Mixture of 1-Butene + Ethyl Acetate

Datasets

1. P_vap - Vapor or sublimation pressure, kPa (2)

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
318.39	0.2470	195.06
318.39	0.2970	221.96
318.40	0.0340	57.97
318.40	0.0520	70.97
318.40	0.1010	105.57
318.40	0.1490	137.07
318.40	0.1980	166.87
318.40	0.3460	246.66
318.40	0.3960	270.66
318.40	0.4470	293.76
318.40	0.5080	320.46
318.40	0.7980	435.25
318.40	0.8470	455.35
318.40	0.8980	477.05
318.40	0.9480	499.85
318.41	0.0000	31.27
318.41	0.0140	42.37
318.41	0.4990	316.16
318.41	0.5480	336.66
318.41	0.5980	356.56
318.41	0.6470	376.05
318.41	0.6970	395.45
318.41	0.7470	415.05
318.41	0.9680	509.55
318.41	0.9820	516.35
318.42	1.0000	525.55

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
318.39	0.2470	195.06
318.39	0.2970	221.96
318.40	0.0340	57.97
318.40	0.0520	70.97
318.40	0.1010	105.57
318.40	0.1490	137.07
318.40	0.1980	166.87
318.40	0.3460	246.66
318.40	0.3960	270.66
318.40	0.4470	293.76
318.40	0.5080	320.46
318.40	0.7980	435.25
318.40	0.8470	455.35
318.40	0.8980	477.05
318.40	0.9480	499.85
318.41	0.0000	31.27
318.41	0.0140	42.37
318.41	0.4990	316.16
318.41	0.5480	336.66
318.41	0.5980	356.56
318.41	0.6470	376.05
318.41	0.6970	395.45
318.41	0.7470	415.05
318.41	0.9680	509.55
318.41	0.9820	516.35
318.42	1.0000	525.55

Sources

• Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane