1) prebaked cell
预焙槽
1.
The theoretical calculation of the electrolyte temperature variation rule and heat loss during pole changing of 240kA prebaked cell was represented.
阐述240kA预焙槽换极过程的电解质温度变化规律及对热损失的理论计算。
2.
After the 80kA self-baking anode was replaced by the prebaked cell, the primary wet cleaning system was reserved, but the running had shown that the smoke dust discharge concentration was over proofed and the system breakdown frequently.
80kA侧插自焙槽改为预焙槽后 ,保留原有湿法净化系统 ,运行后发现 ,烟尘排放浓度超标 ,系统故障频繁。
2) pre-baked anode cell
预焙槽
1.
Analyzing CA distance of large pre-baked anode cell;
大型预焙槽阳极极距分析
2.
The paper sets up optimized model for anode exchange sequence of pre-baked anode cell by means of application template designed with usual office software.
利用常用办公软件设计了应用模板,建立了预焙槽阳极更换顺序的产生及优选模型,并使用该模板排出了合理的换极顺序。
3) pre-baked cell
预焙槽
1.
As the aluminum industry facing the strictly environment claim and the drastic market competition, it is very important to reconstruct of self-baking cell replaced cell by the original pre-baked cell.
利用预焙槽实施对自焙槽的改造有以下两种方式:一是保留电解厂房,整流所容量扩大,用大型现代化预焙槽取代小型自焙槽;保留原有自焙槽系列大部分设施如整流所、电解厂房、槽壳等,改造成同级的小型预焙槽。
2.
The practical experience of the first 280 kA pre-baked cell which reduced anode effect coefficient in our country was comprehensively summarized in this paper.
总结了我国第一条280 kA预焙槽生产系列降低阳极效应系数的生产实践经验,提出现场浓度和原材料质量控制是有效降低阳极效应系数的保证,同时深入分析了提高效应管理的途径,指出新时期加强效应管理的重要性和迫切性,认为国内铝行业在效应管理方面赶上世界先进水平是可以实现的。
4) 135kA pre-baked anode reduction cell
135kA预焙槽
1.
Practices of prolonging the service life of 135kA pre-baked anode reduction cell;
根据135kA预焙阳极电解槽的生产实践,提出了采用合理的焙烧方法,控制135kA预焙槽长期低温平稳运行、小炉膛生产的措施,在电流效率提高的同时达到延长槽寿命的目标。
5) kA prebaked cell
85kA预焙槽
1.
Application of an advanced technology to 85kA prebaked cell and its optimization;
“四低一高”工艺在85kA预焙槽的应用与优化
6) kA Prebaking cell
186kA预焙槽
1.
Industrial Experiment for Dry Permiation-proof Material Used in 186kA Prebaking cell;
云南铝业股份有限公司186kA预焙槽干防渗料工业试验
补充资料：焙造
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参考词条