Mixture of Propane, 1,3-dibromo- + Methyl valerate

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Propane, 1,3-dibromo-

Name
Propane, 1,3-dibromo-
InChI
InChI=1S/C3H6Br2/c4-2-1-3-5/h1-3H2
InChI Key
VEFLKXRACNJHOV-UHFFFAOYSA-N
Formula
C3H6Br2
SMILES
BrCCCBr
Mol. Weight (g/mol)
201.89
CAS
109-64-8

Methyl valerate

Name
Methyl valerate
InChI
InChI=1S/C6H12O2/c1-3-4-5-6(7)8-2/h3-5H2,1-2H3
InChI Key
HNBDRPTVWVGKBR-UHFFFAOYSA-N
Formula
C6H12O2
SMILES
CCCCC(=O)OC
Mol. Weight (g/mol)
116.16
CAS
624-24-8
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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 Methyl valerate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0492 0.0239
0.1163 0.0387
0.1938 0.0407
0.2736 0.0321
0.3380 0.0176
0.4100 -0.0099
0.4582 -0.0311
0.4998 -0.0470
0.5481 -0.0609
0.6786 -0.0662
0.7994 -0.0551
0.9065 -0.0355

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

Operational conditions:

Mole fraction of Methyl valerate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0492 0.0239
0.1163 0.0387
0.1938 0.0407
0.2736 0.0321
0.3380 0.0176
0.4100 -0.0099
0.4582 -0.0311
0.4998 -0.0470
0.5481 -0.0609
0.6786 -0.0662
0.7994 -0.0551
0.9065 -0.0355

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Methyl valerate (2) - Liquid Mass density, kg/m3 - Liquid
0.0534 1896.4
0.0937 1841.97
0.1477 1771.31
0.1880 1720.07
0.2439 1650.83
0.2975 1586.35
0.3439 1532.03
0.4116 1455.16
0.4656 1395.81
0.5216 1335.88
0.5922 1262.69
0.6481 1206.41
0.7047 1151.1
0.7835 1076.35
0.8493 1016.07
0.9201 953.2

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Methyl valerate (2) - Liquid Mass density, kg/m3 - Liquid
0.0534 1896.4
0.0937 1841.97
0.1477 1771.31
0.1880 1720.07
0.2439 1650.83
0.2975 1586.35
0.3439 1532.03
0.4116 1455.16
0.4656 1395.81
0.5216 1335.88
0.5922 1262.69
0.6481 1206.41
0.7047 1151.1
0.7835 1076.35
0.8493 1016.07
0.9201 953.2

Sources