A mass transfer model applied to the supercritical extraction with CO2 of curcumins from turmeric rhizomes (Curcuma longa L)

被引:17
作者
Chassagnez-Méndez, AL [1 ]
Corrêa, NCF [1 ]
França, LF [1 ]
Machado, NT [1 ]
Araújo, ME [1 ]
机构
[1] UFPA, Dept Engn Quim, Lab Operacoes Separacao, BR-66050970 Belem, Para, Brazil
关键词
extraction; drying; kinetic; supercritical CO2; natural products; curcuminoids;
D O I
10.1590/S0104-66322000000300007
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
Increasing restrictions on the use of artificial pigments in the food industry, imposed by the international market, have increased the importance of raw materials containing natural pigments. Of those natural substances with potential applications turmeric rhizomes (Curcuma longa L), are one of the most important natural sources of yellow coloring. Three different pigments (curcumin, desmetoxycurcumin, and bis-desmetoxycurcumin) constitute the curcuminoids. These pigments are largely used in the food industry as substitutes fur synthetic dyes like tartrazin. Extraction of curcuminoids from tumeric rhizomes with supercritical CO2 can be applied as an alternative method to obtain curcuminoids, as natural pigments are in general unstable, and hence degrade when submitted to extraction with organic solvents at high temperatures. Extraction experiments were carried out in a supercritical extraction pilot plant at pressures between 25 and 30 MPa and a temperature of 318 K. The influence of drying pretreatment on extraction yield was evaluated analyzing the mass transfer kinetics and the content of curcuminoids in the extracts during the course of extraction. The chemical identification of curcuminoids in both the extract and the residual solid was performed by spectrophotometry. Mass transfer within the solid matrix was described by a linear first-order desorption model, while that in the gas phase was described by a convective mass transfer model. Experimental results showed that the concentration profile for curcuminoids during the supercritical extraction process was higher when the turmeric rhizomes were submitted to a drying pretreatment at 343 K.
引用
收藏
页码:315 / 322
页数:8
相关论文
共 25 条
[1]
ADASOGLU N, 1994, J SUPERCRIT FLUID, V7, P93
[2]
[Anonymous], [No title captured]
[3]
ARAUJO ME, 1997, THESIS U ESTADUAL CA
[4]
SUPERCRITICAL-FLUID EXTRACTION OF OIL-PALM COMPONENTS [J].
BIRTIGH, A ;
JOHANNSEN, M ;
BRUNNER, G ;
NAIR, N .
JOURNAL OF SUPERCRITICAL FLUIDS, 1995, 8 (01) :46-50
[5]
DETERMINATION OF THE DENSITY OF POROUS PARTICLES USING VERY FINE DENSE POWDERS [J].
BUCZEK, B ;
GELDART, D .
POWDER TECHNOLOGY, 1986, 45 (02) :173-176
[6]
CHASSAGNEZMENDE.A, 1998, THESIS U FEDERAL PAR
[7]
Correa N. C. F., 1994, Ciencia e Tecnologia de Alimentos, V14, P29
[8]
SUPERCRITICAL-FLUID EXTRACTION OF FUNGAL LIPIDS - EFFECT OF COSOLVENT ON MASS-TRANSFER RATES AND PROCESS DESIGN AND ECONOMICS [J].
CYGNAROWICZPROVOST, M ;
OBRIEN, DJ ;
BOSWELL, RT ;
KURANTZ, MJ .
JOURNAL OF SUPERCRITICAL FLUIDS, 1995, 8 (01) :51-59
[9]
de França LF, 1999, J SUPERCRIT FLUID, V14, P247
[10]
SUPERCRITICAL CO2 EXTRACTION OF CAROTENE AND LUTEIN FROM LEAF PROTEIN-CONCENTRATES [J].
FAVATI, F ;
KING, JW ;
FRIEDRICH, JP ;
ESKINS, K .
JOURNAL OF FOOD SCIENCE, 1988, 53 (05) :1532-1536