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Production of Diacylglycerols Using Lipase-Catalyzed Esterification and Glycerolysis

机译:脂肪酶催化的酯化和甘油水解法生产二酰基甘油

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Diacylglycerols(DAG) was synthesized through esterification of caprylic acid andglycerol, as well as glycerolysis of medium-chain triacylglycerols(GTCC), catalyzed by lipaseNovozym 435 (from Candida Antarctica), respectively. A comparative study of the esterificationwas conducted in a batch reactor and a packed bed reactor, respectively. The effect of reactionparameters, such as solvent, temperature, molar ratio of the reactants, water removal, enzymeloading and ratio of height to diameter of the reactor on the conversion of caprylic acid and theDAG content in the reaction mixture were studied. The conversion of caprylic acid and the contentof DAG esterification in the packed bed reactor reached 82.30% and 77.26%, respectively, by using200U /g caprylic acid at a space velocity of 34h~(-1), 60°C in 7h; while the esterification in the batchreactor present a caprylic acid conversion of 83.91% and a DAG content of 68.24% with 50U /gcaprylic acid at 60°C in 10h. The glycerolysis in t-butanol yielded 26.26% of monoacylglycerols(MAG), 36.02% of DAG, with a GTCC conversion of 60% under the optimum conditions.
机译:辛酸和辛酸酯化合成了二酰基甘油(DAG)。 脂酶催化甘油以及中链三酰基甘油(GTCC)的甘油分解 Novozym 435(来自南极假丝酵母)。酯化反应的比较研究 分别在间歇反应器和填充床反应器中进行。反应的效果 参数,例如溶剂,温度,反应物的摩尔比,除水量,酶 辛酸和辛酸转化的反应器负荷和反应器的高度与直径之比。 研究了反应混合物中DAG的含量。辛酸的转化率及其含量 填充床反应器中DAG的酯化反应分别达到82.30%和77.26% 200U / g辛酸,空速34h〜(-1),在60℃下7h;而批处理中的酯化 在50U / g的条件下,反应器的辛酸转化率为83.91%,DAG含量为68.24% 辛酸在60°C下10h。叔丁醇中的甘油分解产生26.26%的单酰基甘油 (MAG),占DAG的36.02%,在最佳条件下的GTCC转化率为60%。

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