NATL INST OF STAND & TECH A111D7 231A72

•«,*EAU O* *+ NBS TECHNICAL NOTE 361(Revised)

Metric Supplement - May 1974

U.S. DEPARTMENT OF COMMERCE /National Bureau of Standards

Liquid Densities of Oxygen, Nitrogen,

Argon and Parahydrogen
NATIONAL BUREAU OF STANDARDS

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National Bureau of Standards NOV 11974 Qt\00

Liquid Densities of Oxygen, Nitrogen,

Argon and Parahydrogen (Metric Supplement)

H. M. Roder

Cryogenics Division

Institute for Basic Standards U»5* National Bureau of Standards

Boulder, Colorado 80302

Ted>uu (lqJ vi£ri&, no> Shi /re /i s&d

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U.S. DEPARTMENT OF COMMERCE, Frederick B. Dent, Secretary NATIONAL BUREAU OF STANDARDS. Richard W Roberts. Director Issued June 1974
National Bureau of Standards Technical Note 361 (Revised)

(Metric Supplement)

Nat. Bur. Stand. (U.S.),Tech. Note 361 (Revised), (Metrie Supplement). 114-pages (June 1974) CODEIN: NBTNAE

Revises and up dates NBS Technical Note 361, issued January 31. 1968

For sale by the Superintendent of Documents, U.S. Government Printing Office. Washington, D.C. 20402

(Order by SD Catalog No. 03.46:361 (Revised)

(Metric Supplement). 81.25
CONTENTS

1. INTRODUCTION 1

2. DESCRIPTION OF THE TABLES 2

3. DISCUSSION 5

4. LIMITATIONS 7

5. (OMITTED) 8

6. OXYGEN 9

7. NITROGEN 43

8. ARGON 67

9. PARAHYDROGEN 95

10. REFERENCES 108 APPENDIX 109

List of Figures

Figure 1. Generalized Phase Diagram; Pressure vs. Volume 3 Figure 2. Generalized Phase Diagram; Pressure vs. Temperature 4
CONTENTS

List of Tables

Table 1. Density of Oxygen Near Atmospheric Pressure and Room Temperature . . 9 Table 2. Uncertainties in the Data for Oxygen 10 Table 3. Saturated Liquid Oxygen 11 Table 4. Density of Compressed Liquid Oxygen 23 Table 5. Density of Nitrogen Near Atmospheric Pressure and Room Temperature . 43 Table 6. Uncertainties in the Data for Nitrogen 44 Table 7. Saturated Liquid Nitrogen 45 Table 8. Density of Compressed Liquid Nitrogen 53 Table 9. Density of Argon Near Atmospheric Pressure and Room Temperature ... 67 Table 10. Uncertainties in the Data for Argon 68 Table 11. Saturated Liquid Argon 6 9 Table 12. Density of Compressed Liquid Argon 79 Table 13. Density of Parahydrogen Near Atmospheric Pressure and Room

Temperature 95 Table 14. Uncertainties in the Data for Parahydrogen 96 Table 15. Saturated Liquid Parahydrogen 97 Table 16. Density of Compressed Liquid Hydrogen 101
LIQUID DENSITIES OF

OXYGEN, NITROGEN, ARGON, AND PARAHYDROGEN

[Metric Supplement]

H. M. Roder

Tables of pressure, volume, density and temperature for the saturated

liquid and for compressed liquid states from the triple point to the critical

point, of oxygen, nitrogen, argon, and parahydrogen are presented. The

table entries of temperature are in Kelvin and degrees Celsius, table entries in pressure are in bars and kp/cm2

. Volumes or densities are given in several

different units, and density ratios are tabulated for each entry. Estirrv. . „_ :>_' the uncertainty for the tabulated data are given. The tables were prepared

in the style and in the units preferred by the users. They are intended as source for both technician and engineer.

Key Words: Argon; compressed liquid; density; density ratios; liquid; nitrogen; oxygen; parahydrogen; pressure; saturated liquid; tables; temperature; uncertainties; volume.

1. INTRODUCTION

In this supplement standard density data for the saturated liquid and for compressed

liquid states of four commercially important gases are presented in units commonly used by

the European cryogenic industry. The supplement was prepared at the express request of the Industrial Gases Committee (IGC) of the Commission Permanente Internationale de

l'Acetylene, de la Soudure Autogene et des Industries qui s'y Pattachent (CPI). The values presented are derived from the identical sources and computer programs which have been

used earlier to prepare standard density data for users in the United States. The basic document is National Bureau of Standards (U.S.) Technical Note 361 (Revised), (Poder,

et al. 1972), which was prepared to support a Code for Cryogenic Liquid- Measur ing Devices. This code was presented at the 57th National Conference on Weights and Measures

(U.S. ), and has since been adopted by the conference. The basic document is a logical extension of earlier efforts. The first effort was

pamphlet P-6, "Standard Density Data Atmospheric Gases and Hydrogen," by the Compressed Gas Association (CGA, 1965). In this pamphlet, values of pressure, temperature, and density for the Normal Boiling Point (NBP) ' and Standard Temperature and Pressure (STP) were presented. NBP: 1 atm (760 torr) STP: 1 atm, 0°C
The second effort was NBS Technical Note 361, "Saturated Liquid Densities of Oxygen, Nitrogen, Argon, and Parahydrogen" (Roder, et al. 1968). In addition to the two

state points NBP and STP, this document included the definition of the saturated liquid curve. The sources selected were the best available at that time. In particular the compilations of oxygen, argon, and parahydrogen selected, each representing at least two man years of effort, were not available to the CGA in 1965. The basic document includes all of the data presented previously in tables and graphs.

It also provides the extension to the compressed liquid states which was forecast in Technical Note 361. In addition, the source selected for oxygen is based on a large body of new and

highly accurate data, only a small portion of which was available in 1968. Numerical values

differ from earlier selections by no more than 0. 16%. We hope that the values presented here will serve as "agreed- on" values for some time to come. The supplement follows the basic document in outline and in structure, however, at the request of the sponsor all but two figures were omitted from the supplement. Also

omitted is section 5, in which the use of tables and graphs was described. The appendix has been changed to include the additional conversion factors required for the supplement.

Finally, the sponsor requested that we emphasize the number of significant digits printed in the tables (see also section 4). We print no more than 5 significant figures because the precision in even the best PVT experiments is no better than 1 part in 10000. The accuracy

of the liquid densities is considerably less, on the order of 1 to 4 parts in 1000.

2. DESCRIPTION OF THE TABLES

To understand the properties that are presented in the tables and graphs, it is helpful

to recall one of the "standard" phase diagrams. Try to recollect the presentation of isotherms in pressure-volume (P-V) coordinates as given in figure 1. You may recall the rectangular hyperbolas of PV = constant of the ideal gas, and the critical isotherm first presented in a discussion of the "Van der Waals equation of state. This report concerns the compressed liquid region and the equilibrium boundary between the single phase compressed

liquid region and the two phase liquid-gas region. The compressed liquid region is shown

dotted while the boundary is emphasized in figure 1. The boundary extends from the triple point to the critical point.

Strictly speaking, in this phase diagram the NBP and the triple point are lines extending from liquid to vapor side at the pressure indicated.

2
? Critical \

isotherm \

^Liquid \

isotherm V

^COMPRESSED \

/

1 ZVW/0 REGION

i

1 ^-Critical

^^Point \ <-Gas \( isotherm

X\. VAPOR or GAS ^\^

REGION ^\^

h| TWO PHASE REGION

w~-^~ Saturated

J Liquid Saturated-^

\^Normal Boiling Point Vapor

(is- Triple Point VOLUME

Figure 1. Generalized Phase Diagram; Pressure vs. Volume A second way to show the region of interest is in a pressure- temperature (P-T) phase

diagram. In figure 2 we recognize the vapor pressure curve, the melting line, and we recall

that lines of constant volume or density are very nearly straight lines. The compressed

liquid region is again shown dotted. The equilibrium boundary of concern coincides with the vapor pressure curve. For each gas the various properties are presented in a series of tables: A table giving the densities near atmospheric pressure and room temperature A table giving uncertainties in the data A table giving property values for the saturated liquid A table giving property values for compressed liquid. The first table for each fluid presents values of density for pressures of 1 bar

(0.98692 atm) and 760 torr (1 atm) at temperatures of 0°C and 15° C. (These are the pressures and temperatures specified by the sponsor as representing the 'standards' used by

3
its members). Density ratios from boiling pressures of 1 bar and 760 torr to the room

temperatures values are included in this table.

Typical Line of Constant Density

FLUID

Normal Boiling Point

Triple Point

Critical Point Vapor Pressure Curve VAPOR

or GAS

TEMPERATURE

Figure 2. Generalized Phase Diagram; Pressure vs. Temperature

The second table for each fluid presents values for the uncertainties in the data. The

uncertainties at low temperatures include both the error in the experimental values and the contribution to the error by using an analytical function to represent the experimental values. Errors for values near room temperature are seen to be much smaller because PVT

measurements near room temperature can be made to great accuracy and a better fit to the equation of state can be made. The third table presents values of increasing pressures and corresponding temperatures along the saturated liquid boundary. These two variables define the vapor pressure

curve. The table contains in ascending order even values of pressure in both bar and kp/cm2 and even values of temperature in both K and °C. Other columns contain entries in density, volume, and density ratios. There are two columns of density ratios. The first column is the ratio of the actual density as compared to the density at a boiling pressure of

1 bar. The second column is also a ratio of densities, namely the ratio of the actual density

of the liquid as compared to the density at a boiling pressure of 760 torr. Both ratios are dimensionless. Entries in pressure are closely spaced so that interpolation between values

should not be required. For parahydrogen, the increment in pressure is 0. 1 bar. For the

designates kilogram- force per cm3

, see also appendix

4
other fluids the increment is 0.2 bar. The tables include entries for the Triple Point, a

boiling pressure of 1 kp/cm2

, a boiling pressure of 1 bar, and the Critical Point. These

points are set off by double spacing in the table. In addition a line is included for a boiling pressure of 760 torr. Conversion of units are given in the appendix. Please note that the number of significant figures presented in the tables is not justified on the basis of accuracy,

but are given to maintain internal consistency. The fourth table presents density and density ratios for the compressed liquid states. The horizontal index of this table is pressure given for selected values in even bar. An

additional line shows the equivalent pressure in kp/cm . The primary vertical index is temperature given in Kelvin. Auxiliary entries give the Kelvin equivalent in degrees Celsius, and the vapor pressure corresponding to this temperature in bar. Entries in the table proper are:

a. ) a density ratio, the actual density divided by the saturation density at a boiling pressure of 1 bar. The ratio is of course dimensionless; it corresponds to the first column of ratios in the saturation table described earlier.

b. ) a second density ratio, the actual density divided by the saturation density at a

boiling pressure of 760 torr. This density ratio is also dimensionless and it corresponds to the second column of ratios given in the saturation tables.

c. ) the density in kg/dmJ (kg/litre).

3. DISCUSSION

The nature of progress in cryogenics is such that today's "best" value may be super- seded tomorrow. In the initial effort, Pamphlet P-6 of the Compressed Gas Association

(1965), only values for the NBP and values at NTP were presented. The next report included values for the saturated liquid boundary. The present report includes the PVT values in the compressed fluid states because we know that in many applications the fluid entering pump

intakes is subcooled to prevent cavitation. We have selected the following sources: Weber (1970) for oxygen; Strobridge (1962)

for nitrogen; Gosman, et al. (1969) for argon; and Roder, et al. (1965) for parahydrogen. In addition, we use Hilsenrath, et al. (1955) to establish the NTP and STP values for parahydrogen. The sources selected differ only slightly from earlier selections. The oxygen

reference in particular has become available only in recent years. The most compelling reason for selecting these compilations as sources is that we require consistent values for

the saturated liquid and the compressed liquid states. In our experience the "best" set of values is obtained when in addition to PVT and vapor pressure data other experimental data such as measurements of the liquid specific heats, the heats of vaporization, or the velocity

of sound in the liquid are included in the establishment of the basic PVT surface. One advantage in selecting these sources is that industry and one major user,

National Aeronautics and Space Administration (NASA) will now be using consistent data.

5
The data in the NASA references for oxygen and hydrogen [NBS Tech. Note 384, McCarty and Weber (1971), and NBS Tech. Note 617, McCarty and Weber (1972)] are taken from Weber

(1970) and Eoder, et al. (1965). One other advantage arises when we select these compilations

as sources: except for hydrogen, we can get the values at or near room temperature directly from the equation of state, interpolated to the accuracy of the original data. The last point requires a bit more discussion because it ties in with the uncertainties

in the values presented at or near room temperatures. In the present report we have used a high order interpolation - the equation of state - to get these values. We are justified

in using a high order interpolation because the various experimenters went to considerable

lengths to get the most accurate PVT values at conditions close to room temperature. According to Cragoe (1941), relative measurements of pressure and volume near room temperature can be made to a few parts per million, and the scatter between PVT values of different observers can to a large extent be explained by the use of different fundamental

constants. In tables 2, 6, 10, and 14 we indicate an uncertainty of 0.01% as the uncertainty

in molar volume at room temperature. The molar volume at 0°C and 1 atmosphere is the familiar 22.4 liters per mole encountered in elementary texts. The uncertainty is based on

a consideration of the ice point temperature, T Q

, rather than on a comparison of different experiments. The fundamental constant T Q

is now defined to be 273. 15 K, but the average

over a large number of determinations of different investigators for different gases was

273. 165 (Beattie, 1941). We have taken the difference between these two numbers as an

indication of the true uncertainty in the molar volumes. Even if the values of different authors are compared directly, the differences are not much larger than 0.01%. Take for example hydrogen, the molar volume is 22428.5 cm3 /mole according to Woolley, et al. (1948), while it is 22433. 6 cm3 /mole according to Michels, et al. (1959). The difference is 0.0 22%. In contrast to this there is no difference between recent measurements on oxygen

by Weber (1970) and those of Michels, et al. (1954) if one uses identical values for the gas

constant, R, and T Q

. Another word on the uncertainties in tables 2, 6, 10, and 14: The uncertainties are

of course ultimately based upon the accuracy of the various experiments. We take them from the authors' estimates, from the statistics of the coefficients of the equation of state, and from the differences between practical temperature scales and the absolute thermo- dynamic one. We present uncertainties for all three variables, pressure, volume, and

temperature. This allows the user to enter the tables with any combination of variables and

obtain the uncertainty in the remaining one. For example, in obtaining entries for the other

tables, we have assumed either temperature and density or temperature and pressure to be

exact. Thus, only uncertainties in pressure in the first case and density in the second case are of concern in determining the number of digits presented in each table.
From the first effort to the present one, changes In property values have been

minimal. The actual changes are best described in terms of density. The room temperature

values presented in this report of oxygen and argon at 1 atmosphere differ by about 0. 02% from those given by the CGA in 1965, while those for nitrogen and parahydrogen are

unchanged. On the other hand, the densities of the saturated liquid at 760 torr have changed from earlier values by 0. 16% for oxygen and 0. 1% for nitrogen. They are virtually unchanged

for argon and parahydrogen.

4. LIMITATIONS

In practice, a number of problems are encountered that introduce errors beyond what we might expect from the uncertainties inherent in the data. A few of the practical problems

are indicated below.

Instrumentation. Pressure and temperature measuring devices used in custody transfer

situations will rarely be capable of the best state of the art measurements, i.e. , those that are

possible under controlled laboratory conditions. Thus, in most cases the error in instru- mentation will be much larger than the uncertainties given for the property tables. Equilibrium vs. Non- equilibrium Properties . The informed engineer recognizes that the processes of transfer, transport, pressurizing, siphoning, and stratification in storage tanks are all non- equilibrium events. The properties presented in this report are equilibrium

properties.

Subcooling . We have indicated that pump intakes, or, for that matter, flow meter intakes, are usually subcooled to prevent cavitation. It is important to recognize that the degree of subcooling, that is the pressure and temperature parameters, may change during liquid transfer. Purity . The purity of the product will also play a role. The properties presented here are

for the pure product made available under laboratory conditions. They may not be appropriate for certain purity grades of commercially available gases without some adjustment for

the known impurities.

Significant Digits . The values presented in this report were obtained from various computer programs. We have in the past made these programs available to any user requesting them. However, different computers will return different results from the same programs;

in particular, they will round differently. The user should be aware of the following: The

accuracy of the data for liquid conditions is on the order of 0. 1 to 0.3%, while the accuracy

of the room temperature values is on the order of 0.01 to 0.02%. We have, therefore,

printed no more than 5 digits anywhere. Please bear in mind that even the fourth digit is uncertain for roost values , that is, the digits printed are only to maintain internal consist- ency of the tables and to allow you to check out your computer programs. If occasionally

pairs of values or reciprocals do not seem to correspond, then the fault can be traced to rounding errors.

7
(OMITTED)
6 . OXYGEN

The data for oxygen tabulated here are based on the paper by Weber (1970). Additional, extensive tables of values based on this source were prepared by McCarty and Weber (1971)

for NASA. Values for the saturated liquid were obtained by first solving the vapor pressure

equation for either pressure or temperature, and then using the resulting P and T as input to Weber's programs to obtain the corresponding liquid density. Densities for the compressed

liquid were obtained from Weber's programs directly using appropriate values of P and T as

input.Values near room temperature are given in table 1, uncertainties for the data in table 2, values for the saturated liquid are given in table 3, and values for the compressed liquid are shown in table 4.

Table 1 Density of Oxygen Near Atmospheric Pressure and Room Temperature

Temperature Pressure Density Volume

gram- mole/cm3 kg /dm3 cm3 /gram- mole dm3 /kg 0°C 1 bar

760 torr 4.4073xl0~ 5 4.4658xl0" 6 1.4103xl0" 3 1.4290xl0" 3 22690.22392. 709.08 699.79 15°C 1 bar

760 torr

4. 1770xl0~ 5 4.2324xl0~ 5 1.3366xl0" 3

1. 3543xl0~ 3 23940.23627.

748. 17 738.37

Density Ratios - Dimensionless

Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 0° C

Liquid Density at a boiling pressure of 1 bar/density at 1 bar and 15° C

809.50

854. 13 Liquid Density at a boiling pressure of 760 torr /density at 760 torr and 0°C

Liquid Density at a boiling pressure of 760 torr /density at 760 torr and 15° C

798.47 842.49

Liquid density at a boiling pressure of 1 bar 1 . 1416 kg/dm3 Liquid density at a boiling pressure of 760 torr 1.1410 kg /dm3
Densities at the boiling point at 760 torr differ by 0.05% from CGA pamphlet P-6, and by 0. 03% from the value given in the earlier version of Technical Note 361 . The densities

for the saturated liquid differ by a maximum of 0. 16% from the earlier values at temperatures

up to 150 K, that is, the new values are within the uncertainties previously specified. Above

150 K to the critical point the departures rise to several percent because better values for both critical density and critical temperature are now available. The present values are considered to be better because in addition to PVT data, experimental specific heats and

dielectric constant measurements near the critical point were used to establish the PVT

surface.

Table 2

Uncertainties in the Data for Oxygen

variable uncertainty range of temperature temperature 0.05 K

0.02% 0.1%

0. 015 K

below 90 K

between 90 and 154 K

near critical room temperature volume 0.1% 0.2%

larger

than 0. 5% 0.01%

between 54.353 and 60 K

between 65 and 150 K

between 150 K and critical room temperature

pressure 0. 1% 0.02%

0. 1% 0.01%

below 90 K

between 90 and 154 K

near critical room temperature

Routine checks of values in the present tables against those of Technical Note 361 (Revised) revealed a discrepancy in table 4 of the basic document. Entries 2. and 3. of table 4 of the basic document are too small by a factor of 1.0003. An Erratum for the basic document has been prepared.

10
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DENSITY OF COKPRESSEO LIOUID

TABLE E TRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR 3

DENSITY

DENSITY

DENSITY

RATIO,

RATIO,

, KG/DM3

-IQUIO DENS IOUID OENS TY/CENSITY AT A TY/CENSITY AT A BCILING

BOILING PRESSURE OF PRFSSURE OF

1 BAR,

760 TCRR MENSICNL

CIMENSI

_ SS :nless

BAR KP/CM*0.800 1.000 0.816 1.020 2.000 2.0394.000 4.0796.000 6.1188.000 8.1580.000 0.197 15.000

15.296

20.000

20.394

25.000

25.493

0.000

0.591 J5.000 J5.690

.0.000 .0.789

88.0 -165.15

0.802

1.0089

1.0095 1.1518 1.00911.0097

1.1520

1.0095

1.0100 1.1525 1.0099

1.0104

1.1529 1.0102 1.01081.1533

.0106

.0111 .1537

1.0115 1.0121 1.1546

1.0124

1.0130

1.0133

1.0139 1.1568.0148

.1579

.0151 .0157

.1589

1.0160

1.0166

1.159?

38.1 -185.05

0.810

1.0085

1.0090 1.1513 1.00871.0092

1.1515

1.0091 1.0096

1.1520

1.0094

1.0100

1.1524 1.0098

1.0103

1.1528

.0102

.0107

.1532 1.0116 1J1543

1.0120 1.0126

1.1553

1.012? 1.0135

1.1564

.0144

.1574

.0147

.0153 1.1584

1.0156 .0161

1.1594

88.2

-181.. 95 0.819 1.0086

1.1508 1.0062

1.0068

1.1510

1.0092

1.1515 1.0090

1.0095

1.1519 1*0099 1.1523

.0097

.0103 .1527

1.0107

1.0112

1.1538

1.0116

1.1548 1.0125

1.0130 1.1559

.0134 .0139

.1569

.0143 L.0148

1.0152

1.0157

1.1590

88.3

-18",. 85 0.828

1.0076

1.0082

1.1503 1.0076

1.008". 1.1506

1.0082

1.0087 1.1510 1.00861.0091

1.1514 1.0089

1.0095 1.1518

.0093

.0099 .1523

1.0102

1.0108 1.1533

1.0112 1.0117

1.1544

1.0121 1.0126

1.1554

.0130

.0135 .1564

.0139

1.014". .1575

1.0153

1.1585

88 .4

-18".. 75 0.836

1.0072

1.0077

1.11.98

1.0074

1.0079

1.1501

1.0078

1.0083

1.1505

1.0081

1.0087 1.1509

1.0065

1.0091 1.1513

.0069 .0094 .1518

1.'0098 1.0104

1.152e

1.0107 1.0113

1.1539

1.0116 1.0122

1.1549

.0125

.1560

.0134

.0140

.1570

L.0143

1.0149

1.1580

88.5

-16".. 65

0.81.7

1.0068 1.0073

1.11.93 1.0070

1.0075 1.1496

1.0073

1.0079

1.1500

1.0077

1.0083 1.1504 1.0081 1.0066

1.1509

.TJ085 .0090 .1513

1.0094 1*15231.0103

1.0105 1.1534

1.0112

1.0118

1.1544

.0121

.0127

.1555

.0130

.0136

.1565

1.0139

1.0145 .1575

88.6 -184.55

0.856

1.0063

1 . 69 1.11.89 1.0065

1.0071

1.1491

1.0069

1.0074

1.1495

1.0073

1.0078 1.1*99

1.0076 1.0082

1.1504

.0080

.0086 .1508

1.0090

1.0O95

1.1519

1.0099

1.0104

1.1529

1.0108 1.0113

1.1540

.0117

.0123

.1550

.0126

.0132

.1560

.0135

. 0141 .1571

88.7

-18".. 1,5 0.865

1.0059

1.006". 1.0061

1.0066

1.11)86

1.0065

1.0070 1.1490

1.006B

1.0074 1.1494

1.0072

1.0078

1.1499

.0076

.0081 .1503

1.0085

1.0091 1.1514

1.0095

1.0100 1.1524

1.0104 1.0109

1.1535

.0113

.0118 .1545

.0122

.0127 .1555

.0131

.0136

.1566

88.8

-16".. 35 0.875

1.0055

1.0060

1.11.79 1.0057

1.0062

1.11.81

1.0060

1.0066 1.1485

1.0064

1.0070 1.1489

1.0068

1.0073

.0072 .0077

.1498 1.0081

1.0087

1.1509 1.0O90

1.0096

1.1519

1.0099

1.0105

1.1530

.0109 .0114

.1540 .0123.1551

.0127

.0132 .1561

68.9

-18".. 25

0.88".

1.0050 1.0056

1.11.71. 1.0052

1.0058 1.1476

1.0056

1.0061 1.1480

1.0060

1.0065 1.1485

1.0064

1.0069 1.1489

.0067

.0073 .1493

1. 0077 1.15041.0086

1.0092 1.1514

l.,0095 1.0101 1.1525

.0104 .1535

.0114

.0119 .1546

.0123

.0128

.1556

89.0

-18".. 15

0.89".

1.001.6 1.0051

1.11.69

1.001)8 1.0053

1.11.71

1.0052

1.0057

1.1475

1.0055 1.0061

1.1480 1.0059

1.0065 1.1484 1

.0063

.0069 .1468

1.0072

1.0076

1.1499

1.0082

1.0087

1.1510

1.0097

1.1520

.0100 .0106

.1531

.0109

.0115

.1541

.0118 .0124

.1551

89.1

-16".. 05

0.901.

1.001.2 1.0 0471.001. 1) 1.1466

1.0047 1.0053

1.1470

1.0051

1.0057 1.1475

1.0055

1.0060 1.1479

.0059

.0064

.1463

1.0068

1.0074

1.1494

1.0077 1.0OB3

1.1505

1.0087 1.0092

1.1515

.0096 .1526.0105

.Clll .1536

.0114

.0120 .1547

89.2 -163.95

0.913

1.0 037

1.001.3 1.11.59 1.0039

1.0045

1.1461

1.0043 1.0048

1.1465

1.0047

1.0052

1.1470

1.0051

1.0056

1.1474

.0054

.0060

.1478

1.0064 1.0069

1.1489

1.0073

1.0O79

1.1500

1.0083

1.0086 1.1511

.0092

.0097

.1521

.0101

.0106

.1531

.0110 .0116

.1542

89.3 -183.85

0.923

1.0033

1.0O38

1.11.51.

1.0035 1.0040 1.14561.0039

1.0044 1.1460

1.0042

1.0046 1.1465 1.0052

1.1469

.0050

.0056 .1473 1.00601.0065 1.0069

1.0074

1.1495

1.0076 1.0084

1.1506

.0093

.1516

.0097 .0102

.1527

.0106

.1537

89.". -183.75

0.933

1.0029

1.0034

1.11)1)9

1.0030 1.0036

1.1451

1.0040 1.1455

1.0038

1.0044

1.1460 1.00471.1464

.0046

.0051 .1469

1.0055 1.0061

1.1479

1.0065

1.0070

1.1490

1.0074

1.0080

1.1501

.0063

.0089

.1511

.0093

.0098 .1522

.0102

.0107

1.1532

89.5 -183.65

0.91)3

1.0021) 1.0030 1.1*41) 1.0026 1.00321.0030

1.0035

1.1451

1.0034

1.0039

1.1455

1.0038

1.0043

1.1459

.0041

.0047 .1464

1.0051 1.C0561.0O60 1.0066 1.14851.0070 1.0075

1.1496

.0079

.0085

.1507

.0086

.0094 .1517

L.0097

1.0103 .1528

89.6 -163.55

0.953

1.0020 1.0025 1.14391.0022 1.00271.0026 1.0031

1.1446 1.0029

1.0035

1.1450 1.0033

1.0039

1.1454

.0037

.0043

.1459

1.0047 1.0052

1.1470

1.0D62

1.1460

1.0066

1.0071

1.1491

.0075

.0080

.1502

.0084

.0090

.1512

.0093

.0099

.1523

89.7

-183.1.5 0.963 1.0015

1.0021

1.11)31) 1.0017 1.0023 1.1436

1.0021

1.0027

1.1441 1.0025

1.0031

1.1445 1.0029

1.0034

.0033

.0038 .1454 1.00421. 0048

1. 1465

1.0052

1.0057

1.1476 1.0061

1.0067

1. 1486

.0071

.0076 .1497.0085

.1507 .0095.1518

89.6 -163.35

0.971.

1.0011

1.0 017 1.1429

1.0013

1.0019 1.1431

1.0017 1.0022 1.1436

1.0021 1.0026

1.1440

1.0025

1.0030 1.1444

.0029 .0034

.1449

1.0038 1.0044

1.1460

1.0048

1.0053

1.1471

1.0057 1.0063.0066

.0072 .1492

.0076

.0061

.1503

.0085

.0090

1.

c l?

69.9 -183.25

0.98". 1.0007

1.0012

1. ll)2l> 1.0009

1.0014

1.1426

1.0013

1.0018

1.1431

1.0016

1.0022

1.1435 1.0020

1.0026

1.1440

.0024

.0030

.1444

1.0034

1.0039 1.1455

1.0043

1.1466

1.0053

1.0058

1.1477

.0068

.1487

.0071 .0077

.1496

1.0081 .0086

1.1508
XYGEN - CONTINUE!)

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

2

3

DENSITY

DENSITY DENSITY

RATIO, L RATIO, L

, KG/DM3

IOUIO DENSITY/OENSITY AT A IOUID OENSITY/DEf.SITY AT A BOILING PRESSURE OF BCILING PRESSURE CF 760 TCRR MENSICNL

OIHENSI

SSNLESS

BAR KP/CM 2 0.800 1.000 2.000

0.816 1.020 2.039

4. 000

l».079 6.000

6.118 8.0008.158 10.00010.197 15.000

15.296 20.00020.354

25.000 25.49330.000

30.591

35.000 35.690 0.000

.789

90.0 -183.15

0.99<, 1.0002 1.0001, 1.0 08 1.00101.11,19 1.11,21

1.0008

1.11,26

1.0012

1.0018

1.11(30

1.0016

1.0021

1.11,35

1.0020 1.0025

1.11(39

1.0025 1.0035 1.1450

1.0039 1.0O45

1.146

1.0054

1. 1472

1.0058 1.0063

1. 1482

1.0067 .0073

1.1493

.0076 .0082

1.1504

90.1 -183.05

1.005 1.0000

1.0005

1.11,16

1.0004

1. 11,21

1.0008 1.0013

1.11,25 1.0012

1.0017

1.11,30

1.0016

1.0021 I.U34

1.0025

1.0031 1.1445

1.0O35

1.0040 1.00441.0050 1.1467

1.0054 1.0059

1.1478

1.0063

1.006e .0072

.0078

90.2 -182.95

1.015

0.9996 1.0001

1.11,11

1.0000 1.0005

1. 11,1

1.0003

1.0009

1. 1<,20

1.0007 1.0013

1.11,25

1.0011

I.O017

1. 0021 1.0026 1.14401.0030

1.0036

1.1451

1.0040

1.0045

1.0049 1.0055

1.1473

1.0059

1.0064 1.1483

.0068

.0074

.1494

90.3 -162.85

1.026

0.9991 0.9997

1.11,06

0.9995 1.0001

1.11,11

0.9999

1.0005

1.11,15 1.0003

1.0008

1.11(20

1.0007

1.0012

1.1424

1.0017

1.0022

1.1435

1.0026

1.0032 1.00361.0041 1.1457

1.0045 1.0051 1.14681.0055

1.0060

1.1475

1.0064 .0069 .1469

90.4 -162.75

1.0 37

0.9987

0.9992

1.11,01

0.9991 0.9996

1.11,06 0.9995

1.0000

1.11,10 0.9999

1.0001,

1.11(15

1.0003

1.0008

1.11(19

1.0012

1.0016

1.1430

1.0922

1.0027

1. 1441

1.0031 1.0037

1.1452

1.0041 1.0046

1.1463

1.0050

1.0056

1.1474

1.0060 .0065

1.1484

90.5 -162.65

1.01,8 0.9982

0.9986 1.1396

0.9986

0.9992

l.lltOl

0.9990

0.9996

1.11(05 0.9994

1.0000

1.11(10

0.9998

1.0004

1. 11,11. 1.C008 1.00131.1425

1.0018 1.0023

1.1436

1.0027

1.0033

1.1447

1.0037 1.0042

1.1458

1 .0046 1.00521.0055 .0061

1.1480

90.6 -182.55

1.059

0.9978

0.9981, 1.1391

0.9982

0.9988 1.1396

0.9986

0.9991

1.11(00 0.9990

0.5995

1.11(05

0.5991, 0.5999

I. 1409

1.0004 1.000 c 1.142C1.0013

1.0019 1.1431

1.0023

1.0028 1.1442

1.0032

1.0038 1.14531 .0047

1. 1464

1.0051 1.0057

1.1475

90.7

-182. ",5 1.070

0.9971, 0.9979

1.1386

0.9978 0.9983

1.1391

0.9982 0.9987

1.1395 0.9991

1.11(00

0.9990 0.9995

1.1404

0.9999 1.0005

1.1427

1.001° 1.0024

1.0028 1.00341.0036 1.0043

1.1459

1.0047

1.0052

1.1470

90.8 -182.35

1.081

0.9969

0.9975

1.1381

0.9973 0.9979 1.13860.9977

0.9983 1.1390 0.99810.9967 1.1395

0.9985

0.9991

1.1399

0.5995 1.0000

1. 1411

1.0005

1.0010 1.1422

1.0014

1.0020 1.1433

1.0024

1.0029 1.1444

1.0033

1.0039

1.1454

1.0043

1.0046

1.1465

90.9 -182.25

1.092

0.9965

0.9970 1.1376

0.9969

0.9971, 1.1381

0.9973

D.9978 1.1385

0.9977

0.9962

1.1350

0.9981 8.9986

1.1394

0.9991

0.5996

1.1406

1.0000

1.0006

1.1417

1.0010 1.0015

1.1426

1.0020 1.0025

1.1439

1.0029

1.0035 1.1450

1.0039

1.1460

91.0 -182.15

1.103

0.9961 0.9966 1.13710.9965

0.9970 1.1376

0.9969

0.9971, 0.9972

0.9978

1.1365

0.9976

1.1389

0.5986

0.999?

1. 1401

0.9996 1.14121.0006

1.0011

1.1423

1.0015

1.0021

1.1434

1.0025

1.0030

1.1445

1.0040

1.1455

91.1 -162.05

1.115

0.9956 0.9962

1.1366

0.9960 0.9966 1.1371

0.9961, 0.9970

1.1375 0.9968

0.997l( 1.1380

0.9972 0.9978

1.1364 0.9962

0.9987

1.1396

0.9952

0.9997

1.1407

1.0001 1.0007

1.1418

1.0011 1.0017

1.1429

1.C021 1.0026

1.1440

1.0030

1.0036

1.1451

91.2 -181.95

1.126

0.9952 0.9957

1.1361

0.9956

0.9961 1.1366

0.9960

0.9965

1.1370

0.996l( 0.9969

1.1375

0.9968

0.9973

1.1379

0.9978

1.1391

0.9987

0.9993

1.1402

0.9997

1.0003

1.1413

1.0007

1.0012

1.1424

1.0016 1.0022

1.1435

1.0026

1.0031 1.1446

91.3 -161.85

1.138

0.991t7 0.9953 1.1356

0.9951 0.9957

1.1361

0.9955

0.9961 1.1365

0.9959

0.9965

1.1370

0.9963

0.9969

1.1374

0.9973

0.9979

1.138?

0.9983

0.9989

1.1397

0.9993

0.9998 1.1408

1.0003

1.0008

1.1419

1.0012

1.0018

1.1430

1.0022

1.0027

1.1441

91.* -161.75

1.149

0.991,3

0.991,8 1.1351

0.991(7 0.9952 1.1356

0.9951

0.9956 1.1360 0.99550.9960 1.1365

0.9959

0.9964

1.1369

0.9965

0.9974

1.1381

0.9979

0.9964

1.1392

0.5989 0.9994

1.1403

0.9998 1.0004

1.1414

1 .0008 1.0013

1.1425

. 0017 .0023

1.1436

91.5 -181.65

1.161

0.9939

0.991,1, 1.131,6

.991,3 0.991*6 1.13510.991(7 0.9952

1.1355

0.9951

0.9956

1.1360

0.5955

0.9960

1.1365

0.5965

0.9970

1.1376

0.9974

0.9980

1.1387

0.9984

0.9990

1.1398

0.9994

0.9999

1.1409

1.0004

.0009 1.1420

.0013

.0019

.1431

91.6 -181.55

1.173

0.9931. 0.991,0

1.131,1

0.9938

0.991,1, 1.131,6

0.991(2

0.991,8 1.1350

0.991(6 0.9952

1.1355

1.9950 0.9956

1.1360

0.5960

0.9966

1. 1371

0.9970 0.9976

1.1382

0.9980

0.9985

1.1393

0.9990 0.9995

1.1405

1.0005

1.1416

.0009

.0014

.1427

91.7

-161.1,5 1.185 0.9930

0.9935

1.1336

0^9939

1.131,1

0.9938

0.991.3

1.131,5

0.991(2

0.991.7 1.1350

0.5946

0.5951

1.1355

0.5956 0.5961

1.1366

0.9966 0.9971

1.1377

0.9976 0.99810.9985 0.9991

1.1400

1.0001

.1411

.0005

.1422

91.8 -181.35

1.197

0.9925 0.9931

1.1331

0.9929

0.9935

1.1336

0.9933

0.9939

1.131(0 0.9937

0.991.3 1.1345

0.5942

0.9947 1.1350

0.9952

0.9957

1.1361

0.9961 0.9967

1.1372

0.9971 0.9977

1.1384

0.9981

0.9987 1.1395

.5991

.9996

.1406

.0000

.0006 .1417

91.9 -181.25

1.209 0.9921

0.992E 1.1326

0.9925

0.9930 1.1331

0.9929

0.993i( 1.1335

0.9933

0.9939

0.5037

TJ.9943 1.1345

0.5947

0.5953

1.1356

0.9967 0.9963 1.13670.9967

0.9973

1.1379

0.9977

0.9982

1.1390

.9587

.1401

.9996

.000? .1412
IOUID OXYGEN - CONTINUED

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR12

3

DENSIT

. DENSIT

DENSIT

Y RATIO, LIQUID DENSITY/OEN

Y RATIO, LIQUID OENSITY/OEN

Y, KG/DM3

SITY AT A SITY AT A BOILING FOILING PRFSSURE OF 1 9AR, DIHENSIONL ESS PRESSURE OF 760 TCRR, CIMENSI CNLFSS

BAR 0.800 1.000 KF/CM 2 0.816 1.020 2.000 2.039h.OOO

11.079 6.O00 6.118

8.000

8.158

10.000

10.197 15.000

15.296 20.00020.394 25^93

30.000 30.59135.000

35.690

40.000

40.789

92.0 -181.15

1.221

0.9916

0.9922 1.1321

0.9921

0.9926 1.1326

0.9925

0.9930 1.1330

0.9929

0.9934

1.1335

0.5933

0.9938

1.1340

0.9943

0.9948

1J1351

0.9953 0.9956

1.1362

0.9963

0.9968

1.1374

0.9973

0.9978 1.13B5

0.5962

1.1396

0.9992

0.9997 1.1407

92.1 -181.05

1.233 0.9917 1.1316

0.9916 0.9922

1.1321

0.9920 0.9926 1.1325 0.9924

0.9930

1.1330

0.9928 0.9934

1.1335

0.5938

0.5944

1. 1346

0.9948

0.9954 1.1357

0.9958

0.9964

1.1369

0.9968 0.9974

1.1380

0.9578 0.5584

1.1391

0.9988

0.9993

1.1402

92.2 -160.95

1.246

0.9908

0.9913

1.1311

0.9912

0.9917

1.1316

0.9916

0.9921

1.1320

0.9920

0.9925 1.1325

0.9924

0.9929 1.1330

0.5934

0.5940

1. 1341

0.9944

0.9950 0.9954

0.9960

1.1364

0.9964

0.9969 1.1375

0.5974

0.9575

1.1386

0.9964

0.9989 1.1397

92.3 -180.85

1.258

0.9903

0.9909 1.1306

0.9907

0.9913

1.1310 0.9911

0.9917 1.1315 0.9916

0.9921 1.1320

0.9920 0.9925

1.1325

0.9930

0.9935 1.1336

0.9940

0.9945

1.1348

0.9950

0.9955 1.1359

0.9960 0.9965

1.1370

0.5970 0.5975

0.9979

0.9985

1.1393

92. "4 -180.75

1.271

0.9899

0.9901. 1.1301

0.9903

0.9908 1.1305

0.9907

0.9912

1.1310

0.9911

0.9917

1.1315

0.5915

8.9921 1.1320

0.9925

0.5931 1.1331

0.9935

0.9941

1.1343

0.9945

0.9951 1.1354

0.9955

0.9961 1.1365

0.9965

0.5571 1.1377

0.9975

0.9980 1.1388

92.5 -180.65

1.283

0.5891. 0.9900 1.1296

0.9898

0.9904

1.1300

0.9903

0.9906 1.1305 0.99070.9912

1.1310

0.9911 0.9916

1.1314

0.5921

0.5926

1.1326

0.9931 0.9937

1.1338

0.9941 0.9947

1.1349

0.9951 0.9957

1.1360

0.9961 0.5566

1.1372

0.9971

0.9976

1.1383

92.6 -180.55

1.296

0.9890 0.9895

1.1291

0.9891. 0.9899 1.1295

0.9896 0.9904

1.1300

0.9902 0.9908

1.1305

0.9906

0.9912

1.1309

0.5917

0.9922

1.1321

0.9927

0.9932 1.1333

0.9937 0.9942

1. 1344 0.9947

0.9952 1.1356

0.5957

0.5962 1.13670.9972

1.1378

92.7

-180.1(5 1.309

0.9865

0.9891

1.1286

0.9890

0.9895

1.1290

0.9894

0.9899

1.1295

0.9898

0.9903 1.1300

0.9902 0.9907

1.1304 0.5912

0.59ie

1.1316

0.9922

0.9928

1.1328

0.9932

0.9938 1.1339

0.9942

0.9948

1.1351

0.5952

0.9956 1.1362

0.9962

0.9968 1.1373

92.8 -180.35

1.322 0.9681

0.9886 1.1260

0.9885

0.9891 1.1285

0.9889

0.9895

1.1290

0.9893

0.9899

1.1295

0.5898

0.9903

1.1299

o.5°oe 0.9913

1.1311

0.9918 0.9923

1.1323

0.9928

0.9934

1.1334

0.9938

0.9944

1.1346

.994e 0.9954

1.1357

0.9958 0.9963

1.1368

92.9 -180.25

1.335

0.9877

0.9882 1.1275

0.9861

0.9866 1.1280

0.9685

0.9890 1.1285

0.9689

0.9894 1.1290

0.9893

0.9899 1.1294

0.5904

0.5909

1.1306

0.9914

0.9919

1.1318

0.9924

0.9929

1.1329

0.9934

0.9939 1.1341

0.9944

0.9949

1.1352

0.9954

0.9959 1.1363

93.0 -180.15

1.31.8

0.9672

0.9878 1.1270

0.9876

0.9882

1.1275

0.9881

0.9886

1.1280 0.5885

0.9890

1.1285

0.9894

1.1289

0.9899 0.9905

1.1301

0.9909

0.9915

1.1313

0.3919 0.9925

1.1324

0.9930

0.9935

1.1336 0.5940

0.5945

1.1347

0.9949

0.9955 1.1359

93.1 -160.05

1.361 0.9866

0.9873 1.12650^9877

1.1270

0.9876

0.9681 1.1275 0.9866

1.1288 •;E

0.9895

0.5900

1.1296

0.9905 0.9910

1.1308

0.9915 0.9921 1.13190.992S

0.9931

1.1331

0.5935

0.9941

1.1342

0.9946

0.9951 1.1354

93.2 -179.95

1.375

0.9863

0.9869 1.1260

0.9867

0.9873 1.1265

0.9872

0.9877 1.1270 0.98760.9881

1.1275

0.5S80

0.9365

1.1279

0.9890 0.9896

1.1291

C.9901 0.9906

1.1303

0.9911

0.9916

1.1314

0.9921

0.9926

1.1326

.5531 0.5536

1.1337

0.9941 0.9946

1.1349

93.3 -179.85

1.388

0.9859

0.9661. 1.1255

0.9863

0.9868

1.1260

0.9867

0.9673 1.1265

0.9871

0.9677

1.1269

0.9876

0.5881

1.1274

0.5886

0.9891

1.1286

0.9896

0.9902

1.1298

0.9906

0.9912

1.1310

0.9917

0.9922

1.1321

0.5927 0.9932

1.1333

0.9937

0.9942

1.1344

93.4 -179.75

1.1)02

0.9851. 0.9860 1.12500.9859

0.986l( 1.1255

0.9863

0.9868 1.1260

0.9867

0.9872 1.1264

0.9871

0.5877 1.1269

0.5682

0.5687

1.1281

0.9892

0.9897 1.1293

0.9902

0.9908 1.1305

0.9912

0.9918 1.1316 0.99220.9926

1.1326

0.9932

0.9938 1.1339

93.5 -179.65

l.*15

0.9850

0.9855

1.121.5

0.985l( 0.9859

1.1250

0.9858

0.9864

1.1255

0.9863

0.9868 1.1259

0.9867

0.9872

1.1264

0.5877

0.5883

1.1276

0.9888

0.9893

l.izea

0.9696 0.9903

1.1300

0.9908

0.9913

1.1311

0.9918 0.9923

1 .1323

0.992K 0.9933

1. 1334

93.6 -179.55

1.1.29

0.981.5 0.9851

1.121(0

0.9850

0.9655

1.121(5

0.9854 0.9859

1.1249 0.9858

0.9863

1.1254

0.9862

0.9868

1.1259

0.5873

0.5878

1,1271

0.9883

0.9889

1.1283

0.9893

0.9899 1.1295

0.9904

0.9909 1.13060.9919 1.1318

0.9924

0.9929

1.1329

93.7

-179. ".5 1.443

0.981.1

0.981.6 1.1235

0.981(5 0.9851

1.1240 0.9849

0.9655

1.1244 0.9854

0.9859

1.1249

0.9858

0.9963

1.1254 0.5874 1.1266

0.9879

0.9884 1.1279

0.9869

0.9894

1.1290

0.9899

0.9905

1.1301 O.9909

0.5515

1.1313

0.9919

0.9925

1.1324

93.8 -179.35

1.1.57

0.9836

0.981.2 1.1230

0.981(1

0.981.6 1.1234

0.9845

0.9850 1.1239

0.9649

0.9655

1.1244

0.9853

0.5859

1.1249

0.5864

0.5865

1.1261

0.9874

0.9860

1.1273

0.9865 0.9890

1.1285

0.9395

0.9900 1.1296

0.5905

0.5511 1.1306

0.9915

0.9921

1.1319

93.9 -179.25

1.1.71 0.9832

0.9837 1.1224

0.9836

0.981(2 1.1229

0.9641

0.9846 1.1234

0.9845

0.5850

1.1239

0.9849

0.9854

1.1244

0.9660

0.5865

1.1256

0.9870 0.9875 1.12660.9860 0.5886

1.1280

0.9891

0.9396

1.1291

0.9901

0.5506 1.1303

0.9911 0.9916 1.1315
TABLE * - CONTINUE! :OMFRESSEO LIOUIO OXYGE

1. TEMPERATURE, K 2. TEMPERATIRE, C 3. VAPOR PRESSURE, BAR

OENSI Y RATIO, LIQUID OENSI TY/CENSI

DENSI Y RATIO, LIOUIO OENSITY/OENSI

OENSI Y, KG/OM3

9<».2 L78.95

1.511.

9*.

178.85 1.528

95.2

177.95 1.663

95.3

L77.85 1.679

95.5

.77.65 1.710

95.7

.77.1.5

1.71.2

«76»

1152

9836

0.981.1 1.1229

978?

9768 1168

9776 9783 1163

9773

9779

1157

9755

9761

11 37

981.0 0.981.5

981.6

123". 1.1239 1.1251

9627

983?

12 19

9796

9801

1183

97 c 5 9761

1137

0.9B66

0.9871 1.1263

9857

9862

1251

981.8 9853

121.3

9766 9792

117?

9876

9881

1?75

9867 9873

1 2 6 5

9833

1220

1?67

9865

0.9902

0.9908 1.1305

0.9898

0.9903

1.1300

0.9891. 0.9B99 1.1295

9885 0.9895

0.9872 0.9878

1.1270

9531. 9939

1227

0.581.5 0.9850

1.1239

0.9855

1.1251

9830 9835

1222

0.581.0 0.581.6

1.1231,

0.9851

0.9856

1.121.6

9825

9831

1217 0.5836 0.5e*l1.1229

0.981.6 0.9652

1.12*1

9821 9826

1212

0.5831

0.5837

1.1221.

0.98*2

0.981.7 1.1236

9817 9822

1207

0.5827

0.5832 1.1215

0.9838

0.98*7

1.1231

9812 9817

1202

0.5823

1.1211.

0.9833

0.9839

1.1226

9808 9813

1197

0.5818

0.5821. 1.1209

0.9e29

0.983*

1.1221

9803

9809

1192

0.5811. 0.5819

1.1201.

0.9625

0.9830

1.1216
OENSITY OF COMPRESSED LIOUID OXYGEN

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

TAeLE ENTPIES OENSITY RATIO, LIQUID OENSITY/OENSITY

OENSITY RATIO, LIQUID OENSITY/OEKSITY

OENSITY, KG/DM3

96.2

L76.95

1.821.

96.5

L76.65

1.871,

96.8

L76.35 1.926

96.9

L76.25

1.91.3

97.1

L76.05 1.978

97.6

175.55 2.068

97.7

L75.1.5 2.086

9696 0.9701

9701 0.9706

1069 1.1075

9721. 9729

110 1

9719

97?i. 1095

9663

96 8 8 1051.

96 6 5 967.. 10 3 8

9773

9778

1157

971.6 9751

1126

9697

9702

1070

9706 9713

1083
CCNTINUEC PRESSED LICUIO OXYGEN

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE,

98.0 .75.15

2.11.2

96.7

L71..1.5 2.276

98.9

L7U.25 2.316

99.0

-17".. IS 2.336

99.1

.71.. 05 2.356

99.5

.73.65

2.1.38

99.7

173.1.5

2.1.79

1. 0ENSITY RATIO, LIQUIO DENSITY/DEN

2. OENSITY RATIO, LIOUIO OENSITY/OEN

3. OENSITY, KG/DM3

6.000 e.ooo io.ooo

9655 0.966O 0.9661.

1656 0.9660 0.9665 0.967O

.017 1.1022 1.1028 1.1033

96 = 5 9660

1023

9637

961.2 1001 1

9576 9582

09 33

9572 9577

9 2 7

9670 9675

1039

9661 9666

1029

9 6 ? 6 961.3 1003

1052 1

9702

9707

1076

10*5

9631. 9640

3999

0.9698 0.9703

1.1071

0.9693

0.9698 1.1066

.033 1.101.

0.9667

0.9672

1.1036

0.9653

0.9658

1.1020
DENSITY OF COMFRESSED LIQUIO

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSIT

2. DENSIT

3. DENSIT

Y RATIO,

Y RATIO,

Y, KG/OM3

LIQUID OENSITY/CENSITY AT A LIQUID DENSITY/OENSITY AT A BOILING

BOILING PRESSURE

PRFSSURE

OF 1 BAR, DIMENSIC

OF 760 TCRR, OIMEN NLESS SIONLESS

BAR 0.800 1.000 2.000 4.000 KP/CM2 0.816 1.020 2.039 4.079

6.000 6.118 8.000

8.158

10.000 10.197 15.000 15.29620.000

20.394

25.000 25.49330.000 30.591

35.000 35.69040.000

40.789

100.0

-173. IS 2.542

0.9557

0.9563 1.0911

0.9562 0.9568

1.0917

0.9567

0.9573 1.0922

0.9572

0.9578

1.0928

0.9585

0.9590

1.0942

0.9597

0.9602 1.0956

0.9609

0.9614 1.0970

0.9621 0.9626

1.0983

0.9633 0.9636

1.0997

0.9644

0.9650

100.1 -173.05

2.564

0.9553

0.9558 1.0906

0.9558 0.9563 1.0911

0.956*3 0.9568 1.0917

8.9568

0.9573 1.0923

0.9580

0.5585 1.0937

0.9592

0.9557

1.0951

0.9604

0.9610 1.0965

0.9616

0.9622 1.0978

0.9628

0.9633 1.0992

0.9640

0.9645 1.1005 100.2 -172.95

2.585 0.9548

0.9553 1.0900

0.9553 0.9558

1.0906 0.9558

0.9563 1.0912

0.9563 0.9568

1.0917 0.9575

0.9581 1.0932

0.9566

0.9593

1.0946

0.9600

0.9605 1.0959

0.9612

0.9617 1.0973 0.96240.9629 1.0987

0.9635

0.9641 1.1000

100.3 -172.85

2.607 0.9543

0.951.9 1.0895

0.9548

0.955<4 1.0901 0.9553

0.9559

1.0906

0.9558

8.9561. 1.0912

0.5571 0.9576

1.0926

0.9583

0.9588

1.0940

0.9595

0.9600 1.0954

0.9607 0.9612

1.0968

0.9615

0.9624

1.0961

0.9631

0.9636 1.0995

100.4 -172.75

2.629

0.9539

0.9544

1.0890

0.954") 0.9549 1.08950.951.9

0.9551. 1.0901

0.9554

0.9559

1.0907

0.9566

0.9571 1.0921

0.9578

0.9564

1.0935

0.9591 0.9596 1.09490.9603

0.9606 1.0963

0.9615

0.9620

1.0976

0.9626 0.9632 1.0990

100.5 -172.65

2.651

0.9534 0.9539

1.0884

0.9539 0.9544 1.08900.9544

0.9549 1.0896

0.9549

0.9551. 1.0901 0.9562

0.5567 1.0916

0.9574

0.9579

1.0930

0.9586

0.9591

1.0944

0.9598

0.9603

1.0958 0.9610

0.5615

1.0971

0.9622

0.9627

1.0985

100.6 -172.55

2.673

0.9529

0.9534

1.0879

0.9534

0.9539

1.0885

0.9539

0.9545

1.0890

0.9544

0.-9550 1.0896

0.9557

0.9562

1.0910

0.9569

0.9S74

1.0925

0.9582

0.9587 1.0939

0.9594

0.9599

1.0952

0.9606

1.0966

0.9617

0.9623

1.0980

100.7 -172.45

2.695

0.9524

0.9530

1.0873

0.9530

0.9535 1.0879

0.9535

0.951.0 1.0885

0.9540

0.951.5 1.0891

0.9552

0.9557 1.0905

0.9565

0.9570

1.0919

0.9577

0.5582 1.0933

0.9589

0.9594 1.0947

0.9601

1.0961

0.9613

0.9616 1.0974

100.8 -172.35

2.717

0.9520

0.9525

1.0868

0.9525

0.9530 1.0874

0.9530 0.9535

1.0880

0.9535

0.951.0 1.0885 0.9548

0.9553

1.0900

0.9560

0.9565 1.0914

0.9572

0.9578

1.0928

0.9585

0.9590 1.0942 0.95970.9602 1.0956

0.9609

0.9614

1.0969

100.9

-172.25

2.740

0.9515

0.9520 1.0863

0.9520 0.9525

1.0866

0.9525

0.9530 1.0874

0.9530 0.9536

1.0880

0.9543

0.9546

1.0895

0.9555

0.9561 1.0909

0.9568

0.9573 1.0923

0.9580 0.9585

1.0937

0.9592

0.5597

1.0951

0.9604

0.9609

1.0964

101.0 -172.15

2.763

0.9510 0.9516 1.08570.9515

0.9521 1.0863 0.95210.9525

1.0869

0.9526

0.9531

1.0875

0.9536 0.9544

1.0889

0.9551 0.9556 1.09030.9563

0.9568

1.0918

0.9575

0.9581

1.0932

0.5588

0.5593

1.0945

D.9600 0.9605

1.0959

101.1 -172.05

2.785

0.9506

0.9511 1.0852 0.95110.9516 1.0858 0.95160.9521 1.0864

0.9521 0.9526

1.0869 0.5534

0.9539 1.0884

0.9546

0.9551

1.0898

0.9559

0.9564

1.0912

0.9571

0.9576

1.0926 0.9583

0.9588

1.0940

0.9595

0.9600

1.0954

101.2 -171.95

2.808

0.9501

0.9506 1.0846

0.9606

0.9511 1.0852 0.95110.9516

1.0858

0.9516

1.9521 1.0864 0.55290.9534

1.0875 0.9542

0.9547. 1.0893

0.9554

0.9559 1.0907

0.9566

0.9572

1.0921

0.9578

0.9584

1.0535

0.9591

0.9596

1.0949

101.3 -171.85

2.831

0.9496

0.9501 0.95010.9506 1.0847 0.95060.9512 1.0853

0.9512

0.9517

1.0859

0.9524 0.9530

1.0673

0.9537

0.9542 1.0866

0.9549

0.9555 1.0902

0.9562

0.9567

1.0916 0.9574

0.9579 1.0530

0.9586

0.9591 1.0944

101.4 -171.75

2.854

0.9491

0.9497 1.0836

0.9497

0.9502

1.081.2 0.9502

0.9507

1.061.7

0.9507

0.9512

1.0853 0.5520

0.9525 1.0866

0.9532

0.9538 1.0«B2

0.9545

0.9550

1.0897

0.9557

0.9562

1.0911 0.9569 0.9575

1.0925

0.9582 0.9587

1.0939

101.5 -171.65

2.878

0.9487

0.9492

1.0830

0.9492

0.91.97 1.0836

0.9497 0.9502

1.0842

0.9502 0.9507

1.0040

0.9515 0.5520 1.06630.9528

0.9533 1.0877

0.9540 0.9545

1.0891

0.9553

0.9558

1.0906

.5565 0.5570

1 .0°20

0.9577 0.958? 1.0933

101.6 -171.55

2.901

0.9482

0.9487

1.0825

0.9487

0.9492 1.0831

0.9492

0.9497 1.0837

0.9497

0.9503

1.0843

0.5510

0.5516 1.0857

0.9523

0.9528 1.0B72

0.9536

0.9541 1.0886

0.9540

0.9553

1.0900

0.9560

0.5566

1.0914

0.9573

0.9578

1.0928

101.7 -171.45

2.925

0.9477

0.9482 1.0819

0.9482

0.91.88 1.0825 0.9468 0.9493

1.0831

0.9493

0.9498

1.0837 0.9506

0.9511 1.0852

0.9518

0.9524 1.0866

0.9531

0.9536

1.0881

0.9543

0.9549

1.0395

0.9556

0.5561 1.0509

0.9568

0.9573 1.0923

101.8 -171.35

2.949

0.9472 0.9478

1.0814

0.9478

0.9483

1.0820

0.9483

0.9488

1.0826

0.9488

0.9493

1.0832

0.5506 1.0847

0.9514

0.9519

1.0861

0.9526

0.9532

1.0876

0.9539

0.9544

1.0390

0.9551 0.9556

1.0904

0.9563

0.9569 1.0918

101.9 -171.25

2.972

0.9468

0.9473 1.0808

0.9473

0.9478 1.0814

0.9478 0.9463

1.0820

0.9483

8.9489 1.0626

0.9496

0.9501 0.95090.9514 1.0856

0.9522

0.9527

1.0870

0.9534

0.9540 1.0885

0.9547

0.9552

1.0899

0.9559

0.9564 1.0913
"OMPPE^SED LIOUIO oxyge*

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO, RATIO,

, KG/DM3 IOUID OENSITY/CEN

IQUID OENSITY/OEN

=ITY AT A SITY AT A BOILING PRESSURE Of BOILING PRESSURE OF

1 BAR,

760 TC DIMENSICNLESS

(R, CIMEKSIONLESS

BAR 0.800 1.000 2.000 I.. 000 KP/CM2 0.616 1.020 2.039 "..079 6.000

6.118

8.000

8.158

10.000 10.197 15.000

15.296 20.00020.394

25.000

25.493

30.000 30.59135.000 35.690

40.000 40.789

102.0 -171.15

2.997

0.91.63

0.91.68 1.0803

0.91.68

0.91.73 1.0809

0.91.73

0.91.79 1.0815

0.9479

0.9464

1.0821

0.9492

0.9497

1.0836

0.9504

0.9510

1.0851

0.9517

0.9522

1.0865

0.9530

0.9535

1.0879

0.9542 0.9547

1.0894

0.9554

0.9560 1.0908

102.1 -171.05

3.021

0.91.58 0.91.63 1.07980.91.63

0.91.6 9 1.0801.

0.91.69

0.91.71. 1.0810

0.9474 0.9479

1.0816

0.9487 0.9492

1.0831

0.9500

0.9505

1.0845

0.9513

0.9518

1.0860

0.9525

0.9530

1.0874

0.9538 0.9543

1.0888

0.9550

0.9555 1.0902

102.2 -170.95

3.01.5

0.91.53 0.91.58 1.07920.91.59 0.9464 1.07980.9461.

0.91.69

1.0801.

0.9469

0.9474

1.0810

0.9482

0.9487 1.0625

0.9495

0.9500

1.0840

0.9508

0.9513

1.0855

0.9521

0.9526 1.0869

0.9533

0.5538 1.0883

0.9545

0.9551 1.0897

102.3 -170.65

3.070

0.91. ".6 0.91.51. 1.0787

0.91.51. 0.91.59 1.0793

0.91.59

0.91.61. 1.0799

0.9464

B.9470

1.0805

0.9478

0.9483

1.0820

0.9490 0.9496

1.0835

0.9503

0.9508

0.9516

0.9521 0.9528 0.9534

1.0878

0.9541

0.9546 1.0892

102.'. -170.75

3.09".

0.91.1.1. 0.91.1.9 1.0781

0.9<t 1.9 0.91.51. 1.07870.945*

0.946O

1.0793

0.9460

0.9465

1.0799

0.9473

0.9478

1.0814

0.9486

0.9491 1.0829

0.9499

0.9504

1.0844

0.9511 0.9517

1.0858

0.9524

0.5529 1.0873

0.9536 0.9542

1.0687

102.5 -170.65

3.119

0.91.39

0.91.1.1. 1.0776

0.91.1.1. 0.91.1.9 1.0782

0.91.50

0.91.55 1.0788

0.9455

0.9460

1.0794

0.9466 0.9473

1.0809

0.9486

1.0824

0.9494 0.9499

1.0839

0.9507 0.9512

1.0853

0.9519

0.9525

0.9532

0.9537

1.0882

102.6 -170.55

3.11.1.

0.91.31. 0.91.39 1.07700.91.39

0.91.1.5 1.0776

0.91.1.5 .91.50 1.0783

0.9455 1.0789

0.9463

0.9465 1.0804

0.9476

0.9482

1.0619

0.9469

0.9495 1.0633

0.9502

0.9507

1.0S48

0.9515

0.9520 1.0e62

0.9527

0.9532

1.0877

102.7

-170.1.5 3.169

0.9.1.29

0.91.31. 1.0765

0.91.35

0.91.1.0 1.0771

0.91.1.0

0.91.1.5 1.0777

0.9445

0.9451

1.0783 0.94591.0798

0.9472

0.9477 1.0B13

0.9485

0.9490 1.0828

0.9498

0.9503

1.0943

0.9510

0.9515 1.0857

0.9523

0.9528 1.0871

102.8 -170.35

3.191.

0.91.25

0.91.30 1.0759

0.91.30

0.91.35 1.0765

0.91.35

0.91.1.0 1.07720.9446

1.0778

0.5454

0.9459 1.0793

0.9467 0.9472

1.0808

0.9480 0.9485 1.0823

0.9493

0.9498 1.0337 0.95060.9511

1.0852

0.9518

0.9523

1.0866

102.9 -170.25

3.219

0.91.25 1.0751.

0.91.25

0.91.30 1.0760

0.91.31

0.91.36 1.0766

0.9436

0.9441

1.0772

0.9445 0.9454

1.C786

0.9462

0.9468 1.0803

0.9475

0.9481 1.0817

0.9488

0.9493 1.0832

0.9501

0.9506

1.0847

0.9514

0.9519

1.0861

103.0 -170.15

3.21.5

0.91.15

0.91.20

1.071.8

0.91.20

0.91.25 1.0755

0.91.26

0.91.31 1.0761

0.9431

0.9436

1.0767 0.9446

0.5450

1.0782

0.9458 0.9463

1.0797

0.9471 0.9476

1.0812

0.9484

0.9489

1.0827

0.6496

0.9502

1.0841

0.9509 0.9514

1.0856

103.1 -170.05

3.271 0.9MO

0.91.15 1.071.3

0. 91.16 0.91.21

1.071.9

0.91.21

0.91.26 1.0755

0.9426

0.9432

1.0761

0.5440

0.9445

1. 0777

0.9453

0.9458

1.0792

0.9466

0.9471

1.0807

0.9479

0.9484

1.0822

0.9492

0.9497

1.0836

0.9504

0.9510 1.0851

103.2 -169.95

3.296

0.9U05

0.91.10 1.0737

0.91.11 0.9416

1.071.1.

0. 91.16 0.91.21 1.0750

0.9422

0.9427

1.0756

0.5435

1.0771

0.9448

0.9453

1.0766

0.9461 1.08010.947*

0.9480 1.0816

0.9487

0.9492

1.0831

0.9500

0.9505 1.0845

103.3 -169.85

3.322

0.91.00 1.0732

0.91.06 0.91.11 1.07380.91.11 0.91.17 1.074*0.9417

0.9422 1.0751

0.9430

0.5435

1.0766

0.9444 0.9449

1.0781

0.9457 0.9462

1.0796

0.9470

0.9475

1.0811

0.9483

0.9488

1.0826

0.9495 0.9501

1.0840

103.1. -169.75

3.31.8

0.9396

0.91.01 1.0726

0.91.01 0.91.06 1.0733

0.9407

0.9412 1.0739

0.9412

0.9417

1.0745 0.5431 1.0760

0.9439 0.9444

1.0776

0.9452 0.9457

1.0791

0.9465

0.9470

1.0806

0.9478

0.9483

1.0820

0.9491

0.9496 1.0835

103.5 -169.65

3.3 75

0.9391

0.9396

1.0721

0.9396

0.91.01 1.0727 0.9402

0.9407

1.0733

0.9407

0.9412

1.0740

0.9421

0.'9426 1.0755

0.9434

0.9439

1.0770 0.9447

0.9453

1.0785

0.9466

1.08O0

0.9473

0.9479

1.0815

0.9486

0.9491

1.0830

103.6 -169.55

3.1.01

0.9386

0.9391

1.0715

0.9391 0.9397

1.0722

0.9397

0.9402

1.0728

0.9402

0.9408 1.0734

0.5416 1.0750

0.9429

0.9435 1.0765

0.9448

1.0780

0.9456

0.9461 1.0795 1.0810

0.9482

0.9487

1.0824

103.7

-169.1.5

3.1.28

0.9381

0.9386

1.0710

0.9387

0.9392

1.0716

0.9392 0.9397

1.0722

0.9398 0.9403

1.0729

0.9411 l!o7440.9425

0.9430

1.0760

0.9438 0.9443

1.0775

0.9451

0.9456

1.0790

.9464 0.9469

1.0805

0.9477

0.9482 1.0619

103.8 -169.35

3.1.51.

0.9376

0.9381

1.0701.

0.9382 0.9387

1.0711

0.9387

0.9392

1.0717

0.9393

0.9398

1.0723

0.9407

1.0739

0.9420 0.9425

1.0754

0.9433

0.9439

1.0769

0.9447

0.9452

1.0784

0.9460

0.9465

1.0799

0.9472

0.9478 1.0814

103.9 -169.25

3.1.81

0.9371 0.9376 1.0699

0.9377

0.9382 1.0705 0.9382

0.9388

1.0711

0.9388

0.5393

1.0718

0.940?

0.9407 1.0733

0.9415

0.9420 1.0749

0.9429 0.9434

1.0764

0.9442 0.9447

1.0779

0.9455

0.9460

1.0794

0.9468

0.9473
DENSITY OF COMPRESSEO LIOUIC

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. OENSITY

3. DENSITY

RATIO,

RATIO,

, KG/OK3

-IQUIO OENSITY/DENSITY AT A LIQUID OENSITY/DENSITY AT A BOILING

SOILING PRESSURE

PRESSURE

OF 1 BAR,

OF 760 TC DIMENSICNLESS

*R, CIWENSICNLFSS

BAR 0.800 LOGO 2.000 "..000 KP/CM 2 0.816 1.020 2.039 It. 079 6.000

6.118

8.000 8.15810.000

10.197 15.000

15.296 20.000

20.39*

25.000 25.*9330.000

30.591 35.00035.690

*0.000

*0.789

10*. -169.15

3.508

0.9366

0.9372 1.0693

0.9372

0.9377 1.0699 0.937S0.9383

1.0706

0.9383

8.9388

1.0712

0.9397 0.9*02

1. 072e

0.9*11

0.9*16

1.07*3

0.9*2*

0.9*29 1.0759

0.9*37

0.9**2 1.077* 0.9*50 0.9*55

1.0789

0.9*63 0.9*68 1.080*

10<t.l -169.05

3.536

0.9362 0.9367 1.0687

0.9367

0.9372

1.069* 0.9373

0.9378 1.0700

0.9378

0.938* 1.8707 0-9392

0.9397

1.0722

0.9*06

0.9*11

1.0738

0.9*19

0.9*2* 1.0753

0.9*33

0.9*38 1.0768 0.9**6

0.9*51

1.0763

0.9*59

0.9*6* 1.0798

10",.

-168.95

3.563

0.9357

0.9362 1.0682

0.9362 0.9367 1.06880.9368

0.9373 1.0695

TJ.937* 0.9379

1.0701

0.9387 0.9393

1.0717

0.9*01 0.9*06

1.0733

0.9*15

0.9*20 1.07*8

0.9*28

0.9*33 1.0763

0.9**1 0.9**6

1.0778

0.9*5*

0.9*59

1.0793

10*. 3 -168.85

3.590 0.9352

0.9357 1.0676

0.9358 0.9363 1.0683 0.9363

0.9368

1.0669

0.9369

B.937*

1.0696

0.9383 0.9386

1.0711

0.9396

0.9*01 1.0727

0.9*10

0.9*15

1.07*3

0.9*23

0.9*28

1.0758

0.9*36 0.9**2

1.0773

0.9**9

0.9*55 1.0788

10*.* -168.75

3.618

0.93*7

0.9352

1.0671

0.9353

0.9358

1.0677 0.9358

0.9363

1.068*

0.936* 0.9369 1.06900.9376 0.9383

1. 0706 0.9352

0.9397

1.0722

0.9*05

0.9*10

1.0737

0.9*19 0.9*2*

1.0752

0.9*32 0.9*37 1.0766

0.9**5

0.9*50

1.0783

104.5 -168.65

3.6*6

0.93*2 0.93*7

1.0665

0.93*8 0.9353 1.06720.9353

0.9359 1.0678

0.9359

0.936*

1.0685

0.9373 1.07010.93e7

0.9392

1.0716

0.9*00 0.9*06

1.0732

0.9*1*

0.9*19

1.07*7

0.9*27

0.9*32 1.0762

0.9**0 0.9**5

1.0777

10*. 6 -168.55

3.67*

0.9337

0.93*2 1.0660

0.93*3

0.93*8

1.0666 0.93*9

0.935* 1.0673

8.935*

0.9359

1.8679

0.9368 0.9373

1.0695

0.9382

0.9387

1.0711

0.9396

0.9*01

1.0726

0.9*09

0.9*1* 1.07*2 0.9*220.9*26

1.0757

0.9*36

0.9**1

1.0772

10*.

-168. *5 3.702

0.9332 0.9337

1.065*

0.9338

0.93*3 1.0661

0.93**

0.93*9 1.0667

0.93*9

0.935*

1.067*

0.5363

1.0690

0.9377

0.9382

1.0705

0.9391

0.9396

1.0721

0.9*0*

0.9*10

1.0736

0.9*18 0.9*23

1.0752

0.9*31

0.9*36 1.0767

10*. 8 -168.35

3.730

0.9327

0.9332

1.06*8

0.9333

0.9338 1.0655

0.9339 0.93**

1.0662

TJ.53*5 0.9350

1.0668 0.5359

0.536* 1.068*

0.9372

0.9378

1.0700

0.9386 1.07160.9*00

0.9*05

1.0731

0.9*13

0.9*16

1.07*6

0.9*26

0.9*32

1.0761

10*.

-168.25

3.759

0.9322

0.9328 1.06*3

0.9328

0.9333 1.06*9 0.933*0.9339 1.0656

(.93*0 0.93*5

1.0662

0.935*

0.9355

1.C675

0.9368 0.9373

1.069*

0.5361 0.53870.9395

0.9*00 1.0726

0.9*06 0.9*1*

1. 07*1

0.9*22

0.9*27

1.0756

105.0 -168.15

3.787

0.9318 0.9323

1.0637

0.9323

0.9326 1.06**

0.9329 0.933*

1.0650

0.9335 l!o6E70.53*5 0.935*

1.0673

0.9363

0.9368

1.0689

0.9377

0.9382

1.07115

0.9390 0.9395

1.0720

0.9*0* 1.0736

0.9*17

0.9*22

1.0751

105.1 -168.05

3.816

0.9313

0.9318 1.0632

0.9318

0.932*

1.0638 0.932*

0.9329

1.06*5

11.9330 0.9335

1.0651 0.53**

0.53*9

1.0666

0.9358

0.9363 0.93720.9377

1.0699

0.9386

0.9391 1.0715 1.0730

0.9*12

0.9*18 1.07*6

105.2 -167.95

3.8*5

0.9308

0.9313 0.931*0.9319

1.0633

0.9319

0.932*

1.0639

0.9325 0.93300.5339

0.93**

0.9353

0.9358 1.0678

0.9367

0.9372

1.069*

0.9381 0.9386

1.0*10

0.939* 1.07250.9*08

0.9*13

1.07*0

105.3 -167.85

3.87*

0.9303

0.9308

1.0620

0.9309 0.931* 1.06270.931*

0.9320 1.063*

0.9320 0.9325

1.06*0

0.933* 0.93*0

1.0657

0.93*9 0.935*

1.0673

0.9362

0.9366 1.0668

0.9376

0.9381 1.070*

0.5390 0.9395

1.0720

0.9*03 1.0735

105.* -167.75

3.903

0.9298

0.9303 1.0615

0.930* 0.9309

1.0621

0.9310 0.9315

1.0628

0.9315

0.9320

1.8635

0.5330 0.9335

1.0651

0.93** 0.93*9

1.0667

0.9358 0.9363

1.0683

0.9372 0.9377

1.0699

0.9385

0.9390

1.071*

0.5399

0.9*0* 1.0730

105.5 -167.65

3.933

0.9293

0.9298 1.0609

0.9299

0.930* 1.0616

0.9305

0.9310

1.0622

0.9310

0.9316

1.0629

0.5326 0.9330

1.06*5

0.9339

0.93**

1.0662

0.9353

0.9358

1.0678

0.9367

0.9372 1.0693

0.5380

0.9386

1.0709

0.939* 0.9399

1.072*

105.6 -167.55

3.962

0.9288

0.9293 1.0603

0.929*

0.9299

1.0610

0.9300

0.9305

1.0617

0.9306

8.9311

1.0623 0.5320

0.9325

1.06*0

0.933*

0.9339 1.0656

0.93*8

0.9353

1.0672

0.9362

0.9367

0.9376 0.5381

1.070*

0.9369

0.939*

1.0719

105.7

-167. *5 3.992

0.9263

0.9288 1.0598

0.9289

0.929* 1.0605 0.9295

0.9300

1.0611

0.9301

0.9306

1.0618

0.9316 0.9320

1.063*

0.9329 0.933*

1.0651

0.93*3 0.93*9

1.0667

0.9357

0.9362 1.0683

.9371 0.9376

1.0696

0.9385

0.9390

1.071*

105.8 -167.35

*.022

0.928*

0.9289 1.0599

0.9290

0.9295

1.9296 0.9301

1.0612

0.5310 0.9315

1.0629

0.9325

0.9330

1.06*5

0.9339 0.93**

1.0661

0.9353

0.9358

1.0677

0.9366

0.9371

1.0693

0.9380

0.9385 1.0706

105.9 -167.25

*.052

0.9279

0.928*

1.0593

0.92e5

0.9290 1.0600

0.9291 0.9296 1.0607 0.5305

0.5310

1.0623

0.9320

0.9325

1.06*0

0.933* 1.06560.93*8

0.9353

1.0672

0.9362

0.9367

1.0686

0.9375

0.9380

1.070?
TAeiE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUIO OENSITY/OENSITY AT A 2. OENSITY RATIO, LIQUID DENSITY/DENSITY AT A 3. OENSITY, KG/OM3 90ILING BOILINGPRESSURE

PRESSURE

OP 1 BAR, OIMEKSICNLESS

OF 760 TORR, OIMEKSIONLFSS

BAR 0.800 1.000 2.000 <• . 6.000 KP/CM 2 0.816 1.020 2.039 "..079 6.1188.008 10.000

10.197 15.00015.296 20.000

20.391. 25.00025.1.93 30.000

30.591 35.000 35.690

1.0.000 1.0.789

106.0 -167.15

11.082

0.927". 0.9279 1.0588 0.9280

0.9285

1.0591,

0.9286

0.9291

1.0601

0.5300

0.9306

1.0618

0.9315

0.9320

1.063l| 0.9329

0.9331. 1.0650

0.931,3 1.06660.9357

0.9362 1.0682

0.9371

0.9376

1.0698

106.1 -167.05

it. 113

0.9269

0.9271. 1.0582

0.9275

0.9280

1.0589

0.9281 0.9286

1.0595

0.5296

0.9301

1.0612

0.9310

0.9315

1.0629

0.9321. 0.9329

1.0645

0.9338 0.9343

1.0661

0.9352

0.9357

1.0677

0.9366

0.9371 1.0692

106.2 -166.95

<..11.3

0.9261. 0.9269 1.0576 0.9270

0.9275

1.0583

1.9276

0.9281

1.0590 0.5291 0.52961.0607

0.9305

0.9310 1.0623 0.93190.9325

1.0639

0.9331. 0.9J39 1.0655

0.931,8 0.9353

1.0671

0.9361 0.9366 1.0687

106.3 -166.85

I..171. 0.9259

0.9261. 1.0571

0.9265 0.9270

1.057T

0.5271 0.9276

1.058lt 0.5286

0.5291

0.9300 0.9305

1.0618

0.9315

0.9320

1.0631,

0.9329

0.9331i 1.0650

0.931.3 0.931.8 1.0666

0.9357

0.9362

1.0682

106.1. -166.75

"..205

0.9251. 0.9259

1.0565

0.9260

0.9265

1.0572

0.9266 0.9271

1.0579 0.5281

0.9286 1.0595

0.9296

0.9301 1.0612

0.9310

0.9315

0.9321. 0.9329

1.061.5

0.9338

0.931.3 1.0661

0.9352

0.9357

1.0676

106.5 -166.65

"..236

0.921.9

0.9251. 1.0559

0.9255

0.926O 1.0566

0.9261 0.9266

1.0573 0.5276

0.5281 1.0590

0.9291

0.9296

1.0607

0.9305

0.9310 1.0623

0.9319

0.9321. 1.0639

0.9333

0.9338

1.0655

0.931.7 0.9352

1.0671

106.6 -166.55

«l.Z67

0.92 111. 0.921.9

1.0551.

0.9250

0.9255

1 .0560

0.9256

0.9261

1.0567

0.5271

0.5276

1.0581.

0.9286

0.9291

1.0601

0.9300 0.9305

1.0617

0.9315

0.9320

1.0631. 0.5329

0.9331. 1.0650

0.931,2

0.931.8 1.0666

106.7

-166.1.5

It. 299

0.9239

0.921.1. 1.0548

0.921,5 0.9250 1.05558.9251

0.9256

1.0562

0.5266

0.5271

1.0575

0.9281 0.9266

1.0595

0.9295

0.9301

1.0612

0.9310 0.9315

1.0628

0.9321. 0.9329

1.061.1.

0.9338

0.931.3 1.0660

106.8 -166.35

It. 330

0.9231. 0.9239

1.051.2

0.921.0

0.921,5

1.051.9 0*9251 1.0556 0.5261 1.057?

0.9276

0.9281 1.0590

0.9291 0.9296

1.0606

0.9305 0.9310

1.0623

0.5315

0.9321. 1.0635

0.9333

0.9338 1.0655

106.9 -166.25

It. 362

0.9229

0.9231. 1.0536

0.9235

0.921.0

1.051.3

0.92ltl 0.92li7 1.0550

0.5256

0.5262 1.0567

0.9271

0.9276

1.0581.

0.9286

0.9291 1.0601

0.9300

0.93O5

1.0617

0.9311. 0.5319

1.0631.

0.9328

0.9333 1.0650

107.0 -166.15

1..39I.

0.9221, 0.9229

1.0531

0.923O

0.9235

1.0538

0.9237

0.921.2

1.051.5

0.9252

0.5257 1.0562

0.9266

0.9271 1.0579 0.9296

1.0595

0.9295

0.9300 1.0612

0.9310 0.9315

1.0628

0.9321. 0.9329

1.061.1.

107.1 -166.05

"t.lt26

0.9219

0.9221. 1.0525 0.9225

0.9230 1.0532

0.9232 0.9237

1.0539

0.921.7 0.5252

1.0556

0.9261 0.9267

1.0573 0.9276

0.9281

1.0590

0.9291 0.9296

1.0606 0.9305

0.9310 1.0623

0.9319

0.9321. 1.0639

107.2 -165.95

<i.l|58

0.9211. 0.9219

1.0519

0.9220 0.9225

1.0526

t.9227

0.9232 1.0533

0.521.2

0.921.7 1.0551

0.9257

0.9262 1.0568

0.9271

0.9276

1.0581.

0.9286

0.9291 1.0601

0.9300

0.9305

1.0617

0.9311. 0.9319

1.0633

107.3 -165.85

'..'191

0.9209

0.9211.

1.0511. 0.9215

0.9220 1.0521

0.5222

0.9227 1.0528

0.5237

0.521.2 1.051.5

0.9252

0.9257 1.0562

0.9266

0.9271 1.0579

0.9281 0.9286

1.0595

0.5295

0.9300 1.0612

0.9310

0.9315

1.0628

107.". -165.75

I.. 523

0.9201. 0.9209

1.0508 0.9210

0.9215

1.0515

0.9217

0.9222

1.0522

0.5232 0.5237

1.0535

0.921.7 0.9252

1.0556

0.9262 0.9267

1.0573

0.9276 0.9281

1.0590 0.5291

0.9296 1.0606

0.9305

0.9310 1.0623

107.5 -165.65

I.. 556

0.9199

0.9201. 1.0502

0.9205

0.9210

1.0509

0.9212

0.9217

1.0516

0.5227

0.5232

1.0531.

0.921.2

0.921.7 1.0551

0.9257

0.9262 1.0568

0.9271 0.9276

1.0581.

0.9286

0.9291

1.0601

0.9300

0.9305 1.0617

107.6 -165.55

..589

0.9191. 0.9199

1.01,96

0.9200 0.9205 1.05030.9207

0.9212

1.0511

0.5222

0.5227

1.0528

0.9237

0.921.2

1.051.5

0.9252 0.9257

1.0562

0.9267

0.9272 1.0579

0.5281 0.5286

1.0595

0.9295

0.9300

1.0612

107.7

-165.1.5

1..622 0.9189

0.9191. 1.01,91 0.91950.9200

1.01.98

0.9202 0.9207

1.0505

0.5217 0.5222

1.0522

0.9232

0.9237

1.051.0

0.921.7 0.9252

1.0557

0.9262

0.9267

1.0573 0.9276

0.5281

1.0590

0.9291

0.9296

1.0606

107.8 -165.35

I.. 655

0.9181, 0.9189

1.01.85 0.9190

0.9195

1.01t92

0.9197

8.9202

1.01.99

0.5212

0.5217

1. 0517

0.9227

0.9232

1.05311

0.921.2 0.921.7 1.05510.9257

0.9262

1.0568

0.9271 0.9277 1.05850.9286

0.9291

107.9 -165.25

4. 689 0.9179

1*01.79 0.9185

0.5190

I.OI186 0.9192

0.9197

1.01.93

0.9207

0.5212

1.0511

0.9222

0.9227 1.0528

0.9237

0.921.2

1.051,6

0.9252

0.9257

1.0562 0.9267

0.9272

1.0575

0.9281

0.9286 1.0598
OF COMPRESSED LIQUID OXYGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO,

2. DENSITY RATIO,

3. DENSITY, KG/DM3 LIQUIO OENSITY/CEN

LIQUID DENSITY/OEN

SITY AT A SITY AT A BCILING EOILING

PRESSURE

PRESSURE

OE 1 BAR, DIMENSIC

Of 760 TCRR, CIMEN NLESS SIONLESS

BAR 0.800 1.000 2.000 "..€00 6.000 KP/CM? 0.616 1.020 2.039 1..079 6.118

8. 001 8.158 I0.0OD

10'. 197 15.000

15.296

20.000

20.391. 25.00025.1.93 30.000 30.591

35.000

35.690

1(0.000 1(0.789

108.0 -165.15

1.. 723

0.9171. 0.9179

1.01.73 o.°ieo

0.9165

1.01,80

11.9187 0.9192

1.01.88 0.9202

0.9207 1.0505

0.9217

0.9222

1.0523

0.9232

0.9237

1.051.0

0.921.7 0.9252

1.0557

0.9262 0.9267

1.0571.

0.9276

0.9281 1.0590

108.1 -165.05

14.756

0.9169

0.9171.

1.01.67 0.9175

0.9180

1.01.75

0.9182

0.9187

1.01.82 0.5197

0.9202

1.0500

0.9212

0.9217

1.0517

0.9227

0.9233

1.0531.

0.921,2

0.921.7 1.0551 0.9257

0.9262

1.0566

0.9272

0.9277 1.0585

108.2

-161.. 95 ..790

0.9161. 0.9169

1.01462 0.9170

0.9175

1.01.69

0.9176

0.9181

1.01.76 0^5192

0.9197

1. 01.91.

0.9207

0.9212

1.0511

0.9223

0.9228 1.0529

0.9238

0.921.3

1.051.6 0.9252

0.9257

1.0563

0.9267

0.9272 1.0579

108.3

-16",. 85 •.825

0.9159

0.91614 1.01.56 0.91650.917O

1.0463

0.9171 0.9176

1.01.70

0.9187

0.9192

1.01.86

0.9202

0.9208

1.0506

0.9218 0.9223 1.05230.9233

0.9238

1.051.0

0.921.7 0.9252 1.0557

0.9262

0.9267

1.0571(

106.*

-iei..75

it. 859

0.9151. 0.9159

1.01.50 0.9160 0.91651.01.57

0.9166

0.9171

1.01.65 0.5182

0.5187

1.01.83

0.9198

0.9203

1.0500

0.9213

0.9218 1.0518

0.9228

0.9233 1.0535

0.921.3

0.921.8 1.0552

0.9257

0.9262

1.0S68

108.5

-16<i.65

1..891,

0.911.9

0.9151.

I.O1.I4I4 0.9155

0.9160

1. 01.52

0.9161 0.9166

1.01.59 0.9177

0.9182

1.01.77 0.9193

0.9196 1.0*95

0.9208

0.9213

1.0512

0.9223

0.9228 1.0529

0.9238

0.921.3

1.051.6

0.9252

0.9258

1.0563

108.6

-161.. 55

fc.926

0.91143

0.911.8

1.01.36 0.9150

0.9155

1.01.1.6

0.9156 0.9161

1.01.53 0.5172

0.9177

1.01.71

0.9168

0.9193

1.01.89

0.9203

0.9208 1.0506

0.9218

0.9223

1.0521.

0.9233

0.9238

1.051.1

0.921.8 0.9253 1.0557

108.7

-16ii.ii5 4.963

0.9138

0.911.3

1.01.33

0.911.5 0.9150

1.01.1.0

0.9151

0.9156

1.01.1.7 0.9167

0.9172

1.01.65

0.9183

0.9168

1.01.63

0.9198

0.9203

1.0501

0.9213

0.9218

1.0518

0.922e

0.9233

1.0535

0.921.3

0.92l.e 1.055?

108.8

-161.. 35

it. 998

0.9133

0.9138

1.01.27

0.911.0 0.9H.5

1. 01.31.

«. 911.6 0.9151

1.01.1.2 0.9162

0.5167

1.01.60

0.9178

0.9183

1.01.76 0.9193

0.9198

1.01.95

0.9206 0.9213 1.05120.9223

0.9228 1.0530

0.9238

0.921.3 1.051.6

108.9

-161.. 25

5.031.

0.9128

0.9133

1.01.21 0.9135

0.911.0

1.01.28

0.911.1

0.911.6

1.01.36

0.5157

0.5162

1.01.51.

0.9173

0.9178

1.01.72

0.9188 0.9193

1.01.90

0.9203

0.9208 1.0507

0.9218

0.9221.

1.0521.

0.9233

0.9238

1.051.1

109.0

-161.. 15 5.069

0.9123

0.9128

1.01.15

0.9130

0.9135

1.01.23

0.9136

0.911.1 1.01.30

0.5152

0.5157

0.9168

0.9173

1.01.66

0.9183

0.9168

1.01.61.

0.9199

0.9201. 1.05O1

0.9211. 0.5215 1.0519

0.9229

0.9231. 1.0536

109.1

-161.. 05 5.105

0.9118 0.9123

1.01.09

0.9121. 0.9129

1.01.17

0.9131

0.9136

1.01.21.

0.511.7 0.5152

1.01.1.2 0.9163

0.9168

1.01.60

0.9176

0.9183

1.01.78

0.9191, 0.9199

1.01(96 0.9209

0.9211. 1.0513

0.9221. 0.9229 1.0530

109.2 -163.95

5.11.1

0.9113

0.9118

1.01403 0.9119

0.9121. 1.01.11

0.9126

0.9131

1.01.18

0.511.2

0.511.7

1.01.37

0.9158

0.9163

1.01.55

0.9173

0.9176

1. 01.73

0.9169

0.919l(

1.01.90

0.9201. 0.9209 1.0507

0.9219

0.9221. 1.0525

109.3 -163.85

5.177

0.9106 0.9113

1.0396

0.9111. 0.9119

1.01.05

0.9121

0.9126

1.01.12 0.5137

0.511.2

1.01.31 0.9153

0.9158

0.9168 0.9173

1.01.67

0.916l( 0.9189

1.01(85 0.9199

0.5201. 1.0502

0.9211. 0.9219 1.0519

109.1. -163.75

5.213

0.9102 0.9107

1.0392 0.9109

0.9111. 1.0399

0.9116 0.9121

1.01.07 0.5132

0.9137

1.01.25

0.911.8 0.9153

1.01.1(3 0.9163

0.9168

1.01.61

0.9179

0.918l(

1.01.79

0.9191. 0.9199

1.01.96 0.9209

0.92H.

1.0511.

109.5 -163.65

5.21.9 0.9097

0.9102 1.0386

0.9101. 0.9109 1.03930.9111 0.9115

l.fll.01

0.9127

0.5132

1.01.19

0.911.3

0.911.8 0.91590.9161.

1.01.56

0.9171. 0.9179

1.01.73 0.5189

1.01.91

0.9201. 0.9209 1.0508

109.6 -163.55

5.286

0.9092

0.9097 0.9099

0.9101. 1.0387

0.9105

0.9110

1.0395

0.9122

0.9127

1. 01.11.

0.9138

0.911.3

1.01.32

0.91514 0.9159

1.01.50

0.9169

0.9171.

1.01.66 0.51851.01.85

0.9200

0.9205 1.0503

109.7

-163.1.5 5.323

0.9087

0.9092

1.037*4 0.909*

0.9099

1.0382

0.9100

0.9105

1.0389

0.9117

0.5122

1. 01.08

0.9133

0.9138

1.01.26

0.911.9

0.9151.

1.01.1.1.

0.9161. 0.9169

1.01,62

0.9180 0.9185

1.01.80

0.9195

0.9200

1.01.97

109.8 -163.35

5.359

0.9062

0.9087 1.0368

0.9088 0.9093

1.0376

0.9095

0.9100 1.0363

0.9112 0.5117

1.01.02

0.9128

0.9133

1.01.20

0.911.11 0.911.9

1.01.39

0.9159

0.9161.

1.01.56

0.9175 0.5180

1.01.71.

0.9190

0.9195

1.01.92

109.9 -163.25

5.397

0.90 77 1.0362 1.03700.9090

0.9095

1.0377

0.9106

0.9111

1.0396

0.9123

0.9128

1.01.15

0.9139

0.91<<l. 1.01.33

0.9151. 0.9159

1.01.51

0.9170 0.9175

0.9185

0.9190

1.01.86
OENSITY OF COMPRESSED LICUIO OXYGEN - COM

TABLE EN TRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUID OENSI

2. OENSITY RATIO, LIQUID OENSI

3. OENSITY, KG/DM3

TY/OENSIT

TY/OENSIT

Y AT A BOILING PRESSURE

BOILING PRFSSU9E C

- 1 BAR,

" 760 Tf OIMENSIC

R, CIMEN

NLESS SICNLESS

BAR 0.800 1.000 2.000 "..000 6.000 KP/CM2 0.816 1.020 2.039 4.079 6.118 8.000 1 e.158 i 0.000 1 0.197 1 5.000

5.296 20.394 25.000

25.493

30.000

30.591 35.000

35.690

40.000

40.789

110.0 -163.15

5.434

0.9071

0.9076 1.0356

0.9078 e 0.5083 t 1.0364 1

.9085

.9090

.0372 1 .9106 .0390

0.9118

0.9123 1.0409

0.9134 0.9139

1.0427

0.9149

0.9154

1.0445

0.9165

0.9170

1.0463

0.9180

0.9185

1.0480

110.1 -163.05

5. (.71

0.9066

0.9071 1.0350

0.9073 0.9078 e 1.0358 1

.9080 C .9065

.0366 .9096

.9101 .0385

0.9113

0.9118 1.0403

0.9129

0.9134

1.0422

0.9144 0.9149

1.0440

0.9160

0.9165

1 .0457

0.9175 0.9180

1.0475

110.2 -162.95

5.509

0.9061

0.9066

1 .031.1. 0.9068 I 0.9073 [ 1.0352 ]

.9075 t .9080 C .0360 .9091

.9096 .037?

0.9108

0.9113

1.0397

0.9129

0.9140 0.9144

1.0434

0.9155

0.9160

1.0452

0.9171

0.9176 1.0469

110.3 -162.85

5.547

0.9056

0.9061

1.0338

0.9063

0.9068 I 1.0346 1

.9069 .9074 C .0354.9086

.9091 .0373

0.9*02 0.9107

1.0392

0.9119 0.9124

1.0410

0.9135

0.9140

1.0428

0.9150 0.9155

1.0446

0.9166

0.9171 1.0464

110. "4 -162,75

5.585

0.9051

0.9056 1.0332 0.9057 1 0.9062 t 1.0340

.9064 t .9069 C .0348 1

.9081

.9086 .0367

0.9097

0.9102 1.0386

0.9114

0.9119

1.0404

0.9130 0.9135

1.0423

0.9145

0.9150

1.0441

0.9161

0.9166

1.0458

110.5 -162.65

5.623

0.901.5 0.9050 1.03260.9052

0.9057 1.0334

.9059 .9064 .0342.9076

.9081 .0361

0.9092

0.9097

1.0380

0.9109

0.9114

1.0399

0.9125

0.9130

1.0417

0.9140

0.9145

1.0435

0.9156

0.9161 1.0453

110.6 -162.55

5.662

0.9040 0.9045

1.0321

0.9047 0.9052

1.0328

.9054

«6 59 .0336

.9071 .9076

.0355

0.9O87

l!o374

0.9104

0.9109 1.0393

0.9120

0.9125 1.0411

0.9135

0.9140 1.0425

0.9151

0.9156 1.0447

110.7

-162.1.5 5.700

0.9035 0.9040

1.0315

0.9042

0.9047

1.0322

.9049

.0330 .9071 .0350

0.9082 0.9087

1.0368

0.9099

0.9104

1.0387

0.9115

0.9120 1.0406

0.9131 0.9136

1.0424

0.9146

0.9151 1.0442

110.8 -162.35

5.739

0.9030

0.9035

1.0309 0.9037 0.90421.0316

.9043

.0324

.5060 .9065 .0344

0.9077

0.9082 1.0363

0.9094

0.9098

1.0381

0.9110 0.9115

1.0400

0.9126

0.9131

1.0418

0.9141 1.0436

110.9 -162.25

5.778

0.9024

0.9029

1.0303

0.9031

0.9036 1 1.0310

.9038

.9043 .0318

.5055 .5060

.0338

0.9072

0.9O77

1.0357

0.5088

0.9093

1.0376

0.9105

0.9110 1.0394

0.9121 0.9126

1.0412

0.9136

0.9141

1.0430

111.0 -162.15

5.818

0.9019

0.9024

1.0297 0.9026

0.9031

1.0305

.9033 .9038 .5050 .9055

. 0332

0.90F7 0.9072

1.0351

0.9083

0.9088

1.0370

0.9100

0.9105

1.0388

0.9116 0.9121

1 .0407

0.9131 0.9136

1.0425

-162.05

5.857

0.9014 0.9019

1.0291

0.90 21 0.9026 1.0299

.9028 .9033

.0306

.5045

.5050

• C326

0.9O62 0.9067

1.0345

0.9078

0.9093

1.0364

0.9095

0.9100 1.0383

0.9116

1.0401

0.9127

0.9132

1.0419

111.2 -161.95

5.897

0.90 9 0.9014 1.0285

0.9016

0.9021 1.0293

.9023 .9028

.0300 .5040.0320

0.9057 0.9062

1.0339

0.9073

0.9078

1.0358

0.9090 0.9095

1.0377

0.5106

0.9111

1.0395

0.9122

0.9127

111.3 -161.85

5.936

0.9003 0.9008

1.0279 0.9010

0.9015 1.0287

.9017 .9022

.0295 .9035

.5040 .0314

0.9O52

0.9057

1.0334

0.9068

0.9073

1.0353

0.9065

0.9090

1.0371

0.91O1

1.0390

0.9117 0.9122 1.0408

lll.lt -161.75

5.976

0.8998

0.9003

1.0272

0.9005

0.9010 1.0281

.5012 .9017

.0289

.5029 .5034

.0308

0.9O46

0.9051 1.0328

0.9063

0.9068 1.0347

0.9080

0.9085

1.0366

0.6096

0.9101

1.0384

0.9112 0.9117

1.0402

111.5 -161.65

6.017

0.9000

0.9005 1.0275

.9007

.9012

.0283

.9024 .5029

.0302

0.9041

0.9046

1.0322

0.9058 0.9063

1.0341

0.907S 0.9080

1.0360

0.5091

0.9096

1.0378

0.9107

0.9112 1.0397

111.6 -161.55

6.057

0.8995

1.0268

.9002

.9007

.0277

.9019 .5024

.C29F

0.9036

0.9O41 1.0316

0.9053

0.9058

1.0335

0.9070 0.9075

1.0354

0.9086

0.9091

1.0373

0.9102

0.9107 1.0391

-161.45

6.098

0.8969 0.8994

1.0262

.8996

.9001

.0271 .9014

.9019

.0291

0.9031 0.9036

1.0310

0.9048 0.9053

1.0325

0.9065

0.907O 1.0348

0.9081

1.0367

0.9097

0.9102 1.0385

-161.35

6.139

0.8984

0.8989

1.0256

.8991 .8996

.0265

.9009

.5014

.0285

0.9026

0.9031 1.0304

0.9043

0.9048

1.0324

O.906O

0.9065

1.0343

0.9076 0.9081 1.03610.9092

0.9097 1.0380

111.9 -161.25

6.180

0.8979

0.8984

1.0250

.8986

.0259

.6003

.9ooe .0276

0.9O21

0.9026

1.0298

0.9038

0.9043

0.9055

0.9059

1.0337

0.9071

0.9076

1.0356

0.9087

0.9092 1.0374
DENSITY OF COMPRESSED LIQUID OXYGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUIO UENSITY/OENSITY AT A 2. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 3. DENSITY, KG/DM3

BOILING

BOILING PRESSUREPRESSURE

OF 1 BAR,

OF 760 TC OIMENSIC

?R, DIMES NLESS SIGNLESS

BAR 0.800 1.000 2.000 *.000 6.000 8.000 KP/CM2 0.616 1.020 2.039 *.079 6.118 8.158

10.000

10.197 15.00015.296

20.000

20.391. 25.00025.1.93 30.000 30.591 35.00035.690

*0.000 *0.7S9

112.0 -161.15

6.221

0.8973

0.8976

1.021.*

0.8961 0.8965 1.02520.8998 0.9003

1.0273

0.9016

0.9021

1.0292

0.9033

0.9O38

1.0312

0.901.9 0.9051. 1.0331

0.9066

0.9071 1.0350

0.9082

0.9087 1.0369

112.1 -161.05

6.262

0.8968

0.8973

1.0238

0.6975

0.8980

1.021.6 0.8993

1.0267

0.9O10

0.9015 1.0287

0.9028 0.9032

1.0306

0.901.1. 0.901.9 1.0325

0.9061

0.9066

0.9O77

0.9082 1.0363

112.2 -160.95

6.30". 0.8963

0.8968

1.0232

0.6970

0.6975

1.021.0 0.8988

0.8993

1.0261

0.9005

0.9O10 1.0261

0.9022 0.9027

1.0300

0.9039

0.901,1. 1.0320 0.9056

0.9061 1.0339

0.9072

0.9077

1.0357

112.3 -160.85

6.3*6

0.695T

0.6962

1.0226

0.8965

0.8970

1.0231.

0.8983 0^987

1.0255

0.9000

0.9O05

1.0J75

0.9017

0.9022

1.0291.

0.9031. 0.9039

1.031*

0.9051 0.9056

1.0333

0.9067

0.9072

1.0352

112.1. -160.75

6.388

0.8952

0.8957 1.0220

0.8959

0.8961. 1.0228

0.e977 0.8982

1.021.9

0.8995

0.9O00 1.0269

0.9012

0.9017

1.0289

0.9029

0.903* 1.0308

0.90*6

0.9051

1.0327

0.9062

0.9067

1.03*6

112.5 -160.65

6.1,30

0.891.7 0.6962 1.0214

0.6951. 0.8959

1.0222 0.6972

0.8977

1.021.3

0.8990 0.8995

1.0263

0.9007

0.9012 1.0283

0.902* 0.9029

1.0302

0.90*1

0.90*6

1.0321

0.9057

0.9062

1.03*0

112.6 -160.55

6."»72

0.891.1

0.891.6 1.0208

0.891.9

0.8951. 1.0216

0.8967

0.8972

1.0237

0.6981. 0.8989 1.0257

0.9002

0.9007

1.0277

0.9019 0.902*

1.0296

0.9036

0.90*1 1.0316

0.9052

0.9057 1.0335

112.7

-160.1.5 6.515

0.8936

0.891.1 1.0202

0.691.3 0.891.8 1.02100.8962

0.e96f

1.0231

0.8579

0.8981. 1.0251

0.8997

0.9002

1.0271

0.901*

0.9019

1.0291 0.9031

0.9036

1.0310

0.90*7

0.9052

1.0329

112.8 -160.35

6.558

0.8931

0.8936

1.0196

0.8938

0.891.3

1.0201.

0.8956 0.6961 1.0225

0.8971. 0.8979

1.0*1.5

0.8992

0.9997

1.0265

0.9009 0.901*

1.0285

0.9026

0.9031 1.030*

0.90*2

0.90*7 1.0323

112.9 -160.25

6.601

0.8925

0.8930 1.0189

0.8933

0.8936

1.0198

0.6951 0.8956

1.0219

0.8969

0.8971. 1.0239

0.8986

0.8991 1.0259

0.900*

0.9009

1.0279

0.9021 0.9037

0.90*2

1.0317

113.0 -160.15

6.61.1.

0.892O

0.6925 1.0163

0.8927

0.8932 1.0192

0.891.6 0.8951

1.0213

0.6961. 0.8969

1.0233

0.8981 0.8986

1.0253

0.8999

0.900*

1.0 27 3 0.9016

0.9021

1.0293

0.9032 0.9037

1.0312

113.1 -160.05

6.667

0.8915

0.8919 1.0177

0.8922

0.8927 1.0186

0.891.0 0.891.5 1.02070.6956

0.8963

1.0227 0.8976

0.8981

1.021.7

0.8993

0.8998 1.0267

0.9011 0.9016

1.0267

0.9027

0.9032 1.0306

113.2 -159.95

6.731

0.8909

0.8911. 1.0171

0.8917

0.6922

1.0180

0.8935

0.891.0 1.0201

0.6953

0.6958

1.0221

0.8971

0.8976

0.8986

0.8993

1.0261

0.9006

0.5010

0.9022

0.9027

1.0300

113.3 -159.85

6.7 75

0.8901. 0.8909

1.0165

0.8911 0.6916

1.0173

0.8930

0.8935

1.0191.

0.891.8 0.8953

1.0215

0.8966

0.9971 1.0236

0.8983

0.8988 1.0256

0.9000 0.5005

1.0275

0.9017

0.9022 1.0295

113.1. -159.75

6.819

0.8898

0.6903

1.0159

0.8906

0.8911 1.0167

0.8921. 0.8929

1.0188

0.891.3

0.891.8 1.0209

0.9961 0.9965

1.G230

0.8978

0.8963 1.0250 0.89950.9000

1.0269

0.9012

0.9017 1.0289

113.5 -159.65

6.863

0.6693

0.6898

1 .0152

0.8901

0.6905

1.0161

0.8919

0.8921. 1.0182

0.8937

0.891.2 1.0203

0.9955 0.8960

1.0221.

0.8973

0.8976

1.02**

0.8990

0.8595

1.026*

0.9007

0.9012

1.0283

113.6 -159.55

6.908

0.8669 0.6692

0.8895 0.8900

1.0155

0.8911. 0.8919

1.0176

0.8932

0.8937 1.0197

0.6950

0.8955 1.0218

0.896 6 0.8973 1.02380.8985

O.e990

1.0258

0.9002

0.9007 1.0277

113.7

-159.1.5 6.952

0.6882

0.8667

1.011.0

0.8690

0.8895

1.011.9

0.8906 0.8913

1.0170

0.6927

0.8932

1.0191

0.891.5 0.8950

1.0212

0.6963

0.8968

1.0232

0.8980

0.8985

1.0252

0.8997

0.9002

1.0272

113.8 -159.35

6.997

0.8877

0.8882

1.0131.

0.6861. 0.8989

1. 011.3 0.8903

0.8908

1. 0161.

0.8922

0.8926

1.0185

0.891.0

0.991.5 1.0206

0.8957

0.8962

1.0226

0.8975 0.8980

1.02*6

0.8992

0.8997

1.0266

113.9 -159.25

7.01.2

0.8671 0.8676

1.0128

0.8879

0.8881. 1.0136

0.689e

0.8903 1.0156

0.8916

0.6921 1.0179

0.8931. 0.9939

1.0200

0.8952

0.8957

1.0220

0.8970

0.8975

1.02*0

0.8967

0.8992 1.0260
OFNSITY OF COMPRESSEO LIOUIO

TAeLE ENTRIES

1. TEMPERATLRE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID OENSITY/OENSITY AT A 2. OENSITY RATIO, LIQUID OENSITY/DENSITY AT A 3. OENSITY, KG/DM3 PCILING PRESSURE OF 1 BAR, OI MENSICNLESS

BOILING PRESSURE OF 760 TCRR, 0IMENSIONLFSS

BAR 0.600 1.000 2.000 *.000 6.000 8.001) 10.000 15.000 KP/CM2 0.816 1.020 2.039 *.079 6.118 8.158 10.197 15.296 20.000

20.391. 25.00025.1.93 30.00030.591 35.000 35.690

*0.000 *0.789

11".. -159.15

7.088

0.8866 8.6873 0.8892 0.8871 0.8876 0.e897 1.0121 1.0130 1.01520.8911

0.8916

1.0173

0.8929

0.8931. 1.0191.

0.891.7 0.8952

1.021*

0.6965

0.8970

1.023*

0.8982 0.8967

1.025*

11"..

-159.05

7.133

0.6860 8.8868 0.6887 0.8865 0.8873 0.8692

1.0115 1.0121. 1.011.6

0.8906

0.8911 1.0167

0.8921. 0.S929

1.0188

0.89*2

0.89*7

1.0208

0.6960

0.8965 1.0225

0.8977

0.8982

1.02*8

lid. 2 -158.95

7.179

0.8855 0.8863 0.6882

0.6860 0.8867 0.6666 1.0109 1.0118 1.011.0

0.8900

0.8905

1.0161

0.8919

0.3921. 1.0182

0.8937 0.89*2

1.0202

0.8955

0.8959 1.0223

0.8972

0.8977

1.02*3

111..

-158.85

7.225

0.881.9 0.8857 0.8676

0.6851. 0.8862 0.6881 1.0103 1.0112 1.0133

0.8895

0.6900 1.0155

0.8913

0.8916 1.0176

0.8932

0.6936

1.0197

0.89*9 0.695*

1.0217

0.8967

0.8972 1.0237

11*.* -158.75

7.271

0.881.1. 0.8852 0.8871

0.881.9 0.8656 0.6676 1.0096 1.0105 1.0127

0.8890

1.011.9 0.8908

0.8913

1.0170

0.8926

0.8931

1.0191 0.69**

0.89*9

1.0211

0.8962 0.8967

1.0231

111..

-158.65

7.317

0.8830 0.681.6 0.e865

0.881.3 0.8851 0.8870

1.0090 1.0099 1.0121

0.6661. 0.8689

1.011.3

0.8903

0.3908

1.0161.

0.8921

0.6926 1.0185

0.8939 0.85**

1.0205

0.8957

0.8962 1.0225

11"..

-158.55

7.361.

0.8833 0.881.1 0.6860 0.8838 0.881.6 0.8865

1.0061. 1.0093 1.0115

0.8879

0.8881. 1.0137

0.8898

0.8903 1.01580.8921

1.0179

0.893*

.6939 1.0199

0.8952

0.8956 1.0219

11*.

-158. ".5 7.1.11

0.8827 6.6835 0.8855 0.8832 0.681.0 0.885? 1.0077 1.O086 1.0109

0.8671. 0.8879

1.0130

0.8692

0.8697

1.0152

0.8911

0.8916

1.0173 0.8929

0.693*

1.0193

0.89*6

0.6951 1.021*

11*.

-158.35

7.1.58

0.6822 1.8830 0.681.9 0.6827 0.6835 0.6651. 1.0071 1.0080 1.0102

0.8673

1.0121.

0.9887 0.3892

1.011.6

0.8905

0.8910

1.0167

0.692*

0.6926 1.0187

0.89*1

0.89*6 1.0208

111..

-158.25

7.505

0.8616 0.8821. o.efUl

0.8821 0.6829 0.861.5 1.0065 1.0071. 1.0096

0.8863

0.8868

1.0118

0.8882

1.011.0

0.8900 0.8905

1.0161

0.8918

0.6923

1.0182

0.6936

0.89*1

1.0202

115.0 -158.15

7.552

0.8811 0.8819 0.6836 0.8815 11.6823 0.681.3 1.0059 1.0068 1.0090

0.8858 0.8B62 1.0112

0.8876

0.3881

1.0131.

0.6895

0.8900

1.0155

0.6913

0.8918 1.0176

0.8931

0.8936 1.0196

115.1 -158.05

7.600

0.6605 0.6813 0.6633 0.8610 0.6818 0.6838 1.0052 1.0061 1.0061.0.6852

0.8857

1.0106

0.3871

0.3876

1.0128

0.8890 0.8895

1.01*9

0.8906 0.6913

1.0170

0.8926

0.8931 1.0190

115.2 -157.95

7.61.8

0.8600 0.6806 0.6827

0.6801. 0.8812 0.6832

1.001.6 1.0055 1.007e

0.881.7 0.6852 1.0100

0.8866

0.9871 1.0121

0.8985

0.8889 1.01*3

0.8903

1.016*

0.8921

0.8926 1.018*

115.3 -157.85

7.696

0.e79* 0.8802 0.e622

0.6799 0.8807 0.e827 1.0039 1.001.9 1.0071

0.881.1

0.881.6 1.0091.

0.8861

0.9865

1.0115

0.8979

0.888*

1.0137 0.6898

0.8903

1.0158

0.8916

0.8921 1.0178

115.1. -157.75

7.71.1.

0.6788 0.6797 0.6816 0.6793 0.6801 0.e821 1.0033 1.001.2 1.0065

0.8836

l!ofj87

0.9855

0.9860 1.0109

0.887*

0.8379

1.0131

0.6692 0.6897

1.0152

0.8911

0.8915 1.0173

115.5 -157.65

7.793

0.6783 0.8791 0.e811 0.8788 0.6796 0.6816 1.0027 1.0036 1.0055

0.8831

0.8835 1.0081

0.9850

0.8855 1.0103

0.8669

0.837*

1.0125

0.6887

0.e692

1.011.6

0.8905

0.8910

1.0167

115.6 -157.55

7.8*2

0.8777 0.6785 0.6805 0.8782 0.8790 0.8810 1.0020 1.0030 1.0053

0.8825

0.8830

1. 01)75

0.981.1. 0.981.9 1.0097

0.8863

0.6968

1.0119

0.6682 0.e687

1.01*0

0.8900 0.8905

1.0161

115.7

-157.1.5 7.891

0.8772 0.8780 0.6600 0.8776 0.e785 0.6805

1.0011. 1.0023 1.001.6

0.8820

0.8825 1.0069

0.9839

0.981.1. 1.0091

0.8858

0.8963

1.0113

0.8877

0.8882

1 .0131.

0.8895

0.8900

1.0156

115.8 -157.35

7.91.0

0.8766 0.8771. 0.e79* 0.8771 0.6779 0.6795 1.0008 1.0017 1.00*0

0.6811. 0.8819

1.0TJ63

0.3831. 0.9639

1.0085

0.8853

0.8658 1.0107

0.8872

o.ee76

1.0128

0.8890

0.8895 1.01*9

115.9 -157.25

7.989

0.8760 0.6769 0.e769

0.8765 0.8773 0.6791. 1.0001 1. 0011 1.C03*

0.6609

0.8811. 1.0056

0.6826

0.8833

1.0079

0.88*8

0.8852

1.010 I

0.8866

0.8871

1.0122

0.8885

0.8890

1.01*3
DENSITY OF COMPRESSED LICUIO OXYGEt*

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 2. OENSITY RATIO, LIQUID OENSITY/OENSITY AT A 3. DENSITY, KG/Df3

BOILING BOILING

PRESSURE

PRESSURE

OF 1 BAR, DIMENSIC

OF 760 TCRR, CIMEN NLESS SICNLESS

BAR 0.600 1.000 2.000 <• . 6.000 8.000 10.000 15.000 KP/CM2 0.816 1.020 2.039 4.079 6.116 6.156 10.197 15.296 20.000

20.394 25.000

25.493

30.000 30.591

35.000 35.69040.000 40.789

116.0 -157.15

6.039

8.8763 0.6783

0.6768 0^6786

1.0004 1.0027

0.8803

0.6808 1.0O50

0.9823

0.5826 1.0073

0.8842

0.8847 1.0095 0.8861

0.6666 1.0116

0.8680

0.6884 1.0137

116.1 -157.05

6.069

0.6757 0.6778

0.8762 0.8783

0.9598 1.0021

0.8796 0.8803

1.0O44

0.8818 0.8822

1.0066

0.8937

0.8842 1.0066

0.6856

0.6661 1.0110

0.8874

0.8879 1.0131

116.2 -156.95

6.139

0.8752 0.8772

0.6757 0.e777

0.9991 1.0015

0.8792

0.8797 1.0038

0.9812

0.8817 1.0060

0.6832

0.8836

1.0082

0.6851

0.6855 1.0104

0.8869

0.8874 1.0125

116.3 -156.85

8.169

0.8746 0.8767

0.6751 0.8772

0.5985 1.0008

0.8787

0.8792

1.0TJ32

0.8807

0.8812 1.0054

0.8326

0.8831 1.0076 0.86450.8850

1.0098

0.8864

0.8669 1.0119

116.". -156.75

e.2<>o

0.8741 0.8761

0.8745 0.8766

0.9978 1.0002

0.8762

0.6766

1.0025

0.3801

0.9606

1.0048

0.8821

0.8826 1.0070

0.6840

.8845 1.0092

0.8659

0.8864 1.0113

116.5 -156.65

8.291

0.8735 0.8756

0.8740 0.8760

8.9972 0.5996

0.8776

0.8781

1.01)19

0.3796

0.9801 1.0042

0.8816

0.6920 1.0064

0.8835

0.8840

1.0066

0.8853

0.8656 1.0107

116.6 -156.55

6.342

8.6729 0.8750

8.8734 0.6755

6.9966 0.5985

0.8771

0.8775 1.0013

0.8791

0.6795 1.0036

0.8310

0.8815

1.0058

0.8829

0.e834

1.0080

0.6648

0.8853

1.0101

116.7

-156.1,5 6.393

0.8724 0.8744

8.8728 0.8745

0.9959 0.5983

0.8765

0.8770 1.0OO6

0.8785

0.8790

1.0029

0.8805

0.8810 1.0052

0.8824

0.8829 1.0074

0.8643

0.6648 1.0095

116.8 -156.35

B.*«f5

0.8718 0.8739

TJ.6723 0.8744

0.9953 0.5977

0.8759

0.8764 1.0000

0.9790 0.8784

1.0023

0.8799

0.8804

1.0046

0.8819

0.8824

1.0068

0.8838 0.8643 1.0089

116.9 -156.25

8. 496

0.8712 0.e733

0.8717 0.8738

0.9946 0.597D

0.6754

0.6759 0.9994

0.5774 0.8779

1.0017

0.8794

0.8799

1.0040

.8013 0.8818

1.0062

0.8633

0.8837

1.0083

117.0 -156.15

6.548

8.8706 0.e728

0.8711 0.8732

0.9940 0.9964

0.8748

0.8753 0.9967

0.9769

0.8774

1.0011

0.8789

0.8793

1.0033 o.eeoe

0.6813 1.0056

0.6827

0.8832 1.0077

117.1 -156.05

8.600

0.8701 0.8722

0.8706 0.8727

fl.9933 0.9957

0.8743

0.6748 0.9961

0.8763

0.3768 1.5004

0.8783

0.8788

1.0027

0.8803

1.0050

0.8822

0.8827 1.0071

117.2 -155.95

8.653

0.8695 0.6716

0.8700 0.8721

8.9926 0.5951

0.8737

0.8742 0.9975

0.9758 0.9763 0.99960.8778 0.8783

1.0021

0.8797 0.8802

1.0043

0.8817

0.8622

1.0065

117.3 -155.65

8.705

8.8689 0.6711

0.8694 0.e716

0.9920 0.5944

0.8732

0.8737 0.9968

0.9752

D.9757

0.9992

0.8772

0.8777

1.0015 0.8792

0.8797

1.0037

0.8811 0.8616 1.0059

117.4 -155.75

6.758 0.8688 0.871C

0.9913 0.9936

0.6726

0.8731 0.9962

0.9747

0.8752 0.9986

0.8767

0.8772

1.0009 0.8787

0.8792

1.0031

0.8806 0.8811

1.0053

117.5 -155.65

8.611

0.8678 0.8699

0.8683 0.8704

8.9907 0.5932

0.6721 0.8725

0.9956

0.9741

0.8746

0.9979

0.8762

0.9766 1.0002 0.6781.6786 1.0025

0.8601

0.8806 1.0047

117.6 -155.55

6.865

0.8672 0.8694 0.6677 0.6695

0.5900 0.9925

0.8715

0.8720 0.9949

0.8736

0.9741

0.9973

0.8756

0.9761 0.9996

0.6776

0.8781

1.0015

0.6796

1.0041

117.7 -155.45

8.918

8.8666 0.668e

0.8671 0.6693

0.5894 0.9919

0.8709 0.8714 0.99430.8730 0.9735 0.99670.8751 0.8755

0.9990

0.8771 0.6776

1.0013

0.6790

0.8795

1.0035

117.8 -155.35

6.972

0.8661 0.e682

0.6665 0.6687

0.9667 0.5912

0.8704

0.6709 0.9937

0.9725

0.9730

0.5960

0.8745

0.8750

0.9984

0.8766

0.8770

1.0007

0.8785

0.8790 1.0029

117.9 -155.25

9.026

0.6655 0.8677

0.8659 0.8661

0.9860 0.9906

0.8696 0.8703

0.9930

0.8719 0.8724

0.9954

0.8740 0.3745

0.9976

0.6760 0.8765

1.0001

0.8780

0.8784 1.0023
CONTINUED COMPRFSSEO LIOUIO

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 2. OENSITY RATIO, LIQUID OENSITY/DEKSITY AT A 3. DENSITY, KG/OH3 BOILING

eOILING

PRFSSU°E

PRESSURE

OF 1 BAR, OIMENSICNLESS

OF 760 TCRR, OIMENSICNLESS

BAR 0.800 1.000 2.000 4.000 6.000 8. 001) 10.000 15.000 KP/CM2 0.816 1.020 2.039 4.079 6.118 8.158 10.197 15.296 20.000

20.394

25.000

25.493

30.000

30.591 35.00035.690

40.000

40.789

-155.15

9.080

0.8649 0.8671

0.8654 0.8676

0.9874 0.9895

0.8693

0.8697

0.9924

0.8714

0.9718 0.9948

0.8734

0.8739

0.9971

0.8755

0.9759 0.9994

0.8774

0.8779 1.0017

118.1 -155.05 9.1350.8643 0.8665

0.8648 0.6670

0.9867 0.5893

0.8687 0.8692

0.9917

0.8708 0.9713

0.9941

0.8729

0.8734

0.9965

0.8749 0.8754

0.9988

0.8769 0.8774

1.0011

118.2

-151.. 95 9.189

0.8637 O.8660 0.6642 0.8664

0.9861 0.5886

0.8681 0.8666

0.9911

0.9703

0.8707

0.9935

0.8723

0.8728 0.9959

0.8744

.8749 0.9982

0.8764

0.8768 1.0005

118.3

-15".. 85

9.2<rt

0.8631 0.8654

0.8636 0.8655

1.9854 0.9875

0.8676

0.8680

0.9904

0.8697 0.8702

0.9929

0.8718

0.8723

0.9953

0.8738

0.8743 0.9976

0.8758

0.8763

0.9999

118.".

-15".. 75 9.299

0.8626 0.8648

0.8630 0.8653

0.5847 0.5873

0.8670

0.8675

0.9898

0.9691 0.9696

0.9922

0.8712

0.8717 0.9946 0.8733

0.8738 0.9970

0.8753

0.6758

0.9993

118.5 -154.65

9.355

8.8620 0.8642

0.8624 0.8647

0.9841 0.9866 N

0.8664

0.8669

0.9891

0.9686

0.8691 0.9916

0.8707 0.8712

0.9940

0.8727

0.8732 0.9964

0.8748

0.8752

0.9987

-IS".. 55

9. 411

0.8614 0.8637

0.8619 0.8641 0.5834 0J9860

0.8659

0.8663 0.9885

0.3680

0.8685

0.9910

0.8701 0.8706

0.9934

0.8722

0.8727 0.9957

0.8742

0.8747

0.9980

118.7

-154.1.5 9.4 66

0.8608 0.e631

0.8613 0.8635

0.9827 0.585J

0.8653

0.8658

0.9878

0.8675

0.8679 0.9903

0.8696

0.*9927 0.8717

0.8721

0.9951

0.8737

0.8742

0.9974

118. B -154.35

9.523

0.8602 0.e62E

8.8607 0.6630

0.9820 0.5646

0.8647

0.8652 0.9872

0.8669

0.9897

0.8695 0.9921

0.8711

0.8716 0.9945

0.8731

0.8736

0.9968

118.9 -154.25

9.579

0.8596 0.8619

B.8601 0.8624

0.5814 0.5840

0.6642 0.8646

0.9865

0.9663

0.9668

0.9890

0.8685

0.8589

0.9915

0.8706 0.8710

0.9939

0.8726

0.8731 0.9962

119.0 -154.15

9.636

C.8590 0.8613

0.8595 o.e6ie

0.9807 0.5633

0.8B36

0.8641 0.9859

0.8658

0.9662

0.9884

0.8679

0.8684

0.9908

.8700 0.S705

0.9932

0.8721 0.8725

0.9956

119.1 -154.05

9.693

0.8584 0.8608

0.8589 0.8612

0.9800 0.9827

0.8630

0.8635 0.9852

0.9652 0.8657

0.9877

0.8674

0.8678

0.9902

0.8695 0.8699

0.9926

0.8715

0.8720

0.9950

119.2 -153.95

9.750

0.8578 0.660?

0.8583 0.8606

0.9793 0.5820

0.8624

0.8629

0.9846

0.8646

0.8651

0.9871 0.9573 0.9996 0.86940.9520

0.6710 0.8715

0.9943

119.3 -153.85

9.607

0.8573 0.8596

0.8577 0.8601

0.9787 0.5813

0.6619

0.6623

0.9839

0.8645 0.9865

0.8662

0.8667

0.9989

0.8684

0.5914

0.8704

0.8709 0.9937

119.4 -153.75

9.865

0.8567 0.8590

6.8571 0.e595

0.9780 0.9807

0.6613

0.B618

0.9833

0.8635

0.9640

0.9858

0.8557 0.8662

0.9863

0.8678 0.8663

0.9507

0.8699

0.8704 0.9931

119.5 -153.65 9.922

0.8561 0.8594

0.8565 0.8589

0.9773 0.5800

0.8607

0.8612 0.9826

0.3629 0.9634 0.9852

0.8651 0.8656

0.9877

0.8673

0.8677 0.5901

0.8694

0.8698

0.9925

119.6 -153.55

9.981

0.8555 0.8578

0.6559 0.6583

0.9766 0.579?

0.8601 0.8606 0.9819

0.9624

0.9845

0.8646

0.8650

0.9870

0.8667

0.8672

0.5895

0.8688

0.8693

0.9919

119.7 -153.45

10.039

0.8572 0.e577

0.5766

0.8595

0.8600 0.9811

0.8618

0.8623

0.9839

0.8545 0.9864

0.8662

0.8666

0.9888

0.8683

0.8687 0.9912

119.8 -153.35 10.097

0.e566

0.8571

0.5790

0.8550

0.8594 0.9806

0.8612

0.9617

0.9832

0.8534

0.8539 0.9857

0.8656

0.8661

0.9862

0.8677

0.8682

0.9906

119.9 -153.25

10.156

0.8561

0.8565

0.5773

0.8564

0.8589

0.9800

0.9607 0.3611

0.9826

0.8629

0.8634

0.9851

0.8650

0.6655

0.9876

0.8672

0.8676

0.9900
DENSITY OF COMPRESSED LIQUID OXYGEN - CONTINUED

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 2. DENSITY RATIO, LIQUIO BENSITY/OENSITY AT A 3. DENSITY, KG/D«3 BCILING

eOILING PRESSURF

PRESSURE

OF 1 9AR,

OF 760 TC DIMENSIC

?R, DIMEN NLESS SIONLESS

BAR 0.800 1.000 2.000 1..000 6.000 6.000 10.000 15.000 KP/CM2 0.816 1.020 2.039 "..079 6.118 6.158 10.197 15.29620.000

20.391. 25.000

25.1.93 30.000 30.591

35.000

35.690

1.0.000

1.0.789

120.0 -153.15

10.215

0.8555 0.855? 0J97660.8578

0.6583

0.9753

0.8601 0.8606

0.9819

0.8623

0.8626

0.98l»<i

0.861.5 0.6650 0.9869

0.8666

0.8671

0.9891.

120.1 -153.05 10.275

0.e5i.9 0.6553 0.9759

0.8572

0.8577

0.9786

0.8595

0.8600 0.9812

0.8617

0.8622

0.9838 0.6639

0.861.1. 0.5663

0.8661

0.8665 0.9887

120.2 -152.95

10. 33",

0.65<»3 0.85"i7 0.97530.8566

0.6571

0.9780

0.8589

0.3591. 0.9806 0.8612

0.8617

0.9832

0.8631. 0.8639 0.9857

0.8655

0.8660 0.9881

120.3 -152.85

10.39'. 0.6537

0.851.1 0.571.6

0.8560

0.8565

0.9773

0.8581. 0.8588 0.9799

0.36O6

0.6611 0.9925 0.8633

0.5650

0.8650

0.8651. 0.9875

120.'. -152.75

10.<tS<i

0.8531

0.6535

0.5739

0.8555

0.8559 0.9766

0.8576

0.8583 0.9793

0.8600

0.8605 0.9819

0.8623 0.6627

0.981.!.

0.861.1. 0.861.9 0.9868

120.5 -152.65

10.511. 0.8525

0.6529 0.9732

0.851.9 0.8553

0.9759

0.8572

0.8577 0.9786

0.8595

0.8599

0.9312

0.8617

0.6622

0.9837

0.8639

0.861.3 0.9862

120.6 -152.55

10.575

0.6515

0.6523 0.9725

0.851.3

0.851.8 0.9753

0.8566

0.9571 0.9779

0.8589

0.8591. 0.9806

0.6611 0.6616

0.5631

0.6633

0.8638

0.9856

120.7

-152.1.5 10.636

0.8513

0.6517

0.9718

0.8537

0.651.2 0.971.6

0.8560

0.9565

0.9773

0.8583

0.8568

0.9799

0.8606 0.6610

0.9825

0.8628

0.8632

0.9850

120.8 -152.35 10.6970.8507

0.6511 0.9712

0.8531

0.8536

0.9739

0.8555

0.8559 0.9766

0.8578

0.8582

0.9793

0.6600

0.8605

0.9618

0.8622

0.8627

0.981.3

120.9 -152.25

10.758

0.8501

0.6505 0.9705

0.6525

0.8530

0.9733

0.851.9 0.9553

0.9760

0.8572

0.8577 0.9786

0.6591. 0.6595 0.5612

0.8617

0.8621 0.9837

121.0 -152.15

10.620

0.61.95

0.81.9? 0.9698

0.8519

0.6521. 0.9726

0.851.3

0.951.8 0.5753

0.8566

0.8571

0.9779 0.6589

0.6591. 0.5805

0.8611

0.8616

0.9831

121.1 -152.05

10.882

0.81.89

0.61.93 0.5691

0.8513

0.8516 0.9719

0.9537

0.951.2 0.971.6

0.8560

0.8565

0.9773 0.6583

0.6586 0.9799

0.8605

0.8610

0.9821.

121.2 -151.95 10.9M.

0.81.83

0.81.B7

0.9681.

0.8507

0.8512

0.9712

0.9531 0.9536

0.971.0

0.8555

0.6559 0.9766

0.6576 0.e562 0.5792

0.8600

0.8601. 0.9818

121.3 -151.65 11.006

0.81.77 0.8*81

0.5677

0.8501 0.8506

0.9705

0.9525

0.8530

0.9733

0.851.9

0.8551. 0.9760 0.6572

0.6577

0.9786

0.8591. 0.8599

0.9811

121.1. -151.75

11.069

0.61.70 0^96700.81.95 0.8500

0.9699

0.8520

0.3521. 0.9726

0.851.3

0.951.6 0.9753

0.8566

0.8571

0.9779

0.8589

0.8593

0.9805

121.5 -151.65 11.132

0.81.61. 0.61.65 0.9663

0.61.89 0.9692

0.951U

0.9518 0.9719

0.8537

0.851.2

0.971.6 0.6560

0.6565

0.9773

0.8583

0.6588 0.9799

121.6 -151.55

11.195

o.ei.5e 0.81.63 0.56560.81.83 0.81.68 0.9685

0.8508

0.9512

0.9713

0.6532

0.8536

0.971.0

0.8555

0.655?

0.9766

0.8577

0.8582

0.9792

121.7

-151. 1.5 11.258

0.61.52 0.61.57

0.561.9

0. 61.77 0.81.82 0.96780.9502 0.9506

0.9706

0.8526

0.8530 0.9733

0.e5i.9

0.6551. 0.9760

0.8572

0.8576

0.9786

121.8 -151.35

11.322

0.61.51

0.961.2

0.81.71 0.81.76 0.96710.81.96 0.8501 0.96990.8520 0.8525

0.9727

0.851.3

0.851.8 0.9753

0.8566

0.8571 0.9779

121.9 -151.25 11.386

0. 61. 1.0 0.61. !.< 0.9635

0.81.65

0.81.70

0.9661.

0.91.95 0.9692

0.8511. 0.8519

0.9^20

0.6536

0.651.2

0.971.7

0.8560

0.8565

0.9773
- CONTINUED COMPPESSEO LIQUIO OXYGEN - CONTINUED

TAeLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUID OENSITY/OENSITY AT A 2. OENSITY RATIO, LIQUIO OENSITY/CENSITY AT A 3. DENSITY, KG/DM3

PCILING P EOILING P RESSURE OF RESSURE OF1 9AR, OIHEKSICNLESS

760 TORR, OIMENSIONLESS

BAR 0.6 00 1.000 2.000 I». 00 6.000 8.000 tO.000 16.000 KP/CM* 0.816 1.020 2.039 it. 079 6.118 8.158 10.197 15.296 20.000

20.391. 25.000

25.1.93 30.000 30.591

35.000 35.690

1.0.000 1.0.789

122.0 -161.15

11.1.50

0,81.31. o.eitje 0.9628

0.81.59 0.9657

0.81.81. 0.91.89 0.9686

0.8506

0.8513

0.9713

0.8532 0.8536

0.971.0

0.8555

0.8559

0.9766

122.1 -151.05

11.511)

0. 81.27 0.61.32 0-9621

0.81.53

0.81.66 0.9650

0.81.76 0.81.83 0.96790.8502

0.8507

0.9707

0.8526

0.6531

0.9731.

0.851.9

0.8551. 0.9760

122.2 -150.95

11.579

0.81.21

0.81.26

0.9611.

0.81.1.7 0.81.52

0.961.3

0.81.72

0.31.77 0.9672

0.81.97 0.8501 0.97000.6520

0.8525

0.9727

0.851.3

0.651.8 0.9753

122.3 -150.85

11.61.1.

o.ei.15 0.61.20 0.5607

0.81.1.6 0.9636

0. 91.66 0.81.71 0.9665

0.81.91

0.81.95 0.9693

0.8515

0.6519

0.9720

0.8538

0.851.2

0.971.7

122.1. -150.75 11.709

0. 81.09 0.81.13 0.5600

0.81.35 0.81.39 0.9629

0.91.60 0.81.65 0.96560.61.65 0.81.89 0.9686 0.6509

0.6513

0.9711.

0.8532 0.8537

0.971.0

122.5 -150.65

11.771.

0.81.03

0.81.07 0.9593

0.81.29

0.81.33 0.9623

0.81.51. 0.91.59 0.9652

0.81.79 0.96800.8503

0.8508

0.9707

0.8526

0.8531

0.9731.

122. 6 -150.55

0.6396

0.81.01 0.9586

0.81.23 0.81.27 0.9616

0.91.1.8 0.91.53

0.961.5

0.81.73

0.81.78 0.9673

0.61.97 0.8502

0.9701

0.8521

0.8525 0.9727

122.7

-150.1.5 11.906

0.8390

0.8395 0.9578

0.81.16

0.81.21

0. 91.1.2 0.9638

0.81.67

0.81.72 0.9666

0.81.91

0.61.96

0.9691.

0.8515

0.8520 0.9721

122.8 -150.35 11.972

0.8381. 0.8388

0.9571

0.81.10

0.81.15 0.9601

0.81.36 0^96310.81.61

0.81.66 0.9659

0.81.85

0.61.90 0.9687

0.8509

0.6511. 0.9711.

122.9 -150.25 12.039

0.e376 0.8382

0.9561.

0.81.0l| 0.81.09 0.9591.

0.81.30

0.81.35 0.9621.

0.81.55

0.81.60 0.9653

0.81.80

0.81.61. 0.9661

0.8503

0.8508

0.9708

123.0 -150.15

12.106

0.8371 0.8376 0.95570.8398

0.81.03 0.9587

0.81.21. 0.91.29 0.9617

0.81.1.9

0.81.51. 0.961.6

0.81.71. 0.9671.0.81.98 0.8502

0.9701

123.1 -150.05 12.173

0.8365 0.8369

0.9550

0.8352

0.8396

0.9580

0.91.16 0.9610

0.81.1.3 0.81.1.8 0.96390.81.68

0.61.73 0.9667

0.61.92 0.81.97 0.9695

123.2 -H9.95

12.21.0

0.6355

0.8363

0.551.2

0.8386 0.8390

0.9573

0. 91.12 0.91.16 0.9603

0.81.37

0.81.1.2 0.9632

0.81.62

0.81.67 0.5661

0.81.86

0.81.91 0.9688

123.3 -H9.85

12.308

0.8352

0.8357

0.5535

0.8379

0.8381. 0.9566

0.81.06

0. 31.1 0.9596

0.81.31

0.81.36 0.9625

0.81.56 0.9651.

0.81.80

0.81.85 0.9681

123.1. -11.9.75 12.375

0.831.6 0.6350

0.9528

0.8373 0.8378

0.9559

0.81.00

0. 91.01. 0.9589

0.81.25

0.81.30 0.9619

0.81.50

O.ei.55 0.961.7

0.81.75

0.81.79 0.9675

123.5

-11.9.65

12.1.1.3

0.8339

0.831.1. 0^9521

0.8367

0.6371

0.9552

0.3393

0.8398

0.9582

0.8*19

0.81.21. 0.9612

0.81.1.1. 0.81.1.9 0.81.69

0.81.73 0.9668

123.6

-11.9.55 12.512

0.8333 0.8338

0.5513

0.6361 0.8365

0.951.5

0.9387 0.9392

0.9575

0.81.13

0.81.18 0.9505

0.81.36

0.61)1.3 0.9631.

0.81.63

0.81.68 0.9662

123.7

-11.9.1.5 12.581

0.8327

0.8331

0.5506

0.8359

0.9538

0.9386

0.9568

0.81.07

0.81.12 0.9598

0.81.33

0.61.37 0.5627

0.81.57

0.81.62 0.9655

123.8

-11.9.35

12.61.9

0.6320

0.8325

0.51.99

0.831.8 0.8353

0.9530

0.9375 0.8380

0.9561

0.81.01

0.81.06 0.9591

0.61.27

0.81.31 0.9620

0.81.51

0.81.56

0.961.8

123.9

-11.9.25 12.719

0.8311. 0.8318

0.91.91

0.631.2 0.831.6 0.95230.8369 0.9373

0.9551.

0.8395

0.91.00

0.9581.

0.81.21 0.81.25 0.9613

0.81.1.6

0. 61.50 0.961.2
ICUIO OXYGEN

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID OENSITY/0EMSITY AT A 2. OENSITY RATIO, LIQUID OENSITY/DEKSITY AT A 3. DENSITY, KG/Df^

BOILING

BOILING

PRESSURE PRESSUREOF 1 BAR, OIMENSIONLESS

OF 760 TCRR, CIMENSICNLESS

BAR 0.800 1.000 2.000 "..000 6.000 8.000 10.000 15.000 KP/CM2 0.816 1.020 2.039 it. 079 6.118 8.158 10.197 15.296

20. BOO

20.391. 25.00025.1.93 30.000 30.591 35.000 40.000 35.690 40.789

12-.. -149.15

12.788

0.8307

0.8312

0.91.81.

0.8335

0.831.0 0.9516

0.8363

0.8367

0.951.7

0.8389

0.8391. 0.9S77

0.8415 0.8440 0.8415 0.8444 0.9606 0.9635

125.0 -H8.15

13.1)98

0.82<>2 0.824E

0.91.09

0.8272

0.8276

0.91.1.3

0.8300

0.3305

0.91.76

0.8328 0.8332

0.9507

0.6354 0.6381 0.6359 0.8385 0.9536 0.9567

126.0

-11.7.15

11.. 236

0.ei7E 0.8179

0.9333

0.8206

0.8210 0.9368

0.8236

0.921.1

0.91.02

0.8265

0.8270

0.91)36 0.6293 0.8320 0.6298 0.8325 0.9468 0.9499

127.0

-11.6.15 15.002

0.8139

0.811.3 0.9291

0.S170 0.8175

0.9328

0.8201

0.8205

0.9362 0.8230 0.8259 0.8235 0.8263 0.5396 0.9426

128.0

-11.5.15 15.797

0.BD70

0.8071. 0.9213

0.S103

0.9108 0.9251

0.8135

0.811)0 0.9287

0.8166 0.8196 0.8171 0.8201 0.9323 0.9357

129.0

-11.1.. 15 16.622

0.7999

0.8001. 0.9132

0.8031. 0.8038 0.9172

0.8067

0.8071

0.9209

0.8099 0.8130 0.8103 0.8135 0.9246 0.9282

130.0

-11.3.15

17.1.78 0.7925

0.7930 0.9048

0.7962

0.7967 0.9090

0.7998

0.8002 0.9130

0.8032 0.8064 0.8036 0.8069 0.9169 0.9207

131.0

-11.2.15 18.365

0.7851

0.7665 0.8963

0.7890

0.7891. 0.9007 0.7927

0.7931

0.901)9 0.7963 0.7997 0.7967 0.8002 0.9091 0.9130

132.0

-11.1.15 19.283

0.7772

0.7776 0.8873

0.7811. 0.7818

0.8921

0.7851) 0.7858 0.8966

0.7692 0.7928 0.7896 0.7933 0.9009 0.9051

133.0

-11.0.15 20.235

0.7737

0.771.1 0.8833

0.7779

0.7783

0.8381

0.7819 0.7858 0.7824 0.786? 0.8927 0.8971

131.. -139.15 21.219

0.7656

0.7660

0.7701

0.7706 0.8792 0.7745 0.7786 0.7745 0.7790

0.681.1 0.8888

135.0 -138.15 22.2370.7572 0.7576

0.861.1.

0.7620 0.7625

0.8700

0.7667 0.7710 0.7671 0.7715 0.8753 O.8603

136.0 -137.15 23.291

0.71,83 0.7487

0.851.3

0.7536

0.751>1

0.8601. 0.7586 0.7633

0.7590 0.7637 0.8661 0.8714

137.0 -136.15

21.. 379

0.7390

0.7391. 0.91.37

0.71.1)9 0.71,53 0.8504

0.7503 0.7553 0.7507 0.7557 0.8565 0.8622

138. -135.15

25.501.

0.7357

0.7361

0.8399 0.7415 0.7470 0.7419 0.7474 0.8466 0.8527

139.0

-131.. 15 26.666

0.7259

0.7263

0.8287

0.7324 0.7383 0.7328 0.7387 0.8361 0.8429

11.0.0 -133.15

27.866

0.7157

0.7161

0.8170 0.7226 0.7292 0.7232 0.7296 0.8252 0.6325

11.1.0 -132.15

39.101.

0.7045

0.7049

0.8043

0.7126 0.7197

0.7130 0.7201 0.8135 0.8216

11.2.0 -131.15

30.383

0.7018 0.7097 0.7021 0.7101 0.8012 0.8102

143.0 -130.15 31.702

0.6895 0.6989 0.6903 0.6993 0.7e76 0.7979
COMPRESSED LICUIO OXYGEN - CONTINUED

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID OENSITY/OENSITY AT A BOILING PRESSURE OF 1 BAR, 01 MENSICNL ESS

2. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A BOILING PRESSURE OF 760 TCRR, OIMENSIONLESS

3. DENSITY, KG/OH*

BAR 0.800 1.000 2. KP/CM2 0.816 1.020 2. 000 it. 000 6.000 8.000 10.000 15.000 20.000 25.000 30.000 35.000 1.0.000 039 1..079 6.116 8.156 10.197 15.296 20.391. 25.1.93 30.591 35.690 1.0.789

l<t<«.0 -129.15

3 3.0 6<t

0.6772 0.6875 0.6776 0.6679 0.7731 0.781.9

K.5.0 -128.15

0.6627 0.671.9 0.6631 0.6753 0.7565 0.7705

-127.15

35.918

0.6612 0.6615

0.751.8

11.7.0 -126.15

37.1.13

0.61.56

0.61.59 0.7370

11.6. -125.15

38.955

0.6277

0.6280 0.7166
7. NITROGEN

The data tabulated for nitrogen are based on the paper by Strobridge (1962). The satu- rated liquid values were calculated by solving simultaneously the vapor pressure equation and

the equation of state. First the vapor pressure equation was solved for either pressure or temperature depending on the integral value desired, then using the resulting P and T, the equation of state was solved for the corresponding density. All of the tabulated values were

obtained in this manner except the critical point. At the critical point the vapor pressure

equation was used to calculate the pressure from an input temperature of 126.26 K but the density was calculated using the theory of rectilinear diameters and the saturation densities

tabulated by Strobridge. Values near room temperature are given in table 5, uncertainties for the data in table 6, values for the saturated liquid are given in table 7, and values for the compressed liquid are shown in table 8. Near the critical point, the deviations between calculated and

Table 5 Density of Nitrogen Near Atmospheric Pressure and Room Temperature

Temperature Pressure Density Volume

gram- mole/cm3 kg /dm3 cm /gram- mole dm3 /kg 0°C 1 bar

760 torr 4.4051xl0~ 5 4.4635xl0" 5 1.2341xl0~ 3 1.2505xl0~ 3 22701.

22404. 810.28

799.68 15°C 1 bar

760 torr

4. 1752xl0~ 5

4. 2305xl0~ s

1. I697xl0~ 3

1. 1852x1

0" 3 23951.

23638.

854. 91 843. 73 Density Ratios - Dimensionles s Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 0° C

Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 15° C

654.63

690.70

Liquid Density at a boiling pressure of 760 torr /density at 760 torr and 0°C

Liquid Density at a boiling pressure of 760 torr/density at 760 torr and 15° C

645.67

681.23

Liquid density at a boiling pressure of 1 bar 0. 8079 kg/dm

Liquid density at a boiling pressure of 760 torr 0.8074 kg/dm3
experimental data range from 0. 2% at 125 K to 5% at 126 K. The critical density given Ln table 7 is uncertain by 5% as well. The value of the density at the boiling point at 760 torr in table 7 should be the same as in the CGA pamphlet P-6, yet they differ by 0. 1%. This is surprising as the source has not changed, and we can only suspect an error in the printing of the pamphlet.

Table 6 Uncertainties in the Data for Nitrogen

variable uncertainty range of temperature temperature 0.5% 64 to 72 K

0.1% 72 to 125 K

0.015 K room temperature volume 0.4% up to 125 K

increases to 5% at 126 K

0.01% room temperature

pressure 1% 64 to 72 K

0.1% 72 to 126 K

0.01% room temperature

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OENSITY OF CCI-PPESSEO LIQUID NITROGEN

TEMPERATURE, K TEMPERATURE, C VAPOR PRESSURE, BAR

ABLE ENTRIES DENSITY

DENSITY

DENSITY

75.5

-197.65

0.809

75.6

-197.55 0.819

75.9 -197.25

0.850

76.0

-197.15

0.860

76.2

L96.95 0.882

76.3

-196.85

0.892

76.1. L96.75 0.903

76.5

L96.65

0.91".

76.6

L96.55 0.925

76.7

L96.1.5 0.936

.8161,

,0099

.0023

.0029

.8098

.012". .0131

.8179

.0113

.0119

.8170

.0107

.011". .8166

.oi".i .01U7

.8193

.0118

.0125

.8175

D146 .0152

.8197

.0125

.0130 B179

.811.8

.0079

.016". .0171 .8212

.0153

.0160

.8203

.0066

.813".

.0062 1.

.0057 .0063

.8125

.007". .0080 .ei39

.0075

.0080

.6139

.00".0 .00".6 .em

.0097 .0103 o„ei5e

.0126 .0132

.8161

.0120

.0127

.8176

.0115

.0121

.6172

0099

.0106

.3160

1091. 0100

.3155

0150

CIS fc 920

01J3 0129

3178

0079 1.0092

0065 1.0099

811.3 0.S15". 0073 1.0087

0080 1.0093

8138 .61".=

C15?

015 = e202
OENSITY OF COMPRESSED LIQUID NITROGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR1 . 2.

3.

OENSITY

DENSITi

DFNSIT1

RATIO, L RATIO, I

, KG/DP 3 IOUIO OENSITY/CEKSI

IQUID BENSITY/OENSI

Y AT A BOILING PRt

Y AT A BOILING PR SSURE OF SSURE OF

1 BAR, OIMENSICNLESS

760 TCRR, OIMENSIONLFSS

BAR KP/CM20.800 1.000 0.816 1.020 2.000

2.039

1..000 1..079 6.000 6.1168.008 6.15810.000

10.197 2.500

2.71.6 5.000

5.296

7.500 20.000

7.81.5 20.391. 25.000

25.1,93 30.00030.591

77.0 -196.15

0.971

1.001", 1.0021

0.8 091

.0017

.0021, .8093

.0023 .0029

.6098

1.0029

1.0035

0.8102

1.0031.

1.001.1 0.8107

1.001.0 0.8111

.001.7 .0053 .8117.0051. .6123

.0061 .0067

.3128

.0071. .8131.

1.0061 1.0088

0.611.5

1.0095 1.0101

0.8156

77.1 -196.05

0.962

1.0009

1.0015 0.6086

.0012

.0016

.0017

.0021. .8093 1.0029

0.6098

1.0029

1.0035

0.8102

1.0031,

1.001.1 0.8107

.001.1

. oo<*e .8113

.001.8 .0055

.8118

.0055 .0062

.8121.

.0062

.0069

.6129

1.0076

1.0062

0.011.0

1.0089

1.0096 0.8151

77.2 -195.95

0.994

1.0003 1.0009

0.8062

.0006

L.0012 .0012

.0018

.6089

1.0017

1.0021. 0.6093 1.00231.0029

0.6098

1.0029

1.0035 0.6102

.0036

.001.2 .6108

.001.3

.001.9 .0050 .0056

.8119

.0057

.0063 .8125

1.0070 1.0077

0.8136

1.0061. 1.0090

0.811.7

77.3 -195.65

1.0 06

.0000 .0007

.8079 :"" 1.0012

1.0018 0.8089

1.0017

1.0021. 0.8093

1.0023

1.0029

0.8098

L.003C L.0037

.eioi.

.0037

.8109

.001.1. .0051 .9115

.0051

.0057 .8120

1.0065

1.0071 0.8132

1.0079

1.0065

0.811.3

77.1, -195.75.9991. .0001

.e075

.0000 .0007

.8079

1.0006

1.0012

0.8081. 1.0012 1.00180.8089

1.0017

1.0021. 0.6093 -0025 .0031

.6099

.0032 .0038

.8105

.0039

. 01,5 .8110

.001.6 .0052 .6116

1.0055

1.0066 0.(127

1.0073 1.0079

77.5 -195.65

1.030

.9989

.9995

.8070

.9995

.0001 .8075

1.0000 1.0007

0.8079

1 .0006 1.0012

0.8081.

1.0012 0.8089.0019

1.0025 .0026

.0032

.8100

.0033

.0039

.001,0

.001,6 .8112

1.0051. 1.0060 0.8123

1.0068

1.0071,

0.8131.

77.6 -195.55 LOW

.9983

.9989 .8065

.9989

.9995

.8070

0.9995

1.0001

0.8075 1.0000

1.0007

0.8080

I.O005 1.0013

0.8081.

.0013

L.C020 .8090

.0020

.0-027 .8096

.0027

.0031. .8101

.0031.

.001.1 .8107

1 . 001.8 1.0055 0.8118

1.0062

1.0069

0.8129

77.7

-195.1.5

1.05".

.9977

.9961. .8061

.9983 .9989

.8066

0.9989 0.9995

O.8070

0.9995

1.0001

0.8075

1.0001 1.0007 0.8080.oooe .0015

.0021 .0022.0028 .8097

.0029

.0035 .8103

1.001.3 1.001.9

0.8111.

1.0057

1.0063 0.8125

77.6 -195.35

1.0 66

.9972

.9978 .6056

.9977

.9981. .8061

0.99 6 3 0.9990

0.8066 0.9989

0.9995 0.8070

0.5995

1.0001 0.6075

L.0002 .8081

.0009

.0016

.6067

1.0023 .8092

.0023

.0030

.8098

1 .0037

1.001.1. 0.8109

1.0051

1.0058

0.8121

77.9 -195.25

1.079

.9966

.9972

.6052

.9972

.9978 .8056

0.9978

0.9981. 0.6061 0.9983

0.9990

0.8066

0.9989 0.9996

0.8070

.9996

1. 0003 .e076

.0001. .0010

,80e2

.0011

L. 0017 .9098

.0018

.0021.

.8091.

1.0032

1.0038 0.8105

1.001.6 1.0052 0.8116

78.0 -195.15

1.091

.9960 .9966

1.601.7

.9966

.9972

.8052

0.9972

0.9978

0.8056 0.9976

0.9981. 0.8061

0.5981. 0.9990

0.8066 .5991

3.5997

..8072

.9999 .8078.0005 .0012

.8083

.0012

.0019

.8089

1.0026 1.0033

0.8100

1.001,0 1.001,7 0.8112

78.1 -195.05

1.101,

.9951. .9961

.601.2

.9960

.9967

.801.7

0.9966 0.9973

0.8052

0.9972 0.9978

0.8057

0.9978

0.5981. 0.8061

3.5565 1.9992

0.8O67

.9992 .9999

.8073

.0000

L.1006 .9079

.0007

.0013

.8085

1.0021 1.0027

0.8096

1.0035 1.00U1

0.8107

78.2

-191,. 95 1.117

.991.9 .9955

.8038

.9955

.9961

.601,2

0.9960

0.9967

0.801(7

0.9966

0.9973 0.8052

0.9972

0.9979

0.8057 .99861.8063

.9987

.9993

.6066

.9991. .0000

.9071.

.GOO 1 .0007

.8080

1.0015

1.0022

0.8092

1.0029

1.0036

0.8103

78.3

-19"». 85 1.130

.991.3

.991.9

J. 8033

.991.9 .9955

.8038

0.9955

0.9961

0.801.3

0.9961

0.9967

0.801.7

0.9967

0.9973

8.6052

1.597* .9960

i.eosf

.9981

.8061.

.9988 .9995

.9070 .8076

1.0010

1.0016 0.8087

1.0021, 1.0030 0.8098

78.', -19",. 75

1.11,3

.9937

.991.3 .6026

.991.3

.991.9 .6033

0.991.9 0.9955 0.603e 0.9955

0.9961

0.801.3 0.9961

0.9967

0.801.8 .9968

• 5°75

.16053

.9976 .9982

.8059

.9983 .9989

.3065

.9990

.9996 .3071

1.0001. 1.0011 0.6083

1.0018 1.0025

0.8091.

78.5

-19".. 65 1.156

.9931 .9938

• eo2i.

.9937

.991.1. .8029

0.991.3 0.9950 0.80330.991.9 0.9956

0.8038

0.9955

0.9962

0. 801.3 .5969

1.801.5

.9970

.9976

.8055

.9977 .9983

.8061

.9991. .8067 0.9995

1.0005

0.8078

1.0013

1.0019

0.8090

78.6

-191.. 55 1.169

J. 9926

1.9932 .8019

.9932

.9936

.8021.

0.99 3 8 0.991.1. 0.8029

0.991.1. 0.9950

0.6031.

0.991.9 0.9956

6.8036

1.9957 .5963

3.801.1.

.9961. .9971 .8050.9972 .9978

.9056

.9979 .9985 .80620.9993

1.0000

0.8071.

1.0007

1.0011.

78.7

-191,. 1,5 1.182

.9920 .9926

J. 6011.

.9926

.9932 .8019

0.9932

0.9938

0.8021. 0.9938

0.991.1. 0.8029

0.99<< i. 0.9950

0.8031.

1.5951 .9958 .eco

.9959

.9965

.8TJI.6

.9966

.9972

.9052

.9973 .9980 .8057

0.5588

0.9991. 0.8069

1.0002

1.0008

0.8061

78.8

-19<».35 1.196

.9911. .9920 .8010

.9920

.9926

.8015

0.9926 0.9932 0.9932

0.9938

0.6021.

0.9938

0.991.1. O.8029

.591.6 .5952

.8035

.9953

.9959

.801.1

.9960 .9967

.901.7

.9968

.9971. .8053

0.9962

0.9988

0.8065

0.9996 1.0003 0.8076

78.9

-191..25 1.209

.9908

.9911. .8005

.9911. .9921

.8010

0.9920 0.9927

0.8015

0.9926 0.9933

0.6020

0.9932

0.5939 0.8025

.591.0 .991.6 .8031

.991.7

.9951. .8037

.9955

.9961

.801.3

.9962

.9968

.801,8

0.9976 0.9983

0.8060

0.9991 0.9997

0.8072
CCNTINUEO XPPRESSEC LIQUID NITROGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

12

3

. DENSITY

. DENSITY

. DENSITY

RATIO, LIQUID OENSITY/OEN

RATIO, LIQUID OENSITY/OEN

, KG/OM3

SITY AT A SITY AT A BOILING PRESSURE

BOILING PRESSURE

OF 1 BAR, DIMENSICNLESS

OF 760 TORR, OIMENSIONLESS

BAR KP/CM2

0.800 1.000 2.000 0.816 1.020 2.039

l.. 000 4.079

6.000 6.118 6.15810.000

10.197 12.5

12. 71.6 15.00015.296

17.500

17.81.5 20.00020.391. 25.00025.1.93 30.000 30.591

79.0

-19".. 15 1.223

.9902 0.9909

0.8000

0.9908

0.9915 0.8005

0.9915

0.99 21 0.6010

0.9921 0.9927

0.8015

8.9527

0.9933

(.8020

0.9931.

0.591.0 0.8026

0.991.2

0.991.8

0.8TJ32

0.991.9 0.9955 0.90380.9956

0.9963

0.801.1.

0.5971 0.5977

0.8056

0.9985

0.9992 0.8067

79.1

-194. 05 1.237

0.9697

0.9903 0.7996

0.9903

0.9909

0.8001

0.9909

0.9915

0.8005

0.9915

0.9921

0.8010

0.9921

0.9927 0.8015

0.9928

0.9935 0.8021

0.9936

0.991(2

0.8TJ27

0.991.3 0.9950

0.8033

0.9951 0.9957

0.8039

0.5965

0.9972 0.8051

0.9980

0.9986 0.8063

79.2 -193.95

1.251

0.9891

0.9897

0.7991

0.9897

0.9903 0.7996

0.9903

0.9909

0.8001

0.9909

0.9915

0.8006

0.9915 0.9922

8.8011

0,9923

0.9929

0.8017

0.9930 0.9937

0.8D2 3

0.9938

0.991.1. 0.8029

0.991.5 0.9951

0.8035 0.9560

0.9966 0.8047

0.9974 0.9961

0.8058

79.3 -193.85

1.265

0.9885

0.9891 0.7986

0.9891 0.9897

0.7991

0.9897

0.9901. 0.7996 0.99030.9910

0.8001

t.9909

B.S916 O.8006

0.9917

0.9923

0.8012

0.9925

0.9931

0.8T118

0.9932

0.9938

0.8021.

0.9939

0.991.6 0.8030

0.9951. 0.9961

0.801.2

0.9969

0.9975

0.8054

79.". -193.75

1.Z79

0.9879 0.9885

0.7981

0.9885

0.9892

0.7987

0.9891 0.9698

0.7991

0.9898 0.9904

0.7996

0.9901. 0.9910

0.8001 0.9911

0.9918

0-8008

0.9919

0.9925

0.8O14

0.9926

0.9933

0.9931. 0.9940 0.80260.9945

0.9955

0.8038

0.9963

0.9970 0.8049

79.5 -193.65

1.293

0.9873

0.9880 0.7977

0.9880

0.9886 0.7982

0.9886 0.9892

0.7987

0.9892

0.989B

0.7991

0.9898

0.9901. 0.7997

0.5906

0.9912

0.8003

0.9913

0.9920

0.8O09

0.9921

0.9927

0.8015

0.9928

0.9935

0.8021

0.991.3

0.991.9 0.6033

0.9958

0.9964

0.8045

79.6 -193.55

1.308

0.9867

0.9871. 0.7972

0.9871. 0.9880 0.7977

0.9880 0.9886

0.7982

0.9886 0.9892

0.7987

0.9892

0.9999

0.7992

0.9900

0.9906 0.7998

0.9908 0.99m

0.8U04

0.9915

0.9921

0.8011

0.9923

0.9929 0.8017

0.9937

0.591.11 0.8029

0.9952

0.9958

0.8040

79.7

-193.1.5 1.322

0.9862

0.9668 0.7967

0.9868

0.9871. 0.7972

0.9871. 0.98 8 0.79770.9880

0.9887

0.7982

0.9887 0.9893

0.7987

0.9891. 0.9900

0.7991.

0.9902

0.9908

0.6000

0.9909 0.9917

0.9923

0.8012 0.9932

0.9938

0.8021.

0.9947

0.9953

0.8036

79.8 -193.35

1.337

0.9856

0.9862 0.7963

0.9862

0.9668

0.7968

0.9868 0.9875

0.7973 0.9875

0.9681

0.7978

0.9887

0.7983 0.5895 0.7989

0.9896

0.9902

0.7995

0.9901. 0.9910

0.8001

0.9911

0.9918

0.8007 0.9926

0.9933

0.8020

0.9941 0.9947

0.8032

79.9 -193.25

1.352

0.9850 0.9856

0.7956

0.9856

0.9862

0.7963

0.9863

0.9669

0.7968

0.9869

0.9875

0.7973

0.9875

0.9881

0.7=78 0.9889

0.7981(

0.9890 0.9897

0.7991

0.9898

0.9901. 0.7997

0.9906 0.9912

0.9003

0.9921

0.9927 0.8015

0.9935

0.9942

0.8027

80.0 -193.15

1.367 0.9850

0.7953

0.9850 0.9857

0.7958

0.9857

0.9863

0.7963

0.9863

0.9869

0.7968

0.9869

0.9875 0.7973

0.9877 0.9883

0.7980

0.9885

0.9891

0.7966

0.9892 0.3899

0.7992

0.9900 0.9906

0.7998

0.9915 0.9921 0.80100.9930 0.9936

0.8023

80.1 -193.05

1.382

0.9836

0.981.11 0.791.8

0.981.5 0.9851

0.7951.

0.9851

0.9657 0.7959

0.9857 0.9663

0.7961.

0.9963

0.9870

0.7969

0.5871

0,15877 0.7975

0.9879

0.9885

0.7981

0.9887

0.9693

0.7988

0.9891. 0.9901

0.7991.

0.5509

0.9916

0.6006

0.9924

0.9931

0.8018

80.2 -192.95

1.397

0.9832 0.9839 0.79440.9839

0.981.5

0.791.9

0.961.5 0.9851

0.7951. 0.9851

0.9658 0.7959

0.9858

0.9861.

0.7961.

0.9865

0.9872

0.7970

0.9873

0.9880

0.7977

. 0.9881

0.9887 0.7983

0.9889

0.9895 0.7989

0.5901. 0.9910

0.8001

0.9919

0.9925 0.8014

80.3 -192.85

1.1.12

0.9826

0.9833 0.7939

0.9833 0.9639

0.79l(l( 0.9839

0.981.5 0.791.9

0.981.6 0.9852

0.795l( 0.9852 0.5858

0.7959

0.5860

0.9866

0.7966

0.9869

0.987i( 0.7972

0.9875

0.9882

0.7978 0.9889

0.7985

0.569e

.9901. 0.7997

0.9913

0.9919

0.8009

80.lt -192.75

1.1.28

0.9821 0.9827

0.7931.

0.9827

0.9833 0.7939

0.9833

0.961.0 0.791.5

0.981(0 0.981(6 0.79500.981.6 0.9e52

0.7955

0.9851. 0.9860

0.7961

0.9862

0.9868 0.7967

0.9870

0.9876

0.7971.

0.9877

0.9881. 0.7980

0.5893

0.9899 0.7992

0.9908

0.8005

80.5 -192.65

1.1.1.3

0.9615

0.9821 0.7929

0.9821

0.9627

0.7935

0.9628

0.9631.

0.791.0

0.9831.

0.981.0 0.791.5

0.581.0

0.981.7 0.7950

0.9846

0.9851. 0.7956

0.9856 0.9B62

0.7963

0.9870 0.7969

0.9872

0.9878

0.7975

0.9687 0.5893

0.7968

0.9902

0.9908

0.8000

80.6 -192.55

1.1.59

0.9809

0.9815 0.7925

0.9815 0.9821

0.7930

0.9822

0.9828

0.7935 0.9828

0.9631.

0.791.0

0.9831.

0.581.1 0.791.5

0.581.2 0.981.5 0.79520.9850

0.9857 0.7958 0.5858

0.9861. 0.7965

0.9866

0.9972

0.7971

0.5881

.5888 0.7983

0.9896

0.9903

0.7995

80.7

-192.1.5

1.1.75

0.9803

0.9609

0.7920

0.9809

0.9816

0.7925

0.9816

0.9822

0.7930 0.9822

0.9828 0.7936

0.9829

0.9935

0.791.1

0.9837

0.581.3

0.791.7

0.981(5 0.9651 0.79540.9852

0.9859

0.7960

0.9860 0.9366

0.7966

0.9876

0.7979

0.9891 0.9897

0.7991

80.8 -192.35

1.1.91

0.9797

0.9803 0.7915

0.9803

0.9810 0.7920

0.9610 0.9616 0.7926

0.9816

0.9823 0.7931

0.9823

0.5829 0.7936

0.5831

0.791.2

0.9839

0.9845

0.791.9 0.9853

0.'955

0.9851. 0.9861 0.79620.5e70 0.9876 0.7974

0.9885

0.9e91 0.7986

80.9 -192.25

1.507

0.9791 0.9797

0.7910

0.9796

0.9801. 0.7916

0.9601. 0.9810

0.7921

0.9811

0.9B17

0.7926

0.9917

0.9823 0.7931

0.5625

0.5831

0.7938

0.9833 0.9839

0.791.1.

0.981.1 0.981.7 0.79510.981.9 0.9855

0.7957

0.9864

0.7970

0.9880 0.9886

0.7982
:5SE0 LIQUID NITROGEN - CONTINUED

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BARl

2

3

. DENSITY

. DENSITY

. DENSITY

RATIO,

RATIO,

, KG/0M3

.IQUID DENSITY/DENSITY AT A .iaUIO OENSITY/OENSITY AT A BCILING PRESSURE SOILING PRESSUREOF 1 9AR, OIMENSIO

OF 760 TCRR, CIMEK

ML ESS SICNLESS

BAR KP/CM^

0.800 1.000 2.000

0.816 1.020 2.039

1..000 I..079 6.000 6.118 8.000

6.158

10.000

10.197 12.50012.71,6 15.000

15.296

17.500

17.81,5 20.000

20.391. 25.00025.1,93 30.000 30.591

61.0 -192.15

1.523

0.9785

0.9791 0.7906

0.9792

0.9798

0.7911

0.9798

0.9801, 0.7916

0.9605 0.9811

0.7921

0.9811 0.9817

8.7927

0.5615 0.5825

0.7933

0.9827 0.9833

0.791.0

0.9835

0.981.1

0.791,6

0.981.3

0.981.9 0.7952

0.5859

0.9865

0.7965

0.9871, 0.9860 0.7977

81.1 -192.05

1.539

0.9779

0.9785

0.7901

0.9786

0.7906

0.9792 0.9799

0.7911 0.9799

0.9805 0.7917

0.9805 0.9812

0.7922 0.9817

0J5820

0.7926

0.9821

0.9628

0.7935

0.9829 0.9636

0.791.1

0.9837

0.981,1, 0.791,8

0.5653 0.9859

0.7960

0.9868 0.9875

0.7973

81.2 -191.95

1.556 0.9773 0.97790.7896

0.9780 0.9786

0.7901

0.9786

0.9793 0.7907 0.97930.9799

0.791S

0.9800

0.9906 0.7917 0.9806

0.5811.

0.7921. 0.9816

0.9822

0.7930

0.9921. 0.9830 0.7937

0.9832

0.9838

0.791,3

0.981,7 0.9851, 0.79560.9863 0.9869

0.7968

81.3 -191.85

1.57Z

0.9767

0.9773

0.7891

0.9771, 0.9780 0.78970.9781 0.9767

0.7902 0.9787 0.97930.7907

0.9791, 0.9800 0.79120.580? 0.9606

0.7919

0.9610

0.9816 0.7926

0.9818

0.9821, 0.7932

0.9826

0.9832 0.7938

0.581,2

0.581.6 0.7951

0.9857

0.9863

0.7961.

81. t, -191.75

1.589

0.9761 0.9768 0.76860.9766

0.9771, 0.7892

0.9775

0.9781 0.7897

0.9761 0.9787

0.7902

0.9788

0.9791, 0.7908

0.5796

0.9802 0.79H

0.9801. 0.9810 0.7921

0.981?

0.9918

0.7927

0.9820

0.9626

0.7931,

0.9836

0.981.2 0.791,7

0.9652

0.9656 0.7959

81.5 -191.65

1.606

0.9755

0.9762

0.7882

0.9762

0.9768

0.7887

0.9769

0.9775

0.7692

0.9775

0.9782

0.7896

0.9782

0.9788 0.7903

0.9790

0.9796 0.7910

0.9798

0.9801. 0.7916

0.9806

0.9813

0.7923 0.98K,

0.9821 0.7929

0.9830

0.9836

0.791,2

0.'9852 0.7955

81.6 -191.55

1.623

0.97h9

0.9756 0.7877

0.9756

0.9762 0.7882

0.9763 0.9769

0.7688

0.9769

0.9776

0.7B93

•.9776

0.9782 0.7898

0.5761. 0.9791 0.7905

0.9792 0.9799

0.7911

0.9801 0.9807

0.7916

0.9809

0.9815 0.7925

0.5925

0.5831 0.7537

0.981,0 0.981,6 0.7950

81.7

-191.1,5

1.61,0

0.971,3 0.9750

0.7872

0.9750

0.9756 0.7877

0.9757

0.9763

0.7883

0.9761, 0.9770

0.7888

0.9770 0.9776

0.7891.

0.9776 0.9785 0.7900

0.9767

0.9793

0.7-907 0.9795

0.9901

0.791

0.9803

0.9809 0.7920

0.5619

0.9625 0.7933

0.9635

0.961,1

0.791,6

81.8 -191.35

1.657

0.9737

0.971,1. 0.7867

0.971,1, 0.9750

0.7873

0.9751 0.9757

0.7878 0.9758

0.9761, 0.7883

0.9761, 0.9771

0.7S89

0.9773

0.9775

0.7B95

0.9781

0.9787

0.7902

0.9789 0.9795

0.7909

0.9797

0.9803 0.7915

0.5813

0.5815 0.7928

0.9829 0.9835

0.791,1

81.9 -191.25

1.67",

0.9732

0.9738 0.7862

0.9738

0.971,1, 0.7868

0.971,5 0.9751 0.787301975*

0.9758 0.7879

0.9758

0.9765

0.7881.

0.9767

0.9773

0.7891

0.9775

0.9781 0.7897

0.9783

0.9769 0.97910.9798 0.7911

0.5807

0.7921,

0.9823

0.9830 0.7936

82.0 -191.15

1.692

0.9726

0.9732 0.7857

0.9732

0.9739 0.7663

0.9739

0.971,5 0.7868

0.971,6 0.9752

0.7871.

0.9753

0.9759 0.7379

0.5761

0.5767

0..7886

0.9769

0.9775

0.7893

0.9777

0.5731, 0.7899

0.9786 0.9792 0.79060.9802

0.5608 0.7919

0.9818

0.9821. 0.7932

82.1 -191.05

1.709

0.9720 0.9726 0.7853

0.9726

0.9733 0.7856

0.9733

0.9739

0.7861,

0.971,0 0.97U6

0.7869

0.971.7 0.9753 0.7875 0.5755

0.5761 0.7681

0.9763

0.9770 0.7888

0.9772

0.5776 0.7895

0.9780

0.9786

0.7901

0.9796

0.5802

0.7911,

0.9812

0.9818 0.7927

82.2 -190.95

1.727

0.9711, 0.9720

0.781,8

0.9720 0.9727

0.7853

0.9727

0.9733 0.7859

0.9731, 0.971,0

0.7861,

0.971,1 0.971,7 0.7870

0.571.5 0.5755

0.7877

0.9758

0.9761. 0.7683

0.9766 0.9772

0.7890

0.9771. 0.9780 0.7897

0.5790 0.9796

0.7910

0.9806

0.9813

0.7923

82.3 -190.85

1.71.5

0.9708

0.9711, 0.781,3

0.9711, 0.9721

0.781,6

0.9721

0.9727

0.7851,

0.9721

0.9731, 0.7859

0.9735

0.971,1 0.7865

0.971.3 0.975C

0.7672

0.9752

0.9758

0.7879

0.9760

0.9766

0.7885

0.9768

0.9771. 0.7892

0.9785

0.9791 0.7905

0.9601

0.9807

0.7918

82.1. -190.75

1.763

0.9702

0.9708

0.7838

0.9706

0.9715

0.781,1.

0.9715

0.9721

0.781,9 0.9722 0.97280.7855

S.9729 0.9735

0.7960

0.9737

0.971.1. 0.7867

0.971.6 0.9752

0.7871.

0.9751. 0.9760

0.7881

0.9762

0.9769

0.7887

0.9779

0.9785

0.7900

0.9795

0.9801 0.7913

82.5 -190.65

1.781

0.9695

0.9702

0.7833

0.9702 0.9709

0.7839

0.9709

0.9716

0.781,1, 0.9716 0.9722

0.7650

0.9723

0.5729 0.7955

0.5732

0.5736 0.7862

0.971.0 0.971,6 0.76690.971.8 0.9755

0.7876

0.9757

0.9763 0.7683

0.9773

0.9779

0.7896

0.9789

0.9795 0.7909

82.6 -190.55

1.800

0.9689

0.9696

0.7828

0.96 96 0.9703

0.7831,

0.9703

0.9710

0.761,0 0.9710

0.9716

0.781.5

0.9717 0.9723

0.7651

0.5726 0.5732 0.7856

0.9731,

0.971.0

0.7861,

0.971.3

0.971.9 0.9751 0.9757

0.7878

0.9767

.7691

0.9781. 0.9790

0.7901.

82.7

-190.1,5 1.818

0.9683

0.9690

0.7823

0.9690 0.9697

0.7829

0.9697

0.97 01, 0.7835

0.9701. 0.9710

0.781.0

0.9711 0.9717

0.781,6

0.5720 0.5726

0.7853

0.9726

0.9731, 0.7860

0.9737

0.971.3 0.7866

0.971,5 0.9751

0.7873

0.9762

0.5768 0.7887

0.9778

0.9781. 0.7900

82.8 -190.35

1.837

0.9677

0.9681, 0.7819

0.9681, 0.9691

0.7821.

0.9691

0.96 9 6 0.7630

0.9699 0.9705

0,7835

B.9705

0.9711

6.791.1

0.5711, 0.5720

0.781,6

0.9722

0.9729

0.7855

0.9731 0.9737

0.9739

0.971,5 0.7868

0.5756

0.9762

0.7882

0.9772 0.9778

0.7895

82.9 -190.25

1.856

0.9671 0.9677

o.7eii,

0.9676

0.9685

0.7819

0.9685

0.9692

0.7825 0.9692

0.9699

0.7831

0.9699

1.9705 0.7836 0.5708

0.5711.

0.781,3

0.9716

0.9723

0.7850

0.9725

0.9711 0.7657

0.9733

0.971.0

0.7861.

0.5750

0.9756

0.9766

0.9773

0.7690
DENSITY OF CCPI6RESSEC LIQUID NITROGEN - CONTINUE:

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

23

. DENSITY

. DENSITY

. DENSITY

RATIO,

RATIO,

, KG/DK3 LIQUIO OENSITY/CENSITY AT A LIQUID DENSITY/DENSITY AT A PCILING

BOILING PRESSURE PRESSURE

- 1 8AR, OIHENSICNLESS

F 760 TCR9, CIMENSIONLESS

BAR KP/CH2

0.800 1.000 2.000

0.816 1.020 2.039

l.. 000 *.079

6.000 S.OOi

6.158

10. COO 10.197 12.500

12.71.6 15.000

15.296

17.500

17.8U5 20.000

20.39<i 25.000

25.1.93 30.000

30.591

83.0 -190.15

1.875 0.9665

0.9671 0.7809

0.9672

0.9679

0.7811. 0.9679

0.9686

0.7820 0.9686

0.9693

0.7826

0.9693

0.5700 0.7831 0.9702

0.5708

0.7836

0.9711

0.9717

0.781.5 0.9719

0.9725 0.7852

0.9728

0.9731, 0.7859 0.97**

0.5750 0.7873

0.9761

0.9767

0.7686

83.1 -190.05

1.89". 0.9659

0.9665

0.7801. 0.9666

0.9672

0.7810 0.9673

0.9680

0.7815 0.968O

0.9687

0.7621

0.5687

0.9691. 0.7827 0.5696 0.5702

0.7831. 0.9705

0.9711 1.78*1

0.9713

0.9719

0.781.7

0.9722

0.9728 0.785*

0.9738 0.97*5

0.7668

0.9755

0.9761

0.7881

83. 2 -189.95

1.913 0.9653

0.9659 0.7799

0.9660 0.9666

0.7605 0.9667

0.9671. 0.7810

0.9671. 0.9681 0.7816

1.5681

0.9688 8.7822 0.569C0.5696 0.7829

0.9599

0.9705

0.7836 0.9707

0.9711.

0.781.3

0.9716

0.9722 0.7850 0.9733

0.9739

0.7863

0.97*9

0.9755

0.7677

83.3 -189.85

1.932 0.96*7

0.9653

0.7791.

0.9651. 0.9660

0.7800

0.9661

0.9666 0.7806 0.96680.9675

0.7811

0.9676

0.9682 0.78170.5690

0.7821. 0.9693

0.9699

0.7831

0.9702

0.9708

0.7838

0.9710

0.9716

0.73*5 0.5727 0.9733

0.7859

0.97**

0.9750 0.7872

83.1. -189.75

1.952

0.961.1

0.961.7 0.7789

0.961.8

0.9651. 0.7795

0.9655

0.9661 0.7601

0.9662

0.9669 0.7806

0.9670 0.9676

0.7812 0.9676

0.5681. 0.7815

0.9687

0.9693

0.7826 0.9696

0.9702 0.7833

0.970*

0.9710

0.79*0

0.9721 0.5727

0.785*

0.9738

0.97**

0.7867

83.5 -169.65

1.971

0.9635

0.961.1

0.7781.

0.961.2

0.961.8 0.7790

0.961.9 0.9655

0.7796 0.9656

0.9663

0.7602

0.966l| 0.9670 0.7807 0.9672

0.9678

0.7811.

0.9661

0.9687

0.7821

0.9690

0.7826

0.9698

0.9705

0.7835

0.9716 0.5722

0.78*5

0.9732

0.9738

0.7e63

83.6 -189.55

1.991

0.9629

0.9635 0.7779

0.9636

0.961.2 0.7785

0.961.3

0.961.9 0.7791

0.9650

0.9657 0.7797

0.9658

0.9661. 8.7802

0.5666

0.5673

0.7610

0.9675 0.9661

0.7817

0.5681. 0.9690

0.7621.

0.9692 0.9699

0.7831

0.9710 0.9716

0.78*1.

0.9726

0.9733

0.7858

83.7

-169.1.5 2.011

0.9630 0.9636

0.7780

0.9637

0.961.3 0.7766 0^9651

0.7792

0.9652

0.9658 0.7798 0.56600.9667

0.7806

0.9669 0.9675

0.7812

0.9678

0.9681. 0.7819 0.9687

0.9693

0.7826 0.570*

0.5710 0.76*0

0.9721 0.9727

0.7853

63.8 -189.35

2.0 31

0.9621. 0.9630 0.77750.9631 0.9637

0.7781 0.5638

0.961.5 0.7787

0.561.6 0.5652

0.7793

0.5651. 0.5661

0.7800

0.9663

0.9669

0.7807

0.9672 0.9678

0.7811. 0.9687 0.7821

0.5696

0.970*

0.7836

0.9715

0.9721

0.78*9

63.9 -169.25

2.052

0.9618

0.9621. 0.7770

0.9625

0.9631

0.7776

0.9632

0.9638

0.7782

0.961.0

0.961.6 0.7788

0.561.8 0.5655

0.7795

0.9657

0.9663

0.7602

0.9666

0.9672 0.7809

0.9675

0.9661

0.7316

.5692

.5698 0.7830

0.9709 0.9715

0.78**

8*.0 -189.15

2.072

0.9612

0.9618

0.7765

0.9619

0.9625 0.7771

0.9626

0.9632

0.7777

0.9631. 0.961.0 0.77930.961.3

0.561.5 0.7790

0.9651

0.9658

0.7799

0.9660

0.9666

0.7805

0.9669 0.9675

0.7312

0.5686

0.6692

0.7626

0.9703

0.9710

0.7839

8*.l -169.05

2.092

0.9606

0.9612

0.7761 0.9613

0.9615

0.7766 0.9620

0.9626

0.7772

0.9628

0.9631. 0.7778

0.5637

0.66*3 0.7785

0.961.5 0.9652

C.77<=3

0.9651. 0.9660

0.7800

0.9563

0.9669

0.7807 0.96870.7621

0.9698 0.970*

0.7835

Bit. 2 -168.95

2.113

0.9600 0.9606

0.7756 0.9607 0.96130.7762

0.9611. 0.9620 0.7767

0.9621

0.7773 0.5631

0.5637 0.7781

0.9639

0.7788

0.9655

0.7795 0.9657

0.9663

0.7802 0.9675

0.6681 0.7ei6

0.9692

0.9698

0.7830

81.. 3 -188.85

2.131.

0.9593 0.9599

0.7751

0.9601

0.96 7 0.7757 0.96080.9611. 0.7763

0.9615 0.9622

(.7768 0.56250.7776

0.961.0 0.7783

0.961.2 0.7790

0.9651

0.9657

0.7797 0.5675

0.7812

0.9666

0.9692

0.7825

61.. 1. -188.75

2.155

0.9587

0.9593

0.771.6 0.9595 0.9601

0.7752 0.9602

0.9608

0.7758

0.5609

6.9616

0.7761. 0.5615

0.5625

0.7771

0.9628

0.9631. 0.7779

0.9637

0.961.3 ?.779 c 0.96*50.9652

0.7793

.9663 0.6665

0.7807

0.9680

0.9686

0.7821

81.. 5 -188.65

2.176

0.9581

0.9587

0.771.1

0.9589

0.9595

0.771.7 0.9596

0.9602

0.7753

0.9603

0.9509

0.7755

0.5613 0.5615

0.7766

0.9622

0.9628

0.7773

0.9637

0.7791

0.9639 0.96*6

0.7786

0.6657 0.5663

0.7802

0.967*

0.7816

81.. 6 -188.55

2.197

0.9575

0.9581 0.7736

0.9582

0.9589

0.771.2 0.9590

0.9596

0.771.8

0.5597

0.9603

0.7751. 0.5606

0.7761

0.9616 0.9622

0.7765

0.9625

0.9631 0.963*0.96*0 0.7783

0.5651 0.6657 0.77970.9669

0.9675

0.7811

84. 7 -168.1.5 2.2190.9569

0.9575

0.7731

0.9576 0.9582

0.7737

0.9581. 0.9590

0.771.3

0.9591 0.5597

0.771.9 0.5600

0.9607

0.7756

0.9610

0.9616

0.7761.

0.3619 0.9625

0.7771

0.9628

0.953*

0.7778 0.66*5

0.9652 0.7793

0.9663

0.9666

0.7607

81.. 8 -188.35

2.21.1 0.9563

0.9569

0.7726

0.9570

0.9576

0.7732

0.9578

0.9581. 0.7739

0.9565

0.5591

0.771,1,

0.5591- 0^5601

0.7751

0.9601. 0.9610

0.7759

0.9613

0.9619 0.7766

0.9622

0.9628

0.777*

0.96*0

0.7788

0.9657

0.9663 0.7e02

81..

-188.25

2.2 62

0.9557

0.9563

0.7721

0.9561. 0.9570 0.7727 0.9572

0.9578

0.7733

8.5579

0.5585

0.7739 0.5538

0.5591. 0.771.7

0.9593

0.9601.

0.7751.

0.9607

0.3613

0.7761

0.9616

0.9622

0.7769 0.963*

0.66*0 0.7763

0.9651

0.9657 0.7797
DENSITY OF CCMPRESSEC LIQUIO NITROGEN - CONT

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO, LIQUID OENS ITY/OENSITY AT A RATIO, LIQUID OENSITY/OENSITY AT A

, KG/DP3

BOILING

BOILING PRESSUREPRESSURE

OF 1 OAR, OIMENSICNLESS

OF 760 TCRR, DIMFNSI ONLESS

BAR 0.800 1.000 2.000 It. 000 KP/CM? 0.816 1.020 2.039 1..079 6.000 6.118

8. 001 6.158

10.000

10.197 12.500

12. 71,6 15.00015.296

17.500

17.81.5 20.00020.391, 25.000

25.1.93 30.00030.591

85.0 -168.15

2.281,

0.9550 0.9556

0.7716

0.9558

0.9561. 0.7722 0.9566

0.9572

0.7728

0.9573

0.9579

8.7731,

0.5582

0.5586

0.771.2

0.9592

0.9598

0.771.9

0.9601

0.9607 0.7757

0.9610

0.9616

0.7761,

0.9628

0.9631. 0.7778

0.961,5 0.9652

0.7793

85.1 -188.05

2.306

0.951,1. 0.9550

0.7711

0.9552

0.9558

0.7717

0.9559

0.9565 0.7723

0.9567

0.9573 0.7729

0,5576 0.5582

0.7737

0.9586

0.9592

0.771,1,

0.9595

0.9601 0.7752

0.9601, 0.9610

0.7759

0.9622

0.9628

0.7771.

0.961,0 0.961,6 0.7788

85.2 -187.95

2.329

0.9538

0.95'.'. 0.7706

0.951.6 0.9552

0.7712 0.9553

0.9559

0.7718

0.9561 0.9567

0.7721, 0.9570

0.9576 0.7732

0.9580 0.9586

0.7739 0.9589

0.9595

0.771,7

0.9598

0.9601.

0.7751, 0.9616

0.9622 0.7769

0.9631, 0.961.0 0.7783

85.3 -187.85

2.351

0.9532

0.9538

0.7701

0.951.0

0.951.6 0.7707

0.951,7 0.9553 0.77130.9555

0.9561 0.7719

0.5561. 0.5570

0.7727

0.9571, 0.9580 0.77350.9583

0.9589

0.771,2

0.9592

0.9598

0.771,9

0.9610

0.5616

0.7761,

0.9628

0.9631. 0.7779

85.". -187.75

2.3 7<»

0.9526

0.9532 0.7696

0.9533 0.9539

0.7702

0.951.1

0.951.7 0.7708

0.951,9 0.9555

0.7711,

0.5556

0.9561. 0.7722

0.9567

0.9571. 0.7730

0.9577 0.9583

0.7737

0.9586

0.9592

0.771.5

0.5601. 0.5610

0.7759

0.9622

0.9628

0.7771,

85.5 -187.65

2.396

0.9519

0.9525

0.7691 0.9527

0.9533

0.7697 0.9535

0.951.1 0.7703

0.951.3

0.951.9 0.7710 0.9552

0.955P 0.7717

0.9561 0.9567

0.7725

0.9571 0.9577

0.7732

0.9580 0.9586

0.771,0 0.9598

0.9601. 0.7755

0.9616

0.9622

0.7769

85.6 -187.55

2.1.19

0.9513

0.9519 0.7666

0.9521 0.9527

0.7692 0.9529

0.9535

0.7698

0.9536

0.951.2 0.7705

0.951,6 0.9552

0.7712

0.9555

0.9561

0.7720

0.9565 0.9571

0.7727

0.9571, 0.9580 0.7735

0.5592

0.9598 0.7750

0.9610

0.9617

0.7761,

85.7

-167.1.5

2.1.1.2

0.9507

0.9513

0.7681

0.9515

0.9521 0.7667 0.95230.9529

0.7693

0.9530

0.9536 0.7700

0.951.0

0.951,6 0.7707

0.951.9 0.9555

0.7715

0.9559

0.9565

0.7723

0.9568

0.9571, 0.7730

0.9586

0.9593

0.771.5

0.9605

0.9611 0.7760

85.8 -187.35

2.1.65

0.9501

0.9507 0.7676

0.9509

0.9515

0.7682 0.9516

0.9522 0.768B

0.9521. 0.9530

0.7695

0.5531.

0.951.0 0.7702

0.951.3 0.951.9 0.77100.9553 0.9559

0.7718

0.9562

0.9568 0.7725

0.5581

0.9587

0.771,0

0.9599

0.9605 0.7755

85.9 -167.25

2.<tB9

0.91.95 0.9501

0.7671

0.9502

0.95 8 0.7677 0.9510 0.9516

0.7683

0.9518

0.5521, 0.769B

0.5526

0.5531. 0.7698

0.9537

0.951.3 0.7705

0.951.7 0.9553

0.7713

0.9556

0.9562

0.7720 0.5575

0.9581

0.7735

0.9593

0.9599

0.7750

86.0 -187.15

2.512

0.91.88

0.91.91. 0.7666

0.91.96 0.9502

0.7672

0.9501, 0.9510

0.7678

0.9512

0.9518

0.7685

0.5522

0.9526 0.7693

0.9531

0.9537

0.7700

0.95U1

0.951.7 0.7708

0.9550 0.9556

0.7716

0.5569

0.9575

0.7731

0.9587

0.9593

0.771,5

66.1 -167.05

2.536

0.9<t82 0.91.66 0.7661

0.91.90

0.91.96 0.7667

0.91.98

0.9501. 0.7673

0.9506

0.5512

0.7680

0.9515

0.5521

0.7696

0.9525

0.9531 0.7695

0.9535

0.951.1 0.7703

0.951,1, 0.9550

0.7711

0.9563 0.9569

0.7726

0.9581 0.9567

0.771,1

86.2 -166.95

2.560

0.91.76 0.91.82 0.7656

0.91.81. 0.91.90 0.7662

0.91.92

0.91.96 0.7668

0.9500 0.9506 0.76750.9509

0.5515 0.7683

0.9519

0.9525

0.7690

0.9529

0.9535

0.7698

0.9536 0.95m

0.7706

0.9557

0.9563

0.7721

0.9575

0.9581 0.7736

86.3 -166.85

2.58".

0.91.69

0.91.75 0.7651

0.91.77

0.91.81. 0.7657

0.91.65

0.91.91 0.7663

0.91,93

0.51.99 0.7670

0.5503

0.9509

0.7678

0.9513

0.9519 0.7666

0.9522 0.9528

0.7693

0.9532

0.9538

0.7701

0.9551 0.9557

0.7716

0.9569 0.9575

0.7731

86.". -166.75

2.606

0.91.63

0.91.69

0.761.5

0.91.71

0.91.77 0.7652

0.91.79

0.51.85 0.7658

0.91.87 0.91.93 0.76650.91.97 0.5503

0.7673

0.9507

0.9513

0.7681

0.9516

0.9522

0.7686

0.9526

0.9532 0.7696

0.951,5 0.5551

0.7711

0.9563

0.9569

0.7726

86.5 -186.65

2.633

0.91.57

0.91.63 0.761.0

0.91.65

0.91.71 0.761.7

0.91.73 0.91.79 0.765J0.51.81

0.91.87 0.7660

0.51,91 0.51.97 0.7666

0.9501

0.9507 0.7676

0.9510

0.9516

0.7681.

0.9520 0.9526

0.7691

0.9539

0.951.5 0.7707

0.9558

0.9561, 0.7722

86.6 -166.55

2.657

0.91.51 0.91.57 0.76350.91.59

0.91.65 0.761,2

0.91.67

0.91.73

0.761.8

0.91.75 0.91.81 0.76550.91.85 0.7663

0.91.91. 0.9501

0.7671

0.9501. 0.9510 0.76790.9511. 0.9520 0.76860.9533

0.9539

0.7702

0.9552

0.9556 0.7717

86.7

-166.1.5 2.682

0.91.1.1. 0.91.50 0.7630

0.91.52

0.91.58 0.7637

0.91.61

0.91.67

0.761.3

0.91.69

0.91.75 0.7650

0.91,79

0.91.85 0.765P

0.91.88

0.91.9H 0.7666

0.91.98

0.9501.

0.7671.

0.9508

0.9511, 0.7681

0.9527

0.5533

0.7697

0.951,6 0.9552 0.7712

66.8 -166.35

2.707

0.91.38

0.91.1.11 0.7625

0.91.1.6 0.91.52 0.7632

0. 91,51, 0.91.68 0.7638

0.91.62

0.91.68 0.761.5

0.91.72 0.91,76 0.76530.91,82 0.9U66 0.7661

0.91.92 0.91.98 n.76690.9502

0.9508 0.7677

0.9521 0.9527

0.7692

0.951.0 0.951,6 0.7707

86.9 -166.25

2.732

0.91.32

0.91.38 0.7620

0.91.1.0 0.91.1.6 0.7627

0.91.1.8

0.91.51. 0.7633

0.91,56

0.91.62

0.761.0 0.91.720.761.6

0.91.76 0.91.62 0.76560.91.86

0.7661. 0.9502 0.7672

0.9515 0.5521

0.7687

0.9531,

0.951.0 0.7703
DENSITY OF CCKFRESSEC LIQUIt

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY

2. OENSITY

3. OENSITY

RATIO, LIQUID OENSITY/CENSITY AT A RATIO, LIQUID OENSITY/DENSITY AT A

, KG/01" 3 BOILING BOILING

PRESSURE PRESSUPFCF 1 9AR, OIMESSIC

0^ 760 TCRR, OIKEK NLESS SICNLESS

BAR 0.800 1.000 2.000 "..000 KP/CM? 0.816 1.020 2.039 4.079

6.000

6.118

8.000

8.158 10.000

10.197 12.500

12.71.6 15.000

15.296

17.500 20.394 25.000 25.493

30.000

30.591

87.0 -186.15

2.757

0.91.25

0.91.31 0.7615

0.91.31.

0.91.1.0 0.7622

0.91. 1.2 0.91.1,8 0.7628

0.91.50

I.9"i56 1.7635

0.546C

0.91.66 0.761.3

0.91.70 0.91.76 0.76510.5480

0.9486

0.7659

0.9490

0.9496 0.7667

0.9509

0.9515 0.7682

0.9528

0.9534

0.7698

87.1 -186.05

2.783

0.91.19

0.91.25 0.7610

0.91.27

0.91.33 0.7616

0.91.36

0.91.1.8 0.7623

0.91.1.1. 0.91.50 0.7630

0.91.51. 0.91.60 0.7638

0.9*6i.

0.91.70 0.761.6

0.9474

0.9480

0.7654

0.9484

0.9490

0.7662 0.9503

0.9505

0.7678

0.9522

0.9528 0.7693

87.2 -185.95

2.808

0.91.13

0.91.19 0.7605

0.91.21 0.91.27 0.76110.91.29

0.91.35 0.7618

0.91.37

0.91.1.3 0.7625

0.9". "(8 0.51.51. 0.7633

0.91.58 0.9464

0.761.1

0.9468 0.9474

0.7649

0.9477

0.9483

0.7657 0.9497

0.5503

.7673

0.9516 0.9522

0.7688

87.3 -165.85

2.831.

0.91.06

0.91.12 0.7600

0.91.15

0.91.21 0.7606

0.91.23

0.91.29 0.7613

0.91.31 0.91.37 0.76200.91.1.1

0.51.1.7 0.7628

0.9451

0.91.57 0.7636

0.9461 0.9467

0.7644

0.9471

0.9477

0.7652 0.5491

0.9497

0.7668

0.9510

0.9516

0.7683

87.1. -185.75

2.860

0.91.00 0.91.06

0.7591.

0.91.08

0. 91.11. 0.7601

0.91.17

0.91.23 0.7608

0.91.25

0.91.31 0.7615

0.91.35

0. 91.1.1 0.7623

0.91.1.5 0.91.51 0.7631

0.9455

0.9461

0.7639

0.9465

0.9471 0.7647 0.9485

0.9491

0.7663

0.9504

0.9510 0.7679

87.5 -185.65

2.886

0.9391.

0.91.00 0.7589

0.91.02

0.91.08 0.7596

0.91.10

0. 91.16 0.7603

8.91.19

0.51.25 0.7609

0.51,29

0.91.35 0.7618

0.91.39

0.91.1.5 0.7626

0.9449

0.9455

0.7634

0.9459

0.9465

0.7642 0.9475

0.9485

0.765e

0.9498 0.9504 0.7674

87.6 -185.55

2.912

0.9387

0.9393

0.7581.

0.9396

0.91.02 0.7591

0.91.01. 0.91.10 0.75980.91.12 0.941B

0.7601.

0.91.23 0.51.25 0.7613

0.91.33

0.91.39 0.7621

0.9443 0.9449 0.76290.9453

0.9459

0.7637

0.9473 0.9479

0.7653

0.9492

0.9498

0.7669

87.7

-185.1.5 2.939

0.9381 0.9387

0.7579

0.9389

0.9395 0.7586 0.5398

0.91.01. 0.7593

0.91.06

0.91.12 0.75990.91.22 0.7608

0.91.27

0.91.33 0.7616

0.9437

0.9443

0.7624 0.9447

0.9453

0.7632 0.9467

.9473 0.7648

0.9486

0.9492 0.7664

87.8 -185.35

2.965

0.9371. 0.9380

0.7571.

0.9383

0.9389

0.7581 0.9391

0.9397

0.7587

0.91.00

.91.06 0.7591.

0.51.1C 0.9416 0.7603

0.91.20

0.91.26 0.7611

0.9437 0.94410.9447

0.7627 0.9467 0.7643

0.9480

0.9486 0.7659

87.9 -165.25

2.992

0.93E8

0.9371. 0.7569

0.9377

0.9383

0.7576 0.9385

0.9391

0.7582

0.939". 0.9399

0.7589

0.91.01. 0.51.10 0.7598

0.91.11. 0.91.20 0.7606

0.9424

0.9430 0.7614

0.9435 0.9441

0.7522 0.9455

0.5461 0.7639

0.9474 0.9480 0.7654

88.0 -165.15

3.019

0.9362

0.9368

0.7563

0.9370 0.9376

0.7570

0.9379

0.9385

0.7577

0.9387

0.9393

0.7581.

0.9396

0.91.01. 0.7593

0.9409

0. 91.11. 0.76C1

0.9424 0.7609

0.9434

0.7617

0.9449

0.9455

0.7634

0.946e 0.9474

O.7650

88.1 -185.05

3.01.6

0.9355

0.9361 0.7558

0.9361. 0.9370

0.7565 0.9372

0.9378 0.7572

0.9381

0.9387

0.7579 0.5391 0.53970.7587

0.9402

0.9408

0.7596

0.9412 0.9418

0.7604

0.9422

0.9428 0.7612

0.9442

0.9448

0.7625

0.9462

0.946e

0.7645

88.2 -184.95

3.071.

0.931.9 0.9355 0.75530.9357

0.9363 0.7560

0.9366

0.9372

0.7567

0.9375

0.9381

0.7571.

0.9385 0.5391 0.75820.9396

0.9402

0.7591 o!?599

0.9416

0.9422 0.7607 0.9436

0.9442

0.7624

0.9456

0.9462

0.7640

88.3

-18".. 85 3.101

0.931.2

0.93li8

0.751.8

0.9351

0.9357 0.7555

0.9360

0.9366 0.7562

0.9368

0.9371. 0.7569

0.5375

0.9385 0^7577

0.9389

0.9395

0.7566

0.9400 0.9406

0.7594

0.9410

0.9416 0.7602 0.94300.9436 0.7619

0.9450

0.9456 0.7635

88.1. -181.. 75 3.1290.9336

0.931.2

0.751.3

0.931.5 0.9351

0.7550

0.9353

0.935= 0.7557

0.9362

0.9368

0.7561. 0.937?

0.537e

0.757?

0.9383

0.9389 0.7581

0.9394

0.9399

0.7589 0.9404

0.9410 0.7598 0.94240.5430 0.7614

0.9444

0.9450 0.7630

88.5

-18".. 65 3.157

0.9329

0.9335

0.7537

0.9338 0.93m.

0.751.5

0.931.7 0.9353

0.7552

0.9356 0.9361

0.7558

0.5366 0.9372

0.7567

0.9377 0.9383

0.7576

0.9387 0.9393 0.75840.9398

0.9404

0.7593

0.5418

0.9424

0.7609

0.9438 0.9444

0.7625

88.6

-181.. 55 3.185

0.9323 0.9329

0.7532

0.9332

0.9338

0.7539

0.931.1

0.931.6 0.75h6

0.531.9 0.9355

0.7553 0.9360

0.9366 -0.7562

0.9371 0.9376

0.7571

0.9381 0.75790.9391

0.9397 0.7588 0.94120.9418 0.7604

0.9432

0.9438 0.7620

86.7 -18*. US 3.213 0.9317

0.9322 0.7527

0.9325

0.9331

0.7531.

0.9331.

0.931.0

0.751.1

0.931.3

0.931.9 0.751.8

0.9351. 0.536C

0.7557

0.9364

0.9370

0.7566

0.9375 0.9381

0.7574

0.9385

0.9391

0.7583 0.94120.7599

0.9426

0.943? 0.7615

88.8

-181.. 35

3.21.2

0.9310

0.9316 0.7522

0.9319

0.9325

0.7529

0.9328

0.9331. 0.7536

0.9336

0.931.2

0.751.3

0.5347 0.9353

0.7552

0.9358 0.9364

0.7560

0.9369

0.9375

0.7569

0.9379 0.9385

0.7577

.5400 o!75940.9420 0.9426

0.7611

88.9

-181.. 25 3.270

0.9301. 0.9309 0.75160.9312

0,9318

0.7521.

0.9321

0.9327

0.7531

O.9330

0.9336 0.7538

0.531.1 0.931.7

0.751.7

0.9352

0.9358 0.7555

0.9362

0.9368

0.7564

0.9373

0.9379 0.7572

0.9394

0.9400

0.7589

0.9414

0.9420 0.7606
DENSITY OF CCMPRESSEC

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO, I RATIO, I

, KG/OM3

IOUID OENSITY/OENSITY AT A IQUIO OENSITY/0ENSITY AT A BOILING BOILING

PRESSURE

PRESSURE

OF 1 9AR, OIMENSICNLESS

OF 760 TCRR, OIMENSICNLESS

BAR 0.800 1.000 2.000 "..000 KP/CM2 0.616 1.020 2.039 4.079

6.OO0 6.118

e.000 8.158

10.000

10.197 12.500

12.71.6 15.000

15.296

17.500

17.81.5 20.00020.391. 25.00025.1.93 30.000

30.591

89.0

-181.. 15 3.299

0.9297

0.9303

0.7511

0.9306

0.9312

0.7518

0.9315

0.9321 0.7526

0.9321. B.9?30

0.7533

0.9335

0.531.1 0.751.2

0.931.5 0.9351 0.7550

0.9356

0.9362 0.7559

0.9367

0.9373

0.7567

0.9387

0.5393

0.7581.

0.9406

0.9414

0.7601

89.1

-18".. 05

3. 326

0.9291

0.9296 0.7506

0.9300

0.9305 0.7513 0.9306

0.9311. 0.7520

0.9317

0.9323

0.7528 0.9328

0.5331. 0.7536

0.9339

0.931.5 0.751.5 0.9350

0.9356

0.7551. 0.9360 0.9366

0.7562 0.9361

0.9367

0.7579

0.9402

0.9408 0.7596

89.2 -163.95

3.357

0.9261. 0.9290

0.7501

0.9293

0.9299

0.7508 0.9302

0.9308 0.7515

0.9311

0.9317 0.7522

0.932?

0.5328 0.7531

0.9333

0.9339

0.751.0

0.931.1. 0.931.9 0.751.9

0.9351. 0.9360

0.7557 0.9375

0.9381

0.7571.

0.9396

0.9402

0.7591

69.3 -183.85

3.387

0.9277

0.9263

0.71.95

0.9287

0.9292

0.7503 0.9296

0.9301

0.7510

0.9301. 0.9310

0.7517

0.9316

0.5321 0.7526

0.9326

0.9332 0.7535

0.9337

0.931.3

0.751.1.

0.931,8 0.9351. 0.7552

0.9369

0.5375 0.7569

0.9390 0.9396

0.7586

89.". -183.75

3.1.16

0.9271

0.9277

0.71.90

0.9280 0.9286

0.71.98 0.9269

0.9295

0.7505

0.9298

0.9301. 0.7512

0.9309 0.5315

0.7521

0.9320

0.9326

0.7530

0.9331

0.9337

0.7539

0.931.2 0.931,8

0.751,7

0.9363

0.5369

0.7561.

0.9384

0.9390

0.7561

89.5 -183.65

3.1.1.6

0.9261. 0.9270

0.71.85

0.9271. 0.9279

0.71.92 0^92690.7500

0.9292

0.9298

0.7507 0.9303 0.930?0.7516

0.9311. 0.9320

0.7525

0.9325

0.9331

0.7531.

0.9335

0.931.1 0.75*2

0.9357

0.9363

0.7559

0.9378

0.9384 0.7576

89.6 -163.55

3.1.76

0.9258

0.9261.

0.71.80

0.9267

0.9273

0.71.87 0.9282

0.71.91.

0.928S

0.9291 0.7502

0.9296

0.7511

0.9307

0.9313

0.7520

0.9316

0.9321. 0.7528

0.9329

0.9J35 0.7537

0.9351 0.9356

0.7551.

0.9371 0.9377

0.7571

89.7

-163.1.5 3.506

0.9251 0.9257

0.71.71.

0.9261

0.9266

0.71.82

0.9270

0.9276

0.71.89

0.9279

8.9285

0.71.96

0.529C

0.9296

0.750E

0.9301

0.9307

0.7511.

0.9312

0.9318 0.7523

0.9323

0.9329

0.7532

.9344, 0.9350

0.751.9

0.9365

0.9371 0.7566

89.8 -183.35

3.536

0.921.5 0.9251

0.71.69

0.9251. 0.9260

0.71.76 0.9263

0.92E9

0.9272 0.9278

0.71.91

0.5261

0.5289

0.750C

0.9295

0.9301 0.7509

0.9306 0.9312

0.7518

0.9317

0.9323

0.7527

0.9336

0.934,1.

0.751.1.

0.9359

0.9365

0.7561

89.9 -183.25

3.567

0.9238

0.921.1. 0. 71.61.

0.921.7 0.9253

0.71.71

0.9257 0.9263

0.71.79

0.9266

0.9272

0.7U86

0.5277 0.5283

0. 71.9S

0.9286 0.9294

0.7501.

0.9299

0.9305

0.7513

0.9310

0.9316 0.7522 0.9332

0.5338 0.7539

0.9353

0.9359 0.7557

90.0 -183.15

3.596

0.9232

0.9237

0.71.58

0.921.1 0.921.7

0.71.66

0.9250 0.9256

0.71.73

0.9259 0.9265

0. 71.81

0.9271

0.5277

0.71.90

0.9262

0.92e8

0.71,99

0.9293 0.5299

0.7S08

0.9301. 0.9310 0.7517

0.9326

0.9332

0.7531.

0.9347

0.9353

0.7552

90.1 -183.05

3.629

0.9225

0.9231

0.71.53

0.9231.

0.921.0

0.71.61

0. 921.1. 0.921.9

0.71.68

0.9253

0.9259

0.71.76

0.5261.

0.71.85

0.9276

0.9281

0.9287 0.9293

0.7503

0.9296

0.9301. 0.7512

0.9320

0.9325

0.7529

0.9341 0.9347

0.7547

90.2 -182.95

3.660

0.9218

0.9221.

0.71.1.6

0.9226

0.9231. 0.71.55

0.9237

0.921.3

0.71.63 0.9252

0.71.70

0.525e

0.5261.

0.71.8

0.9269

0.9275

0.71.69

0.9280

0.5286

0.9291

0.9297

0.7507

0.9313

0.9319

0.7521.

0.9335

0.9341 0.7542

90.3 -182.85

3.691

0.9212 0.9218

0.71.1.2 0.9221

0.9227

0.71.50

0.9231 0.9236

0.71.57

S. 921.0 0.921.6 0.71.65

0.5251 0.5257

0.71.71.

0.9263

0.9269

0.71.83

0.9271. 0.9280

0.7i.°3 0.9285

0.9291 0.7502

0.5307

0.9313 0.7519

0.9329

0.9334 0.7537

90.1. -162.75

3.722

0.9205

0.9211

0.71.37

0.9215

0.9220

0.71.1.5

0.9221. 0.9230

0.71.52

0.9233

0.9239

0. 71.60

0.5245

0.5251

0.71.69

0.9256

0.9262

0.71,7*

0.9266 0.9273

0.71.87

0.9279 0.9265

0.71.96 0.9301

0.5307

0.7514

0.9322

0.9328

0.7532

90.5 -182.65

3.751.

0.9198

0.9201.

0.71.32

0.9208

0.9211.

0.71.39

0.9217

0.9221

0.71.1.7

0.9227

0.9233

0.71.5I.

0.5238

0.921.1. 0.9250

0.9256

0.71.73

0.9261 0.9267

0.71.82

0.9272

0.9278

0.71.91

0.9295

0.9300 0.7509

0.9316

0.9322

0.7527

90.6 -162.55

3.786

0.9192

0.9196

0.71.26

0.9201 0.9207

.74.31.

0.9211 0.9217

0.71.1.2

8.9220

0.9226

8 .71.1.9 0.5232

0.5238

0.71.55

0.921.3

0.71.68

0.9255

0.9261

0.71.77

0.9266

0.9272

0.71.86

0.5268

0.9294 0.7504

0.9310 0.9316

0.7522

90.7

-162.1.5 3.818

0.9185

0.9191

0.71.21

0.9195

0.9201

0.71.29

0.9201. 0.9210

0.71.36

0.9211. 0.9220

0.71.1.1.

0.5225

0.5231

0.71.53

0.9237

0.921.3 0.71.63

0.921.8 0.9251. 0.9260

0.9266

0.71.81

0.9282

0.9288 0.7499

0.9304

0.9310 0.7517

90.8 -ie2.35

3.850

0.9176

0.9181. 0.7*15

0.9188

0.9191. 0.71.23

0.9196 0.9203

0.71.31

0.9207

0.9213

0.71.39

0.5215

0.5225

0.71.1.8

0.9231 0.9236

0.71.57

0. 921.2 0.71.67

0.9253

0.9259

0.71.76

0.9276 0.9282 0.74940.9298 0.9304 0.7512

90.9 -182.25

3.883

0.9172

0.9178

0.71.10 0.9181 0.9187

0. 71.18 0.9191

0.9157

0.71.26

0.9201 0.9206

0.71.33

0.5212

0.5218 0.7443

0.922". 0.9230

0.71.52

0.9236

0.921.1 0.71.62

0.921.7 0.9253

0.71.71

0.9270 0.9275

0.7485

0.9292

0.9297 0.7507
OF CCHPRESSEC LIOUIC NITROGEN t CONTINUEO

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO, LIQUID OENSITY/OENSITY AT A RATIO, LIQUID DENSITY/OE NSITY AT A

, KG/0M3

BCILING PRESSURE

BOILING PRESSURE

" 1 BAR, DIMENSION

F 760 TORR, CIHENS

LESS IONLESS

BAR 0.600 LOGO 2.000 14.000 KP/CM? 0.816 1.020 2.039 "..079 6.118

8.000 6.158 10.000

10.197 12.50012.746

15.000

15.296

17.500

17.845 20.000 20.394 25.00025.493

30.000 30.591

91.0 -162.15

3.916

0.9165 0.9171

0.7405

0.9175

0.9181

0.7412 0.9190

0.7420

0.9194

0.9200 0.7428

0.920f 0.9212

0.7436

0.9218

0.9223

0.7447

0.9229

0.9235

0.7456

0.9241 0.9247

0.7466

0.5263

0.9269

0.9285

0.9291 0.7502

91.1 -182.05

3.9<t9

0.9158

0.9164 0.7399

0.9168

0.9174 0.7407 0.91780.9184

0.7415

0.9187

0.9193

0.7423 0.5199

0.5205

0.7432

0.9211 0.9217

0.7442

0.9223

0.9229

0.7451

0.9234

0.9240 0.7461

0.9257

0.9263 0.7479

0.9279

0.9285 0.7497

91.2 -181.95

3.982

0.9152

0.9157 0.7394

0.9161

0.9167 0.7402

0.9171 0.9177

0.7410

0.9187 0.7417 0.9193

0.5199 0.7427

0.9205

0.9210 0.7437

0.9216

0.9222 0.7446

0.9228 0.9234

0.7455

0.9251 0.9257

0.7474

0.9273

0.9279 0.7492

91.3 -181.85

4.015

0.9155

0.9161 0.7396 0.9165

0.9170 0.7404

0.9174 O.9180

0.7412

0.9186

0.9192

0.7422

0.9198

0.9204

0.7431

0.9210

0.9216 0.7441

0.9221

0.9227

0.7450

0.9244 0.5250

0.7465

0.9267

0.9273

0.7487

91.1. -181.75

4.048

0.9148

0.9154

0.7391 0.9156

0.9164 0.7399

0.9168 0.9173

B.7407 0.5180

0.5186

0.7416

0.9192

0.9197 0.7426 0.9203

0.9209 0.7436

0.9215

0.9221 0.7445 0.92380.9244

0.7464

0.9260

0.9266 0.7482

91.5 -181.65

4.082

0.9141

0.9147 0.7385

0.9151

0.9157

0.7393

0.9161

O.7401

0.9173

0.7411

0.9185

0.9191

0.7421 0.9197

0.9203

0.7430 0.9209

0.9215 0.7440

0.9232

0.9238 0.7458

0.9254

0.9260 0.7477

91,6 -181.55

4.116

0.9135

0.9140 0.7380

0.9145

C.9150 0.7388

0.9154

0.9160 0.7396 0.5172

0.7406

0.9179 0.9184 0.7416

0.9190

0.9196 0.7425

0.9202

0.9208 0.7435

0.9225

0.5231 0.7453

0.9248

0.9254 0.7472

91.7 -181.45

4.150

0.9128

0.9134 0.7375

0.9138

0.9144

0.7383

0.9148

0.9154

0.7391

0.9160

0.9166 0.7400

0.9172 0.9178

0.7410

0.9184 0.9190

0.7420

0.9196 0.9202

0.7429

0.9219

0.5225

0.7448

0.9242

0.9248 0.7467

91.8 -181.35

4.185

0.9121 0.9127

0.7369 0.9131

0.9137 0.7377

0.9141

0.9147

0.7385

0.9153

0.5155

0.7395

0.9166

0.9171 0.74050^9183

0.7415

0.9189

0.9195

0.7424

0.9213

0.9219

0.7443

0.9235

0.9241 0.7461

91.9 -181.25

4.219

0.9114 0.9120

0.7364

0.9124

0.9130 0.7372

0.9134

0.9140

0.7380

0.9147

0.5153

0.7390

0.9159

0.9165

0.7400

0.9171 0.9177 0.74090.9183

0.9189

0.7419

0.9206

0.5212

0.7438

0.9229

0.9235 0.7456

92.0 -161.15

4.254

0.9108

0.9113

0.7358

0.9118

0.9124 0.7366

0.9128 0.9134

0.7374

0.5140

0.5146 0.7384

0.9152 0.9158

0.7394

0.9164

0.7404

0.9176

0.9182

0.71,14

0.9200

0.9206 0.7433

0.9223

0.9229

0.7451

92.1 -181.05

4.289

0.9101 0.9107 0.73530.9111 0.9117

0.7361

0.9121 0.9127 0.7369

0.5134

0.5135 0,7379

0.9146

0.9152 0.7389

0.9158 0.9164 0.73990.9170 0.9176

0.7409

0.9194 0.5195

0.7428

0.9217

0.9223 0.7446

92.2 -160.95

4.324

0.9094

0.9100

0.7347 0.9104

0.9110 0.7355

0.9114

0.9120 0.7364

0.5127 0.5133

0.7374

0.9139 0.9145

0.7384

0.9151 0.91570.9163 0.9169

0.7403

0.5187

0.5193

0.7422

0.9210 0.9216

0.7441

92.3 -180.85

4.359

0.9087

0.9O93 0.7342 0.90960.9103

0.7350

0.9108 0.9113

0.7358

0.5120

0.5126

0.7368

0.9133

0.9138

0.7378

0.9145

0.9151 0.7388

0.9157

0.9163

0.7398

0.9181 0.9187

0.7417

0.9204

0.9210 0.7436

92.4 -180.75

4.395

0.9080 0.9086

0.7336 0.9091

0.9097

0.7345

0.5101 0.9107

0.7353

0.5114 0.9119

0.7363

0.9126

0.9132

0.7373

0.9138

0.9144 0.7383

0.9151

0.9156 0.7393

0.9174

0.9180

0.7412

0.9198

0.9204

0.7431

92.5 -180.65

4.431

0.9074

0.9079

0.7331

0.9084

0.9090 0.7339

0.9094

0.9100 0.7347

0.5107

0.9113

0.7356

0.9119 0.9125

0.7368

0.9132 0.9138

0.'378

0.9144

0.9150 0.7388

0.9168

0.9174

0.7407

0.9191 0.9197

0.7426

92.6 -160.55

4.467

0.9067 0.9073

0.7325

0.9077 0.9063

0.7334

0.9088 0.9093

0.7142

0.5100 0.73520.9113

0.9119

0.7362

0.9125

0.9131 0.7372

0.9137

0.9143 0.7382 0.9167

0.7402

0.9185

0.9191

0.7421

92.7 -180.45

4.503

0.9060

0.9066

0.7320

0.9070

0.9076 0.7328

0.9081

0.9087

0.7336

0.5094

0.9095

0.7347

0.9106

0.9112

0.7357

0.5119

0.9124 0.7367

0.9131

0.9137 0.7377

0.9155

0.5161

0.7397

0.9179

0.9185 0.7416

92.6 -ieo.35

4.540

0.9053

0.9059

0.7314

0.9064

0.9069

0.7323

0.9074

0.9080

0.7331

0.9087 0.5093

0.7341

0.9100

0.9105 0.7352

0.9112

0.9116 0.7362

0.9124 0.9130

0.7372

0.9149 0.9155

0.7391

0.9172 0.9178

0.7411

92.9 -160.25

4.576

0.904E

0.9052

0.7309

0.9057

0.9063

0.7317

0.9067

0.5073

0.7326

0.9080

0.5086 0.7336

0.9O93

0.9TJ99 0.7346

0.9105

0.9111 0.7356

0.9118 0.9124

0.7366

0.9142

0.9146 0.7386

0.9166

0.9172

0.7405
DENSITY Of COMPRESSED LIQUID NITROGEN - CONTINUE:

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATLRE, C

3. VAPOR PRESSURE, BAR

1. OENSITV RATIO, LIQUID OENSITY/CENS

2. OENSITY RATIO, LIQUIO OENSITY/OEN 5 3. DENSITY, KG/Df-3

ITY AT A ITY AT A BOILING PRESSURE

BOILING PRESSURE

OF 1 9AR,

OF 760 TC OIMENSICNLESS

»R, OIMENSICNLESS

BAR 0.600 1.000 2.000 "..000 6.000 KP/CM 2 0.816 1.020 2.039 "..079 6.118 s!l58

10.000

10.197 12.500 12.746

15.000

15.296

17.500

17.845 20.000

20.394 25.000 25.493

30.000 30.591

93.0 -180.15

4.613

0.9039

0.90"45 0.7303 0.9050

0.9056

0.7312

0.9060

0.9066 O.7320

0.9073

0.9079

0.7331

0.9086

0.9092

0.9099

0.9105

0.7351

0.9111 0.9117

0.7361

0.9136 0.9142

0.7381

0.9166

0.7400

93.1 -180.05

<4.650

0.9032

0.9038 0.7297

0.90".3 0.9049

0.7306

0.9054

0.9059 0.7315 0.5067

0.9072 0.7325

0.9060

0.9085 0.7335

0.9092 0.9098

0.7346

0.9105 0.9111 0.73560.9129

0.9135 0.7376

0.9153

0.9159 0.7395

93.2 -179.95

it. 688

0.9026

0.9031 0.7292

0..9036 0.90"42 0.73010. 9047 0.9053 0.73090.9060

0.5066 0.7320

0.9073

0.9079

0.7330

0.9096

0.9091

0.7340

0.9098

0.9104 0.7351

0.9123

0.9129

0.7371

0.9147

0.9153

0.7390

93.3 -179.85

"..725

0.9019

0.902"4 0.7286

0.9029

0.9035 0.7295

0.9040

0.9046

fl.7304

0.5053

0.5055

0.7314

0.9066 0.9072

0.7325

0.9079

0.9085

0.7335

0.9092

0.9097

0.7345

0.9116

0.9122

0.7365

0.9141 0.9146

0.7385

93.4 -179.75

"4.763

0.9012

0.9017

0.7281

0.9023

0.9028

0.7269

0.9033

0.9039

B.7298

0.5046 0.9052

0.7309

0.9059

0.9065

0.7319

0.9072

0.9078

0.7330

0.9085

0.9091 0.7340

0.9110

0.9116 0.7360

0.9134

0.9140 0.7380

93.5 -179.65

"4.801

0.9005

0.9011 0.7275 0.90160.9021

0.728",

0.9026

0.9032

0.7293

0.5040

0^5045 0.7303

0.9053

0.9058

0.7314

0.9066 0.9071

0.7324

0.9078

0.9084 0.7335

0.9103

0.9109 0.7355

0.9128

0.9134 0.7375

93.6 -179.55

0.639

0.8998

O.9O0"4 0.7270 0.9009

0.7278

0.9020 0.9025

0.7267

0.9033

0.9039

0.729e

0.9046

0.9052

0.7308

0.9059

0.9065

0.7319

0.9072

0.9078 0.7329

0.9097

0.9103 0.7350

0.9121 0.9127 0.7369

93.7

-179. "45 "4.877

0.8991 0.8997

0.726"4 0.9002

0.9008

0.7273

0.9013

0.9018

0.7281

0.5026

0.5032

0.7292

0.9039

0.9045

0.7303

0.9052

0.9058

0.7313

0.9065

0.9071 0.7324

0.9090 0.9096

0.7344

0.9115

0.9121 0.7364

93.8 -179.35

"4.916

0.898"4 0.6990

0.7258

0.8995

0.9001

0.7267

0.9012

i.7?76

0.5015

0.5025

0,7287

0.9033

0.9038

0.72 = 8

0.9046

0.9051

n.7306 0.9059

0.9064

0.7319

0.9084 0.9090

0.7335

0.9109

0.9114 0.7359

93.9 -179.25

"4.955

0.8977

0.8983 0.7253

0.6986

0.899"4 0.7262

0.6=99

0.9005

0.7270

0.5012

0.5018

0.7251

0.9026

0.9031 0.7292

0.9039

0.9045

0.7303

0.9052

0.9058

0.7313

0.9077

0.9083

0.7334

0.9102

0.9108 0.7354

9"4.0 -179.15

"4.99<4

0.8970 0.8976

0.7247 0.69670.7256

0.6992

0.6996

0.7265

0.5006

0.727E

0.9019

0.9025 0.72e7

0.5032 0.9038

0.72°7

0.9045

0.9051

0.7308

0.9071

0.9077 0.7328

0.9096

0.9102 0.7349

9<4.1 -179.05

5.033

0.6963

0.6969

0.721.1

0.897"4 0.8980

0.7250

0.8965 0.8991

8.7259

0.6995

0.5004

0.727C

0.9O12

0.9018

f.7281

0.9025

0.9031 0.7292

0.9039

0.9044

0.7302

0.9064

0.9070 0.7323

0.9089

0.9095 0.7343

9"4.2 -178.95

5.073

0.8956 0.8962

0.7236

0.8967

0.8973

0.72"45

0.8978 0.6964

0.7254

0-e992 0.8?9e

0.7265

0.9005

0.9011

0.7276

0.901°

0.9024 0.7286

0.9032

0.9038 0.7297

0.9058 0.5063

0.7316

0.9083 0.9089

0.7338

9<4.3 -178.65

5.113

0.8949

0.8955

0.7230 0.6960

0.6966

0.7239

8.8971

0.8977

0.7248

0.8985

0.8991

0.7251:

0.8955

0.9004

0.7270

0.9112 0.9018

0.7261

0.9025

0.9031

0.7292

0.5051 0.9057

0.7313

0.9082

0.7333

94.4 -178.75

5.153

0.6942

0.6947

0.722"4 0.8953 0.6959

0.7233

0.8964

0.6970

0.7242

0.897e

0.6984

0.7254

0.8992

0.8997

0.7265

0.5005

0.9011

0.7275

0.9019 0.9024

0.9045 0.5050

.7307

0.9070 0.9076 0.7328

9<4.5 -178.65

5.193

0.8935

0.89"40 0.721?

0.691.6 0.8952

0.7228

0.6957

0.6963

0.7237

0.8971 0.8977

0.724C

0.8985

0.8991

0.72=5

0.3998

0.9004

0.7270

0.9012

0.9018

0.7281

0.9038

0.9044 0.7302

0.9063 0.9069

0.7323

9"4.6 -178.55

5.233

0.8928

0.8933

0.7213 0.6939

0.89".5 0.7222

3.8950

0.8956

0.7231

0.6964

0.8970

0.7242

0.8978 0.6964

0.7254

0.8992

0.9997

0.7265

0.9005

0.9011 0.7275

0.5031 0.5037

0.7257

0.9057 0.9063

0.7317

9"4.7 -178. "45 5.27".

0.8921

0.8926 0.7207

0.8932

0.6938

0.7216

0.6943

0.e949

0.7226

0.6957

0.7237

0.6971 C.6977

0.7248

0.89H5 0.8991

0.7259

0.8998 0.9004

0.7270

0.5025 0.5030

.7291

0.9050 0.9056

0.7312

9<4.8 -178.35

5.315

0.8913

0.8919

0.7201

0.6925

0.8931

0.7211

0.8936

0.8942

8.7220

0.6951 0.8956

0.7231

0.6964

0.8970

0.7242

0.S976

0.9984

0.7254

0.6992

0.8997 0.7264

0.5018 0.9024

0.7286

0.9044

0.9050

0.7307

9"».9 -178.25

5.356

0.8906

0.7196 0.8918

0.892"4 0.7205

0.8929

0.8935 0.7214

0.8944 0.6945

0.7226 0.8963

0.7237

0.8971

0.3977

0.7248

0.8965 0.9991

0.7259

0.9011 0.9017

0.7261

0.9037

0.9043
TABLE 8 - CCNTINUEC DENSITY OF COMPRESSBC LIQUID NITROGEN r COr.

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. OENSITY RATIO,

2. OENSITY RATIO,

3. DENSITY, KG/OM3 LIQUID OENSITY/OEN

LIQUID OENSITY/OEN

SITY AT A SITY AT A BOILING

eCILTNG PRESSURE

PRESSURE

OF 1 BAR, OIMENSIC

OF 760 TCRR, CIMEK NLESS SIONLESS

BAR 0.800 1.000 2.000 1..000 6.000 KP/CM* 0.816 1.020 2.039 1..079 6.118

8.000 6.158

10. 000 10.197 12.500

12.71.6 15.000

15.296

17.500

17.81.5 20.00020.391. 25.00025.1.93 30.000

30.591

95.0 -178.15

5.397

0.8699

0.8905 0.7190 0.89110.8917

0.7199

B.6922

0.8928 0.7209

0.8937

0.691.2 0.7220

0.6951 0.8956

0.7231

0.9961. 0.8970

0.721.3

0.8978

0.8981. 0.7251.

0.9005

0.9011 0.7275

0.9031

0.9037 0.7296

95.1 -178.05

5.1.39 0.8692

0.8898

0.7181.

0.8901* 0.6909

0.7191.

0.8915 0.8921 8.72030.6930 0.6935

0.721L

0.891.1. 0.891.9 0.72260.8956 0.3963

0.7237

0.8971 0.8977

0.721,8 0.6S98

0.9001. 0.7270

0.9021. 0.9030

0.7291

95.2 -177.95

5.1.81 0.8885

0.8891 0.7178 0.88970.8902

0.7188

0.S508

0.89H. 0.7197

0.6923

0.8928 0.7209

0.8937

0.891.3 0.7220

0.6951 0.8956

0.7231

0.8965

0.8970

0.721,3 0.6592

0.6997

0.7261.

0.9018

0.9021. 0.7286

95.3 -177.85

5.523

0.8878 0.8883

0.7172

0.8890 0.8895 0.7182O.8901

0.6907

0.7191

0.6916 0.8921

0.7203

0.8930

0.8936 0.7215

0.391.1. 0.9950

0.7226

0.8958 0.8963 0.72370.6985

0.8991 0.725?

0.9011

0.9017 0.7280

95.1, -177.75

5.565

0.8671 0.8876

0.7167 0.8882 0.6888

0.7176

0.8891. 0.8900 0.7186

0.8909

0.8911. 0.7197

0.6923

0.8929

0.7209

0.9937

0.391.3 0.7220

0.8951

0.8957 0.7232

0.6978

0.7251.

0.9005

0.9010 0.7275

95.5 -177.65

5.608

0.8663

0.8869

0.7161 0.8875

0.8861 0.7170

0.8887 0.6893

0.71B0 0.8902

0.8907 0.7192

0.8916

0.8922 0.7203

0.9930

0.3936

0.7215

0.89l>l| 0.8950 0.7226

0.8972 0.8977

0.721.8

0.6998

0.9001. 0.7270

95.6 -177.55

5.650

0.6856

0.8862 0.7155

0.8871. 0.7165

0.8880

0.8866

0.7171, 0.6895

0.6900

0.7186

0.8909

0.8915 0.7198

0.9923

0.9929

0.7209

0.8937

0.891.3 0.7221 0.89650.8970

0.721.3

0.8992 0.8997

0.726K

95.7

-177.1.5 5.693

0.881.9 0.8855

0.711.9

0.8861

0.8867

0.7159

0.8873

0.6679

0.7169

o.eeae

0.6893 0.7180

0.8902

0.6906 0.7192

0.1916

0.8922

0.7201.

0.8931

0.8936

0.7215

o.e?5e

0.8961. 0.7237

0.8985

0.8991 0.7259

95.6 -177.35

5.737

0.881.2 0.861.7

0.711.3

0.8851. 0.8859 0.7153

0.8866

0.8871 0.7163

0.6881

0.6886

0.7175

0.8895

0.8901

0.7167

0.8910 0.8915

0.7198

0.8921. 0.8929 0.7210

0.6951 0.8957

0.7232

0.8978

0.8981. 0.7251.

95.9 -177.25

5.780

0.8831.

0.861.0 0.7137

0.881.7

0.711.7

0.8859

0.6861. 0.7157

0.8871. 0.687?

0.7169

0.8386

0.8891. 0.7iei

0.8903

0.9906 0.7193

0.8917

0.9922

0.7201,

0.891.5 0.8950 0.7227

0.8972

0.9977

0.721.8

96.0 -177.15

5.821,

0.8627

0.8833

0.7132

0.8839

0.861.5

0.711.1

0.6852

0.8857

0.7151

0.8866 0.8672

0.7163

0.8881

0.8887 0.7175

0.8896

0.8901 0.7187

0.8910

0.8916

0.7198

0.8938

0.691.1. 0.7221

0.8965

0.8971

0.721.3

96.1 -177.05

5.668

0.8820 0.8825

0.7126 0.8832

0.8838 0.7136

0.861.1. 0.8850

0.711.5 0.6855

0.e665 0.7156

0.8671. 0.8860

0.7170

0.9899

0.8891. 0.8903

o!7193

0.8931 0.6937

0.7216

0.8958

0.B961. 0.7238

96.2 -176.95

5.912

0.8813

0.8818

0.7120 0.8825

0.8831 0.7130

0.8837

0.661.3

0.711.0 0.6852

0,e856

0.7152 0.8B67

0.8873

0.7161, 0.9862

0.8887

0.7176

0.8896

0.8902

0.7187

0.e92i< 0.6930

0.7210

0.8952

0.8958 0.7232

96.3 -176.85

5.957

0.8805

0.8811

0.7111. 0.8818

0.8823

0.7121.

0.6830 0.8836

0.7131.

0.881.5 0.8851

0. 711.6 0.8866 0.7156

0.3880 0.88890.8995

0.7182

0.69ie

0.8923

0.7205

0.891.5 0.8951 0.7227

96.1. -176.75

6.001

0.8810 0.8816

0.7118

0.8823

0.8828 0.7128

0.8836

0.681.1. 0.7H.0

0.8853

0.8859

0.7152

0.3868

0*7161. 0.8862

0.8988

0.7176

0.8911 0.7195

0.8939

0.891.1. 0.7222

96.5 -176.65

6.01.6

0.8803

0.8809

0.7112

0.6816

0.8821

0.7122

0.6631 0.6836

0.7135

0.881.6 0.8852

0.711.7

0.3861

0.9866

0.7159

0.8875

0.8381 0.7171

0.6901. 0.8910

0.7191.

0.8932 0.8538

0.7216

96.6 -176.55

6.091 0.8796

0.8801

0.7106

0.8808

0.8811. 0.7116

0.8821. 0.8825

0,7129

0.8839

0.881.1. 0.711.1

0.3851. 0.8859

0.7153

0.8368

0.8971. 0.7165

0.8897 0.6903

0.7188

0.8925

0.8931

0.7S11

96.7

-176.1.5 6.137

.8768

0.8791. 0.7100

0.8807 0.71U

o.eei7 0.6822

0.7123

0.B832 0.8837

0.7135

0.881.7 0.9852

0.711.7 0.9962

0.8867

0.7159 0.88960.7183

0.8918

0.8921. 0.7205

96.8 -176.35

6.182

0.8761 0.8787 0.6799

0.7105

0.680? 0.7117

0.8B25

0.8830

0.7130

0.981,5

0.711.2

0.8855

0.8860

0.7151,

0.6681. 0.8889

0.7177

0.8912 0.8917

0.7200

96.9 -176.25

6.228

0.677H

0.8779 0.7088

0.6767

0.8792

0.7099

0.6802

0.7111

0.8818 0.8823

0.7121.

0.9833

0.8638

0.7136

0.891.8 0.9953

0.711.8

0.8877 0.8682

0.7172

0.8905

0.8911 0.7195
(DENSITY OF COKPRESSEC LIOUIC NITROGEN - CONTTNUFO

TABLE ENTRIES

1. TEMPERATLRE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUID OENSITY/OENSITY AT A 2. DENSITY RATIO, LIQUIO BENSITY/DENSITY AT A 3. DENSITY, KG/DM*

BOILING PRESSURE OF 1 BAR, OIMENSICNL ESS BOILING PRESSURE OF 761) TCRR, OIMEInSIONLESS

GAR 11.800 1.000 2.000 i. . 6.000 6.000 KP/CM2 0.816 1.020 2.039 "..079 6.116 8.156 10^197 12.500

12.7U6 15.800

15.296

17.500 20.000

20.391, 25.00025.1.93 30.00030.591

97.0 -176.15

6.27",

0.8766

0.6772 0.7083

0.8779 0.8785 8.7093

0.8795

o.eeoi 0.7106

0.8810

0.8B16

0.7118

0.8826

0.9831 0.7130

0.881, 1 0.881,6

0.711.2 0.6870

0.6675 0.7166

0.8898

0.8901, 0.7189

97.1 -176.05

6.321

0.8759

0.8765 0.7077

0.8772

0.6777 8.7087

0.6788

0.e793 0.7100

0.8803

0.8609

0.7112

0.8819

0.8821, 0.7125

0.8831, 0.8839

0.7137

0.8663

0.7161

0.8892

0.6897

0.7181,

97.2 -175.95

6.366

0.8752

0.8757 0.7071

0.8765

8.8770

1.7081 0.6780

0.6786

0.7091. 0.8796

0.8802

0.7106

0.9811

0.8817

0.7119

0.8827

0.8832

0.7131

0.8856

0.7155

0.8885

0.8890

0.7178

97.3 -175.85

6.1.11,

0.871.1, 0.8750

0.7065

8.8757 8.6763

0.7075

0.6773

0.6779 0.7086

0.8789

0.8791. 0.7101

0.9801, 0.9810 0.71130.8920 0.9925

0.7125

0.881.9 0.6655 0.7H90.8678

0.8881. 0.7173

97.1, -175.75

6.1,62

0.8737

0.671,2 0.7059

1.8750 0.8755

0.7069

0J6766

0.6771 0.7082

0.8782

0.8767

0.7095

0.8797 0.9803

0.7107

0.8312

0.3318

0.7120

0.681,2

o.eei.8

.711,1,

0.8871 0.8877

0.7167

97.5 -175.65

6.509

0.8729

0.8735 0.7053

0.971,3

0.671,8 1.7063

0.e75<= 0.6761, 0.7076

0.6771. 0.6760

0.7O89

0.8790 0.8796

0.7102

0.8805

0.8811

0.7111,

.8835

0.661,1 0.7138

0.6865

0.8870 0.7162

97.6 -175.55

6.557

0.8722

0.8727

0.701.7

8.6735

8.671,1 1.7057

0. e751 0.6757 0.7070

0.8767 0.8773

0.7083

0.8763

0.8789

0.7096

0.6798

0.3901, 0.7108

0.8828

0.8831, 0.7133

0.8858

0.8663

0.7156

97.7

-175.1.5 6.605

0.8711, 0.872O

0.701,1

1.8728 0.8733

0.7051

0.671.1. 0.6750

0J706I,

0.8760

0.8766

0.7TJ77

0.8776

0.9791

0.7090

0.8791

0.8797

0.7103

0.8822

0.8827 0.7127

0.6851 0.8657

0.7151

97.8 -175.35

6.653

0.8707 0.8713

0.7035

8.8720

0.8726

0.701,5

0.6737

0.671.2 0.7056

0.8753

0.8758 0.7072

0.9769

0.9771.

0.8781, 0.8790 0.7097

0.8815

0.6620

0.7121

O.881.1. 0.8850

0.711,5

97.9 -175.25

6.701

0.6699

0.6705

0.7028

0.8713 0.8718

0.7039 0.6735 0.7053

0.871,6 0.8751 0.7066

0.9'61 0.3757

0.7078

0.9777 0.8783

0.7091

0.6808 0.8813

0.7116

0.8837

0.861,3

0.711,0

98.0 -175.15

6.750

0.6692

0.8697

0.7022

0.6705

0.6711

0.7033

0. 6722 0.6757

0.701.7

0.8738

0.871.1. 0.7860

0.3751. O.e760

0.7073

0.8770

0.8776

0.7085

0.8601

0.9606

0.7110

O.8830 0.8636

0.7131,

98.1 -175.05

6.799

0.8681, 0.6690

0.7016

1.6698

1.8703 0.7027

0-e71E 0.672C

0.701.1

0.6731

0.8736

0.7O51.

0.871.7 0.3753

0.7067

0.8763

0.8768 0.7080

0.8791, 0.6799

0.7105

0.8821. 0.8829 0.7129

98.2

-171.. 95

6.81.8

0.8677

0.8662

0.70 1U

0.8690

0.8696 0.7021

0^6707

0.703 e

0.8721. 0.6729

0.701,6

0.871.0 0.971.5 0.7061

0.8756

0.7071.

0.6787

0.8792 0.7099

0.8817

0.882? 0.7123

98.3

-171,. 65 6.897

0.8669

0.6675

0.7001,

8.8663

0.8688 0.7015

0.6700

0.e705

0.702<=

0.8716

0.8722

0. 701.2

0.9733

0.9738

0.'955

0.871.9

0.3751, 0.7068

0.6760 0.8785

0.7093

o.aeio

0.8815

0.7116

98.1, -171.. 75

6.91,7

0.8662

0.8667

0.6998

0.8675 0.6681 0.70090..6692 0.669e 0.7023

0.8711, 0.7036

0.3725

0.8731

0.701.9

0.371.1 0.871.7 0.7062

0.8773 0.6778

0.7088

0.8803

0.6809

0.7112

98. i -171,. 65 6.997

0.8651, 0.8660

0.6992

0.6668 0.8673

0.7003

0.6685

0.6690

0.8702

0.8707

0.7O3O

0.8718

0.8721. 0.701*3

0.3731.

0.871,0 0.70560.8771 0.7062

0.8796

0.8802

0.7107

98.6

-171,. 55

7.01,7

0.861,6 0.8652

0.6966

0.8660 1.6666

0.6997

0.8677 0.6683

0.7011

0.8691, 0.8700

0.7021,

0.8711

0.3716

0.7036

0.8727

0.8732

0.7051

0.8759

0.8761, 0.7076

0.8789

0.8795

0.7101

98.7

-171,. 1,5 7.098

0.8639

0.861,1. 0.6979

8.8653

0.6658

0.6591

0.e670

0.6675

0.7005

0.8687 0.8692

0.7016

0.870.3 0.8709

0.7032

0.3720

0.3725

0.701,5

0.8752

0.8757

0.7070

0.8782

0.8786 0.7095

98.8

-171,. 35 7.1*8

0.8631

0.8637 0.6973

0.661,5 0.8651 0.69850.6662

0.e666

0.699?

C.6679

0.8665 0.7012

0.8696

n.8702

0.7026

0.8713 0.8718

0.7039

0.871,1, 0.6750

0.7065

0.8775

0.8781

0.7090

98.9

-171,. 25 7.199

0.8623

0.8629

0.6967

0.6638

0.861,3 0.6978

0.6655

0.6660 0.6992

0.867' 0.8678

0.7006

0.8689

0.3691. 0.7020

0.9705 0.8711

0.7133

0.6737

0.871,3 0.7059

0.8768

0.8771.

0.7081.
CCNTINUEC OF COHPRESSEC LIQUID NITROGEN - CONTINUED

TAPLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO, LIQUID OENSITY/OENSITY AT A 2. OENSITY RATIO, LIQUID UENSI TY/OENSITY AT A 3. DENSITY, KG/Oh^ FOILING

BOILING

PRESSURE

PRESSURE

OF 1 BAR, DIMENSICNLESS

OF 760 TCRR, OIMEI*SI ONLESS

BAR 0.600 1.000 2. KP/CM2 0.816 1.020 2. 000 it. 000 6.000 8.000 10.000

039 1..079 6.118 8.158 10.197 12.500

12.71,6 15.000

15.296

17.500

17.81,5 20.00020.391) 25.00025.1,93 30.000 30.591

99.0

-171.. 15 7.251

0.8616 0.8630 0.8621 0.8635 0.6961 0.6972

0.e6i.7 0.8653 0.6986

0.8665

0.8670 0.7000

0.8681

0.8687

0.7011,

0.8698

0.8701, 0.7027

0.8730

0.8736

0.7053

0.8761 0.8767

0.7079

100.0 -173.15

7.77a

0.8538 0.8553

0.851,3 0.8558 0.6898 0.6910

0.8571 0.8577

0.6925

0.8589

0.8595

0.6939

0.8607

0.8613

0.6951.

0.8625

0.8630

0.6968

0.8659

0.8661, 0.6995

0.8691

0.6697

0.7022

101.0 -172.15

8.332

0.81,71, 0.81,79

1.681,6

0.81,93 0.68620.8512

0.8518 0.6877

0.8531

0.S537

0.6892

0.8550

0.8555

0.6907 0.8585

0.8591

0.6936

0.8620

0.8625

0.6961,

102.0 -171.15

8.91".

1.8392

0.8398 0.6780

0.8l.ie 0.6797

0.81,33 0.81,39

0.6811,

0.81*53

0.81,59 0.6830

0.81.73

0.91.78

0.681.5 o.esn

0.8516 0.6876

0.851.7 0.8552

0.6905

103.0 -170.15 9.525

0.8309

0.8311, 8.6713 0.8331

0.8336

0.6731

0.8352

0.8358

0.671,8

0.8371, 0.8379

0.6765

0.8391.

0.81.00 0.6782

0.81,31,

0.81,1,0 0.6811.

0.81,78 0.681,5

10*.. -169.15 10.1650.621,6 0.8251 0.6662

0.8269

0.8271, 0.6681

0.8292

0.8297 0.6699

0.3311. 0.8319

0.6717 0.8356

0.8361

0.6751

0.8397

0.61,02

0.6781,

105.0 -168.15

10.836

0J8158

0.8163

0.6591

0.8183

0.8188

0.6611

0.9207

0.9212

0.6631

0.8231 0.8236

0.6650

0.8276

0.8281

0.8319

0.8321, 0.6721

106.0 -167.15 11.538

0-e068 0.8073

0.65ie

0.8091. 0.8099 0.6539

0.8120 0.8125

0.6560

0.8H.5

0.8150

0.65BI

0.8193

0.8199 0.6619

0.8239

0.821,1, 0.6656

107.0 -166.15

12.271

0.7973

0.7978

0.6U1.2 0.8O02

0.8O07

0.61,65

0.9030

0.8035

0.61,86

0.8057

0.8062 0.6509

0.8108

o!e551

0.8157

0.8162

0.6590

108.0 -165.15

13.038

0.7906 0.7911

0.6368

0.7936

0.791,1 0.61,12

0.7966

0.7971

0.61.35

0.6021

0.8026

0.61,80

0.8073

0.8078 0.6522

109.0

-161.. 15 13.838

0.7B06

0.7811 0.6307

0.7839

0.781.1. 0.6333

0.7971 0.7876

0.6359

0.7930 0.7935

0.61,07

0.7986

0.7991

0.61,52

110.0 -163.15

11,. 672

0.7701 0.7706

0.6222

0.7737 0.77U2

0.6251

0.7772 0.7776

0.6279

0.7836

0.781,1 0.6331

0.7896

0.7901 0.6380

111.0 -162.15

15.51.2

0.7630

0.7635

0.6161,

0.7668

0.7673

0.6195

.7738

0.771.3 0.6252

0.7803

0.7808

0.6301,

112.0 -161.15

0.7517

0.7521 0.5073

0.7559

0.7563

0.6107

0.7636

0.761.1 0.6169

0.7707 0.7712

0.6226

113.0 -160.15 17.392

0.7396

0.71,01 0.5975

0.71,1,3

0.71,1,8 0.5013

0.7529

0.7531. 0.6083

0.7606

0.7611

0.611.5

11*. -159.15

18.373

0.7319

0.7321, 0.5913

0.71.15 0.71,20 0.5991

0.7501 0.7505 0.6060

115.0 -158.15

19.39".

0.7186

0.7190 0.5906

0.7295

0.7299 0.5893

0.7389

0.7391, 0.5970

116.0 -157.15

20.1,55

0.7165 0.7170

0.5789

0.7272 0.7276

0.5875

117.0 -156.15

21.558

0.7025

0.7029

0.5675

0.711.6 0.7151

0.5771,

118.0 -155.15

22.701,

0.6870

0.6871, 0.5550

0.7011 0.7016

0.5665
DENSITY OF COMFRESSEC LIQUIC CONTINUED

TAELE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. YAPOR PRESSURE, BAR

1 DENSITY DENSITY

DENSITY

RATIO, LIQUID DENSITY/DENSITY AT » RATIO, LIQUIO DENSITY/OENSITY AT « KG/DM3

BCILING PPESSURE OF 1 BAR, DIMENSICN

BOILING PRESSURE OF 760 TCRR, CIMEhS

LESS ICNLESS

BAR 0.600 1 KP/CM2 0.816 1 .000 2 .020 2 000 039

1..000 1..079 6.000 8.000 10.000 12.500

6.116 8.158 10.197 12.71.6 15.000 17.500 20.000 25.00015.296 17.61.5 20.39". 25.1.93 30.000 30.591

119.0

-1S1..15 23.693

0.6695 0.6699

0.51.09 0.66660.551.5

120.0 -153.15 25.128

0.6701 0.6705

0.51.11.

121.0 -152.15

26.410

0.6515 0.6519

0.5261.

122.0 -151.15

27.71.1

0.6297

0.6301 0.5067

123.0 -150.15 29.122

0.6O21 0.6025

0.1.861.
The data for argon given here are from Gosman, et al. (1969). The entire PVT tabulations were calculated by a simultaneous solution of the vapor pressure equation and the equation of state reported by these authors. The calculation of each point was performed by- solving the vapor pressure equation for either P or T depending on which was the integral value input. Using the P and T so obtained, a corresponding density was found from the equation of state. Values near room temperature are given in table 9, uncertainties for the data in table 10, values for the saturated liquid are given in table 11 and values for the compressed liquid are shown in table 12. The values differ from those in the CGA pamphlet P-6

Table 9 Density of Argon Near Atmospheric Pressure and Room Temperature

Temperature Pressure Density Volume

gram- mole/cm3 kg /dm3 cm3 /gram- mole dm3 /kg 0°C 1 bar

760 torr 4.4074xl0~ 5 4.4659xlO" B 1.7606xl0~ 3 1.7840xl0~ 3 22689.22392.

567. 96 560. 53 15°C 1 bar

760 torr

4. 1772xl0" 5 4.2326xl0~ 5 1.6687xl0~ 3 1.6908xl0~ 3 23940.

23626. 599.27

591.43

Density Ratios - Dimensionless

Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 0° C

Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 15° C

792. 13 835.79

Liquid Density at a boiling pressure of 760 torr /density at 760 torr and C C

Liquid Density at a boiling pressure of 760 torr /density at 760 torr and 15° C

781.34

824.40

Liquid density at a boiling pressure of lbar 1.3 94 7 kg /dm

Liquid density at a boiling pressure of 760 torr 1.3939 kg/dm3

67
by about 0.02% primarily because a higher order interpolation is used here. The value of the density at the boiling point at 760 torr differs from that in the CGA pamphlet P-6 by 0.4%. The new correlation includes quite recent data, both on PVT and on the temperature scale corrections, and should, therefore, be more accurate.

Table 10 Uncertainties in the Data for Argon

variable uncertainty range of temperature

temperature 0.08%

0.02%

0.015 K

84 to 87 K

87 to 154 K

room temperature volume 0. 1%

increase to 1% 0.01%

triple point to 145 K

linearly from 145 K to critical room temperature

pressure 0. 1% 0.02%

0.01%

84 to 87 K

87 to 154 K

room temperature

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DENSITY OF COMPRESSED

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR 3

. DENSITY

. DENSITY

. DENSITY

RATIO,

RATIO,

, KG/OH 3 LIQUID OENS LIQUID OENS TY/BENSI

TY/DENSI Jy St a BOILINGBOILING

PRESSURE OF PRESSURE OF1 BAR, D 760 TORR MENSIC

OIMEN

NLESS SIONLESS

BAR KP/CM2

0.800 1.000 0.816 1.020 2.000

2.0 39 4.000

l*. 079 6.000 6.118

8.000 8.1580.000

0.197 15.000 15.396

20.000

20.39*

25.000 25.*9330.000 50.59155.000

55.690 *0.000 *0.789

85.0 -168.15

0.790

1.0093 1.0093

1.0058 1.0099

1.1.076 1.1.077

1.0 095 1.0101

l.i.080

1.0100 1.0105

1.1.086

1.010* 1.0109

l.*092

1.0108

1.0113

l.*097

.0112 .0118

.*103 1.0123

1.0128

1.0133 1.0138

l.*132

1.01*3 1.0153

.0159 .*160

.0163

!*17*

1.0173 1.0179

l.*186

85.1 -188.05

0.799

1.0089 1.0089

1.0091. 1.0091.

1.1.070 1.1.071 1.0091 1.0097

1.1.071. 1.0095

1.0101

1.1.080

1.0100

1 . 01 5 1.0109

l.*092

.0108

.0113

• *097 l.one

1. 012* l.*112

1.0129

1.013* l.*126

1.0139 .01*9

.0155

.*155

.0159 .0165 1.0169

1.0175

l.*183

85.2 -187.95

0.808

1.0085

1.0090

1.1.065 1.0087

1.0092

1 .1.068

1.0091 1.0097

1.1.071, 1.0095

1.0101 l.*080

1.0100

1.0105

.010*

.0109

• *091 1.011*

1.0120

i.*ioe

1.0125

1.0130

l.*120

1.0135

l!*135

1.01*5 .0150 .*1*9.0155

L.0160 .*163

1.0165 1.0170

l.*177

85.3 -187.85

0.817

1.0080 1.0086

1.1.059

1.0083

1.0088

1.1.062

1.0087

1.0092

1.1.066

1.0091 1.0097

l.*07*

1.0095 1.0101

l.*080

.0100

.0105

.*066

1.0110 1.0115

l.*100

1.0120

1.0126

l.*115

1.0131 1.0136

l.*129

.01*1 .01*6 ,*1*3.0151 .0156

.*157

1.0161 1.0166

1.1.171

85.1. -187.75

0.826 1.0076 1.00621.1.053 1.0078

1.0061. 1.1.056

1.0083 1.0088

1.1.062 1.0087

1.0092

1.1.068 1.0091

1.0097 l.*07*

.TJ095 .0101

.*080 l.oioe

1.0111 l.*09*

1.0116

1.0122

l.*109

1.0126 1.3132

l.*123

.0137 .01*2

.*137

.01*7

.0152

.*151

1.0157 1.0162

l.*165

85.5 -187.65

0.835

1.0072

1.0077

1.1.01.7

1.0071. 1.0079

1.1.050

1.0076 1.008*

l.*056

1.0083

1.0088

l.*062

1.0087

1.0092

l.*068

.0091

.0097

.*07*

1. 0102 1.0107

l.*088

1.0112

1.0117 1.0122

1.0128

1.4117

.0132

.0138 .*132.01*8

.*1*6

1.0153

1.0158

l.*160

85.6 -187.55

0.8'.'.

1.0068

1.0073

1.1)01.1 1.0070

1.0075

1.1.01.1.

1.007*

1.0079

l.*050

1.0078

1.008*

l.*056

1.0083

1.0086

l.*062

.0087

.TJ092 .*068

1. 0097 1.01031.0108 1.0113

l.*097 1.1.111

.0128 .013*

• *126

.0138 .*1*0

1.01*9

1.015* l.*15*

85.7

-187.1.5

0.851. 1.0063

1.0069

1.1.035 1.0065

1.0071

1.1.036

1.0070 1.0075

l.*0**

1.007* 1.0079

l.*050

1.0078 1.008*

l.*056

.0083

.0088 .*062 1.00931.0099 l.*077

1.010*

1.0109 l.*091

1.011*

1.0119

.012*

.0130

• *120

.013*

.01*0 .*13*

1.01** 1.0150

i.*i*e

85.8 -187.35

0.863

1.0059

1. 0061. 1.1.029

1.0061 1.0067

1.1.032

1.0065 1.0071

l.*038

1.0070

1.0075

l.*0**

1.007* 1.0079 l.*050.0078 .006*

.*056

1. 0089 1.009*

l.*071

1.0099

1.0105

l.*085

1.0110 1.0115

l.*100

.0120 .0125

.*11*

.0130 .0136

.*128

1.01*0 1.01*6 l.*l*2

85.9 -187.25

0.873 1.0055

1.0060

1.1.023 1.0057

1.0062

1.1.026

1.0061

1.0067

l.*032

1.0065

1.0071

l.*038

1.0070

1.0075

.007*

.0079 .*050

1. 0085 1.0090

l.*065

1.0095

1.0101

l.*079 1.0111l.*09*

.0121

.*108

.0126

.0131

.*123 1.01*2

l.*137

86.0 -187.15

0.682

1.0050 1.0056

1.1.017

1.0053 1.0058

1.1.020

1.0057

1.0062 l.*026

1.0061

1.0067 l.*032

1.0065 1.0071

l.*038

.0070

.0075 1.0080

1.0086 l.*059

1.0091 1.0096

l.*07*

1.0101 1.0107 l.*088.0112

.0117

,*102

.0122 .0127

• *117

1.0132 1.0137

1.1.131

86.1 -167.05

0.692

1.0 01.6 1.0051

1.1.011

1.001.8 1.0051.

1.1.011.

1.0053 1.0056

l.*020

1.0057

1.0062

l.*026

1.0061

1.0067

1.1.033

.0065

.0071 .*038

1.0076

1.0082

l.*053

i.ooe7

1.01)92 l.*068

1.0097 1.0103

l.*082

.0107 .0113

.*097

.0118 .0123 1.0128 1.0133

l.*125

86.2 -186.95

0.902

1.001.2

1.001.7 1.1.005

1.001.1. 1.001.9 1.00*8 1.005*

l.*01*

1.0053 1.0058

l.*020

1.0057

1.0062

l.*026

.0061

.•0067 .*032

1.0072 1.0077

l.*0*7

1.0082 1.0086

l.*062

1.0093

1.0098

.0103 .0109

.*091

.011*

.0119 1.012*1.0129 l.*119

86.3 -186.85

0.912

1.0037

1.001.3 1.3999

1.001.0 1.001.5

1.1.002

1.00**

1.00*9 1.00*81.005*

l.*01*

1.0053 1.0058

l.*020

.8057

.0062

.*026

1.0068 1.0073

l.*0*l

1.0O78

1.0 08*

l.*TJ56

1.008° 1.009*

.0099

.010* .*085

.0105 .0115 1.0120 1.0125

l.*113

66.1. -ie6.75

0.922

1.0033

1.0039 1.3993

1.0035

1.001.1 1.39961.00*5 l.*002

1.00**

1.00*9 i.*ooe

1.00*8 1.005*

1 .*01*

.0053

.0058

.*020 1.0063

1.0065 l.*035

1.0TJ7* 1.0O79

l.*050

1.008*

1.0090 l.*065

.0095

.0100

.*079

.0105

.0111

.*093

1.0115

1.0121

86.5 -186.65

0.932 1.0029

1.0031. 1.3987

1.0031 1.0036

1.3990

1.0035 1.00*1

1.3996

1.00*5 l.*002

1.00**

1.00*9 l.*008

.00*8 .005*

.*01*

1. 0055 l.*025

1.0O70 1.0U75

l.*0**

1.0080 1.0086

l.*059

.0091 .0096

.*073

.0106

.*068

1.0111 1.0117

l.*102

-166.55

0.91.2

1.0021. 1.0030 1.3981 1.0027

1.0032

1.3981.

1.0031 1.0036

1.3990

1.0035

1.3996 1.00*5

l.*002

.00**

.00*9

• *008

1.C055

1.0060 l.*023

1.0065

1.0071 l.*038

1,0076

1.0061 l.*053

.0086

.0092 .*067

.0097

.0102 .*062

1.0107

1. Oil' l.*096

86.7

-166.1.5 0.952

1.0020

1. 25 1.3975

1.0D22

1.0028 1.3978

1.0027 1.0032

1.398*

1.0031 1.0036

1.3990

1.0035

1.0 0*1 1.3996

.00*0 .00*5

.*002

1.0050

1.0056

l.*017

1.0061 1.0067

l.*032

1.0072

1.0077

l.*0*7

.0082

.0088

.*061

.0093

.0098

.*076

1.010?

1.0108

86.8 -186.35

0.962 1.0016

1.0021 1.3969

1.0018 1.0023

1.3972

1.0022 1.0026

1.3978

1.0027 1.0032 1.398*1.0031

1.0036 1.3990

.0035

.00*1

.3996

1. 00*6

1. 0052 l.*011

1.0057

1. 01)62 1.0067 1.0O73

l.*0*l

.0078 .0083

.*056

.0088

.*070

1.0099

1.010*

l.*08*

86.9 -186.25

0.973

1.0011 1.0017

1.3963

1.0011. 1.0019

1.3966

1.0018 1.0023

1.3972

1.0022 1.0026

1.3978

1.0027 1.0032

1.398*

.0031 .0037

.3990

1.00*2 1.00*7

1. * 005

1.0053

1.0TJ58 l.*020

1.0063 1.0069

1 . *035

.007* .0079

.*050 .0090 1.009* 1.0100l.*079
KPRESSEO LIuUID ARG

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

2

3

OENSITY

DENSITY DENSITY

RATIO, LIQUID OENSITY/DENSIT

RATIO, LIQUIO OENSITY/DENSIT

, KG/OM3

Y AT A BOILING BOILING

=RESSURE OF 'RFSSUPE OF

1 BAR, OlfENSICNLESS

760 TCRR, CIMENSICNLFSS

BAR KP/CM20.800 1.000 2.000

0.816 1.020 2.039 4.0004.079 6.0006.118

8.000

8.156

10.000 1 10.197 1 5.000

5.296 20.000

20.394

25.000 25.493

0.000

0.591 35.00035.690

40.000

40.769

87.0 -166.15

0.963

1.0007 1.0009

1.0012 1.0015

1.3957 1.3960

1.0011. 1.0019 1.39661.0018

1.0023 1.3972

1.0022

1.0026 1.3978

1.0027 1 1.0032 1 1.3984 1.0038

.'0043 .3995

1.0048

1.0054

1.4014

1.0059

1.0064

1.4029

.0070 .0075

L.4044

1 .0080

1 .0085 1.4056

1.0090 1.0096 1.4073

87.1 -186.05

0.99",

1.0003 1.0005

1.0008 1.0010

1.3950 1.3951. 1.0009

1.0015

1.3960

1.0014

1.0019

1.3966

1.0018 1.0023

1.3972

1.0022 1 1.0028 1 1.3978 1.0033

.0035 .3993

1.0044

1.0O49 1.4O08

1.0055

1.0060 1.4023

1.0065

L.0071 L.4038

1.0076

1.0061 1.4052

1.0066

1.0092 1.4067

87.2 -185.95

1.001. 1.0000

1.0006

1.391.7 1.0005

1.0010

1.3951. 1.0009

1.0015

1.3960

1.0011. 1.0019

1.3966

1.0018 1 1.0024 1 1.3972 1 .0025

.0034 .3987

1.0040 1.0045

1.4002

1.0050 1.0056

1.4017

1.0061 .0066

1.4032

1.0072 1.0077

1.4047

1.0082

1.0067

1.4061

87.3 -185.85

1.015

0.9996

1.0001

1.391.1

1.0001

1.0006

1.391.8 1.0005

l!3954 1.0009

1.0015 1.3960

1.0014 1 1.0019 1 1.3966 1 .0025

.0030 .3981

1.0035

1.0041

1.3996

1.0046 1.0052

1.4011

1.0057 1.0062

1.4026 1.0067

1.0073

1.0076

1.4055

87.1. -185.75

1.026

0.9992

0.9997 1.3935

0.9996

1.0002

1.391.1

1.0001

1.0006

1.391.8 1.0005

1.0010

1.3951.

1.0009 1 1.0015 1 1.3960 1.0020 .0026

.3975

1.0031

1.0037

1.3990

1.0042

1.0047

1.4005

1.0053

1.0056

1.4020

1.0063 1.0069

1.4035

1.0073 1.0079

1.4049

87.5 -185.65

1.037

0.9987

0.9993

1.3929

0.9992

0.9997 1.3935

0.9996

1.0002

1.391.2

1.0001 1.0006

1.391.8

1.0005 1 1.0010 1 1.3954 1.0016

• 00?1 .3969

1.0027 1.0O32 1.3984

1.0038

1.0043 1.3999

1.0048

1.0054 1.00591.0064

1.0069 1.0075

1.4043

87.6 -185.55

1.01.8 0.9983

0.9986 1.3923

0.9987

0.9993 1.3929

0.9992

0.9997

1.3935 0.9996

1.0002 1.3942

1.0001 1 1.0006 1 1.3948 1 .0012

.0017 .3963

1.0023 1.0O28

1.3978

1.0033 1.0039 1.39931.0044

1.0049

1.4008

1.0055

1.0060 1.4023

1.0065

1.0071

1.4036

87.7

-165.1.5 1.059

0.9979

0.9981. 1.3917

0.9983 0.9988

1.3923

0.9986

0.9993

1.3929 0.9992

0.9997

1.3936

0.9996 1 1.0002 1 1.3942 1 .0007

.0013 .3957

1.0018 1.0024

1.3972

1.0029 1.0035

1.3987

1.0040 1.0045 1.40021.0050

1.0056 1.4017

1.0061 1.0066

1.4032

87.8 -185.35

1.070

0.9971. O.9980 1.39110.9979

0.9961. 1.3917

0.9983

0.9969 1.3923

0.9968

0.9993

1.3929

0.9992 1 0.9997 1 1.3936 1

.0003

.0008

.3951

1.0O14 1.0O19 1.3966

1.0025

1.0030

1.3981

1.0036

1.0041

1.3996

1.0046 1.00521.0057

1.0062

1.4026

87.9 -185.25

1.081

0.9970

0.9975 1.3905

0.9971. 0.9960 1.39110.9979

0.9961. 1.3917

0.9983

0.9989

1.3923

0.5986 0.9993 1 1.3930 1 .5995

.0001. .3945

1.0010

1.0015 1.3960

1.0021 1.0026

1.3975

1.0031

1.0037

1.3990 1.0042

1.0047 1.4005

1.0052

1.0056 1.4020

88.0 -185.15

1.092

0.9965 0.9971 1.38960.9970

0.9975 1.3905

0.9971. 0.99 8 1.39110.9979

0.9961. 1.3917

8.9983

0.9989 1 1.3923 1

.5994

.0000 .3935

1.0005

1.0011 1.3954

1.0016 1.0022 1.3969

1.0027 1.0032 1.39841.0036 1.0043 1.39991.0048 1.0054

1.4014

88.1 -185.05

1.101.

0.9961

0.9966 1.3892

0.9965

0.9971 1.3899

0.9970 0.9975

1.3905 0.9974

0.9980

1.3911

0.9979

0.9984 1.3917 1 .9990 ^3933

1.0001 1.0O06

1.3948

1.0012

1.0017 1.3963

1.0023

1.0028 1.3978

1.0033

1.0039 1.3993

1.0044 1.0049

1.4008

88.2

-18".. 95 1.115

0.9956

0.9962 1.3886

0.9961 0.9966

1.3692

0.9966

0.9971 1.3899

0.9970

0.9975

1.3905

0.9975 0.9980

1.3911 1 .5991

.3927

0.9997 1.0002

1.3942

1.0008 1.0013

1.3957

1.0018

1.0024 1.3972

1.0029

1.0035 1.3987

1.0040 1.0045 1.4002

88.3

-181.. 85 1.127

0.9952 0.9957

1.3860

0.9957

0.9962 1.3886

0.9961 0.9967 0.9966

0.9971

1.3899

0.9970 0.5976

1.3905 1

.5981

.9987

.3921

0.99°2 0.9998

1.3936

1.0003

1.0009 1.3951

1.0014

1.0020 1.3966

1.0025

1.0030 1.3581

1.0035

1.0041

1.3996

88. 1. -181.. 75

0.991.8 0.9953

1.3871. 0.9952

0.9958 0.9957

0.9962

1.3686

0.9961

0.9967

1.3893

0.9966

0.9971

1.3899 1 .5977 0.9988

0.9993

1.3930

0.9999

1.0004

1.3945

1.0015

1.3960

1.0021

1.0026 1.3975

1.0031 1.0037 1.3990

88.5

-161.. 65 1.150

0.991.3

0.991.9 1.38680.9953

1.3871.

0.9952

0.9956

1.3680

0.9957

0.9962

1.3867

0.9961

0.9967 .9978

• 390 c 0.9984

0.9989 1.3924

0.9O95

1.0000

1.3939

1.0006

1.0011 1.3954

1.0016 1.0022

1.3569

1.0027

1.0032 1.3984

88.6

-18".. 55 1.162

0.9939

0-.9944 1.3861

0.991.3

0.991.9 1.3668

0.991.6 0.9953

1.3871. 0.9952

0.5958

0.9957

0.5962 C 1.3887 1 .9968 .390?

0.9979

0.9965 1.3918

0.9990

0.9996

1.3933

1.0001

1.0007

1.3948

1.0012 1.0017

1.3964

1.0023

1.0028 1.3978

88.7

-181.. 1.5 1.171.

0.9931.

0.991.0 1.3655

0.9939

0.991.1. 1.3862

0.991.3 0.9949 1.3868

0. 991.8 0.9953 1.38740.9953 C 0.9958 C 1.3381 1

.9964

.9969

.3896

0.9975 0.9980

1.3912

0.9991

1.3927

0.9997

1.0002 1.3942

1.0008 1.0013

1.3958

1.0018

1.0024 1.3972

88.8

-181.. 35 1.186

0.9930

0.9935

1.381.9

0.9931.

0.991.0 1.3855

0.9939

0.991.1. 1.3862

0.991.4 0.9949 1.38680.9948

0.9954 C 1.3874 1

.5959

.9965 .3890

0.9971 0.9976

1.3906

0.9982

0.9987

1.3921

0.9993

0.9998 1.3936

1.0003

1.0005 1.3952

1.0014 1.0020 1.3967

88.9

-181.. 25 1.199

0.9925

0.9931

1.381.3

0.9930

0.9935

1.381.9

0.9935

0.991.0 1.3856

0.9939

0.9945

1.3862

0.9944 C 0.9949 C 1.3868 1

.9955

.5960

.3864

0.9966 0.9972

1.3900

0.9977 l!3915

0.9988

0.9994 1.3930

0.9999

1.0005

1 .3946

1.0010 1.0015

1.3961
IBLE 12 - CONTINUED DENSITY OF CChPRESSEO LICUIO ARGON - CCNTINUEC

TAeLE ENTRIES

1. TEMPERATIRE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

2

. DENSITY

. DENSITY

. DENSITY

RATIO, LIQUID BENSITY/OEN

RATIO, LIQUID OENSITY/DEN

, KG/DM3

SITY AT A SITV AT A ECILING BOILING

=RESSU9E

'RESSURE

OF 1 BAR, OIMENSKNL

OF 760 TCRR, OIMENSI

ESS CNLESS

BAR KP/CM2

0.600 1.000 2.000

0.816 1.020 2.039

4.000 4.079 till

8.000 10.000 8.158 10.197 15.000

15.296

20.000 20.394

25.000 25.49330.000

30.591 35.00035.690

40.000 40.789

89.0

-18".. 15 1.211

0.9921

0.9926 1.3837

0.9926

0.9931

1.3843

0.9930 0.9936

1.3849

0.9935 0.9939 0.9940 0.9945 1.3856 1.38620.9951

0.5956 1.3876

0.9962

0.9967 1.3894

0.9973

0.9978

1.3909

0.9984

0.9989 1.3924

0.9995

1.0000 1.39401.0011 1.3955

-let. 05 1.223

0.9916

0.9922 1.3830

0.9921

0.9926 1.3837

0.9926

0.9931 1.3843 0.9930 0.9935 0.9936 0.9940 1.3850 1.3856 0.9946

0.19952 1.3872

0.9957

0.9963

1.3687

0.9969

0.9974

1.3903

0.9980

0.9985

1.3918

0.9991

0.5996 1.3934

1.0001

1.0007

1.3949

89.2 -183.95

1.236

0.9912 0.9917 1.38240.9917

0.9922 1.3831

0.9921

0.9927 1.3837

0.9926 0.9930 0.9931 0.9936 1.3843 1.38500.9942

0.5947 1.3666

0.9953

0.9958 1.3661

0.9964 0.9970 1.38970.9975

0.9981 1.3912

0.9986

0.9992 1.3928

0.9997

1.0002 1.3943

89.3 -183.85

1.21,8 0.9908

0.9913

1.3818

0.9912

0.9918 1.3824

0.9917

0.9922 1.3831 0.9921 (.9926 0.992T 0.9931 1.3637 1.3844

0.5937 0.9943

1.3860

0.9949

0.9954

1.3875

0.9960 0.9965

1.3891

0.9971

0.9976 1.3906

0.5982

0.9987

1.3922

0.9993

0.9996

1.3937

89. <t -183.75

1.261

0.9903

0.9908 1.3812

0.9906

0.9913 1.3818

0.9912 0.9918

1.3825 0.9917 0.9922 0.5922 0.9927 1.3831 1.3837 0.5933

0.9938 1.3853

0.9944

0.9950 1.3869

0.9956

0.9961

1.3885 0.9967

0.9972 1.3900

0.9976 0.5983

1.3916

0.9986 0.9994

1.3931

89.5 -163.65

1.27", 0.9899

0.9904 1.3805

0.9903

0.9909 1.3812

0.9908 0.9913

1.3818 0.9913 0.9917 0.9918 0.9923 1.3825 1.3831

0.5925 1^3847

0.9940

0.9945 1.3863

0.9951 0.9957

1.3879

0.9962

0.9968 1.3894 0.99730.9979 1.3910

0.9984

0.9990 1.3925

89.6 -183.55

1.286

0.9894

0.9899 1.3799

0.9899

0.9904 1.3806

0.9903

0.9909 1.3812

0.9908 0.9913 0.9913 0.9916 1.3819 1.38250.9924

0.5930 1.3841

0.9936

0.9941 1.3857

D.9947 0.9952

1.3873

0.9958

0.9963 1.3388

0.9969

0.9974 1.3903

0.9980 0.9985 1.3919

89.7

-163.1,5 1.299

0.9890

0.9895 1.3793

0.9894

0.9900 1.3799

0.9899

0.9904 1.3806

0.9904 0.9908 0.9909 0.9914 1.3812 1.3819 0.9920

0.9925

1.3835

0.9931 0.9937

1.3851

0.3942

0.9946

1.3866

0.9954

0.9959 1.3882

0.9965

0.5970

1.3697

0.9976

0.9981 1.3913

89.8 -183.35

1.312

0.9885

0.9890 1.3787

0.9890 0.9895 1.37930.9894

0.9900 1.3800 0.9699 0.9904 0.9905 0.9909 1.3806 1.3813

0.9915 0.9921

1.3825

0.9927 0.9932

1.3645

0.9938 0.9943

1.3860

0.9949

0.9955 1.3876

0.9960

1.3891

0.9971

0.9977 1.3907

89.9 -183.25

1.326

0.9881

0.9886 1.3780

0.9865 0.9891

1.3787

0.9890 0.9895

1.3793

0.9895 0.9899 0.9900 0.9905 1.3800 1.3806

0.9911 0.9916

1.3823

0.9922

0.9928 1.3838

0.9934 0.9939

1.3854

0.9945

0.9950

1.3870

0.9956

0.9961

1.3685

0.9967

0.9972

1.3901

90.0 -183.15

1.339

0.9876

0.9881

1.3774

0.9881

0.9866

1.3761

0.9686

0.9691 1.3787

0.9890 0.9895 0.9696 0.9900 1.3794 1.3800

0.9906 0.9912

1. 3816

0.9918

0.9923

1.3832

0.9929

0.9935

1.3848

0.9941

0.9946

1.3364

0.5952 0.9957

1.3875

0.9963

0.9968 1.3895

90.1 -163.05

1.352

0.9872 0.9677

1.3768

0.9876

0.9882 1.3774

0.9881 0.9886

1.3761

0.9886 fl.9890 0.9891 0.9896 1.3787 1.3794

0.9902

0.9907

1.3810

0.9914

0.9919 1.3626

0.9925

0.9930

1.3842

0.9936

0.9942

1.3858

0.5947

0.9953

1.3873

0.9958 0.9964

1.3889

90.2 -162.95

1.366

0.9867 0.9872 1.37610.9872

0.9877

1.3768

0.9677 0.9882 1.3775

0.9881 0.9886 0.9887 0.9691 1.3781 1.37860.5896 0.9903 1.3804

0.9909 0.9914

1.3620

0.9921 0.9926

1.3836

0.9932 0.9937

1.3652

0.9943 0.9948

1.3867

0.9954

0.9955

1.3883

90.3 -182.85

1.379

0.9863

0.9866 1.3755

0.9867

0.9873

1.3762

0.9872

0.9877 1.3768 0.9677 0.9661 0.9862 0.9687 1.3775 1.3761 0.9893

0.9898

1.379e

0.9905 0.9910

1.3814

0.9916

0.9921

1.3830 0.9927

0.9933

1.3846

0.9939

0.9944

1.3661

0.9950

0.9955 1.3877

90.1, -182.75

1.393

0.985.8 0.9863 1.37490.9863

0.9868

1.3755

0.9666

0.9873

1.3762

0.9872 0.9877 0.9676 0.5882 1.3769 1.3775 0.9889

0.5894

1.3792

0.9900 0.9906

1.3806

0.9912

0.9917

1.3624

0.9923

0.9928

1.3939 0.9934

0.9940 1.3855

0.9945

0.9951 1.3671

90.5 -182.65

1.1,07

0.9853

0.9859 1.3742

0.9858

0.9664 1.3749

0.9863

0.9866

1.3756 0.9868 0.9872 0.9873 0.9678 1.3762 1.3769

0.9884

0.9890

1.3785

0.9896

0.9901

1.3801

0.9907 0.9913

1. 3617

0.9919

0.9924 0.9930 0.9935 1.3645

0.9941 0.9946

1.3e65

90.6 -182.55

1.1,20

0.9849

0.9854

1.3736

0.9854

0.9859 1.3743

0.9859

0.9864 1.3749

0.9863 0.9868 0.9869 0.9873 1.3756 1.3763

0.9880

0.5885

1.377c

0.9891

0.9897

1.3795

0.9903

0.9906

1.3611

0.9914

0.9920

1.3827

0.9926

0.9931

1 .3843

0.9937

0.994? 1.3658

90 .7 -162.1,5 1.434

0.9844

0.9850

1.3730

0.9849

0.9855 1.3736

0.9854

0.9859

1.3743 0.9859 0.9864 0.9864 0.9869 1.3750 1.3756

0.9875

0.9861 1.3773

0.9887 0.9892

1.3789

0.3896 0.5904

1.3805

0.991O 0.9915

1.3821

0.5921 0.9927

1.3637

0.9932

0.9938 1.365?

90.8 -162.35

1.448

0.9840

0.9845

1.3723

0.9845

0.9850

1.3730

0.9849

0.9855

1.3737

0.9854 0.9859 0.9860 0.9864 1.3743 1.3750

0.9671

0.9876

1.3767

0.9*62

0.9888

1.3783

0.9894

0.9899

1.3799

0.9905

0.9911 1.3815

0.9917

0.9922

1.3831

0.992e

0.9933 1.3846

90.9 -162.25

1.463

0.9835

1.3717

0.9840

0.9845

1.3724

0.9845

0.9650

1.3731

0.9650 0.9854 0.9655 0.9860 1.3737 1.3744

0.9866 0.5672

1.3760

0.9878

0.9863

1.3777

0.9890

0.9895

1.3793

0.9901 0.9906 1.38090.9912

0.9916

1.3e25

0.9924

0.9929 1.3840
DENSITY OF CCfPRESSEO

TAPLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

23

DENSITY

DENSITY

DENSITY

RATIO, L RATIO, L KG/DP3IOUID OENSITY/DENSITY AT A IOUI0 OENSITY/OENSITY AT A BCILING P BOILING F RESSURE OF RESSURE Of

1 BAR, OIMENSICNLESS

760 TCRR, CIMEKSIONLESS

BAR KP/CM20.800 1.000 2.000

0.816 1.020 2.039 4.000

4.079

6.000 6.1186.000

8.158

10.001)

I0-.197 15.000

15.296 20.00020.394

25.000 25.49330.000

30.591 35.00035.690

40.000 40.789

91.0 -182.15

1.1,77

0.9831

0.9836 1.3711

0.9836

0.9841 1.3717

O.9640

0.9646

1.3724

0.9845

0.9851 1.3731

0.9850

0.9855

1.3738 0^5667 1.3754

0.9874

0.9879

1.3770

0.9685

0.9891 1.3767

0.9897

0.9902

1.3803

0.9906

0.9913

1.3819

0.9919

0.9925

1.3834

91.1 -162.05

1.1,91

0.9826

0.9831 1.3704

0.9831

0.9836

1.3711

0.9836

0.9841 1.3718

0.9841

0.9846 1.3725

(.9845

0.9851 1.3731

0.5857

0.9863

1.3746

0.9669

0.9874 1.3764

0.9881 0.9886

1.3760

0.9892

0.9698 1.3797 0.9904

0.9909 1.3612

0.9915

0.9920 1.3628

91.2 -161.95

1.506

0.9822

0.9827 1.3696

0.9826

0.9832 1.3705

0.9831

0.9837 1.3712

0L9836

0.9641

1.3718

0.9841 0.9846

1.3725 0.9853

0.5858 1.3742

0.9665

0.9870 1.3758

0.9876

0.9862

1.3774

0.9868 0.9893

1.3790 0.9899

0.5905

1.3806

0.9911 0.9916

1.3822

91.3 -161.85

1.520

0.9817

0.9822 1.3692

0.9822

0.9827

1.3698

0.9827

0.9632

1.3705

0.9832

0.9837 1.3712

0.9836

0.9842

1.3719 0.9854

1.2735

0.9860

0.9866

1.3752

0.9872

0.9877

1.3768

0.9883

0.9889 1.3764

0.9895

0.9900

1.3800

0.9906

0.9912

1.3816

91.4 -181.75

1.535

0.9812

0.9618 1.3685

0.9817

0.9823

1.3692

0.9622

0.9628 1.3699

0.9827

0.9832 1.3706

0.9837

1.3712

0.5844

0.9849

1.3725

0.9956

0.9861 1.3746

0.9867

0.9873

1.3762

0.9879 0.9884

1.3776

0.9690 0.5896

1.3794

0.9902

0.9907

1.3810

91.5 -181.65

1.550

0.9806 0.9813

1.3679

0.9813

0.9818 1.3686

0.9818

0.9623 1.3692

0.9823

0.9828

1.3699

0.9827

0.9833

1.3706

0.9839

0.984S

1.3723

0.9851

0.9857

1.373=

0.9863

0.9868 1.3756

0.9875

0.9880 1.3772

0.9866

0.9891

1.3788

0.9897

0.9903

1.3804

91.6 -181.55

1.565

0.9603

0.9809 1.3672

0.9808

0.9814 1.3679

0.9613

0.9818

1.3686

0.9818

0.9623 1.3693

0.9823

0.9828 1.3700

0.9835 0.9840

1.3716

0.9847

0.9852 1.3733

0.9859 0.9664

1.3749

0.9870 0.9875

1.3766

0.9882

0.9887

1.3782

0.9693

0.9698

1.3798

91.7 -161.45

1.580

0.9799 0.9804

1.3666

0.9604 0.9609

1.3673

0.9809

0.9814

1.3680 0.9813

0.9819 1.3687

0.9824

1.3693

0.58 3 0.9836 1.3710

0.981.2 0.9848

1.3727

0.9654

0.9859

1.3743

0.9866

0.9871

1.3760

0.9877

1.3776

0.9889

0.9894

1.3792

91.8 -181.35

1.595

0.9794 0.9799

1.3660

0.9799

0.9604 1.3667

0.9604

0.9809 1.3673

0.9809

1.3680

0.9814

0.9619

1.3687

0.9826 1.37040.9S38

0.9843

1.3721

0.9850

0.9855 1.3737

0.9861 0.9867

1.3753

0.9873

0.5878

1.3769

0.9864

0.9890 1.3765

91.9 -181.25

1.610

0.9790

0.9795

1.3653

0.9794

0.9800

1.3660

0.9799

0.9805 1.3667

0.9604

0.9810 1.3674

0.5809 0.9814

1.3681 ol5627 1.3696

0.9833

0.9839 1.3714

0.9845

0.9650

1.3731

0.9857

0.9862 1.3747

0.9866 0.9874

1.3763

0.9880

0.9885 1.3779

92.0 -161.15

1.625

0.9785 0.9790

1.3647

0.9790

0.9795

1.3654

0.9795

0.9600 1.3661

0.9600

0.9605

1.3667

0.9905

0.9810

1.3674

0.5817 0.5822

1.3691

0.9829

0.9834

1.3708

0.9841 1.37250.9852

0.9858

1.3741

0.9664

0.9865 1.3757

0.9676

0.9881 1.3773

92.1 -161.05

1.641

0.9780 0.9786

1.3640

0.9785

0.9791 1.3647

0.9790

0.9796

1.3654

0.9795

0.9600

1.3661

0.9800 0.9605

1.3668

0.5812

0.58ie

1. 3685

0.9824

0.9870

1.3702

0.9636

0.9841

1.3716

0.9848

0.9853

1.3735

0.5660 0.5665

1.3751

0.9671

0.9676

1.3767

92.2 -160.95

1.656

0.5776

0.9781 1.3634

0.9781 0.9786

1.3641

0.9786

0.9791 1.3648

0.9791 0.9796

1.3655

0.5795

0.9601 1.3662

0.9608

0.9813

1.3675

0.9820

0.9825 1.3695

0.9832

0.9837

1.3712

0.9843

0.9849 1.3729

0.5855

0.9860 1.3745

0.9867

0.9872

1.3761

92.3 -180.85

1.672

0.9771

0.9776

1.3627

0.9776

0.9781 1.3634

0.97 81 0.9786

1.3641

0.9786

0.9791

1.3648

0.9791

0.9796

1.3655

0.980?

0.5808 1.3672

0.9815

0.9821 1.3689

0.9827 0.9633

1.3706

0.9839

0.9844

1.3722

0.9851

0.9856 1.3739

0.9862

0.9868 1.3755

92.4 -180.75

1.688

0.9766

0.9772

1.3621

0.9771

0.9777 1.3628

0.9776 0.9782

1.3635

0.9781

0.9787

1.3642

0.9786

0.5792

1.3649

0.5795

0.9604

1.3666

0.9B11 0.9816

1.3663

0.9823

0.9826

1.3700

0.9835

0.9840 1.3716

0.5846

0.9852 1.3732

0.9858

0.9663 1.3749

9Z.5 -180.65

1.704

0.9762

0.9767

1.3615

0.9767

0.9772 1.3622

0.9772 0.9777

1.3629

0.9777 0.9782

1.3636

0.9762 0.9787

1.3642

0.5794 0.5799 1.3660

0.9606 1.3677

0.98ie 0.9824

1.3693

0.9830

0.9335

1.3710

0.5842 0.5847

1.3726

0.9654

0.9659 1.3742

92.6 -180.55

1.720

0.9757

0.9762 1.3608

0.9762

0.9767

1.3615

0.9767

0.9773

1.3622

0.9772 0.9778

1.3629

0.9777

0.9782

1.3636

0.9790

0.9795

1.3653

0.9802 0.9807

1.3670

0.9814

0.9819 1.3687

0.9626

0.9831

1.3704

0.5837 0.9843

1.3720

0.9649

0.9654

1.3736

92.7 -160.45

1.736

0.9753 0.9758

1.3602

0.9758 0.9763 1.3609

0.9763 0.9768

1.3616

0.9768

0.9773 1.3623

0.9773

0.9778

1.3630

0.5785 0.5790

1.3647

0.9797

0.9802

1.3664

0.9809

0.9815 1.3681

0.9821

0.9826

1.3597

0.5633

0.9838

1.3714

0.9845

0.9850 1.3730

92.8 -180.35

1.752

0.9748

0.9753 1.3595

0.9753

0.9758 1.3602

0.9758

0.9763 1.3609

0.9763

0.9768 1.3616

0.9768 0.9773

1.3623

0.9780

0.9786

1.3640

0.9793

0.97°8 1.3656

0.9805

0.9810 1.3674

0.9817

0.9822

1.3691

0.9829

0.9834 1.3708

0.9840

0.9846

1.3724

92.9 -160.25

1.768

0.9743

0.9749

1 .3589

0.9748

0.9754

1.3596

0.9753 0.9759 1.3603

0.9758

0.9764 1.3610

0.9763 0.9769

1.3617

0.9776

0.5781 1.3634

0^9793 1.3651

0.9800 0.9806 1.3668

0.9812 0.9818

1.-3685 0.5624

0.5829

1.3701

0.9836

0.9641

1.3718
OF COPPRESSEO LIQUID ARGON - CONTINUED

TABLE ENTPIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

2

3

. CENSITV

. DENSITY

. DENSITY

RATIO, I RATIO, L

, KG/DM 3 IQUID DENSITY/DEN

IQUID DENSITY/DEN

SITY AT A SITY AT A BOILING BOILINGPRESSURE

PRESSURE

OF 1 9AR, DIMENSICNLESS

OF 760 TORR, DIHESSICNLESS

BAR KP/CM20.800 1.000 2.000 0.816 1.020 2.0394.000 4.079

6.000

6.118

8.000 6.158 10.000

10.197 15.000

15.296 20.000

20.394

25.000 25.49330.000

30.591 35.000 35.690

40.000

40.789

93.0 -160.15

1.785 0.9739

0.9744 1.3562

0.9744

0.9749 1.3589

0.9749

0.9754 1.3596 0.97540.9759 1.3603

0.9759

0.9764 1.3610

0.9771 0.9777

1.3626

0.9784

0.9789 1.3645

0.9796

0.9801 1.3662

0.9808

0.9813 1.3679

0.9820

0.9825 1.3695

0.9831

0.9837 1.3712

93.1 -160.05

1.801 0.9734

0.9739 1.3576

0.9739

0.9744 1.3583

0.9744

0.9749 1.3590

0.9749 0.9754

1.3597

0.9754

0.9759 1.3604

0.9767

0.9772

1.3621

0.9779 0.9784 1.36390.9791 0.9796

1.3656

0.9803

0.9809 1.3672

0.9815

0.9820 1.3689

0.9827

0.9832 1.3705

93.2 -179.95

1.818

0.9729

0.9735 1.3569

0.9734

0.9740 1.3576

0.9739 0.9745 1.3583

0.9745

0.9750 1.3591

0.9750 0.9755

1.3598 0.9762

0.9767

1.3615

0.9774

0.9780 1.3632

0.9787 0.9792

1.3649

0.9799

0.9804 1.3666 0.98110.9816 1.3683

0.9623

0.9828 1.3699

93.3 -179.85

1.835 0.9725

0.9730 1.3563

0.9730 0.9735 1.3570

0.9735

0.97 4 1.3577

0.9740

0.9745 1.3584

0.9745

0.9750 1.3591

0.9758

0.5763 1.3609

0.9770

0.9775 1.3626

0.9782 1^3643

0.9794

1.3660 0.9806

0.9812 1.3677

0.9818 0.9823 1.3693

93.1. -179.75

1.852 0.9720

0.9725 1.3556

0.9725

1.3563

0.9730

0.9735 1.3570 0.97350.9741

1.3578

0.9740 0.9746

1.3565 0.9753

0.9758 1.3602

0.9765 0.9771

1.3619

0.9778

0.9783

1.3637

0.9790 0.9?95

1.3654

0.9802

0.9807 1.3670

0.9814

0.9819 1.3687

93.5 -179.65

1.869

0.9715

0.9721 1.3550

0.9720

0.9726 1.3557

0.9726

0.9731 1.3564

0.9731 0.9736

1.3571

0.9736

0.9741

1.3576

0.9748

0.9754

1.3596

0.9761 0.9766 1.36130.9773

0.9778

1.3630

0.9785

0.9791 1.3647

0.9797 0.9803

1.3664

0.9809

0.9814 1.3681

93.6 -179.55

1.886

0.9711 0.9716 1.35430.9716

0.9721 1.3550

0.9721 0.9726

1.3558

0.9726

0.9731 1.3565

0.9731 0.9736

1.3572

0.9744

0.9749 1.3589

0.9756

0.9761 1.3607

0.9769 0.9774

0.9781

0.9786 1.3641

0.9793

0.9798 1.3658

0.9805 0.9810 1.3674

93.7 -179.45

1.903 0.9706

0.9711 1.3537

0.9711

0.9716 1.3544 0.97160.9721 1.3551 0.97210.9727 1.3558

0.9726

0.9732

1.3565 0.9739 0.57441.3583

0.9752

0.9757 1.3600

0.9764

0.9769

0.9776

0.9782 1.3635

0.9788

0.5794

1.3652

0.9800 0.9806

1.3668

93.8 -179.35

1.921

0.9701 0.9706

1.3530

0.9706

0.9712

1.3537

0.9712

0.9717 1.3545

0.9717

0.9722

1.3552

0.9722 0.9727

1.3559

0.9735

0.9740 1.3577

0.9747 0.9752

1.3594

0.9759

0.9765

1.3611

0.9772

0.9777 1.3628

0.9784 0.9789 1.3645

0.9796

0.9801 1.3662

93.9 -179.25

1.938 0.9697

0.9702 1.3524

0.9702

0.9707 1.3531

0.9707

0.9712

1.3538

0.9712

0.9717 1.3545

0.9717

0.9722 1.3552

0.9730 0.9735

1,3570

0.9742

0.9748

1.35e8

0.9755

0.9760

1.3605

0.9767 0.9772

1.3622

0.9775 0.5785

1.3635

0.9791

0.9797 1.3656

9*.0 -179.15

1.956 0.9692

0.9697

1.3517

0.9697

0.9702

1.3524 0.9702

0.9707

1.3531

0.9707

0.9713 1.3539

0.9713

0.9718

1.3546 ol5731 1.3564

0.9738 0.9743

1.35ei

0.9750 0.9756

1.3599

0.9763

0.9768

1.3616

0.5775

0.9780 1.3633

0.9787 0.9792 1.3650

9<f. 1 -179.05

1.971, 0.9687

0.9692 1.3510

0.9692

0.9698 1.3518

0.9698 0.9703

1.3525

0.9703

0.9708 1.3532

0.9709 0.9713

1.3539

0.5721 0.5726

1.3557

0.9733

0.9739 1.3575

0.9746

0.9751

1.3592

0.9758

0.9763

1.3609

0.5770

0.9776

1.3626

0.9782 0.9788

1.3643

94.2 -178.95

1.992

0.9682

0.9688

1.3504

0.9688

0.9693

1.3511

0.9693

0.9698

1.3518

0.9698

0.9703

1.3526

O.9703

0.9708

1.3533

0.571f 0.5721

1.3551

0.9729 0.9734

1.3568

. 0.9741 0.9746

1.3586

0.9754 0.9759

1.3603

0.9766 0.9771 1.36200.9778 0.9783 1.3637

94.3 -178.85

2.010

0.9683

0.9688 1.3505

0.9688 0.9693 1.35120.9693

0.9699

1.3519

0.9699

0.9704 1.3526

0.5711 0.5717

1.3544

0.9724 0.9729

1.3562

0.9737

0.9742 1.3579

0.9749 0.9754

1.3597

0.9761 0.9767

1.3614

0.9773 0.9779

1.3631

911.1, -178.75

2.028

0.9678 0.9683 1.34980.96 8 3 0.9689 1.3505 0.9689

0.9694

1.3513

0.9694

0.9699 1.3520

0.5707 0.5712

1.3538

0.9720 0.9725

1.3556

0.9732 0.9737 1.3573

0.9745

0.9750 1.3590

0.9757 0.9762

1.3608

0.9769

0.9774. 1.3625

94.5 -178.65

2.046

0.9674

0.9679

1.3491

0.9679

0.9684 1.3499 0.96640.9689 1.3506

0.9689

0.9694

1.3513

0.9702

0.5707

1.3531

0.9715

0.9720 1.3549

0.9726 1.3567

0.9740 0.9745

1.3584

0.5752 0.9758

1.3601

0.9764

0.9770

1.3618

94.6 -178.55

2.064

0.9669

0.9674

1.3485

0.9674

0.9679

1.3492

0.9679

0.9685 1.3500

0.S685

0.9690

1.3507

0.9698

0.5703

1.3525

0.9710 0.9716

1.3543

0.9723

1.3560

0.9735

0.9741

1.3578

0.9746 0.9753

1.3595

0.9760 0.9765

1.3612

94.7 -178.45

2.083

0.9664

0.9669

1.3478

0.9669

0.9675 1.3486

0.9675

0.9680 1.3493

0.9680 0.9685

1.3500

0.5693

0.9698

1.3518

0.9706

0.9711 1.3536

0.9718 0.9724 1.3554

0.9731 0.9736

1.3571 0.9743

.9749 1.3589

0.9755

0.9761 1.3606

94.8 -178.35

2.101

0.9659 0.9665

1.3472 0.9665

0.9670

1.347S

0.9670 0.9675

1.3486

0.9675

0.9680

1.3494

0.5688

1.3512

0.9701 0.9706

1.3530

0.9714 0.9719

1.3548

0.9726 0.9732

1.3565

0.9739 0.9744

1 .3582

0.9751 0.9756

1. 3599

94.9 -178.25

2.120

0.9655 0.9660

1.3465 0.96651.3473

0.9665 0.9670

1.3480

0.5671 0.9676

1.3487

0.9684 0.9696 0.9702

1.3523

0.5709 0.97H

1.3541

0.9722

0.9727 1.3559

0.9734

.5735 1.3576

C.9746

0.9752

1.3593
OF COMPFESSEO

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR1. OENSITY

2. OENSITY

3. OENSITY

RATIO, LIQUIO OENSITY/OEKSITY AT A RATIO, LIQUIO UENSITY/OENSITY AT A

, KG/OM3 eOILING

POILING

PRESSURE

PRESSURE C F 1 BAR, OIMENSICNLESSF 760 TCRR, OIMENSICNLESS

BAR 0.800 1.000 2.000 4.000 KP/CM 2 0.816 1.020 2.039 I.. 079 6.000 6.1188.000 8.15810.000 1 10.197 1 5.000

5.296

20.000 20.39425.000 25.49330.000

30.591 35.00035.690

40.000

40.789

95.0 -178.15

2.139

0.9650

0.9655 1.3459

0.9655

0.9660 1.3466 0.9661

0.9666 1.3473

t.9666

0.9671

1.3461 1

.9679 .9684

.3499

0.9692 0.9697

1.3517

0.9705

0.9710 1.3535

0.9717

0.9722

1.3552

0.9730

0.9735

1.3570

0.9742 0.9747

1.3587

95.1 -178.05

2.158

0.9645

0.9650 1.3452

0.9651

0.9656 1.3459

0.9656 0.9661 1.3467

0.9661 0.9666

1.3474 1

.5674

.9679

.3492

0.9667

0.9692 1.3510

0.9700 0.9705

1.3528

0.9713

0.9718 1.3546

0.9725 0.9730

1.3563

0.9737

0.9743

1.3581

95.2 -177.95

2.177

0.9640 0.9646 1.34450.9646

0.9651 1.3453 0.9651 0.9656

1.3460

0.9656

0.9662

1.3466 1

.9670 .9675

.3486

0.9683

0.9686 1.3504

0.9695

0.9701

1.3522

0.9708

0.9713

1.3540

0.9721

0.9726 1.3557

0.9733

0.9738 1.3574

95.3 -177.85 2.1960.9636

0.9641

1.3439

0.9641

0.9646 1.3446 0.9646

0.9652 1.3454

0.9652

0.9657 1.3461 1 .9665.9670 .3479

0.9678

0.9683 1.3458

0.9691

0.9696 1.3515

0.9703

0.9709

1.3533

0.9716 0.9721 1.35510.9728

0.9734 1.3568

95.4 -177.75

2.216

0.9631 0.9636 1.3432

0.9636 0.9642 1.3440 0.9642

0.9647 1.3447

0.9647

0.9652 1.3454 1 .9660.9665

.3473

0.9673

0.9676 1.3491

0.9686

0.9691 1.3509

0.9599

0.9704 1.3527

0.9711 0.9717 1.35440.9724

0.9729

1.3562

95.5 -177.65

2.235

0.9626

0.9631 1.3425

0.9632

0.9637

1.3433

0.9637

0.9642

1.3440

0.9642 0.9648

1.3448 1

.9656

.5661 .3466

0.9669

0.9674 1.3465

0.9662

0.96S7

1.3503

0.9694

0.9700 1.3520

0.9707

0.9712

1.3536

0.9719

0.9725 1.3555

95.6 -177.55

2.255

0.9621

0.9627

1.3419

0.9627

0.9632 1.3426

0.9632

0.9637 1.3434

0.9638

0.9643 C 1.3441 1

.9651

.9656 .3460

0.9664 0.9669

1.3476

0.9677

1.3496

0.9690

0.9695 1.3514

0.9702

0.5708

1.3532

0.9715

0.9720 1.3549

95.7 -177.45

2.275

0.9617

0.9622 1.3412

0.9622

0.9627 1.3420

0.9627

0.9633 1.3427

0.9633 t 0.9638 C 1.3435 1 .5646

.5651 .3453

0.9659

0.9665

1.3472

0.9672

0.9678 1.3490

0.9685

0.9690 1.3508

0.9698

0.5703

1.3525

0.9710 0.9716

1.3543

95.8 -177.35

2.29".

0.9612

0.9617 1.3405

0.9617 0.9623

1.3413

0.9623

0.9628

1.3421

0.9626 C 0.9633 1.3420 1

.9641

.3447

0.9655

0.9660

1.3465

0.9666 0.9673

1.3483

0.9681

0.9686

1.3501

0.9693

0.5698

1.3515

0.9706

0.9711 1.3536

95.9 -177.25

2.314

0.9607

0.9612 1.3399

0.9613

0.9618

1.34 6

0.9618

0.9623 1.3414

0.9623 C 0.9629 C 1.3422 1

.9637

.5642

. 344C

0.9650

0.9655 1.3459

0.9663

0.9666 1.3477

0.9676

0.9681 1.3495

0.9689

0.5694

1.3513

0.9701

0.9706 1.3530

96.0 -177.15

2.335

0.9602

0.9606

1.3392

0.9608

0.9613

1.3400

0.9613

0.9618 1.3407

0.9619

0.9624

1.3415

.5632 .5637

.3434

0.9645

0.9651

1.3452

0.9658

0.9664

1.3470

0.9671

0.9677 1.3488

0.9664

0.5689

1.3506

0.9697

0.9702

1.3524

96.1 -177.05

2.355

0.9598

0.9603

1.3385

0.9603

0.9606 1.3393

0.9608 0.9614

1.3401

0.9614

0.9619

1.3408 .5627

.5633 .3427

0.9641 0.9646

1.3446

0.9654

0.9659 1.3464

0.9667 0.9672

1.3482

0.5660

0.5685 1.3500

0.9692

0.9697

1.3517

96.2 -176.95

2.375

0.9593

0.9596

1.3379 0.9598

0.96 3 1.3386

0.9604

0.9609 1.3394

0.9609

0.9614

1.3402

.9623 .9626 .3420

0.9636

0.9641

1.3439

0.9649 0.9654

1.3457

0.9662

0.9667

1.3476

0.9675

0.9660

1.3493

0.9686

0.9693

1.3511

96.3 -176.85

2.396

0.9588

0.9593 1.3372

0.9593

0.9599 1.3380

0.9599

0.9604

1.3387

0.9604 0.9610

1.3395

.5618

.9623 .3414

0.9631

0.9636 1.3433

0.9644

0.9650

1.3451

0.9657

0.9663 1.3469

0.9670

0.9676 1.3487

0.9683

0.9668 1.3505

96.4 -176.75

2.416

0.9583

0.9568 1.3365 0.9589

0.9594 1.3373 0.95940.9599 1.3381

0.9600

0.9605 1.3388

.9613

.9618 .3407

0.9627

0.9632

1.3426

0.9640 0.9645

1.3444

0.9653

0.9658 1.3463

0.9666

0.9671

1.3481

0.9679

0.9684

96.5 -176.65

2.437

0.9578

0.9584 1.3359

0.9584

0.9589

1.3366

0.9589

0.9595

1.3374

0.9595

0.9600

1.3362

.9606

.9614 .3401

0.9622

0.9627

1.3419

0.9635

0.9640

1.3438

0.9648

0.9653 1.3456

0.9661

0.9666

1.3474

0.9674

0.9679 1.3492

96.6

-17 6.55 2.458

0.9574

0.9579

1.3352

0.9579

0.9564 1.3360

0.9585

0.9590 1.336T

0.9590

0.9595 1.3375 .3394

0.9617 0.9622

1.3413

0.9630

0.9636

1.3431

0.9644 0.9649

1.3450

0.9657

0.5662

1.3466

0^9675

1.3466

96.7 -176.45

2.479

0.9569 0.9574 1.3345

0.9574

0.9579 1.3353

0.95BO

0.9585 1.3361

0.9565 0.9591

1.3366 .9599

.5604

0.9613

0.9618 1.3406

0.9626

0.9631

1.3425

0.9639

0.9644

1.3443

0.9652

0.9657 1.3461

0.9665

0.9670

1.3475

96.8 -176.35

2.500

0.9564

0.9569 1.3339

0.9570

0.9575 1.3346

0.9575

0.9568

1.3354

0.9581

0.9586

1.3362

.5594

.5595 .3381

0.9608 0.9613

1.3400

0.9621 0.9626

1.3418

0.9634

0.9540

1.3437

0.5647 0.5653

1.3455

0.9665

1.3473

96.9 -176.25

2.522

0.9559

0.9564 1.3332

0.9565

0.9570 1.3340

0.9570

0.9575 1.3347

0.9576

0.9561

1.3355

.9590 .5595

0.9603 0.9606

1.3393

0.9616

0.9622

1.3412

0.9630 0.9635

1.3430

0.9643

.9648 0.9656

1.3467
DENSITY OF COMPRESSED LIQUID ARGON - CONTINUED

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO,

RATIO,

, KG/DM*

LIQUID DENSITY/DEN

LIOUID DENSITY/DEN

SITY AT A SITY AT A ROILING

BOILING PRESSURF

PRESSURE

OF 1 BAR, DIMENSIC

OF 760 TCRR, OIMEIn NLESS SICNLESS

BAR 0.600 1.000 2.000 4.000 KP/CM2 0.816 1.020 2.039 4.079

6.000

6.116

8.000 8.15810.000

10.197 15.00015.296 20.00020.394

25.000 25.49330.000

30.591 35.00035.690

40.000

40.769

97.0 -176.15

2.51.3

0.9551. 0.9559 1.33250.9560 0.9565 1.3333

0.9565

0.9571

1.3341

11.9571 0.9576

1.3346

0.5585

0.5590

1.3368

0.9598

0.9604 1.3387

0.9612 0.9617

1.3405

0.9625

0.9630 1.3424

0.5638 0.9643 1.34420.9651 0.9656

1.3460

97.1 -176.05

2.565

0.951.9 0.9555 1.3318

0.9555

0.9560 1.3326

0.9561

0.9566 1.3334

0.9566

0.9571 1.3342

0.5580 0.9585

1.3361

0.9594

0.9599 1.3380

0.9607

0.9612 1.3399

0.9620 0.9626

1.3417

0.9634

0.5639 1.3436

0.9646

0.9652

1.3454

97.2 -175.95

2.586

0.951.5 0.9550 1.3312

0.9550

0.9555

1.3319 0.9556

0.9561 1.3327

0.9561 0.9567

1.3335 0.5575

0.5580 1.3354

0.9589

0.9594 1.3373

0.9602

0.9606 1.3392

0.9616

0.9621 1.3411

0.9634

0.9642

0.9647 1.3447

97.3 -175.85

2.608

0.951.0

0.951.5 1.3305

0.9545 0.9551 0.9551

0.9556

1.3321

1.9557

0.9562 1.3326

0.9571 0.5576 1.33460.9584

0.9589

1.3367

0.9598 0.9603 1.3386

0.9616 1.3404

0.9624 0.9629

1.3423

0.9637

0.9643

1.3441

97.4 -175.75

2.630

0.9535

0.951.0 1.3298

0.951.1 0.9546

1.3306 0.9546

0.9551 1.3314

0.9552

0.9557

1.3322 0.5566

0.5571

1.3341 0.9579

0.9565

1.3360 0.9593

0.9598

1.3379

0.9606

0.9612 1.3398

0.9620

0.9625

1.3416

0.9633

0.9638

1.3435

97.5 -175.65

2.653

0.9530

0.9535

1.3291

0.9536

0.9541 1.3299

0.9541

0.9547 1.3307

0.9547

0.9552 1.3315

0.9561

0.9566

1.3334

0.9575

0.9560

1.3354

0.9588

0.9594 1.3373

0.9602

0.9607 1.3391

0.9615

0.9620

1.3410

0.9628

0.9633

1.3428

97.6 -175.55

2.675

0.9525

0.9530 1.3285

0.9531

0.9536

1.3293

0.9537

0.9542

1.3300

0.9542

0.9547

1.3308

0.9556 0.9561 1.33280.9570 0.9575

1.3347

0.9584

0.9589 1.3366

0.9597

0.9502 1.3385

0.9610

0.9616 1.3403

0.9624

0.9629

1.3422

97.7

-175. 1.5 2.697

0.9520

0.9525 1.3278

0.9526

0.9531 1.3286

0.9532

0.9537 1.3294

0.9537 0.9543

1.3302

0.9551

0.5557

1.3321

0.9565

0.9570 1.3340

0.9579

0.9584

1.1360

0.9592

0.9598 1.3378

0.9606

0.9611 1.3397

0.9619 0.9624

1.3415

97.8 -175.35

2.720

0.9515

0.9521 1.3271

0.9521

0.9526 1.3279 0.95270.9532

1.3287

0.9533

0.9538

1.3295 0.5547

0.5552

1.3314

0.9561

0.9566

1.3334

0.9574

0.9579

1.3353

0.9588

0.9593 1.3372

0.9601

0.9606 1.3390

0.9614

0.9619 1.3409

97.9 -175.25

2.71.2

0.9511

0.9516

1.3261.

0.9516

0.9521 1.3272 0.95220.9527 1.3260

0.9528

0.9533

1.3288

0.9542

0.5547

1.3308

0.9556

0.9561 1.3327

0.9570

0.9575 1.3346

0.9583

0.9588 1.3365

0.5596

0.5602 1.3384

0.9610

0.9615 1.3402

98.0 -175.15

2.765

0.9506

0.9511 1.3257

0.9511 0.9517

1.3265 0.9517

0.9522

1.3273

0.9523

0.9528

1.3261

0.5537

0.5542

1.3301

0.9551

0.9556

1.3321

0.9565

0.9570

1.3340

0.9578

0.9584 1.3359

0.9592

0.9597

1.3377

0.9605

0.9610 1.3396

98.1 -175.05

2.788

0.9501 0.9506

1.3251 0.9507

0.9512

1.3259 0.9512

0.9518 1.3267

0.5518

0.5523

1.3275 0.5532

0.9537 1.3294

0.9546

0.9551 1.3314

0.9560

0.9565 1.3333

0.9574

0.9579

1.3352 0.9587

0.9592 1.3371

0.9600

0.9606 1.3389

98.2

-17".. 95 2.811

0.91.96 0.9501

1.321.1. 0.9502

0.9507

1.3252

0.9508

0.9513 1.3260

0.9513

0.9516

1.3268

0.9527 0.5533

1.3286

0.9541 0.9547

1.3307

0.9555

0.9560

1.3327

0.9569

0.9574

1.3346

0.9582

0.9566

1.3364

0.9596

0.9601 1.3383

98.3

-171.. 85 2.835

0.9491

0.91. g6 1.3237

0.9497

0.9502

1.3245

0.9503

0.9506

1.3253

0.9508 0.9514

1.3261

0.9523

0.5526

1.3281

0.9537

0.9542

1.3301

0.9551

0.9556

1.3320

0.9564 0.9569

1.3339 0.9578

0.9583

1.3358

0.9591

0.9596 1.3377

98.1. -17*. 75 2.8580.91.66

0.91.91 1.3230 0.94920.91.97 1.3238 0.94980.9503 1.3246

0.9504

0.9509 1.3254 0.95180.5523

1.3274

0.9532

0.9537

1.3254 0.9546

0.9551

1.3313

0.9560

0.9565 1.3333 0.95730.9578

1.3351

0.9587

0.9592 1.3370

98.5 -174.65

2.882

0.91.81 0.91.66 1.32230.9487

0.9492 1.3231

0.9493

0.9498

1.3240

0.9499

0.9504

1.3248

0.9513

0.9516

1.3266

0.9527

0.9532 1.3267

0.9541

0.9546 1.3307

0.9555

0.9560 1.3326

0.9568 0.9574 1.33450.9582

0.9587 1.3364

98.6

-171.-55 2.905

0.9476

0.9481 1.3216

0.9482

0.9467

1.3225

0.9488

0.9493

1.3233

0.9494 0.9499

1.3241

0.9506 0.5513

1.3261

0.9522

0.9526

1.3281

0.9536 0.9542

1.3300

0.9550

0.9555 1.3319

0.9564

0.9569 1.3336

0.9577

0.9582

1.3357

98.7

-171.. 1,5 2.929

0.9471

0.9477

1.3210

0.9477

0.9482

1.3218

0.9483 0.9488

1.3226

0.9494

1.3234

0.5503

0.9509

1.3254

0.9518 0.9523

1.3274

0.9532 0.9537

1.3294

0.9545

0.9551 1.3313

0.9555

0.9564

1.3332

0.9573 0.9578

1.3351

98.8

-171.. 35 2.953 0.9466

0.9472 1.3203

0.9472

0.9478

1.3211 0.9478

0.9463

1.3219

0.9489

1.3227

0.9499

0.9504

1.3247

0.9513

0.9518

1.3267

0.9527 0.9532

1.3287

0.9541

0.9546 1.33060.9560

1.3325

0.9568 0.9573

1. 3344

98.9

-171.. 25 2.977

0.9462

0.91.67 0.9473

1.3204 0.9473

0.9478

1.3212

0.9479

0.9464

1.3220

0.5494

0.9499

1.3241

0.9508 0.9513

1.3261

0.9522

0.9527

1.3280

0.9536

0.9541

1.3300

0.5550

0.9555

1.3315

0.9563 0.9568

1.3336
TABLE 12 - CCNTINUEO DENSITY OF COMPPESSEO LIOUIO ARGON - CCNTINUEO

TAPLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. OENSITY

3. DENSITY RATIO, LIQUID OENSITY/OEK

RATIO, LIQUID DENSITY/DEN

KG/DC3 SITY AT A SITY AT A eCILING PRESSURE OF 1 BAR, 01 MENS UNLESS

BOILING PRFSSUPF OF 760 TCRR, OIMENSIONLESS

BAR 0.800 1.000 2.000 4.000 KP/CM2 0.816 1.020 2.039 "..079 6.000 6.118 8.158

10.000 10.197 15.000

15.296

20.000

20.394

25.000

25.493

30.000

30.591 35.000

35.690

40.000

40.769

99.0

-17".. 15 3.001

0.91.57

0.91.62 1.3189

0.91.63

0.91.68 1.3197 0.9468

0.9474

1.3205

0.9474

0.9479

1.3214 0.9489

0.5494

1.3231. 0.9503

0.9508

1.3254

0.9517 0.3522

1.1274

0.9531 0.9536

1.3293

0.9545

0.9550

1.3312

0.9559

0.9564

1.3331

99.1 -174.05

3.026

0.91.57 1.3162

0.91.58

0.91.63 1.3190

0.9464

0.9469

1.3199

0.S469

0.9475

1.3207 0.94891.3227

0.9498

0.9504

1.3247

0.9513

0.9518 1.3267

0.9527

0.9532

1.3286

0.9540

0.9546 1.3306

0.9554

0.9559

1.3325

99.2 -173.95

3.050

0.91.1.7 0.91.52 1.3175

0.91.53

0.91.58 1.3184 0.9459

0.9464 1.3192

0.9465

0.9470 0.9475

0.9484

1.3220

0.9494

0.9499

1.3240

0.9508 0.9513

1.3260

0.9522

0.9527

1.3280

0.9536 0.9541 1.32950.9549

0.9554

1.3316

99.3 -173.85

3.075

0.91.1.2 0.91.1.7 1.3168

0.91.1.8 0.91.53 1.3177 0.9454

0.9459

1.3185

0.9460 0.9465

1.3193

0.5474 0.9479

1.3214

0.9469 0.9494

1.3234

0.9503 0.9508

1.3254

0.9517

0.9522

1.3273

0.9531 0.9536 1.3293

0.9645

0.9550 1.3312

99. 4 -173.75

3.100

0.91.37

0.91.1.2 1.3161

0.<»443

0.91.1.8 1.3170 0.9449

0.9454 1.3178

0.9455 0.9460

1.3186

0.5465

0.5475

1.3207

0.9464 0.9489

1.3227

0.9498 0.9503

1.3247

0.9512

0.9517

1.3267

0.9526

0.9531 1.3286

0.9540 0.9545

1.3305

99.5 -173.65

3.125

0.91.32 0.91.37

1.3151.

0.91.38

0.91.1.3 1.31630.91.49 1.3171

0.9450

0.9455

1.3180

0.9465

0.9470

1.3200

0.9479

0.9484

1.33 2

0.9493

0.9499

1.3240

0.9508 0.9513

1.3260

0.9522

0.9527

1.3275

0.9535

0.9540 1.3299

99.6 -173.55

3.150

0.91.27

0.91.32

1.311.8

0.9433

0.91.38 1.3156

0.9439 0.9444

1.3164

0.9445

0.9450

1.3173

0.9460

0.5465

1.3193

0.9474

0.9479

1.3214

0.9489

1.3234

0.9503

0.9508 1.3253

0.9517

0.9522 1.3273

0.9531 0.9536

1.3292

99.7

-173.1.5 3.175

0.91.22

0.91.27 1.311.1

0.9428

0.91.33

1.311.9 0.9434

0.9439 1.3157

0.9440 0.9445

1.3166 0.5455

0.9460

1.3186

0.9469

0.9475 1.3207

0.9484

0.9489

1.3227

0.9498

0.9503 1.3247 0.9512

0.9517

1.3266

0.9526

0.9531 1.3266

99.8 -173.35

3.201

0. 9U17

0.91.22

1.3131.

0.91.23

0.91.28 1.311.2 0.9429

0.9434 1.3151

0.91.35 0.9440 1.3159

0.9450

0.5455

1.3180

0.9465

0.9470

1.3200

0.9479

0.9484

1.1220

0.9493

0.9498

1.3240

0.9507 0.5513

1.3260

0.9521 0.9526

1.3279

99.9 -173.25

3.227

0.91.12

0.91.17 1.3127

0.91.18

0.91.23 1.3135

0.9424 0.9429

1.3144

0.9430 0.9435

1.3152 0.5450 1.3173

0.9460 0.9465

1.3193

0.9474 0.9479

1.3214

0.9489

0.9494

1.3233

0.9503

0.9508

1.3253

0.9517

0.9522

1.3273

100.0 -173.15

3.252

0.91*07

0.91.12 1.3120

0.9413

0.91.18 1.3128

0.9419

0.9424

1.3137

0.9425

0.9430

1.3145

0.5440

1.3166

0.9455

0.9460

1.31S7

0.946° 0.9475

1. 3207

0.9484

0.9489

1.3227

.9498 0.9503

1.3247

0.9512

0.9517

1.3266

100.1 -173.05

3.278

0.91.02 0.91.07 1.3113

0.91.08

0.91.13 1.3121 0.9419

1.3130

0.91.20 0.91.25 1.3138

0.543? 0.5440 1.3155

0.94"=0 0.9455

1.31P0

0.9465 0.9470

1.1200

0.9479

1.3220

0.5493

0.5498

1.324C

0.9507 0.9512

1.3259

100.2 -172.95

3.301.

0.9397

0.91.02 1.3106

0.91.03

0.91.08 1.31 14

0.9409

0.91.14 1.3123

0.9415

0.9420

1.3131

0.5430

0.5436

1.315?

0.9445

0.9450

1.3173

0.9460

0.9465

1.3193

0.9474

0.9479

1.3214

0.9488 0.9494

1.3233

0.9502

0.9508 1.3253

100.3 -172.85

3.330

0.9392

0.9397 1.3099

0.9398

0.9403 1.3108

0.9404 0.9409

1.3116

0. 9410 0.9416

1.3125

0.5426

0.5431 1.3146

0.9440

0.9445

1.3166

0.9455 0.9460

1.1167

0.9469

0.9475 1.3207

0.9484

0.9465 1.3227

0.9496 0.9503 1.3246

100.1. -172.75

3.357

0.9387 0.9392 1.3092

0/9393

0.9398

1.3101

0.9399

0.9404

1 .3109

0.9406 0.9411

1.3118

0.5421 0.5426 1.31350.9436 1.3159

0.9450 0.9455

1.3180

0.9465

0.9470

1.1200

0.9475 0.5484

1.3220

0.9493

0.9496 1.3240

100.5 -172.65

3.383

0.9382 0.9387

1.3085

0.93 8 8 0.9393

1.3094 0.93941.3102

O.9401

0.9406

1.3111

0.5416

0.9421 1.313?

0.9431 0.9436

1.3153

0.3445 0.9450

1.1173

0.9460

0.9465

1.3193

0.5474 0.9479

1.3213

0.9488

0.9493

1.3233

100.6 -172.55

3.1.10

0.9377

0.9382

1.3078

0.9383

0.9388 1.3087 0.93890.9395

1.3095

0.9396 0.9401

1.3104

0.5411 0.5416

1. 3125

0.9426

0.9431 1.3146

0.9441 0.9446

1.3166

0.9455

0.9460 1.3187 0.9469

0.9475

1.3207

0.9484

0.9489

1.3227

100.7

-172.1.5

3.1.37

0.9372

0.9377

1.3071

0.9378 0.9383

1.3080 0.9384

0.9390

1.3068

0.9391

0.9396 1.3097

0.9406

0.5411

1. 311P

0.9421

0.9426 1.3139

0.9436

0.9441

1.3160

0.9450

0.9455 1.3180

0.9465 0.9470 1.32000.9479 0.9484

1.3220

100.8 -172.35

3.1.61.

0.9367

0.9372

1.3064

0.9373 0.9378 1.30730.9379

0.9365

1.3081

0.9386 0.9391

1.3090 0.5406

1.3111

0.9416

0.9421 1.3132

0.9431

0.9436

1.1153

0.9445

0.9451

1.3173

0.9460

0.5465

1.319 4

0.9474

1.3213

100.9 -172.25

3.1.91

0.9362 0.9367

1.3057

0.9368 0.9373 1.3066

0.9375 0.9380

1.3074

0.5381

0.9386

1.3083

0.9396 0.5401

1. 3104 0.9416

1.3125

0.9426

0.9431 1.3146

0.9441 0.9446

1.3167

0.9455

0.9460

1.3187

0.9469

0.9475

1.3207
COKPFESSED LICUID 'GON - CCNT

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUID OENSITY/DENSITY AT A 2. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 3. DENSITY, KG/0M3BOILING

BOILING PRESSURE

PRFSSURE

05 1 9AR, DIMENSICNLESS

OF 760 TCRR, DIMENSICNLESS

BAR 0.800 1.000 2.000 It. 000 KP/CM2 0.816 1.020 2.039 4. 079 6.000 6.118

e.oot

6.158 10.00010.197 15.000

15.296

20.000

20.391. 25.00025.1.93 30.000 30.591 35.00035.690

40.000 40.789

101.0 -172.15

3.518

0.9357

0.9362 1.3050

0.9363

0.9368 1.3059 0.93700.9375 1.3067

0.9376

0.9381

1.3076 0.9391

0.9396 1.3096

0.91.06

0.91.11 1.3119

0.9421

0.91.26 1.3139

0.9436

0.9441 1.3160

0.9450

0.5455

1.3180

0.9465

0.9470 1.3200

101.1 -172.05

3.51,6

0.9352

0.9357

1.301.3 0.9358

0.9363 1.3052

0.9365

0.9370

1.3060

0.9371 0.9376

1.3069 0.9386

0.9391 1.3091

0.91(01 0.9406

1.3112

0.91.16

0.91.21 1.3133

0.9431

0.9436

1.3153 0.94511.3174

0.9460

0.9465

1.3194

101.

-171.95

3.573

0.931.7 0.9352 1.30360.9353

0.9356

1.301.5 0.9359

0.9365 1.3053

0.9366

0.9371 1.3062 0.53810.9386

1.3084 0.9396

0.9402

1.3105

0.91.11

0.91.17 1.3126

0.9426

0.9431

1.3147 0.9441

0.9446 1.3167

0.9455

0.9460 1.3187

101.3 -171.85

3.601

0.931.2 1.30290.931.8 0.9353 1.3038

0.9351. 0.9360

1.301.6 0.9366 1.3055

0.9376

0J5381 1.3077

0.9392

0.9397

1.3098

0.91.07

0.91.12 1.3119

0.9421

0.9426 1.3140

0.5436 1.3160

0.9450 0.9456 1.3180

101.1, -171.75

3.629

0.9337

0.931.2 1.3022

0.931.3

0.931.6 1.3031

0.931.9 0.9355

1.3039

0.9356

0.9361

1.301.8

0.5371 0.5376 1.30700.9387

0.9392

1.3091

0. 91.02 0.91.07 1.31120.9417

0.9422 1.3133

0.9431

0.9436 1.3154

0.9446

0.9451 1.3174

101.5 -171.65

3.657

0.9332 0.9337

1.3015

0.9338

0.931.3 1.3021.

0. 931.1. 0.931.9 1.3032TJ.9351 0.5356 0.5366

0.5371 1.3063

0.9382

0.9387

1.3081,

0.9397

0.91.02 1.3106

0.9412

0.9417 1.3126

0.9426 0.9432

1.3147

0.9441

0.9446

1.3167

101.6 -171.55

3.685

0.9327

0.9332 1.3008

0.9333

0.9338 1.3017

0.9339

0. 931.1. 1.3025

0.931.6 0.9351

1.3034

0.9361 0.5366 1.30560.9377

0.9382 1.3078

0.9392 0.9397

1.3099

0.9407

0.9412 1.3120 0.94220.9427

1.3140

0.9436

0.9441

1.3160

101.7

-171.1.5

3.711, 0.9322

0.9327 1.3001

0.9328 0.9333

1.3010

0.9331. 0.9339 1.3018

0.931.1

0.931.6 1.3027 0.9356

0.9361

1.301.9 0.9372

0.9377

1.3071 0.9387

0.9392 1.3092

0.9402

0.9407

1.3113 0.9417

0.9422 1.3133

0.9431 0.9437 1.3154

101.8 -171.35

3.71,2

0.9316

0.9322

1.2991.

0.9323

0.9328 1.3002 0.93290.9331. 1.3011

0.9336

0.931.1 1.3020

0.5351 0.9356

1.3042

0.9367

0.9372

1.306".

0.9382

0.5387

1.3085

0.9397

0.9402 1.3106

0.5412 0.5417

1.3127

0.9427 0.9432

1.3147

101.9 -171.25

3.771

0.9311 U29860.9318

0.9323 1.2995

0.9321. 0.9329 1.3004

0.9331

0.9336

1.3013

0.931.6 0.5351

1.3035

0.9362

0.9367

1.3057

0.9377

0.9382 1.3076

0.9392

0.9397

1.3099

0.9412

1.3120

0.9422

0.9427

1.3140

102.0 -171.15

3.800

0.9306

0.9311 1.2979

0.9313

0.9318 1.2986

0.9319

0.9321. 1.2997

0.9326

0.9331 1.3006

0.531.1 0.931.7 1.3026

0.9357

0.9362

1.3TJ50

0.9372

0.9377 0.9387

0.9393

1.3093

0.5402

0.9407

1.3113

0.9417 0.9422 1.3134

102.1 -171.05

3.829

0.9301 0.9306 1.2972

0.9308 0.9313 1.2981

0.9311. 0.9319

1.2990

0.9321

0.9326

1.2999

0.5336

0.531.2 1.3021

0.9352 0.9357

1.301.3

0.9367 0.3373

1.3065

0.9363

0.9388

1.3086- 0.9398

0.9403

1.3107

0.9412

0.9417 1.3127

102.2 -170.95

3.856

0.9296

0.9301

1.2965

0.9303

0.9308

1.2971. 0.9309

0.9311. 1.2983

0.9321

1.2992

0.5331 0.5337

1.3011. 0.9352 1.3036

0.3363

0.9358 1.3058

0.9378 0.9383

1.3079

0.5393 0.5396

1.3100

0.9408

0.9413 1.3120

102.3 -170.85

3.887

0.9291 0.9296

1.2958

0.9296 0.9303

1.2967

0.9301. 0.9309

1.2976

0.9311 0.5316

1.2985

0.9326 0.5332 1.3007

0.931.2 0.931.7 1.3029

0.9358

0.9363

1.3051

0.9373

0.9378

1.3072 0.9388

0.5393

1.3093

0.9403

0.9408 1.3114

102.1. -170.75

3.917 0.9286

0.9291

1.2951

0.9292 0.9297

1.2960 0.9299

0.9301. 1.2969

0.9305 O.9310

1.2978 0.9321 0.9326

1.3000

0.9337

0.931.2 1.3022

0.9353

0.9358

1.3041. 0.9368

0.9373

1.3065 0.5383

0.5388

1.3086

0.9398 0.9403

1.3107

102.5 -170.65

3.91.6

0.9281

0.9286

1.291.1. 0.9287

0.9292

1.2953

0.9291. 0.9299 1.2962

0.9300

0.9305 1.2971 0.5316

0.9321 1.2993

0.9332

0.9337

1.3015

0.9348

0.9353

1.3037 0.9363

0.9368

1.3059

0.9378 0.9383

1.3080

0.9393

0.9398

1. 3100

102.6 -170.55

3.976

0.9276

0.9281 1.2937

0.9282

0.9287

1.291.6

0.9289

0.9291. 1.2955

0.9295

0.5300

1.2961.

0.9311 0.5316

1.2986

0.9327 0.9332

1.3009

0.9343

0.9348

1.303P

0.9358

0.9363

1.3052

0.5373

0.F378 1.3073

0.9388

0.9393

1.3094

102.7

-170.1.5

11.006

0.9277

0.9282 1.2939

0.9284 0.9289

1.291-8

0.9290

0.9295 1.2957 0.9306

0.5311 1.2975

0.9322

C.9327

1.3002

0.933P 0.9343

1.3023

0.9353

0.9358

1.3045 0.9369 0.53741.3066

0.9384

0.9389

1.3087

102.8

-170. 35 4.0 36

0.9272

0.9277

1.2932

0.9279

0.9281. 1.291.1

0.9285

0.9290

1.2950

0.5301

0.5306 1.2972

0.9317

0.9322 1.2995

0.9333

0.9338

1.3017

0.9348

0.9354

1.3038

0.9364

0.9369

1.3059

0.9379

0.9384 1.3080

102.9 -170.25

4.067 0.9267

0.9272

1.2921.

0.9271. 0.9279 1.2934

0.5280

0.9285

1.291.3 0.5301 1.2965

0.9312

0.9317

1.29? S

0.9328 0.9333

1.3010

0.9344

0.9349 1.3031

0.9359

l!3053

0.9374

0.9379

1.3074
CONTINUED OF COMPRESSEO LIQUIO

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, I 2. OENSITY RATIO, I 3. OENSITY, KG/OM3 IOUIO OENSITY/OENSITY AT A IQUIO OENSITY/OENSITY AT A FOILING PRESSURF OF BOILING PRESSURE OF

1 BAR, OIMENSICNLESS

760 TCRR, OIMENSIONLFSS

BAR O.80O 1.000 2.000 '•.000 6.000 KP/CM2 0.616 1.030 2.039 It. 079 6.118

8.000

8.156 10.00010.197 15.000

15.296

20.000

20.391. 25.00025.1.93 30.000 30.591 35.000 35.690

*0.000 *0.789

103.0 -170.15

*.097

0.9262

0.9267

1.2917

0.9266

0.9273

1.2926

0.9275

0.9280 1.2936

0.9291

0.9296 1.2958

0.9307

0.9312

1.2981

0.9323

0.9128

1.3003

0.9339

0.931.1. 1.3021.

0.9351. 0.9359

1.301.6

0.9369 0.937*

1.3067

103.1 -170.05

<>.128

0.9257

0.9262 1.2910

0.9263

0.9268 1.2919

0.9270

11.9275 1.2929

0.9266

0.9291 1.2951

0.9302

0.9307

1.2971.

0.9316 0.9323

1.2996

0.933". 0.9339 0.93*9 0.935*

1.3035

0.936*

0.9369

1.3060

103.2 -169.95

*.159

0.9252

0.9257

1.29 3 0.9256

0.9263

1.2912

6.9265

0.9270 1.2921 0.52810.9286 1.29**

0.9297

0.9302 1.2967

0.9313

0.9318

1.2989

0.9329

0.9331. 1.3011

0.93** 0.93*9

1.3032

0.9359

0.9365 1.3053

103.3 -169.85

"..190

0.921.6 0.9251

1.2896 0.9253

0.9258

1.2905

0.9260 0.9265

1.2911.

0.9276

0.9281 1.2937

0.9292 0.9297

1.2960

0.9308

0.9313

1.2982

0.932". 0.9329

1.300". 0.9339

0.93**

1.3025

0.9355

0.9360 1.30*7

103. * -169.75

l*. 221

0.921.1

0.921.6 1.2889

0.921.8 0.9253 1.28980.9255

0.9260

1.2907

0.9271

0.5276 1.2930

0.9287

0.9292 1.2953

0.9303

0.9308 1.2975

0.9319

0.932". 1.2997 0.93350.93*0

1.3019

0.9350

0.9355

1.30*0

103.5 -169.65

*.252

0.9236

0.921.1 1.2881

0.921.3

0.921.8 1.2891

0.9250 0.9255 0.9266

0.5271 1.2923

0.9282

0.9267

1.29*6

0.9298

0.9303

1.2966

0.9311. 0.9319

1.2990

0.9330

0.9335

1.3012

0.93*5

0.9350 1.3033

103.6 -169.55

*.28*

0.9231

0.9236

1.2871. 0.9238

0.921.3

1.2881.

0.921.9 1.2893

0.9261

0.9266 1.2916

0.9277

0.9282

1.2939

0.9293

0.9298

1.2961

0.9309

0.931". 1.2983

0.9325

O.9330

1.3005

0.93*0

0.93*5 1.3026

103.7

-169.1.5 *.316

0.9226

0.9231 1.2867

0.9233

0.9238 1.2876

0.9239

0.921.1. 0.5256

0.9261 1.2905

0.9272

0.9277

1.2932

0.9288 0.9293

1.2951.

0.930". 0.9309

1.2976

0.9320

0.9325

1.2998

0.9335

0.93*0

1.3020

103.8 -169.35

*.3*7

0.9221 0.9226 1.2860 0.9227

0.9232 1.2869

0.9231. 0.9239 1.26790.5251

0.9256 1.2902

0.9267

0.9272 1.2925

0.9283

0.9288

1.291.7

0.9299

0.930". 1.2970

0.5315 0.9320

1.2991

0.9330 0.9335 1.3013

103.9 -169.25

*.379

0.9215

0.9220 1.2853 0.9222

0.9227

1.2862

0.9229

0.9231. 1.2871

0.921.6 0.5251 1.2895

0.9262

0.9267 1.2918

0.9278 0.9283

1.29*0

0.929". 0.9299

1.2963

0.5310

0.9315

1.2985

0.9326

0.9331 1.3006

10".. -169.15

'..',12

0.9210

0.9215

1.281.6

0.9217

0.9222

1.2855

0.9221. 0.9229

1.2861.

0.521.1 0.521.6 1.26880.9257

0.9262

1.2911

0.9273 0.9278

1.2933

0.9289

0.929". 1.2956

0.9305

0.9310

1.2576

0.9321

0.9326

1.2999

101..

-169.05

0.9205

0.9210

1.2836

0.9212

0.9217

1.281.8

0.5219

0.9221. 1.2857

0.5236

0.521.1 1.2881

0.9252

0.9257

1.2901.

0.9268

0.9273 1.2926

0.928". 0.9289

1.291.9

0.9300

0.9305

1.2571

0.9316

0.9321 1.2993

10"..

-168.95

*.*77

0.9200

0.9205

1.2831

0.9207 0.9212

1.281.0

0.9211. 0.9219

1.2850

0.5230

0.9235

1.2871.

0.921.7 0.9252 1.28970.9263

0.9269

1.2919

0.9280 0.9285

1.291.2

0.5295

0.9300 1.256*

0.9311 0.9316 1.2986

10<..

-168.85

"..509

0.9195

0.9200

1.2821. 0.9202

0.9207

1.2633

0.9206 0.9213

1.281.3 0.5225

0.5230 1.2866

0.921.2

0.921.7 1.2890

0.9258

0.9263 1.2912

0.9275

0.9280 1.2935

0.9290 0.5295

1.2957

0.9306

0.9311 1.2979

101.. 1, -168.75

"..51.2

0.9189

0.9191. 1.2816

0.9196

0.9201 1.2826

«. 9203

0.9208

1.2836

0.9220 0.9237

0.921.2 1.2883

0.9253

0.9258

1.2905

0.9270 0.9275

1.2928 0.9286

0.5291

1.2950

0.9301

0.9306

1.2972

101..

-168.65

"..575

0.9181. 0.9189

1.2609 0.9191

0.9196 1.2819

0.9198 0.9203

1.2628

0.5215 0.5220

1.2e52

0.9232

0.9237

1.2875

0.921.6 0.9253

1.2898

0.9265

0.9270

1.2921

0.9281

0.9286 1.29*3

0.9296

0.9301 1.2965

101..

-168.55

*.609

0.9179

0.9181. 1.2802

0.9186

0.9191

1.2811

0.9193

0.9198 1.2821

0.9210 0.9215

1. 281.5

0.9227 0.9232

1.2868

0.921.3

0.921.6 1.2891

0.9260 0.9265

1.291".

0.9276

0.9281

1.2937

0.9291

0.9296 1.2959

10"..

-168.1.5

It. 61,2

0.9171. 0.9179

1.2791.

0.9181

0.9186

1.2601.

0.5188 0.9193

1.2611.

0.9205 0.5210

1.283P

0.9222

0.9227

1.2861

0.9238

0.921.3 0.9255 1.2907

0.9271 0.5276

1.2930

0.9287

0.9292 1.2952

101..

-168.35

l.. 676

0.9169 0.9173 1.2767

0.9176

0.9160 1.2797

0.9183

0.9187

1.2807

0.5200

0.5205

1.2831

0.9217

0.9222

1.2851.

0.9233 0.9238

1.2877

0.9250 0.9255

1.2900

0.9266 0.5271

1.2923

0.9282 0.9287

1.2°*5

101..

-168.25

*.709

0.9163 0.9166

1.2780

0.9170

0.9175 1.2790

0.9177 0.9182

1.2799

0.5195

0.9200 1.2823

0.9212 0.9217

1.281.7

0.9228

0.9233

1.2870

0.921.5 0.9250 1.28930.9261

0.5266

1.2916

0.9277

0.9262
OF COPPRESSEO LIQUID ARGON - CONTINUED

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, DENSITY RATIO, LIQUID DENSITY/DENSITY

DENSITY RATIO, LIQUID OENSI TY/DENSITY

OENSITY, «G/Df3

105.2 L67.95

1..812

105.3 167.85

4. 81,6

105.1, 167.75

i.. 881

105.5

L67.65

"..916

105.7

-167. ".5 "..986

106.1, 166.75 5.237

106.9 -166.25

5.1,23

0.9158 0.9165

0.9163

1.2773 1.2782 9153

9158

2765

911.8 9152

2758

9132 9137

27 36

9126

9131

2728

9089

9091. 2677

9079

9083

2662

9097 9102

2687

9075

9060 2657

9077

2653

9206 0.9223

9211 0.9228

2863

9196

9211 2826

9121| 9129

2725

911<. 9119

2711

0.921,0 0.921,5 1.2886

92 35

92".0 2879

9230 9235

2872 9225

9230 2865

9220

972 5

2 3 5 8

921 9215

231.1.

9205 9210

2137
TABLE 12 - CONTINUED DENSITY OF COMPPESSEO LIQUID APGC

TEMPERATURE, K TEMPERATURE, C VAPOR PRESSURE, BAR

rABLE ENTRIES

DENSITY RATIO, DENSITY RATIO,

DENSITY, KG/Of

107.0 L66.1S

5.1,60

107.1

L66.05

5.1.98

107.2

L65.95 5.536

107.3 165.65

5.571,

107.5 165.65 5.651

107.7

165.1.5 5.729

108.0 165.15

6.81,7

108.2

161.. 95 5.926

0.9052

0.9057

1.2621. 0.9059

0.9 061. 1.2635

9051. 9059 2627

9025

90 30 2587

9009

9013

256".

8992

8997

251.1

901.3

901.8 2612

9032

9037

2597

9027

9032

2590

9005

9010 2560

696? 8972

2506

8956 8961

21.91

9061

9066

2638

0.9121

0.9126

1.2721

9072 9077

2653

9061

9066 2638

9027 9032

2 C 9C

90 19 90 21. 2579

91 39

911.1. 271,5

9072 9077

2652

9062

9066

2638
TABLE 12 OENSITY OF CCfPRESSEO LIOUI

TEMPERATIRE, K TEMPERATURE, C l/APOR PRESSURE, BAR1. OENSITY RATIC

2. OENSITY RATIC

3. OENSITY, KG/C

109.0

L6<t.l5 6.253

109.2

L63.95 6.336

109.3

163.85 6.378

109. <t L63.75

6.1.20

109.5 L63.65

6.1*63

109.7

-163.1.5

6.51.8

109.9 L63.25 6.635

110.5 -162.65 6.899

110.6 162.55

6.91.1.

110.7

-162.1.5 6.969

1.21.95 1

891.5 8950

21.76

8929

8931. ?U53

ee°o 8895

? 3 9 9

e862 8867

2359

8960

8965

21.97

8°13 8917

21.29

017 0.903

?539

3985

8973

8977

2511.

8935

891.0

21.62

8986

e991 2533
COHPRESSEO LIQUID

TAPLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSITY RATIO, LIQUID OENSITY/DEXSITY AT A 2. DENSITY PATIO, LIQUID OENSITY/OENSITY AT A 3. OENSITY, KG/DM3 FOILING

FOILING

PRESSURE OF 1 BAR, OIMEKS ICNL ESS PRESSURE OF 760 TCRR, OIMEtvSIONLESS

BAR 0.800 1.000 2.000 4.000 6.000 8.000 10.000 KP/CM* 0.816 1.020 2.039 4.079 6.118 e.158 10.197 15.000

15.296

20.000

20.391, 25.00025.1,93 30.00030.591

35.000 35.69040.000

40.769

111.0 -162.15

7.125

0.8839 0.881,8

0.881,1, 0.8853 1.2326 1.231,0

0.6869

0.8871. 1.2370

0.8690 0.8895 1.2398

0.8910

0.1915

1.21,27

0.8930 0.8935 1.24550.8950

0.8954 1.2482

0.8969

0.8973 1.2508

112.0 -161.15

7.592

0.6781 0.8791 0.8767 0.8796

1.221.9 1.2261

0.8813

o.eeie 1.2292

0.8B35

0.861,0 1.2322

0.8856

0.8661 1.2351

0.8876

0.8881

1.2360

0.8896

0.8901

1.2408

0.8916

0.8921 1.2435

113.0 -160.15

8.061

0.8731. 0.8736

1.7181 0.8757

0.8761 1.2213

0.8779

0.8781,

1.221.1. 0.S801

0.8805

1.2271, 0.8622

0.6827 1.2304 0.8643

.8848 1.2333

0.6863

0.8868

1.2361

1JA.0 -159.15

6.592

0.6675

0.6680

1.2099

0.8699

0.8701. 1.2132

0.8722

0.8727

1.2165 0.87501.2196

0.8767

0.6772

1.2227

0.8788

0.8793

1.2257

o.eeio

0.8614 1.2286

115.0 -158.15

9.126

0.8616

0.8620 1.2016 0.86m0.8645

1.2051

0.8665

0.6669

1.2061,

0.8668 0.8693

1.2117

0.8711 0.8716

1.2149

0.8733

0.8738 1.2180

0.8755

0.8760

1.2211

116.0 -157.15

9.663

0.6555

0.8560

1.1932

0.8531 0.8586 1.19680.6606

0.8611 1.2D03

0.9631

0.8635

1.2037

0.3654

0.8659 1.207O

0.9678

0.6662

1.2102

0.8700

0.8705

1.2134

117.0 -156.15

10.261,

0.8521 0.8525

1.1883

0.851,7 0.8551 1.19200.8572

0.8577

1.1955

0.8597

0.8601 1.1990

0.8621

0.8626 1.2023

0.8644

0.8649

1.2056

-155.15

10.670

0.81,5?

0.81,63 1.1797

0.81,86

0.81,91 1.1636

0.8513

0.9517

1.1872

0.8538

0.8543

1.1908

0.6563

0.8568

1.1943

0.6588

0.8592

1.1977

119.0

-15".. 15 11.500

0.839E

0.61,01 1-1710 0.84250.61,29 1.1750

0.81,52

0.91,57 1.1798

0.8479 0.8484

1.1825

0.8605

0.8510

1.1862

0.8530

0.8535

1.1897

120.0 -153.15 12.156

0.8332

0.8336 1.1620

0.6362

0.8366

1.1662

0.9391

0.9395 1.1732

0.6419 0.8423

1.1741

0.8446

0.8450

1.177?

0.8472 0.8477

1.1816

121.0 -152.15 12.839

0.8271 1.152?

0.6298

0.8302

1.1572

0.9328

0. 3332 1.1615

0.8357

0.9362 1.1655

0.8365

0.6390

1.1695

0.8413 0.8417

1.1733

122.0 -151.15

13.51,8

0.819?

0.8203

1.11,3?

0.8232

0.8236

1.11,81

0.3261, 0.9268

1.1525

0.8294

0.8299

1.1568

0.8324

.8328 1.1609

0.8353 0.8357

1.1649

123.0 -150.15

11,. 285

0.8130

0.ei34

1.133?

0.8165

0.8169

1.1387

0.9198 0.9203

1.11,31.

0.8230

0.8235

1.1479

0.8261 0.8266

1.1522

0.8291

0.8296 1.1564

121,. -11,9.15 15.051

0.8096

0.8100 1.1291

0.9131 0.8136

1.1340

0.9165 0.8169

1.1387

0.8197

0.6202

1.1433

0.8229

0.8233 1.1476

125.0

-11,8.15 15.645

0.6025

0.8030 1.1193

0.3062

0.8067

1.1245

0.8098

0.3102

1.1294

0.8132

1.1342

0.8165

0.8169

1.1387

-11,7.15 16.668

0.7953

0.7957

0.7992

0.7996

1. 1146

0.8029 0.8034

1.1198

0.8065

0.8070

1.1249

0.6100

0.6104

1.1297

127.0

-11.6.15 17.522

0.7878 0.7882

1.0967

0.7919

0.7924

1.1045

0.7959

0.7963

1.1100

0.7?97

0.8001

1.1153

0.8033

0.8038 1.1204

128.0

-11,5.15

16.1,06

0.7800

0.7801. 1.0879

0.7845

1.0941

0.7887

0.7391 1.0999

0.7927

0.7931 1.1055

0.7965

0.7969

1.1109

129.0

-ll.it. 15 19.322

0.7720

0.7721. 1.0766

0.7767

0.7771 1.0833

0.7812

0.7816

1.0895

0.7855 0.7859

1.0955

0.7895

0.7899

1.1011

130.0

-11,3.15 20.271

0.7667

0.7691

1.0721

0.7735

0.7739

1.0788

0.7780

.7765 1.0851

0.7823

0.7e26

1.0911
DENSITY OF COMPRESSEO LIQUID ARGON

TABLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. OENSITY

RATIO, LIQUID DENSITY/DENSITY AT RATIO, LIQUID OENSITY/OENSITY AT KG/DM*A BOILING

A BOILING PRESSUREPRESSURE

OF 1 BAR, DIMENSIONLESS

OF 760 TCRR, DIMENSI CNLFSS

BAR 0.800 1.000 2. KP/CM2 0.816 1.020 2. 000 *.000

039 *.079

6.000 8.000 10.000 15.00 6.118 8.158 10.197 15.29

20.000

E 20.39*

25.000 25.*9330.000

30.591 35.000 *0.00035.690 *0.7B9

131.0

-11.2.15 21.253

0.7608 1.0605

0.7656

0.7660 1.0677

0.770* 0.77*9 0.7708 0.775* 1.07** 1.0808

132.0

-1 1.1.15 22.268

0.7517

0.7521

1.0*8*

0.7573

0.7577

1.0562

0.7625 0.7673 0.7629 0.7677

1.063* 1.0702

133.0

-11.0.15 23.318

0.7*26

0.7*30 1.0357

0.7*86

0.7*91

1.0**1

0.75*2 0.759*

0.75*6 0.7599 1.0519 1.0592

13*. O -139.15 2*.*0*

0.7330

0.733*

1.0223

0.7196

0.7*00 1.0315

0.7*57 0.7513 0.7*61 0.7517 1.0*00 1.0*78

135.0 -138.15

25.525

0.7301

0.7305 1.0183

0.7367 0.7*26 0.7371 0.7*32 1.0276 1.0359

136.0 -137.15 26.6850.7201

0.720*

1.00*3 0.7273 0.7339 0.7277 0.73*3 1.01** 1.0236

137.0 -136.15 27.882

0.7093

0.7097

0.9893

0.717* 0.72*6

0.7178 0.7250 1.0005 1.0106

138.0 -135.15 29.1180.6978

0.6981 0.9732

0.7069 0.71*9 0.7072 0.7152 0.9858 0.9970

139.0

-131.. 15 30.391.

0.6955 0.70*5 0.6959 0.70*9 0.5700 0.9825

1*0.0 -133.15

31.711

0.6832 0.693* 0.6836 0.6938 0.9529 0.9671

1*1.0 -132,15

33.071

0.6697 0.681* 0.6701 0.6818

0.53*0 0.950*

1*2.0 -131.15 3*,*730.65** 0.668* 0.65*8 0.6687 0.9127 0.9322

1*3.0 -130.15

35.920

0.6538

0.65*2 0.9119

1**.0 -129.15 37.*12

0.6372

0.6375 0.8887

1*5.0 -128.15

38.951

0.6173 0.6177

0.8610

9. PARAHYDROGEN

The data for parahydrogen tabulated here are based on the monograph by Roder,

et al. (1965). Additional, extensive tables of values based on this source were prepared by

McCarty and Weber (1972) for NASA. The tables for the saturated liquid were calculated using the explicit equations for vapor pressure (Weber, et al. , 1962) and saturated liquid density (Roder, et al. , 1963) which were incorporated unchanged into the final compilation

(Roder, et al. , 1965). The values for temperatures near room temperature were taken from

Hilsenrath, et al. (1955), using a high order interpolation. This is the source used by the experimenters in their determination of the liquid densities. The CGA pamphlet P-6 cites Dean (1961), who also presents a high order interpolation of Hilsenrath' s values. Values near room temperature are given in table 13, uncertainties for the data in table 14, values for the saturated liquid are given in table 15, and values for the compressed liquid are shown in table 16. As stated before, these values do not differ from those presented in Table 13 Density of Parahydrogen Near Atmospheric Pressure and Room Temperature

Temperature Pressure Density Volume

gram- mole/cm kg /dm3 cm3 /gram- mole dm3 kg 0°C 1 bar

760 torr 4.4004xl0~ 5 4.4588xl0~ 5 8.8709xl0~ B 8.9885xl0~ 5 22725.

22428.

11273.

11125. 15°C 1 bar

760 torr

4. 17l6xl0~ 5 4.2268xl0" 5 8.4097xl0-6 8.5210xl0~ 5 23972. 23658.11891.

11735. Density Ratios - Dimensionless

Liquid Density at a boiling pressure of 1 bar ' /density at 1 bar and 0° C

Liquid Density at a boiling pressure of 1 bar /density at 1 bar and 15° C

798. 52 842.31

Liquid Density at a boiling pressure of 760 torr /density at 760 torr and 0°C

Liquid Density at a boiling pressure of 760 torr/density at 760 torr and 15° C

787.50

830.73

Liquid density at a boiling pressure of 1 baj 0.07084 kg/dm£ Liquid density at a boiling pressure of 760 torr 0.07079 kg/dm3

95
the CGA pamphlet P- 6 . An astute observer may detect a difference of one part in 4000 in the density at the boiling point at 760 torr between this table and pamphlet P-6, but that difference

is caused only by accumulative rounding errors. The properties presented here pertain to parahydrogen. Specifications for delivery

of parahydrogen are usually stated as 95% parahydrogen with the remainder being ortho- hydrogen. As a matter of fact, producers do not send less than 97% parahydrogen to storage

tanks, and the liquid when shipped is, or is very close to being, equilibrium hydrogen.

Equilibrium parahydrogen is 99.79% para at the boiling point at 760 torr, and the difference between it and 95% parahydrogen amounts to about 0.008 K or about 2 mm in pressure. It is easy to see that sophisticated equipment is required to detect ortho-para composition. The

matter of composition is mentioned because the amount of orthohydrogen present has a very pronounced effect on the length of storage but only a very slight effect on the density.

Table 14 Uncertainties in the Data for Parahydrogen

variable uncertainty range of temperature temperature 0.02 K

0.015 K

triple point to critical point room temperature volume 0.1%

increases to 0.3%

0.01%

triple point to 32 K

near critical room temperature

pressure 0.05% 0.01%triple point to critical point room temperature

96
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DENSITY CF COMPRESSED LIQUIO HYDROGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO,

2. DENSITY RATIO,

3. OENSITY, KG/DM*

LIQUIO OENSITY/OENSITY AT A eOILING PRESSURE OF LIQUID OENSITY/OENSITY AT A BOILING PRESSURE OF1 BAR,

760 TCRR PENSICNLf CIMENSI

ssNLESS

BAR KP/CM*0.800 1.000 0.816 1.020 2.000

2.039

3.000

3.059 I.. 079 5.000 5.099

6.000

6'. 118 7.000 7.138

8. O00 8.158 9.177

0.000 0.1971.000

1.217 2.000

19.5 -253.65

0.801

1.0116

1.0121. 0.0 7166

1.0135

1.011.2

0. 07179

1.0153 1.0160 0.07192

1.0171 1.0178

0.07205 1.0189

1.0196

0.07217

1.0206

I. 0214 0i07230 1.02241.0231 0.07242

.0241 .0248 07254

.0258

.0265 07266

.0274

.0282 07278

.0291

.0296 07290

.0307

.0314

07301

19.6 -253.55

0.827

1.0101 1.0108

0.07155

1.0119 1.0126

0.07168

1.0138

1.011.5 0.07181

1.0156 1.0163

0.07191.

1.0171. 1.0181

0.07207

1.0191

1.0199 0.07219 1.0209

0.07232

.0226

.0233

07244

.0243

.0250

07256

.0260

.0267 07268

.0276

.0284 07275

.0293

.0300

07291

19.7

-253.1.5 0.653

1.0085

1.0092 0.071M.

1.0101. 1.0111

0. 07157

1.0122 1.0129

0.07170

1.011.0

1.011.8 0.07183 1.0158

1.0166

0.07196

1.0176

1.0181. 0;07208

1.0194

1.0201 0.07221

.0211

.0218

07233

.0228

.0236 07245

.0245 .0252 07257.0262

.0269 07269

.0279 .0286

07281

19.8 -253.35

0.860

1.0069

1. 0076

0. 07133

1.0088

1.0095

0.0711.6 1.0107

0.07159

1.0125 1.0132 0.071721.011.3 1.015O 0.071851.0161 1.0168 0.071981.0179 1.0186 0.07210

.0196 .0204

07223

.0214

.0221 07235

.0231 .0236 07247

.0247 .0255 07255.0264

.0271 07271

19.9 -253.25

0.907 1.0053

1.0060

0.07121 1.0072

1.0079

0. 07135

1.0091 1.0098

0.0711.8 1.0109

1.0117

0. 07161 1.0128 1.0135

0.07171.

1.011.6 1.B153

0.07187 1.0164

1.0171 0.07200

.0181 .0189 07212.0199 .0206

07224

.0216

.0223 07237

.0233

.0240 07249

.0250 .0257

07260

20.0 -253.15

0.935 1.0037 LOOM.0.07110 1.0056 1.00630. 07123

1.0075 1.0082 0.07137

1.0091. 1.0101

0. 07150 1.0112 1.0119

0.07163

1.0131

1.0138 0.07176 1.014?1.0156

0.07185

.0173 07201

.0184 .0191

07214

.0201 .0208

07226

.0225

07238

.0235

.0242

07250

20.1 -253.05

0.961.

1.0021

1.0028

0.07098

1.001.0

1.001.7 0.07112

1.0059

1.0066 0.07126 1.0O78 1.0085

0.07139

1.0097

1.0101. 0.07152

1.0115

1.0122 0.07165

1.0133

1.0140

0.0717?

.0151 .0158

07191

.0169

.0176

07203

.0186 .0193

07216

.0204 .0211

07228

.0221

.0228 07240

20.2 -252.95

0.993

1.0001. 1.0O11

0.07087

1.0021. 1.0031

0. 07101

1.001.3 1.0060

0.07111. 1.0062

1.0069

0.07128 1.0061

1.0088

0.0711.1

1.0099 1.0107 0.07154 1.0118

1.0125 0.07167

.0136 .0143

07160

.0154

.0161 07192

.0171

.0178 07205

.0185 .0196 07217.0206

.0213

07229

20.3 -252.85

1.023

1.0008

1.0015 0.07089

1.0027

1.0031. 0.07103

1.001.6 1.0053

0.07116

1.0065 1.0072

0.07130

1.0084 1.0091

0.-07143 1.01O2

1.0109

0.07156

.0121 .0128

07169

.0138 .0146

07182

.0156

.0163 07194

.0174

.0181 07207

.0191

.0198 07219

20.1. -252.75

1.053 0.9991

0.9998 0.07077

1.0011 1.0016

0.07091

1.0030 1.0037 0.07105

1.001.9 1.0056

0.07119

1.0068

1.0075 0;07132

1.0097

1.0094 0.07145

.0105

.0112

07158

.0123

.0130

07171

.0141

.0148 07184

.0155

.0166 07196

.0176

.0183

07208

20.5 -252.65

1.0 81. 0.9975

0.9982

0.07066

0.9991. 1.0002

0.07080

1.0011. 1.0021

0.07091. 1.0033

1.001.0 0.07107

1.0052

1.0059 0.07121

1. 0071 1.0078 0.07134.0090 .0097 07147.0108 .0115

07160

.0126 .0133 07173.0144

.0151 07186.0169

07198

20.6 -252.55

1.116

0.9958

0.5965

0. 07051. 0.9978

0.9985 0.07068

0.9998 1.0005

0.07082

1.0017

1.0021. 0.07096

1.0036

1.O043 0.07109 1.00551.0062 0.07123

.0074

.0081 07136

.0092

.0099

0714?

.0111

.0118 07162

.0126

.0136 07175

.0146 .0153 07187

20.7

-252.1.5

1.11.9

0.991.1

0.991.8

0. 0701.2

0.9961

0.9966 0.07056

0.9991

0.9988

0.07070

1.0001

1.0008

0.07081.

1.0020 1.0027 0.070981.0039

1.0046 0.07111.0065 07125

.0077 .0084

07138

.0095

07151

.0120 07164

.0131

.0138 07176

20.8 -252.35

1.182

0.9921. 0.9931 0.07030

0.991.1. 0.9951

0.0701.1.

0.9965

0.9972

0. 07059 0.9984

0.9992

0.07073

1.0004 1.0011 0.07086

1.0023 1.003t

0.07100

!o049

07114

.0061 07177 n.0080

.0087 07140

.009e

.0105 07153

.0116

.0123 07166

20.9 -252.25

1.216

0.99 07 0.9911. 0.070180.9927

0.9935 0.07032

0.991.8 0.9956

0.0701.7 0.9968

0.9975

0.07061

o!9995 0.07075

1.0014 0.07085

.0026

.0033

07102

.0045 .0052 07116.0064

.0071 07129

.0082

.0089 07142

.0100

.0108 07155

21.0 -252.15

1.250

0.9889

0.9897

0. 07005

0.9910 0.9917 0.070200.9931

0.9938 0.07035 0.99510.9958

0.0701.?

0.9971 0.07063

0.9991

0W5998 0.07077

.0010

.0017

07O91

.0029

.1036 0710U

.0048 .0055

07118

.0067

.0074 07131

.0085

.0092 07144

21.1 -252.05

1.285

0.9872 0.9879

0. 06993

0.9893

0.9900 0.07008

0.9911. 0.070230.9935

0.991.2 0.07037

0.5955

0.9962 0.07052

0.9975 0.5982

0.07066

.9994

.0001 07079

.0013

.0020 07093

.0032

.0039

0'107

.0051

.0058

D7120

.0070 .0077 07133

21.2 -251.95

1.321

0.9855

0.9862

0. 06981

0.9876

0.9883 0.06996

0.9897

0.9901. 0.07011

0.9918

0.9925 0.07025

0.9938

8.9945 0.07040

0.5956

0.9966

0.07051.

.9978

.9965 0706S

.9997 .0004

07082 1

.0016

.0024 07095

.0035

.0042 07105

.0054

.0061 07122

21.3 -251.85

1.357

0.9837

0.06968

0.9859

0.9866

0.9880 0.9887 0.069990.9901

0.9908 0.07013

0.5921 0.5926 0.07028

0.5942 0.5949

0.07042

.9961 .9968 07056.9981

.9996

07070 1

.0000

.0007 C7084

.0027

07097

. 0038 .0045

07111

21.1. -251.75

1.395

0.9819 0.9626

0. 06956

0.981.1 0.981.6 0.06971 0.9863

0.9870 0.06986

0.9881. 0.9891

0.07001

9.5904

0.9911 0.07016 0.9925

0.9932 0.07030

.9945 .9952 07045.9955 .9972 07059

.9984

.9991 07072

.0003

.0011 07086

.0022

.0030 0709?
»ei_E 16 - CONTINUED DENSITY OF COMPRESSED LIQUID HYDROGEN

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE,

r RATIO, L

1 RATIO, L 1, KG/OM3

21.5 251.65

1.1.33

21.6 251.55

1.471

21.7 251.45

1.511

0.9784

0.9790

0. 06930

0.9765

0.9772

0.06917

0.9B23

0.9630

0. 06959

0.9806

0.9813

0. 06946

0.9828 0.9835 3.06961

0.9866

0.9873

0.06989

0.9832

0.9839

0.06964

0.9887

0.9894 0.07004

0.9870 0.9877 0.06592

0.9353 (.9860 0.06980

0.590e 0.9915

O.070ie

0,9891

0.9896 0.07006

0.9928

0.9935 0.07033

J. 9932

1.9939

.07035

0.9952

0.9959

1.07049

0.9935

0.9942 0.07038

0.5567 1.0007 0.9994 1.0014 0.07075 0.0708»

0.9971 0.9991 0.9978 0.9598 0.07063 0.07077

0.9955 0.9974 0.9962 0.9981 0.07052 0.07065

0.9792 0.9799

3.06936

0.9836

0.9843

1.06967

0.5857

0.5864

0.06982

0.9878 0.9885

1.06997

0.9898 O.9905

0.07012

0.9919

0.9926 0.07026

0.9939 0.9958 0.9946 0.9965 0.07040 0.07054

21.9 251.25

1.592

o.9eie

0.9825 0.06955 06965 0.070

0.9710

0.9717

0.06878

0.9733

0.9740

D. 06895

0.9756 0.9763

0.06911 0.9779

0.5785

0.06927

.9906 0.9913 3.07017

0.9738 0.9745 0.06698

0.97F1 0.9768

0.06914

0.990 0.9916 0.07019

0.5672

0.9679 0.06851

0.9765 8.5772 0.06917

0.9787

0.5794

D. 06933 0.06993 0.07007

0.9653

0.9660

0. 06838

0.9676

0.9664 0.06855

0.9701

0.9708 0.06872

0.9747 0.9754 0.069040.979

0.979 0.0693

0.9613

0.9820

0.06°51 .06966 0.06981

0.9876 0.9883 0.06996

0.9634

0.9641

0. 06824

0.9682

0.9689 0.06859

0.9706

0. 06875

0.9729

0.5736

1.06891

22.5 -250.65

1.855

0.9614

0.9621

0.06810

0.9663

0.9670 0.06845

0.5710

8.9717 0.06879

0.5733 0.5740

0.06695

0.9821 0.9828 0.06957

0.9842 0.9649 0.06972

0.9595 0.9601

0. 06796

0.9620 0.964 0.9692 0.5699

1.06865

0.9782

0.9789

1.06929

0.5803

0.5810 0.06944

22.7 -250.45

1.949

0.9575

0.9581 0.06782

0.9742

0.9749

0.06901

0.9764

0.9771 1.06917

22.8 -250.35

1.997

0.9555

0.9561

0.06766

0.9580 0.9567

1.06786

0.9606 0.9612

1.06604 0.06622 0.06839 0.0ee56

0.9747

D.9753

.36904

22.9 -250.25 2.047

0.9560 0.9567

0. 06772

0.9635

8.9642 0.06825

3.9729

0.9736

1.06891

0.9751 0.9758

0.06507

0.9773

0.9780 1.06923

23.0 -250.15 2.096

0.9566 0.9573

0.06776

0.5733 0.5740

0.06895

0.9755 0.9762 0.06910

23.1 -250.05 2.147

0.9546 0.9572 9892 0.5715 0.9737 9699 0.9722 0.9744 06760 0.06798 0.06798 0.06616 0.06833 0.06849 0.06866 0.06882 0.06898

0.56? 0.962 0.06616

23.2 -249.95 2.199

0.9552

0.9559

0.06766

0.9627 0.9651 0.9634 0.9657 0.06819 0.06636

0.9720 0.9726

1.06e85

0.9506 0.9513 0.06734

0.5533

0.9590 0.06736

0.9608 0.9632

0.9615 0.9639

3.06806 0.06823

0.9458

0.9465

. 06700

5545 0.557 0.9589 0.9613 0.9595 0.9620

3.06792 0.0630<=

0.9684

0.9690 0.06659
TAELE 16 - CONTINUED DENSITY OF COMPRESSED LIQUID HYDROGEN - CONTINUEC

TAPCE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. OENSIT

2. DENSIT

3. OENSIT

Y RATIO,

Y RATIO,

Y, KG/DM J LIQUID OENSITY/DENSITY AT A LIOUID OENSITY/DENSITY AT A BCILING

BOILING

FRESSURE PRESSURE

OF 1 BAR, OIMENSIC

CF 760 TCRR, CIMEN NLESS SICNLFSS

BAR 0.800 i.000 2.000 3.000 KF/CM2 0.816 1.020 2.039 3.059

it. *.079 5.000

5.099

6.000 6.118 7.000

7.138 8.0003.158

9.000 9.17710.000

10.197 11.000

11.217

12.000 12.237

23.5 -2*9.65

2.360

0.91.37 0.06685

0.91.65

0.91.72 0.06705

0.91.92

0.91.99 0.06721.

0.9518

8.9525

0.0671.2

0.951.1. 0,9551

0.06761

0.9569

0.9576 0.06778

0.9591. 0.9601 0.06796

0.9618 0.9625 0.06313

0.961.2 0.96*9

0.9665 0.967? 0.06e*6

23.6

-2<t9.55

2.1(15

0.91.16 0.91.23 0.06670

0.91.1.1. 0.91.51 0.06690

0.9A71

0.91.78 0.06709

0. 91.98 8.9505 0.067280.9521. 0.9531

0.0671.7

0.9550

0.9556 0.06765

0.9575 0.9582

0.06782

0.9599

0.9606 0.9623 0.9630 0.06817

0.96*7

0.965* 0.06633

23.7

-21.9.1.5 2.1.71

0.9395

0.91.01 0.06655

0.91.23

0.91.30 B.06675

0.91.51

0.91.57 0.06695

0.91.78

0.91.81. 0.06711.

0.9501. 0.5511 0.067320.9530 0.9537

0.06751

0.9555

0.9562 0.06769

0.9580 0.9587

0.06786

0.960* 0.5611 0.068030.9628

0.9635 0.06820

23.8

-21.9.35 2.526

0.9373 0.9380 0.06639

0.91.02

0.91.08 0.06660

0.91.30

0.91.37 0.06680

0.91.57

0.91.61. 0.06699

0.51.81. 0.51.91 0.06718

0.9510

0.9517 0.06737

0.9536

0.951.3 0.06755

0.9561

0.9568 0.06773

0.9586 0.5592

0.06790

0.9610 0.9616 0.06807

23.9

-21.9.25 2.586

0.9351 0.9358

0.06621.

0.9380 0.9387

0.0661.5

0.91.09

0. 91.16 0.06665

0.9*37

0.91. 1.3 0.06685

0.51.61. 0.51.70 0.06701.

0.91.90

0.91.97 0.06723 0.9516

0.9523

0.0671.1

0.951,2

0.951,8 0.06759

0.9566 0.5573 0.067770.9591 0.9598 0.0679*

21.. -21.9.15

2.61.5

0.9329 0.9336 0.066080.9359

0.9365 0.06629

0.9367

0.9391. 0.06650

0.°*16

0.91.22 0.06670

0.91. l»3 0.91.50 0.066890.91.70

0.91.77 0.06708

0.91.96 0.9503 0.06727

0.9522

0.9529

0.0671.5

0.55*7

0.955* 0.06763

0.9572

0.9579 0.06780

2*.l

-21.9.05 2.705

0.9307

0.9313 0.06592

0.9337

0.931.3 0.06611. 0.9373

0. 06631.

0.9395

0.91.01 0.06655

0.91.23

0.91.25 0.06675

0.91.50

0.91.56 0.06691.

0.91.76

0.91.83 0.06713

0.9502

0.9509 0.06731

0.9528

0.9535 0.067*9

0.9553

0.9560 0.06767

21. .2 -21.8.95 2.766

0.9281. 0.9291 0.065760.9315

0.9321

0.06598

0.931.!. 0.9351

0.06619

8.9373

0.9380

0.0661.0

0.51.02

0.91.08 0.06660

0.91.29

0.91.36 0.06679

0.91.56

0.91.63 0.06698

0.91.83

0.91(89 0.06717

0.9508

0.9515 0.06735

0.953*

0.95*0 0.06753

21..

-21.8.85 2.828

0.9261 0.92E6 0.065600.9292 0.9299 0.06582 0.9322

0.9329

0. 06601.

0.9352

0.9358

0.06621. 0.9380

0.9387

0.0661.5

0.91.09

0.91.15 0.06665

0.91.36

0.91.1.3 0.06691.

0.91(62

0.91(69 0.06703 0.9*95

0.06721

0.951*

0.9521 0.06739

21.. * -21.8.75 2.891

0.9238

0.921.1. 0.0651.1.

0.9270

0.9276

0. 06566

0.9300

0.9307

0.06588

8.9330 0.9337 0.066090.5359

0.9366 0.06630

0.9387

0.9391. 0.06650

0.91(22 0.06669

0.91.1.2 0.91.1.9 0.06689 0.9*69

0.9*75

0.06707

0.9*95

0.9501 0.06726

21..

-21.8.65

2.951.

0.9211. 0.9221 0.065270.921.6 0.9253

0.06550 0.9278

0.928*

0.06572

0.9306

0.9315 0.06593

0.9338

0.531.1. 0.06611.

0.9366

0.9373 0.06635

0.9395

0.91.01 0.06655

0.91.22 0.91.29 0.06671.0.9**9

0.9*55

0. 06693

0.9*75

0.9*82 0.06712

21. .6 -21.8.55 3.019

0.92 2 3 0.9230 0.06533

0.9255

0.9262

0.06556

0.9286

0.9293

0.06578

0.9316 0.9322

0.0659<=

0.931.5 0.9352 0.066200.9373

0.9380

0.0661.0

0.91,01 0.91.08 0.06660

0.9*28

0.9*35 0.06675

0.9*55

0.9*62 0.06696

21..

-21.8.1.5 3.085

0.9200

0.9206 0.06517

0.9232

0.9239

0.0651.0

0.9261. 0.9270 0.06562

0.9291. 0.9301 0.065830.9323

0.9330

0.06601.

0.9352 0.9359

0.06625

0.9380

0.9387

0.0651.5 o!9*15 0.0666*

0.9*35 0.9**2 0.06683

21..

-21.8.35 3.152

0.9176 0.9183

0.06500 0.9209

0.9215

0.06523

0.921.7 0.0651.6 0.9272

0.9278

0.06568

0.9302 0.9308

0.06589

0.9331 0.9338

0.06610

0.9359

0.9366 1.0663O

0.5387 0.939*

0.06650

0.9*15

0.9*21 0.06669

21..

-21.8.25 3.220

0.9152 0.9159

0.061.83 0.9186

0.9192

0. 06507

0.9J18

0.9221. 0.06530 0.9256 0.06552

0.9280

0.9286

0.06571.

0.9309

0.9316

0.06591.

0.9338

0.931.5 0.06615 0.9367

0.9373 0.06635

0.939*

0.9*01 0.06655

25.0

-21.8.15 3.288

0.9128

0.9135

0.061.66

0.9162 0.9169

0.061.90

0.9195

0.9201 0.06513

0.9226 0.9233

0.06536

0.9258

0.9261. 0.065S8

0.9288

0.9291. 0.06579

0.9317

0.9321(

n. 06600

0.93*6 0.9352 0.06620

0.9373

0.9380 0.066*0

25.1

-21.8.05 3.358

0.9101. 0.9110

0.061.1.9

0.9138

0.911.5

0. 061.73 (.9178

0.061.97

0-920*

0.9210 0.0651?

0.9235

0.921.1 0.0651.2 0.92660.927?

0.05561.

0.9296

0.9302 0.06585

0.532*

0.9331 0.06605

0.9353

0.9359 0.06625

25.2

-21.7.95

3.1.29

0.9079

0.9085

0.061.31 0.91H. 0.91200.061.56

0.911.8

8.9151. 0.061.80

0.9181 0.5187 0.065030.9212 0.9219

0.06526

0.921.3 0.9250

0.0651.8

0.9Z7l( 0.9280 0.06569

0.5303 0.9310 0.06590

0.9332

0.933e 0.06610

25.3

-21.7.85 3.501

0.9051. 0.9060

0.061.13 0.9089

0.9096

0.061.39

0.9121. 0.9130

0.061.63 0.9157

0.9161. 0.061.87

0.9190

0.9196 0.06510

C.9221 0.9227 0.05532

0.9252 0.9258

0.06551. 0.9282

0.9288 0.06575

0.9311 0.9317 0.06595

25.1. -21.7.75

3.571,

0.9028

0.9035 0.06395

0.9065

0.9071

0.061.21

O.9100

0.9106

0.061.1.6

0.9131.

. 061.70

0.9167

0.9173 0.06*°3

0.9198

0.9205 0.06516

0.9229 0.9236 0.06538

0.9260 0.5267 0.065590.9289

0.9296 0.06580
TAELE 16 - CONTINLEC OF COMPRESSED LIQUID HYOROGEN - CCNTINUEC

TAELE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY RATIO,

2. OENSITY RATIO,

3. DENSITY, KG/DC 3 LIQUIO OENSITY/CEKSITY AT A LIQUID OENSITY/OEt-SITY AT A eCILING PRESSURE OF 1 BAR, DIMENS ICNL ESS BOILING PRESSURE OF 760 TCRR, OIMEKSIONLFSS

BAR 0.8C0 1.000 2. KP/CM? 0.616 1.020 2. 000 3.000 1..00 039 3.059 i(.079 5.000

5.099

6.000 7.000

6.118 7.136

8.000 8.158

9.000

9.177 10.00010.197 11.00011.217

12.000

12.237

25.5

-2147.65

3.61,8

0.9003 0.9009 0.063770. 9040 0.9046

0.06403

0.9075 0.9110

1.9062 0.'9116 0.06428 0. 06453

0.9143

0.9150 0.06477

0.9176

0.9182 0.06500

0.9207

0.9214

.06522

0.5238

0.5244 0.06544

0.9268

0.9274 0.06565

25.6

-21,7.55 3.723

0.8977

0.8983 0.06359 0.9014

0.9021

0.06385

0.9050 0.9085

8.9057 0.9092

0i06411 0.06436

0.9120

0.9126

0.9153

0.9159 0.06483

0.9185

0.9191 .06506

0.9216

0.9222 0.06528

0.9246

0.9252 0.06549

25.7

-21.7. 1.5 3.799

0.8950

0.8956

0.0631(0 0.8989

0.8995

0.06367

0.9025 0.9061

1.9032 0.5068

0.06393 0.06419

0.9O96 0.9102 0.06443

0.9129

0.9136

0.06467 0.9162

0.9166

.06490 0.9193

0.9200 0.06512

0.9224

0.9230 0.06534

25.8

-21.7.35 3.877

0.8923

0.8929

0.06321

0.8962

0.8968

0.06348

8.9000 0.9036

8.9007 0.5043

0.06375 0.06401

0.9O72

0.9O78 0.06426

0.9105 0.9112

0.06450

0.9139

0.9145

). 06473

0.9171

0.5177 0.06496

0.9202

0.9206 0.06518

25.9

-21.7.25

3. 955

C.8896

0.8902

0.06301 0.8936

0.8942

0. 06330

8.8975 0.9012

0.6981 0.9016 0.06357 0.06383

0.9047

0.9054 0.06409

0.9082

0.9088 0.06433

0.9115

0.9122 0.06457

0.5148

0.9154

0.06480

0.9180 0.9186 0.06502

26. o -21.7.15 4.035

0.6909

0.8915

0.06311

0.8948 0.8986

0.8954 0.6993

0.'06338 0.06366

0.9O23

0.9029 0.06391

0.9058

0.9064 0.909Z

0.9098

0. 06440

0.5125

0.9131 0.06464

0.9157

0.9164 0.06486

26.1

-21.7.05 4.115

0.6882

0.8888 0.06292

1.8922 0.e960

0.8928 0.6966

0.06320 0.06347

0.8996 0.9004 0.06374

0.9033

0.9040 0.06399

0.9068

0.9074 0.06423

0.9101

0.9108 0.06447

0.9134

0.9141 0.06470

26.2

-21.6.95 4.197

0.8855

0.8861 0.06272

6.6895 0.8934

8.8901 0.891,0 0;06301 0.06329

0.8972

0.8979 0.06356

0.9009

0.9015

0.06381

0.9044

0.9050 0.06406

0.9078

0.5084 0.06430

0.9111

0.9116 0.06454

26.3

-21.6.85 4.280

0.882?

0.6833

0.06252

0.8868 0.8906

0.8874 0.6914

0.06282 0.06310

0.8946

0.8953 0.06337

0.8984

0.9990

0.06364

0.9020 0.9026 0.063890.9054

0.9061 0.06414

0.9088

0.9094 0.06437

26.1. -21.6.75 4.364

0.8797

0.6803

0.06232

0.8841 0.6681

0.8847 o.eeae

0.06262 0.06291

0.8920

0.8927 0.06319

0.9958

0.9964

0.06346

0.8995

0.9001 0.06372

0.5030 0.5037

0.06397

0.9064

0.9071 0.06421

26.5

-21.6.65

Ii.itit9

0.8769

0.8775

0.06211

0.8812 0.8854

0.8918 0.6861

0.06242 0.06272

0.8894

0.8901 0.06300

0.8933 0.3939

0.06328

0.8970

0.8977 0.06354

0.9006 0.9012

0.06380

0.9041

0.9047 0.06404

26.6

-21.6.55 4.535

0.8748

0.6746

0.06191

8.8784 0.8827

O.e7=0 0.6833

0.06222 0.06253

0.8868 0.8874 0.06262

0.9907 0.063090.8945

0.9951 0.06336

0.6981 0.06362

0.9017 0.9023 0.06387

26.7

-21(6.1(5 4. 623

0.8710

0.8716

0.06170

0.8755 0.e796

8.6761 0.6605

0.06202 0.06232

0.6841 0.6847 0.06263

0.9867

0.06 291

0.8919

0.8925 0.06J18

0.6956

0.6963 0.06344

0.8993

0.8999 0.06370

26.8

-21(6.35 4.712

0.6679

0.6665

0.06148

0.e726 0.e770

0.8732 0.6777

0.06161 0.06213

0.8813 0.8819 0.06243

0.8854

0.9861 0.06272

0.8893

0.8900 0.06300

0.6931 0.8937 0.063260.8968

0.8974 0.06353

26.9

-21.6.25 0.8649

0.8655

0. 06126

8.e697 0.671,2 0.8703 0.e746

0.06161 0.06193

0.8765 0.062230.9828 0.8834

0.06253

0.9867

0.9874 0.06281

0.6906

0.8912 0.06305

0.8943

0.8949 0.06335

27.0

-21.6.15 4.892

0.8618

0.8624

0.06104

0.e666 0.6713

8.8672 0.6715 0.06139 0.06172

0.8757

0.8763 0.06203

0.9800

0.3806 0.06233

0.8841

0.9847 0.06263

0.6880

0.6886 0.06290

0.8518

0.8924 0.06317

27.1

-21.6.05 4.985

0.6586

0.8592

0.06082

0.e536 0.e684

8.6642 0.6690 0.06117 0.06151

0.8729 0.8735 0.06163

0.9772 0.8778 0.062140.8814

0.9820 0.6854.8860 0.06272

0.8893

0.8899 0.06299

27.2

-21.5.95 5.078

0.8605 0.6653

0.8611 0.6659

0.06095 0.06130

0.8700

0.8706 0.06163

0.9744

0.9750 0.06194

0.8787

0.8793 0.06224

0.8828 0.8834 0.06253

0.8867

0.8673 0.06281

27.3

-21.5.85 5.173

0.e573 0.e623

0.6=79 0.6629

0.06073 0.06106

0.8670

0.6676 0.06142

0.8716 0.9722 0.8759

0.8765 0.06205

0.6801 0.6807 0.06234

0.8841 0.8847 0.06263

27.1. -21.5.75 5.269

0.6541 0.e592

0.6547 0.'6598 0.06050 0.0608F

0.8641 0.8647

0.06121

0.9697

0.8693 0.06154

0.9731

0.9738 0.06185

0.8774

0.6780 0.06215

0.8814

0.8621 0.06244
TAELE 16 - CONTINIEO DENSITY OF COMPRESSED LIQUID HYDROGEN

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR1. DENSITY RATIO, LIQUID OENSITY/OEKSITY AT A 2. DENSITY RATIO, LIQUID DENSITY/DENSITY AT A 3. DENSITY, KG/DM3 eCILING FOILING

PRESSURE OF PRESSURE OF

1 BAR, DIKENSICNLESS

760 TCRR, OIMENSICNLESS

BAR 0.8C0 1.000 2.000 3.000 4.000 5.000 6.000 7.000 KP/CM? 0.816 1.020 2.039 3.059 it. 079 5.099 6.118 7.138 8.000

8.158 9.0009.177

10.000 11.000

10.197 11.217

12.000

12.237

27.5

-21,5.65 5.366

B.8507 0.6561

8.8513 0.8567 0.06026 0.06064

0.8610 0.8617 0.06099

0.8658 0.8664

0.05133

0.8703 0.8746

0.8709 0.8753

.06165 0.06196

0.8788

0.8794 0.06225

27.6

5.l,6<t

0.8473 0.8527

0.6479 0.8533

0.06002 0.06040

0.8580

0.6586

0.06TJ78

0.8628

0.8634 0.06112

0.9674 0.8719

0.9680 0.8725

.06144 0.06176

0.8761 0.8767 0.06206

27.7 -245.45

5. 564

0.B439 0.8495

8. 8445 0.8501

0.05978 0.06017

0.8548

0.8555 0.06O55

0.8598

0.8604

0.06090

0.8645 0.8691

0.8651 0.8697

.06124 0.06156

0.8734

0.8740 0.06187

27.8

-21.5.35 5.665

0.8404 0.8462

0.8410 0.8468 0.05953 0.05994

0.8515

0.8522 0.06O32

0.8567

0.8574

0.06069

0.8616 0.8662

0.3622 0.e668

.06103 0.06136

0.8706

0.8712 0.06167

27.9

-21.5.25 5.767

0.8368 0.8428

0.8374 0.8434

0.05928 0.05970

0.8483

0.84e9

0.061)09

0.9535

0.9541 0.06046

0.8586 0.8633

0.8592 0.8639

.06082 0.06115

0.8678 0.06147

2S.0

-21.5.15 5.871

0.8332 0.8393

8.«338 0.e399

0.06902 0.0S945

0.8450

0.8456 0.05986

0.8504

o.esio 0.06024

0.8555 0.8604

0.8561 0.6610

.06060 0.06094

0.8650 0.8656 0.06127

28.1

-2lt5.05 5.976

0.8295 0.8358

1.8301 0.8364

0.05876 0.05920

0.8417 0.8423 0.059620.8472

0.3478 0.06001

0.8524 0.8574

0.8530 0.e580

.06038 0.06073

0.8621

0.8627 0.06107

28.2

-2itit.95 6.082

0.8322

o.e32e 0.05895

0.8382

0.8388 0.05939

0.8439 0.9445

0.05978

0.8492 0.8544

0.8499 0.8550

.06016 0.06052

0.8592

0.8598 0.06086

28.3

-2ltlt.85 6.189

0.8285 0.6291

0.05869

0.8347

0.8353 0.05913

0.9406

0.9412 0.05954

0.8461 0.8512

0.8467 0.8518

.05993 0.06030

0.8562

0.8568 0.06065

28.lt -2l.lt.75 6.298

0.e24f 0.8252 0.058410.8312 0.8318

0.05888

0.3372 0.9378

0.05930

0.8428 0.8481

0.8434 0.8487

.05970 0.06008

0.8532

0.8538 0.06043

28.5

-21tlt.65 6.<t08

0.820E

o.e2i4 0.05614

0.8275 0.8281 0.058620.9337

0.8343

0.05906

0.8395 0.8450

0.8401 0.8456

.05947 0.05985

0.8501

0.8507

28.6

-21.1,. 55 6.519

o.eis? 0.8174 0.05786

0.8237 0.8243

0.05835

0.3302

0.3308 0.05891

0.8361 0.8417

0.8367 0.8423

.05923 0.05953

0.8470

0.8476 0.06000

28.7

-21.lt.lt5 6.632

0.8128 0.8134 0.05758

0.8199

0.8205 0.05808

0.9266 0.3272

0.05855

0.9327 0.9384

0.3333 0.8390

.05899 0.05939

0.8439 0.8445 0.05978

26.8

-2l.lt. 35 6.746

o.eose 0.8092

0.05728

0.8160 0.057810.3228 0.9234

0.05829

0.8292 0.8351

0.8298 0.8357

.05374 0.05916

0.8407 0.8413 0.05955

28.9 -244.25

6.861

0.8043 O.e04 c 0.0E69e0.6121 0.6126 0.057520.8191

0.8197 0.05802

0.8257 0.6317

0.8262 0.8323

.15849 0.05692

0.8374 0.8380 0.05932

29.0 -244.15

6.978

0.799?

0.8005

0.05666

0.81)79

0.61)85 0.05723

0.9152

0.9158 0.05775 n

0.9220 0.6283

0.8225 0.8289 .05822 0.05867

0.8341

0.8347 0.05909

29.1 -244.05

7.096

0.8037 0.8043 0.05693

0.8113

0.9119 0.05747

0.8183 0.8247

0.8188 0.8253

.05796 0.05642

0.8308

0.8313 0.05685

29.2 -243.95

7.216

0.7994

0.8000 0.05663

0.8072

0.3078 0.05718

0.9145 0.6211

0.8150 0.8217

.05769 0.05816

0.8279 0.05661

29.3 -243.85

7.337

0.7949 0.056310.9031

0.?037 0.05689

0.8106 0.6174

0.3111 0.8190

."5742 0.05790

0.8238 0.8244 0.05836

29.4 -243.75

7.459

0.7902 0.7908 0.05598

0.7994

0.05659 " 0.8066 0.ei37

0.8071 0.8143

.05713 0.05764

0.8203

0.8206 0.05610
IELE 16 - CONTINUFC rSSEO LIOUIO HYOPOGEN - CONTINUEC

TABLE ENTRIES

1. TEMPERATURE, K 2. TEMPERATURE, C

3. VAPOR PRESSURE, BAR

1. DENSITY

2. DENSITY

3. DENSITY

RATIO, LIQUID DENSI TT/OENSI TY AT A RATIO, LIQUID OENSITY/DENSITY AT A KG/0M3

BOILING

BOILING PRFSSURE OF 1 HAR, DIMENS ICNLESS PRESSURE OF 760 TCRR, OIMENSICNLFSS

BAR 0.800 1.000 2. KP/CM* 0.816 1.020 2. 000 3.000

039 3.059

"..000 5.000 6.000 7.000

1..079 5.099 6.118 7.138

8.000

8.158

9.000 10.000 11.000 12.000 9.177 10.197 11.217 12.237

29.5

-21.3.65 7.583

0.7B55

0.7860

0.05561.

0.79".". 0.8025 0.8098 0.8166 0.7950 0.8031 0.8101. 0.8172 0.05627 0.05685 0.05737 0.05785

29.6

-21.3.55 7.709

0.7805

0.7811 0.05529

0.7899 0.7983 0.8059 0.8130 0.7905 0.7989 0.8065 0.8135 0.05595 0.05655 0.05709 0.05759

29.7

-2".3. 1.5 7.836

0.775". 0.7759

0.051.92

0.7852 0.791.0 0.8019 0.8092 0.7858 0.791.6 0.8025 0.8097 0.05562 0.05621. 0.05680 0.05732

29.8

-21.3.35 7.96*

0.7700

0.7706

0.051.5".

0.7801. 0.7896 0.7978 0.8053 0.7810 0.7901 0.7981. 0.8059 0.05528 0.05593 0.05651 0.0570".

29.9

-2<.3.25

8.091.

0.775". 0.7350 0.7936 0.801". 0.7760 0.7356 0.791.1 0.8019

0.051.93 0.05561 0.05621 0.05676

30.0

-21.3.15 6.225

0.7702 0.7303 0.7892 0.7973

0.7708 0.7309 0.7898 0.7979

0.051.56 0.05528 0.05591 0.056«.t

30.1

-21.3.05 8.356

0.761.9 0.7755 0.781.8 0.7932 0.7655 0.7760 0.7853 0.7937

0.051.18 0.05".93 0.05559 0.05619

30.2

-21.2.95

8.1.93

0.7593 0.7701. 0.7802 0.7889

0.7598 0.7710 0.7808 0.7895 0.05378 0.05"t57 0.05527 0.05588

30.3

-21.2.85 8.629

0.7536 0.7653 0.7755 0.761.6

0.75".l 0.7656 0.7760 0.7851 0.05338 0. 051.21 0.051.93 0.05558

30.1. -21.2.75 8.766

0.71.7". 0.7598 0.7706 0.7801

0.71.79 0.7601. 0.7711 0.7807

0.05291. 0.05382 0.051.59 0.05526

30.5

-21.2.65 8.906

0.71.08 0.751.2 0.7656 0.7755

0.71.13 0.751.7 0.7661 0.7760

0.0521.8 0.0531.2 0.051.23 0.051.93

30.6

-21.2.55

9.01.7

D.7"t8". 0.760". 0.7708

0.71.90 0.7609 0.7713 0.05302 0.05386 0.051.60

30.7

-21.2.1.5 9.169

0.7"t22 0.75U9 0.7659

0.71,27 0.7555 0.766". 0.05257 0.0531.8 0.051.25

30.8

-21.2.35 9.333

0.7358 0.71.91. 0.7608 0.7363 0.71.95 0.7611. 0.052ia 0.05308 0.05389

30.9

-21.2.25

9.1.79

0.7288 0.71.35 0.7556 0.7293 0.71.1.0 0.7561 0.05163 0.05266 0.05352

31.0

-21.2.15 9.627

0.7215 0.7373 0.7502 0.7220 0.7379 0.7508 0.05111 0.05223 0.05311.

31.1

-21.2.05 9.776

0.7135 0.7308 0.71.1.6 0.711.0 0.7313 0.71.51 0.0505". 0.05177 0.05271.

31.2

-21.1.95 9.927

0.7053 0.721.0 0.7387 0.7058 0.721.5 0.7393

0.01.996 0.05129 0.05233

31.3

-21.1.85 10.079

0.7166 0.7326 0.7171 0.7331 0.05076 0.05189

31.1. -21.1.75

10.231.

0.7091 0.7261 0.7096 0.7266 0.05023 0.0511.3
1ELE 16 - CONTINUEC CF CCHFRESSEO LIOUIC HYOROGEN - CONTINUED

TAPLE ENTRIES

1. TEMPERATURE, K

2. TEMPERATURE, C 3. VAPOR PRESSURE, BAR

12

3

. DENSITY

. DENSITY

. DENSITY

RATIO, LIQUID DENSITY/DENSITY AT RATIO. LIQUIO OENSITY/CENSITY AT

, KG/DH 3

A PCILING PRESSURE OF 1 BAR, OICEKSIC

A PCILII^G PRESSURE OF 760 TCRR, OIMEh NLESS SICNLESS

BAR 0.600 1.000 2. KF/CM? 0.816 1.020 2. 39 3.000

3.059 4.000 5.000 6.000 7.O004.079 5.099 6.118 7.13e

8.(100 9.000 10.000 11.000 8.158 9.177 10.197 11.217

12.000

12.237

31.5 -241.65

10.390

0.7007

0.7012

0. 04963

0.7193 0.7198 0.05095

31.6 -241.55

10.5<(8

0.6916 0.6921 0.048990.7121 0.7126 0.05044

31.7 -241.45

10.707

0.6616

0.6821 0.04828

0.7046

0.7051 0.04991

31.8 -241.35

10.869

0.6700 0.6705 0.04746

0.6965

0.6970 0.04934

31.9 -241.25

11.032

0.6875

0.6680 0.04870

32.0 -2*1.15

11.198

0.6779

0.6784 0.04602
10. REFERENCES

Beattie, James A. , "The Thermodynamic Temperature of the Ice Point," Temperature, Its Measurement and Control in Science and Industry , (Reinhold Pub. Corp. , New York,

N. Y. , 1941) pp. 78-88. Compressed Gas Association, Standard Density Data Atmospheric Gases and Hydrogen,

Pamphlet P-6, first ed. , Compressed Gas Association, Inc., New York, N. Y. (1965). Cragoe, C. S. , "Slopes of the PV Isotherms of Some Thermometric Gases at Pressures Below Two Atmospheres," Temperature, Its Measurement and Control in Science and

Industry , (Reinhold Pub. Corp., New York, N. Y., 1941) pp. 89-126. Dean, J. W. , "A Tabulation of the Thermodynamic Properties of Normal Hydrogen from Low

Temperatures to 300°K and from 1 to 100 Atmospheres, " Nat. Bur. Stand. (U.S.), Tech. Note 120 (1961). Gosman, A. L. , McCarty, R. D. , and Hust, J. G. , "Thermodynamic Properties of Argon

from the Triple Point to 300 K at Pressures to 1000 Atmospheres," Nat. Stand. Ref. Data Ser. , Nat. Bur. Stand. (U.S.), 27, 146 pages (March 1969). Hilsenrath, Joseph, et al. , "Tables of Thermal Properties of Gases, Comprising Tables of Thermodynamic and Transport Properties of Air, Argon, Carbon Dioxide, Carbon

Monoxide, Hydrogen, Nitrogen, Oxygen, and Steam," Nat. Bur. Stand. (U.S.), Circ.

564, (U. S. Government Printing Office, Washington, D. C.) (Nov. 1955). IUPAC Revises Atomic Weight Values, Chem. Engr. News ^9, 42-43 (Nov. 20, 1961). McCarty, R. D. , and Weber, L. A. , "Thermophysical Properties of Oxygen from the Freezing Liquid Line to 600 R for Pressures to 5000 Psia," Nat. Bur. Stand. (U.S.), Tech. Note 384, 189 pages (July 1971). McCarty, R. D. , and Weber, L. A. , "Thermophysical Properties of Parahydrogen from the Freezing Liquid Line to 5000 R for Pressures to 10, 000 Psia, " Nat. Bur. Stand. (U.S.), Tech. Note 617, 169 pages (April 1972). Mechtly, E. A., "The International System of Units ," NASA Spec. Pub. 7012, revised (1969). Michels, A., DeGraaff, W. , Wassenaar, T. , Levelt, J. M. H. , and Louwerse, P., "Compressibility Isotherms of Hydrogen and Deuterium at Temperatures Between

-175° C and +150° C (at Densities up to 960 Amagat), " Physica 25, 25-51 (1959). Michels, A. , Schamp, H. W. , DeGraaff, W. , "Compressibility Isotherms of Oxygen at 0°, 25°C and 50°C and at Pressures up to 135 Atmospheres, " Physica 2_0, 1209-14

(1954). Roder, H. M. , Diller, D. E. , Weber, L. A., and Goodwin, R. D. , "The Orthobaric

Densities of Parahydrogen, Derived Heats of Vaporization, and Critical Constants," Cryogenics 3, 16-22 (1963). Roder, H. M. , McCarty, R. D. , and Johnson, V. J., "Saturated Liquid Densities of Oxygen,

Nitrogen, Argon, and Parahydrogen, " Nat. Bur. Stand. (U.S.), Tech. Note 361,

67 pages (Jan. 1968). Roder, H. M. , McCarty, R. D. , and Johnson, V. J. , "Liquid Densities of Oxygen,

Nitrogen, Argon, and Parahydrogen," Nat. Bur. Stand. (U.S.), Tech. Note 361 (Revised), 181 pages (October 1972). 108
Roder, H. M. , Weber, L. A., and Goodwin, R. D. , "Thermodynamic and Related Properties of Parahydrogen From the Triple Point to 100°K at Pressures to 340 Atmospheres, " Nat. Bur. Stand. (U.S.), Monogr. 94 (U. S. Government Printing

Office, Washington, D. C.) (1965). Strobridge, T. R. , "The Thermodynamic Properties of Nitrogen from 64 to 200 Atmospheres,

Nat. Bur. Stand. (U.S.), Tech. Note 129 (Jan. 1962); and Strobridge, T. R., "The Thermodynamic Properties of Nitrogen from 114 to 540°R between 1.0 and 3000 PSIA, Supplement A (Br itish Units) ," Nat. Bur. Stand. (U.S.), Tech. Note 129A (Feb. 1963). Weber, L. A. , "P-V-T, Thermodynamic and Related Properties of Oxygen from the Triple

Point to 300 K at Pressures to 33 MN/m3

, " J. Res. Nat. Bur. Stand. (U. S. ), 74A , (Phys. and Chem.), No. 1, 93-129 (Jan. -Feb. 1970). Weber, L. A. , Diller, D. E. , Roder, H. M. , and Goodwin, R. D. , "The Vapour Pressure

of 20° K Equilibrium Hydrogen, " Cryogenics 2_, 236-8 (1962). Woolley, Harold W. , Scott, Russell B. , and Brickwedde, F. G. , "Compilation of Thermal

Properties of Hydrogen in Its Various Isotopic and Ortho-Para Modifications," J. Res.

Nat. Bur. Stand. (U.S.) 41, 379-475 (Nov. 1948). APPENDIX

Units and Conversions The calculations for all fluids were performed with equations whose units were

atmospheres, Kelvin, and molar volumes. The various units presented in the tables involved the following conversion factor s (IUPAC 1961 and Mechtly 1969): Molecular Weight Conversion Factors Parahydrogen 2.01594 latm = 1.01325 bar Oxygen 31.9988 760 torr = 1.01325 bar Nitrogen 28.016 latm = 1 . 033227453 kp/cm3 Argon 39.948 1 kp/cm3 = 1 kgf/cm2

1 kg/dm3 = 1 kg/litre °C = K - 273. 15

Acknowledgment

This work was financed by the Industrial Gases Committee (IGC) of the Commission

Permanente Internationale de l'Acetylene, de la Soudure Autogene et des Industries qui s'y Rattachent (CPI).

109

NBS-114A (Rev. 7-73) U.S. DEPT. OF COMM. BIBLIOGRAPHIC DATA

SHEET

1. PUBLICATION OR REPORT NO. NBS TN-361 (Revised)

(Metric Supplement)

2. Gov't Accession

No.

3. Recipient's Accession No.

4. TITLE AND SUBTITLE LIQUID DENSITIES OF OXYGEN, NITROGEN, ARGON

AND PARAHYDROGEN

5. Publication Date May 1974

6. Performing Organization Code

7. AUTHOR(S) H. M. Roder

Performing Organ. Report No.

9. PERFORMING ORGANIZATION NAME AND ADDRESS NATIONAL BUREAU OF STANDARDS DEPARTMENT OF COMMERCE

WASHINGTON, D.C. 20234

10. Project/Task/Work Unit No. 2750592

11. Contract/Grant No.

12. Sponsoring Organization Name and Complete Address (Street, City, State, ZIP) Industrial Gases Committee (IGC) of the Commission

Permanente Internationale de l'Acetylene, de la Soudure

Autogene et des Industries qui s'y Rattachent (CPI)

,

32, Boulevard de la Chapelle, 75 - Paris I8 e

, FRANCE

13. Type of Report & Period Covered

14. Sponsoring Agency Code

15. SUPPLEMENTARY NOTES

16. ABSTRACT (A 200-word or less factual summary of most significant information. If document includes a significant bibliography or literature survey, mention it here.) Tables of pressure, volume, density and temperature for the saturated liquid and

for compressed liquid states from the triple point to the critical point, of oxygen,

nitrogen, argon, and parahydrogen are presented. The table entries of temperature

are in Kelvin and degrees Celsius, table entries in pressure are in bars and kp/cm3

. Volumes or densities are given in several different units, and density ratios are

tabulated for each entry. Estimates of the uncertainty for the tabulated data are

given. The tables were prepared in the style and in the units preferred by the users. They are intended as source for both technician and engineer.

17. KEY WORDS (six to twelve entries; alphabetical order; capitalize only the first letter of the first key word unless a proper name; separated by semicolons) Argon; compressed liquid; density; density ratios; liquid; nitrogen, oxygen;

parahydrogen; pressure; saturated liquid; tables; temperature; uncertainties; volume,

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of National Standard Data Act (Public Law 90-396). See also Section 1.2.3. Building Science Series—Disseminates technical infor- mation developed at the Bureau on building materials, components, systems, and whole structures. The series presents research results, test methods, and performance criteria related to the structural and environmental functions and the durability and safety characteristics of building elements and systems.

Technical Notes—Studies or reports which are complete

in themselves but restrictive in their treatment of a

subject. Analogous to monographs but not so comprehensive in scope or definitive in treatment of the subject area. Often serve as a vehicle for final reports of work performed at NBS under the sponsorship of other government agencies. Voluntary Product Standards—Developed under pro- cedures published by the Department of Commerce in Part 10, Title 15, of the Code of Federal Regulations. The purpose of the standards is to establish nationally recognized requirements for products, and to provide

all concerned interests with a basis for common understanding of the characteristics of the products. The

National Bureau of Standards administers the Voluntary Product Standards program as a supplement to the activities of the private sector standardizing

organizations. Federal Information Processing Standards Publications (FIPS PUBS) —Publications in this series collectively constitute the Federal Information Processing Standards Register. The purpose of the Register is to serve

as the official source of information in the Federal Gov- ernment regarding standards issued by NBS pursuant

to the Federal Property and Administrative Services Act of 1949 as amended, Public Law 89-306 (79 Stat. 1127), and as implemented by Executive Order 11717

(38 FR 12315, dated May 11, 1973) and Part 6 of Title 15 CFR (Code of Federal Regulations). FIPS PUBS

will include approved Federal information processing standards information of general interest, and a complete index of relevant standards publications. Consumer Information Series—Practical information, based on NBS research and experience, covering areas

of interest to the consumer. Easily understandable language and illustrations provide useful background

knowledge for shopping in today's technological marketplace. NBS Interagency Reports—A special series of interim

or final reports on work performed by NBS for outside sponsors (both government and non-government). In

general, initial distribution is handled by the sponsor;

public distribution is by the National Technical Infor- mation Service (Springfield, Va. 22151) in paper copy

or microfiche form. Order NBS publications (except Bibliographic Subscription Services) from: Superintendent of Documents, Government Printing Office, Washington, D.C. 20402. BIBLIOGRAPHIC SUBSCRIPTION SERVICES

The following current-awareness and literature-survey bibliographies are issued periodically by the Bureau:

Cryogenic Data Center Current Awareness Service

(Publications and Reports of Interest in Cryogenics). A literature survey issued weekly. Annual subscription: Domestic, $20.00; foreign, $25.00. Liquefied Natural Gas. A literature survey issued quarterly. Annual subscription: $20.00. Superconducting Devices and Materials. A literature survey issued quarterly. Annual subscription: $20.00. Send subscription orders and remittances for the preceding bibliographic services to the U.S. Department

of Commerce, National Technical Information Service, Springfield, Va. 22151. Electromagnetic Metrology Current Awareness Service (Abstracts of Selected Articles on Measurement

Techniques and Standards of Electromagnetic Quantities from D-C to Millimeter-Wave Frequencies).

Issued monthly. Annual subscription: $100.00 (Special rates for multi-subscriptions). Send subscription order and remittance to the Electromagnetic Metrol- ogy Information Center, Electromagnetics Division, National Bureau of Standards, Boulder, Colo. 80302.
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