堿液循環(huán) (陰極) 系統(tǒng)-中英對照
供給堿液的主要工藝設(shè)計特征，在電解槽加滿和沖洗停車要求中作出定義正如3.2.4章節(jié)中的描述。本章節(jié)內(nèi)容對這些規(guī)定和其它額外要求進行

了闡述。
必須提供堿液進料低流量跳閘裝置，通過斷開整流器，防止陽極液室的堿液水位下降和組件損壞。由于短期流量控制造成的干擾，在低流量故

障時候保留60秒的斷開延遲，防止不必要的跳閘。
電解槽停車時，電解槽的堿液進料必須立即進行灌滿，并保持完整的進料流程。電解槽的灌滿流程有兩項可接受選項提供：
1.由一個專用的壓力槽提供。
2.由一個預(yù)留容器在鹽水進料槽通過一個完整的泵送系統(tǒng)提供。
以上兩例中，電解槽堿液進料的灌滿流程通過緊急啟動/停車閥門控制，而不受堿液供給流量控制閥控制。
在長期停車極化條件期間，所有的選擇必須保證裝滿和沖洗電解槽的鹽水進料，同時保證在排水之前進行電解槽的強制冷卻操作。要求至少安

裝二臺鹽水供給泵。
輸送管線設(shè)計
排放總管布局
對于BICHLORTM 電解槽而言，產(chǎn)生的液體和氣體流入每個單元槽的頂部時并不分開，而是順BICHLORTM出口總管排出，同時傳輸氣體和液體兩個

產(chǎn)品。這些氣體和液體通常用一個較大的T形連接裝置通過出口總管排出。
在氣體/液體分離點的輸送管線必須設(shè)計為，液體采用重力方式分離到陽極液和陰極液槽。在全部可能的操作條件下，出口輸送管線里的液體水

位必須保持在氣體液體分離點的水平下面。防止給離子膜和電解槽造成任何背面加壓，避免將液體帶進氣體總管。
為了這種情況，電解車間通常設(shè)置在底樓，方便對電解液槽發(fā)出指令。電解槽的氣體和液體分開點之間的升高差別和電解液槽的入口，必須能

承受液體壓降、電解槽和大氣壓，以及電解液槽的滿負荷操作壓力 （250 mbar） 之間的壓力差。如圖4.4.1 說明
在輸送管線的排水處設(shè)置進料封閉器，當電解槽準備維修時，電解槽流體出口處設(shè)置有一個隔間或者鏟形物，確保其它電解槽里沒有生產(chǎn)的氣

體進入該通道。 經(jīng)驗表明，連接電解車間液體壓力槽頂部的輸送管道可能發(fā)生問題，當隔間背后側(cè)的出氣口可能發(fā)生故障¬——或許受氣壓影

響和從壓力槽產(chǎn)生釋放氣體。連接電解車間壓力槽的底部可以使這個問題減小到最少，但會擋住封閉器，造成排水和收集破碎殘渣的困難。在

總管下方一半的位置采用一個斜角連接是最好的選擇。
Lye recycling (cathode) system
Supply main technological design features of lye in electrolytic cell fill and flushing the parking requirements been defined as described in section 3.2.4. This chapter is about the content of regulations and other additional requirements in this paper.
Low alkali liquor feed flow tripping device, must be provided by disconnect rectifier, prevent the anolyte chamber of lye water level decline and damage of components. Interference caused by short-term flow control, in the low flow
Disabled when disconnection of reserved 60 seconds delay, prevent unnecessary trip.
Parking electrolytic cell, cell inlet must immediately lye to fill up, and keep a complete feed process. Electrolytic tank filling process has two acceptable options provide:
(1) is provided by a dedicated pressure tank.
2. Reserve by a container in salt water feed channel through a complete system of pumping.
Both cases the electrolyser lye feed fill process through the emergency start/stop valve control, and there is no lye supply flow control valve control.
During the long-term parking polarization conditions, all you have to choose to ensure full and flushing feed brine electrolyzer, at the same time guarantee for forced cooling of electrolyzer operation before drainage. Requires at least Ann
Two salt water supply pump.
Pipeline design
Discharge duct layout
For BICHLORTM cell produced by liquid and gas flow into each unit tank top is not separated, but a suitable discharge BICHLORTM export manager, at the same time two transmission of gas and liquid
Products. Usually these gases and liquids with a larger tee joint device through the export manager.
In gas/liquid separation point must be designed for conveying pipeline, and liquid separation by way of gravity to the liquid anode and cathode liquid trough. In all possible operating conditions, the export of liquid water in the pipeline
Who must remain under the level of gas liquid separation point. To prevent to cause any pressure on the back of ionic membrane and electrolytic cell, to avoid the liquid into gas main.
To this case, the electrolytic workshop is usually set on the ground floor, convenient for electrolyte slot issue instructions. Electrolytic tank of gas and liquid separation point and the rise of differences between the electrolyte slot entrance, must be able to
Liquid pressure drop and electrolytic cell and atmospheric pressure, and electrolyte slot at full capacity the pressure differential between the operating pressure (250 mbar). As shown in figure 4.4.1 instructions
A setting in the drainage pipeline feed closure, when cell ready to repair, cell fluid outlet set have a compartment or spade, ensure there is no other cell production
Access to the channel. Experience has shown that connecting the electrolytic workshop liquid pressure tank at the top of the pipeline problem can occur, when the lateral compartment behind the outlet may be down, perhaps by air pressure
Ring and release gases from pressure tank. Connect the bottom of the electrolysis workshop pressure tank can reduce the problem to a minimum, but will block closure, cause problems for drainage and collecting crushing residue. in
The position of the main below half USES a bevel connection is the best choice.

2014.8.27