Mixture of Dimethyl Sulfoxide + Tetrahydrofuran

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Dimethyl Sulfoxide

Name
Dimethyl Sulfoxide
InChI
InChI=1S/C2H6OS/c1-4(2)3/h1-2H3
InChI Key
IAZDPXIOMUYVGZ-UHFFFAOYSA-N
Formula
C2H6OS
SMILES
CS(C)=O
Mol. Weight (g/mol)
78.13
CAS
67-68-5

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
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Datasets

  1. Activity coefficient (2)
  2. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
  3. η - Viscosity, Pa*s (2)
  4. Excess molar enthalpy (molar enthalpy (2)
  5. ρl - Mass density, kg/m3 (2)

Activity coefficient of Tetrahydrofuran (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Activity coefficient of Tetrahydrofuran (2) - Liquid
298.15 0.0000 3.32

Activity coefficient of Tetrahydrofuran (2) [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Activity coefficient of Tetrahydrofuran (2) - Liquid
298.15 0.0000 3.32

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0807 132.90
0.1171 133.60
0.2353 135.90
0.3233 137.70
0.4932 141.40
0.5284 142.30
0.5833 143.60
0.6359 144.90
0.7298 147.20
0.8269 149.80
0.8930 151.60
0.9507 153.20

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (1) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0807 132.90
0.1171 133.60
0.2353 135.90
0.3233 137.70
0.4932 141.40
0.5284 142.30
0.5833 143.60
0.6359 144.90
0.7298 147.20
0.8269 149.80
0.8930 151.60
0.9507 153.20

Viscosity, Pa*s [ref]

Operational conditions:

Mass fraction of Tetrahydrofuran (2) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0020
0.2500 0.0015
0.5000 0.0011
0.7500 0.0007
1.0000 0.0005

Viscosity, Pa*s [ref]

Operational conditions:

Mass fraction of Tetrahydrofuran (2) - Liquid Viscosity, Pa*s - Liquid
0.0000 0.0020
0.2500 0.0015
0.5000 0.0011
0.7500 0.0007
1.0000 0.0005

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0457 0.2130
0.0875 0.3720
0.1257 0.4900
0.1608 0.5790
0.2233 0.6990
0.2771 0.7650
0.3651 0.8530
0.4339 0.8700
0.5349 0.8740
0.6332 0.8390
0.6970 0.7730
0.7753 0.6820
0.8215 0.5880
0.8735 0.4740
0.9020 0.4000
0.9325 0.2910
0.9650 0.1630

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0457 0.2130
0.0875 0.3720
0.1257 0.4900
0.1608 0.5790
0.2233 0.6990
0.2771 0.7650
0.3651 0.8530
0.4339 0.8700
0.5349 0.8740
0.6332 0.8390
0.6970 0.7730
0.7753 0.6820
0.8215 0.5880
0.8735 0.4740
0.9020 0.4000
0.9325 0.2910
0.9650 0.1630

Mass density, kg/m3 [ref]

Operational conditions:

Mass fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 1095.8
0.2500 1036.7
0.5000 984.7
0.7500 934.0
1.0000 881.1

Mass density, kg/m3 [ref]

Operational conditions:

Mass fraction of Tetrahydrofuran (2) - Liquid Mass density, kg/m3 - Liquid
0.0000 1095.8
0.2500 1036.7
0.5000 984.7
0.7500 934.0
1.0000 881.1

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