Mixture of Toluene + Isopropyl Alcohol

Datasets

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

Mole fraction of Isopropyl Alcohol (2) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Isopropyl Alcohol (2) - Gas
0.0000	101.30	0.0000
0.0000	121.30	0.0000
0.0000	161.30	0.0000
0.0000	201.30	0.0000
0.0566	201.30	0.3166
0.0598	161.30	0.3491
0.0650	121.30	0.3689
0.0745	101.30	0.3947
0.1054	201.30	0.4846
0.1129	161.30	0.4771
0.1197	121.30	0.5051
0.1265	101.30	0.5052
0.1945	201.30	0.5772
0.2061	161.30	0.5800
0.2142	121.30	0.5855
0.2172	101.30	0.5794
0.2741	201.30	0.6193
0.2987	121.30	0.6196
0.2987	161.30	0.6296
0.3061	101.30	0.6443
0.3696	201.30	0.6921
0.3790	161.30	0.6922
0.3802	121.30	0.6786
0.3925	101.30	0.6516
0.4940	201.30	0.7258
0.4948	161.30	0.7215
0.5042	121.30	0.7002
0.5085	101.30	0.6878
0.5943	161.30	0.7382
0.5943	201.30	0.7415
0.5958	101.30	0.7206
0.5974	121.30	0.7217
0.6522	201.30	0.7551
0.6545	161.30	0.7513
0.6553	121.30	0.7502
0.6581	101.30	0.7338
0.7155	101.30	0.7669
0.7285	201.30	0.7844
0.7306	161.30	0.7830
0.7313	121.30	0.7686
0.8025	201.30	0.8306
0.8037	121.30	0.8162
0.8038	101.30	0.8095
0.8113	161.30	0.8197
0.8200	201.30	0.8391
0.8222	161.30	0.8336
0.8225	101.30	0.8232
0.8248	121.30	0.8262
0.8356	101.30	0.8330
0.8356	121.30	0.8378
0.8385	161.30	0.8442
0.8472	201.30	0.8601
0.8476	161.30	0.8549
0.8484	101.30	0.8423
0.8517	121.30	0.8483
0.8752	201.30	0.8798
0.8757	121.30	0.8680
0.8757	161.30	0.8739
0.8761	101.30	0.8641
0.9059	201.30	0.9047
0.9367	101.30	0.9220
0.9372	161.30	0.9296
0.9373	121.30	0.9273
0.9378	201.30	0.9325
1.0000	101.30	1.0000
1.0000	121.30	1.0000
1.0000	161.30	1.0000
1.0000	201.30	1.0000

Mole fraction of Isopropyl Alcohol (2) [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of Isopropyl Alcohol (2) - Gas
0.0000	101.30	0.0000
0.0000	121.30	0.0000
0.0000	161.30	0.0000
0.0000	201.30	0.0000
0.0566	201.30	0.3166
0.0598	161.30	0.3491
0.0650	121.30	0.3689
0.0745	101.30	0.3947
0.1054	201.30	0.4846
0.1129	161.30	0.4771
0.1197	121.30	0.5051
0.1265	101.30	0.5052
0.1945	201.30	0.5772
0.2061	161.30	0.5800
0.2142	121.30	0.5855
0.2172	101.30	0.5794
0.2741	201.30	0.6193
0.2987	121.30	0.6196
0.2987	161.30	0.6296
0.3061	101.30	0.6443
0.3696	201.30	0.6921
0.3790	161.30	0.6922
0.3802	121.30	0.6786
0.3925	101.30	0.6516
0.4940	201.30	0.7258
0.4948	161.30	0.7215
0.5042	121.30	0.7002
0.5085	101.30	0.6878
0.5943	161.30	0.7382
0.5943	201.30	0.7415
0.5958	101.30	0.7206
0.5974	121.30	0.7217
0.6522	201.30	0.7551
0.6545	161.30	0.7513
0.6553	121.30	0.7502
0.6581	101.30	0.7338
0.7155	101.30	0.7669
0.7285	201.30	0.7844
0.7306	161.30	0.7830
0.7313	121.30	0.7686
0.8025	201.30	0.8306
0.8037	121.30	0.8162
0.8038	101.30	0.8095
0.8113	161.30	0.8197
0.8200	201.30	0.8391
0.8222	161.30	0.8336
0.8225	101.30	0.8232
0.8248	121.30	0.8262
0.8356	101.30	0.8330
0.8356	121.30	0.8378
0.8385	161.30	0.8442
0.8472	201.30	0.8601
0.8476	161.30	0.8549
0.8484	101.30	0.8423
0.8517	121.30	0.8483
0.8752	201.30	0.8798
0.8757	121.30	0.8680
0.8757	161.30	0.8739
0.8761	101.30	0.8641
0.9059	201.30	0.9047
0.9367	101.30	0.9220
0.9372	161.30	0.9296
0.9373	121.30	0.9273
0.9378	201.30	0.9325
1.0000	101.30	1.0000
1.0000	121.30	1.0000
1.0000	161.30	1.0000
1.0000	201.30	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.55
0.0000	121.30	390.25
0.0000	161.30	400.75
0.0000	201.30	409.65
0.0566	201.30	396.55
0.0598	161.30	387.65
0.0650	121.30	376.65
0.0745	101.30	369.15
0.1054	201.30	389.05
0.1129	161.30	381.25
0.1197	121.30	370.35
0.1265	101.30	364.55
0.1945	201.30	383.35
0.2061	161.30	376.05
0.2142	121.30	365.95
0.2172	101.30	360.35
0.2741	201.30	380.85
0.2987	121.30	364.05
0.2987	161.30	373.45
0.3061	101.30	358.25
0.3696	201.30	377.75
0.3790	161.30	371.35
0.3802	121.30	362.35
0.3925	101.30	357.25
0.4940	201.30	376.45
0.4948	161.30	370.15
0.5042	121.30	361.35
0.5085	101.30	356.25
0.5943	161.30	369.45
0.5943	201.30	375.25
0.5958	101.30	355.15
0.5974	121.30	360.35
0.6522	201.30	374.55
0.6545	161.30	369.05
0.6553	121.30	360.25
0.6581	101.30	355.05
0.7155	101.30	354.65
0.7285	201.30	374.15
0.7306	161.30	367.45
0.7313	121.30	359.85
0.8025	201.30	373.35
0.8037	121.30	359.45
0.8038	101.30	354.35
0.8113	161.30	367.35
0.8200	201.30	373.25
0.8222	161.30	367.25
0.8225	101.30	354.15
0.8248	121.30	359.35
0.8356	101.30	354.15
0.8356	121.30	359.15
0.8385	161.30	366.85
0.8472	201.30	373.05
0.8476	161.30	366.75
0.8484	101.30	354.25
0.8517	121.30	359.05
0.8752	201.30	372.95
0.8757	121.30	359.15
0.8757	161.30	366.65
0.8761	101.30	354.45
0.9059	201.30	372.95
0.9367	101.30	354.55
0.9372	161.30	366.85
0.9373	121.30	359.55
0.9378	201.30	373.15
1.0000	101.30	355.35
1.0000	121.30	359.95
1.0000	161.30	367.65
1.0000	201.30	373.65

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Isopropyl Alcohol (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	101.30	383.55
0.0000	121.30	390.25
0.0000	161.30	400.75
0.0000	201.30	409.65
0.0566	201.30	396.55
0.0598	161.30	387.65
0.0650	121.30	376.65
0.0745	101.30	369.15
0.1054	201.30	389.05
0.1129	161.30	381.25
0.1197	121.30	370.35
0.1265	101.30	364.55
0.1945	201.30	383.35
0.2061	161.30	376.05
0.2142	121.30	365.95
0.2172	101.30	360.35
0.2741	201.30	380.85
0.2987	121.30	364.05
0.2987	161.30	373.45
0.3061	101.30	358.25
0.3696	201.30	377.75
0.3790	161.30	371.35
0.3802	121.30	362.35
0.3925	101.30	357.25
0.4940	201.30	376.45
0.4948	161.30	370.15
0.5042	121.30	361.35
0.5085	101.30	356.25
0.5943	161.30	369.45
0.5943	201.30	375.25
0.5958	101.30	355.15
0.5974	121.30	360.35
0.6522	201.30	374.55
0.6545	161.30	369.05
0.6553	121.30	360.25
0.6581	101.30	355.05
0.7155	101.30	354.65
0.7285	201.30	374.15
0.7306	161.30	367.45
0.7313	121.30	359.85
0.8025	201.30	373.35
0.8037	121.30	359.45
0.8038	101.30	354.35
0.8113	161.30	367.35
0.8200	201.30	373.25
0.8222	161.30	367.25
0.8225	101.30	354.15
0.8248	121.30	359.35
0.8356	101.30	354.15
0.8356	121.30	359.15
0.8385	161.30	366.85
0.8472	201.30	373.05
0.8476	161.30	366.75
0.8484	101.30	354.25
0.8517	121.30	359.05
0.8752	201.30	372.95
0.8757	121.30	359.15
0.8757	161.30	366.65
0.8761	101.30	354.45
0.9059	201.30	372.95
0.9367	101.30	354.55
0.9372	161.30	366.85
0.9373	121.30	359.55
0.9378	201.30	373.15
1.0000	101.30	355.35
1.0000	121.30	359.95
1.0000	161.30	367.65
1.0000	201.30	373.65

Sources

• Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa