Mixture of Acetic acid, butyl ester + Butane, 1,4-dibromo-

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

Name: Butane, 1,4-dibromo-
InChI: InChI=1S/C4H8Br2/c5-3-1-2-4-6/h1-4H2
InChI Key: ULTHEAFYOOPTTB-UHFFFAOYSA-N
Formula: C4H8Br2
SMILES: BrCCCCBr
Mol. Weight (g/mol): 215.91
CAS: 110-52-1

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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 (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0576	0.0140
0.1350	0.0240
0.2211	0.0260
0.3056	0.0150
0.3729	-0.0040
0.4291	-0.0260
0.4798	-0.0520
0.4866	-0.0660
0.5277	-0.0780
0.5406	-0.0880
0.6030	-0.0980
0.6715	-0.0990
0.7464	-0.0930
0.8416	-0.0650
0.9307	-0.0300

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 (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0576	0.0140
0.1350	0.0240
0.2211	0.0260
0.3056	0.0150
0.3729	-0.0040
0.4291	-0.0260
0.4798	-0.0520
0.4866	-0.0660
0.5277	-0.0780
0.5406	-0.0880
0.6030	-0.0980
0.6715	-0.0990
0.7464	-0.0930
0.8416	-0.0650
0.9307	-0.0300

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butane, 1,4-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0600	1754.15
0.1131	1699.34
0.1633	1648.18
0.2229	1588.24
0.2748	1536.73
0.3886	1426.0
0.4426	1374.38
0.5000	1320.28
0.6216	1207.87
0.6806	1154.38
0.8076	1041.44
0.8633	992.97
0.9298	935.67

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butane, 1,4-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0600	1754.15
0.1131	1699.34
0.1633	1648.18
0.2229	1588.24
0.2748	1536.73
0.3886	1426.0
0.4426	1374.38
0.5000	1320.28
0.6216	1207.87
0.6806	1154.38
0.8076	1041.44
0.8633	992.97
0.9298	935.67

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butane, 1,4-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0600	1.2000e-08
0.1131	2.5000e-08
0.1633	3.1000e-08
0.2229	4.0000e-08
0.2748	4.7000e-08
0.3886	5.0000e-08
0.4426	4.9000e-08
0.5000	4.7000e-08
0.6216	4.2000e-08
0.6806	3.5000e-08
0.8076	2.3000e-08
0.8633	1.6000e-08
0.9298	0.0000

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butane, 1,4-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0600	1.2000e-08
0.1131	2.5000e-08
0.1633	3.1000e-08
0.2229	4.0000e-08
0.2748	4.7000e-08
0.3886	5.0000e-08
0.4426	4.9000e-08
0.5000	4.7000e-08
0.6216	4.2000e-08
0.6806	3.5000e-08
0.8076	2.3000e-08
0.8633	1.6000e-08
0.9298	0.0000

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