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

Name: Butanoic acid, butyl ester
InChI: InChI=1S/C8H16O2/c1-3-5-7-10-8(9)6-4-2/h3-7H2,1-2H3
InChI Key: XUPYJHCZDLZNFP-UHFFFAOYSA-N
Formula: C8H16O2
SMILES: CCCCOC(=O)CCC
Mol. Weight (g/mol): 144.21
CAS: 109-21-7

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 Butanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0478	0.0230
0.1102	0.0390
0.1831	0.0440
0.2568	0.0320
0.3257	0.0040
0.3879	-0.0330
0.4528	-0.0680
0.5333	-0.0910
0.6324	-0.1030
0.7588	-0.0940
0.8755	-0.0660

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

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0478	0.0230
0.1102	0.0390
0.1831	0.0440
0.2568	0.0320
0.3257	0.0040
0.3879	-0.0330
0.4528	-0.0680
0.5333	-0.0910
0.6324	-0.1030
0.7588	-0.0940
0.8755	-0.0660

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0790	1834.63
0.1205	1768.32
0.2060	1641.3
0.2513	1578.66
0.3045	1509.31
0.3560	1445.76
0.4085	1384.26
0.4703	1315.94
0.5404	1243.38
0.5989	1186.32
0.7409	1059.86
0.8162	998.93
0.8997	935.58
0.9428	904.65

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0790	1834.63
0.1205	1768.32
0.2060	1641.3
0.2513	1578.66
0.3045	1509.31
0.3560	1445.76
0.4085	1384.26
0.4703	1315.94
0.5404	1243.38
0.5989	1186.32
0.7409	1059.86
0.8162	998.93
0.8997	935.58
0.9428	904.65

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0790	4.8000e-08
0.1205	5.8000e-08
0.2060	8.5000e-08
0.2513	1.1000e-07
0.3045	1.2000e-07
0.3560	1.2400e-07
0.4085	1.2900e-07
0.4703	1.3500e-07
0.5404	1.3200e-07
0.5989	1.2900e-07
0.7409	1.0400e-07
0.8162	7.7000e-08
0.8997	4.9000e-08
0.9428	2.1000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0790	4.8000e-08
0.1205	5.8000e-08
0.2060	8.5000e-08
0.2513	1.1000e-07
0.3045	1.2000e-07
0.3560	1.2400e-07
0.4085	1.2900e-07
0.4703	1.3500e-07
0.5404	1.3200e-07
0.5989	1.2900e-07
0.7409	1.0400e-07
0.8162	7.7000e-08
0.8997	4.9000e-08
0.9428	2.1000e-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