• 文献检索
  • 文档翻译
  • 深度研究
  • 学术资讯
  • Suppr Zotero 插件Zotero 插件
  • 邀请有礼
  • 套餐&价格
  • 历史记录
应用&插件
Suppr Zotero 插件Zotero 插件浏览器插件Mac 客户端Windows 客户端微信小程序
定价
高级版会员购买积分包购买API积分包
服务
文献检索文档翻译深度研究API 文档MCP 服务
关于我们
关于 Suppr公司介绍联系我们用户协议隐私条款
关注我们

Suppr 超能文献

核心技术专利:CN118964589B侵权必究
粤ICP备2023148730 号-1Suppr @ 2026

文献检索

告别复杂PubMed语法,用中文像聊天一样搜索,搜遍4000万医学文献。AI智能推荐,让科研检索更轻松。

立即免费搜索

文件翻译

保留排版,准确专业,支持PDF/Word/PPT等文件格式,支持 12+语言互译。

免费翻译文档

深度研究

AI帮你快速写综述,25分钟生成高质量综述,智能提取关键信息,辅助科研写作。

立即免费体验

Physical and reactive extraction equilibria of penicillin G in a hydrogen-bond acceptor solvent system.

作者信息

Lee Sang Cheol

机构信息

Department of Chemical Engineering, Kunsan National University, Kunsan, Chonbuk 573-701, South Korea.

出版信息

Biotechnol Prog. 2006 May-Jun;22(3):731-6. doi: 10.1021/bp050380y.

DOI:10.1021/bp050380y
PMID:16739956
Abstract

Physical and reactive extraction equilibria of penicillin G were investigated experimentally and theoretically in the existence of n-butyl acetate as a hydrogen-bond acceptor solvent. Physical extraction equilibrium experiments were carried out varying the pH of aqueous phase and overall penicillin concentration. We compared the experimental data with the calculated results from four physical extraction equilibrium models suggested here and obtained the most reasonable model. Also, penicillin G was reactively extracted using Amberlite LA-2 in n-butyl acetate. The experimental variables were pH of the aqueous phase, overall amine concentration, and overall penicillin concentration. A combined equilibrium model including our physical extraction equilibrium expression and the reactive extraction equilibrium expression suggested by Reschke and Schügerl was used so as to analyze the current reactive extraction equilibrium system. The calculated results from the reactive extraction equilibrium model were in good agreement with the experimental data.

摘要

相似文献

1
Physical and reactive extraction equilibria of penicillin G in a hydrogen-bond acceptor solvent system.
Biotechnol Prog. 2006 May-Jun;22(3):731-6. doi: 10.1021/bp050380y.
2
Reaction equilibrium of penicillin G with amberlite LA-2 in a nonpolar organic solvent.
Biotechnol Prog. 2002 Jan-Feb;18(1):108-15. doi: 10.1021/bp010145p.
3
Synergistic extraction of penicillin G with aliphatic alcohols and butyl acetate.青霉素G与脂肪醇和乙酸丁酯的协同萃取
J Chem Technol Biotechnol. 1994 Nov;61(3):247-50. doi: 10.1002/jctb.280610311.
4
Facilitated transport of penicillin G by bulk liquid membrane with TBP as carrier.以磷酸三丁酯(TBP)为载体的支撑液膜对青霉素G的促进传输
Appl Biochem Biotechnol. 2009 Feb;152(2):286-94. doi: 10.1007/s12010-008-8242-z. Epub 2008 Jun 25.
5
Penicillin G extraction from model media using an emulsion liquid membrane: determination of optimum extraction conditions.
J Chem Technol Biotechnol. 1994 Apr;59(4):371-6. doi: 10.1002/jctb.280590410.
6
Penicillin G extraction from model media using an emulsion liquid membrane: a theoretical model of product decomposition.
J Chem Technol Biotechnol. 1994 Apr;59(4):365-70. doi: 10.1002/jctb.280590409.
7
Equilibrium modeling of extractive enzymatic hydrolysis of penicillin G with concomitant 6-aminopenicillanic acid crystallization.青霉素G萃取酶水解与6-氨基青霉烷酸结晶同时进行的平衡模型
Biotechnol Bioeng. 2002 May 20;78(4):395-402. doi: 10.1002/bit.10242.
8
The extraction of penicillin G with aliphatic amines in organic solvents of different polarities.
J Chem Technol Biotechnol. 1992;53(1):97-103. doi: 10.1002/jctb.280530114.
9
Novel reactive perstraction system applied to the hydrolysis of penicillin G.
Biotechnol Bioeng. 2005 Jul 20;91(2):227-36. doi: 10.1002/bit.20514.
10
Simultaneous extraction and concentration of penicillin G by hollow fiber renewal liquid membrane.中空纤维更新液膜同步萃取浓缩青霉素G
Biotechnol Prog. 2009 Mar-Apr;25(2):468-75. doi: 10.1002/btpr.152.

引用本文的文献

1
An Adsorption Based Downstream Processing Approach for Penicillin V from a BIONCL I22 Culture Filtrate.一种基于吸附的从BIONCL I22培养滤液中提取青霉素V的下游加工方法。
ACS Omega. 2024 Jun 3;9(24):25859-25869. doi: 10.1021/acsomega.4c00251. eCollection 2024 Jun 18.