Mixture of Butane + 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 Butane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
318.40	0.0000	31.37
318.40	0.0130	44.27
318.40	0.0340	62.77
318.40	0.0520	78.47
318.40	0.1020	116.47
318.40	0.1500	148.57
318.40	0.2000	177.76
318.40	0.2500	203.56
318.40	0.3000	226.36
318.40	0.3510	246.76
318.40	0.4010	264.96
318.40	0.5970	323.26
318.40	0.6960	348.96
318.40	0.7460	361.65
318.40	0.7970	374.95
318.40	0.8470	388.45
318.40	0.8970	402.95
318.40	0.9480	418.75
318.40	0.9680	425.25
318.40	0.9880	432.15
318.40	1.0000	436.55
318.41	0.4520	281.76
318.41	0.4980	295.76
318.41	0.5020	297.36
318.41	0.5480	309.96
318.41	0.6470	336.26

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
318.40	0.0000	31.37
318.40	0.0130	44.27
318.40	0.0340	62.77
318.40	0.0520	78.47
318.40	0.1020	116.47
318.40	0.1500	148.57
318.40	0.2000	177.76
318.40	0.2500	203.56
318.40	0.3000	226.36
318.40	0.3510	246.76
318.40	0.4010	264.96
318.40	0.5970	323.26
318.40	0.6960	348.96
318.40	0.7460	361.65
318.40	0.7970	374.95
318.40	0.8470	388.45
318.40	0.8970	402.95
318.40	0.9480	418.75
318.40	0.9680	425.25
318.40	0.9880	432.15
318.40	1.0000	436.55
318.41	0.4520	281.76
318.41	0.4980	295.76
318.41	0.5020	297.36
318.41	0.5480	309.96
318.41	0.6470	336.26

Sources

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