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, Reaction thermochemistry data, Henry's Law 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, Reaction thermochemistry data, Henry's Law 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 |
Reaction thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law 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:
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
RCD - Robert C. Dunbar
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
C3H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1636.4 ± 1.3 | kJ/mol | G+TS | Ellison, Davico, et al., 1996 | gas phase; calculated dSacid=24.2±1.0 eu; B |
ΔrH° | 1634. ± 4.2 | kJ/mol | D-EA | Wenthold, Polak, et al., 1996 | gas phase; B |
ΔrH° | 1635. ± 8.8 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1632.8 ± 2.7 | kJ/mol | G+TS | Mackay, Lien, et al., 1978 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1605.8 ± 0.42 | kJ/mol | IMRE | Ellison, Davico, et al., 1996 | gas phase; calculated dSacid=24.2±1.0 eu; B |
ΔrG° | 1606. ± 4.6 | kJ/mol | H-TS | Wenthold, Polak, et al., 1996 | gas phase; B |
ΔrG° | 1607. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1605.0 ± 2.1 | kJ/mol | IMRE | Mackay, Lien, et al., 1978 | gas phase; B |
By formula: HBr + C3H6 = C3H7Br
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -85.48 | kJ/mol | Cm | Lacher, Kianpour, et al., 1957 | gas phase; ALS |
ΔrH° | -83.889 | kJ/mol | Cm | Lacher, Lea, et al., 1950 | gas phase; Heat of hydrobromination at 367°K; ALS |
ΔrH° | -84.10 ± 0.59 | kJ/mol | Cm | Lacher, Walden, et al., 1950 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -84.4 ± 1.0 kJ/mol; Heat of hydrobromination; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -123.4 ± 5.0 | kJ/mol | Chyd | Kistiakowsky and Nickle, 1951 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -124.9 ± 2.1 kJ/mol; ALS |
ΔrH° | -125.0 ± 0.42 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1935 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -126.00 ± 0.054 kJ/mol; At 355 °K; ALS |
C3H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1698. ± 8.4 | kJ/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrH° | >1693.5 ± 2.5 | kJ/mol | G+TS | Froelicher, Freiser, et al., 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1665. ± 8.8 | kJ/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrG° | >1661.0 | kJ/mol | IMRB | Froelicher, Freiser, et al., 1986 | gas phase; B |
By formula: HI + C3H5I = C3H6 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -33.3 ± 1.4 | kJ/mol | Eqk | Rodgers, Golden, et al., 1966 | gas phase; ALS |
ΔrH° | -39.7 ± 4.2 | kJ/mol | Eqk | Rodgers, Golden, et al., 1966 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -34.9 ± 0.96 kJ/mol; At 527 K; ALS |
By formula: C3H7Cl = C3H6 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 72.4 ± 0.8 | kJ/mol | Eqk | Noren and Sunner, 1970 | gas phase; ALS |
ΔrH° | 73.72 ± 0.63 | kJ/mol | Eqk | Kabo and Andreevskii, 1963 | gas phase; At 415.5 K; ALS |
ΔrH° | 73.0 ± 2.1 | kJ/mol | Eqk | Howlett, 1955 | gas phase; ALS |
By formula: Co+ + C3H6 = (Co+ • C3H6)
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
180. (+7.1,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M | |
180. (+6.7,-0.) | CID | Haynes and Armentrout, 1994 | gas phase; guided ion beam CID; M |
By formula: C3H9Si+ + C3H6 = (C3H9Si+ • C3H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 128. | kJ/mol | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 178. | J/mol*K | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
By formula: C3H6 + Br2 = C3H6Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -122.5 ± 0.84 | kJ/mol | Cm | Conn, Kistiakowsky, et al., 1938 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -123.1 ± 0.84 kJ/mol; At 355 °K; ALS |
C3H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | >1693.5 ± 3.8 | kJ/mol | G+TS | Froelicher, Freiser, et al., 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | >1661.0 | kJ/mol | IMRB | Froelicher, Freiser, et al., 1986 | gas phase; B |
By formula: Li+ + C3H6 = (Li+ • C3H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 96. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 extrapolated; M |
By formula: Rh+ + C3H6 = (Rh+ • C3H6)
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
118. | CID | Chen and Armetrout, 1995 | gas phase; ΔrH>=, guided ion beam CID; M |
By formula: Fe+ + C3H6 = (Fe+ • C3H6)
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
145. (+7.1,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
(CAS Reg. No. 25012-80-0 • 4294967295) + = CAS Reg. No. 25012-80-0
By formula: (CAS Reg. No. 25012-80-0 • 4294967295C3H6) + C3H6 = CAS Reg. No. 25012-80-0
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.2 ± 8.8 | kJ/mol | N/A | DePuy, Gronert, et al., 1989 | gas phase; B |
(CAS Reg. No. 59513-13-2 • 4294967295) + = CAS Reg. No. 59513-13-2
By formula: (CAS Reg. No. 59513-13-2 • 4294967295C3H6) + C3H6 = CAS Reg. No. 59513-13-2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 61.1 ± 8.8 | kJ/mol | N/A | DePuy, Gronert, et al., 1989 | gas phase; B |
By formula: C3H6 + HCl = C3H7Cl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -73.39 | kJ/mol | Eqk | Kabo and Andreevskii, 1963 | gas phase; At 385°K; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -86.27 | kJ/mol | Eqk | Furuyama, Golden, et al., 1969 | gas phase; ALS |
By formula: C3H6 + H2O4S = isopropyl hydrogen sulphate
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -38. ± 0.8 | kJ/mol | Eqk | Entelis, Korovina, et al., 1960 | liquid phase; ALS |
By formula: C3H6I2 = C3H6 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 47. ± 2. | kJ/mol | Eqk | Benson and Amano, 1962 | gas phase; ALS |
By formula: C3H7Br = HBr + C3H6
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 81. ± 2. | kJ/mol | Eqk | Rozhnov and Andreevskii, 1962 | gas phase; ALS |
By formula: C3H6 + C3F6O = C6H6F6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -78.2 ± 4.2 | kJ/mol | Eqk | Moore, 1971 | gas phase; ALS |
By formula: Au+ + C3H6 = (Au+ • C3H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | >310. | kJ/mol | IMRB | Schroeder, Hrusak, et al., 1995 | RCD |
Henry's Law data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction 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 by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
0.0048 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0048 | L | N/A | ||
0.0074 | 3400. | L | N/A | |
0.0048 | V | N/A |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law 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,
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Parks and Huffman, 1931
Parks, G.S.; Huffman, H.M.,
Some fusion and transition data for hydrocarbons,
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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]
Ellison, Davico, et al., 1996
Ellison, G.B.; Davico, G.E.; Bierbaum, V.M.; DePuy, C.H.,
Thermochemistry of theb Benzyl and Allyl Radicals and Ions,
Int. J. Mass Spectrom. Ion Proc., 1996, 156, 1-2, 109-131, https://doi.org/10.1016/S0168-1176(96)04383-2
. [all data]
Wenthold, Polak, et al., 1996
Wenthold, P.G.; Polak, M.L.; Lineberger, W.C.,
Photoelectron Spectroscopy of the Allyl and 2-Methylallyl Anions,
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. [all data]
Bartmess, Scott, et al., 1979
Bartmess, J.E.; Scott, J.A.; McIver, R.T., Jr.,
The gas phase acidity scale from methanol to phenol,
J. Am. Chem. Soc., 1979, 101, 6047. [all data]
Mackay, Lien, et al., 1978
Mackay, G.I.; Lien, M.H.; Hopkinson, A.C.; Bohme, D.K.,
Experimental and theoretical studies of proton removal from propene,
Can. J. Chem., 1978, 56, 131. [all data]
Lacher, Kianpour, et al., 1957
Lacher, J.R.; Kianpour, A.; Park, J.D.,
Reaction heats of organic halogen compounds. X. Vapor phase heats of hydrobromination of cyclopropane and propylene,
J. Phys. Chem., 1957, 61, 1124-1125. [all data]
Lacher, Lea, et al., 1950
Lacher, J.R.; Lea, K.R.; Walden, C.H.; Olson, G.G.; Park, J.D.,
Reaction heats of organic fluorine compounds. III. The vapor phase heats of hydrobromination of some simple fluoroolefins,
J. Am. Chem. Soc., 1950, 72, 3231-3234. [all data]
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Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law 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 T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Ttrs Temperature of phase transition Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions 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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