Exploration and Practice of Pharmaceutical Equipment & Workshop Design by Using the Task-driven Teaching / 中国药房

OBJECTIVE:To provide reference for the improvement of Pharmaceutical Equipment & Workshop Design teach-ing. METHODS:Task-driven teaching was adopted,CIDO engineering educational model was referred to,task was designed from the conception to run with task-based;theoretical and teaching exploration and practice was carried out by cross-learning of individ-uals and groups,applying of pilotscale experiment platform,developing course design and forming evaluation. RESULTS & CON-CLUSIONS:It changed the traditional teaching method that emphasized on class teaching to make students participate in multi-task learning,so that students can better grasp the equipment selection,understanding and application of workshop design in pharmaceu-tical process. The method gives full play to students' initiative and creativity and it is conducive to students’comprehensive ability for adapting the development of pharmaceutical industry.

To optimize the concentrate process ofDanshen injection by nanofiltration technique / 国际中医中药杂志

Objective To optimize the concentrate process ofDanshen injection.Methods The concentration changes of Salvianic acid A sodium, Protocatechuic aldehyde and Salvianolic acid B were selected as indexes to compare mospheric concentrate, vacuum concentrate, nanofiltration concentrate and nanofiltration-vacuum coupling concentrate methods with HPLC. Results Phenolic acid composition changed when atmospheric and vacuum concentrate method were used. Retention rate of three phenolic acids were over 93% after nanofiltration concentration, but the concentration efficiency was limited by solution viscosity. Nanofiltration-vacuum coupling concentrate methods could solve the above problems, meanwhile, retention rate of three phenolic acids were over 91%.Conclusions Nanofiltration technology takes advantage in medicine extraction concentrate with heat sensitive ingredients, and its application prospect in traditional Chinese medicine pharmaceutical industry would be broad.

Comparative Study of Separation on Phenolic Acids Components by Nanofiltration Process / 中国药房

OBJECTIVE:To investigate the effect of polyamide on the separation on phenolic acids components by nanofiltra-tion process. METHODS:Phenolic acids components were selected as targets,extracted from the Salvia miltiorrhiza,Lonicera ja-ponica or intermediate preparations (tea polyphenols) with water,and filtered with membranes with different pore sizes. The con-tent changes of components were analyzed by HPLC. RESULTS:Danshensu,protocatechuic aldehyde and caffeic acid could better transmit nanofiltration membranes with 3 different pore sizes;with the decrease of pore size,the rejection rates of neochlorogenic acid,chlorogenic acid,rosmarinci acid,ECG and EGCG grew in different levels. But salvianolic acid B was almost retained by the membrane with low molecular weight except 600-800 Da. CONCLUSIONS:Molecular weight importantly influenced nanofiltra-tion separation on phenolic acid components;nanofiltration has a good prospect in enrichment of phenolic acids components.

Process of Removing Bacterial Endotoxins by Ultrafiltration from Dextran 40 Injection / 医药导报

Objective To study the process of removing bacterial endotoxins by ultrafiltration technology in dextran 40 injection. Methods Dextran 40 solution was ultrafiltrated by 100,200,and 300 kDa aperture ultrafiltration membranes with composite, PES and PVDF materials. In order to optimize ultrafiltration process,the content of effective component and endotoxins were detected by HPLC and kinetic-turbidimetry,respectively,and the change of particle size distribution in dextran 40 solution was analyzed before and after ultrafiltration. Results The transmittance of dextran 40 was close to the same MWCO and different membrane material. When MWCO reached 300 kDa,the transmittance was above 91%,which met the requirement of filtration. The endotoxin removal rates by 100-300 kDa composite ultrafiltration membranes were more than 99%. But the endotoxin removal rates of both of PES and PVDF membranes were less than 40%,which were unable to guarantee the removal efficiency of the endotoxin in dextran 40 solution. The particle size declined after ultrafiltration by 300 kDa composite membrane, and level of the insoluble particles decreased. Conclusion The 300 kDa composite ultrafiltration membrane can effectively remove endotoxin in dextran 40 solution with less main components loss. The material can meet requirements for producing dextran 40 injection.