“…These results could therefore also be used to significantly lower power input (and hence operating costs) in pelleted fermentations [k L a = 77.4P/V) 0.6 ] and obtain similar mass transfer rates as dispersed morphology fermentations [k L a = 16.7(P/V) 0.8 ]. Considering the importance of these complex morphologies on fermentation performance, and reports that changes in the morphology of P. chrysogenum can be caused by mechanical forces (Dion et al, 1954;Metz et al, 1981;van Suijdam and Metz, 1981;Smith et al, 1990;Nielsen, 1992;Makagiansar et al, 1993;Ayazi Shamlou et al, 1994;Jüsten et al, 1996Jüsten et al, , 1998a, the direct effect of agitation on morphology in submerged fermentations requires attention. As well as the total power input, the choice of impeller geometry determines the hydrodynamic forces that might affect the morphology (Jüsten et al, 1996;Amanullah et al, 1999) and differentiation (Jüsten et al, 1998a) of filamentous species, thereby influencing growth or production (König et al, 1981;Buckland et al, 1988a;Jüsten et al, 1998a;Amanullah et al, 1999).…”