Mixture of Hexane, 1,6-dibromo- + Acetic acid, butyl ester

Name: Hexane, 1,6-dibromo-
InChI: InChI=1S/C6H12Br2/c7-5-3-1-2-4-6-8/h1-6H2
InChI Key: SGRHVVLXEBNBDV-UHFFFAOYSA-N
Formula: C6H12Br2
SMILES: BrCCCCCCBr
Mol. Weight (g/mol): 243.97
CAS: 629-03-8

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
0.0742	0.0340
0.1664	0.0580
0.2700	0.0750
0.3625	0.0750
0.4313	0.0630
0.4863	0.0500
0.5098	0.0400
0.5385	0.0310
0.5631	0.0170
0.5869	0.0070
0.6272	-0.0100
0.6989	-0.0220
0.7827	-0.0260
0.8669	-0.0200
0.9422	-0.0100

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
0.0742	0.0340
0.1664	0.0580
0.2700	0.0750
0.3625	0.0750
0.4313	0.0630
0.4863	0.0500
0.5098	0.0400
0.5385	0.0310
0.5631	0.0170
0.5869	0.0070
0.6272	-0.0100
0.6989	-0.0220
0.7827	-0.0260
0.8669	-0.0200
0.9422	-0.0100

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Acetic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.1369	1513.56
0.2111	1464.63
0.2634	1429.52
0.3292	1384.72
0.3855	1345.64
0.4456	1303.3
0.5046	1260.95
0.5622	1219.05
0.6175	1178.12
0.7334	1090.14
0.7855	1049.66
0.8433	1003.91
0.8909	965.75
0.9462	920.67

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Acetic acid, butyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
0.1369	1513.56
0.2111	1464.63
0.2634	1429.52
0.3292	1384.72
0.3855	1345.64
0.4456	1303.3
0.5046	1260.95
0.5622	1219.05
0.6175	1178.12
0.7334	1090.14
0.7855	1049.66
0.8433	1003.91
0.8909	965.75
0.9462	920.67

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Acetic acid, butyl ester (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.1369	-1.4000e-08
0.2111	-2.5000e-08
0.2634	-3.1000e-08
0.3292	-4.0000e-08
0.3855	-4.4000e-08
0.4456	-4.7000e-08
0.5046	-4.8000e-08
0.5622	-5.3000e-08
0.6175	-5.2000e-08
0.7334	-4.7000e-08
0.7855	-4.4000e-08
0.8433	-3.5000e-08
0.8909	-2.7000e-08
0.9462	-1.8000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Acetic acid, butyl ester (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.1369	-1.4000e-08
0.2111	-2.5000e-08
0.2634	-3.1000e-08
0.3292	-4.0000e-08
0.3855	-4.4000e-08
0.4456	-4.7000e-08
0.5046	-4.8000e-08
0.5622	-5.3000e-08
0.6175	-5.2000e-08
0.7334	-4.7000e-08
0.7855	-4.4000e-08
0.8433	-3.5000e-08
0.8909	-2.7000e-08
0.9462	-1.8000e-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