Mixture of Formic acid, butyl ester + Propane, 1,3-dibromo-

Name: Formic acid, butyl ester
InChI: InChI=1S/C5H10O2/c1-2-3-4-7-5-6/h5H,2-4H2,1H3
InChI Key: NMJJFJNHVMGPGM-UHFFFAOYSA-N
Formula: C5H10O2
SMILES: CCCCOC=O
Mol. Weight (g/mol): 102.13
CAS: 592-84-7

Name: Propane, 1,3-dibromo-
InChI: InChI=1S/C3H6Br2/c4-2-1-3-5/h1-3H2
InChI Key: VEFLKXRACNJHOV-UHFFFAOYSA-N
Formula: C3H6Br2
SMILES: BrCCCBr
Mol. Weight (g/mol): 201.89
CAS: 109-64-8

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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 Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0631	0.0650
0.1489	0.1280
0.2355	0.1660
0.3208	0.1820
0.3958	0.1790
0.4589	0.1710
0.5144	0.1580
0.5498	0.1490
0.5621	0.1440
0.6372	0.1210
0.7237	0.0950
0.8208	0.0600
0.9151	0.0290

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

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0631	0.0650
0.1489	0.1280
0.2355	0.1660
0.3208	0.1820
0.3958	0.1790
0.4589	0.1710
0.5144	0.1580
0.5498	0.1490
0.5621	0.1440
0.6372	0.1210
0.7237	0.0950
0.8208	0.0600
0.9151	0.0290

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0550	1904.29
0.1095	1839.0
0.1626	1776.37
0.2171	1712.74
0.2730	1648.68
0.3252	1589.49
0.5003	1397.08
0.5617	1331.4
0.6186	1271.46
0.6866	1200.91
0.8026	1082.84
0.8655	1020.08
0.9344	952.37

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Mass density, kg/m3 - Liquid
0.0550	1904.29
0.1095	1839.0
0.1626	1776.37
0.2171	1712.74
0.2730	1648.68
0.3252	1589.49
0.5003	1397.08
0.5617	1331.4
0.6186	1271.46
0.6866	1200.91
0.8026	1082.84
0.8655	1020.08
0.9344	952.37

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0550	1.6000e-08
0.1095	3.7000e-08
0.1626	5.7000e-08
0.2171	8.4000e-08
0.2730	9.5000e-08
0.3252	1.1000e-07
0.5003	1.0900e-07
0.5617	1.0500e-07
0.6186	9.5000e-08
0.6866	7.9000e-08
0.8026	5.8000e-08
0.8655	4.1000e-08
0.9344	1.7000e-08

Excess molar volume, m3/mol [ref]

Operational conditions:

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

Mole fraction of Formic acid, butyl ester (1) - Liquid	Excess molar volume, m3/mol - Liquid
0.0550	1.6000e-08
0.1095	3.7000e-08
0.1626	5.7000e-08
0.2171	8.4000e-08
0.2730	9.5000e-08
0.3252	1.1000e-07
0.5003	1.0900e-07
0.5617	1.0500e-07
0.6186	9.5000e-08
0.6866	7.9000e-08
0.8026	5.8000e-08
0.8655	4.1000e-08
0.9344	1.7000e-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