Reaction and diffusion in a gel membrane reactor containing immobilized cells
- 20 June 1992
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 40 (2) , 322-328
- https://doi.org/10.1002/bit.260400217
Abstract
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 and 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. © 1992 John Wiley & Sons, Inc.Keywords
This publication has 17 references indexed in Scilit:
- Diffusion in gels containing immobilized cells: A critical reviewBiotechnology & Bioengineering, 1991
- Growing Saccharomyces cerevisiae in calcium‐alginate beads induces cell alterations which accelerate glucose conversion to ethanolBiotechnology & Bioengineering, 1990
- Scanning Microfluorimetry of Ca-Alginate Immobilized Zymomonas MobilisNature Biotechnology, 1988
- Effects of immobilization on the nature of glycolytic oscillations in yeastBiotechnology & Bioengineering, 1987
- Effects of inoculum size on ethanol inhibition modeling and other fermentation parametersBiotechnology & Bioengineering, 1987
- Diffusion in κ-carrageenan gel beadsBiotechnology & Bioengineering, 1986
- Growth of Saccharomyces cerevisiae is controlled by its limited respiratory capacity: Formulation and verification of a hypothesisBiotechnology & Bioengineering, 1986
- Diffusion coefficients of glucose and ethanol in cell‐free and cell‐occupied calcium alginate membranesBiotechnology & Bioengineering, 1986
- Reaction characteristics of an immobilized yeast producing ethanolBiotechnology & Bioengineering, 1983
- Ethanol production in an immobilized‐cell reactorBiotechnology & Bioengineering, 1980