Mixture of Butane + 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 Butane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.50	0.4954	1065.70
364.50	0.5462	1099.00
364.50	0.8459	1250.50
364.50	0.8952	1268.40
364.51	0.0000	297.10
364.51	0.0305	393.00
364.51	0.0481	443.70
364.51	0.0935	558.60
364.51	0.1408	659.00
364.51	0.1889	744.90
364.51	0.2381	818.40
364.51	0.2890	883.00
364.51	0.3919	986.80
364.51	0.4439	1029.30
364.51	0.4960	1067.00
364.51	0.6943	1181.80
364.51	0.7446	1206.40
364.51	0.7951	1229.70
364.51	0.9485	1282.00
364.51	0.9687	1284.80
364.51	0.9781	1285.40
364.51	0.9884	1285.40
364.51	1.0000	1284.50
364.52	0.3401	938.40
364.52	0.6446	1156.20
364.53	0.5954	1129.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butane (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
364.50	0.4954	1065.70
364.50	0.5462	1099.00
364.50	0.8459	1250.50
364.50	0.8952	1268.40
364.51	0.0000	297.10
364.51	0.0305	393.00
364.51	0.0481	443.70
364.51	0.0935	558.60
364.51	0.1408	659.00
364.51	0.1889	744.90
364.51	0.2381	818.40
364.51	0.2890	883.00
364.51	0.3919	986.80
364.51	0.4439	1029.30
364.51	0.4960	1067.00
364.51	0.6943	1181.80
364.51	0.7446	1206.40
364.51	0.7951	1229.70
364.51	0.9485	1282.00
364.51	0.9687	1284.80
364.51	0.9781	1285.40
364.51	0.9884	1285.40
364.51	1.0000	1284.50
364.52	0.3401	938.40
364.52	0.6446	1156.20
364.53	0.5954	1129.00

Sources

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