electrolyzer
electrolyzer
1. 16- type metal anode electrolyzer
16型金属阳极电解槽
2. 20 kt/a BM 2.7 Uhde electrolyzer and its operation
2万t/a伍迪BM2.7电解槽装置及运行
3. Keywords AZM-F_2 electrolyzer;anode gas separator;corrosion;
2型电解槽;阳极气体分离器;腐蚀;
4. Keywords F2 ionic membrane electrolyzer;recoating;activated coating;
2离子膜电解槽;重涂;活性涂层;
5. BM 2.7 electrolyzer
BM2.7型电解槽
6. BM 2.7 electrolyzer units
BM2.7电解槽
7. F2 ionic membrane electrolyzer
F2离子膜电解槽
8. n-BiTAC electrolyzer
n-BiTAC电解槽
9. NCS electrolyzer
NCS电槽
10. NCZ electrolyzer
NCZ电解槽
11. bipolar type ion-exchange membrane electrolyzer
[化] 复极式离子膜电解槽
12. Hooker electrolyzer
[化] 虎克型电解槽
13. medium- temperature fluorine electrolyzer
中温制氟电解槽
14. For prolonging the life of electrolyzer, quality of diaphragm and clarified brine should be guaranteed, and the concentration of fresh soda should be controlled.
为了延长电槽运行时间,要保证隔膜和精制盐水的质量、稳定地调控淡碱浓度。
15. The effective methods for low voltage of electrolyzer were that power consumption and distances between poles were decreased, and voltage drop between solutions of poles was reduced.
为了获得低的槽电压从而降低电耗,缩短电极间的距离,减少电极间溶液的电压降是非常有效的方法。
16. The paper introduces the basic structure of 30DD350 Electrolyzer, generalizes the ways of its damage and the methods of its maintenance.
介绍了30DD350电解槽的基本结构，总结了其损坏形式及维修方法。
17. The structure of bipolar components of 38DD350 type ion-exchange membrane electrolyzer is introduced.
介绍了38DD350型离子膜电解槽复极元件的结构。
18. Structure characteristics of Uhde electrolyzer and De Nora electrolyzer, design fixing and the improvement on the basis of the situation of Yangzhou pesticide and chemical Co.
介绍了伍迪电解槽的结构、设计安装特点以及结合扬州农药化工公司自身情况所做的改进工作。
19. The process of acceptance brine by bittern of Ye county were introduced. Calculations showed that the concentration of secondary brine met the requirements of electrolyzer.
介绍了利用叶县卤水制合格盐水的工艺。通过计算证明二次盐水浓度可满足电解槽的工艺要求。
20. The problems in current increase of diaphragm electrolyzer and the countermeasures were introduced.
介绍了在隔膜电解槽电流提升过程中所遇到的问题及采取的解决方法和措施。
21. The present status of high voltage of rectification equipment in bipolar type ion-exchange membrane electrolyzer was 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。
22. The primary purified brine process innovation was introduced. Through innovation, the process was briefed, and the quality of brine and the capacity of ionic membrane electrolyzer were improved.
介绍了对一次精制盐水工艺的改造内容。通过改造,简化了工艺过程,提高了一次盐水的质量及离子膜电解槽的生产能力。
23. The technological innovation for changing input brine from faintly alkaline to weakly acid was introduced. The side reaction was reduced, so the current efficiency of electrolyzer was raised.
介绍了对进槽盐水由酸碱性改为微酸性的技术改造,减少了副反应的发生,从而提高了电解槽的电流效率。
24. The fluctuation of electrolyzer diaphragm rose in adsorption and series countermeasures on the steady running were introduced.
介绍了电槽隔膜吸附中出现的波动及通过一系列调整使电槽稳定运行的过程。
25. The hazards caused by transient voltage loss for electrolyzer are introduced,and the preventative measures are proposed.
介绍了瞬间失压对电解槽的危害,提出了相应的预防措施。
26. The principle,composition,selection of hydraulic fluid,matters needing attention in use of domestic oil-pressure system for ion-exchange membrane electrolyzer are introduced.
介绍了离子膜电解槽国产化油压系统的原理、组成及液压油的选用和使用中应注意的事项。
27. Process, characteristics and parameters of refined brine by new process for ionic membrane electrolyzer were introduced.
介绍了采用新工艺精制离子膜电解槽盐水的工艺概况、特点及参数。
28. Process, characteristics and parameters of refined brine by new process for ionic membrane electrolyzer were introduced. The existing problem and points for attention were pointed out.
介绍了采用新工艺精制离子膜电解槽盐水的工艺概况、特点及参数。指出了存在的问题及注意事项。
29. Abnormal phenomenon in operation of electrolyzer and its production reasons were introduced. After adoption of countermeasures, electrolyzer operates with stability and high efficiency.
介绍了金属阳极电解槽运行中的异常现象及产生的原因,经采取相应的改进措施,使电槽平稳高效地运行。
30. The design and operation status of the first domestic ionic membrane electrolyzer with high current density natural circulation system were introduced.
介绍国内第一套国产高电流密度自然循环离子膜电解槽装置的设计及运行情况。
31. Discussion on running of anode plate after recoating according to the electrolyzer voltage distribution
从分布电压看阳极片重涂后的运行
32. Improvement of electrolyzer from forced circulation of high current density to natural circulation
从强制循环到高电流密度自然循环电槽的改造
33. Taking the 20 kt/a ion-exchange membrane facility of our plant for example,the electrolyzer structure used in Asahi Kasei forced-circulalion ion-exchange membrane process is summarized.
以我厂2万t／a离子膜装置为例，对旭化成强制循环离子膜工艺的电解槽结构进行综述。
34. uhdenora electrolyzer
伍德-迪诺拉电槽
35. Optimizing the diaphragm manufacturing process to improve the running status of electrolyzer
优化制膜工艺提高电槽运行质量
36. Optimize electrolyzer management for consumption reduction
优化电槽管理努力降低消耗
37. Base on some factors of electrolyzer cell voltage composition, this article introduces the present status and progress of electrolyzer cell voltage composition.
依据槽电压构成的诸多因素,介绍了目前槽电压构成的现状和进展。
38. unit electrolyzer
单元槽
39. Keywords monopolar type ion-exchange membrane electrolyzer;structure;performance;
单极式离子膜电解槽;结构;性能;
40. monopolar electrolyzer operation
单槽投用
41. Keywords monopolar;ion-exchange membrane electrolyzer;running;
单级;离子膜电解槽;运行;
42. The processing of glass-reinforced plastic cover for Model 16 Hooker electrolyzer with vinyl ester based unsaturated polyester resin was introduced. The performances of vinyl ester based unsaturated polyester resin were described.
叙述了用乙烯基酯不饱和聚酯树脂制作虎克－16型玻璃钢电解槽盖的施工方法，介绍了乙烯基酯不饱和聚酯树脂的性能。
43. Capacity of caustic soda production of high density bipolar type ion-exchange membrane electrolyzer and the benefit conditions for multiphase rectification composition was introduced.
叙述了高电密复极式离子膜电槽的产碱能力和对整流所形成多相整流的有利条件。
44. Application of Current Balancing Device with Random Variation on the Large Powet Controlled Rectifier for Aluminum Electrolyzer
可任意置换的均流装置在铝电解大功率可控整流器中的应用
45. Meanwhile, a concept and method is put forward for decreasing the electrolytic power consumption by cleaning the electrolyzer, based on an example.
同时,根据一个实例,提出了一种通过清洗电解槽来降低其电解电耗的思路和方法。
46. Meanwhile, the causes of electrolyzer A's voltage arising was analyzed, and some preventive measures was mentioned.
同时分析了A槽槽电压升高的原因,介绍了预防事故发生的措施。
47. solid oxide electrolyzer ceils
固体氧化物电解池
48. SPE water electrolyzer
固体聚合物电解质（SPE）水电解槽
49. Introduction to the structure and performance of homemade monopolar type ion-exchange membrane electrolyzer
国产单极式离子膜电解槽结构与性能介绍
50. bioplar type ion-exchange membrane electrolyzer
复极式离子膜电槽
51. a bipolar type ion-exchange membrane electrolyzer
复极式离子膜电解槽
52. Keywords bipolar type ion-exchange membrane electrolyzer;features;operation status;
复极式离子膜电解槽;特点;运行情况;
53. Keywords bipolar-type ion-exchange membrane electrolyzer;natural circulation;caustic potash;running;
复极式离子膜电解装置;自然循环;氢氧化钾;运行;
54. Operation summary on Asahi multipole type natural circulation electrolyzer
复极式自然循环电解槽运行总结
55. Data analysis on cell voltage of bipolar type ion-exchange membrane electrolyzer
复极离子膜电槽电压数据分析
56. Selection of large-scale bipolar type ion-exchange membrane electrolyzer and its running status
大型复极式离子膜电解槽的选择和运行情况
57. How to improve current efficiency of diaphragm electrolyzer with metal anodes
如何提高金属阳极隔膜电解的电流效率
58. Various possible problems arised in runing of monopolar type ion-membrane electrolyzer are analyzed thoroughly and the effective countermeasure are proposed.
对单极式离子膜电解槽运行过程中可能出现的各种问题进行了深入细致地分析,并提出了有效的解决方法。
59. Auto-control system of electrolyzer of caustic soda units were introduced. The traditional method were optimized. And according to production condition, the lectotype of instrument were discussed.
对烧碱装置中电解槽的自动控制系统进行了阐述,对传统控制手段进行了优化设计,并根据生产条件,对仪表的选型进行了较为详细的论述。
60. Keywords X-ray fluorescence analysis method;electrolyzer;metal aode;
射线荧光分析法;电解槽;金属阳极;
61. The operation of DeNora 29DD350 ion-exchange membrane electrolyzer during the production are summarized.
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。
62. A mathematical model of electric field in electrolyzer is built.
建立了计算电解槽内部电场的数学模型;
63. electrolyzer with forced circulation
强制循环电解槽
64. Influential factors and reducing measures of electrolyzer cell voltage
影响槽电压的因素及降低措施
65. Keywords expandable DSA DR;modified diaphragm;electrolyzer;technology;application;
扩张阳极;改性隔膜;电槽;技术;应用;
66. Application of control diagram for bipolar type electrolyzer control
控制图在复极电解槽控制中的应用
67. Operation summary on the experimental electrolyzer using modified diaphragm with matched spread anode
改性隔膜配扩张阳极试验槽运行总结
68. Improving causticization of asbestos fiber, optimizing diaphragm manufacture, reducing cell voltage of electrolyzer
改进石棉绒苛化工艺优化隔膜制作降低槽电压
69. Summary on operation status of NCH Asahi electrolyzer
旭化成NCH型电解槽运行总结
70. Cause of differential pressure fluctuation of AC and domestic multi-pole type enforced circulation electrolyzer and it's countermeasures
旭化成和国产化强制循环复极电解槽压差波动原因及对策
71. Reasons for blockage of the inlet flexible pipe of ACI bipolar ion-exchange membrane electrolyzer
旭化成离子膜复极电槽进口软管堵塞原因
72. This document introduces the brief point of technology and performance in the first set of electrolyzer of Ion - Exchanger - Membrane in NingXia.
本文介绍了我区第一套离子膜法制碱工艺及设备引进中的工艺及性能要点。
73. plate and frame electrolyzer
板框式电化学反应器
74. Keywords plate and frame electrolyzer;resident time distribution;flowing law;Electroredox;dichromic acid;p-aminophenol;
板框式电化学反应器;停留时间分布;流动规律;电氧化还原;重铬酸;对氨基苯酚;
75. Keywords plate and frame electrolyzer;resident time distribution;flowing law;dichromic acid;p-aminophenol;
板框式电化学反应器;停留时间分布;流动规律;重铬酸;对氨基苯酚;
76. Relation of the polar plate voltage and the electrolyzer operation status
极片电压高低与电槽运行状况的关系
77. Quantity of transfer water were calculated by parameters of ionic membrane electrolyzer, and the operation status of ionic membrane by the changing trends of transfer water were analysed.
根据离子膜电槽运行数据计算出水迁移量,并通过其变化趋势分析了离子膜的运行状况。
78. Influence of electrolyzer voltage on regeneration characteristics of desulfurization liquor of sodium alkali
槽压对钠碱脱硫吸收液再生特性影响的研究
79. voltage of electrolyzer
槽电压
80. Keywords hydrogen energy;renewable energy;Water Electrolysis;Alkaline Electrolyzer;Polymer Electrolyte Membrane Electrolyzer;Solid Oxide Electrolyzer;
氢能;可再生能源;电解水;碱性电解槽;聚合物薄膜电解槽;固体氧化物电解槽;
