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Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
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Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
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Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli

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Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli
Journal Article

Production of p-amino-l-phenylalanine (l-PAPA) from glycerol by metabolic grafting of Escherichia coli

2018
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Overview
Background The non-proteinogenic aromatic amino acid, p -amino- l -phenylalanine ( l -PAPA) is a high-value product with a broad field of applications. In nature, l -PAPA occurs as an intermediate of the chloramphenicol biosynthesis pathway in Streptomyces venezuelae . Here we demonstrate that the model organism Escherichia coli can be transformed with metabolic grafting approaches to result in an improved l -PAPA producing strain. Results Escherichia coli K-12 cells were genetically engineered for the production of l -PAPA from glycerol as main carbon source. To do so, genes for a 4-amino-4-deoxychorismate synthase ( pabAB from Corynebacterium glutamicum ), and genes encoding a 4-amino-4-deoxychorismate mutase and a 4-amino-4-deoxyprephenate dehydrogenase ( papB and papC , both from Streptomyces venezuelae ) were cloned and expressed in E. coli W3110 (lab strain LJ110). In shake flask cultures with minimal medium this led to the formation of ca. 43 ± 2 mg l −1 of l -PAPA from 5 g l −1 glycerol. By expression of additional chromosomal copies of the tktA and glpX genes, and of plasmid-borne aroFBL genes in a tyrR deletion strain, an improved l -PAPA producer was obtained which gave a titer of 5.47 ± 0.4 g l −1 l -PAPA from 33.3 g l −1 glycerol (0.16 g l -PAPA/g of glycerol) in fed-batch cultivation (shake flasks). Finally, in a fed-batch fermenter cultivation, a titer of 16.7 g l −1 l -PAPA was obtained which is the highest so far reported value for this non-proteinogenic amino acid. Conclusion Here we show that E. coli is a suitable chassis strain for l -PAPA production. Modifying the flux to the product and improved supply of precursor, by additional gene copies of glpX , tkt and aroFBL together with the deletion of the tyrR gene, increased the yield and titer.