电渗析

diàn shèn xī
  • electrodialysis;electroosmosis
电渗析电渗析
电渗析[diàn shèn xī]
  1. 降度用水采用深井水,并通过离子交换、反渗透和电渗析处理。

    The water used in the adjustment of alcohol content was from deep well and under the treatment of ion exchange , reverse osmosis and electroosmosis .

  2. 本文介绍了电渗析膜技术在烧碱生产和锅炉给水处理中的应用效益及其设备生产厂家。

    This paper introduced the technology of electroosmosis film used in the production of caustic soda and boiler supply water treatment , its profits , together with the equipment producers .

  3. 双极性膜电渗析技术在维生素C生产中的应用研究

    Application of bipolar membrane electrodialysis in production of vitamin C

  4. PLC控制在循环水再生电渗析系统中的应用

    PLC control applied in electrodialysis system of circulating water recycling engineering

  5. pH值对电渗析法回收厨房垃圾发酵液中乳酸的影响

    Effects of pH on recovery of lactic acid from kitchen garbage fermentation broth by electrodialysis

  6. 循环水回用电渗析装置的PLC控制系统设计

    Design of the PLC control system of electrodialysis device in circulating water reuse engineering

  7. HF离子交换膜在电渗析器上的性能研究

    Study on Properties of HF Ion-Exchange Membranes in the Electrodialysis Process

  8. 化学除氟首先推荐调pH活性氧化铝技术,苦咸水淡化可用电渗析法。

    We recommended activated alumina process ( with pH adjustment ) for fluoride removal and the electrodialysis process for desalination .

  9. 油田污水电渗析处理后浓水ASP体系的配制

    Preparation of an ASP system using high salinity water from oilfield sewage treated by electrodialysis

  10. (HF)高性能电渗析器用离子交换膜介绍

    Introduction on properties of HF ion exchange membranes in the implement of electrodialysis

  11. 去除COD和颜色常常使用好氧菌或厌氧菌的生物处理办法,电渗析或反渗透技术适合除去盐份。

    For the removal of COD and color , biological treatment , both aerobic and or anaerobic , is often used .

  12. 本文介绍了用电渗析设备脱除HSS的研究结果。

    This paper introduces the removal research of the HSS using a dedicated electrodialyser .

  13. 配置不同浓度的NaCl盐溶液,研究了料液浓度和流速对电渗析极限电流密度的影响。

    With different NaCl concentrations , the effects of liquid concentrations and flow velocity on limited current density in electrodialysis are investigated .

  14. 介绍了PLC自控系统在电渗析工艺处理高矿化度矿井水工程中的应用,对PLC自控系统的工作原理、硬件结构和软件设计进行了分析。

    This paper introduces an application of PLC control system in high mineralized mine water treatment , and analyzes working principle , hardware structure and software design of the system .

  15. 凹版印刷VOCs废气的净化治理联用工艺用电渗析、超滤组合工艺治理碱性蓄电池污染

    Application of Combined Treatment Process for Purification of VOCs in Gravure Printing Treat basic storage battery pollution with electrodialysis and superfilter composed technology

  16. 配位化合物在电渗析分离Co-Ni离子过程中的应用

    Separating Co-Ni ions by electrodialysis & the application of coordination compounds to separation process

  17. 本文介绍了应用于实验室规模电渗析装置的实验数据、模糊模型(FL)、数学模型(MM)。

    This paper presents experimental data , a fuzzy logic ( FL ) model , a mathematical model ( MM ) for a laboratory scale electrodialysis ( ED ) cell .

  18. 本文用电渗析法制备得了纯度较高的次磷酸钴;合成了CoP非晶态合金,并用于PH3的催化分解。

    This paper we produced cobalt hypophosphite by the method of electrodialysis ; prepared CoP amorphous alloy and used to decomposition of PH3.1 .

  19. 电渗析频繁倒极(EDR)工艺探讨

    Study of Electrodialysis Reversal ( edr ) process

  20. 钠化钒渣的钒浸出率为95~99%.对此浸出液采用电渗析器脱钠,伯胺萃取提钒,最后可得到纯度大于99%的V2O5产品。

    After the recovery of sodium in the V-containing solution by electro-dialysis and the extraction of vanadium from anolyte by using primary amine , the V_2O_5 product with 99 % purity can finally be separated out .

  21. 电渗析(简称MAE)技术是膜分离技术之一,也是对草浆黑液中钠离子回收的可选方法,用直流电可一步从草浆黑液中回收苛性钠。

    Membrane assisted electrolysis ( MAE ) is a membrane separation technique , and is one of feasible methods to recover sodium from straw pulping black liquor ( SPBL ) .

  22. EDI装置在形式上看,是在电渗析器的隔板中填充离子交换树脂,在直流电场的作用下同时实现连续的去离子和离子交换树脂的连续电再生过程。

    EDI device is similar to electrodialysis device which filled with ion exchange resins in the form . It can achieve continuous deionization and continuous electric regeneration of ion exchange resins under electric filed effect .

  23. 含有HSS的胺液流经电渗析离子交换装置后,HSS由胺液介质转换为水介质。

    Amine solution containing HSS and methyldiethanolamine ( MDEA ) flowed through the device , in which MDEA was reserved on the resin after exchanging with hydronium ions on the strong acidic cation-exchange resin .

  24. 将双极膜(BPM)和填充床电渗析(EDI)技术相结合,组装成三隔室BPM-EDI装置,将其应用于复床离子交换树脂的电再生。

    Will bond of Bipolar Membrane ( BPM ) and Packed bed Electrodialysis EPI Technology . Was made up of three compartment BPM-EDI The apparatus . It can be used in complex-bed .

  25. 电渗析脱盐的适宜操作条件为:循环脱盐,脱盐前调节料液pH至4.0,恒定操作电流11A,废液流速9cm/s,脱盐率达99%以上时结束实验。

    The optimum technological conditions of desalinating by electrodialysis were found out . Under the condition of pH4.0 , electric current 11A , flow rate of effluent 9cm / s and 2 hours ' circulation , the desalination rate reached more than 99 % .

  26. 以大庆油田常规处理后的油田采出水为处理对象,建立日产水300t的超滤预处理和电渗析脱盐处理中试试验装置。

    A ultrafiltration pretreatment and electrodialysis desalinization pilot apparatus with a capacity of 300 tons water per day was set up to treat produced water after conventional processing for reuse in the Daqing Oilfield .

  27. 清液利用超滤、纳滤和反渗透的组合工艺,把污水的盐分进一步浓缩,浓水继续通过电渗析再次浓缩后,进入MVR蒸发器进行蒸发结晶。

    The supernatant by ultrafiltration , nanofiltration and reverse osmosis combination process , the sewage of salt further concentration , concentration of water by electrodialysis concentrated continue again , enter the MVR evaporator for evaporation crystallization .

  28. 通过电渗析过程拆分DL-对羟基苯甘氨酸(DL-4-hydroxyphenylglycine,DL-HPG)外消旋混合物以评价该膜的手性拆分效果。

    Electrodialysis process for the separation of DL-4-hydroxyphenylglycine racemic mixture was carried out to evaluate these chiral selective cation-exchange membranes .

  29. 可以使一步结晶所得的亚氨基二乙酸产品纯度达到97%,收率达到90%以上。同时针对常规结晶工艺的不足,本文探讨性地研究IDA的双极性膜电渗析分离方法。

    As a result , under process conditions , the purity of IDA is more than 97 % , and the yield is about 90 % At the same time for overcoming the deficiency of crystallization technology Bipolar Membrane Electrodialysis method has been probed .

  30. 结果表明,使用电解电渗析可以将NaOH从阳极转移到阴极,当装入阳极室和阴极室的液体体积相当时,阴极室溶液中的NaOH质量分数可以达到4.4%;

    It is known from the experimental data that with this method NaOH could be transferred from anode room to cathode room , and if the liquid volumes in these two rooms were the same , the mass fraction of NaOH in cathode room could reach 4.4 % .