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Model-assisted DoE software: optimization of growth and biocatalysis in Saccharomyces cerevisiae bioprocesses.
Moser, André; Kuchemüller, Kim B; Deppe, Sahar; Hernández Rodríguez, Tanja; Frahm, Björn; Pörtner, Ralf; Hass, Volker C; Möller, Johannes.
Affiliation
  • Moser A; Faculty of Medical and Life Sciences, Furtwangen University of Applied Sciences, Villingen-Schwenningen, Germany.
  • Kuchemüller KB; Institute of Bioprocess and Biosystems Engineering, Hamburg University of Technology, Hamburg, Germany.
  • Deppe S; Biotechnology and Bioprocess Engineering, Ostwestfalen-Lippe University of Applied Sciences and Arts, Lemgo, Germany.
  • Hernández Rodríguez T; Biotechnology and Bioprocess Engineering, Ostwestfalen-Lippe University of Applied Sciences and Arts, Lemgo, Germany.
  • Frahm B; Biotechnology and Bioprocess Engineering, Ostwestfalen-Lippe University of Applied Sciences and Arts, Lemgo, Germany.
  • Pörtner R; Institute of Bioprocess and Biosystems Engineering, Hamburg University of Technology, Hamburg, Germany.
  • Hass VC; Faculty of Medical and Life Sciences, Furtwangen University of Applied Sciences, Villingen-Schwenningen, Germany.
  • Möller J; Institute of Bioprocess and Biosystems Engineering, Hamburg University of Technology, Hamburg, Germany. johannes.moeller@tuhh.de.
Bioprocess Biosyst Eng ; 44(4): 683-700, 2021 Apr.
Article in En | MEDLINE | ID: mdl-33471162
Bioprocess development and optimization are still cost- and time-intensive due to the enormous number of experiments involved. In this study, the recently introduced model-assisted Design of Experiments (mDoE) concept (Möller et al. in Bioproc Biosyst Eng 42(5):867, https://doi.org/10.1007/s00449-019-02089-7 , 2019) was extended and implemented into a software ("mDoE-toolbox") to significantly reduce the number of required cultivations. The application of the toolbox is exemplary shown in two case studies with Saccharomyces cerevisiae. In the first case study, a fed-batch process was optimized with respect to the pH value and linearly rising feeding rates of glucose and nitrogen source. Using the mDoE-toolbox, the biomass concentration was increased by 30% compared to previously performed experiments. The second case study was the whole-cell biocatalysis of ethyl acetoacetate (EAA) to (S)-ethyl-3-hydroxybutyrate (E3HB), for which the feeding rates of glucose, nitrogen source, and EAA were optimized. An increase of 80% compared to a previously performed experiment with similar initial conditions was achieved for the E3HB concentration.
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Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Saccharomyces cerevisiae / Industrial Microbiology / Batch Cell Culture Techniques Type of study: Health_economic_evaluation Language: En Journal: Bioprocess Biosyst Eng Journal subject: BIOTECNOLOGIA / ENGENHARIA BIOMEDICA Year: 2021 Type: Article Affiliation country: Germany

Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Saccharomyces cerevisiae / Industrial Microbiology / Batch Cell Culture Techniques Type of study: Health_economic_evaluation Language: En Journal: Bioprocess Biosyst Eng Journal subject: BIOTECNOLOGIA / ENGENHARIA BIOMEDICA Year: 2021 Type: Article Affiliation country: Germany