Mixture of Ethanol + Dimethyl Sulfoxide

Excel

Ethanol

Name
Ethanol
InChI
InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
InChI Key
LFQSCWFLJHTTHZ-UHFFFAOYSA-N
Formula
C2H6O
SMILES
CCO
Mol. Weight (g/mol)
46.07
CAS
64-17-5

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
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Datasets

  1. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
  2. η - Viscosity, Pa*s (2)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. ρl - Mass density, kg/m3 (2)
  5. γ - Surface tension liquid-gas, N/m (2)
  6. λ - Thermal conductivity, W/m/K (2)

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

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0356 117.90
0.0504 119.10
0.1092 121.70
0.1636 121.80
0.2647 124.60
0.3441 126.30
0.4469 129.90
0.5570 133.00
0.6498 136.80
0.7615 141.00
0.8872 146.60
0.9408 148.00

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

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
0.0356 117.90
0.0504 119.10
0.1092 121.70
0.1636 121.80
0.2647 124.60
0.3441 126.30
0.4469 129.90
0.5570 133.00
0.6498 136.80
0.7615 141.00
0.8872 146.60
0.9408 148.00

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl Sulfoxide (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0011
303.15 0.1008 0.0012
303.15 0.2004 0.0012
303.15 0.2994 0.0012
303.15 0.4005 0.0012
303.15 0.4995 0.0013
303.15 0.6005 0.0014
303.15 0.7012 0.0015
303.15 0.8011 0.0016
303.15 0.8999 0.0017
303.15 1.0000 0.0018
308.15 0.0000 0.0010
308.15 0.1008 0.0011
308.15 0.2004 0.0011
308.15 0.2994 0.0011
308.15 0.4005 0.0011
308.15 0.4995 0.0012
308.15 0.6005 0.0012
308.15 0.7012 0.0013
308.15 0.8011 0.0014
308.15 0.8999 0.0015
308.15 1.0000 0.0017
313.15 0.0000 0.0009
313.15 0.1008 0.0010
313.15 0.2004 0.0010
313.15 0.2994 0.0010
313.15 0.4005 0.0010
313.15 0.4995 0.0011
313.15 0.6005 0.0012
313.15 0.7012 0.0012
313.15 0.8011 0.0013
313.15 0.8999 0.0014
313.15 1.0000 0.0015
318.15 0.0000 0.0008
318.15 0.1008 0.0009
318.15 0.2004 0.0009
318.15 0.2994 0.0009
318.15 0.4005 0.0010
318.15 0.4995 0.0010
318.15 0.6005 0.0011
318.15 0.7012 0.0011
318.15 0.8011 0.0012
318.15 0.8999 0.0013
318.15 1.0000 0.0014
323.15 0.0000 0.0007
323.15 0.1008 0.0009
323.15 0.2004 0.0008
323.15 0.2994 0.0009
323.15 0.4005 0.0009
323.15 0.4995 0.0009
323.15 0.6005 0.0010
323.15 0.7012 0.0010
323.15 0.8011 0.0011
323.15 0.8999 0.0012
323.15 1.0000 0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl Sulfoxide (2) - Liquid Viscosity, Pa*s - Liquid
303.15 0.0000 0.0011
303.15 0.1008 0.0012
303.15 0.2004 0.0012
303.15 0.2994 0.0012
303.15 0.4005 0.0012
303.15 0.4995 0.0013
303.15 0.6005 0.0014
303.15 0.7012 0.0015
303.15 0.8011 0.0016
303.15 0.8999 0.0017
303.15 1.0000 0.0018
308.15 0.0000 0.0010
308.15 0.1008 0.0011
308.15 0.2004 0.0011
308.15 0.2994 0.0011
308.15 0.4005 0.0011
308.15 0.4995 0.0012
308.15 0.6005 0.0012
308.15 0.7012 0.0013
308.15 0.8011 0.0014
308.15 0.8999 0.0015
308.15 1.0000 0.0017
313.15 0.0000 0.0009
313.15 0.1008 0.0010
313.15 0.2004 0.0010
313.15 0.2994 0.0010
313.15 0.4005 0.0010
313.15 0.4995 0.0011
313.15 0.6005 0.0012
313.15 0.7012 0.0012
313.15 0.8011 0.0013
313.15 0.8999 0.0014
313.15 1.0000 0.0015
318.15 0.0000 0.0008
318.15 0.1008 0.0009
318.15 0.2004 0.0009
318.15 0.2994 0.0009
318.15 0.4005 0.0010
318.15 0.4995 0.0010
318.15 0.6005 0.0011
318.15 0.7012 0.0011
318.15 0.8011 0.0012
318.15 0.8999 0.0013
318.15 1.0000 0.0014
323.15 0.0000 0.0007
323.15 0.1008 0.0009
323.15 0.2004 0.0008
323.15 0.2994 0.0009
323.15 0.4005 0.0009
323.15 0.4995 0.0009
323.15 0.6005 0.0010
323.15 0.7012 0.0010
323.15 0.8011 0.0011
323.15 0.8999 0.0012
323.15 1.0000 0.0013

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

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0332 0.1230
0.0642 0.2150
0.0933 0.2810
0.1207 0.3400
0.1707 0.4090
0.2154 0.4550
0.2917 0.5020
0.3543 0.5090
0.4516 0.4890
0.5527 0.4420
0.6222 0.3970
0.7119 0.3220
0.7671 0.2730
0.8317 0.2020
0.8682 0.1570
0.9081 0.1180
0.9518 0.0620

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

Operational conditions:

Mole fraction of Dimethyl Sulfoxide (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0332 0.1230
0.0642 0.2150
0.0933 0.2810
0.1207 0.3400
0.1707 0.4090
0.2154 0.4550
0.2917 0.5020
0.3543 0.5090
0.4516 0.4890
0.5527 0.4420
0.6222 0.3970
0.7119 0.3220
0.7671 0.2730
0.8317 0.2020
0.8682 0.1570
0.9081 0.1180
0.9518 0.0620

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl Sulfoxide (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 783.4
303.15 0.1008 836.0
303.15 0.2004 870.1
303.15 0.2994 902.4
303.15 0.4005 933.9
303.15 0.4995 963.3
303.15 0.6005 991.6
303.15 0.7012 1018.4
303.15 0.8011 1043.6
303.15 0.8999 1067.5
303.15 1.0000 1090.7
308.15 0.0000 779.0
308.15 0.1008 831.6
308.15 0.2004 865.6
308.15 0.2994 897.7
308.15 0.4005 929.0
308.15 0.4995 958.2
308.15 0.6005 986.3
308.15 0.7012 1013.0
308.15 0.8011 1038.3
308.15 0.8999 1062.1
308.15 1.0000 1084.7
313.15 0.0000 774.6
313.15 0.1008 827.6
313.15 0.2004 861.7
313.15 0.2994 894.0
313.15 0.4005 925.6
313.15 0.4995 955.0
313.15 0.6005 983.4
313.15 0.7012 1010.3
313.15 0.8011 1035.9
313.15 0.8999 1059.8
313.15 1.0000 1082.3
318.15 0.0000 769.8
318.15 0.1008 822.8
318.15 0.2004 856.7
318.15 0.2994 888.8
318.15 0.4005 920.1
318.15 0.4995 949.2
318.15 0.6005 977.4
318.15 0.7012 1004.1
318.15 0.8011 1029.5
318.15 0.8999 1053.1
318.15 1.0000 1075.1
323.15 0.0000 766.1
323.15 0.1008 818.1
323.15 0.2004 852.1
323.15 0.2994 884.0
323.15 0.4005 915.3
323.15 0.4995 944.4
323.15 0.6005 972.4
323.15 0.7012 999.3
323.15 0.8011 1024.7
323.15 0.8999 1048.4
323.15 1.0000 1070.0

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Dimethyl Sulfoxide (2) - Liquid Mass density, kg/m3 - Liquid
303.15 0.0000 783.4
303.15 0.1008 836.0
303.15 0.2004 870.1
303.15 0.2994 902.4
303.15 0.4005 933.9
303.15 0.4995 963.3
303.15 0.6005 991.6
303.15 0.7012 1018.4
303.15 0.8011 1043.6
303.15 0.8999 1067.5
303.15 1.0000 1090.7
308.15 0.0000 779.0
308.15 0.1008 831.6
308.15 0.2004 865.6
308.15 0.2994 897.7
308.15 0.4005 929.0
308.15 0.4995 958.2
308.15 0.6005 986.3
308.15 0.7012 1013.0
308.15 0.8011 1038.3
308.15 0.8999 1062.1
308.15 1.0000 1084.7
313.15 0.0000 774.6
313.15 0.1008 827.6
313.15 0.2004 861.7
313.15 0.2994 894.0
313.15 0.4005 925.6
313.15 0.4995 955.0
313.15 0.6005 983.4
313.15 0.7012 1010.3
313.15 0.8011 1035.9
313.15 0.8999 1059.8
313.15 1.0000 1082.3
318.15 0.0000 769.8
318.15 0.1008 822.8
318.15 0.2004 856.7
318.15 0.2994 888.8
318.15 0.4005 920.1
318.15 0.4995 949.2
318.15 0.6005 977.4
318.15 0.7012 1004.1
318.15 0.8011 1029.5
318.15 0.8999 1053.1
318.15 1.0000 1075.1
323.15 0.0000 766.1
323.15 0.1008 818.1
323.15 0.2004 852.1
323.15 0.2994 884.0
323.15 0.4005 915.3
323.15 0.4995 944.4
323.15 0.6005 972.4
323.15 0.7012 999.3
323.15 0.8011 1024.7
323.15 0.8999 1048.4
323.15 1.0000 1070.0

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0870 0.0393
298.15 0.1740 0.0367
298.15 0.2610 0.0344
298.15 0.3480 0.0323
298.15 0.4350 0.0305
298.15 0.5220 0.0288
298.15 0.6090 0.0273
298.15 0.6960 0.0260
298.15 0.7830 0.0246
298.15 0.8700 0.0234
308.15 0.0870 0.0383
308.15 0.1740 0.0358
308.15 0.2610 0.0336
308.15 0.3480 0.0315
308.15 0.4350 0.0297
308.15 0.5220 0.0281
308.15 0.6090 0.0266
308.15 0.6960 0.0252
308.15 0.7830 0.0239
308.15 0.8700 0.0227
318.15 0.0870 0.0373
318.15 0.1740 0.0349
318.15 0.2610 0.0327
318.15 0.3480 0.0307
318.15 0.4350 0.0290
318.15 0.5220 0.0273
318.15 0.6090 0.0258
318.15 0.6960 0.0244
318.15 0.7830 0.0231
318.15 0.8700 0.0219
328.15 0.0870 0.0364
328.15 0.1740 0.0340
328.15 0.2610 0.0319
328.15 0.3480 0.0300
328.15 0.4350 0.0282
328.15 0.5220 0.0266
328.15 0.6090 0.0252
328.15 0.6960 0.0236
328.15 0.7830 0.0224
328.15 0.8700 0.0211
298.15 0.0000 0.0424
308.15 0.0000 0.0413
318.15 0.0000 0.0402
328.15 0.0000 0.0391
298.15 1.0000 0.0217
308.15 1.0000 0.0210
318.15 1.0000 0.0202
328.15 1.0000 0.0192

Surface tension liquid-gas, N/m [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Ethanol (1) - Liquid Surface tension liquid-gas, N/m - Liquid
298.15 0.0870 0.0393
298.15 0.1740 0.0367
298.15 0.2610 0.0344
298.15 0.3480 0.0323
298.15 0.4350 0.0305
298.15 0.5220 0.0288
298.15 0.6090 0.0273
298.15 0.6960 0.0260
298.15 0.7830 0.0246
298.15 0.8700 0.0234
308.15 0.0870 0.0383
308.15 0.1740 0.0358
308.15 0.2610 0.0336
308.15 0.3480 0.0315
308.15 0.4350 0.0297
308.15 0.5220 0.0281
308.15 0.6090 0.0266
308.15 0.6960 0.0252
308.15 0.7830 0.0239
308.15 0.8700 0.0227
318.15 0.0870 0.0373
318.15 0.1740 0.0349
318.15 0.2610 0.0327
318.15 0.3480 0.0307
318.15 0.4350 0.0290
318.15 0.5220 0.0273
318.15 0.6090 0.0258
318.15 0.6960 0.0244
318.15 0.7830 0.0231
318.15 0.8700 0.0219
328.15 0.0870 0.0364
328.15 0.1740 0.0340
328.15 0.2610 0.0319
328.15 0.3480 0.0300
328.15 0.4350 0.0282
328.15 0.5220 0.0266
328.15 0.6090 0.0252
328.15 0.6960 0.0236
328.15 0.7830 0.0224
328.15 0.8700 0.0211
298.15 0.0000 0.0424
308.15 0.0000 0.0413
318.15 0.0000 0.0402
328.15 0.0000 0.0391
298.15 1.0000 0.0217
308.15 1.0000 0.0210
318.15 1.0000 0.0202
328.15 1.0000 0.0192

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Mass fraction of Dimethyl Sulfoxide (2) - Liquid Temperature, K - Liquid Thermal conductivity, W/m/K - Liquid
0.1028 280.31 0.1700
0.1028 290.23 0.1670
0.1028 300.13 0.1640
0.1028 309.91 0.1620
0.1028 319.71 0.1590
0.1028 329.37 0.1570
0.1028 339.41 0.1550
0.4060 280.19 0.1730
0.4060 289.67 0.1700
0.4060 299.77 0.1680
0.4060 309.74 0.1660
0.4060 319.47 0.1640
0.4060 329.62 0.1620
0.4060 339.18 0.1590
0.7006 279.97 0.1780
0.7006 289.86 0.1770
0.7006 299.80 0.1740
0.7006 309.85 0.1730
0.7006 319.51 0.1710
0.7006 329.67 0.1690
0.7006 339.27 0.1660
0.2005 280.00 0.1700
0.2005 290.06 0.1680
0.2005 299.81 0.1650
0.2005 309.71 0.1630
0.2005 319.61 0.1610
0.2005 329.47 0.1580
0.2005 339.51 0.1570
0.5007 279.97 0.1740
0.5007 289.71 0.1720
0.5007 300.23 0.1710
0.5007 309.84 0.1680
0.5007 319.66 0.1660
0.5007 329.72 0.1640
0.5007 339.56 0.1620
0.8004 279.39 0.1810
0.8004 289.18 0.1790
0.8004 299.05 0.1770
0.8004 308.94 0.1760
0.8004 318.75 0.1740
0.8004 328.70 0.1720
0.8004 338.46 0.1700
0.3004 280.15 0.1710
0.3004 289.71 0.1680
0.3004 299.79 0.1660
0.3004 309.88 0.1640
0.3004 319.57 0.1620
0.3004 329.60 0.1600
0.3004 339.18 0.1570
0.6016 280.20 0.1770
0.6016 289.79 0.1740
0.6016 299.87 0.1720
0.6016 309.61 0.1700
0.6016 319.66 0.1680
0.6016 329.64 0.1660
0.6016 339.25 0.1630
0.9000 280.00 0.1840
0.9000 289.82 0.1830
0.9000 299.88 0.1820
0.9000 309.42 0.1800
0.9000 319.18 0.1780
0.9000 328.94 0.1760
0.9000 338.72 0.1740

Thermal conductivity, W/m/K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Mass fraction of Dimethyl Sulfoxide (2) - Liquid Temperature, K - Liquid Thermal conductivity, W/m/K - Liquid
0.1028 280.31 0.1700
0.1028 290.23 0.1670
0.1028 300.13 0.1640
0.1028 309.91 0.1620
0.1028 319.71 0.1590
0.1028 329.37 0.1570
0.1028 339.41 0.1550
0.4060 280.19 0.1730
0.4060 289.67 0.1700
0.4060 299.77 0.1680
0.4060 309.74 0.1660
0.4060 319.47 0.1640
0.4060 329.62 0.1620
0.4060 339.18 0.1590
0.7006 279.97 0.1780
0.7006 289.86 0.1770
0.7006 299.80 0.1740
0.7006 309.85 0.1730
0.7006 319.51 0.1710
0.7006 329.67 0.1690
0.7006 339.27 0.1660
0.2005 280.00 0.1700
0.2005 290.06 0.1680
0.2005 299.81 0.1650
0.2005 309.71 0.1630
0.2005 319.61 0.1610
0.2005 329.47 0.1580
0.2005 339.51 0.1570
0.5007 279.97 0.1740
0.5007 289.71 0.1720
0.5007 300.23 0.1710
0.5007 309.84 0.1680
0.5007 319.66 0.1660
0.5007 329.72 0.1640
0.5007 339.56 0.1620
0.8004 279.39 0.1810
0.8004 289.18 0.1790
0.8004 299.05 0.1770
0.8004 308.94 0.1760
0.8004 318.75 0.1740
0.8004 328.70 0.1720
0.8004 338.46 0.1700
0.3004 280.15 0.1710
0.3004 289.71 0.1680
0.3004 299.79 0.1660
0.3004 309.88 0.1640
0.3004 319.57 0.1620
0.3004 329.60 0.1600
0.3004 339.18 0.1570
0.6016 280.20 0.1770
0.6016 289.79 0.1740
0.6016 299.87 0.1720
0.6016 309.61 0.1700
0.6016 319.66 0.1680
0.6016 329.64 0.1660
0.6016 339.25 0.1630
0.9000 280.00 0.1840
0.9000 289.82 0.1830
0.9000 299.88 0.1820
0.9000 309.42 0.1800
0.9000 319.18 0.1780
0.9000 328.94 0.1760
0.9000 338.72 0.1740

Sources