NBS

publications!

NATL INST. OF STAND & TECH

A 1 1 1 fc. BblQ3b

NBSIR 83-1692

COMPILATION AND EVALUATION

OF AVAILABLE DATA ON PHASE

EQUILIBRIA OF NATURAL AND

SYNTHETIC GAS MIXTURES

F.R. Williamson

N.A. Olien

National Bureau of Standards

U.S. Department of Commerce

Boulder, Colorado 80303

June 1983

QC

100

• U56

83-1692

1983

Research information Center /Vj?>SR

National Bureau of Standards

Gaithersburg, Maryland 20899

N BSI R 83-1 692 nv. 2 Z- IL i

COMPILATION AND EVALUATION OF

AVAILABLE DATA ON PHASE

EQUILIBRIA OF NATURAL AND

SYNTHETIC GAS MIXTURES

F.R. Williamson

N.A. Olien

Chemical Engineering Science Division

National Engineering Laboratory

National Bureau of Standards

U.S. Department of Commerce

Boulder, Colorado 80303

June 1983

Final Report to: Texas A & M Research Foundation

Under contract with:

Gas Research Institute

8600 West Bryn Mawr Avenue

Chicago, Illinois 60631

~Co

/ ¥ \

\%rcs o* h/

U.S. DEPARTMENT OF COMMERCE, Malcolm Baldrige, Secretary

NATIONAL BUREAU OF STANDARDS, Ernest Ambler, Director

CONTENTS

Page

Abstract 1

Introduction. 2

Approach 2

Results 3

Recommendations 4

Acknowledgments 6

References 7

Figure 1 9

Figure 2 10

Table 1 11

Table 2 13

Table 3 16

Appendices 17

Appendix A. 18

Appendix R.. 123

Appendix C 127

iii

ABSTRACT

This report summarizes the results of a two-year effort to identify,

compile, and evaluate the data available in the open literature for

the liquid-vapor equilibria for binary and multicomponent mixtures

of He, H 2 , Ci - C 5 alkanes, N 2 , CO, C0 2 , NH 3 , H 2 S, H 2 0, CS 2 , COS, HCN,

NO and SO . There were 276 binary systems relevant to the gas industry.

The result of the evaluation is that there are: 46 systems for which

data are imperative and 104 systems for which data are needed but not

imperative. The report lists the data needs in temperature and pressure

range for each system for both Priority 1 and 2. The report includes

three appendices: A — a listing cf the ranges and quality of all

available data for binary systems; B - the same for all multicomponent

systems; and C - a complete bibliography of the 543 citations identified

in the project.

Key words: bibliography; compilation; evaluation; liquid-vapor equilibrium

natural gas; phase equilibrium; synthetic natural gas.

1
Compilation and Evaluation of Available Data on Phase Equilibria

of Natural and Synthetic Gas Mixtures

INTRODUCTION

Accurate data for the thermophysical properties of fluid mixtures

are important to the natural gas industry for the efficient operation of

existing plant, the design of new plant, and the custody transfer of

gaseous fuels. The gas industry faces severe problems in the near future due to the Jack of data, correlations, and predictive techniques

for the properties of fluid mixtures associated with anticipated

technological needs in the conversion of fossil resources, especially

coal, to gaseous fuel [1-6]. In particular, it is imperative that we evaluate the current data base for natural gas (from conventional

and unconventional sources) and for synthetically produced gas. From

the standpoint of gas processing and separation operations, the most

important properties are phase equilibria, because of the large

effect they have on capital costs and production efficiency [7-9].

This report summarizes the results of the available data for liquidvapor phase equilibria of selected systems important to the gas industry;

other properties were assessed elsewhere. Binary systems were stressed

although multicomponent mixture data were compiled and evaluated. The

constituents of the mixtures are: He, H 2 , - C 5 alkanes, N 2 , CO,

C0 2 , N1I 3 , H2 S, H 2 0, CS 2 , COS, HCN, NO and SO (24 constituents).

Naturally, not all of the possible binary combinations are of interest

to the gas industry. Of the 276 possible binary systems, 124 were

considered irrelevant to the natural gas industry.

APPROACH

The Chemical Engineering Science Division of the National Bureau of

Standards has a substantial and long-standing research program in fluid

properties, and the work reported here is dependent upon this previous

work [10-14]. Of special importance is the recently completed work of

Hiza, Kidnay, and Miller.

The work reported here was conducted as follows:

1) Literature Search

Fluid Mixtures Data Center - NBS-Boulder

Chemical Abstracts Service

Selected Phase Equilibria compilations [13-18]

DECHEMA/ Berlin Tech. Univ. Data Bank

Science Citation Index

Bulletin of Chemical Thermodynamics

2) Preparation of a machine-readable bibliography of the

results from 1) above.

2
3) Acquisition of copies of original data sources.

4) Assessment of the quality of data. The data sets for

each relevant system were assessed using the following

rating system (all organizations involved in the project

used the same rating system)

A - Those data assigned a weight of 0.75 - 1.00 for

correlation purposes.

B - Those data assigned a weight of 0.25 - 0.74 for

correlation purposes.

C - Those data assigned a weight of 0.00 - 0.24 for

correlation purposes.

5) Recommendations for needed measurement. The following four

categories were established for the data of the binary systems:

N - No data available, none needed

M^ - Measurements needed (imperative)

M

2 - Measurements desirable, but not imperative

X - No priority 1 or 2 needed

RESULTS

1 - Literature Search

All of the sources listed in the previous section were searched

initially, and then update searches cn specific systems were

performed at intervals during the course of the project. A total

of 543 relevant references were identified.

2 - Preparation of machine-readable bibliography.

The bibliographic citations to the references identified in the

above section were put into machine-readable form and entered into an information bank. They are identified by a six-digit accession

number. The resulting bibliography appears as an Appendix C to

this report.

3 - Acquisition of copies of original data sources.

Copies of all references identified in 1 ) above were acquired. Over

75% were already available to NBS through the NBS-Fluid Mixtures

Data Center which is supported by the NBS-Office of Standard Reference

Data.

3
4 - Assessment of the quality of the data.

Figure 1 shows the form prepared to record the relevant parameters

regarding the data contained in each reference. A separate form was prepared for each system in each reference. The data assessment

was performed at this time also. Data assignment normally requires

a reasonable amount of subjective judgment involving the quality

of a given investigator's previous work or the overall quality of

the experimental results from a given laboratory. Where possible,

the present report relied on more objective criteria such as judgment of published critical evaluations such as reported in

[11, 12, 15, 16] or comparisons with standard correlation techniques

such as reported in [8, 18]. The level of effort involved in the

present work did not allow independent evaluation of each data set

so that, as stated above, subjective judgments were often applied.

However, the assessment was re-evaluated at the time the form shown

in Fig. 2 was completed for each system (1 bar = 0.1 MPa). The

summary tables for each of the relevant binary systems appear as Appendix A to this report, and the multicomponent systems as Appendix B. Appendix A includes tables for systems for which data

are needed, but none are available.

RECOMMENDATIONS

The results of the tables in Appendix A were examined in light of current

and future reeds of the gas industry. Figure 2 is the form used to

summarize the data for the relevant binary systems. The final results

of the assessment and the ensuing recommendations are shown in Table 1,

Priority 1 measurement needs; Table 2, Priority 2 measurement needs; and

Table 3, a summary of the assessment and recommendations.

Priority 1 data needs are those for which adequate data do not exist and

phase equilibria fall within the operating range of current or planned

natural gas systems, natural gas and natural gas liquids processing plants,

and synthetic gas plants. Also in priority 1 are systems which are important in the development of correlations, theories and the like.

Priority 2 data are those which are of less importance to current or planned gas industry needs as well as possible future generations of

synthetic gas plants. Also included in priority 2 data are data which

would provide a more complete coverage of given systems.

4
The resulting statistics of the available data and measurement reeds for

the 276 relevant systems are as follows:

N - 124 (No data available, none needed)

- 46 (Measurements imperative)

- 104* (Measurements needed)

X - 22 (Current data are adequate)

296*

*There are only 276 relevant systems, but

20 M^ systems are also included in M^ systems.

The measurements required for the 46 Priority 1 systems are extensive

and will require a substantial effort by the research community. In

addition, some of the measurements are exceedingly difficult. It is

suggested that GRI in consort with its Research Advisory Board and its

thermophysical property contractors establish some sort of priority order

or grouping for the Priority 1 systems.

V

5
ACKNOWLEDGMENTS

First of all, it would not have been possible to complete this project

at the level of effort assigned to it without the pioneering work of

M. J. Hiza, A. J. Kidnay, and R. C. Miller as reported in [13, 14]. In

addition, we are grateful to the Office of Standard Reference Data and

Dr. Howard J. White, Jr., for supporting that pioneering work. Finally,

we express our thanks to Dr. Ferol Fish and Dr. Frank Little of the

Gas Research Institute for their leadership in the project and to

Professor K. R. Hall of Texas A & M University for the coordination and

overall direction he provided to all participants in this project.

6
REFERENCES

[1] Fundamental data needs for coal conversion processes. RECON

Systems, Inc., Somerville, N.J., Executive Summary Rept.,

Department of Energy Contract No. EY-76-C-02-4059 , 6 p.

[2] Miller, R. P. Prospective needs for physical property data in

the chemical and allied industries during the next decade.

National Physical Lab., Teddington, England, Rept. No. NPL Chem.

84, 1978 June. 34 p.

[3] Brule, M. R, ; Lee, L. L. ; Starling, K. E. Predicting thermodynamic

properties for fossil-fuel chemicals. Chem. Eng. (New York),

Vol. 86, No. 25, 1979 November. 155-164.

[4] Bondi, A. What thermophysical and other physical properties data

are needed? Chem. Eng. Progr., Vol. 75, 1979 April. 70-74.

[5] Yen, L. C.; Firth, J. F. S.; Chao, K. C.; Lin, H. M. Data deficiency

hampers coal-gasification plant design. Chem. Eng. (New York),

Vol. 84, 1977 May. 127-130.

[6] Synfuel trends. Chem. Eng. Progr., Vol. 76, No. 3, 1980 March. 43-92.

[7] Zudkevich, D. ; Weinstein, N. J. ; Daubert, T. E. Present phase

equilibrium data and correlations in view of needs for producing

fluid fuels from coal. RECON Systems, Inc., Somerville, N.J.,

Reprint from Fluids and Fluid Mixtures, Proc. National Physical

Lab. Conf., Teddington, England, 1978 September 11-12. 87-102.

[8] Elliot, D. G. ; Chappelear, P. S.; Chen, R. J. J.; McKee, R. L.

Thermophysical properties: their effect on cryogenic gas processing.

Amer . Chem. Soc. Symp . , Ser. No. 60, 1977. 289-308.

[9] Miller, E. J.; Geist, J. M. Impact of recent developments in

thermodynamics on chemical process design. Presented at the Joint

meeting of the Chemical Industry Engineering Society of China

and the American Institute of Chemical Engineers, Beijing, China,

1982 September.

[10] Hiza, M. J. ; Drayer, D. E. ; Flynn, T. M. Low temperature physical

equilibria of some binary hydrogen systems. American Institute of

Chemical Engineers 48th National Meeting, Denver, CO, 1962, August 26-29.

Paper

.

[11] Hiza, M. J. ; Heck, C. K. ; Kidnay, A. J. Liquid-vapor and solid-vapor

equilibrium in the system hydrogen-ethane. Advances in Cryogenic

Engineering, Vol. 13, Proc. 1967 Cryogenic Engineering Conf.,

Stanford, CA, Aug. 21-23, 1967, K. D. Timmerhaus, Editor. Plenum

Press, New York, 1968. 343-356.

7
[12] Miller, R. C.; Kidnay, A. J. ; Hiza, M. J. Liquid-vapor equilibria

at 112.00 K for systems containing nitrogen, argon and methane.

AIChE J., Vol . 19, No. 1, 1973, January. 145-151.

[13] Hiza, M. J.; Kidnay, A. J.; Miller, R. C.. Equilibrium properties

of fluid mixtures - a bibliography of data on fluids of cryogenic

interest. NSRDS Bibliographic Series. IFI/Plenum Press, New York,

1975. 166 p.

[14] Hiza, M. J.; Kidnay, A. J. ; Miller, R. C. Equilibrium properties

of fluid mixtures - 2, a bibliography of experimental data on selected fluids, NSRDS Bibliographic Series. IFI/Plenum Press, New

York, 1982. 246 p.

[15] Miller, R. C.; Kidnay, A. J.; Hiza, M. J. Liquid + vapor equilibria

in methane+ethene and in methane+ethane from 150.00 to 190.00 K.

J. Chem. Thermodyn. , Vol. 9, No. 2, 1977 February. 167-178.

[16] Hiza, M. J.; Miller, R. C.; Kidnay, A. J. A review, evaluation, and

correlation of the phase equilibria, heat of mixing and change

in volume on mixing for liquid mixtures of methane + ethane.

J. Phys. Chem. Ref. Data, Vol. 8, No. 3, 1979. 799-816.

[17] Wichterle, I.; Linek, J. Hala, E. Vapor-liquid equilibrium data

bibliography. Elsevier Scientific Publishing Co., New York, 1973.

Supplement I, 1976, Supplement II, 1979.

[18] Knapp, H. ; Doring, R. ; Oellrich, L. ; Plocker, U. ; Prausnitz, J. M.

Vapor-liquid equilibria for mixtures of ]ow boiling substances.

DECHEMA Chemistry Data Series, Vol. 6, 1982. 890 p.

8
FIGURE 1

VLE DATA EVALUATION

Accession number:

Author(s):

Publication year:

Mixture system:

Temperatures Pressure range Composition range

Number of isotherms:

Number of mixtures:

End points

Type of data: Vapor and liquid compositions Q

Total vapor pressures Q

Dew points / bubble points [~]

Other

Form of data: Numerical Q

Correlation Q

Graphical Q

Additional properties reported:

Rating: A

B

C

G _

Number of points

o

D

G

G ptotal C3

Other

Comments

a

a

a

9
System:

Vapor-liquid

equilibrium

data:

II

Author

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

Comp.

Range,

mol

•

Press.

Range,

bar

Temp.

Rang®,

1C

Data

Saia

With

Rating

s

A

m

k

s

)

Data

Seta

With

Rating

= B

(N

B

=)

10

'Same

data
Vapor-liquid

equilibrium

measurements

needed:

Priority

1

(imperative)

ts n

»

<0 o o O o O o O o O O o O o o o o o o o o

o o o o o o O o o or o o o o o o o o o o

o 1—

1

I—

1

1—

1

LO 1—

1

1—

1

LO 1—

1

LO LO LO LO 1—

1

1—

1

LO I—

1

LO LO LO

hm &

1 o1 o1 o1 o o o o o o o O O O o o o o o o O

G&q U0 o LO o o o o o o o o o o o o o o o o o

CO o- LO o O- LO MD LO o LO LO LO 'nO LO 'nO LO LO LO or oT or vO or or sD or vO VO or or or VO v£> C 1 LP)

1 O

i o

1 oi o

1 o o

1 o1 O o O o O o o O o o o o

© LO OJ o LO On LO o O'* or On o o LO o O-N 0^ H

CM co CO vO OJ CsJ Cs] OJ or CM or CM CM CO CO OJ CO or CM CM

OJ CM CM

i—

1

»

rH CM 33 33 33 o OJ OJ LO LO LO o

33 OJ OJ rH i—

1

1—

1

CJ CJ o CJ o CM Ed LO i—

i

1

33 33 33 i i CM 1 CM 33 ® cj :u 33 or LO LO rH •H c 33 •H 33

i LO LO CJ CJ CJ o +

Cffi o a CJ o 1 i O 1 04 o o o + + + + + o

CD i i OJ c •H OJ •H 33 CJ OJ OJ Csl or CM >* c •H (3 33 33 1 33 33 33 o o O o o o 33

(/) + + + +

c 1—

1

1

i—1 rH 1—

1

CM + + + + + + + + + 33 33 £3 33 33 23 +

vO v£> oo oo or or or Of or \ CM Csl OJ OJ 33 33 o 33 33 co CO CO CO CJ CJ CJ CJ CJ CM CM o o o o OJ CM OJ CO co OJ OJ o 33 1 1 1 i 1 o o

CJ CJ CJ a CJ CJ 23 CJ CJ 33 33 CJ 23 •H *H •H p c 3 CO

k.

<0 .o« o o o o o o LO o o o O o o O o o o o o o o

LO o o LO o o CO o oo m or or or O CO o o o o o o IP Csl OJ 1—

1

OJ CsJ OJ I 1 LO 1—

1

1—

1

OJ 1—

1

1—

1

III !§ o o o o o o o o o o o o o o o o o o 50- o o

&

o o

rH 1—

1

or of o

1 Q O

CL co CO EA LO o LO o o o LO o O LO LO o o LO LO o LO o LO o o w CO o o i—1 O- oo co 00 rH OJ CO o o o On. LO o On O^ 1—1 CO H 1—1 OJ CO CO co Csl 1—1 OJ co or or or or CO CO vQ CO CO co or or o o o o o o LO O o o o o o o o o O o o o o

o o- or ON <

1 CO LO rH LO LO LO On o o or LO o

1—1 rH CsJ i—

I

co 1—1 1—

1

rH CN CO CM OJ OJ CM OJ or CM CO CM co or

04 P rH Q o

O 33 CM OJ rH 1—1 • rH LO 1—

1

i—

i

33 33 33 CJ 33 33 MD CO or

vO CO or 1 LO LO OJ CO o 33 33 co CJ a © or OJ 33 33 CO co CJ o CJ CJ o CM Cs CM co CM 1 i o 33 o 04 co 33 o 33 1 a) i 1 CJ 33 33 CJ a 33 •H C

cj CJ CJ CJ CJ CJ S P (3 c P (0 + + + + + + + + + + + + + + + + + + + +

or or or CM CM CM CM CM CS OJ Cs CNI OJ CsJ OJ Csl CM CM 04 OJ 33 33 33 o o o o o

33 33 33 33 33 33 23 2 2 a 23 23 CJ CJ CJ CJ CJ CJ CJ a

11
Vapor-liquid

equilibrium

measurements

needed:

Priority

1

(imperative)

12
Vapor-liquid

equilibrium

measurements

needed:

Priority

2

(needed)

13
Vapor-liquid

equilibrium

measurements

needed:

Priority

2

(needed)

fc. CO A

Q (0

(0 o o LO O O O o O O O O O O O o o o o O O O O O O O

o o CO O O CO oo O co CM O O O <r oo 00 CM O O LO o o O

1—1 LO <1

1

1 rH rH 1 1

1

1

1

1 CM rH rH rH rH CM 11 Is 1 o O o o o o o o o O o o o o o o o o O o o o O O o

Q. CO

o LO

CM ro CO Kf O o

LH o LO LO o c o LO o LO o o o o LO O LO O o LO o o O LO LO CO LO T—

oo <N O CM r- CO CO o LO M0 mo mo LO oo o LO o o rH m

i

1 1i—1 CM CO 1—1 CO vt CO CM CM CM <j- MO i—1 CN CM CM CO CO

1 1 i i i 1 rs

i i * 1 i i 1 1 1 1 i l 1 1 i i i o o O LO o c o o o o o o o o O O

lo <r o o o LO o LO o o o

© vO r- o O CN a> CM M3 LO LO oo M3 LO <f LO o CTn O LO oo H

1—1 C\1 i—1 CM CM CM CM CM CM CM rH CM rH CO >—i m CO rH rH CM '

1 O O

00 o>

rH 1—1

CM g i—1 o 33 CM CM © CM LO rH rH

cj 33 33 (0 vO oo "—

1 LO LO MO

CM o CM 33 o 33 CM CM o 33 a cj o "d* CM 33 o

CO CN o o o CM CM CO o o OJ CJ 1 1 CM o 33 o <N CM

</J a CJ 2 cj cj 33 ° 33 CO c K •H 33 33 a CJ CJ 33 + + + + + + + + + + + + + + + + + + + +

(N CN CN CN CM CM CM CN CM CM CM CM CN CM CM O o o o O

33 33 s 33 33 3 55 33 2 33 z CJ CJ CJ CJ CJ

fe» <0 £

•t

(0 O o o O O LO O O O o O o o o o o o o o o

(0©

o o o O LO rH CM CO o CM o CO <J" LO CM o o LO o

rH 1—

CM LO rH 1—

i—

'—

'—

i—

rH

1 o

1 o O o o o O o O o o o o o o O o o o o

a

a

e a

E

©

LO LO LO o o o o o o LO o LO o o o LO LO o o LO o o LO CO o CTn i—

oo t—

CO CO CO MO oo a> i— CO CO v£> rH rH rH CM 1—

CO CO CO CO <1-

1 CO1 o o o 00 o o o o LO LO o o o o LO o o o

M0 o o M0 03 oo 00 CO 1—

CO M0 o> MO On

1—

CN rH rH rH 1—

rH rH <—CM rH CM 1—

CM

E o o O CN © i—

rH CM <—

33 33 33 00 M3 00 " LO

CM 33 o CM 33 o 33 CO CO a CJ CM CM 2 CJ CO >

<n

CSl o CO CM CN o 33 o CN CN CO CM o i i o o CJ i o

cj cj 33 cj CJ cj cj 33 cj 33 U •H c CO 33 c CO + + + + + + + + + + + + + + + + + + + +

d) 0) <u QJ CM CM CN CM CN CN CN CM CM CM CM CM CM CM CM CM

rtj 33 33 33 33 33 33 33 33 33 33 33 33 33 33 33 33 33 14
Vapor-liquid

equilibrium

measurements

needed:

Priority

2

(needed)

15
Vapor-Liquid

Equilibrium

Data

”0

»*

©

„£

®

(W®

©

C

'E cm © © z ©©

=0©©

°Z

m

© C0 E ©

0. E

“0©

X3m

CM

© > 5

«&* 0 'E © O ©

*E

®

(L E ©©

“S *o » ©

<ffl T3 - © ffl m -*-* S © E o © 1 

cm

O

O

CO

CM XUO 01o©c zOX

CM X

(O

CM

O

i" t o!

<0 O

CO

cmp COo oCM X

X01 Xcr1c

CM Oz %

COoo

co Xz o1 o £o oCM z

€0 X

Xo oz oo

CM Z

CM 2

CM 2

CM 2

CM

CM

CM

CM

CM

CM 2

CM

CM

CM

CM

CM 1

CM

CM

CM

CM

CM

CM

CM 2

CM

CM

CM 2

CM

CM

CM 2

CM

CM

CM

CM

CM

CM 2

CM 2

CM 2

CM

CM

CM

CM

CM

CM 2

CM

CM

CM

CM

CM

CM

CM

CM

CM z

CM 5

CM

CM

CM

CM

CM 2

CM 2X

CM

CM

CM CM

CM

CM

CM

CM 2

CM X

CM CM CM CM CM CM CM CM 2 m

CM 2

CM 2

CM CM CM 2 x© M

CM 2

CM CM CM

©X

CM X £ 8 g f ow

x % x

69 3- §

16
APPENDICES

Appendix A System: Vapor-Liquid Equilibrium Data:*

Appendix B Multicomponent Vapor-Liquid Equilibrium Data*

Appendix C Data Source References (a listing in alphabetical order

of all references to experimental data listed in

Appendices A and B; included is a cross-reference

between accession number and author)

.

*The appendices are arranged as follows for each system: N is the number

of references; Temp., Press., and Comp. Range are self-explanatory; Accession

number refers to an identification number assigned to each reference;

Author is the first author of each reference.

17
System:

Vapor-liquid

equilibrium

data:

II

©

JS3<eo

35®oo<©E0» c

CB ££a aE©O

-X •K bO i—1 T—

r—

Cti OJ

cti cti 03 4-J C/5 1 1 c OJ

ctf

U 4-> 4-J c •H

OJ 0) 0) o o 4-J CO

01 * * * * 00 00 4-J 4-J 00

•N C3 4-) 4-J 0) •H -C xl 4J u QJ OJ C <—1

Cti 4-J <u c c 0) 01 tu rH N 0) c c 5-J u 0) OJ •H e c o o 4-J 4-J 5-4 o

EE CO CO CO CO CO CO

O

O

CM co CO CO CO M3 oo CM

C\J oo rH CM UO CO CM i—

o o CM 1—

X) o CO o o

UO 00 UO pH uO v£> UO 1—

CO LO CM 04 CM CO '•d- r—

01 0) 0) 01 0) 0) 0> 0) OJ EC EC EC EC EE EC EE Ed 1 1 CO CO CO uO CO vO o CO o U0 o CM

CO o CO CM 1—CM o r

—

o • • • * • i CM 1—

CO CM CO M3 rH i—

o o o o o o o o o o • o o o o o • o

CM uo o co o UO '—

o • CM UO 1—

CO CO CO CO rH M3

r—

CM ON CM CM CM M3 i—

CM i—

oo oom in uO M3 • • • • • • '—

co CM >—

CM oo

CM CM CO CO CO o CM o | i 1 1 i o i CO Mf UO LO UO rH i—i CO o LO UO o U0 M3 vO

CM T—

1—

rH CM rH CM i

i rH

mnOK 9Wc

<9 £a «©<0 IIoz me«

££e aE®H

O

IIOSc

•M

(0

AC

EC

a> EE (0®

CO

CO

1801

«fi e r s <

is ^ ^ E

II< m®

COma

18m

H e^ CO > ®E

88

ffl Z 50+>®

CO®D

18

Same

data
System:

Vapor-liquid

equilibrium

data: 3<

lo

II

Co

CO<0©oo<o£

9k o

0)c

<0 cc• aEoo

PmPh . < • CJ • • • • •X w cs • O PQ PQ PQ < r, • • • (3 23 • • • • o S • • <d s’ H > S S i

43u • o • 3 a * • O X ** * * • QJ (3 P4

>> 33 1—1

cd 4—1 4-J 4-J > 4-J (3 cd * QJ 33 cd 43 u 4-» 4-) c •H cd 33 3 CO (3 cd s C3 QJ QJ QJ X 54 e >L O •H cd n QJ •H QJ QJ QJ > , o aj r—1 M N > > cd X) h 54 54 54 > X 43 i—1 3 3 cd QJ 43 o 43 -u) 4-J 4-) cc QJ 3 3

PQ PQQ

Q 33 03 CO CO CO CO

Q Pm

H

rH

LO i">* Nt CTn MO CT\ oo CM LO o Nt

CO CN] rH CN 1 1 LO o- co i—1

LD rH CM CO

o> **d" lO i—1

r—1 '—i o M0 •<f o a> o i—i

co i—i o CO M0 o CM LO o MO LO LO On

C\| I—1

CN CM M0 CM •<r lO LO 00 i—1CM MO

54

qj OJ (3 a) oj QJ QJ QJ 0) QJ

O QJ QJ QJ 33 33 33 33 33 33 33 33 33 33 Q. 33 33 33

CC > CO

LO oo CM

O o*. CO

a oo CO o vO 1 1 o M0 LO 33 co o • o t—i i—1 O • • lO 00 O o • • o • • • • o • o LO cr. r—I T 1 o o 1 o o o o 1 o 1 • • • 1 1 MO 1 1 i 1 r^* 1 M0 o o o O

1—1

CN LO CO i—1

CN o <d* lO l 1 i 1 MO o o o o o o o <r CO <—1 I

<—1 T 1 o o o o o o o o CM o o I

o O o o o o o o o o o o o o o O o

00 co M0 o

v3 CO C"* o oo o o O LO 1—1 1 co i—1

LO o o CM o LO LO o

Ln MO 1—1

CN lO CM 1—1

Nj- 00 1i—1 1—1CM

LO i—1

<r to M> 1 1 o LO LO 1—I i—1 i—1

!“1 '—1o\ CM MO -X CO o T 1 r—i o

CM

COi—1 • CO On o o i—1 • CN co • • i—1

LO

O LO • • CM 1—1

CO

Cs] CM • o lO CM CN

r\ i—1 i—1 I 1 a\ 1 1 i—1 i

oo oo lO o i i t 1 i 1 1 co i i o o CM

o-* l£> CN

m 1 1 On LO r—1 i—1

CO o t—1

r—1 i—1 • • • • 1 • • • i • l i i CM r-* MO co o* CM oo -cC -X CM 00 r-* O- lO M0 lO i—1

r>* LO lO CM i—1 5 1

u~1 o

u~l o

LO

LT| o

(0 £3

9» O0> c

(0 cca (0

(0® 18O ®0) c

(0 cca aE®

hO

SiO)cam

44

(0 cc

53+

oj 33

«©9

(/)

(0

44ma

ii £ e

+* < £ w ^ uc

II<

(0

44@

0)

II0)

*”“ ,E

M CO ^ ID £ 44

t: > <0

<0 fir a

iim £

(0

44®

(0

<0 44

(0 o

19

Same

data
System:

Vapor-liquid

equilibrium

data:

II

o

o

+

0)

Author

Parrish,

Steward

Sinor,

Kurata

Data

Sets

With

Rating

=C

(N

c

=)

Accession

Mo.

105282 40404

Comp.

Range,

mol

.005-.

10

He

.003-.

167

He

Press.

Range,

bar

5-137

17-136

Temp.

Range,

K

80-120 77-128

Data

Sets

With

Rating

= A

(N

a

=

2)

Data

Sets

With

Rating

- 8

«n

b

=)

20

Same

data
System:

Vapor-liquid

equilibrium

data:

00

II

<r X

o

+

CL) X

Author

DeVaney,

et

al

Heck,

Hiza

Hiza,

Kidnay

Kharakhorin

Rhodes,

et

al

Sinor,

et

al

Streett,

et

al

Gonikberg,

Fastovski

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

70826 44762 29397 9643

69667 36006 94794 6364

Comp.

Range,

mol

.008-.

06

He

.0001-.

14

He

.991-.

998

He

0-.041

He

.002-.

34

He

0-.13

He

.002-.

75

He 3H

TO

•-T00*

Press.

Range,

bar

14-69

5-205

13-103 .1-170 69-262 .2-138

34-9807 25-159

Temp.

Range,

K

124-191

95-185 1691-150 94-192 93-188 95-290 o

i—t

i o

O'*

Data

Sets

With

Rating

= A

<n

a=

7

>

Data

Sets

With

Rating

= B

<n

b

=

1)

21

Same

data
System:

Vapor-liquid

equilibrium

data:

II

CM O

u

+

<u

Author

MacKendrick,

et

al

Burfield,

et

al

Liu

Accession

No.

53324 63709 62792

Comp.

Range,

mol

.0006-.

06

He

0-0.049

He

.003-.

Oil

He

Press.

Range,

bar

10-199

19.5-139.3

20-120

ln

co

co

'

i

pHIIo

z

o

IIO)

c

<0 oc

*»

QS5SB

CO©

(/)

(0

<+* (0

O

Temp.

Range,

K

220-290 253,273,293 181,190,200

Data

Sets

With

Rating

= A

(N

a

=

1

)

Data

Sets

With

Rating

= B

«N

b

=

2)

22

Same

data
System:

Vapor-liquid

equilibrium

data:

VO

II

vO X

CM 0

+

01 X

Author

Heck Hiza,

Duncan

Nikitina,

et

al

Cannon,

et

al

Maslennikova,

et

al

r—

1

CTn

i—

1

o

m

t—

i

i—

iio

z

O

n

o>c

?

co oc

**

C

0

4-* o

m

CO

co a

Accession

No.

61654 51011

CMo

o

o

00o

m

150259

Comp.

Range,

mol

.002-.

09

He

.000001-.

004

He

.0004-.

025

He

.0007-.

Oil

He

.065-.

435

He

Press.

Range,

bar

9-202 4-132 5-118 00

1

i—

1

CN

84-505

Temp.

Range,

K

170-290

95-150

113-273 144-227 288-310

Data

Sets

With

Rating

= A

(N

a

=

3)

Data

Sets

With

Rating

= B

<N

b

=

2)

23

Same

data
System:

Vapor-liquid

equilibrium

data:

IS

o

oj 3

+

<D

Author

Parrish,

Steward

Data

Sets

With

Rating

=C

(N

c

=)

Accession

Mo.

105282

Comp.

Range,

mol

.0052-.

042

He

Press.

Range,

bar

39-138

Temp.

Range,

K

195-285

Data

Sets

With

Rating

= A

<n

a

=

1)

Data

Sets

With

Rating

= B

(n

b

=)

24

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

II

00 a

on u

+

<u a

Author

Schindler,

et

al

Cannon,

et

al

Data

Sets

With

Rating

=C

(N

c

=

1

)

7961

Accession

No.

40036 54087

'

Comp.

Range,

mol

0-.13

He

.001-.

Oil

He

Press.

Range,

bar

.07-207 00

1 T—

1

Csj

Temp.

Range,

K

123-348 172-255

Data

Sets

With

Rating

= A

CN

a

=

1)

Data

Sets

With

Rating

= B

«n

b

=

1)

25

Same

data
System:

Vapor-liquid

equilibrium

data:

CN

II

m

33+

0) 33

Author

Cannon,

et

al

Tsiklis

Data

Sets

With

Rating

sC

(N

c

=)

Accession

f^J©.

54087 13359

C@mp.Rarsg@

5

moi

.00009-.

0009

He

0-.15

He

Press.

Flang©

5

bar

21-48

o

o

1 o1—

1

Temp.

Hang©*

K

228-283 293-473

Data

Sets

With

Rating

= A

«n

a

=)

Data

Sets

With

Rating

= B

«N

b

=2)

26

Same

data
System:

Vapor-liquid

equilibrium

data:

II

0

X

o

1 +

<u

Author

Nikitina,

et

al r

Data

Sets

With

Rating

=C

{U

c

=)

Comp.

Range,

mol

Accession

No.

68441

.0001-.

014

He

Press.

Range,

bar

5-39

Temp.

Range,

K

143-273

Data

Sets

With

Rating

= A

(N

a

=

1)

Data

Sets

With

Rating

= B

«N

B

=)

27

Same

data
System:

Vapor-liquid

equilibrium

data:

©£

•u

0)e

*H

4-J •H

m

•o®S

S3 ©5

<N

II

<r

colo

a) oooo

CT\ COI LO

-cr oi c+

cu sc

©»e©

ffi8 ai©H

co

r^- OJI co

LO

«©#

<0 2 5 mQ

IITOe

•-^ ohe *- ^< w

fi£

II< 9mm ^

IS 5 Q

18TO ^ s — s ffl II <9

28

Data

Sets

With

Rating

=C

(Nc=1)

45496
System:

Vapor-liquid

equilibrium

data:

II

CM

i—

I

PCm

u

ic+

PC

Author

Makranczy,

et

al

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150177

Comp.

Range,

mol

i

i

Press.

Range,

bar

r-H

Temp.

Range,

K

00

CM

Data

Sets

With

Rating

= A (N*r

)

Data

Sets

With

Rating- B

(n

b

=

i)

29

Same

data
System:

Vapor-liquid

equilibrium

data:

CN

CNIIo

CM +

CL) 33

Author

Shoor,

et

al

Feillolay,

Lucas

Luker,

et

al

Potter,

Clynne

00

<}oo

LO

r—

r^oomi—1 LO

*CN CO o

com oho *

LOCsl i—1 ''tH (NO

com Or—

o - LO<T

i—ICO O—1 CN O

cNm Ot—1 o - Ln<r »—

1—i —i oocom

CT\ M3 - Oin '—i o

•o ooo

cum

COM

CO * CK3

MOO

•o f—IO com COM o - r^cM *m

<fo ooo <fm

Mj" t—| mo ~ *0

CO<f OOMOom

COM

ooM

11ozo

II0)c

33

(0 oc

0gt3 £

<0®

(0

<0 o

Accession

No.

150021 150037 150241 125573

Comp.

Range,

mol

.000007-.

000008

He ii

.295

He

.0001-.

0002

He

Press.

Range,

bar

T—| r—

138

3-10

Temp.

Range, K

298-353 298-308

573

377-548

Data

Sets

With

Rating = A

(na=1)

Data

Sets

With

Rating = B

CNg=

3)

30

Same

data
System:

Vapor-liquid

equilibrium

data:

vOi—I

If

CN

13+

CM

i—1

-V

cO o rH 1—1 1—1

ncl CO cO cn cO rH

4—1 CO 44 *H o a> r—I t—1

4-J 4-J c 4-J EX JZ co cO 0) QJ cO QJ 3

CJ

O QJ bO 4-J •x 3 44 1 1 3 5-i a) D 0) 0J W 1 1 O >4 < QJ •H 4-J c c C •H Q o

42 c 4-J CO CO cO r> CX 43 44 ex o a) N N N cn 3 rs a

•H ex

H cu •H •H •H 54

O 5j cn c CO •H 5-4 5-4 5-4 5-4 QJ 44 cO u o e CO 4-J O O O 44 O 6 QJ o « s cn >4 >* >-i C Q O > • ozco cn CM

(0 cn cm CM o xO

un 00 CM c- Ln

m 1 1 CO M0

CO

m 00 Mf rH Ln i—i o in CM rH 0 MO o rH CM o M0 o CM MO CM o

Ln r—1 t—1 i—1

CM Ln 00

m i—1

M0 o<“o CM C CM CM CM CM CM CM c CM CN E a EC EC eg EG EG EC EG EC EG EC

ex. <0

0)£© Ln

m

vO *—1MO MO oo \ 1 Ln OC i—1

MO mT cn CM CM Ln

a • oo • cn • • M0 0 • • • a i i • i i cn 1 i i i CM • i—1 1 Ln m • cn i—1

CM E o i o rH o o i o CM o o o • o • • • • o e • • • o

fc= (0 A0

6)c oo CM o o CM oo

c- v£> CM CM Ln cn i—1Ln cn vv i—I

Mf Ln *—1 i—1 i—I i—i

Ln CM c cn o MO 00 C Ln eg m cn CM (0 '—i

cn rH rH CM CM rH (0

a>

ha CL

xz

me ©

O)£

(0 oc On o CM o CM Ln 1—1

00 oo CM o m 00 • 1—1 i—1 CM rH 00 oo '—1

e- co

a cm o O cn C'* c- cn 1 Ln l cn 1 cn E

On CM MO c- c- oo vO vD MO

©

iCM

moCM

cn

in

e-o

cmcn

v£> CMmcnoo

oo

CMcn

c-Ln

iioo

iio>

(0 oc

<0 M©

0)

(0

<0 o

IIUi

&, c +* — V, ^ 0£

II<

(0«

11 f _ gi

</> £ C

<0 5 5 m

t; > <» <0 nr Q

IIm

(0

4*< ©

(/>

(0

4-« (0 o

31

Same

data
System:

Vapor-liquid

equilibrium

data:

LO

II

o

u

+

CM

Author

Tsang,

Streett

Yorizane,

et

al

Akers,

Eubanks

Verschoyle

Accession

No.

150221 50157 LOo

00

kO

1—1 CM

kO

Comp.

Range,

mol

.01-.

99

H

?

0-.395

H

2 CM PiLO

CM

1 *<r o

CS Pi

<r

LO

i COo

Data

Sets

With

Rating

=C

(N

c

=

1)

5732

Press.

Range,

bar

50.7-529

Csl in

i—

i

i kO

22-138 17-228

Temp.

Range,

K

LO

CM

i—

1

1 o

CO

eg

i—

I

l rCsJ CM

i—1

1 co

00

oo

oo

i ooMD

Data

Sets

With

Rating

= A

(N

A

=

3)

Data

Sets

With

Rating

= B

<n

b

=

1)

32

Same

data
System:

Vapor-liquid

equilibrium

data:

II

W

cj+

CNl EC

Author

Benham,

Katz

Freeth,

Verschoyle

Kirk,

Ziegler

Sagara,

et

al

Tsang,

et

al

Yorizane,

et

al

Co

sway,

Katz

Fastovskii,

Gonikber

Levitskaya

kO

CNo>

LO

CO

00

00

uo

CNJn

o

z

o

II0»

c

to QC

IOH 3

to M

©

0)

to

(0

o

Accession

No.

6251 5679

24862 94700

150236 50157 6572 5617 6241

Comp.

Range,

mol

.02-.

35

H

9

.004-.

10

H

2

.01-.

12

H

2

.003-.

225

H

2

.002-.

61

H

?

0-.29

H

2

.08

H

?

.02-.

16

Z.

.02-.

15

H

?

Press.

Range,

bar

34-276

00o

C\1

1

i—

i

10-127

00o

t—

1

1 o1—

2-1380

10-152 69

31-229

r~H oo

1 o

cn

Temp.

Range,

K

116-172

91

90-117

103-174 o

00

i—

1

1 CN

103-163

144

90-127

158-188

Data

Sets

With

Rating

= A

(N

A

=

6)

Data

Sets

With

Rating

= B

(N

b

=

3)

33

Same

data
System:

Vapor-liquid

equilibrium

data:

II

CNI o

CJ+

CNI

Author

Kaminishi,

Toriumi

Spano,

et

al

Tsang,

Streett

Yorizane* Yorizane,

et

al*

.1,150212

Accession

No.

39337 50699

150505 90120 76576

Comp.

Rang©,

mol

.01-.

18

H

?

.0013-.

14

H

2

.0015-.

56

H

9

.05-.

47

H

2

.05-.

47

H

?

Data

Sets

With

Rating

=C

(N

c

s

6

)

8000

,

9518

,

150090

,

150109

,

1502 ]

Press.

Rang©,

bar

51-200 10.

7-200.5

9-1718

61-375 61-375

Temp.

Rang©,

K

233-298 220-290 220-290

273 273

Data

Sets

With

Rating

= A

<

n

a=

5

>

Data

Sets

With

Rating

- B

(Ng=

)

34

Same

data
System:

Vapor-liquid

equilibrium

data:

II z

co

paCM u

+

CM

pa

Author

Cohen,

et

al

Hiza,

et

al

Sagara,

et

al

Levitskaya,

E.

Cosway,

Katz

Levitskaya

Williams,

Katz

Data

Sets

With

Rating

=C

(N

c

=

1

)

639

Accession

No.

50609 45223 94700

150515 6572

«—

1

Cs] kO

6369

Comp.

Range,

mol

.003-.

09

H

2

.92-.

99

H

2 CM

pa

o

1 vOO

o

0.0-0.03

H

2 CN X

<TO

.005-.

03

H

2

i

i

Press.

Range,

bar

7-138 6-156

20-81

ii 00

1 o

1—1 69

30-81

11-552

Temp.

Range,

K

143-200 108-190 148-223

00

00

1—

1

00

i—I 00

kO

r—

1

00

LO

o

o

CM

158-188 103-283

Data

Sets

With

Rating

= A

<N

a

=

4)

Data

Sets

With

Rating

= B

<N

b

=

3)

35

Same

data
System:

Vapor-liquid

equilibrium

data:

in

II

co

PCCO u

+

OJ

SC

Author

Burriss,

et

al

Trust,

Kurata

Ahland

Williams,

Katz

r"* kOO

o

m

i

i

r—

IIo

z

o

II0)

c•MB

<** (0

f£

amm 5

(0

•+* o

(/) (0

(0

a

Accession

No.

150095 69775

150136 6369

Comp.

Range,

mol

.01-.

57

H

2

.002-.

35

H

? CN X

05

1 CO

i

i

Press.

Range,

bar

25-528 10-207 6-65 17-552

Temp.

Range,

K

278-361 98-348

271-273

89-297

Data

Sets

With

Rating

= A

(N

a

=

2)

Data

Sets

With

Rating

= B

<N

b

=

2)

36

Same

data
System:

Vapor-liquid

equilibrium

data:

vO

II

CO

+

CM

EC

Author

Reamer,

Sage

Krasheninnikov

,

etal

Krichevskii

,

Khazanova

<—

1

05

coo

IT)

i—1

05

00COo

uO

T—

1

-<r 0050

00

00

CO

ISo

z

o

ISCD

ciai 44

to CL

3

•44

®

</>

(Q

<0 o

Accession

No.

150544 150517 150514

Comp.

Range,

mol

0-.15

H

2

.03-.

37

H

?

.69-.

98

H

?

Press.

Range,

bar

34-414 .03-.

9

101-304

Temp.

Range,

K

278-394 283-293 273-348

Data

Sets

With

Rating

= A

(N

a

=

1

)

Data

Sets

With

Rating

= B

<N

b

=

2)

37

Same

data
System:

Vapor-liquid

equilibrium

data:

II

+

CN

PC

Author

Dean,

Tooke

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150060

Comp.

Range,

mol

.02-.

25

H

2

Press.

Range,

bar

34-207

Temp.

Range,

K

311-394

Data

Sets

With

Rating

= A

<N

A

=

1

)

Data

Sets

With

Rating

= B

(n

b

=)

38

Same

data
System:

Vapor-liquid

equilibrium

data:

LO

II

o

X

u

ie

CM X

Author

Aroyan,

Katz

Klink,

et

al

Ahland Nelson,

Bonnell

Data

Sets

With

Rating

=C

(N

c

-

i)

150067

Accession

No.

5100

105717 150136 30143

Comp.

Range,

mol

.01-.

30

H

?

.02-.

27

H

2

.86-.

97

H

2

.02-.

11

H

2

Press.

Range,

bar

21-541 28-169 11-65

22-107

Temp.

Range,

K

144-297 328-394 273-274 297-389

t

Data

Sets

With

Rating

= A

(N

a

=)2

m

«

11 —

£ c

® = m " * a 5

39

Same

data
System:

Vapor-liquid

equilibrium

data:

CNJ

II

cni

r-H PCLn o

i c

CN

PC

Author

Makranczy,

et

al

O

LO

r—l

r—

IIo

z

o

II0)

c

(0 cc

»

o

(/) (0 *»

(0

o

Accession

No.

150177

Comp.

Range,

mol

i

i

Press.

Range,

bar

i—

Temp.

Range,

K

00

ON

Osl

Data

Sets

With

Rating

= A

(n

a

=)

Data

Sets

With

Rating

= B

(N

B

=

1)

40

Same

data
System:

Vapor-liquid

equilibrium

data:

CM

CM

II o

CM

X+

CNI W

Author

Bartlett Morrison,

Billett

Schroeder

Seward,

Franck

Shoor,

et

al

COCO

r—1 o

uOi—

CMi

l Om

rHkO

CM

T—i om1—1 cm 05 UO O O O UO

uO i—1 i—1 c\ CO

CsJ CsJ 00 CM o o O UO

UO r—1

rH *

e. 05

oo VO rH o o o m

UO rH

rH *

#sOsl 00

in i—i o o o m

UO rH rH r " 00 kO

"d" rH o o O UO

UO rH

rH

r

CM rH O O o m

UO rH i—1 r r.U0 CO CO

''d’ 1—1 uO Om

05 rH

rH

IIozo

II0)ce«Ei 4*m

CCamm 5m

44o

(/>

(0

<0 o

Accession

No.

5121

150091 150183 150262 150021

Comp.

Range,

mol

.9986-.

9997 H2 ii

.018-.

025 H

.005-.

90H2

.000013-.

00014 H2

Press.

Range,

bar

100-1010

rH ooi—i i o

I—1

100-2500 i—1

Temp.

Range, K -

323

285-345 293-408 440-656 298-333

Data

Sets

With

Rating = A

<Na=

0)

Data

Sets

With

Rating = B

(NB=

5)

41

Same

data
System:

Vapor-liquid

equilibrium

data: oe3uc3Q

OO

Cl,

PCOHa

on

II ou+ CO

toto®oo<oE®

©»c

<0 ccaEo

u>

<0 An©

O*C

<0 CC

to

to©®

O)c©

ccs a£®h

o-

-dmj- coouoI CM

l£> o

lOoO

r-^ oooI o

CM

a-, coo

CJooI o oI CM

CMI MfCMI o

CT\ o

oo

lO

CMoo

CO00

CM

00

CO

oo >o

•Hc

J3

cn

Cl> x:oo

)-i oH

mT

CO

O'

CMoooI

CMI CM

CM

CM,—

I Om

(0

4*

(0 a

S2

J3

•H>

0)

j*: rC

C/) 3

><

ooOO

LO

cO

oooI oo

CM

CMI lO

oo

r—

CM

1“tI O

C^

18Ol £ C

cS Z < ^ * ^ cc

11<

cn

a)3O

l_>

PM

0)

CJ

a)

ccH

EHo

J3

CJ

U)3

a; > ouoI CM o

<r

CMvOO

CJ

a^

cooi lO

CM

lOOao

cooi o

CM

U0O

00 I CO I CM I co

CM

o-co

CO

oo

r^-

LO

r-'-

ism

m*d> m

v> 5 A 5

•;

m 2 > CB W fie o

IIGQ

IIozo

II0)camm 44

ce cc$m

44®

</>

(0

44

(0 a

42

Same

data
System:

Vapor-liquid

equilibrium

data:

II

CO

S3 . CJ . rx H • <d >

Ite . . • > • • o o H • X • • Pi • re CJ Jsi J= s • ”) • CJ • e • a • rx • • •H O • rx • Q • 13 PQ ol a •H • rx > 3 J X c c Pi • o • •H • >* 4-J 33 3 rx a o rx rx in r> CO jLi • M • u rx CO < H rx rx 4-J rx <d rx J3 rx CO C/3 CJ cd cd CD ai 4-1 00 rx oo >x 5-i 5-i (A rx CD e rx > rx • oo 33 e T3 3 CO c CT3 3 CD •H •I-) o 00 o rx CO PQ 00 O o 3 3 a) •H c 1 1 1 1 !-i o kO 03 e 4-1 CO <D cd •H O O 03 CD c r—1

T) CJ r—I

!-i 5-1 )-i i—1

03 CO JlC 3 rx E-* 3 3 X •H i—1

•H CJ •H cd

a 4-J •H -3 03 3 O 3 CJ 3T

O

PQ pq cj cj

M s s ce CO CO rs CJ

mm H) kJ

a CO

H

Ozco 00 i—1

CO LO oo *“ CTn nt <r v£) CO rH Nf o VsD CN co LO cn (0 1—1 o o oo CN LO CN o CO LO 1—1

ND rH rH co

<0 o CO LO <T rH o <N CO r^. xO ON co NT o a> LO i—i ®oo

CN LO LO CO C\1 CD i—1

CO o O'. 00 o GT> LO ON LO o> NT

ON T—1

CN xO i—l 1 1 i—100 tH co oo LO CN i—1 1—1

Osl oo LO <—o <3 N <3 NT -d E M X o re X CC X re re re re CN CN re re re o i re CN re CJ a ss cj cj CJ CJ CJ CJ CJ CJ a a CJ CJ CJ CJ CJ ©

CD v£> LO vO oo c oo LO i—1 CTn nt CTn LO CO xO o LO CTn <0 • CTn LO CTn 00 oo On • • o • • o • o o o o On • • • oo • o o

oc o o i o o o • o • • • • • o o o • o • I 1 i ON 1 1 1 1—1 i i—1 1—1 rH 1—1 o i 1 1 o i i—1 LO d LO o 1—1 LO o 1 LO i 1 i 1 1 oo co o 1 CO i CN o CN o o o 1—1 o o o o o o o i—1 co CN rH co o CN Eo o o o o o o o o o o o o o o o o o o o o O

w»®A® vO 0) v£) o o <r kO • c 1—1 • LO oo • CO LO • o LO o \D • rH CN LO LO nT NT i—1 CN LO i—1 LO rH CN 3 rH CN © i 1 i 1 i i i i 1 i i i i i O On i i IE ND CM o o o T—I oo CN rH o o LO o NT o

CO1 o i—1

oo 8 ®® o CO o r—1 1—1 CN O rH o o 1—1

rH co rH i—1 H rH i—1 o ®1®0.E

LO

®

<!• o rH NT o o o • • ' 1 CN 0) 1—1 • • • CO rH • LO 0^5 c • LO o o oo o • • oo CN i—1

rH oo CN « LO CN i—l 1—1 i—1 i 1—1 o CO cc o <—1 i xO 1 o i rH CO rx o 1 1—1 i—1

On i—l i CN oo o oo o o o LO i—1

rH Oxl 1 i r—1 i vO oo 1—1 • ND • o vD • • • rH ON • • LO oo i • • 1 CN • CN • • CO o CN i i o LO • CO • a i—1 ro rH o i—1 o i—1 LO o 1—1 i—1 CN CN *<r CO rH CT> E i

l ON oo i—1 rH 1—1 i—1 i—1 oo oo i—i

rH co rH CO

®

1-

IIOzo

II0)ce«K M

(0

GC

<*& 9

<0

(0

+•» (0 o

-<r re

cj (09

<0

(0

(0 Q

IIos £ C H “ 5 <0 ^ oc

it<

(ft m

11

®

_ re <0 £ e « > ^ a w S *

ooIIm

43

Same

data
System:

Vapor-liquid

equilibrium

data:

I!oo+

04

a

Author

Arai,

Y.

Kaminishi,

G.

Krichevskii,

I.R.

Somait,

F.A.

Yorizane,

M.

Yorizane,

M.

Zenner,

G.H.

Abdullaev,

Ya.

A.

05

Csl Omi—

vO

CNOmi—

05oi—om

T—

o

05oomi—

yOmot—

coo

COm

COooo

oo

r-'

IIozo

II0)cM

(0

AC

+*

BOMB £

(0o

<0

(0

+-* (0 a

Accession

No.

76499 39337

150270 123894 90120 76576 19620 9518

Comp.

Range,

mo!

0-0.57 N9

0.05-0.25 N2

0.006-0.19 N?

0.0-0.353 N90.01-0.30 N20.01-0.30 N20.02-0.30 N2

0.01-0.285 N?

Press.

Range,

bar

24-144 37-127 61-103

31.6-121.8

41-118 41-118 13-139 41-152

Temp.

Range, K

253.15-288.15 233.15-298.15 288.15-301.15

270

273.15 273.15

218.15-273.15

273.15 i

Data

Sets

With

Rating = A

<na=

1)

Data

Sets

With

Rating = B

(Nb

=i )

44

Same

data
System:

Vapor-liquid

equilibrium

data:

II

H k> • o [H PS • £ # . X s X 3 d 3 o #s 4-1 * P-S Jo bO o 3 3 • cd 3 Cfl •ro O pL, s •H 3 K*S CO

CO i—1 3 3 1—1 * o i—1 U 4-J *H 3 o w O cn a EH • ozc•o vC

<d*O Csl 00

CO CN oo CO co LO LO (0 C0 co rH LO CSl 1—1

oo <t CP lO rH 1—1

OS oo LO oo<

mmm Oc Csl CS Csl CM CsJ CS c a a a a a a ®

0>g 1—1 o 00

Csl 00 CO Os

(0 • • LO o • fir o o • • • o 1 1 o o rH 1 o LO i 1 i LO £L

t—1 o o o o CM E o o d o o o oo

h.(0 £c* O

0) sO Csl LO

Csl CO CO LO c OS <—1

rH

T 1 i—1 I—1

(0 v£> i l 1 i •<r 1 o o r—1 o i E MT • • • • 00 a CO CM o oi r—1

(0

(0®

fc> a* CM00 lO © os O

CM O* ON • <r

r—I

rH o Os c o as rH <g * CO OJ i CO

LO i 1 i—1 co CO E CM rH o os i—1 • • • • • i e Os o 00 o a o o co 1—1 rH E

rH i—1 CM rH 1—1 rH

®

iooo

LOa

cmOI LOo

bC3mo

CM CM X

0033

QJ XO

•<r o

co

LO

CMoI LOoo

ooMrI oI CM o

11ozo

il0> cm

oc5©0)

te 4*ma

m

Csl

CNJI co

<r

oo

CN

Os

sO

P3CM o0)

CD

*-» (0 o

IIo> £ c £ ~ < ^ a

(0

II< o0)

II

_ o> £ e « 5 5 «

ts > «® 5 a u

CO IICB

45

Same

data
System:

Vapor-liquid

equilibrium

data:

It

o

CM 2

+

CM 2

Author

Zeininger

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

79086

Comp.

Range,

mol eg

53

LO

i—1

1 o

Press.

Range,

bar

5-79

Temp.

Range,

K

213-253

Data

Sets

With

Rating

= A

(N

a

=

1)

Data

Sets

With

Rating

= B

Wg§

s

)

46

Same

data
System:

Vapor-liquid

equilibrium

data:

47

Sam®

data
System:

Vapor-liquid

equilibrium

data:

n

cn

CNl w

+

OJ

Author

Besserer,

G.J.

Kalra,

H.

Robinson,

D.B.

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

101683 110898 150522

Comp.

Range,

mol

0.004-0.16

N

?

0.0004-0.02

N

9

0.0-0.16

N

2

o

Press.

Range,

bar

17-207 1-137

17-207

Temp.

Range,

K

256.4-344.3

200.15-227.98

256,278,300,322,344

Data

Sets

With

Rating

= A

(N

a=3

>

Data

Sets

With

Rating

= B

CN

B

=)

48

Same

data
System:

Vapor-liquid

equilibrium

data:

II

on

EC3+

CM 3'

Author

Lindroos,

Dodge

Reamer,

Sage

Cannon,

et

al

Krichevskii

Khazanova

r—1 C\| LOo

LO1—1 o

CN

LOom\—i

r—1

COo

LO

T—1 o

ON

COo

u~l 1—1

00vO

co j oo

LO

IIozo

II0)ca sa

<0 cc

*-* IH

(0o

(/) <0

(0 Q

Accession

No.

150534 150543 54087

150514

Comp.

Range,

mol

<N 53m

ON1 mo

0-.16 N2

.0003-.

003 N

CN 3

vD

o>1 rH

Press.

Range,

bar

970-3810 34-414

21-48

101-304

Temp.

Range, K

303-383 278-394 200-283 273-348

(0 || 0 Q)

M

</) -C c 1 * S

£* o

Data

Sets

With

Rating = B

<Nb=

2)

49

Same

data
System:

Vapor-liquid

equilibrium

data:

Si

0

O

1 +

CM

53

Author

Kalra,

H.

Pvobinson.

D.B.

Barsuk.

S.D.

Ryabtsev,

N.I.

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

123897 119280 150190 150162

Comp.

Range,

mol

0.005-0.46

N

0

0.006-0.46

N„ M

0.015-0.21

N. z

Solubility

Press.

Range,

bar

2.0-207 6.0-207 10-118 7.0-99

Temp.

Range,

K

255.37-394.26

283.21,338.65,399.26

153.15-273.15

258.

15-318.15

Data

Sets

With

Rating

= A

(N

a

=

2)

Data

Sets

With

Rating

= B

(N

a

=2

)

50

Same

data
System:

Vapor-liquid

equilibrium

data

! co

Author

Akers,

W.

W.

Lehigh,

W.R.

Roberts,

L.R.

Skripka,

V.G.

Haufe,

S.

Ryabtsev,

N.I.

Steinbach,

H.

Data

Sets

With

Rating

=C

(N

c

=

,)

150067

Accession

No.

150075 36802150209 61574

150132 150162 41049

Comp.

Range,

mol

0.011-0.55

N

0

0.23-0.61

N

2

0.02-0.66

N

2

0.0008-0.28

N

2

Not

given

Not

given

0.004-0.014

N

9

Press.

Range,

bar

36-291 14-2916-235

5.0-196

Not

given o

o

i—

1

1 o

t''.

4.0-11

Temp.

Range,

K

310.93-422.04

310.93

310.93-410.93 153.15-273.15

303.15 298.15

273.15,283.15,293.15

Data

Sets

With

Rating

= A

(N

a

=

a

)

Data

Sets

With

Rating

= B

(N

b

=3)

51

Same

data
System:

Vapor-liquid

equilibrium

data:

n

CN o

C/2 +

CM 3

Author

Dean,

Walls

1

)

150547

Accession

No.

150546

Comp.

Range,

mol

.003-.

014

N

2

Press.

Range,

bar

16-36

Temp.

Range,

K

241-301

Data

Sets

With

Rating

=C

(!

Data

Sets

With

Rating

= A

(N

A

=

Data

Sets

With

Rating

= B

<n

b

=)

52

Same

data
System:

Vapor-liquid

equilibrium

data:

!

ii

i

CNJ

T 1 PCm

u

I +

CNJ £2

Author

Krishnan,

T.R.

Haufe,

S.

Data

Sets

With

Rating

=C

(N

c

=

o)

Accession

No.

116899 150132

Comp.

Range,

mol

0.001-0.44

N

2

Not

given

Press.

Range,

bar

2.0-208

Not

given

Temp.

Range,

K

277.59-377.37 303.15,333.15

Data

Sets

With

Rating

= A

<n

a=

o

<0«w

11 — jgfi « S I - „ S rr i

o

“ w

53

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

II

CN

t—

ECm

U

l C+

CM 3

Author

Kalra,

H.

Makranczy,

J.

vO

00

rH

IIo

z

o

II0>

c

*»

(0

AC

•mam §

m++o

</)

to

<*=» (D O

Accession

No.

115116 150177

Comp.

Range,

mol

0.002-0.40

N

2

Not

given

Press.

Range,

bar

3.0-208

10

Temp.

Range,

K

277.43-377.59 298.15,313.15

Data

Sets

With

Rating

= A

(N

a

=

1)

Data

Sets

With

Rating

= 8

(N

b

~i)

54

Same

data
System:

Vapor-liquid

equilibrium

data:

co

II + 3< QH3

co

Co

05(0©oo<©E©

9)£©

ocaEoo o

oo<r

<rXoooI ooooo ©A©

O)c©

cc

inm©

XI ©

0)c©

ccaE©

i00

a\COXX

roXx

<r

CMoo

to XI

00

•H

at

oo<r

<r

p

-fl

O' •H p,

ct

O >

cm

PCCMOoI oooo

CMOI T"H CN

CO

ooI X

00

<7\ CM

(D 44o

(/>

(0 2 £

ii0>c = 3= <

(0

II<

(0 o

cd >H• . vO > r-. • • o

P- X) • C • • • O

03 • c CO

X

m • a > H ' • • o c * o a (X r r-H • X rs cd o p • NT rH

4- •H

C rH 4-4 0)

rr

O 4- c o rH 01 x) 03 X O X a c 03 a) c a> * •H a i— 03 •H 4-4 •H o X i—1 o in * 4- i—1

S-i cd X)

p 4-4

X

u rH

O

p 03p

p XJ

X •H •H rH

r LO

cc 03 o cd cd CJ

B 03 •H rH

pc s S fp CO CO CO

H :s

x o o X O i—1 m * rH CO

e,CO 00 rH m o o m O i—1 m * <—1 o co NT co i—1

rH CT\

mO 00 C\| co NT 1—1

co ''CN

CNJ o 1—1rH rH o o CO rH

Cs oo o o X o o o o m o co m m X m m m m o m LT oo i—i

rH <r i—i i—i i—i

rH

O rH m * p rH

)- o ''CN c p* in rH c c - CL) p CN o

K'

O

X > c a 3 O rP

CNJ c CN •H Cd

m

r 23 CNH 23 > CN CN rH i—I 3 CN vO 2 23 ''CN X vO 2 o CN rH O o o CN O o m o O o o in On On o O • • O e • On c o m o On CL) o • a> 1 vO CN rH 00 1 • > 1 o > rH O <—1

nT o •H CO 1 •H rH • o O rH oo 1 00 o NT oo o o o 00 o O CO o o o 1 o asm o o 4-» o oo 4-4 o o o VO rH • • o 0 • o • • • o - o o 23 o o 23 o o o rHf^

'0> vOO

COO Nmr—1 1—1

CNJ

r

'CsJ oo

oo o NO 1—1 o NT ox o n- o o o CNi—1

rH o CO CO o o i up 1 1 O X o 1 o rH 1 1 o rH o o i r—1 o

rHm 1 1 rH i—1

vO rH rH CN

iiozwo

II

CO vO 00 CO co 00 0)

CNJ Nt NT o X

m CO c X CO co m co 1—1

vO BOOB i i i i • i CO oo X 00 co oo CO co 00

CNJ o (0 oo o CN O o o o

CO CN CN CN CO C\| CO vO CN QC

£,

4+

(0

<** o

<0

IICD 7 C

10

r *-5

(0 o ? (0 cc

O

II $

CDO

CO

CO

(0 o

<s o©E

co CO

55
System:

Vapor-liquid

equilibrium

data:

II

<r

CJ+o

cj

Author

Cheung,

Wang

Christiansen,

et

al

Mathot,

et

al

Sprow,

Prausnitz

Toyama,

et

al

Yorizane,

et

al

Jones,

Rowlinson o

Oni—1 00

wO

CsJ Omi—

vOo

<ri—

COIIozo

II0)cIKI

(0 oc

ira 5

(0

*4o

(/>

(0 4

(0 a

Accession

No.

25304 88244 17785 39204 11381 55395 19414

Comp.

Range,

mol

.03-.

25

CO

.03-.

97

CO

0-1

CO o

CJ1—1 1 o

.02-.

79

CO o

CJo

oo1 <

1 o

CJ

001 CN

Press.

Range,

bar

.3-5.2 4-47

.01-. 

CO1 i—1 7-50

15-39 11

Temp.

Range, K

91-124

123-178

91 91

114-186

143

146-181

Data

Sets

With

Rating = A

(Na

=6)

Data

Sets

With

Rating = B

(NB=

1)

56

Same

data
System:

Vapor-liquid

equilibrium

data:

LO

II

CN Oo+ou

Author

Christiansen,

et

al

Kaminishi,

et

al

<r

<r

04

001—1

LO

O'* Oo

oo

rn

11ozo

IIo>cooan

(0 cc

amm £

<00

(0

(Q

(S a

Accession

No.

88751 62196 •

Comp.

Range,

mol

.003-.

46

CO

.04-.

37

CO

Press.

Range,

bar

8-142

24-131

Temp.

Range, K

223-283 223-283

Data

Sets

With

Rating = A

(N*=

2)

Data

Sets

With

Rating = B

<NB=)

57

Same

data
System:

Vapor-liquid

equilibrium

data:

II

vO XCM O

+o

u

Author

Trust,

Kurata

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

73928

Comp.

Rang®,

moi

.01-.

83

CO

Press.

Rang®,

bar

9-117

Temp.

Range,

K

173-273

Data

Sets

With

Rating

= A

(N

A

=

i)

Data

Sets

With

Rating

= B

<N

8

=)

58

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

II

OO

•xcn o

+o

u

Author

Trust,

Kurata

Widdoes,

Katz

Cheung,

Wang

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

73928 3616

25304

Comp.

Range,

mol

.02-.

43

CO

.20-.

62

CO

.008-.

21

CO

Press.

Range,

bar

14-172 7-184

1 CN

Temp.

Range,

K

148-323 252-360

OO

CN

i—

1

1 OO

Data

Sets

With

Rating

= A

<N

a

=

2)

Data

Sets

With

Rating

= B

(N

b

=i )

59

Same

data
System:

Vapor-liquid

equilibrium

data:

II

COCM w

+O

c_>

Author

^redenslund

,Mollerup

Data

Sets

With

Rating

=C

(N

c

=)

*Same

data

Accession

No.

102912

*

Comp.

Range,

mol

.0004-.

17

CO

Press.

Range,

bar

2-237

Temp.

Range,

K

203-293

Data

Sets

With

Rating

= A

<n

a=

1)

Data

Sets

With

Rating

= B

(N

b

=)

60

Data

Sets

With

Rating

=
System:

Vapor-liquid

equilibrium

data:

CN

i—

I

ECm

u

ic+o

u

Author

Makranczy,

et

al

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150177

Comp.

Range,

mol

i

i

i

Press.

Range,

bar

i—

1

Temp.

Range,

K

298

Data

Sets

With

Rating

= A

(N

a

=)

Data

Sets

With

Rating

= B

(N

b

=

i)

61

Same

data
System:

Vapor-liquid

equilibrium

data:

v£>

II o

CM

3C+oo

Author

Granzhan

CNm

r—

o

LO1—

CO

COi—

o

ini—

CM

i—

omi—

m

CMi—

omi—

COmoomi—

mnGZo

II0)c>8» M

CO ccsmo

<n

CO +*

CO Q

Accession

No.

150280

Comp.

Range,

mol o

CJ

<ri—

oo1 CNi—

oo

Press.

Range,

bar

51

Temp.

Range, K

298-348

Data

Sets

With

Rating - A <n

a= )

Data

Sets

With

Rating = B

«nb=

1)

62 1

Same

data
System:

Vapor-liquid

equilibrium

data:

IIo+oz O

0)

01

<0

(09o0<o£9mc

<0 oca£o

o_

(0 A©

©>c

<0 oc• (0999

O)C

(0 oca£9

ICMmomoz

CNII o

cooi

'O'I 00

n.

CM

<0 *40J £ 2 i

«e a

iiOc

*5 < <0 oc

II< 0) £

to 5 « * o

IIw£5 CD

(0 oc

II

ffi

IIoo

IIo>cns

<0 oc$

(0

(/>

<o

(0 a

63

Same

data
System:

Vapor-liquid

equilibrium

data:

CsJ

II

o

CM X

+o

2

Author

•

Data

Sets

With

Rating

=C

(N^=

2)

150125,150127

Accession

No.

Comp.

Range,

mol

Press.

Range,

bar

Temp.

Range,

K

Data

Sets

With

Rating

= A

(n

a

=)

Data

Sets

With

Rating

= 3

<n

b

=)

64

Same

data
System:

Vapor-liquid

equilibrium

data:

II

53cj+

CM O

CJ

©©®QO<oE©

o>c

(0 aa aEo

o_

hm©A•k ©

0)c©

GCa ©©©©

0>c©

GCa aE©H

•H53

rH C/3 03 i—1

•H

T 1 N 53 03 kO c

03 4—* 4-J o 03 •H i—1

03 i—1<u rH

u c E

1—14—1 03 03 <—1

03 CD TO 03

03 (U * cfl & •rH 53

4-> #s 4-) •H *

4J #\ 0) a) 53 4-J * c e> 0) 03 rH 03 ai c o * •H pi o #s rH #i •H c u 03 4-) E 03

r\ rH C/3 a) oo c rv 03 c •H 5 C

*H 03 •H c C •H 5 E 03 •H 03 •H Pi

03 > > c ca E 03 5 53 E pi a;

03 03 o S P3 Pi <U •H

O o o -U c o Q Q 53 53 S3 Pm X CO H C/3

CO

m <r CM co

05

m c- oo o 50 CM 05 00 00

05 o CO uo c- 05 05 c- CO o oo CM <3* o m \—l

rH o o -d* o co o CO

50 o LO rH CN CM CO

m CM U0 i—1 1—1 t—1 i—1

50 »—1

uo ao rH i—1 t—1 i—1 N <r < X X X 53 53 53 53 53 53 h-U 53 53 53 CJ cj cj CJ U CJ CJ CJ CJ CJ CJ CJ CJ

00

05

LO 05 CN 05 CN oo 05 05

uo • 05 • U0 05 05 05 1 • l • • rH • c- CM • i r->. uo i 00 i l 1 i co CN i • 05 CO mo o uo o co • • o o t c- o o <—1

CM oo rH i i i—1 o o o

00 -55 CM CO co co i—1

MO 50 oo uo uo i 05 1 CN 1 M> l co i 00 uo i c- MO oo MO CO M3 oo CM i 00 i • i • 1 m • i • MO 1 rH 1 1 uo <—l

MO i 05 1 1 m

CM 05 i—1rH CO i—I

CM 00 50 CO 4

oo o M> rH Oo CO 05 o 00 co 00

oo o rH oo «1 CM CN 05 UO

CN CN CN CN CN CN CN CM CM CN CM CO o O O CO CO CO CO CO oo o co 50

LO CO CO o m CO uo P"- c- co M>

CN CM

r—1CN rH CN i—1rH rH CM CN CM rH

</>

(D 2 £

iio>c — +• ^<

CM

(0 Q

®

CC

II

CM

VsO

®

0)s 5

II01

_ c r 5 n ii

®a

®

oc

IIoo

II0>®

oc

32«®

(0®

44ao

65

Same

data
System:

Vapor-liquid

equilibrium

data:

66

Same

data
System:

Vapor-liquid

equilibrium

data:

II

EUO

+o

OJ

Author

Zeininger

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

79086

Comp.

Range,

mol

0-.58

CH.

4_

Press.

Range,

bar

4-51

Temp.

Range,

K

213-253

Data

Sets

With

Rating

= A

(n

a

=

i)

Data

Sets

With

Rating

= B

(N

b

=)

67

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

CNI

II

oo

SC

<T) o+

SC

cj o£*» CD 3 rH CD (D < u 00 00 •H cd

0)

C o S-i 00 S-i 03 cd js! AC

CD 0) 4-J o XJ 0) 0) C/D c a) > > CJ PC cd

C/D C/D 35 C/D 03 1 1 CJ

u S3 i—

4-1 03 cd CD •H c S-i 01 CD CJ r—

i—

1 1 •H CD CD 4-J o C/D C/D o S-i o rH

•H •H •H 03 •H

u 3 3 o CD CD 4-J J<5 o cd S3 S3 S3 3 CJ s Cm <c CJ CJ Pi >-i SH C/D C/D pp Si

a Ozco•cm 3) 1—

CO 00 CO CO uo i—

1 1 CO u0 vD o CO CO CO

CO uo uo 1 1 oo o CO U0 i—

CO e-- CO

®

co CO CM 1^ CO

O i—

co o- uo o uo UO CM UO CO 00 o uO uO uo oo UO CO 1—

oo o © vO VO oo CO 1—

i—

CO eg eg UO 3) oo oo i—

©<

ass©E

r_ 1—

~°r— r- 1—

1

i—

'—

tr- \ rH i

rH irH 1r- CJ cj CJ cj CJ CJ CJ CJ a CJ CJ CJ CJ CJ CJ CJ CJ eg00

® i—

o m uo c«

uo LO CO i—

uo o o e-* o oo

K • • o o o oo • • • • • o • CO e- o o • • • • o 1—

o T—

• o • 1—

• o a 1 1 i—

1—

1—

o 1 1 1 1 o 1 rH 1 o o

uo o i 1 1 1 o 1—

CO UO i CO i r—

1 LO E 1—

o o o >—

CO o o o o eg eg eg o rH o 1—

© o o o o o o o o o o o o o o o o o e- o

vOO

U0i—

.a o

co

®

vO CO rH uo o CO • • • eg eg c o . 1—

o o i—

• m o v£> I—

o 1 1 o oo oo i i eg oc

oo <r 1 1 o o 1—

1—

CO vO uo o i o 1 i vO r—

eg rH o o i i 1 o o uo uo e 00 i • • w 1 i • • \D • • • i eg i—

CM o o sc CO o o uO rH rH o o o CO

n® iio & z © o m 00 11 e

<o

CO egi—

0>

£C \—

uo CO CO ON v-O o CO CO CM c r—

<—

CO eg 00 CM o m UO eg UO eg CO CO eg '—

T—eg eg i—

t—

CO CO co rH i—

Q a 00 oo i o 1—

v£> 1 1 1 <3- i oo

rH 1—

1 i uo i o i o 1 CO l <r (0

g

CO i—

CM uO eg o o rH 00 1—

eg i—

i—

nr

eg CM <—

1—

r—CO i—

i—

co CO CO eg 1—

CO i—

i—

eg

®h nr—

5

(0 11

m (0 9 o& 9 y

nt eg

m

</>

(0

»** <0 a

With

Ratin

A 11 i m

+»

(0 a

With

Rating

B

rH11mz

c/)

(0 **ma

68

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

CM

II

I 00

i tu

i cn

! a

i +

> <)

I EC

! u

!

!

>

Author

Reamer Ahland

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150083 150136

Comp.

Range,

mol

0.1-0.

9

C

1

0.4-0.

9

C

Press.

Range,

bar

14-680 6-65

Temp.

Range,

K

277-511 271-274

Data

Sets

With

Rating

= A

(N

A

=)

Data

Sets

With

Rating

= B

(N

B

=)

69

Same

data
System:

Vapor-liquid

equilibrium

data:

LO

II

SBo

+

coOJ

SB

Author

Kohn,

Kurata

Reamer,

et

al

Robinson,

Bailey

Robinson,

et

al

Kohn,

Kurata

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

47671

150098 150040 150042 150086

Comp.

Range,

mol

.005-.

24

CH.4

0-.73

CH.4

.03-.

26

CH.

a <

scCO

cO

CN

1 c\i O

-

sb"' cj

CT4 OO

1 o

Press.

Range,

bar

14-110 12-134 41-124 28-110 .5-75

Temp.

Range,

K

189-366 278-344

311

278-344 192-353

Data

Sets

With

Rating

= A

<N

a

=

4

)

Data

Sets

With

Rating

" B

(N

b

=i)

70

Same

data
System:

Vapor-liquid

equilibrium

data:

<r

EEU

+

cn

EE3

Author

Data

Sets

With

Rating

=C

(N

c

=

2

)

88684,150520

Accession

No.

Comp.

Range,

mol

Press.

Range,

bar

Temp.

Range,

K

Data

Sets

With

Rating

= A

<n

a=

)

Data

Sets

With

Rating

= B

(N

b

=)

71

Same

data
System:

Vapor-liquid

equilibrium

data:

CO

II0i—

X

CJ1 +Xu

Author

Barsuk Olds

kO

o>mi—

SIoz0

II0)c

S3

(0 cc1

CO#

(0

co

(9 a

Accession

No.

84578

150070

Comp.

Range,

mol d~

ooo1 oo

0.0-0.38 C1

Press.

Range,

bar

5-118 6-116

Temp.

Rang®, &

198-377 310-378

Data

Sets

With

Rating = A

(Na=2)

Data

Sets

With

Rating = B

<nb=)

72

Same

data
System:

Vapor-liquid

equilibrium

data

II

x_ui GX

CJ cO©

(0©oo<oE©0> c

(0 ccaEo

o_

(0 13

v* ©

O)c

(0 cc

<0

<0©©

o>c©

ccaE©

IX3 4-J c 00

03 03

C/D pH

G

4-J 4-> t—1 X X) G <D CD o o CO C/D G c 3

CD 00 C/D

G •H

X CD 03 03 CD c CD cd C/D

X

C 0) rG i—1 1—1 00 00 00 00 CD X) 1 1 G o 03 •H cO i—1 3 cd •H •H 03 X CD X 03

prf s 04

w S COX

X CO cj 2 < P3

*NT co CO uO NO

O

co oo vO vO CN oo UO vO CO CO

CN CO NO o o UO NO

X o »—1 I—1 o CO CN o o o o <T o o o

r—1 o o i—1

LO UO UO 00 o LO UO UO i—i

CN co On CTn 1—1 i—1 i—1nT On '—1 1—1 i—1

rH t—1

r— rH i—1

r- ^ rH r- 1 1—1 1 1

r~ ^ rH

cj

O o o u cj

u

a cju cj CJ CJ

a

CN oo

CO 00 00 Nf CN NT CO • co • o o oo Nf • CO o • CO • o • o • • • • • o e • o • o i o 1 <—1 I—1 o o o 1 o rH 1 o 1 CO 1 co 1 1 1 1 1 rH 1 l CO 1 NO o 00 o o o o o co CO t—1 vO o o o o o o o o o o o o o o o o

CN CN i—1 oo oo

CN CO vO I—1 CO CO CN o CO o 1—1 CO rH 1—1 r—1

CN 1 CO i—1 t—

H 1—1 CN CO UO »

1 t—1 i—1 1 i—1 i—1 i—1 i i CN i—1 i X 1 1 1 CO i i • i vO i i o i o

CN LO 1—1 o o o CN NO vo o rH 1—1 <r 1—1 i—1 < 1 00 CO 00 oo vO CO

rH T—1

oo co G\ CO 1 1 CO co CN CN CN CO CO Csl CO CN CN

r—1

00 00 NO uO 1 NT t—1 1—1

Nf CN CN CO i—1 o co <

1 1—1 co u~i r-* i—1 CN i—1

CN 1 1 «—i

<N CN co co CN i—1 CN CN CN o

if) S 2

(0 Q

II9C

— * < <0 CC

II<

vDO

LO

CN00

if) W >>

II9 _ C - s;

m ii

<o a

(0 cc

DO

IIozo

II9cBOB M

(0

CC5

(0

44®

(/>

(0 4*

(0 a

73

Same

data
System:

Vapor-liquid

equilibrium

data:

If

EEo

+

CM O

co

Author

Dean,

Walls

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150546

Comp.

Range,

mol EEO

m

O

1 m

t—

o

Press.

Range,

bar

17-36

Temp.

Range,

K

241,301

Data

Sets

With

Rating

” A

(N

a

=

1)

Data

Sets

With

Rating

“ B

(Ng=

)

74

Same

data
System:

Vapor-liquid

equilibrium

data

CM

<—

I

X

m

u

l o

<uc

K

CJ

Author

Rogers

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

71134

Comp.

Range,

mol X

u

on

oo

l o

Press.

Range,

bar

T—

|

m

l C\1

i—

l

Temp.

Range,

K

298

Data

Sets

With

Rating

= A

<N

A

=

')

Data

Sets

With

Rating

= B

(N

b

=)

75

Same

data
System:

Vapor-liquid

equilibrium

data:

It

C\l

LO u

I •-H +w

u

Author

Amick

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150081

Comp,

Range,

mol <r u

o

ro

1 O 0

Press.

Range,

bar

28-69

Temp.

Range,

K

344-450

Data

Sets

With

Rating

= A

<N

a=

i)

Data

Sets

With

Rating

= B

(N

B

=)

76

'Same

data
System:

Vapor-liquid

equilibrium

data:

77

•Sam®

data
System:

Vapor-liquid

equilibrium

data: m

CO

II o

CM

PE+

Ml" PC

cj

03 03 QJ p*i

4-» 4-J PC •H CD 00 QJ 4-J 4J 4-J 4-J N PC 03 pH 3 CD 03 4-J QJ QJ •H 4-J 1—

o pH i—

03 QJ 03 PO QJ

pp: pc; 03 r-H

B •H 03 o 03 00 P3 CJ XI t 1 1—

u a 4-1 03 CO 3 03 r-H 4-J N 3 pH pH 03

O s s 4-1 i—

CD r-H

u 03 4-J o QJ 4-J l-J 03 •h £ QJ 03 4-J <—

P' 3 03 QJ p-1 QJ CE e •r-> PE 4-J

r.

p PC QJ 03 3 03 r\ QJ ** CJ QJ ** C c CJ 4-1 03 3 4-J es r> * * 3 PE QJ 3 o o s qj P' 4-J > Ph QJ > B B 3 O 03 r* 4-1 3 p <

CD CD CD 0) •H o •H •H 0) CD r> rH oc 4-1

O CD e H p r—4 i—

* * 3 03 03 CD s-t 3 o 3 *H CD 4-J 0) 0) CD Pm QJ * r—

Pm 3 03 P3 CD 0) QJ rH 3 pH •H E

J3 P= •H 4-4 cc CD 3 PC o 4-J 1 i 3 po rPP pH 3 3 QJ 1 1 1 1 > 4-1 CJ X CO M o 1—

c 3 03 i—

O •H 3 < Ei 33 3 3 03 3 •H i—

- •H pc 3 QJ QJ r-H 3 3 QJ 03 U O O

CJ

aQa s o o Pd CO CO PC PC CJ CJ

W pH kJ S PS • Ozco

<T

m t 1 CO 00 pH

T 1 CO vD u0 uO oo o- o CO pH co 1 1 i—

O 04 O- CO co CM CO CO m oo pH co CO 04 05 pH (0 o o CM i—

o o oo o 1—

o o o o o o i—

o o uo ® o o o o o o i—

o o o o o o o o o o o o m m m m LO m CO m uo m U0 LO U0 UO U0 m U0 uo LO o i—

i—i—

<—1 1 i—

i—

pH r-H pH r-H pH pH pH pH pH rH pH o<

mm9 >d < |- < r <r <!• E

PC PC PC PC PC PC PC PC PC PE PE PE PE o cj o cj o CJ CJ CJ CJ CJ CJ CJ CJ

® VO

04o

0) o rH o e 00 o o CO o

<0

LO o o o o v£5 o CM o o

CO o • • o 05 o o • m o

jQC On • 1 1 • CO • • 1 oo i i i • i i i i OJ • 1 VO v£> 1 CO 1 1 1—

CO i i i 1 i i i OJ i UO

a i CO o o VO • CO o • i i i co i i i o i • 00 o o o o i «—

o o 1 o o 1 E o o o o uo o o o o o o

co o o o o CO o o o o o o uo o • • • o1 Sto «n©

atc On CO CO

ooo r-H co

m

m 00 MD oo MO CO oo o

CC

COl vO1 38 52 1

'sO1 1 1 1 CO1 CO1 vOl

r—l1 • CM OJ i i i—

O'. o <t CO vO MO

in 04 CO OJ r—

OJ <—

<r pH t—

i—

co '—

pH i—pH pH 1 1 a© IIo &*a© o

o> II e© 0>

CO CO 1—

uC On o 04

r—

00 CO CO co co oo co CO oo o oo o c 

CO O'-

m CO o CO >—CO o rH oo

CO CO UO CO CO CO vO co OJ co OJ CO CO co 04 **

a i—l i 00 i i—1 1 oo 1 00 1 1—

1 m 00 1 00 i CO 1 CO 1 00 1 U0 oo CO co i r—

oo l m 1 CO to E i—

ON pH On CO 1—

04 CO CO OJ oo CO o- CO 05 CO co uo

CO CM CO 04 04 CO CO OJ OJ OJ 04 04 04 04 OJ 04 OJ OJ OJ cc

©

»- s m gft ce m

II +*

© 9 o m 9 m

to **

to Q

With c ^ 3 < '< m 5

</> to

<** to a

With

Rating

B

04

IIta z

(0

to +*

to Q

78

Same

data
System:

Vapor-liquid

equilibrium

data:

79

Same

data
System:

Vapor-liquid

equilibrium

data:

80
System:

Vapor-liquid

equilibrium

data

81

'Same

data
System:

Vapor-liquid

equilibrium

data:

LO

II z

00

scro u

+

Csl O

u

Author

Hamam,

Lu

Reamer,

et

al

Akers,

et

al

Poettmann,

Katz

Roof,

Baron

Accession

No.

110896 150099

3518

150059

<Tm

m

<T

•

Go§np.

Range,

mol O' o

o

egoo

1 O

c O

u

05

l o

CN

si c o

CJ

i—i

i o

J CM O

u

vD

05

1 50

CO

0O

o

o

05

1 CO

'—

)

Press.

Rang®,

bar

<tvO

C\|

1 CO

7-69 1-34

12-70 49-68

Data

Sets

With

Rating

=C

(N

c

=)

Temp.

Rang®,

K

244-267 278-344 233-273

290-367

.

305-361

Data

Seta

With

Rating

= A

(N

a

=

2)

Data

Seta

With

Rating

= B

(N

b

=

3)

82

'Same

data
System:

Vapor-liquid

equilibrium

data

83

Data

Sets

With

Ratings
System:

Vapor-liquid

equilibrium

data:

84

•Same

data

System:

Vapor-liquid

equilibrium

data:

'Same

data
System:

Vapor-liquid

equilibrium

data:

II

CM

t—I wLT| uIc+

CM o

CJ

Author

Besserer,

Robinson | 1—1 03 4J

<u• Nac

03

03 a

Poettmann,

Katz -

vO

o>

001—1

IIo

zgO

II0>cOSES -M

(0 cc

j£•e

(a

(0

(S o

Accession

No.

150197 150177 150059

Comp.

Range,

mol CM OU

i—1 1 o iii C O

CJ

vO1 \D

<T

Z.|

Press.

Range,

bar

.3-96 i—1 !

1-98

Temp.

Range, K

278-378 298-313

296-405-

Data

Sets

With

Rating = A

<NA=)

Data

Sets

With

Rating^

B

(NbS

2)

87

Same

data
System:

Vapor-liquid

equilibrium

data:

CMNT

II £Q*m9O«<og

9k 9

0»£

<9 KaEQ

U_

k.(S

<43A©

0*£

<0 cc

<0

<89

01£

<0 OEa Q.g®H

T)

C cd •H c o c c c

•H 0) cd i—1 g

cd fH £ * bo *H rs C rs J3 <D •H > O nO o c 3 •H g •H O 0)

rs cd c c D3 c 4-J •H <d nj

cd •H r—

A! a) o cd cd o o £ H H

r—

LO o m 00 nO LO o o 1—1 T—

1—I 1—1 o o O o o

LO LO LO U~l LO i—1 i—1 i—1 1 1 i—1 c J CN o CM <N o o* o o o o o CJ o o

LO ON LO m

On CO CM CO

on I—1 1 LO 1 <r 00 • 1—

o o i o o o o ' ' o o o o

LO oo LO LO 1—

o co r—

CO

LO LO i i 1 1 I o o I—

00 o o i—

on 1—CM

CO CO co CO CO o CM CM CO NO NO NO 1 00 CO CO CO CO

CN

CN co co CO +oo ©m2 5

itc — ** <

<8 o ©

AC

N< 1—1 O

x

cd 4J CNOn <9

4-J i—ir^

r

4-J Cl) oh (9

cd 1 1 LOO T3

0) 05

T 1 J-l I—|LT|

rs 05 •H cd *vH • ! rN c cd CQ c rs c cd •H •H i—INO

05 <u £ rs cd •H i—ir- 00 1 £ C o Oh to

r—

<D rs o 05 LOO * i cd rG rs c 05 * c i—liO c u 05 cd CD 3 CD •>

1 -C 4-J 05 00 J-l C o > rH ^ r» CD *rH cd i-l J-l o 1—1 rH rH00

cd

u cd o o 4—1 *H CD i—INO i—

K W £ £ £ cn > NJ Oi—

CM LOO o

rHLO LO #>H rH f NO r. rs i On o i—

vO rH Oi—

CM LOO o i—liO LO i —

i—

NT rv rs co CO CO Nf i—

CN i—

an LON) CM On CN CO oo an CO o sO oo o

r—i—

o co o LO 1—

CM OM Csl o o o o o o o o LOO o

LO LO LO LO LO LO LO Ln <—IlO LO

r—i—l—

<

1 1—

i—1 rH 1—1 *rH i—1 LO r rs NTO vO Olo on

C>i

—1 rH i—IlO LO CN CN c 4 CM CM CN c J n—

i—

o o o o o o o <r r rs U a o u CJ a o

Olo On OM i—1 LOO o i—IlO LO

rH

—

rH o CO r r< oo o CO CO NfCO CM o CN o 1 • o o OcO on • • 1 1 • • Ol—

rH 1 i—1 • 1 1 CN i i LOO o

CM i i LO o oo r—

rH LO LO o LO o o o o o ®Y— *—

o CN o o o o nT rs • • • • • • OCX) oo OCM oo Or- i—

LOO o

rH LO LO l

rH

rs CNNt N) rCM CM oo co Oi

i—1 LO oo o o

LOlO LO LO i—1 <—

1—

CO an T—

nD -<r LO CM 1 1 i i an i 1 00 1 LO LO 1 an

r—

LO • 1 1—rH CM rH CM

ilozwO

IIa

co CO Nt co 00 NO 00 co c 00 o LO an Nf as o •an

CN CO Nt CN co CM CO co 1 co 1 CO 1 co NO CO co

©

oCM CMan N>

CO CM 00CN CM CM

an

CM

K • £ 9

in

iia

a 5 s ffl £? ^

(8 G

(8

OC

00 II

ffl $©©©©o

88
System:

Vapor-liquid

equilibrium

data:

II

CM

CJ

Author

o

<rLno

LO

i—

1

i—

IIo

z

O

II0)

c

<0 AC

5

«

e

(0

(0 **

(B O

Accession

No.

Comp.

Range,

mol

Press.

Range,

bar

Temp.

Range,

K

•

Data

Sets

With

Rating

= A

(N

a

=)

5 £ f M „ S ^ ® |Q %

5

s 2

a

“ w

89

*8ame

data
System:

Vapor-liquid

equilibrium

data:

ON

II

oo

ECco o

+o

ECCN

CJ

Author

Price

Miksovsky Matschke

Dj

ordj

evich

Skripka

Miniovich

Hirata

Miksovsky

Accession

No.

,

150116 150139 13495 64372 84579 91853

150102 150137

©

g

9k ®

w

c

m

re

s &

E

o

o

0.02-0.9

C

? p

CJ

o

I—!

1 O

o

1

0.0

-

1.0

c

0 1 CM

CJ

o

1—

1 o

o

0.

0-1.0

C

0.97-0.99

C„

1 CM

CJ

o

1—1

1 o

o

c- o

o

1—

1 o

o

Press.

Range,

bar

7-21

11-50 14-28 0-15

0.2-24 47-490.2-24 o

i o

i—

Data

Sets

With

Rating

=C

(N

c

=

1

)

108496

Temp.

Range,

K

255,283 303-369

•

311-367 127-250 203-273 304-307

197,202,273

303-369

Data

Seta

With

Rating

= A

(N

A

=

2)

Data

Seta

With

Rating- B

<N

b

=

6)

90

*Same

data
System:

Vapor-liquid

equilibrium

data:

II

vO

EEC4 U

+

C/D(N w

Author

Kay,

Brice

Robinson,

Kalra

Robinson,

et

al

Data

Sets

With

Rating

zC

(N

c

=

i

)

76312

Accession

No.

150096 150181 119280

Comp.

Range,

mol

.11-.

89

C„H,

3 ^0 a4 OJ O

LO

03

1 CNo

C u

05

1

i—

1

o

)

4

•

Press.

Range,

bar

17-83 16-31 .7-31

Temp.

Range,

K

267-360

283

200-283

Data

Sets

With

Rating

= A

(N

a

=

3)

Data

Sets

With

Rating

= B

(N

b

=)

91

'Same

data
System:

Vapor-liquid

equilibrium

data:

91

0

t—

W

o- u

1 •H+

sO

33

CnI

c_>

Author

Besserer Robinson Skripka

Accession

No.

87420

150522 84579

Comp.

Range,

mol

'si X0

U

kOON

1 o

0-.96

C

0 H^4

Mo U

i—

1 o

)

J

Press.

Range,

bar

5-54

11-54 0-24

Data

Sets

With

Rating

=C

(N

c

=)

Temp.

Range,

K

311-394 311-394 203-273

Data

Seta

With

Rating

= A

(N

a

=

2)

te«

11 -

m £

®

W AC

^

D

“ w

92

'Same

data
System:

Vapor-liquid

equilibrium

data: 3<

•He

to

t>0 s

*Ho

44

cO UO

hJ

II

CJIco eo0

<e

d>oo<oE

9k 0

0»C0

cca aEo

o_

h.0a0

01c0ca 0000mc0

oca aE0

LO

CN

v£> O

LOO

LO

vO o

00I LO

CnJ

CJ

COONI o

vO

LOI <r

CO

LOi

vO\D

COI o

CO

vD

COI COo

CO 2 H 9 9

(A

C

C 5 i 3

** o

CN

II<

03

tou

42

a) S

>n 42

•Hi—I U

(0 09£a

CO

CNJ cOOo

LO

cDO

CNI om

r-'. o

cno

LO

CD

(_>

OC

OCI o m

r^-

mom

m1 un

Nfmi CNcn

r-~ ml 'O’ m

IIo

<ri

CnJ CN

<r

<T\ COI CO

CO

ON

co

COA

M

,5 r- 9 w £ c 9 5 5 ~ > • a *

IIas

93

Data

Sets

With

Rating =
System:

Vapor-liquid

equilibrium

data:

II

CM

i—

PflLO o

I c+

vO

X

CM

CJ

Author

Reamer Herlihy

G>

\D

Accession

No.

150119 150370

Comp.

Range,

mol

o

T

!

1 O

O

K-Values

Press.

Range,

bar

3-61

34-63

Data

Sets

With

Rating

:C

(Nq

—2

)

87946

,

150 :

Temp.

Range,

K

<r

i 00

C\! 339

Data

Sets

With

Rating

= A

(N

A

=

1)

Data

Sets

With

Rating

= B

(N„=

i)

94

'Same

data
System:

Vapor-liquid

equilibrium

data:

00! 1

II

T—1

cd cd cd CU p: -u 4-J •H co

00 pi 4-J

4-J 4-J 4-J rH MO cd Jd cd 4-J i—l

<u cu CU cd

O rH i—i

CU 6 <u cd Iks PC PC rH a cd DO MD <D rH i—1 O

r\

a CJ 4-J cd rH cd 1 1 N *H rH cd 4-J P S s a> cd cd 4-> O 4-J 3 •H cu

p> 4-) >-i cu Pd Pi PQ 4-J o 00 r» r» * CU 4-J cu * CU * 3 3 c pi Pi c 0) r\ *•> r* 3 PM cu <rs DC Pi 1 •H o o o »N e e C 01 H—1

Pi * C CU 1 1 CO CO C0 1 1 #\ •H *H cu r' cd <4-1 o CO P> <4-4 W Pi Pi S-4 •H cd cd CO C Ml •H CO 4-J 3 pi * <U a) a) 01 <D 3 3 CO cu Td rH •H Pi cd 3 c MO Ml MO c 6 1 1 p) Mi «—i

pi Pi CU * rH

O cd I 1 rH i—1 c cd pi

C cd

u cd <! Pi 3 Pi 4-J rd o P) pi p> cd CU <u 0) i—i

p) •» ) o OO cu cu

C cj CJ cj CJ

a DC PQ PQ CJ

H

a S S 3 3 3 • ozco

CO o T 1 Nfr 00 MO UO LO <—1

ON

T 1 CO o o

r^. 3 00 i—1

00 co U0 co CO UO i—i

CO CM ON rH CM LO CO T—1 o o o o o o o o o o i—1 o o U0 o o ® O o o o o o o o o o o o o o o o o o

uo LP| LO UO UO UO UO UO 3 UO UO 3 LO LO 3 3 LO i—1 i—1 i—1 T 1 i—1 i—1 i—1

rH 1 1 rH iH i—1 1 1 i—1 o<

MBo 3 VI MO 3 M ) M

V 0 MP NO 3

PC PC 3 PC PC PC PC 3 3 3 c CN O' CM C\ c <n C 4 CN CN CM Sb CJ cj cj CJ CJ CJ CJ CJ CJ CJ ®

0) CO e o CM o

(0 nt o o o U0 o • o • LO AC CM • 1 • 1 CM ON i i i i i CO .1 i • ON 1 1 CO CO CO i i i i co Mi i • I i Q, • on o OO o • i i i i o O ! i 1 t i o o O o 1 • o O 00 E 00 o o o o CM 1 o O 1—1 o

M0 o o o o o oo o O o o

hm«nm®

0) o c o o 3 CM <0 MO LO CM CO oo (C co oo 1—1 <t i 3 00 i 3 1 00 o ! NO

co i CM 1 o CM l CO 1 1 CM Nt CM Os] i—1 i—1 I—1 T 1 1 1 CO rH rH «0©

0.*

Ok o

0)c

(0 oc co CO co rH co 00 CO CO M> oo 00 CO

in -d- rH o ON 1—1 ON oo o rH • co co MO m CO CM co CM CO CM co co a l nO 00 i—i 1—1 1 r-H 1 co 1 rH 1 CO 1 00 1 LO CO oo 00 u0 i-1 CO CO E•H

00 ii rH i—1 i—1 CO r- o- ON ON 00 3

CM CM co cn CO nJ- co CM CM CM CM CM CM CM CM CM CM «V9E

CO

95

Data

Sets

With

Rating

sC

(Nc

Si)

150125
System:

Vapor-liquid

equilibrium

data:

96

'Same

data
System:

Vapor-liquid

equilibrium

data

97

*Same

data
System:

Vapor-liquid

equilibrium

data:

I!

00 XCO a

+

in01 X

Author

Brewer,

et

al

Gilliland,

Scheeline

Kay

,

Rambosek [

Steckel

Accession

No.

150199 150105 150260

00

t-H o

Ln

i—

Comp.

Range,

moB c

CN W

LO

00o\

1 CNo

COCN

US

m

ro

<T

1 rHO

CO

CN

o

1 kD

r—

CO0

H3

i—l

1 o

4

>

Press.

Range,

bar

1.4-27.6

28-41 7-80 2-17

(1O

z

o

li0)

c

**

<0 oc

«**e

(/) <0

(0

Q

Temp.

Range,

K

217-344 324-367 272-366 • «

‘

243-288

Data

Sets

With

Rating

= A

(n

a

=

3)

Data

Sets

With Ratings B

«N

b

=i )

98

Same

data
System:

Vapor-liquid

equilibrium

data:

j

,1

i

i

II

00 X

CO

CJ+

COo

u

Author

Miranda,

et

al

Data

Sets

With

Rating

=C

(N

c

=)

Accession

No.

150374

Comp.

Range,

mol

0-1

COS

Press.

Range,

bar

4-39

Temp.

Range,

K

266-355

Data

Sets

With

Rating

= A

<

N

A=

1

>

Data

Sets

With

Rating^ B

(N

b

=)

99

*Sama

data
System:

Vapor-liquid

equilibrium

data:

il

0

t—

<r

CJ

1 +

co

rcco u

Author

Hipkin |

Skripka

Hirata Hirata

Accession

No.

39202 m

00

150102 150103

Comp.

Range,

moi

CO

CJ

o

1 o

o

0.

0-1.0

c

3

o.o-i.

o

c

3 CO o

o

r—t

i o

o

•

Press.

Range,

bar

1.2-41

1 r^. o

CN

1 O

10-24

Data

Sets

With

Rating

sC

(N

c

=)

Temp.

Range,

K

267-394

253,263,273

237,249

340

Data

Sets

With

Rating

= A

«N

aS

1)

Data

Sets

With

Rating

= B

«N

b

=

3)

100

’Same

data
System:

Vapor-liquid

equilibrium

data:

v£>

II

0<—

i

X

<t u

1c+

oo Xro U

Author

Kay

Beranek Skripka Grieves

Nysewander

Hirata

Ito

z

o

IS9

c

S3

CO oc

JZ

s

•**o

0)

(0

*s®» CO a

Accession

No.

150203 150507 84579

150056 150061 150102

Comp.

Range,

mol co o

o

i—i

i o

o

a~ u

1—1 O'* o

1 o

o

0.

0-1.0

0.46,0.7

C

0

3

0.16-0.82

C3

0.

0-1.0

C

Press.

Range,

bar

20-43 4-34

l LT) O

1

42-43

5.5-42

CN

1 CNO

Temp.

Range,

K

332-425

303,323,343,363

253,263,273

391,404 310-411 237,249

Data

Sets

With

Rating

= A

(N

A

=

2)

Data

Sets

With

Rating^ B

(N

b

=

4)

101

•

Santa

data
System:

Vapor-liquid

equilibrium

data:

II

oo

tccn o

+

CsJ o

CO

Author

Glowka

Accession

No.

150524

Comp.

Range,

mol CM O

CO

1 kD

ro

Press.

Range,

bar

13-44

IIo

z

o

IIo>c

<0 cc

*»

•

e

(0

(0

(0

o

Temp.

Range,

K

323-363

Data

Seta

With

Rating

= A

(N

a

=)

Data

Seta

With

Rating

= B

(Ng=

)1

102

Same

data
System:

Vapor-liquid

equilibrium

data

I

II

C\! XLO 0

1 •H+

oo Xcn o

:

Author

Vaughn

Data

Sets

With

Rating

=C

(N

c

=)

*Same

data

Accession

No.

150069

Comp.

Range,

mol 00 Xm

a

1

t—

1

Press.

Range,

bar

1-45

Temp.

Range,

K

273-448

Data

Sets

With

Rating

= A

(N

a

=)

Data

Sets

With

Rating^ B

(N

b

=

1)

103

Data

Sets

With

Rating

=
System:

Vapor-liquid

equilibrium

data:

II

CM

r-H XUO ai c+

co XCO u

Author

Vej

rosta

CD00

ctf CO

a)00d

co

Accession

No. i—

00O'

COO

CMO

LO

r—

CO

CO

LO0

LO

rH

co

\DO

LO

1—

Comp.

Range,

mol

a Xo U

co031 UO

00

K3 co U

rH1 O

a

O

00

XCO 0

O'1 LO

CO

Press.

Range,

bar

00co1 COco 1 0

Csl

rH1

lO1 CM

Data

Sets

With

Rating

=C

(Nc=)

Temp.

Range, K

CO00

co1 co

co

00

vO

<1*1 CM

co

CO

co

co1

CM 1 CMco

Data

Seta

With

Rating = A

(Na=3)

Data

Seta

With

Rating = 3

<N„=

1) =^

r.

104

Same

data
System:

Vapor-liquid

equilibrium

data:

O3<

IIo

CM a

00 a

CO u

CO«

(0ooo<oEm®

0»e

(0 OC• aEo

o_

fcr (0 nmO

O)C

<0 ccm <0

(0®

O)e

(0 QC• aE•

a3 <u

4-1 CO 4->

4-> 03 4-> i—1 cu N c rH <u ctf a 4-» i—1 o3 00 i—1 u 03 03 OJ rH 1—1 rH rH 4J s a Q t—1 o 03 •H cu

4-» o a

a * cu a 4-J

a CO •H 3 * 0) 0) t>0 3

CO •H

a *>C * c a 4-4 c 3 (U o 4-1 CO a 03 N cu r* 4-4 4-4 o 3 4-4 o 3 cfl 0) e CU CO CO 3 •H C/3 a 3 c CO a a 4-1 a CO o E i—1 •H cd 3 3 03 CO 4-1 CJ 3 o a 3 3 r» rH

03 03

a 0) 01 c TO

a CJ < 3 3 4—1

N i—1 o l-l o 3 t 1 0) 03

U

O CU cu <c a a a a CO o T3 a S s s 3

C5 o CO o u~l LO 05 LO 05 1—1 o o o LO CO CM rH LO LO 05 05 CM 05 CM LO 1—1

rH LO o rH CM o 05 rH o o o o o o o o o o o '—1 o o o o o

LO 03 LO LO LO LO u-l CO LO LO LO LO LO

rH rH 1—1

rH i—1 i—1 t 1 rH rH i—1 i—1

rH '—1 a 0 2 00 a c o oc 00 a ) 00

a

aaa

aa

aaa <r P > CO P c "3 P" C^ P 3 CO o u CJ o o CJ CJ CJ O

50 CO a o o CO o 05 o 05 05 o LO 05 o 05 05 o o 05 • O'X 05 • o m 05 1 « • 1 • LO 1 50 • i i I 1—1 i i CM i o 1 CM i 50 i i l o 04 CM o co • 1 • LO o i 1 1 o o o o o 1 i 05 o o o o o o I—1 CO 05 o o o o o o o o 05 o o CM oo 00 CO PM <

1 LO 05 1 1 CO i i—1 o *<f i CO i co

r—1

T—1

50 rH rH CM rH rH rH 1—1 i—1 i—1 i—1 i—1 O CM CO 05 CO CO CO rH co oo i—1 CM CM LO 05 o a i—1 o rH CO CO co LO co a CO CO co CO

05 r—105 05 CO 1 CO 1 1 CO oo LO 00 00 oo rH 00 05 co 05 co c04 CO CM OJ CM CM LO CM CM CM CM CM » II «

44• 01 50 •

II

C/> (0

44

to a

With 1

CC < ££

(Am9a

With

Rating

B II00 z

CS XI•E

<e co

IIOz

105

Data

Sets

With

Rating s
System:

Vapor-liquid

equilibrium

data:

C\l

II

u

i •H

coCN

EC

Author

Besserer,

Robinson*

Robinson,

Besserer*

'Same

data

Accession

No.

150104 150522

Comp.

Range,

mol COOJ

EC

«—l

l o

CO

Csl EC

i—

1 O

Press.

Range,

bar

2-62 2-62

•

Data

Sets

With

Rating

=C

(N

c

=)

Temp.

Range,

K

278-378 278-378

Data

Sets

With

Rating

= A

(N

a

=)2

Data

Sets

With

Rating

= B

<N„=

)

106

Data

Sets

With

Rating

=
System:

Vapor-liquid

equilibrium

data

,i

107

Data

Sets

With

Rating

=C

(Nc=1)

150041
System:

Vapor-liquid

equilibrium

data:

gg z

Csl

r-H X

U

I c

c/)CN X

Author

Reamer,

et

al

Makranczy,

et

al

Accession

No.

150093 150177

Comp.

Range,

mol CO

CsJ SC

CTn

1 kDo

i

i

i

Press.

Range,

bar

1-90

Data

Sets

With

Rating

=C

(N

c

=)

Temp.

Range,

K

278-444 298-313

Data

Seta

With

Rating

= A

(n

a

=

1)

Data

Seta

With

Rating

= B <N„=i

)

108

*Same

data
System:

Vapor-liquid

equilibrium

data

1

II

!

I

o

CM

ca+

cnCM X

Author

Clarke,

Glew

Kozintseva

;

Selleck,

et

al

Lee,

Mather

3

o

ln

^

i CN

CO

CNo

LO

rH

CN

CN

CNO

LO

rH

CO

IIo

z

o

IIo

C ! m

tr

+*

5

•**e

cn

(0

m

a

Accession

No.

150002 150276 150250 150273

Comp.Range,mol

coCM X

cno

o

i uno

o

o

c

n

CM X

<r

i—

i

o

i ooo

o

o

CO

CN X

vO

i—

i

l COo

o

coCM X

o

i rHO

o

Press.

Range,

bar

T—

1

1 Ln

rH

7-345

20-670

Temp.

Range,

K

273-323 433-603 311-444 283-453

Data

Sets

With

Rating

= A

(N

a

=

3)

Data

Sets

With

Rating^ B

CN

b

=i

)

109

Same

data
System:

Vapor-liquid

equilibrium

data:

if z

u

i c+

110

"Same

data
System:

Vapor-liquid

equilibrium

data: 3< g

cu

4-1 C3

33XGO

4-4 O

CD

a)Go

•"j 3

hJ

34

CO T—I O

CG

Il eo00ooo<oEm9mc

(0 oc• aEoo

CM

-cr LOom

•x

NO

CNI O

NO

00COOm

33X

ooi—i oooI r-'' i—i ooooo m

coomXX

<rol OnO

NO

CO

inomX3m

ooi ono

eg a9k 9

0»C

eg OC• 0

(09 I Csl I I COo •

o>e

eg oc

ft aE9 o

CN<rl co

co

CO

on

ON

-<rl o

CN<r o

CN

'O'I <r

NO

co

co

NO

coi OO

r-'

Csl

X+

332

CO

(0 o

II9 * 5 O

*H 34 1—1 G

cd 4-» i—1 3 CO cd X •H 4J CO Ph 3 c (U cd O c cd * pa cu r\ a G a 33 3 G n o «N CO CU -V •N CO c 3 G

cd CO cd cd cd QJ G CO u oc 33 -G O cd 4J g 3 CJ > cd •H o 3 3 Q a a a 2 3

oo CO oo 00 05

CN CO CO 00 o rH m o in CO m m o o o o o o m m m in m m

T—1

rH i—i i—i i—i t—i

CO CO co O’ CO CO

33

X 33 33 33 33

a

X 3 a 3

CN nD o o r—1

co • m m • NO 1 • • 1 • co i i CM 1 o 05 rH o m rH o nj o CN i ' ‘ o o1—1 o 1 CM i CO i m i i rH i i r—1 i i—1 i rH

CO oo CO o m CO 05 1—1

r>* co CN CO co i »—i

co co CO <r \D n- CM CO co CN cm CM CM

II

«s TP®£«

«>

A

11 £ 9 ^ c

<0 £ ~ CO 3 “

NO

IIOB

111

Data

Sets

With

Rating

=C

(Nc“2)

150518,150539
System:

Vapor-liquid

equilibrium

data:

112

'Same

data
System:

Vapor-liquid

equilibrium

data:

I

vO

II

Author

Black,

et

al

Reed,

McKetta

.

Kazaryan,

Ryabtsev

McAulif

f

e

Nosov,

Barlyaev

Wetlaufer,

et

al

«

9

<9 o

0

E

0

CO•

Accession

No.

150027 150207 150169 150029 150154 150050

Data

Sets

With

Rating

=C

(N

c

=)

Comp.

Range,

mol

.9997-.

99991

C.H

ir

a

LL cr

1—

1

EE

-o- o

o

o

o

o

1 rHo

o

o

o

•

i

i

i

EE

CJ>

uno

o

o

o

i

i

i

i

i

i

Press.

Range,

bar

3-4

2-22 '

u~>

1 CM i—

1

i—

1

r—

H

Temp.

Range,

K

:

280-295 311-378 283-313

298

278-343 278-318

Data

Sets

With

Rating

= A

<N

a

=)2

m~ 11 ~

r- 01 ** 5 £ _ H S +* ® §g

S tr

^

Q w

113

Data

Sots

With

Rating

=
System:

Vapor-liquid

equilibrium

data:

CNJ

II

CNJ

I—

LO

CJ

I co1—

K

Nt

CJ

I c

Author

Kay

[calingaert

n

o

z

o

II0) c

33

m

cc

++3

<a9

<0

(0

(0

o

Accession

Mo.

103629 150362

Comp.

Range,

mol CJ

i e

00o

1

1-1 o

0.02-0.27

C.4

Press.

Range,

bar

10-37

i—

rH

i r-- o

Temp.

Range,

&

1

358-464 298.15

Data

Seta

With

Rating

= A

<N

a

=i)

Data

Seta

With Rating

= B

<n

b

=)

114

Same

data
System:

Vapor-liquid

equilibrium

data: I

II o

<N

EE+oai ee

CD >

cd CO (D 4-J u cd CO 4-J <—l 4J rH rH 4J CD cd rH rH CD cd 00 jp 1 1 \—l

cd cd rH rH cd rH cd 1 1 4-J

V 1

1 cd CJ cd cd 4-J 4—1 0 En •H a) £ cd 4-) 4-> XI rH 4—1 CD Ph PE PE

4-1 CD CD 4-) 4-» cd CD rs

a 4—> <u rs CD CD c rs rs rs CD rs PO 5-i 0) *s rs EE 4-J CJ G EE c lh EE EE CD < rs 1 1 j*i O rs rs aj s •H CD cd M

1 O P LH

rs CO •H CD 4-) 5-1 5-i cd CO •H CO EC

p

CD PE CD CD CD rs rs EE CO 1—1

•H cd

CJ 0 C COU

G

G CD <D 1 p cd

p 5h rs, <—1

cd 0 C CD pp cd cd

a

C EE

CflN c 5h EE 4-J 1—1

5-1 cd 5-1 CD CD CD •H CD ai 1—1

cd CJ

O CD CD PQ PP Q EC hJ PE ES PE) 0 E*E S s E2 & • 0ze0Cd3CO CO xr CO m LO tH 00 LO LO LO rH 0 O

CXI 0 00 CN 00 xr CO 0 CN CO LO vD CN CN LO 0 rH 0 0 0 LO LO CN LO 0 0 < 1 0 0 0 0 O 0 0 0 0 0 0 0 0 0 0 0 O 0 0 0 0

#%

m LD LO LO

m LO LO LO LO LO LO LO LO LO LO LO

WO 1—1

rH 1—1rH 1

1 1—1 1

1 11 I1 <

1 rH rH rH 11 tH 1

1 < 0 c (. j u c O CE c 1 0 0 O rH r H 1

1 1

1

1 r—!

1- 1 1

1 rH

EC EC EC EC EC EC EC c c EE

g xr Xj - X] XT xr

X xr xr

CJO

O CJ

a CJ CJ CJ 0 CJ

®0)

v-O 00

CN 0 <

1 CN c r-. 0 0 0

(0 On 0

CT\ LO 1—1

UL CTn • • • cx • • 1 O 1 1 O''! 1 cj\ l 1 1 l l 1 a 1 0 xT 1

1 CN rH CTn l 1 1 vO l 1 1 00 0 • 0 0 • 0 0 • 1 1 1 0 l 1 1 E 0 1 0 0 1 0 0 1 0 ON 0 in 0 0 LO • 0 0 W On 0 0 0 0 1 0 0 O • • • * • • 0 • •

h.aa*®0) u-i c CN xr 1—1

co H# a> 1—1

vO c 1 VsD xr 1 xr 1 in xr xr CO xr 1 CO m 1 1 • 1 1 01

CO

CO CN 1—1

rH xr 1—1 1—1

xr 1—1rHT

—1 1—1 l

1 5 1 r

1 ®

fe 0. *6* O0) • e

CO cc XT 00 CO i—1

LO rH CN 1—1 C30 CO CO a> 00 00

CO C\J '—1

CN rH on 1—1 0 rH xr 0 1—1 •

cxj CO vO,# CO XT xr LO CN xr CN CO CO co CO co

a 1 00 1 rH 00 1 r>. 1 1—1 1 r—1 1 r—I 1 0 1 rH 1 co 1 CO 1 CO 00 1 xr 1 00 1 00 c 1—1

CM i

1 1—1 1—1

0- 1

1 CXJ a> 00 r--

O

CN CO \D CN CO CO CO CN CO CN CN CN CN CN CN CN

H

stm•Ea { m++9

(/>

<0

to a

ii

to oc < m

<0

to *3a

ii

(0

GC

CD iim

115

Data

Sets

With

Rating

=C

(Ne

=i )

150012
System:

Vapor-liquid

equilibrium

data:

116

Sams

data
System:

Vapor-liquid

equilibrium

data:

II

Author

Campbell,

Maass,

Hudson Morgan,

Maass •

Vosolsobe,

e't

al

OsJ mo

LO1—1 o

LOo

LO1—1

00

COo

LO1—1

c\i COCOo

LO1—1

r-H COO

LO1—1 1—1 vO

COo

LOt—1

\Q

IIozo

II0>c

(0 oc£5m

+*o

(0

(0 **

(0 Q

Accession

No. ;——

150363 150535 150384!

15.0510

Comp.

Range,

mol CN O

cn

r"- oi r-H o

C\] O

CO

vDi

1 1 i—1 O

CM O

CO

•vf1 ooooo

Cn o

cn

OsJ oi r—| t—1 oo

Press.

Range,

bar *

.14-5

CO1—1 1 o1—1 111 111

Temp.

Range, K

298-393 283-363 273-298 293-333

Data

Sets

With

Rating = A

(Na=) a* « - r a ^ a s m ii * s 5 z o w

117

'Same

data

System:

Vapor-liquid

equilibrium

data:

119

•

Serna

data
System:

Vapor-liquid

equilibrium

data:

II

CN

i—

PC

LT> u

ie+

CNI

t—

PCLO o

I •H

Author

McCormick

McClain

•

Accession

No.

150205 150278

.

Comp.

Range,

mol

Cr 33

u CJ

1 C

vDON

1 CO

siH ZI HS

0-u

1-0

Press.

Range,

bar

00

l CO

CN

* o

(N

1 r—) rH

Data

Sets

With

Rating

=C

(N

c

=)

Temp.

Range,

K

328-385 311-322

Data

Sets

With

Rating

= A

(N

A

=

1

)

Data

Sets

With

Rating

= 3

(N

0

s

i)

120

*Same

data
System:

Vapor-liquid

equilibrium

data:

121

'Same

data
System:

Vapor-liquid

equilibrium

data:

Ifo

CM

a+

CM1 1 a

UO 01 c

Author

Black,

et

al

Connolly

Liabastre

Namiot,

Beider

McAulif f

Accession

No.

150027 150200 150160 i

150161 150029

Comp.

Range,

mol

.9995-.

9999?

.01-.

41CI _H10 1 CMi— a

uO

O

COoooo

.00003-.

00006 CSH

1? o a"

i/ o

<roooo 11

Press.

Range,

bar

i—

152-709

rH

cni m

T—

CNl CNl rHO

LOi—

i—

11ozo

II0)cOfScD £

•OB $w©

<0

(0 o

Temp.

Range, K

279-298 573-625 278-308 293-344

298

Data

Sets

With

Rating = A

(Na=

a)

«• ^

18

— « £ i « I S ® "a

ts > -sT # nr **» O w

122

"Same

data
Multicomponent

Vapor-Liquid

Equilibrium

Data

1—

1

03 rH rH rH

rH C/3 3 > 03 03 ca

i—

1

33 0) rH a) <u c 4-J x •H o 3

o

I—

1

3 3 a) 03 1—

1

0 0) 3 3 3 CO X N •H CN 4-1 4-J 4-J 3 O X 4J 03 X X 03 H 4J CO 4-J (u <u <d Ihb u 3 4-> dj -u r. JD Q3 c 03 H 03

4-J <D 4J r> d) 4J d

#» ' 3 3 «—

1

X x X Cl n —J dJ C/3 N r* aj N 3 ai W 3 tn co co * > 4-J > 0) CD < * <u r >, 3 0 '—

1

3 O dJ > *

1

1 * 03 4-J o 3 3 * 03 i—

1

4-J d) 4- rH 0 X 03 X X o 03 pN 03 0) X 3 03

a) d) > d) T3 3 3 T 03 Cs 3 CO s U u C 03 X 3 rH 03 N N 3 "d rH N 3 o5 3 c N 4-j •H 3 <u CO Od) s

a s 3 4-J •H *H o o rH c cO > O 0 3 X d) X 5-1 30 CO dj CO X S-i CO 3 3

o 43 3 o 3 3 O c O z o X d <u O (U O

4-J o X 03 o O O X X H u X Q X 3 O X C/3 C X > HM CJ C/3 CJ <C X X >H Sh

6

z

c

o o- in <r r> 1

1 (A ON O' o m CN CN LT O NT NO CO v£> co vO X LO 00 C\ o x CN CN o CN co X CN CN CN CN CN co CN CN CN

CD o «—

i

c r>. o o O' a o o CO o OO CN o o o rH CN o t—

I

LO LO o LO o o\ X X LO X LO CN LO LO LO o rH i

m rH <—

1

rH LO NT CO X x 1—

1

v£> co v£> 00 X rH i—

1

'—

1

o

<

U.CO

©‘O)

C 00 r-N co X

o

CO CO CO CO r—

1

NT <r Nf ON o co o o> o\ o o 'sO CN QC rH 00 00 vO CO co X O" X CN rH 1 l rH X 1 \D

j CN

| rH i

0 o> r—

1

r> CO NT CN

1 1 1 CN1 NT nT CN 1 o 00 00

CO rH CO X CO CO X o

CO rH ©

k_ Q_

©‘O)

c

CO QC o

CO orH rH NT LO 00 LO CO LO X co CN 1 1 U

1 o co co i

i i rH CN x CN X X CO CN 1 l 1 o ON CN i h m LO i—1 CN CN CN X CN CN rH rH CN

| CN

1 CO © x X o o CO ON

1 CO

1 LO1 rH

1 CO CO

1 co CO NT Nt co

1 00 CO CO 1- 00 o o 00 o c rH CN oo r^. NT NT a\ Oh orH rH rH rH '—

1

rH X rH rH CN CN CN CN

O)

c

CO < < < 03 < <C <C <C X X < < CJ CJ < < CJ <c X X CJ X X

QC

CN CN a 00 X oc X

X X LO X x

• v X

<r CO CJ x CJ X

cj cj 1 CJ i CO

•rH •H CJ + + + +

+ + +

vC X X NO \D

X X o X o X PC CN CN

CN CN i—

1

CN CN <T CN o o

E

cj CJ m

nJ* CJ scNf

CJ X

CJ

CJ CJ CJ © + + CJ + CJ + 4- + +

i 1 o oo +

CO <r 3 NT 3 X NT C\ o <r

33 X X X X X CO o O Sx X O CN X X X

/A CJ z r CJ CJ + CJ + CJ NT r z - CJ CJ z z O CJ * CJ CJ X CJ CJ CJ w + + + O + O CN +

CJ

1 + + + + + + + + + +

1 1 rH t—1 3

CN CN CN X CN X X CN CN CN CN CN CN Os CN o o o

2 r X 2 NT 2 NT x 2 + z z z 2 2 z z 2 2

“ 2 2 2 CJ CJ CJ CJ CJ CJ + + + i + i t + oo + + + + + + + + + +

*H •rH 3 X <u d) d) d) <D CO a> CN CN CN CN fsl CN CN CN CN X X X + X + + X CJ X X X X X X X X X X

123
Multicomponent

Vapor-Liquid

Equilibrium

Data 3<C

.2

<ow©oo<

eg n©

05c

eg DC

COw©

•H •H B 33

—1 3 CO 1 1 1—

d •H •H d 3 c 3 H 4-J o •H d 4-J d <u d u <u H B H 4-J i

1 N N <u 3 N 3 <u

<u

d

d

d

d

U 4-J no 4-JO -1 4-J

#Nd 3 PJ <0

d «3 *N

H

dO <u

«N •H 4-J 3 4-J >•> 3 d 3 3 3 t—

3 1 1 +

05 -3 33 rv <15 3 cu

d 3 3 d

d

N * d CO CO •H * CN •H •N <u Po d -H B

r> CN CN >N CO

B no 3 4-J * 3 4-J 3 4-J

H Pj

N

ad 3) d 4-J (3

d 4-1

d <3 CO •H bO

d cu <ud o

•H •H *H •H •H CO <u 3 •rH 3 d

d

d 3 ? N 00

b & PJ 0) 33 3 CO > 3 t—

3 B

d co * 3 <u

O

dd o 4-J Pj o o <u <u 3 d o 3 o 3 3 3 O

>< 3 3 H in

H CJ CJ 3 PQ < co CO CJ CJ 3 3 >< CJ CJ

<T co 00 <f vD 'mD oo UO CO CO <t CO o CO t 1 CO 3 ro CM G't CM uo o CM H 1—

t—

Nl* oo t—

CM i—

mO CM o H o H 'sO C*. Nj- 3 o MO CO M0 o NT H o

LO CM CN

U0 t—

ON o UO CM CN uO o CM o UO

m ON Nf o U0 3 H i—

NO uo v£> vD NO

H 00

H UO 3 H MO 3 UO

H

CO 00 oo

H o

vO o co CO CO

H ON <t o 1— CO 

o CO UO uo

CM 1 i i <1 1—1 MO co

M3 MO

HH

u0 MO i CO UO <T 1 ON 1 H 1 1 <r co o <r UO H u0 o nJ* UO CM CM u0 CO i

1 co CO co MO Nf co '

1 H

co 1 i i co 3 o oo in CO CO t

1 o 3 On

H o

00 1 1 i CN

U0 o oo

U0 o H CM o o

CM CO CM CM t

1 CM CM CM i

1 CM t—

H CM CM

co 1 CO 1 CO 1 UO 00 Nf <—

co o CM nTH CM 3 uo CO CM H Nf UO Nt co CM NT o t—

i—I 1 H

CM CN CM

HH t—

t

1 CM CM CM

H

H

HH i—

1 1 H

pq < cj CJ cj <5 < c 3 <3 3 <3 <3 3 <3 3 3 <3 3 <3 oT 1 X!O O | I 1 d 3

NT 00 + CJ1 XCO

CM c CJ Oo

00 + + + 3 3 oo NO 3 vD

oc 3 3 CN 3 3 3

CM 3 CN CO CO o CM CM CM £ o CO CJ a CJ CJ a CJ CJ o cj : - cj : + = - + + + + “ ” + + - 4- + +

<r Ml <T <r <r 3 o o 3 3 3 3 3 3 3 O cj - = CJ = CJ - CJ a CJ - CJ - “ = CJ CJ - + + + + + + + + + +

CM CM C\ CM CM CM C\ CM CM CM 3 3 3 3 3 3 3 3 3 3 c

<u i—

a)co

to

coc

ect PQO

COON3

a>

coi 00

CN

•H33

CMO

UO

CONOI CO

LO

©

05C

(0 DCdE©

CMo

CMI UO

r^-

co

UO

CMI 00

O'.

05C

eg DC

CO

cj E©•*-> 60>

(/,

3CJ 2

35 + cT

3^-H

co

33co

<J +

33S

33 <f CMC

cj i e + +

Mf

33

O O'—l i—

33 35 + 0-3 O O

CM I I 3 tH 3

CM

124
Multicomponent

Vapor-Liquid

Equilibrium

Data

"

I 1 G3

cd CO

cd

Cd 4—1 kN cd C •H Ps

4-> cd QJ 33 QJ rH c O G3 1—

1

cd

4-1 4-1 4-» I j cd QJ CO CO cd 33

0) QJ 4-1 * o *H XI c cd cd O H o a) 3 00 a) G CO cd 4-» cd •H 4-» kO 4—1 23 3 2 u c 33 0) CO pp QJ co 33 4-1 cd 0) o aaa s: cd u CO cd O QJ 33 Td rs p P p tP p

r> 33 s c S3 rs Pi 23 O p QJ QJ QJ QJ cd pp

'jJ N G * cd c G c o 23 o QJ '

1 4-1 4—» 4-1 2 < 0) 31 CO •N •H CO * o O o * S3 <4H 33 P CO CO CO tH U OO 33 4-1 o i—

1

CO CO CO TO rv p cd QJ QJ QJ a; r» C

TO * Pi P c OO CO r—

1

QJ c c c C QJ QJ G 4-1 •H •H •H P o

N C QJ CL) G •H •H cd CO •H •H •H QJ PC U 33 cd 33 p p p QJ w

G o 3 3 QJ 33 p > c G X G 1*3 G •H 4-1 4-1 a Ph Ph Ph 4-1 c

O o O cd 33 QJ 33 cd QJ O o O cd cd p G cd •H QJ 0) QJ 4-» cd QJ Ph pi co qj 2 qj Q 33 pi 33 33 CO J3 Ph Pi 32 32 Q a Q w 2

d

z

c

_o co o CN v£> ON oo 00 00 CT\ rH o co uO CN r—

i

LO r^> NT Nf '

1 oo vD lO) NT NT nT CO LO o LO CN o o m o CN o o i—

I

r-l CO 1

1

i—

1

i—

1

co CN CN CN CN pm o CO 00 r-. r-> CN o o CN 1

1 <t O o <r CN o o o o o 0) o 00 CO LO NO oo o NO LO LO o CN t—

1

LO UP co LO LO LO) LO) LO UP o LO) 00 r—

1

t—

1

CN co oo 1—

1

CN rH i—

1

x> NO CN rH rH NO 1—

1

i—

1

i—

1

rH rH o

<

U.CO JQ

0)O)

c r-* o o Gj CO CN o o CN o 00 ON <—

1

i—

i

o o o CN DC LO CN CN CN CN i vO CO Nf rH rH 1 i rH N>. i 33 CN i rH

• CN o o i—

1

i—

1

rH 00 CO i—

1

CN Nf Nf VO

CO CO co CN ON <t CN ON >—

1

i—

1

co

CO

CD

2^, CL

<DO)

C

CO DCo o CN i—

i

oo i CO CN Nf 1 i

i—

1

CO i oo Nf l CN CN »—

i

! CO Nf 1 i rH oo i CN <—

1

i E CN i—

1

-d- co 00 CN CN co co ON CN CN

CD sD r—

1

i

l CO o CN rH oo CO NT NT 00 Nf CN NT 1—

1

h- i—

1

i—

1

rH i—i CN LO CN T 1 Nf 1—

1

UO NT CN NT rH

i—

1

i—

1

CO co CN CN CN co CN i

l i—

1

rH 1—

1

CN CN CN co

CDC

CO

CP pp <d <3 pp CJ <3 <3 <3 <3 <3 QJ QJ <3 <3 QJ <3 <3 pp pp pp CJ <

DC o o O

rH rH rH

33 33 33 + NT Nf NT

QJ QJ QJ co 1 1 1 33 •H C c

CO

qj c C + + + o t— r— c + i—

1

33 oo cc oo oo 00 c 33 oo -<r vO ’33 33 33 33 33 ® lD co 33 o 33 00 CJ CO o* CO CO CO

33 33 QJ co 1 CN CN CN 1 CJ CJ QJ CJ QJ CO CN CO 1 QJ c o CJ 33 c

Vi qj a G qj + + -j- + +

21 + + -f + z z + z Z z z z CO + + + + vO LO vO NO vC CN CN CN 33 33 33 33 33 CN

33 33 <d o o o CN Os CN CN CN i—

1

33 O 33 33 CN C\ 33 QJ QJ QJ QJ QJ QJ QJ QJ 33 CJ > 1 C_> QJ - cj cj CJ z z z z z LO) z z

, 33 + + + + + + + + QJ + -3 + + + + + 1 QJ nT nT -3 Nf NT C

CN 1 CN CN CN CN o 33 33 33 33 33 33 33 33 N n 3 3 z 23 CJ CJ CJ QJ QJ CJ CJ CJ CJ +

125
Multicomponent

Vapor-Liquid

Equilibrium

Data

cD

d

d o CO

CO i—I“H a) CO o o cD t-H CD X d X CO CO X 1—

V i—1 CD cD •H o o o o 4-J CO CD 4-J CO x sc x) -C X) sc 0) 4-1 0) o H X to o X o H 4-J -ui cu PC s) cD CO X CD 3 x a> 01 c X r. X X H X < H * c c O CO d cD CL * d o CO CD a) #s rs r\ r\ cD 6 CO 0) 0) CO d d e > Ci d cD d

cD s T 1 CO CO 4-J

d *H 0) CD a) <u a)

d <U

4-J

d 1 1 00 a)d S)

xX e •H 4-J 4-J

X 4J o o •H *H •H CD O o CD cd Ci 4-J 4J 01 4-J o PH PC PC cj Q pc; CO X CJ w w S w

dzco co CO Csl t-H uO NO ON ON LO ON o 04 CO <r on LO CO CO t—

co

00 04 CN] Csl CM Csl t—

t-H Csl

O CN CM CM Csl (0 nO o o o CO o o ON t—

t—

o o o o o

0) CO uO uO ln in UO o CM t-H lo uO LO UO LO o i—

t—

«—

r—vO t-H t-H NO

X t-H rH t-H t—

t-H rH o<

CO jQ

CDO)c oo i—

oo oo

co CO CN t-H CO CO o UO cc i 1 i—

rH t-H t-H t-H i 1 co UO i 1 NO i o NO t-H CO co LO t-H co co sc CO

CO0

ft— 0=

CDO)c

co a• i 1 00 oo i 1 NO i 1 CM i Q. i 1 i 1 NO ON i 1 CN i E

co CO CM CO Nt

CD t—

t-H 00 t—

<1* CO NO

H 1—

i—

t—

NO co CO Csl co co Csl co CO

O)c

cd

cj cj <1 <3 c c < a CJ <3 pp CJ CJ <3 CJ cc

CN CN + i

t-H

X

X o o CM LO uO o CN c: Csl t-H t-H t-H CJ CJ

t-H i

r—

q sc

XX i 1 sc sc CC sc NT Nt uO d d

UO *vf UP sc oc CJ CJ CJ E CJ a cj CJ Nt SC 1 i i + +

CD 1 i i 1 CJ C“

d

dd c (C c c 1 CJ o o d + + + t—

! 1 + + + + + X X z z + z oo 00 co Nt CO NO X oo oo nC sc X X CJ CJ

sc SC sc sc CO sc CO CO CO i 1 CN CN CO CO CN CN CJ CJ CJ d d

cj

a CJ CJ sc CJ CM z z z + + r—i + + + + + + + + + X

NO SO uO NO NO 00

Nfr <r <r NT Nt Cs

XHCX

XX

sc cc sc sc sc o CM Csl 1 CM CN CO

cj cj CJ CJ CJ CJ CJ

C

n CJ CJ CJ

126
APPENDIX C

Data Source References

8000 Abdulaev, Ya. A. Phase relations in mixtures of carbon dioxide with

hydrogen, nitrogen and carbon monoxide, (in Russian) Zh. Fiz. Khim.,

13(7), 986-8 (1939).

8283 Abdulaev, Ya. A. Study of the solubility of ni trogen-hydrogen mixtures

in liquid carbon dioxide, (in Russian) Zh. Prikl. Khim. (Leningrad),

14(3), 302-4 (1941).

9518 Abdullaev, Ya. A. Study of equilibria of the liquid carbon dioxide

system in the presence of technical gases, (in Russian) Zh. Khim.

Promsti., 16(2), 37-40 (1939).

150170 Abou El-Nour, F. , Harting, P., Schuetze, H. Thermodynamic carbon isotope

effect for solubility of ethane in water. Isotopenoraxis , 13(8), 296-8

(1977).

103328 Abrosimov, V. K., Strakhov, A. N., Krestov, G. A. Solubility of He, Ne

and Ar in heavy water of various isotopic compositions at 283-318 degrees

K. (in Russian) Izv. Vyssh. Uchebn. Zaved., Khim. Khim. Tekhnol .

,

17(10), 1463-5 (1974).

150150 Adeney, W. E., Becker, H. G. The determination of the rate of solution

of atmospheric nitrogen and oxygen by water. Part II. Sci. Proc. R.

Dublin Soc., 15, 609-28 (1919).

150136 Ahland, E. The determination and computation of condensation points in

hydrocarbon gas mixtures with a high hydrogen content, (in German) GWF,

Gas-Wasserfach, 107(11), 273-9 (1966).

150048 Akerloef, G. The solubility of noble gases in aqueous salt solutions at

25 degrees. J. Am. Chem. Soc., 57, 1196-201 (1935).

150075 Akers, W. W., Attwell, L. L., Robinson, J. A. Volumetric and phase

behavior of nitrogen-hydrocarbon systems. Nitrogen-butane system. Ind.

Eng. Chem., 46(12), 2539-40 (1954).

3518 Akers, W. W. , Burns, J. F., Fairchild, W. R. Low-temperature phase

equilibria. Methane-propane system. Ind. Eng. Chem., 46(12), 2531-4

(1954).

8905 Akers, W. W. , Eubanks, L. S. Vapor-liquid equilibria in the system

hydrogen-nitrogen-carbon monoxide. Adv. Cryog. Eng., 3, 275-93 (1960).

3518 Akers, W. W., Kelley, R. E., Lipscomb, T. G. Low- temperature phase

equilibria. Carbon dioxide-propane system. Ind. Eng. Chem., 46(12),

2535-6 (1954).

150279 Altunin, V. V., Gvozdkov, A. V., Sosinovskii, V. K. Study of

liquid-vapor phase equilibrium in binary systems with carbon dioxide.

(in Russian) Tr. Mosk. Energ. Inst., 177, 28-32 (1974).

127
150081 Amick, E. H., Jr., Johnson, W. B., Dodge, B. F. P-V-T-X relationships

for the system: methane-isopentane. Chem. Eng. Prog., Symp. Ser.,

48(3), 65-72 (1952).

150246 Andrews, T. On the properties of matter in the gaseous and liquid states

under various conditions of temperature and pressure. Philos. Trans. R. Soc. London, Ser. A, 178, 45-56 (1887).

76499 Arai, Y., Kaminishi, G., Saito, S. The experimental determination of the

P-V-T-X relations for the carbon dioxide-nitrogen and the carbon

dioxide-methane systems. J. Chem. Eng. Jpn., 4(2), 113-22 (1971).

5100 Aroyan, H. J., Katz, D. L. Low temperature vapor-liquid equilibria in

hydrogen-n-butane system. Ind. Eng. Chem., 43(1), 185-9 (1951).

150107 Azarnoosh, A., McKetta, J. J. The solubility of propane in water. Pet.

Refiner, 37(11) , 275-8 (1958)

59300 Banks, R., Haselden, G. G. The measurement and prediction of enthalpies

and phase equilibria in natural gas mixtures. Pap. - Int. Conf.

Liquefied Nat. Gas, 1969, 117-37 (1969).

150190 Barsuk, S. D., Benyaminovich, 0. A. Investigation of liquid-vapor

equilibria in mixtures of ni trogen- isobutane and methane-n-butane at low

temperatures, (in Russian) Tr., Vses. Nauchno-Issled. Inst. Prir. Gazov,

100-5 (1975).

84578 Barsuk, S. D„, Skripka, V. G., Benyaminovich, 0. A. Investigation of the

liquid-vapor equilibrium in the methane- isobutane system at low

temperatures, (in Russian) Gazov. Promst., 15(9), 38-41 (1970).

150106 Bartholome, E., Friz, H. Solubility of carbon dioxide in water at high

pressures, (in German) Chem. -Ing. -Tech. , 28(11), 706-8 (1956).

5121 Bartlett, E. P. The concentration of water vapor in compressed hydrogen,

nitrogen and a mixture of these gases in the presence of condensed water.

J. Am. Chem. Soc., 49, 65-78 (1927).

150196 Barton, J. R., Hsu, C. C. Solubility of cyclopropane in alkyl carboxylic

acids. J. Chem. Eng. Data, 16(1), 93-5 (1971).

150092 Basset, J., Dode, M. Solubility of nitrogen in water at high pressures

to 4500 kg/cm(2). C. R. Hebd. Seances Acad. Sci., 203, 775-7 (1936).

150257 Behnke, A. R. , Yarbrough, 0. D. Physiologic studies of helium. U. S. Nav. Med. Bull., 36, 542-9 (1938).

6251 Benham, A. L., Katz, D. L. Vapor-liquid equilibria for hydrogen-1 ighthydrocarbon systems at low temperatures. AIChE J., 3(1), 33-6 (1957).

150035 Ben-Naim, A., Wilf, J., Yaacobi, M. Hydrophobic interaction in light and

heavy water. J. Phys. Chem., 77(1), 95-102 (1973).

128
150036 Ben-Naim, A., Yaacobi, M. Effects of solutes on the strength of

hydrophobic interaction and its temperature dependence. J. Phys. Chem.,

78(2), 170-8 (1974).

106980 Benson, B. B., Krause, D., Jr. Empirical laws for dilute aqueous

solutions of nonpolar gases. J. Chem. Phys., 64(2), 689-709 (1976).

150025 Benson, B. B., Parker, P. 0. M. Relations among the solubilities of

nitrogen, argon and oxygen in distilled water and sea water. J. Phys.

Chem., 5, 1489-96 (1961).

150507 Beranek, P., Wichterle, I. Vapour-liquid equilibria in the propane-nbutane system at high pressures. Fluid Phase Equilib., 6, 279-82

(1981).

'

76314 Besserer, G. J., Robinson, D. B. A high pressure autocol 1 imating

refractometer for determining coexisting liquid and vapor phase

densities. Can. J. Chem. Eng., 49(5), 651-6 (1971).

87419 Besserer, G. J., Robinson, D. B. Equilibrium-phase properties of

i-butane-carbon dioxide system. J. Chem. Eng. Data, 18(3), 298-301

(1973).

87420 Besserer, G. J., Robinson, D. B. Equilibrium-phase properties of

i-butane-ethane system. J. Chem. Eng. Data, 18(3), 301-4 (1973).

150197 Besserer, G. J., Robinson, D. B. Equilibrium-phase properties of

n-pentane-carbor. dioxide system. J. Chem. Eng. Data, 18(4), 416-9

(1973).

150373 Besserer, G. J., Robinson, D. B. Equilibrium-phase properties of

isopentane-carbon dioxide system. J. Chem. Eng. Data, 20(1), 93-6

(1975).

101683 Besserer, G. J., Robinson, D. B. Equilibrium-phase properties of

nitrogen- hydrogen sulfide system. J. Chem. Eng. Data, 20(2), 157-61

(1975).

150104 Besserer, G. J., Robinson, D. B. The equilibrium phase properties of the

i -butane-hydrogen sulfide system. J. Chem. Eng. Jpn., 8(1), 11-5

(1975).

150361 Beuschlein, W. L., Simenson, L. 0. Solubility of sulfur dioxide in

water. J. Am. Chem. Soc., 62, 610-2 (1940).

150171 Bierlein, J. A., Kay, W. B. Phase-equilibrium properties of system

carbon dioxide-hydrogen sulfide. Ind. Eng. Chem., 45(3), 618-24 (1953).

150233 Billman, G. W. , Sage, B. H., Lacey, W. N. Phase behavior in the

methane-ethane-n-pentane system. Trans. Am. Inst. Min., Metall . Pet.

Eng., 174, 13-24 (1948).

150027 Black, C., Joris, G. G., Taylor, H. S. The solubility of water in

hydrocarbons. J. Chem. Phys., 16(5), 537-43 (1948).

129
150018 Bloomer, 0. T., Garni, D. C., Parent, J. D. Physical-chemical properties

of methane-ethane mixtures. Inst. Gas Technol., Chicago, Res. Bull., 22,

44 pp (1953).

924 Bloomer, 0. T., Parent, J. D. Liquid-vapor phase behavior of the

methane-nitrogen system. Chem. Eng. Prog., Symp. Ser., 49(6), 11-24

(1953)

150537 Boexkes, W. , Emig, G. Determination of C0(2) solubility in water, (in

German) Chem. -Ing. -Tech. , 41(23), 1273-6 (1969).

150111 Bohr, C. Definition and method of determination of the invasion and

evasion coefficients of solution of gases in liquids. Values of the

named constants as well as of the absorption coefficients of carbon

dioxide with solution in water and in sodium chloride solutions, (in

German) Ann. Phys. (Leipzig), 68, 500-25 (1899).

150224 Boone, W. J., Jr., De Vaney, W. E., Miller, J. E. Low- temperature phase

equilibria of helium-bearing natural gases: Exell gas. Rep. Invest. - U.

S., Bur. Mines, 6008, 23 pp (1962).

17059 Boone, W. J., Jr., DeVaney, W. E., Stroud., L. Vapor-liquid equilibria

for a helium-nitrogen-methane system. Rep. Invest. - U. S., Bur. Mines,

6178, 35 pp (1963).

150511 Borgstedt, H. H., Gillies, A. J. Determination of the solubility of

nitrous oxide in water by gas chromatography . Anesthesiology, 26(5),

675-8 (1965).

150198 Brandt, L. W. , Stroud, L. Phase equilibria in natural gas systems.

Apparatus with windowed cell for 800 p.s.i.g. and temperatures to -320

degrees F. Ind. Eng. Chem., 50(5), 849-52 (1958).

11765 Brandt, L. W., Stroud, L., Miller, J. E. Phase equilibria in natural gas

systems. Data for two helium-bearing natural gases. J. Chem. Eng. Data,

6(1), 6-13 (1961).

150199 Brewer, J., Rodewald, N., Kurata, F. Phase equilibria of the propanehydrogen sulfide system from the cricondontherrn to the solid-liquid-vapor

region. AIChE J., 7(1), 13-6 (1961).

150108 Brooks, W. B., Gibbs, G. B., McKetta, J. J. Mutual solubilities of light

hydrocarbon-water systems. Pet. Refiner, 30(10), 118-20 (1951).

21435 Burch, R. J. Low temperature phase equilibria of the gas-liquid system

helium- neon- nitrogen. J. Chem. Eng. Data, 9(1), 19-24 (1964).

63709 Burfield, D. W., Richardson, H. P., Guereca, R. A. Vapor-liquid

equilibria and dielectric constants for the helium-carbon dioxide system.

AIChE J., 16(1) , 97-100 (1970).

150095 Burriss, W. L., Hsu, N. T., Reamer, H. H., Sage, B. H. Phase behavior of

the hydrogen-propane system. Ind. Eng. Chem., 45(1), 210-3 (1953).

130
18927 Buzyna, G., Macriss, R. A., Ellington, R. T. Vapor-liquid equilibrium in

the hel i urn- nitrogen system. Chem. Eng. Prog., Symp. Ser., 59(44), 101-11

(1963).

150089 Cady, H. P., Elsey, H. M., Berger, E. V. The solubility of helium in

water. J. Am. Chem. Soc., 44, 1456-61 (1922).

98955 Cal ado, J. C. G., Garcia, G. A., Staveley, L. A. K. Thermodynamics of

the liquid system methane + propane. J. Chem. Soc., Faraday Trans. 1,

70(8), 1445-51 (1974).

133074 Cal ado, J. C. G., Gomes de Azevedo, E. J. S., Soares, V. A. M. Thermodynamic properties of binary liquid mixtures of ethane and ethylene with

methane and the rare gases. Chem. Eng. Commun., 5, 149-63 (1980).

150362 Calingaert, G., Hitchcock, L. B. The application of the phase rule to

the calculation of liquid and vapor compositions in binary systems.

Deviations from Raoul t's law for hydrocarbon mixtures. J. Am. Chem.

Soc., 49, 750-65 (1927).

150363 Campbell, W. B., Maass, 0. Equilibria in sulphur dioxide solutions.

Can. J. Res., 2, 42-64 (1930).

54087 Cannon, W. A., Robson, J. H., English, W. D. Liquid propellant gas

absorption study. Douglas Missile Space Syst. Div., Astropower Lab.,

Newport Beach, Calif., Rep., DAC-60510-F2, 72 pp (1968).

150271 Carter, R. T., Sage, B. H., Lacey, W.N. Phase behavior in the

methane-propane-n-pentane system. Trans. Am. Inst. Min., Metal 1. Pet.

Eng., 142, 170-8 (1941).

150541 Caubet, F. The liquefaction of gas mixtures, (in German) Z. Phys.

Chem., Stoechiom. Verwandschaftsl . , 49, 101-16 (1904).

50610 Chang, S.-D., Lu , B. C.-Y. Vapor-liquid equilibria in the nitrogenmethane-ethane system. Chem. Eng. Prog., Symp. Ser., 63(81), 18-27

(1967).

39075 Chari esworth, P. L., Ruhemann, M. Low temperature hydrogen recovery from

industrial gases. Bull. Inst. Int. Froid, Annexe, 1965-4, 467-75

(1965).

90465 Chen, R. J. J., Chappelear, P. S., Kobayashi, R. Dew-point loci for

methane-n-butane binary system. J. Chem. Eng. Data, 19(1), 53-8 (1974).

90466 Chen, R. J. J., Chappelear, P. S., Kobayashi, R. Dew-point loci for

methane-n-pentane binary system. J. Chem. Eng. Data, 19(1), 58-61

(1974)

.

82412 Chen, R. J. J., Ruska, W. E. A., Chappelear, P. S. , Kobayashi, R. Development of a method for direct determination of dew point loci of

methane-heavier hydrocarbon mixtures at low temperatures and elevated

pressures. Adv. Cryog. Eng., 18, 202-7 (1973).

131
25304 Cheung, H., Wang, D. I.-J. Solubility of volatile gases in hydrocarbon

solvents at cryogenic temperatures. Ind. Eng. Chem. Fundam., 3(4),

355-61 (1964).

88751 Christiansen, L. J., Fredenslund, A., Gardner, N. Gas-liquid equilibria

of the CO ( 2

) -CO and C0(2)-CH(4)-C0 systems. Adv. Cryog. Eng., 19, 309-19

(1974)

88244 Christiansen, L. J., Fredenslund, A., Mollerup, J. Vapour-liquid

equilibrium of the CH(4)-Ar, CH(4)-C0, and Ar-CO systems at elevated

pressures. Cryogenics, 13(7), 405-13 (1973).

150133 Christoff, A. On the dependence of absorption on the surface tension.

(in German) Z. Phys. Chem., Stoechiom. Verwandschaf tsl . , 55, 622-34

(1906)

107051 Chu, T.-C., Chen, R. J. J., Chappelear, P. S., Kobayashi, R. Vaporliquid equilibrium of methane-n-pentane system at low temperatures and

high pressures. J. Chem. Eng. Data, 21(1), 41-4 (1976).

6350 Cines, M. R., Roach, J. T., Hogan, R. J., Roland, C. H. Nitrogen-methane

vapor-liquid equilibria. Chem. Eng. Prog., Symp. Ser. , 49(6), 1-10

(1953).

150002 Clarke, E. C. W. , Glew, D. N. Aqueous nonelectrolyte solutions. Part

VIII. Deuterium and hydrogen sulfides solubilities in deuterium oxide

and water. Can. J. Chem., 49(5), 691-8 (1971).

150055 Claussen, W. F., Polglase, M. F. Solubilities and structures in aqueous

aliphatic hydrocarbon solutions. J. Am. Chem. Soc., 74, 4817-9 (1952).

150118 Clever, H. L., Battino, R., Saylor, J. H., Gross, P. M. The solubility

of helium, neon, argon and krypton in some hydrocarbon solvents. J.

Phys. Chem., 61, 1078-82 (1957).

150542 Clifford, I. L., Hunter, E. The system ammonia-water at temperatures up

to 150 degrees C. and at pressures up to twenty atmospheres. J. Phys.

Chem., 37, 101-18 (1933).

150051 Coan, C. R., King, A. D., Jr. Solubility of water in compressed carbon

dioxide, nitrous oxide, and ethane. Evidence for hydration of carbon

dioxide and nitrous oxide in the gas phase. J. Am. Chem. Soc., 93(8),

1857-62 (1971).

50609 Cohen, A. E., Hipkin, H. G. , Koppany, C. R. Experimental vapor-liquid

equilibrium data for hydrogen-ethane and hydrogen-methane-ethane. Chem.

Eng. Prog., Symp. Ser., 63(81), 10-7 (1967).

150079 Connolly, J. F. Ideality of n-butane: isobutane solutions. J. Phys.

Chem., 66(6), 1082-6 (1962).

150200 Connolly, J. F. Solubility of hydrocarbons in water near the critical

solution temperatures. J. Chem. Eng. Data, 11(1), 13-6 (1966).

132
150364 Cook, D. The carbon-dioxide-nitrous-oxide system in the critical region.

Proc. R. Soc. London, Ser. A, 219, 245-56 (1953).

6572 Cosway, H. F. , Katz, D. L. Low- temperature vapor-liquid equilibria in

ternary and quaternary systems containing hydrogen, nitrogen, methane,

and ethane. AIChE J.,* 5(1), 46-50 (1959).

'

13680 Cota, H. M., Thodos, G. Critical temperatures and critical pressures of

hydrocarbon mixtures. Methane-ethane-n-butane system. J. Chern. Eng.

Data, 7(1), 62-5 (1962).

94543 Crozier, T. E. , Yamamoto, S. Solubility of hydrogen in water, seawater,

and NaCl solutions. J. Chem. Eng. Data, 19(3), 242-4 (1974).

150088 Culberson, 0. L., Horn, A. B., McKetta, J. J., Jr. Phase equilibria in

hydrocarbon-water systems. The solubility of ethane in water at

pressures to 1200 pounds per square inch. Trans. Am. Inst. Min., Metal!

.

Pet. Eng., 189, 1-6 (1950).

150087 Culberson, 0. L. , McKetta, J. J., Jr. Phase equilibria in hydrocarbonwater systems. II - The solubility of ethane in water at pressures to

10,000 psi. Trans. Am. Inst. Min., Metall. Pet. Eng., 189, 319-22

(1950)

.

150015 Culberson, 0. L., McKetta, J. J., Jr. Phase equilibria in hydrocarbonwater systems. Ill - The solubility of methane in water at pressures to

10,000 psia. Trans. Am. Inst. Min., Metall. Pet. Eng., 192, 223-6

(1951)

.

150014 Culberson, 0. L., McKetta, J. J., Jr. Phase equilibria in hydrocarbonwater systems. IV - vapor-liquid equilibrium constants in the

methane-water and ethane-water systems. Trans. Am. Inst. Min., Metall.

Pet. Eng., 192, 297-300 (1951).

*

28799 Cutler, A. J. B., Morrison, J. A. Excess thermodynamic functions for

liquid mixtures of methane+propane. Trans. Faraday Soc., 61(3), 429-42

(1965)

.

150084 Danneil, A., Toedheide, K., Franck, E. U. Vaporization equilibria and

critical curves in the systems ethane/water and n-butane/water at high

pressures, (in German) Chem. -Ing. -Tech., 39(13), 816-22 (1967).

107053 Davalos, J., Anderson, W. R., Phelps, R. E., Kidnay, A. J. Liquid-vapor

equilibria at 250. 00K for systems containing methane, ethane, and carbon

dioxide. J. Chem. Eng. Data, 21(1), 81-4 (1976).

150377 Davis, J. A., Rodewald, N. , Kurata, F. Sol id-1 iqui d-vapor phase behavior

of the methane-carbon dioxide system. AIChE J., 8(4), 537-9 (1962).

21414 Davis, J. A., Rodewald, N., Kurata, F. An apparatus for phase studies

between 20 degrees K. and 300 degrees K. Ind. Eng. Chem., 55(11), 36-42

(1963)

.

133
150201 Davis, J. E., McKetta, J. J. Solubility of methane in water. Pet.

Refiner, 39(3) , 205-6 (1960).

86467 Davydov, I. A., Budnevich, S. S. Study of equilibrium composition of a nitrogen-hel ium mixture, (in Russian) Inzh.-Fiz. Zh., 20(6), 1082-6

(1971).

150060 Dean, M. R., Tooke, J. W. Vapor-liquid equilibria in three hydrogenparaffin systems. Ind. Eng. Chem., 38(4), 389-93 (1946).

150546 Dean, M. R., Walls, W. S. Solubility of nitrogen and methane in sulfur

dioxide. Ind. Eng. Chem., 39(8), 1049-51 (1947).

131999 de Loos, T. W., Wijen, A. J. M, Diepen, G. A. M. Phase equilibria and

critical phenomena in fluid (propane + water) at high pressures and

temperatures. J. Chem. Thermodyn., 12(2), 193-204 (1980).

150248 DePriester, C. L. Light-hydrocarbon vapor-liquid distribution

coefficients. Pressure-temperature-composi tion charts and pressuretemperature nomographs. Chem. Eng. Prog., Symp. Ser. , 49(7), 1-43

(1953)

20429 DeVaney, W. E., Dalton, B. J., Meeks, J. C., Jr. Vapor-liquid equilibria

of the hel ium- nitrogen system. J. Chem. Eng. Data, 8(4), 473-8 (1963).

70826 DeVaney, W. E., Rhodes, H. L., Tully, P. C. Phase equilibria data for

helium-methane system. J. Chem. Eng. Data, 16(2), 158-61 (1971).

150225 De Vaney, W. E., Stroud., L., Boone, W. J., Jr. Low- temperature phase

equilibria of a natural gas of low helium content. Rep. Invest. - U. S.,

Bur. Mines, 6499, 20 pp ( 1964).

150172 de Wet, W. J. Determination of gas solubilities in water and some organic liquids. J. S. Afr. Chem. Inst., 17, 9-13 (1964).

125467 Dingrani, J. G., Thodos, G. Vapor-liquid equilibrium behavior of the

ethane-n-butane-n-hexane system. Can. J. Chem. Eng., 56(5), 616-23

(1978).

64372 Djordjevich, L., Budenholzer, R. A. Vapor-liquid equilibrium data for

ethane-propane system at low temperatures. J. Chem. Eng. Data, 15(1),

10-2 (1970).

5651 Dokoupil, Z., Van Soest, G., Swenker, M. D. P. On the equilibrium

between the solid phase and the gas phase of the systems hydrogennitrogen, hydrogen-carbon monoxide and hydrogen-nitrogen-carbon monoxide.

Commun. Kamerlingh Onnes Lab. Univ. Leiden, 297, 59 pp (1955); reprinted

from Appl . Sci . Res., Sect. A, 5, 182-240 (1955).

47558 Donnelly, H. G., Katz, D. L. Phase equilibria in the carbon dioxidemethane system. Ind. Eng. Chem., 46(3), 511-7 (1954).

150547 Dornte, R. W., Ferguson, C. V. Solubility of nitrogen and oxygen in

liquid sulfur dioxide. Ind. Eng. Chem., 31, 112-3 (1939).

134
150232 Douabul , A. A., Riley, J. P. The solubility of gases in distilled water

and seawater - V. Hydrogen sulphide. Deep-Sea Res. Oceanogr. Abstr.,

26 A( 3 ) , 259-68 (1979).

21436 Douglas, E. Solubilities of oxygen, argon, and nitrogen in distilled

water. J. Phys. Chem., 68(1), 169-74 (1964).

150244 Dourson, R. H. , Sage, B. H. , Lacey, W. N. Phase behavior in the

methane-propane-n-pentane system. Trans. Am. Inst. Min., Metall. Pet.

Eng., 151, 206-15 (1943).

150143 Duffy, J. R., Smith, N. 0., Nagy, B. Solubility of natural gases in

aqueous salt solutions - I. Liquidus surfaces in the system

CH(4)-H(2)0-NaCl-CaCl (2) at room temperatures and at pressures below 1000

psia. Geochim. Cosmochim. Acta, 24, 23-31 (1961).

37444 Duncan, A. G., Staveley, L. A. K. Thermodynamic functions for the liquid

systems argon + carbon monoxide, oxygen + nitrogen, and carbon monoxide + nitrogen. Trans. Faraday Soc., 62(3), 548-52 (1966).

150528 Dvorak, K., Boublik, T. Liquid-vapour equilibria. XXIX. Measurement of

equilibrium data in systems with high equilibrium ratio of the

components. Collect. Czech. Chem. Commun., 28, 1249-55 (1963).

150369 Ekiner, 0., Thodos, G. Critical temperatures and critical pressures of

the ethane-n-pentane system. J. Chem. Eng. Data, 11(2), 154-5 (1966).

12784 Ellington, R. T., Eakin, B. E., Parent, J. D., Garni, D. C., Bloomer,

0. T. Vapor-liquid phase equilibria in the binary systems of methane,

ethane and nitrogen. Thermodyn. Transp. Prop. Gases, Liqu., Solids, Pap.

Symp. Therm. Prop., 1959, 180-94 (1959).

90468 Elliot, D. G., Chen, R. J. J., Chappelear, P. S., Kobayashi, R. Vaporliquid equilibrium of methane-n-butane system at low temperatures and

high pressures. J. Chem. Eng. Data, 19(1), 71-7 (1974).

150156 Ellis, A. J. The solubility of carbon dioxide in water at high

temperatures. Am. J. Sci., 257, 217-34 (1959).

150155 Ellis, A. J., Golding, R. M. The solubility of carbon dioxide above 100

degrees C in water and in sodium chloride solutions. Am. J. Sci., 261,

47-60 (1963).

150022 Enns, T., Scholander, P. F. , Bradstreet, E. D. Effect of hydrostatic

pressure on gases dissolved in water. J. Phys. Chem., 69(2), 389-91

(1965)

.

150192 Ermolaev, M. I., Kapitanov, V. F. , Nesterova, A. K., Batishchev, V. V. The carbon dioxide-water binary system. Russ. J. Phys. Chem. (Engl.

Transl . ) , 45(1), 167 (1971).

150134 Estreicher, T. The solubility ratio of argon and helium in water, (in

German) Z. Phys. Chem., Stoechiom. Verwandschaftsl . , 31, 176-87 (1899).

135
150239 Etter, D. 0., Kay, W. B. Critical properties of mixtures of normal

paraffin hydrocarbons. J. Chem. Eng. Data, 6(3), 409-14 (1961).

150017 Eucken, A., Hertzberg, G. Salting out effects and ion hydration, (in

German) Z. Phys. Chem. (Leipzig), 195(1), 1-23 (1950).

150129 Farhi, L. E., Edwards, A. W. T.-, Homma, T. Determination of dissolved

M ( 2 ) in blood by gas chromatography and (a-A)N(2) difference. J. Appl

Physiol., 18, 97-106 (1963).

5617 Fastovskii, V. G., Gonikberg, M. G. Solubility of gases in liquids at

low temperatures and high pressures. III. Solubility of hydrogen in

liquid methane, (in Russian) Zh. Fiz. Khim., 14(3), 427-8 (1940).

29966 Fastovskii, V. G., Petrovskii, Yu. V. An investigation of the

liquid/vapour equilibrium in the nitrogen-methane system, (in Russian)

Zh. Fiz. Khim. , 31(10), 2317-21 (1957).

150151 Fedoritenko, A., Ruhemann, M. Equilibrium diagrams of helium-nitrogen

mixtures. Tech. Phys. USSR, 4, 36-43 (1937).

150037 Feillolay, A., Lucas, M. The solubility of helium and methane in aqueous

tetrabutyl ammonium bromide solutions at 25 and 35 degrees. J. Phys.

Chem., 76(21), 3068-72 (1972).

150173 Fischer, F., Zerbe, C. On the solubility of methane in water and organic

solvents under pressure, (in German) Brennst. -Chem. , 4(2), 17-9 (1923).

70550 Foerg, W., Wirtz, P. Helium and nitrogen removal from natural gas.

Linde Rep. Sci . Techno!., 15, 46-53 (1970); transl. of Linde Ber. Tech.

Wiss., 28, 44-50 (1970).

150223 Forman, J. C., Thodos, G. Experimental determination of critical

temperatures and pressures of mixtures: the methane-ethane-n-butane

system. AIChE J., 8(2), 209-13 (1962).

150174 Fox, C. J. J. On the coefficients of absorption of nitrogen and oxygen

in distilled water and sea-water, and of atmospheric carbonic acid in

sea-water. Trans. Faraday Soc., 5, 68-87 (1909).

150124 Franck, E. U., Toedheide, K. Thermal properties of supercritical

mixtures of carbon dioxide and water to 750 degrees C and 2000 atm. (in

German) Z. Phys. Chem. (Frankfurt am Main), 22, 232-45 (1959).

98958 Fredenslund, A., Mollerup, J. Measurement and prediction of equilibrium

ratios for the C(2)H(6)+C0(2) system. J. Chem. Soc., Faraday Trans. 1,

70(9), 1653-60 (1974).

102912 Fredenslund, A., Mollerup, J. Gas-liquid equilibrium of hydrogen

sulphide + carbon monoxide. J. Chem. Thermodyn., 7(7), 677-82 (1975).

5679 Freeth, F. A., Verschoyle, T. T. H. Physical constants of the system

methane-hydrogen. Proc. R. Soc. London, Ser. A, 130, 453-63 (1931).

136
150049 Friedman, H. L. The solubilities of sulfur hexafluoride in water and of

the rare gases, sulfur hexafluoride and oxmium tetroxide in nitromethane.

J. Am. Chem. Soc., 76, 3294-7 (1954).

150067 Frolich, P. K., Tauch, E. J., Hogan, J. J., Peer, A. A. Solubilities of

gases in liquids at high pressure. Ind. Eng. Chem., 23(5), 548-50

(1931)

.

150122 Fuehner, H. Water solubility in homologous series, (in German) Ber.

Dtsch. Chem. Ges., 5713, 510-5 (1924).

45392 Fuks, S., Bellemans, A. Excess free energies and volumes of two simple

binary liquid mixtures: methane-krypton and nitrogen-methane. Bull. Soc.

Chim. Bel g. , 76(5-6), 290-9 (1967).

150038 Gardiner, G. E., Smith, N. 0. Solubility and partial molar properties of

helium in water and aqueous sodium chloride from 25 to 100 degrees and

100 to 600 atmospheres. J. Phys. Chem., 76(8), 1195-202 (1972).

150105 Gilliland, E. R. , Scheeline, H. W. Hi gh-pressure vapor-liquid

equilibrium for the systems propyl ene- i sobutane and propane-hydrogen

sulfide. Ind. Eng. Chem., 32(1), 48-54 (1940).

150518 Ginzburg, D. M., Pikulina, N. S., Litvin, V. P. System NH(3)-H(2)S-H(2)0

at 600 mm Hg. (in Russian) Zh. Prikl. Khim. (Leningrad), 39(10), 2371-3

(1966)

.

150131 Gjaldbaek, J. C., Niemann, H. The solubility of nitrogen, argon and

ethane in alcohols and water. Acta Chem. Scand. , 12(5), 1015-23 (1958).

150524 Glowka, S. Liquid-vapour equilibria and thermodynamic functions of

propane- sul phur dioxide and propane- dimethyl ether systems up to 300

degrees C. Bull. Acad. Pol. Sci., Ser. Sci . Chim., 20(2), 163-7 (1972).

150175 Gonikberg, M. G., Fastowsky, W. G. The solubility of gases in liquids at

low temperatures and high pressures. 2. The solubility of helium in

liquid nitrogen at temperatures from 78.0 to 109.0 degrees K and

pressures up to 295 atm. (in German) Acta Physicochim. URSS, 12(1),

67-72 (1940).

6364 Gonikberg, M. , Fastowsky, W. The solubility of gases in liquids at low

temperatures and high pressures. IV. The solubility of helium in liquid

methane at temperatures of 90.3 degrees K and 106.0 degrees K and

pressures up to 160 atm. (in German) Acta Physicochim. URSS, 13(3),

399-404 (1940).

5657 Gonikberg, M. G., Fastowsky, W. G., Gurwitsch, J. G. The solubility of

gases in liquids at low temperatures and high pressures. I. The

solubility of hydrogen in liquid nitrogen at temperatures of 79.0-109.0

degrees K and pressures up to 190 atm. (in German) Acta Physicochim.

URSS, 11(6), 865-82 (1939).

50700 Gonzalez, M. H., Lee, A. L. Dew and bubble points of simulated natural

gases. J. Chem. Eng. Data, 13(2), 172-6 (1968).

137
150074 Goodman, J. B., Krase, N. W. Solubility of nitrogen in water at high

pressures and temperatures. Ind. Eng. Chem. , 23(4), 401-4 (1931).

150280 Granzhan, V. A. Solubility of carbon monoxide in methanol, water, acetic

acid, methyl acetate and in binary mixtures of solvents at a pressure of

50 at. (in Russian) Tr. Gos. Nauchno-Issled. Proektn. Inst. Azotn.

Promsti. Prod. Org. Sint., 37, 5-9 (1974).

118306 Grauso, L., Fredenslund, A., Mollerup, J. Vapour-liquid equilibrium data

&/2 4(e systems C(2)H(6) + N(2), C(2)H(4) + N(2), C(3)H(8) + N(2), and

(3) (6) + N ( 2 ) . Fluid Phase Equilib., 1(1), 13-26 (1977).

46018 Greene, N. E., Sonntag, R. E. Solid-liquid-vapor equilibrium in the

system hydrogen-helium. Adv. Cryog. Eng., 13, 357-62 (1968).

150234 Gregory, D. P., Djordjevich, L., Kao, R., Anderson, G. L., Eakin, B. E.,

Bodle, W. W. Thermodynamic properties of a lean natural gas at cryogenic

conditions. Tech. Rep. - Inst. Gas Technol . (Chicago), 11, 91 pp

(1973).

150056 Grieves, R. B., Thodos, G. Critical temperatures and pressures of

ternary hydrocarbon mixtures: the ethane-propane-n-butane system. J.

Appl . Chem., 13, 466-70 (1963).

88424 Gugnoni, R. J., Eldridge, J. W. , Okay, V. C., Lee, T. J. C0(2)-ethane

system predictions. Hydrocarbon Process., 52(9), 197-8 (1973).

99626 Gugnoni, R. J., Eldridge, J. W. , Okay, V. C., Lee, T. J. Carbon

dioxide-ethane phase equilibrium and densities from experimental

measurements and the B-W-R equation. AIChE J., 20(2), 357-62 (1974).

150080 Guter, M., Newitt, D. M., Ruhemann, M. Two-phase equilibrium in binary

and ternary systems. II. The system methane- ethyl ene. III. The system

methane-ethane-ethylene. Proc. R. Soc. London, Ser. A, 176, 140-52

(1940)

150195 Hachrnuth, K. H. Dehydrating commercial propane. West. Gas, 8(1),

55-6+62-4 (1932).

150193 Haehnel , 0. On the strength of aqueous carbonic acid manufactured at

higher pressures, (in German) Zentralbl. Mineral., Geol . Palaeontol.,

25-32 (1920).

66179 Hakuta, T., Nagahama, K., Suda, S. Binary vapor-liquid equilibria of

CO ( 2

) -C ( 2 ) hydrocarbons. Kagaku Kogaku, 33(9), 904-7 (1969).

138
105715 Hall, K. R., Eubank, P. T. , Myerson, A. S. , Nixon, W. E. A new technique

for collecting binary vapor-liquid equilibrium data without measuring

composition: the method of intersecting isochores. AIChE J., 21(6),

1111-4 (1975).

98719 Hamam, S. E. M. , Lu, B. C.-Y. Vapor-liquid equilibrium in the ethanecarbon dioxide system. Can. J. Chem. Eng., 52(2), 283-6 (1974).

110896 Hamam, S. E. M. , Lu, B. C.-Y. Isothermal vapor-liquid equilibria in

binary system propane-carbon dioxide. J. Chem. Eng. Data, 21(2), 200-4

(1976).

111245 Hamam, S. E. M. , Lu, B. C.-Y. Phase equilibria for the system propaneethane-carbon dioxide. Can. J. Chem. Eng., 54(4), 333-6 (1976).

150251 Hanson, G. H. , Brown, G. G. Vapor-liquid equilibria in mixtures of

volatile paraffins. Ind. Eng. Chem., 37(9), 821-5 (1945).

150132 Haufe, S. Contribution ot the investigation of evaporation equilibria at

high pressures, (in German) Z. Phys. Chem. (Leipzig), 233(5/6), 353-64

(1966)

.

150202 Hayduk, W., Malik, V. K. Density, viscosity, and carbon dioxide

solubility and diffusivity in aqueous ethylene glycol solutions. J.

Chem. Eng. Data, 16(2), 143-6 (1971).

61654 Heck, C. K., Jr. Experimental and theoretical liquid-vapor equilibria in some binary systems. Univ. Colo., Boulder, Ph.D. Thesis, 265 pp (1968).

44762 Heck, C. K., Hiza, M. J. Liquid-vapor equilibrium in the system

helium-methane. AIChE J., 13(3), 593-9 (1967).

26297 Hensel, W. E., Jr., Massoth, F. E. Phase equilibria for the ternary

system: CH(4)-C0(2)-H(2)S at low temperatures. J. Chem. Eng. Data, 9(3),

352-6 (1964).

150370 Herlihy, J. C., Thodos, G. Vapor-liquid equilibrium constants:

ethane-n-butane-n-pentane system at 150 degrees F. J. Chem. Eng. Data,

7(3), 348-51 (1962).

5964 Hill, E. S., Lacey, W. N. Rate of solution of methane in quiescent

liquid hydrocarbons. II. Ind. Eng. Chem., 26(12), 1324-7 (1934).

39202 Hipkin, H. Experimental vapor-liquid equilibrium data for

propane- isobutane. AIChE J., 12(3), 484-7 (1966).

150142 Hi rata, M., Suda, S. Equilibrium measurements by the vapor-liquid flow

method. Vapor-liquid equilibrium measurements for three binary mixtures

of n-butane at 0 degrees C. Bull. Jpn. Pet. Inst., 10, 20-7 (1968).

150141 Hirata, M., Suda, S., Hakuta, T., Nagahama, K. High pressure vaporliquid equilibria for binary system containing C(4)-hydrocarbons. (in

Japanese) Sekiyu Gakkai Shi, 12(10), 773-7 (1969).

139
150102 Hirata, M. , Suda, S., Hakuta, T. , Nagahama, K. Light hydrocarbon

vapor-liquid equilibria. Mem. Fac. Technol., Tokyo Metrop. Univ., 19,

103-22 (1969).

150103 Hirata, M. , Suda, S. , Miyashita, R. , Hoshino, T. High pressure vaporliquid equilibria. Experimental data on the system propane- i sobutane at

66.60 degrees C. Mem. Fac. Technol., Tokyo Metrop. Univ., 20, 1811-7

(1970).

150220 Hiza, M. J. Liquid-vapor equilibria in binary systems containing (4)He

or (3)He with nH ( 2 ) or nD ( 2) . Fluid Phase Equi lib., 6(3-4), 203-27

(1981)

51011 Hiza, M. J., Duncan, A. G. Equilibrium gas-phase compositions of ethane

and ethylene in binary mixtures with helium and neon below 150 degrees K and a correlation for deviations from the geometric mean combining rule.

Adv. Cryog. Eng., 14, 30-40 (1969).

117815 Hiza, M. J., Haynes, W. M. Liquid mixture excess volumes and total vapor

pressures using a magnetic suspension densimeter with compositions

determined by chromatographic analysis: methane plus ethane. Adv. Cryog.

Eng., 23, 594-601 (1978).

45223 Hiza, M. J., Heck, C. K., Kidnay, A. J. Liquid-vapor and solid-vapor

equilibrium in the system hydrogen-ethane. Adv. Cryog. Eng., 13, 343-56

(1968)

29397 Hiza, M. J., Kidnay, A. J. Solid-vapor equilibrium in the system

helium-methane. Adv. Cryog. Eng., 11, 338-48 (1966).

73945 Hsi, C., Lu, B. C.-V. Vapor-liquid equilibria in the methane-ethyleneethane system. Can. J . Chem. Eng., 49(1), 140-3 (1971).

150535 Hudson, J. C. The solubility of sulphur dioxide in water and in aqueous

solutions of potassium chloride and sodium sulphate. J. Chem. Soc., 127,

' 1332-47 (1926).

16075 Hunter, M. A. The molecular aggregation of liquefied gases. J. Phys.

Chem. , 10, 330-60 (1906)

111705 Hwang, S.-C., Lin, H.-M., Chappelear, P. S., Kobayashi, R. Dew point

study in the vapor- liquid region of the methane-carbon dioxide system.

J. Chem. Eng. Data, 21(4), 493-7 (1976).

150148 Ipatev, V., Teodorovich, V. P. Solubility of hydrogen in water under

pressure at high temperatures, (in Russian) Zh. Obshch. Khim. , 4(3),

395-9 (1934).

150135 Ipatiew, W. W. , Drushina-Artemowitsch, S. I., Tichomirow, W. I. Solubility of hydrogen in water under pressure, (in German) Ber.

Dtsch. Chem. Ges. B, 65, 568-71 (1932).

140
150387 Johnstone, H. F. , Leppla, P. W. The solubility of sulfur dioxide at low

partial pressures. The ionization constant and heat of ionization of

sulfurous acid. J. Am. Chem. Soc., 56, 2233-8 (1934).

45496 Jones, A. E., Kay, W. B. The phase and volumetric relations in the

hel ium-n-butane system: part I. Phase and volumetric behavior of mixtures

of low helium concentration. AIChE J., 13(4), 717-20 (1967).

19414 Jones, I. W. , Rowlinson, J. S. Gas-liquid critical temperatures of

binary mixtures. Part 2. Trans. Faraday Soc., 59, 1702-8 (1963).

150386 Jones, M. E. Ammonia equilibrium between vapor and liquid aqueous phases

at elevated temperatures. J. Phys. Chem., 67, 1113-5 (1963).

150058 Jung, J., Knacke, 0., Neuschuetz, D. Solubility of carbon monoxide and

hydrogen in water up to 300 degrees C. (in German) Chem. -I ng. -Tech.,

43(3), 112-6 (1971).

90467 Kahre, L. C. Low- temperature K data for methane-n-butane. J. Chem. Eng.

Data, 19(1), 67-71 (1974).

150275 Kalaida, Yu. A., Katkov, Yu. D., Kuznetsov, V. A., Lostovtsev, A. Yu.,

Lastochkin, A. P., Sysoev, V. S. Solubility of nitrogen in water. Sov.

At. Energy (Engl. Transl.), 48(2), 102-6 (1980); transl . of At. Energ.,

48(2), 91-4 (1980).

110898 Kalra, H., Krishnan, T. R., Robinson, D. B. Equilibrium-phase properties

of carbon dioxide-n-butane and nitrogen-hydrogen sulfide systems at

subambient temperatures. J. Chem. Eng. Data, 21(2), 222-5 (1976).

123897 Kalra, H., Ng, H.-J., Miranda, R. D., Robinson, D. B. Equilibrium phase

properties of the nitrogen- isobutane system. J. Chem. Eng. Data, 23(4),

321-4 (1978).

102931 Kalra, H., Robinson, D. B. An apparatus for the simultaneous measurememt

of equilibrium phase composition and refractive index data at low

temperatures and high pressures. Cryogenics, 15(7), 409-12 (1975).

115116 Kalra, H., Robinson, D. B., Besserer, G. J. The equilibrium phase

properties of the nitrogen-n-pentane system. J. Chem. Eng. Data, 22(2),

215-8 (1977).

62196 Kaminishi, G., Arai , Y. , Saito, S., Maeda, S. Vapor-liquid equilibria

for binary and ternary systems containing carbon dioxide. J. Chem. Eng.

Jpn. , 1(2), 109-16 (1968).

39337 Kaminishi, G., Toriumi, T. Vapor-liquid phase equilibrium in the

CO ( 2

) -H ( 2 ) , CO ( 2

) -N ( 2 ) and C0(2)-0(2) systems, (in Japanese) Kogyo

Kagaku Zasshi, 69(2), 175-8 (1966).

62447 Kaminishi, G., Toriumi, T. Vapor-liquid equilibria in the systems:

CO ( 2

) - CO , CO ( 2

) -C0-H ( 2 ) and C0(2)-CH(4) . Rev. Phys. Chem. Jpn., 38(1),

79-84 (1968).

141
150062 Kay, W. B. Li quid- vapor equilibrium relations in binary systems. The

ethane-n-butane system. Ind. Eng. Chem. , 32(3), 353-7 (1940).

150203 Kay, W. B. Vapor-liquid equilibrium relations of binary systems. The

propane-n-al kane systems, n-butane and n-pentane. J. Chem. Eng. Data,

15(1) , 46-52 (1970).

150096 Kay, W. B., Brice, D. B. Liquid-vapor equilibrium relations in

ethane-hydrogen sulfide system. Ind. Eng. Chem., 45(3), 615-8 (1953).

150378 Kay, W. B., Fisch, H. A. Phase relations of binary systems that form

azeotropes: I. The arnnoni a- n-butane system. AIChE J., 4(3), 293-6

(1958)

103629 Kay, W. B., Hoffman, R. L., Davies, 0. Vapor-liquid equilibrium

relationships of binary systems n-butane-n-pentane and n-butane-n-hexane.

J. Chem. Eng. Data, 20(3), 333-8 (1975).

150260 Kay, W. B., Rambosek, G. M. Liquid-vapor equilibrium relations in binary

systems. Propane-hydrogen sulfide system. Ind. Eng. Chem., 45(1), 221-6

(1953).

150169 Kazaryan, T. S., Ryabtsev, N. I. Solubility of saturated propylene,

i-butylene, i-butane and n-butane in water and in aqueous solutions, (in

Russian) Neft. Khoz., 47(10), 54-6 (1969).

6361 Kharakhorin, F. F. The phase relations in systems of liquefied gases.

The binary mixture nitrogen - helium. Foreign Pet. Techno!., 9(11/12),

397-410 (1941); transl . of Zh. Tekh. Fiz., 10(18), 1533-40 (1940).

9643 Kharakhorin, F. F. The liquid-vapor equilibrium in the system heliummethane. (in Russian) Inzh.-Fiz. Zh., 2(5), 55-9 (1959).

51325 Khazanova, N . E., Lesnevskaya, L. S. Phase and volume relations in the

system ethane-carbon dioxide, (in Russian) Zh. Fiz. Khim., 41(9),

2373-6 (1967).

42929 Khazanova, N. E., Lesnevskaya, L. S., Zakharova, A. V. Equilibrium of

liquid-vapor in the system ethane-carbon dioxide, (in Russian) Khim.

Promst. (Moscow), 42(5), 364-5 (1966).

122297 Khazanova, N. E., Sominskaya, E. E., Rozovskii, M. B. Systems with

azeotropism at high pressures. IX. Volumetric and thermodynamic

behavior of the ethane-carbon dioxide system near specific points on the

critical curve, (in Russian) Zh. Fiz. Khim., 52(4), 915-7 (1978).

112414 Khazanova, N. E., Sominskaya, E. E., Zakharova, A. V., Rozovskii, M. B.

Thermodynamic properties of the ethane-carbon dioxide system. p,V,T,N

data, (in Russian) Teplofiz. Svoistva Veshchestv Mater., 10, 213-9

(1976)

150187 Khitarov, N. I., Malinin, S. D. Experimental characteri sties of a part

of the system H ( 2 ) 0-C0 ( 2 ) . Geochemistry (USSR), 3, 246-56 (1956);

transl. of Geokhimiia, 3, 18-27 (1956).

142
150168 Khitarov, N. I., Malinin, S. D. On the equilibrium phase relations in

the system H ( 2 ) 0-C0 ( 2) . (in Russian) Geokhimiya, 7, 678-9 (1958).

150191 Khodeeva, S. M. Visual observation of gas-gas equilibrium. Russ. J.

Phys. Chem. (Engl. Transl.), 40(8), 1061-3 (1966).

104961 Kidnay, A. J . , Miller, R. C., Parrish, W. R., Hiza, M. J. Liquid-vapour

phase equilibria in the N ( 2

) -CH ( 4 ) system from 130 to 180 K. Cryogenics,

15(9), 531-40 (1975).

24862 Kirk, B. S. , Ziegler, W. T. A phase-equilibrium apparatus for gas-liquid

systems and the gas phase of gas-solid systems: application to methanehydrogen from 66.88 degrees to 116.53 degrees K and up to 125

atmospheres. Adv. Cryog. Eng., 10(Sect. M-U), 160-70 (1965).

150159 Klausutis, N. Phase equilibrium in the propane-propyl ene-water system in

the three-phase region. Univ. Tex., Austin, Ph.D. Thesis, 127 pp

(1968).

105717 Klink, A. E., Cheh, H. Y., Amick, E. H., Jr. The vapor-liquid equilibrium of the hydrogen-n-butane system at elevated pressures. AIChE J.,

21(6), 1142-8 (1975).

20499 Klots, C. E., Benson, B. B. Solubilities of nitrogen, oxygen, and argon

in distilled water. J. Mar. Res., 21(1), 48-57 (1963).

108433 Knapp, H., Schmoelling, K., Neumann, A. Measurement of the molal heat

capacity of H(2)-N(2) mixtures. Cryogenics, 16(4), 231-7 (1976).

150530 Kobayashi , R., Katz, D. L. Vapor-liquid equilibria for binary

hydrocarbon-water systems. Ind. Eng. Chem., 45(2), 440-51 (1953).

47671 Kohn, J. P., Kurata, F. Heterogeneous phase equilibria of the methanehydrogen sulfide system. AIChE J., 4(2), 211-7 (1958).

150086 Kohn, J. P., Kurata, F. Volumetric behavior of the methane-hydrogen

sulfide system at low temperatures and high pressures. J. Chem. Eng.

Data, 4(1), 33-52 (1959).

150237 Kosyakov, N. E., Ryabinkin, V. V., Chobotko, L. L. Phase equilibria in

the hydrogen-carbon monoxide-methane system. Russ. J. Phys. Chem. (Engl.

Transl.), 52(8), 1235 (1978); transl. of Zh. Fiz. Khim., 52(8), 2132

(1978).

150276 Kozintseva, T. N. Solubility of hydrogen sulfide in water and salt

solutions at high temperatures, (in Russian) Geokhim. Issled. Obi.

Povysh. Davlenii Temp., 121-34 (1965).

150517 Krasheninnikov, S. A., Golubev, S. S., Sabaev, I. Ya. Method and

apparatus for the analysis of water-ammonia solutions, (in Russian)

Khim. Prornst. (Moscow), 6, 76-7 (1960).

143
150023 Kresheck, G. C., Schneider, H., Scheraga, H. A. The effect of D( 2 ) 0 on the thermal stability of proteins. Thermodynamic parameters for the

transfer of model compounds from H(2)0 to D ( 2 ) 0 - J. Phys. Chem. , 69(9),

3132-44 (1965).

150514 Krichevskii, I. R., Khazanova, N. E. Content of ammonia in compressed

hydrogen and nitrogen in equilibrium with liquid ammonia, (in Russian)

Zh. Fiz. Khim., 13(11), 1690-3 (1939).

150270 Krichevskii, I. R., Khazanova, N. E., Lesnevskaya, L. S., Sandalova,

L. Yu. Equilibrium of liquid- gas at high pressures in the system

nitrogen-carbon dioxide, (in Russian) Khim. Promst. (Moscow), 38(3),

169-71 (1962).

150520 Krichevsky, I., Ziclis, D. Gas-gas equilibrium and phase equilibria in

binary systems. Acta Physicochim. URSS, 18(4), 264-74 (1943).

116899 Krishnan, T. R., Kalra, H., Robinson, 0. B. The equilibrium phase

properties of the nitrogen-i sopentane system. J. Chem. Eng. Data, 22(3),

282-5 (1977).

150521 Kritschewsky , I., Bolshakov, P. The heterogeneous equilibria in the

amnoni a- nitrogen system at high pressures, (in German) Acta Physicochim.

URSS, 14(3), 353-64 (1941).

150123 Kritschewsky, I. R. , Shaworonkoff , N. M. , Aepelbaum, V. A. Mutual

solubility of gases in liquids under pressure. I. Solubility of carbon

dioxide in water from its mixtures with hydrogen at 20 and 30 degrees C

and total pressure to 30 kg/cm(2). (in German) Z. Phys. Chem., Abt. A,

175, 232-8 (1936).

150526 Kueffer, A. New data on the solubility of SO ( 2 ) in water, (in Czech)

Pap. Cel ul . , 17(6), 125-6 (1962).

150115 Kuenen, J. P. Experiments on the condensation and critical phenomena of some substances and mixtures. Philos. Mag., 44(267), 174-99 (1897).

150512 Kuenen, J. P. On ethane prepared from ethyl iodide, and on the

properties of some mixtures of ethane and butane. Proc. R. Soc.

Edinburgh, 21, 433-42 (1897).

150540 Kuenen, J. P. Experiments on the condensation and the critical phenomena

of mixtures of two materials, (in German) Z. Phys. Chem., Stoechiom.

Verwandschaftsl . , 24, 667-96 (1897).

150030 Kuenen, J. P., Robson, W. G. Observations on mixtures with maximum or minimum vapour-pressure. Philos. Mag., 4(19), 116-32 (1902).

107564 Kulikov, N. E. Study of phase equilibrium under pressure in the system

carbon dioxide (liquid) - nitrogen (gas), (in Russian) Tr. Gork.

Politekh. Inst., 25(13), 18-24 (1969).

150034 Kunerth, W. Solubility of C0(2) and N(2)0 in certain solvents. Phys.

Rev., 19(5), 512-24 (1922).

144
14706 Lambert, M. Simon, M. Excess thermodynamic properties of the liquid

systems A-CH(4) andC0-CH(4). Physica (Utrecht), 28, 1191-6 (1962).

150052 Lannung, A. The solubilities of helium, neon and argon in water and some organic solvents. J. Am. Chem. Soc., 52, 68-80 (1930).

150130 Lannung, A., Gjaldbaek, J. C. The solubility of methane in hydrocarbons,

alcohols, water and other solvents. Acta Chem. Scand., 14(5), 1124-8

(1960).

150085 Le Breton, J. G., McKetta, J. J. Low pressure solubility of n-butane in

water. Hydrocarbon Process. Pet. Refiner, 43(6), 136-8 (1964).

150273 Lee, J. I., Mather, A. E. Solubility of hydrogen sulfide in water. Ber.

Bunsenges. Phys. Chem., 81(10), 1020-3 (1977).

36802 Lehigh, W. R., McKetta, J. J. Vapor-liquid equilibrium in the ethane-nbutane- nitrogen system. J. Chem. Eng. Data, 11(2), 180-2 (1966).

6241 Levitskaya, E. P. Study of the liquid-vapor equilibria of the ternary

system ethane-methane- hydrogen, (in Russian) Zh. Tekh. Fiz., 11(3),

197-204 (1941).

150515 Levitskaya, E., Pryannikov, K. Liquid-vapor equilibrium in the binary

system hydrogen-ethane, (in Russian) Zh. Tekh. Fiz., 9(20), 1849-53

(1939).

'

150506 Lhotak, V., Wichterle, I. Vapour-liquid equilibria in the ethane-nbutane system at high pressures. Fluid Phase Equi lib., 6, 229-35

(1981).

'

150160 Liabastre, A. A. Experimental determination of the solubility of small

organic molecules in H ( 2 ) 0 and D ( 2 ) 0 and the application of the scaled

particle theory to aqueous and nonaqueous solutions. Ga. Inst. Technol.,

Atlanta, Ph.D. Thesis, 240 pp (1974).

5884 Likhter, A. I., Tikhonovich, N. P. Vapor-liquid equilibrium in the

system ethylene-methane- hydrogen, (in Russian) Zh. Tekh. Fiz., 10(14),

1201-6 (1940).

150534 Lindroos, A. E., Dodge, B. F. Phase-equilibria at high pressures. The

system: nitrogen-ammonia at pressures above 1000 atm. Chem. Eng. Prog.,

Symp. Ser., 48(3), 10-7 (1952).

62792 Liu, K. F. Phase equilibria in the helium-carbon dioxide, -argon,

-methane, -nitrogen, and -oxygen systems. Ga. Inst. Technol., Atlanta,

Ph.D. Thesis, 199 pp (1969).

150176 Loprest, F. J. A method for the rapid determination of the solubility of

gases in liquids at various temperatures. J. Phys. Chem., 61(8), 1128-30

(1957).

145
150138 Lu, B. C.-Y., Chang, S.-D., Elshayal, I. M. , Yu, P., Gravelle, D.,

Poon,D.P.L. Low temperature phase equilibria of natural gas components.

Proc. Int. Conf. Calorimetry Thermodyn., 1st, 1969, 755-66 (1969).

69471 Lu, B. C.-Y., Yu, P., Poon, D. P. L. Formation of a third liquid layer

in the nitrogen-methane-ethane system. Nature (London), 222(5195), 768-9

(1969)

150241 Luker, J. A., Gniewek, T., Johnson, C. A. Saturation composition of

steam-helium-liquid water system and P-V-T data for a superheated steamhelium mixture. Chem. Eng. Data Ser. , 3(1), 3-7 (1958).

150033 Maass, 0., Mennie, J. H. Aberrations from the ideal gas laws in systems

of one and two components. Proc. R. Soc. London, Ser. A, 110, 198-232

(1926)

53324 MacKendrick, R. F., Heck, C. K., Barrick, P. L. Liquid-vapor equilibria

of the helium-carbon dioxide system. J. Chem. Eng. Data, 13(3), 352-3

(1968).

11759 Maimoni, A. Liquid-vapor equilibria in the hydrogen-nitrogen and

deuterium-nitrogen systems. AIChE J., 7(3), 371-5 (1961).

150177 Makranczy, J., Megyery-Bal og, K., Rusz, L. , Patyi , L. Solubility of

gases in normal-alkanes. Hung. J. Ind. Chem., 4, 269-80 (1976).

150165 Malinin, S. D. The system H(2)0-C0(2) at high temperatures and

pressures, (in Russian) Geokhimiya, 3, 235-45 (1959).

150194 Malinin, S. D. Investigation of the solubility of carbon dioxide in

water at low partial pressures in conditions of high temperature. (By

method of sample interception), (in Russian) Tr. Soveshch. Eksp. Tekh.

Mineral. Petrogr., 8th, 1968, 229-34 (1971).

150167 Malinin, S. D., Saveleva, N. I. Experimental investigations of C0(2)

solubility in NaCl and CaCl ( 2 ) solutions at temperatures of 25, 50 and 75

degrees and elevated C0(2) pressure, (in Russian) Geokhimiya, 6, 643-53

(1972).

150043 Markham, A. E., Kobe, K. A. The solubility of carbon dioxide and nitrous

oxide in aqueous salt solutions. J. Am. Chem. Soc., 63, 449-54 (1941).

150204 Marti nez-Ortiz, J. A., Manley, D. B. Vapor pressures for the system

isobutane-isobutylene-n-butane. J. Chem. Eng. Data, 23(2), 165-7

(1978)

150258 Maslennikova, V. Ya. Solubility of nitrogen in water, (in Russian) Tr.

Gos. Nauchno-Issled. Proektn. Inst. Azotn. Promsti. Prod. Org. Sint.,

(12), 82-7 (1971).

150147 Maslennikova, V. Ya. , Goryunova, N. P., Subbotina, L. A., Tsiklis, D. S.

The solubility of water in compressed hydrogen. Russ. J. Phys. Chem.

(Engl. Transl . ) , 50(2), 240-3 (1976); transl . of Zh. Fiz. Khim. , 50(2),

411-4 (1976).

146
150259

83825

87946

150268

19707

17785

150128

13495

39627

150029

150278

111233

150205

Maslennikova, V. Ya., Vdovina, N. A.,

gas-gas in the helium-ethane system.

Nauchno-Issled. Proektn. Inst. Azotn.

143-6 (1971).

Maslennikova, V. Ya., Vdovina, N. A.,

in compressed nitrogen, (in Russian)

(1971).

Tsiklis, D. S. Equilibrium of

(in Russian) Tr. Gos.

Promsti. Prod. Org. Sint., (12),

Tsikl is,D.S. Solubility of water

Zh. Fiz. Khim. , 45(9) , 2384

Massoudi, R., King, A. D. , Jr. Solubility of alcohols in compressed

gases. A comparison of vapor-phase interactions of alcohols and

homomorphic compounds with various gases. II. 1-butanol, diethyl ether,

and n-pentane in compressed nitrogen, argon, methane, ethane, and carbon

dioxide at 25 degrees. J. Phys. Chem. , 77(16), 2016-8 (1973).

Mathot, V. Thermodynamic properties of the carbon monoxide-methane

system at 90.67 degrees K. (in French) Bull. Inst. Int. Froid, Annexe,

342-3 (1955).

Mathot, V. Thermodynamic properties of solutions of liquefied gases.

(in French) Mem. Cl. Sci., Acad. R. Belg., Collect. 8, 33(6), 33 pp

(1963).

Mathot, V., Staveley, L. A. K., Young, J. A., Parsonage, N. G.

Thermodynamic properties of the system methane + carbon monoxide at 90.67

degrees K. Trans. Faraday Soc., 52, 1488-500 (1956).

Matous, J., Sobr, J., Novak, J. P., Pick, J. Solubility of carbon

dioxide in water at pressures up to 40 atm. Collect. Czech. Chem.

Commun., 34(12), 3982-5 (1969).

Matschke, D. E. , Thodos, G. Vapor-liquid equilibria for the ethanepropane system. J. Chem. Eng. Data, 7(2), 232-4 (1962).

Matyash, I. V., Mank, V. V., Starkov, M. G. Dissolubility of hydrogen in

liquid nitrogen and of helium in liquid hydrogen, (in Ukrainian) Ukr.

Fiz. Zh. (Ukr. Ed.), 11(5), 497-501 (1966).

McAuliffe, C. Solubility in water of C(l)-C(9) hydrocarbons. Nature

(London), 200, 1092-3 (1963).

McClain, R. A. K. W. Isothermal P-x data and phase equilibrium behaviour

in the isopentane-n-pentane-isoprene system (100 degrees F-120 degrees

F). Univ. Kans., Lawrence, Ph.D. Thesis, 256 pp (1977).

McClure, D. W., Lewis, K. L., Miller, R. C., Staveley, L. A. K. Excess

enthalpies and Gibbs free energies for nitrogen + methane at temperatures

below the critical point of nitrogen. J. Chem. Thermodyn., 8(8), 785-92

(1976).

McCormick, R. H., Walsh, W. H., Hetrick, S. S., Zudkevitch, D. Relative

volatility data for isopentane: n-pentane mixtures. J. Chem. Eng. Data,

8(4), 504-8 (1963).

147
29935 McTaggart, H. A., Edwards, E. Composition of the vapour and liquid

phases of the system methane-nitrogen. Proc. Trans. R. Soc. Can., 13,

57-66 (1919).

150152 Meadows, R. W. , Spedding, D. J. The solubility of very low concentrations of carbon monoxide in aqueous solution. Tellus, 26(102), 143-50

(1974).

150215 Mehra, V. S., Thodos, G. Vapor-liquid equilibrium constants for the

ethane-n-butane-n-pentane system at 200 degrees, 250 degrees, and 300

degrees F« J. Chem. Eng. Data, 8(1), 1-8 (1963).

150206 Mehra, V. S., Thodos, G. Vapor-liquid equilibrium in the ethane-n-butane

system. J. Chem. Eng. Data, 10(4), 307-9 (1965).

150028 Michels, A., Gerver, J., Bijl, A. The influence of pressure on the

solubility of gases. Physica (Utrecht), 3(8), 797-808 (1936).

26757 Michels, A. ,Nederbragt, G. W. Isotherms of methane-aethane mixtures at 0

degrees, 25 degrees and 50 degrees C up to 60 atmospheres. Physica

(Utrecht), 6(7), 656-62 (1939).

150137 Miksovsky, J., Wichterle, I. High pressure vapor-liquid equilibrium in

the ethane-propane system. Int. Congr. Chem. Eng., Chem. Equip. Des.

Automat., 5th, 1975, Pap., (F2.15), 12 pp (1975).

150139 Miksovsky, J., Wichterle, I. Vapour-liquid equilibria in the

ethane-propane system at high pressures. Collect. Czech. Chem. Commun.,

40, 365-70 (1975).

83757 Miller, R. C., Kidnay, A. J., Hiza, M. J. Liquid-vapor equilibria at

112.00 K for systems containing nitrogen, argon, and methane. AIChE J.,

19(1), 145-51 (1973).

114006 Miller, R. C., Kidnay, A. J., Hiza, M. J. Liquid + vapor equilibria in

methane + ethene and in methane + ethane from 150.00 to 190.00 K. J.

Chem. Thermodyn., 9(2), 167-78 (1977).

104717 Miller, R. C., Staveley, L. A. K. Excess enthalpies for some binary

liquid mixtures of low-molecular-weight alkanes. Adv. Cryog. Eng., 21,

493-500 (1976).

150109 Mills, J. R., Miller, F. J. L. Liquefaction of carbon dioxide. Can.

Chem. Process Ind., 29, 651-3 (1945).

91853 Miniovich, V. M., Sorina, G. A. P-V-T-N relations in the system

ethane-propane, (in Russian) Tr. Gos. Nauchno-Issled. Proektn. Inst.

Azotn. Promsti. Prod. ,0rg. Sint., 12, 125-32 (1971).

108496 Miniovich, V. M., Sorina, G. A. Initial section of the critical

liquid-gas equilibrium curve for the ethane-propane system in p-V-T-N

space. Russ. J. Phys. Chem. (Engl. Transl.), 47(4), 586 (1973); transl

of Zh. Fiz. Khim., 47(4), 1032 (1973).

148
108496 Miniovich, V. M., Sorina, G. A. p-V-T-N relations for dilute solutions

of propane in ethane near the critical point of ethane. II. Rosen's

equation of state. Partial molar volumes of ethane and propane. Russ.

J. Phys. Chem. (Engl. Transl.), 47(4), 586-7 (1973).

108496 Miniovich, V. M., Sorina, G. A. p-V-T-N relations for dilute solutions

of propane in ethane near the critical point of ethane. III. Phase

diagram for the ethane-propane system near the critical point of ethane.

Russ. J. Phys. Chem. (Engl. Transl.), 47(4), 587 (1973).

150374 Miranda, R. D., Robinson, D. B., Kalra, H. Equilibrium-phase properties

of propane-carbonyl sulfide system. J. Chem. Eng. Data, 21(1), 62-5

(1976).

150538 Mittasch, A., Kuss, E., Schlueter, H. Densities and vapor pressures of

aqueous ammonia solutions and of liquid nitrogen tetroxide for the

temperature range 0 degrees to 60 degrees, (in German) Z. Anorg. Allg.

Chem., 159, 1-36 (1926).

.8793 Moran, D. W. Low temperature equilibria in binary systems, including the

solid phase. Univ. London, Ph.D. Thesis, 197 pp (1959).

150384 Morgan, 0. M. , Maass, 0. An investigation of the equilibria existing in

gas-water systems forming electrolytes. Can. J. Res., 5, 162-99 (1931).

150091 Morrison, T. J., Billett, F. The salting-out of non-electrolytes. Part

II. The effect of variation in non-electrolyte. J. Chem. Soc., 3819-22

(1952).

150114 Morrison, T. J., Johnstone, N. B. Solubilities of the inert gases in

water. J. Chem. Soc., 3441-6 (1954).

120924 Mraw, S. C., Hwang, S.-C., Kobayashi , R. Vapor-liquid equilibrium of the

CH ( 4

) -CO ( 2 ) system at low temperatures. J. Chem. Eng. Data, 23(2), 135-9

(1978).

35303 Muirbrook, N. K., Prausnitz, J. M. Multicomponent vapor-liquid

equilibria at high pressures: Part I. Experimental study of the

nitrogen-oxygen-carbon dioxide system at 0 degrees C. AIChE J., 11(6),

1092-6 (1965).

91294 Mul hoi land, K. L. An empirical study of the Benedict, Webb and Rubin

mixture rules and experimental vapor-liquid data for the binary

methane-n-butane. Univ. Kans., Lawrence, Ph.D. Thesis, 223 pp (1970).

150179 Murray, C. N., Riley, J. P. The solubility of gases in distilled water

and sea water - IV. Carbon dioxide. Deep-Sea Res. Oceanogr. Abstr.,

18(5), 533-41 (1971).

150178 Murray, C. N., Riley, J. P., Wilson, T. R. S. The solubility of gases in

distilled water and sea water - I. Nitrogen. Deep-Sea Res. Oceanogr.

Abstr., 16(3), 297-310 (1969).

149
150161 Namiot, A. Yu., Beider, S. Ya. Solubility in water of n-pentane and

n-hexane. (in Russian) Khim. Tekhnol. Topi. Masel , 5, 52-5 (1960).

150282 Namiot, A. Yu., Bondareva, M. M. Solubility in water at high pressures

of mixtures of helium and methane, (in Russian) Nauchno-Tekh. Sb.

Dobyche Nefti , 18, 82-91 (1962).

150065 Nederbragt, G. W. Gas-liquid equilibria for the system methane-butane.

Ind. Eng. Chem., 30(5), 587-8 (1938).

30143 Nelson, E. E., Bonne! 1, W. S. Solubility of hydrogen in n-butane. Ind.

Eng. Chem., 35(2), 204-6 (1943).

150508 Neuhausen, B. S., Patrick, W. A. A study of the system ammonia-water as

a basis for a theory of the solution of gases in liquids. J. Phys.

Chem., 25, 693-720 (1921).

53074 Neumann, A., Walch, W. Vapor/liquid equilibrium of C0(2)/CH(4) in the

region of low temperatures and small CO ( 2 ) mole fractions, (in German)

Chem. -Ing. -Tech., 40(5), 241-4 (1968).

150166 Nezdoiminoga, N. A. To the question of solubility of carbon dioxide in

water, (in Russian) Izv. Akad. Nauk Arm. SSR, Ser. Tekh. Nauk, 21(3),

11-7 (1968).

68441 Nikitina, I. E., Skripka, V. G., Gubkina, G. F., Benyaminovich, 0. A. Solubility of helium in iso- and n-butane at low temperatures and

pressures, (in Russian) Gazov. Pronst., 14(12), 35-7 (1969).

70002 Nikitina, I. E., Skripka, V. G., Gubkina, G. F., Sirotin, A. G.,

Benyaminovich, 0. A. Solubility of helium in liquid ethane at low

temperatures and pressures up to 120 kg/cm(2). (in Russian) Gazov.

Promst., 15(6), 35-7 (1970).

150261 Nikitina, I. E. , Zhdanovich, L. A., Sirotin, A. G., Benyaminovich, 0. A. Study of liquid-vapor phase equilibria of Orenburg deposit gas. (in

Russian) Gazov. Promst., 17(3), 41-3 (1972).

150154 Nosov, E. F., Barlyaev, E. V. Solubility of hexafl uoropropylene and

isobutane in water, (in Russian) Zh. Obshch. Khim., 38(2), 211-2

(1968).

150061 Nysewander, C. N., Sage, B. H., Lacey, W. N. Phase equilibria in

hydrocarbon systems. The propane-n-butane system in the critical region.

Ind. Eng. Chem., 32(1), 118-23 (1940).

118307 Ohgaki, K., Katayama, T. Isothermal vapor-liquid equilibrium data for

the ethane-carbon dioxide system at high pressures. Fluid Phase

Equi lib., 1(1), 27-32 (1977).

150073 Olds, R. H., Reamer, H. H., Sage, B. H., Lacey, W. N. Phase equilibria

in hydrocarbon systems. The n-butane-carbon dioxide system. Ind. Eng.

Chem., 41(3), 475-82 (1949).

150
150070 Olds, R. H., Sage, B. H. , Lacey, W. N. Methane-isobutane system. Ind.

Eng. Chem., 34(8), 1008-13 (1942).

150071 Olds, R. H., Sage, B. H. , Lacey, W. N. Phase equilibria in hydrocarbon

systems.- Composition of the dew-point gas of the methane-water system.

Ind. Eng. Chem., 34(10), 1223-7 (1942).

14286 Omar, M. H., Dokoupil, Z. Some supplementary measurements on the

vapour-liquid equilibrium of the system hydrogen-nitrogen at temperatures

higher than the triple point of nitrogen. Commun. Kamerlingh Onnes Lab.

Univ. Leiden, 330a, 11 pp (1962); reprinted from Physica (Utrecht), 28,

33-43 (1962).

64489 O'Sullivan, T. D., Smith, N. 0. The solubility and partial molar volume

of nitrogen and methane in water and in aqueous sodium chloride from 50

to 125 degrees and 100 to 600 atm. J. Phys. Chem., 74(7), 1460-6

(1970).

150180 Paratella, A., Sagramora, G. Solubility of liquids in gases, (in

Italian) Ric. Sci., 29(12), 2605-13 (1959).

100275 Parrish, W. R. , Hiza, M. J. Liquid-vapor equilibria in the nitrogenmethane system between 95 and 120 K. Adv. Cryog. Eng., 19, 300-8

(1974).

105282 Parrish, W. R., Steward, W. G. Vapor- liquid equilibria data for

helium-carbon monoxide and helium-nitrous oxide systems. J. Chem. Eng.

Data, 20(4), 412-6 (1975).

150078 Partington, E. J., Rowlinson, J. S., Weston, J. F. The gas-liquid

critical temperatures of binary mixtures. Part I. Trans. Faraday Soc.,

56, 479-85 (1960).

9443 Pikaar, M. J. A study of phase equilibria in hydrocarbon-C0(2) systems.

Univ. London, Ph.D. Thesis, 196 pp (1959).

150110 Poettmann, F. H., Dean, M. R. Water content of propane. Pet. Refiner,

25(12), 635-8 (1946).

150059 Poettmann, F. H., Katz, D. L. Phase behavior of binary carbon dioxideparaffin systems. Ind. Eng. Chem., 37(9), 847-53 (1945).

150375 Polak, J., Lu, B. C.-Y. Vapor-liquid equilibria in system ammonia-water

at 14.69 and 65 psia. J. Chem. Eng. Data, 20(2), 182-3 (1975).

150090 Pollitzer, F. , Strebel , E. On the influence of an indifferent gas on the

saturation vapor concentration of a liquid. Z. Phys. Chem., Stoechiom.

Verwandschaftsl . , 110, 768-85 (1924).

16067 Pool, R. A. H., Saville, G., Herrington, T. M., Shields, B. D. C.,

Staveley, L. A. K. Some excess thermodynamic functions for the liquid

systems argon + oxygen, argon + nitrogen, nitrogen + oxygen, nitrogen + carbon monoxide, and argon + carbon monoxide. Trans. Faraday Soc.,

58(9), 1692-704 (1962).

151
88753 Poon, D. P. L. , Lu, B. C.-Y. Phase equilibria for systems containing

nitrogen, methane, and propane. Adv. Cryog. Eng., 19, 292-9 (1974).

125573 Potter, R. W. , II, Clynne, M. A. The solubility of the noble gases He,

Ne, Ar, Kr, and Xe in water up to the critical point. J. Solution Chem.,

7(11), 837-44 (1978).

150097 Pray, H. A., Schweickert, C. E., Minnich, B. H. Solubility of hydrogen,

oxygen, nitrogen, and helium in water at elevated temperatures. Ind.

Eng. Chem., 44(5), 1146-51 (1952).

150116 Price, A. R., Kobayashi, R. Low temperature vapor-liquid equilibrium in

light hydrocarbon mixtures: methane-ethane-propane system. J. Chem.

Eng. Data, 4(1), 40-52 (1959).

150371 Rabe, A. E., Harris, J. F. Vapor liquid equilibrium data for the binary

system, sulfur dioxide and water. J. Chem. Eng. Data, 8(3), 333-6

(1963) .

36403 Ramsay, W. , Collie, J. N., Travers, M. Helium, a constituent of certain

minerals. J. Chem. Soc., Trans., 67, 684-701 (1895).

150057 Reamer, H. H., Olds, R. H., Sage, B. H. , Lacey, W. N. Phase equilibria

in hydrocarbon systems. Composition of dew-point gas in ethane-water

system. Ind. Eng. Chem., 35(7), 790-3 (1943).

150545 Reamer, H. H., Olds, R. H., Sage, B. H., Lacey, W. N. Phase equilibria

in hydrocarbon systems. Compositions of the coexisting phases of

n-butane-water system in the three-phase region. Ind. Eng. Chem., 36(4),

381-3 (1944).

150077 Reamer, H. H. , Sage, B. H. Demonstration of critical phenomena for pure

substances and mixtures. Am. J. Phys., 25, 58-63 (1957).

150544 Reamer, H. H. , Sage, B. H. Phase behavior in the hydrogen-ammonia

system. J. Chem. Eng. Data, 4(2), 152-4 (1959).

150543 Reamer, H. H., Sage, B. H. Phase behavior in the nitrogen-ammonia

system. J. Chem. Eng. Data, 4(4), 303-5 (1959).

150083 Reamer, H. H., Sage, B. H., Lacey, W. N. Phase equilibria in hydrocarbon

systems. Volumetric and phase behavior of the methane-propane system.

Ind. Eng. Chem., 42(3), 534-9 (1950).

150099 Reamer, H. H., Sage, B. H., Lacey, W. N. Phase equilibria in hydrocarbon

systems. Volumetric and phase behavior of the propane-carbon dioxide

system. Ind. Eng. Chem., 43(11), 2515-20 (1951).

150098 Reamer, H. H., Sage, B. H., Lacey, W. N. Phase equilibria in hydrocarbon

systems. Volumetric and phase behavior of the methane- hydrogen sulfide

system. Ind. Eng. Chem., 43(4), 976-81 (1951).

152
150531 Reamer, H. H., Sage, B. H., Lacey, U. N. Phase equilibria in hydrocarbon

systems, n-butane-water system in the two-phase region. Ind. Eng.

Chem., 44(3), 609-15 (1952).

150093 Reamer, H. H., Sage, B. H. , Lacey, W. N. Phase equilibria in hydrocarbon

systems. Volumetric and phase behavior of n-pentane-hydrogen sulfide

system. Ind. Eng. Chem., 45(8), 1805-9 (1953).

150119 Reamer, H. H., Sage, B. H., Lacey, W. N. Phase equilibria in hydrocarbon

systems. Volumetric and phase behavior of ethane-n-pentane system. J.

Chem. Eng. Data, 5(1), 44-50 (1960).

150207 Reed, C. D., McKetta, J. J. The solubility of i-butane in water. Pet.

Refiner, 38(4), 159-60 (1959).

69667 Rhodes, H. L. , DeVaney, W. E., Tully, P. C. Phase equilibria data for

helium-methane in the vapor-liquid and fluid-fluid region. J. Chem. Eng.

Data, 16(1), 19-23 (1971).

91184 Rhodes, H. L., Stroud, L., Tully, P. C. Vapor-liquid equilibria data for

two heli urn- nitrogen-methane mixtures from 76.5 degrees to 164 degrees K and pressures to 1,200 psia. Rep. Invest. - U. S., Bur. Mines, 7598,

34 pp (1972).

150208 Rice, P. A., Gale, R. P., Barduhn, A. J. Solubility of butane in water

and salt solutions at low temperatures. J. Chem. Eng. Data, 21(2), 204-6

(1976).

150068 Rigas, T. J., Mason, D. F. , Thodos, G. Vapor-liquid equilibria.

Microsampling technique applied to a new variable-volume cell. Ind. Eng.

Chem., 50(9), 1297-300 (1958).

150523 Rigas, T, J., Mason, D. F., Thodos, G. Vapor-liquid equilibria:

microsampling technique for multicomponent systems. Prepr., Div. Pet.

Chem., Am. Chem. Soc., 3(1), 291-300 (1958).

150242 Rigas, T. J., Mason, D. F. , Thodos, G. Vapor-liquid equilibria. The

system methane-propane-n-butane at 100 degrees F. J. Chem. Eng. Data,

4(3), 201-4 (1959).

49148 Rigby, M. , Prausnitz, J. M. Solubility of water in compressed nitrogen,

argon, and methane. J. Phys. Chem., 72(1), 330-4 (1968).

150209 Roberts, L. R., McKetta, J. J. Vapor- liquid equilibrium in the n-butanenitrogen system. AIChE J., 7(1), 173-4 (1961).

19027 Roberts, L. R., McKetta, J. J. Vapor-liquid equilibrium in the n-butanemethane-nitrogen system. J. Chem. Eng. Data, 8(3), 161-3 (1963).

14027 Roberts, L. R., Wang, R. H., Azarnoosh, A., McKetta, J. J. Methane-nbutane system in the two-phase region. J. Chem. Eng. Data, 7(4), 484-5

(1962).

153
150513 Roberts, 0. L., Brownscombe, E. R., Howe, L. S., Ramser, H. Phase

diagrams of methane and ethane hydrates. Pet. Manage., 13(3), 56-62

(1941)

.

150040 Robinson, D. B., Bailey, J. A. The carbon dioxide-hydrogen sulphidemethane system. Part I: phase behaviour at 100 degrees F. Can. J. Chem.

Eng., 35, 151-8 (1957).

150522 Robinson, D. B., Besserer, G. J. The equilibrium phase properties of the

binary systems: nitrogen-hydrogen sulfide, isobutane-hydrogen sulfide,

isobutane-carbon dioxide, isobutane-ethane. Nat. Gas Process. Assoc.,

Tulsa, Res. Rep., RR-7 , 32 pp (1972).

150041 Robinson, D. B., Hughes, R. E., Sandercock, J. A. W. Phase behavior of

the n-butane-hydrogen sulphide system. Can. J. Chem. Eng., 42, 143-6

(1964).

150181 Robinson, D. B., Kalra, H. The phase behavior of selected hydrocarbon - non-hydrocarbon systems. Proc., Annu. Conv., Gas Process. Assoc., Tech.

Pap., 53, 14-20 (1974).

119280 Robinson, D. B., Kalra, H., Krishnan, T. , Miranda, R. D. The phase

behavior of selected hydrocarbon - non hydrocarbon binary systems:

C(2)-H(2)S and N(2)-iC(4) systems. Proc., Annu. Conv., Gas Process.

Assoc., Tech. Pap., 54, 25-31 (1975).

150042 Robinson, D. B., Lorenzo, A. P., Macrygeorgos, C. A. The carbon dioxidehydrogen sulphide-methane system. Part II. Phase behavior at 40 degrees

F. and 160 degrees F. Can. J. Chem. Eng., 37, 212-7 (1959).

60917 Robinson, D. B., Saxena, A. C. Hydrocarbon K-ratios in the presence of

hydrogen sulfide and carbon dioxide. Proc., Annu. Conv., Nat. Gas

Process. Assoc., Tech. Pap., 45, 58-63 (1966).

26156 Rodewald, N. C., Davis, J . A. , Kurata, F. The heterogeneous phase

behavior of the helium-nitrogen system. AIChE J., 10(6), 937-43 (1965).

150026 Roellig, L. 0., Giese, C. Solubility of helium in liquid hydrogen. J.

Chem. Phys., 37(1), 114-6 (1962).

71134 Rogers, B. L., Prausnitz, J. M. High pressure vapor-liquid equilibria

for argon + neopentane and methane + neopentane. J. Chem. Thermodyn.,

3(2), 211-6 (1971).

45574 Roof, J. G., Baron, J. D. Critical loci of binary mixtures of propane

with methane, carbon dioxide, and nitrogen. J. Chem. Eng. Data, 12(3),

292-3 (1967).

24301 Rowlinson, J. S. , Sutton, J. R. , Weston, J. F. Liquid-vapour equilibrium

in the ternary system carbon dioxide-nitrous oxide-ethylene. Proc. Jt.

Conf. Thermodyn. Transp. Prop. Fluids, 1957, 10-4 (1958).

154
25920 Ruemann, R. M. , Fedoritenko, A. Physical basis of separating helium and

nitrogen. Redstone Sci. Inform. Center, Redstone Arsenal, Ala., Transl.,

RSIC-226 , 15 pp (1964); transl . of Zh . Tekh. Fiz., 7(4), 335-42 (1937).

150024 Ruetschi, P., Amlie, R. F. Solubility of hydrogen in potassium hydroxide

and sulfuric acid. Salting-out and hydration. J. Phys. Chem. , 70(3),

718-23 (1966).

6249 Ruhemann, M. Two-phase equilibrium in binary and ternary systems. I. The system methane-ethane. Proc. R. Soc. London, Ser. A, 171, 121-36

(1939).

5732 Ruhemann, M. , Zinn, N. The system hydrogen-ni trogen-carbon monoxide and

the carbon monoxide wash, (in German) Phys. Z. Sowjetunion, 12(4),

389-403 (1937).

150182 Rutherford, W. M. Miscibility relationships in the displacement of oil

by light hydrocarbons. Soc. Pet. Eng. J., 2(4), 340-6 (1962).

150162 Ryabtsev, N. I., Khuchua, R. S. Solubility of nitrogen in components of

compressed hydrocarbon gases, (in Russian) Gazov. Delo, 6, 25-8

(1970).

46672 Saddington, A. W. , Krase, N. W. Vapor-liquid equilibria in the system

nitrogen-water. J. Am. Chem. Soc., 56, 353-61 (1934).

94700 Sagara, H., Arai , Y., Saito, S. Vapor-liquid equilibria of binary and

ternary systems containing hydrogen and light hydrocarbons. J. Chem.

Eng. J pn. , 5(4), 339-48 (1972).

150533 Sage, B. H., Backus, H. S., Vermeulen, T. Phase equilibria in hydrocarbon systems. XII. Specific heats of some mixtures of propane,

n-butane, and n-pentane. Ind. Eng. Chem., 28(4), 489-93 (1936).

48068 Sage, B. H., Budenholzer, R. A., Lacey, W. N. Phase equilibria in

hydrocarbon systems. Methane-n-butane system in the gaseous and liquid

regions. Ind. Eng. Chem., 32(9), 1262-77 (1940).

150064 Sage, B. H., Hicks, B. L., Lacey, W. N. Phase equilibria in hydrocarbon

systems. The methane-n-butane system in the two-phase region. Ind. Eng.

Chem. , 32(8) , 1085-92 (1940)

.

150063 Sage, B. H. , Lacey, W. N . Phase equilibria in hydrocarbon systems.

Propane-n-pentane system. Ind. Eng. Chem., 32(7), 992-6 (1940).

5730 Sage, B. H., Lacey, W. N., Schaafsma, J. G. Phase equilibria in

hydrocarbon systems. II. Methane-propane system. Ind. Eng. Chem.,

26(2), 214-7 (1934).

150072 Sage, B. H., Reamer, H. H., Olds, R. H., Lacey, W. N. Phase equilibria

in hydrocarbon systems. Volumetric and phase behavior of methane-npentane system. Ind. Eng. Chem., 34(9), 1108-17 (1942).

155
150066 Sage, B. H. , Webster, D. C. , Lacey, W. N. Phase equilibria in hydrocarbon systems. XVI. Solubility of methane in four light hydrocarbons.

Ind. Eng. Chem., 28(9), 1045-7 (1936).

150255 Sanchez, M., Coll, R. System propane-water at high pressures and

temperatures. I. Region of two phases, (in Spanish) An. Quim.,

74(11), 1329-35 (1978).

150117 Sander, W. On the solubility of carbon dioxide in water and some other

solvents under high pressures, (in German) Z. Phys. Chem., Stoechiom.

Verwandschaftsl . , 78, 513-49 (1912).

80644 Sarashina, E., Arai , Y., Saito, S. Vapor-liquid equilibria for the

ni trogen-methane-carbon dioxide system. J. Chem. Eng. Jpn., 4(4), 377-8

(1971).

13445 Sauer, R. N. Vapor-liquid equilibria in the ni trogen-methane-n-butane

system. Tex. Univ., Austin, Ph.D. Thesis, 57 pp (1959).

62117 Saxena, A. C., Robinson, D. B. Phase behavior of the methane-carbon

dioxide-n-butane and methane-hydrogen sul phide-n-butane systems. Can. J.

Chem. Eng., 47(1), 69-75 (1969).

40036 Schindler, D. L., Swift, G. W., Kurata, F. More low temperature V-L

design data. Hydrocarbon Process., 45(11), 205-10 (1966).

150183 Schroeder, W. Observations on solutions of gases in liquids, (in

German) Z. Naturforsch . , Teil B, 24, 500-8 (1969).

150082 Schroeder, W. Research on the temperature dependence of gas solubility

in water, (in German) Chem. -Ing .-Tech. , 45(9+10), 603-8 (1973).

150250 Selleck, F. T., Carmichael, L. T., Sage, B. H. Phase behavior in the

hydrogen sulfide-water system. Ind. Eng. Chem., 44(9), 2219-26 (1952).

150529 Selleck, F. T., Reamer, H. H., Sage, B. H. Volumetric and phase behavior

of mixtures of nitric oxide and nitrogen dioxide. Ind. Eng. Chem.,

45(4), 814-9 (1953).

150262 Seward, T. M. , Franck, E. U. The system hydrogen - water up to 440

degrees C and 2500 bar pressure. Ber. Bunsenges. Phys. Chem., 85(1), 2-7

(1981).

150021 Shoor, S. K. , Walker, R. D., Jr., Gubbins, K. E. Salting out of nonpolar

gases in aqueous potassium hydroxide solutions. J. Phys. Chem., 73(2),

312-7 (1969).

35926 Shtekkel , F. A., Tsin, N. M. Determination of the liquid-vapor

composition diagram of the methane- nitrogen- hydrogen system, (in

Russian) Zh. Khim. Promsti., 16(8), 24-8 (1939).

40404 Si nor, J. E., Kurata, F. Solubility of helium in liquid argon, oxygen,

and carbon monoxide. J. Chem. Eng. Data, 11(4), 537-9 (1966).

156
36006 Sinor, J. E., Schindler, D. L., Kurata, F. Vapor-liquid phase behavior

of the helium-methane system. AIChE J., 12(2), 353-7 (1966).

13188 Sister, G. A., Sokolov, P. P. Obtaining technical hydrogen from

coke-oven gas at low temperatures. U. S. Dep. Commer., Off. Tech. Serv.,

Transl., 63-24285, 5 pp (1963); transl . of Zh. Khim. Promsti . , 17(4/5),

44-5 (1940).

61574 Skripka, V. G. , Barsuk, S. D., Nikitina, I. E., Gubkina, G. F.

,

Benyaminovich, 0. A. Investigation of liquid-vapor equilibrium in the

nitrogen-n-butane system, (in Russian) Gazov. Promst., 14(4), 41-5

(1969).

40179 Skripka, V. G., Dykhno, N. M. Solubility of helium and neon in liquid

oxygen, nitrogen and argon (in the temperature range from 67 to 90

degrees K and pressures from 6 to 26 ata). (in Russian) Tr., Vses.

Nauchno-Issled. Inst. Kislorodn. Mashinostr., 8, 163-79 (1964).

84579 Skripka, V. G. , Nikitina, I. E., Zhdanovich, L. A., Sirotin, A. G.,

Benyaminovich, 0. A. Phase equilibria of liquid-vapor at low

temperatures in binary systems, formed by components of natural gas. (in

Russian) Gazov. Promst., 15(12), 35-6 (1970).

150144 Smith, N. 0., Kelemen, S., Nagy, B. Solubility of natural gases in

aqueous salt solutions - II. Nitrogen in aqueous NaCl , CaCl(2),

Na(2)S0(4) and MgS0(4) at room temperatures and at pressures below 1000

psia. Geochim. Cosmochim. Acta, 26, 921-6 (1962).

3728 Smith, S. R. I. Gas-liquid phase equilibrium in the system He-H(2).

II. Development of mass spectrograph techniques for analysis of He-H(2)

and their isotopes. Ohio State Univ., Columbus, Ph.D. Thesis, 136 pp

(1952)

.

54119 Sneed, C. M., Sonntag, R. E. , Van Wylen, G. J. Hel i urn- hydrogen liquidvapor equilibrium to 100 atm. J. Chem. Phys., 49(5), 2410-4 (1968).

2201 Sobocinski, D. P., Kurata, F. Heterogeneous phase equilibria of the

hydrogen sulfide-carbon dioxide system. AIChE J., 5(4), 545-51 (1959).

123894 Somait, F. A., Kidnay, A. J. Liquid-vapor equilibria at 270.00 K for

systems containing nitrogen, ethane, and carbon dioxide. J. Chem. Eng.

Data, 23(4), 301-5 (1978).

28623 Sonntag, R. E., Crain, R. W., Jr., Streett, W. B., Van Wylen, G. J.

Liquid-vapor equilibrium in the system hydrogen-helium. Final report.

Univ. Mich., Ann Arbor, Coll. Eng., Rep., 05664-2-F, 72 pp (1964).

25053 Sonntag, R. E., Van Wylen, G. J., Crain, R. W., Jr. Liquid-vapor

equilibrium in the system equilibrium hydrogen-helium. J. Chem. Phys.,

41(8), 2399-402 (1964).

150382 Spall, B. C. Phase equilibria in the system sulphur dioxide-water from

25-300 degrees C. Can. J. Chem. Eng., 41, 79-83 (1963).

157
50699 Spano, J. 0., Heck, C. K., Barrick, P. L. Liquid-vapor equilibria of the

hydrogen-carbon dioxide system. J. Chem. Eng. Data, 13(2), 168-71

(1968)

.

39204 Sprow, F. B., Prausnitz, J. M. Vapor-liquid equilibria for five

cryogenic mixtures. AIChE J., 12(4), 780-4 (1966).

6240 Steckel , F. Dew and boiling curves of ni trogen-carbon monoxide mixtures

up to 17 atmospheres, (in German) Phys. Z. Sowjetunion, 8, 337-41

(1935)

.

150184 Steckel, F. Vapor- liquid equilibria of some binary, hydrogen sulfide

containing systems under pressure, (in German) Sven. Kern. Tidskr.,

57(9), 209-16 (1945).

11157 Stein, F. P., Claitor, L. C., Geist, J. M. A study of the phase equilibria of the hydrogen-carbon monoxide-propane system at low temperatures.

Adv. Cryog. Eng., 7, 106-13 (1962).

41049 Steinbach, H.-G., Stei nbrecher, M. Solubility of nitrogen in C ( 4

)

liquefied gases, (in German) Chem. Tech. (Leipzig), 18(10), 633

(1966)

.

150229 Stephan, E. F. , Hatfield, N. S., Peoples, R. S., Pray, H. A. H. The

solubility of gases in water and in aqueous uranyl salt solutions at

elevated temperatures and pressures. Battel! e Mem. Inst., Columbus,

Ohio, Rep., BMI-1067, 63 pp (1956).

11348 Sterner, C. J. Phase equilibria in C0(2 )-methane systems. Adv. Cryog.

Eng., 6, 467-74 (1961).

150188 Stewart, P. B., Munjal , P. K. The solubility of carbon dioxide in

distilled water, synthetic sea water and synthetic sea-water

concentrates. Calif. Univ., Richmond, Sea Water Convers. Lab., Rep.,

69-2, 49 pp (1969).

150210 Stewart, P. B., Munjal, P. Solubility of carbon dioxide in pure water,

synthetic sea water, and synthetic sea water concentrates at -5 degrees

to 25 degrees C. and 10- to 45-atm. pressure. J. Chem. Eng. Data, 15(1),

67-71 (1970).

71490 Stoeckli, H. F. , Staveley, L. A. K. The excess Gibbs function and the

volumes of mixing for the system methane + propane at 90.68 K. Helv.

Chim. Acta, 53(8), 1961-4 (1970).

150532 Stone, H. W. Solubility of water in liquid carbon dioxide. Ind. Eng.

Chem., 35(12), 1284-6 (1943).

50612 Streett, W. B. Gas-liquid and fluid-fluid phase separation in the system

helium-nitrogen near the critical temperature of nitrogen. Chem. Eng.

Prog., Symp. Ser., 63(81), 37-42 (1967).

95426 Streett, W. B. Phase equilibria in molecular hydrogen-helium mixtures at

high pressures. Astrophys. J., 186(3), 1107-25 (1973).

158
124829 Streett, W. B., Calado, J. C. G. Liquid-vapour equilibrium for hydrogen

+ nitrogen at temperatures from 63 to 110 K and pressures to 57 MPa. J.

Chem. Thermodyn., 10(11), 1089-100 (1978).

92174 Streett, W. B., Erickson, A.L. Phase equilibria in gas mixtures at high

pressures: implications for planetary structures. Phys. Earth Planet.

Inter., 5, 357-66 (1972).

94794 Streett, W. B., Erickson, A. L., Hill, J. L. E. Phase equilibria in

fluid mixtures at high pressures: the He-CH(4) system. Phys. Earth

Planet. Inter., 6(1-3), 69-77 (1972).

65038 Streett, W. B., Hill, J. L. E. Phase equilibria in fluid mixtures at

high pressures: the helium- nitrogen system. J. Chem. Phys., 52(3),

1402-6 (1970).

21933 Streett, W. B., Sonntag, R. E., Van Wylen, G. J. Liquid-vapor equilibrium in the system normal hydrogen-helium. J. Chem. Phys., 40(5), 1390-5

(1964).

97331 Stryjek, R. , Chappelear, P. S., Kobayashi , R. Low- temperature vaporliquid equilibria of nitrogen-methane system. J. Chem. Eng. Data, 19(4),

334-9 (1974).

97332 Stryjek, R. , Chappelear, P. S., Kobayashi, R. Low- temperature vaporliquid equilibria of nitrogen-ethane system. J. Chem. Eng. Data, 19(4),

340-3 (1974).

150247 Stutzman, L. F., Brown, G. M. Low temperature vapor- liquid equilibria.

Part I - Phase equilibria in natural gas at low temperatures. Chem. Eng.

Prog., 45(2), 139-42 (1949).

150189 Suciu, S, , Sibbitt, W. L. A study of the nitrogen and water and hydrogen

and water systems at elevated temperatures and pressures. Purdue Univ.,

Lafayette, Ind., Eng. Exp. Sta., Rep., ANL-46Q3, Pt. II, 23 pp (1951).

150163 Sultanov, R. G., Skripka, V. G., Namiot, A. Yu. Moisture content of

methane at high temperatures and pressures, (in Russian) Gazov.

Promst., 16(4), 6-8 (1971).

150146 Sultanov, R. G., Skripka, V. G. , Namiot, A. Yu. Phase equilibria and

critical phenomena in the water-methane system at elevated temperatures

and pressures. Russ. J. Phys. Chem. (Engl. Transl.), 46(8), 1238 (1972);

transl . of Zh. Fiz. Khim., 46(8), 2160 (1972).

150164 Sultanov, R. G., Skripka, V. G., Namiot, A. Yu. Solubility of methane in

water at increased temperatures and pressures, (in Russian) Gazov.

Promst., 17(5), 6-7 (1972).

150157 Takenouchi , S. , Kennedy, G. C. The binary system H ( 2 ) 0-C0( 2 ) at high

temperatures and pressures. Am. J. Sci., 262, 1055-74 (1964).

150140 Taylor, H. S., Wald, G. W., Sage, B. H., Lacey, W. N. Phase behavior of

the methane-n-pentane system. Oil Gas J., 38(13), 46-50 (1939).

159
76312 Tiwari, K. K., Robinson, D. B. Volumetric behavior of the ethanehydrogen sulphide system. Can. J. Chem. Eng., 49, 637-41 (1971).

150100 Toedheide, K., Franck, E. U. The two-phase region and the critical curve

in the carbon dioxide-water system up to a pressure of 3500 bar. (in

German) Z. Phys. Chem. (Frankfurt am Main), 37, 387-401 (1963).

150283 Toriumi, T., Kaminishi, G. Studies on the vapor-liquid equilibria at

high pressures, (in Japanese) Asahi Garasu Kogyo Gijutsu Shoreikai

Kenkyu Hokoku, 14, 67-79 (1968).

29934 Torocheshnikov, N. S. Isotherms and isobars of the nitrogen-carbon

monoxide system, (in Russian) Zh. Tekh. Fiz., 7(10), 1107-10 (1937).

5717 Torocheshnikov, N. S., Levius, L. A. Liquid-vapor equilibrium in the

nitrogen-methane system, (in Russian) Zh. Khim. Promsti., 16(1), 19-22

(1939).

150281 Torocheshnikov, N. S. , Semenova, V. A. Equilibrium of liquid-vapor in

the system hydrogen-methane-nitrogen-carbon monoxide at a temperature of

78 degrees K. (in Russian) Tr. Mosk. Khim.-Tekhnol . Inst., 18, 115-7

(1954)

.

11381 Toyama, A., Chappelear, P. S., Lei and, T. W., Kobayashi, R. Vapor-liquid

equilibria at low temperatures: the carbon monoxide-methane system. Adv.

Cryog. Eng., 7, 125-36 (1962).

69775 Trust, D. B., Kurata, F. Vapor-liquid phase behavior of the hydrogenpropane and hydrogen-carbon monoxide-propane systems. AIChE J., 17(1),

86-91 (1971).

73928 Trust, D. B. , Kurata, F. Vapor-liquid and liquid-liquid vapor phase

behavior of the carbon monoxide-propane and the carbon monoxide-ethane

systems. AIChE J., 17(2), 415-9 (1971).

150236 Tsang, C. Y., Clancy, P., Calado, J. C. G., Streett, W. B. Phase

equilibria in the H(2)/CH(4) system at temperatures from 92.3 to 180.0 K and pressures to 140 MPa. Chem. Eng. Commun., 6, 365-83 (1980).

150505 Tsang, C. Y., Streett, W. B. Phase equilibria in the H ( 2 ) /CO ( 2 ) system

at temperatures from 220 to 290 K and pressures to 172 MPa. Chem. Eng.

Sci., 36, 993-1000 (1981).

150221 Tsang, C. Y., Streett, W. B. Phase equilibria in the H ( 2

) -CO system at

temperatures from 70 to 125 K and pressures to 53 MPa. Fluid Phase

Equilib., 6, 261-73 (1981).

13359 Tsiklis, D. S. Limited mutual solubility of gases at high pressures in

the systems helium-ammonia and helium-carbon dioxide, (in Russian)

Dokl . Akad. Nauk SSSR, 86(6), 1159-61 (1952).

7961 Tsiklis, D. S. Limited mutual solubility of gases in the helium-propane

system at high pressures, (in Russian) Dokl. Akad. Nauk SSSR, 101(1),

129-30 (1955).

160
150012 Tsiklis, D. S., Maslennikova, V. Ya. Mutual limited solubility of gases

in the water-butane system, (in Russian) Dokl . Akad. Nauk SSSR, 157(2),

426-9 (1964).

150013 Tsiklis, D. S., Maslennikova, V. Ya. Mutual limited solubility of gases

in the water- nitrogen system, (in Russian) Dokl. Akad. Nauk SSSR,

161(3), 645-7 (1965).

67034 Tully, P. C., DeVaney, W. £., Rhodes, H. L. Phase equilibria of the

hel i urn- nitrogen system from 122 to 126 degrees K. Adv. Cryog. Eng., 16,

88-95 (1971).

120297 Tully, P. C., Stroud, L. Vapor-liquid equilibria data for a heliumnitrogen-methane mixture from 80 to 144 K and pressures to 1,200 psia.

Rep. Invest. - U. S., Bur. Mines, 8181, 20 pp (1976).

639 Uehara, K. Research on gas mixturs of low hydrocarbons. Part 2.

Solubilities of hydrogen and methane in liquid ethane, (in Japanese)

Nippon Kagaku Kaishi (1921-47), 53, 931-2 (1932).

150069 Vaughan, W. E., Collins, F. C. P-V-T-x relations of the system propaneisopentane. Ind. Eng. Chern., 34(7), 885-90 (1942).

99841 Vejrosta, J., Wichterle, I. The propane-pentane system at high

pressures. Collect. Czech. Chem. Commun., 39(5), 1246-8 (1974).

150516 Velikovskii, A. S., Stepanova, G. S., Vybornova, Ya. I. Phase equilibria % of binary mixtures of methane with hydrocarbons of the normal paraffin

series, (in Russian) Gazov. Promst., 9(2), 1-6 (1964).

6255 Vellinger, E., Pons, E. On the solubility of nitrogen in liquid methane

and liquid propane, (in French) C. R. Hebd. Seances Acad. Sci., 217,

689-91 (1943).

150211 Verschaffel t, J. Measurements on the system of isothermal lines near the

plaitpoint, and especially on the process of the retrograde condensation

of a mixture of carbonic acid and hydrogen. Commun. Kamerlingh Onnes

Lab. Univ. Leiden, 45, 15 pp (1898); transl . from Versl . Gewone Vergad.

Afd. Natuurkd., K. Ned. Akad. Wet., 7, 281-9 (1898).

150212 Verschaffel t, J. Measurements on the system of isothermal lines near the

plaitpoint, and especially on the process of the retrograde condensation

of a mixture of carbonic acid and hydrogen (continued). Measurements on the change of pressure by substitution of one component by the other in

mixtures of carbonic acid and hydrogen (continued). Commun. Kamerlingh

Onnes Lab. Univ. Leiden, 47, 19 pp (1899); transl. from Versl. Gewone

Vergad. Afd. Natuurkd., K. Ned. Akad. Wet., 8, 389-400 (1899).

6216 Verschoyle, T. T. H. The ternary system carbon monoxide-nitrogenhydrogen and the component binary systems between temperatures of -185

degrees and -215 degrees C. , and between pressures of 0 and 225 atm.

Philos. Trans. R. Soc. London, Ser. A, 230, 189-220 (1931).

161
150101 Vilcu, R., Gainar, I. Solubility of gases under pressure in liquids. I. The carbon dioxide-water system, (in German) Rev. Roum. Chim., 12(2),

181-9 (1967).

150032 von Antropoff, A. The solubility of xenon, krypton, argon, neon, and

helium in water. Proc. R. Soc. London, Ser. A, 83, 474-82 (1910).

150510 Vosolsobe, J., Simecek, A., Michalek, J., Kadlec, B. Solubility of

sulphur dioxide in water, (in Czech) Chem. Prum., 15(7), 401-4 (1965).

21434 Wang, R. H., McKetta, J. J. Vapor-liquid equilibrium of the methane-nbutane-carbon dioxide system at low temperatures and elevated pressures.

J. Chem. Eng. Data, 9(1), 30-5 (1964).

63416 Watanabe, K., Kuriki, M. , Ogura, M., Saito, I. Vapour-1 iquid-equil ibrium

of LNG . Cryog. Eng., 4(6), 292-301 (1969).

150525 Wehe, A. H., McKetta, J. J. n-butane-l-butene-water system in the threephase region. J. Chem. Eng. Data, 6(2), 167-72 (1961).

64484 Weiss, R. 7. Helium isotope effect in solution in water and seawater.

Science, 168, 247-8 (1970).

70831 Weiss, R. F. Solubility of helium and neon in water and seawater. J.

Chem. Eng. Data, 16(2), 235-41 (1971).

150186 Weiss, R. F. Carbon dioxide in water and seawater: the solubility of a non-ideal gas. Mar. Chem., 2(3), 203-15 (1974).

150509 Wells, F. L., MacClaren, R. H. Total pressures for the system: sulphur

dioxide-water. Tappi, 38(11), 668-71 (1955).

150020 Wen, W.-Y., Hung, J. H. Thermodynamics of hydrocarbon gases in aqueous

tetraalkyl ammonium salt solutions. J. Phys. Chem., 74(1), 170-80

( 1970) .

'

150050 Wetlaufer, D. B., Malik, S. K., Stoller, L. , Coffin, R. L. Nonpolar

group participation in the denaturation of proteins by urea and

guanidinium salts. Model compound studies. J. Am. Chem. Soc., 86,

508-14 (1964).

74084 Wichterle, I., Chappelear, P. S., Kobayashi , R. Determination of

critical exponents from measurements of binary vapor-liquid equilibrium

in the neighborhood of the critical line. J. Comput. Phys., 7(3), 606-20

(1971).

75233 Wichterle, I., Kobayashi, R. Vapor-liquid equilibrium of methane-propane

system at low temperatures and high pressures. J. Chem. Eng. Data,

17(1), 4-9 (1972).

75234 Wichterle, I., Kobayashi, R. Vapor-liquid equilibrium of methane-ethane

system at low temperatures and high pressures. J. Chem. Eng. Data,

17(1), 9-12 (1972).

162
75235 Wichterle, I., Kobayashi, R. Vapor-liquid equilibrium of methane-ethanepropane system at low temperatures and high pressures. J. Chem. Eng.

Data, 17(1), 13-8 (1972).

3616 Widdoes, L. C., Katz, D. L. Vapor-liquid equilibrium constants for

carbon monoxide. Ind. Eng. Chem., 40(9), 1742-6 (1948).

150046 Wiebe, R., Gaddy, V. L. The solubility of hydrogen in water at 0, 50, 75

and 100 degrees from 25 to 1000 atmospheres. J. Am. Chem. Soc., 56, 76-9

(1934)

.

150047 Wiebe, R. , Gaddy, V. L. The solubility of helium in water at 0, 25, 50

and 75 degrees and at pressures to 1000 atmospheres. J. Am. Chem. Soc.,

57, 847-51 (1935).

150391 Wiebe, R., Gaddy, V. L. The solubility in liquid ammonia of hydrogen at

0 degrees and of nitrogen at 0, 50, 75, 90 and 100 degrees at pressures

to 1000 atmospheres. Critical phenomena of ammonia-nitrogen mixtures.

J. Am. Chem. Soc, 59, 1984-7 (1937).

150045 Wiebe, R., Gaddy, V. L. The solubility in water of carbon dioxide at 50,

75 and 100 degrees, at pressures to 700 atmospheres. J. Am. Chem. Soc.,

61, 315-8 (1939).

150044 Wiebe, R. , Gaddy, V. L. The solubility of carbon dioxide in water at

various temperatures from 12 to 40 degrees and at pressures to 500

atmospheres. Critical phenomena. J. Am. Chem. Soc., 62, 815-7 (1940).

150054 Wiebe, R., Gaddy, V. L. Vapor phase composition of carbon dioxide-water

mixtures at various temperatures and at pressures to 700 atmospheres. J.

Am. Chem. Soc., 63, 475-7 (1941).

150527 Wiebe, R., Gaddy, V. L. , Heins, C., Jr. Solubility of hydrogen in water

at 25 degrees C. from 25 to 1000 atmospheres. Ind. Eng. Chem., 24(7),

823-5 (1932).

150076 Wiebe, R., Gaddy, V. L, Heins, C., Jr. Solubility of nitrogen in water

at 25 degrees C. from 25 to 1000 atmospheres. Ind. Eng. Chem., 24, 927

(1932)

.

150053 Wiebe, R. , Gaddy, V. L., Heins, C., Jr. The solubility of nitrogen in

water at 50, 75 and 100 degrees from 25 to 1000 atmospheres. J. Am.

Chem. Soc., 55, 947-53 (1933).

150390 Wiebe, R., Tremearne, T. H. Solubility of nitrogen in liquid ammonia at

25 degrees from 25 to 1000 atmospheres. J. Am. Chem. Soc., 55, 975-8

(1933)

.

150389 Wiebe, R., Tremearne, T. H. The solubility of hydrogen in liquid ammonia

at 25, 50, 75 and 100 degrees and at pressures to 1000 atmospheres. J.

Am. Chem. Soc., 56, 2357-60 (1934).

163
64379 Wiese, H. C., Jacobs, J., Sage, B. H. Phase equilibria in the

hydrocarbon systems. Phase behavior in the methane-propane-n-butane

system. J. Chem. Eng. Data, 15(1), 82-91 (1970).

64378 Wiese, H. C., Reamer, H. H., Sage, B. H. Phase equilibria in hydrocarbon

systems. Phase behavior in the methane-propane-n-decane system. J.

Chem. Eng. Data, 15(1), 75-82 (1970).

150031 Wilcock, R. J., Battino, R. Solubility of oxygen-ni trogen mixture in

water. Nature (London), 252(5484), 614-5 (1974).

6369 Williams, R. B., Katz, D. L. Vapor liquid equilibria in binary systems.

Hydrogen with ethylene, ethane, propylene, and propane. Ind. Eng. Chem.,

46(12), 2512-20 (1954).

88754 Wilson, G. M. Vapor-liquid equilibria of nitrogen, methane, ethane, and

propane binary mixtures at LNG temperatures from total pressure

measurements. Adv. Cryog. Eng., 20, 164-71 (1975).

150536 Wilson, T. A. The total and partial vapor pressures of aqueous ammonia

solutions. 111., Univ., Eng. Exp. Stn., Bull., 146, 48 pp (1925).

150126 Winkler, L. W. The solubility of gases in water. (Part 1.). (in

German) Ber. Dtsch. Chem. Ges., 24, 89-101 (1891).

150121 Winkler, L. W. The solubility of gases in water. (Part 2). (in German)

Ber. Dtsch. Chem. Ges., 24, 3602-10 (1891).

150127 Winkler, L. W. Regularity with the absorption of gases in liquids, (in

German) Z. Phys. Chem., Stoechiom. Verwandschaftsl . , 9, 171-5 (1892).

150125 Winkler, L. W. The solubility of gases in water, (in German) Ber.

Dtsch. Chem. Ges., 34, 1408-22 (1901).

150539 Wrewsky, M. On the equilibrium between vapor and liquid aqueous

solutions of ammonia, (in German) Z. Phys. Chem., Stoechiom.

Verwandschaftsl., 112, 117-27 (1924).

150222 Wright, R. H., Maass, 0. The solubility of hydrogen sulphide in water

from the vapor pressures of the solutions. Can. J. Res., 6, 94-101

(1932).

150519 Wucherer, J. Measurements of pressure, temperature and composition of

the liquid and vapor phases of ammonia- water mixtures in the saturated

state, (in German) Z. Gesamte Kaelte-Ind., 39(6), 97-104 (1932); 39(7),

136-40 (1932).

150213 Yamamoto, S., Alcauskas, J. B., Crozier, T. E. Solubility of methane in

distilled water and seawater. J. Chem. Eng. Data, 21(1), 78-80 (1976).

150120 Yeh, S.-Y., Peterson, R. E. Solubility of carbon dioxide, krypton, and xenon in aqueous solution. J. Pharm. Sci . , 53(7), 822-4 (1964).

164
150214

59455

67016

150266

90120

55395

76576

150264

76577

50157

64158

13187

79086

Yen, L. C., McKetta, J. J., Jr. Solubility of nitrous oxide in some nonpolar solvents. J. Chem. Eng. Data, 7(2), 288-9 (1962).

Yesavage, V. F., Katz, D. L., Powers, J. E. Experimental determinations

of several thermal properties of a mixture containing 77 mole % propane

in methane. J. Chem. Eng. Data, 14(2), 137-49 (1969).

Yesavage, V. F., Katz, D. L., Powers, J. E. Experimental determinations

of several thermal properties of a mixture containing 51 mole percent

propane in methane. AIChE J., 16(5), 867-75 (1970).

YoKoyama, K., Ohe, S. Studies on apparatus for measuring vapor-liquid

equilibrium at high pressures, (in Japanese) Ishikawajima-Harima Giho,

11(1), 5-11 (1971).

Yorizane, M. The determination of vapor-liquid equilibrium data at high

pressure and low temperature, (in Japanese) Asahi Garasu Kogyo Gijutsu

Shoreikai Kenkyu Hokoku, 18, 61-76 (1971).

Yorizane, M., Sadamoto, S., Yoshimura, S., Masuoka, H., Shiki, N .

,

Kimura, T., Toyama, A. Vapor-liquid equilibria at low temperature, (in

Japanese) Kagaku Kogaku, 32(3), 257-64 (1968).

Yorizane, M., Yoshimura, S., Masuoka, H. Vapor liquid equilibrium at

high pressure ( N ( 2

) -CO ( 2 ) , H ( 2) -CO ( 2 ) system), (in Japanese) Kagaku

Kogaku, 34(9), 953-7 (1970).

Yorizane, M., Yoshimura, S., Masuoka, H. Measurements and predictions of

multicomponent vapor-liquid equilibria. Bull. Jpn. Pet. Inst., 14(1),

105-13 (1972).

Yorizane, M. , Yoshimura, S., Masuoka, H., Naka, T. The measurement and

prediction of the vapor-liquid equilibrium relation at low temperature

and high pressure for the H(2)-N(2) system, (in Japanese) Kagaku

Kogaku, 35(6), 691-3 (1971).

Yorizane, M. , Yoshimura, S., Masuoka, H., Toyama, A. Low temperature

vapour-liquid equilibria of hydrogen-containing binaries. Proc. Int.

Cryog. Eng. Conf., 1st, 1967, 57-62 (1968).

Yu, P., El shayal , I. M., Lu, B. C.-Y. Liquid-liquid-vapor equilibrium in

the nitrogen-methane-ethane system. Can. J. Chem. Eng., 47(5), 495-8

(1969).

Yushkevich, N. F., Torocheshni kov, N. S. Study of the coexistence of

liquid and vapor phases of solutions of nitrogen and carbon monoxide.

(in Russian) Zh. Khim. Promsti., 13(21), 1273-83 (1936).

Zeininger, H. Liquid/vapor equilibria of the binary systems N ( 2 ) 0/N ( 2 )

,

N ( 2 )0/0 ( 2 ) and N ( 2 ) 0/CH ( 4 ) at low temperatures and high pressures, (in

German) Chem. -Ing. -Tech. , 44(9), 607-12 (1972).

165
88684 Zeininger, H. Li quid/ vapor equilibria of the systems

N(2)/H(2)/CH(4)/NH(3) at 25 degrees C and pressures up to 500 bar. (in

German) Chem.-Ing.-Tech. , 45(17), 1067-70 (1973).

150269 Zelvenskii, Ya. D. Solubility of carbon dioxide in water under pressure,

(in Russian) Zh. Fiz. Khim., 14(17-18), 1250-7 (1937).

19620 Zenner, G. H., Dana, L. I. Liquid-vapor equilibrium compositions of

carbon dioxi de-oxygen-ni trogen mixtures. Chem. Eng. Prog., Symp. Ser.,

59(44), 36-41 (1963).

166
639

924

2201

3518

3518

3616

3728

5100

5121

5617

5651

5657

5679

5717

5730

5732

5884

5964

6216

6240

6241

6249

6251

6255

6350

6361

6364

6369

6572

7961

8000

8283

8793

8905

9443

9518

9643

11157

11348

11381

11759

11765

12784

13187

13188

13359

13445

13495

13680

14027

14286

14706

CROSS INDEX BY ACCESSION NUMBER

Uehara,K. (1932)

Bloomer, 0. T. , Parent,J.D. (1953)

Sooocinski ,D.P. , Kurata,F. (1959)

Akers, W.W., Burns, J.F., Fairchil d,W.R. (1954)

Akers, W.W., Kelley, R.E., Lipscomb, T.G. (1954)

Widdoes,L.C. , Katz,D.L. (1948)

Smith, S.R. (1952)

Aroyan, H.J., Katz,D.L. (1951)

Bartlett, E.P. (1927)

Fastovskii ,V.G. , Gonikberg,M.G. (1940)

Dokoupil ,Z. , Van Soest,G., Swenker,M.D.P. (1955)

Gonikberg,M.G. , Fastowsky ,W.G. , Gurwitsch,J .G. (1939)

Freeth,F.A., Verschoyle,T.T.H. (1931)

Torocheshnikov,N.S. , Levius,L.A. (1939)

Sage,B.H., Lacey, W.N., Schaafsma ,J .G. (1934)

Ruhemann ,M. , Zinn,N. (1937)

Likhter,A. I . , Tikhonovich, N.P. (1940)

Hill ,E.S., Lacey, W.N. (1934)

Verschoyle,T.T.H. (1931)

Steckel,F. (1935)

Levitskaya, E.P. (1941)

Ruhemann,M. (1939)

Benham,A.L., Katz,D.L. (1957)

Vellinger,E., Pons,E. (1943)

Cines,M.R., Roach,J.T., Hogan, R.J., Roland, C.H. (1953)

Kharakhorin,F.F. (1940)

Gonikberg,M., Fastowsky, W. (1940)

Williams, R.B., Katz,D.L. (1954)

Cosway, H.F., Katz,D.L. (1959)

Tsiklis,D.S. (1955)

Abdul aev ,Ya.A. (1939)

Abdul aev,Ya. A. (1941)

Moran, U.W. (1959)

Akers, W.W., Eubanks, L.S. (1960)

Pikaar,M.J. (1959)

Abdul laev,Ya.A. (1939)

Kharakhori n,F.F. (1959)

Stein, F.P., Cl ai tor ,L.C . , Geist,J.M. (1962)

Sterner,C.J. (1961)

Toyama, A., Chappel ear,P .S . , Leland,T.W., Kob... (1962)

Maimoni,A. (1961)

Brandt, L.W., Stroud, L., Miller, J.E. (1961)

Ellington, R.T., Eakin,B.E., Parent, J.D., Gam... (1959)

Yushkevich,N.F. , Torocheshnikov,N.S. (1936)

Sister, G. A., Sokolov, P.P. (1940)

Tsikl is,D.S. (1952)

Sauer, R.N. (1959)

Matschke,D.E. , Thodos,G. (1962)

Cota,H.M., Thodos,G. (1962)

Roberts, L. R. , Wang,R.H., Azarnoosh,A. , McKet... (1962)

Omar,M.H., Dokoupil, Z. (1962)

Lambert, M. Simon, M. (1962)

167
16067

16075

17059

17785

18927

19027

19414

19620

19707

20429

20499

21414

21434

21435

21436

21933

24301

24862

25053

25304

25920

26156

26297

26757

28623

28799

29397

29934

29935

29966

30143

35303

35926

36006

36403

36802

37444

39075

39202

39204

39337

39627

40036

40179

40404

41049

42929

44762

45223

45392

45496

45574

46018

46672

Pool,R.A.H., Saville,G., Herrington, T. M. , Sh... (1962)

Hunter, M. A. (1906)

Boone, W. J . ,Jr. , DeVaney,W. E . , Stroud. ,L. (1963)

Mathot,V., Staveley,L.A.K. , Young, J. A., Pars... (1956)

Buzyna,G., Maori ss,R.A. , El 1 ington,R.T. (1963)

Roberts, L. R. , McKetta,J.J. (1963)

Jones, I. W., Rowl inson,J .S. (1963)

Zenner,G.H., Dana, L. I. (1963)

Mathot,V. (1963)

DeVaney,W.E . , Dalton,B.J., Meeks,J .C. ,Jr. (1963)

Klots,C.E., Benson, B.B. (1963)

Davis, J. A., Rodewald,N., Kurata.F. (1963)

Wang,R.H., McKetta,J.J. (1964)

Burch, R.J. (1964)

Douglas, E. (1964)

Streett,W.B . , Sonntag,R.E. , Van Wylen,G.J. (1964)

Rowl inson,J .S. , Sutton,J.R., Weston, J.F. (1958)

Kirk,B.S., Ziegler, W.T. (1965)

Sonntag,R.E. , Van Wylen,G.J., Crain, R. W. , Jr. (1964)

Cheung, H., Wang,D.I.-J. (1964)

Ruemann,R.M. , Fedoritenko,A. (1937)

Rodewal d,N.C. , Davis,J. A., Kurata,F. (1965)

Hensel ,W.E . ,Jr. , Massoth,F.E. (1964)

Michel s, A. ,Nederbragt,G. W. ( 1939)

Sonntag,R.E. , Crain, R. W. , Jr. , Streett,W.B. , ... (1964)

Cutler, A. J .B. , Morri son,J .A. (1965)

Hiza,M.J., Kidnay,A.J. (1966)

Torocheshnikov,N.S. (1937)

McTaggart,H.A. , Edwards, E. (1919)

Fastovskii ,V.G., Petrovskii ,Yu.V. (1957)

Nelson, E.E., Bonnell,W.S. (1943)

Muirbrook,N.K ., Prausnitz,J .M. (1965)

Shtekkel ,F.A. , Tsin,N.M. (1939)

Sinor,J.E., Schindler, D. L. , Kurata,F. (1966)

Ramsay, W. , Collie,J.N., Travers, M. (1895)

Lehigh, W.R., McKetta,J.J. (1966)

Duncan, A. G., Stavel ey ,L. A.K . (1966)

Charlesworth,P.L. , Ruhemann,M. (1965)

Hipkin,H. (1966)

Sprow,F.B., Prausnitz,J.M. (1966)

Kaminishi ,G. , Toriumi.T. (1966)

Matyash,I .V. , Mank,V.V., Starkov,M.G. (1966)

Schindler, D.L., Swift, G.W., Kurata,F. (1966)

Skripka, V. G. , Dykhno,N.M. (1964)

Sinor,J.E., Kurata,F. (1966)

Steinbach,H.-G. , Steinbrecher,M. (1966)

Khazanova,N.E. , Lesnevskaya,L.S. , Zakharova,... (1966)

Heck,C.K. , Hiza.M.J. (1967)

Hiza,M.J., Heck,C.K., Kidnay,A.J. (1968)

Fuks,S., Bellemans,A. (1967)

Jones, A. E., Kay,W.B. (1967)

Roof ,J .G . , Baron, J.D. (1967)

Greene, N.E., Sonntag,R.E. (1968)

Saddington,A.W. , Krase,N.W. (1934)

168
47558

47671

48068

49148

50157

50609

50610

50612

50699

50700

51011

51325

53074

53324

54087

54119

55395

59300

59455

60917

61574

61654

62117

62196

62447

62792

63416

63709

64158

64372

64378

64379

64484

64489

65038

66179

67016

67034

68441

69471

69667

69775

70002

70550

70826

70831

71134

71490

73928

73945

74084

75233

75234

75235

Donnelly, H. G. , Katz,D.L. (1954)

Kohn,J.P., Kurata,F. (1958)

Sage,B.H., Budenhol zer, R.A. , Lacey, W.N. (1940)

Rigby,M., Prausnitz,J .M. (1968)

Yorizane,M., Yoshimura,S. , Masuoka,H., Toyam. .. (1968)

Cohen, A. E., Hipkin,H.G., Koppany,C.R. (1967)

Chang, S.-D. , Lu,B.C.-Y. (1967)

Streett,W.B. (1967)

Spano,J.O., Heck,C.K., Barrick,P.L. (1968)

Gonzalez, M.H., Lee,A.L. (1968)

Hiza,M.J., Duncan, A. G. (1969)

Khazanova,N.E. , Lesnevskaya,L. S. (1967)

Neumann, A., Walch,W. (1968)

MacKendrick,R.F. , Heck,C.K., Barrick,P.L. (1968)

Cannon, W. A., Robson,J.H., English, W.D. (1968)

Sneed, C.M., Sonntag,R.E. , Van Wylen,G.J. (1968)

Yorizane,M., Sadamoto,S., Yoshimura,S. , Masu... (1968)

Banks, R., Hasel den,G .G. (1969)

Yesavage ,V.F. , Katz,D.L., Powers, J.E. (1969)

Robinson, D.B., Saxena,A.C. (1966)

Skripka, V.G., Barsuk,S.D., Nikitina, I. E., Gu... (1969)

Heck,C.K. ,Jr. (1968)

Saxena,A.C., Robinson, D.B. (1969)

Kami ni shi ,G. , Arai,Y., Saito,S., Maeda,S. (1968)

Kaminishi ,G. , Toriumi,T. (1968)

Liu,K.F. (1969)

Watanabe,K., Kuriki,M., Ogura,M., Saito,I. (1969)

Burfield,D.W., Richardson, H. P. , Guereca,R.A. (1970)

Yu,P. , El shayal ,1 .M. , Lu,B.C.-Y. (1969)

Djordjevich,L., Budenhol zer, R.A. (1970)

Wiese, H.C., Reamer, H.H., Sage,B.H. (1970)

Wiese, H.C., Jacobs,J., Sage,B.H. (1970)

Weiss, R.F. (1970)

O'Sullivan, T.D. , Smith, N.O. (1970)

Streett,W.B. , Hill.J.L.E. (1970)

Hakuta,T., Nagahama,K., Suda,S. (1969)

Yesavage, V.F., Katz,D.L., Powers, J.E. (1970)

Tully,P.C., DeVaney,W.E. , Rhodes, H.L. (1971)

Nikitina, I. E. , Skripka, V.G., Gubkina, G. F. , B... (1969)

Lu,B.C.-Y. , Yu ,P. , Poon,D.P.L. (1969)

Rhodes, H.L., DeVaney ,W.E. , Tully,P.C. (1971)

Trust, D.B., Kurata,F. (1971)

Nikitina, I. E., Skripka,V .G. , Gubkina, G. F. , S... (1970)

Foerg,W., Wirtz,P. (1970)

DeVaney, W.E., Rhodes, H. L®.

, Tully.P.C. (1971)

Weiss, R.F. (1971)

Rogers, B.L., Prausnitz,J .M. (1971)

Stoeckli ,H.F. , Staveley,L.A.K. (1970)

Trust, D.B., Kurata,F. (1971)

Hsi ,C. , Lu,B.C.-Y. (1971)

Wichterle,I. , Chappelear,P.S. , Kobayashi,R. (1971)

Wichterle,I ., Kobayashi,R. (1972)

Wichterle,I. , Kobayashi,R. (1972)

Wichterle,!., Kobayashi,R. (1972)

169
76312

76314

76499

76576

76577

79086

80644

82412

83757

83825

84578

84579

86467

87419

87420

87946

88244

88424

88684

88751

88753

88754

90120

90465

90466

90467

90468

91184

91294

91853

92174

94543

94700

94794

95426

97331

97332

98719

98955

98958

99626

99841

100275

101683

102912

102931

103328

103629

104717

104961

105282

105715

105717

106980

Tiwari,K.K., Robi nson,D.B . (1971)

Besserer,G.J . , Robinson, D.B. (1971)

Arai,Y., Kami nishi ,G. , Saito,S. (1971)

Yorizane,M., Yoshimura,S. , Masuoka,H. (1970)

Yorizane,M., Yoshimura,S. , Masuoka,H., Naka,T. (1971)

Zeininger,H. (1972)

Sarashina.E. , Arai,Y., $aito,S. (1971)

Chen,R„J .J. , Ruska,W.E.A. , Chappelear,P.S., ... (1973)

Miller, R.C., Kidnay,AoJ., Hiza.M.J. (1973)

Maslennikova, V .Ya. , Vdovina, N. A. , Tsi kl i s , D . S . (1971)

BarsukjS.D. , Skripka, V. G. , Benyami novich,0.A. (1970)

Skripka, V. G. , Nikitina, I .E. , Zhdanovich.L.A. . . . (1970)

Davydov, I. A. , Budnevich,S .S. (1971)

Besserer,G.J . , Robinson ,D.B. (1973)

Besserer,G.J . , Robinson, D.B. (1973)

Massoudi,R., King, A. D. , Jr. (1973)

Christiansen, L. J. , Fredenslund,A. , Mollerup,J. (1973)

Gugnoni ,R.J. , El dridge,J .W. , Okay ,V.G., Lee,... (1973)

Zeininger,H. (1973)

Christiansen, L. J. , Fredensl und, A. , Gardner, N. (1974)

Poon,D.P.L., Lu,B.C.-Y. (1974)

Wilson, G.M. (1975)

Yorizane,M. (1971)

Chen,R.J.J., Chappelear,P.S. , Kobayashi.R. (1974)

Chen,R.J.J., Chappel ear,P.S. , Kobayashi,R. (1974)

Kahre,L.C. (1974)

Elliot, D.G., Chen,R.J.J., Chappelear,P.S. , K... (1974)

Rhodes, H.L., Stroud, L., Tully,P.C. (1972)

Mul Holland, K.L. (1970)

Mi niovich,V.M. , Sorina,G.A. (1971)

Streett,W.B. , Erickson , A. L. (1972)

Crozier,T.E. , Yamamoto, S. (1974)

Sagara.H., Arai,Y., Saito,S. (1972)

Streett.W.B. , Erickson, A. L. , Hill ,J.L.E. (1972)

Streett s W.B . (1973)

Stryjek,R., Chappel ear, P .S. , Kobayashi,R. (1974)

Stryjek,R., Chappelear,P.S. , Kobayashi,R. (1974)

Hamam,S.E.M. , Lu,B.C.-Y. (1974)

Calado.J .C.G. , Garcia, G. A., Staveley ,L.A.K. (1974)

Fredenslund,A. , Mollerup,J. (1974)

Gugnoni ,R.J . , Eldridge,J.W., 0kay,V.C., Lee,... (1974)

Vejrosta,J., Wichterle,I. (1974)

Parrish, W.R. , Hiza,M.J. (1974)

Besserer,G.J . , Robinson, D. B. (1975)

Fredenslund,A. , Mollerup,J. (1975)

Kalra,H., Robinson, D.B. (1975)

Abrosimov, V. K. , Strakhov, A. N. , Krestov, G. A. (1974)

Kay,W.B., Hoffman, R.L. , Davies, 0. (1975)

Miller, R.C., Stavel ey ,L. A.K. (1976)

Kidnay,A.J., Miller, R.C., Parri sh,W.R. , Hiza... ( 1975)

Parrish, W. R. , Steward, W.G. (1975)

Hall,K.R., Eubank, P.T., Myerson,A.S. , Nixon,... ( 1975)

Klink,A.E., Cheh,H.Y., Amick,E.H. ,Jr. (1975)

Benson, B.B., Krause, D. , Jr. (1976)

170
107051 Chu,T.-C., Chen,R.J.J., Chappelear,P.S. , Kob... (1976)

107053 Davalos,J., Anderson, W. R. , Phelps, R.E., Kidn... (1976)

107564 Kulikov, N.E. (1969)

108433 Knapp, H., Schmoell ing,K. , Neumann, A. (1976)

108496 Miniovich,V.M. , Sorina,G.A. (1973)

108496 Miniovich,V.M. , Sorina,G.A. (1973)

108496 Mi niovich,V.M., Sorina,G.A. (1973)

110896 Hamam,S.E.M. , Lu,B.C.-Y. (1976)

110898 Kalra,H., Krishnan,T.R., Robinson, D.B. (1976)

111233 McClure, D.W., Lewis, K.L., Miller, R.C., Stave... (1976)

111245 Hamam,S.E.M. , Lu,B.C.-Y. (1976)

111705 Hwang, S.-C., Lin,H.-M., Chappel ear,P .S. , Kob... (1976)

112414 Khazanova,N.E., Sominskaya,E.E. , Zakharova, A. . . (1976)

114006 Miller, R.C., Kidnay,A.J., Hiza,M.J. (1977)

115116 Kalra,H., Robinson, D. B. , Besserer,G.J . (1977)

116899 Krishnan,T.R. , Kalra,H., Robinson, D.B. (1977)

117815 Hiza,M.J., Haynes, W.M. (1978)

118306 Grauso,L., Fredensl und,A. , Mollerup,J. (1977)

118307 0hgaki,K., Katayama,T. (1977)

119280 Robinson, D. B. , Kalra,H., Krishnan,T., Mirand... (1975)

120297 Tully ,P.C. , Stroud, L. (1976)

120924 Mraw,S.C., Hwang, S.-C., Kobayashi.R. (1978)

122297 Khazanova,N.E. , Sominskaya,E.E. , Rozovskii ,M.B. (1978)

123894 Somait,F.A., Kidnay,A.J. (1978)

123897 Kalra,H., Ng,H.-J., Miranda, R.D. , Robinson, D.B. (1978)

124829 Streett.W.B. , Calado,J .C.G. (1978)

125467 Dingrani ,J .G. , Thodos,G. (1978)

125573 Potter, R.W. ,11, Clynne,M.A. (1978)

131999 de Loos,T.W., Wijen,A.J.M, Diepen,G. A.M. (1980)

133074 Calado,J .C.G. , Gomes de Azevedo,E.J .S. , Soar... (1980)

150002 Clarke, E.C.W., Glew,D.N. (1971)

150012 Tsikl is,D.S. , Maslennikova, V.Ya. (1964)

150013 Tsiklis,D.S., Maslennikova, V.Ya. (1965)

150014 Cul berson,0.L. , McKetta,J .J . ,Jr. (1951)

150015 Culberson, 0. L. , McKetta,J .J . ,Jr. (1951)

150017 Eucken,A., Hertzberg,G. (1950)

150018 Bloomer, 0. T. , Garni, D.C., Parent, J.D. (1953)

150020 Wen,W.-Y. , Hung,J.H. (1970)

150021 Shoor,S.K., Walker, R. D. , Jr. , Gubbins,K.E. (1969)

150022 Enns,T., Scholander,P.F. , Bradstreet,E.D. (1965)

150023 Kresheck,G.C. , Schneider, H. , Scheraga,H.A. (1965)

150024 Ruetschi ,P. , Amlie,R.F. (1966)

150025 Benson, B.B., Parker, P.D.M. (1961)

150026 Roell ig,L.O., Giese,C. (1962)

150027 B1 ack ,C. , Joris,G.G., Taylor,H.S. (1948)

150028 Michels, A., Gerver,J., Bijl,A. (1936)

150029 McAul iffe,C . (1963)

150030 Kuenen,J.P., Robson, W.G. (1902)

150031 Wilcock,R.J . , Battino,R. (1974)

150032 von Antropoff,A. (1910)

150033 Maass,0., Mennie,J.H. (1926)

150034 Kunerth,W. (1922)

150035 Ben-Naim,A., Wilf,J., Yaacobi,M. (1973)

150036 Ben-Naim,A., Yaacobi,M. (1974)

171
150037 Feillolay.A., Lucas, M. (1972)

150038 Gardiner,G.E. , Smith, N.O. (1972)

150040 Robinson, D. B. , Bailey,J.A. (1957)

150041 Robinson, D. B. , Hughes, R.E., Sandercock,J.A.W. (1964)

150042 Robinson, D.B. , Lorenzo, A.P . , Macrygeorgos,C.A. (1959)

150043 Markham, A. E., Kobe, K. A. (1941)

150044 Wiebe.R., Gaddy ,V.L. (1940)

150045 Wi ebe,R. , Gaddy, V.L. (1939)

150046 Wiebe.R., Gaddy, V.L. (1934)

150047 Wiebe.R., Gaddy, V.L. (1935)

150048 Akerloef ,G. (1935)

150049 Friedman, H.L. (1954)

150050 Wetlaufer,D.B. , Malik, S.K., Stoller.L., Coff... (1964)

150051 Coan,C.R., King, A. D. ,Jr. (1971)

150052 Lannung.A. (1930)

150053 Wiebe.R., Gaddy, V.L., Heins, C.,Jr. (1933)

150054 Wiebe.R., Gaddy, V.L. (1941)

150055 Cl aussen.W.F . , Polgl ase.M.F. (1952)

150056 Grieves, R. B. , Thodos.G. (1963)

150057 Reamer, H.H., Olds.R.H., Sage.B.H., Lacey ,W.N. (1943)

150058 Jung.J., Knacke.O., Neuschuetz.D. (1971)

150059 Poettmann,F.H. , Katz,D.L. (1945)

150060 Dean,M.R., Tooke.J.W. (1946)

150061 Nysewander.C.N. , Sage.B.H., Lacey, W.N. (1940)

150062 Kay ,W.B. (1940)

150063 Sage.B.H., Lacey, W.N. (1940)

150064 Sage.B.H., Hicks, B.L., Lacey, W.N. (1940)

150065 Nederbragt.G. W. (1938)

150066 SagejB.H., Webster, D.C. , Lacey, W.N. (1936)

150067 Frol ich.P.K. , Tauch.E.J., Hogan, J.J., Peer, A. A. (1931)

150068 Rigas.T.J., Mason, D.F., Thodos.G. (1958)

150069 Vaughan, W.E., Collins, F.C. (1942)

150070 Olds.R.H., Sage.B.H., Lacey, W.N. (1942)

150071 Olds.R.H., Sage.B.H., Lacey.W.N. (1942)

150072 Sage.B.H., Reamer, H.H., Olds.R.H., Lacey, W.N. (1942)

150073 Olds.R.H., Reamer, H.H., Sage.B.H., Lacey, W.N. (1949)

150074 Goodman,J .B. , Krase.N .W. (1931)

150075 Akers, W.W., Attwell,L.L., Robinson.J .A. (1954)

150076 Wiebe.R. , Gaddy, V.L, Heins, C., Jr. (1932)

150077 Reamer, H.H., Sage.B.H. (1957)

150078 Partington, E.J . , Row! inson.J .S. , Weston, J.F. (1960)

150079 Connolly, J.F. (1962)

150080 Guter.M., Newitt.D.M., Ruhemann.M. (1940)

150081 Amick.E.H. ,Jr. , Johnson, W. B. , Dodge, B.F. (1952)

150082 Schroeder.W. (1973)

150083 Reamer, H.H., Sage.B.H., Lacey, W.N. (1950)

150084 Danneil.A., Toedheide,K. , Franck, E.U. (1967)

150085 Le Breton.J.G., McKetta.J.J. (1964)

150086 Kohn.J.P., Kurata.F. t 1959)

150087 Culberson.O.L. , McKetta.J .J . ,Jr. (1950)

150088 Culberson, 0. L. , Horn, A. B., McKetta.J .J . ,Jr. (1950)

150089 Cady ,H .P. , El sey ,H.M. , Berger, E.V. (1922)

150090 Pollitzer.F., Strebel ,E. (1924)

150091 Morrison, T.J . , Billett.F. (1952)

172
150092 Basset,J . , Dode,M. (1936)

150093 Reamer, H.H., Sage,B.H., Lacey, W.N. (1953)

150095 Burriss,W.L. , Hsu,N.T., Reamer,H.H., $age,B.H. (1953)

150096 Kay ,W.B . , Brice, D.B. (1953)

150097 Pray, H. A., Schweickert,C.E. , Minnich,B.H. (1952)

150098 Reamer, H.H., Sage,B.H., Lacey, W.N. (1951)

150099 Reamer, H.H., Sage,B.H., Lacey, W.N. (1951)

150100 Toedheide,K. , Franck, E.U. (1963)

150101 Vilcu,R. , Gainar,I. (1967)

150102 Hirata,M., Suda,S., Hakuta,T., Nagahama,K. (1969)

150103 Hirata,M., Suda,S., Miyashita,R., Hoshino,T. (1970)

150104 Besserer,G.J . , Robinson, D. B. (1975)

150105 Gilliland, E.R., Scheel ine,H.W. (1940)

150106 Bartholomew. , Friz,H. (1956)

150107 Azarnoosh,A., McKetta,J.J. (1958)

150108 Brooks, W.B., Gibbs, G.B., McKetta,J.J. (1951)

150109 Mills,J.R., Miller, F.J.L. (1945)

150110 Poettmann,F.H. , Dean,M.R. (1946)

150111 Bohr,C. (1899)

150114 Morrison, T.J ., Johnstone, N.B. (1954)

150115 Kuenen,J.P. (1897)

150116 Price, A. R. , Kobayashi ,R. (1959)

150117 Sander, W. (1912)

150118 Clever, H.L., Battino,R., Saylor,J.H., Gross,... (1957)

150119 Reamer, H.H., Sage,B.H., Lacey, W.N. (1960)

150120 Yeh,S.-Y., Peterson, R. E . (1964)

150121 Winkler, L.W. (1891)

150122 Fuehner,H. (1924)

150123 Kritschewsky,I.R. , Shaworonkoff ,N.M. , Aepelb... (1936)

150124 Franck,E.U., Toedheide,K. (1959)

150125 Winkler, L.W. (1901)

150126 Winkler, L.W. (1891)

150127 Winkler, L.W. (1892)

150128 Matous,J., Sobr,J., Novak ,J.P., Pick,J. (1969)

150129 Farhi,L.E., Edwards, A. W. T. , Homma,T. (1963)

150130 Lannung,A., Gjaldbaek,J.C. (1960)

150131 Gjaldbaek,J .C., Niemann, H. (1958)

150132 Haufe,S. (1966)

150133 Christoff, A. (1906)

150134 Estreicher,T. (1899)

150135 Ipatiew,W.W., Drushina-Artemowitsch,S.I . , Ti... (1932)

150136 Ahland,E. (1966)

150137 Miksovsky,J . , Wichterle,I. ( 1975)

150138 Lu,B.C.-Y. , Chang, S.-D., El shayal ,1 .M. , Yu,P... (1969)

150139 Miksovsky,J . , Wichterle,I. (1975)

150140 Taylor, H.S., Wald,G.W., Sage,B.H., Lacey, W.N. (1939)

150141 Hi rata, M., Suda,S., Hakuta,T., Nagahama,K. (1969)

150142 Hi rata,M. , Suda,S. (1968)

150143 Duffy,J.R., Smith, N.O., Nagy,B. (1961)

150144 Smith, N.O., Kelemen,S., Nagy,B. (1962)

150146 Sul tanov,R.G. , Skripka, V .G. , Namiot,A.Yu. (1972)

150147 Maslennikova,Y.Ya., Goryunova, N. P. , Subbotin... (1976)

150148 Ipatev, V., Teodorovich, V.P. (1934)

150150 Adeney ,W.E. , Becker, H.G. (1919)

173
150151 Fedoritenko,A. , Ruhemann,M. (1937)

150152 Meadows, R.W., Spedding,D.J . (1974)

150154 Nosov, E.F., Bar1yaev,E.V. (1968)

150155 Ellis, A.J., Golding, R.M. (1963)

150156 El 1 i s,A.J . (1959)

150157 Takenouchi ,S. , Kennedy ,G.C. (1964)

150159 Klausutis,N. (1968)

150160 Li abastre,A.A. (1974)

150161 Namiot, A. Yu. , Beider, S.Ya. (1960)

150162 Ryabtsev,N. I . , Khuchua,R.S. (1970)

150163 Sul tanov,R.G. , Skripka, V. G. , Namiot, A. Yu. (1971)

150164 Sul tanov,R.G. , Skri pka,V .G. , Namiot,A.Yu. (1972)

150165 Malinin,S.D. (1959)

150166 Nezdoiminoga,N.A. (1968)

150167 Malinin, S. D. , Saveleva,N.I. (1972)

150168 Khitarov,N.I., Malinin, S.D. (1958)

150169 Kazaryan,T.S. , Ryabtsev,N.I . (1969)

150170 Abou El-Nour,F., Harting,P., Schuetze,H. (1977)

150171 Bi erl ein,«J .A. , Kay,W.B. (1953)

150172 de Wet.W.J. (1964)

150173 Fischer,F., Zerbe,C. (1923)

150174 Fox,C.J.J. (1909)

150175 Gonikberg,M.G. , Fastowsky ,W.G. (1940)

150176 Loprest,F.J. (1957)

150177 Makranczy,J . , Megyery-Bal og,K. , Rusz,L., Pat...

150178 Murray, C.N., Riley,J.P., Wil son,T.R.S. (1969)

150179 Murray ,C.N., Riley ,J.P. (1971)

150180 Paratella,A., Sagramora,G. (1959)

150181 Robinson, D.B. , Kalra,H. (1974)

150182 Rutherford,W.M. (1962)

150183 Schroeder,W. (1969)

150184 Steckel ,F. (1945)

150186 Weiss, R.F. (1974)

150187 Khitarov,N.I . , Mai Inin, S.D. (1956)

150188 Stewart, P.B., Munjal,P.K. (1969)

150189 Suciu,S. , Sibbitt,W.L. (1951)

150190 Barsuk,S.D., Benyaminovich,0.A. (1975)

150191 Khodeeva,S.M. (1966)

150192 Ermolaev, M. I . , Kapi tanov,V .F. , Nesterova, A. K. .

.

150193 Haehnel ,0. (1920)

150194 Malinin, S.D. (1971)

150195 Hachmu th,K.H. (1932)

150196 Barton,J .R. , Hsu,C.C. (1971)

150197 Besserer,G.J . , Robinson, D.B. (1973)

150198 Brandt, L.W., Stroud, L. (1958)

150199 Brewer ,J., Rodewald,N., Kurata,F. (1961)

150200 Connolly ,J.F. (1966)

150201 Davi s,J.E. , McK@tta,J.J. (1960)

150202 Hayduk ,W. , Malik, V.K. (1971)

150203 Kay.W.B. (1970)

150204 Martinez-Ortiz,J.A. , Manley, D.B. (1978)

150205 McCormick, R. H. , Walsh, W.H., Hetrick ,S.S. , Zu...

150206 Mehra,V.S. , Thodos,G. (1965)

150207 Reed,C.D. , McKetta,J.J. (1959)

(1976)

(1971)

(1963)

174
150208 Rice, P. A., Gale,R.P., Barduhn,A.J. (1976)

150209 Roberts, L.R., McKetta,J.J. (1961)

150210 Stewart, P.B., Munjal.P. (1970)

150211 Verschaffel t,J. (1898)

150212 Verschaffel t,J . (1899)

150213 Yamamoto, S., A1 causkas,J .B. , Crozier,T.E. (1976)

150214 Yen,L.C. , McKetta,J .J . ,Jr. (1962)

150215 Menra,V.S. , Thodos,G. (1963)

150220 Hiza,M.J . (1981)

150221 Tsang,C.Y. , Streett.W.B. (1981)

150222 Wright, R.H., Maass,0. (1932)

150223 Forman,J.C., Thodos,G. (1962)

150224 Boone, W.J., Jr., De Vaney,W.E., Miller, J.E. (1962)

150225 De Vaney,W.E., Stroud. ,L., Boone, W.J ., Jr. (1964)

150229 Stephan, E. F. , Hatfiel d,N.S. , Peopl es,R.S. , P... (1956)

150232 Douabul ,A.A. , Riley ,J.P. (1979)

150233 Billman,G.W. , Sage,B.H., Lacey, W.N. (1948)

150234 Gregory ,D.P. , Djordjevich,L. , Kao,R., Anders... (1973)

150236 Tsang,C.Y., Clancy, P., Cal ado,J .C .G. , Street... (1980)

150237 Kosyakov, N.E. , Ryabinkin.V .V. , Chobotko,L.L. (1978)

150239 Etter,D .0. , Kay,W.B. (1961)

150241 Luker,J.A., Gniewek,T., Johnson, C. A. (1958)

150242 Rigas,T.J., Mason, D.F., Thodos,G. (1959)

150244 Dourson,R.H. , Sage,B.H., Lacey, W.N. (1943)

150246 Andrews, T. (1887)

150247 Stutzman,L.F. , Brown, G.M. (1949)

150248 DePriester,C.L. (1953)

150250 Selleck,F.T. , Carmichael ,L.T. , Sage,B.H. (1952)

150251 Hanson, G.H., Brown, G.G. (1945)

150255 Sanchez, M., Coll.R. (1978)

150257 Behnke, A. R. , Yarbrough,O.D. (1938)

150258 Maslennikova, V.Ya. (1971)

150259 Maslennikova, V. Ya. , Vdovi na,N.A. , Tsikl is,D.S. (1971)

150260 Kay ,W.B. , Rambosek ,G.M. (1953)

150261 Nikitina, I. E. , Zhdanovich,L . A. , Si roti n,A.G. . . . (1972)

150262 Seward, T. M. , Franck, E.U. (1981)

150264 Yorizane.M., Yoshimura,S . , Masuoka,H. (1972)

150266 Yokoyama,K. , Ohe,S. (1971)

150268 Mathot.Y. (1955)

150269 Zel venskii ,Ya.D. (1937)

150270 Krichevski i ,1 .R. , Khazanova,N.E. , Lesnevskay. .. (1962)

150271 Carter, R.T., Sage,B.H., Lacey, W.N. (1941)

150273 Lee.J.I. , Mather, A. E. (1977)

150275 Kalaida,Yu.A., Katkov, Yu. D. , Kuznetsov, V. A.,... (1980)

150276 Kozintseva, T.N. (1965)

150278 McClain, R.A.K.W. (1977)

150279 A1 tunin,V.V. , Gvozdkov,A.V. , Sosi novski i ,V.K. (1974)

150280 Granzhan.V.A. (1974)

150281 Torocheshnikov,N.S. , Semenova, V. A. (1954)

150282 Namiot,A.Yu. , Bondareva, M.M. (1962)

150283 Toriumi,T., Kaminishi,G. (1968)

150361 Beuschl ei n,W.L. , Simenson,L.O. (1940)

150362 Calingaert,G. , Hi tchcock ,L.B. (1927)

150363 Campbell ,W.B. , Maass,0. (1930)

175
150364 Cook ,D. (1953)

150369 Ekiner,0., Thodos,G. (1966)

150370 Herl ihy ,J .C. , Thodos,G. ( 1962)

150371 Raoe, A.E . , Harris, J.F. (1963)

150373 Besserer,G.J . , Robinson, D.B. (1975)

150374 Miranda, R. D. , Robinson, D. B. , Kalra,H. (1976)

150375 Polak,J. , Lu,B.C.-Y. (1975)

150377 Davis, J. A., Rodewald,N., Kurata,F. (1962)

150378 Kay ,W.B. , Fi sch ,H.A. (1958)

150382 Spall, B.C. (1963)

150384 Morgan, O.M., Maass,0. (1931)

150386 Jones, M.E. (1963)

150387 Johnstone, H. F. , Leppla,P.W. (1934)

150389 Wiebe,R., Tremearne,T.H. (1934)

150390 Wiebe,R. , Tremearne,T. H. (1933)

150391 Wiebe.R. , Gaddy, V.L. (1937)

150505 Tsang,C.Y. , Streett.W.B. (1981)

150506 Lhotak,V., Wichterle,I. (1981)

150507 Beranek,P., Wichterle,I. (1981)

150508 Neuhausen,B„ S. , Patrick, W. A. (1921)

150509 Wells, F.L., MacCl aren,R.H. (1955)

150510 Vosolsobe,J . , Simecek,A., Michalek,J., Kadle...

150511 Borgstedt,H.H. , Gillies, A. J. (1965)

150512 Kuenen,J.P. (1897)

150513 Roberts, 0. L. , Brownscombe,E .R. , Howe,L.$., R. .

.

150514 Krichevski i

, I .R. , Khazanova,N.E. (1939)

150515 Levitskaya, E. , Pryannikov,K. (1939)

150516 Vel ikovski i ,A.S. , Stepanova., G. S. , Vybornova, . .

.

150517 Krasheninnikov,S.A. , Gol ubev,S.S. , Sabaev,I.Ya.

150518 Gi nzburg,D.M. , Pikul ina,N.S., Litvin, V.P. (1966)

150519 Wucherer,J. (1932)

150520 Krichevsky,I. , Ziclis,D. (1943)

150521 Kritschewsky ,1., Bolshakov, P. (1941)

150522 Robinson, D.B. , Besserer,G .J . (1972)

150523 Rigas,T.J., Mason, D.F., Thodos,G. (1958)

150524 Glowka.S. (1972)

150525 Wehe, A.H. , McKetta,J.J. (1961)

150526 Kueffer,A. (1962)

150527 Wiebe,R., Gaddy ,V.L., Heins, C.,Jr. ( 1932)

150528 Dvorak, K., Boublik,T. (1963)

150529 Sel leck,F.T. , Reamer, H.H., Sage,B.H. (1953)

150530 Kobayashi ,R. , Katz,D. L. (1953)

150531 Reamer, H.H., Sage,B.H., Lacey, W.N. (1952)

150532 Stone, H.W. (1943)

150533 Sage,B.H., Backus, H.S., Vermeulen,T. (1936)

150534 Lindroos,A.E., Dodge, B.F. (1952)

150535 Hudson, J.C. (1926)

150536 Wilson, T. A. (1925)

150537 Boexkes,W., Emig,G. (1969)

150538 Mittasch,A., Kuss,E., Schlueter,H. (1926)

150539 Wrewsky ,M. (1924)

150540 Kuenen,J.P. (1897)

150541 Caubet.F. (1904)

150542 Cl i fford,I .L. , Hunter, E. (1933)

(1965)

(1941)

(1964)

(1960)

176
150543 Reamer, H.H., Sage,B.H. (1959)

150544 Reamer, H.H., Sage,B.H. (1959)

150545 Reamer, H.H., 01ds,R.H., Sage,B.H., Lacey, W.

150546 Dean,M.R. , Walls,W.S. (1947)

150547 Dornte,R.W., Ferguson, C.V. (1939)

. (1944)

177
NBS-1HA (REV. 2-80

U.s. DEPT. OF COMM.

BIBLIOGRAPHIC DATA

SHEET (See instructions)

1. PUBLICATION OR

REPORT NO.

NBSIR 83-1692

2. Performing Organ. Report No 3. Publication Date June 1983

4. TITLE AND SUBTITLE

Compilation and Evaluation of Available Data on Phase Equilibria of Natural and

Synthetic Gas Mixtures

5. AUTHOR(S)

F. R. Williamson and N. A. Olien

6. PERFORMING ORGANIZATION (If joint or other than NBS, see instructions) 7. Contract/Grant No. NATIONAL BUREAU OF STANDARDS

DEPARTMENT OF COMMERCE

WASHINGTON, D.C. 20234

8. Type of Report & Period Covered

9. SPONSORING ORGANIZATION NAME AND COMPLETE ADDRESS (Street. City. State, ZIP)

Gas Research Institute

8600 West Bryn Mawr Avenue

Chicago, IL 60631

10. SUPPLEMENTARY NOTES

Document describes a computer program; SF-185, FIPS Software Summary, is attached.

11. ABSTRACT (A 200-word or less factual summary of most sign ifi cant information. If document includes a significant

bibliography or literature survey, mention it here)

This report summarizes the results of a two-year effort to identify, compile,

and evaluate the data available in the open literature for the liquid-vapor

equilibria for binary and multicomponent mixtures of He, H2 , Ci - C 5 alkanes,

N2

, CO, C02 , NH 3

, H2 S, H2 0, CS 2 , COS, HCN, N0x and S0X . There were 276 binary

systems relevant to the gas industry. The result of the evaluation is that

there are: 46 systems for which data are imperative and 104 systems for which

data are needed but not imperative. The report lists the data needs in temperature and pressure range for each system for both Priority 1 and 2. The report

includes three appendices: A - a listing of the ranges and quality of all

available data for binary systems; B - the same for all multicomponent systems;

and C - a complete bibliography of the 543 citations identified in the project.

12. KEY WORDS (Six to twelve entries; alphabetical order; capitalize only proper names; and separate key words by semicolons)

bibliography; compilation; evaluation; liquid-vapor equilibrium; natural gas; phase

equilibrium; synthetic natural gas.

13. AVAILABILITY 14. NO. OF

PRINTED PAGES

[Xfj Unlimited

| | For Official Distribution. Do Not Release to NTIS 181

~| Order From Superintendent of Documents, U.S. Government Printing Office, Washington, D.C. 20402. 15. Price

(X[j Order From National Technical Information Service (NTIS), Springfield, VA. 22161 $17.50

USCOMM-DC 6 C 4 3-P 8 0

*U.S. GOVERNMENT PRINTING OFFICE:1983—679-781 / 332