Propene
- Formula: C3H6
- Molecular weight: 42.0797
- IUPAC Standard InChIKey: QQONPFPTGQHPMA-UHFFFAOYSA-N
- CAS Registry Number: 115-07-1
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Isotopologues:
- Other names: Propylene; 1-Propene; Methylethylene; 1-Propylene; CH3CH=CH2; Methylethene; NCI-C50077; UN 1077; R 1270
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Condensed phase thermochemistry data
Go To: Top, Phase change data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 195.7 | J/mol*K | N/A | Chao, Hall, et al., 1983 |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
102. | 298.15 | Chao, Hall, et al., 1983 | T = 14 to 340 K. |
98.9 | 300. | Auerbach, Sage, et al., 1950 | T = 300 to 344 K. Datum at 80°C is Cp at the bubble point, 0.5615 Btu/lb*R. |
92.09 | 230. | Powell and Giauque, 1939 | T = 14 to 225 K. |
90.0 | 210.3 | Huffman, Parks, et al., 1931 | T = 69 to 210 K. Value is unsmoothed experimental datum. |
Phase change data
Go To: Top, Condensed phase thermochemistry data, 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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 225.6 ± 0.6 | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 88.0 | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 0.3 K; TRC |
Tfus | 87.9 | K | N/A | Haselden and Snowden, 1962 | Uncertainty assigned by TRC = 0.4 K; TRC |
Tfus | 88.25 | K | N/A | Parks and Huffman, 1931 | Uncertainty assigned by TRC = 1. K; TRC |
Tfus | 87.95 | K | N/A | Coffin and Maass, 1927 | Uncertainty assigned by TRC = 0.6 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 87.8 ± 0.8 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 9.50 | bar | N/A | Angus, Armstrong, et al., 1980 | Uncertainty assigned by TRC = 0.15 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 365.2 ± 0.8 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 46.0 ± 0.3 | bar | N/A | Tsonopoulos and Ambrose, 1996 | |
Pc | 45.79 | bar | N/A | Ohgaki, Umezono, et al., 1990 | Uncertainty assigned by TRC = 0.15 bar; TRC |
Pc | 46.646 | bar | N/A | Angus, Armstrong, et al., 1980 | Uncertainty assigned by TRC = 2.00 bar; TRC |
Pc | 46.21 | bar | N/A | Marchman, Prengle, et al., 1949 | Uncertainty assigned by TRC = 0.1519 bar; TRC |
Pc | 45.9468 | bar | N/A | Seibert and Burrell, 1915 | Uncertainty assigned by TRC = 0.3333 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.1846 | l/mol | N/A | Tsonopoulos and Ambrose, 1996 | |
Vc | 0.192 | l/mol | N/A | Marchman, Prengle, et al., 1949 | Uncertainty assigned by TRC = 0.005 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 5.42 ± 0.03 | mol/l | N/A | Tsonopoulos and Ambrose, 1996 | |
ρc | 5.549 | mol/l | N/A | Ohgaki, Umezono, et al., 1990 | Uncertainty assigned by TRC = 0.07 mol/l; TRC |
ρc | 5.309 | mol/l | N/A | Angus, Armstrong, et al., 1980 | Uncertainty assigned by TRC = 0.36 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 16.04 | kJ/mol | N/A | Majer and Svoboda, 1985 |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
18.42 | 225.5 | N/A | Majer and Svoboda, 1985 | |
18.418 | 225.35 | N/A | Powell and Giauque, 1939 | DH |
18.7 | 312. | A | Stephenson and Malanowski, 1987 | Based on data from 297. to 363. K.; AC |
22.2 | 146. | A | Stephenson and Malanowski, 1987 | Based on data from 104. to 161. K.; AC |
18.7 | 256. | A | Stephenson and Malanowski, 1987 | Based on data from 228. to 271. K.; AC |
18.5 | 285. | A | Stephenson and Malanowski, 1987 | Based on data from 270. to 327. K.; AC |
18.8 | 340. | A | Stephenson and Malanowski, 1987 | Based on data from 325. to 363. K.; AC |
19.2 | 227. | A | Stephenson and Malanowski, 1987 | Based on data from 161. to 242. K. See also Dykyj, 1970.; AC |
18.7 | 360. | N/A | Michels, Wassenaar, et al., 1953 | Based on data from 298. to 423. K.; AC |
19.6 | 211. | N/A | Powell and Giauque, 1939 | Based on data from 166. to 226. K.; AC |
19.3 | 268. | N/A | Maass and Wright, 1921 | Based on data from 236. to 283. K. See also Boublik, Fried, et al., 1984.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
81.73 | 225.35 | Powell and Giauque, 1939 | DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
165.81 to 225.98 | 3.97488 | 795.819 | -24.884 | Powell and Giauque, 1939 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.003 | 87.85 | Chao, Hall, et al., 1983 | DH |
3.002 | 87.85 | Powell and Giauque, 1939 | DH |
2.933 | 88.2 | Huffman, Parks, et al., 1931 | DH |
2.93 | 88.2 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
34.18 | 87.85 | Chao, Hall, et al., 1983 | DH |
34.18 | 87.85 | Powell and Giauque, 1939 | DH |
33.3 | 88.2 | Huffman, Parks, et al., 1931 | DH |
Temperature of phase transition
Ttrs (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|
56.0 | crystaline | glass | Takeda, Oguni, et al., 1990 | DH |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Chao, Hall, et al., 1983
Chao, J.; Hall, K.R.; Yao, J.M.,
Thermodynamic properties of simple alkenes,
Thermochim. Acta, 1983, 64(3), 285-303. [all data]
Auerbach, Sage, et al., 1950
Auerbach, C.E.; Sage, B.H.; Lacey, W.N.,
Isobaric heat capacities at bubble point,
Ind. Eng. Chem., 1950, 42, 110-113. [all data]
Powell and Giauque, 1939
Powell, T.M.; Giauque, W.F.,
Propylene. The heat capacity, vapor pressure, heats of fusion and vaporization. The third law of thermodynamics and orientation equilibrium in the solid,
J. Am. Chem. Soc., 1939, 61, 2366-2370. [all data]
Huffman, Parks, et al., 1931
Huffman, H.M.; Parks, G.S.; Barmore, M.,
Thermal data on organic compounds. X. Further studies on the heat capacities, entropies and free energies of hydrocarbons,
J. Am. Chem. Soc., 1931, 53, 3876-3888. [all data]
Streng, 1971
Streng, A.G.,
Miscibility and Compatibility of Some Liquid and Solidified Gases at Low Temperature,
J. Chem. Eng. Data, 1971, 16, 357. [all data]
Haselden and Snowden, 1962
Haselden, G.G.; Snowden, P.,
Equilibrium Properties of the Carbon Dioxide+ Propylene and Carbon Dioxide + Cyclopropane Systems at Low Temperatures,
Trans. Faraday Soc., 1962, 58, 1515-28. [all data]
Parks and Huffman, 1931
Parks, G.S.; Huffman, H.M.,
Some fusion and transition data for hydrocarbons,
Ind. Eng. Chem., 1931, 23, 1138-9. [all data]
Coffin and Maass, 1927
Coffin, C.C.; Maass, O.,
The Prepartion and Physical Properties of Isobutylene,
Trans. R. Soc. Can., Sect. 3, 1927, 21, 33. [all data]
Angus, Armstrong, et al., 1980
Angus, S.; Armstrong, B.; de Reuck, K.M.,
International Thermodynamic Tables of the Fluid State - 7 Propylene(Propene), Pergamon, New York, 1980. [all data]
Tsonopoulos and Ambrose, 1996
Tsonopoulos, C.; Ambrose, D.,
Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons,
J. Chem. Eng. Data, 1996, 41, 645-656. [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]
Marchman, Prengle, et al., 1949
Marchman, H.; Prengle, H.W.; Motard, R.L.,
Compressibility and Critical Constants of Propylene Vapor,
Ind. Eng. Chem., 1949, 41, 2658. [all data]
Seibert and Burrell, 1915
Seibert, F.M.; Burrell, G.A.,
The Critical Constants of Normal Butane, Iso-butane and Propylene and Their Vapor Pressures at Temperatures Bewtween 0 deg.C and 120 deg.C,
J. Am. Chem. Soc., 1915, 37, 2683-91. [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]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2
. [all data]
Dykyj, 1970
Dykyj, J.,
Petrochemica, 1970, 10, 2, 51. [all data]
Michels, Wassenaar, et al., 1953
Michels, A.; Wassenaar, T.; Louwerse, P.; Lunbeck, R.J.; Wolkers, G.J.,
Isotherms and thermodynamical functions of propene at temperatures between 25° and 150°c and at densities up to 340 amagat (pressures up to 2800 atm),
Physica, 1953, 19, 1-12, 287-297, https://doi.org/10.1016/S0031-8914(53)80030-3
. [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]
Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E.,
The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]
Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,
Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III,
J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985
. [all data]
Takeda, Oguni, et al., 1990
Takeda, K.; Oguni, M.; Suga, H.,
A DTA apparatus for vapour-deposited samples. Characterisation of some vapour-deposited hydrocarbons,
Thermochim. Acta, 1990, 158(1), 195-203. [all data]
Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure Ptriple Triple point pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Ttrs Temperature of phase transition Vc Critical volume ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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