Mixture of Butanoic acid, propyl ester + Propane, 1,3-dichloro-

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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

Propane, 1,3-dichloro-

Name
Propane, 1,3-dichloro-
InChI
InChI=1S/C3H6Cl2/c4-2-1-3-5/h1-3H2
InChI Key
YHRUOJUYPBUZOS-UHFFFAOYSA-N
Formula
C3H6Cl2
SMILES
ClCCCCl
Mol. Weight (g/mol)
112.99
CAS
142-28-9
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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 (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0386 -0.0200
0.0938 -0.0530
0.1590 -0.0960
0.2273 -0.1570
0.2973 -0.2120
0.3649 -0.2620
0.4253 -0.2980
0.5121 -0.3390
0.5732 -0.3340
0.6582 -0.3150
0.7480 -0.2730
0.8421 -0.1940
0.9299 -0.0980

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

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0386 -0.0200
0.0938 -0.0530
0.1590 -0.0960
0.2273 -0.1570
0.2973 -0.2120
0.3649 -0.2620
0.4253 -0.2980
0.5121 -0.3390
0.5732 -0.3340
0.6582 -0.3150
0.7480 -0.2730
0.8421 -0.1940
0.9299 -0.0980

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (1) - Liquid Mass density, kg/m3 - Liquid
0.0366 1161.49
0.0766 1143.1
0.1186 1124.61
0.1603 1107.03
0.2067 1088.41
0.2552 1069.83
0.3066 1051.21
0.3595 1032.94
0.4152 1014.72
0.5357 978.32
0.5999 960.48
0.6691 942.33
0.7439 923.8
0.8228 905.44
0.9064 887.12
1.0000 867.9

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Butanoic acid, propyl ester (1) - Liquid Mass density, kg/m3 - Liquid
0.0366 1161.49
0.0766 1143.1
0.1186 1124.61
0.1603 1107.03
0.2067 1088.41
0.2552 1069.83
0.3066 1051.21
0.3595 1032.94
0.4152 1014.72
0.5357 978.32
0.5999 960.48
0.6691 942.33
0.7439 923.8
0.8228 905.44
0.9064 887.12
1.0000 867.9

Sources