Mixture of Propane, 1,2-dichloro- + Methyl propionate

Name: Propane, 1,2-dichloro-
InChI: InChI=1S/C3H6Cl2/c1-3(5)2-4/h3H,2H2,1H3
InChI Key: KNKRKFALVUDBJE-UHFFFAOYSA-N
Formula: C3H6Cl2
SMILES: CC(Cl)CCl
Mol. Weight (g/mol): 112.99
CAS: 78-87-5

Name: Methyl propionate
InChI: InChI=1S/C4H8O2/c1-3-4(5)6-2/h3H2,1-2H3
InChI Key: RJUFJBKOKNCXHH-UHFFFAOYSA-N
Formula: C4H8O2
SMILES: CCC(=O)OC
Mol. Weight (g/mol): 88.11
CAS: 554-12-1

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Datasets

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

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

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0580	-0.0598
0.0980	-0.1029
0.1570	-0.1474
0.1970	-0.1728
0.2570	-0.2073
0.2970	-0.2302
0.3570	-0.2524
0.3970	-0.2627
0.4570	-0.2668
0.4970	-0.2667
0.5570	-0.2608
0.5970	-0.2551
0.6580	-0.2330
0.6980	-0.2126
0.7580	-0.1782
0.7990	-0.1541
0.8590	-0.1111
0.9000	-0.0810
0.9400	-0.0492

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

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0580	-0.0598
0.0980	-0.1029
0.1570	-0.1474
0.1970	-0.1728
0.2570	-0.2073
0.2970	-0.2302
0.3570	-0.2524
0.3970	-0.2627
0.4570	-0.2668
0.4970	-0.2667
0.5570	-0.2608
0.5970	-0.2551
0.6580	-0.2330
0.6980	-0.2126
0.7580	-0.1782
0.7990	-0.1541
0.8590	-0.1111
0.9000	-0.0810
0.9400	-0.0492

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0491	922.11
0.0980	933.85
0.1476	945.76
0.2006	958.45
0.2506	970.4
0.3014	982.53
0.3525	994.71
0.4008	1006.22
0.4507	1018.12
0.5019	1030.27
0.5519	1042.16
0.6004	1053.7
0.6526	1066.11
0.7010	1077.62
0.7518	1089.7
0.8013	1101.47
0.8474	1112.47
0.8990	1124.77
0.9481	1136.53

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0491	922.11
0.0980	933.85
0.1476	945.76
0.2006	958.45
0.2506	970.4
0.3014	982.53
0.3525	994.71
0.4008	1006.22
0.4507	1018.12
0.5019	1030.27
0.5519	1042.16
0.6004	1053.7
0.6526	1066.11
0.7010	1077.62
0.7518	1089.7
0.8013	1101.47
0.8474	1112.47
0.8990	1124.77
0.9481	1136.53

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0491	0.0000
0.0980	1.7800e-08
0.1476	2.5500e-08
0.2006	3.3500e-08
0.2506	4.1000e-08
0.3014	5.0000e-08
0.3525	5.6900e-08
0.4008	6.3800e-08
0.4507	6.7900e-08
0.5019	7.2900e-08
0.5519	7.6000e-08
0.6004	7.7000e-08
0.6526	7.6800e-08
0.7010	7.4600e-08
0.7518	7.0100e-08
0.8013	6.3000e-08
0.8474	5.4800e-08
0.8990	4.2900e-08
0.9481	2.5000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,2-dichloro- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0491	0.0000
0.0980	1.7800e-08
0.1476	2.5500e-08
0.2006	3.3500e-08
0.2506	4.1000e-08
0.3014	5.0000e-08
0.3525	5.6900e-08
0.4008	6.3800e-08
0.4507	6.7900e-08
0.5019	7.2900e-08
0.5519	7.6000e-08
0.6004	7.7000e-08
0.6526	7.6800e-08
0.7010	7.4600e-08
0.7518	7.0100e-08
0.8013	6.3000e-08
0.8474	5.4800e-08
0.8990	4.2900e-08
0.9481	2.5000e-08

Sources

Excess molar volumes and excess molar enthalpies for binary mixtures of 1,2-dichloropropane with methyl ethanoate, methyl propanoate, and methyl butanoate at T = 298.15K