On‐line optimal control for fed‐batch culture of baker's yeast production
- 1 May 1985
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 27 (5) , 756-760
- https://doi.org/10.1002/bit.260270525
Abstract
A method of on-line optimal control for fed-batch culture of bakers yeast production is proposed. The feed rate is taken as the control variable. The specific growth rate of the yeast is the output variable and is determined from the balance equation of oxygen. A moving model is obtained by using the data from the feed rate and the specific growth rate. Based on the moving model, an optimal feed rate for fed-batch culture is then achieved.This publication has 8 references indexed in Scilit:
- Parameter identification of systems with unmeasured disturbancesJournal of the Chinese Institute of Engineers, 1984
- Suboptimal control of nonlinear dynamic systems via moving modelComputers & Chemical Engineering, 1983
- Modelling and realization of multiple time delays systems via moving modelsInternational Journal of Systems Science, 1983
- Maximum production in a bakers' yeast fed‐batch culture by a tubing methodBiotechnology & Bioengineering, 1981
- Computer control of bakers' yeast productionBiotechnology & Bioengineering, 1979
- Real‐time estimation of aerobic batch fermentation biomass concentration by component balancingAIChE Journal, 1978
- Computer‐aided material balancing for prediction of fermentation parametersBiotechnology & Bioengineering, 1977
- Fed batch culture of Saccharomyces cerevisiae: A perspective of computer control to enhance the productivity in baker's yeast cultivationBiotechnology & Bioengineering, 1976