Supercritical fluid extraction of peach (Prunus persica) almond oil: Kinetics, mathematical modeling and scale-up

被引:147
作者
Mezzomo, Natalia [1 ]
Martinez, Julian [1 ]
Ferreira, Sandra R. S. [1 ]
机构
[1] Univ Fed Santa Catarina, Chem & Food Engn Dept, EQA, BR-88040900 Florianopolis, SC, Brazil
关键词
Peach almond; Supercritical fluid extraction; Modeling; Scale-up; Mass transfer phenomena; Overall extraction curves; CARBON-DIOXIDE EXTRACTION; GIGANTEUM L. OLEORESIN; CO2; SOLUBILITY;
D O I
10.1016/j.supflu.2009.07.008
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
Peach almonds contain oil with important therapeutic and nutritional properties due to the presence of unsaturated fatty acids, high content of oleic acid and other substances. In this study, peach almond oil was obtained by means of supercritical fluid extraction (SFE), with yield up to 24% w/w. The objective of this work was to evaluate the effect of the operation variables in the process kinetics in order to define scale-up parameters, like extractor volume and solvent flow rate. In spite of the importance for industrial application, the definition of a scale-up methodology is difficult. Therefore, the main goal of this work was to study the kinetic aspects of the SFE by modeling the extraction curves and, with these results, suggests a scale-up methodology. The parameters evaluated were extraction pressure, CO2 flow rate and particle size. The mass transfer models used to describe the extraction curves were logistic model, diffusion model and Sovova model. Four scale-up methodologies, based on mass transfer mechanisms, were applied. The results indicate the best curve fitting by means of Sovov's model, while the best scale-up criterion was maintaining the ratio Q(CO2)/M (solvent flow rate/raw material mass) constant. This study also indicated the convection as the dominant mass transfer mechanism, while the diffusion was the limiting factor. Moreover, the SFE of peach almond oil could be predicted by the scale-up method used. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:10 / 16
页数:7
相关论文
共 31 条
[1]
Angus S., 1976, INT THERMODYNAMIC TA
[2]
Supercritical fluid extractive fractionation - study of the antioxidant activities of propolis [J].
Wang, BJ ;
Lien, YH ;
Yu, ZR .
FOOD CHEMISTRY, 2004, 86 (02) :237-243
[3]
Brunner G., 1994, GAS EXTRACTION INTRO, V4
[4]
Experimental data and modeling the supercritical fluid extraction of marigold (Calendula officinalis) oleoresin [J].
Campos, LMAS ;
Michielin, EMZ ;
Danielski, L ;
Ferreira, SRS .
JOURNAL OF SUPERCRITICAL FLUIDS, 2005, 34 (02) :163-170
[5]
Clavier J.-Y., 2004, SCALE UP ISSUES SUPE, V1
[6]
Correia J., 2006, ESTUDO MODELOS TRANS
[7]
Crank J., 1975, MATH DIFFUSION
[8]
Horsetail (Equisetum giganteum L.) oleoresin and supercritical CO2:: Experimental solubility and empirical data correlation [J].
Danielski, Leandro ;
Michielin, Eliane M. Z. ;
Ferreira, Sandra R. S. .
JOURNAL OF FOOD ENGINEERING, 2007, 78 (03) :1054-1059
[9]
Supercritical fluid extraction of black pepper (Piper nigrun L.) essential oil [J].
Ferreira, SRS ;
Nikolov, ZL ;
Doraiswamy, LK ;
Meireles, MAA ;
Petenate, AJ .
JOURNAL OF SUPERCRITICAL FLUIDS, 1999, 14 (03) :235-245
[10]
Modeling the supercritical fluid extraction of black pepper (Piper nigrum L.) essential oil [J].
Ferreira, SRS ;
Meireles, MAA .
JOURNAL OF FOOD ENGINEERING, 2002, 54 (04) :263-269