Supercritical CO2 extraction of essential oil from orange peel;: effect of the height of the bed

被引:85
作者
Berna, A [1 ]
Tárrega, A
Blasco, M
Subirats, S
机构
[1] Univ Valencia, Dept Chem Engn, E-46100 Burjassot, Valencia, Spain
[2] AgroFood Technol Inst, AINIA, Valencia 46890, Spain
关键词
orange essential oil; supercritical fluid extraction; modeling; effect of bed height; carbon dioxide;
D O I
10.1016/S0896-8446(00)00082-6
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The influence of the height of the particle bed on the kinetics of supercritical fluid extraction (SFE) of essential oil from orange peel is analyzed in this article. Peel of dehydrated oranges of the satsuma and naveline cultivars was used. A series of experiments were designed wherein, for the same conditions, particle height varied widely. These experiments were also carried out on different scales with extraction volumes of 0.5 and 5 1. The results of the experiments were interpreted using Sovova's extended flow model as has been done in previous studies. The bibliography indicates that a number of phenomena may distort the process. One of these phenomena is the formation of masses of particles, due to their oil content, which increases resistance to mass transfer inside the particle. However, this phenomenon was barely noticeable in our experiments. Also, some reordering of the particles may take place due to the differing densities of the two phases and a certain drag effect exercised on the particles by the fluid. This situation can cause a lack of homogeneity in the fluid, further reducing the effectiveness of the process. In the experiments with the satsuma cultivar, where the bed-height range was broader, a base of diatomaceous earth was added in the extractor in order to reduce the lack of homogeneity in the fluid flow. Very similar behavior was found in all the experiments and we can, therefore, conclude that where there is homogeneous flow the height of the bed has very little effect, at least on the same scale of operation. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:227 / 237
页数:11
相关论文
共 41 条
[1]  
AMANO A, 1976, Patent No. 76108136
[2]  
BENVENUTI F, 1997, P 4 IT C SUP FLUIDS, P65
[3]  
Bisio A, 1985, SCALEUP CHEM PROCESS
[4]  
Brunner G., 1997, P 4 IT C SUP FLUIDS, P27
[5]   Countercurrent deterpenation of citrus oils with supercritical CO2 [J].
Budich, M ;
Heilig, S ;
Wesse, T ;
Leibküchler, V ;
Brunner, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 1999, 14 (02) :105-114
[6]  
CARLES M, 1996, P 3 C FLUID SUP, P181
[7]   Scale-up of a supercritical extraction unit for the deacidification of olive oil [J].
Carmelo, PJ ;
Pereira, PJ ;
Simoes, PC ;
daPonte, MN .
HIGH PRESSURE CHEMICAL ENGINEERING, 1996, 12 :487-492
[8]   Extrapolation from pilot plant to industrial scale SFE: A case study [J].
Clavier, JY ;
Majewski, W ;
Perrut, M .
HIGH PRESSURE CHEMICAL ENGINEERING, 1996, 12 :639-644
[9]  
Coulson J. M., 1991, CHEM ENG, V2
[10]   High pressure CO2 extraction.: Fundamentals and applications in the food industry [J].
del Valle, JM ;
Aguilera, JM .
FOOD SCIENCE AND TECHNOLOGY INTERNATIONAL, 1999, 5 (01) :1-24