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:
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Gas phase thermochemistry data
Go To: Top, Phase change data, 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:
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 |
Phase change data
Go To: Top, Gas phase thermochemistry data, 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:
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 |
Mass spectrum (electron ionization)
Go To: Top, Gas phase thermochemistry data, Phase change 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
View image of digitized spectrum (can be printed in landscape orientation).
Due to licensing restrictions, this spectrum cannot be downloaded.
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 | 23 |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, 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.
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]
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]
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]
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]
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]
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]
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]
Roder, 1976
Roder, H.M.,
The heats of transition of solid ethane,
J. Chem. Phys., 1976, 65, 1371-1373. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Mass spectrum (electron ionization), References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Pc Critical pressure Ptriple Triple point pressure 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 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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