Mixture of Propane, 1,3-dibromo- + Ethyl Acetate

Excel

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

Ethyl Acetate

Name
Ethyl Acetate
InChI
InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key
XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
CCOC(C)=O
Mol. Weight (g/mol)
88.11
CAS
141-78-6
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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 Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0601 0.0547
0.1270 0.0934
0.1950 0.1235
0.2607 0.1394
0.3258 0.1433
0.3855 0.1388
0.4407 0.1273
0.4829 0.1134
0.4870 0.1126
0.5298 0.0918
0.5741 0.0706
0.6280 0.0457
0.6870 0.0222
0.7498 0.0032
0.8153 -0.0073
0.8813 -0.0101
0.9434 -0.0057

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

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0601 0.0547
0.1270 0.0934
0.1950 0.1235
0.2607 0.1394
0.3258 0.1433
0.3855 0.1388
0.4407 0.1273
0.4829 0.1134
0.4870 0.1126
0.5298 0.0918
0.5741 0.0706
0.6280 0.0457
0.6870 0.0222
0.7498 0.0032
0.8153 -0.0073
0.8813 -0.0101
0.9434 -0.0057

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Mass density, kg/m3 - Liquid
0.0570 1910.48
0.1189 1845.49
0.1785 1782.59
0.2647 1691.31
0.3199 1632.54
0.4187 1526.9
0.4660 1476.19
0.5091 1429.89
0.6323 1296.79
0.6746 1250.93
0.7715 1145.6
0.8309 1080.67
0.8892 1016.69
0.9615 937.08

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl Acetate (2) - Liquid Mass density, kg/m3 - Liquid
0.0570 1910.48
0.1189 1845.49
0.1785 1782.59
0.2647 1691.31
0.3199 1632.54
0.4187 1526.9
0.4660 1476.19
0.5091 1429.89
0.6323 1296.79
0.6746 1250.93
0.7715 1145.6
0.8309 1080.67
0.8892 1016.69
0.9615 937.08

Sources