Physical Properties
Property
Value
Unit
Source
ω
0.1910
KDB
PAff
830.90
kJ/mol
NIST
BasG
801.20
kJ/mol
NIST
Δc H°liquid
-2181.50 ± 0.30
kJ/mol
NIST
μ
1.50
debye
KDB
Δf G°
6.95
kJ/mol
KDB
Δf H°gas
[-37.60; -32.40]
kJ/mol
Δf H°gas
-37.56
kJ/mol
KDB
Δf H°gas
-37.50 ± 2.00
kJ/mol
NIST
Δf H°gas
-37.60 ± 0.59
kJ/mol
NIST
Δf H°gas
-32.40
kJ/mol
NIST
Δf H°liquid
[-65.44; -60.20]
kJ/mol
Δf H°liquid
-65.40 ± 1.50
kJ/mol
NIST
Δf H°liquid
-65.44 ± 0.59
kJ/mol
NIST
Δf H°liquid
-60.20
kJ/mol
NIST
Δfus H°
5.07
kJ/mol
Joback Calculated Property
Δvap H°
[27.50; 27.99]
kJ/mol
Δvap H°
27.99
kJ/mol
NIST
Δvap H°
27.90 ± 0.60
kJ/mol
NIST
Δvap H°
27.90 ± 0.60
kJ/mol
NIST
Δvap H°
27.90
kJ/mol
NIST
Δvap H°
Outlier 27.50
kJ/mol
NIST
Δvap H°
27.70
kJ/mol
NIST
Δvap H°
27.80 ± 0.04
kJ/mol
NIST
Δvap H°
27.80
kJ/mol
NIST
IE
[8.50; 8.72]
eV
IE
8.69 ± 0.02
eV
NIST
IE
8.60
eV
NIST
IE
8.72
eV
NIST
IE
Outlier 8.50 ± 0.10
eV
NIST
IE
8.60
eV
NIST
IE
8.69
eV
NIST
IE
8.71 ± 0.01
eV
NIST
IE
8.67
eV
NIST
IE
8.57 ± 0.04
eV
NIST
IE
8.70
eV
NIST
IE
8.69 ± 0.01
eV
NIST
IE
8.68 ± 0.03
eV
NIST
IE
8.70 ± 0.10
eV
NIST
IE
8.69 ± 0.01
eV
NIST
IE
8.67
eV
NIST
IE
8.70
eV
NIST
IE
8.70
eV
NIST
IE
8.71
eV
NIST
IE
8.71
eV
NIST
IE
8.67
eV
NIST
IE
8.65
eV
NIST
IE
8.65
eV
NIST
IE
8.71
eV
NIST
IE
8.67
eV
NIST
log 10 WS
[-0.45; -0.45]
log 10 WS
-0.45
Aq. Sol...
log 10 WS
-0.45
Estimat...
log Poct/wat
0.979
Crippen Calculated Property
McVol
55.390
ml/mol
McGowan Calculated Property
NFPA Fire
4
KDB
NFPA Health
4
KDB
Pc
[5530.00; 5530.00]
kPa
Pc
5530.00
kPa
KDB
Pc
5530.00 ± 40.53
kPa
NIST
ρc
[300.73; 308.93]
kg/m3
ρc
308.93 ± 1.86
kg/m3
NIST
ρc
300.73 ± 1.86
kg/m3
NIST
Inp
[493.00; 565.00]
Inp
533.70
NIST
Inp
543.60
NIST
Inp
532.00
NIST
Inp
530.20
NIST
Inp
528.00
NIST
Inp
508.00
NIST
Inp
523.00
NIST
Inp
522.00
NIST
Inp
520.00
NIST
Inp
500.00
NIST
Inp
497.00
NIST
Inp
500.00
NIST
Inp
497.00
NIST
Inp
520.00
NIST
Inp
532.00
NIST
Inp
516.00
NIST
Inp
515.00
NIST
Inp
516.00
NIST
Inp
523.00
NIST
Inp
528.00
NIST
Inp
Outlier 550.00
NIST
Inp
526.00
NIST
Inp
500.00
NIST
Inp
505.00
NIST
Inp
513.00
NIST
Inp
515.00
NIST
Inp
517.00
NIST
Inp
526.00
NIST
Inp
516.00
NIST
Inp
515.00
NIST
Inp
500.00
NIST
Inp
509.00
NIST
Inp
511.00
NIST
Inp
Outlier 550.00
NIST
Inp
521.00
NIST
Inp
514.00
NIST
Inp
532.00
NIST
Inp
518.00
NIST
Inp
505.00
NIST
Inp
505.00
NIST
Inp
506.00
NIST
Inp
495.00
NIST
Inp
523.00
NIST
Inp
523.00
NIST
Inp
516.00
NIST
Inp
538.00
NIST
Inp
500.00
NIST
Inp
505.00
NIST
Inp
525.00
NIST
Inp
527.00
NIST
Inp
508.00
NIST
Inp
522.00
NIST
Inp
527.00
NIST
Inp
508.00
NIST
Inp
508.00
NIST
Inp
514.00
NIST
Inp
529.00
NIST
Inp
515.00
NIST
Inp
526.00
NIST
Inp
534.00
NIST
Inp
Outlier 565.00
NIST
Inp
507.00
NIST
Inp
521.00
NIST
Inp
517.00
NIST
Inp
517.00
NIST
Inp
523.00
NIST
Inp
Outlier 550.00
NIST
Inp
543.00
NIST
Inp
528.00
NIST
Inp
521.00
NIST
Inp
521.00
NIST
Inp
503.00
NIST
Inp
508.00
NIST
Inp
503.00
NIST
Inp
506.00
NIST
Inp
506.00
NIST
Inp
508.00
NIST
Inp
527.00
NIST
Inp
512.00
NIST
Inp
493.00
NIST
Inp
526.00
NIST
Inp
513.00
NIST
Inp
515.00
NIST
I
[715.00; 793.00]
I
774.00
NIST
I
777.00
NIST
I
777.00
NIST
I
769.00
NIST
I
760.00
NIST
I
760.00
NIST
I
716.00
NIST
I
720.00
NIST
I
729.00
NIST
I
725.00
NIST
I
757.00
NIST
I
754.00
NIST
I
757.00
NIST
I
757.00
NIST
I
745.00
NIST
I
715.00
NIST
I
763.00
NIST
I
737.00
NIST
I
751.00
NIST
I
773.00
NIST
I
773.00
NIST
I
733.00
NIST
I
755.00
NIST
I
755.00
NIST
I
757.00
NIST
I
772.00
NIST
I
751.00
NIST
I
753.00
NIST
I
748.00
NIST
I
746.00
NIST
I
754.00
NIST
I
745.00
NIST
I
748.00
NIST
I
716.00
NIST
I
746.00
NIST
I
740.00
NIST
I
753.00
NIST
I
740.00
NIST
I
757.00
NIST
I
Outlier 793.00
NIST
I
716.00
NIST
I
757.00
NIST
I
755.00
NIST
I
753.00
NIST
I
748.00
NIST
I
774.00
NIST
I
777.00
NIST
I
720.00
NIST
Tboil
[310.48; 316.20]
K
Tboil
310.48
K
KDB
Tboil
310.50
K
NIST
Tboil
310.50
K
NIST
Tboil
310.60 ± 0.30
K
NIST
Tboil
311.20 ± 2.00
K
NIST
Tboil
310.50 ± 0.30
K
NIST
Tboil
310.60 ± 0.50
K
NIST
Tboil
Outlier 316.20 ± 0.60
K
NIST
Tboil
310.50 ± 0.50
K
NIST
Tboil
310.55 ± 0.30
K
NIST
Tc
[503.00; 503.00]
K
Tc
503.00
K
KDB
Tc
503.00
K
NIST
Tc
503.00 ± 0.40
K
NIST
Tc
503.00 ± 0.40
K
NIST
Tfus
[174.80; 178.82]
K
Tfus
178.82
K
Aq. Sol...
Tfus
174.80
K
KDB
Tfus
174.88 ± 0.06
K
NIST
Tfus
174.90 ± 0.10
K
NIST
Ttriple
174.85 ± 0.03
K
NIST
Vc
0.201
m3 /kmol
KDB
Zc
0.2657760
KDB
Zra
0.27
KDB
Temperature Dependent Properties
Correlations
Similar Compounds
Find more compounds similar to Dimethyl sulfide .
Mixtures
Dimethyl sulfide + Methane
Dimethyl sulfide + Hydrogen sulfide
Dimethyl sulfide + 1-Butene
Dimethyl sulfide + 2-Butene, (Z)-
Dimethyl sulfide + 2-Butene, (E)-
Dimethyl sulfide + 1-Propene, 2-methyl-
Dimethyl sulfide + Butane
Dimethyl sulfide + Isobutane
Dimethyl sulfide + n-Hexane
Dimethyl sulfide + 1-Hexene
Dimethyl sulfide + Pentane, 2,2,4-trimethyl-
Dimethyl sulfide + 1-Pentene, 2,4,4-trimethyl-
Dimethyl sulfide + Propane
Dimethyl sulfide + Ethanol
Dimethyl sulfide + Acetic acid, methyl ester
Dimethyl sulfide + Dimethyl ether
Dimethyl sulfide + Water
Dimethyl sulfide + Methyldiethanolamine + Water
Sources
KDB Pure (Korean Thermophysical Properties Databank)
KDB Vapor Pressure Data
Crippen Method
Measurement of VLE (TPx or TPxy data) for hydrogen sulfide + (dimethylsulfide or ethylmethylsulfide or carbon disulfide) and methane solubilities in (dimethylsulfide or ethylmethylsulfide or methylmercaptan or ethylmercaptan)
Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
Measurement and correlation for the solubility of dimethyl succinylsuccinate in (methanol + water) and (methanol + dimethyl succinate) binary solvent mixtures
Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
Measurement of Henry s Law Constants and Infinite Dilution Activity Coefficients of Propyl Mercaptan, Butyl Mercaptan, and Dimethyl Sulfide in Methyldiethanolamine (1) + Water (2) with w1 ) 0.50 Using a Gas Stripping Technique
Liquid-Liquid Equilibria on Three Binary Systems: Methyl Cyclopropanecarboxalate + Water; Dimethyl Sulfide + Water; and Dimethyl Disulfide + Water
Limiting Separation Factors and Limiting Activity Coefficients for Hexanal, 2-Methylbutanal, 3-Methylbutanal, and Dimethylsulfide in Water at (98.1 to 99.0) deg C
Measurement through a Gas Stripping Technique of Henry's Law Constants and Infinite Dilution Activity Coefficients of Propyl Mercaptan, Butyl Mercaptan, and Dimethyl Sulfide in Methyldiethanolamine (1) + Water (2) with w1 = 0.25 and 0.35
Joback Method
KDB
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.