Ren Zhongqi, Lv Yuanyuan, Zhang Weidong
State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing, People's Republic of China.
Appl Biochem Biotechnol. 2009 Feb;152(2):286-94. doi: 10.1007/s12010-008-8242-z. Epub 2008 Jun 25.
The facilitated transport of penicillin G from aqueous solutions to the stripping phase through bulk liquid membrane (BLM) containing TBP in 3% iso-octanol and n-butyl acetate was studied. Na(2)CO(3) solution was used as the stripping phase. Experiments were performed as a function of stirring rate, TBP concentration and type of diluent in the liquid membrane phase, pH, and initial penicillin G concentration in the feed phase, Na(2)CO(3) concentration in the stripping phase, etc. The results showed that the BLM process could carry out the simultaneous separation and concentration of penicillin G from dilute aqueous solutions, and arise "up-hill" effect due to the characteristic of non-equilibrium mass transfer. The diffusion of penicillin G complex in the liquid membrane phase played an important role in BLM process. The mass transfer mechanism of BLM for this system was also discussed.
研究了青霉素G在含3%异辛醇和乙酸正丁酯的磷酸三丁酯(TBP)支撑液膜(BLM)中从水溶液到反萃相的促进传递。用碳酸钠溶液作为反萃相。实验考察了搅拌速率、液膜相中TBP浓度、稀释剂类型、pH值、料液相中青霉素G的初始浓度、反萃相中碳酸钠浓度等因素的影响。结果表明,支撑液膜过程可实现从稀水溶液中同时分离和浓缩青霉素G,且由于非平衡传质特性产生“上坡”效应。青霉素G络合物在液膜相中的扩散在支撑液膜过程中起重要作用。还讨论了该体系支撑液膜的传质机理。