Relation of shear stress and KLa on bikaverin production by Fusarium oxysporum CCT7620 in a bioreactor.

This study involved evaluating the effects of rotational impeller speed agitation (N) and specific air flow rate (Фair) on bikaverin production and on the growth of Fusarium oxysporum employing 11 bench-scale bioreactor assays. The results showed that the maximum bikaverin production (close to 300 mg L-1) was achieved after 48 h of fermentation in rice medium (20 g L-1 milled rice in water) at 28 °C with a volumetric oxygen transfer coefficient (KLa) and shear stress values of approximately 20 h-1 and 17 N m-2, respectively. We reached this combination of parameters using an N of 340 rpm and Фair of 0.935 vvm. These KLa and shear stress values can be used as references when upscaling this process. Thus, this study was important to demonstrate how the main parameters in bioreactors affect bikaverin production and it presented important indications for upscaling this bioprocess.

Comparison of Two Methods for Counting Molds in Fermentations Using the Production of Bikaverin by Fusarium oxysporum CCT7620 as a Model.

The dry cell weight (DCW) measurement is one of the preferred methods to determine the growth of filamentous fungi. However, this technique is not applicable to insoluble culture media, besides being possibly influenced by the presence of extracellular biomass. The standard plate counting (SPC) is a reference method for detecting viable cells; however, it is referred as imprecise. In this study, we did a comprehensive analysis of the errors associated to each procedure and also determined the growth kinetics of Fusarium oxysporum in soluble (DCW and SPC) and insoluble (SPC) culture media. Finally, we used the production of bikaverin in airlift bioreactor containing insoluble medium as a case study to estimate red pigment production and to monitor biomass growth via SPC. We concluded that SPC can be used to give reliable fungal growth kinetics in media with insoluble matter, yielding errors equivalent to DCW depending on the number of replicates done for serial dilutions and plate counting.