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, Henry's Law 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:
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, Henry's Law 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 | 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
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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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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 |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change 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: 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 |
---|---|---|---|---|
0.0019 | 2300. | L | N/A | |
0.0020 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0020 | L | N/A | ||
0.0018 | 2400. | L | N/A | |
0.0020 | V | N/A | ||
0.011 | V | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, 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 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
LL - Sharon G. Lias and Joel F. Liebman
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 C2H6+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 11.52 ± 0.04 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 142.5 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 136.2 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
11. ± 1. | PI | Au, Cooper, et al., 1993 | LL |
11.52 | EST | Luo and Pacey, 1992 | LL |
11.57 | EI | Plessis and Marmet, 1987 | LBLHLM |
11.56 ± 0.02 | EI | Plessis and Marmet, 1987, 2 | LBLHLM |
11.4 ± 0.4 | EI | Chatham, Hils, et al., 1984 | LBLHLM |
11.5 ± 0.1 | EI | Suzuki and Maeda, 1977 | LLK |
11.56 ± 0.02 | PE | Bieri, Burger, et al., 1977 | LLK |
11.76 ± 0.05 | EI | Flesch and Svec, 1973 | LLK |
11.45 ± 0.05 | TE | Stockbauer and Inghram, 1971 | LLK |
11.51 | PE | Dewar and Worley, 1969 | RDSH |
11.66 ± 0.05 | EI | Williams and Hamill, 1968 | RDSH |
11.55 | CI | Cermak, 1968 | RDSH |
11.56 | PE | Baker, Baker, et al., 1968 | RDSH |
11.521 ± 0.007 | PI | Nicholson, 1965 | RDSH |
11.99 | PE | Kimura, Katsumata, et al., 1981 | Vertical value; LLK |
12.0 | PE | Bieri and Asbrink, 1980 | Vertical value; LLK |
12.1 ± 0.1 | PE | Bieri, Burger, et al., 1977 | Vertical value; LLK |
12.00 | PE | Doucet, Sauvageau, et al., 1975 | Vertical value; LLK |
Appearance energy determinations
De-protonation reactions
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 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law 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.
Manion, 2002
Manion, J.A.,
Evaluated Enthalpies of Formation of the Stable Closed Shell C1 and C2 Chlorinated Hydrocarbons,
J. Phys. Chem. Ref. Data, 2002, 31, 1, 123-172, https://doi.org/10.1063/1.1420703
. [all data]
Gurvich, Veyts, et al., 1991
Thermodynamic Properties of Individual Substances, 4th edition, Volume 2, Gurvich, L.V.; Veyts, I.V.; Alcock, C.B.;, ed(s)., Hemisphere, New York, 1991. [all data]
Pittam and Pilcher, 1972
Pittam, D.A.; Pilcher, G.,
Measurements of heats of combustion by flame calorimetry. Part 8.-Methane, ethane, propane, n-butane and 2-methylpropane,
J. Chem. Soc. Faraday Trans. 1, 1972, 68, 2224-2229. [all data]
Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D.,
Heats of combustion and formation of the paraffin hydrocarbons at 25° C,
J. Res. NBS, 1945, 263-267. [all data]
Rossini, 1934
Rossini, F.D.,
Calorimetric determination of the heats of combustion of ethane, propane, normal butane, and normal pentane,
J. Res. NBS, 1934, 12, 735-750. [all data]
Gurvich, Veyts, et al., 1989
Gurvich, L.V.; Veyts, I.V.; Alcock, C.B.,
Thermodynamic Properties of Individual Substances, 4th ed.; Vols. 1 and 2, Hemisphere, New York, 1989. [all data]
Pitzer K.S., 1944
Pitzer K.S.,
Thermodynamics of gaseous paraffins. Specific heat and related properties,
Ind. Eng. Chem., 1944, 36, 829-831. [all data]
Chao J., 1973
Chao J.,
Ideal gas thermodynamic properties of ethane and propane,
J. Phys. Chem. Ref. Data, 1973, 2, 427-438. [all data]
Pamidimukkala K.M., 1982
Pamidimukkala K.M.,
Ideal gas thermodynamic properties of CH3, CD3, CD4, C2D2, C2D4, C2D6, C2H6, CH3N2CH3, and CD3N2CD3,
J. Phys. Chem. Ref. Data, 1982, 11, 83-99. [all data]
Halford J.O., 1957
Halford J.O.,
Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity,
J. Phys. Chem., 1957, 61, 1536-1539. [all data]
Eucken A., 1933
Eucken A.,
Molar heats and normal frequencies of ethane and ethylene,
Z. Phys. Chem., 1933, B20, 184-194. [all data]
Kistiakowsky G.B., 1939
Kistiakowsky G.B.,
Gaseous heat capacities. I. The method and the heat capacities of C2H6 and C2D6,
J. Chem. Phys., 1939, 7, 281-288. [all data]
Dailey B.P., 1943
Dailey B.P.,
The heat capacities at higher temperatures of ethane and propane,
J. Am. Chem. Soc., 1943, 65, 42-44. [all data]
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,
J. Am. Chem. Soc., 1937, 59, 273-276. [all data]
Atake and Chihara, 1976
Atake, T.; Chihara, H.,
Calorimetric study of the phase changes in solid ethane,
Chem. Lett., 1976, (7), 683-688. [all data]
Roder, 1976
Roder, H.M.,
The heats of transition of solid ethane,
J. Chem. Phys., 1976, 65, 1371-1373. [all data]
Roder, 1976, 2
Roder, H.M.,
Measurements of the specific heats, Ca, and Cv, of dense gaseous and liquid ethane,
J. Res., 1976, NBS 80A, 739-759. [all data]
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,
J. Am. Chem. Soc., 1930, 52, 611-622. [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]
Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
Bull. Soc. Chim. Belg., 1935, 44, 17-40. [all data]
Younglove and Ely, 1987
Younglove, B.A.; Ely, J.F.,
Thermophysical Properties of Fluids II. Methane, Ethane, Propane, Isobutane, and Normal Butane,
J. Phys. Chem. Ref. Data, 1987, 16, 577. [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]
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,
J. Chem. Eng. Data, 1973, 18, 2, 115-126, https://doi.org/10.1021/je60057a009
. [all data]
Reid, 1972
Reid, Robert C.,
Handbook on vapor pressure and heats of vaporization of hydrocarbons and related compounds, R. C. Wilhort and B. J. Zwolinski, Texas A Research Foundation. College Station, Texas(1971). 329 pages.$10.00,
AIChE J., 1972, 18, 6, 1278-1278, https://doi.org/10.1002/aic.690180637
. [all data]
Loomis and Walters, 1926
Loomis, A.G.; Walters, J.E.,
THE VAPOR PRESSURE OF ETHANE NEAR THE NORMAL BOILING POINT 1,
J. Am. Chem. Soc., 1926, 48, 8, 2051-2055, https://doi.org/10.1021/ja01419a006
. [all data]
Regnier, 1972
Regnier, J.,
J. Chim. Phys. Phys.-Chim. Biol., 1972, 69, 6, 942. [all data]
Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
J. Chem. Eng. Data, 1963, 8, 3, 371-381, https://doi.org/10.1021/je60018a027
. [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]
Hunter and Lias, 1998
Hunter, E.P.; Lias, S.G.,
Evaluated Gas Phase Basicities and Proton Affinities of Molecules: An Update,
J. Phys. Chem. Ref. Data, 1998, 27, 3, 413-656, https://doi.org/10.1063/1.556018
. [all data]
Au, Cooper, et al., 1993
Au, J.W.; Cooper, G.; Brion, C.E.,
The molecular and dissociative photoionization of ethane, propane, and n-butane: Absolute oscillator strengths (10-80 eV) and breakdown pathways,
Chem. Phys., 1993, 173, 241. [all data]
Luo and Pacey, 1992
Luo, Y.-R.; Pacey, P.D.,
Effects of alkyl substitution on ionization energies of alkanes and haloalkanes and on heats of formation of their molecular cations. Part 2. Alkanes and chloro-, bromo- and iodoalkanes,
Int. J. Mass Spectrom. Ion Processes, 1992, 112, 63. [all data]
Plessis and Marmet, 1987
Plessis, P.; Marmet, P.,
Electroionization study of ethane: structures in the ionization and appearance energy curves,
Can. J. Chem., 1987, 65, 2004. [all data]
Plessis and Marmet, 1987, 2
Plessis, P.; Marmet, P.,
Electroionization study of ethane: Ionization and appearance energies, ion-pair formations and negative ions,
Can. J. Chem., 1987, 65, 1424. [all data]
Chatham, Hils, et al., 1984
Chatham, H.; Hils, D.; Robertson, R.; Gallagher, A.,
Total and partial electron collisional ionization cross sections for CH4, C2H6, SiH4, and Si2H6,
J. Chem. Phys., 1984, 81, 1770. [all data]
Suzuki and Maeda, 1977
Suzuki, I.H.; Maeda, K.,
Ionization efficiency curves of ethane by electron impact,
Int. J. Mass Spectrom. Ion Phys., 1977, 24, 147. [all data]
Bieri, Burger, et al., 1977
Bieri, G.; Burger, F.; Heilbronner, E.; Maier, J.P.,
Valence ionization enrgies of hydrocarbons,
Helv. Chim. Acta, 1977, 60, 2213. [all data]
Flesch and Svec, 1973
Flesch, G.D.; Svec, H.J.,
Fragmentation reactions in the mass spectrometer for C2-C5 alkanes,
J. Chem. Soc. Faraday Trans. 2, 1973, 69, 1187. [all data]
Stockbauer and Inghram, 1971
Stockbauer, R.; Inghram, M.G.,
Experimental relative Franck-Condon factors for the ionization of methane, ethane, and propane,
J. Chem. Phys., 1971, 54, 2242. [all data]
Dewar and Worley, 1969
Dewar, M.J.S.; Worley, S.D.,
Photoelectron spectra of molecules. I. Ionization potentials of some organic molecules and their interpretation,
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Williams and Hamill, 1968
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law 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 Pc Critical pressure Ptriple Triple point pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 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 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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