Mixture of 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol + o-Xylene

Datasets

1. Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of o-Xylene (2) - 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
384.15	0.1003	7.65
392.15	0.1003	9.47
400.15	0.1003	11.44
408.15	0.1003	14.53
416.15	0.1003	17.86
360.15	0.2995	9.38
366.15	0.2995	10.99
372.15	0.2995	13.43
378.15	0.2995	15.59
384.15	0.2995	19.59
341.15	0.5211	6.40
348.15	0.5211	8.31
355.15	0.5211	10.72
362.15	0.5211	13.78
369.15	0.5211	17.70
346.15	0.7007	8.26
352.15	0.7007	10.40
358.15	0.7007	13.05
364.15	0.7007	16.20
370.15	0.7007	19.86
345.15	0.9008	8.52
350.15	0.9008	10.46
355.15	0.9008	12.68
360.15	0.9008	15.29
365.15	0.9008	18.37
345.15	1.0000	9.18
350.15	1.0000	11.27
355.15	1.0000	13.73
360.15	1.0000	16.62
365.15	1.0000	20.00

Sources

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

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