Mixture of 1-Butene + Acetone

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
364.51	0.0148	336.40
364.51	0.0321	380.60
364.51	0.0501	425.00
364.51	0.0960	529.40
364.51	0.2420	797.90
364.51	0.3431	940.70
364.51	0.3940	1002.70
364.51	0.6447	1245.40
364.51	0.6940	1285.80
364.51	0.7443	1325.50
364.51	1.0000	1510.50
364.52	0.0000	296.80
364.52	0.1434	626.70
364.52	0.1916	714.90
364.52	0.2922	872.50
364.52	0.4450	1059.80
364.52	0.4967	1112.90
364.52	0.4979	1113.50
364.52	0.5466	1159.80
364.52	0.5951	1203.30
364.52	0.7939	1364.10
364.52	0.8436	1401.90
364.52	0.8955	1440.10
364.52	0.9686	1491.40
364.52	0.9789	1498.00
364.53	0.9485	1478.00
364.53	0.9893	1505.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of 1-Butene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.51	0.0148	336.40
364.51	0.0321	380.60
364.51	0.0501	425.00
364.51	0.0960	529.40
364.51	0.2420	797.90
364.51	0.3431	940.70
364.51	0.3940	1002.70
364.51	0.6447	1245.40
364.51	0.6940	1285.80
364.51	0.7443	1325.50
364.51	1.0000	1510.50
364.52	0.0000	296.80
364.52	0.1434	626.70
364.52	0.1916	714.90
364.52	0.2922	872.50
364.52	0.4450	1059.80
364.52	0.4967	1112.90
364.52	0.4979	1113.50
364.52	0.5466	1159.80
364.52	0.5951	1203.30
364.52	0.7939	1364.10
364.52	0.8436	1401.90
364.52	0.8955	1440.10
364.52	0.9686	1491.40
364.52	0.9789	1498.00
364.53	0.9485	1478.00
364.53	0.9893	1505.00

Sources

• Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone