斯塔特公司及垂耳公司的电解槽较小。
利用该控制器实现对预焙铝电解槽的温度控制。
The controller is applied to realize the control of pre-baked aluminium electrolytic cell temperature.
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.
这两个层次构成了电解槽的消极和积极的电极。
These two layers form the Electrolyser's negative and positive electrode.
此化学过程通过一个先进的双室电解槽来完成。
The chemical course is finished by a advanced double electrobath.
这种电解槽用于废水处理时，经济上是可取的。
The use of such a cell for waste water treatment would be economical.
铝电解槽的寿命直接关系到铝冶炼企业的经济效益。
Service life of aluminum electrolytic cell affects directly the economic benefit of aluminum smelting enterprise.
定位板主要是用来固定阳、阴极板在电解槽中的位置。
Positioning plate is usually used in fixing the place of anode plate and cathode plate in electrobath.
利用氧阴极与DSA阳极组装成一种新型氯酸盐电解槽。
A new chlorate cell system with a DSA anode and an oxygen cathode was set up.
在实验室电解槽中获得了致密、平整和光滑的阴极沉积物。
In laboratory cell was obtained dense, flat and smooth cathode deposit.
介绍了瞬间失压对电解槽的危害，提出了相应的预防措施。
The hazards caused by transient voltage loss for electrolyzer are introduced, and the preventative measures are proposed.
铝电解槽的电能消耗率同平均电压和电流效率两个因素有关。
The energy consumption rate of aluminum electrolytic bath is related with the average voltages and current efficiency.
在此基础上，对今后铝电解槽流场的研究提出了指导性意见。
Based on this, the direction to the research on flow field in drained cell is present.
太阳能板提供的电能将输出到电解槽以分解水成为氢和氧分子。
The solar panels will be used to give energy to the electrolyser to break the molecules of water into hydrogen and oxygen molecules.
总结了S-3000型压滤式F4隔膜电解槽的开发研制过程。
The development of F4 diaphragm electrolyzer with S-3000 press filter is summarized.
在磁场作用下，电解槽里通电电解质溶液能发生明显的环向流动。
Electrolytic solution shows a circular motion when electric current flowed in a magnetic field through a electrolytic cell.
国外先进国家同类型的电解槽的平均寿命可以达到2500天左右。
But in advanced countries, the mean life of the same type of aluminium cell can reach about 2500 days.
通过模拟实验研究了稀土电解槽的电阻常数与其结构参数之间的关系。
Relationship between constant of electric resistance and structure parameter in rare earth electrolysis cell was studied through simulation experiment.
本文对电解槽破损原因进行了综合分析，探讨延长电解槽寿命的措施。
This article analyses the reason of the trough breakage and discusses the measures to prolong its service life.
然后我们要尽量把硫酸都移出电解槽。最后再稀释留在电解槽底部的硫酸。
Then, we recover as much of the sulfuric acid as possible, before diluting what remains in the bottom of the electrolytic cell.
本文分析了铝电解槽的破损形式，提出了铝电解槽破损的检查与修补方法。
The text analyzes the damage types of aluminum reduction cell, and proposes the methods to check out and repair the aluminum electrolytic plots.
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.
采用双阴极室隔膜电解槽，以多孔圆筒铸铁为阳极电解制备水处理剂高铁酸盐。
The water treatment agent ferrate is prepared by electrolysis in diaphragm bath with double cathode chamber and porous cylinder cast iron anode.
基于流体动力学理论，推导了水电解槽密封泄漏率公式，并分析了其密封性能。
The sealing leakage ratio formula of water electric tank was deduced based on hydrodynamic theory and the sealing performance was analyzed.
分析了电解槽进出口系统各主要设备杂散电流产生原因，提出了针对性的解决方案。
Causes of the stray current corrosion in inlet and outlet of the electrolytic bath were analyzed to put forward a solution.
铝电解槽电流强化技术对挖掘现有设备产能、提高企业经济效益具有重要的现实意义。
The technology of line current raise is very important to improve the capacity of installation and economic benefits of aluminium corporations.
本文对预焙阳极铝电解槽阳极炭耗问题进行了论述，并介绍了阳极降耗技术的开发应用。
The article discusses the issue concerning with decreasing anode consumption of prebaked anode pot, and it also introduces its development and application.
通过28种橡胶、塑料、合成树脂在食盐电解槽盖中的现场挂片试验，研究其腐蚀行为。
Corrosion behaviour of 28 kinds of synthetic materials including rubber, plastic and synthetic resin was investigated by in situ exposure testing in production line.
分析了槽电阻与氧化铝浓度的之间的关系，对铝电解槽氧化铝浓度的控制方法进行了探讨。
The article analyses relation between cell resistance and alumina concentration and discusses the method for controlling alumina concentration in aluminium smelting cell.
引起阳极在电解槽中化学消耗、物理消耗因素部分是原料因素外，工艺过程控制至关重要。
The reasons leading to excessive consuming of electrochemistry and physics partly attribute to row material, process control are important as well.
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