Mixture of Butane, 1,4-dichloro- + Acetic acid, propyl ester

Butane, 1,4-dichloro-

Name
Butane, 1,4-dichloro-
InChI
InChI=1S/C4H8Cl2/c5-3-1-2-4-6/h1-4H2
InChI Key
KJDRSWPQXHESDQ-UHFFFAOYSA-N
Formula
C4H8Cl2
SMILES
ClCCCCCl
Mol. Weight (g/mol)
127.01
CAS
110-56-5

Acetic acid, propyl ester

Name
Acetic acid, propyl ester
InChI
InChI=1S/C5H10O2/c1-3-4-7-5(2)6/h3-4H2,1-2H3
InChI Key
YKYONYBAUNKHLG-UHFFFAOYSA-N
Formula
C5H10O2
SMILES
CCCOC(C)=O
Mol. Weight (g/mol)
102.13
CAS
109-60-4
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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 Acetic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0555 -0.0200
0.1316 -0.0550
0.2183 -0.0980
0.3079 -0.1500
0.3915 -0.2010
0.4560 -0.2300
0.4663 -0.2340
0.4979 -0.2410
0.5721 -0.2360
0.6576 -0.2190
0.7494 -0.1870
0.8443 -0.1330
0.9296 -0.0730

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

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0555 -0.0200
0.1316 -0.0550
0.2183 -0.0980
0.3079 -0.1500
0.3915 -0.2010
0.4560 -0.2300
0.4663 -0.2340
0.4979 -0.2410
0.5721 -0.2360
0.6576 -0.2190
0.7494 -0.1870
0.8443 -0.1330
0.9296 -0.0730

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0583 1118.51
0.1175 1103.2
0.1743 1088.55
0.2320 1073.72
0.3494 1043.76
0.4650 1014.55
0.5230 999.98
0.5845 984.6
0.6424 970.19
0.7011 955.64
0.7618 940.61
0.8813 911.2
0.9397 896.91
1.0000 882.08

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Acetic acid, propyl ester (2) - Liquid Mass density, kg/m3 - Liquid
0.0583 1118.51
0.1175 1103.2
0.1743 1088.55
0.2320 1073.72
0.3494 1043.76
0.4650 1014.55
0.5230 999.98
0.5845 984.6
0.6424 970.19
0.7011 955.64
0.7618 940.61
0.8813 911.2
0.9397 896.91
1.0000 882.08

Sources

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