Ma. Priede et al., HYDRODYNAMIC, PHYSIOLOGICAL, AND MORPHOLOGICAL-CHARACTERISTICS OF FUSARIUM-MONILIFORME IN GEOMETRICALLY DISSIMILAR STIRRED BIOREACTORS, Biotechnology and bioengineering, 48(3), 1995, pp. 266-277
The influence of two mixing geometries (at the same scale) with differ
ent flow energy distributions on the performance of the gibberellic ac
id fermentation and on the morphology of the producing fungus Fusarium
moniliforme was investigated. Fermentations were performed using a tu
rbine mixing system (TMS) and a counterflow mixing system (CMS), which
were high and low power number mixing systems, respectively. Differen
t agitator speed rate profiles were maintained to obtain equal specifi
c power inputs to both mixing systems. Substantial differences in morp
hology and productivity of F. moniliforme were found. To investigate t
he causes of these differences, local values and spectra of the kineti
c energy of flow fluctuations were measured during the fermentations u
sing a stirring intensity measuring device (SIMD) and a frequency spec
trum analyzer. Biomass and gibberellic acid concentrations were found
to be higher in the TMS, where the energy distribution was less even,
and where the main part of the energy was at small frequencies (large
eddies). An automated image analysis method was used for quantitative
characterization of F. moniliforme freely dispersed mycelia and clump
morphology. A higher proportion of clumped mycelia with clumps of larg
er area, perimeter, and roughness was observed in the TMS. A correlati
on between the morphology and productivity was found, and TMS favored
the development of more productive mycelia with longer and thinner hyp
hae. Introduced power was not a good parameter to characterize differe
nt impellers, even at a given scale. (C) 1995 John Wiley & Sons, Inc.