Literature DB >> 18623028

Use of respiratory quotient as a control parameter for optimum oxygen supply and scale-up of 2,3-butanediol production under microaerobic conditions.

A P Zeng1, T G Byun, C Posten, W D Deckwer.   

Abstract

The respiratory quotient (RQ) was found to be a suitable control parameter for optimum oxygen supply for the production of 2,3-butanediol + acetoin under microaerobic conditions. In laboratory scale continuous cultures optimum production of 2,3-butanediol + acetoin was obtained at an RQ value between 4.0 to 4.5. This agreed well with optimum RQ value (4.0) stoichiometrically derived from the bioreactions involved. In fed-batch cultures product concentrations as high as 102.9 g/L (96.0 g/L butanediol + 6.9 g/L acetoin) can be achieved within 32 h cultivation with an RQ control algorithm for oxygen supply. Under similar conditions only 85.7 g/L product (77.6 g/L butanediol + 8.1 g/L acetoin) was obtained with control of constant oxygen supply rate throughout the cultivation.In pilot scale batch cultures under identical oxygen supply rate the achievable RQ value was found to be strongly influenced by the reactor type and scale. The initial oxygen supply rate influenced the achievable RQ as well. However, in all the reactors studied the specific product formation rate of cells in the exponential growth phase was only a function of RQ. The same optimum RQ value as found in continuous cultures was obtained. It was thus concluded that RQ can be used as a control parameter for optimum production of 2,3-butanediol + acetoin in both laboratory and pilot plant scale reactors.

Entities:  

Year:  1994        PMID: 18623028     DOI: 10.1002/bit.260440912

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


  10 in total

1.  Estimation of rates of oxygen uptake and carbon dioxide evolution of animal cell culture using material and energy balances.

Authors:  Z L Xiu; W D Deckwer; A P Zeng
Journal:  Cytotechnology       Date:  1999-05       Impact factor: 2.058

Review 2.  Microbial production of 2,3-butanediol for industrial applications.

Authors:  Chan Woo Song; Jong Myoung Park; Sang Chul Chung; Sang Yup Lee; Hyohak Song
Journal:  J Ind Microbiol Biotechnol       Date:  2019-08-29       Impact factor: 3.346

3.  Optimization and scale-up of 2,3-butanediol production by Bacillus amyloliquefaciens B10-127.

Authors:  Taowei Yang; Xian Zhang; Zhiming Rao; Shenghui Gu; Haifeng Xia; Zhenghong Xu
Journal:  World J Microbiol Biotechnol       Date:  2011-11-26       Impact factor: 3.312

4.  Oxygen transfer rate during the production of alginate by Azotobacter vinelandii under oxygen-limited and non oxygen-limited conditions.

Authors:  Esteban Lozano; Enrique Galindo; Carlos F Peña
Journal:  Microb Cell Fact       Date:  2011-02-27       Impact factor: 5.328

5.  Production of Poly-3-Hydroxybutyrate (P3HB) with Ultra-High Molecular Weight (UHMW) by Mutant Strains of Azotobacter vinelandii Under Microaerophilic Conditions.

Authors:  Elsa Gómez-Hernández; Holjes Salgado-Lugo; Daniel Segura; Andrés García; Alvaro Díaz-Barrera; Carlos Peña
Journal:  Appl Biochem Biotechnol       Date:  2020-08-19       Impact factor: 2.926

6.  Enhanced 2,3-butanediol production from biodiesel-derived glycerol by engineering of cofactor regeneration and manipulating carbon flux in Bacillus amyloliquefaciens.

Authors:  Taowei Yang; Zhiming Rao; Xian Zhang; Meijuan Xu; Zhenghong Xu; Shang-Tian Yang
Journal:  Microb Cell Fact       Date:  2015-08-22       Impact factor: 5.328

7.  Metabolic flux analysis and the NAD(P)H/NAD(P)+ ratios in chemostat cultures of Azotobacter vinelandii.

Authors:  Andres García; Pau Ferrer; Joan Albiol; Tania Castillo; Daniel Segura; Carlos Peña
Journal:  Microb Cell Fact       Date:  2018-01-22       Impact factor: 5.328

8.  Effect of oxygen mass transfer rate on the production of 2,3-butanediol from glucose and agro-industrial byproducts by Bacillus licheniformis ATCC9789.

Authors:  Stefano Rebecchi; Davide Pinelli; Giulio Zanaroli; Fabio Fava; Dario Frascari
Journal:  Biotechnol Biofuels       Date:  2018-05-23       Impact factor: 6.040

9.  Shake flask methodology for assessing the influence of the maximum oxygen transfer capacity on 2,3-butanediol production.

Authors:  Benedikt Heyman; Robin Lamm; Hannah Tulke; Lars Regestein; Jochen Büchs
Journal:  Microb Cell Fact       Date:  2019-05-03       Impact factor: 5.328

10.  Model-assisted DoE software: optimization of growth and biocatalysis in Saccharomyces cerevisiae bioprocesses.

Authors:  André Moser; Kim B Kuchemüller; Sahar Deppe; Tanja Hernández Rodríguez; Björn Frahm; Ralf Pörtner; Volker C Hass; Johannes Möller
Journal:  Bioprocess Biosyst Eng       Date:  2021-01-20       Impact factor: 3.210

  10 in total

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