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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.
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页码:859 / 865
页数:7
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