目的制备聚阳离子膜材料并表征。
Objective: To study synthesis and characterization of polycation-membrane material.
论述了复极式离子膜电解槽运行过程中的维护。
The maintenance of bipolar ion-exchange membrane electrolyzer during its operation is discussed.
介绍了离子膜系统淡盐水脱氯原理、目的和方法。
The principle, object and method of depleted brine in ionic membrane system were introduced.
离子膜性能提高；
介绍了离子膜烧碱装置中空气吹除脱氯和真空脱氯工艺。
The dechlorination process by air purge and vacuum in ionic membrane caustic soda units were introduced.
提出了建设新离子膜烧碱项目中对整流装置设计的建议。
Suggestions on the design of rectifying units in new project of ionic membrane caustic soda were put forward.
介绍了38dd350型离子膜电解槽复极元件的结构。
The structure of bipolar components of 38dd350 type ion-exchange membrane electrolyzer is introduced.
介绍了离子膜装置的技改情况以及试车、运行中存在的问题。
Technical status of ionic membrane units, and the existing problem of test run and operation were introduced.
介绍了复极式离子膜电解装置整流设备的电压值偏高的现状。
The present status of high voltage of rectification equipment in bipolar type ion-exchange membrane electrolyzer was introduced.
介绍了离子膜烧碱盐水精制的工艺过程及影响盐水质量的各项因素。
The process of brine refining of ionic membrane caustic soda, and the each influential factor of the quality of brine were introduced.
分析总结了离子膜出现鼓泡的原因，提出了针对性的预防措施和建议。
The reasons of bulling were analysed, and the typical countermeasures and suggestions were put forward.
介绍了离子膜电解盐水系统中黏性酸碱不溶物的成因和危害以及解决措施。
Results, harm and solution of viscous acid-base insoluble object in ionic membrane electrolysis brine system were introduced.
介绍了离子膜电解槽在生产运行过程中的腐蚀现象，讨论了产生腐蚀的原因。
The corrosion phenomenon of ionic membrane electrolyzer in production process was introduced. The reasons of corrosion were also discussed.
介绍了DCS在离子膜制碱工艺中的应用及常用控制方案的实现和运行效果。
The application of DCS in the production process of ion-exchange membrane caustic soda, the realization of common controlling plans and the practical results are introduced.
介绍了离子膜烧碱生产中的新工艺、新技术的应用及产生的经济效益和社会效益。
Application of new process and new technology in ionic membrane caustic soda production. Its economic and social benefit were introduced.
介绍了横河公司的分布式控制系统CS3000在离子膜烧碱生产过程中的应用。
The application of Yokogawa distributing CS3000 controlling system in ionic membrane caustic soda production was introduced.
介绍某公司引进的离子膜制碱装置采用国产dcs系统的原由，系统的结构及特点。
The reasons for adopting homemade DCS to introduction ion membrane alkali produced device in Hangzhou Electrochemical Group Ltd.
就迪诺拉公司29DD350 型离子膜电解槽在生产中的运行情况进行技术总结。
The operation of DeNora 29DD350 ion-exchange membrane electrolyzer during the production are summarized.
本研究采用铂阳极、铅阴极，阳离子膜和滤布分别作为隔膜，通直流电进行电解操作。
In our research, we adopt platinum as anode lead as cathode cation membrane and filtration fabric as septum separately, electrolysis operation was carried out through electrifying DC.
阐述了离子膜烧碱主要生产工序介质的腐蚀性及对主要设备、泵、阀所采取的防腐措施。
The corrosiveness of medium in the main process of ionic membrane caustic soda production, and anticorrosion measures of main equipment such as pumps and valves were explained.
阐述了离子膜烧碱主要生产工序介质的腐蚀性及对主要设备、泵、阀所采取的防腐措施。
The corrosiveness of medium in the main process of ionic membrane caustic soda production, and anticorrosion measures of main equipment such as pumps and valves were explained.
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