Mixture of Propanoic acid, ethyl ester + Propane, 1,3-dibromo-

Name: Propanoic acid, ethyl ester
InChI: InChI=1S/C5H10O2/c1-3-5(6)7-4-2/h3-4H2,1-2H3
InChI Key: FKRCODPIKNYEAC-UHFFFAOYSA-N
Formula: C5H10O2
SMILES: CCOC(=O)CC
Mol. Weight (g/mol): 102.13
CAS: 105-37-3

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

Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

Excess molar enthalpy (molar enthalpy (2)
ρ_l - Mass density, kg/m3 (2)

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, ethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0471	0.0234
0.1006	0.0364
0.1564	0.0384
0.2139	0.0329
0.2707	0.0162
0.3244	-0.0034
0.3765	-0.0253
0.4201	-0.0466
0.4478	-0.0654
0.4591	-0.0817
0.4930	-0.0604
0.4983	-0.0857
0.5563	-0.1026
0.6207	-0.1086
0.6908	-0.1051
0.7671	-0.0915
0.8476	-0.0687
0.9262	-0.0379

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

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, ethyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0471	0.0234
0.1006	0.0364
0.1564	0.0384
0.2139	0.0329
0.2707	0.0162
0.3244	-0.0034
0.3765	-0.0253
0.4201	-0.0466
0.4478	-0.0654
0.4591	-0.0817
0.4930	-0.0604
0.4983	-0.0857
0.5563	-0.1026
0.6207	-0.1086
0.6908	-0.1051
0.7671	-0.0915
0.8476	-0.0687
0.9262	-0.0379

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, ethyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.1075	1839.36
0.1610	1775.98
0.2159	1711.67
0.2732	1645.81
0.3842	1520.67
0.4468	1451.66
0.5011	1392.66
0.5622	1327.28
0.6827	1201.05
0.7443	1137.95
0.8686	1013.23

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Propanoic acid, ethyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.1075	1839.36
0.1610	1775.98
0.2159	1711.67
0.2732	1645.81
0.3842	1520.67
0.4468	1451.66
0.5011	1392.66
0.5622	1327.28
0.6827	1201.05
0.7443	1137.95
0.8686	1013.23

Sources

Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6