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Preparation of 6-APA by Enzymatic Bioconversion in an Emulsion Liquid Membrane Reactor 被引量:2

Preparation of 6-APA by Enzymatic Bioconversion in an Emulsion Liquid Membrane Reactor
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摘要 Production of 6-aminopenicillanic acid (6-APA) by hydrolysis using penicillin acylase (PA) was studied as a model of an enzymatic emulsion liquid membrane (ELM) process. The loss of PA activity was examined for various membrane compositions (organic solvent, surfactant, carrier). The effects of some experimental variables on the stability of emulsion were investigated. It was found that the choice of organic solvent greatly affected tilestability of the emulsion. Increasing the concentration of the carrier in the membrane phase increases the transfer rate of substrate and products but also has a destabilizing effect on the emulsion. The recovery of 6-APA obtained by a di-carrier system (N263-N1923) was much higher than those when either of the di-carriers was used separately.The whole process was controlled both by the enzymatic reaction rate and by the transfer rate of the substrate and the products, however, the ratio of them could be changed by varying the composition of the system. For an optimum condition, it was obtained that the recovery ratio of 6-APA was over 80% and the conversion of benzyl penicillin (PG) was up to 90% in the external phase after 30 minutes. Meanwhile, the breakage percentage of the emulsion was less than 2%. Production of 6-aminopenicillanic acid (6-APA) by hydrolysis using penicillin acylase (PA) was studied as a model of an enzymatic emulsion liquid membrane (ELM) process. The loss of PA activity was examined for various membrane compositions (organic solvent, surfactant, carrier). The effects of some experimental variables on the stability of emulsion were investigated. It was found that the choice of organic solvent greatly affected the stability of the emulsion. Increasing the concentration of the carrier in the membrane phase increases the transfer rate of substrate and products but also has a destabilizing effect on the emulsion. The recovery of 6-APA obtained by a di-carrier system (N263-N1923) was much higher than those when either of the di-carriers was used separately. The whole process was controlled both by the enzymatic reaction rate and by the transfer rate of the substrate and the products, however, the ratio of them could be changed by varying the composition of the system. For an optimum condition, it was obtained that the recovery ratio of 6-APA was over 80% and the conversion of benzyl penicillin (PG) was up to 90% in the external phase after 30 minutes. Meanwhile, the breakage percentage of the emulsion was less than 2%.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2001年第4期431-435,共5页 中国化学工程学报(英文版)
基金 the National Natural Science Foundation of China (No. 29136130).
关键词 乳状液膜 反应器 制备 6-APA 生物转化酶 6-氨基青霉烷酸 青霉素 中间产品 6-aminopenicillanic acid, penicillin, enzymatic bioconversion, emulsion liquid membrane, reactor
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参考文献8

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同被引文献34

  • 1吴子生,贾颖萍,褚莹,王玉洁,刘沛妍,马占芳.反胶团相转移法提取青霉素G的研究[J].高等学校化学学报,1993,14(10):1427-1431. 被引量:14
  • 2陈坚.随程离子交换法促进青霉素G水解生产6-氨基青霉烷酸[J].化工学报,1995,46(6):689-694. 被引量:3
  • 3戈悦慈,孙克俭.大孔离子交换树脂从青霉素结晶母液中回收青霉素的探索[J].中国抗生素杂志,1996,21(2):155-155. 被引量:3
  • 4Xu Curong( 许翠荣) . Study for manufacturing process of 6-aminopenicillanic acid [D].Shijiazhuang: Hebei University ofScience and Technology( 河北科技大学) ,2013.
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