Bioreactor Retrofitting to Avoid Aeration with Oxygen in Pichia Pastoris Cultivation Processes for Recombinant Protein Production

It is demonstrated that bioreactor construction is of practical importance to some recombinant protein production processes. Here we focus on a case where the oxygen mass transfer capability of the bioreactor depicts a limitation to productivity that must be overcome by technical measures. Choosing different impellers can significantly enhance the mass transfer capability of the bioreactor. This is shown through the concrete example of cultivation of Pichia pastoris on methanol. In order to operate the bioreactor at biomass concentrations larger than 150 g kg −1 and specific growth rates larger than 0.03 h −1 , it is usually necessary to supplement the aeration with molecular oxygen. When, however, as is shown here, the standard Rushton turbines in the bioreactor are replaced by a set of lower power number impellers with improved air handling capabilities it is possible to operate the reactor at even more demanding growth and biomass conditions without additional oxygen while achieving even higher productivities. Here we took a combination of two hollow blades and a single hydrofoil impeller in order to enhance the mass transfer rates. Its advantage is shown at the 10-litre laboratory-scale with a Pichia pastoris culture that produces the recombinant protein dipeptidylpeptidase IV. The enzyme serves as a target for the development of specific inhibitors to control blood glucose homeostasis. Optimization of the fermentation process and higher enzyme yields allow inhibitor evaluation and co-crystallization studies.

[1]  William C. Raschke,et al.  Recent Advances in the Expression of Foreign Genes in Pichia pastoris , 1993, Bio/Technology.

[2]  A. Daugulis,et al.  Sorbitol as a non-repressing carbon source for fed-batch fermentation of recombinant Pichia pastoris , 1999, Biotechnology Letters.

[3]  R. Takors,et al.  Human Chymotrypsinogen B Production with Pichiapastoris by Integrated Development of Fermentation and Downstream Processing. Part 1. Fermentation , 2001, Biotechnology progress.

[4]  T. Hoffmann,et al.  Characterisation of Human Dipeptidyl Peptidase IV Expressed in Pichia pastoris. A Structural and Mechanistic Comparison between the Recombinant Human and the Purified Porcine Enzyme , 2003, Biological chemistry.

[5]  Alvin W. Nienow,et al.  Gas-liquid mixing studies : A comparison of Rushton turbines with some modern impellers , 1996 .

[6]  G. Fischer,et al.  The conformation around the peptide bond between the P1- and P2-positions is important for catalytic activity of some proline-specific proteases. , 1983, Biochimica et biophysica acta.

[7]  T. Egli,et al.  Simultaneous utilization of methanol–glucose mixtures by Hansenula polymorpha in chemostat: Influence of dilution rate and mixture composition on utilization pattern , 1986, Biotechnology and bioengineering.

[8]  H. Demuth,et al.  Reactions between dipeptidyl peptidase IV and diacyl hydroxylamines: mechanistic investigations. , 1989, Journal of enzyme inhibition.

[9]  Methods and Instruments in Fermentation Gas Analysis , 2001 .

[10]  A. W. Nienow,et al.  Gas dispersion performance in fermenter operation , 1990 .

[11]  K. Schneider,et al.  Use of a silicone tubing sensor to control methanol concentration during fed batch fermentation of Pichia pastoris , 1997 .

[12]  A W Nienow,et al.  A fluid dynamic study of the retrofitting of large agitated bioreactors: Turbulent flow , 1994, Biotechnology and bioengineering.

[13]  Amanullah,et al.  The influence of impeller type in pilot scale xanthan fermentations , 1998, Biotechnology and bioengineering.

[14]  M. Moo-young,et al.  The continuous phase heat and mass transfer properties of dispersions , 1961 .

[15]  S. J. Pirt,et al.  Principles of microbe and cell cultivation , 1975 .

[16]  K. Riet,et al.  Review of Measuring Methods and Results in Nonviscous Gas-Liquid Mass Transfer in Stirred Vessels , 1979 .

[17]  Alvin W. Nienow,et al.  POWER, GAS DISPERSION AND HOMOGENISATION CHARACTERISTICS OF SCABA SRGT AND RUSHTON TURBINE IMPELLERS , 1992 .

[18]  Wenhui Zhang,et al.  Improved Production of Recombinant Ovine Interferon‐τ by Mut+ Strain of Pichiapastoris Using an Optimized Methanol Feed Profile , 2003, Biotechnology progress.

[19]  G. Fischer,et al.  [Catalytic mechanism of dipeptidyl-peptidase IV]. , 1978, Acta biologica et medica Germanica.