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      Real-time estimation of biomass and specific growth rate in physiologically variable recombinant fed-batch processes

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          Abstract

          The real-time measurement of biomass has been addressed since many years. The quantification of biomass in the induction phase of a recombinant bioprocess is not straight forward, since biological burden, caused by protein expression, can have a significant impact on the cell morphology and physiology. This variability potentially leads to poor generalization of the biomass estimation, hence is a very important issue in the dynamic field of process development with frequently changing processes and producer lines. We want to present a method to quantify “biomass” in real-time which avoids off-line sampling and the need for representative training data sets. This generally applicable soft-sensor, based on first principles, was used for the quantification of biomass in induced recombinant fed-batch processes. Results were compared with “state of the art” methods to estimate the biomass concentration and the specific growth rate µ. Gross errors such as wrong stoichiometric assumptions or sensor failure were detected automatically. This method allows for variable model coefficients such as yields in contrast to other process models, hence does not require prior experiments. It can be easily adapted to a different growth stoichiometry; hence the method provides good generalization, also for induced culture mode. This approach estimates the biomass (or anabolic bioconversion) in induced fed-batch cultures in real-time and provides this key variable for process development for control purposes.

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          Data-driven Soft Sensors in the process industry

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            Metabolic load and heterologous gene expression.

            The expression of a foreign protein(s) in a recombinant host cell or organism often utilizes a significant amount of the host cell's resources, removing those resources away from host cell metabolism and placing a metabolic load (metabolic drain, metabolic burden) on the host. As a consequence of the imposed metabolic load, the biochemistry and physiology of the host may be dramatically altered. The numerous physiological changes that may occur often lowers the amount of the target foreign protein that is produced and eventually recovered from the recombinant organism. In this review the physiological changes to host cells, the causes of the phenomenon of metabolic load, and several strategies to avoid some of the problems associated with metabolic load are elaborated and discussed.
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              High-cell-density fermentation for production of L-N-carbamoylase using an expression system based on the Escherichia coli rhaBAD promoter.

              A high-cell-density fed-batch fermentation for the production of heterologous proteins in Escherichia coli was developed using the positively regulated Escherichia coli rhaBAD promoter. The expression system was improved by reducing of the amount of expensive L-rhamnose necessary for induction of the rhamnose promoter and by increasing the vector stability. Consumption of the inducer L-rhamnose was inhibited by inactivation of L-rhamnulose kinase encoding gene rhaB of Escherichia coli W3110, responsible for the first irreversible step in rhamnose catabolism. Plasmid instability caused by multimerization of the expression vector in the recombination-proficient W3110 was prevented by insertion of the multimer resolution site cer from the ColE1 plasmid into the vector. Fermentation experiments with the optimized system resulted in the production of 100 g x L(-1) cell dry weight and 3.8 g x L(-1) of recombinant L-N-carbamoylase, an enzyme, which is needed for the production of enantiomeric pure amino acids in a two-step reaction from hydantoins. Copyright 2001 John Wiley & Sons, Inc.
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                Author and article information

                Contributors
                pwechsel@mail.tuwien.ac.at
                +43-1-58801166400 , christoph.herwig@tuwien.ac.at
                Journal
                Bioprocess Biosyst Eng
                Bioprocess Biosyst Eng
                Bioprocess and Biosystems Engineering
                Springer Berlin Heidelberg (Berlin/Heidelberg )
                1615-7591
                1615-7605
                23 November 2012
                23 November 2012
                2013
                : 36
                : 1205-1218
                Affiliations
                Research Area Biochemical Engineering, Institute of Chemical Engineering, Vienna University of Technology, Gumpendorfer Straße 1a, 1060 Vienna, Austria
                Article
                848
                10.1007/s00449-012-0848-4
                3755222
                23178981
                d1a133bb-ec02-4b40-88f1-b51cee4c68b7
                © The Author(s) 2012
                History
                : 20 September 2012
                : 2 October 2012
                Categories
                Original Paper
                Custom metadata
                © Springer-Verlag Berlin Heidelberg 2013

                Biomedical engineering
                recombinant protein production,process model,soft sensor,real-time biomass quantification,process analytical technology (pat)

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