Mixture of Propane, 1,2-dichloro- + Acetic acid, methyl ester

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Propane, 1,2-dichloro-

Name
Propane, 1,2-dichloro-
InChI
InChI=1S/C3H6Cl2/c1-3(5)2-4/h3H,2H2,1H3
InChI Key
KNKRKFALVUDBJE-UHFFFAOYSA-N
Formula
C3H6Cl2
SMILES
CC(Cl)CCl
Mol. Weight (g/mol)
112.99
CAS
78-87-5

Acetic acid, methyl ester

Name
Acetic acid, methyl ester
InChI
InChI=1S/C3H6O2/c1-3(4)5-2/h1-2H3
InChI Key
KXKVLQRXCPHEJC-UHFFFAOYSA-N
Formula
C3H6O2
SMILES
COC(C)=O
Mol. Weight (g/mol)
74.08
CAS
79-20-9
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Datasets

  1. Excess molar enthalpy (molar enthalpy (2)
  2. ρl - Mass density, kg/m3 (2)
  3. Excess molar volume, m3/mol (2)

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

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0490 -0.0303
0.0990 -0.0658
0.1510 -0.0956
0.2040 -0.1249
0.2590 -0.1504
0.2950 -0.1654
0.3520 -0.1804
0.4100 -0.1931
0.4490 -0.1986
0.5090 -0.2023
0.5500 -0.2018
0.5920 -0.1976
0.6560 -0.1873
0.6990 -0.1789
0.7440 -0.1628
0.8110 -0.1331
0.8580 -0.1098
0.9050 -0.0773
0.9520 -0.0438

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

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0490 -0.0303
0.0990 -0.0658
0.1510 -0.0956
0.2040 -0.1249
0.2590 -0.1504
0.2950 -0.1654
0.3520 -0.1804
0.4100 -0.1931
0.4490 -0.1986
0.5090 -0.2023
0.5500 -0.2018
0.5920 -0.1976
0.6560 -0.1873
0.6990 -0.1789
0.7440 -0.1628
0.8110 -0.1331
0.8580 -0.1098
0.9050 -0.0773
0.9520 -0.0438

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Mass density, kg/m3 - Liquid
0.0490 939.96
0.0998 952.99
0.1508 965.82
0.1995 977.91
0.2490 989.88
0.2996 1001.96
0.3498 1013.72
0.3993 1025.11
0.4462 1035.68
0.4951 1046.55
0.5475 1057.97
0.6024 1069.74
0.6505 1079.88
0.6961 1089.35
0.7451 1099.3
0.7979 1109.94
0.8498 1120.18
0.9045 1130.8
0.9513 1139.78

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Mass density, kg/m3 - Liquid
0.0490 939.96
0.0998 952.99
0.1508 965.82
0.1995 977.91
0.2490 989.88
0.2996 1001.96
0.3498 1013.72
0.3993 1025.11
0.4462 1035.68
0.4951 1046.55
0.5475 1057.97
0.6024 1069.74
0.6505 1079.88
0.6961 1089.35
0.7451 1099.3
0.7979 1109.94
0.8498 1120.18
0.9045 1130.8
0.9513 1139.78

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0490 2.8400e-08
0.0998 6.1300e-08
0.1508 8.9700e-08
0.1995 1.0660e-07
0.2490 1.2740e-07
0.2996 1.4080e-07
0.3498 1.4890e-07
0.3993 1.5620e-07
0.4462 1.6030e-07
0.4951 1.6150e-07
0.5475 1.5960e-07
0.6024 1.5330e-07
0.6505 1.4350e-07
0.6961 1.3290e-07
0.7451 1.2350e-07
0.7979 1.0220e-07
0.8498 8.2600e-08
0.9045 5.9100e-08
0.9513 3.3300e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid Excess molar volume, m3/mol - Liquid
0.0490 2.8400e-08
0.0998 6.1300e-08
0.1508 8.9700e-08
0.1995 1.0660e-07
0.2490 1.2740e-07
0.2996 1.4080e-07
0.3498 1.4890e-07
0.3993 1.5620e-07
0.4462 1.6030e-07
0.4951 1.6150e-07
0.5475 1.5960e-07
0.6024 1.5330e-07
0.6505 1.4350e-07
0.6961 1.3290e-07
0.7451 1.2350e-07
0.7979 1.0220e-07
0.8498 8.2600e-08
0.9045 5.9100e-08
0.9513 3.3300e-08

Sources