Literature DB >> 22100433

Glucose-limited high cell density cultivations from small to pilot plant scale using an enzyme-controlled glucose delivery system.

Julia Glazyrina1, Mirja Krause, Stefan Junne, Florian Glauche, Dirk Storm, Dirk Strom, Peter Neubauer.   

Abstract

The enzyme controlled substrate delivery cultivation technology EnBase(®) Flo allows a fed-batch-like growth in batch cultures. It has been previously shown that this technology can be applied in small cultivation vessels such as micro- and deep well plates and also shake flasks. In these scales high cell densities and improved protein production for Escherichia coli cultures were demonstrated. This current study aims to evaluate the scalability of the controlled glucose release technique to pilot scale bioreactors. Throughout all scales, that is, deep well plates, 3 L bioreactor and 150 L bioreactor cultivations, the growth was very similar and the model protein, a recombinant alcohol dehydrogenase (ADH) was produced with a high yield in soluble form. Moreover, EnBase Flo also was successfully used as a controlled starter culture in high cell density fed-batch cultivations with external glucose feeding. Here the external feeding pump was started after overnight cultivation with EnBase Flo. Final optical densities in these cultivations reached 120 (corresponding to about 40 g L(-1) dry cell weight) and a high expression level of ADH was obtained. The EnBase cultivation technology ensures a controlled initial cultivation under fed-batch mode without the need for a feeding pump. Because of the linear cell growth under glucose limitation it provides optimal and robust starting conditions for traditional external feed-based processes.
Copyright © 2011 Elsevier B.V. All rights reserved.

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Year:  2011        PMID: 22100433     DOI: 10.1016/j.nbt.2011.11.004

Source DB:  PubMed          Journal:  N Biotechnol        ISSN: 1871-6784            Impact factor:   5.079


  12 in total

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Journal:  N Biotechnol       Date:  2018-10-29       Impact factor: 6.490

4.  Scale-up bioprocess development for production of the antibiotic valinomycin in Escherichia coli based on consistent fed-batch cultivations.

Authors:  Jian Li; Jennifer Jaitzig; Ping Lu; Roderich D Süssmuth; Peter Neubauer
Journal:  Microb Cell Fact       Date:  2015-06-12       Impact factor: 5.328

5.  Generic Protocol for Optimization of Heterologous Protein Production Using Automated Microbioreactor Technology.

Authors:  Johannes Hemmerich; Lars Freier; Wolfgang Wiechert; Eric von Lieres; Marco Oldiges
Journal:  J Vis Exp       Date:  2017-12-15       Impact factor: 1.355

6.  Effect of culture medium, host strain and oxygen transfer on recombinant Fab antibody fragment yield and leakage to medium in shaken E. coli cultures.

Authors:  Kaisa Ukkonen; Johanna Veijola; Antti Vasala; Peter Neubauer
Journal:  Microb Cell Fact       Date:  2013-07-29       Impact factor: 5.328

7.  Parallel use of shake flask and microtiter plate online measuring devices (RAMOS and BioLector) reduces the number of experiments in laboratory-scale stirred tank bioreactors.

Authors:  S J Wewetzer; M Kunze; T Ladner; B Luchterhand; S Roth; N Rahmen; R Kloß; A Costa E Silva; L Regestein; J Büchs
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Review 8.  Lanthipeptides: chemical synthesis versus in vivo biosynthesis as tools for pharmaceutical production.

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Journal:  Microb Cell Fact       Date:  2016-06-07       Impact factor: 5.328

9.  High-level fed-batch fermentative expression of an engineered Staphylococcal protein A based ligand in E. coli: purification and characterization.

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Review 10.  The fed-batch principle for the molecular biology lab: controlled nutrient diets in ready-made media improve production of recombinant proteins in Escherichia coli.

Authors:  Mirja Krause; Antje Neubauer; Peter Neubauer
Journal:  Microb Cell Fact       Date:  2016-06-17       Impact factor: 5.328

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