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

Name: Propanoic acid, butyl ester
InChI: InChI=1S/C7H14O2/c1-3-5-6-9-7(8)4-2/h3-6H2,1-2H3
InChI Key: BTMVHUNTONAYDX-UHFFFAOYSA-N
Formula: C7H14O2
SMILES: CCCCOC(=O)CC
Mol. Weight (g/mol): 130.18
CAS: 590-01-2

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

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:

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

Mole fraction of Propanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0450	0.0320
0.1122	0.0520
0.1829	0.0540
0.2541	0.0380
0.3191	0.0090
0.3797	-0.0340
0.4331	-0.0630
0.4438	-0.0710
0.5107	-0.0960
0.5886	-0.1090
0.6793	-0.1100
0.7807	-0.0920
0.8921	-0.0550

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, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0450	0.0320
0.1122	0.0520
0.1829	0.0540
0.2541	0.0380
0.3191	0.0090
0.3797	-0.0340
0.4331	-0.0630
0.4438	-0.0710
0.5107	-0.0960
0.5886	-0.1090
0.6793	-0.1100
0.7807	-0.0920
0.8921	-0.0550

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0443	1900.67
0.0867	1836.4
0.1297	1773.45
0.1758	1708.87
0.2241	1643.68
0.2725	1580.97
0.3240	1517.05
0.4335	1389.62
0.4911	1326.87
0.6187	1197.0
0.6880	1131.33
0.7551	1070.67
0.8298	1006.49
0.9086	941.97

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0443	1900.67
0.0867	1836.4
0.1297	1773.45
0.1758	1708.87
0.2241	1643.68
0.2725	1580.97
0.3240	1517.05
0.4335	1389.62
0.4911	1326.87
0.6187	1197.0
0.6880	1131.33
0.7551	1070.67
0.8298	1006.49
0.9086	941.97

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0443	1.8000e-08
0.0867	2.8000e-08
0.1297	4.8000e-08
0.1758	5.8000e-08
0.2241	7.2000e-08
0.2725	8.5000e-08
0.3240	9.1000e-08
0.4335	9.9000e-08
0.4911	9.7000e-08
0.6187	9.0000e-08
0.6880	7.7000e-08
0.7551	6.8000e-08
0.8298	4.7000e-08
0.9086	3.2000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0443	1.8000e-08
0.0867	2.8000e-08
0.1297	4.8000e-08
0.1758	5.8000e-08
0.2241	7.2000e-08
0.2725	8.5000e-08
0.3240	9.1000e-08
0.4335	9.9000e-08
0.4911	9.7000e-08
0.6187	9.0000e-08
0.6880	7.7000e-08
0.7551	6.8000e-08
0.8298	4.7000e-08
0.9086	3.2000e-08

Sources

Thermodynamic study of (alkyl esters + alpha,beta-alkyl dihalides) VI.H and V for 20 binary mixtures {xCu-1H2u-1CO2(CH2)3CH3 + (1 - x)alpha,omega-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, alpha = 1, and v = omega = 2 to 6