Mixture of Isobutyl acetate + Ethyl Acetate

Datasets

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

Mole fraction of Ethyl Acetate (2) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	50.00	0.0000
0.0610	50.00	0.1920
0.2560	50.00	0.5580
0.3740	50.00	0.6980
0.4590	50.00	0.7730
0.5260	50.00	0.8150
0.6040	50.00	0.8640
0.6300	50.00	0.8730
0.7120	50.00	0.9130
0.8330	50.00	0.9550
0.9490	50.00	0.9870
1.0000	50.00	1.0000
0.0000	100.00	0.0000
0.0580	100.00	0.1700
0.1520	100.00	0.3740
0.2600	100.00	0.5420
0.3790	100.00	0.6810
0.4650	100.00	0.7570
0.5490	100.00	0.8210
0.6060	100.00	0.8530
0.6370	100.00	0.8660
0.7080	100.00	0.9040
0.8290	100.00	0.9500
0.9410	100.00	0.9850
1.0000	100.00	1.0000
0.0000	150.00	0.0000
0.0530	150.00	0.1490
0.1480	150.00	0.3540
0.3120	150.00	0.6030
0.4610	150.00	0.7430
0.5540	150.00	0.8080
0.5990	150.00	0.8380
0.6310	150.00	0.8540
0.7000	150.00	0.8920
0.8170	150.00	0.9430
0.9290	150.00	0.9800
1.0000	150.00	1.0000

Mole fraction of Ethyl Acetate (2) [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Ethyl Acetate (2) - Gas
0.0000	50.00	0.0000
0.0610	50.00	0.1920
0.2560	50.00	0.5580
0.3740	50.00	0.6980
0.4590	50.00	0.7730
0.5260	50.00	0.8150
0.6040	50.00	0.8640
0.6300	50.00	0.8730
0.7120	50.00	0.9130
0.8330	50.00	0.9550
0.9490	50.00	0.9870
1.0000	50.00	1.0000
0.0000	100.00	0.0000
0.0580	100.00	0.1700
0.1520	100.00	0.3740
0.2600	100.00	0.5420
0.3790	100.00	0.6810
0.4650	100.00	0.7570
0.5490	100.00	0.8210
0.6060	100.00	0.8530
0.6370	100.00	0.8660
0.7080	100.00	0.9040
0.8290	100.00	0.9500
0.9410	100.00	0.9850
1.0000	100.00	1.0000
0.0000	150.00	0.0000
0.0530	150.00	0.1490
0.1480	150.00	0.3540
0.3120	150.00	0.6030
0.4610	150.00	0.7430
0.5540	150.00	0.8080
0.5990	150.00	0.8380
0.6310	150.00	0.8540
0.7000	150.00	0.8920
0.8170	150.00	0.9430
0.9290	150.00	0.9800
1.0000	150.00	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	50.00	367.51
0.0610	50.00	363.08
0.2560	50.00	351.87
0.3740	50.00	346.72
0.4590	50.00	343.46
0.5260	50.00	341.49
0.6040	50.00	338.84
0.6300	50.00	338.22
0.7120	50.00	336.20
0.8330	50.00	333.44
0.9490	50.00	331.06
1.0000	50.00	330.41
0.0000	100.00	389.37
0.0580	100.00	384.96
0.1520	100.00	378.93
0.2600	100.00	372.80
0.3790	100.00	367.40
0.4650	100.00	364.03
0.5490	100.00	360.78
0.6060	100.00	359.32
0.6370	100.00	358.28
0.7080	100.00	356.36
0.8290	100.00	353.11
0.9410	100.00	350.69
1.0000	100.00	349.70
0.0000	150.00	403.64
0.0530	150.00	399.57
0.1480	150.00	393.26
0.3120	150.00	383.99
0.4610	150.00	377.44
0.5540	150.00	374.17
0.5990	150.00	372.52
0.6310	150.00	371.75
0.7000	150.00	369.77
0.8170	150.00	366.19
0.9290	150.00	363.89
1.0000	150.00	362.48

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Ethyl Acetate (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	50.00	367.51
0.0610	50.00	363.08
0.2560	50.00	351.87
0.3740	50.00	346.72
0.4590	50.00	343.46
0.5260	50.00	341.49
0.6040	50.00	338.84
0.6300	50.00	338.22
0.7120	50.00	336.20
0.8330	50.00	333.44
0.9490	50.00	331.06
1.0000	50.00	330.41
0.0000	100.00	389.37
0.0580	100.00	384.96
0.1520	100.00	378.93
0.2600	100.00	372.80
0.3790	100.00	367.40
0.4650	100.00	364.03
0.5490	100.00	360.78
0.6060	100.00	359.32
0.6370	100.00	358.28
0.7080	100.00	356.36
0.8290	100.00	353.11
0.9410	100.00	350.69
1.0000	100.00	349.70
0.0000	150.00	403.64
0.0530	150.00	399.57
0.1480	150.00	393.26
0.3120	150.00	383.99
0.4610	150.00	377.44
0.5540	150.00	374.17
0.5990	150.00	372.52
0.6310	150.00	371.75
0.7000	150.00	369.77
0.8170	150.00	366.19
0.9290	150.00	363.89
1.0000	150.00	362.48

Sources

• Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil