Literature DB >> 10861391

Influence of scale-up on the quality of recombinant human growth hormone.

F Bylund1, A Castan, R Mikkola, A Veide, G Larsson.   

Abstract

The aerobic fed-batch production of recombinant human growth hormone (rhGH) by Escherichia coli was studied. The goal was to determine the production and protein degradation pattern of this product during fed-batch cultivation and to what extent scale differences depend on the presence of a fed-batch glucose feed zone. Results of laboratory bench-scale, scale-down (SDR), and industrial pilot-scale (3-m(3)) reactor production were compared. In addition to the parameters of product yield and quality, also cell yield, respiration, overflow, mixed acid fermentation, glucose concentration, and cell lysis were studied and compared. The results show that oxygen limitation following glucose overflow was the critical parameter and not the glucose overflow itself. This was verified by the pattern of byproduct formation where formate was the dominating factor and not acetic acid. A correlation between the accumulation of formate, the degree of heterogeneity, and cell lysis was also visualized when recombinant protein was expressed. The production pattern could be mimicked in the SDR reactor for all parameters, except for product quantity and quality, where 30% fewer rhGH-degraded forms were present and where about 80% higher total yield was achieved, resulting in 10% greater accumulation of properly formed rhGH monomer. Copyright 2000 John Wiley & Sons, Inc.

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Year:  2000        PMID: 10861391     DOI: 10.1002/(sici)1097-0290(20000720)69:2<119::aid-bit1>3.0.co;2-9

Source DB:  PubMed          Journal:  Biotechnol Bioeng        ISSN: 0006-3592            Impact factor:   4.530


  8 in total

Review 1.  Living with heterogeneities in bioreactors: understanding the effects of environmental gradients on cells.

Authors:  Alvaro R Lara; Enrique Galindo; Octavio T Ramírez; Laura A Palomares
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2.  Recombinant protein production in an Escherichia coli reduced genome strain.

Authors:  Shamik S Sharma; Frederick R Blattner; Sarah W Harcum
Journal:  Metab Eng       Date:  2006-10-21       Impact factor: 9.783

3.  Influence of bioreactor hydraulic characteristics on a Saccharomyces cerevisiae fed-batch culture: hydrodynamic modelling and scale-down investigations.

Authors:  Annick Lejeune; F Delvigne; P Thonart
Journal:  J Ind Microbiol Biotechnol       Date:  2009-04-07       Impact factor: 3.346

4.  Escherichia coli metabolism under short-term repetitive substrate dynamics: adaptation and trade-offs.

Authors:  Eleni Vasilakou; Mark C M van Loosdrecht; S Aljoscha Wahl
Journal:  Microb Cell Fact       Date:  2020-05-29       Impact factor: 5.328

Review 5.  Bioprocess engineering issues that would be faced in producing a DNA vaccine at up to 100 m3 fermentation scale for an influenza pandemic.

Authors:  Mike Hoare; M Susana Levy; Daniel G Bracewell; Steven D Doig; Simyee Kong; Nigel Titchener-Hooker; John M Ward; Peter Dunnill
Journal:  Biotechnol Prog       Date:  2005 Nov-Dec

6.  Development of a miniature bioreactor model to study the impact of pH and DOT fluctuations on CHO cell culture performance as a tool to understanding heterogeneity effects at large-scale.

Authors:  Roman Zakrzewski; Kenneth Lee; Gary J Lye
Journal:  Biotechnol Prog       Date:  2022-05-07

7.  High cell density media for Escherichia coli are generally designed for aerobic cultivations - consequences for large-scale bioprocesses and shake flask cultures.

Authors:  Jaakko Soini; Kaisa Ukkonen; Peter Neubauer
Journal:  Microb Cell Fact       Date:  2008-08-07       Impact factor: 5.328

Review 8.  Biofuel production: an odyssey from metabolic engineering to fermentation scale-up.

Authors:  Whitney Hollinshead; Lian He; Yinjie J Tang
Journal:  Front Microbiol       Date:  2014-07-09       Impact factor: 5.640

  8 in total

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