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, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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)
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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, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Mass spectrum (electron ionization), 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 |
IR Spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Mass spectrum (electron ionization), References, Notes
Data compiled by: Coblentz Society, Inc.
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Mass spectrum (electron ionization)
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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Owner | NIST Mass Spectrometry Data Center Collection (C) 2014 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
NIST MS number | 50 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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.,
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Notes
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- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas 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 ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions 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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