Mixture of Ethane, 1,2-dibromo- + Acetic acid, butyl ester

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

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
0.0399	-0.0010
0.0964	-0.0030
0.1625	-0.0160
0.2339	-0.0430
0.3039	-0.0730
0.3717	-0.1030
0.4237	-0.1290
0.4749	-0.1470
0.5228	-0.1520
0.5985	-0.1530
0.6854	-0.1390
0.7854	-0.1160
0.8989	-0.0620

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
0.0399	-0.0010
0.0964	-0.0030
0.1625	-0.0160
0.2339	-0.0430
0.3039	-0.0730
0.3717	-0.1030
0.4237	-0.1290
0.4749	-0.1470
0.5228	-0.1520
0.5985	-0.1530
0.6854	-0.1390
0.7854	-0.1160
0.8989	-0.0620

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0411	2088.28
0.0776	2020.04
0.1229	1938.53
0.1646	1867.04
0.2132	1787.29
0.2547	1722.15
0.3138	1633.77
0.3655	1560.33
0.4245	1480.67
0.4793	1410.27
0.5474	1327.38
0.6060	1259.71
0.6776	1181.2
0.7476	1108.57
0.8230	1034.7
0.9008	962.52

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Mass density, kg/m3 - Liquid
0.0411	2088.28
0.0776	2020.04
0.1229	1938.53
0.1646	1867.04
0.2132	1787.29
0.2547	1722.15
0.3138	1633.77
0.3655	1560.33
0.4245	1480.67
0.4793	1410.27
0.5474	1327.38
0.6060	1259.71
0.6776	1181.2
0.7476	1108.57
0.8230	1034.7
0.9008	962.52

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0411	2.5000e-08
0.0776	4.4000e-08
0.1229	8.8000e-08
0.1646	1.0700e-07
0.2132	1.2800e-07
0.2547	1.4200e-07
0.3138	1.6200e-07
0.3655	1.7300e-07
0.4245	1.7700e-07
0.4793	1.8200e-07
0.5474	1.7100e-07
0.6060	1.6100e-07
0.6776	1.4500e-07
0.7476	1.2200e-07
0.8230	8.1000e-08
0.9008	4.6000e-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- (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0411	2.5000e-08
0.0776	4.4000e-08
0.1229	8.8000e-08
0.1646	1.0700e-07
0.2132	1.2800e-07
0.2547	1.4200e-07
0.3138	1.6200e-07
0.3655	1.7300e-07
0.4245	1.7700e-07
0.4793	1.8200e-07
0.5474	1.7100e-07
0.6060	1.6100e-07
0.6776	1.4500e-07
0.7476	1.2200e-07
0.8230	8.1000e-08
0.9008	4.6000e-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