Accumulation of methylglyoxal in anaerobically grown Escherichia coli and its detoxification by expression of the Pseudomonas putida glyoxalase I gene.

Anaerobic glycerol fermentation by Escherichia coli strains expressing genes from the Klebsiella pneumoniae dha regulon showed that cell growth and 1,3-propanediol (1,3-PD) production are significantly inhibited when 5 g/L or higher of glycerol is initially present. One reason for this inhibition may be methylglyoxal (MG) accumulation. Assays of both intracellular and extracellular MG levels indicated an accumulation of MG in anaerobic glycerol fermentation of transgenic E. coli. Pseudomonas putida glyoxalase I was expressed in the transgenic E. coli to enhance MG detoxification. The activity of glyoxalase I in the transgenic E. coli with the P. putida glyoxalase I under anaerobic conditions was 12-fold higher than that in the control cells. Compared to the control cells, the transgenic cells with the P. putida glyoxalase I displayed a reduction of 35-43% in intracellular MG and a decrease of 30% in extracellular MG. These decreases were statistically significant (P>94). Furthermore, the expression of the P. putida glyoxalase I in the transgenic E. coli markedly improved cell growth and resulted in a 50% increase in 1,3-PD production.

Purification and characterization of a Bacillus licheniformis phosphatase specific for D-alpha-glycerophosphate.

Bacillus licheniformis ("Ford's type") was found to contain a novel enzyme, D-alpha-glycerophosphatase. The enzyme is highly specific for D-alpha-glycerophosphate, effecting little or no hydrolysis of L-alpha- or beta-glycerophosphate or other similar compounds. All other known alpha-glycerophosphatases preferentially hydrolyze the L isomer. The products of the D-alpha-glycerophosphatase reaction were identified as glycerol and inorganic phosphate. The enzyme is a monomer with an apparent molecular mass of approximately 25 kDa. As with most phosphatases, it requires divalent magnesium for activity, but unlike the nonspecific acid and alkaline phosphatases, its optimum pH is around neutral. Its K(m) for D-alpha-glycerophosphate in the presence of 1 mM Mg2+ was found to be 4.3 mM. D-alpha-glycerophosphatase was produced in B. licheniformis fermentations whether or not high levels of phosphate were present; the same was true of glycerol formation. D-alpha-glycerophosphatase is not strongly inhibited by inorganic phosphate and would therefore be capable of catalyzing the formation of glycerol in the presence of high levels of phosphate. The D-alpha-glycerophosphatase of B. licheniformis is similar in characteristics to L-alpha-glycerophosphatases known to synthesize glycerol in vivo, suggesting that D-alpha-glycerophosphatase may be the final enzyme in the fermentative glycerol formation pathway of B. licheniformis.

Construction and characterization of a 1,3-propanediol operon.

The genes for the production of 1,3-propanediol (1,3-PD) in Klebsiella pneumoniae, dhaB, which encodes glycerol dehydratase, and dhaT, which encodes 1,3-PD oxidoreductase, are naturally under the control of two different promoters and are transcribed in different directions. These genes were reconfigured into an operon containing dhaB followed by dhaT under the control of a single promoter. The operon contains unique restriction sites to facilitate replacement of the promoter and other modifications. In a fed-batch cofermentation of glycerol and glucose. Escherichia coli containing the operon consumed 9.3 g of glycerol per liter and produced 6.3 g of 1,3-PD per liter. The fermentation had two distinct phases. In the first phase, significant cell growth occurred and the products were mainly 1,3-PD and acetate. In the second phase, very little growth occurred and the main products were 1,3-PD and pyruvate. The first enzyme in the 1,3-PD pathway, glycerol dehydratase, requires coenzyme B12, which must be provided in E. coli fermentations. However, the amount of coenzyme B12 needed was quite small, with 10 nM sufficient for good 1,3-PD production in batch cofermentations. 1,3-PD is a useful intermediate in the production of polyesters. The 1,3-PD operon was designed so that it can be readily modified for expression in other prokaryotic hosts; therefore, it is useful for metabolic engineering of 1,3-PD pathways from glycerol and other substrates such as glucose.