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. 2021 Apr 26;20(1):90.
doi: 10.1186/s12934-021-01577-4.

Scalable production and application of Pichia pastoris whole cell catalysts expressing human cytochrome P450 2C9

Affiliations

Scalable production and application of Pichia pastoris whole cell catalysts expressing human cytochrome P450 2C9

Javier Garrigós-Martínez et al. Microb Cell Fact. .

Abstract

Background: Currently, the numerous and versatile applications in pharmaceutical and chemical industry make the recombinant production of cytochrome P450 enzymes (CYPs) of great biotechnological interest. Accelerating the drug development process by simple, quick and scalable access of human drug metabolites is key for efficient and targeted drug development in response to new and sometimes unexpected medical challenges and needs. However, due its biochemical complexity, scalable human CYP (hCYP) production and their application in preparative biotransformations was still in its infancy.

Results: A scalable bioprocess for fine-tuned co-expression of hCYP2C9 and its essential complementary human cytochrome P450 reductase (hCPR) in the yeast Pichia pastoris (Komagataella phaffii) is presented. High-throughput screening (HTS) of a transformant library employing a set of diverse bidirectional expression systems with different regulation patterns and a fluorimetric assay was used in order to fine-tune hCYP2C9 and hCPR co-expression, and to identify best expressing clonal variants. The bioprocess development for scalable and reliable whole cell biocatalyst production in bioreactors was carried out based on rational optimization criteria. Among the different alternatives studied, a glycerol carbon-limiting strategy at high µ showed highest production rates, while methanol co-addition together with a decrease of µ provided the best results in terms of product to biomass yield and whole cell activity. By implementing the mentioned strategies, up to threefold increases in terms of production rates and/or yield could be achieved in comparison with initial tests. Finally, the performance of the whole cell catalysts was demonstrated successfully in biotransformation using ibuprofen as substrate, demonstrating the expected high selectivity of the human enzyme catalyst for 3'hydroxyibuprofen.

Conclusions: For the first time a scalable bioprocess for the production of hCYP2C9 whole cell catalysts was successfully designed and implemented in bioreactor cultures, and as well, further tested in a preparative-scale biotransformation of interest. The catalyst engineering procedure demonstrated the efficiency of the employment of a set of differently regulated bidirectional promoters to identify transformants with most effective membrane-bound hCYP/hCPR co-expression ratios and implies to become a model case for the generation of other P. pastoris based catalysts relying on co-expressed enzymes such as other P450 catalysts or enzymes relying on co-expressed enzymes for co-factor regeneration.

Keywords: Bidirectional promoters; Bioprocess optimisation; Human CYP2C9; Ibuprofen; Pichia pastoris; Whole cell biocatalyst.

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Conflict of interest statement

The authors of TU Graz and bisy declare that they have commercial interests in the use of bidirectional promoters for protein coexpression. Bisy GmbH owns and commercializes tools for recombinant bidirectional coexpression of genes.

Figures

Fig. 1
Fig. 1
a Diclofenac and 7-methoxy-4-(trifluoromethyl)-2H-chromen-2-one (MCF) oxidation reactions catalysed by P. pastoris CYP2C9/CPR whole cell biocatalyst. b Screening of producer clones based on bidirectional expression system using different promoter variants towards to identify the most active CYP2C9/CPR whole cells
Fig. 2
Fig. 2
Effect of culture pH for the production of P. pastoris CYP2C9/CPR whole cells biocatalyst. Chemostat cultivations were carried out, setting the dilution rate to 0.10 h−1. Error bars represent the activity assay standard deviation determined by triplicates
Fig. 3
Fig. 3
a Biomass time-profile of the fed-batch cultures performed. Experiment labels: FB1: μ = 0.05 h−1; FB2: μ = 0.10 h−1; FB3: μ = 0.15 h−1; FB4: μ = 0.05 h−1 + MetOH pulses; FB5: μ = 0.05 h−1 + constant MetOH = 3 g L−1
Fig. 4
Fig. 4
Biocatalyst activity time-profiles obtained in fed-batch cultures 1–5. Experiment labels: FB1: µ = 0.05 h−1; FB2: µ = 0.10 h−1; FB3: µ = 0.15 h−1; FB4: µ = 0.05 h−1 + MetOH pulses; FB5: µ = 0.05 h−1 + constant MetOH = 3 g L−1
Fig. 5
Fig. 5
Product-related parameters obtained in fed-batch cultures: specific product generation rate (qp) and product-to-biomass yield (YP/X). Experiment labels: FB1: µ = 0.05 h−1; FB2: µ = 0.10 h−1; FB3: µ = 0.15 h−1; FB4: µ = 0.05 h−1 + MetOH pulses; FB5: µ = 0.05 h−1 + constant MetOH = 3 g L−1
Fig. 6
Fig. 6
a Ibuprofen oxidation reactions catalysed by human CYPs. b Preparative scale ibuprofen oxidation by P. pastoris CYP2C9/CPR whole cells biocatalyst. Substrate concentration: 2 mM, reaction volume: 500 mL

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