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离子液体/水混合物热致可逆相分离中青霉素的酶促水解及原位产物分离

Enzymatic hydrolysis of penicillin and in situ product separation in thermally induced reversible phase-separation of ionic liquids/water mixture.

作者信息

Mai Ngoc Lan, Koo Yoon-Mo

机构信息

Department of Biological Engineering, Inha University, Incheon 402-751, Republic of Korea.

Department of Biological Engineering, Inha University, Incheon 402-751, Republic of Korea.

出版信息

Enzyme Microb Technol. 2014 Sep;63:34-8. doi: 10.1016/j.enzmictec.2014.05.002. Epub 2014 May 17.

Abstract

Enzymatic hydrolysis of penicillin G to produce 6-aminopenicillanic acid, key intermediate for the production of semisynthetic β-lactam antibiotics, is one of the most relevant example of industrial implementation of biocatalysts. The hydrolysis reaction is traditionally carried out in aqueous buffer at pH 7.5-8. However, the aqueous rout exhibits several drawbacks in enzyme stability and product recovery. In this study, several ionic liquids (ILs) have been used as media for enzymatic hydrolysis of penicillin G. The results indicated that hydrophobic ILs/water two-phase system were good media for the reaction. In addition, a novel aqueous two-phase system based on the lower critical solution temperature type phase changes of amino acid based ILs/water mixture was developed for in situ penicillin G hydrolysis and product separation. For instance, hydrolysis yield of 87.13% was obtained in system containing 30 wt% [TBP][Tf-ILe] with pH control (pH 7.6). Since the phase-separation of this medium system can be reversible switched from single to two phases by slightly changing the solution temperature, enzymatic hydrolytic reaction and product recovery were more efficient than those of aqueous system. In addition, the ILs could be reused for at least 5 cycles without significant loss in hydrolysis efficiency.

摘要

青霉素G的酶促水解以生产6-氨基青霉烷酸,这是半合成β-内酰胺抗生素生产中的关键中间体,是生物催化剂工业应用中最具代表性的例子之一。传统上,水解反应在pH值为7.5-8的水性缓冲液中进行。然而,水性途径在酶稳定性和产物回收方面存在几个缺点。在本研究中,几种离子液体(ILs)已被用作青霉素G酶促水解的介质。结果表明,疏水性离子液体/水两相体系是该反应的良好介质。此外,基于氨基酸基离子液体/水混合物的低临界溶液温度型相变,开发了一种新型的水相两相体系,用于青霉素G的原位水解和产物分离。例如,在含有30 wt% [TBP][Tf-ILe]且pH值控制为7.6的体系中,水解产率达到了87.13%。由于该介质体系的相分离可以通过稍微改变溶液温度从单相可逆地切换为两相,因此酶促水解反应和产物回收比水性体系更有效。此外,离子液体可以重复使用至少5个循环,而水解效率没有明显损失。

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