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1)  seabed anode
海床阳极
2)  The anode bed
阳极地床
3)  Deep well anode ground bed
深阳极地床
4)  shallow anode bed
浅阳极地床
5)  deep-well anode groundbed
深井阳极地床
1.
The applicable condition of the impressed current cathodic protection and sacrificial anode cathodic protection are analyzed, and the determination of main parameters, the process calculation and the application example for deep-well anode groundbed impressed current cathodic protection are discussed .
分析了强制电流阴极保护和牺牲阳极阴极保护的适用条件,论述了深井阳极地床强制电流阴极保护系统设计主要参数的确定、工艺计算及应用实例。
6)  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。
补充资料:银阳极泥提银(见铜阳极泥提金银)


银阳极泥提银(见铜阳极泥提金银)
extraction of silver from silver anode slime

y In yongJ,nl tlyln银阳极泥提银(extraetion of Silve:fr()nl 511一ver anode slime)见铜阳极泥提金银
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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