填充床反应器中酶法连续合成甘油二酯的研究

近年来,1,3-甘油二酯(DAG)由于其广泛用途及健康作用日益受到人们的重视。报道了一种无溶剂条件下填充床反应器中连续酶促合成1,3-DAG的方法。研究了填充柱的长径比、进料体积流速、温度、底物摩尔比对酯化率和1,3-DAG产量的影响。结果表明固定化酶填充柱长径比7.8,亚油酸、甘油摩尔比1∶2 ,进料速度1.2mL/min ,65℃条件下酯化反应可实现脂肪酸酯化率、1,3-DAG纯度及生产效率的统一。填充床反应器中固定化酶连续催化酯化反应的一个主要问题即体系水分清除困难。实验研究了采用过量甘油吸附脱水的可行性,亚油酸、甘油摩尔比为1∶2时,可明显改善固定化酶的稳定性,增加LipozymeRMIM的使用寿命。连续运行10d ,残余酶活仍保持在80 %以上,而对照组则仅为52%。

Synthesis of Diacylglycerol Using Immoblized 1, 3-Regiospecific Lipase in Continuously Operated Fixed Bed Reactors

Diacylglycerol, DAG, because of its multifunctional and nutritional properties, attracted considerable attention recently. Enzymatic synthesis of diacylglycerols from linoleic acid was investigated in a solvent-free reaction in a continuously operated fixed bed reactors containing Lipozyme RM IM. By appropriate manipulation of the fluid-residence time, the relative proportions of the various acylglycerols in the effluent stream can be controlled. In addition, the presence of excess glycerol is effective for the removal of water produced during the esterification reactions. Under the conditions of molar ratio of linoleic acid to glycerol of 0.5, the immoblized enzyme maintained high stability and allowed the reaction to continue for 10 days without significant deterioration in enzyme activity. It was determined that the conversion of fatty acid, content of 1,3-DAG and volume efficiency of reactor reached optima under the conditions: a packaged-bed reactor(with a ratio of packed length to inner diameter of 7.8), reacting temperature at 65 degrees C, molar ratio of linoleic acid to glycerol of 0.5, and feeding flow rate of 1.2 mL/min.