Mixture of Ethane, 1,2-dichloro- + Butanoic acid, propyl ester

Excel

Ethane, 1,2-dichloro-

Name
Ethane, 1,2-dichloro-
InChI
InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2
InChI Key
WSLDOOZREJYCGB-UHFFFAOYSA-N
Formula
C2H4Cl2
SMILES
ClCCCl
Mol. Weight (g/mol)
98.96
CAS
107-06-2

Butanoic acid, propyl ester

Name
Butanoic acid, propyl ester
InChI
InChI=1S/C7H14O2/c1-3-5-7(8)9-6-4-2/h3-6H2,1-2H3
InChI Key
HUAZGNHGCJGYNP-UHFFFAOYSA-N
Formula
C7H14O2
SMILES
CCCOC(=O)CCC
Mol. Weight (g/mol)
130.18
CAS
105-66-8
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Datasets

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

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

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0365 -0.0350
0.0999 -0.0960
0.1556 -0.1520
0.2176 -0.2200
0.2810 -0.2860
0.3430 -0.3560
0.3848 -0.3980
0.4055 -0.4100
0.4534 -0.4420
0.5266 -0.4560
0.6369 -0.4170
0.7616 -0.3120
0.8961 -0.1670

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

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0365 -0.0350
0.0999 -0.0960
0.1556 -0.1520
0.2176 -0.2200
0.2810 -0.2860
0.3430 -0.3560
0.3848 -0.3980
0.4055 -0.4100
0.4534 -0.4420
0.5266 -0.4560
0.6369 -0.4170
0.7616 -0.3120
0.8961 -0.1670

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0329 1222.22
0.0650 1200.67
0.1029 1176.79
0.1385 1155.7
0.1815 1132.09
0.2225 1110.75
0.2703 1087.77
0.3191 1065.93
0.3743 1043.05
0.4285 1022.26
0.4904 1000.19
0.5560 978.67
0.6280 956.91
0.7087 934.51
0.7989 911.8
0.8938 890.06
1.0000 867.9

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0329 1222.22
0.0650 1200.67
0.1029 1176.79
0.1385 1155.7
0.1815 1132.09
0.2225 1110.75
0.2703 1087.77
0.3191 1065.93
0.3743 1043.05
0.4285 1022.26
0.4904 1000.19
0.5560 978.67
0.6280 956.91
0.7087 934.51
0.7989 911.8
0.8938 890.06
1.0000 867.9

Sources