Mixture of 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol + Benzene, 1,3-dimethyl-

Datasets

1. Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Benzene, 1,3-dimethyl- (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
375.15	0.1000	6.24
383.15	0.1000	7.84
391.15	0.1000	9.62
399.15	0.1000	11.55
407.15	0.1000	14.81
350.15	0.2997	6.85
357.15	0.2997	8.96
364.15	0.2997	11.16
371.15	0.2997	14.01
378.15	0.2997	17.42
345.15	0.5001	8.19
351.15	0.5001	10.11
357.15	0.5001	12.57
363.15	0.5001	15.45
369.15	0.5001	18.98
345.15	0.6998	9.50
350.15	0.6998	11.45
355.15	0.6998	13.73
360.15	0.6998	16.50
365.15	0.6998	19.65
342.15	0.9003	9.28
347.15	0.9003	11.37
352.15	0.9003	13.58
357.15	0.9003	16.45
362.15	0.9003	19.79
345.15	1.0000	11.00
350.15	1.0000	13.44
355.15	1.0000	16.32
360.15	1.0000	19.68
365.15	1.0000	23.59

Sources

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

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