JPH01127096A - Water treatment apparatus of electric precipitator - Google Patents
Water treatment apparatus of electric precipitatorInfo
- Publication number
- JPH01127096A JPH01127096A JP28697487A JP28697487A JPH01127096A JP H01127096 A JPH01127096 A JP H01127096A JP 28697487 A JP28697487 A JP 28697487A JP 28697487 A JP28697487 A JP 28697487A JP H01127096 A JPH01127096 A JP H01127096A
- Authority
- JP
- Japan
- Prior art keywords
- amount
- flocculant
- sewage
- polluted water
- storage tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 239000012716 precipitator Substances 0.000 title abstract 3
- 238000005406 washing Methods 0.000 claims abstract description 4
- 239000010865 sewage Substances 0.000 claims description 54
- 239000012717 electrostatic precipitator Substances 0.000 claims description 29
- 239000000428 dust Substances 0.000 claims description 22
- 239000002351 wastewater Substances 0.000 claims description 19
- 239000004071 soot Substances 0.000 claims description 18
- 230000006866 deterioration Effects 0.000 abstract description 2
- 238000001514 detection method Methods 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 22
- 238000000034 method Methods 0.000 description 8
- 239000002245 particle Substances 0.000 description 5
- 239000000701 coagulant Substances 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000004887 air purification Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Abstract
Description
この発明は、電気集じん装置、特に自動車道トンネル内
の空気を清浄化するために設置される電気集じん装置の
洗浄汚水を処理する水処理装置に関する。The present invention relates to an electrostatic precipitator, and particularly to a water treatment device for treating waste water washed from an electrostatic precipitator installed to purify the air in a highway tunnel.
煤じんを含んだ空気を清浄化する装置として電気集じん
装置が知られている。この電気集じん装置は、コロナ放
電を利用して空気中の煤じん粒子に電荷を与え、この帯
電粒子にクーロン力を作用させて集じん極板に捕集する
ものであるが、捕集された煤じんば集じん通路内に堆積
するので、−定期間ごとにこの煤じんを除去する必要が
ある。
煤じん除去手段としては、一般に空気洗浄方式が用いら
れており、例えば特公昭57−16864号公報にも示
されている。これは極板に堆積した煤じんに空気を吹付
けて払い落とすもので、装置が簡便であり、除去した煤
じんの機外への排出も容易であるため一般に広く採用さ
れている。
しかし上記空気洗浄方式は、非粘着性の煤じんの除去に
は有効であるが、粘着性を有する煤じんの除去に対して
は洗浄力が弱いという欠点がある。
一方、近時自動車に対するスパイクタイヤの装着が増え
、冬期路面が削られて発生するコンクリートダストが問
題となっているが、自動車道トンネルの空気清浄化設備
で用いられる電気集じん装置にもその影響が及んできて
いる。
すなわち、コンクリートダストは塩化カルシウムなどの
融雪剤と結合すると粘土状の粒子となるが、この粘着粒
子がタイヤに付着して上記トンネル内に持ち込まれ電気
集じん装置に捕集されると、上記空気洗浄方式では除去
できないのである。
このような場合の有効な洗浄手段として水洗浄方式があ
る。これは、上記空気吹付けに替えて加圧した水を吹付
けるもので、噴水の洗浄力は空気に比べて遥かに大きく
、上記粘着粒子に対しても十分な効力を有している。
ところが、洗浄力の点では非常に優れた水洗浄方式もそ
の他の面でいろいろと厄介な問題を含んでおり、その一
つに洗浄により発生する汚水の処理がある。電気集じん
装置の洗浄はこれまで空気洗浄方式が主流で、水洗浄は
その後の汚水処理が面倒なことから、特に電気集じん装
置が大規模に用いられている自動車道トンネルの空気清
浄化設備などでは未だ実用化されるに至っていない。
したがって上記汚水の処理も色々の点で不分明で、懸濁
煤じんの凝集剤の選定、凝集後の煤じんの分離、さらに
その後の汚泥の脱水処理など電気集じん装置の水洗浄の
実施化には解決すべき課題が多い。Electrostatic precipitators are known as devices for cleaning air containing soot and dust. This electrostatic precipitator uses corona discharge to charge soot and dust particles in the air, applies Coulomb force to the charged particles, and collects them on a dust collecting electrode plate. Since the soot and dust accumulates in the dust collection passage, it is necessary to remove this soot and dust at regular intervals. As a means for removing soot and dust, an air cleaning method is generally used, and is disclosed in, for example, Japanese Patent Publication No. 16864/1983. This method blows air off the soot and dust that has accumulated on the electrode plates, and is widely used because the device is simple and the removed soot and dust can be easily discharged outside the machine. However, although the above-mentioned air cleaning method is effective in removing non-adhesive soot and dust, it has a drawback in that its cleaning power is weak in removing sticky soot and dust. On the other hand, as more and more cars are being fitted with spiked tires, concrete dust generated by scraping the road surface in winter has become a problem, and this also has an impact on electrostatic precipitators used in air purification equipment in expressway tunnels. is reaching. In other words, concrete dust becomes clay-like particles when combined with a snow melting agent such as calcium chloride, but when these sticky particles adhere to tires and are brought into the tunnel and collected by the electrostatic precipitator, the air It cannot be removed by cleaning methods. A water cleaning method is an effective cleaning method in such a case. This sprays pressurized water in place of the above-mentioned air spray, and the cleaning power of the fountain is far greater than that of air, and is also sufficiently effective against the above-mentioned adhesive particles. However, even the water cleaning method, which has excellent cleaning power, has many troublesome problems in other aspects, one of which is the treatment of wastewater generated during cleaning. Up until now, air cleaning has been the mainstream method for cleaning electrostatic precipitators, and water cleaning is difficult to treat afterward, so it has been particularly useful for air purification equipment in expressway tunnels where electrostatic precipitators are used on a large scale. It has not yet been put into practical use. Therefore, various aspects of the treatment of the above-mentioned sewage are unclear, including the selection of a flocculant for suspended soot, the separation of soot after flocculation, and the implementation of water cleaning for electrostatic precipitators, including subsequent dewatering of sludge. There are many issues that need to be solved.
さて、下水道の水処理など従来一般の水処理では、排水
量が多く、かつ大体一定している。そのため、水処理の
凝集工程で使用する凝集剤の溶解液は、排水量に合わせ
て1〜数日分を作業員が手作業で調製している場合が多
い。
ところが、電気集じん装置の洗浄の場合は、−般の場合
とは異なり、発生する汚水量が日によって一定しないこ
とが多い。すなわち、汚水量は電気集じん装置の洗浄回
数に依存するのであるが、この洗浄回数は空気中の煤じ
んの量に左右されるため、その日の条件によって大いに
異なってくる。
例えば、上記自動車道トンネル用の電気集じん装置にお
いても、その日の交通量によって洗浄回数、したがって
洗浄汚水量が大変に不規則である。
一方、トンネル内に作業員を常駐させておくことは困難
であるため、凝集剤の溶解液は数日分まとめて調製して
おくのであるが、安全を考えて予想される汚水の最大発
生量に合わせて調製していた。
しかし、これでは汚水の実際の発生量が少なかった場合
、特に時として汚水が全熱発生しなかった場合には凝集
剤の溶解液が余ることになる。凝集剤は一度溶解させる
と数日で性能が劣化するので、余った溶解液は廃棄しな
ければならず大変無駄であった。
そこでこの発明は、凝集処理する電気集じん装置の洗浄
汚水の量と、その水処理のために調製する凝集剤の溶解
液の量とを常に均衡させ、効率良く汚水の凝集処理を行
うことのできる電気集じん装置の水処理装置を提供する
ことを目的とするものである。Now, in conventional water treatment such as sewerage water treatment, the amount of wastewater is large and generally constant. Therefore, in many cases, a solution of the flocculant used in the flocculation step of water treatment is manually prepared by a worker for one to several days depending on the amount of waste water. However, in the case of cleaning an electrostatic precipitator, unlike in other cases, the amount of sewage generated is often not constant from day to day. In other words, the amount of sewage depends on the number of times the electrostatic precipitator is washed, and the number of times the electrostatic precipitator is washed depends on the amount of soot and dust in the air, and therefore varies greatly depending on the conditions of the day. For example, even in the above-mentioned electrostatic precipitator for highway tunnels, the number of times of cleaning, and therefore the amount of cleaning wastewater, is very irregular depending on the traffic volume of the day. On the other hand, it is difficult to keep workers permanently stationed inside the tunnel, so the flocculant solution is prepared in batches for several days, but for safety reasons, the maximum amount of wastewater expected to be generated is It was prepared accordingly. However, this results in a surplus of flocculant solution when the actual amount of sewage generated is small, especially when the sewage does not generate all of its heat. Once the flocculant is dissolved, its performance deteriorates within a few days, so the remaining solution had to be discarded, which was very wasteful. Therefore, this invention aims to constantly balance the amount of washed sewage from an electrostatic precipitator to be coagulated and the amount of a flocculant solution prepared for the water treatment, thereby efficiently coagulating sewage. The purpose of this invention is to provide a water treatment device using an electrostatic precipitator that can be used as an electrostatic precipitator.
この発明は上記目的を達成するために、電気集じん装置
を水洗浄して生じた汚水に凝集剤を添加し、前記汚水中
の懸濁煤じんを凝集させて分離する電気集じん装置の水
処理装置において、電気集じん装置から生じる汚水を一
旦貯溜する汚水貯溜槽と、この汚水貯溜槽内の汚水が一
定量に達したことを検知するレベル計と、このレベル計
からの信号により前記汚水貯溜槽内の汚水量に対応する
所定量の凝集剤溶解液を調製する凝集剤溶解装置とを設
けるものとする。In order to achieve the above object, this invention adds a flocculant to the waste water generated by washing an electrostatic precipitator with water, and collects and separates the suspended soot and dust in the waste water. In the treatment equipment, there is a sewage storage tank that temporarily stores sewage generated from the electrostatic precipitator, a level meter that detects when the sewage in this sewage storage tank has reached a certain amount, and a signal from this level meter that collects the sewage. A flocculant dissolving device for preparing a predetermined amount of flocculant solution corresponding to the amount of wastewater in the storage tank shall be provided.
この発明によれば、凝集剤溶解液の調製は汚水量が一定
量に達してから初めて開始され、しかも溶解液の量はこ
の汚水量に対応したものであるので、発生する汚水の量
の変動にかかわらず、常に必要十分な量の凝集剤溶解液
を準備することができる。According to this invention, the preparation of the flocculant solution is started only after the amount of sewage reaches a certain amount, and since the amount of the solution corresponds to this amount of sewage, fluctuations in the amount of sewage generated can be avoided. Regardless of the situation, it is possible to always prepare a necessary and sufficient amount of flocculant solution.
以下図に基づいて、この発明の詳細な説明する。
第1図はこの発明の水処理装置の要部の構成を示す系統
図である。
第1図において、電気集じん装置1には洗浄配管2を通
して加圧された洗浄水が供給され、この洗浄水は煤じん
が堆積した集じん通路に図示しない噴水ノズルを介して
噴射される。煤じんを洗い落とした洗浄水は、煤じんが
懸濁した汚水となり、排水管3を通してひとまず集じん
装置下部の汚水ピット4に受は入れられる。電気集じん
装置の洗浄には、1回当たり約4rrrの水が使用され
、汚水ピット4の容量は5ボになっている。
汚水ピット4には、汚水の水位を検知するレベル計5が
設けられており、汚水ピット内の水量がある量まで達す
るとこのレベル計5の信号により制御装置6を通して凝
集剤溶解装置7がONされる。これにより、凝集剤溶解
装置7には図示しない凝集剤貯蔵箱から所定量の凝集剤
が投入され、さらに水が加えられて溶解槽7a内で凝集
剤の溶解液が調製される。
また上記レベル針の信号により、同時に汚水ピット4の
ポンプ8がONされ、汚水は汚水貯溜槽9に輸送される
。汚水貯溜槽9は、汚水ピット4とほぼ同一の容量を有
しているが、汚水ピット4内の汚水が移され汚水貯溜槽
9内の汚水量が一定量まで達するとレベル計lOが動作
する。このレベル計10の信号により制御装置11を通
してポンプ8がOFFされ、同時にポンプ12がONさ
れて溶解槽7a内の凝集剤の溶解液が全部汚水貯溜槽9
内に注入される。
汚水貯溜槽9内では、撹拌機13の撹拌の下に汚水と凝
集剤との混合が行われる。所定時間、例えば10分程度
経過して、汚水貯溜槽9での煤じんの凝集・フロック形
成が十分行われると、図示しないタイマの動作によりポ
ンプ14がONされ、汚水貯溜槽9内の被処理液は次の
固液分離工程に送られる。
上記実施例では、汚水ピット4のレベル計5の動作によ
り凝集剤溶解装置7をONする場合を示したが、汚水貯
溜槽9のレベル計13の動作により凝集剤溶解装置7を
ONL、その後タイマの動作により一定時間後にポンプ
12をONして凝集剤の溶解液を汚水貯溜槽9内に注入
することも可能である。特に、電気集じん装置1及びこ
れに付設される汚水ピット4が複数基設備されており、
これらに共通して1基の゛汚水貯溜槽9が設けられてい
るときには、各電気集じん装置1から汚水貯溜槽9に随
時流入する汚水が一定量に達したとき、レベル計13の
動作により凝集剤溶解装置7をONする方式が良い。The present invention will be described in detail below based on the drawings. FIG. 1 is a system diagram showing the configuration of the main parts of the water treatment apparatus of the present invention. In FIG. 1, pressurized cleaning water is supplied to an electrostatic precipitator 1 through a cleaning pipe 2, and this cleaning water is sprayed through a fountain nozzle (not shown) into a dust collection passage where soot and dust have accumulated. The washing water that has washed away the soot and dust becomes sewage in which soot and dust are suspended, and is temporarily received in the sewage pit 4 at the bottom of the dust collector through the drain pipe 3. Approximately 4 rrr of water is used each time to clean the electrostatic precipitator, and the capacity of the sewage pit 4 is 5 bottles. The sewage pit 4 is provided with a level meter 5 that detects the water level of the sewage, and when the amount of water in the sewage pit reaches a certain level, a signal from the level meter 5 turns on the flocculant dissolving device 7 through the control device 6. be done. As a result, a predetermined amount of flocculant is charged into the flocculant dissolving device 7 from a flocculant storage box (not shown), water is further added, and a flocculant solution is prepared in the dissolution tank 7a. Furthermore, the pump 8 of the sewage pit 4 is turned on at the same time by the signal from the level needle, and the sewage is transported to the sewage storage tank 9. The sewage storage tank 9 has almost the same capacity as the sewage pit 4, but when the sewage in the sewage pit 4 is transferred and the amount of sewage in the sewage storage tank 9 reaches a certain amount, the level meter IO is activated. . The signal from the level meter 10 turns off the pump 8 through the control device 11, and at the same time turns on the pump 12, so that all of the coagulant solution in the dissolution tank 7a is drained into the wastewater storage tank 9.
injected into the body. In the wastewater storage tank 9, the wastewater and the flocculant are mixed under stirring by the stirrer 13. When a predetermined period of time, for example about 10 minutes, has passed and the soot and dust have sufficiently coagulated and formed flocs in the wastewater storage tank 9, the pump 14 is turned on by the operation of a timer (not shown), and the to-be-treated wastewater in the wastewater storage tank 9 is turned on. The liquid is sent to the next solid-liquid separation step. In the above embodiment, the flocculant dissolving device 7 is turned ON by the operation of the level meter 5 of the sewage pit 4, but the flocculant dissolving device 7 is turned ON by the operation of the level meter 13 of the sewage storage tank 9, and then the timer is activated. It is also possible to turn on the pump 12 after a certain period of time and inject the flocculant solution into the wastewater storage tank 9 by the operation of the above. In particular, a plurality of electrostatic precipitators 1 and sewage pits 4 attached thereto are installed,
When one sewage storage tank 9 is provided in common to these devices, when the sewage that flows from each electrostatic precipitator 1 into the sewage storage tank 9 reaches a certain amount, the level meter 13 operates. It is preferable to turn on the flocculant dissolving device 7.
この発明は、電気集じん装置から生じる汚水を一旦貯溜
する汚水貯溜槽と、この汚水貯溜槽内の汚水が一定量に
達したことを検知するレベル計と、このレベル計からの
信号により前記汚水量に対応する所定量の凝集剤溶解液
を調製する凝集剤溶解装置とを設け、汚水量が一定量に
達するとこの汚水量に対応する所定量の凝集剤溶解液を
調製し、汚水の凝集処理に際してこの凝集剤溶解液をそ
の都度使い切るようにしたので、凝集剤を無駄に劣化さ
せることを防止し、電気集じん装置の洗浄汚水の水処理
を効率的に行うことができる。This invention includes a sewage storage tank that temporarily stores sewage generated from an electrostatic precipitator, a level meter that detects when the sewage in this sewage storage tank reaches a certain amount, and a signal from the level meter that detects whether the sewage is A flocculant dissolving device is installed to prepare a predetermined amount of coagulant solution corresponding to the amount of sewage, and when the amount of sewage reaches a certain amount, a predetermined amount of coagulant solution corresponding to the amount of sewage is prepared, and the sewage is coagulated. Since this flocculant solution is used up each time during treatment, wasteful deterioration of the flocculant can be prevented, and wastewater washed from an electrostatic precipitator can be efficiently treated.
第1図は、この発明の実施例を示す要部系統図である。
1;電気集じん装置、2;洗浄配管、3:汚水排水管、
4:汚水ピット、5ニレベル計、7:凝集剤溶解装置、
9:汚水貯溜槽、10ニレベル計。FIG. 1 is a system diagram of main parts showing an embodiment of the present invention. 1; Electrostatic precipitator, 2; Cleaning pipe, 3: Sewage drain pipe,
4: Sewage pit, 5 double level meter, 7: Coagulant dissolving device,
9: Sewage storage tank, 10 level meter.
Claims (1)
添加し、前記汚水中の懸濁煤じんを凝集させて分離する
電気集じん装置の水処理装置において、電気集じん装置
から生じる汚水を一旦貯溜する汚水貯溜槽と、この汚水
貯溜槽内の汚水が一定量に達したことを検知するレベル
計と、このレベル計からの信号により前記汚水貯溜槽内
の汚水量に対応する所定量の凝集剤溶解液を調製する凝
集剤溶解装置とを設けたことを特徴とする電気集じん装
置の水処理装置。1) In a water treatment device for an electrostatic precipitator, in which a flocculant is added to the wastewater generated by washing the electrostatic precipitator with water, and the suspended soot and dust in the wastewater is coagulated and separated, from the electrostatic precipitator. A sewage storage tank that temporarily stores the generated sewage, a level meter that detects when the sewage in this sewage storage tank reaches a certain amount, and a signal from this level meter that corresponds to the amount of sewage in the sewage storage tank. 1. A water treatment device for an electrostatic precipitator, comprising: a flocculant dissolving device for preparing a predetermined amount of flocculant solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28697487A JPH0632819B2 (en) | 1987-11-13 | 1987-11-13 | Water treatment equipment for electric dust collector |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28697487A JPH0632819B2 (en) | 1987-11-13 | 1987-11-13 | Water treatment equipment for electric dust collector |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01127096A true JPH01127096A (en) | 1989-05-19 |
JPH0632819B2 JPH0632819B2 (en) | 1994-05-02 |
Family
ID=17711368
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28697487A Expired - Lifetime JPH0632819B2 (en) | 1987-11-13 | 1987-11-13 | Water treatment equipment for electric dust collector |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0632819B2 (en) |
-
1987
- 1987-11-13 JP JP28697487A patent/JPH0632819B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0632819B2 (en) | 1994-05-02 |
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