Mixture of Toluene + Diisopropyl ether

Excel

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

Diisopropyl ether

Name
Diisopropyl ether
InChI
InChI=1S/C6H14O/c1-5(2)7-6(3)4/h5-6H,1-4H3
InChI Key
ZAFNJMIOTHYJRJ-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CC(C)OC(C)C
Mol. Weight (g/mol)
102.17
CAS
108-20-3
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Datasets

  1. Mole fraction (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. Pvap - Vapor or sublimation pressure, kPa (2)
  4. ρl - Mass density, kg/m3 (2)

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0192 0.1066
0.0399 0.1958
0.0597 0.2703
0.0793 0.3269
0.1194 0.4249
0.1692 0.5232
0.2291 0.6117
0.2888 0.6749
0.3486 0.7221
0.4084 0.7644
0.4681 0.7993
0.5287 0.8284
0.5888 0.8549
0.6484 0.8764
0.7085 0.8960
0.7688 0.9176
0.8293 0.9314
0.8789 0.9529
0.9198 0.9691
0.9393 0.9775
0.9603 0.9850
0.9795 0.9926

Mole fraction of Diisopropyl ether (2) [ref]

Operational condition: Temperature, K = 333.15 (Gas)

Mole fraction of Diisopropyl ether (2) - Liquid Mole fraction of Diisopropyl ether (2) - Gas
0.0192 0.1066
0.0399 0.1958
0.0597 0.2703
0.0793 0.3269
0.1194 0.4249
0.1692 0.5232
0.2291 0.6117
0.2888 0.6749
0.3486 0.7221
0.4084 0.7644
0.4681 0.7993
0.5287 0.8284
0.5888 0.8549
0.6484 0.8764
0.7085 0.8960
0.7688 0.9176
0.8293 0.9314
0.8789 0.9529
0.9198 0.9691
0.9393 0.9775
0.9603 0.9850
0.9795 0.9926

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

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0570 0.0273
0.1030 0.0422
0.1400 0.0519
0.2280 0.0593
0.3140 0.0548
0.3970 0.0419
0.4550 0.0323
0.6730 0.0032
0.7520 -0.0091
0.8890 -0.0081

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

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0570 0.0273
0.1030 0.0422
0.1400 0.0519
0.2280 0.0593
0.3140 0.0548
0.3970 0.0419
0.4550 0.0323
0.6730 0.0032
0.7520 -0.0091
0.8890 -0.0081

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
263.15 0.0843 0.76
263.15 0.1517 1.22
263.15 0.2846 1.49
263.15 0.4047 1.88
263.15 0.6416 2.07
263.15 0.7718 2.69
263.15 0.8702 2.89
273.15 0.0843 1.42
273.15 0.1517 2.14
273.15 0.2846 2.70
273.15 0.4047 3.37
273.15 0.6416 3.87
273.15 0.7718 4.81
273.15 0.8702 5.18
283.15 0.0843 2.52
283.15 0.1517 3.60
283.15 0.2846 4.65
283.15 0.4047 5.73
283.15 0.6416 6.80
283.15 0.7718 8.17
283.15 0.8702 8.80
293.15 0.0843 4.27
293.15 0.1517 5.86
293.15 0.2846 7.66
293.15 0.4047 9.35
293.15 0.6416 11.33
293.15 0.7718 13.27
293.15 0.8702 14.29
303.15 0.0843 6.95
303.15 0.1517 9.22
303.15 0.2846 12.14
303.15 0.4047 14.68
303.15 0.6416 18.03
303.15 0.7718 20.72
303.15 0.8702 22.31
313.15 0.0843 10.90
313.15 0.1517 14.11
313.15 0.2846 18.57
313.15 0.4047 22.30
313.15 0.6416 27.56
313.15 0.7718 31.25
313.15 0.8702 33.64
323.15 0.0843 16.58
323.15 0.1517 21.02
323.15 0.2846 27.55
323.15 0.4047 32.85
323.15 0.6416 40.69
323.15 0.7718 45.72
323.15 0.8702 49.18
333.15 0.0843 24.50
333.15 0.1517 30.57
333.15 0.2846 39.75
333.15 0.4047 47.12
333.15 0.6416 58.24
333.15 0.7718 65.09
333.15 0.8702 69.95
343.15 0.0843 35.28
343.15 0.1517 43.52
343.15 0.2846 55.93
343.15 0.4047 65.98
343.15 0.6416 81.10
343.15 0.7718 90.41
343.15 0.8702 97.07

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (2) - Liquid Vapor or sublimation pressure, kPa - Liquid
263.15 0.0843 0.76
263.15 0.1517 1.22
263.15 0.2846 1.49
263.15 0.4047 1.88
263.15 0.6416 2.07
263.15 0.7718 2.69
263.15 0.8702 2.89
273.15 0.0843 1.42
273.15 0.1517 2.14
273.15 0.2846 2.70
273.15 0.4047 3.37
273.15 0.6416 3.87
273.15 0.7718 4.81
273.15 0.8702 5.18
283.15 0.0843 2.52
283.15 0.1517 3.60
283.15 0.2846 4.65
283.15 0.4047 5.73
283.15 0.6416 6.80
283.15 0.7718 8.17
283.15 0.8702 8.80
293.15 0.0843 4.27
293.15 0.1517 5.86
293.15 0.2846 7.66
293.15 0.4047 9.35
293.15 0.6416 11.33
293.15 0.7718 13.27
293.15 0.8702 14.29
303.15 0.0843 6.95
303.15 0.1517 9.22
303.15 0.2846 12.14
303.15 0.4047 14.68
303.15 0.6416 18.03
303.15 0.7718 20.72
303.15 0.8702 22.31
313.15 0.0843 10.90
313.15 0.1517 14.11
313.15 0.2846 18.57
313.15 0.4047 22.30
313.15 0.6416 27.56
313.15 0.7718 31.25
313.15 0.8702 33.64
323.15 0.0843 16.58
323.15 0.1517 21.02
323.15 0.2846 27.55
323.15 0.4047 32.85
323.15 0.6416 40.69
323.15 0.7718 45.72
323.15 0.8702 49.18
333.15 0.0843 24.50
333.15 0.1517 30.57
333.15 0.2846 39.75
333.15 0.4047 47.12
333.15 0.6416 58.24
333.15 0.7718 65.09
333.15 0.8702 69.95
343.15 0.0843 35.28
343.15 0.1517 43.52
343.15 0.2846 55.93
343.15 0.4047 65.98
343.15 0.6416 81.10
343.15 0.7718 90.41
343.15 0.8702 97.07

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0500 853.94
0.0995 845.89
0.2004 829.97
0.2999 814.46
0.4001 799.53
0.5003 784.92
0.6001 770.99
0.7004 757.31
0.8003 744.27
0.9003 731.28
0.9498 725.19

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (2) - Liquid Mass density, kg/m3 - Liquid
0.0500 853.94
0.0995 845.89
0.2004 829.97
0.2999 814.46
0.4001 799.53
0.5003 784.92
0.6001 770.99
0.7004 757.31
0.8003 744.27
0.9003 731.28
0.9498 725.19

Sources