Multiphase Equilibrium Calculations from Soave Equation of State with Chang-Twu/UNIFAC Mixing Rules for Mixtures Containing Water, Alcohols, and Esters

被引:5
|
作者
Hong, Gui-Bing
Hsieh, Cheng-Ting [2 ]
Lin, Ho-mu [1 ]
Lee, Ming-Jer [1 ]
机构
[1] Natl Taiwan Univ Sci & Technol, Dept Chem Engn, Taipei 10607, Taiwan
[2] Atom Energy Council, Inst Nucl Energy Res, Div Phys, Longtan Township, Taoyuan County, Taiwan
关键词
LIQUID-LIQUID EQUILIBRIA; VAPOR-LIQUID; TERNARY MIXTURES; BUTYL PROPIONATE; AQUEOUS SYSTEMS; CUBIC EQUATION; ALPHA-FUNCTION; PRESSURE; UNIFAC; COEXISTENCE;
D O I
10.1021/ie202456v
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Various versions of the Soave-Redlich-Kwong (SRK) equation of state incorporating different mixing rules were applied to calculate vapor-iquid equilibrium (VLE), liquid-liquid equilibrium (LLE), and vapor-liquid-liquid equilibrium (VLLE) properties for the systems containing water, alcohols, and esters. The calculated results showed that the SRK equation with the T-type a function and the Chung-Twu (CT) mixing rules embedded in the UNLFAC-Lyngby model (SRK-T/CT-UNIFAC- Lyngby) not only predicts accurately the VLE properties of the constituent binaries but also represents the ternary LLE and VLLE phase behavior reasonably well. Using this model, the vapor pressure data of the pure constituent components are the only required property for the phase equilibrium calculations.
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页码:5073 / 5081
页数:9
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