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

Name: Propanoic acid, butyl ester
InChI: InChI=1S/C7H14O2/c1-3-5-6-9-7(8)4-2/h3-6H2,1-2H3
InChI Key: BTMVHUNTONAYDX-UHFFFAOYSA-N
Formula: C7H14O2
SMILES: CCCCOC(=O)CC
Mol. Weight (g/mol): 130.18
CAS: 590-01-2

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 Propanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0509	0.0240
0.1183	0.0260
0.1960	0.0120
0.2750	-0.0100
0.3518	-0.0320
0.4473	-0.0550
0.4843	-0.0630
0.5517	-0.0680
0.6323	-0.0710
0.7319	-0.0670
0.8302	-0.0520
0.9193	-0.0360

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

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

Mole fraction of Propanoic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0509	0.0240
0.1183	0.0260
0.1960	0.0120
0.2750	-0.0100
0.3518	-0.0320
0.4473	-0.0550
0.4843	-0.0630
0.5517	-0.0680
0.6323	-0.0710
0.7319	-0.0670
0.8302	-0.0520
0.9193	-0.0360

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
0.0993	1702.4
0.1484	1647.38
0.2006	1590.44
0.2485	1539.57
0.3070	1478.88
0.3593	1426.19
0.4138	1372.46
0.4767	1312.32
0.5324	1260.38
0.5968	1201.95
0.6549	1150.66
0.7210	1093.83
0.7870	1038.79
0.8544	984.01
0.9302	924.33

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
0.0993	1702.4
0.1484	1647.38
0.2006	1590.44
0.2485	1539.57
0.3070	1478.88
0.3593	1426.19
0.4138	1372.46
0.4767	1312.32
0.5324	1260.38
0.5968	1201.95
0.6549	1150.66
0.7210	1093.83
0.7870	1038.79
0.8544	984.01
0.9302	924.33

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
0.0993	0.0000
0.1484	0.0000
0.2006	0.0000
0.2485	0.0000
0.3070	-0.0000
0.3593	-0.0000
0.4138	-1.0000e-08
0.4767	-1.8000e-08
0.5324	-1.9000e-08
0.5968	-2.2000e-08
0.6549	-2.4000e-08
0.7210	-2.6000e-08
0.7870	-2.5000e-08
0.8544	-1.8000e-08
0.9302	-1.0000e-08

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
0.0993	0.0000
0.1484	0.0000
0.2006	0.0000
0.2485	0.0000
0.3070	-0.0000
0.3593	-0.0000
0.4138	-1.0000e-08
0.4767	-1.8000e-08
0.5324	-1.9000e-08
0.5968	-2.2000e-08
0.6549	-2.4000e-08
0.7210	-2.6000e-08
0.7870	-2.5000e-08
0.8544	-1.8000e-08
0.9302	-1.0000e-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