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建立了一套超临界ＣＯ２中酶催化反应装置，实现了脂肪酶催化苯甲醇与乙酸丁酯的酯交换反应，并分别探讨了压力、水含量、温度和脂肪酶用量对反应速度和转化率的影响以及酶的稳定性。
A set of supercritical CO 2 medium catalytic reactor was set up to realize the transesterification between benzyl alcohol and butyl acetate catalyzed by lipase. The influences of pressure, water content, temperature and lipase dosage on the reaction rate and conversion rate Impact and enzyme stability.