Propane
- Formula: C3H8
- Molecular weight: 44.0956
- IUPAC Standard InChI: InChI=1S/C3H8/c1-3-2/h3H2,1-2H3
- IUPAC Standard InChIKey: ATUOYWHBWRKTHZ-UHFFFAOYSA-N
- CAS Registry Number: 74-98-6
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
View 3d structure (requires JavaScript / HTML 5) - Isotopologues:
- Other names: n-Propane; Dimethylmethane; Freon 290; Liquefied petroleum gas; LPG; Propyl hydride; R 290; C3H8; UN 1978; A-108; Hydrocarbon propellant A-108; HC 290
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
- NIST / TRC Web Thermo Tables, "lite" edition (thermophysical and thermochemical data)
- NIST / TRC Web Thermo Tables, professional edition (thermophysical and thermochemical data)
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Critical temperature
Go To: Top, References, Notes
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 ± 0.1 | Ambrose and Tsonopoulos, 1995 | |
| 369.77 | Holcomb, Magee, et al., 1995 | Uncertainty assigned by TRC = 0.2 K; TRC |
| 364.59 | Ohgaki, Umezono, et al., 1990 | Uncertainty assigned by TRC = 0.15 K; TRC; Data excluded from overall average |
| 369.83 | Sychev, Vasserman, et al., 1989 | Uncertainty assigned by TRC = 0.1 K; TRC |
| 369.82 | Teja, Lee, et al., 1989 | TRC |
| 369.91 | Brunner, 1988 | Uncertainty assigned by TRC = 0.1 K; Visual, optical cell 30cm high. TE cal. vs PRT; TRC |
| 369.85 | Younglove and Ely, 1987 | Uncertainty assigned by TRC = 0.07 K; TRC |
| 369.98 | Brunner, 1985 | Uncertainty assigned by TRC = 0.05 K; TRC |
| 369.8 | Majer and Svoboda, 1985 | |
| 370.00 | Barber, Kay, et al., 1982 | Uncertainty assigned by TRC = 0.2 K; TRC |
| 369.85 | Goodwin and Haynes, 1982 | TRC |
| 369.85 | Thomas and Harrison, 1982 | Uncertainty assigned by TRC = 0.1 K; TRC |
| 369.8 | Kratzke, 1980 | Uncertainty assigned by TRC = 0.0037 K; TRC |
| 369.8 | Goodwin, 1977 | TRC |
| 369.74 | Mousa, 1977 | Uncertainty assigned by TRC = 0.2 K; TRC |
| 369.76 | Kay and Young, 1974 | Uncertainty assigned by TRC = 0.1 K; TRC |
| 369.76 | Kay and Young, 1974, 2 | Uncertainty assigned by TRC = 0.1 K; TRC |
| 369.8 | Kay and Young, 1974, 3 | Uncertainty assigned by TRC = 0.15 K; TRC |
| 369.75 | Kay and Young, 1974, 4 | Uncertainty assigned by TRC = 0.15 K; TRC |
| 369.75 | Kay and Young, 1974, 5 | Uncertainty assigned by TRC = 0.15 K; TRC |
| 369.75 | Kay and Young, 1974, 6 | Uncertainty assigned by TRC = 0.15 K; TRC |
| 369.74 | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.2 K; TRC |
| 370.02 | Kreglewski and Kay, 1969 | Uncertainty assigned by TRC = 0.2 K; TRC |
| 370.0 | Kay, 1964 | Uncertainty assigned by TRC = 0.4 K; TRC |
| 369.9 | Kreglewski, 1957 | Uncertainty assigned by TRC = 0.4 K; TRC |
| 369.81 | Clegg and Rowlinson, 1955 | Uncertainty assigned by TRC = 0.06 K; TRC |
| 369.81 | Kay and Rambosek, 1953 | Uncertainty assigned by TRC = 0.22 K; TRC |
| 370.45 | Kreglewski, 1953 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
| 370.2 | Ipatieff and Monroe, 1942 | Uncertainty assigned by TRC = 1. K; TRC |
| 372. | Scheeline and Gilliland, 1939 | Uncertainty assigned by TRC = 2.22 K; TRC; Data excluded from overall average |
| 369.96 | Beattie, Poffenberger, et al., 1935 | Uncertainty assigned by TRC = 0.05 K; TRC |
| 373.3 | Sage, Schaafsma, et al., 1934 | Uncertainty assigned by TRC = 0.55 K; TRC; Data excluded from overall average |
| 367.8 | Maass and Wright, 1921 | Uncertainty assigned by TRC = 0.6 K; TRC; Data excluded from overall average |
| 370.7 | Lebeau, 1905 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
| 370.15 | Kuenen, 1903 | Uncertainty assigned by TRC = 1. K; TRC |
| 370. | Olszewski, 1895 | Uncertainty assigned by TRC = 3. K; TRC |
| 375. | Hainlen, 1894 | Uncertainty assigned by TRC = 5. K; TRC; Data excluded from overall average |
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-ρ-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
Go To: Top, Critical temperature, References
- Symbols used in this document:
Tc Critical temperature - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.