Mixture of Butanoic acid, butyl ester + Ethane, 1,2-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: 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

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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
0.0408	0.0260
0.0978	0.0480
0.1663	0.0580
0.2361	0.0510
0.2997	0.0320
0.3488	0.0150
0.4085	-0.0020
0.4847	-0.0270
0.5816	-0.0480
0.7159	-0.0540
0.8632	-0.0370
0.9347	-0.0220

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
0.0408	0.0260
0.0978	0.0480
0.1663	0.0580
0.2361	0.0510
0.2997	0.0320
0.3488	0.0150
0.4085	-0.0020
0.4847	-0.0270
0.5816	-0.0480
0.7159	-0.0540
0.8632	-0.0370
0.9347	-0.0220

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0340	2084.99
0.0680	2006.19
0.1037	1928.71
0.1757	1786.46
0.2194	1707.65
0.2700	1623.15
0.3645	1481.33
0.4193	1407.36
0.5507	1250.61
0.6263	1171.44
0.7028	1098.24
0.7871	1024.55
0.8864	945.82

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Mass density, kg/m3 - Liquid
0.0340	2084.99
0.0680	2006.19
0.1037	1928.71
0.1757	1786.46
0.2194	1707.65
0.2700	1623.15
0.3645	1481.33
0.4193	1407.36
0.5507	1250.61
0.6263	1171.44
0.7028	1098.24
0.7871	1024.55
0.8864	945.82

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Ethane, 1,2-dibromo- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0340	3.7000e-08
0.0680	8.0000e-08
0.1037	1.2000e-07
0.1757	1.6000e-07
0.2194	1.9700e-07
0.2700	2.1700e-07
0.3645	2.5000e-07
0.4193	2.5300e-07
0.5507	2.4000e-07
0.6263	2.1700e-07
0.7028	1.8700e-07
0.7871	1.3700e-07
0.8864	7.0000e-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- (2) - Liquid	Excess molar volume, m3/mol - Liquid
0.0340	3.7000e-08
0.0680	8.0000e-08
0.1037	1.2000e-07
0.1757	1.6000e-07
0.2194	1.9700e-07
0.2700	2.1700e-07
0.3645	2.5000e-07
0.4193	2.5300e-07
0.5507	2.4000e-07
0.6263	2.1700e-07
0.7028	1.8700e-07
0.7871	1.3700e-07
0.8864	7.0000e-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