Mixture of Toluene + 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 - Liquid	Mole fraction of Toluene (1) - Liquid	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
383.15	0.1018	15.37
388.15	0.1018	17.73
393.15	0.1018	20.22
398.15	0.1018	22.79
305.15	0.3008	2.87
313.15	0.3008	3.98
321.15	0.3008	5.55
329.15	0.3008	7.52
337.15	0.3008	9.83
315.15	0.4998	6.11
321.15	0.4998	7.88
327.15	0.4998	9.93
333.15	0.4998	12.49
339.15	0.4998	15.55
315.15	0.7005	7.11
320.15	0.7005	8.73
325.15	0.7005	10.68
330.15	0.7005	12.99
335.15	0.7005	15.71
321.15	0.9010	10.11
325.15	0.9010	12.11
330.15	0.9010	14.90
335.15	0.9010	18.01
340.15	0.9010	21.80
315.15	1.0000	8.62
320.15	1.0000	10.77
325.15	1.0000	13.34
330.15	1.0000	16.40
335.15	1.0000	20.02

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	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
383.15	0.1018	15.37
388.15	0.1018	17.73
393.15	0.1018	20.22
398.15	0.1018	22.79
305.15	0.3008	2.87
313.15	0.3008	3.98
321.15	0.3008	5.55
329.15	0.3008	7.52
337.15	0.3008	9.83
315.15	0.4998	6.11
321.15	0.4998	7.88
327.15	0.4998	9.93
333.15	0.4998	12.49
339.15	0.4998	15.55
315.15	0.7005	7.11
320.15	0.7005	8.73
325.15	0.7005	10.68
330.15	0.7005	12.99
335.15	0.7005	15.71
321.15	0.9010	10.11
325.15	0.9010	12.11
330.15	0.9010	14.90
335.15	0.9010	18.01
340.15	0.9010	21.80
315.15	1.0000	8.62
320.15	1.0000	10.77
325.15	1.0000	13.34
330.15	1.0000	16.40
335.15	1.0000	20.02

Sources

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