Mixture of Ethyl formate + Butane, 1,4-dibromo-

Name: Ethyl formate
InChI: InChI=1S/C3H6O2/c1-2-5-3-4/h3H,2H2,1H3
InChI Key: WBJINCZRORDGAQ-UHFFFAOYSA-N
Formula: C3H6O2
SMILES: CCOC=O
Mol. Weight (g/mol): 74.08
CAS: 109-94-4

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

Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

Excess molar enthalpy (molar enthalpy (2)
ρ_l - Mass density, kg/m3 (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 Ethyl formate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0799	0.2295
0.1652	0.3752
0.2469	0.4937
0.3246	0.5666
0.3970	0.6055
0.4607	0.6217
0.5109	0.6154
0.5179	0.6188
0.5525	0.6077
0.5649	0.5985
0.5973	0.5863
0.6082	0.5739
0.6459	0.5499
0.6929	0.5056
0.7514	0.4310
0.8051	0.3543
0.8598	0.2574
0.9121	0.1583
0.9614	0.0594

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

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0799	0.2295
0.1652	0.3752
0.2469	0.4937
0.3246	0.5666
0.3970	0.6055
0.4607	0.6217
0.5109	0.6154
0.5179	0.6188
0.5525	0.6077
0.5649	0.5985
0.5973	0.5863
0.6082	0.5739
0.6459	0.5499
0.6929	0.5056
0.7514	0.4310
0.8051	0.3543
0.8598	0.2574
0.9121	0.1583
0.9614	0.0594

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0952	1765.32
0.1744	1716.81
0.2604	1660.33
0.3295	1611.72
0.4012	1557.95
0.4668	1505.48
0.5355	1446.96
0.5888	1398.87
0.6436	1346.56
0.6981	1291.4
0.7934	1186.14
0.9238	1023.59
0.9623	970.42

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl formate (1) - Liquid	Mass density, kg/m3 - Liquid
0.0952	1765.32
0.1744	1716.81
0.2604	1660.33
0.3295	1611.72
0.4012	1557.95
0.4668	1505.48
0.5355	1446.96
0.5888	1398.87
0.6436	1346.56
0.6981	1291.4
0.7934	1186.14
0.9238	1023.59
0.9623	970.42

Sources

Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6