Carbon disulfide

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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

Quantity Value Units Method Reference Comment
Δfgas27.949kcal/molReviewChase, 1998Data last reviewed in December, 1976
Δfgas27.98 ± 0.19kcal/molCcrGood, Lacina, et al., 1961ALS
Quantity Value Units Method Reference Comment
Δcgas-265.8kcal/molCcbGuerin, Marthe, et al., 1949ALS
Quantity Value Units Method Reference Comment
gas,1 bar56.879cal/mol*KReviewChase, 1998Data last reviewed in December, 1976

Gas Phase Heat Capacity (Shomate Equation)

Cp° = A + B*t + C*t2 + D*t3 + E/t2
H° − H°298.15= A*t + B*t2/2 + C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 − E/(2*t2) + G
    Cp = heat capacity (cal/mol*K)
    H° = standard enthalpy (kcal/mol)
    S° = standard entropy (cal/mol*K)
    t = temperature (K) / 1000.

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View table.

Temperature (K) 298. to 1000.1000. to 6000.
A 8.56929114.63980
B 12.545700.329547
C -9.760381-0.033585
D 2.8684400.002219
E -0.053736-0.775345
F 24.7378121.52750
G 63.6137071.56049
H 27.9501027.95010
ReferenceChase, 1998Chase, 1998
Comment Data last reviewed in December, 1976 Data last reviewed in December, 1976

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
Δfliquid21.37 ± 0.17kcal/molCcrGood, Lacina, et al., 1961ALS
Quantity Value Units Method Reference Comment
Δcliquid-403.24 ± 0.12kcal/molCcrGood, Lacina, et al., 1961Reanalyzed by Cox and Pilcher, 1970, Original value = -402.09 ± 0.12 kcal/mol; ALS
Quantity Value Units Method Reference Comment
liquid36.09cal/mol*KN/ABrown and Manov, 1937DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
18.88298.Staveley, Tupman, et al., 1955T = 286 to 317 K.; DH
17.90294.81Zhdanov, 1945T = 7 to 31°C. Value is unsmoothed experimental datum.; DH
18.6293.Mazur, 1939T = -100 to 20°C.; DH
18.2301.2Phillip, 1939DH
18.17297.43Brown and Manov, 1937T = 15 to 297 K. Value is unsmoothed experimental datum.; DH

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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil319.2 ± 0.6KAVGN/AAverage of 13 out of 14 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus161. ± 3.KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple161.11KN/ABrown and Manov, 1937, 2Uncertainty assigned by TRC = 0.02 K; TRC
Ttriple161.59KN/AStull, 1937Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc552.KN/AMajer and Svoboda, 1985 
Quantity Value Units Method Reference Comment
Δvap6.6 ± 0.1kcal/molAVGN/AAverage of 6 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
6.391319.4N/AMajer and Svoboda, 1985 
6.86270.N/ADykyj, Svoboda, et al., 1999Based on data from 255. to 354. K.; AC
6.48369.N/ADykyj, Svoboda, et al., 1999Based on data from 354. to 552. K.; AC
6.81275.AStephenson and Malanowski, 1987Based on data from 260. to 353. K.; AC
6.55353.AStephenson and Malanowski, 1987Based on data from 338. to 408. K.; AC
6.45403.AStephenson and Malanowski, 1987Based on data from 388. to 497. K.; AC
6.86505.AStephenson and Malanowski, 1987Based on data from 490. to 533. K.; AC
6.86270.EBBoublík and Aim, 1972Based on data from 255. to 318. K. See also Stephenson and Malanowski, 1987.; AC
6.72292.EBWaddington, Smith, et al., 1962Based on data from 277. to 353. K.; AC
6.72 ± 0.02282.CWaddington, Smith, et al., 1962AC
6.38 ± 0.02319.CWaddington, Smith, et al., 1962AC
6.60318.N/AThomson, 1946Based on data from 303. to 358. 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)

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Temperature (K) A (kcal/mol) β Tc (K) Reference Comment
282. to 319.8.8600.2264552.Majer and Svoboda, 1985 

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (atm)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
276.74 to 353.084.061121168.62-31.616Waddington, Smith, et al., 1962Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
1.049161.11Brown and Manov, 1937DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
6.511161.11Brown and Manov, 1937DH

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.

Chase, 1998
Chase, M.W., Jr., NIST-JANAF Themochemical Tables, Fourth Edition, J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]

Good, Lacina, et al., 1961
Good, W.D.; Lacina, J.L.; McCullough, J.P., Methanethiol and carbon disulfide: Heats of combustion and formation by rotating-bomb calorimetry, J. Phys. Chem., 1961, 65, 2229-2231. [all data]

Guerin, Marthe, et al., 1949
Guerin, M.H.; Marthe, M.; Bastick, J.; Adam-Gironne, J., Sur la chaleur de combustion du sulfure de carbon, Compt. Rend., 1949, 228, 87-89. [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]

Brown and Manov, 1937
Brown, O.L.I.; Manov, G.G., The heat capacity of carbon disulfide from 15 to 300°K. The entropy and heat of fusion of carbon disulfide, J. Am. Chem. Soc., 1937, 59, 500-502. [all data]

Staveley, Tupman, et al., 1955
Staveley, L.A.K.; Tupman, W.I.; Hart, K.R., Some thermodynamice properties of the systems benzene + ethylene dichloride, benzene + carbon tetrachloride, acetone + chloroform, and acetone + carbon disulphide, Trans. Faraday Soc., 1955, 51, 323-342. [all data]

Zhdanov, 1945
Zhdanov, A.K., On the thermal capacity of some pure liquids and azeotropic mixtures, Zhur. Obshch. Khim., 1945, 15, 895-902. [all data]

Mazur, 1939
Mazur, J., Über die spezifische Wärme des Äthyläthers, des Nitrobenzols und des Schwefelkohlenstoffs, Z. Physik., 1939, 113, 710-720. [all data]

Phillip, 1939
Phillip, N.M., Adiabatic and isothermal compressibilities of liquids, Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]

Brown and Manov, 1937, 2
Brown, O.L.I.; Manov, G.G., The heat capacity of carbon disulfide from 15 to 300 k: the entropy and heat of fusion of carbon disulfide, J. Am. Chem. Soc., 1937, 59, 500. [all data]

Stull, 1937
Stull, D.R., A Semi-micro Calorimeter for Measuring Heat Capacities at Low Temp., J. Am. Chem. Soc., 1937, 59, 2726. [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]

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]

Boublík and Aim, 1972
Boublík, T.; Aim, K., Heats of vaporization of simple non-spherical molecule compounds, Collect. Czech. Chem. Commun., 1972, 37, 11, 3513-3521, https://doi.org/10.1135/cccc19723513 . [all data]

Waddington, Smith, et al., 1962
Waddington, Guy; Smith, J.C.; Williamson, K.D.; Scott, D.W., CARBON DISULFIDE AS A REFERENCE SUBSTANCE FOR VAPOR-FLOW CALORIMETRY; THE CHEMICAL THERMODYNAMIC PROPERTIES, J. Phys. Chem., 1962, 66, 6, 1074-1077, https://doi.org/10.1021/j100812a025 . [all data]

Thomson, 1946
Thomson, George Wm., The Antoine Equation for Vapor-pressure Data., Chem. Rev., 1946, 38, 1, 1-39, https://doi.org/10.1021/cr60119a001 . [all data]


Notes

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