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

Excel

Ethyl formate

Name
Ethyl formate
InChI
InChI=1S/C3H6O2/c1-2-5-3-4/h3H,2H2,1H3
InChI Key
WBJINCZRORDGAQ-UHFFFAOYSA-N
Formula
C3H6O2
SMILES
CCOC=O
Mol. Weight (g/mol)
74.08
CAS
109-94-4

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
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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 formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0727 0.1762
0.1458 0.3018
0.2104 0.4011
0.2886 0.4733
0.3588 0.5136
0.4253 0.5284
0.4828 0.5237
0.5358 0.5105
0.5812 0.4868
0.6324 0.4548
0.6925 0.4037
0.7529 0.3393
0.8177 0.2594
0.8820 0.1731
0.9449 0.0879

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

Operational conditions:

Mole fraction of Ethyl formate (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0727 0.1762
0.1458 0.3018
0.2104 0.4011
0.2886 0.4733
0.3588 0.5136
0.4253 0.5284
0.4828 0.5237
0.5358 0.5105
0.5812 0.4868
0.6324 0.4548
0.6925 0.4037
0.7529 0.3393
0.8177 0.2594
0.8820 0.1731
0.9449 0.0879

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl formate (1) - Liquid Mass density, kg/m3 - Liquid
0.0717 1908.92
0.1454 1844.11
0.2149 1781.28
0.2791 1721.26
0.3468 1656.48
0.4099 1594.33
0.4685 1534.98
0.5893 1407.8
0.6459 1345.63
0.6988 1285.95
0.7521 1224.47
0.8028 1164.26
0.8548 1101.12
0.9056 1037.67

Mass density, kg/m3 [ref]

Operational conditions:

Mole fraction of Ethyl formate (1) - Liquid Mass density, kg/m3 - Liquid
0.0717 1908.92
0.1454 1844.11
0.2149 1781.28
0.2791 1721.26
0.3468 1656.48
0.4099 1594.33
0.4685 1534.98
0.5893 1407.8
0.6459 1345.63
0.6988 1285.95
0.7521 1224.47
0.8028 1164.26
0.8548 1101.12
0.9056 1037.67

Sources