Dimethyl sulfide

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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.

Quantity Value Units Method Reference Comment
Δfgas-8.96 ± 0.48kcal/molCcbVoronkov, Klyuchnikov, et al., 1989ALS
Δfgas-8.98 ± 0.14kcal/molCcrMcCullough, Hubbard, et al., 1957ALS
Δfgas-7.74kcal/molN/ADouglas, 1946Value computed using ΔfHliquid° value of -60.2 kj/mol from Douglas, 1946 and ΔvapH° value of 27.8 kj/mol from McCullough, Hubbard, et al., 1957.; DRB

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
DRB - Donald R. Burgess, Jr.

Quantity Value Units Method Reference Comment
Tboil311. ± 3.KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus174.88KN/AHaines, Helm, et al., 1956Uncertainty assigned by TRC = 0.06 K; TRC
Tfus174.90KN/AMcallan, Cullum, et al., 1951Uncertainty assigned by TRC = 0.1 K; TRC
Quantity Value Units Method Reference Comment
Ttriple174.85KN/AOsborne, Doescher, et al., 1942Uncertainty assigned by TRC = 0.03 K; TRC
Quantity Value Units Method Reference Comment
Tc503.KN/AMajer and Svoboda, 1985 
Tc503.0KN/ABerthoud and Brum, 1924Uncertainty assigned by TRC = 0.4 K; by disappearance of meniscus; TRC
Tc503.0KN/ABerthoud and Brum, 1924Uncertainty assigned by TRC = 0.4 K; by apperanance of turbidity; TRC
Quantity Value Units Method Reference Comment
Pc54.58atmN/ABerthoud and Brum, 1924Uncertainty assigned by TRC = 0.4000 atm; vapor pressure at Tc; TRC
Quantity Value Units Method Reference Comment
ρc4.972mol/lN/ABerthoud and Brum, 1924Uncertainty assigned by TRC = 0.03 mol/l; TRC
ρc4.84mol/lN/AHerz and Neukirch, 1923Uncertainty assigned by TRC = 0.03 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap6.65 ± 0.07kcal/molAVGN/AAverage of 8 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
6.5310.5N/AMajer and Svoboda, 1985 
6.91283.AStephenson and Malanowski, 1987Based on data from 268. to 319. K.; AC
6.62322.AStephenson and Malanowski, 1987Based on data from 307. to 379. K.; AC
6.36387.AStephenson and Malanowski, 1987Based on data from 372. to 453. K.; AC
6.38462.AStephenson and Malanowski, 1987Based on data from 447. to 503. K.; AC
6.88 ± 0.02276.CMcCullough, Hubbard, et al., 1957AC
6.67 ± 0.02292.CMcCullough, Hubbard, et al., 1957AC
6.45 ± 0.02310.CMcCullough, Hubbard, et al., 1957AC
6.74302.EBWhite, Barnard--Smith, et al., 1952Based on data from 287. to 318. K.; AC
6.91278.N/AOsborne, Doescher, et al., 1942, 2Based on data from 251. to 293. K.; AC
6.91310.N/AThompson and Linnett, 1935AC

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
276. to 311.9.9280.2731503.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
250.60 to 293.244.281421201.134-29.906Osborne, Doescher, et al., 1942, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
1.91174.9Domalski and Hearing, 1996AC

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 Comment
0.483100.MN/A 
0.080 EN/ACalculated molecular structure relationship.
0.483500.XN/AValue given here as quoted by missing citation.
0.563500.MN/A 
0.62 XN/AValue given here as quoted by missing citation.
0.44 CN/A missing citation refer to an unpublished manuscript; no details are available. Solubility in sea water.
0.563700.MN/A 
0.61 MN/AValue at T = 293. K.
0.70 RN/AValue at T = 293. K.
0.16 MN/A 
0.55 VN/A 

References

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Notes

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

Voronkov, Klyuchnikov, et al., 1989
Voronkov, M.G.; Klyuchnikov, V.A.; Kolabin, S.N.; Shvets, G.N.; Varusin, P.I.; Deryagina, E.N.; Korchevin, N.A.; Tsvetnitskaya, S.I., Thermochemical properties of diorganyl chalcogenides and dichalcogenides RMnR(M = S, Se, Te; n = 1, 2)., Dokl. Phys. Chem. (Engl. Transl.), 1989, 307, 650-653, In original 1139. [all data]

McCullough, Hubbard, et al., 1957
McCullough, J.P.; Hubbard, W.N.; Frow, F.R.; Hossenlopp, I.A.; Waddington, G., Ethanethiol and 2-thiapropane: Heats of formation and isomerization; the chemical thermodynamic properties from 0 to 1000°K, J. Am. Chem. Soc., 1957, 79, 561-566. [all data]

Douglas, 1946
Douglas, T.B., Heats of formation of liquid methyl sulfoxide and crystalline methyl sulfone at 18°, J. Am. Chem. Soc., 1946, 68, 1072-1076. [all data]

Haines, Helm, et al., 1956
Haines, W.E.; Helm, R.V.; Cook, G.L.; Ball, J.S., Purification and Properties of Organic Sulfur Compounds, J. Phys. Chem., 1956, 60, 549-55. [all data]

Mcallan, Cullum, et al., 1951
Mcallan, D.T.; Cullum, T.V.; Dean, R.A.; Fidler, F.A., The Preparation and Properties of Sulfur Compounds Related to Petroleum I. The Dialkyl Sulfides and Disulfides, J. Am. Chem. Soc., 1951, 73, 3627-32. [all data]

Osborne, Doescher, et al., 1942
Osborne, D.W.; Doescher, R.N.; Yost, D.M., The heat capacity, heats of fusion and vaporization, vapor pressure and entropy of dimethyl sulfide., J. Am. Chem. Soc., 1942, 64, 169-72. [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]

Berthoud and Brum, 1924
Berthoud, A.; Brum, R., Physical Properties of Some Organic Compounds., J. Chim. Phys. Phys.-Chim. Biol., 1924, 21, 143-60. [all data]

Herz and Neukirch, 1923
Herz, W.; Neukirch, E., On Knowldge of the Critical State, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1923, 104, 433-50. [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]

White, Barnard--Smith, et al., 1952
White, P.T.; Barnard--Smith, D.G.; Fidler, F.A., Vapor Pressure--Temperature Relationships of Sulfur Compounds Related to Petroleum, Ind. Eng. Chem., 1952, 44, 6, 1430-1438, https://doi.org/10.1021/ie50510a064 . [all data]

Osborne, Doescher, et al., 1942, 2
Osborne, D.W.; Doescher, R.N.; Yost, D.M., The heat capacity, heats of fusion and vaporization, vapor pressure and entropy of dimethyl sulfide, J. Am. Chem. Soc., 1942, 64, 169-172. [all data]

Thompson and Linnett, 1935
Thompson, H.W.; Linnett, J.W., The vapour pressures of some alkyl sulphides, Trans. Faraday Soc., 1935, 31, 1743, https://doi.org/10.1039/tf9353101743 . [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

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