Abstract

BackgroundPichia pastoris is a widely-used host for recombinant protein production; expression is typically driven by methanol-inducible alcohol oxidase (AOX) promoters. Recently this system has become an important source of recombinant G protein-coupled receptors (GPCRs) for structural biology and drug discovery. The influence of diverse culture parameters (such as pH, dissolved oxygen concentration, medium composition, antifoam concentration and culture temperature) on productivity has been investigated for a wide range of recombinant proteins in P. pastoris. In contrast, the impact of the pre-induction phases on yield has not been as closely studied. In this study, we examined the pre-induction phases of P. pastoris bioreactor cultivations producing three different recombinant proteins: the GPCR, human A2a adenosine receptor (hA2aR), green fluorescent protein (GFP) and human calcitonin gene-related peptide receptor component protein (as a GFP fusion protein; hCGRP-RCP-GFP).ResultsFunctional hA2aR was detected in the pre-induction phases of a 1 L bioreactor cultivation of glycerol-grown P. pastoris. In a separate experiment, a glycerol-grown P. pastoris strain secreted soluble GFP prior to methanol addition. When glucose, which has been shown to repress AOX expression, was the pre-induction carbon source, hA2aR and GFP were still produced in the pre-induction phases. Both hA2aR and GFP were also produced in methanol-free cultivations; functional protein yields were maintained or increased after depletion of the carbon source. Analysis of the pre-induction phases of 10 L pilot scale cultivations also demonstrated that pre-induction yields were at least maintained after methanol induction, even in the presence of cytotoxic concentrations of methanol. Additional bioreactor data for hCGRP-RCP-GFP and shake-flask data for GFP, horseradish peroxidase (HRP), the human tetraspanins hCD81 and CD82, and the tight-junction protein human claudin-1, demonstrated that bioreactor but not shake-flask cultivations exhibit recombinant protein production in the pre-induction phases of P. pastoris cultures.ConclusionsThe production of recombinant hA2aR, GFP and hCGRP-RCP-GFP can be detected in bioreactor cultivations prior to methanol induction, while this is not the case for shake-flask cultivations of GFP, HRP, hCD81, hCD82 and human claudin-1. This confirms earlier suggestions of leaky expression from AOX promoters, which we report here for both glycerol- and glucose-grown cells in bioreactor cultivations. These findings suggest that the productivity of AOX-dependent bioprocesses is not solely dependent on induction by methanol. We conclude that in order to maximize total yields, pre-induction phase cultivation conditions should be optimized, and that increased specific productivity may result in decreased biomass yields.Electronic supplementary materialThe online version of this article (doi:10.1186/s12934-014-0127-y) contains supplementary material, which is available to authorized users.

Highlights

  • Pichia pastoris is a widely-used host for recombinant protein production; expression is typically driven by methanol-inducible alcohol oxidase (AOX) promoters

  • Since it is established that lowering the temperature to 22°C during induction increases the functional yield of human A2a adenosine receptor (hA2aR) [13,14,18], the cultivation temperature was lowered during phase in the transition phase (III)

  • green fluorescent protein (GFP) is produced in the pre-induction phases of glycerol-grown P. pastoris bioreactor cultivations In order to assess whether pre-induction expression was specific to hA2aR as the recombinant target protein, we examined the production of recombinant soluble GFP

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Summary

Introduction

Pichia pastoris is a widely-used host for recombinant protein production; expression is typically driven by methanol-inducible alcohol oxidase (AOX) promoters. This system has become an important source of recombinant G protein-coupled receptors (GPCRs) for structural biology and drug discovery. In its most widely used format, protein production is driven by a very strong, methanol-inducible alcohol oxidase (AOX) promoter, which is generally accepted to be tightly regulated [4]. In a subsequent fed-batch phase, the same carbon source is fed continuously with the objective of yielding high preinduction biomass; during this phase, growth is nutrient limited and a constant specific growth rate, lower than μmax, is achieved. In the induction phase, methanol is added in a controlled manner [5,6] to induce AOX-driven recombinant protein production

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