Mixture of Butanoic acid, butyl ester + Butane, 1,4-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: 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 Butanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0526	0.0270
0.1195	0.0490
0.1947	0.0580
0.2716	0.0490
0.3471	0.0230
0.4134	-0.0110
0.4710	-0.0490
0.5005	-0.0650
0.5790	-0.0860
0.6761	-0.0930
0.7901	-0.0820
0.9017	-0.0510

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
0.0526	0.0270
0.1195	0.0490
0.1947	0.0580
0.2716	0.0490
0.3471	0.0230
0.4134	-0.0110
0.4710	-0.0490
0.5005	-0.0650
0.5790	-0.0860
0.6761	-0.0930
0.7901	-0.0820
0.9017	-0.0510

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0459	1757.74
0.1377	1643.47
0.1788	1594.83
0.2814	1479.86
0.3346	1423.4
0.3891	1367.86
0.5003	1260.78
0.5704	1197.33
0.6285	1146.9
0.7046	1083.68
0.7684	1032.96
0.8513	970.06
0.9156	923.4

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0459	1757.74
0.1377	1643.47
0.1788	1594.83
0.2814	1479.86
0.3346	1423.4
0.3891	1367.86
0.5003	1260.78
0.5704	1197.33
0.6285	1146.9
0.7046	1083.68
0.7684	1032.96
0.8513	970.06
0.9156	923.4

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0459	-0.0000
0.1377	-1.0000e-08
0.1788	-1.0000e-08
0.2814	-0.0000
0.3346	0.0000
0.3891	0.0000
0.5003	1.9000e-08
0.5704	2.6000e-08
0.6285	3.1000e-08
0.7046	3.2000e-08
0.7684	3.5000e-08
0.8513	2.6000e-08
0.9156	1.8000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Butanoic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0459	-0.0000
0.1377	-1.0000e-08
0.1788	-1.0000e-08
0.2814	-0.0000
0.3346	0.0000
0.3891	0.0000
0.5003	1.9000e-08
0.5704	2.6000e-08
0.6285	3.1000e-08
0.7046	3.2000e-08
0.7684	3.5000e-08
0.8513	2.6000e-08
0.9156	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