Mixture of p-Xylene + 2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-

Datasets

1. Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of p-Xylene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
350.15	0.0000	0.04
357.15	0.0000	0.06
364.15	0.0000	0.10
371.15	0.0000	0.15
378.15	0.0000	0.22
368.15	0.1006	5.24
376.15	0.1006	6.86
384.15	0.1006	8.32
393.15	0.1006	10.24
402.15	0.1006	13.24
351.15	0.3009	7.88
357.15	0.3009	9.53
363.15	0.3009	11.28
370.15	0.3009	14.00
377.15	0.3009	17.23
345.15	0.5008	8.67
350.15	0.5008	10.39
355.15	0.5008	12.19
360.15	0.5008	14.49
365.15	0.5008	17.22
345.15	0.7004	9.96
350.15	0.7004	12.08
355.15	0.7004	14.88
360.15	0.7004	17.55
365.15	0.7004	20.69
344.15	0.9000	10.40
349.15	0.9000	12.92
354.15	0.9000	15.34
359.15	0.9000	18.18
364.15	0.9000	21.87
345.15	1.0000	11.39
350.15	1.0000	13.90
355.15	1.0000	16.85
360.15	1.0000	20.30
365.15	1.0000	24.30

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of p-Xylene (1) - Gas	Vapor or sublimation pressure, kPa - Gas
350.15	0.0000	0.04
357.15	0.0000	0.06
364.15	0.0000	0.10
371.15	0.0000	0.15
378.15	0.0000	0.22
368.15	0.1006	5.24
376.15	0.1006	6.86
384.15	0.1006	8.32
393.15	0.1006	10.24
402.15	0.1006	13.24
351.15	0.3009	7.88
357.15	0.3009	9.53
363.15	0.3009	11.28
370.15	0.3009	14.00
377.15	0.3009	17.23
345.15	0.5008	8.67
350.15	0.5008	10.39
355.15	0.5008	12.19
360.15	0.5008	14.49
365.15	0.5008	17.22
345.15	0.7004	9.96
350.15	0.7004	12.08
355.15	0.7004	14.88
360.15	0.7004	17.55
365.15	0.7004	20.69
344.15	0.9000	10.40
349.15	0.9000	12.92
354.15	0.9000	15.34
359.15	0.9000	18.18
364.15	0.9000	21.87
345.15	1.0000	11.39
350.15	1.0000	13.90
355.15	1.0000	16.85
360.15	1.0000	20.30
365.15	1.0000	24.30

Sources

• Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression