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One of the major challenges in metabolic engineering for enhanced synthesis of value-addedchemicals is to design and develop new strains that can be translated into well-controlledfermentation processes using bioreactors. The aim of this study was to assess the influence ofvarious fed-batch strategies in the performance of metabolically engineered Pseudomonasputida strains, Δgcd and Δgcd-pgl, for improving production of medium-chain-length polyhydroxyalkanoates(mcl-PHAs) using glucose as the only carbon source. First we developed afed-batch process that comprised an initial phase of biomass accumulation based on anexponential feeding carbon-limited strategy. For the mcl-PHA accumulation stage, threeinduction techniques were tested under nitrogen limitation. The substrate-pulse feeding wasmore efficient than the constant-feeding approach to promote the accumulation of thedesirable product. Nonetheless, the most efficient approach for maximum PHA synthesis wasthe application of a dissolved-oxygen-stat feeding strategy (DO-stat), where P. putida Δgcdmutant strain showed a final PHA content and specific PHA productivity of 67% and0.83 g·l-1·h-1, respectively. To our knowledge, this mcl-PHA titer is the highest value that hasbeen ever reported using glucose as the sole carbon and energy source. Our results alsohighlighted the effect of different fed-batch strategies upon the extent of realization of theintended metabolic modification of the mutant strains.

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