Abstract

As Pichia pastoris (syn. Komagataella sp.) yeast can secrete pure recombinant proteins at high rates, it is a desirable production system. The function of a novel synthetic variant of the AOX1 promoter was characterised comprehensively using a strain secreting Candida antarctica lipase B (CALB) as a model. A new time-saving approach was introduced to determine, in only one experiment, the hitherto unknown relationship between specific product formation rate (qp) and specific growth rate (μ). Tight control of recombinant protein formation was possible in the absence of methanol, while using glycerol as a sole carbon/energy source. CALB was not synthesised during batch cultivation in excess glycerol (>10 g l−1) and at a growth rate close to μmax (0.15 h−1). Between 0.017 and 0.115 h−1 in glycerol-limited fedbatch cultures, basal levels of qp > 0.4 mg g−1 h−1 CALB were reached, independent of the μ at which the culture grew. At μ > 0.04 h−1, an elevated qp occurred temporarily during the first 20 h after changing to fedbatch mode and decreased thereafter to basal. In order to accelerate the determination of the qp(μ) relationship (kinetics of product formation), the entire μ range was covered in a single fedbatch experiment. By linearly increasing and decreasing glycerol addition rates, μ values were repeatedly shifted from 0.004 to 0.074 h−1 and vice versa. Changes in qp were related to changes in μ. A rough estimation of μ range suitable for production was possible in a single fedbatch, thus significantly reducing the experimental input over previous approaches comprising several experiments.

Highlights

  • The PAOX1 variant is a novel promoter for use with P. pastoris to produce heterologous proteins that can be controlled without induction by methanol

  • Candida antarctica lipase B (CALB) production under the control of the PAOX1 variant was investigated in batch cultivations with glycerol in excess (10 to 50 g l−1)

  • Relationship between CALB production controlled by the PAOX1 variant and specific growth rate

Read more

Summary

Introduction

A variety of promoters are available, the most commonly used being the glyceraldehyde-3-phosphate dehydrogenase promoter (PGAP) for constitutive production and the alcohol oxidase 1 promoter (PAOX1) for inducible methanoldependent production. Both systems have their drawbacks, methanol as a substrate and PGAP as a noninducible promoter (Kovar et al 2010; Mellitzer et al 2014). Systems are sought in which production can be regulated without using methanol induction (Hartner et al 2008; Prielhofer et al 2013; Stadlmayr et al 2010; Vogl and Glieder 2013; Vogl et al 2016). Recombinant protein production can be repressed during batch phase with excess glycerol, and recombinant gene expression can be initiated during substrate-limited fedbatch cultivation with glucose (Prielhofer et al 2013)

Methods
Results
Conclusion

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.