Hiroshi Tsunekawa

Biotransformation of L -Lysine to L -Pipecolic Acid Catalyzed by L -Lysine 6-Aminotransferase and Pyrroline-5-carboxylate Reductase

The enzyme involved in the reduction of Δ 1-piperideine-6-carboxylate (P6C) to L-pipecolic acid (L-PA) has never been identified. We found that Escherichia coli JM109 transformed with the lat gene encoding L-lysine 6-aminotransferase (LAT) converted L-lysine (L-Lys) to L-PA. This suggested that there is a gene encoding “P6C reductase” that catalyzes the reduction of P6C to L-PA in the genome of E. coli. The complementation experiment of proC32 in E. coli RK4904 for L-PA production clearly shows that the expression of both lat and proC is essential for the biotransformation of L-Lys to L-PA. Further, We showed that both LAT and pyrroline-5-carboxylate (P5C) reductase, the product of proC, were needed to convert L-Lys to L-PA in vitro. These results demonstrate that P5C reductase catalyzes the reduction of P6C to L-PA. Biotransformation of L-Lys to L-PA using lat-expressing E. coli BL21 was done and L-PA was accumulated in the medium to reach at an amount of 3.9 g/l after 159 h of cultivation. It is noteworthy that the ee-value of the produced pipecolic acid was 100%.

Insight into functional diversity of cytochrome P450 in the white-rot basidiomycete Phanerochaete chrysosporium: involvement of versatile monooxygenase.

To elucidate functional diversity of cytochrome P450 monooxygenases from the white-rot basidiomycete Phanerochaete chrysosporium (PcCYPs), we conducted a comprehensive functional screening using a wide variety of compounds. A functionomic survey resulted in characterization of novel PcCYP functions and discovery of versatile PcCYPs that exhibit broad substrate profiles. These results suggested that multifunctional properties of the versatile PcCYPs would play crucial roles in diversification of fungal metabolic systems involved in xenobiotic detoxification. To our knowledge, this is the first report describing multifunctional properties of versatile P450s from the fungal kingdom. An increased compilation of PcCYP functions will facilitate a thorough understanding of metabolic diversity in basidiomycetes and provide new insights that could also expedite practical applications in the biotechnology sector.

Hyper-production of l-trytophan via fermentation with crystallization

A stable and fast l-tryptophan producer, AGX1757, was isolated from Escherichia coli W3110 trpAE1 trpR tnaA, which carried pSC101-trpI15·14. Cells of AGX1757 did not lose the composite plasmid during fermentation. Whenever a fed-batch culture of AGX1757 attained an l-tryptophan concentration of about 30 g/l, indole began to appear in the broth. The emergence of indole was caused by inhibition of tryptophan synthase due to accumulated l-tryptophan. Hence, the production rate of l-tryptophan sharply decreased. A higher solubility of l-tryptophan in the supernatant of culture broth (about 32 g/l) than that in the initial medium (about 22 g/l) was attributed to some unknown interaction between l-tryptophan and certain macromolecular material(s) coming from the bacterial cells. An addition of non-ionic detergents into the supernatant was effective for decreasing the solubility of l-tryptophan, hence causing crystallization of l-tryptophan. Pluronic L-61 was supplied from outside to an extent of 0.5% in terms of wt% concentration at around 45 h of fermentation when the l-tryptophan accumulated reached about 25 g/l. This addition actually caused crystallization of l-tryptophan and, as a result, the inhibitory effect of tryptophan synthase by l-tryptophan accumulated in the broth could be alleviated. Thus far, further fermentation became possible. l-Tryptophan of more than 50 g/l was finally produced by feeding solutions of both glucose and anthranilic acid.

Increase in the Rate of L -Pipecolic Acid Production Using lat-Expressing Escherichia coli by lysP and yeiE Amplification

Biotransformation of L-lysine (L-Lys) to L-pipecolic acid (L-PA) using lat-expressing Escherichia coli has been reported (Fujii et al., Biosci. Biotechnol. Biochem., 66, 622-627 (2002)). The rate-limiting step of this biotransformation seemes to be the transport of L-Lys into cells. To improve the L-PA production rate, we attempted to increase the rate of L-Lys uptake. E. coli BL21 carrying a plasmid with lat and lysP (pRH125) caused a 5-fold increase in the rate of L-PA production above the level of cells carrying a plasmid with lat (pRH124). Moreover, E. coli BL21 carrying a plasmid with lat, lysP, and yeiE (pRH127) caused a 6.4-fold increase in the rate of L-PA production above the level of cells carrying pRH124. Our results from RT-PCR experiments and the sequence similarity of YeiE to LysR transcriptional regulators suggest the possibility that yeiE expression induces lysP expression. The amplification of lysP, or rather both lysP and yeiE, increases the rate of L-PA production using lat-expressing E. coli.

Optimization of Tylosin Feeding Rate Profile in Production of Acetyl-Isovaleryl Tylosin(AIV) from Tylosin by Streptomyces thermotolerans YN554.

An optimal feed rate profile of a substrate (tylosin) for a novel antibiotic, acetyl-isovaleryl tylosin (AIV) production process was investigated. In the first step of optimization, a kinetic model for production of AIV from tylosin by Streptomyces thermotolerans was established properly using the least square method, followed by the confirmation that the proposed model could be used to predict the production process of AIV from tylosin. An objective function, state equations and an inequality constraint with respect to the tylosin feeding rate profile were applied to maximize the amount of AIV produced from tylosin in a fed-batch culture. The optimized tylosin feeding rate profile was determined using a direct iterative search algorithm based on the modified complex method. The simulation of AIV production at the optimal tylosin feeding profile indicates that the final amount of AIV is expected to be about 30% higher than that at the conventional constant tylosin feeding rate, which was also confirmed experimentally using a 30-l jar fermentor.