Phase equilibria of palm oil, palm kernel oil, and oleic acid plus supercritical carbon dioxide and modeling using Peng-Robinson EOS

被引:16
|
作者
Hong, Seung-Ah [1 ,2 ]
Kim, Jae-Duck [1 ]
Kim, Jaehoon [1 ]
Kang, Jeong Won [2 ]
Kang, Ik-Joong [3 ]
机构
[1] Korea Inst Sci & Technol, Energy & Environm Res Div, Supercrit Fluid Res Lab, Seoul 163791, South Korea
[2] Korea Univ, Dept Chem & Biol Engn, Seoul 136701, South Korea
[3] Kyungwon Univ, Dept Chem & Bioengn, Songnam 461701, Kyongki Do, South Korea
关键词
Oleic acid; Palm oil; Palm kernel oil; Equilibrium; Supercritical; Peng-Robinson Equation of State (PR-EOS); RICE BRAN OIL; VAPOR-LIQUID-EQUILIBRIA; CUBIC EQUATIONS; BINARY-MIXTURES; LEMON FLAVORS; ETHYL-ESTERS; MIXING RULE; SOYBEAN OIL; FRYING OIL; FATTY OILS;
D O I
10.1016/j.jiec.2010.03.009
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Vapor-liquid equilibria of the binary supercritical carbon dioxide (scCO(2)) + oleic acid, scCO(2) + palm oil, and scCO(2) + palm kernel oil were measured at a wide range of temperatures from 333.2 to 373.2 K and pressures from 8.5 to 35 MPa in a circulation-type phase equilibrium apparatus. The samples from liquid and vapor phases were analyzed using UV-vis spectrometer and a liquid hold-up equipment. The phase equilibrium data were correlated with Peng-Robinson Equation of State (PR-EOS) using Wong-Sandler mixing rule and optimum values of binary interaction parameters were determined. The relative deviation between experimental data and predicted data was in the range of 6.9-8.7%, suggesting that the PR-EOS with Wong-Sandler mixing rule is capable of predicting the vapor-liquid equilibria of oleic acid + scCO(2), palm oil + scCO(2), and palm kernel oil + scCO(2). (C) 2010 Published by Elsevier B.V, on behalf of The Korean Society of Industrial and Engineering Chemistry.
引用
收藏
页码:859 / 865
页数:7
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