No abstract

It was observed that during fermentative production of recombinant ovine interferon-tau (r-oIFN-tau) in Pichia pastoris, a secreted recombinant protein, the protein was degraded increasingly after 48 h of induction and the rate of degradation increased towards the end of fermentation at 72 h, when the fermentation was stopped. Proteases, whose primary source was the vacuoles, was found in increasing levels in the cytoplasm and in the fermentation broth after 48 h of induction and reached maximal values when the batch was completed at 72 h. Protease levels at various cell fractions as well as in the culture supernatant were lower when glycerol was used as the carbon source instead of methanol. It can be concluded that methanol metabolism along with cell lysis towards the end of fermentation contributes to increased proteolytic activity and eventual degradation of recombinant protein.

Recombinant ovine interferon-tau (r-oIFN-tau) production by Pichia pastoris was studied using methanol as the sole carbon source during induction. The cells were grown on glycerol up to a certain cell density before induction of the AOX1 promoter by methanol for expression of the recombinant protein. Cell growth on methanol has been modeled using a substrate-feed equation, which served as the basis for an effective computer control of the process. The r-oIFN-tau concentration in the culture began to decline despite continued cell growth after 50 (+/- 6) h of induction, which was associated with an increase in proteolytic activity of the fermentation broth. A specific growth rate of 0.025 h(-1) was found to be optimal for r-oIFN-tau production. No significant improvement in r-oIFN-tau production was observed when the specific growth rate was stepped up before the critical point when r-oIFN-tau concentration started decreasing during fermentation. However, best results were obtained when the specific growth rate was stepped down from 0.025 to 0.02 h(-1) at 38 h of induction, whereby the active production period was prolonged until 70 h of induction and the broth protease activity was correspondingly reduced. The corresponding maximum protein yield was 391.7 mg x L(-1) after 70 h of fermentation. The proteolytic activity could be reduced by performing fermentations at specific growth rates of 0.025 h(-1) or below. The recombinant protein production can be performed at an optimal yield by directly controlling the methanol feed rate by a computer-controlled model. The production profile of r-oIFN-tau was found to be significantly different from other secreted and intracellular recombinant protein processes, which is an indication that recombinant protein production in Pichia pastoris needs to be optimized as individual processes following established principles.

Smith, Leonard A.; and Meagher, Michael M., "Pichia pastoris fermentation with mixed-feeds of glycerol and methanol: growth kinetics and production improvement" (2003 Abstract Fed-batch fermentation of a methanol utilization plus (Mut + ) Pichia pastoris strain typically has a growth phase followed by a production phase (induction phase). In the growth phase glycerol is usually used as carbon for cell growth while in the production phase methanol serves as both inducer and carbon source for recombinant protein expression. Some researchers employed a mixed glycerol-methanol feeding strategy during the induction phase to improve production, but growth kinetics on glycerol and methanol and the interaction between them were not reported. The objective of this paper is to optimize the mixed feeding strategy based on growth kinetic studies using a Mut + Pichia strain, which expresses the heavy-chain fragment C of botulinum neurotoxin serotype C [BoNT/C(Hc)] intracellularly, as a model system. Growth models on glycerol and methanol that describe the relationship between specific growth rate (l) and specific glycerol/ methanol consumption rate (m gly , m MeOH ) were established. A mixed feeding strategy with desired l gly / l MeOH =1, 2, 3, 4 (desired l MeOH set at 0.015 h )1 ) was employed to study growth interactions and their effect on production. The results show that the optimal desired l gly /l MeOH is around 2 for obtaining the highest BoNT/C(Hc) protein content in cells: about 3 mg/g wet cells.