Mixture of 2-Propanol, 2-methyl- + 1-Pentene, 2,4,4-trimethyl-

Datasets

1. Azeotropic composition: mole fraction (4)
2. P_vap - Vapor or sublimation pressure, kPa (2)
3. Azeotropic pressure, kPa (2)

Azeotropic composition: mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Temperature, K - Gas	Azeotropic composition: mole fraction of 2-Propanol, 2-methyl- (1) - Liquid
313.16	0.5250
333.14	0.6300
353.18	0.7600

Mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Gas
0.0000	313.16	0.0000
0.0000	333.14	0.0000
0.0000	353.18	0.0000
0.0728	333.14	0.3470
0.0728	353.18	0.3160
0.0731	313.16	0.3020
0.1576	353.18	0.4330
0.1606	333.14	0.4470
0.1633	313.16	0.3760
0.2583	353.18	0.5010
0.2588	313.16	0.4220
0.2606	333.14	0.4940
0.3349	353.18	0.5460
0.3408	333.14	0.5210
0.3435	313.16	0.4560
0.4042	333.14	0.5120
0.4050	353.18	0.5780
0.4059	313.16	0.4750
0.4620	353.18	0.6010
0.4627	313.16	0.4960
0.4639	333.14	0.5810
0.5191	333.14	0.5850
0.5225	353.18	0.6390
0.5250	313.16	0.5240
0.5253	313.16	0.5230
0.6176	313.16	0.5500
0.6215	333.14	0.6230
0.6264	353.18	0.6750
0.6300	333.14	0.6280
0.6911	333.14	0.6570
0.6981	313.16	0.5970
0.6993	353.18	0.7140
0.7340	353.18	0.7340
0.7591	333.14	0.6890
0.7645	313.16	0.6330
0.7648	353.18	0.7530
0.7999	333.14	0.7220
0.8000	353.18	0.7770
0.8017	313.16	0.6640
0.8399	353.18	0.7990
0.8406	333.14	0.7590
0.8451	313.16	0.7090
0.8810	353.18	0.8130
0.8815	333.14	0.7990
0.8861	313.16	0.7550
1.0000	313.16	1.0000
1.0000	333.14	1.0000
1.0000	353.18	1.0000

Azeotropic composition: mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Temperature, K - Gas	Azeotropic composition: mole fraction of 2-Propanol, 2-methyl- (1) - Liquid
313.16	0.5250
333.14	0.6300
353.18	0.7600

Mole fraction of 2-Propanol, 2-methyl- (1) [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Mole fraction of 2-Propanol, 2-methyl- (1) - Gas
0.0000	313.16	0.0000
0.0000	333.14	0.0000
0.0000	353.18	0.0000
0.0728	333.14	0.3470
0.0728	353.18	0.3160
0.0731	313.16	0.3020
0.1576	353.18	0.4330
0.1606	333.14	0.4470
0.1633	313.16	0.3760
0.2583	353.18	0.5010
0.2588	313.16	0.4220
0.2606	333.14	0.4940
0.3349	353.18	0.5460
0.3408	333.14	0.5210
0.3435	313.16	0.4560
0.4042	333.14	0.5120
0.4050	353.18	0.5780
0.4059	313.16	0.4750
0.4620	353.18	0.6010
0.4627	313.16	0.4960
0.4639	333.14	0.5810
0.5191	333.14	0.5850
0.5225	353.18	0.6390
0.5250	313.16	0.5240
0.5253	313.16	0.5230
0.6176	313.16	0.5500
0.6215	333.14	0.6230
0.6264	353.18	0.6750
0.6300	333.14	0.6280
0.6911	333.14	0.6570
0.6981	313.16	0.5970
0.6993	353.18	0.7140
0.7340	353.18	0.7340
0.7591	333.14	0.6890
0.7645	313.16	0.6330
0.7648	353.18	0.7530
0.7999	333.14	0.7220
0.8000	353.18	0.7770
0.8017	313.16	0.6640
0.8399	353.18	0.7990
0.8406	333.14	0.7590
0.8451	313.16	0.7090
0.8810	353.18	0.8130
0.8815	333.14	0.7990
0.8861	313.16	0.7550
1.0000	313.16	1.0000
1.0000	333.14	1.0000
1.0000	353.18	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	313.16	11.78
0.0000	333.14	26.37
0.0000	353.18	53.00
0.0728	333.14	36.20
0.0728	353.18	72.36
0.0731	313.16	15.83
0.1576	353.18	82.85
0.1606	333.14	40.18
0.1633	313.16	17.14
0.2583	353.18	89.39
0.2588	313.16	17.70
0.2606	333.14	42.50
0.3349	353.18	92.67
0.3408	333.14	43.60
0.3435	313.16	18.02
0.4042	333.14	44.28
0.4050	353.18	95.06
0.4059	313.16	18.19
0.4620	353.18	96.66
0.4627	313.16	18.25
0.4639	333.14	44.78
0.5191	333.14	45.07
0.5225	353.18	98.04
0.5250	313.16	18.27
0.5253	313.16	18.27
0.6176	313.16	18.18
0.6215	333.14	45.38
0.6264	353.18	99.67
0.6300	333.14	45.38
0.6911	333.14	45.34
0.6981	313.16	17.93
0.6993	353.18	100.24
0.7340	353.18	100.30
0.7591	333.14	44.87
0.7645	313.16	17.58
0.7648	353.18	100.24
0.7999	333.14	44.40
0.8000	353.18	99.98
0.8017	313.16	17.27
0.8399	353.18	99.47
0.8406	333.14	43.76
0.8451	313.16	16.80
0.8810	353.18	98.58
0.8815	333.14	42.85
0.8861	313.16	16.20
1.0000	313.16	13.72
1.0000	333.14	38.57
1.0000	353.18	92.54

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	313.16	11.78
0.0000	333.14	26.37
0.0000	353.18	53.00
0.0728	333.14	36.20
0.0728	353.18	72.36
0.0731	313.16	15.83
0.1576	353.18	82.85
0.1606	333.14	40.18
0.1633	313.16	17.14
0.2583	353.18	89.39
0.2588	313.16	17.70
0.2606	333.14	42.50
0.3349	353.18	92.67
0.3408	333.14	43.60
0.3435	313.16	18.02
0.4042	333.14	44.28
0.4050	353.18	95.06
0.4059	313.16	18.19
0.4620	353.18	96.66
0.4627	313.16	18.25
0.4639	333.14	44.78
0.5191	333.14	45.07
0.5225	353.18	98.04
0.5250	313.16	18.27
0.5253	313.16	18.27
0.6176	313.16	18.18
0.6215	333.14	45.38
0.6264	353.18	99.67
0.6300	333.14	45.38
0.6911	333.14	45.34
0.6981	313.16	17.93
0.6993	353.18	100.24
0.7340	353.18	100.30
0.7591	333.14	44.87
0.7645	313.16	17.58
0.7648	353.18	100.24
0.7999	333.14	44.40
0.8000	353.18	99.98
0.8017	313.16	17.27
0.8399	353.18	99.47
0.8406	333.14	43.76
0.8451	313.16	16.80
0.8810	353.18	98.58
0.8815	333.14	42.85
0.8861	313.16	16.20
1.0000	313.16	13.72
1.0000	333.14	38.57
1.0000	353.18	92.54

Azeotropic pressure, kPa [ref]

Temperature, K - Gas	Azeotropic pressure, kPa - Liquid
313.16	18.27
333.14	45.38
353.18	100.31

Azeotropic pressure, kPa [ref]

Temperature, K - Gas	Azeotropic pressure, kPa - Liquid
313.16	18.27
333.14	45.38
353.18	100.31

Sources

• Vapor-Liquid Equilibrium for Benzaldehyde with 1-Methylethylbenzene and for 2-Methyl-propan-2-ol with 2,4,4-Trimethyl-1-pentene