Efficiency of a fixed-bed and a gas-lift three-column reactor for continuous production of ethanol by pectate-and alginate-immobilized Saccharomyces cerevisiae cells

Valach, M., Navrátil, M., Horváthová, V., Zigová, J., Šturdík, E., Hrabárová, E. and Gemeiner, P. Efficiency of a fixed-bed and a gas-lift three-column reactor for continuous production of ethanol by pectate-and alginate-immobilized Saccharomyces cerevisiae cells Chemical Papers, Vol.60, No. 2, 2006, 154-159

Document type: Článok z časopisu / Journal Article
Collection: Chemical papers  

Author(s) Valach, M.
Navrátil, M.
Horváthová, V.
Zigová, J.
Šturdík, E.
Hrabárová, E.
Gemeiner, P.
Title Efficiency of a fixed-bed and a gas-lift three-column reactor for continuous production of ethanol by pectate-and alginate-immobilized Saccharomyces cerevisiae cells
Journal name Chemical Papers
Publication date 2006
Year available 2006
Volume number 60
Issue number 2
ISSN 0366-6352
Start page 154
End page 159
Place of publication Poland
Publisher Versita
Collection year 2006
Language english
Subject 270000 Biological Sciences
270100 Biochemistry and Cell Biology
Abstract/Summary Ethanol-tolerant and thermo-tolerant yeast strain Saccharomyces cerevisiae C11-3 cells immobilized in calcium pectate and calcium alginate gels were used for ethanol fermentation in a three-reactor system with a gradient temperature control. The fermentation process has been tested in a fixed-bed and a gas-lift arrangement. The gas-lift system was more efficient due to a better mass transport between the phases. Abrasion was more evident in calcium alginate particles, while calcium pectate beads were not significantly damaged. Two different concentrations of alginate were tested and calcium pectate gel was demonstrated to be more suitable as an immobilization material in comparison with calcium alginate due to its mechanical resistance and favourable diffusion parameters, providing an ethanol production of more than 7.5 g dm−3 h−1 over a period of 630 h.
 
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