Mixture of Diisopropyl ether + Benzene, 1,3-dimethyl-

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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

Benzene, 1,3-dimethyl-

Name
Benzene, 1,3-dimethyl-
InChI
InChI=1S/C8H10/c1-7-4-3-5-8(2)6-7/h3-6H,1-2H3
InChI Key
IVSZLXZYQVIEFR-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1cccc(C)c1
Mol. Weight (g/mol)
106.17
CAS
108-38-3
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. Pvap - Vapor or sublimation pressure, kPa (2)
  3. γ - Surface tension liquid-gas, N/m (2)
  4. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1330 0.0448
0.1470 0.0470
0.2210 0.0574
0.2590 0.0593
0.3500 0.0571
0.4240 0.0514
0.4830 0.0453
0.6220 0.0261
0.6560 0.0226
0.7520 0.0115
0.9020 0.0013

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

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1330 0.0448
0.1470 0.0470
0.2210 0.0574
0.2590 0.0593
0.3500 0.0571
0.4240 0.0514
0.4830 0.0453
0.6220 0.0261
0.6560 0.0226
0.7520 0.0115
0.9020 0.0013

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
263.15 0.0572 0.42
263.15 0.1682 1.13
263.15 0.3929 1.72
263.15 0.7981 2.70
263.15 0.8639 2.90
273.15 0.0572 0.78
273.15 0.1682 2.04
273.15 0.3929 3.06
273.15 0.7981 4.79
273.15 0.8639 5.14
283.15 0.0572 1.40
283.15 0.1682 3.49
283.15 0.3929 5.19
283.15 0.7981 8.10
283.15 0.8639 8.66
293.15 0.0572 2.40
293.15 0.1682 5.72
293.15 0.3929 8.44
293.15 0.7981 13.09
293.15 0.8639 13.98
303.15 0.0572 3.94
303.15 0.1682 9.03
303.15 0.3929 13.19
303.15 0.7981 20.38
303.15 0.8639 21.74
313.15 0.0572 6.23
313.15 0.1682 13.78
313.15 0.3929 19.94
313.15 0.7981 30.64
313.15 0.8639 32.67
323.15 0.0572 9.55
323.15 0.1682 20.38
323.15 0.3929 29.23
323.15 0.7981 44.71
323.15 0.8639 47.65
333.15 0.0572 14.22
333.15 0.1682 29.34
333.15 0.3929 41.72
333.15 0.7981 63.49
333.15 0.8639 67.66
343.15 0.0572 20.63
343.15 0.1682 41.20
343.15 0.3929 58.11
343.15 0.7981 88.00
343.15 0.8639 93.79

Vapor or sublimation pressure, kPa [ref]

Fixed Measured
Temperature, K - Liquid Mole fraction of Diisopropyl ether (1) - Liquid Vapor or sublimation pressure, kPa - Liquid
263.15 0.0572 0.42
263.15 0.1682 1.13
263.15 0.3929 1.72
263.15 0.7981 2.70
263.15 0.8639 2.90
273.15 0.0572 0.78
273.15 0.1682 2.04
273.15 0.3929 3.06
273.15 0.7981 4.79
273.15 0.8639 5.14
283.15 0.0572 1.40
283.15 0.1682 3.49
283.15 0.3929 5.19
283.15 0.7981 8.10
283.15 0.8639 8.66
293.15 0.0572 2.40
293.15 0.1682 5.72
293.15 0.3929 8.44
293.15 0.7981 13.09
293.15 0.8639 13.98
303.15 0.0572 3.94
303.15 0.1682 9.03
303.15 0.3929 13.19
303.15 0.7981 20.38
303.15 0.8639 21.74
313.15 0.0572 6.23
313.15 0.1682 13.78
313.15 0.3929 19.94
313.15 0.7981 30.64
313.15 0.8639 32.67
323.15 0.0572 9.55
323.15 0.1682 20.38
323.15 0.3929 29.23
323.15 0.7981 44.71
323.15 0.8639 47.65
333.15 0.0572 14.22
333.15 0.1682 29.34
333.15 0.3929 41.72
333.15 0.7981 63.49
333.15 0.8639 67.66
343.15 0.0572 20.63
343.15 0.1682 41.20
343.15 0.3929 58.11
343.15 0.7981 88.00
343.15 0.8639 93.79

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1019 0.0264
0.2111 0.0249
0.3002 0.0237
0.3999 0.0227
0.4991 0.0217
0.6006 0.0209
0.6994 0.0199
0.7998 0.0190
0.8981 0.0181

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

Operational condition: Temperature, K = 298.15 (Liquid)

Mole fraction of Diisopropyl ether (1) - Liquid Surface tension liquid-gas, N/m - Liquid
0.1019 0.0264
0.2111 0.0249
0.3002 0.0237
0.3999 0.0227
0.4991 0.0217
0.6006 0.0209
0.6994 0.0199
0.7998 0.0190
0.8981 0.0181

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0514 -1.3500e-07
0.1002 -2.4200e-07
0.1526 -3.5500e-07
0.1997 -4.4100e-07
0.2501 -5.2000e-07
0.3002 -5.7900e-07
0.3498 -6.3700e-07
0.4001 -6.7000e-07
0.4516 -7.1100e-07
0.5012 -7.1500e-07
0.5509 -7.1800e-07
0.6001 -6.9200e-07
0.6500 -6.7100e-07
0.6944 -6.1700e-07
0.7498 -5.5800e-07
0.8005 -4.7700e-07
0.8506 -3.9300e-07
0.8998 -2.8300e-07
0.9500 -1.6400e-07

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Diisopropyl ether (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0514 -1.3500e-07
0.1002 -2.4200e-07
0.1526 -3.5500e-07
0.1997 -4.4100e-07
0.2501 -5.2000e-07
0.3002 -5.7900e-07
0.3498 -6.3700e-07
0.4001 -6.7000e-07
0.4516 -7.1100e-07
0.5012 -7.1500e-07
0.5509 -7.1800e-07
0.6001 -6.9200e-07
0.6500 -6.7100e-07
0.6944 -6.1700e-07
0.7498 -5.5800e-07
0.8005 -4.7700e-07
0.8506 -3.9300e-07
0.8998 -2.8300e-07
0.9500 -1.6400e-07

Sources