Propane, 2-methyl-2-(methylthio)-

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Gas phase thermochemistry data

Go To: Top, Condensed 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: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein

Quantity Value Units Method Reference Comment
Δfgas-121.0 ± 0.75kJ/molCcbScott, Good, et al., 1962 

Condensed phase thermochemistry data

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 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-156.9 ± 0.75kJ/molCcbScott, Good, et al., 1962ALS
Quantity Value Units Method Reference Comment
Δcliquid-4127.2 ± 0.63kJ/molCcbScott, Good, et al., 1962ALS
Quantity Value Units Method Reference Comment
liquid276.14J/mol*KN/AScott, Good, et al., 1962DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
199.95298.15Scott, Good, et al., 1962T = 15 to 364 K.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed 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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil373. ± 3.KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus190.85KN/ALanum and Morris, 1969Uncertainty assigned by TRC = 0.2 K; TRC
Tfus190.9KN/AAnonymous, 1952Uncertainty assigned by TRC = 0.3 K; TRC
Quantity Value Units Method Reference Comment
Ttriple190.84KN/AScott, Good, et al., 1962, 2Uncertainty assigned by TRC = 0.02 K; TRC
Ttriple184.86KN/AScott, Good, et al., 1962, 2Metastable crystal phase; Uncertainty assigned by TRC = 0.06 K; TRC
Quantity Value Units Method Reference Comment
Tc569.8KN/AMajer and Svoboda, 1985 
Quantity Value Units Method Reference Comment
Δvap35.9kJ/molN/AMajer and Svoboda, 1985 
Δvap34.2kJ/molN/ASawaya, Mokbel, et al., 2004Based on data from 245. to 352. K.; AC
Δvap35.9kJ/molN/AReid, 1972AC
Δvap35.8kJ/molVScott, Good, et al., 1962ALS
Δvap35.9kJ/molN/AScott, Good, et al., 1962DRB

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
31.47372.1N/AMajer and Svoboda, 1985 
36.5291.N/ADykyj, Svoboda, et al., 1999Based on data from 276. to 397. K.; AC
35.1320.A,EBStephenson and Malanowski, 1987Based on data from 305. to 411. K. See also Scott, Good, et al., 1962, 3 and Osborn and Douslin, 1966.; AC

Enthalpy of vaporization

ΔvapH = A exp(-βTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kJ/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) A (kJ/mol) β Tc (K) Reference Comment
330. to 372.51.750.2906569.8Majer and Svoboda, 1985 

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
306.86 to 410.243.972041259.672-54.455Scott, Good, et al., 1962Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
8.414190.84Scott, Good, et al., 1962DH
8.41190.8Domalski and Hearing, 1996AC

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
44.09190.84Scott, Good, et al., 1962DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


References

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

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

Scott, Good, et al., 1962
Scott, D.W.; Good, W.D.; Todd, S.S.; Messerly, J.F.; Berg, W.T.; Hossenlopp, I.A.; Lacina, J.L.; Osborn, A.; McCullough, J.P., 3,3-Dimethyl-2-thiabutane: Chemical thermodynamic properties and barriers to internal rotation, J. Chem. Phys., 1962, 36, 406-412. [all data]

Lanum and Morris, 1969
Lanum, W.J.; Morris, J.C., Physical Properties of Some Sulfur and Nitrogen Compounds, J. Chem. Eng. Data, 1969, 14, 93-8. [all data]

Anonymous, 1952
Anonymous, R., , Physical Properties of Chemical Substances, Dow Chemical Co., 1952. [all data]

Scott, Good, et al., 1962, 2
Scott, D.W.; Good, W.D.; Todd, S.S.; Messerly, J.F.; Berg, W.T.; Hossenlopp, I.A.; Lacina, J.L.; Osborn, A.G.; McCullough, J.P., 3,3-Dimethyl-2-Thiabutane: Chemical Thermodynamic Properties and Barriers to Internal Rotation, J. Chem. Phys., 1962, 36, 406-12. [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]

Sawaya, Mokbel, et al., 2004
Sawaya, Terufat; Mokbel, Ilham; Rauzy, Evelyne; Saab, Joseph; Berro, Charles; Jose, Jacques, Experimental vapor pressures of alkyl and aryl sulfides, Fluid Phase Equilibria, 2004, 226, 283-288, https://doi.org/10.1016/j.fluid.2004.10.007 . [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]

Dykyj, Svoboda, et al., 1999
Dykyj, J.; Svoboda, J.; Wilhoit, R.C.; Frenkel, M.L.; Hall, K.R., Vapor Pressure of Chemicals: Part A. Vapor Pressure and Antoine Constants for Hydrocarbons and Sulfur, Selenium, Tellurium and Hydrogen Containing Organic Compounds, Springer, Berlin, 1999, 373. [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]

Scott, Good, et al., 1962, 3
Scott, D.W.; Good, W.D.; Todd, S.S.; Messerly, J.F.; Berg, W.T.; Hossenlopp, I.A.; Lacina, J.L.; Osborn, Ann; McCullough, J.P., 3,3-Dimethyl-2-Thiabutane: Chemical Thermodynamic Properties and Barriers to Internal Rotation, J. Chem. Phys., 1962, 36, 2, 406, https://doi.org/10.1063/1.1732519 . [all data]

Osborn and Douslin, 1966
Osborn, A.G.; Douslin, D.R., Vapor Pressure Relations of 36 Sulfur Compounds Present in Petroleum., J. Chem. Eng. Data, 1966, 11, 4, 502-509, https://doi.org/10.1021/je60031a014 . [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]


Notes

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, References