Mixture of 1-Hexene + Tetrahydrofuran

Datasets

1. Excess molar enthalpy (molar enthalpy (2)
2. P [kPa] x T [K] x x1[mol/mol] (5)

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

Operational conditions:

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

Mole fraction of 1-Hexene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.0675
0.0970	0.1271
0.1507	0.1865
0.1994	0.2300
0.2501	0.2716
0.3003	0.3049
0.3499	0.3298
0.3999	0.3490
0.4500	0.3593
0.4977	0.3665
0.5494	0.3636
0.6006	0.3533
0.6490	0.3378
0.6905	0.3182
0.7499	0.2823
0.7999	0.2454
0.8501	0.1972
0.8995	0.1401
0.9500	0.0755

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

Operational conditions:

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

Mole fraction of 1-Hexene (1) - Liquid	Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0501	0.0675
0.0970	0.1271
0.1507	0.1865
0.1994	0.2300
0.2501	0.2716
0.3003	0.3049
0.3499	0.3298
0.3999	0.3490
0.4500	0.3593
0.4977	0.3665
0.5494	0.3636
0.6006	0.3533
0.6490	0.3378
0.6905	0.3182
0.7499	0.2823
0.7999	0.2454
0.8501	0.1972
0.8995	0.1401
0.9500	0.0755

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid
4.002	263.55	0.0993
6.99	273.51	0.0993
11.488	283.28	0.0993
18.429	293.27	0.0993
28.382	303.22	0.0993
42.531	313.29	0.0993
61.624	323.3	0.0993
86.981	333.33	0.0993

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid
4.27	263.52	0.2140
7.385	273.44	0.2140
12.175	283.36	0.2140
19.374	293.26	0.2140
29.742	303.25	0.2140
44.274	313.23	0.2140
63.987	323.21	0.2140
90.283	333.24	0.2140

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid
4.405	263.51	0.3003
7.582	273.37	0.3003
12.482	283.29	0.3003
19.87	293.26	0.3003
30.473	303.25	0.3003
45.238	313.22	0.3003
65.271	323.2	0.3003
91.866	333.22	0.3003

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid
3.712	263.55	0.0000
6.471	273.38	0.0000
10.779	283.29	0.0000
17.371	293.26	0.0000
26.899	303.25	0.0000
40.358	313.23	0.0000
58.719	323.21	0.0000
83.325	333.23	0.0000

P [kPa] x T [K] x x1[mol/mol] [ref]

Fixed	Measured
P [kPa] - VLE	T [K] - VLE	x1[mol/mol] of 1-Hexene (1) - Liquid
4.542	263.45	1.0000
7.774	273.32	1.0000
12.78	283.24	1.0000
20.138	293.22	1.0000
30.632	303.22	1.0000
45.04	313.2	1.0000
64.421	323.19	1.0000
89.73	333.23	1.0000

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Excess molar enthalpies of the ternary mixtures (1-hexene + tetrahydrofuran or 2-methyltetrahydrofuran + methyl tert-butyl ether) at the temperature 298.15K.