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

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

Name: Acetic acid, butyl ester
InChI: InChI=1S/C6H12O2/c1-3-4-5-8-6(2)7/h3-5H2,1-2H3
InChI Key: DKPFZGUDAPQIHT-UHFFFAOYSA-N
Formula: C6H12O2
SMILES: CCCCOC(C)=O
Mol. Weight (g/mol): 116.16
CAS: 123-86-4

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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 Acetic acid, butyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0548	0.0080
0.1295	0.0120
0.2133	0.0080
0.2909	-0.0070
0.3612	-0.0360
0.4240	-0.0710
0.4792	-0.1050
0.5321	-0.1210
0.6141	-0.1240
0.7077	-0.1160
0.8080	-0.0910
0.9143	-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 Acetic acid, butyl ester (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0548	0.0080
0.1295	0.0120
0.2133	0.0080
0.2909	-0.0070
0.3612	-0.0360
0.4240	-0.0710
0.4792	-0.1050
0.5321	-0.1210
0.6141	-0.1240
0.7077	-0.1160
0.8080	-0.0910
0.9143	-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- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0468	1904.88
0.0981	1834.95
0.1458	1771.86
0.1939	1709.59
0.2394	1652.62
0.2955	1584.12
0.3458	1524.51
0.4083	1452.85
0.5206	1329.82
0.5824	1265.26
0.6465	1200.31
0.7071	1140.83
0.7784	1072.94
0.8482	1008.73
0.9172	947.42

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0468	1904.88
0.0981	1834.95
0.1458	1771.86
0.1939	1709.59
0.2394	1652.62
0.2955	1584.12
0.3458	1524.51
0.4083	1452.85
0.5206	1329.82
0.5824	1265.26
0.6465	1200.31
0.7071	1140.83
0.7784	1072.94
0.8482	1008.73
0.9172	947.42

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0468	2.4000e-08
0.0981	4.5000e-08
0.1458	5.5000e-08
0.1939	8.3000e-08
0.2394	8.9000e-08
0.2955	1.0900e-07
0.3458	1.2200e-07
0.4083	1.2700e-07
0.5206	1.2500e-07
0.5824	1.2000e-07
0.6465	1.0700e-07
0.7071	9.2000e-08
0.7784	7.5000e-08
0.8482	6.0000e-08
0.9172	2.5000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Propane, 1,3-dibromo- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0468	2.4000e-08
0.0981	4.5000e-08
0.1458	5.5000e-08
0.1939	8.3000e-08
0.2394	8.9000e-08
0.2955	1.0900e-07
0.3458	1.2200e-07
0.4083	1.2700e-07
0.5206	1.2500e-07
0.5824	1.2000e-07
0.6465	1.0700e-07
0.7071	9.2000e-08
0.7784	7.5000e-08
0.8482	6.0000e-08
0.9172	2.5000e-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