JPH06238111A - Method for washing filter casing of filter - Google Patents
Method for washing filter casing of filterInfo
- Publication number
- JPH06238111A JPH06238111A JP41A JP11689792A JPH06238111A JP H06238111 A JPH06238111 A JP H06238111A JP 41 A JP41 A JP 41A JP 11689792 A JP11689792 A JP 11689792A JP H06238111 A JPH06238111 A JP H06238111A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- liquid
- tank
- layer
- outlet
- 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.)
- Pending
Links
Landscapes
- Filtration Of Liquid (AREA)
Abstract
(57)【要約】
【目的】 濾過層を紙等の繊維材,粉状態等の分散材か
らなる濾過助材を用いて形成するようにした濾過装置に
あって、濾過助材の効果的な除去が可能な濾過筒洗浄方
法を提供すること。
【構成】 濾材19を周面に設けた濾過筒17を一〜複
数個設け、前記濾材19の周面に濾過助材層xを形成し
たものにおいて、比重が水よりも小さな浮遊小片pを供
給して、その液面近くに密集させるようにしたから、液
の排出に伴う液面下降により、濾過助材層xを浮遊小片
pが掻き落とすこととなり、濾過助材層xの除去を効率
的に施し得る。
(57) [Abstract] [Purpose] A filter device in which a filter layer is formed by using a filter aid made of a fibrous material such as paper and a dispersant in a powder state. To provide a method for cleaning a filter cylinder that can be removed. [Structure] One to a plurality of filter cylinders 17 provided with a filter material 19 on the peripheral surface are provided, and a filter aid layer x is formed on the filter material 19, and floating small pieces p having a specific gravity smaller than that of water are supplied. Since the particles are made to be dense near the liquid surface, the floating small pieces p scrape off the filter auxiliary material layer x due to the liquid surface lowering accompanying the discharge of the liquid, and the removal of the filter auxiliary material layer x is efficiently performed. Can be applied to.
Description
【0001】[0001]
【産業上の利用分野】本発明は、メッキ処理液等の汚濁
液を清浄する濾過装置にあって、その濾過筒洗浄方法に
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter device for cleaning a contaminated liquid such as a plating solution, and a method for cleaning the filter cylinder.
【0002】[0002]
【従来の技術】被処理液の供給口,清浄液の流出口及び
液排出口を備えたタンク内に、外周の濾材面に繊維材,
布材等の分散材からなる濾過助材が被覆される濾過筒を
一〜複数個垂設して、その内部を前記流出口と連通させ
て、被処理液を前記濾過助材及び濾材面を透過させて濾
過筒内に流入させ、これにより、被処理液の濾過を施す
ようにした濾過装置は公知である。2. Description of the Related Art In a tank having a supply port for a liquid to be treated, an outlet for a clean liquid and a liquid outlet, a fiber material is attached to a filter medium surface on the outer periphery.
One to a plurality of filter cylinders covered with a filter aid made of a dispersant such as a cloth material are hung vertically, and the inside thereof is communicated with the outflow port, so that the liquid to be treated is transferred to the filter aid and the filter material surface. A filter device is known in which the liquid to be treated is filtered by allowing the liquid to permeate and flow into the filter cylinder.
【0003】この濾過筒の濾材面に紙等の繊維層を形成
して、これを濾過材層として、該濾過面に透過した被処
理液の濾過処理を施す濾過装置は、例えば特開昭55ー
59818号に開示されている。また、紙等の繊維材
と、粉状体とを濾材面に被着したものは特開昭62−4
5306号に開示されている。A filtering device for forming a fibrous layer of paper or the like on the filter material surface of this filter cylinder and using this as a filter material layer to filter the liquid to be treated which has permeated the filter surface is disclosed, for example, in Japanese Patent Laid-Open No. 55-55. -59818. Further, a filter material having a fibrous material such as paper and a powder material adhered to the surface of the filter material is disclosed in JP-A-62-4.
No. 5306.
【0004】[0004]
【発明が解決しようとする課題】本発明は、上述のよう
に濾過層を紙等の繊維材,粉状態等の分散材からなる濾
過助材を用いて形成するようにしたものにあって、濾過
筒の効果的な洗浄が可能な濾過装置の濾過筒洗浄方法の
提供を目的とするものである。DISCLOSURE OF THE INVENTION The present invention resides in that the filter layer is formed using a filter aid made of a fibrous material such as paper and a dispersant in a powder state as described above. An object of the present invention is to provide a method for cleaning a filter cylinder of a filtration device, which enables effective cleaning of the filter cylinder.
【0005】[0005]
【課題を解決するための手段】本発明は、タンク内に、
比重が水よりも小さな、浮遊小片を無数分散させ、液排
出口からの液排出によるタンク内の液位の下降にともな
って、前記浮遊小片により濾過助剤を掻き落とすように
したことを特徴とするものである。DISCLOSURE OF THE INVENTION The present invention is provided in a tank,
The specific gravity is smaller than that of water, innumerable floating pieces are dispersed, and as the liquid level in the tank is lowered by discharging the liquid from the liquid discharge port, the filter aid is scraped off by the floating particles. To do.
【0006】そして、浮遊小片としては合成樹脂片、多
角状ゴム片、大粒状活性炭、セラミック片等種々の材料
が適用される。As the floating small pieces, various materials such as synthetic resin pieces, polygonal rubber pieces, large granular activated carbon and ceramic pieces are applied.
【0007】[0007]
【作用】供給口から助材が分散含有された液をタンク内
に供給し、該分散液を濾過筒周面に形成された濾材を透
過させることにより、該濾材面に液中の濾過助材が被着
し、濾過助材層が形成される。そして、タンク内に被処
理液を供給して濾過運転すると、濾材と濾過助材層とに
より濾過作用を生じ、被処理液は清浄液となって流出口
から排出される。この時あらかじめ、タンク内には浮遊
小片が供給される。この浮遊小片は、比重が軽いから液
面側位置に密集する。The liquid containing the auxiliary material dispersed therein is supplied from the supply port into the tank, and the dispersion is passed through the filter material formed on the peripheral surface of the filter cylinder, whereby the filter auxiliary material in the liquid is applied to the surface of the filter material. Are deposited and a filter aid layer is formed. Then, when the liquid to be treated is supplied into the tank and the filtration operation is performed, the filtering action is caused by the filter medium and the filter aid layer, and the liquid to be treated becomes a clean liquid and is discharged from the outlet. At this time, floating pieces are supplied in advance into the tank. Since the floating particles have a low specific gravity, they are densely gathered at the liquid surface side position.
【0008】この濾過運転を継続すると、濾過助材層の
表面には濾塵層が形成され、その層厚の増加とともに、
タンク内の圧力が増大して、濾過効率が低下する。そこ
で処理液の供給口を遮断し、液排出口を開放してタンク
内の液を排出する。これに伴って、液面が下降し、液面
に密集する浮遊小片も該液面と共に下降し、濾過筒周面
の濾過助材を該濾材面から掻き落とす。このとき液面の
下降は液排出口からの空気の流入と、液の排出とが交互
して行われることによる上下の波動(バブリング)を生
じながら下降させれば、前記浮遊小片は濾過助材を上下
に擦過して掻き落とすこととなり、良好な剥離効率を達
成できる。When this filtration operation is continued, a filter dust layer is formed on the surface of the filter aid layer, and as the layer thickness increases,
The pressure in the tank increases and the filtration efficiency decreases. Therefore, the supply port of the processing liquid is shut off and the liquid discharge port is opened to discharge the liquid in the tank. Along with this, the liquid surface descends, and the floating pieces that are densely packed on the liquid surface also descend together with the liquid surface, scraping the filter aid on the peripheral surface of the filter cylinder from the filter material surface. At this time, if the liquid surface is lowered while causing the inflow of air from the liquid discharge port and the discharge of the liquid alternately to cause a vertical wave (bubbling), the floating small particles are filtered. Is scraped off by rubbing it up and down, and good peeling efficiency can be achieved.
【0009】またこの時流出口にエアー供給源を接続
し、濾過筒内に圧力空気を供給しても良い。Also, at this time, an air supply source may be connected to the outlet to supply pressurized air into the filter cylinder.
【0010】[0010]
【実施例】本発明の一実施例を添付図面について説明す
る。図1において、1はタンクであって、上部に鍔が形
成された管状本体2の上面に、円弧膨隆状の蓋枠3が被
着されてボルト4で固定されるとともに、管状本体2の
下部には、底枠5が外嵌している。前記底枠5の内周面
と管状本体2の周面間には、液流路6が形成され、前記
底枠5に液流路6に連通する供給口7が設けられる。該
供給口7は三方切換え弁8により開閉制御される流入管
路9と連通している。また底枠5の下底には開閉弁11
により開閉制御される液排出口10が設けられている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the accompanying drawings. In FIG. 1, reference numeral 1 denotes a tank, and an arc-bulging lid frame 3 is attached to the upper surface of a tubular main body 2 having a collar formed on the upper portion thereof and fixed with bolts 4, and a lower portion of the tubular main body 2 is attached. A bottom frame 5 is fitted on the outer frame. A liquid flow path 6 is formed between the inner peripheral surface of the bottom frame 5 and the peripheral surface of the tubular body 2, and a supply port 7 communicating with the liquid flow path 6 is provided in the bottom frame 5. The supply port 7 communicates with an inflow conduit 9 which is opened / closed by a three-way switching valve 8. On the lower bottom of the bottom frame 5, an on-off valve 11
A liquid outlet 10 is provided which is controlled to be opened and closed by.
【0011】前記管状本体2の上部内面には係止突起2
aが形成され、該係止突起2aには、伸縮性濾過筒17
が上方から挿入する複数の連結孔12が形成された取付
け板13が乗載されている。A locking projection 2 is formed on the inner surface of the upper portion of the tubular body 2.
a is formed, and the elastic projection cylinder 17 is provided on the locking projection 2a.
A mounting plate 13 having a plurality of connecting holes 12 inserted from above is mounted.
【0012】前記濾過筒17は、図1,4のように長尺
状コイル18の外周面に布材,ガラス繊維,テトロン,
ポリプロピレン等の繊維材からなる濾材19を周設し、
その一端のコイル18を密に拡径してこれを口縁20と
するとともに、他端には、ポリプロピレン等の樹脂製栓
材21を配設し、その下部で濾材19を加熱溶着するこ
とにより封止している。而て、一端が開口し、他端が閉
鎖した長尺方向に伸縮性を有する伸縮性濾過筒17が構
成される。この濾過筒17は例えば長さが 500mm,外径
12mm等の比較的細状のものが適用され得る。前記濾過筒
17の数は、一〜数十本その所要処理能力に対応して設
けることができる。As shown in FIGS. 1 and 4, the filter cylinder 17 has a cloth material, glass fiber, tetron,
A filter material 19 made of a fiber material such as polypropylene is provided around the
By closely expanding the diameter of the coil 18 at one end to use this as the rim 20, and disposing a resin plug material 21 such as polypropylene at the other end, and heating and welding the filter material 19 under the same. It is sealed. Thus, the stretchable filtration cylinder 17 having one end opened and the other end closed and having elasticity in the longitudinal direction is configured. The filter cylinder 17 has a length of 500 mm and an outer diameter, for example.
A relatively thin one such as 12 mm can be applied. The number of the filter cylinders 17 can be set to one to several tens corresponding to the required processing capacity.
【0013】前記濾過筒17は、連結孔12に上方から
挿入して、口縁20を連結孔12周縁に掛けて吊持され
る。そして取付け板13上には、前記連結孔12と上下
で一致する透孔14が形成された保持板15が被着され
てボルト16により相互に連結されている。The filter cylinder 17 is inserted into the connecting hole 12 from above, and the mouth edge 20 is hung from the periphery of the connecting hole 12 to be suspended. A holding plate 15 having a through hole 14 which is vertically aligned with the connecting hole 12 is attached to the mounting plate 13 and is connected to each other by a bolt 16.
【0014】前記保持板15と蓋枠3間には清浄液の液
溜23が形成され、蓋枠3上端に設けた流出口24と連
通している。すなわち、前記流出口24は、連結孔1
2,透孔14を介して各濾過筒17の内部と連通するこ
ととなる。さらに前記管状本体2の上部側壁には、エア
ー抜き口を兼用する液排出口30が設けられている。A liquid reservoir 23 for clean liquid is formed between the holding plate 15 and the lid frame 3 and communicates with an outlet 24 provided at the upper end of the lid frame 3. That is, the outlet 24 is connected to the connecting hole 1
2, It will connect with the inside of each filter cylinder 17 through the through hole 14. Further, on the upper side wall of the tubular body 2, there is provided a liquid outlet 30 which also serves as an air vent.
【0015】次に供給口7,流出口24及び液排出口3
0の管接続について説明する。前記流出口24は、清浄
液を回収する処理済槽(図示せず)と流出管路25によ
り連通している。そして流出管路25には清浄液の流下
を制御する三方切換え弁26と、加圧空気を発生させる
エアー供給源27への切換えを制御する三方切換え弁2
8が設けられている。Next, the supply port 7, the outlet 24 and the liquid outlet 3
The tube connection of 0 will be described. The outflow port 24 communicates with a treated tank (not shown) for collecting the clean liquid through an outflow pipe line 25. A three-way switching valve 26 that controls the flow of the clean liquid in the outflow conduit 25 and a three-way switching valve 2 that controls the switching to the air supply source 27 that generates pressurized air.
8 are provided.
【0016】また前記供給口7は、メッキ液槽等の原液
タンク40と流入管路9により連通している。前記流入
管路9には、ポンプ34が介装され、その吸入側に三方
切換え弁8を介して、助材液槽35の流出口に連通する
管路39が接続している。さらに三方切換え弁8の他供
給口は前記原液タンク40と接続されている。The supply port 7 communicates with a stock solution tank 40 such as a plating solution tank through an inflow conduit 9. A pump 34 is interposed in the inflow conduit 9, and a conduit 39 communicating with the outlet of the auxiliary material liquid tank 35 is connected to the suction side of the pump 34 via a three-way switching valve 8. Further, the other supply port of the three-way switching valve 8 is connected to the stock solution tank 40.
【0017】前記助材液槽35は、撹拌翼38が内装さ
れた供給筒36が立設され、開閉弁37を介して助材液
槽35内と連通している。また助材液槽35は、三方切
換え弁26を介して流出管路25と接続する管路41の
口端が挿入され、同じく液排出口30と開閉弁31が介
装された迂回管路32の口端が挿入されており、流出口
24及び液排出口30からの液が流入し得るようになっ
ている。The auxiliary material liquid tank 35 is provided with a supply cylinder 36 in which a stirring blade 38 is installed, and communicates with the auxiliary material liquid tank 35 through an opening / closing valve 37. Further, the auxiliary material liquid tank 35 is inserted with the mouth end of a conduit 41 connected to the outflow conduit 25 via the three-way switching valve 26, and a bypass conduit 32 in which a liquid discharge port 30 and an opening / closing valve 31 are also interposed. Is inserted so that the liquid from the outflow port 24 and the liquid discharge port 30 can flow in.
【0018】また前記タンク本体1a内には、比重が水
よりも小さな浮遊小片pが無数供給され、その比重差に
より液面近くで密集させている。この浮遊小片pとして
は合成樹脂片、多角状ゴム片、大粒状活性炭、セラミッ
ク片等種々の材料が適用される。具体的形状としては、
多角形状、短円柱形等種々の形状が適用され得る。前記
構成にあって、各種運転態様を以下説明する。In addition, an infinite number of floating small pieces p having a specific gravity smaller than that of water are supplied into the tank body 1a, and the small pieces p are concentrated near the liquid surface due to the difference in specific gravity. As the floating small pieces p, various materials such as synthetic resin pieces, polygonal rubber pieces, large granular activated carbon, and ceramic pieces are applied. As a concrete shape,
Various shapes such as a polygonal shape and a short cylindrical shape can be applied. In the above-mentioned configuration, various operating modes will be described below.
【0019】[濾過助材層形成]前記構成において、濾
過筒17の濾材19に濾過助材層xを形成する工程につ
いて説明する。まず、あらかじめ液を供給してある供給
筒36内に紙を供給して、撹拌翼38を回転し、該供給
筒36内で紙を繊維状に裁断し分散させる。次に、活性
炭,珪素土,石炭,金属粉末等種々の材料から一種又は
複数種混合してなる粉状体を混入する。この量は、例え
ば、液20lに対して50g程度とする。さらに、撹拌翼3
8を回転し、液中の繊維と共に撹拌する。この粉状体の
混合により、繊維はさらに細かく裁断され、液中に分散
する。[Formation of Filter Aid Material Layer] A process of forming the filter aid material layer x on the filter material 19 of the filter cylinder 17 in the above structure will be described. First, the paper is supplied into the supply cylinder 36 to which the liquid has been supplied in advance, the stirring blade 38 is rotated, and the paper is cut into the fibrous shape and dispersed in the supply cylinder 36. Next, a powdery material formed by mixing one or more kinds of various materials such as activated carbon, silicon earth, coal, and metal powder is mixed. This amount is, for example, about 50 g for 20 liters of liquid. Furthermore, the stirring blade 3
Rotate 8 and stir with fiber in solution. By mixing this powdery material, the fibers are further cut into smaller pieces and dispersed in the liquid.
【0020】かかる分散液を、開閉弁37を開放して、
助材液槽35本体に移し換える。次に、流出管路25の
切換え弁26を切換えて、前記流出口24を助材液槽3
5側に連通させておいてから、前記切換え弁8を助材液
槽35側に切換えて、ポンプ34を駆動し、前記分散液
を供給口7から通入孔6の周方向へ流出させる。分散液
は、通入孔6を旋回して下降し、渦流となってタンク本
体1a内に流入する。かかる渦流を生じさせたのは、濾
材19の外周面に、繊維材,粉状体等の濾過助材を均一
に付着させるためである。The dispersion liquid is opened by opening the on-off valve 37,
The auxiliary material liquid tank 35 is transferred to the main body. Next, the changeover valve 26 of the outflow pipe 25 is changed over so that the outflow port 24 is connected to the auxiliary material liquid tank 3
After communicating with the No. 5 side, the switching valve 8 is switched to the auxiliary material liquid tank 35 side, the pump 34 is driven, and the dispersion liquid is caused to flow from the supply port 7 in the circumferential direction of the through hole 6. The dispersion liquid swirls through the through hole 6 and descends, forming a vortex and flowing into the tank body 1a. The reason why such a vortex flow is generated is that the filter aid such as the fibrous material and the powdery material is uniformly attached to the outer peripheral surface of the filter material 19.
【0021】前記分散液は、濾材19に繊維と粉状体と
からなる濾過助材を付着し、流出口24から流出管路2
5を介して、助材液槽35に回収され、さらに供給口7
から流出する循環路を経て、再び濾材19を透過する。
この循環により、分散液の濾過助材は濾材19周部に付
着し、助材液槽35内の液は清浄となり、而て、濾材1
9周部に第2図に示すように濾過助材層xが形成され
る。この濾過助材層xは濾材19の上下方向に沿って厚
が略均一であり、繊維中に粉状体が分散されることによ
り、高密度となる。このため、後記する濾過工程に際し
て、良好な濾過能を得ることができる。In the dispersion liquid, a filter aid consisting of fibers and powders is attached to the filter medium 19, and the outflow conduit 24 is discharged from the outlet 24.
5 is collected in the auxiliary material liquid tank 35 via the supply port 7
After passing through the circulation path flowing out of the filter medium 19, it permeates the filter medium 19 again.
By this circulation, the filter aid of the dispersion liquid adheres to the peripheral portion of the filter medium 19, and the liquid in the aid liquid tank 35 becomes clean, thus the filter medium 1
As shown in FIG. 2, the filter aid material layer x is formed on the nine circumferences. The filter aid material layer x has a substantially uniform thickness along the vertical direction of the filter material 19, and the powdery material is dispersed in the fibers to have a high density. Therefore, good filtration performance can be obtained in the filtration step described later.
【0022】濾過助材層xをさらに高密度にするには、
濾過助材層xの形成を完了した後に、次に粉状体のみを
供給筒36の開口から供給して液中に分散させ、前記と
同様に濾材19を透過させて循環させる。これにより前
記濾過助材層xの周面に粉状層yが付着し、前記したポ
ンプ34の作用により、各粒子が濾過助材層xを押付け
る。このため濾過助材層xがその周部から圧縮され、図
3のようにさらに密状態となる。To further increase the density of the filter aid material layer x,
After the formation of the filter aid material layer x is completed, only the powdery material is then supplied from the opening of the supply cylinder 36 to be dispersed in the liquid, and the filter material 19 is permeated and circulated as described above. As a result, the powdery layer y is attached to the peripheral surface of the filter aid layer x, and the particles press the filter aid layer x by the action of the pump 34 described above. Therefore, the filter aid material layer x is compressed from its peripheral portion, and becomes more dense as shown in FIG.
【0023】[濾過運転]前記濾過助材層xの形成後、
前記切換え弁26を元の位置に切換えて前記流出口24
を処理槽に連通し、さらに切換え弁8を切換えて、供給
口7を汚濁液槽に連通し、前記濾過助材層xを透過させ
て、その濾過処理を施す。[Filtration Operation] After the formation of the filter aid layer x,
By switching the switching valve 26 to the original position, the outlet 24
Is communicated with the treatment tank, the switching valve 8 is switched, the supply port 7 is communicated with the contaminated liquid tank, the filter aid layer x is permeated, and the filtration treatment is performed.
【0024】すなわち、切換え弁8,26を制御して、
供給口7を原液タンクに連通し、流出口24を処理済槽
側に連通して、ポンプ34を駆動すると、から処理液を
流入すると、供給口7から通入孔6を経由してタンク本
体1aへ処理液が流入する。この処理液は各濾過筒17
内へ、濾過助材層x及び濾材19を透過して流入し、濾
過作用を受けて清浄液となる。前記濾過筒17の濾材1
9により濾過された清浄液は、流出口24から流出管路
25を経て、処理槽側に流出する。この濾過作業中にあ
って、濾過筒17は図4イに示すように下方からの圧力
により収縮状態にある。That is, by controlling the switching valves 8 and 26,
When the supply port 7 is communicated with the stock solution tank, the outlet 24 is communicated with the treated tank side, and the pump 34 is driven, the process liquid flows from the tank body through the supply port 7 and the through hole 6. The processing liquid flows into 1a. This processing liquid is used in each filter cylinder 17
It permeates the filter aid layer x and the filter medium 19 into the inside, and receives the filtering action to become a clean liquid. Filter medium 1 of the filter cylinder 17
The clean liquid filtered by 9 flows out from the outlet 24 through the outflow pipe 25 to the processing tank side. During this filtering operation, the filter cylinder 17 is contracted by the pressure from below as shown in FIG.
【0025】[簡易逆洗]前記濾過作業を連続すると、
濾材19の表面に濾塵層zが形成され、濾材19に目詰
まりを生じ、タンク1内の水圧が上昇する。この圧力上
昇を公知の圧力検出手段により検知し、次の簡易逆洗工
程に入る。[Simple backwashing] When the filtration work is continued,
A filter dust layer z is formed on the surface of the filter medium 19, the filter medium 19 is clogged, and the water pressure in the tank 1 rises. This increase in pressure is detected by a known pressure detecting means, and the next simple backwashing process is started.
【0026】この簡易逆洗は濾過助材を消耗させること
なく濾過助材層xを再生させるものであって、まずポン
プ34の作動を停止し、切換え弁8を閉じて、液排出口
30に連通する迂回管路32の開閉弁31を開放し、さ
らに切換え弁28を切換えて、エアー供給源27からゲ
ージ圧1〜2Kg/c〓程度の加圧空気を流出口24に数秒
程度連通させる。次に、切換え弁28を閉鎖し、液排出
口30を開放のまま数十秒静止させる。This simple backwash is to regenerate the filter aid layer x without consuming the filter aid. First, the operation of the pump 34 is stopped, the switching valve 8 is closed, and the liquid outlet 30 is discharged. The on-off valve 31 of the bypass passage 32 which is in communication is opened, and further the switching valve 28 is switched so that pressurized air having a gauge pressure of 1 to 2 kg / c〓 is communicated with the outlet 24 from the air supply source 27 for several seconds. Next, the switching valve 28 is closed, and the liquid discharge port 30 is left open for several tens of seconds.
【0027】これにより液溜23及び濾過筒17内の清
浄液は、その圧力により、濾材19から排出される。こ
のとき、濾過筒17の内圧は周囲の水圧よりも大きくな
るから、濾過処理中には収縮していたコイル18は図4
ロのように上下方向へ伸張する。このため、前記濾材1
9の周面に形成された濾過助材層xは濾塵層zととも
に、亀裂及び剥落を生じ、その洗浄がなされる。また濾
材19から流出した液は液排出口30から助材液槽35
側へ排出される。なおこのとき浮遊小片pも排出されな
いように前記30に浮遊小片pの透過を不能とする遮断
網30aを被着する。As a result, the cleaning liquid in the liquid reservoir 23 and the filter cylinder 17 is discharged from the filter medium 19 due to the pressure thereof. At this time, since the internal pressure of the filter cylinder 17 becomes higher than the surrounding water pressure, the coil 18 that has contracted during the filtering process is not shown in FIG.
It stretches vertically like b. Therefore, the filter medium 1
The filter aid material layer x formed on the circumferential surface of 9 is cracked and peeled off together with the filter dust layer z, and is cleaned. Further, the liquid flowing out from the filter medium 19 is supplied from the liquid outlet 30 to the auxiliary liquid tank 35.
Discharged to the side. At this time, a shielding net 30a that prevents the floating small pieces p from permeating is attached to the above-mentioned 30 so that the floating small pieces p are not discharged.
【0028】尚、ポンプ34の作動を停止し、液供給を
休止して放置するだけでも、濾過助材層xへの加圧が解
除されるため、濾過助材層xが膨張し、その表面に付着
した濾塵が自重により剥落する。The pressure applied to the filter aid layer x is released even if the operation of the pump 34 is stopped, and the liquid supply is stopped and allowed to stand. The filter dust adhering to is peeled off by its own weight.
【0029】この簡易逆洗後に、液排出口30を遮断
し、前記した濾過助材層形成を行い、濾材19の周面に
再び濾過助材層xを形成する。After this simple backwash, the liquid outlet 30 is shut off, the above-mentioned filter aid layer is formed, and the filter aid layer x is formed again on the peripheral surface of the filter medium 19.
【0030】[本格逆洗]前記簡易逆洗は濾過助材を消
耗させることなく、濾過助材層xの再生を生じさせるも
のであるが、塵芥は排出されないまま循環するため、純
粋な濾過助材層xを再生することができない。そこで、
適宜に次の本格逆洗を行う。すなわち、ポンプ34の作
動を停止し、開閉弁8及び開閉弁26を閉じ、液排出口
30に連通する管路8の開閉弁31を開放し、さらに切
換え弁28を切換えて、エアー供給源27からゲージ圧
1〜2Kg/c〓程度の加圧空気を流出口24に数秒程度連
通させて後に、開閉弁11を切換えてドレイン口となる
液排出口10を開放する。[Authentic backwashing] The simple backwashing causes regeneration of the filter aid layer x without exhausting the filter aid, but since dust is circulated without being discharged, pure filter aid is obtained. The material layer x cannot be regenerated. Therefore,
Perform the following full-scale backwash as appropriate. That is, the operation of the pump 34 is stopped, the open / close valve 8 and the open / close valve 26 are closed, the open / close valve 31 of the pipe line 8 communicating with the liquid discharge port 30 is opened, and the changeover valve 28 is changed over to change the air supply source 27. Then, pressurized air having a gauge pressure of about 1 to 2 kg / c〓 is communicated with the outflow port 24 for several seconds, and then the on-off valve 11 is switched to open the liquid discharge port 10 serving as the drain port.
【0031】これにより液溜23及びタンク本体1a内
の液は、その圧力により、液排出口10から排出され
る。As a result, the liquid in the liquid reservoir 23 and the tank body 1a is discharged from the liquid discharge port 10 due to its pressure.
【0032】この排出により前記濾過筒17内の液面が
取付け板13よりも下方にくると、加圧空気は管状本体
2の液面にも作用し、その液面降下を生ずる。この液面
降下に伴って、液面近くに密集していた無数の浮遊小片
pも下降する。そして図4ロで示すように、濾過筒17
の周面に付着形成されていた、濾過助材層xが濾塵層z
とともに掻き落とされる。このとき、前記液排出口10
の開放により、液面の下降は液排出口10からの空気の
流入と、液の排出とが交互して行われることによる上下
の波動(バブリング)を生じながら下降し、前記浮遊小
片pは濾過助材を上下に擦過して掻き落とすこととな
り、良好な剥離効率を達成できる。When the liquid level in the filter cylinder 17 becomes lower than the mounting plate 13 by this discharge, the pressurized air also acts on the liquid level of the tubular main body 2 to cause the liquid level drop. Along with this liquid level drop, the innumerable floating small pieces p that are densely packed near the liquid level also descend. Then, as shown in FIG.
Of the filter aid layer x formed on the peripheral surface of the
It is scraped off with. At this time, the liquid outlet 10
Is opened, the liquid level is lowered while causing an inflow and outflow of air from the liquid discharge port 10 and liquid is discharged alternately, and the floating small pieces p are filtered. The auxiliary material is rubbed up and down and scraped off, and good peeling efficiency can be achieved.
【0033】一方、液面降下とともに濾過筒17内から
濾材19を透過して圧力空気が液面側へ噴出し、さらに
濾過処理中には収縮していたコイル18は上下方向へ伸
張する。このため、浮遊小片pによる掻き落とし作用と
相俟って、前記濾材19の周面に形成された濾過助材層
xは濾塵層zとともに、亀裂及び剥落を生じ、その洗浄
が効果的になされる。特に、濾過筒17の上部は取付け
板13に固定され、下方に比して、コイル18の伸長度
は小さいから、浮遊小片pの下降による掻き落とし作用
が効果的となる。On the other hand, as the liquid level drops, pressure air is ejected from the inside of the filter cylinder 17 through the filter medium 19 toward the liquid level side, and the coil 18 contracted during the filtering process extends vertically. Therefore, in combination with the scraping action by the floating pieces p, the filter aid layer x formed on the peripheral surface of the filter medium 19 is cracked and peeled off together with the dust layer z, and the cleaning is effectively performed. It In particular, the upper portion of the filter cylinder 17 is fixed to the mounting plate 13, and the degree of extension of the coil 18 is smaller than that of the lower portion, so that the scraping action by lowering the floating piece p is effective.
【0034】その他、前記濾過筒17は、図5のように
円筒形保持枠50の外周に、繊維材を巻回してなる肉厚
の濾材51を設け、その内部を覆ってなるものでもよ
い。そしてかかる構成にあっても、図のように濾材51
の周面に濾過助材層xが形成され得る。In addition, as shown in FIG. 5, the filter cylinder 17 may be one in which a thick filter medium 51 formed by winding a fiber material is provided on the outer periphery of the cylindrical holding frame 50 and the inside thereof is covered. Even with such a configuration, as shown in the figure, the filter medium 51
A filter aid material layer x may be formed on the peripheral surface of the.
【0035】前記した切換え弁8,26,28及び開閉
弁11,31は、夫々電磁弁により構成することがで
き、各弁の開閉制御を前記タンク1内に設けた圧力検出
手段と関係させることにより、前記各工程を全自動的に
施すことできる。The switching valves 8, 26, 28 and the on-off valves 11, 31 described above can each be constituted by electromagnetic valves, and the opening / closing control of each valve is related to the pressure detecting means provided in the tank 1. Thus, each of the above steps can be performed automatically.
【0036】[0036]
【発明の効果】本発明は、上述したように、濾材を周面
に設けた濾過筒を一〜複数個設け、前記濾材の周面に濾
過助材層xを形成したものにおいて、比重が水よりも小
さな浮遊小片pを供給して、その液面近くに密集させる
ようにしたから、液の排出に伴う液面下降により、濾過
助材層xを浮遊小片pが掻き落とすこととなり、濾過助
材層xの除去を効率的に施し得る優れた効果がある。As described above, according to the present invention, one to a plurality of filter cylinders provided with a filter material on the peripheral surface are provided, and the filter aid material layer x is formed on the peripheral surface of the filter material. Since the smaller floating pieces p are supplied to be concentrated near the liquid surface, the floating small pieces p scrape off the filter aid material layer x due to the liquid level lowering accompanying the discharge of the liquid. There is an excellent effect that the material layer x can be efficiently removed.
【図1】本発明を適用した濾過装置の縦断側面図であ
る。FIG. 1 is a vertical sectional side view of a filtration device to which the present invention is applied.
【図2】濾過助材層xの形成を示す濾材19の一部拡大
縦断側面図FIG. 2 is a partially enlarged vertical side view of a filter medium 19 showing formation of a filter aid layer x.
【図3】粉状層yの形成を示す濾材19の一部拡大縦断
側面図FIG. 3 is a partially enlarged vertical side view of a filter medium 19 showing formation of a powdery layer y.
【図4】濾過助材層xの隔離動作を示す拡大縦断側面図
である。FIG. 4 is an enlarged vertical cross-sectional side view showing the separating operation of the filter aid material layer x.
【図5】濾過筒17の他の構成を示す縦断側面図であ
る。5 is a vertical cross-sectional side view showing another configuration of the filter cylinder 17. FIG.
1 タンク 6 通入孔 7 供給口 10 液排出口 17 濾過筒 18 コイル 19 濾材 24 流出口 x 濾過助材層 p 浮遊小片 1 Tank 6 Inlet Hole 7 Supply Port 10 Liquid Discharge Port 17 Filter Cylinder 18 Coil 19 Filter Material 24 Outlet x Filter Aid Layer p Floating Pieces
Claims (1)
液排出口を備えたタンク内に、外周の濾材面に繊維材,
布材等の分散材からなる濾過助材が被覆される濾過筒を
一〜複数個垂設して、その内部を前記流出口と連通させ
た濾過装置において、前記タンク内に、比重が水よりも
小さな、浮遊小片を無数供給して液面近くで密集させ、
液排出口からの液排出によるタンク内の液位の下降にと
もなって、前記浮遊小片により濾過助剤を掻き落とすよ
うにしたことを特徴とする濾過装置の濾過筒洗浄方法。1. A fiber material is provided on a filter medium surface of an outer periphery in a tank provided with a supply port for a liquid to be treated, an outlet for a clean liquid and a liquid outlet.
In a filter device in which one to a plurality of filter cylinders covered with a filter aid made of a dispersant such as a cloth material are vertically provided, and the inside of which is communicated with the outlet, in the tank, a specific gravity is higher than that of water. Even a small number of small floating particles are supplied to make them close to the liquid surface,
A method of cleaning a filter cylinder of a filter device, wherein the filter aid is scraped off by the floating particles as the liquid level in the tank is lowered by discharging the liquid from the liquid discharge port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP41A JPH06238111A (en) | 1992-04-09 | 1992-04-09 | Method for washing filter casing of filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP41A JPH06238111A (en) | 1992-04-09 | 1992-04-09 | Method for washing filter casing of filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06238111A true JPH06238111A (en) | 1994-08-30 |
Family
ID=14698353
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP41A Pending JPH06238111A (en) | 1992-04-09 | 1992-04-09 | Method for washing filter casing of filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06238111A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012110815A (en) * | 2010-11-24 | 2012-06-14 | Nippon Rensui Co Ltd | Method and apparatus for treating wastewater |
-
1992
- 1992-04-09 JP JP41A patent/JPH06238111A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012110815A (en) * | 2010-11-24 | 2012-06-14 | Nippon Rensui Co Ltd | Method and apparatus for treating wastewater |
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