Butane, 2,2,3-trimethyl-

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Gas phase thermochemistry 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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-204.8 ± 1.1kJ/molCcbProsen and Rossini, 1945ALS
Δfgas-205.9kJ/molN/ADavies and Gilbert, 1941Value computed using ΔfHliquid° value of -238.0±1.0 kj/mol from Davies and Gilbert, 1941 and ΔvapH° value of 32.1 kj/mol from Prosen and Rossini, 1945.; DRB

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
111.46200.Scott D.W., 1974Recommended values were obtained from the consistent correlation scheme for alkanes [ Scott D.W., 1974, 2, Scott D.W., 1974]. This approach gives a good agreement with experimental data available for alkanes. Results of statistical thermodynamics calculation for 2,2,3-trimethylbutane [ Scott D.W., 1953] also agree well with experimental data at low temperatures. However, the values of S and Cp at 1500 K are 15 and 33 J/mol*K below than those given by [ Scott D.W., 1974].; GT
150.46273.15
163.3 ± 0.4298.15
164.22300.
212.84400.
256.06500.
293.72600.
326.35700.
355.22800.
380.74900.
402.921000.
422.581100.
440.161200.
456.061300.
468.611400.
481.161500.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
178.82 ± 0.18328.80Waddington G., 1947GT
188.66 ± 0.19348.85
198.28 ± 0.20369.20
213.05 ± 0.21400.40
228.20 ± 0.23434.30
239.99 ± 0.24461.80

Condensed phase thermochemistry data

Go To: Top, Gas phase 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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Δfliquid-236.9 ± 1.1kJ/molCcbProsen and Rossini, 1945ALS
Δfliquid-238. ± 1.kJ/molCcbDavies and Gilbert, 1941ALS
Quantity Value Units Method Reference Comment
Δcliquid-4803.99 ± 0.50kJ/molCmCoops, Mulder, et al., 1946Reanalyzed by Cox and Pilcher, 1970, Original value = -4802.1 ± 0.3 kJ/mol; Corresponding Δfliquid = -237.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-4804.4 ± 1.0kJ/molCcbProsen and Rossini, 1945Corresponding Δfliquid = -236.9 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-4803. ± 1.kJ/molCcbDavies and Gilbert, 1941Corresponding Δfliquid = -238.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid292.25J/mol*KN/AHuffman, Gross, et al., 1961DH
liquid27.11J/mol*KN/AHuffman, Parks, et al., 1930Extrapolation below 90 K, 14.0 cal mol-1 K-1.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
213.51298.15Huffman, Gross, et al., 1961T = 10 to 300 K.; DH
208.4293.9Huffman, Parks, et al., 1930T = 89 to 294 K. Value is unsmoothed experimental datum.; DH

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

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]

Davies and Gilbert, 1941
Davies, G.F.; Gilbert, E.C., Heats of combustion and formation of the nine isomeric heptanes in the liquid state, J. Am. Chem. Soc., 1941, 63, 2730-2732. [all data]

Scott D.W., 1974
Scott D.W., Chemical Thermodynamic Properties of Hydrocarbons and Related Substances. Properties of the Alkane Hydrocarbons, C1 through C10 in the Ideal Gas State from 0 to 1500 K. U.S. Bureau of Mines, Bulletin 666, 1974. [all data]

Scott D.W., 1974, 2
Scott D.W., Correlation of the chemical thermodynamic properties of alkane hydrocarbons, J. Chem. Phys., 1974, 60, 3144-3165. [all data]

Scott D.W., 1953
Scott D.W., Thermodynamic functions of 2,2,3-trimethylbutane, J. Am. Chem. Soc., 1953, 75, 2006-2007. [all data]

Waddington G., 1947
Waddington G., An improved flow calorimeter. Experimental vapor heat capacities and heats of vaporization of n-heptane and 2,2,3-trimethylbutane, J. Am. Chem. Soc., 1947, 69, 22-30. [all data]

Coops, Mulder, et al., 1946
Coops, J.; Mulder, D.; Dienske, J.W.; Smittenberg, J., The heats of combustion of a number of hydrocarbons, Rec. Trav. Chim. Pays/Bas, 1946, 65, 128. [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]

Huffman, Gross, et al., 1961
Huffman, H.M.; Gross, M.E.; Scott, D.W.; McCullough, I.P., Low temperature thermodynamic properties of six isomeric heptanes, J. Phys. Chem., 1961, 65, 495-503. [all data]

Huffman, Parks, et al., 1930
Huffman, H.M.; Parks, G.S.; Thomas, S.B., Thermal data on organic compounds. VIII. The heat capacities, entropies and free energies of the isomeric heptanes, J. Am. Chem. Soc., 1930, 52, 3241-3251. [all data]


Notes

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