Mixture of Diethyl carbonate + Toluene

Excel

Diethyl carbonate

Name
Diethyl carbonate
InChI
InChI=1S/C5H10O3/c1-3-7-5(6)8-4-2/h3-4H2,1-2H3
InChI Key
OIFBSDVPJOWBCH-UHFFFAOYSA-N
Formula
C5H10O3
SMILES
CCOC(=O)OCC
Mol. Weight (g/mol)
118.13
CAS
105-58-8

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
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0006
298.15 0.1014 0.0006
298.15 0.1984 0.0006
298.15 0.3006 0.0006
298.15 0.4024 0.0006
298.15 0.5212 0.0006
298.15 0.6022 0.0007
298.15 0.7016 0.0007
298.15 0.7995 0.0007
298.15 0.8975 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0005
303.15 0.1014 0.0005
303.15 0.1984 0.0006
303.15 0.3006 0.0006
303.15 0.4024 0.0006
303.15 0.5212 0.0006
303.15 0.6022 0.0006
303.15 0.7016 0.0006
303.15 0.7995 0.0007
303.15 0.8975 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0005
313.15 0.1014 0.0005
313.15 0.1984 0.0005
313.15 0.3006 0.0005
313.15 0.4024 0.0005
313.15 0.5212 0.0005
313.15 0.6022 0.0006
313.15 0.7016 0.0006
313.15 0.7995 0.0006
313.15 0.8975 0.0006
313.15 1.0000 0.0006
323.15 0.0000 0.0004
323.15 0.1014 0.0004
323.15 0.1984 0.0004
323.15 0.3006 0.0005
323.15 0.4024 0.0005
323.15 0.5212 0.0005
323.15 0.6022 0.0005
323.15 0.7016 0.0005
323.15 0.7995 0.0005
323.15 0.8975 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0004
333.15 0.1014 0.0004
333.15 0.1984 0.0004
333.15 0.3006 0.0004
333.15 0.4024 0.0004
333.15 0.5212 0.0004
333.15 0.6022 0.0004
333.15 0.7016 0.0005
333.15 0.7995 0.0005
333.15 0.8975 0.0005
333.15 1.0000 0.0005
343.15 0.0000 0.0003
343.15 0.1014 0.0004
343.15 0.1984 0.0004
343.15 0.3006 0.0004
343.15 0.4024 0.0004
343.15 0.5212 0.0004
343.15 0.6022 0.0004
343.15 0.7016 0.0004
343.15 0.7995 0.0004
343.15 0.8975 0.0004
343.15 1.0000 0.0004
353.15 0.0000 0.0003
353.15 0.1014 0.0003
353.15 0.1984 0.0003
353.15 0.3006 0.0003
353.15 0.4024 0.0003
353.15 0.5212 0.0004
353.15 0.6022 0.0004
353.15 0.7016 0.0004
353.15 0.7995 0.0004
353.15 0.8975 0.0004
353.15 1.0000 0.0004
363.15 0.0000 0.0003
363.15 0.1014 0.0003
363.15 0.1984 0.0003
363.15 0.3006 0.0003
363.15 0.4024 0.0003
363.15 0.5212 0.0003
363.15 0.6022 0.0003
363.15 0.7016 0.0003
363.15 0.7995 0.0003
363.15 0.8975 0.0004
363.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Viscosity, Pa*s - Liquid
298.15 0.0000 0.0006
298.15 0.1014 0.0006
298.15 0.1984 0.0006
298.15 0.3006 0.0006
298.15 0.4024 0.0006
298.15 0.5212 0.0006
298.15 0.6022 0.0007
298.15 0.7016 0.0007
298.15 0.7995 0.0007
298.15 0.8975 0.0007
298.15 1.0000 0.0007
303.15 0.0000 0.0005
303.15 0.1014 0.0005
303.15 0.1984 0.0006
303.15 0.3006 0.0006
303.15 0.4024 0.0006
303.15 0.5212 0.0006
303.15 0.6022 0.0006
303.15 0.7016 0.0006
303.15 0.7995 0.0007
303.15 0.8975 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0005
313.15 0.1014 0.0005
313.15 0.1984 0.0005
313.15 0.3006 0.0005
313.15 0.4024 0.0005
313.15 0.5212 0.0005
313.15 0.6022 0.0006
313.15 0.7016 0.0006
313.15 0.7995 0.0006
313.15 0.8975 0.0006
313.15 1.0000 0.0006
323.15 0.0000 0.0004
323.15 0.1014 0.0004
323.15 0.1984 0.0004
323.15 0.3006 0.0005
323.15 0.4024 0.0005
323.15 0.5212 0.0005
323.15 0.6022 0.0005
323.15 0.7016 0.0005
323.15 0.7995 0.0005
323.15 0.8975 0.0005
323.15 1.0000 0.0005
333.15 0.0000 0.0004
333.15 0.1014 0.0004
333.15 0.1984 0.0004
333.15 0.3006 0.0004
333.15 0.4024 0.0004
333.15 0.5212 0.0004
333.15 0.6022 0.0004
333.15 0.7016 0.0005
333.15 0.7995 0.0005
333.15 0.8975 0.0005
333.15 1.0000 0.0005
343.15 0.0000 0.0003
343.15 0.1014 0.0004
343.15 0.1984 0.0004
343.15 0.3006 0.0004
343.15 0.4024 0.0004
343.15 0.5212 0.0004
343.15 0.6022 0.0004
343.15 0.7016 0.0004
343.15 0.7995 0.0004
343.15 0.8975 0.0004
343.15 1.0000 0.0004
353.15 0.0000 0.0003
353.15 0.1014 0.0003
353.15 0.1984 0.0003
353.15 0.3006 0.0003
353.15 0.4024 0.0003
353.15 0.5212 0.0004
353.15 0.6022 0.0004
353.15 0.7016 0.0004
353.15 0.7995 0.0004
353.15 0.8975 0.0004
353.15 1.0000 0.0004
363.15 0.0000 0.0003
363.15 0.1014 0.0003
363.15 0.1984 0.0003
363.15 0.3006 0.0003
363.15 0.4024 0.0003
363.15 0.5212 0.0003
363.15 0.6022 0.0003
363.15 0.7016 0.0003
363.15 0.7995 0.0003
363.15 0.8975 0.0004
363.15 1.0000 0.0004

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
303.15 0.0000 1.99
303.15 0.1002 3.03
303.15 0.2005 3.49
303.15 0.3021 3.77
303.15 0.3958 3.98
303.15 0.5071 4.27
303.15 0.5996 4.37
303.15 0.7000 4.37
303.15 0.7999 4.66
303.15 0.8987 4.58
303.15 1.0000 4.87
308.15 0.0000 2.65
308.15 0.1002 3.98
308.15 0.2005 4.41
308.15 0.3021 5.04
308.15 0.3958 5.33
308.15 0.5071 5.43
308.15 0.5996 5.70
308.15 0.7000 5.96
308.15 0.7999 5.93
308.15 0.8987 6.17
308.15 1.0000 6.32
313.15 0.0000 3.45
313.15 0.1002 5.03
313.15 0.2005 5.81
313.15 0.3021 6.15
313.15 0.3958 6.60
313.15 0.5071 6.76
313.15 0.5996 7.02
313.15 0.7000 7.28
313.15 0.7999 7.53
313.15 0.8987 7.50
313.15 1.0000 7.78
318.15 0.0000 4.51
318.15 0.1002 6.36
318.15 0.2005 7.41
318.15 0.3021 8.01
318.15 0.3958 8.48
318.15 0.5071 8.77
318.15 0.5996 9.14
318.15 0.7000 9.40
318.15 0.7999 9.73
318.15 0.8987 9.62
318.15 1.0000 9.89
323.15 0.0000 5.83
323.15 0.1002 8.05
323.15 0.2005 9.32
323.15 0.3021 10.22
323.15 0.3958 10.34
323.15 0.5071 11.16
323.15 0.5996 11.32
323.15 0.7000 11.79
323.15 0.7999 11.86
323.15 0.8987 12.10
323.15 1.0000 12.27

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Toluene (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
303.15 0.0000 1.99
303.15 0.1002 3.03
303.15 0.2005 3.49
303.15 0.3021 3.77
303.15 0.3958 3.98
303.15 0.5071 4.27
303.15 0.5996 4.37
303.15 0.7000 4.37
303.15 0.7999 4.66
303.15 0.8987 4.58
303.15 1.0000 4.87
308.15 0.0000 2.65
308.15 0.1002 3.98
308.15 0.2005 4.41
308.15 0.3021 5.04
308.15 0.3958 5.33
308.15 0.5071 5.43
308.15 0.5996 5.70
308.15 0.7000 5.96
308.15 0.7999 5.93
308.15 0.8987 6.17
308.15 1.0000 6.32
313.15 0.0000 3.45
313.15 0.1002 5.03
313.15 0.2005 5.81
313.15 0.3021 6.15
313.15 0.3958 6.60
313.15 0.5071 6.76
313.15 0.5996 7.02
313.15 0.7000 7.28
313.15 0.7999 7.53
313.15 0.8987 7.50
313.15 1.0000 7.78
318.15 0.0000 4.51
318.15 0.1002 6.36
318.15 0.2005 7.41
318.15 0.3021 8.01
318.15 0.3958 8.48
318.15 0.5071 8.77
318.15 0.5996 9.14
318.15 0.7000 9.40
318.15 0.7999 9.73
318.15 0.8987 9.62
318.15 1.0000 9.89
323.15 0.0000 5.83
323.15 0.1002 8.05
323.15 0.2005 9.32
323.15 0.3021 10.22
323.15 0.3958 10.34
323.15 0.5071 11.16
323.15 0.5996 11.32
323.15 0.7000 11.79
323.15 0.7999 11.86
323.15 0.8987 12.10
323.15 1.0000 12.27

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 862.01
298.15 0.1014 874.5
298.15 0.1984 885.94
298.15 0.3006 897.67
298.15 0.4024 908.97
298.15 0.5212 921.72
298.15 0.6022 930.18
298.15 0.7016 940.28
298.15 0.7995 949.95
298.15 0.8975 959.36
298.15 1.0000 968.97
303.15 0.0000 858.32
303.15 0.1014 870.46
303.15 0.1984 881.62
303.15 0.3006 893.06
303.15 0.4024 904.06
303.15 0.5212 916.47
303.15 0.6022 924.71
303.15 0.7016 934.52
303.15 0.7995 943.93
303.15 0.8975 953.08
303.15 1.0000 962.39
313.15 0.0000 848.92
313.15 0.1014 860.95
313.15 0.1984 872.04
313.15 0.3006 883.39
313.15 0.4024 894.33
313.15 0.5212 906.66
313.15 0.6022 914.85
313.15 0.7016 924.6
313.15 0.7995 933.95
313.15 0.8975 943.04
313.15 1.0000 952.32
323.15 0.0000 838.75
323.15 0.1014 850.49
323.15 0.1984 861.33
323.15 0.3006 872.43
323.15 0.4024 883.11
323.15 0.5212 895.17
323.15 0.6022 903.16
323.15 0.7016 912.68
323.15 0.7995 921.81
323.15 0.8975 930.72
323.15 1.0000 939.78
333.15 0.0000 829.93
333.15 0.1014 841.39
333.15 0.1984 852.01
333.15 0.3006 862.85
333.15 0.4024 873.3
333.15 0.5212 885.09
333.15 0.6022 892.88
333.15 0.7016 902.2
333.15 0.7995 911.11
333.15 0.8975 919.81
333.15 1.0000 928.69
343.15 0.0000 820.3
343.15 0.1014 831.46
343.15 0.1984 841.79
343.15 0.3006 852.32
343.15 0.4024 862.48
343.15 0.5212 873.94
343.15 0.6022 881.51
343.15 0.7016 890.57
343.15 0.7995 899.24
343.15 0.8975 907.69
343.15 1.0000 916.33
353.15 0.0000 810.54
353.15 0.1014 821.53
353.15 0.1984 831.67
353.15 0.3006 842.02
353.15 0.4024 852.02
353.15 0.5212 863.29
353.15 0.6022 870.74
353.15 0.7016 879.66
353.15 0.7995 888.2
353.15 0.8975 896.52
353.15 1.0000 905.02
363.15 0.0000 797.68
363.15 0.1014 808.79
363.15 0.1984 819.07
363.15 0.3006 829.57
363.15 0.4024 839.71
363.15 0.5212 851.16
363.15 0.6022 858.77
363.15 0.7016 867.85
363.15 0.7995 876.55
363.15 0.8975 885.04
363.15 1.0000 893.71

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Diethyl carbonate (1) - Liquid Mass density, kg/m3 - Liquid
298.15 0.0000 862.01
298.15 0.1014 874.5
298.15 0.1984 885.94
298.15 0.3006 897.67
298.15 0.4024 908.97
298.15 0.5212 921.72
298.15 0.6022 930.18
298.15 0.7016 940.28
298.15 0.7995 949.95
298.15 0.8975 959.36
298.15 1.0000 968.97
303.15 0.0000 858.32
303.15 0.1014 870.46
303.15 0.1984 881.62
303.15 0.3006 893.06
303.15 0.4024 904.06
303.15 0.5212 916.47
303.15 0.6022 924.71
303.15 0.7016 934.52
303.15 0.7995 943.93
303.15 0.8975 953.08
303.15 1.0000 962.39
313.15 0.0000 848.92
313.15 0.1014 860.95
313.15 0.1984 872.04
313.15 0.3006 883.39
313.15 0.4024 894.33
313.15 0.5212 906.66
313.15 0.6022 914.85
313.15 0.7016 924.6
313.15 0.7995 933.95
313.15 0.8975 943.04
313.15 1.0000 952.32
323.15 0.0000 838.75
323.15 0.1014 850.49
323.15 0.1984 861.33
323.15 0.3006 872.43
323.15 0.4024 883.11
323.15 0.5212 895.17
323.15 0.6022 903.16
323.15 0.7016 912.68
323.15 0.7995 921.81
323.15 0.8975 930.72
323.15 1.0000 939.78
333.15 0.0000 829.93
333.15 0.1014 841.39
333.15 0.1984 852.01
333.15 0.3006 862.85
333.15 0.4024 873.3
333.15 0.5212 885.09
333.15 0.6022 892.88
333.15 0.7016 902.2
333.15 0.7995 911.11
333.15 0.8975 919.81
333.15 1.0000 928.69
343.15 0.0000 820.3
343.15 0.1014 831.46
343.15 0.1984 841.79
343.15 0.3006 852.32
343.15 0.4024 862.48
343.15 0.5212 873.94
343.15 0.6022 881.51
343.15 0.7016 890.57
343.15 0.7995 899.24
343.15 0.8975 907.69
343.15 1.0000 916.33
353.15 0.0000 810.54
353.15 0.1014 821.53
353.15 0.1984 831.67
353.15 0.3006 842.02
353.15 0.4024 852.02
353.15 0.5212 863.29
353.15 0.6022 870.74
353.15 0.7016 879.66
353.15 0.7995 888.2
353.15 0.8975 896.52
353.15 1.0000 905.02
363.15 0.0000 797.68
363.15 0.1014 808.79
363.15 0.1984 819.07
363.15 0.3006 829.57
363.15 0.4024 839.71
363.15 0.5212 851.16
363.15 0.6022 858.77
363.15 0.7016 867.85
363.15 0.7995 876.55
363.15 0.8975 885.04
363.15 1.0000 893.71

Sources