Admassu W, Korus R A, Heimsch R C
Department of Chemical Engineering, University of Idaho, Moscow, Idaho 83843.
Biotechnol Bioeng. 1983 Nov;25(11):2641-51. doi: 10.1002/bit.260251112.
Biomass production and carbohydrate reduction were determined for a two-stage continuous fermentation process with a simulated potato processing waste feed. The amylolytic yeast Saccharomycopsis fibuligera was grown in the first stage and a mixed culture of S. fibuligera and Candida utilis was maintained in the second stage. All conditions for the first and second stages were fixed except the flow of medium to the second stage was varied. Maximum biomass production occurred at a second stage dilution rate, D(2), of 0.27 h (-1). Carbohydrate reduction was inversely proportional to D(2), between 0.10 and 0.35 h (-1).