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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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics 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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | 20.41 | kJ/mol | Eqk | Furuyama, Golden, et al., 1969 | ALS |
ΔfH°gas | 20.41 | kJ/mol | Cm | Lacher, Walden, et al., 1950 | Heat of hydrobromination; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -2057.8 ± 1.1 | kJ/mol | Cm | Wiberg and Fenoglio, 1968 | Corresponding ΔfHºgas = 19.8 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -2057.7 ± 0.6 | kJ/mol | Cm | Rossini and Knowlton, 1937 | Reanalyzed by Cox and Pilcher, 1970, Original value = -2057.42 ± 0.62 kJ/mol; Corresponding ΔfHºgas = 19.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
34.35 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Recommended entropies and heat capacities are in good agreement with other statistically calculated values [ Crawford B.L., 1939, Kilpatrick J.E., 1946, Kilpatrick J.E., 1947, Chao J., 1975] as well as with ab initio value of S(298.15 K)=266.82 J/mol*K [ East A.L.L., 1997].; GT |
39.07 | 100. | ||
44.34 | 150. | ||
50.24 | 200. | ||
60.47 | 273.15 | ||
64.32 | 298.15 | ||
64.61 | 300. | ||
80.45 | 400. | ||
95.17 | 500. | ||
108.00 | 600. | ||
119.09 | 700. | ||
128.72 | 800. | ||
137.12 | 900. | ||
144.44 | 1000. | ||
150.83 | 1100. | ||
156.40 | 1200. | ||
161.25 | 1300. | ||
165.48 | 1400. | ||
169.18 | 1500. | ||
176.54 | 1750. | ||
181.90 | 2000. | ||
185.89 | 2250. | ||
188.91 | 2500. | ||
191.24 | 2750. | ||
193.08 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
44.52 | 148.2 | Bier K., 1974 | Please also see Kistiakowsky G.B., 1940, Kistiakowsky G.B., 1940, 2, Telfair D., 1942.; GT |
45.44 | 157.6 | ||
52.22 | 213.1 | ||
53.09 | 220.1 | ||
53.68 | 223.7 | ||
58.45 | 258.0 | ||
59.78 | 270. | ||
60.08 ± 0.13 | 272.29 | ||
61.45 | 280. | ||
63.43 | 291.1 | ||
63.79 ± 0.13 | 298.15 | ||
64.73 ± 0.13 | 299.33 | ||
64.71 | 300. | ||
67.89 | 320. | ||
67.88 ± 0.14 | 323.15 | ||
70.04 ± 0.17 | 333.86 | ||
71.03 | 340. | ||
71.78 ± 0.14 | 348.15 | ||
74.13 | 360. | ||
74.47 ± 0.15 | 365.15 | ||
75.02 ± 0.08 | 367.11 | ||
75.79 ± 0.15 | 373.15 | ||
79.85 ± 0.16 | 378.15 | ||
77.14 | 380. | ||
80.15 | 400. | ||
83.17 | 420. | ||
83.61 ± 0.17 | 423.15 | ||
86.09 | 440. | ||
87.44 ± 0.17 | 448.15 | ||
89.02 | 460. | ||
91.18 ± 0.18 | 473.15 | ||
91.91 | 480. | ||
94.76 | 500. | ||
96.18 | 510. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics 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. |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Gas phase ion energetics 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 |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C3H6+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.73 ± 0.01 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 751.6 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 722.7 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
Appearance energy determinations
De-protonation 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 |
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 |
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 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Furuyama, Golden, et al., 1969
Furuyama, S.; Golden, D.M.; Benson, S.W.,
Thermochemistry of the gas phase equilibria i-C3H7I = C3H6 + HI, n-C3H7I = i-C3H7I, and C3H6 + 2HI = C3H8 + I2,
J. Chem. Thermodyn., 1969, 1, 363-375. [all data]
Lacher, Walden, et al., 1950
Lacher, J.R.; Walden, C.H.; Lea, K.R.; Park, J.D.,
Vapor phase heats of hydrobromination of cyclopropane and propylene,
J. Am. Chem. Soc., 1950, 72, 331-333. [all data]
Wiberg and Fenoglio, 1968
Wiberg, K.B.; Fenoglio, R.A.,
Heats of formation of C4H6 hydrocarbons,
J. Am. Chem. Soc., 1968, 90, 3395-3397. [all data]
Rossini and Knowlton, 1937
Rossini, F.d.; Knowlton, J.W.,
Calorimetric determination of the heats of combustion of ethylene and propylene,
J. Res. NBS, 1937, 19, 249-262. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Thermodynamics Research Center, 1997
Thermodynamics Research Center,
Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
Crawford B.L., 1939
Crawford B.L., Jr.,
The entropy and heat capacity of propylene,
J. Am. Chem. Soc., 1939, 61, 2980-2981. [all data]
Kilpatrick J.E., 1946
Kilpatrick J.E.,
Heat content, free energy function, entropy, and heat capacity of ethylene, propylene, and the four butenes to 1500 K,
J. Res. Nat. Bur. Stand, 1946, 37, 163-171. [all data]
Kilpatrick J.E., 1947
Kilpatrick J.E.,
Normal coordinate analysis of the vibrational frequencies of ethylene, propylene, cis-2-butene, trans-2-butene, and isobutene,
J. Res. Nat. Bur. Stand., 1947, 38, 191-209. [all data]
Chao J., 1975
Chao J.,
Ideal gas thermodynamic properties of ethylene and propylene,
J. Phys. Chem. Ref. Data, 1975, 4, 251-261. [all data]
East A.L.L., 1997
East A.L.L.,
Ab initio statistical thermodynamical models for the computation of third-law entropies,
J. Chem. Phys., 1997, 106, 6655-6674. [all data]
Bier K., 1974
Bier K.,
Thermodynamic properties of propylene from calorimetric measurements,
J. Chem. Thermodyn., 1974, 6, 1039-1052. [all data]
Kistiakowsky G.B., 1940
Kistiakowsky G.B.,
The low temperature gaseous heat capacities of certain C3 hydrocarbons,
J. Chem. Phys., 1940, 8, 970-977. [all data]
Kistiakowsky G.B., 1940, 2
Kistiakowsky G.B.,
Gaseous heat capacities. II,
J. Chem. Phys., 1940, 8, 610-618. [all data]
Telfair D., 1942
Telfair D.,
Supersonic measurement of the heat capacity of propylene,
J. Chem. Phys., 1942, 10, 167-171. [all data]
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]
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,
J. Phys. Chem., 1996, 100, 17, 6920, https://doi.org/10.1021/jp953401n
. [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]
Kistiakowsky and Nickle, 1951
Kistiakowsky, G.B.; Nickle, A.G.,
Ethane-ethylene and propane-propylene equilibria,
Faraday Discuss. Chem. Soc., 1951, 10, 175-187. [all data]
Kistiakowsky, Ruhoff, et al., 1935
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy S°liquid Entropy of liquid at standard conditions T Temperature ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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