Mixture of Hexane, 1,6-dibromo- + Ethyl Acetate

Name: Hexane, 1,6-dibromo-
InChI: InChI=1S/C6H12Br2/c7-5-3-1-2-4-6-8/h1-6H2
InChI Key: SGRHVVLXEBNBDV-UHFFFAOYSA-N
Formula: C6H12Br2
SMILES: BrCCCCCCBr
Mol. Weight (g/mol): 243.97
CAS: 629-03-8

Name: Ethyl Acetate
InChI: InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
InChI Key: XEKOWRVHYACXOJ-UHFFFAOYSA-N
Formula: C4H8O2
SMILES: CCOC(C)=O
Mol. Weight (g/mol): 88.11
CAS: 141-78-6

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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 Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0852	0.1350
0.1790	0.2159
0.2657	0.2693
0.3506	0.3091
0.4238	0.3309
0.4890	0.3372
0.5186	0.3340
0.5344	0.3315
0.5598	0.3265
0.6031	0.3075
0.6495	0.2831
0.7011	0.2543
0.7507	0.2184
0.8025	0.1802
0.8542	0.1380
0.9062	0.0925
0.9578	0.0443

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 Acetate (2) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0852	0.1350
0.1790	0.2159
0.2657	0.2693
0.3506	0.3091
0.4238	0.3309
0.4890	0.3372
0.5186	0.3340
0.5344	0.3315
0.5598	0.3265
0.6031	0.3075
0.6495	0.2831
0.7011	0.2543
0.7507	0.2184
0.8025	0.1802
0.8542	0.1380
0.9062	0.0925
0.9578	0.0443

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1101	1558.02
0.2056	1515.22
0.2841	1476.78
0.3679	1432.01
0.4348	1393.28
0.5035	1350.27
0.6230	1266.72
0.7330	1177.88
0.8165	1101.03
0.8582	1059.17
0.8988	1015.65
0.9703	932.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Ethyl Acetate (2) - Liquid	Mass density, kg/m3 - Liquid
0.1101	1558.02
0.2056	1515.22
0.2841	1476.78
0.3679	1432.01
0.4348	1393.28
0.5035	1350.27
0.6230	1266.72
0.7330	1177.88
0.8165	1101.03
0.8582	1059.17
0.8988	1015.65
0.9703	932.2

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