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Fig. 2 | BMC Biotechnology

Fig. 2

From: Transferability of bioprocessing modes for recombinant protease production: from fed-batch to continuous cultivation with Bacillus licheniformis

Fig. 2

A: Schematic sketch of the chemostat cultivation set-up. A dip-pipe is adjusted to the required volume height. A bleed pump operated at higher pump speed than the feed pump ensures for a constant dilution rate (D). B: Model identification of the performed chemostat cultivations with a D of 1: 24%, 2: 39%, 3: 72% of the maximum specific growth rate (µ [h-1])

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