Mixture of Phenol, 2-methoxy- + Benzene, 1,2-dimethoxy-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Phenol, 2-methoxy- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Gas
413.50	0.0000	0.0000
413.50	0.1020	0.1170
413.50	0.1990	0.2170
413.50	0.3020	0.3310
413.50	0.4020	0.4330
413.50	0.4960	0.5190
413.50	0.6040	0.6250
413.50	0.7040	0.7260
413.50	0.8190	0.8290
413.50	0.9140	0.9210
413.50	1.0000	1.0000
428.15	0.0000	0.0000
428.15	0.1040	0.1150
428.15	0.2020	0.2150
428.15	0.3000	0.3250
428.15	0.4050	0.4260
428.15	0.4900	0.5190
428.15	0.6060	0.6300
428.15	0.7030	0.7160
428.15	0.8240	0.8370
428.15	0.9160	0.9210
428.15	1.0000	1.0000
443.15	0.0000	0.0000
443.15	0.1030	0.1150
443.15	0.2040	0.2180
443.15	0.2980	0.3210
443.15	0.4070	0.4230
443.15	0.4890	0.5120
443.15	0.6050	0.6180
443.15	0.7060	0.7220
443.15	0.8250	0.8310
443.15	0.9140	0.9180
443.15	1.0000	1.0000

Mole fraction of Phenol, 2-methoxy- (1) [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Gas
413.50	0.0000	0.0000
413.50	0.1020	0.1170
413.50	0.1990	0.2170
413.50	0.3020	0.3310
413.50	0.4020	0.4330
413.50	0.4960	0.5190
413.50	0.6040	0.6250
413.50	0.7040	0.7260
413.50	0.8190	0.8290
413.50	0.9140	0.9210
413.50	1.0000	1.0000
428.15	0.0000	0.0000
428.15	0.1040	0.1150
428.15	0.2020	0.2150
428.15	0.3000	0.3250
428.15	0.4050	0.4260
428.15	0.4900	0.5190
428.15	0.6060	0.6300
428.15	0.7030	0.7160
428.15	0.8240	0.8370
428.15	0.9160	0.9210
428.15	1.0000	1.0000
443.15	0.0000	0.0000
443.15	0.1030	0.1150
443.15	0.2040	0.2180
443.15	0.2980	0.3210
443.15	0.4070	0.4230
443.15	0.4890	0.5120
443.15	0.6050	0.6180
443.15	0.7060	0.7220
443.15	0.8250	0.8310
443.15	0.9140	0.9180
443.15	1.0000	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
413.15	0.0000	13.70
413.15	0.1020	13.90
413.15	0.1990	14.10
413.15	0.3020	14.30
413.15	0.4020	14.50
413.15	0.4960	14.60
413.15	0.6040	14.70
413.15	0.7040	14.90
413.15	0.8190	15.00
413.15	0.9140	15.10
413.15	1.0000	15.20
428.15	0.0000	23.10
428.15	0.1040	23.30
428.15	0.2020	23.70
428.15	0.3000	23.80
428.15	0.4050	24.10
428.15	0.4900	24.40
428.15	0.6060	24.60
428.15	0.7030	24.70
428.15	0.8240	24.90
428.15	0.9160	25.20
428.15	1.0000	25.30
443.15	0.0000	37.20
443.15	0.1030	37.80
443.15	0.2040	38.00
443.15	0.2980	38.50
443.15	0.4070	38.80
443.15	0.4890	39.20
443.15	0.6050	39.50
443.15	0.7060	39.70
443.15	0.8250	39.90
443.15	0.9140	40.10
443.15	1.0000	40.30

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Phenol, 2-methoxy- (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
413.15	0.0000	13.70
413.15	0.1020	13.90
413.15	0.1990	14.10
413.15	0.3020	14.30
413.15	0.4020	14.50
413.15	0.4960	14.60
413.15	0.6040	14.70
413.15	0.7040	14.90
413.15	0.8190	15.00
413.15	0.9140	15.10
413.15	1.0000	15.20
428.15	0.0000	23.10
428.15	0.1040	23.30
428.15	0.2020	23.70
428.15	0.3000	23.80
428.15	0.4050	24.10
428.15	0.4900	24.40
428.15	0.6060	24.60
428.15	0.7030	24.70
428.15	0.8240	24.90
428.15	0.9160	25.20
428.15	1.0000	25.30
443.15	0.0000	37.20
443.15	0.1030	37.80
443.15	0.2040	38.00
443.15	0.2980	38.50
443.15	0.4070	38.80
443.15	0.4890	39.20
443.15	0.6050	39.50
443.15	0.7060	39.70
443.15	0.8250	39.90
443.15	0.9140	40.10
443.15	1.0000	40.30

Sources

• Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine