Bioproduction of p-hydroxystyrene from glucose by the solvent-tolerant bacterium Pseudomonas putida S12 in a two-phase water-decanol fermentation.

Two solvent-tolerant Pseudomonas putida S12 strains, originally designed for phenol and p-coumarate production, were engineered for efficient production of p-hydroxystyrene from glucose. This was established by introduction of the genes pal and pdc encoding L-phenylalanine/L-tyrosine ammonia lyase and p-coumaric acid decarboxylase, respectively. These enzymes allow the conversion of the central metabolite L-tyrosine into p-hydroxystyrene, via p-coumarate. Degradation of the p-coumarate intermediate was prevented by inactivating the fcs gene encoding feruloyl-coenzyme A synthetase. The best-performing strain was selected and cultivated in the fed-batch mode, resulting in the formation of 4.5 mM p-hydroxystyrene at a yield of 6.7% (C-mol of p-hydroxystyrene per C-mol of glucose) and a maximum volumetric productivity of 0.4 mM h(-1). At this concentration, growth and production were completely halted due to the toxicity of p-hydroxystyrene. Product toxicity was overcome by the application of a second phase of 1-decanol to extract p-hydroxystyrene during fed-batch cultivation. This resulted in a twofold increase of the maximum volumetric productivity (0.75 mM h(-1)) and a final total p-hydroxystyrene concentration of 21 mM, which is a fourfold improvement compared to the single-phase fed-batch cultivation. The final concentration of p-hydroxystyrene in the water phase was 1.2 mM, while a concentration of 147 mM (17.6 g liter(-1)) was obtained in the 1-decanol phase. Thus, a P. putida S12 strain producing the low-value compound phenol was successfully altered for the production of the toxic value-added compound p-hydroxystyrene.

Optimization of the solvent-tolerant Pseudomonas putida S12 as host for the production of p-coumarate from glucose.

A Pseudomonas putida S12 strain was constructed that is able to convert glucose to p-coumarate via the central metabolite L: -tyrosine. Efficient production was hampered by product degradation, limited cellular L: -tyrosine availability, and formation of the by-product cinnamate via L: -phenylalanine. The production host was optimized by inactivation of fcs, the gene encoding the first enzyme in the p-coumarate degradation pathway in P. putida, followed by construction of a phenylalanine-auxotrophic mutant. These steps resulted in a P. putida S12 strain that showed dramatically enhanced production characteristics with controlled L: -phenylalanine feeding. During fed-batch cultivation, 10 mM (1.7 g l(-1)) of p-coumarate was produced from glucose with a yield of 3.8 Cmol% and a molar ratio of p-coumarate to cinnamate of 85:1.