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

Datasets

1. Vapor or sublimation pressure, kPa

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Benzene, ethyl- (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
380.15	0.0991	7.57
388.15	0.0991	9.40
396.15	0.0991	11.42
404.15	0.0991	13.96
412.15	0.0991	18.02
345.15	0.3009	6.44
352.15	0.3009	8.27
359.15	0.3009	10.44
366.15	0.3009	13.06
373.15	0.3009	16.17
335.15	0.4997	6.31
341.15	0.4997	8.04
347.15	0.4997	9.95
353.15	0.4997	12.29
359.15	0.4997	15.11
330.15	0.7009	5.60
336.15	0.7009	7.32
342.15	0.7009	9.37
348.15	0.7009	11.95
354.15	0.7009	14.76
325.15	0.9028	4.98
331.15	0.9028	6.38
337.15	0.9028	8.32
343.15	0.9028	10.56
349.15	0.9028	13.44
320.15	1.0000	4.08
326.15	1.0000	5.41
332.15	1.0000	7.09
338.15	1.0000	9.19
344.15	1.0000	11.79

Sources

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

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