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Fig. 3 | Microbial Cell Factories

Fig. 3

From: Scale-up of an amoeba-based process for the production of the cannabinoid precursor olivetolic acid

Fig. 3

Influence of constant εmax on the fermentation parameters in larger reactor systems. At constant εmax, an increase in tip speed and kLa can be observed, while the stirring rate and volumetric power input are decreasing with increasing reactor filling volume. All necessary geometric details and calculated values for the 1.6-L, 7-L, 75-L and 300-L reactor systems are presented in Table 2

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