Ethane
- Formula: C2H6
- Molecular weight: 30.0690
- IUPAC Standard InChIKey: OTMSDBZUPAUEDD-UHFFFAOYSA-N
- CAS Registry Number: 74-84-0
- 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. - Species with the same structure:
- Isotopologues:
- Other names: Bimethyl; Dimethyl; Ethyl hydride; Methylmethane; C2H6; UN 1035; UN 1961
- Information on this page:
- Other data available:
- Data at other public NIST sites:
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering 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:
DRB - Donald R. Burgess, Jr.
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. ± 0.1 | kcal/mol | Review | Manion, 2002 | adopted recommendation of Gurvich, Veyts, et al., 1991; DRB |
ΔfH°gas | -20.04 ± 0.07 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | ALS |
ΔfH°gas | -20.24 ± 0.12 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -373.01 ± 0.06 | kcal/mol | Ccb | Pittam and Pilcher, 1972 | Corresponding ΔfHºgas = -20.04 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -372.82 ± 0.11 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Hf derived from Heat of Hydrogenation; Corresponding ΔfHºgas = -20.23 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -372.81 ± 0.11 | kcal/mol | Ccb | Rossini, 1934 | Corresponding ΔfHºgas = -20.24 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.533 | 100. | Gurvich, Veyts, et al., 1989 | p=1 bar. Recommended entropies and heat capacities are in good agreement with those obtained from other statistical thermodynamic calculations [ Pitzer K.S., 1944, Chao J., 1973, Pamidimukkala K.M., 1982].; GT |
10.11 | 200. | ||
12.55 | 298.15 | ||
12.60 | 300. | ||
15.65 | 400. | ||
18.63 | 500. | ||
21.32 | 600. | ||
23.70 | 700. | ||
25.798 | 800. | ||
27.655 | 900. | ||
29.290 | 1000. | ||
30.724 | 1100. | ||
31.979 | 1200. | ||
33.076 | 1300. | ||
34.034 | 1400. | ||
34.871 | 1500. | ||
35.607 | 1600. | ||
36.250 | 1700. | ||
36.816 | 1800. | ||
37.318 | 1900. | ||
37.763 | 2000. | ||
38.157 | 2100. | ||
38.509 | 2200. | ||
38.822 | 2300. | ||
39.104 | 2400. | ||
39.357 | 2500. | ||
39.587 | 2600. | ||
39.792 | 2700. | ||
39.981 | 2800. | ||
40.153 | 2900. | ||
40.308 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.957 ± 0.074 | 189.20 | Halford J.O., 1957 | Please also see Eucken A., 1933, Kistiakowsky G.B., 1939, Dailey B.P., 1943.; GT |
10.34 ± 0.076 | 209.30 | ||
10.77 ± 0.081 | 229.65 | ||
11.30 ± 0.084 | 249.90 | ||
11.27 ± 0.084 | 250.15 | ||
11.87 ± 0.088 | 272.00 | ||
11.83 ± 0.01 | 272.07 | ||
12.11 ± 0.10 | 279.00 | ||
12.46 ± 0.093 | 292.00 | ||
12.73 ± 0.02 | 302.70 | ||
13.72 ± 0.01 | 335.82 | ||
14.08 | 347.65 | ||
14.43 | 359.75 | ||
14.59 ± 0.024 | 364.78 | ||
14.84 ± 0.11 | 373.60 | ||
15.27 | 387.55 | ||
17.31 | 451.95 | ||
19.14 | 520.55 | ||
20.62 | 561.65 | ||
21.62 | 603.25 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering 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 | 30.28 | cal/mol*K | N/A | Witt and Kemp, 1937 | Entropy from 0 to 15 K calculated using a Debye function. |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
16.41 | 100. | Atake and Chihara, 1976 | T = 50 to 100 K. Data given graphically. Cp = 0.69933 (T/K) - 2.385 J/mol*K (50 to 70 K, for solid). |
16.4 | 94. | Roder, 1976 | From data 90.3 to 94 K. Average value over range. |
16.36 | 100.32 | Roder, 1976, 2 | T = 93 to 301 K (saturation line), 91 to 330 K, pressures from 0 to 33 MPa. |
17.26 | 180. | Witt and Kemp, 1937 | T = 15 to 185 K. |
17.80 | 200. | Wiebe, Hubbard, et al., 1930 | T = 67 to 305.2 K. Heat capacity of saturated liquid given to 295 K is 136.1 J/mol*K. |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Ion clustering 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:
DH - Eugene S. Domalski and Elizabeth D. Hearing
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 184.6 ± 0.6 | K | AVG | N/A | Average of 23 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 101. | K | N/A | Streng, 1971 | Uncertainty assigned by TRC = 1. K; TRC |
Tfus | 89.2 | K | N/A | Timmermans, 1935 | Uncertainty assigned by TRC = 1.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 91. ± 6. | K | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.000011 | atm | N/A | Younglove and Ely, 1987 | Uncertainty assigned by TRC = 5.×10-9 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 305.3 ± 0.3 | K | AVG | N/A | Average of 41 out of 46 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 49. ± 1. | atm | AVG | N/A | Average of 28 out of 29 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.147 ± 0.002 | l/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 6.9 ± 0.4 | mol/l | AVG | N/A | Average of 19 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 2.33 | kcal/mol | N/A | Majer and Svoboda, 1985 |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
3.5141 | 184.1 | N/A | Witt and Kemp, 1937 | DH |
3.66 | 288. | A | Stephenson and Malanowski, 1987 | Based on data from 273. to 305. K.; AC |
3.75 | 170. | A | Stephenson and Malanowski, 1987 | Based on data from 154. to 185. K.; AC |
4.23 | 114. | A | Stephenson and Malanowski, 1987 | Based on data from 95. to 129. K.; AC |
3.56 | 214. | A | Stephenson and Malanowski, 1987 | Based on data from 185. to 229. K.; AC |
3.56 | 259. | A | Stephenson and Malanowski, 1987 | Based on data from 228. to 274. K.; AC |
4.09 | 129. | N/A | Carruth and Kobayashi, 1973 | Based on data from 91. to 144. K.; AC |
3.51 | 210. | N/A | Reid, 1972 | AC |
3.51 | 184. | N/A | Witt and Kemp, 1937 | AC |
3.66 | 185. | N/A | Loomis and Walters, 1926 | Based on data from 136. to 200. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kcal/mol) | β | Tc (K) | Reference |
---|---|---|---|---|
289. to 301. | 7.034 | 0.3696 | 305.4 | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
19.09 | 184.1 | Witt and Kemp, 1937 | DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
91.33 to 144.13 | 4.50135 | 791.3 | -6.422 | Carruth and Kobayashi, 1973 | Coefficents calculated by NIST from author's data. |
135.74 to 199.91 | 3.93264 | 659.739 | -16.719 | Loomis and Walters, 1926 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
5.40 | 85. | N/A | Regnier, 1972 | Based on data from 80. to 90. K.; AC |
4.90 | 90. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
0.139 | 90.341 | Atake and Chihara, 1976 | Triple point.; DH |
0.667 | 89.5 | Domalski and Hearing, 1996 | AC |
0.14 | 90.3 | Atake and Chihara, 1976 | AC |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
1.54 | 90.341 | Atake and Chihara, 1976 | Triple; DH |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.5454 | 89.813 | crystaline, II | crystaline, I | Atake and Chihara, 1976 | DH |
0.6828 | 89.87 | crystaline, I | liquid | Witt and Kemp, 1937 | DH |
0.6675 | 89.50 | crystaline, I | liquid | Wiebe, Hubbard, et al., 1930 | DH |
0.58258 | 89.77 | crystaline, II | crystaline, I | Roder, 1976 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
6.090 | 89.813 | crystaline, II | crystaline, I | Atake and Chihara, 1976 | DH |
7.60 | 89.87 | crystaline, I | liquid | Witt and Kemp, 1937 | DH |
7.46 | 89.50 | crystaline, I | liquid | Wiebe, Hubbard, et al., 1930 | DH |
6.489 | 89.77 | crystaline, II | crystaline, I | Roder, 1976 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Ion clustering 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:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
MS - José A. Martinho Simões
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
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
By formula: Co+ + C2H6 = (Co+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 22.3 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)CH4, ΔrS(500 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
23.9 (+1.2,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M | |
28.0 (+1.6,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)CH4, ΔrS(500 K); M |
By formula: (Co+ • CH4) + C2H6 = (Co+ • C2H6 • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 25.9 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
28.4 (+1.3,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
3 (g) + (l) = AlH3O3 (amorphous) + 3 (g)
By formula: 3H2O (g) + C6H15Al (l) = AlH3O3 (amorphous) + 3C2H6 (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -154.7 ± 1.5 | kcal/mol | RSC | Fowell, 1961 | Please also see Cox and Pilcher, 1970. Liquid triethylaluminum contains a very small molar fraction of monomer at 298 K, ca. 0.1% Smith, 1967, so that the "real" liquid should be described as [Al(Et)3]2.; MS |
C2H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 420.1 ± 2.0 | kcal/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrH° | 421.0 ± 2.0 | kcal/mol | Bran | DePuy, Bierbaum, et al., 1984 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 411.7 ± 2.1 | kcal/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
By formula: (Co+ • C2H6) + CH4 = (Co+ • CH4 • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 26.4 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
24.4 (+1.1,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
By formula: HBr (g) + C2H5Li (cr) = C2H6 (g) + BrLi (cr)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -82.62 ± 0.48 | kcal/mol | RSC | Holm, 1974 | Please also see Pedley and Rylance, 1977. The reaction enthalpy was quoted from Pedley and Rylance, 1977. See Liebman, Martinho Simões, et al., 1995 for comments; MS |
By formula: C5O5W (g) + C2H6 (g) = C7H6O5W (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -7.4 ± 2.0 | kcal/mol | EqG | Brown, Ishikawa, et al., 1990 | Temperature range: ca. 300-350 K; MS |
ΔrH° | -9.7 ± 3.0 | kcal/mol | EqG | Ishikawa, Brown, et al., 1988 | Temperature range: 298-363 K; MS |
By formula: Fe+ + C2H6 = (Fe+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18. ± 3. | kcal/mol | MKER | Carpenter, van Koppen, et al., 1995 | gas phase; M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
15.3 (+1.4,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
By formula: C2H4Cl2 + 2H2 = C2H6 + 2HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -34.18 ± 0.23 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | gas phase; Reanalyzed by Cox and Pilcher, 1970, 2, Original value = -35.32 ± 0.12 kcal/mol; At 250 C; ALS |
By formula: 2H2 + C2H4Cl2 = C2H6 + 2HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -33.66 ± 0.25 | kcal/mol | Chyd | Lacher, Amador, et al., 1967 | gas phase; Reanalyzed by Cox and Pilcher, 1970, 2, Original value = -34.65 ± 0.12 kcal/mol; At 250C; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -74.58 ± 0.15 | kcal/mol | Chyd | Conn, Kistiakowsky, et al., 1939 | gas phase; Reanalyzed by Cox and Pilcher, 1970, 2, Original value = -75.06 ± 0.66 kcal/mol; At 355 K; ALS |
(l) + ( • 100) (solution) = 2 (g) + ( • 100) (solution)
By formula: C4H10Zn (l) + (H2O4S • 100H2O) (solution) = 2C2H6 (g) + (O4SZn • 100H2O) (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -84.7 ± 1.0 | kcal/mol | RSC | Carson, Hartley, et al., 1949 | Please also see Pedley and Rylance, 1977 and Cox and Pilcher, 1970.; MS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -32.6 ± 0.5 | kcal/mol | Chyd | Kistiakowsky and Nickle, 1951 | gas phase; ALS |
ΔrH° | -32.58 ± 0.06 | kcal/mol | Chyd | Kistiakowsky, Romeyn, et al., 1935 | gas phase; ALS |
2 (g) + (l) = AlCl3 (cr) + 2 (g)
By formula: 2HCl (g) + C4H10AlCl (l) = AlCl3 (cr) + 2C2H6 (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -63.34 ± 0.79 | kcal/mol | RSC | Shaulov and Shmyreva, 1968 | The reaction enthalpy was derived from data in Shaulov and Shmyreva, 1968.; MS |
By formula: C2H4+ + C2H6 = (C2H4+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.3 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21. | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1980 | gas phase; M |
By formula: 2H2 + C2H3Cl = C2H6 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -51.2 ± 0.2 | kcal/mol | Chyd | Lacher, Emery, et al., 1956 | gas phase; At 298 K, see Lacher, Kianpour, et al., 1956; ALS |
(g) + C2H5BrMg (solution) = (solution) + Br2Mg (solution)
By formula: HBr (g) + C2H5BrMg (solution) = C2H6 (solution) + Br2Mg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -71.51 ± 0.53 | kcal/mol | RSC | Holm, 1981 | solvent: Diethyl ether; MS |
By formula: (Co+ • 2C2H6) + C2H6 = (Co+ • 3C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12. | kcal/mol | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrH<; M |
By formula: Al+ + C2H6 = (Al+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.0 ± 2.0 | kcal/mol | CIDC,EqG | Stockigt, Schwarz, et al., 1996 | Anchored to theory; RCD |
By formula: 2H2 + C2H3Br = HBr + C2H6
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -47.61 ± 0.46 | kcal/mol | Chyd | Lacher, Kianpour, et al., 1957 | gas phase; ALS |
By formula: H2 + 2C2H5I = 2C2H6 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -21.2 ± 0.80 | kcal/mol | Chyd | Ashcroft, Carson, et al., 1965 | liquid phase; ALS |
By formula: H2 + C2H5Br = HBr + C2H6
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -14.11 ± 0.27 | kcal/mol | Chyd | Fowell, Lacher, et al., 1965 | gas phase; ALS |
By formula: H2 + 2C2H5Br = 2C2H6 + Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 5.6 ± 3.0 | kcal/mol | Chyd | Ashcroft, Carson, et al., 1965 | liquid phase; ALS |
By formula: H2 + C2H5Cl = C2H6 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -16.6 ± 0.1 | kcal/mol | Chyd | Lacher, Emery, et al., 1956 | gas phase; ALS |
By formula: Ni+ + C2H6 = (Ni+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29. ± 3. | kcal/mol | MKER | Carpenter, van Koppen, et al., 1995 | gas phase; M |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, 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 as indicated in comments:
RCD - Robert C. Dunbar
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
By formula: Al+ + C2H6 = (Al+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.0 ± 2.0 | kcal/mol | CIDC,EqG | Stockigt, Schwarz, et al., 1996 | Anchored to theory; RCD |
By formula: C2H4+ + C2H6 = (C2H4+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.3 | kcal/mol | PHPMS | Hiraoka and Kebarle, 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21. | cal/mol*K | PHPMS | Hiraoka and Kebarle, 1980 | gas phase; M |
By formula: (Co+ • CH4) + C2H6 = (Co+ • C2H6 • CH4)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 25.9 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
28.4 (+1.3,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+).2CH4, ΔrS(480 K); M |
By formula: Co+ + C2H6 = (Co+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrS° | 22.3 | cal/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)CH4, ΔrS(500 K); M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
23.9 (+1.2,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M | |
28.0 (+1.6,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; switching reaction(Co+)CH4, ΔrS(500 K); M |
By formula: (Co+ • 2C2H6) + C2H6 = (Co+ • 3C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12. | kcal/mol | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrH<; M |
By formula: Fe+ + C2H6 = (Fe+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18. ± 3. | kcal/mol | MKER | Carpenter, van Koppen, et al., 1995 | gas phase; M |
Enthalpy of reaction
ΔrH° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
15.3 (+1.4,-0.) | CID | Armentrout and Kickel, 1994 | gas phase; guided ion beam CID; M |
By formula: Ni+ + C2H6 = (Ni+ • C2H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29. ± 3. | kcal/mol | MKER | Carpenter, van Koppen, et al., 1995 | gas phase; M |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Manion, 2002
Manion, J.A.,
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Pittam, D.A.; Pilcher, G.,
Measurements of heats of combustion by flame calorimetry. Part 8.-Methane, ethane, propane, n-butane and 2-methylpropane,
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Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D.,
Heats of combustion and formation of the paraffin hydrocarbons at 25° C,
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Rossini, 1934
Rossini, F.D.,
Calorimetric determination of the heats of combustion of ethane, propane, normal butane, and normal pentane,
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Gurvich, Veyts, et al., 1989
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Pitzer K.S., 1944
Pitzer K.S.,
Thermodynamics of gaseous paraffins. Specific heat and related properties,
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Chao J., 1973
Chao J.,
Ideal gas thermodynamic properties of ethane and propane,
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Pamidimukkala K.M., 1982
Pamidimukkala K.M.,
Ideal gas thermodynamic properties of CH3, CD3, CD4, C2D2, C2D4, C2D6, C2H6, CH3N2CH3, and CD3N2CD3,
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Halford J.O., 1957
Halford J.O.,
Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity,
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Eucken A., 1933
Eucken A.,
Molar heats and normal frequencies of ethane and ethylene,
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Kistiakowsky G.B., 1939
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Gaseous heat capacities. I. The method and the heat capacities of C2H6 and C2D6,
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Dailey B.P., 1943
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The heat capacities at higher temperatures of ethane and propane,
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Witt and Kemp, 1937
Witt, R.K.; Kemp, J.D.,
The heat capacity of ethane from 15°K to the boiling point. The heat of fusion and the heat of vaporization,
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Atake and Chihara, 1976
Atake, T.; Chihara, H.,
Calorimetric study of the phase changes in solid ethane,
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Roder, 1976
Roder, H.M.,
The heats of transition of solid ethane,
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Roder, 1976, 2
Roder, H.M.,
Measurements of the specific heats, Ca, and Cv, of dense gaseous and liquid ethane,
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Wiebe, Hubbard, et al., 1930
Wiebe, R.; Hubbard, K.H.; Brevoort, M.J.,
The heat capacity of saturated liquid ethane from the boiling point to the critical temperature and heat fusion of the solid,
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Streng, 1971
Streng, A.G.,
Miscibility and Compatibility of Some Liquid and Solidified Gases at Low Temperature,
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Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
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Younglove and Ely, 1987
Younglove, B.A.; Ely, J.F.,
Thermophysical Properties of Fluids II. Methane, Ethane, Propane, Isobutane, and Normal Butane,
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Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
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Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
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Carruth and Kobayashi, 1973
Carruth, Grant F.; Kobayashi, Riki,
Vapor pressure of normal paraffins ethane through n-decane from their triple points to about 10 mm mercury,
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Reid, 1972
Reid, Robert C.,
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Loomis and Walters, 1926
Loomis, A.G.; Walters, J.E.,
THE VAPOR PRESSURE OF ETHANE NEAR THE NORMAL BOILING POINT 1,
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Regnier, 1972
Regnier, J.,
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Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
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Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,
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Kemper, Bushnell, et al., 1993
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Binding Energies of Co+(H2/CH4/C2H6)1,2,3 Clusters,
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Armentrout and Kickel, 1994
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Fowell, 1961
Fowell, P.A.,
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Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
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Smith, 1967
Smith, M.B.,
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DePuy, Gronert, et al., 1989
DePuy, C.H.; Gronert, S.; Barlow, S.E.; Bierbaum, V.M.; Damrauer, R.,
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DePuy, Bierbaum, et al., 1984
DePuy, C.H.; Bierbaum, V.M.; Damrauer, R.,
Relative Gas-Phase Acidities of the Alkanes,
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Holm, 1974
Holm, T.,
J. Organometal. Chem., 1974, 77, 27. [all data]
Pedley and Rylance, 1977
Pedley, J.B.; Rylance, J.,
Computer Analysed Thermochemical Data: Organic and Organometallic Compounds, University of Sussex, Brigton, 1977. [all data]
Liebman, Martinho Simões, et al., 1995
Liebman, J.F.; Martinho Simões, J.A.; Slayden, S.W.,
In Lithium Chemistry: A Theoretical and Experimental Overview Wiley: New York, Sapse, A.-M.; Schleyer, P. von Ragué, ed(s)., 1995. [all data]
Brown, Ishikawa, et al., 1990
Brown, C.E.; Ishikawa, Y.; Hackett, P.A.; Rayner, D.M.,
J. Am. Chem. Soc., 1990, 112, 2530. [all data]
Ishikawa, Brown, et al., 1988
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Carpenter, van Koppen, et al., 1995
Carpenter, C.J.; van Koppen, P.A.M.; Bowers, M.T.,
Details of Potential Energy Surfaces Involving C-C Bond Activation: Reactions of Fe+, Co+ and Ni+ with Acetone,
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Lacher, Amador, et al., 1967
Lacher, J.R.; Amador, A.; Park, J.D.,
Reaction heats of organic compounds. Part 5.-Heats of hydrogenation of dichloromethane, 1,1- and 1,2-dichloroethane and 1,2-dichloropropane,
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Cox and Pilcher, 1970, 2
Cox, J.D.; Pilcher, G.,
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Conn, Kistiakowsky, et al., 1939
Conn, J.B.; Kistiakowsky, G.B.; Smith, E.A.,
Heats of organic reactions. VIII. Some further hydrogenations, including those of some acetylenes,
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Carson, Hartley, et al., 1949
Carson, A.S.; Hartley, K.; Skinner, H.A.,
Thermochemistry of metal alkyls. Part II.?The bond dissociation energies of some Zn?C and Cd?C bonds, and of Et?I.,
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Ethane-ethylene and propane-propylene equilibria,
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Kistiakowsky, Romeyn, et al., 1935
Kistiakowsky, G.B.; Romeyn, H., Jr.; Ruhoff, J.R.; Smith, H.A.; Vaughan, W.E.,
Heats of organic reactions. I. The apparatus and the heat of hydrogenation of ethylene,
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Shaulov and Shmyreva, 1968
Shaulov, Yu.Kh.; Shmyreva, G.O.,
Russ. J. Phys. Chem., 1968, 42, 1008. [all data]
Hiraoka and Kebarle, 1980
Hiraoka, K.; Kebarle, P.,
Ion Molecule Reactions in Ethane. Thermochemistry and Structures of the Intermediate Complexes: C4H11+ and C4H10+ Formed in the Reactions of C2H5+ and C2H4+ with C2H6,
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Lacher, Emery, et al., 1956
Lacher, J.R.; Emery, E.; Bohmfalk, E.; Park, J.D.,
Reaction heats of organic compounds. IV. A high temperature calorimeter and the hydrogenation of methyl ethyl and vinyl chlorides,
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Lacher, Kianpour, et al., 1956
Lacher, J.R.; Kianpour, A.; Oetting, F.; Park, J.D.,
Reaction calorimetry. The hydrogenation of organic fluorides and chlorides,
Trans. Faraday Soc., 1956, 52, 1500-1508. [all data]
Holm, 1981
Holm, T.,
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Stockigt, Schwarz, et al., 1996
Stockigt, D.; Schwarz, J.; Schwarz, H.,
Theoretical and Experimental Studies on the Bond Dissociation Energies of Al(methane)+, Al(acetylene)+, Al(ethene)+, and Al(ethane)+,
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Lacher, Kianpour, et al., 1957
Lacher, J.R.; Kianpour, A.; Montgomery, P.; Knedler, H.; Park, J.D.,
Reaction heats of organic halogen compounds. IX. The catalytic hydrogenation of vinyl and perfluorovinyl bromide,
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Ashcroft, Carson, et al., 1965
Ashcroft, S.J.; Carson, A.S.; Carter, W.; Laye, P.G.,
Thermochemistry of reductions caused by lithium aluminium hydride. Part 3.- The C-halogen bond dissociation energies in ethyl iodine and ethyl bromide,
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Fowell, Lacher, et al., 1965
Fowell, P.; Lacher, J.R.; Park, J.D.,
Reaction heats of organic compounds. Part 3.-Heats of hydrogenation of methyl bromide and ethyl bromide,
Trans. Faraday Soc., 1965, 61, 1324-1327. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Ion clustering data, References
- 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 Vc Critical volume ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 ΔsubH Enthalpy of sublimation 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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