Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15 K
作者： R.M. Villamañán , C.R. Chamorro , M.C. Martín , J.J. Segovia
DOI: 10.1016/J.FLUID.2005.11.017
关键词: Non-random two-liquid model 、 Isobutanol 、 Chemistry 、 Thermodynamics 、 Phase (matter) 、 Organic chemistry 、 Binary system 、 Isothermal process 、 UNIQUAC 、 Ternary operation 、 Ternary numeral system
摘要: Abstract Isothermal vapour–liquid equilibrium data have been measured for the ternary system (di-isopropyl ether + isobutanol + benzene) and two of binary systems involved ether + isobutanol) (isobutanol + benzene) at 313.15 K. A static technique consisting an isothermal total pressure cell was used measurements. Data reduction by Barker's method provides correlations G E using Margules equation Wohl expansion system. Wilson, NRTL UNIQUAC models applied successfully to both systems.
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