265 . 52.0938 . 0*710 * 3.72 .00177

270 . 50 • 0

4

P 6 . 0**21 40.12 .00161 270 . 50.6130 . 0*505 * 1.10 .00167

275 . 48 . 354 ? . 0*237 37.47 .00151 275 . * 0 . 0251 . 0*323 36 . 5 * .00158

290 . 46 .4916 . 0*063 34.83 . 001*1 280 . * 7.3039 . 0 * 1*8 36.01 . 001*0

285 . 44.4114 .03831 3 ? . 16 .00128 2 85 . * 5.4102 .03925 33.49 .00138 290 . 42.0430 . C 3 6 06 29 . 44 .00115 200 . * 3.3301 .03700 30.06 .00126

295 . 39.2071 . 033"8 26.63 .00103 205 . * 0.0870 .03501 28.42 .00115

300 . 36.1123 .03173 23.79 . 00003 300 . 38 . 3*76 .03300 25.86 .00106

310 . 29.1634 .02723 18 . 84 .00003 310 . 32.3731 .02007 21 .00 .00008

320 . 23.6803 .02300 15.96 .00117 320 . 26.8207 .02521 17.71 .00111

330 . 20.1511 .02018 14.57 . 0015 * 330 . 22.7580 .02200 15.80 .00139

340 . 17.8303 .01050 13.87 . 0010 * 3 * 0 . 10. 0703 .02000 14.78 .00173

35 C . 16.1803 . 017*0 13.50 . 0023 * 350 . 17.9885 .01869 1 * .22 .00209

360 . 14.9271 . 016»7 13.31 .00273 360 . 16.5000 . 0178 * 13.90 . 002*6

370 . 13.9287 . 01**8 13.22 .00311 370 . 15 . 330 * .01730 13.72 . 00282

390 . 13.1052 .01625 13.20 . 003*8 380 . 14.3756 .01606 13.63 .00317

390 . 12.4082 .01612 13.22 .00385 3 00 . 13.5750 . 0167 * 13.61 .00352

400 . 11 .9067 .01607 13.27 . 00*21 * 00 . 12.8891 .01662 13 .62 . 00386

410 . 11 .2794 .01607 13.35 . 00*57 * 10 . 12.2918 .01657 13.67 . 00*20

420 . 10.8115 .01611 13.45 . 00*03 * 20 . 11 . 76*4 .01657 13 . 7 * . 00 * 5 * 430 . 10.3920 .01610 13.55 .00520 * 30 . 11.2037 .01661 13.82 . 00*88

440 . 10.0126 .01628 1

3

• *7 .00565 **0 . 10.8607 .01667 13.92 .00522

450 . 9.6672 .01640 13.80 .00601 * 50 . 10 . 48*9 .01676 14 . 0 * .00556

460 . 9.3506 .01653 13.94 .00638 *60 . 10.1333 .01687 14.16 .00590

470 . 9.0590 .01667 14.08 . 0067 * * 70 . 9.8102 .01700 14.29 . 0062 * 490 . 8.7891 .01683 14.22 .00710 * 80 . 0.5118 .01713 14.42 • 0065 e 490 . 8 . 538 ? .01600 14 , 37 . 007*7 * 00 . 9.2351 .01728 1 * .56 .00693

500 . 8.3043 .01715 14.52 . 0078 * 500 . 3.0775 . 017*3 14.70 . 00727

510 . 8.0953 .01733 14.68 .00821 510 . 8.7367 .01750 14.85 .00762

*2 0 . 7.8790 .01750 14.83 .00858 520 . 8.5111 .01776 15.00 .00797

530 . 7.6964 .01760 14 . 99 .00806 530 . 8.2000 .01703 15.15 .00832

540 . 7. 5039 . 017"7 15.15 . 0003 * 5 * 0 . 3. 0902 .01811 15.30 .00867

* Two Phase Boundary

65
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units

1 500 . psla Isobar 1 600 • ps

a Isobar

Temp • D en s 1 t y Thermal Viscosity Thermal Temp

Density Ther maViscosity Thermal

C on d • micro- D 1 f f us 1 v 1 t y C ond • micro- D i f f us 1 v i ty

P 1 b/f t**3 BTL/ft.h.P Ib/ft.s ft**2/h R 1 b/ ft**3 BTU/f t.h •R Ib/ft.s f t**2/h

99. 969 81.9538 • 1 1 013 347. 24 .00367

IOC . 81.9493 . 1101 ? 347.10 .00367 100.109 81.9806 .11923 348.62 .00367

105 . 81 .2099 .11630 324.52 .00362 105 . 81.2588 .11648 326.36 . 00362

110 . 80 .4726 .11368 302.51 .00357 110 . 80. 5231 .11387 304.19 .00358

115 . 79.7353 .11121 281.47 .00353 115 . 79. 7877 .11140 283.03 .00354

12 0 . 78.9964 .10886 261.65 .00340 120 . 79.0511 .10906 263 .09 .00350

125 . 78 .2549 .10661 243.15 .00346 125 . 70.3121 .10681 244.49 . 00346

130 . 77. 5098 .10643 226.01 .00342 130 . 77. 5698 .10464 227.26 .00343

135 . 76.7606 .10230 210.20 .00330 135 . 76. 8235 .10252 211.38 .00339

140 . 76.0065 .10021 105.67 .00335 140 . 76.0725 .10043 196.77 .00336

145 . 75.2469 .00814 182.33 .00331 145 . 75. 3164 .09838 183.37 .00332

150 . 74.4815 .00610 170.10 .00328 150 . 7*. 5546 .09635 171.09 .00329

155 . 73.7095 .00407 158.00 .00324 155 . 73.7865 .09432 159.84 .00325

160 . 72.9304 .00204 148.63 .00320 160 . 73.0116 .09230 149.52 .00321

165 . 72.1436 .00001 130.21 .00316 165 . 72.2293 .09029 140.07 .00317

170 . 71.3483 .08708 130.56 .00312 170 . 71.4389 .08827 131 .38 .00313

175 . 70.5438 .06504 122 .61 .00307 175 . 70.6396 .08624 123.40 .00308

ieo . 69.7290 .08300 115.20 .00302 180 . 69.8306 .08421 116.06 . 00304

15 5 . 68.9031 .08185 108.53 .00207 185 . 69.0108 .08217 109.28 .00299

190 . 68.0647 .07070 102.20 .00202 100 . 68.1793 .08013 103.02 .00294

195 . 67.2127 .07772 06.51 .00287 105 . 67. 3347 .07807 97.22 . 00288

200 . 66.3455 .07563 01.14 .00281 200 . 66.4757 .07600 91 .83 .00282

205 . 65.4616 .07354 86.14 .00275 205 . 65.6009 .07393 86.83 .00277

210 . 64.5590 .07144 81 .48 .00268 210 . 64.7084 .07184 82.16 .00270

215 . 63.6356 .06032 77.12 .00262 215 . 63.7964 .06975 77.79 .00264

220 . 62.6892 .06720 73.03 .00255 220 . 62.8627 .06765 73.70 .00257

225 . 61.7171 .06506 60.18 .00248 225 . 61.9049 .06553 69.86 .00250

230 . 60.7162 .06202 65.55 .00240 230 . 60.9204 .06341 66.23 .00243

235 . 59.6833 .06077 62.12 .00233 235 . 59.9061 .06129 62 .81 .00236

240 . 58.6143 .05660 56.86 .00225 240 . 58.8586 .05916 59.56 .00228

245 . 57.5048 .05644 55.76 .00217 245 . 57.7740 .05702 56.48 .00220

250 . 86.3497 .05427 52.80 .00208 250 . 56.6480 .05489 53.53 .00212

255 . 55.1430 .05211 40.96 .00200 255 . 55.4754 .05276 50.72 .00204

260 . 53.8773 .04006 47.23 .00101 260 . 54.2503 .05066 48.02 .00195

265 . 52.5442 .04786 44.59 .00182 265 . 52.9660 .04860 45.42 .00187

270 . 51.1331 .04586 42.03 .00173 2 70 . 51.6141 .04662 42.90 .00179

275 . 49.6310 .04405 30.53 .00165 275 . 50. 1850 .044 83 40.46 .00171

280 . 48.0216 .04231 37 . 08 .00156 280 . 48 . 6668 .04309 38.08 .00163

285 . 46.2842 .04014 34.67 .00146 285 . 47.0452 .04099 3 5.76 .00153

290 . 44.3932 .03605 32.20 .00136 200 . 45.3035 .03896 33 .47 .00144

295 . 42.3189 .03604 20.02 .00126 295 . 43.4229 .03701 31.23 .00135

300 . 40.0347 .03412 27.56 .00117 300 . 41.3863 .03514 29.02 .00127

310 . 34.8761 .03047 23.07 .00106 310 . 36.8457 .03166 24.78 .00115

320 . 29.6303 .02701 10.48 .00111 320 . 32.0332 .02846 21.17 .00115

330 . 25.3207 .02300 17.16 .00131 330 . 27.7163 .02551 18.57 .00128

340 . 22.1526 .02156 15.80 .00150 340 . 24.3046 .02307 16.91 .00150

350 . 19.8495 .01006 15.01 .00101 350 . 21.7272 .02126 15.88 .00177

360 . 18.1201 .01880 14.54 .00224 360 . 19.7659 .01999 15.25 .00208

370 . 16.7684 .01819 14.26 .00258 370 . 18.2318 .01912 14.86 .00239

380 . 15.6746 .01772 14.10 .00201 380 . 16.9950 .01852 14.61 .00270

390 . 14 .7641 .01741 14 .02 .00324 3 90 . 15.9709 .01811 14.47 .00301

400 . 13.9894 .01721 13.00 .00357 400 . 15.1039 .01783 14.39 .00332

410 . 13.3184 .01710 14.01 .00380 410 . 14.3565 .01766 14.36 .00362

420 . 12 .7289 .01705 14.05 .00421 420 . 13.7026 .01756 14.37 .00393

430 . 12.2048 .01705 14.11 .00453 430 . 13.1235 .01751 14.41 .00423

440 . 11.7345 .01708 14.10 .00485 440 . 12.6054 .01751 14.47 .00453 450 . 11.3089 .01714 14.28 .00517 450 . 12.1379 .01754 14.54 .00484

460 . 10.9211 .01723 14.30 .00540 460 . 11.7130 .01760 14.63 .00514

470 . 10.5656 .01733 14.50 .00581 470 . 11.3243 .01768 14.73 .00544

480 . 10.2381 .01745 14.63 .00613 480 . 10.9668 .01778 14.84 .00575

490 . 9.9348 .01758 14.75 .00646 490 . 10.6365 .01789 14.96 .00605

500 . 9.6529 .01772 14.80 .00678 500 . 10.3299 .01801 15.08 .00636

510 . 9.3899 .01787 15.03 .00711 510 . 10.0443 .01815 15.21 .00667

520 . 9.1438 .01602 15.17 .00744 520 . 9.7774 .01829 15.34 .00698

530 . 8.9128 .01818 15.31 .00777 530 . 9.5271 .01844 15.48 .00729

540 . 8.6953 .01835 15.46 .00810 540 . 9.2918 .01859 15 .62 .00760

* Two Phase Boundary

66
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units.

1700. psla Isobar 1800. psla Isobar

T emp* Dens 1 ty Thermal Viscosity Thermal Temp • Dens 1 1

y

Ther ma 1 Viscosity Therma

1

Cond

.

micro- Dlffuslvlty Cond. micro- Dlffuslvlty

R Ib/f t**3 BTU/ft.h.R Ib/ft.s f t**2/h R lb/ft**3 BTU/ft.h.R Ib/ft.s f t**2/h

100.250 82.0074 .11933 349.99 .00368 100.390 82.0341 .11942 351.36 .00368

1C5

,

81.3074 .11666 328.20 .00363 105. 81.3559 .11684 330.04 .00363

110. 80.5734 .11405 305.88 .00358 110. 80.6235 .11423 307.57 .00359

115. 79.8400 .11159 284.58 .00354 115. 79. 8920 .11178 286.14 .00355

120. 79.1056 .10926 264.53 .00350 120. 79.1598 .10945 265.97 .00351

125. 78.3690 .10702 245.83 .00347 125. 78.4257 .10722 247.18 .00348

130. 77.6294 .10485 228.52 .00343 130. 77.6887 .10506 229.77 .00344

135. 76.8860 .10274 212.55 .00340 135. 76. 9481 .10295 213.72 .00341

140. 76.1382 .10066 197.87 .00337 140. 76.2034 .10089 198.98 . 00337

145. 75.3854 .09862 184 .41 .00333 145. 75.4539 .09885 185.45 .00334

150. 74.6272 .09659 172.08 .00330 150. 74.6992 .09684 173.06 .00330

155. 73.8629 .09458 160.77 .00326 155. 73.9388 .09483 161.71 .00327

160. 73.0922 .09257 150 .42 .00322 160 . 73.1720 .09283 151 .31 .00323

165. 72.3143 .09056 140.92 .00318 165. 72.3985 .09084 141.78 .00319

170. 71.5286 .08855 132.21 .00314 170. 71.6175 .08884 133.03 .00315

175. 70.7345 .08654 124.20 .00309 175 . 70. 8284 .08684 124.98 .00311

180. 69.9310 .08452 116.82 .00305 180. 70.0303 .08483 117.58 .00306

185. 69.1173 .08250 110.02 .00300 185. 69.2225 .08282 110 .76 . 00301

1<3C. 68.2923 .08046 103.74 .00295 190. 68.4039 .08080 104 .46 .00296

195. 67.4550 .07842 97 . 92 .00290 195. 67.5736 .07877 98.62 .00291

200. 66.6040 .07637 92.53 .00284 200. 66.7303 .07673 93.21 .00286

205. 65.7379 .07431 87.51 .00278 205. 65.8726 .07469 88.18 .00280

210. 64.8551 .07224 82.83 .00272 210 . 64. 9992 .07264 83.50 .00274

215. 63.9539 .07017 78.46 .00266 215. 64.1085 .07058 79.12 .00268

220. 63 .0324 .06808 74.37 .00260 220 . 63. 1985 .06852 75 .03 .00262

225. 62.0882 .06599 70.52 .00253 225 . 62.2674 .06645 71.18 .00255

230. 61 .1192 .06390 66.90 .00246 230. 61.3129 .06437 67.56 .00248

235. 60. 1224 .06180 63 .49 .00239 235 . 60. 3327 .06230 64.15 . 00241

24C. 59.0950 .05969 60.25 .00231 240. 59.3240 .06022 60.92 .00234

245. 58.0335 .05759 57.18 .00224 245 . 58.2840 .05814 57.86 .00227

250. 56.9341 .05549 54.25 .00216 250 . 57.2093 .05607 54.95 .00219

255. 55.7927 .05340 51.46 .00208 255. 56.0963 .05401 52.18 .00212

260. 54.6041 .05133 48.78 .00200 260. 54. 9409 .05198 49.52 .00204

265. 53.3630 .04931 46.21 .00192 265. 53.7385 .04999 46.98 .00196

270. 52.0629 .04736 43.74 .00184 270. 52.4841 .04807 44.54 .00189

275. 50.6962 .04558 41.34 .00176 275 . 51.1717 .04630 42.18 .00181

280. 49.2543 .04385 39.02 .00169 280. 49. 7998 .04458 39.90 . 00174

285. 47.7270 .04180 36.76 .00160 285. 48.3460 .04258 37.70 . 00166

290. 46.1028 .03983 34.56 .00151 290. 46. 8173 .04065 35.56 .00158

295. 44.3694 .03793 32 .40 .00143 2 95 . 45.2003 .03879 33.47 .00150

300. 42.5156 .03610 30.30 .00135 300. 43.4876 .03701 31.45 . 00143

310. 38.4395 .03272 26.28 .00123 310. 39.7679 .03370 27.60 .00131

320. 34.0543 .02967 22.72 .00120 320 . 35.7569 .03074 24.14 .00126

330. 29.8796 .02690 19.96 .00128 330. 31.7947 .02810 21.31 .00130

340. 26.3604 .02448 18.06 .00145 340. 28.2751 .02575 19.22 . 00143

350. 23.5799 .02255 16.81 .00168 350 . 25.3690 .02377 17.78 .00162

360. 21 .4146 .02111 16.01 .00195 360. 23.0407 .02222 16.82 . 00136

370. 19.7067 .02008 15. 49 .00723 370 . 21.1769 .02106 16.17 .00211

380. 18.3283 .01935 15.16 .00252 380 . 19.6640 .02021 15.74 .00238

390. 17.1894 .01884 14 .94 .00281 3 90. 18.4127 .01959 15 .45 .00265

400. 16.2284 .01848 14.81 .00310 400. 17.3580 .01915 15.26 .00293

410. 15.4029 .01824 14.75 .00339 410. 16.4540 .01884 15.15 .00320

420. 14.6832 .01808 14 .72 .00368 420. 15.6677 .01862 15.08 .00348

430. 14.0477 .01799 14.73 .00397 430. 14.9752 .01849 15.06 .00375

440. 13.4808 .01795 14 .76 .00426 440 . 14.3587 .01840 15.07 .00402

450. 12.9705 .01795 14.82 .00455 450. 13.8050 .01837 15.10 .00430

460. 12.5077 .01798 14.89 .00484 460 . 13.3039 .01837 15.15 . 00457

470. 12. 0852 .01803 14.97 .00512 470. 12.8472 .01840 15 .22 . 00484

480. 11.6973 .01811 15.07 .00541 480. 12.4285 .01846 15.30 .00512

490. 11.3395 .01821 15.17 .00570 490 . 12.0428 .01853 15.39 .00539

500. 11.0078 .01831 15.28 .00599 500. 11.6859 .01862 15.49 .00567

510. 10.6993 .01843 15.40 .00629 510. 11. 3542 .01872 15.60 .00595

520. 10.4112 .01856 15.53 .00658 520. 11. 0448 .01884 15.72 .00623

530. 10.1414 .01870 15.65 .00687 530. 10.7554 .01896 15.83 .00651

540. 9.8881 .01884 15.79 .00717 540 . 10. 4838 .01909 15.96 .00679

Two Phase Boundary

67
Table 7, Transport Properties of Oxygen* Isobars* Engr. Units

1900 . ps I a I sober 2000. ps i a I sobar

Temp • Dens 1 t

y

Thermal Vi scos i ty Thermal Temp. Dens 1 1 y Thermal Viscosity Therms 1 C ond • m i c ro- D i f f us i v i t y C ond • micro- 0 1 f f us 1 v 1 1

y

P Ib/f t**3 BTU/ft.h • R Ib/ft.s f t**2/b R 1 b/f t**3 BTU/ft.h. R Ib/ft.s f t**2/h

* 100. 529 82.0607 .11952 352.72 •00368 * 100.669 82.0872 .11962 35A .08 .00368

105. 81.A0A2 .11702 331.89 •00364 105. 81.A52A .11720 333. 7A . 0036A

110. 80.673A . 1 1 AA2 309.26 • 00359 110. 80.7231 . 1 1 A 60 310.96 .00360

115. 79.9A38 .11197 287.70 .00355 115. 79.9953 .11216 289.26 .00356

120. 79.2137 .10965 267. A2 .00352 120. 79.267A . 1 09 8 A 268.86 .00352

125. 78.A820 •107A2 2AB.52 •00348 125. 78.5360 .10762 2A9.86 • 003A9

130. 77.7A76 .10527 231.02 .00345 130. 77.8063 • 105A8 232.27 . 00 3A 5 135. 77.0099 .10317 21A .90 .00341 135 . 77.0713 .10339 216.07 . 003A2

1 AO. 76.2682 .10111 200.08 .00338 1 AO . 76.3326 .1013A 201.18 .00339

1A5. 75.5220 .09909 186. A9 .00335 1A5 . 75.5896 .09932 187.5 3 .00336

150. 7A.7708 .09708 17A. 05 .00331 150. 7 A , 8A 18 .09732 175.03 .00332

155. 7A.01A0 .09508 162.65 .00328 155. 7A.0887 . 095 3A 163.58 .00329

160. 73.2513 .09310 152.20 .00324 160. 73.3299 .09336 153.09 .00325

165. 72.A820 .09111 1A2.63 .00320 165. 72. 56A7 .09138 1A3.A8 .00321

170. 71.7055 .08912 133. 8A .00316 170. 71.7928 •089A1 13A.66 .00317

175. 70.9213 .08713 125.77 .00312 175. 71 .013A ,0 87 A3 126.55 .00313

180. 70.1286 . 0 851118. 3A .00307 180. 70.2258 . 085AA 119.10 .00309

185. 69.3265 .0831A 111.50 .00303 185. 69. A293 .083A5 112.23 . 0030A

190. 68.51A2 .08113 105.17 .00298 190. 68.6231 .081A6 105.88 .00299

195. 67.6906 .07911 99.32 .00293 195. 67. 8062 .079A6 100.02 . 0029A

200. 66.85A8 .07709 93.90 .00288 2 00. 66. 9775 •077A5 9A .58 .00289

205. 66.0053 .07506 88.86 .00282 205. 66.1359 .075A3 89.52 • 0028A

210. 65.1A09 .07303 8A . 16 .00276 210. 65.2802 •073A1 8A.82 .00278

215. 6A.2601 .07099 79. 78 .00270 215. 6A.A090 .07139 80. A3 .00272

220. 63.3612 . 0689A 75.68 .00264 220 . 63. 5208 .06936 76.32 .00266

225. 62.AA25 .06689 71.83 .00258 225. 62.6138 .06733 72 . A8 .00260

230. 61.5019 .06A8A 68.22 .00251 230 . 61.686A .06530 68.86 .00253

235. 60. 5373 .06279 6A. 81 .00244 235. 60.7366 .06327 65. A5 • 002A7

2AP. 59.5A63 .06073 61.59 .00237 2A0. 59.7622 .0612A 62 .2A . 002A0

2 A 5

58.5263 .05868 58.53 .00230 2A5 . 58.7610 .05921 59.19 .00233

250. 57.A7A5 . 0566A 55. 6A .00223 250. 57. 730A .05719 56.30 .00226

255. 56.3876 . 05A61 52.88 .00215 255. 56.6678 .05519 53.56 .00219

260. 5 5 . 262 A .05261 50. 2A .00208 260. 55.5703 .05322 50. 9A .00212

265. 5A .0950 .0506A A7.72 .00200 265. 5A.A3A6 .05128 A8 .AA • 0020A

270. 52.8813 , 0A87 5 A 5 . 30 .00193 270. 53. 2575 . 0 A 9 AA6.05 .00197

275 . 51.6166 •0A700 A2.9R .00186 275. 52.0353 •0A767 A3. 75 .00191

280. 50.2960 . CA5 29 A0.7A .00179 280 . 50. 76A1 •0A598 A1.5A • 00 18 A 285. A8.91A0 •0A333 38.58 .00172 285. A 9 , A 3 97 .0AA05 39. A2 .00177

290. A7.A6A8 .0A1AA 36. A9 .00164 290. A8.0581 .0A220 37.37 .00170

295. A5.9A27 .03962 3A.A7 .00157 295 . A6.6151 . 0 AO A35.39 .00163

300. A A . 3 A 27 .03787 32.51 .00150 300. A 5 , 10 7 A .03870 33. A8 .00156

310. AO. 9037 • 03A62 28.79 .00139 310. Al. 8951 . 03 5A9 29.88 , 001A5

320. 37.2070 .03172 25.83 .00132 320. 38.A600 .0326A 26.60 .00138

330. 33.A765 .02916 22.58 .00134 330. 3A. 9531 .03012 23.77 .00138

3A0. 30.0281 .02688 20.37 .00143 3A031.6170 .02790 21 .A8 • 001A5

350. 27.0657 , 02 A 9

18.77 .00159 350. 28.6529 .02596 19.76 .00157

360. 2A ,620A .02330 17.65 .00179 360. 26. 13A9 .02A32 18.50 .00175

370. 22.6260 .02203 16.88 .00202 370. 2A. 0387 .02299 17.61 .00195

380. 20.9911 .02108 16.35 .00226 3 80 . 22.2983 . 0 2 1 9 A 16.98 .00217

390. 19.6331 .02037 15.98 .00252 390. 20. 8A27 .02115 16. 5A • 002A

A00. 1 8 . A 873 . 01 9 815.73 .00278 A00. 19.6106 •0205A 16.22 .00265

A10. 17.5058 « 0 1 9 A 6 15.57 .00304 A10. 18. 55A1 .02009 16.01 .00290

A 2 C

16.6532 .01919 15. A7 .00330 A20. 17. 636A .01976 15.86 • 0031A

A30

15.9035 .01900 15. A1 .00356 A30 . 16.8303 .01952 15.77 .00339

A A 0

15.237A .01887 15.39 .00382 A AO

16. 11A7 .01936 15.72 • 0036A

A 5 0

1A.6A01 .01880 15. AO .00408 A50. 15.A739 .01925 15.71 .00389

A60. 1 A , 1 003 .01877 15 .A3 .00434 A60

1A. 8955 .01919 15 .72 • 00A1

A 70

13.6091 .01878 15. A8 .00460 A 70

1A. 3699 .01916 15.75 • OOA38

A80. 13.1595 .01881 15.55 .00486 A 80 • 13.8893 .01917 15.80 » 00A63

A 90 . 12.7A58 .01886 15.62 .00512 A 90 , 13.AA75 .01920 15.86 , OOA 8 8

500. 12.3633 . 0 1 8915.71 .00539 500. 13.0395 .01926 15.93 .00513

510. 12.0083 .01902 15.81 . 00565 510. 12.6611 .01933 16 .02 .00539

520. 11.6776 .01912 15.91 .00592 520. 12.3089 . 0 19 A

16.11 . 0056A

530. 11.368A .01923 16.02 .00618 530 . 11.9799 .01951 16.21 .00589

5 A 0 . 11. 078 A .01935 16. 1A .00645 5AO. 11 . 6716 .01961 16.32 .00615

* Two Phase Boundary

68
Table 7. Transoort Properties of Oxygen* Isobars* Engr. Units.

2200. d s 1 a I sohar 2400 • os 1 a Isobar

Temo

.

Density Thermal V 1 sco s 1 1 y Ther ira 1 Temp . Density Therma

1

Viscosity Thermal

C on d

.

tr 1 c r o- 01 f f us Ivl ty C and . m 1 c ro- Olffusivlty

R lb/ft**3 BTU/ft.h • R Ib/ft.s f t**2/h R lb/ft**3 BTU/ft.h •R Ib/ft.s f t**2/h

* 100.9*8 82.1*00 .11981 356.77 .00369 * 101.226 82.1925 .12000 359. *5 .00369

105. 81.5*81 .11756 337. *6 .00365 105. 81.6*31 .11791 3*1.20 .00366

110. 80.8219 .11*97 31*. 36 .00361 110. 80. 9198 .11533 317.78 .00362

115. 80.0978 .11253 292.39 .00357 115. 80.1993 .11291 295.53 .00358

120. 79 .37*0 .11023 271 .76 .00353 120. 79. *796 .11061 27* .66 .0035*

125. 78.6*93 .10802 252.55 .00350 125. 78.759* .108*2 255 .2* .00351

130. 77.9226 .10589 23* .78 .003*7 130. 78. 0376 .10630 237.29 .003*8

135. 77.1931 .10382 218. *2 .003** 135. 77.3135 .10*2* 220.76 .003*5

1*0. 76. *602 .10178 203.39 .003*0 1*0. 76. 5863 .10223 205.59 .003*2

1*5. 75.7235 .09978 189.61 .00337 1*5 . 75. 8557 .1002* 191 .68 .00339

150. 7*. 982* .09780 176.99 .0033* 150. 75.1210 .09828 178.95 .00336

155. 7* .236* .0958* 165 .** .00330 155. 7*. 3820 .09633 167.30 .00332

160. 73. *852 .09388 15*. 86 .00327 160. 73.6381 .09*39 156.63 .00329

165. 72.7282 .09192 1*5.17 .00323 165. 72.8890 .092*5 1*6.86 .00325

170. 71.96*9 .08996 136.28 .00319 170. 72.13*0 .09052 137.89 .00321

175. 71.19*8 .08801 128.11 .00315 175. 71.3729 .08858 129.66 .00318

160. 70. *173 .08605 1 20.60 .00311 180. 70.60*9 .0866* 122.10 .00313

185. 69.6316 .08*08 113. 68 .00307 185. 69. 8296 .08*69 115.13 .00309

190. 68.8371 .08211 107.30 .00302 190. 69.0*61 .08275 108.70 .00305

195. 68.0328 .oeoi3 101.39 .00297 195 . 68.2538 .08079 102.76 .00300

200. 67.2179 .07815 95.92 .00292 200. 67. *519 .0788* 97.25 .00295

205. 66.391* .07616 90.8* .00287 205. 66.6396 .07688 92.1* .00290

210. 65.5522 .07*17 86.12 .00282 210. 65. 8157 .07*91 87. *0 .00285

215. 6* .6991 .07218 81 .71 .00276 215. 6*. 9795 .07295 82.97 .00280

220. 63.8308 .07018 77.59 .00270 220. 6*. 1297 .07099 78.8* .0027*

225. 62.9*60 .06819 73.7* .0026* 225. 63.2651 .06902 7*. 97 .00268

230. 62.0*31 .06619 70.12 .00258 230. 62.38*6 .06706 71.35 .00262

235 . 61.1206 .06*20 66.71 .00252 235. 61. *868 .06511 67.9* .00256

2*0. 60.1767 .06221 63.50 .002*5 2*0 . 60.570* .06316 6*. 7* .00250

2*5. 59.2097 .06023 60. *7 .00239 2*5. 59.6338 .06122 61.71 .002**

250. 58.2176 .05827 57.60 .00232 250. 58.6756 .05929 58.85 .00238

255. 57.1983 .05631 5*. 87 .00225 255 . 57.69*3 .05738 56.1* .00231

260. 56.1*99 .05*39 52.28 .00219 260. 56.6881 .05550 53.56 .00225

265. 55.0700 .05250 *9.81 .00212 265. 55.6557 .05366 51.12 .00219

270. 53.9563 .05068 *7. *6 .00205 270. 5*. 5952 .05187 *8.79 .00213

275. 52.8065 .0*896 *5.20 .00199 275. 53.5052 .05018 *6.57 .00207

280. 51.6181 .0*729 *3.05 .00193 280. 52.38*1 .0*853 **.*5 .00201

285. 50.3889 .0*5*3 *0.98 .00186 235. 51 . 2306 .0*673 *2. *2 .00195

290. *9.116* .0*36* 38.99 .00180 290. 50.0*35 .0**99 *0 .*8 .00189

295. *7.7989 .0*191 37.09 .0017* 295. *8.8217 .0*331 38 .62 .00183

300. *6. *3*7 .0*025 35.26 .00168 300. *7.56*9 .0*169 36.85 .00178

310. *3.5667 .03713 31.82 .00157 310. **. 9*76 .0386* 33.52 .00168

320. *0.53*3 .03*33 28.68 .00150 320. *2.207* .03589 30.50 .00161

330. 37. *139 .03187 25.91 .001*7 330 . 39. 3892 .033*5 27.79 .00157

3*0. 3*. 3**3 .02971 23.56 .00150 3*0. 36. 575* .03131 25.** .00157

350. 31 .*797 .02782 21.67 .00158 350. 33.8715 .029*5 23 .*7 .00162

360. 28.9239 .02618 <\J o <\J .00171 360. 31.3709 .02782 21.87 .00171

370. 26.7086 .02*78 19.11 .00187 370. 29.1275 .026*0 20.62 .00183

380. 2*. 81*5 .02363 18.30 .00205 380. 27.1531 .02520 19.65 .00198

390. 23.1995 .02269 17.70 .00225 390. 25. *317 .02*18 18 .90 .00215

*00. 21.816* .02196 17.26 .002*6 *00 . 23.93*1 .02335 18.3* .00233

*10. 20.6228 .02138 16.93 .00267 *10. 22.6276 .02267 17.91 .00252

*20. 19.5830 .0209* 16.70 .00290 *20. 21. *818 .02213 17.58 .00272

*30. 18.6687 .02060 16.53 .00312 *30. 20. *700 .02170 17.3* .00292

**0. 17.8573 .02035 16. *2 .0033* **0. 19.5701 .02137 17.16 .00312

*50. 17.131* .02017 16.35 .00357 *50. 18.76*2 .02111 17.0* .00333

*60. 16. *771 .0200* 16.32 .00380 *60. 18.0375 .02092 16.95 .00353

*70. 15.8833 .01996 16.31 .00*02 *70. 17.3781 .02078 16.90 .0037*

*80. 15.3*1

2

.01992 16.32 .00*25 *80. 16.7765 .02069 16.88 .00395

*90. 1* .8*37 .01990 16.36 .00**8 *90. 16.22*8 .02063 16.88 .00*16

500. 1 * . 3 8* 9 .01992 16. *0 .00*71 500 . 15.716* .02060 16.90 .00*37

510. 13.9601 .01995 16. *6 .00*9* 510. 15.2*60 .02059 16.93 .00*58

520. 13.5651 .02000 16.53 .00517 520. 1*. 8090 .02061 16.98 .00*80

530. 13.1966 .02007 16.61 .005*0 530. 1* . *0 17 .02065 17.0* .00501

5*0. 12.8518 .02015 16.70 .0056* 5*0. 1*. 0208 .02070 17.11 .00522

* Two Phase Bounria ry

69
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units

7 600 • psla Isobar 2 POO . os i a Isobar

Temp. Dens 1 t

y

The rma I Viscosity T* er rna 1 Temp. Density Thermal Viscosity The r ma

C ond

micro- 0 1 f f us 1 v i t

C on d . micro- 0 I f f us 1 v 1 t y P 1 b/f t**3 BTU/ f t . h

. P 1 b /f t .s f P 1 b/ f t **3 PTU/ft.h,,P 1 h /f t . s f t**2/n

101 .504 82.2447 .12019 362.11 .00370 * 101.731 82 . 2965 .1 2039 364.75 . 00370

105. 81.7374 .11827 344 . 95 .00367 105 . 81 . 8311 .11862 348.71 . 00367

11C. 81 .0170 .11569 321 . 20 .00362 110. 81.1134 .1 1605 324.63 . 00 3*3 115. 80.2999 .11328 7 98 0 68 .00359 115 . 80. 3997 .11365 301 .83 . 00360

120. 79.5842 .11100 277.56 • 0 C 3 56 120. 79. 6878 .11138 280.47 . 00357

125. 78.8684 .10881 257 . 94 .00352 125. 78 . 976? .10921 260.63 .00354

130. 78.1514 .10671 239.80 .00349 130. 78.2640 .10712 242.31 .00351

135. 77.4325 .10467 2

7 3 . 1

.00346 135. 77. 5501 .10509 225.45 . 00 3 4.8 140. 76.7109 .10267 207.79 .00343 140 . 76. 8340 .10310 209.99 . 00345

145 . 75.9862 .10070 193.76 .00340 145. 76.1150 .10115 195.83 .00342

150. 75.2578 .09875 IPO .91 .00337 150. 7 5 . 3928 .09922 182.86 . 00339

155. 74.5255 .09682 169.16 .00334 1 55 . 74.6669 .09730 171 .00 . 00336

160. 73.7887 .09490 158.39 .00371 160. 73.9371 .09540 160.15 .00332

165. 73.0471 .09298 148 . *4 .00327 155 . 73.2028 .09350 150.21 .00329

170. 72.3003 .09106 139. *0 .00324 170. 72.4637 .09160 141.10 .00326

175. 71.5477 • 0 P 9 1 4 131.21 .00320 175 . 71 . 7194 .08970 132.74 .00322

1 80. 70 .7889 . 0 8 7 7 2 123.58 .00316 180. 70. 9695 .08780 125.06 . 00318

185. 70.0234 .08530 116.56 .00312 1 8

c

. 70. 2133 .08590 117.98 . 00314

190. 69. 2505 .08337 110.09 .00307 190. 69.4505 .08399 111.46 .00310

195. 68.4696 .08144 104 . 10 .00303 195. 68 . 6805 .08208 105.44 .00306

200. 67.6800 .07951 98 . 57 .00298 200 . 67. 9025 .08017 99 .87 . 0^301

205. 66.8809 .07758 93.43 .00293 205 . 67. 1160 .07826 94 .70 .00296

210. 66.0716 .07564 88.66 .00288 210. 66.3201 .07635 89 .90 .00292

215. 65.2510 .07370 84.21 .00283 215 . 65.5143 .07444 35.43 . 00287

220. 64.4183 .07177 80.06 .00278 220. 64.6975 .07253 81 . 27 . 00281

225. 63.5725 . 06983 76.19 .00272 225 . 63. 8691 .07062 77.38 . 00276

230. 62.7125 .06790 72 .55 .00267 230. 63.0280 .06873 73.73 . 00271

235 . 61.8373 .06598 69.14 .00261 2 35 . 62. 1735 .06683 70.31 . 00265

240. 60.9456 .06407 65.93 .00255 240 . 61. 3044 .06495 67.10 .00260

245. 60.0364 .06216 62.91 .00249 245. 60.4200 .06308 64.08 .00254

250. 59.1085 . 060 7 8 60.06 .00243 250 . 59. 5191 .06123 61.22 . 0C248

?55. 58.1*05 .05841 57.35 .00237 255 . 58.6010 .05939 58.53 .00242

260. 57.1914 .05657 54 .79 .00231 260. 5 7 . 6646 .05759 55 .98 .00237

265 . 56.1999 .05476 52.36 . 00225 265 . 56. 7091 .05581 53.56 .00231

270. 55 .1 «50 .05301 50.06 .00219 270. 55.7336 .05409 51.27 . 00226

275. 54.1455 .05134 47 . 86 .00214 275 . 54.7376 .05245 49.08 .00220

280. 53.0805 .04971 45.76 .00208 280. 53.7203 .05083 47.01 .00215

285. 51 .9892 .04796 43.77 .00203 285 . 52.6812 .04913 45.03 . 00210

290. 50.8710 .04626 41.86 .00197 290. 51.6203 .04747 43.15 . 00204

295 . 49.7255 .04462 o o -t' .00191 295. 50.5373 .04587 41 .36 .00199

300. 48.5527 . C4304 38.30 .00186 300 . 49. 4325 .04432 39.65 .00194

310. 46.1277 .04006 35.05 .00177 310. 47. 1607 .04139 36.46 .00186

320. 43.6088 .03734 32.11 .00170 320. 44.8157 .03871 33.57 .00179

330. 41.0260 .03492 29.46 .00166 330. 42.4196 .03630 30.98 .00174

340. 38.4318 .03278 27.13 .00165 340. 40.0083 .03416 28.67 .00172

350. 35.5975 .03092 25.13 .00167 350 . 37.6313 .03229 26.65 . 00173

360. 33.4963 .02929 23.45 .00173 360. 35.3435 .03065 24.92 .00177

370. 31.2835 .02787 22.08 .00183 370 . 33.1932 .02922 23.48 .00184

380. 29.2864 .02664 20.99 .00195 380. 31.2125 .02797 2 2.29 .00194

390. 27.5075 .02558 20.12 .00209 390. 29.4144 .02688 21 .32 .00206

400. 25.9331 . 02468 19.44 .00224 400. 27.7969 .02594 20.55 .00219

410. 24.5420 .02393 18.91 .00241 410. 26. 3484 .02514 19.93 .00234

420. 23.3104 .02331 18.50 .00258 420. 25.0525 .02446 19.43 .00249

430. 22.2158 . 022 °0 18.18 .00277 430. 23 . 8915 .02389 19.04 .00265

440. 21 .2380 .02240 17 .94 .00295 440. 22.8482 .02342 18.73 .00282

450. 20.3597 .02207 17.75 .00314 450 . 21.9070 .02303 18.49 .00299

460. 19.5663 .02182 17.62 .00333 460. 21 . 0542 .02272 18.30 .00316

470. 1 8 . 84 5 7 .02162 17 .52 .00352 470 . 20.2779 .02247 18.16 .00334

480. 18.1878 .02147 17.46 • C03 7 l 480. 19. 5681 .02227 18.06 .00352

490. 1 7 . 5 84 3 .02137 17.42 .00390 490. 18.9165 .02212 17.99 .00370

500. 17.028 7 .02129 17.41 .00410 500. 18. 3156 .02200 17.94 .00388

510. 16.5140 .02125 17.42 .00429 510. 17.7596 .02192 17.92 . 00406

520. 16.0363 .02123 17.44 .00449 520. 17.2432 .02187 17.92 .00424

5 3 C

15.5913 .02124 17.48 .00469 530. 16.7621 .02184 17.93 .00442

540. 15.17*4 .02126 17. c 2 • 004 P8 540 . 16. 3124 .02183 17.96 . 00460

* Two Phase Boundary
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units

3000 . psla Isobar 3200. ps i a Isobar

Temp

.

Density Thermal Viscosity Thermal Temp . Density Thermal Viscosity Thermal

C ond

.

micro- D 1 f f us 1 v 1 t y C on d

.

micro- D 1 f fusl v 1 ty

p 1 h/f t**3 BTU/ft.h.R Ib/ft.s f t**2/h p 1 b/ f t**3 BTU/ft.h.R Ib/ft.s f t**2/h

102.058 82.3481 .12058 367.36 .00371 * 102.334 82. 3994 .12077 369.96 .00371

105 . 81.9240 .11897 3 5 2 . 4.9 .00368 105 . 82 . 016 ? .11932 356.29 .00369

110 . 81.2090 .11641 328 . 08 .00364 110 . 81 . 3039 .11676 331.54 .00365

115 . 80.4086 .11401 304.99 .00361 115 . 80.5966 .11438 308.16 . 00362

120 . 79.7905 .11175 283 . 39 .00358 120 . 79.8923 .11213 286.31 .00359

125 . 79.0832 .10960 263.33 .00355 125 . 79. 1890 .10998 266.04 . 00356 no . 78.3755 .10752 244.82 .00352 130 . 78.4858 .10792 247.33 . 00353

135 . 77 .6665 .10550 227.80 .00349 135 . 77. 7816 .10592 230.14 . 00350

140 . 76.9556 .10353 212 . 19 .00346 140 . 77.0759 .10396 214.38 .00347

145 . 76.2423 .10159 197 . 89 .00343 145 . 76.3680 .10204 199.96 .00345

150 . 75.5260 .09968 184 .81 .00340 150 . 75.6575 .10014 1 86 .76 .00342

155 . 74.8066 .09778 172.85 .00337 155 . 74 . 9441 .09826 174.69 .00339

160 . 74 .0833 .09589 161 .90 .00334 160 . 74. 2274 .09639 163.65 . 00336

165 . 73.3561 .09401 151 . 88 .00331 165 . 73.5070 .09452 153.54 .00333

170 . 72.6245 .09213 142 .70 .00328 170 . 72.7827 .09266 144.28 . 00329

175 . 71.8881 .09025 134.27 .00324 175 . 72. 0540 .09080 135.79 .00326

180 . 71.1466 .08837 126.52 .00320 180 . 71 . 3207 .08893 127.98 .00322

185 . 70.3995 .08649 119.40 .00316 185 . 70.5822 .08707 120.80 .00319

190 . 69.6464 .08460 112.83 .00312 190 . 69. 8382 .08520 114.19 .00315

195 . 68.8866 .08272 106.77 .00308 195 . 69. 0883 .08334 108 .06 . CC 311

200 . 68.1197 . OeC 83 101 . 16 .00304 200 . 68.3319 .08147 102.43 . 00307

205 . 67.3450 .07894 95.96 .00299 205 . 67.5685 .07960 97.20 .00302

210 . 66.5620 . 07705 91.13 .00295 210 . 66.7975 .07773 92.34 . 00298

215 . 65.7699 .07516 86.64 .00290 215 . 66.0184 .07587 87.83 . 00293

220 . 64.9681 .07328 82 .45 .00285 220 . 65.2306 .07401 83.62 , 0028 b 225 . 64.1558 .07140 78 . 55 .00280 225 . 64.4334 .07215 79.70 . 00203

230 . 63.3322 .06952 74.89 .00275 230 . 63.6261 .07031 76.02 .00278

235 . 62 .4967 .06766 71.46 .00269 235 . 62. 8082 .06847 72 .59 .00273

240 . 61 . 6484 .06581 68 . 24 .00264 240 . 61 . 9789 .06664 69.36 . 00268

245 . 60.7864 .06397 65.21 .00259 245 . 61.1376 .06483 66.32 .00263

250 . 59.9102 .06215 62.36 .00253 250 . 60. 2837 .06304 63.47 . 00258

255 . 59.0188 .06034 59. 67 .00248 255 . 59.4166 .06126 60.77 .00252

260 . 58.1116 . C 5«57 57.12 .00242 260 . 58.5357 .05951 58.23 . 00247

265 . 57.1880 .05683 54.71 .00237 265 . 57.6405 .05780 55 .82 . 00242

270 . 56.2473 .05513 52.43 .00231 270 . 56.7307 .05613 53.54 .00237

275 . 55.2890 .05351 50.26 .00226 275 . 55 . 8058 .05453 51.38 . 00232

280 . 54.3129 .05191 48.20 .00221 280 . 54 . 8657 .05295 49.33 .00227

285 . 53.3186 .05024 46.24 .00216 285 . 53. 9103 .05131 47.39 . 00222

290 . 52.3062 .04862 44 . 37 .00211 290 . 52. 9397 .04972 45.53 . 00217

295 . 51.2757 . 04705 42.60 .00206 ? 95 . 51 . 9541 .04818 43.77 . 0021 ?

300 . 50.2276 .04553 40.91 .00202 300 . 50.9540 .04669 42 .10 . 00209

310 . 48.0814 .04265 37.77 .00194 310 . 48.9132 .04385 38 .99 . 0020 1 320 . 45.8772 .04000 34 . 92 .00187 320 . 46.8260 .04123 36.18 . 00194

330 . 43.6323 .03760 32.36 .00182 330 . 44 . 7063 . 03 ee 5 33.64 .00189

340 . 41.3731 .03547 30.07 .00179 340 . 42.5745 .03671 31 .37 .00186

350 . 39.1350 .03358 28 . 05 .00179 350 . 40.4572 .03481 29.35 .00185

360 . 36.9503 .03193 26.30 .00182 360 . 38 . 3858 .03314 27.59 .00187

370 . 34 .8056 .03048 24 . 80 .00187 370 . 36.3921 .03167 26.05 . 001 91 380 . 32 . 04*47 .02921 23 . 54 .00195 380 . 34.5033 .03038 24 .74 .00197

390 . 31.1545 .02810 22 .50 .00205 390 . 32. 7384 .02925 23 .64 . 0 C 2 0 5

400 . 29.5203 .02713 21.64 .00216 400 . 31.1070 .02826 22.71 .00215

410 . 28.0381 .02629 20 . 94 .00229 410 . 29.6101 .02739 21 .94 . 00226

420 . 26.6980 .02557 20.37 .00243 420 . 28. 2429 .02663 21 . 30 .00239

430 . 25 .4 870 .02495 19.91 .00257 430 . 26. 9967 • 0

2

c 97 20.78 .00252

440 . 24.3913 .02442 19.54 .00272 440 . 25 . 8612 .02540 20.35 . 002 p 5 450 . 23.3976 .02396 19. 24 .00288 450 . 24.8254 . 02*92 20.00 .00279

460 . 22.4935 .02362 19.01 .00304 460 . 23. 8787 .02451 19.72 .00294

470 . 21 .6681 .02332 18.82 .00320 470 . 23.0111 .02417 19.49 . 00309

480 . 20.9117 .02307 18.68 .00336 480 . 22.2138 .02388 19.31 . 00324

490 . 20. 2160 .02288 18.57 .00353 490 . 21.4788 .02364 19.16 .00339

500 . 19.5738 .02272 18.49 .00369 500 . 20.7991 .02345 19.05 .00354

510 . 18.9790 .02260 18.44 .00386 510 . 20.1687 .02329 18.97 .00370

520 . 18.4262 .02252 18.41 . 00*03 520 . 15. 5822 .02317 18.91 . 00386

530 . 17.9109 .02245 18.40 .00420 530 . 19 . C 35 C .02307 10.88 .00401

540 . 17.4291 .02242 18,40 .00437 540 . 18.5231 .02301 18.86 .00417

* Two Phase Boundary
Table 7* Transport Properties of Oxygen* Isobars* Engr« Units.

3400. psla Isobar 3600. ps i a Isobar

TempDens 1 ty Therma 1 Viscosity Thermal Temo • Density Therma

Viscosity Therma

C ond • ml cro- oirrusivity C ond • m 1 c ro- Dlffuslv

R lb/ft**3 BTU/ft.h .P Ib/ft.s f t**2/h R 1 b / f t ** 3 BTU/ft.h,.R Ib/ft.s f t**2/

102.610 82.6503 .12096 372.53 .00372 102.886 82.5010 .12115 375.08 .00372

105. 82.1079 .11967 360.10 .00370 105. 82. 1988 .12001 363.93 .00370

110. 81.3980 .11712 335.01 .00366 110. 81.6916 .11767 338.68 .00367

115. 80.6939 .11676 311.36 .00363 115. 80.7903 .11510 316.52 .00366

120. 79.993

.11250 289.23 .00360 120. 80.0930 .11287 292.16 .00361

125. 79. 2938 .11037 268.76 .00357 125. 79.3977 .11075 271.65 .00358

130. 78.5950 .10831 269.85 .00356 130. 78.7030 .10871 252.37 .00355

135. 77.8955 .10633 232.69 .00352 135. 78. 0081 .10673 236.83 .00353

160. 77.1967 .10638 216.58 .00369 160. 77. 3123 .10680 218.77 .00350

165. 76.6922 .10268 202.02 .00366 165. 76. 6169 .10291 206.08 .00368

150. 75.7873 .1005v 188.70 .00363 150. 75.9155 .10106 190.66 .00365

155. 75.0799 .09873 176.53 .00361 155. 75. 2139 .09919 178.36 .00362

160. 76.3696 .09687 165.39 .00338 160. 76.5095 .09736 167.13 .00339

165. 73.6557 .09502 155.20 .00335 165. 73.8022 .09552 156.85 .00336

170. 72.9386 .09318 165.86 .00331 170. 73.0917 .09369 167.66 .00333

175. 72.2171 .09133 137.30 .00328 175. 72.3776 .09187 138.80 .00330

180. 71 .6916 .08969 129.63 .00325 180. 71.6596 .09006 130.88 .00327

185. 70.7615 .08766 122.20 .00321 185. 70.9375 .08821 123 .59 .00323

190. 70.0263 .08580 115.53 .00317 190. 70.2108 .08638 116.87 .00319

195. 69.2858 .08395 109.38 .00313 195. 69. 6793 .08655 110.67 .00316

2CC. 68.5396 .08210 103.70 .00309 200. 68.7626 .08272 106 .95 .00312

205. 67.7867 .08025 98.63 .00305 205. 67. 9999 .08089 99.65 .00308

210. 67.0272 .07861 9 3. 56 .00301 210. 67.2512 .07907 96.73 .00303

215. 66.2603 .07656 89.00 .00296 215. 66.6960 .07725 90.16 .00299

220. 65.6856 .07672 86 .77 .00291 220. 65.7336 .07563 85.91 .00295

225. 66.7025 .07289 80.83 .00287 225. 66.9638 .07362 81.96 . 00290

230. 63.9106 .07107 77.16 .00282 230. 66.1859 .07182 78.26 .00285

235. 63.1088 .06926 73.69 .00277 235. 63.3996 .07002 76.77 .00281

260. 62.2972 .06765 70.65 .00272 260. 62.6063 .06825 71.52 .00276

265. 61.6769 .06567 67.61 .00267 265. 61.7996 .06668 68.67 .00271

250. 60.6615 .06390 66.55 .00262 250. 60.9850 .06676 65.60 .00266

255. 59.7965 .06215 61 .85 .00257 255 . 60.1602 .06302 62.90 .00261

260. 58.9396 .06063 59. 31 .00252 260. 59.3269 .06132 60.35 .00256

265. 58.0699 .05876 56.90 .00267 265. 58.6787 .05965 57.95 .00252

270. 57.1877 .05710 56.63 .00262 270. 57.6216 .05803 55 .67 .00267

275. 56.2925 .05551 52.67 .00237 275. 56.7530 .05666 53.52 .00262

280. 55.3 866 .05395 50.63 .00233 280. 55.8733 .05692 51 .68 .00238

285. 56.6637 .05236 68.69 .00228 285. 56.9825 .05336 69.56 .00233

290. 53.5291 .05078 66.66 .00223 2 90. 56.0808 .05180 67.71 .00229

295. 52. 5875 .06926 66.89 .00219 295. 53.1666 .05031 65.96 .00225

300. 51 .6238 .06779 63.23 .00215 300. 52.2660 .06886 66.31 .00221

310. 69.6731 .06500 60.16 .00207 310. 50.3736 .06610 61 .26 .00216

320. 67.6868 .06261 37. 35 .00201 320. 68.6701 .06353 38.67 .00207

330. 65.6706 .06006 36.86 .00196 330. 66.5666 .06118 35.97 .00202

360. 63.6669 .03790 32.58 .00193 360. 66.6155 .03906 33.72 .00199

350. 61.6366 .03599 30.57 .00192 350. 62.6962 .03713 31 .71 .00197

360. 39.6575 .03630 28.79 .00192 360. 60.8019 .03562 29.92 .00198

370. 37.7616 .03281 27.23 .00195 370. 38 . 9591 .03391 28.35 .00200

380. 35.9100 .03150 25.88 .00200 3 80 . 37.1856 .03258 26.97 .00206

390. 36.1809 .03035 26.73 .00207 390. 35.6976 .03160 25.78 .00209

600. 32.5656 .02933 23.75 .00215 600. 33.9067 .03036 26.75 .00216

610. 31.0681 .02866 22 .92 .00225 610. 32.6191 .02966 23.87 .00225

620. 29.6877 .02765 22.23 .00236 620. 31.0366 .02863 23.13 .00235

630. 28.6193 .02696 21.65 .00268 630. 29.7561 .02791 22.50 .00265

660. 27.2553 .02636 21.16 .00260 660. 28.5736 .02728 21.97 .00256

650. 26.1872 .02586 20.76 .00273 650. 27.6817 .02673 21.52 .00268

660. 25.2061 .02539 20. 63 .00286 660. 26.6739 .02625 21.15 . 00280

670. 26.3036 .02500 20.16 .00300 670. 25.5627 .02583 20.86 .00293

680. 23.6710 .02668 19.96 .00316 680. 26.6810 .02567 20.58 .00306

690. 22.7016 .02660 19. 76 .00328 690. 23.8821 .02515 20.37 .00319

500. 21 .9886 .02617 19.62 .00362 500. 23.1399 .02689 20.20 .00332

510. 21.3260 .02398 19.51 .00357 510. 22.6689 .02667 20.06 .00366

520. 20.7088 .02382 19.63 .00371 520. 21.8060 .02668 19.95 .00359

530. 20.1322 .02370 19.37 .00386 530. 21.2008 .02632 19.86 .00373

5*C. 19. 59?*

Two Phase Boundary

.02360 19.33 .00601 560. 20.6353 .02620 19.80 .00387

72
Table 7« Transport Properties of Oxygen* Isobars* Engr. Units.

3800. ps I a Isobar 4000. psla Isobar Temp

.

Dens 1 ty Therma

1

Viscosity Thermal Temp • Density Thermal V 1 scosl ty Therma

Cond. mi cr o- Dlffusivlty C ond

.

m 1 c ro- Dlffusly

R 1 b / f t **3 BTU/ft.h.,R Ib/ft.s f t**2/h R 1 b / f t ** 3 BTU/ft.h. R Ib/ft.s f t**2/

* 1C3.159 82.5513 .12135 377.61 .00373 * 103.933 82.6013 .12159 380.12 .00373

105. 82.2892 .12036 367.77 .00371 105. 82.3788 .12070 371 .63 .00372

110. 81.5891 .11782 391.97 .00368 110. 81.6760 .11816 395.97 .00368

115. 80.8859 .11596 317.71 .00369 115. 80.9807 .11581 320.91 .00365

120. 80.1920 .11329 295.10 .00362 120. 80. 2902 .11360 298.09 .00363

125. 79.5005 .11113 279.17 .00359 125. 79.6029 .11150 276.88 .00360

130. 78.8100 .10910 259.88 .00356 130. 78.9159 .10999 257.90 .00358

135. 78.1196 .10719 237.18 .00359 135. 78.2299 .10759 239.53 .00355

190. 77.9285 .10522 220.97 .00351 190. 77.5935 .10569 223.16 .00353

195. 76.7362 .10339 206.19 .00399 195. 76.8561 .10377 208.19 .00350

150. 76.0922 .10199 192.58 .00396 150. 76.1673 .10193 199.51 .00398

155. 75.3961 .09966 180.19 .00399 155. 75.9767 .10011 182.01 .00395

160. 79.6977 .09783 168 . 86 .00391 160. 79.7891 .09831 170.59 .00393

165. 73.9967 .09602 158.50 .00338 165. 79.0891 .09651 160.19 .00390

170. 73.2927 .09920 199.00 .00335 170. 73. 3915 .09971 150.57 .00337

175. 72.5355 .09239 190.30 .00332 175. 72.6910 .09291 191.79 .00339

180. 71.8298 .09058 132.31 .00329 180. 71.9879 .09112 133.79 .00331

185. 71.1109 .08877 129.96 .00325 185. 71.2809 .08933 126.39 .00327

190. 70.3919 .08696 118.20 .00322 190. 70.5697 .08753 119.52 .00329

195. 69.6690 .08515 111.96 .00318 195. 69.8550 .08579 113 .23 .00320

200. 68.9913 .08339 106.19 .00319 200. 69.1360 .08399 107.93 .00317

205. 68.2089 .08153 100.85 .00310 205 . 68. 9125 .08215 102 .05 .00313

210. 67.9700 .07972 95.91 .00306 210. 67.6839 .08036 97.07 .00309

215. 66.7258 .07792 91 .31 .00302 215. 66.9501 .07858 92.99 .00305

220. 65.9752 .07612 87.03 .00298 220. 66.2105 .07680 88.19 .00301

225. 65.2178 .07933 83.09 .00293 225. 65.9650 .07503 89.13 .00296

230. 69.9533 .07255 79.32 .00289 230. 69.7130 .07326 80.39 .00292

235. 63.6812 .07078 75.89 .00289 235. 63.9593 .07151 76.89 .00288

290

.

62.9011 .06902 72.58 .00279 290. 63.1885 .06978 73 .61 .00283

295. 62.1127 .06728 69.51 .00275 295. 62.9153 .06806 70.59 .00278

250. 61 .3156 .06556 66.69 .00270 250. 61.6393 .06636 67.65 .00279

255. 60.5095 .06386 6 3.93 .00265 255 . 60. 8959 .06968 69.93 .00269

260. 59.6990 .06218 61 . 38 .00261 260. 60.0983 .06302 62.38 .00265

265. 58.8691 .06059 58.97 .00256 265. 59.2929 .06190 59.96 .00260

270. 58.0395 .05893 56.69 .00252 270. 58.9291 .05981 57.68 .00256

275. 57.1902 .05738 59 .59 .00297 275. 57.6068 .05827 55.53 .00252

280. 56.3362 .05586 52.50 .00293 280. 56.7760 .05676 53.99 .00298

285. 55.9726 .05930 50.57 .00239 285. 55.9371 .05523 51.56 .00299

290. 59.5997 .05278 98.73 .00239 2 90. 55.0901 .05373 99.72 .00239

295. 53.7178 .05131 96.99 .00230 29 5. 59.2359 .05228 97.99 .00236

300. 52.8279 .09988 95.39 .00226 300. 53.3736 .05087 96.39 .00232

310. 51.0239 .09715 92.28 .00219 310. 51.6305 .09817 93.29 .00225

320. 99.1999 .09962 39.52 .00213 320. 99.8669 .09566 90.53 .00219

330. 97. 3991 .09228 37 .09 .00209 330. 98.0905 .09333 38.05 .00219

390. 95.9988 .09015 39.79 .00205 390. 96.3112 .09121 35.82 .00211

350. 93.6575 .03822 32 .79 .00203 350. 99.5909 .03928 33.81 .00209

360. 91.8908 .03650 30.99 .00203 360. 92.7913 .03755 32.01 .00208

370. 90.0656 .03997 29.90 .00209 370. 91.0780 .03600 30.91 .00209

380. 38.3989 .03362 28.00 .00207 380. 39.9193 .03962 28.99 .00211

390. 36.7036 .03292 26.78 .00212 390. 37.8128 .03390 27.79 .00215

900. 35.1923 .03135 25.71 .00218 900. 36.2838 .03232 26.69 .00220

910. 33.6716 .03091 29.80 .00226 910. 39.8395 .03135 25 .69 .00227

920. 32.2996 .02958 29 .01 .00239 920. 33.9688 .03099 29.86 .00239

930. 31.0107 .02883 23.33 .00299 930. 32.1879 .02973 29.15 .00293

990. 29.8173 .02818 22.76 .00259 990. 30.9902 .02905 23.59 .00252

950. 28.7096 .02760 22.27 .00265 950. 29.8728 .02899 23.01 .00262

960. 27.6820 .02709 21.86 .00276 960. 28.8313 .02791 22.57 .00272

970. 26.7289 .02669 21.51 .00287 970. 27. 8608 .02793 22.18 .00283

980. 25.8928 .02629 21.22 .00299 980. 26.9562 .02701 21.86 .00299

990. 25.0191 .02590 20.98 .00312 990. 26.1121 .02669 21 .58 .00306

500. 29 .2519 .02561 20.77 .00329 500. 25.3238 .02632 21.35 .00317

510. 23.5359 .02535 20.61 .00337 510. 29.5863 .02609 21.16 .00329

520. 22.8669 .02519 20.97 .00399 520. 23.8959 .02579 21 .00 .00391

530. 22. 2393 .02995 20. 36 .00362 530. 23.2970 .02558 20.87 .00353

590. 21 .6506 .02980 20.28 .00375 590. 22.6379 .02590 20.76 .00365

* Two Phase Boundary
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units

4 500 • ps I a I sobar 5000. ps

a Isobar

T err o . Oens 1 t y Ther fra 1 Viscosity T h p r m a 1 Temp. Density Thermal Viscosity Thermal

C on d • micro- 0 I f f us 1 v 1 ty C on dmicro- Dlffusivity

P 1 b / f t**3 BTU/ft.h.R Ib/ft.s f tt*2/h 0 1 b / f t **3 BTU/ft.h.R Ib/ft.s f t**2/h

* 104.115 82.7251 .12202 ”* 86 . 30 .00374 * 104.793 92.8470 .12249 392.34 .00375

105 . 82.6003 .32155 381 . 34 .00373 105 . 82. 8181 .12239 391 .14 .00375

110 . 81 .9029 .11903 354.27 .00370 no . 82.1256 . 1 1988 363.14 . 00372

115 . 81.2144 .11669 328.94 .00367 115 . 81 . 4435 .11756 337.02 . 0C369

12C . 80.5318 .11451 305 .41 .00365 120 . 90.7684 .11540 312.81 . 00367

125 . 79.8530 .11243 283.68 .00363 125 . 80.0979 .11335 290.50 .00365 no . 79. 1763 .11045 263.70 .00360 130 . 79.4305 .11139 270.02 . 00363

135 . 78.5007 .10853 245 . 39 .03 5 8 135 . 79.7648 .10950 251.25 .00361

140 . 77.8255 .10666 228.63 .00356 140 . 79. 1001 .10766 ’ 34.10 . 00359

14 *', 77.1499 .10483 213.32 . 00354 145 . 77.4357 .10587 218.44 . 00357

150 . 7 6 • 4 73 6 .10303 199.34 .00351 150 . 76.7711 .10410 204.14 .00355

155 . 75.7961 .10124 186.56 .00340 155 . 76. 1059 .10235 191.09 .00352

160 . 75 . 117 ? .09947 174.89 .00346 160 . 75.4399 . 10061 179.17 .00350

165 . 74 .4366 .09771 164 . 22 .00344 165 . 74.7728 .09888 163.27 .00348

1 7 C • 73 • 7

C 4

.09595 154.45 .00341 170 . 74 . 1043 .09716 158.30 . 00345

175 . 73.0605 .09419 145.50 .00338 175 . 73. 4344 , 09544 1 49.16 . 00343

180 . 72. 3825 .09244 137. 28 .00335 180 . 72.7627 .09372 140.79 .00340

185 . 71 .6929 .09068 129 . 7 ? .00332 185 . 72.0892 .09200 133.09 .00337

190 . 71 .0006 . 08°93 122.79 .00329 190 . 71.4137 • 0 90 2 8 126.01 .00334

195 . 70.3052 .08717 116. 38 .00326 195 . 70.7359 .08857 119.48 .00331

200 . 69.6066 . 08542 110.47 .00322 200 . 70. 0558 .08685 - 113.46 .00328

205 . 68 .9045 . 0P367 105.00 .00319 205 . 69. 3730 .08514 107.89 .00325

210 . 68 . 1 986 .08192 99 . 93 .00315 210 . 68 . 6875 .08343 102.74 .00321

215 . 67.488 7 .08018 95.23 .00311 215 . 67.9989 .08173 97.95 . 00318

22 C . 66.7745 .07844 90.86 .00308 220 . 67.3073 .08003 93.51 .00314

225 . 66.0558 .07672 86.79 .00304 225 . 66.6122 .07834 89.38 .00310

23C . 65.3323 .07500 82.99 .00300 230 . 65. 9136 .07666 85.52 .00307

235 . 64.6037 .07330 79 . 4.5 .00295 235 . 65.2112 .07500 81.93 .00303

240 . 63.8698 .07160 76 . 1 ? .00291 240 . 64.5050 .07335 78.56 .00299

24 * . 63.1304 .06993 73.02 .00287 245 . 63.7947 .07171 75.41 .00295

250 . 62.3854 .06828 70.10 .00283 250 . 63.0803 .07010 72.46 .00291

255 . 61.6345 .06664 67.36 .00279 255 . 62.3617 .06850 69.68 . 00287

260 . 60.8776 .06503 64.78 .00275 260 . 61 . 6387 .06693 67.08 .00283

265 . 60.1148 .06345 62.35 .00270 265 . 60. 9114 .06539 64.62 . 00280

270 . 59.3458 .06191 60.06 .00266 270 . 60.1798 .06388 62.31 .00276

275 . 58.5709 .06040 57 .89 .00263 275 . 59. 4440 .06241 60 .12 . 00272

280 . 57.7901 .05893 55.84 .00259 280 . 58 . 7040 .06096 £> O

ao .00269

285 . 57.0035 .05744 53.91 .00255 285 . 57.9601 .05951 56.11 . 00265

290 . 56.2115 .05599 52.07 .00251 290 . 57.2124 .05810 54.27 . 00262

295 . 55.4142 .05458 50.33 .00247 295 . 56.4613 .05672 52.52 .00258

300 . 54.6122 .05320 48.68 .00244 300 . 55.7070 .05538 50.86 .00255

3 1 C • 52.9958 .05058 45.64 .00238 310 . 54.1909 .05281 47.80 .00249

320 . 51.3670 .04811 42.89 .00232 320 . 52.6677 .05039 45.04 . 00244

330 . 49.7318 .04582 40. 41 .00227 330 . 51 . 1423 .04813 42 .56 . 00239

340 . 48.0973 .04371 38.17 .00224 340 . 49.6200 .04604 40.31 .00236

350 . 46.4715 .04178 36.16 .00221 350 . 48. 1069 .04411 38.28 . 00233

360 . 44.8634 .04003 34.35 .00220 360 . 46.6095 .04234 36.46 .00231

370 . 43.28 22 .03844 32.72 .00220 370 . 45. 1345 .04073 34.81 .00231

380 . 41.7375 .03702 31.26 .00221 390 . 43.6886 .03928 33.32 .00231

390 . 40.2381 .03575 2 9.97 .00224 3 90 . 42.2784 .03796 31.99 . 00232

400 . 38.7919 .03461 29.81 .00227 400 . 40. 9098 .03678 30.80 .00235

410 . 37.4053 .03359 27.79 . 0023 ? 410 . 39.5877 .03571 29.73 .00238

420 . 36.0827 .03268 26.90 .00238 4 ?0 . 38. 3164 .03475 28.77 .00243 430 . 34.8269 .03186 26 . 11 .00244 430 . 37.0987 .03388 27.93 . 00248

440 . 33.6386 .03113 25.41 .00252 440 . 35.9362 .03310 27.17 .00254

450 . 32.5173 .03047 24.81 .00259 450 . 34. 8296 .03240 26.51 .00260

460 . 31 .4613 .02988 24.28 .00268 460 . 33.7784 .03176 25.92 .00267

470 . 30.4678 .02935 23 . 82 .00277 470 . 32.7816 .03118 25.40 .00274

480 . 29.5336 .02887 23.43 .00286 480 . 31. 8372 .03065 24.94 .00282

490 . 28.6553 .02844 23.08 .00296 4 90 . 30.9430 .03018 24.54 .00290

500 . 27.8293 .02806 22.78 .00306 500 . 30.0967 .02974 24.18 . 00299

510 . 27.0518 .02772 22.53 .00316 510 . 29.2956 .02935 23.87 .00307

520 . 26.3195 .02741 22.31 .00326 520 . 28. 5369 .02899 23.60 .00316

530 . 25. 6290 .02714 22.12 .00336 530 . 27.8182 .02867 23.37 .00325

540 . 24.9771 .02690 21.97 .00346 540 . 27.1367 .02838 23.17 .00334

* Two Phase Boundary
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units.

6000. psla Isobar 7000. osla Isobar

Terr d . Density Thermal Viscosity Thermal Temp o Density Thermal Viscosity T henna 1 Cond

.

micro- Dlffusivlty Cond. micro- Dlffusivlty

R 1 b/f t**3 BTU/ft.h.R Ib/ft.s f t**2/h R 1 b/ ft**3 BTU/ft.h.R Ib/ft.s f t**2/h

106.140 83.0854 .12345 404.01 .00377 107.474 83.3167 .12439 415.12 .00379

110. e2 . 5589 .121 55 381.06 .00375 no. 82.9774 .12318 399.26 .00378

115. 8i .ee84 .11926 353.30 .00373 115. 82.3168 .12092 369.78 .00376

120. 81.2270 .11714 327.71 .00371 120. 81.6676 .11883 342.72 .00375

126. 80.5720 .11514 304.20 .00370 125. 81.0265 .11687 317.97 .00374

130. 79.9215 .11323 282.67 .00368 130. 80.3913 .11502 295.36 .00372

135. 79.7741 .11140 262.99 .00366 135. 79.7604 .11323 274.73 . 00371

140. 78.6289 .10962 245.03 .00365 140 . 79.1326 .11151 255.94 . C03 70 145. 77.9850 • 1 0 7 8 8' 728.65 .00363 145 . 78.5072 .10983 238.83 . 00368

150. 77.3419 .10618 21 3. 72 .00361 150. 77. 8834 .10818 223.24 . 00367

155. 76.6993 . 10449 200.09 .00359 155 . 77. 2610 .10655 209.03 . 00365

1 6 C . 76.0567 .10282 187.66 .00357 160. 76.6394 .10494 196 .07 . 00364

165. 75.4141 .10116 176.30 .00355 165 . 76.0185 .10334 184.24 .00362

170. 74.7711 .09950 165.92 .00353 170. 75 . 3980 .10175 173.44 . 00360

175. 74.1276 .09785 156.41 .00351 175. 74. 7778 .10015 163.54 .00358

180. 73 .4835 .09620 147.69 .00349 180. 74. 1578 .09856 154.48 .00356

185. 72.8387 .09454 139.69 .00346 185. 73.5379 .09697 146.17 . 00354

190. 72.1929 .09289 132.33 .00344 190. 72 . 91 79 .09538 138.52 .00352

195. 71.5462 .09174 125.56 .00341 195. 72. 2979 .09379 131.49 . 00350

200 . 70.8984 .08960 119. 31 .00338 200. 71 . 6777 .09220 125.00 .00347

205. 70.7494 . C8795 113.53 .00335 205 . 71 . 0572 .09061 119.01 . 00345

2 1 C

.

69. 5990 .08631 108 .19 .00332 210. 70.4364 .08903 113.48 .00342

215. 68.9472 .08467 103.24 .00329 215 . 69. 8153 .08745 108.35 . 0C340

220. 68.2939 .08304 98 . 64 .00326 220. 69. 1937 .08588 103 .59 . 00337

225. 67.6389 .08142 94 .37 .00323 225. 68.5716 .08431 99.16 .00334

230. 66.9821 .07981 90.39 .00320 230 . 67. 9490 .09275 95 .05 .00331

235. 66.3235 .07821 86.68 .00316 235. 67.3258 .08121 91.21 . 00328

240. 65.6631 .07663 83.21 .00313 240. 66.7020 .07968 87.63 . CC325

745. 65.0006 .07506 79.97 .00309 245. 66.0775 .07816 84.29 .00322

250. 64.3361 .07351 76 .93 .00306 250. 65.4523 .07667 81.15 . 00319

255. 63.6696 .07198 74.08 .00303 2 55 . 64. 8265 .07519 78.22 . 00316

260. 63.0009 .07047 71.41 .00799 260. 64 . 2001 .07373 75 .46 .00313

265. 62.3303 . 06899 68.89 .00296 265 . 63. 5730 .07229 72 .87 . 00310

2 70. 61.6576 .06753 66. 52 .00293 270. 62.9453 .07088 70.44 . 00307

275. 60.9831 .0661 1 64 .29 .00289 275 . 62. 3171 .06950 68.15 .00304

280. 60.3067 .06471 62.18 .00286 290. 61.6986 .06814 65 .98 .00301

285 . 59.6286 .06333 60.19 .00283 285 . 61 .0597 .06680 63 .94 . 00298

290. 58.9491 .06197 59 .31 .00280 2 90 . 60.4306 .06549 62.01 .00296

295. 58.2687 .06064 56.53 .00277 295 . 59.8015 .06420 60.19 .00293

300. 57.5864 .05935 54 . 85 .00274 309 . 59.1725 .06295 58.46 . C0290

310. 56.2206 .05687 51.73 .00269 310 . 57.9159 .06053 55.28 . 00285

3 2 C

.

54.8544 .05452 48.93 .00764 320. 56.6625 .05824 52.42 .00281

330. 53.4908 .05232 46.4 1 .00260 330. 55.4144 .05607 49.83 . 00277

340. 52.1334 .05026 44.12 .00256 340. 54.1741 .05404 47 .49 . 00273

350. 50.7858 .04834 42.06 .00253 350 . 52.9440 .05214 45.38 . 00271

360. 49.4520 .04656 40.19 .00251 360. 51 .7268 .05036 43.46 .00266

370. 48.1361 .04493 38.49 .00250 370 . 50. 5251 .04871 41 .71 .00267

3 BO

.

46.8420 .04343 36.96 .00249 3 80 . 49. 3416 .04719 40.13 . 00266

390. 45.5735 .04205 3 5.57 .00250 390. 48.1788 .04577 38.69 .00265

400. 44.3342 .04080 34.31 .00251 400 . 47.0390 .04447 37.37 . 00266

410. 43.1273 .03965 33.17 .00253 410. 45.9245 .04327 36.18 . 00267

420. 41 .9556 .03861 32.14 .00255 420. 44 . 8370 .04216 35.09 .00268

430. 40.8213 .03766 31 . 21 .00258 4 30 . 43.7783 .04115 34.10 .00270

440. 39.7262 .03679 30. 37 .00262 440. 42.7496 .04021 33.20 . 00273

450. 38.6713 .03600 29.62 .00266 450 . 41.7519 .03935 32 .38 . 00276

4 6 C • 37.6574 .03528 28.93 .00271 460. 40.7861 .03856 31.64 .00279

470. 36.6845 .03462 28.32 .00276 470 . 39. 8523 .03783 30.96 . 00283

480. 35.7522 .03401 27. 77 .00782 48 C

.

38 . 9508 .03715 30.34 . 00287

490. 34 .8599 .03346 27.28 .00288 4 90 . 39.0«14 .03652 29 .78 .00291

5 00 . 34.0064 .03294 26.84 .00294 500 . 37.2437 .03594 29.28 . 00296

510. 33.1906 .03247 26. 44 .00301 510. 36.4372 .03540 28.81 .00301

520. 32 .4109 .03703 26.09 .00307 520 . 35.6610 .03490 28.40 . CC3C6

530. 31 .6659 .03163 25.77 .00314 530. 34.9143 .03443 28.02 . 00311

540. 30.9539 .03126 35 .49 .00321 540 . 34.1962 .03399 27.67 .00317

* Two Phase Boundary
Table 7. Transport Properties of Oxygen# Isobars# Engr. Units

80 00* ds i a I sobar 9000 . psla Isobar

Temp, Dens 1 ty Tberma I Viscosity Thermal Temp, Density Thermal Viscosity Tberma

C ond • micro- 0 1 f f us 1 v 1 t y C on d

micro- D 1 f fusl v Ity

R 1 h/f t**3 RTU/ft.h.P Ib/ft.s f t**2/h R 1 b / f t ** 3 BTU/ft.h.R Ib/ft.s f t**2/h

108,796 83.5415 .12534 425 .bQ .00380

110 . 83.3820 .12477 417. 72 .00380 * 110.105 83 . 7601 .12628 435.73 .00382

11 K. 82.7302 .12254 386.43 .00379 115 . 83.1295 .12412 403.28 .00382

I 20 . 0 2 .91 7 .12042 3 57 . 87 .00378 IPO . 82.5007 .12209 373.14 .00382

125 . 81.4631 .11856 331 . 82 .00378 125 . 81.8833 .12021 345.75 .00381

130 . 80.8416 .11675 308.09 .00377 130 . 81.2743 .11843 320.87 .00381

135 . 80. 2256 .11501 286.49 .00376 135 . 80.6718 .11674 298 .27 .00380

140 . 79.6137 .11334 266.85 .00375 140 . 80.0743 .11512 277.75 .00379

145 . 79.0050 .11171 248 . 98 .00374 145 . 79.4808 .11354 259.11 .00379

150 . 78 .3987 .11012 232.72 .00373 150 . 78. 8905 .11200 242.17 .00378

155 . 77 .7945 .10855 217 . 91 .00371 155 . 78.3027 .11047 226.75 .00377

160 . 77.1918 .10699 204.42 .00370 160 . 77. 7171 .10897 212.71 . 00376

165 . 7 6.5903 .10545 192.11 .00369 165 . 77.1333 .10748 199.91 .00375

170 . 75.9900 .10391 180.87 .00367 170 . 76.5512 .10599 188.23 .00373

176 . 75 .3906 .10237 170.59 .00366 175 . 75. 9704 .10450 177.55 .00372

180 . 74.7920 .10083 161.17 .00364 180 . 75.3910 .10302 167.77 .00371

185 . 74 . 1 940 .09930 152.53 .00362 185 . 74.8127 .10153 158.81 .00369

190 . 73.5967 .09776 144.60 .00360 100 . 74.2355 .10005 150 .58 .00368

195 . 73.0000 .09622 137.30 .00358 195 . 73. 6594 .09856 143.01 .00366

200 . 72.4037 .09469 130.57 .00356 200 . 73.0843 .09707 136.03 .00364

205 . 71 .8080 .09315 124.36 .00354 205 . 72.5102 .09558 129.60 .00362

210 . 71.2126 .09162 118.62 .00351 210 . 71.9371 .09409 123.65 .00360

215 . 70.6176 .09009 113.31 .00349 215 . 71. 3648 .09261 118.14 . 00358

22 C . 70.0230 . 0 eP 56 108.38 .00347 220 . 70.7935 .09113 113.04 .00356

225 . 69.4286 .08705 103 . 80 .00344 225 . 70.2231 .08965 108.30 .00353

230 . 68.8346 .08554 99. 54 .00341 230 . 69. 6535 .08819 103.90 .00351

235 . 68.2409 .08404 95.57 .00339 235 . 69.0849 .08673 99.80 .00349

240 . 67.6474 .08255 9 ] . 87 .00336 240 . 68.5170 .08528 95 .97 .00346

245 . 67.0541 .08108 88.42 .00333 245 . 67.9501 .08385 92.40 .00344

250 . 66.4611 .07963 85.18 .00331 250 . 67.3841 .08243 89.06 .00341

255 . 6 ^. 868 ? .07819 82.15 .00328 255 . 66. 8189 .08103 85.93 .00339

260 . 65.2759 .07677 79 . 31 .00325 260 . 66.2547 .07964 83.00 .00336

265 . 64.6837 .07537 76.64 .00323 265 . 65.6914 .07828 80.24 .00334

270 . 64.0919 .07400 74 , 1 ? .00320 270 . 65.1290 .07693 77.65 .00331

276 . 63.5005 .07265 71.77 .00317 275 . 64.5677 .07561 75.22 .00329

280 . 62.9095 .07133 69.55 .00315 280 . 64.0075 .07431 72.93 .00327

285 . 62.3192 .07002 67.45 .00312 285 . 63.4485 .07303 70.76 .00324

290 . 61.7295 .06874 65.46 .00309 290 . 62.8906 .07178 68.72 .00322

295 . 61 .1405 .06748 63 . 59 .00307 295 . 62.3341 .07055 66.79 .00320

300 . 60.5525 .06626 61 .82 .00305 300 . 61.7789 .06934 64.97 .00317

310 . 59.3797 .06389 58.55 .00300 310 . 60.6732 .06702 61.60 .00313

320 . 58.2124 .06164 55.61 .00296 320 . 59.5745 .06480 58.58 .00309

330 . 57.0522 .05951 52.95 .00292 330 . 58.4838 .06270 55.85 . 00306

340 . 55.9005 .05750 50.55 .00289 340 . 57.4024 .06071 53.38 .00302

350 . 54 .7593 .05561 48.38 .00286 350 . 56.3315 .05883 51.14 .00300

360 . 53.6304 .05384 46.40 .00284 360 . 55.2725 .05706 49.11 .00297

370 . 52.5157 .05218 44.61 .00282 370 . 54.2266 .05540 47.26 .00295

380 . 51.4169 .05064 42.97 .00281 380 . 53.1954 .05384 45.57 .00294

390 . 50.3359 .04920 41.48 .00280 390 . 52.1799 .05238 44.03 .00293

400 . 49.2744 .04786 40.12 .00280 400 . 51.1815 .05101 42.62 .00292

410 . 48.2338 .04661 38.88 .00280 410 . 50.2013 .04974 41.33 .00292

420 . 47.2155 .04546 37.74 .00281 420 . 49.2403 .04855 40.15 .00293

430 . 46.2207 .04439 36.70 .00282 430 . 48.2994 .04743 39.06 .00293

440 . 45,2505 .04340 35.75 .00284 440 . 47.3794 .04640 38.07 .00294

450 . 44.3055 . C 424 e 34.88 .00286 450 . 46.4807 .04543 37.15 .00296

460 . 43.3864 .04163 34. 08 .00288 460 . 45.6041 .04452 36.31 .00297

470 . 42.4937 .04084 33.35 .00291 470 . 44.7497 .04366 35.54 .00299

480 . 41.6274 .04010 32.68 .00294 480 . 43.9178 .04288 34.83 .00301

490 . 40.7877 .03941 32.07 .00297 4 90 . 43.1085 .04214 34.17 .00304

500 . 39.9744 .03877 31.51 .00301 500 . 42.3218 .04144 33.57 .00307

510 . 39.1873 .03817 31.00 .00304 510 . 41.5576 .04078 33.02 .00309

520 . 38.4259 .03760 30.53 .00308 520 . 40. 8155 .04016 32 .51 .00313

530 . 37.6898 .03707 30 . 10 .00312 530 . 40.0954 .03958 32.04 .00316

540 . 36.9783 .03658 29.71 .00317 540 . 39.3967 .03903 31.61 .00319

* Two Phase Boundary

76
Table 7

,

T r ansoo r t Prooerti es of Oxygen* Isobar s> Engr . Units.

10000. ps i a Isobar 11000. psla Isobar

T emp. Dens i ty Therme 1 Viscosity Ther rra 1 Temp • De ns 1 ty Thermal V 1 scosl ty Thermal

Cond

.

micro- Olffus i v i ty Cond. m I c ro- 0 1 f f us i v 1 1 y

R Ib/f t**3 BTU/ft.li.R Ib/ft.s ft** 2/

h

R 1 b / f t ** 3 BTU/f t.h •R Ib/ft.s f t**2/h

+ 111. 403 83.9729 .12722 445.26 .00384 * 112.688 84.1803 .12815 454.28 .00385

115. 83.5161 .12566 420.32 .00384 115 . 83.8907 .12718 437 .57 .00386

120. 82.8957 .12366 388.54 .00384 120. 83.2779 .12520 404.08 .00387

125. 82.2884 .12181 359.76 .00384 125. 82.6796 .12338 373.87 .00387

130. 81.6907 .12008 333.70 .00384 130. 82.0923 .12168 346.58 .00387

135. 81.1006 .11843 310.08 .00384 135. 81.5134 .12007 321.91 .00388

140. 80.5163 .11685 288.66 .00384 140. 80.9412 .11853 299.57 .00388

145. 79.9367 .11531 269.23 .00383 145 . 80.3743 .11704 279.33 .00387

150. 79.3608 .11382 251.58 .00383 150. 79. 8118 .11558 260.98 .00387

155. 78.7882 .11234 235.55 .00382 155. 79.2530 .11416 244.31 .00387

160. 78.2182 .11089 220.95 .00381 160. 78.6973 .11275 229.15 .00386

165. 77.6505 .10944 207.66 .00380 165. 78.1444 .11135 215 .35 .00386

170. 77.0848 .10800 195.53 .00379 170. 77.5938 .10996 202.77 .00385

175. 76. 5210 .10657 184. 44 .00378 175. 77. 0455 .10857 191.28 .00384

180. 75.9589 .10513 174.30 .00377 180. 76.4992 .10717 180.76 .00383

185. 75.3983 .10369 165.01 .00376 185 . 75.9547 .10578 171.13 .00382

190. 74.8393 .10225 156.47 .00374 190. 75.4121 .10438 162.29 .00381

195. 74.2817 .10081 148.63 .00373 195. 74.8712 .10298 154.17 .00380

200. 73.7255 .09936 141.40 .00371 2 00. 74.3321 .10158 146 .69 .00378

205. 73.1707 .09792 134.73 .00370 205. 73.7946 .10017 139.79 .00377

210. 72.6172 .09647 128.58 .00368 210. 73.2587 .09877 133.42 .00375

215. 72.0650 .09503 122.88 .00366 215. 72.7245 .09736 127.52 .00374

220. 71.5142 .09359 117.60 .00364 220 . 72.1919 .09595 122.06 .00372

225. 70.9647 .09215 112.70 .00362 225. 71.6609 .09455 116.99 .00370

230. 70.4164 .09072 108.14 .00360 230. 71.1316 .09315 112.28 .00368

235. 69.8695 .08930 103.90 .00358 235 . 70. 6038 .09176 107.90 .00366

240. 69.3239 .08789 99.94 .00356 240. 70.0777 .09038 103.81 .00364

245. 68.7797 .08649 96.25 .00353 245 . 69. 5532 .08901 100.00 .00362

250. 68.2367 .08510 92.80 .00351 250. 69.0304 .08765 96.44 .00360

255. 67.6951 .08372 89.57 .00349 255 . 68. 5092 .08631 93.10 .00358

260. 67.1548 .08237 86.54 .00347 260. 67. 9898 .084 97 89.98 .00356

265. 66.6160 .08103 83.70 .00344 265. 67.4720 .08366 87 .04 .00354

270. 66.0785 .07971 81.03 .00342 270. 66.9559 .08236 84.2 9 .00352

275. 65.5425 .07842 78.52 .00340 275. 66.4416 .08109 81.70 .00350

280. 65.0080 .07714 76.15 .00337 280. 65.9291 .07983 79.26 .00348

285. 64.4751 .07588 73.93 .00335 285. 65.4184 .07859 76.96 .00345

290. 63.9437 .07465 71 .82 .00333 290. 64.9095 .07738 74.79 .00343

295. 63.4140 .07344 69.83 .00331 295. 64.4026 .07618 72 .75 .00341

3C0. 62.8861 .07225 67.95 .00329 300. 63.8977 .07501 70.81 .00339

310. 61.8357 .06996 64.49 .00325 310. 62.8939 .07275 67.24 .00336

320. 60.7932 .06777 61.37 .00321 320. 61.8988 .07058 64.03 .00332

330. 59.7595 .06569 5 8.57 .00318 330. 60.9129 .06851 61 .14 .00329

340. 58.7355 .06371 56.03 .00315 340. 59. 9368 .06655 58.53 .00326

350. 57.7219 .06184 53.72 .00312 350. 58 . 9713 .06468 56.16 .00323

360. 56.7200 .06007 51.63 .00310 360. 58.0170 .06291 54.00 .00321

370. 55.7305 .05840 49.72 .00308 370. 57.0748 .06124 52 .04 .00319

380. 54.7546 .05683 47 . 98 .00306 3 80. 56.1452 .05966 50.24 . 00317

390. 53.7931 .05536 46. 39 .00305 390. 55.2292 .05817 48.60 .00316

400. 52.8470 .05397 44.94 .00304 400. 54.3273 .05677 47.10 .00315

410. 51.9172 .05267 43.60 .00304 410. 53.4402 .05544 45 .72 .00314

420. 51.0043 .05145 42.37 .00304 420. 52.5684 .05419 44.45 .00314

430. 50.1091 .05030 41.25 .00304 430. 51.7126 .05301 43.28 .00314

440. 49.2322 .04922 40.21 .00304 440. 50. 8731 .05190 42.20 .00314

450. 48.3741 .04821 39.25 .00305 450. 50.0503 .05085 41.21 .00314

460. 47. 5350 .04726 38.37 .00306 460, 49. 2446 .04986 40.29 .00315

470. 46.7154 .04636 37.56 .00308 470. 48.4561 .04892 39.45 .00316

480. 45.9154 .04552 36.81 .00309 4 80. 47.6851 .04803 38.66 .00317

490. 45.1350 .04473 36.12 .00311 490. 46. 9315 .04719 37.94 .00318

500. 44.3744 .04398 35.48 .00313 500. 46.1955 .04639 37.26 .00320

510. 43.6335 .04327 34 . 89 .00315 510. 45.4770 .04563 36.64 .00321

520. 42.9120 .04260 34.35 .00318 520. 44.7758 .04491 36.06 .00323

530. 42.2098 .04196 33 . 84 .00320 530. 44. 0919 .04423 35.53 .00325

540. 41.5267 .04136 33.37 .00323 540. 43.4251 .04357 35.03 .00327

* Two Phase Boundary

77
Table 7# Transport Properties of Oxygen* Isobars* Engr. Units.

12000. Psla Isobar 13000. psla Isobar

Temp . Dens i t y Thermal Viscosity T b e r it a 1 Temp. Density Th e r ma 1 Viscosity T he r m a 1 C on d • micro- Olffuslvity C on d

micro- Olffuslvity

P 1 b/f t**3 BTU/ft.h,.P Ib/ft.s f t**2/h P 1 b/ f t**3 BTU/ft.h. R Ib/ft.s f t* + 2/h

113.963 86.3827 .12909 862.83 • OC 3 87 115 . 86.2566 .12 866 655.02 .00387 115.227 89. 5803 .13002 470.91 . 00388

130 . 83.6682 .12670 619.76 .00389 120 . 89. 0076 .12817 435.59 .00390

135 . 83.0581 .12691 388.07 .00390 125 . 83.9298 .12641 402.37 .00392

130 . 82.6801 .12326 359.53 .00390 130 . 82.8553 .12477 372.53 .00393

135 . 81.911.12167 333.77 .00391 135 . 82. 2962 .12323 345.67 . 00394

160 . 81 .3506 .12016 310.69 .00391 160 . 81.7953 .12176 321.43 .00395

165 . 80.7953 .11872 289.63 .00392 165 . 81. 2010 .12035 299.53 .00395

150 . 80.2651 .11731 270.35 .00392 150 . 80.6622 .11898 279.72 .00396

155 . 79.6991 .11592 253.06 .00392 155 . 80. 1280 .11764 261.75 .00396

16 C . 79.1566 .11656 237.32 .00391 160 . 79.5977 .11632 245.45 . 00396

165 . 78.6172 .11320 223.00 .00391 165 . 79.0708 .11500 230.61 .00396

170 . 78.0806 .11185 209.96 .00390 170 . 78. 5970 .11369 217.10 .00396

175 . 77.5666 .11050 198.05 .00390 175 . 78.0260 .11239 204.78 .00395

180 . 77.0166 .10915 187.16 .00389 180 . 77.5075 .11108 193.51 .00395

185 . 76.6869 .10780 177.19 .00388 185 . 76.9919 .10977 183.20 .00394

190 . 75.9573 .10665 166.06 .00387 190 . 76.9776 .10845 173.74 . 00393

195 . 75.6317 .10508 159.66 .00386 195 . 75 . 9660 .10712 165.05 .00392

200 . 76.9080 .10372 151.90 .00385 200 . 75.9565 .10580 1 57.05 .00391

205 . 76.3862 .10235 166.77 .00389 205 . 79 . 9991 .10446 149.68 . 00390

2C . 73.8663 .10098 138.18 .00382 210 . 79 . 94*38 .10313 142.87 .00389

215 . 73.3683 .09961 132.09 .00381 215 . 73.9905 .10179 136.58 .00388

220 . 72.8321 .09826 126.66 .00379 220 . 73.9392 .10045 130.75 .00386

225 . 72.3177 .09687 121 .21 .00378 225 . 72.9399 .09911 125.35 .00385

230 . 71.8052 .09550 116.36 .00376 230 . 72.9926 .09777 120.32 .00383

235 . 71 .2966 .09616 111.81 .00379 235 . 71.9979 .09643 115.65 .00382

260 . 70.7858 . 09279 107.60 .00372 260 . 71 .9592 .09511 111.30 . 00380

265 . 70.2789 .09166 103.66 .00371 265 . 70.9630 .09379 107.24 .00378

250 . 69.7739 .09011 99.98 .00369 250 . 70.9739 .09247 103.44 .00377

255 . 69.2707 • 0 eB 78 96.56 .00367 255 . 69. 9868 .09117 99.89 .00375

260 . 68.7695 .0876 8 93.31 .00365 260 . 69.5018 .08989 96.57 .00373

265 . 68.2702 .08618 90.29 .00363 265 . 69.0189 .08861 93 .45 .00371

270 . 67.7728 .08691 87.65 .00361 2 70 . 68.5380 .08735 90.52 .00369

275 . 67.2776 .08365 36 .78 .00359 275 . 68.0593 .08611 87.77 .00368

280 . 66.7839 .08261 82.26 .00357 280 . 67.5827 .08489 85.18 . 00366

285 . 66.2926 .08119 79.89 .00355 285 . 67.1083 .08368 82.74 .00364

290 . 65.8032 .07999 77.66 .00353 290 . 66.6361 .08249 80.43 .00362

295 . 65.3160 .07881 75.55 .00351 295 . 66.1661 .08133 76.26 .00360

300 . 66.8308 .07765 73.55 .00399 300 . 65.6983 .08018 76.20 .00358

310 . 63.8672 .07561 69 . 88 .00396 310 . 69.7696 .07795 72.42 .00355

320 . 62.9126 .07326 66.58 .00392 320 . 63.8502 .07582 69.02 .00352

330 . 61.9675 .07120 63.60 .00339 330 . 62.9906 .07377 65.96 .00349

360 . 61 .0326 .06926 60.91 .00336 360 . 62.0910 .07182 63.19 .00346

350 . 60.1078 .06738 58.67 .00339 350 . 61.1518 .06996 60.67 . 00343

360 . 59.1962 ,06561 56.25 .00331 360 . 60.2735 .06819 58.39 .00341

370 . 58.2922 .06396 56.22 .00329 370 . 59.9069 .06651 56.31 .00339

380 . 57.6023 .06235 52. 38 .00328 380 . 58.5509 .06491 54.41 .00337

390 . 56.5252 ,06086 50.69 .00326 390 . 57.7075 .06340 52.66 .00336

600 . 55.6612 .05962 69.13 .00325 600 . 56. 8765 .06196 51 .07 .00335

610 . 56.8109 .05807 67.71 .00329 610 . 56.0589 .06059 49.60 . 00334

620 . 53.9767 .05680 66.60 .00329 620 . 55.2539 .05929 48.24 .00333

630 . 53.1531 .05559 65.19 .00323 630 . 59.9618 .05806 47.00 .00332

660 . 52.3663 .05665 66.08 .00323 660 . 53.6890 .05688 45.85 .00332

650 . 51.5568 .05336 63.05 .00323 650 . 52.9201 .05577 44 .78 .00332

66C. 50.7786 .05233 62.10 .00329 660 . 52.1709 .05470 43.80 .00332

670 . 50.0181 .05135 61 .21 .00329 670 . 51.9399 .05369 42.88 .00332

680 . 69.2732 .05062 60.60 .00325 680 . 50.7139 .05272 42 .04 .00332

690 . 68.5662 .06956 39.66 .00326 690 . 50.0072 .05179 41 .25 .00333

500 . 67.8310 .06870 3 8.96 .00327 500 . 99. 3150 .05091 40.52 .00333

510 . 67.1336 .06789 38.29 .00328 510 . 98.6372 .05006 39.84 . 00334

520 . 66.6519 .06713 37.68 .00329 520 . 97 . 9738 .04925 39.21 .00335

530 . 65.7857 .06639 37.12 .00330 530 . 97.3296 .04847 38.62 .00335

560 . 65.1351 .06569 36.59 .00332 560 . 96.6896 .04772 38.07 .00336

Two Phase Boundary

78
Table 7. Transport Properties of Oxygen* Isobars* Engr. Units

14000 • psia Isobar 15000 • osia Isobar

Temp • Density Thermal V 1 s cos 1 1 y Thermal Temo • Density Thermal Viscosity T henna 1 C ond

.

micro- D 1 f f us 1 v 1 1

y

C on d • micro- D 1 f f us 1 v i t y

P 1 b/f t**3 BTU/ft.h.R Ib/ft.s f t**2/h R 1 b/ f t**3 BTU/ft.h.R Ib/ft.S f t+*2/h

* 116 . 6 B 0 84.7737 .13095 478.56 • 00390 * 117.723 86.9630 .13188 685.78 .00392

120 . 84.3568 .12962 451.58 . 0039 ? 120 . 86.6967 .13106 667.73 .00393

125 . 83.7806 .12787 416.78 •00394 125 . 86.1263 .12931 631.30 .00396

130 . 83.2188 .12626 385.61 .00396 130 . 83.5716 .12773 398.76 .00398

135 . 82.6684 .12476 357. 61 .00397 135 . 83.0291 .12625 369.60 .00600 HO . 82.1269 .12333 332.39 • 0039 B 160 . 82.6963 .12685 363.38 .00601

145 • 81.5927 .12195 309.64 .00399 165 . 81.9716 .12351 319.75 .00602

150 . 81.0644 .12062 289.07 .00400 150 . 81.6529 .12222 298.62 .00603

155 . 80.5412 .11932 270.45 .00400 155 . 80. 9398 .12095 279.12 . 00606

160 . 80.0222 .11803 253.55 .00400 160 . 80.6316 .11971 261.63 .00606

165 . 79.5070 .11676 23 e . l 9 .00400 165 . 79.9270 .11867 265.76 .00605

170 . 78.9951 .11549 224. 21 .00400 170 . 79.6262 .11726 231.28 .00605

175 . 78.4862 .11422 211.46 .00400 175 . 78.9287 .11601 218.10 .00605

1 B 0 . 77.9801 .11295 199.81 .00400 180 . 78.6361 .11677 206.07 .00605

185 . 77.6766 .11167 189.15 .00399 185 . 77.9623 .11353 195.06 .00605

100 . 76.9755 .11039 179.38 .00399 190 . 77.6531 .11229 186.97 . 00606

195 . 76.4768 .10911 170.40 •00398 195 . 76.9663 .11106 175.70 . 00606

200 . 75.9804 .10781 162.14 .00397 200 . 76.6820 .10977 167.18 .00603

205 . 75.4863 .10651 154.53 .00396 205 . 76.0001 .10851 159.33 .00602

210 . 74.9943 .10521 147.51 .00395 210 . 75.5205 .10723 152.08 .00601

215 . 74.5045 .10390 141 .01 .00394 215 . 75.0631 .10595 165 .39 .00600

220 . 74.0168 .10259 135.00 .00393 220 . 76.5680 .10667 139.18 .00399

225 . 73.5313 .10128 129.42 . 0039 ? 225 . 76.0951 .10339 133.63 .00398

230 . 73.0479 .09997 124.24 .00390 230 . 73.6265 .10210 128.10 .00397

235 . 72.5667 .09866 119.42 .00389 235 . 73.1561 .10082 123.13 .00396

240 . 72.0876 .09735 114.93 .00387 260 . 72.6899 .09953 118.50 .00396

245 . 71.6107 .09606 110.74 .00386 2 . 5 . 72.2260 .09826 116.19 .00393

250 . 71 .1359 . 0947 ? 106.83 .00384 250 . 71.7663 .09699 110.16 .00391

255 . 70.6633 .09349 103.17 .00382 255 . 71.3069 .09573 106.39 .00390

260 . 70.1929 .09222 99.75 .00381 260 . 70.8677 .09667 102.86 .00388

265 . 69.7247 .09096 96.53 .00379 265 . 70. 3928 .09323 99.55 .00387

270 . 69.2586 .08972 93.52 .00377 270 . 69.9601 .09201 96.65 .00385

275 . 68.7948 .08849 90 .68 .00376 275 . 69.6898 .09079 93.53 . 00383

280 . 68.3333 .08728 88.01 .00374 280 . 69.0618 .08959 90.7 8 .00382

285 . 67.8740 .08608 85.50 .00372 285 . 68. 5960 .08861 88.19 .00380

290 . 67.4169 .08491 83 . 13 .00370 2 90 . 68. 1527 .08725 85.75 .00376

295 . 66.9622 .08375 80.89 .00369 205 . 67.7116 .08610 83.65 .00377

300 . 66.5098 .08262 78.77 .00367 300 . 57.2729 .08697 81 .27 .00375

310 . 65.6119 .08041 74.88 .00364 310 . 66.6027 .08277 77.27 .00372

320 . 64.7237 .07828 71.38 .00361 320 . 65.5622 .08066 73 .67 .00369

330 . 63.8452 .07625 68.23 .00358 330 . 66.6915 .07863 70.63 .00366

340 . 62.9766 .07430 65. 38 .00355 360 . 63.8508 .07669 67.50 .00366

350 . 62.1188 .07244 62.79 .00353 350 . 63.0203 .07683 66.86 .00361

360 . 61.2714 .07067 60.44 .00350 360 . 62.2003 .07305 62.62 .00359

370 . 60.4349 .06898 58.30 .00348 370 . 61.3910 .07136 60.22 .00357

380 . 59.6096 .06737 56.35 .00346 380 . 60. 5925 .06976 56.21 .00355

390 . 58.7959 .06584 54.55 .00345 390 . 59.8051 .06820 56.36 .00353

400 . 57.9939 .06439 52.91 .00343 600 . 59.0290 .06673 56.67 .00352

410 . 57.2041 .06300 51.40 .00342 610 . 58.2665 .06532 53.12 .00351

420 . 56.4267 .06168 50.00 .00341 620 . 57.5116 .06398 51 .68 .00350

430 . 55.6618 .06042 48.72 .00341 630 . 56.7707 .06270 50.36 .00369

440 . 54.9098 .05922 47.53 .00340 660 . 56.0617 .06167 69.16 .00368

450 . 54.1707 .05807 46.43 .00340 650 . 55.3269 .06030 68.00 .00367

4 6 C . 53,4447 . 0569 e 45.41 .00339 660 . 56.6206 .05917 66 .95 .00367

470 . 52.7319 .05593 44 .47 .00339 670 . 53.9281 .05809 65.98 .00366

480 . 52.0324 .05492 43.59 .00339 680 . 53.2683 .05705 65.07 .00366

490 . 51 .3462 .05396 42 .78 .00339 690 . 52.5808 .05606 66.23 .00366

500 . 50.6733 .05303 42.02 .00340 500 . 51.9257 .05508 63.65 .00366

510 . 50.0137 .05214 41 . 31 .00340 510 . 51.2830 .05615 62.71 .00366

520 . 49.3674 .05129 40.65 .00340 520 . 50.6526 .05325 62.03 .00366

530 . 48.7342 .05046 40.04 .00341 530 , 50.0366 .05239 61.60 .00366

540 . 48.1140 .04967 39.47 .00341 560 . 69. 6283 .05155 60.80 .00366

* Two Phase Boundary
Appendix A. Program Listings for Viscosity

The listinqs ere extracted from reference [7],

Note 1. A cal I to the coefficient subroutine* i.e. CALL DATA 02* must precede the use of these routines.

Note 2. Entry variables to FUNCTION VISC(0D*T) are density In mol/L and temperature In K. FUNCTION VISC(DD*T)

C R E TURNS VISCOSITY IN ( G/CM-S ) * E +6 > C T IN K, 0 IN MOL/L COMMON/CP IT/EM DrOD*FM/l 000 . VISC*DILV(T)+FDCV(D*T)+EXCESV(D*T)

RETURN

END FUNCTION DILV(T)

C GIVES DILUTE GAS VISCOSITY AND THERMAL

C CONDUCTIVITY FOR AN INPUT TEMP. IN

C KELVIN. OUTPUT UNITS APE SAME AS

C THOSE IN VISC AND THFPM COMMON/ISP/N,NW*NWW

cqmmqn/datai/gv»gt * F V * F T * E V * ET DIMENSION GV(9)*GT(9)*FV(4)*FT(<»)xEV(8)*ET(8)

SUM = 0 TF=T** ( 1. /3.

TFF«T**(-4. /3.

DO 10 1=1*9 TFF*TFF*TF

10 SUM*SUM+GV( I ) *TFF

IF (NWW.EQ.7) Gn TO 9 DILV=SUM*1000.

GO TO 11

9 D I L V * SUM

11 RETURN

ENTRY DILT

TF = T**(1 ./3.

TFF*T*M-4. / 3 •

SUM-0

DO 20 1=1*9 tff=tff*tf

70 SUM-SUM*GT( I ) *TFF

DIL V-SUM RETURN

END FUNCTION FDCV(D.T)

C FIPST DENSITY CORRECTION

C FOP VISCOSITY AND THERMAL CONDUCTIVITY C0MM0N/DATA]/GV*GT*FV,FT*EV*ET

DIMENSION GV(9),GT(9)*FV(A)*FT<A)*EV(P)*ET<8)

FDCV«(FV(1 ) F V ( 2 ) * ( F V ( 3)-AL0G( T / F V ( A ) ) ) * *2 ) * D RETURN

ENTRY F DC T FDCV*(FT(1)+FT(2)*(FT(3)-AL0G(T/FT(4) ) )**2)*D RETURN

END FUNCTION EXCESV(D»T)

C CALCULATES EXCESS VISCOSITY common/patai/gv*gt*fv*ft.ev*et

common/ ISP/n,NW DIMENSION GV(9)*GT(9)*FV(4)*FT(<»)*EV(8)xET(8)

R 2 * D* * ( • 5 ) * ( ( D-F V ( 8 ) ) / E V ( 8 )

R«D** ( .1

X«EV(l)*EV(2)*R2 + EV(3)*R + EVm*P2/(T*T) + EV(5)*R/T**(1.5)+EV(6)/T

1+FV(7)*R2/T

X1*EV(1)+EV(6) /T EXCESV-EXP (X)-EXP (XI) RETURN

FNTRY FXCEST

C CALCULATES EXCESS THERMAL CONDUCTIVITY

IFCNW.EQ.O ) GO TO 3 R=D** ( . 1

X=ET(1)+ET(2)*P+ET<3)*R/T**(1.5>+ET(4)/T

X1*ET(1 )+ET(4) /T EXCESV* ( E XP (X)-EXP (XI) »/10. RETURN

7 R2=D**( .5)*( (C-FT(e) )/FT(8)

R«D**( .1) X«FT(l)+FT(2)*P?4-ET(3)*R-fET<*)*R2/(T*T) + ET(5)*R/T**(1.5)*ET(6)/T

1+ET(7)*R2/T

X 1 = E T ( 1 ) F T ( 6 ) / T EXCESV*EXP ( X

) -E X P (XI) RETURN

END

80
Appendix B. Program Listings for Thermal Conductivity

The listings are extracted from references [71 and [81.

Note 1. A cafl to the coefficient subroutine, i.e. CALL DATA 02. must precede the use of these routines.

Note 2. Entry variables to FUNCTION THERM(DD.T) are density In mol/L and temperature In K. Note 3. The dilute gas thermal conductivity. ENTRY DILT In FUNCTION DILV(T). Is listed In Appendix A. FUNCTION THE P M ( DD > T

)

C RETURNS TC IN MW/M-K, T IN K, 0 IN MOL/L

COMMON/HAN/CR.TCI

COMMON/ISP/N.NW

COMMON/CRIT/EM — IF(EM.EO. 31. <3988 1 GO TO 4 D«DD*EM/1000.

IF (NW.EO.O ) GO TO 3 CR-0.0

THER*DILT(T)+FDCT(D,T)*100.+EXCEST(D,T)+CR

TCI-THER-CR

THE R MOTHER RETURN

3 CR-0.0

THERM»DILT(T)+FDCT(D,T)+EXCEST(D,T>+CR

TCI-THERM-CR

RETURN —*-4 CR»CRITCR(DD,T)*1000. — TC I-THERMR (DC»T)*1000. — THERM-TC I+CR — RETURN

END FUNCTION THFRMR(RHO.TEMP)

C 4TH SURFACE. COEF. FROM TC02I AND MINIMS. 3 MAR 82 DIMENSION B ( 1 0

)

DATA B/.298644E-5

1,. 59842 E+OO. . 11362 E-Ol.-. 195 20 E-04

2. .47624E+00.-.64769E-0 3. .832 23E-06

3.

-.278141E-4, .153705E-6, .147176E+1/

T-TEMP DEN-RHO

TCZER0«DILT(T)/1000.

AL -B ( 1 ) *T BE-B(2)fB(3)*T+B(4)*T**2

GA-B(5)+B(6)*T+B(7)*T**2

DE-B(8)+B(9)*T+B(10)/T**2

THERMR-TC ZERO'* AL*DEN + DE* ( E X P ( B E*DE N**GA ) -1 .0

)

RETURN

END FUNCTION CRITCRIRHO.TEMP)

C 4TH SURFACE. COEF. FROM TC021 AND MINIMS. 3 MAR 82 DIMENSION C ( 7

)

DATA C/.219200E+0.-145.55. . 7 34 51 2

F -02 28 29 50E-04

1.-.715 99F-3, .13804E+0, .12 980E-5/

DATA {TC«154.581)»(RH0C*13.63)

T-TEMP DEN-RHO

DELD*ABS(DEN-RHOC)/RHOC

IF(T.LT.TC) T-TC+ITC-T)

IF(T.LT.307.443) GO TO 4 CRITCR-O.

RETURN

4 CONTINUE

AMPL-C(l) /(T+C (2) )+C (3 )+C(4)*T

DELT-T-TC

RH0CENT-RH0C+C(5)*DELT**1.5

DELRHO-DEN-RI-OCENT

Xl-C ( 6 ) *D ELR HO IFIDELRHO.LT.O.) X 1 - XI +C ( 7 ) * DE L R HO**

5

CRITCR»AMPL*EXP(-X1**2)

IFIT.GT. 162. 9805) RETURN IF(DEN.LT.7.5.0R.0EN.GT.18. ) RETURN TEST1-SENG8KDEN.T)

IF (TEST1.GT.CRITCR) CRITCR-TEST1

RETURN

END

81
FUNCTION SENG8KRHO, TEMP ) C SCALED EQUATION ONLY, VERSION OF 12 FEB 82

C CRITICAL ENHANCEMENT AS IN SENGERS ET AL 1981 U NARYL. REPORT

C UNITS, IN MOL/L.K, INTERNAL ALSO ATM, OUT W/M-K, ETA G/CM-S»BK J/K

C 1.02 REPLACED BY 1.04, PARAMETER VARIATION FOR WEBER DATA

DATA (TC* 154. 5 81 ) , (DC* 13. 63 ) , ( BK* 1 . 38054 E-23 )» ( PC -49. 77054

)

1 , (ZZ-5.9783E-10)

DATA (E-0.287),(G-1.190),(B-0.355),(0D«2.36),(XZ-0.183),(DE-4.352)

DFN-RHO

T-TEMP OELO-ABS (OEN-DC) /DC

OELT»ABS(T-TC)/TC

DFACT»EXP(-(39.8+DELT**2+5.45*DELD+*4))

RSTAP-DEN/DC

VIS«VISC(DEN,T)*(1. 0E-06)

CALL DPDT ( DPT, DEN, T ) C IF(DELD. LE. 0.25. AND. DELT.LT. 0.03) GO TO 8 C CALL DPDD(DPD,DEN,T)

C CHISTAR»PC*DEN/fDC+*2*DPD)

C GO TO 12

8 IF(DELD.FQ.O.) GO TO 3 X»DELT/DELD**(1.0/B)

Y»(X+XZ)/XZ

TOP»DFLD + +(-G/B)*{ (l. + E )/(l.+E*Y+*(2.*B) ))**( ( G-l • )/ ( 2 •* B ) ) OIV-DD*<OE+<Y-l.)*(DE-l./8+E*Y**<2.+B))/(l.+E*Y**(2.*B)>)

CHISTAR-TQP/DIV

12 CHI *CHI ST AR**0. 468067

UPPER-1. 04*BK/ PC *(T+DPT/RSTAR)**2ACHI*DF AC T*1.01325E+6

SENG81 I UPPER/(ZZ*6.*3.14159*VIS)

RETURN

3 BGAM«XZ + *G/DD*( (l.+E)/E)+*( ( G-l . )/(?.* B ) ) CHISTAP«BGAM*(DELT)**(-G)

GO TO 12 END
Appendix C. Conversion Factors, Oxygen

Temperature

Pressure

Specific Volume

Internal Energy, Enthalpy

Entropy, Specific Heat

Thermal Conductivity

Vi scosity

Speed of Sound

Molecular Weight

Surface Tension

1.8 R = 1 K

14.695949 psia = 1 atm = 1.01325 x 105

(1 N/m^ = 1 Pa)

0.0005005957 ft 3 /lb

m

= 1 cm

3

/g mol

0.0134446 BTU/lb

m

= 1 J/g mol

0.0074692 BTU/1

b

m

R = 1 J/g mol-K

0.0578176 BTU/ft-hr-R = 1 mW/cm-K

0.067196897 lbm /ft-s = 1 g/cm-s = 1 N

= 1 Pa s 3.2808 ft/s = 1 m/s

31.9988

0.5710147 x 10' 5 lb f/i n = 1 dyn/cm

(1 dyn = 10* 5 N)
1. Report No. 2. Government Accession No. NASA RP- 1102

3. Recipient's Catalog No.

4. Title and Subtitle TRANSPORT PROPERTIES OF OXYGEN

5. Report Date April 1983

6. Performina Organization Code

7. Author(s)

H. M. Roder

8. Performing Organization Report No. NBSIR 82-1672

10. Work Unit No.

9. Performing Organization Name and Address National Bureau of Standards

Department of Commerce

Washington, D. C. 20234

11. Contract or Grant No. C-32369 -C

13. Type of Report and Period Covered Reference Publication 12. Sponsoring Agency Name and Address National Aeronautics and Space Administration

Lewis Research Center

Cleveland, Ohio 44135

14. Sponsoring Agency Code

15. Supplementary Notes

16. Abstract This report presents tables of viscosity, thermal conductivity, and thermal diffusivity of oxygen

as a function of temperature and pressure from the triple point to 320 K and at pressures to 100 MPa. Auxiliary tables in engineering units are also given. Viscosity and thermal conductivity are calculated from previously published correlations. Density and specific heat at constant

pressure, required to calculate thermal diffusivity, are obtained from an equation of state. The

Prandtl number can be obtained quite easily from the values tabulated.

17. Key Words (Suggested by Author(s)) Density; Oxygen; Pressure; Tables;

Temperature; Thermal conductivity; Thermal

diffusivity; Viscosity

18. Distribution Statement STAR Category 34

Unclassified - unlimited

19. Security Classif. (of this report) Unclassified

20. Security Classif. (of this page) Unclassified

21. No. of Pages 87

22. Price* A0 5

* For sale by the National Technical Information Service, Springfield, Virginia 22161 NASA-Langley, 1983

THIRD-CLASS BULK RATE National Aeronautics and

Space Administration

Washington, D.C.

20546

Official Business Penalty for Private Use, $300

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