Toward intensifying design of experiments in upstream bioprocess development: An industrial Escherichia coli feasibility study |
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| Authors: | Moritz von Stosch Jan‐Martijn Hamelink Rui Oliveira |
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| Affiliation: | 1. CEAM, Faculty of Science, Agriculture and Engineering, Newcastle University, Newcastle upon Tyne, UK;2. REQUIMTE/DQ, Faculty of Science and Technology, University Nova De Lisboa, Caparica, Portugal;3. GSK Vaccines, Laval, Canada;4. Lallemand Inc., Montreal, Canada |
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| Abstract: | In this study, step variations in temperature, pH, and carbon substrate feeding rate were performed within five high cell density Escherichia coli fermentations to assess whether intraexperiment step changes, can principally be used to exploit the process operation space in a design of experiment manner. A dynamic process modeling approach was adopted to determine parameter interactions. A bioreactor model was integrated with an artificial neural network that describes biomass and product formation rates as function of varied fed‐batch fermentation conditions for heterologous protein production. A model reliability measure was introduced to assess in which process region the model can be expected to predict process states accurately. It was found that the model could accurately predict process states of multiple fermentations performed at fixed conditions within the determined validity domain. The results suggest that intraexperimental variations of process conditions could be used to reduce the number of experiments by a factor, which in limit would be equivalent to the number of intraexperimental variations per experiment. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1343–1352, 2016 |
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| Keywords: | PAT QbD upstream bioprocess development/optimization intensified design of experiments hybrid modeling dynamic excitations |
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