RESUMO
: Microbial fermentations are of major importance in the field of biotechnology. The range of applications is rather extensive, for example, the production of vaccines, recombinant proteins, and plasmids. During the past decades single-use bioreactors have become widely accepted in the biopharmaceutical industry. This acceptance is due to the several advantages these bioreactors offer, such as reduced operational and investment costs. Although this technology is attractive for microbial applications, its usage is rarely found. The main limitations are a relatively low oxygen transfer rate and cooling capacity. The aim of this study was to examine a stirred single-use bioreactor for its microbial suitability. Therefore, the important process engineering parameters volumetric mass transfer coefficient (k L a), mixing time, and the heat transfer coefficient were determined. Based on the k L a characteristics a mathematical model was established that was used with the other process engineering parameters to create a control space. For a further verification of the control space for microbial suitability, Escherichia coli and Pichia pastoris high cell density fermentations were carried out. The achieved cell density for the E. coli fermentation was OD600 = 175 (DCW = 60.8 g/L). For the P. pastoris cultivation a wet cell weight of 381 g/L was reached. The achieved cell densities were comparable to fermentations in stainless steel bioreactors. Furthermore, the expression of recombinant proteins with titers up to 9 g/L was guaranteed.
