逆流再生離子交換器使用說明書

1、逆流再生離子交換器Countercurrent regeneration of ion exchanger使用說明書Operating Instruction- 9 -一、工藝原理Technical principle逆流再生離子交換器（分陽床、陰床、鈉床亦稱軟化器）為無頂壓逆流再生固定床，用于軟化水、除鹽水的制備；在制水工藝上采用逆流制水。Countercurrent regeneration of ion exchanger (Inclouding cation exchanger, anion exchanger, sodium ion exchanger is also called

2、sodium softener) for no roof pressure countercurrent regeneration fixed bed, used to soften water, in addition to the preparation of brine; On the water making process by water flow system.當離子交換器出水再生工藝采用無頂壓逆流再生，具有操作簡單、外部管系簡單、不需要任何頂壓設施，投資省的優(yōu)點。再生時，稀釋好的再生劑由下向上逆向流經(jīng)樹脂層，將從下到上依再生不同層態(tài)的樹脂，這種方式可以使樹脂層獲得較好的再生效果

3、，再生劑可以得到較高的利用率，其次，具有廢液排放量少,自用水率低等優(yōu)點。When ion exchanger regeneration process using no roof pressure water countercurrent regeneration, with easy operation, simple external piping, do not need any jacking facilities, the advantages of saving investment. Regeneration, dilute good regenerant from down t

4、o up reverse flowing through the resin layer, the state of different layers from bottom to top in accordance with the regeneration of the resin, this way can make the resin layer to obtain a good effect of regeneration, regeneration agent can get higher efficiency, second, with less waste emissions,

5、 the low water use ratio etc.二、技術參數(shù)Technical parameters1. 進水濁度Influent water turbidity： < 1-2 NTU2. 出水水質Effluent turbidity 強酸陽床：鈉泄漏不大于100ug/l，一般在20-30ug/lStrong acid cation exchanger:Sodium leakage is not more than 100 ug/l, generally in the 20-30 ug/l.強堿陰床：SiO2泄漏不大于100ug/l，一般在20-50ug/l,出水電導率<

6、 10us/cm。Strong alkali anion exchanger:SiO2 leakage is not more than 100 ug/l, generally in the 20-50 ug/l,effluent conductivity < 10 us/cm.軟化器： 出水硬度< 20ug-N/l。Sodium softener:Effluent hardness< 20ug-N/l.3. 工作壓力Working pressure: < 0.6MPa 4. 工作溫度Working temperature: 5-455. 運行流速Operating v

7、elocity: 20-30m/h6. 水反洗強度Water backwashing strength: 陽樹脂Cation resins 10-15m/h 陰樹脂Anion resins 8-10m/h7. 再生流速Regeneration velocity: 5m/h8. 再生液濃度Renewable liquid concentration: 1-3% 軟化床的食鹽濃度可適當加大9. 填料高度Packing layer height: 1600mm（cation exchanger）；2500mm（anion exchanger） 10承托層Retainer layer：層次Level（

8、自上向下since the last down）尺寸Size（mm）厚度Thcikness（mm）層次Level（自上向下since the last down）尺寸Size（mm）厚度Thcikness（mm）112200481615022415051632250348100注：最下一層承托層的頂部至少應高于配水孔眼100 mm。Note:The next layer of retainer layer must be at least above the top of the water hole 100 mm.三、結構形式Structure form設備本體是帶上下橢圓封頭的圓柱形鋼結構

9、，內(nèi)壁襯兩層耐酸橡膠防腐；內(nèi)部在進水口設有擋水板，設備內(nèi)部中排裝置由不銹鋼管、不銹鋼纏繞管焊制而成; 下部為多孔板水帽集水裝置（或按要求采用承托層）。設備本體內(nèi)根據(jù)具體水質具體要求裝填樹脂。Equipment ontology is with elliptical head up and down cylinder of steel structure, internal lining of two layers of acid-resistant rubber corrosion; Inside the water inlet is equipped with the manger, mid

10、dle device inside the equipment made of stainless steel pipe, stainless steel coil welded; Lower water collection device for the porous plate water cap (or layer USES the retainer as required). Equipment to fill the body according to the requirements to the specific water quality resin.設備的本體外部裝配有各種控

11、制閥門并留有各種儀表接口，便于用戶現(xiàn)場裝接或實現(xiàn)水站正常運行。Equipment ontology external equipped with a variety of control valves and had all kinds of instrument interface, making it easy for users to the site assembling or achieve normal operation of water stations.四. 設備的安裝The installation of the equipment1） 安裝前檢查土建基礎是否按設計要求施工

12、。1）Before the installation check whether civil engineering foundation construction according to design requirements.2） 設備按設計圖紙進行就位，調整支腿墊鐵并檢查進出口法蘭的水平度和垂直度。2）Equipment in place in accordance with design drawings and leg to adjust shim and check the levelness of the import and export of the flange and

13、verticality.3） 將設備和基礎預埋鐵板焊接固定，固定后再次校驗進出口法蘭的水平度和垂直度。3）Based embedded iron welding equipment and fixed, fixed after once again check the levelness of the import and export of the flange and verticality.4） 將設備本體配管按編號區(qū)分后依設計圖紙進行組裝，每段管道組裝前應用干凈抹布對內(nèi)壁進行清潔工作，組裝后應保持配管軸線橫平豎直，閥門朝向合理（手動閥手柄朝前，氣動閥啟動頭朝上）。4）Piping eq

14、uipment body according to the numbered in accordance with the design drawings for assembly, after each section of the pipe assembly application clean dishcloth to clean the lining work before, after assembly should maintain the pipe axis horizontal even vertical, valve towards reasonable (manual val

15、ve handle forward, pneumatic valve start upside).5） 檢查本體閥門開關靈活，有不靈活的情況及時整改。5）Check valve body flexible switch, timely rectification is not flexible.6） 設備本體配管完成后應對閥組進行必要的支撐工作等。6）Piping equipment ontology cope with valve set after the completion of necessary support work, etc.7） 安裝設備上配帶的進出水壓力表、取樣閥等；進出

16、水管道上如有流量、電導等探頭座應用堵頭堵住。7） Installation of equipment on display in and out of the water pressure gauge, sampling valve, etc.; In and out of the water pipe channel such as traffic, conductance probe plug seat application block.五、初次運行For the first time to run1）沖洗wash考慮到設備和管道連接時的電焊殘渣、管道初次投用時的表面污物，設備初次投入運

17、行時應進行沖洗。Considering the equipment and pipeline connection welding residue, pipe surface dirt putting-in-service proactively for the first time, equipment should be put into operation for the first time to wash.A、 打開設備的人孔法蘭將設備內(nèi)的零件重新緊固，并確認罐內(nèi)部件（如水帽等）不缺少；封閉人孔法蘭。A、Open the equipment of manhole flange wil

18、l be retightened equipment within the parts, and confirm the tank parts (like a cap, etc.) no lack; Close the manhole flange.B、打開設備的下排閥，確認設備的出水閥關閉。B、Open the discharge valve of the device, make sure equipment water valve closed.C、打開設備進水閥、排氣閥，開啟前系統(tǒng)，至設備排氣口出水后關閉排氣閥，沖洗設備至出水清晰為沖洗終點。 C、Open the inlet valv

19、e, exhaust valve, open system before, to close the discharge valve, after equipment outlet water flushing equipment to clear water to rinse the end.2）裝填樹脂F(xiàn)illing resin打開人孔，如果出水裝置采用承托層結構則按所設計的承托層高度裝填，裝填完畢后再裝樹脂。按所設計的樹脂高度，依次裝入，填完后抹平，以中排裝置支管以上200mm為基準線（已包括壓脂層的高度）。沒有中排裝置的應在交換器裝填前劃線確認。濾料裝填完畢后封閉人孔。Open man

20、hole, if water device adopts the retainer structure is designed according to the layer of retainer high loading, loading after the reload resin. According to the designed height of resin, load, in turn, after complete branch of the middle device above 200 mm for reference line (including the height

21、of the lipid layer pressure). No bottom of device should be crossed in front of the switch loading confirmation. Filter material manhole closed when loading is finished.3） 按新樹脂處理方法進行再生處理。3）According to the new resin treatment method for regeneration.4）設備正常運行后應檢測進出水壓差不大于0.5bar，檢驗進出水的流量顯示。4）After the

22、normal operation of equipment should detection in and out of the water pressure difference is not greater than 0.5 bar, check in and out of the water flow. 六、操作說明Operating instructions1 正洗Conventional well-flushing打開進水閥、排氣閥，水流從上而下，當水充滿設備時打開下排閥，關閉排氣閥，進入正洗階段，濾速控制在2030m/h，當出水水質達到要求后，打開出水閥，關閉下排閥，進入制水正況。

23、Open the inlet valve, exhaust valve, water flow from the top down, when the water is full of equipment open the discharge valve, close the discharge valve, is into the washing stage, filter speed control in 20 30 m/h, when water quality requirements, open the discharge valve, close the discharge val

24、ve, the water entering the system is.2 制水Water making制水流速控制在2030m/h，直至出水達不到指標或達到規(guī)定產(chǎn)水量，運行周期結束。System of water flow rate control in 20 30 m/h, water rate to water than index or to regulation, end of the run cycle.3 再生Regenerationa. 排水Drainage打開中排閥、排氣閥，將容器內(nèi)積水排至壓脂層面處,并使壓脂層處于干的狀態(tài)。Open the bottom valve, e

25、xhaust valve, pressure container water to lipid levels, and makes the pressure lipid layer in the dry state.b. 再生劑注入Regenerant injection打開再生系統(tǒng)稀釋水閥、濃再生液閥，打開離子交換器進再生液閥、中排閥，再生流速控制在5m/h左右，以樹脂層不擾動為控制標準；供陰床再生水的工作溫度應加熱至40-45，可取得較好的再生效果。Open the regeneration system dilution water valve, strong renewable liq

26、uid valve, open the ion exchanger into renewable liquid valve, bottom valve, regenerative velocity control at about 5 m/h, with the resin layer is not disturbance as the standard; Work for Yin bed reclaimed water should be heated to a temperature of 40-45 , good regeneration effect can be obtained.c

27、. 置換清洗Replacement washing關閉再生系統(tǒng)濃再生液閥，流速同進再生液流速；陽床置換清洗終點，排水酸度達到要求；陰床置換清洗終點，排水堿度達到要求。Closed system strong regenerative liquid valve, flow velocity with into renewable liquid velocity; Yang bed replacement finish cleaning, drainage acidity requirements; Yin bed replacement finish cleaning, drainage bas

28、icity is achieved.d. 小正洗Small conventional well-flushing打開進水閥,排氣閥,當水充滿設備時,關閉排氣閥,打開中排閥，控制小正洗流速在15m/h,小正洗時間在5分鐘。Open the inlet valve, exhaust valve, when the water is full of equipment, close the discharge valve, the valve open, small control is velocity in 15 m/h, small washing time is in 5 minutes.e

29、. 正洗Conventional well-flushing打開下排閥、進水閥 ,以20-30m/h的流速正洗至排放水達到規(guī)定的水質指標,轉入串聯(lián)正洗。Open the discharge valve, inlet valve, with 20-30 m/h of the flow velocity is wash to discharge water to meet the water quality indexes, into series are washed.f. 串聯(lián)正洗In series conventional well-flushing打開陽床進水閥、出水閥，陰床進水閥、下排閥

30、，按正常工作流速控制，以出水水質符合運行控制指標為終點。Open cation exchanger water valve, water valve, Cation exchanger inlet valve, discharge valve, according to the normal work flow rate control, with effluent water quality conforms to the operation control index for the finish.4 大反洗Big backwashing離子交換器的運行操作除上述說明外，還有一項大反洗工序

31、。一般在需要徹底清除樹脂層內(nèi)污垢、破碎樹脂及雜質時進行，實際運行中可間隔幾個或十幾個周期進行一次。大反洗工序在再生之前，操作如下：Ion exchanger operation in addition to the above instructions, there is also a big backwashing process. In need to thoroughly remove dirt, broken resin in the resin layer and the impurities, in the actual operation can be several or a

32、dozen cycle. Big backwashing process before regeneration, the operation is as follows:打開反洗閥、上排閥，松動樹脂層，將被樹脂截留的機械雜質和破碎樹脂，隨反洗水流帶走。時間10-15分鐘或以排水清晰透明為終點，反洗流速為10m/h左右，以樹脂反洗展開率50%-80%，且正常粒徑樹脂不被水帶走來控制。Open the backwashing valves, line valves, loose resin layer, will be resin intercept mechanical impurity an

33、d broken resin, with backwashing water flow away. Time 10-15 minutes or drainage clarity to the finish line, backwashing velocity of about 10 m/h, with resin backwashing expansion rate of 50% to 80%, and the normal resin particle size is not coming water control.再生及再生后的工序，除需增大再生劑用量（一般為平時再生劑量的2倍）外，其他工況操作均同前述。After regeneratio