Fed-batch culture of Escherichia coli for L-valine production based on in silico flux response analysis |
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Authors: | Park Jin Hwan Kim Tae Yong Lee Kwang Ho Lee Sang Yup |
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Institution: | Metabolic and Biomolecular Engineering National Research Laboratory, Department of Chemical and Biomolecular Engineering, BK21 Program, KAIST, Daejeon 305-701, Republic of Korea. |
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Abstract: | We have previously reported the development of a 100% genetically defined engineered Escherichia coli strain capable of producing L ‐valine from glucose with a high yield of 0.38 g L ‐valine per gram glucose (0.58 mol L ‐valine per mol glucose) by batch culture. Here we report a systems biological strategy of employing flux response analysis in bioprocess development using L ‐valine production by fed‐batch culture as an example. Through the systems‐level analysis, the source of ATP was found to be important for efficient L ‐valine production. There existed a trade‐off between L ‐valine production and biomass formation, which was optimized for the most efficient L ‐valine production. Furthermore, acetic acid feeding strategy was optimized based on flux response analysis. The final fed‐batch cultivation strategy allowed production of 32.3 g/L L ‐valine, the highest concentration reported for E. coli. This approach of employing systems‐level analysis of metabolic fluxes in developing fed‐batch cultivation strategy would also be applicable in developing strategies for the efficient production of other bioproducts. Biotechnol. Bioeng. 2011; 108:934–946. © 2010 Wiley Periodicals, Inc. |
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Keywords: | L‐valine fed‐batch culture in silico flux response analysis systems metabolic engineering |
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