Tripathi C K, Agarwal S C, Bihari V, Joshi A K, Basu S K
Fermentation Technology Division, Central Drug Research Institute, Lucknow, India.
Indian J Exp Biol. 1997 Aug;35(8):886-9.
Production of L-phenylacetylcarbinol (L-PAC) through biotransformation of benzaldehyde by free and immobilized cells of the yeast Saccharomyces cerevisiae has been attempted. L-PAC production was found to be maximum (0.4 microliter/ml) when anaerobically grown free cells were used as biocatalyst during aerobic biotransformation for two hours with magnetically stirred bioreactor. Growth under oxygen limited conditions led to accumulation of higher amount of pyruvate decarboxylase enzyme and co-substrate, pyruvate, resulting in higher L-PAC formation. L-PAC yield was low when biotransformations were carried out anaerobically either for aerobically or anaerobically grown free cells. Free cells were found to be more efficient biocatalyst for L-PAC production, as compared with the immobilized cells, with the investigated benzaldehyde concentration (0.3% v/v) and cell density (17.5% w/v). The study has explored and indicated the possibility of optimizing the yield of L-PAC by growing the yeast cells under oxygen limited condition for suitable aerobic mode of benzaldehyde biotransformation.
人们尝试通过酿酒酵母的游离细胞和固定化细胞对苯甲醛进行生物转化来生产L-苯基乙酰甲醇(L-PAC)。当在磁力搅拌的生物反应器中进行需氧生物转化两小时时,使用厌氧培养的游离细胞作为生物催化剂,L-PAC的产量最高(0.4微升/毫升)。在氧气受限条件下生长会导致丙酮酸脱羧酶和共底物丙酮酸积累量增加,从而使L-PAC的生成量更高。当对需氧或厌氧培养的游离细胞进行厌氧生物转化时,L-PAC的产量较低。在所研究的苯甲醛浓度(0.3% v/v)和细胞密度(17.5% w/v)下,发现游离细胞是生产L-PAC更有效的生物催化剂,与固定化细胞相比。该研究探索并表明了通过在氧气受限条件下培养酵母细胞以实现苯甲醛生物转化的合适需氧模式来优化L-PAC产量的可能性。