Mixture of n-Hexane + Ethanol, 2-(1-methylethoxy)-

Datasets

1. Mole fraction (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Gas	Pressure, kPa - Liquid	Mole fraction of n-Hexane (1) - Liquid
0.0000	60.00	0.0000
0.0000	80.00	0.0000
0.0000	100.00	0.0000
0.0940	100.00	0.0110
0.1630	60.00	0.0180
0.2760	100.00	0.0310
0.3360	80.00	0.0410
0.4150	60.00	0.0490
0.4520	100.00	0.0610
0.4960	80.00	0.0690
0.5110	100.00	0.0740
0.5470	100.00	0.0830
0.6130	60.00	0.0930
0.6580	100.00	0.1210
0.7510	80.00	0.1430
0.7740	60.00	0.1580
0.8100	100.00	0.2060
0.8210	80.00	0.1950
0.9030	80.00	0.3250
0.9030	100.00	0.3100
0.9180	60.00	0.3180
0.9290	100.00	0.4290
0.9510	80.00	0.5290
0.9580	60.00	0.4540
0.9610	100.00	0.6170
0.9720	100.00	0.7390
0.9770	60.00	0.6210
0.9780	80.00	0.7220
0.9840	80.00	0.8910
0.9850	100.00	0.8640
0.9890	60.00	0.8200
1.0000	60.00	1.0000
1.0000	80.00	1.0000
1.0000	100.00	1.0000

Mole fraction of n-Hexane (1) [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Gas	Pressure, kPa - Liquid	Mole fraction of n-Hexane (1) - Liquid
0.0000	60.00	0.0000
0.0000	80.00	0.0000
0.0000	100.00	0.0000
0.0940	100.00	0.0110
0.1630	60.00	0.0180
0.2760	100.00	0.0310
0.3360	80.00	0.0410
0.4150	60.00	0.0490
0.4520	100.00	0.0610
0.4960	80.00	0.0690
0.5110	100.00	0.0740
0.5470	100.00	0.0830
0.6130	60.00	0.0930
0.6580	100.00	0.1210
0.7510	80.00	0.1430
0.7740	60.00	0.1580
0.8100	100.00	0.2060
0.8210	80.00	0.1950
0.9030	80.00	0.3250
0.9030	100.00	0.3100
0.9180	60.00	0.3180
0.9290	100.00	0.4290
0.9510	80.00	0.5290
0.9580	60.00	0.4540
0.9610	100.00	0.6170
0.9720	100.00	0.7390
0.9770	60.00	0.6210
0.9780	80.00	0.7220
0.9840	80.00	0.8910
0.9850	100.00	0.8640
0.9890	60.00	0.8200
1.0000	60.00	1.0000
1.0000	80.00	1.0000
1.0000	100.00	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Gas	Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
0.0000	60.00	398.12
0.0000	80.00	407.13
0.0000	100.00	414.21
0.0940	100.00	411.51
0.1630	60.00	393.52
0.2760	100.00	405.08
0.3360	80.00	395.70
0.4150	60.00	384.55
0.4520	100.00	396.61
0.4960	80.00	378.76
0.5110	100.00	393.65
0.5470	100.00	391.60
0.6130	60.00	373.41
0.6580	100.00	383.76
0.7510	80.00	371.16
0.7740	60.00	361.22
0.8100	100.00	370.08
0.8210	80.00	364.26
0.9030	80.00	350.85
0.9030	100.00	358.91
0.9180	60.00	344.22
0.9290	100.00	350.63
0.9510	80.00	340.06
0.9580	60.00	335.15
0.9610	100.00	344.34
0.9720	100.00	342.91
0.9770	60.00	329.01
0.9780	80.00	336.21
0.9840	80.00	335.72
0.9850	100.00	342.11
0.9890	60.00	327.48
1.0000	60.00	326.11
1.0000	80.00	334.61
1.0000	100.00	341.48

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of n-Hexane (1) - Gas	Pressure, kPa - Gas	Boiling temperature at pressure P, K - Gas
0.0000	60.00	398.12
0.0000	80.00	407.13
0.0000	100.00	414.21
0.0940	100.00	411.51
0.1630	60.00	393.52
0.2760	100.00	405.08
0.3360	80.00	395.70
0.4150	60.00	384.55
0.4520	100.00	396.61
0.4960	80.00	378.76
0.5110	100.00	393.65
0.5470	100.00	391.60
0.6130	60.00	373.41
0.6580	100.00	383.76
0.7510	80.00	371.16
0.7740	60.00	361.22
0.8100	100.00	370.08
0.8210	80.00	364.26
0.9030	80.00	350.85
0.9030	100.00	358.91
0.9180	60.00	344.22
0.9290	100.00	350.63
0.9510	80.00	340.06
0.9580	60.00	335.15
0.9610	100.00	344.34
0.9720	100.00	342.91
0.9770	60.00	329.01
0.9780	80.00	336.21
0.9840	80.00	335.72
0.9850	100.00	342.11
0.9890	60.00	327.48
1.0000	60.00	326.11
1.0000	80.00	334.61
1.0000	100.00	341.48

Sources

• Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems