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1)  cation exchanger
阳床
1.
Improvement on reclamation of cation exchanger by two-step acid feeding;
应用"二步进酸"法可提高阳床的再生效果
2.
By analyzing the causes affecting the operational cycles of cation exchangers and conducting experiments,the essay points out that the faulty design resulting in the insufficient height of pressing resin layer, the lower position mid draining device and its slow flow speed causes the unsteady operational periods,overabundance of regenerative ratio cost and difficult washing.
从影响阳离子交换器运行周期的诸多因素入手 ,通过多种试验 ,找出了由于设计原因引起的树脂压脂层高度不够、中排 (中间排液装置 )位置偏低 ,且流速太小 ,从而造成阳床出水周期不稳定、再生比耗过大、正洗困难的状况 ,并对其进行了改造 ,收到了很好的效
3.
It in-dicates that to stre ngthen the control for the condensate cation exchanger can not only reduce the costfor condensate refining,but also guarantee the stable oporation Of condensate refining devlse.
主要是对精制冷凝液阳床运行终点的确定,树脂再生关键步骤的控制以及树脂铁污染后的复苏等问题进行讨论,说明加强冷凝液阳床管理不仅可以降低精制冷凝液的成本,而且是保证冷凝液精制装置稳定运行的重要手段。
2)  The anode bed
阳极地床
3)  fore negative bed
前置阳床
4)  cationic double-chamber bed
阳双室床
1.
After analyzing those problems found in the actual operation of cationic double-chamber bed,the measures are worked out to improve the operating capacity of resin and to reduce the cost of water production.
通过对阳双室床在实际运行中遇到的问题进行分析,制定措施,提高树脂总工作交换容量,降低制水成本。
5)  high speed cation exchanger
高速阳床
1.
Based on the analysis of ammoniated operation principle of high speed cation exchanger for condensate fine treatment,and research of the cause for chlorine leakage and increase of boiler water conductivity,cation exchanger ammoniated operation is proved to be necessary.
通过分析凝结水精处理高速阳床氨化运行的原理,查找榆社电厂高速阴床漏氯和炉水电导率升高的原因,明确了阳床氨化运行的必要性,并提出了改进串联式高速阳、阴床出水水质的措施。
6)  mixed-bed with cation layer
阳层混床
补充资料:沸腾床燃烧(见流化床燃烧)


沸腾床燃烧(见流化床燃烧)
boiling-bed combustion:see fluidized-bed combustion

沸腾床燃烧(boiling一bed eombustion)见流化床燃烧。
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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