以葡萄糖为原料结合生物发酵与化学合成制备酮泛解酸

Ketopantoate production from glucose by combining biological and chemical steps

D-泛酸(维生素B5)是一种重要的维生素,在饲料、化妆品和制药行业均有广阔的市场。酮泛解酸是泛酸生物合成途径的中间体,易内酯化为酮基泛解酸内酯,后者可立体选择性地转化为D-泛解酸,并进一步用于D-泛酸的生产。本工作提供了一种采用α-酮基异戊酸与甲醛经羟醛反应合成酮泛解酸的新方法。其中,反应物α-酮基异戊酸可由葡萄糖原料经发酵法生产。结果表明,以葡萄糖为碳源,经克雷伯氏肺炎杆菌发酵能高水平生产D-泛酸生物合成途径的关键前体—α-酮基异戊酸。采用商品α-酮基异戊酸开发一种新型的酮泛解酸合成方法;分析合成反应机理,确定总反应级数为1.87;经条件优化确定酮泛解酸合成反应的最佳pH=13,最佳温度为45℃,此条件下酮泛解酸转化率达83.5%。调节酮泛解酸溶液pH至强酸性,有助于其内酯化合成酮基泛解酸内酯。之后采用前述优化的方法,由流加发酵制备的25.2 g/Lα-酮基异戊酸合成酮泛解酸19.9 g/L。最后通过异丁醇萃取、活性炭脱色、浓缩结晶方法进行产物提纯,调节酮基泛解酸内酯溶液pH在7~10范围内可使其开环转化回酮泛解酸。最终得到酮泛解酸及其内酯的纯品。本研究建立了以葡萄糖为原料通过α-酮基异戊酸中间体生产酮泛解酸的方法。该方法结合生物发酵和化学合成过程,采用廉价原料,具有绿色高效的特点,有望用于工业化生产泛酸。

D-pantothenic acid(vitamin B5)is an essential vitamin to animals and has large markets in the feed,cosmetics,and pharmaceutical industries.The biochemical role of D-pantothenic acid in all organisms is to form the core of the structure of coenzyme A.Biosynthesis of coenzyme A from pantothenate occurs in all organisms,while the synthesis of D-pantothenic acid is absent from animals.Thus D-pantothenic acid is an essential nutrient to animals.Ketopantoate is an intermediate of pantothenate biosynthesis pathway.Ketopantoate can be stereoselectivity converted to D-pantoic acid and further used for D-pantothenic acid production.However,the economic production of ketopantoate is a bottleneck of D-pantothenic acid production from ketopantoate.Hence,this study provided a novel method for synthesis of ketopantoate by aldol reaction ofα-ketoisovalerate and formaldehyde,andα-ketoisovalerate was produced from fermentation with glucose as the raw material.25.2 g/Lα-ketoisovalerate was produced by an engineering Klebsiella pneumoniae strain with glucose as the main carbon source.19.9 g/L Ketopantoate was synthesized from formaldehyde andα-ketoisovalerate by an aldol reaction at basic conditions.The reaction parameters of reaction were optimized and a conversion ratio of 83.5%was obtained at reaction conditions of pH 13 and 45℃.The ketopantoate in the solution was converted to ketopantoyl lactone at acidic conditions of pH<3.Ketopantoyl lactone was extracted to isobutanol with an extraction rate of 50.9%.The organic phase was decolourized,and ketopantoyl lactone crystal was obtained after concentration.Ketopantoyl lactone was converted back to ketopantoate in an aqueous solution in the pH range of 7~10,and ketopantoate crystal was obtained after concentration.Ketopantoate production from glucose viaα-ketoisovalerate as an intermediate was set up,which suggested a novel and competitive technical route to produce ketopantoate.The whole processes were combinated biological fermentation and chemical reactions and had a high conversion ratio.This method adopted renewable and cheap original materials rather than highly toxic raw materials.The optimal temperature of the reaction was 45℃,which was in mild conditions.Overall,a novel and promising method for ketopantoate and ketopantoyl lactone production was provided.