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

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

Name: Propane, 1,3-dichloro-
InChI: InChI=1S/C3H6Cl2/c4-2-1-3-5/h1-3H2
InChI Key: YHRUOJUYPBUZOS-UHFFFAOYSA-N
Formula: C3H6Cl2
SMILES: ClCCCCl
Mol. Weight (g/mol): 112.99
CAS: 142-28-9

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 (4)

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

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1171	0.0342
0.2311	0.0689
0.3403	0.0846
0.4350	0.0819
0.5147	0.0692
0.5813	0.0519
0.6354	0.0374
0.6820	0.0246
0.7186	0.0124
0.7381	-0.0155
0.7773	-0.0284
0.8208	-0.0385
0.8622	-0.0441
0.9018	-0.0359
0.9383	-0.0189
0.9723	-0.0012

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

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.1171	0.0342
0.2311	0.0689
0.3403	0.0846
0.4350	0.0819
0.5147	0.0692
0.5813	0.0519
0.6354	0.0374
0.6820	0.0246
0.7186	0.0124
0.7381	-0.0155
0.7773	-0.0284
0.8208	-0.0385
0.8622	-0.0441
0.9018	-0.0359
0.9383	-0.0189
0.9723	-0.0012

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101.325 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0760	1161.06
0.1432	1145.36
0.2073	1130.02
0.2696	1114.94
0.3338	1099.05
0.3940	1083.9
0.4558	1068.05
0.5152	1052.57
0.5731	1037.18
0.6297	1021.91
0.6862	1006.34
0.7413	990.94
0.7940	975.98
0.8475	960.54
0.8994	945.31
0.9494	930.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0758	1161.82
0.1392	1147.48
0.2059	1132.04
0.2686	1117.5
0.3360	1101.45
0.3983	1086.31
0.4584	1071.44
0.5183	1056.42
0.5752	1041.98
0.6319	1027.35
0.6884	1012.54
0.7433	997.87
0.7967	983.56
0.8490	969.23
0.9005	954.87
0.9490	941.1

Mass density, kg/m3 [ref]

Operational conditions:

Pressure, kPa = 101.325 (Liquid)
Temperature, K = 298.15 (Liquid)

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0760	1161.06
0.1432	1145.36
0.2073	1130.02
0.2696	1114.94
0.3338	1099.05
0.3940	1083.9
0.4558	1068.05
0.5152	1052.57
0.5731	1037.18
0.6297	1021.91
0.6862	1006.34
0.7413	990.94
0.7940	975.98
0.8475	960.54
0.8994	945.31
0.9494	930.3

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0758	1161.82
0.1392	1147.48
0.2059	1132.04
0.2686	1117.5
0.3360	1101.45
0.3983	1086.31
0.4584	1071.44
0.5183	1056.42
0.5752	1041.98
0.6319	1027.35
0.6884	1012.54
0.7433	997.87
0.7967	983.56
0.8490	969.23
0.9005	954.87
0.9490	941.1

Sources