Mixture of Toluene + Dimethyl Sulfoxide

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Toluene

Name
Toluene
InChI
InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
InChI Key
YXFVVABEGXRONW-UHFFFAOYSA-N
Formula
C7H8
SMILES
Cc1ccccc1
Mol. Weight (g/mol)
92.14
CAS
108-88-3

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. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (2)
  4. Tboil - Boiling temperature at pressure P, K (4)

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Mole fraction of Toluene (1) - Gas
0.9420 0.9899
0.8956 0.9820
0.8066 0.9718
0.7190 0.9621
0.6314 0.9507
0.3824 0.9056
0.2195 0.8306
0.1519 0.7632
0.0974 0.6752
0.0514 0.5102
0.0321 0.3832
0.0239 0.3148
0.0157 0.2289

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Mole fraction of Toluene (1) - Gas
0.9420 0.9899
0.8956 0.9820
0.8066 0.9718
0.7190 0.9621
0.6314 0.9507
0.3824 0.9056
0.2195 0.8306
0.1519 0.7632
0.0974 0.6752
0.0514 0.5102
0.0321 0.3832
0.0239 0.3148
0.0157 0.2289

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

Operational conditions:

Mole fraction of Toluene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0429 0.1342
0.0888 0.2476
0.1395 0.3604
0.1908 0.4763
0.2523 0.5955
0.3042 0.6669
0.3548 0.7135
0.3578 0.7220
0.4026 0.7463
0.4034 0.7455
0.4495 0.7648
0.5071 0.7558
0.5724 0.7400
0.6486 0.6967
0.8211 0.5045
0.9132 0.3063

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

Operational conditions:

Mole fraction of Toluene (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0429 0.1342
0.0888 0.2476
0.1395 0.3604
0.1908 0.4763
0.2523 0.5955
0.3042 0.6669
0.3548 0.7135
0.3578 0.7220
0.4026 0.7463
0.4034 0.7455
0.4495 0.7648
0.5071 0.7558
0.5724 0.7400
0.6486 0.6967
0.8211 0.5045
0.9132 0.3063

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0689 1077.87
293.15 0.1505 1053.27
293.15 0.2269 1031.56
293.15 0.3036 1010.99
293.15 0.3758 992.64
293.15 0.4568 973.24
293.15 0.5177 959.33
293.15 0.5769 946.41
293.15 0.6342 934.37
293.15 0.6885 923.31
293.15 0.7512 911.04
293.15 0.8181 898.38
293.15 0.8856 886.05
293.15 0.9553 873.71
303.15 0.0652 1069.85
303.15 0.1295 1050.38
303.15 0.1806 1035.51
303.15 0.2563 1014.57
303.15 0.3098 1000.5
303.15 0.3845 981.74
303.15 0.4456 967.18
303.15 0.5169 950.98
303.15 0.5813 937.04
303.15 0.6645 919.88
303.15 0.7499 903.18
303.15 0.8114 891.64
303.15 0.8802 879.15
303.15 0.9532 866.39
313.15 0.0661 1059.41
313.15 0.1202 1043.16
313.15 0.1891 1023.36
313.15 0.2403 1009.32
313.15 0.2945 995.06
313.15 0.3615 978.24
313.15 0.4369 960.28
313.15 0.5156 942.59
313.15 0.5813 928.56
313.15 0.6558 913.41
313.15 0.7267 899.63
313.15 0.7956 886.78
313.15 0.8821 871.32
313.15 0.9448 860.52
323.15 0.0884 1042.41
323.15 0.1236 1032.08
323.15 0.1869 1014.1
323.15 0.2536 996.08
323.15 0.3285 976.94
323.15 0.3996 959.75
323.15 0.4501 948.11
323.15 0.4969 937.7
323.15 0.5563 925.0
323.15 0.6160 912.74
323.15 0.6725 901.61
323.15 0.7562 885.79
323.15 0.8532 868.42
323.15 0.9458 852.63
333.15 0.0598 1040.93
333.15 0.1436 1016.4
333.15 0.2258 993.84
333.15 0.2931 976.44
333.15 0.3652 958.78
333.15 0.4112 948.06
333.15 0.4859 931.36
333.15 0.5301 921.94
333.15 0.5965 908.31
333.15 0.6789 892.24
333.15 0.7215 884.23
333.15 0.7899 871.86
333.15 0.8512 861.15
333.15 0.9503 844.53
343.15 0.0599 1030.68
343.15 0.1102 1015.93
343.15 0.1798 996.46
343.15 0.2549 976.61
343.15 0.3169 961.13
343.15 0.3858 944.75
343.15 0.4405 932.38
343.15 0.5258 914.08
343.15 0.5936 900.34
343.15 0.6678 886.01
343.15 0.7166 876.96
343.15 0.7925 863.42
343.15 0.8792 848.65
343.15 0.9552 836.24
353.15 0.0801 1014.55
353.15 0.1526 994.06
353.15 0.2215 975.63
353.15 0.2869 959.04
353.15 0.3568 942.26
353.15 0.4205 927.79
353.15 0.4956 911.6
353.15 0.5723 895.96
353.15 0.6321 884.4
353.15 0.7058 870.71
353.15 0.7680 859.69
353.15 0.8363 848.04
353.15 0.8913 838.96
353.15 0.9524 829.17

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0689 1077.87
293.15 0.1505 1053.27
293.15 0.2269 1031.56
293.15 0.3036 1010.99
293.15 0.3758 992.64
293.15 0.4568 973.24
293.15 0.5177 959.33
293.15 0.5769 946.41
293.15 0.6342 934.37
293.15 0.6885 923.31
293.15 0.7512 911.04
293.15 0.8181 898.38
293.15 0.8856 886.05
293.15 0.9553 873.71
303.15 0.0652 1069.85
303.15 0.1295 1050.38
303.15 0.1806 1035.51
303.15 0.2563 1014.57
303.15 0.3098 1000.5
303.15 0.3845 981.74
303.15 0.4456 967.18
303.15 0.5169 950.98
303.15 0.5813 937.04
303.15 0.6645 919.88
303.15 0.7499 903.18
303.15 0.8114 891.64
303.15 0.8802 879.15
303.15 0.9532 866.39
313.15 0.0661 1059.41
313.15 0.1202 1043.16
313.15 0.1891 1023.36
313.15 0.2403 1009.32
313.15 0.2945 995.06
313.15 0.3615 978.24
313.15 0.4369 960.28
313.15 0.5156 942.59
313.15 0.5813 928.56
313.15 0.6558 913.41
313.15 0.7267 899.63
313.15 0.7956 886.78
313.15 0.8821 871.32
313.15 0.9448 860.52
323.15 0.0884 1042.41
323.15 0.1236 1032.08
323.15 0.1869 1014.1
323.15 0.2536 996.08
323.15 0.3285 976.94
323.15 0.3996 959.75
323.15 0.4501 948.11
323.15 0.4969 937.7
323.15 0.5563 925.0
323.15 0.6160 912.74
323.15 0.6725 901.61
323.15 0.7562 885.79
323.15 0.8532 868.42
323.15 0.9458 852.63
333.15 0.0598 1040.93
333.15 0.1436 1016.4
333.15 0.2258 993.84
333.15 0.2931 976.44
333.15 0.3652 958.78
333.15 0.4112 948.06
333.15 0.4859 931.36
333.15 0.5301 921.94
333.15 0.5965 908.31
333.15 0.6789 892.24
333.15 0.7215 884.23
333.15 0.7899 871.86
333.15 0.8512 861.15
333.15 0.9503 844.53
343.15 0.0599 1030.68
343.15 0.1102 1015.93
343.15 0.1798 996.46
343.15 0.2549 976.61
343.15 0.3169 961.13
343.15 0.3858 944.75
343.15 0.4405 932.38
343.15 0.5258 914.08
343.15 0.5936 900.34
343.15 0.6678 886.01
343.15 0.7166 876.96
343.15 0.7925 863.42
343.15 0.8792 848.65
343.15 0.9552 836.24
353.15 0.0801 1014.55
353.15 0.1526 994.06
353.15 0.2215 975.63
353.15 0.2869 959.04
353.15 0.3568 942.26
353.15 0.4205 927.79
353.15 0.4956 911.6
353.15 0.5723 895.96
353.15 0.6321 884.4
353.15 0.7058 870.71
353.15 0.7680 859.69
353.15 0.8363 848.04
353.15 0.8913 838.96
353.15 0.9524 829.17

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.0478 454.05
0.0722 450.45
0.2264 430.75
0.3522 417.85
0.4709 408.05
0.6163 398.45
0.8007 389.15
0.9125 384.65
1.0000 381.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.9420 384.69
0.8956 385.68
0.8066 387.42
0.7190 389.17
0.6314 391.15
0.3824 399.95
0.2195 411.12
0.1519 418.78
0.0974 427.14
0.0514 439.23
0.0321 446.65
0.0239 450.22
0.0157 454.45

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.0000 460.95
0.0478 454.05
0.0722 450.45
0.2264 430.75
0.3522 417.85
0.4709 408.05
0.6163 398.45
0.8007 389.15
0.9125 384.65
1.0000 381.65

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid Boiling temperature at pressure P, K - Liquid
0.9420 384.69
0.8956 385.68
0.8066 387.42
0.7190 389.17
0.6314 391.15
0.3824 399.95
0.2195 411.12
0.1519 418.78
0.0974 427.14
0.0514 439.23
0.0321 446.65
0.0239 450.22
0.0157 454.45

Sources