Abstract

The methylotrophic yeast Pichia pastoris (Komagataella phaffii) is currently considered one of the most promising hosts for recombinant protein production (RPP) and metabolites due to the availability of several tools to efficiently regulate the recombinant expression, its ability to perform eukaryotic post-translational modifications and to secrete the product in the extracellular media. The challenge of improving the bioprocess efficiency can be faced from two main approaches: the strain engineering, which includes enhancements in the recombinant expression regulation as well as overcoming potential cell capacity bottlenecks; and the bioprocess engineering, focused on the development of rational-based efficient operational strategies. Understanding the effect of strain and operational improvements in bioprocess efficiency requires to attain a robust knowledge about the metabolic and physiological changes triggered into the cells. For this purpose, a number of studies have revealed chemostat cultures to provide a robust tool for accurate, reliable, and reproducible bioprocess characterization. It should involve the determination of key specific rates, productivities, and yields for different C and N sources, as well as optimizing media formulation and operating conditions. Furthermore, studies along the different levels of systems biology are usually performed also in chemostat cultures. Transcriptomic, proteomic and metabolic flux analysis, using different techniques like differential target gene expression, protein description and 13C-based metabolic flux analysis, are widely described as valued examples in the literature. In this scenario, the main advantage of a continuous operation relies on the quality of the homogeneous samples obtained under steady-state conditions, where both the metabolic and physiological status of the cells remain unaltered in an all-encompassing picture of the cell environment. This contribution aims to provide the state of the art of the different approaches that allow the design of rational strain and bioprocess engineering improvements in Pichia pastoris toward optimizing bioprocesses based on the results obtained in chemostat cultures. Interestingly, continuous cultivation is also currently emerging as an alternative operational mode in industrial biotechnology for implementing continuous process operations.

Highlights

  • In recent years, recombinant protein production (RPP) technology has given rise to a multibillion-dollar market offering products for a wide range of industrial activities such as food, detergent, paper, chemical, cosmetic, and pharmaceutical production

  • Derived from the RPP technology, metabolic engineering has opened the door to metabolic flux modification and new heterologous reactions

  • It is common to use manually or automatically constructed “context-specific” core models (Tomàs-Gamisans et al, 2019) to facilitate calculations and handling of data. These methodologies have been used in combination with chemostat cultures to examine the impact of heterologous protein production and the effects of different environmental conditions on P. pastoris metabolism

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Summary

INTRODUCTION

Recombinant protein production (RPP) technology has given rise to a multibillion-dollar market offering products for a wide range of industrial activities such as food, detergent, paper, chemical, cosmetic, and pharmaceutical production. It is common to use manually or automatically constructed “context-specific” core models (Tomàs-Gamisans et al, 2019) to facilitate calculations and handling of data These methodologies have been used in combination with chemostat cultures to examine the impact of heterologous protein production and the effects of different environmental conditions on P. pastoris metabolism. The other most extensively studied factor in P. pastoris continuous cultures in addition to the environmental conditions is the impact of heterologous protein production on MFA For this purpose, the effects of different model proteins on metabolic flux distribution relative to their non-productive counterparts is usually compared under identical cultivation conditions. Yamawaki et al (2007) found qP for scFv to exhibit either a saturation behavior on μ or bell-shaped kinetics depending on the operational mode used (continuous or fed-batch cultivation)

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