JP3458186B2 - Pellet filter material washing device - Google Patents

Pellet filter material washing device

Info

Publication number
JP3458186B2
JP3458186B2 JP29574099A JP29574099A JP3458186B2 JP 3458186 B2 JP3458186 B2 JP 3458186B2 JP 29574099 A JP29574099 A JP 29574099A JP 29574099 A JP29574099 A JP 29574099A JP 3458186 B2 JP3458186 B2 JP 3458186B2
Authority
JP
Japan
Prior art keywords
pellet
water
tank
filter
filter medium
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.)
Expired - Fee Related
Application number
JP29574099A
Other languages
Japanese (ja)
Other versions
JP2001070715A (en
Inventor
石順 田宮
Original Assignee
ホクセイ機装株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ホクセイ機装株式会社 filed Critical ホクセイ機装株式会社
Priority to JP29574099A priority Critical patent/JP3458186B2/en
Publication of JP2001070715A publication Critical patent/JP2001070715A/en
Application granted granted Critical
Publication of JP3458186B2 publication Critical patent/JP3458186B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】発明は、樹脂性ペレット
のエンドレスな洗浄とろ層の再生に関するものであ
る。
TECHNICAL FIELD The present invention relates to a resinous pellet filter.
It concerns the endless cleaning of materials and the regeneration of filter layers.

【0002】[0002]

【従来の技術】従来、樹脂性ペレットろ材の洗浄とろ層
の再生は、スクリューとエアーバブリングによる洗浄、
逆洗を行っていたため、このことによるろ過の運転又
は、負圧によるSS(浮遊物)の除去を停止する必要が
あり、洗浄再生の時間も必要なバッチ式であった。
2. Description of the Related Art Conventionally, cleaning of resin pellet filter media and regeneration of filter layer are carried out by cleaning with a screw and air bubbling,
Since backwashing was performed, it was necessary to stop the operation of filtration or the removal of SS (suspended matter) due to negative pressure due to this, and it was a batch type that required cleaning regeneration time.

【0003】[0003]

【発明が解決しようとする課題】発明は、上記したよ
うな従来の問題を解決するためになされたもので、装置
運転中、断続的にろ層の再生を行い、ろ過運転には支
承なくエンドレスに樹脂性ペレットろ材の洗浄と、ろ
層の再生が行えるペレットろ材の洗浄装置を提供するこ
を目的とする。
The present invention has been described above.
It was made to solve such a conventional problem,
During operation, intermittent performs regeneration of the filter layer, child delivery and cleaning the bearing without endless resinous pellets filtration media in the filtration operation, the cleaning apparatus of the pellet filter media that allows the reproduction of the filtrate layer
The purpose is and.

【0004】[0004]

【課題を解決するための手段】樹脂性ペレット式ろ過槽
の底部に、ろ層のペレットろ材をポンプで吸収するペレ
ット回収桝を取付け、ポンプでペレットろ材を汲み出
し、これを遠心水流式固水分離装置に導入する。遠心
流式固水分離装置は円筒形のタンクで、中心にスクリュ
ーを取付け、これを取り巻くように円錐形の網を取り付
ける。この円筒形の遠心水流式固水分離装置にペレット
ろ材が送入された時、水とペレットろ材が水流の遠心力
によって固水が分離され、汚水だけが排水されるように
する。スクリューはろ層に対し、固水分離されたペレッ
ろ材を押し入るもので、先端を袋状にし、内部に網を
取り付けた部屋として、ここからパイプを取り出し、ポ
ンプのサクションに結束する。この目的は、固形物のペ
レットろ材はポンピングできないため、この水をペレッ
ろ材の吸い込みラインに結束し、調節バルブで水6に
対しペレット4の割合になるよう調節することと、ろ層
内部から流入する水でペレットをすすぎ洗いし、この排
水は吸い出され、水流式固水分離装置から排水されるた
め、運転中にろ層の洗浄再生を行っても処理水が濁らな
い。
The bottom of the resin pellets formula filtration tank SUMMARY OF THE INVENTION, Perret absorbing pellets filter medium of the filter layer by a pump
A pellet collecting filter is attached, the pellet filter medium is pumped out by a pump, and this is introduced into a centrifugal water flow type solid water separator. Centrifugal water type solid-water separator is a cylindrical tank with a screw attached to the center and a conical mesh surrounding the screw. Pellet in this cylindrical centrifugal water flow type solid water separator
When the filter medium is fed, the water and the pellet filter medium are separated into solid water by the centrifugal force of the water flow, and only the waste water is discharged. Screw whereas filtration layer, in which intrude a solid water separated pellets filtration media, the tip and into a bag shape, as room fitted with a mesh inside, here from the take-out pipe, bundling the suction of the port <br/> pump . The purpose of this is that solid pellet filter media cannot be pumped, so this water is bound to the suction line of the pellet filter media and adjusted by a control valve so that the ratio of pellets to water is 4 and that from the inside of the filter bed is adjusted. Rinse and wash the pellets with water, and the wastewater is sucked out and drained from the water-flow type solid-water separator, so the treated water does not become turbid even if the filter layer is washed and regenerated during operation.

【0005】[0005]

【発明の実施形態】ペレットろ材の洗浄を確実に、しか
もスピーディーに循環洗浄処理するためにポンプを使
用する。水とペレットろ材が流体化して、筒形の遠心水
流式固水分離装置11に送入された際、遠心水流を作
り、ここで固水分離され、汚水を排水する遠心水流式固
水分離槽11の中心にスクリュー13を取付け、これを
取り巻くように円錐形の網を取り付ける。固水分離され
たペレットろ材はスクリュー13でろ層に押し込まれ
るが、スクリュー用の筒の先端の内部に、網の筒を作
り、これを取り巻くような部屋を作って、ここにポンプ
のサクションに対し、すすぎ水を供給するパイプを取
り出す。ペレット用のポンプは、ろ槽の底部に取り付
けたペレット回収からペレットろ材を汲み出すが、
固形物のペレットろ材は、スクリュー13の先端から取
り出したすすぎ水とポンプ7入口にて合流する。これを
調節バルブ9、8で水6に対しペレット4の割合に調節
して、ペレットろ材を流体化する遠心水流式固水分離室
11で固水分離されたペレットろ材は、スクリュー13
ですすがれ、この汚水はポンプで固水調整され、流体
として遠心水流式固水分離装置11に送水し、汚水は排
水されエンドレスに循環洗浄をすることができる、運転
中にペレットろ材の洗浄を行っても処理水が濁らない。
BEST MODE FOR CARRYING OUT THE INVENTION A pump 7 is used for reliably and speedily carrying out a circulation cleaning process for cleaning a pellet filter medium . Centrifugal water flow type solid water separation tank for making a centrifugal water flow when the water and the pellet filter medium are fluidized and sent into the tubular centrifugal water flow type solid water separation device 11 where solid water is separated and waste water is discharged A screw 13 is attached to the center of 11 , and a conical net is attached so as to surround the screw. The pellet filter medium separated into solid and water is pushed into the filter layer 4 by the screw 13, but a net cylinder is made inside the tip of the screw cylinder, and a room surrounding this is made, and the pump is installed here.
For the suction of 7 , remove the pipe that supplies the rinse water. The pellet pump 7 pumps out the pellet filter medium from the pellet collecting box 6 attached to the bottom of the filter tank .
The solid pellet filter medium joins the rinse water taken out from the tip of the screw 13 at the inlet of the pump 7. Centrifugal water flow type solid-water separation chamber for fluidizing the pellet filter medium by adjusting this to a ratio of 4 pellets to 6 water with control valves 9 and 8.
The pellet filter medium separated by solid water in 11 is screw 13
Rinsed with, the sewage is adjusted solid water in pump 7, and water in a centrifugal flow type solid-water separating device 11 as the fluid, sewage can circulating cleaning endlessly drained, washed pellets filter material during operation The treated water does not become cloudy even after performing.

【0006】[0006]

【実施例】以下、図面を参照しながら本発明の実施例に
ついて説明する。 (イ)汚水の給水とろ過水の採水 1の原水入口より流入する汚水は、流入管を通ってアッ
プフローでろ層4を通水してろ過され、処理水出口5
り採水される。ろ層の汚れが多くなると通水に対する
ヘッドロスが高くなり、クッションタンク2の水位が上
がるので、ここから情報を得て、ペレットろ材の洗浄が
開始される。
Embodiments of the present invention will be described below with reference to the drawings. (B) sewage flowing from the raw water inlet of the water sampling 1 water supply and filtration of wastewater is filtered by passing water filtrate layer 4 in upflow through the flow pipe is water sampling from treated water outlet 5. If contamination of the filtrate layer 4 increases head loss is increased for passing water, since the water level in the cushion tank 2 increases, wherein after obtaining the information, wash pellet filter media is started.

【0007】(ロ)ろ層の樹脂性ペレットろ材の回収と
この洗浄 アップフローで通水し、ろ過する場合、ろ層は底部か
ら汚れてくる。このため、底部にペレット回収桝6を取
付け、これをポンプに配管接続する。ペレットろ材
固体であり、単独ではポンピングできないため、14の
ペレットすすぎ室から水を取り、調節バルブ8、9で水
6、ペレット4の割合に調節して、これを流体とし
プ7で遠心水流遠心固水分離室11に送水して、ペレッ
ろ材と汚水を分離して、汚水は汚水排水口12より原
水槽に返送する。
[0007] (b) was collected and passed water at the washing-up flow of resinous pellets filter medium of the filter layer, when filtered, the filtrate layer 4 becomes soiled from the bottom. Therefore, mounting a pellet collection basins 6 at the bottom, piping connect it to the pump 7. Pellets filter media is a solid, because alone can not pump takes water from the pellets rinsing chamber 14, the water 6 in the regulation valves 8 and 9, by adjusting the proportion of pellets 4, which was a fluid port down <br / In step 7, water is sent to the centrifugal water flow centrifugal solid water separation chamber 11 to separate the pellet filter medium and sewage, and the sewage is returned from the sewage drainage port 12 to the raw water tank.

【0008】(ハ)ろ槽に対するペレットろ材の送入と
すすぎ遠心水流式固水分離装置 11で固水分離されたペレット
ろ材は、スクリュー13でろ層に送入されるが、ペレ
ットろ材の表面には汚物が付着している。このためスク
リュー13で攪拌し、送入する際ペレットろ材ろ槽
水が合流してすすがれ、このことで発生した汚水は、ペ
レットすすぎ室14からポンプに吸入され、ペレット
ろ材の流体化に利用し、再び遠心水流式固水分離装置
から排水されてペレットろ材はすすがれる。
(C) Pellet filter material is fed into the filter tank and rinsed, and pellets solid-water separated by the centrifugal water-flow type solid-water separator 11
The filter medium is fed into the filter layer 4 by the screw 13 , but dirt is attached to the surface of the pellet filter medium . Therefore stirred at screw 13, the water of the pellet filter media and filtrate tank is rinsed joins when fed, sewage generated by this is sucked from the pellet rinsed chamber 14 to the pump 7, pellet
Centrifugal water flow type solid-water separator 1 used again for fluidization of filter media
The pellet filter medium is rinsed after being drained from No. 1 .

【0009】(ニ)エンドレスな自動運転 クッションタンクの水位は、ろ槽のヘッドロスで水位
が上がり、この情報を得てポンプが作動し、ペレット
ろ材がポンプに回収されて遠心水流固水分離装置11
でペレットろ材と汚水ふるい分け、汚水は汚水排水口
12から排水され、ペレットろ材はスクリュー13で送
入し、すすがれる。この汚水はペレットすすぎ室14か
らポンプに吸い取られて運転するため、運転中にこの
作動があっても処理水出口5から排出される採水に濁り
はでない。この作動で、弊害を起こすろ槽底部の汚物
は、汚水ポンプ16を利用し、断続的にタイマー式に除
去する。
[0009] (d) endless water level automatic operation cushion tank 2, raise the water level in the head loss of the filter tank, pump 7 is operated to obtain this information, pellets
The filter medium is collected by the pump 7 and the centrifugal water flow solid water separation device 11
The pellet filter media and sewage are sifted with, and sewage is sewage drain
It is drained from 12 , and the pellet filter medium is fed by a screw 13 and rinsed. This sewage is sucked by the pump 7 from the pellet rinsing chamber 14 for operation, so that even if this operation is performed during operation, the sampled water discharged from the treated water outlet 5 is not turbid. By this operation, the filth at the bottom of the filter tank , which causes a harmful effect, is intermittently removed by the timer method using the sewage pump 16 .

【0010】[0010]

【発明の効果】発明は以上説明の通り、樹脂性のろ過機
ペレットの洗浄をポンプで行い、原水入口のクッション
タンクの水位でろ層のつまりを感知する事で作動し、ポ
ンプでペレット回収桝から吸入するペレットろ材に対
し、遠心固水分離装置からペレットろ材を送入するスク
リューの先端に取り付けたペレットすすぎ室から水を取
り、これを合流した際、ペレットろ材が流体としてポン
ピングできるように考慮し、ペレットろ材遠心水流式
固水分離装置に送入する。ペレットろ材と汚水を固水分
離して、汚水は排水し、ペレットろ材はろ層に送入する
が、この運転は、ろ過採水中に行っても処理水は濁ら
ず、エンドレスな運転が可能である。
[Effect of the Invention] invention as described above, washed resinous filtration machine pellet pump operates in that sense the clogging of the filter layer in the water level of the raw water inlet of the cushion tank, from the pellet recovered basins pump For the pellet filter media to be inhaled, water is taken from the pellet rinsing chamber attached to the tip of the screw that feeds the pellet filter media from the centrifugal solid water separator, and when this is merged, consider that the pellet filter media can be pumped as a fluid. The pellet filter medium is fed into a centrifugal water flow type solid water separator. Solid water is separated from the pellet filter media and the waste water is drained, and the waste water is drained, and the pellet filter media is sent to the filter layer.However, even if this operation is carried out during filtration water sampling, the treated water does not become turbid and endless operation is possible. .

【図面の簡単な説明】[Brief description of drawings]

【図1】 発明の横断面図による説明図である。FIG. 1 is an explanatory view according to a cross-sectional view of the invention.

【符号の説明】 1 原水入口 2 クッションタンク 3 流入管ろ層 5 処理水出口 6 ペレット回収枡 7 ポンプ 8 ペレット調節バルブ 9 すすぎ水ペレット流体化用調節バルブ 10 ペレット送水ライン 11 遠心水流式固水分離装置 12 汚水排水口 13 スクリュー 14 ペレットすすぎ室 15 ペレット流体化用すすぎ水のライン 16 汚水ポンプ[Explanation of Codes] 1 Raw water inlet 2 Cushion tank 3 Inflow pipe 4 Filter layer 5 Treated water outlet 6 Pellet collection box 7 Pump 8 Pellet control valve 9 Rinsing water Pellet fluidization control valve 10 Pellet water supply line 11 Centrifugal water flow type solid water Separator 12 Sewage drainage port 13 Screw 14 Pellet rinsing chamber 15 Pellet fluidizing rinse water line 16 Sewage pump

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ろ槽内に収容した樹脂性のペレットろ材で
もって、水流によって発生する負圧で浮遊物をろ過する
装置に装備して、前記ろ槽内のペレットろ材を汚水と分
離して洗浄するペレットろ材の洗浄装置であって、 前記ろ槽内に設けたペレット回収枡と、 前記ろ槽内に設けた円筒形のタンクおよびタンク内に配
置したスクリューによりペレットろ材と汚水とを分離す
る遠心水流式固水分離装置と、 前記ペレット回収枡より吸入したペレットろ材と水とを
前記遠心水流式固水分離装置へ送り込むポンプとからな
り、 遠心水流式固水分離装置のタンクの下部に網の筒で区画
したすすぎ室を形成し、 前記ペレット回収枡を通じて取り込んだろ槽内のペレッ
トろ材を前記遠心水流式固水分離装置で以って洗浄しつ
つ、洗浄したペレットろ材をろ槽内へ戻し、 前記スクリューでペレットろ材をすすいだ水を、前記ペ
レットすすぎ室から槽外へ取り出して、ろ材の流体輸送
用として前記ポンプへ供給するよう配管したことを特徴
とする、 ペレットろ材の洗浄装置。
1. A resinous pellet filter medium housed in a filter tank.
Therefore, the suspended matter is filtered by the negative pressure generated by the water flow.
Equipped with the device, the pellet filter media in the filter tank is separated from the wastewater.
A washing device for pellet filter media that is separated and washed, comprising a pellet collecting box provided in the filter tank, a cylindrical tank provided in the filter tank, and a tank provided in the tank.
Separate the pellet filter medium and sewage with the screw placed
Centrifugal water flow type solid water separation device and the pellet filter media and water sucked from the pellet collection box
It consists of a pump that feeds the centrifugal water flow type solid-water separator.
A mesh tube at the bottom of the centrifugal water flow type solid water separator
A rinsing chamber is formed, and the pellets in the tank are taken in through the pellet collecting box.
The filter medium is washed with the centrifugal water flow type solid water separator.
The washed pellet filter medium back into the filter tank, and rinse the pellet filter medium with the screw to remove the water.
Lettuce is removed from the rinsing chamber to the outside of the tank to transport the filter media
It is characterized in that it is connected to the pump for supply
And a cleaning device for pellet filter media.
【請求項2】請求項1において、遠心水流式固水分離装
置で以ってペレットろ材より遠心分離した水を、前記ろ
槽内に返送するようタンクとろ槽の間に配管したことを
特徴とする、ペレットろ材の洗浄装置。
2. The centrifugal water flow type solid-water separator according to claim 1.
The water centrifugally separated from the pellet filter medium in
Make sure that piping was installed between the tank and the filter tank so that it could be returned to the tank.
A characteristic device for washing pellet filter media.
JP29574099A 1999-09-08 1999-09-08 Pellet filter material washing device Expired - Fee Related JP3458186B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29574099A JP3458186B2 (en) 1999-09-08 1999-09-08 Pellet filter material washing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29574099A JP3458186B2 (en) 1999-09-08 1999-09-08 Pellet filter material washing device

Publications (2)

Publication Number Publication Date
JP2001070715A JP2001070715A (en) 2001-03-21
JP3458186B2 true JP3458186B2 (en) 2003-10-20

Family

ID=17824565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29574099A Expired - Fee Related JP3458186B2 (en) 1999-09-08 1999-09-08 Pellet filter material washing device

Country Status (1)

Country Link
JP (1) JP3458186B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100953298B1 (en) 2009-10-07 2010-04-20 주식회사 멀티스하이드로 Industry filter device

Also Published As

Publication number Publication date
JP2001070715A (en) 2001-03-21

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