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Propane

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Critical temperature

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny, director

Tc (K) Reference Comment
369.8 ± 0.1Ambrose and Tsonopoulos, 1995 
369.77Holcomb, Magee, et al., 1995Uncertainty assigned by TRC = 0.2 K; TRC
364.59Ohgaki, Umezono, et al., 1990Uncertainty assigned by TRC = 0.15 K; TRC; Data excluded from overall average
369.83Sychev, Vasserman, et al., 1989Uncertainty assigned by TRC = 0.1 K; TRC
369.82Teja, Lee, et al., 1989TRC
369.91Brunner, 1988Uncertainty assigned by TRC = 0.1 K; Visual, optical cell 30cm high. TE cal. vs PRT; TRC
369.85Younglove and Ely, 1987Uncertainty assigned by TRC = 0.07 K; TRC
369.98Brunner, 1985Uncertainty assigned by TRC = 0.05 K; TRC
369.8Majer and Svoboda, 1985 
370.00Barber, Kay, et al., 1982Uncertainty assigned by TRC = 0.2 K; TRC
369.85Goodwin and Haynes, 1982TRC
369.85Thomas and Harrison, 1982Uncertainty assigned by TRC = 0.1 K; TRC
369.8Kratzke, 1980Uncertainty assigned by TRC = 0.0037 K; TRC
369.8Goodwin, 1977TRC
369.74Mousa, 1977Uncertainty assigned by TRC = 0.2 K; TRC
369.76Kay and Young, 1974Uncertainty assigned by TRC = 0.1 K; TRC
369.76Kay and Young, 1974, 2Uncertainty assigned by TRC = 0.1 K; TRC
369.8Kay and Young, 1974, 3Uncertainty assigned by TRC = 0.15 K; TRC
369.75Kay and Young, 1974, 4Uncertainty assigned by TRC = 0.15 K; TRC
369.75Kay and Young, 1974, 5Uncertainty assigned by TRC = 0.15 K; TRC
369.75Kay and Young, 1974, 6Uncertainty assigned by TRC = 0.15 K; TRC
369.74Mousa, Kay, et al., 1972Uncertainty assigned by TRC = 0.2 K; TRC
370.02Kreglewski and Kay, 1969Uncertainty assigned by TRC = 0.2 K; TRC
370.0Kay, 1964Uncertainty assigned by TRC = 0.4 K; TRC
369.9Kreglewski, 1957Uncertainty assigned by TRC = 0.4 K; TRC
369.81Clegg and Rowlinson, 1955Uncertainty assigned by TRC = 0.06 K; TRC
369.81Kay and Rambosek, 1953Uncertainty assigned by TRC = 0.22 K; TRC
370.45Kreglewski, 1953Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
370.2Ipatieff and Monroe, 1942Uncertainty assigned by TRC = 1. K; TRC
372.Scheeline and Gilliland, 1939Uncertainty assigned by TRC = 2.22 K; TRC; Data excluded from overall average
369.96Beattie, Poffenberger, et al., 1935Uncertainty assigned by TRC = 0.05 K; TRC
373.3Sage, Schaafsma, et al., 1934Uncertainty assigned by TRC = 0.55 K; TRC; Data excluded from overall average
367.8Maass and Wright, 1921Uncertainty assigned by TRC = 0.6 K; TRC; Data excluded from overall average
370.7Lebeau, 1905Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
370.15Kuenen, 1903Uncertainty assigned by TRC = 1. K; TRC
370.Olszewski, 1895Uncertainty assigned by TRC = 3. K; TRC
375.Hainlen, 1894Uncertainty assigned by TRC = 5. K; TRC; Data excluded from overall average

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


References

Go To: Top, Critical temperature, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Ambrose and Tsonopoulos, 1995
Ambrose, D.; Tsonopoulos, C., Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkenes, J. Chem. Eng. Data, 1995, 40, 531-546. [all data]

Holcomb, Magee, et al., 1995
Holcomb, C.D.; Magee, J.W.; Haynes, W.M., Density Measurements on Natural Gas Liquids, Research Report RR-147, Gas Processors Association Project 916, 1995. [all data]

Ohgaki, Umezono, et al., 1990
Ohgaki, K.; Umezono, S.; Katayama, T., Pressure-density-temperature (p-«rho»-T) relations of fluoroform, nitrous oxide, and propene in the critical region, J. Supercrit. Fluids, 1990, 3, 78-84. [all data]

Sychev, Vasserman, et al., 1989
Sychev, V.V.; Vasserman, A.A.; Kozlov, A.D.; Tsymarny, V.A., Thermodynamic Properties of Propane, Standards Publishing House, 1989. [all data]

Teja, Lee, et al., 1989
Teja, A.S.; Lee, R.J.; Rosenthal, D.J.; Anselme, M.J., Correlation of the Critical Properties of Alkanes and Alkanols in 5th IUPAC Conference on Alkanes and AlkanolsGradisca, 1989. [all data]

Brunner, 1988
Brunner, E., Fluid Mixtures at High Pressures VI. Phase Separation and Critical Phenomena in 18 (n-Alkane + Ammonia) and 4 (n-Alkane _ Methanol) Mixtures, J. Chem. Thermodyn., 1988, 20, 273. [all data]

Younglove and Ely, 1987
Younglove, B.A.; Ely, J.F., Thermophysical Properties of Fluids II. Methane, Ethane, Propane, Isobutane, and Normal Butane, J. Phys. Chem. Ref. Data, 1987, 16, 577. [all data]

Brunner, 1985
Brunner, E., Fluid mixtures at high pressures II. Phase separation and critical phenomena of (ethane + an n-alkanol) and of (ethene + methanol) and (propane + methanol), J. Chem. Thermodyn., 1985, 17, 871. [all data]

Majer and Svoboda, 1985
Majer, V.; Svoboda, V., Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]

Barber, Kay, et al., 1982
Barber, J.R.; Kay, W.B.; Teja, A.S., A study of the volumetric and phase behavior of binary systems: part I. critical properties of propane + perfluorocyclobutane mixtures., AIChE J., 1982, 28, 134-8. [all data]

Goodwin and Haynes, 1982
Goodwin, R.D.; Haynes, W.M., Thermophysical Properties of Propane from 85 to 700 K at Pressures to 70 MPa, NBS Monogr. (U. S.) No. 170, 249 pp., 1982. [all data]

Thomas and Harrison, 1982
Thomas, R.H.P.; Harrison, R.H., Pressure-Volume-Temperature Relations of Propane, J. Chem. Eng. Data, 1982, 27, 1-11. [all data]

Kratzke, 1980
Kratzke, H., Thermodynamic quantities for propane. 1. The vapour pressure of liquid propane, J. Chem. Thermodyn., 1980, 12, 305-9. [all data]

Goodwin, 1977
Goodwin, R.D., , Natl. Bur. Stand., [Tech. Rep.] NBSIR (U. S.) 77-860, 1977. [all data]

Mousa, 1977
Mousa, A.H.N., The Physical properties of highly purified purified samnples of propane and n-hexane, J. Chem. Thermodyn., 1977, 9, 1063-5. [all data]

Kay and Young, 1974
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 2, 154. [all data]

Kay and Young, 1974, 2
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 2, 156. [all data]

Kay and Young, 1974, 3
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 2, 158. [all data]

Kay and Young, 1974, 4
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 3, 192. [all data]

Kay and Young, 1974, 5
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 3, 194. [all data]

Kay and Young, 1974, 6
Kay, W.B.; Young, C.L., Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1974, No. 3, 196. [all data]

Mousa, Kay, et al., 1972
Mousa, A.H.N.; Kay, W.B.; Kreglewski, A., The critical constants of binary mixtures of certain perfluoro-compounds with alkanes, J. Chem. Thermodyn., 1972, 4, 301-11. [all data]

Kreglewski and Kay, 1969
Kreglewski, A.; Kay, W.B., The Critical Constants of Conformal Mixtures, J. Phys. Chem., 1969, 73, 3359. [all data]

Kay, 1964
Kay, W.B., P-T-x Diagrams in the Critical Region. Acetone-n-Alkane Systems, J. Phys. Chem., 1964, 68, 827-31. [all data]

Kreglewski, 1957
Kreglewski, A., The Critical Temperature Curves of Mixtures I. The Azeotropic Range Range, Bull. Acad. Pol. Sci., Cl. 3, 1957, 5, 323-7. [all data]

Clegg and Rowlinson, 1955
Clegg, H.P.; Rowlinson, J.S., Physical Properties of Some Fluorine Compounds and Their Solutions II. Part 2. The System Sulfur Hexafluoride + Propane, Trans. Faraday Soc., 1955, 51, 1333-40. [all data]

Kay and Rambosek, 1953
Kay, W.B.; Rambosek, G.M., Liquid-Vapor Equilibrium Relations in Binary Systems. Propane-Hydrogen Sulfide Systems, Ind. Eng. Chem., 1953, 45, 221-6. [all data]

Kreglewski, 1953
Kreglewski, A., The Pre- and Post-critical Region of One-component Systems VI. Isotherms and Isochores of Propane, Rocz. Chem., 1953, 27, 125-33. [all data]

Ipatieff and Monroe, 1942
Ipatieff, V.N.; Monroe, G.S., Determination of Critical Temperatures by the Rotating Bomb, Ind. Eng. Chem., Anal. Ed., 1942, 14, 171-4. [all data]

Scheeline and Gilliland, 1939
Scheeline, H.W.; Gilliland, E.R., Vapor-Liquid Equilibrium in the System Propane-Isobutylene, Ind. Eng. Chem., 1939, 31, 1050. [all data]

Beattie, Poffenberger, et al., 1935
Beattie, J.A.; Poffenberger, N.; Hadlock, C., The Critical Constants of Propane, J. Chem. Phys., 1935, 3, 96. [all data]

Sage, Schaafsma, et al., 1934
Sage, B.H.; Schaafsma, J.G.; Lacey, W.N., Phase Equilibria in Hydrocarbon Systems: Pressure-Volume-Temperature Relations and Thermal Properties of Propane, Ind. Eng. Chem., 1934, 26, 1218-24. [all data]

Maass and Wright, 1921
Maass, O.; Wright, C.H., SOME PHYSICAL PROPERTIES OF HYDROCARBONS CONTAINING TWO AND THREE CARBON ATOMS., J. Am. Chem. Soc., 1921, 43, 5, 1098-1111, https://doi.org/10.1021/ja01438a013 . [all data]

Lebeau, 1905
Lebeau, P., Bull. Soc. Chim. Fr., 1905, 33, 1137. [all data]

Kuenen, 1903
Kuenen, J.P., On the Mutual Solubility of Liquids, Philos. Mag., 1903, 6, 637. [all data]

Olszewski, 1895
Olszewski, K., On the liquefaction of gases, Philos. Mag., 1895, 39, 188. [all data]

Hainlen, 1894
Hainlen, A., Propane and Ethane in the Liquid State., Justus Liebigs Ann. Chem., 1894, 282, 229-45. [all data]


Notes

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