Mixture of Propanoic acid, butyl ester + Ethane, 1,2-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: Ethane, 1,2-dibromo-
InChI: InChI=1S/C2H4Br2/c3-1-2-4/h1-2H2
InChI Key: PAAZPARNPHGIKF-UHFFFAOYSA-N
Formula: C2H4Br2
SMILES: BrCCBr
Mol. Weight (g/mol): 187.86
CAS: 106-93-4

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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
0.0417	0.0220
0.0966	0.0310
0.1618	0.0260
0.2302	0.0080
0.2936	-0.0200
0.3529	-0.0500
0.4091	-0.0750
0.4511	-0.0920
0.4917	-0.1010
0.5694	-0.1110
0.6594	-0.1100
0.7605	-0.0960
0.8773	-0.0630

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
0.0417	0.0220
0.0966	0.0310
0.1618	0.0260
0.2302	0.0080
0.2936	-0.0200
0.3529	-0.0500
0.4091	-0.0750
0.4511	-0.0920
0.4917	-0.1010
0.5694	-0.1110
0.6594	-0.1100
0.7605	-0.0960
0.8773	-0.0630

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0377	2085.27
0.0756	2005.97
0.1117	1934.81
0.1528	1857.84
0.1955	1782.46
0.2371	1712.84
0.2870	1633.9
0.3666	1517.74
0.5139	1328.73
0.5797	1253.45
0.6475	1181.15
0.7224	1106.68
0.8024	1032.76
0.8971	951.87

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0377	2085.27
0.0756	2005.97
0.1117	1934.81
0.1528	1857.84
0.1955	1782.46
0.2371	1712.84
0.2870	1633.9
0.3666	1517.74
0.5139	1328.73
0.5797	1253.45
0.6475	1181.15
0.7224	1106.68
0.8024	1032.76
0.8971	951.87

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0377	4.5000e-08
0.0756	1.0300e-07
0.1117	1.2000e-07
0.1528	1.5100e-07
0.1955	1.6400e-07
0.2371	1.7800e-07
0.2870	1.9000e-07
0.3666	1.9700e-07
0.5139	1.7800e-07
0.5797	1.6700e-07
0.6475	1.4700e-07
0.7224	1.1500e-07
0.8024	8.4000e-08
0.8971	4.1000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0377	4.5000e-08
0.0756	1.0300e-07
0.1117	1.2000e-07
0.1528	1.5100e-07
0.1955	1.6400e-07
0.2371	1.7800e-07
0.2870	1.9000e-07
0.3666	1.9700e-07
0.5139	1.7800e-07
0.5797	1.6700e-07
0.6475	1.4700e-07
0.7224	1.1500e-07
0.8024	8.4000e-08
0.8971	4.1000e-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