REACTION AND DIFFUSION IN A GEL MEMBRANE REACTOR CONTAINING IMMOBILIZED CELLS

被引:31
作者
DEBACKER, L
DEVLEMINCK, S
WILLAERT, R
BARON, G
机构
[1] Department of Chemical Engineering, Vrije Universiteit Brussel, Brussels, B1050
关键词
GEL MEMBRANE REACTOR; DIFFUSIONAL LIMITATIONS; GLUCOSE; GEL IMMOBILIZED CELLS;
D O I
10.1002/bit.260400217
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
To investigate the effect of diffusional limitations and heterogeneous cell distribution in a gel-immobilized cell system, a gel membrane reactor has been constructed. The reactor consists essentially of a gel layer with immobilized cells, flanked by two well-mixed chambers. Through one chamber substrate is pumped, and this chamber is the equivalent of the outside of a spherical gel bead. The second closed measuring chamber contains a small quantity of liquid that can equilibrate with the inside surface of the membrane, eventually after a long transient. Analysis of the liquid in this chamber can give direct information on substrate and product concentrations at the gel surface, and is an indication of the situation in the center of a gel bead. The gel membrane reactor appears to be an excellent tool to study diffusion and reaction in a gel-containing immobilized cells. A mathematical model with time- and position-dependent cell concentration and diffusion coefficient is described. Experimental data show the effective diffusion coefficient of glucose in an alginate gel to decrease with yeast cell concentration. Moreover, kinetic parameters could be determined, using the mathematical model. Microscopic analysis confirmed the proliferation of the gel-entrapped microorganisms in the outer layer of the matrix, as predicted by the model. Potentially, this type of reactor has a clear potential to study the physiology of gel-immobilized cells.
引用
收藏
页码:322 / 328
页数:7
相关论文
共 23 条
[1]   INTRAPARTICLE DIFFUSIONAL EFFECTS IN IMMOBILIZED CELL PARTICLES [J].
DALILI, M ;
CHAU, PC .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1987, 26 (06) :500-506
[2]  
DEBONT JAM, 1990, PHYSL IMMOBILIZED CE
[3]   EFFECTS OF IMMOBILIZATION ON THE NATURE OF GLYCOLYTIC OSCILLATIONS IN YEAST [J].
DORAN, PM ;
BAILEY, JE .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 29 (07) :892-897
[4]   REACTION CHARACTERISTICS OF AN IMMOBILIZED YEAST PRODUCING ETHANOL [J].
FURUSAKI, S ;
SEKI, M ;
FUKUMURA, K .
BIOTECHNOLOGY AND BIOENGINEERING, 1983, 25 (12) :2921-2928
[5]   GROWING SACCHAROMYCES-CEREVISIAE IN CALCIUM-ALGINATE BEADS INDUCES CELL ALTERATIONS WHICH ACCELERATE GLUCOSE CONVERSION TO ETHANOL [J].
GALAZZO, JL ;
BAILEY, JE .
BIOTECHNOLOGY AND BIOENGINEERING, 1990, 36 (04) :417-426
[6]   ETHANOL FERMENTATION IN A YEAST IMMOBILIZED TUBULAR FERMENTER [J].
GENCER, MA ;
MUTHARASAN, R .
BIOTECHNOLOGY AND BIOENGINEERING, 1983, 25 (09) :2243-2262
[7]  
GOSMANN B, 1986, APPL MICROBIOL BIOT, V23, P163
[8]   DIFFUSION-COEFFICIENTS OF GLUCOSE AND ETHANOL IN CELL-FREE AND CELL-OCCUPIED CALCIUM ALGINATE MEMBRANES [J].
HANNOUN, BJM ;
STEPHANOPOULOS, G .
BIOTECHNOLOGY AND BIOENGINEERING, 1986, 28 (06) :829-835
[9]   THE EFFECT OF MICRO-AEROBIC CONDITIONS ON CONTINUOUS ETHANOL-PRODUCTION BY SACCHAROMYCES-CEREVISIAE [J].
HOPPE, GK ;
HANSFORD, GS .
BIOTECHNOLOGY LETTERS, 1984, 6 (10) :681-686
[10]   THE IMMOBILIZATION OF WHOLE CELLS - ENGINEERING PRINCIPLES [J].
KAREL, SF ;
LIBICKI, SB ;
ROBERTSON, CR .
CHEMICAL ENGINEERING SCIENCE, 1985, 40 (08) :1321-1354