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- W2030697148 abstract "The productivity of immobilized yeast cell reactors varies with a number of parameters, including flow, amount and growth rate of yeast, bead size and type of medium. Variation of these parameters has a pronounced effect on reaction rate. This paper presents typical ranges for these productivities and demonstrates the patterns of changes that take place when bead size, flow and reaction medium are varied. Saccharomyces cerevisiae cells were immobilized in calcium alginate beads for the production of ethanol. The productivity of immobilized yeast in a batch reactor (0.2 g ethanol/g yeast · h) was only two-thirds that of free cells suspended at an equivalent cell density (0.3 g ethanol/g yeast · h). Different flow rates and bead sizes were used to ‘optimize’ the productivity. The productivity of 3.34 mm beads at a flow rate of 8.8 litre h−1(superficial velocity: 0.12 cm s−1) was 95% higher than that at 1.0 l h−1. Maximum productivities of 0.34, 0.27, 0.22 g/g yeast· h were obtained (at a flow rate of 8.8 l h−1) for 9.2% yeast-immobilized beads of 3.34, 4.45 and 5.65 mm in diameter, respectively." @default.
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- W2030697148 date "1985-11-01" @default.
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- W2030697148 title "Flow rate and bead size as critical parameters for immobilized-yeast reactors" @default.
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- W2030697148 doi "https://doi.org/10.1016/0141-0229(85)90095-x" @default.
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