Hexane, 1-chloro-

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Condensed 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 by: Eugene S. Domalski and Elizabeth D. Hearing

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference
216.2298.15Shehatta, 1993

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:
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

Quantity Value Units Method Reference Comment
Tboil407.7KN/AWeast and Grasselli, 1989BS
Tboil408.22KN/APaul, Krug, et al., 1988Uncertainty assigned by TRC = 0.08 K; TRC
Tboil408.1KN/AMajer and Svoboda, 1985 
Tboil407.45KN/AMumford and Phillips, 1950Uncertainty assigned by TRC = 0.3 K; TRC
Quantity Value Units Method Reference Comment
Tfus179.15KN/ATimmermans, 1952Uncertainty assigned by TRC = 1.2 K; TRC
Quantity Value Units Method Reference Comment
Tc594.6KN/AMajer and Svoboda, 1985 
Quantity Value Units Method Reference Comment
Δvap42.7 ± 0.6kJ/molAVGN/AAverage of 6 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
35.67408.1N/AMajer and Svoboda, 1985 
41.1334.N/ACabezas, Barcena, et al., 1988Based on data from 319. to 376. K.; AC
43.5303.A,DTAStephenson and Malanowski, 1987Based on data from 288. to 409. K. See also Kemme and Kreps, 1969 and Dykyj, 1972.; AC
40.5 ± 0.1328.CTekac, Majer, et al., 1981AC
40.0 ± 0.1343.CTekac, Majer, et al., 1981AC
39.0 ± 0.1358.CTekac, Majer, et al., 1981AC
38.4 ± 0.1368.CTekac, Majer, et al., 1981AC

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
298. to 368.60.060.2824594.6Majer 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
288. to 408.83.893761304.968-73.092Kemme and Kreps, 1969

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:


Henry's Law 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 by: Rolf Sander

Henry's Law constant (water solution)

kH(T) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference
0.0414500.XLeighton and Calo, 1981

References

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

Shehatta, 1993
Shehatta, I., Heat capacity at constant pressure of some halogen compounds, Thermochim. Acta, 1993, 213, 1-10. [all data]

Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]

Paul, Krug, et al., 1988
Paul, H.-I.; Krug, J.; Knapp, H., Measurements of VLE, vE, and hE for binary mixtures of 1-chlorohexane with three n-alkylbenzenes: toluene, ethylbenzene, n-propylbenzene, J. Chem. Eng. Data, 1988, 33, 453. [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]

Mumford and Phillips, 1950
Mumford, S.A.; Phillips, J.W.C., 19. The Physical Properties of Some Aliphatic Compounds, J. Chem. Soc., 1950, 1950, 75-84. [all data]

Timmermans, 1952
Timmermans, J., Freezing points of organic compounds. VVI New determinations., Bull. Soc. Chim. Belg., 1952, 61, 393. [all data]

Cabezas, Barcena, et al., 1988
Cabezas, Jose L.; Barcena, Lucas A.; Coca, Jose; Cockrem, Michael, Extraction of furfural from aqueous solutions using alcohols, J. Chem. Eng. Data, 1988, 33, 4, 435-437, https://doi.org/10.1021/je00054a014 . [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]

Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I., Vapor pressure of primary n-alkyl chlorides and alcohols, J. Chem. Eng. Data, 1969, 14, 1, 98-102, https://doi.org/10.1021/je60040a011 . [all data]

Dykyj, 1972
Dykyj, J., Petrochemia, 1972, 12, 1, 13. [all data]

Tekac, Majer, et al., 1981
Tekac, V.; Majer, V.; Svoboda, V.; Hynek, V., Enthalpies of vaporization and cohesive energies for six monochlorinated alkanes, J. Chem. Thermodyn., 1981, 13, 659-662. [all data]

Leighton and Calo, 1981
Leighton, D.T.; Calo, J.M., Distribution Coefficients of Chlorinated Hydrocarbons in Dilute Air-Water Systems for Groundwater Contamination Applications, J. Chem. Eng. Data, 1981, 26, 382-385. [all data]


Notes

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