Mixture of Benzene + Acetonitrile + 1-Butanol

Datasets

1. Vapor Liquid Equilibrium at Constant Temperature

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 333.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of 1-Butanol (3) - Liquid	x2[mol/mol] of Acetonitrile (2) - Liquid	y1[mol/mol] of 1-Butanol (3) - Vapour	y2[mol/mol] of Acetonitrile (2) - Vapour
7.879	1.0000	0.0000	1.0000	0.0000
49.076	0.0000	1.0000	0.0000	1.0000
52.196	0.0000	0.0000	0.0000	0.0000
61.488	0.0650	0.6470	0.0250	0.5870
51.782	0.0830	0.8430	0.0380	0.8040
56.915	0.1890	0.3280	0.0540	0.3890
46.17	0.5480	0.1890	0.1240	0.3660
35.65	0.6890	0.2440	0.1740	0.6330
52.422	0.1760	0.0660	0.0660	0.1170
55.195	0.2430	0.3780	0.0660	0.4440
56.209	0.2290	0.3310	0.0590	0.4000
53.662	0.2470	0.1540	0.0720	0.2350
57.835	0.1540	0.2540	0.0500	0.3210
53.142	0.3020	0.4070	0.0760	0.4930
49.129	0.4500	0.1680	0.0980	0.3060
46.689	0.4600	0.3540	0.1060	0.5410
43.57	0.4570	0.4550	0.1210	0.6870
50.329	0.3910	0.1340	0.0910	0.2310

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data