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在有机共溶剂存在下,通过一锅酶促水解和缩合级联反应过程酶法合成阿莫西林。

Enzymatic synthesis of amoxicillin via a one-pot enzymatic hydrolysis and condensation cascade process in the presence of organic co-solvents.

机构信息

Department of Chemistry, Zhejiang University, Hangzhou 310027, People's Republic of China.

出版信息

Appl Biochem Biotechnol. 2010 Apr;160(7):2026-35. doi: 10.1007/s12010-009-8847-x. Epub 2009 Dec 3.

DOI:10.1007/s12010-009-8847-x
PMID:19957210
Abstract

A cascade reaction combining the enzymatic hydrolysis of Penicillin G potassium salt (PGK) with the kinetically controlled enzymatic coupling of in situ formed 6-aminopenicillanic acid (6-APA) with p-hydroxyphenylglycine methyl ester (D-HPGM) to give amoxicillin as the final product by using a single enzyme has been demonstrated successfully. Ethylene glycol (EG) was employed as a component of reaction buffer to improve the synthesis yield. Reaction parameters, including different cosolvents, EG content, the loading of immobilized penicillin G acylase (IPA), and reaction temperature and time were studied to evaluate their effects on the reaction. The best result of 55.2% yield was obtained from the reaction which was carried out in the mixed media containing 40% sodium dihydrogen phosphate buffer (apparent pH 6.0) and 60% EG (v/v), with the initial concentration 150 mM and 450 mM of PGK and D-HPGM, respectively, catalyzed by 50 IU/mL IPA at 25 degrees C for 10 h. The IPA could be recycled for nine batches without obviously losing of catalytic activity. The important strategy will have potential application in the beta-lactam antibiotics industry due to the advantages of saving the effort of isolating 6-APA, reducing usual enzymatic steps and the industrial cost of amoxicillin synthesis.

摘要

已成功证明,通过使用单一酶将青霉素 G 钾盐(PGK)的酶促水解与原位形成的 6-氨基青霉素酸(6-APA)与对羟基苯甘氨酸甲酯(D-HPGM)的动力学控制酶偶联相结合的级联反应,可将青霉素 G 转化为最终产物阿莫西林。乙二醇(EG)被用作反应缓冲液的组成部分,以提高合成产率。研究了不同的共溶剂、EG 含量、固定化青霉素 G 酰化酶(IPA)的负载量以及反应温度和时间等反应参数,以评估它们对反应的影响。在含有 40%磷酸二氢钠缓冲液(表观 pH6.0)和 60%EG(v/v)的混合介质中进行反应,初始浓度分别为 150mM 和 450mM 的 PGK 和 D-HPGM,反应温度为 25°C,反应时间为 10h,IPA 负载量为 50IU/mL 时,产率最高可达 55.2%。IPA 在回收九次后仍保持较高的催化活性,没有明显失活。由于该策略节省了分离 6-APA 的工作量、减少了常规酶促步骤以及降低了阿莫西林合成的工业成本,因此在β-内酰胺类抗生素工业中具有潜在的应用前景。

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