Fermentation kinetics of spent sulfite liquor by Saccharomyces cerevisiae
- 1 July 1986
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 28 (7) , 944-951
- https://doi.org/10.1002/bit.260280703
Abstract
The growth kinetics of the yeast Saccharomyces cerevisiae and the production rate of ethanol have been studied in batch fermentation under anaerobic conditions in a 20-L fermentor. Two substrates were used in fermentation trials: a synthetic mixture of three fermentable sugars, D-glucose, D-mannose, and D-galactose, and a low-yield liquor originating from a bisulfite cooking process. The Monod model adequately described the system in relation to the specific growth rate μx and the specific product formation rate μP. Different fermentation parameters (growth rate, substrate utilization, and product formation) were determined for the synthetic mixture and the bisulfite liquor. It was observed that the specific growth rate is much lower in spent sulfite liquor than in a synthetic medium. However, the specific product formation rate remains the same in both media.This publication has 3 references indexed in Scilit:
- The effects of mixing, temperature, and nutrient concentration on the fermentation of a mixed sugar solution simulating the hexose content of waste sulfite liquorThe Canadian Journal of Chemical Engineering, 1977
- Kinetics of fermentation processesBiotechnology & Bioengineering, 1969
- Utilization of mixed sugars in continuous fermentation. II.Biotechnology & Bioengineering, 1967