Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
369.20
K
0.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[82.31; 158.66]
J/mol×K
[273.00; 1000.00]
Joback Predicted correlation
Equation Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A 2.05610e+01
Coefficient B 2.71900e-01
Coefficient C -1.80000e-04
Coefficient D 4.62000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
82.31
J/mol×K
273.00
Calculated Property
Cp,gas
96.27
J/mol×K
353.78
Calculated Property
Cp,gas
108.52
J/mol×K
434.56
Calculated Property
Cp,gas
119.20
J/mol×K
515.33
Calculated Property
Cp,gas
128.47
J/mol×K
596.11
Calculated Property
Cp,gas
136.46
J/mol×K
676.89
Calculated Property
Cp,gas
143.33
J/mol×K
757.67
Calculated Property
Cp,gas
149.23
J/mol×K
838.44
Calculated Property
Cp,gas
154.29
J/mol×K
919.22
Calculated Property
Cp,gas
158.66
J/mol×K
1000.00
Calculated Property
Similar Compounds
Find more compounds similar to Acetic acid, mercapto- .
Mixtures
Acetic acid, butyl ester + Acetic acid, mercapto- + Water
Acetic acid, 2-methylpropyl ester + Acetic acid, mercapto- + Water
Acetic acid, mercapto- + Isopropyl acetate + Water
Diisopropyl ether + Acetic acid, mercapto- + Water
Propane, 2-methoxy-2-methyl- + Acetic acid, mercapto- + Water
Acetic acid, mercapto- + Water + 2-ethylhexyl thioglycolate
Acetic acid, mercapto- + Water
Acetic acid, butyl ester + Acetic acid, mercapto-
Formic acid, butyl ester + Acetic acid, mercapto-
Acetic acid, 2-methylpropyl ester + Acetic acid, mercapto-
Sources
Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
Cheméo Relay (1.0)
Crippen Method
Crippen Method
Liquid-liquid equilibrium measurement and thermodynamics modeling for the systems water + thioglycolic acid + isopropyl ether/methyl tert-butyl ether at 298.15 and 308.15 K
Measurement and thermodynamic modelling of ternary liquid-liquid equilibrium for extraction of thioglycolic acid from aqueous solution with different solvents
Separation of thioglycolic acid from its aqueous solution by ionic liquids: Ionic liquids selection by the COSMO-SAC model and liquid-liquid phase equilibrium
Isobaric Vapor Liquid Equilibrium for Binary Systems of Thioglycolic Acid with Water, Butyl Acetate, Butyl Formate, and Isobutyl Acetate at 101.3 kPa
Liquid-Liquid Equilibria for the Ternary Systems of Water + Thioglycolic Acid + 2-Ethyl-1-hexyl Thioglycolate and Water + 2-Ethyl-1-hexyl Thioglycolate + 2-Ethyl-1-hexanol at 293.15, 303.15, and 313.15 K under 101 kPa
Joback Method
McGowan Method
NIST Webbook
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