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Recombinant Protein Production with Pichia pastoris in Continuous Fermentation – Kinetic Analysis of Growth and Product Formation
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2002
Year
EngineeringBioenergyBioprocess EngineeringBiosynthesisTransformed Pichia PastorisBioenergeticsBiochemical EngineeringMetabolic EngineeringYeastRecombinant Protein ProductionExcess MethanolContinuous FermentationPichia PastorisBiomass UtilizationBiotransformationFood FermentationBiochemistryIn Vitro FermentationFungal Cell FactoryBiomanufacturingBiotechnologyProtein EngineeringFood BioprocessingMicrobiologyMedicineProduct Formation
Continuous fermentation was applied to the production of recombinant human chymotrypsinogen B (hCTRB) by the methylotrophic yeast Pichia pastoris as a tool for the kinetic analysis of growth and product formation. Using methanol as the sole source of carbon, energy, and induction, cell growth could be described by a non-competitive Monod approach. Maximum growth rate μmax was determined to 0.084 h--1 and the KM-value for methanol to 0.22 g·L--1, respectively. With respect to product formation, a similar model was established exhibiting a methanol concentration of 0.13 g·L--1 as the KM-value and a maximum biomass-specific product-formation rate of πmax = 0.23 mg·g--1·h--1. The production of hCTRB was strictly growth-coupled. The data provided covers the range of methanol concentrations between 0 and 4 g·L--1. Substrate concentrations exceeding this upper value led to a complete collapse of product formation. This change in phenotype turned out to be irreversible indicating a genetic instability of transformed Pichia pastoris caused by excess methanol.