JPH03161003A - Liquid purifying apparatus equipped with centrifugal type self-purifying filter - Google Patents

Liquid purifying apparatus equipped with centrifugal type self-purifying filter

Info

Publication number
JPH03161003A
JPH03161003A JP30003989A JP30003989A JPH03161003A JP H03161003 A JPH03161003 A JP H03161003A JP 30003989 A JP30003989 A JP 30003989A JP 30003989 A JP30003989 A JP 30003989A JP H03161003 A JPH03161003 A JP H03161003A
Authority
JP
Japan
Prior art keywords
cleaning filter
filter
centrifugal self
cylindrical wall
centrifugal
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
Application number
JP30003989A
Other languages
Japanese (ja)
Other versions
JPH0512006B2 (en
Inventor
Kazuo Iijima
飯嶋 和雄
Toshiyuki Iijima
飯嶋 利行
Nobuyoshi Iijima
飯嶋 信芳
Shigesada Iijima
飯嶋 茂定
Yasuaki Saito
斎藤 安明
Shuichi Ishiguro
石黒 修一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IIJIMA SEIMITSU KOGYO KK
Original Assignee
IIJIMA SEIMITSU KOGYO KK
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 IIJIMA SEIMITSU KOGYO KK filed Critical IIJIMA SEIMITSU KOGYO KK
Priority to JP30003989A priority Critical patent/JPH03161003A/en
Publication of JPH03161003A publication Critical patent/JPH03161003A/en
Publication of JPH0512006B2 publication Critical patent/JPH0512006B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To correspond also to the mixed foreign matters having different particle sizes in a fluid to be filtered by providing a three or more filter material layers of multiple cylindrical surfaces and selecting the mesh sizes of the respective filter material layers before use. CONSTITUTION:In a centrifugal type self-purifying filter 1, inside and outside communication ports 14A-16A are provided to the peripheries of respective multiple cylindrical walls 14-16 becoming the centrifugal force generating surfaces of a hollow cylindrical body 11 having three or more multiple cylindrical walls 14-16 arranged in coaxial relationship and the outer peripheries of the multiple cylindrical walls are covered with cloth or filter material layers 14B-16B having fine meshes and an emitting port 7 is provided to the lower rotary shaft part 12 of the hollow cylindrical body 11. The filter 1 is mounted in an airtight filter tank 4 and supported in a freely rotatable manner. Further, the filter 1 is driven by a motor 1. The liquid to be filtered pressurized from above under gravity or by a pump is introduced into the airtight filter tank 4 from an introducing port 5 and the discharge port 6 of the mixed foreign matters increased in the filter tank 4 by filtering action is further provided. Fine particulate matter is hermetically sealed between the adjacent inner and outer cylindrical walls.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、液体浄化に用い、枦過中に吸入口に設けたデ
過材の表面に81層しようとする流体中の混在異物を自
動的に除去できる遠心式自浄フィルタ付枦過装置に関す
る。
Detailed Description of the Invention [Industrial Application Field] The present invention is used for liquid purification, and is capable of automatically removing foreign substances mixed in a fluid that tends to form a layer of 81 on the surface of a depurator provided at an inlet during purification. The present invention relates to a filtration device with a centrifugal self-cleaning filter that can remove water.

[従来の技術] 落差による重力またはボンブを使用して圧送される流体
の流路に混在異拘除去用フィルタを介在させることによ
って、流体の移送と流体中に混在する異物の除去とを同
時に行うことは、あらゆる産業分野に亘って広く行われ
ている。例えば、水道の浄水装置の前処理、中水道浄化
装置の前処理、汚濁水からの取水、排水処理装置、プー
ルの循環水の循環浄化装置、工作用潤滑オイルの循環浄
化装置、工作機械の切削液の枦過装置などのろ過に利用
されている。
[Prior art] By interposing a filter for removing mixed foreign matter in the flow path of the fluid that is pumped by gravity due to a drop or by using a bomb, the transfer of the fluid and the removal of foreign substances mixed in the fluid are performed at the same time. This is widely practiced across all industrial fields. For example, pre-treatment for water purification equipment, pre-treatment for gray water purification equipment, water intake from polluted water, wastewater treatment equipment, circulation purification equipment for pool water, circulation purification equipment for lubricating oil for work, cutting for machine tools. It is used for filtration in liquid filtration devices, etc.

この種のフィルタ(枦過材)としてボンブの注水口にp
布、金網などを装着したものが使われている. 〔発明が解決しようとする課題] 上記のごとき従来の混在異物除去用フィルタは、枦遇す
べき流体中の混在異物の粒径が大きな物から微小な物ま
で多種であれば、全てのサイズの混在異物に対応させる
ことは困難であり、また殊に異物混入量が多い場合には
短期間でF材表面への異物の沈積量が増大し、フィルタ
の洗浄を頻繁に行わなければならず、生産性低下の要因
となっていた. 本発明の目的は、上記課題を解決し、枦過液中の大きな
物から微小な物まで多種の混在異物に対応でき、P過作
業の進行中に同時に、枦材層の表面に沈積しつつある波
枦過液φの異物を枦材表面から除去するV&楕を備え、
さらに、P過液中の多種の混合異物の変化に対応して、
枦材の取替えが容易にできる遠心式自浄フィルタ付き枦
過装置を提供することにある. [課題を解決するための手段コ 本発明の遠心式自浄フィルタ付液体浄化装置は上記の課
題を解決するために、同軸に配した三重以上の多重円筒
壁を有する中空回転体の遠心力発生面となる多重円fi
壁各々に、内外連通口を周設するとともに、該多重円筒
壁の外周を網目が微細な11または枦材層などで覆い、
前記中空回転体の下方向回転軸部に吐出口を設けてなる
遠心式自浄フィルタと、前記遠心式自浄フィルタを内蔵
するとともに回転自在に支持する気密枦過槽と、前記遠
心式自浄フィルタを駆動するモータと、上方から重力ま
たはボンブにより加圧した披♂過液を、前記気密枦過槽
に導入する導入口と−7P過作用により気密P過槽内に
増加する混在異物の排出口とからなる遠心式自浄フィル
タ1寸液体浄化装置において、上記遠心式自浄フィルタ
は、上端を閉塞し、円筒聖に前記内外運通口を周設し、
下端に前記吐出口を設けてなる回転円筒体を中心とし、
該回転円筒体の上下端部に外嵌する上部フランジ板と下
部フランジ板を螺合により固定し、前記多重円筒壁は、
分離独立した各円筒壁がシール材を介して前記上部フラ
ンジ板と下部フランジ板の間に固定され、上部フランジ
板を外すことにより各円筒壁は取外すことができ、所定
の隣合う外測円筒壁と内側円筒壁に、それぞれ微細繊維
群を硬質樹脂で連結強化してなる紐または帯を巻付けて
形戊されるが材層、または網目が微細な布等を固定して
、前記内外連通口を覆い、該外測円筒壁と内側円筒壁の
間に微粒子状物質を密封できるill造であり、前記隣
合う外側円筒壁と内側円筒壁の間に活性炭、珪藻土、白
土または粒子状多孔質セラミック等のろ過材あるいはイ
オン交換樹脂等の粒子状物質を充填したことを技術的手
段とし、 さらに、前記気密枦過槽は、遠心式自浄フィルタと同軸
心の円筒状で上下端が閉塞した形状を呈し、スクリュー
羽根状の液流ガイドが等間隔に斜下方向に向かって周設
され、遠心式自浄フィルタの回転により誘起される回転
液流により、下方向に向かう液流を発生する構造であり
、気密枦過槽の下端部に混在異物の排出口が設けられて
いることを技術的手段とし、 さらに、前記遠心式自浄フィルタの下方向回転軸部に設
けた吐出口には、吐出路が連結され、該吐出路に開閉バ
ルブを取付けるとともに、吐出口と開閉バルブの間に、
ポンプにより加圧された空気を圧送する加圧空気導入路
が開閉バルブを介して接続されていることを技術的手段
とする。
As this kind of filter (filtering material),
Those equipped with cloth, wire mesh, etc. are used. [Problems to be Solved by the Invention] The conventional filter for removing mixed foreign matter as described above can handle all sizes of mixed foreign matter in the fluid to be removed, if the particle size of the mixed foreign matter varies from large to minute particles. It is difficult to deal with mixed foreign matter, and especially when there is a large amount of foreign matter mixed in, the amount of foreign matter deposited on the surface of the F material increases in a short period of time, and the filter must be cleaned frequently. This was a cause of decreased productivity. The purpose of the present invention is to solve the above-mentioned problems, to be able to deal with a wide variety of mixed foreign substances from large to minute particles in the permeation liquid, and to simultaneously deposit on the surface of the permeate layer while the permeation work is in progress. Equipped with V & ellipse to remove foreign matter of liquid φ that passes through a certain wave from the surface of the resin material.
Furthermore, in response to changes in the various mixed foreign substances in the P filtrate,
The object of the present invention is to provide a filtration device with a centrifugal self-cleaning filter that allows easy replacement of the wicker material. [Means for Solving the Problems] In order to solve the above-mentioned problems, the liquid purification device with a centrifugal self-cleaning filter of the present invention uses a centrifugal force generating surface of a hollow rotating body having three or more cylindrical walls coaxially arranged. The multiple circles fi
Each wall is provided with an internal and external communication port, and the outer periphery of the multi-layered cylindrical wall is covered with a fine-mesh layer 11 or a resin layer,
A centrifugal self-cleaning filter having a discharge port provided in the downward rotating shaft of the hollow rotary body, an airtight filter tank that houses the centrifugal self-cleaning filter and rotatably supports the centrifugal self-cleaning filter, and drives the centrifugal self-cleaning filter. an inlet for introducing the filtration liquid pressurized by gravity or a bomb from above into the airtight filtration tank, and an outlet for the mixed foreign matter that increases in the airtight filtration tank due to -7P overaction. In the centrifugal self-cleaning filter 1-inch liquid purification device, the centrifugal self-cleaning filter has an upper end closed, and the inner and outer ports are provided around the cylindrical hole,
Centered around a rotating cylindrical body with the discharge port provided at the lower end,
An upper flange plate and a lower flange plate that are externally fitted to the upper and lower ends of the rotating cylindrical body are fixed by screwing, and the multi-layered cylindrical wall is
Each separate and independent cylindrical wall is fixed between the upper flange plate and the lower flange plate via a sealing material, and each cylindrical wall can be removed by removing the upper flange plate, and is connected to the predetermined adjacent external cylindrical wall and inner side. The inner and outer communication ports are covered by fixing a material layer or a cloth with a fine mesh around the cylindrical wall, which is formed by wrapping a string or band made of fine fibers connected and reinforced with a hard resin. , an illumination structure capable of sealing particulate matter between the outer cylindrical wall and the inner cylindrical wall, and a material such as activated carbon, diatomaceous earth, white clay, or particulate porous ceramic between the adjacent outer cylindrical wall and the inner cylindrical wall. The technical means is that the airtight filter tank is filled with particulate matter such as filter material or ion exchange resin, and furthermore, the airtight filter tank has a cylindrical shape with a coaxial center with a centrifugal self-cleaning filter and whose upper and lower ends are closed, It has a structure in which liquid flow guides in the shape of screw vanes are arranged diagonally downward at equal intervals, and a downward liquid flow is generated by the rotating liquid flow induced by the rotation of the centrifugal self-cleaning filter. The technical means is that a discharge port for mixed foreign matter is provided at the lower end of the filter tank, and a discharge path is connected to the discharge port provided at the lower rotating shaft of the centrifugal self-cleaning filter. , an on-off valve is installed in the discharge passage, and between the outlet and the on-off valve,
The technical means is that a pressurized air introduction path for feeding pressurized air by a pump is connected via an on-off valve.

[作用および発明の効果コ 上方から重力またはポンプにより加圧した?}l:F過
液を気密枦過槽内に導入する。まず遠心式自浄フィルタ
の回転装置を作動させる。つぎにボンブを起動させると
ともに加圧装置を起動させる。重力またはポンプの加圧
により、r材層を境に遠心式自浄フィルタの内側と外側
との間に大きな圧力差が生じて、被枦過流体は枦材の隙
間を通過して遠心式自浄フィルタ内に吸入され、異物の
p過作用が営まれる. また遠心式自浄フィルタの外周面には遠心力が作用する
ので、外周面に沈積しようとする流体中の混在異物は、
遠心作用力を受けてr材表面への沈着が阻止される.こ
のとき、流体中の混在異物が外周面に沈積しようとする
力は、重力またはポンプの加圧による枦材層の内外の圧
力差と混在異物の量に関係し、沈積を阻止する力は、遠
心作用力すなわち遠心式自浄フィルタの回転速度に関1
系するので、遠心式自浄フィルタの吐出口がらの流体の
吐出量を計り、吐出量が減少すれば遠心式自浄フィルタ
の回転速度を増し、吐出量が増加すれば遠心式自浄フィ
ルタの回転速度を減らすことにより、継続して枦過注水
作業が行われる。
[Action and Effect of the Invention Is it pressurized from above by gravity or by a pump? }l: Introduce the F filtrate into an airtight filtration tank. First, the rotation device of the centrifugal self-cleaning filter is activated. Next, start the bomb and start the pressurizing device. Due to gravity or the pressurization of the pump, a large pressure difference is created between the inside and outside of the centrifugal self-cleaning filter with the R material layer as a boundary, and the fluid to be squeezed passes through the gap between the struts and closes the centrifugal self-cleaning filter. The foreign substance is inhaled into the body, causing a p-overeffect. In addition, since centrifugal force acts on the outer circumferential surface of the centrifugal self-cleaning filter, foreign substances in the fluid that tend to settle on the outer circumferential surface are
Deposition on the R material surface is prevented by centrifugal force. At this time, the force that tends to cause the mixed foreign matter in the fluid to settle on the outer circumferential surface is related to the pressure difference between the inside and outside of the resin layer due to gravity or the pressurization of the pump, and the amount of mixed foreign matter, and the force that prevents the deposition is: Regarding the centrifugal force, that is, the rotational speed of the centrifugal self-cleaning filter1
Therefore, measure the amount of fluid discharged from the discharge port of the centrifugal self-cleaning filter, and if the discharge amount decreases, increase the rotation speed of the centrifugal self-cleaning filter, and if the discharge amount increases, increase the rotation speed of the centrifugal self-cleaning filter. By reducing the amount of water, over-injection work will continue.

従って、前記の構成により、本発明の遠心式自浄フィル
タ付液体浄化装置は、 請求項1について、 (イ〉前記多重円筒壁の取付構造により、(効果)多重
円筒壁の取外しが容易になる。
Therefore, with the above configuration, the liquid purification device with a centrifugal self-cleaning filter of the present invention has the following features: (a) Due to the mounting structure of the multiple cylindrical walls, (effect) the multiple cylindrical walls can be easily removed.

(口)前記多重円筒壁と多重円筒壁の隣合う外側円筒壁
と内側円筒壁の間に微粒子状物1質を密封できる構造に
より、 (効果)多量の微粒子状の枦過材あるいはイオン交換樹
脂などを、コンパクトに収納できるとともに多種の混在
異物に対応して取替えが容易になる. (効果)P過液中の多稚の混合異物に対応できるととも
に、各種類の枦通用素材あるいはイオン交換樹脂材の研
究、実験を行うのに便利である。
(Exposure) Due to the structure that can seal particulate matter between the adjacent outer and inner cylindrical walls of the multiple cylindrical walls, (effect) a large amount of particulate filtering material or ion exchange resin. etc., can be stored compactly, and can be easily replaced because it can handle a wide variety of mixed foreign objects. (Effects) Not only can it deal with a large number of mixed foreign substances in the P liquid, it is also convenient for conducting research and experiments on various types of common materials or ion exchange resin materials.

(ハ〉披r過液体中の混在異物を取除くフィルタとして
、三層以上からなる多重円筒面のろ材層を備えているの
で、 (効果)各枦材層の網目を大小を選択して用いることに
より、被F過流体中の粒径が大小異なる混在異物にも対
応でき、また遠心式自浄フィルタの外形寸法に対して枦
材層面積が非常に大きくなり、枦過能力に極めて優れる
(c) Since it is equipped with multiple cylindrical filter media layers consisting of three or more layers as a filter for removing foreign substances mixed in the permeating liquid, (Effects) The size of the mesh of each mesh layer can be selected and used. As a result, it is possible to deal with mixed foreign substances of different sizes in the fluid to be subjected to F-filtration, and the area of the rod layer is extremely large compared to the external dimensions of the centrifugal self-cleaning filter, resulting in extremely excellent permeability.

(二〉が材層を遠心力発生面に設けたことにより、 (効果)流体中の混在異物がP″iA材に沈積するのを
阻止する力が強い。
(2) By providing the material layer on the centrifugal force generation surface, (effect) there is a strong force to prevent foreign matter mixed in the fluid from being deposited on the P″iA material.

(ホ)吐出量の増減に対応して遠心式自浄フィルタの回
転速度を増減することにより、(効果)被枦過流体中の
異物混入量の変化および混入異物の変化に随時対応して
、継続的に枦過注水作業が行うことができる。
(e) By increasing or decreasing the rotational speed of the centrifugal self-cleaning filter in response to the increase or decrease in the discharge volume, (effect) it can continue to respond to changes in the amount of foreign matter mixed in the overflowing fluid and changes in foreign matter mixed in as needed. It is possible to perform overwater injection work.

請求項2について、 枦材表面から除去されp材層周辺に浮遊して増加する混
在異物は、スクリュー羽根状の液流ガイドが等間隔に斜
下方向に向かって周設され、遠心式自浄フィルタの回転
により誘起される回転液流により、下方向に向かう液流
を発生するので、気密枦過槽内の下部に押込まれる。
Regarding claim 2, mixed foreign matter removed from the surface of the resin material and floating around the p-material layer is removed by a centrifugal self-cleaning filter, in which screw blade-like liquid flow guides are arranged diagonally downward at equal intervals. The rotating liquid flow induced by the rotation of the liquid generates a downward liquid flow, so that the liquid is pushed into the lower part of the airtight tank.

(へ)気密枦過槽は、遠心式自浄フィルタと同軸心の円
筒状で上下端が閉塞した形状を呈し、スクリュー羽根状
の液流ガイドが等間隔に斜下方向に向かって周設され、
遠心式自浄フィルタの回転により誘起される回転液流に
より、下方向に向がう液流を発生する横遣であり、気密
枦過檜の下端部に混在異物の排出口が設けられている構
成により、遠心式自浄フィルタの遠心作用力により枦材
表面から除去され枦材層周辺に浮遊して増加する混在異
物は、下方向に向かう回転液流により、気密枦過槽内の
下部に押込まれるので、 (効果)排出口から速やかに排出される。
(f) The airtight filter tank has a cylindrical shape coaxial with the centrifugal self-cleaning filter, with the top and bottom ends closed, and screw blade-shaped liquid flow guides are installed around the circumference diagonally downward at equal intervals.
It is a horizontal type that generates a downward liquid flow by the rotating liquid flow induced by the rotation of the centrifugal self-cleaning filter, and has a configuration in which a discharge port for mixed foreign matter is provided at the lower end of the airtight hinoki cypress. Due to the centrifugal force of the centrifugal self-cleaning filter, foreign matter that is removed from the surface of the resin material and floating around the resin layer is pushed into the lower part of the airtight filter tank by the downward rotating liquid flow. (Effect) It is quickly discharged from the discharge port.

請求項3について (ト)遠心式自浄フィルタの下方向回転軸部に設けた吐
出口には、吐出路が連結され、該吐1u路に開閉バルブ
を取付けるとともに、吐出口と開閉バルブの間に、ポン
プにより加圧された空気を圧送する加圧空気導入路が開
閉バルブを介して接続されていて、遠心式自浄フィルタ
の自浄能力を超えて外周面に混在異物が沈積して、炉過
作業の継続が不可能になった場合、逆進する加圧空気を
遠心式自浄フィルタ内に導き、遠心式自浄フィルタを内
側から吹払う横成により、遠心式自浄フィルタの回転に
よる遠心作用力だけでは、異物の沈積を阻止できない場
合、遠心式自浄フィルタの遠心作用力に加えて遠心式自
浄フィルタを内叫がら加圧空気で吹払うことにより、 (効果)強制的に沈H異’la+を取除くことができる
Regarding claim 3 (g) A discharge passage is connected to the discharge outlet provided in the downward rotating shaft of the centrifugal self-cleaning filter, and an on-off valve is attached to the outlet 1u passage, and an on-off valve is installed between the outlet and the on-off valve. , the pressurized air inlet passage through which pressurized air is fed by a pump is connected via an on-off valve, and the self-cleaning ability of the centrifugal self-cleaning filter is exceeded and foreign matter accumulates on the outer surface, causing overwork in the furnace. If it becomes impossible to continue, the pressurized air moving backwards is guided into the centrifugal self-cleaning filter and the centrifugal self-cleaning filter is blown away from the inside. If the sedimentation of foreign matter cannot be prevented, in addition to the centrifugal force of the centrifugal self-cleaning filter, the centrifugal self-cleaning filter is blown away with pressurized air (effect) to forcibly remove the sediment. Can be removed.

以上に述べた如く、本発明によれば、フィルタの自浄機
能を有し、フィルタ炉材表面から除去されて増加する混
合異物を速かに排出する機能を有するとともに、被枦過
流体中の混在人異物の質の変化に対応して、微粒子状の
枦過材層を容易に取換えることができる遠心式自浄フィ
ルタ付液体浄化装置を提供できる。
As described above, according to the present invention, the filter has a self-cleaning function, has the function of quickly discharging the mixed foreign matter that is removed from the surface of the filter furnace material, and also has the function of quickly discharging the mixed foreign matter that is removed from the surface of the filter furnace material. It is possible to provide a liquid purification device with a centrifugal self-cleaning filter in which the particulate filter material layer can be easily replaced in response to changes in the quality of foreign substances.

[実施例] つぎに本発明をを第1図〜第5図に示す第1実施例に基
づき説明する。
[Example] Next, the present invention will be explained based on a first example shown in FIGS. 1 to 5.

遠心式自浄フィルタ付枦過装置Aは、多重構造の円筒壁
を有する中空回転体の遠心式自浄フィルタ1、遠心式自
浄フィルタ1の回転装置3、遠心式自浄フィルタlを覆
う気密r過槽4、気密枦過槽4の導入口5、混在異物排
出用の排出口6およびF過液体の吐出口7、該吐出口7
と連結された筒状の吐出管71、該吐出管71と連結さ
れた吐出路72、吐出路72の開閉バルグ73、吐出路
72に接続された圧縮空気導入路74およびその開閉バ
ルブ75等から構成される. 気密r過槽4は、遠心式自浄フィルタ1と同軸心で、上
下端が閉塞された円筒形状を呈する.また、別体に形成
されかつ連結された上部室41と下部室42とから或り
、それぞれの端部に設けたフランジ部をボルト締めして
連結されている。
The centrifugal self-cleaning filter A includes a centrifugal self-cleaning filter 1 which is a hollow rotating body having a multi-layered cylindrical wall, a rotating device 3 for the centrifugal self-cleaning filter 1, and an airtight filtration tank 4 that covers the centrifugal self-cleaning filter 1. , an inlet 5 of the airtight filter tank 4, an outlet 6 for discharging mixed foreign matter, a discharge port 7 for F-filtered liquid, and the discharge port 7.
From the cylindrical discharge pipe 71 connected to the discharge pipe 71, the discharge passage 72 connected to the discharge pipe 71, the opening/closing valve 73 of the discharge passage 72, the compressed air introduction passage 74 connected to the discharge passage 72, the opening/closing valve 75 thereof, etc. It is composed. The airtight filtration tank 4 is coaxial with the centrifugal self-cleaning filter 1 and has a cylindrical shape with its upper and lower ends closed. Further, the upper chamber 41 and the lower chamber 42 are formed separately and connected, and are connected by bolting flange portions provided at respective ends.

上部室41には、前記遠心式自浄フィルタ1が回転自在
に装着され、下部室42には、前記筒状の吐出管71が
中心を貫通して装着される。自浄フィルタ1は、吐出管
71に回転自在に外嵌する回転筒2と一体回転するよう
に連結され、気密P過槽4の下側に突出した回転筒2が
、プーり31、■ベルト32およびモータ33からなる
回転装置3により駆動される。また、吐出管71の下端
には吐出路72が連結され、吐出路72には開閉バルブ
73が装着されるとともに、圧縮空気導入路74が接続
され、圧縮空気導入路74にも開閉バルグ75が装Sさ
れている。圧縮空気導入路74は、遠心式自浄フィルタ
1を内側から吹払うために利用される. 前記気密枦過槽4の上部室41は、中心に前記遠心式自
浄フィルタ1が装着され、その外側を取巻いてスクリュ
ー羽根状の液流ガイド43が,等間隔に斜下方向に向か
って周設されている。遠心式自浄フィルタ1の回転によ
り誘起される回転液流により、液流ガイド43が下方向
に向かう液流を発生するm造であり、混在異物を下部室
42に押下げる働きをする.また上端部に導入口5が設
けられている。
The centrifugal self-cleaning filter 1 is rotatably installed in the upper chamber 41, and the cylindrical discharge pipe 71 is installed in the lower chamber 42 passing through the center. The self-cleaning filter 1 is connected to rotate integrally with a rotary tube 2 that is rotatably fitted onto the discharge pipe 71. and a rotating device 3 consisting of a motor 33. Further, a discharge passage 72 is connected to the lower end of the discharge pipe 71, an on-off valve 73 is attached to the discharge passage 72, a compressed air introduction passage 74 is connected, and an on-off valve 75 is also connected to the compressed air introduction passage 74. It is equipped with S. The compressed air introduction path 74 is used to blow away the centrifugal self-cleaning filter 1 from inside. In the upper chamber 41 of the airtight filter tank 4, the centrifugal self-cleaning filter 1 is installed in the center, and screw blade-shaped liquid flow guides 43 are arranged around the outside of the upper chamber 41 in a diagonally downward direction at equal intervals. It is set up. The liquid flow guide 43 is designed to generate a downward liquid flow by the rotating liquid flow induced by the rotation of the centrifugal self-cleaning filter 1, and serves to push mixed foreign matter down into the lower chamber 42. Further, an introduction port 5 is provided at the upper end.

前記気密l過槽4の下部室42には、下端部側壁に前記
混在異物排出用の排出口6が設けられ、またその下端部
には前記回転筒2をシールする気密止カバー49が嵌着
されている. 前記導入口5は、上方からの重力またはポンプにより加
圧した被枦過液を前記気密p過槽4内に導入する。導入
口5に接続ずる導入路51には、開閉バルブ52が装着
されている.また排出口6に接続する排出路61にも開
閉バルブ62、63が装着されている.開閉バルブ62
は、下部室42にM積し、濃縮された混在異物を液体と
ともに排出するために用い、また開閉バルブ63は、フ
ィルタ1の表面に沈積した異物を圧縮空気で吹払う場合
に、異物をR:縮空気とともに排出するために用いる。
The lower chamber 42 of the airtight tank 4 is provided with a discharge port 6 for discharging mixed foreign matter on the lower end side wall, and an airtight cover 49 for sealing the rotary cylinder 2 is fitted to the lower end thereof. It has been done. The introduction port 5 introduces the liquid to be subjected to permeation pressurized by gravity or a pump from above into the airtight permeation tank 4 . An on-off valve 52 is attached to the introduction path 51 connected to the introduction port 5. Further, the discharge passage 61 connected to the discharge port 6 is also equipped with on-off valves 62 and 63. Open/close valve 62
is used to discharge the concentrated mixed foreign matter accumulated in the lower chamber 42 along with the liquid, and the on-off valve 63 is used to discharge the foreign matter accumulated on the surface of the filter 1 with compressed air. : Used to discharge together with compressed air.

遠心式自浄フィルタlは、金属あるいは硬質合或樹脂か
らなり、本実施例では、四g構造の円筒壁を同軸心に配
置してなる中空回転体である。また、上下端で回転自在
に支持される回転固筒体11を中心とする.該回転円筒
休11は、上端が閉鎖され中実回転軸12、下端が内部
に吐出口7を設けた中空回転軸13となっている。また
回転円筒体l1の側壁は、一番内側の第一円箇壁となり
、周壁面に一定間隔を保って穿ったくり抜き穴11Aが
設けられている。
The centrifugal self-cleaning filter 1 is made of metal or hard composite or resin, and in this embodiment is a hollow rotating body having a cylindrical wall of a 4G structure arranged coaxially. Moreover, the rotating solid cylinder 11 is rotatably supported at the upper and lower ends. The rotating cylinder 11 has a closed upper end and a solid rotating shaft 12, and a lower end has a hollow rotating shaft 13 with a discharge port 7 provided therein. The side wall of the rotating cylindrical body l1 is the innermost first circular wall, and hollow holes 11A are provided at constant intervals on the peripheral wall surface.

前記回転円筒体11の外側に位置する第二円筒壁14、
その外側に位置する第三円筒壁l5、さらに外側に位置
する第四円筒壁16は、前記中実回転軸l2および中空
回転軸13の外四面に外嵌し螺合する段付フランジ板1
7、18により○リングを介して上下から挟まれ、一定
間隔を保って固定されている.段付フランジ板17は、
前記中実回転軸12の外側面に螺合する押さえ板17A
により、また段付フランジ板18は、前記中空回転軸1
3の外側面に螺合する連結金具l9により固定されてい
る。第二円筒壁14、第三円筒壁15および第四円筒壁
16にもそれぞれ一定間隔を保って穿ったくり抜き穴1
4A,15A、16Aが設けられるとともに、その外側
面には外圓がら順次に網目が微細になる所定材質のろ材
層14B、15B、16Bが外嵌されている。
a second cylindrical wall 14 located outside the rotating cylindrical body 11;
A third cylindrical wall l5 located on the outside and a fourth cylindrical wall 16 located further outside are formed by a stepped flange plate 1 which is externally fitted and screwed onto the four outer surfaces of the solid rotating shaft l2 and the hollow rotating shaft 13.
7 and 18 are sandwiched from above and below via ○ rings and fixed at a constant interval. The stepped flange plate 17 is
A presser plate 17A screwed onto the outer surface of the solid rotating shaft 12
In addition, the stepped flange plate 18 is connected to the hollow rotating shaft 1.
It is fixed by a connecting metal fitting l9 that is screwed onto the outer surface of 3. Hollow holes 1 are formed in the second cylindrical wall 14, the third cylindrical wall 15, and the fourth cylindrical wall 16 at regular intervals, respectively.
4A, 15A, and 16A are provided, and filter media layers 14B, 15B, and 16B made of a predetermined material and having meshes gradually becoming finer from the outer ring are fitted onto the outer surfaces thereof.

本実施例では、第二円筒壁14と第三円筒壁15の間に
、枦過目的に対応して選択された活性炭、珪藻土、白土
、粒状多孔質セラミックあるいはイオン交換樹脂等の粒
子状の枦過材8が緻密に充填されている。また充填され
たP過材8は、上下端に嵌込まれたシールリング18A
と枦材層14B、15Bにより密閉される。
In this embodiment, between the second cylindrical wall 14 and the third cylindrical wall 15, particulate resin such as activated carbon, diatomaceous earth, white clay, granular porous ceramic, or ion exchange resin is inserted between the second cylindrical wall 14 and the third cylindrical wall 15. The overfill material 8 is densely packed. In addition, the filled P overfill material 8 has seal rings 18A fitted into the upper and lower ends.
and are sealed by the resin layers 14B and 15B.

一方、前記気密枦過槽4の上端はボルト締めされたフラ
ンジ板45により塞がれている。その中央部に遠心式自
浄フィルタlあるいは各円筒g14、15、16を着脱
するための着脱口45Aが設けられている.またその着
脱口45Aは、ボルト締めされた着脱用フランジ板46
により塞がれている。該着脱用フランジ板46の中央部
には、中実回転軸12に外嵌するとともにそれをベアリ
ング47Aを介して回転自在に支持する支持軸47が嵌
着されている。47Bは、ベアリング47Aのラジアル
方向の支持位置を調整するボルト、47Cはシール材で
ある. この気密枦過槽4の上部構造と前記遠心式自浄フィルタ
1の組付け構造により、まず着脱用フランジ板46を取
外すと、連結金具19と一体の遠心式自浄フィルタ1を
上方に引上げて取外すことができ、つぎに押さえ板17
Aおよび段付フランジ板17を着脱することにより、枦
過対象となる混在異物の変化に応じて、各円筒壁14、
15、l6および円筒壁14、15の間に緻密に充填さ
れた(本発明の要旨である)前記枦過材8を容易に取替
えることができる。
On the other hand, the upper end of the airtight tank 4 is closed by a bolted flange plate 45. At the center thereof, an attachment/detachment port 45A is provided for attaching and detaching the centrifugal self-cleaning filter l or each of the cylinders g14, 15, and 16. In addition, the attachment/detachment port 45A is connected to an attachment/detachment flange plate 46 tightened with bolts.
is blocked by. A support shaft 47 is fitted into the center of the attachment/detachment flange plate 46. The support shaft 47 is fitted onto the solid rotation shaft 12 and rotatably supports the solid rotation shaft 12 via a bearing 47A. 47B is a bolt that adjusts the radial support position of the bearing 47A, and 47C is a sealing material. Due to the assembly structure of the upper structure of the airtight tank 4 and the centrifugal self-cleaning filter 1, when the attachment/detachment flange plate 46 is first removed, the centrifugal self-cleaning filter 1 integrated with the connecting fitting 19 can be pulled upward and removed. is completed, and then press plate 17
By attaching and detaching A and the stepped flange plate 17, each cylindrical wall 14,
15, 16 and the cylindrical walls 14, 15 (which is the gist of the present invention) can be easily replaced.

つぎに回転部の連結1造、支持構造および回転装置等を
説明する。
Next, the connection structure of the rotating part, the support structure, the rotating device, etc. will be explained.

前記回転筒2は第一回転円筒21と第二回転円筒22が
連結されてなる.前記遠心式自浄フィルタlと第・一回
転円筒21が連結筒44により連結される.その連結構
造は、遠心式自浄フィルタ1の中空回転軸13の下端に
螺合する連結金具19と連結筒44が、それぞれの穴1
9Aと突起44Aとが嵌合する。また連結筒44は、上
下部室41、42間に嵌込まれた貫通穴付支持板48に
より回転自在に支持される. 第一回転円筒21の下側には、第二回転円筒22が螺着
結合により連結されている。その下端には、ブレス或形
されたプーり板31Aとボス部31Bから戒る回転装置
3のプーり31が螺着結合により連結されている。
The rotating cylinder 2 is formed by connecting a first rotating cylinder 21 and a second rotating cylinder 22. The centrifugal self-cleaning filter l and the first rotating cylinder 21 are connected by a connecting cylinder 44. The connection structure is such that a connection fitting 19 that is screwed onto the lower end of the hollow rotating shaft 13 of the centrifugal self-cleaning filter 1 and a connection tube 44 are attached to each hole 1 of the centrifugal self-cleaning filter 1.
9A and the protrusion 44A fit together. Further, the connecting cylinder 44 is rotatably supported by a support plate 48 with a through hole fitted between the upper and lower chambers 41 and 42. A second rotating cylinder 22 is connected to the lower side of the first rotating cylinder 21 by a screw connection. At its lower end, a pulley 31 of the rotating device 3, which is connected from a brace-shaped pulley plate 31A and a boss portion 31B, is connected by a screw connection.

一体回転する第一回転円筒21、第二回転円筒22およ
びプーり31は、第二回転円筒22の内開に嵌込まれた
第一角グラハイトパッキン(断面四角形の二硫化モリブ
デン塗布した紐状のパッキンで気密性に優れる)34を
介して前記尚状の吐出管71に回転自在に外嵌している
。また第二回転円筒22は、第二角グラハイトパッキン
35を介して支持筒36に回転自在に内嵌する。
The first rotating cylinder 21, the second rotating cylinder 22, and the pulley 31, which rotate together, are made of a first square graphite packing (a string-shaped piece coated with molybdenum disulfide having a rectangular cross section) fitted into the inner opening of the second rotating cylinder 22. It is rotatably fitted onto the elongated discharge pipe 71 via a packing (with excellent airtightness) 34. Further, the second rotating cylinder 22 is rotatably fitted into the support cylinder 36 via a second square grahite packing 35 .

支持筒36は、気密枦過槽4の下端に螺着結合により連
結される第一筒36Aと、該第一筒36Aに内嵌螺合す
る第二m36Bから横成され、ラジアル方向の調整機能
を有し、プーり3lとはボールベアリング37を介して
圧接し、プーり3lを上側からラジアル方向に支持して
いる。
The support cylinder 36 is horizontally composed of a first cylinder 36A connected to the lower end of the airtight overtank 4 by a screw connection, and a second cylinder 36B that is internally screwed into the first cylinder 36A, and has a radial adjustment function. The pulley 3l is in pressure contact with the pulley 3l via a ball bearing 37, and the pulley 3l is supported in the radial direction from above.

また第二回転円筒22の下端には、押え筒38が螺着結
合し、押え筒38は下側支持筒39と回転自在に接合し
ている。筒上の叶出管71にビス止めされた下側支持筒
39は、プーり31および第二回転円筒22を下側から
ラジアル方向に支持している. プーり31に連動する回転部は、支持軸47、貫通穴付
支持板48、支持筒36および十叫支持筒39により回
転自在に支持されている。
Further, a presser tube 38 is screwed to the lower end of the second rotating cylinder 22, and the presser tube 38 is rotatably joined to a lower support tube 39. The lower support cylinder 39 screwed to the protruding pipe 71 on the cylinder supports the pulley 31 and the second rotating cylinder 22 from below in the radial direction. A rotating part interlocked with the pulley 31 is rotatably supported by a support shaft 47, a support plate 48 with a through hole, a support cylinder 36, and a support cylinder 39.

回転部は、以下の如く運動する。モータ33の駆動によ
りVベルト32を介してプーり31が回転する.ブーり
31の回転により、回転筒2が連動し、さらに、連結筒
44を介して遠心式自浄フィルタ1が回転する。
The rotating part moves as follows. The pulley 31 is rotated via the V-belt 32 by the drive of the motor 33. The rotation of the bobbin 31 causes the rotary cylinder 2 to move in conjunction with the rotation, and further rotates the centrifugal self-cleaning filter 1 via the connecting cylinder 44.

つぎに上記実施例の作動について説明する。Next, the operation of the above embodiment will be explained.

開閉バルブ52を開いて、気密枦過槽4の中に約2気圧
に加圧した被?F”″JP3液体(太い実線矢印)を導
入する. この状態のもとに、遠心式自浄フィルタ1をプーり31
を介して駆動するモータ33を低速下にスタートさせる
.つぎに吐出路72と排出i¥861の開閉バルブ73
、62を開く。吐出管7lを通り開閉バルブ73から出
る吐出液の量を観察し、@p過流体中の異狗混入量の変
1ヒおよび混在異物の変化により、流体中の混tFn物
がp村層14B、15B、16Bの外周面に沈積しよう
とする力が増減するのに随時対応して、モータ33の回
転数を増減させる。吐出路72からは枦過液(細い実線
矢印〉が継続して吐出する。また、遠心式自浄フィルタ
1の回転により誘起される回転液流により、液流ガイド
43が下方向に向かう液流を発生するので、遠心式自浄
フィルタ1の遠心作用力によって枦材層14B、15B
、16Bの表面から剥離された被枦過液中の混在異物は
、下部室42に押下げられる。下部室42に押下げられ
混在異物は、排出口6から押出される9以上により、吐
出路72から枦過液が吐出し、排出路6lから混在異物
(太い実線矢印)が排出され、継続的に枦過作業が行わ
れる。
The on-off valve 52 is opened and the airtight tank 4 is pressurized to about 2 atmospheres. Introduce F""JP3 liquid (thick solid arrow). Under this condition, the centrifugal self-cleaning filter 1 is attached to the pulley 31.
The motor 33 driven by the motor 33 is started at a low speed. Next, the discharge path 72 and the opening/closing valve 73 of the discharge i ¥861
, 62. Observe the amount of discharged liquid passing through the discharge pipe 7l and exiting from the opening/closing valve 73, and find that the mixed tFn substances in the fluid are mixed in the p village layer 14B due to changes in the amount of foreign matter mixed in the @p superfluid and changes in the mixed foreign matter. , 15B, 16B, the rotational speed of the motor 33 is increased or decreased in response to the increase or decrease in the force that tends to deposit on the outer peripheral surfaces of the motors 15B, 16B. A permeating liquid (thin solid arrow) is continuously discharged from the discharge passage 72. Also, due to the rotating liquid flow induced by the rotation of the centrifugal self-cleaning filter 1, the liquid flow guide 43 directs the downward liquid flow. The centrifugal force of the centrifugal self-cleaning filter 1 causes the resin layers 14B and 15B to
, 16B are pushed down into the lower chamber 42. The mixed foreign matter pushed down into the lower chamber 42 is discharged from the discharge passage 72 by 9 or more pushed out from the discharge port 6, and the mixed foreign matter (thick solid line arrow) is discharged from the discharge passage 6l, and the mixed foreign matter is continuously discharged. Excessive work is carried out.

また混在異物の量が一時的に極端に増加することにより
、遠心力による外周面への沈積を防ぐ力に、沈積しよう
とする力が勝って、枦材層14B、15B、16Bの外
周面に混在異物が沈積して、P過作業の継続が不可能に
なった場合、下記の操作により、遠心式自浄フィルタ1
に沈積した異物を内側から強力に吹払うことができる。
In addition, due to the temporary and extreme increase in the amount of mixed foreign matter, the force to prevent it from being deposited on the outer circumferential surface due to centrifugal force is overcome by the force that tries to deposit it, and the outer circumferential surface of the resin layers 14B, 15B, and 16B is If mixed foreign matter has accumulated and it becomes impossible to continue the P overflow operation, use the following procedure to clean the centrifugal self-cleaning filter 1.
It can powerfully blow away foreign matter deposited on the inside.

まず遠心式自浄フィルタ1を駆動させたまま、導入路5
lの開閉バルブ52、排出路61の開閉バルブ62と吐
出路72の開閉バルブ73を閉じる.つぎに加圧空気導
入路74の開閉バルブ75と排出路61の開閉バルブ6
3を開き、加『空気(破線矢印)を遠心式自浄フィルタ
1の内側に導入す75.この操作により、枦材層14B
、15B、16Bの外周面に沈積した混在異物には、回
転による遠心作用力に加えて、加圧空気が遠心式自浄フ
ィルタ1の内側から強力に吹払う力が働くので、沈積し
た混在異物は外因面から剥がされて、開閉バルブ63か
ら排出される. 加圧空気は、非常に微細な隙間に侵入するので、微細な
沈積異物に対応でき、沈積異物を取除く作用が強力であ
る. つぎに遠心式自浄フィルタ1の第二円筒壁14、第三円
筒壁l5および第四円筒壁16に外嵌する枦材層につい
て本実施例の場合、第四円筒壁16を例に第2〜4図に
基づき説明する. 第四円筒壁16は円筒形をなし、その周壁面の全面に亘
り一定間隔を保って穿ったくり抜き穴16Aを有する。
First, while driving the centrifugal self-cleaning filter 1,
1, the on-off valve 62 of the discharge path 61, and the on-off valve 73 of the discharge path 72 are closed. Next, the on-off valve 75 of the pressurized air introduction path 74 and the on-off valve 6 of the discharge path 61
75. By this operation, the resin layer 14B
, 15B, and 16B, in addition to the centrifugal force due to rotation, pressurized air exerts a strong blowing force from the inside of the centrifugal self-cleaning filter 1, so that the accumulated foreign substances are removed. It is peeled off from the external surface and discharged from the on-off valve 63. Since pressurized air can penetrate into very small gaps, it can deal with minute deposits of foreign matter and has a powerful effect in removing deposited foreign matter. Next, regarding the resin layers that are fitted onto the second cylindrical wall 14, the third cylindrical wall l5, and the fourth cylindrical wall 16 of the centrifugal self-cleaning filter 1, in this embodiment, the fourth cylindrical wall 16 is taken as an example, and the second to fourth cylindrical walls 16 are This will be explained based on Figure 4. The fourth cylindrical wall 16 has a cylindrical shape and has hollow holes 16A formed at constant intervals over the entire circumferential wall surface.

第四円筒壁16に外嵌するp材層16Bは、微細繊維群
を硬質樹脂(本実施例ではエボキシ樹脂〉で連結してな
る毛撚糸状の紐16Cを巻付けて前記くり抜き穴16A
を全面覆って形或される。本実施例では、平行巻き16
D、傾斜の緩い綾目巻き16E、傾斜のきつい綾目巻き
16Fを順番に2順繰返して形成されており、枦過能力
に優れる. 上記実施例において枦材層16Bとして、微細繊維群を
硬質樹脂(本実施例ではエボキシ樹脂)で連結してなる
毛撚糸状の紐16Cを用いているが、円筒壁に枦材層を
外嵌する構造であるので、P過目的に対応して、r材層
として、材質は金属製あるいは硬質樹脂製を用いても良
く、形状は紐状、帯状、11状、網状または綿状等色々
の種類の−P″ij1材を目的に応じ選別して、手軽に
取替えできる. つぎに前記着脱用フランジ板46と段付フランジ板17
を脱着することにより、対象となるか過物あるいは溶質
の変化に応じて、第二円筒壁14、第三円筒壁15およ
び第四円筒壁16を取外して、円筒壁の間に充填するP
過材あるいはイオン交換樹脂を容易に取替えることがで
きるので、つぎの効果を奏する. 〈い〉11結剤を混合して硬化形成する必要がないので
、枦過材を高純度で使用できる. (ろ)P過あるいは液中のイオン交換を目的として、枦
過材の活性炭、珪藻土、白土、粒状多孔質セラミックま
たはイオン交換樹脂またはそれらに類する所定の微粒子
状または粒状物質材を充填して、p過、硬水の軟化ある
いは放射性物質の処理など各種類の実験を行うのに便利
である。
The p-material layer 16B that is fitted onto the fourth cylindrical wall 16 is formed by wrapping a yarn-like string 16C made of fine fibers connected with a hard resin (in this embodiment, epoxy resin) into the hollow hole 16A.
It is shaped to completely cover the area. In this embodiment, parallel winding 16
D. It is formed by repeating the twill winding 16E, which has a gentle slope, and the twill winding 16F, which has a steep slope, in two orders, and has excellent overloading ability. In the above embodiment, a twisted wool string 16C made of a group of fine fibers connected with a hard resin (in this embodiment, epoxy resin) is used as the resin layer 16B, but the resin layer is externally fitted onto the cylindrical wall. Therefore, depending on the purpose of the P layer, metal or hard resin may be used as the material for the R material layer, and the material may be in various shapes such as string, band, eleven, net, or cotton. -P''ij1 materials can be selected according to the purpose and replaced easily. Next, the detachable flange plate 46 and stepped flange plate 17 are installed.
The second cylindrical wall 14, the third cylindrical wall 15, and the fourth cylindrical wall 16 are removed depending on the change in the target substance or solute, and the P filled between the cylindrical walls is removed.
Since the filter material or ion exchange resin can be easily replaced, the following effects are achieved. <I> 11, so it is not necessary to mix and form a stiffening, so you can use a high purity. (filtration) For the purpose of P filtration or ion exchange in the liquid, the filter is filled with activated carbon, diatomaceous earth, clay, granular porous ceramic, ion exchange resin, or similar predetermined fine particulate or granular material. It is convenient for conducting various kinds of experiments such as p-filtration, softening of hard water, and treatment of radioactive substances.

(は〉第二円筒壁14と第三円筒壁15の間にイオン交
換樹脂を充填し、第三円箇壁15と第四円゛筒壁16の
間に枦過材の活性炭、珪藻土、白土または粒状多孔質セ
ラミック等を充填して、枦過材とイオン交換樹脂を組合
せて用いることにより、披が過液から、まず外側のr材
層で混在異物を枦過し、さらに内側のイオン交換樹脂で
イオン交換して目的液を採取できる。
(〉Ion exchange resin is filled between the second cylindrical wall 14 and the third cylindrical wall 15, and between the third cylindrical wall 15 and the fourth cylindrical wall 16, active carbon, diatomaceous earth, and white clay are used as filter materials. Alternatively, by filling granular porous ceramic etc. and using a combination of filtering material and ion exchange resin, foreign substances are first filtered out from the filtrate through the outer layer of R material, and then the ion exchanger layer inside. The target liquid can be collected by ion exchange with resin.

(に)円筒壁と円筒壁の間に所定の粉末状または粒状の
触媒を充填し、触媒層として用いることにより、所定の
混在異物どうしを触媒反応により処理することができる
(2) By filling a predetermined powder or granular catalyst between the cylindrical walls and using it as a catalyst layer, predetermined mixed foreign substances can be treated by catalytic reaction.

つぎに、第6図に基づき、本発明の装置を連結して用い
ることにより、粒径の大きな異物が混在する液体から粒
径の小さな異物が混在する液体まで順次分離する方法を
説明する. 遠心式自浄フィルタ付枦過装置Aの吐出路72に、装置
Aと同様な遠心式自浄フィルタ付炉過装置Bの導入口5
Bを接続し、さらに該枦過装置Bの吐出路72Bに同様
な遠心式自浄フィルタ付r過装置Cの導入口5Cを接続
する.枦過装置A、B,Cの最小網目のろ材層の網目を
それぞれしい、L2、L3とし、網目の大きさをLl 
>L2 >L,、に設定する.f!過装置A.B,Cを
作動させる.それぞれの吐出路72、72B、72Cに
装着した採取バルブ76、76B、76Cからは、混在
異物の粒径の大きな液体から混在異物の粒径の小さな液
体まで順次分離して採取できる。
Next, based on FIG. 6, a method of sequentially separating a liquid containing foreign substances with large particle size to a liquid containing foreign substances with small particle size by connecting and using the apparatus of the present invention will be explained. The inlet 5 of a centrifugal self-cleaning filter filtration device B similar to the device A is connected to the discharge passage 72 of the centrifugal filtration device A with a self-cleaning filter.
Further, the inlet 5C of a similar centrifugal self-cleaning filter C is connected to the discharge passage 72B of the filtration device B. The minimum mesh size of the filter media layer of filter devices A, B, and C is respectively set as L2 and L3, and the size of the mesh is Ll.
>L2 >L, . f! Passing device A. Activate B and C. From the collection valves 76, 76B, and 76C attached to the respective discharge passages 72, 72B, and 72C, it is possible to sequentially separate and collect liquids from liquids with large particle sizes of mixed foreign substances to liquids with small particle sizes of mixed foreign substances.

つぎに、第7図に基づき、本発明の装置を連結して用い
ることにより、粒径の小さな異物が混在する液体から粒
径の大きな′i4物が混在する液体まで順次分離する方
法を説明する。
Next, based on FIG. 7, a method of sequentially separating a liquid containing foreign substances with small particle size to a liquid containing foreign substances with large particle size by connecting and using the apparatus of the present invention will be explained. .

遠心式自浄フィルタ付枦過装置Aの排出路61に、装置
Aと同様な遠心式自浄フィルタ付P過装置Bの導入口5
Bを接続し、さらに該l過装置Bの排出路61Bに同様
な遠心式自浄フィルタ付枦過装置Cの導入口5Cを接続
する。l過装置A、B,Cの最小網目のろ材層の網目を
それぞれR8、R2 、R3とし、網目の大きさをR 
r < R 2 < R)、に説定する.それぞれの吐
出路72、72B、72Cの開閉バルブ73、73B、
73Cからは、混在異物の粒径の小さな液体から混在異
物の粒径の大きな液体まで順次分離して採取できる.ま
た上記のごとく混在異物を粒径で分級することにより、
粒径の違いによる物質の変化を調べることができる. つぎに第8図は前記微粒子状の枦過材を効率良く迅速に
充填するに用いる治具の一例である.治具100は、回
転円筒体1lと内側円筒壁(第三円簡壁)15に嵌合す
るとともに両者の間隙を覆う漏れ止めキャップ101,
外側円筒壁(第四円筒壁〉16に嵌合する漏れる止め筒
102、連結金具19の下端部に嵌合して、回転円筒体
11.内側円筒壁15、外側円筒壁16および前記漏れ
る止め筒102を支持する安定台103、該安定台10
3をa置する振動台104、押さえ筒105等から或る
The inlet 5 of the centrifugal self-cleaning filter B, which is similar to the device A, is connected to the discharge passage 61 of the centrifugal self-cleaning filter A.
Further, the inlet port 5C of a similar centrifugal self-cleaning filter C is connected to the discharge passage 61B of the filtration device B. The minimum mesh filter media layers of filter devices A, B, and C are R8, R2, and R3, respectively, and the mesh size is R.
r < R 2 < R). Opening/closing valves 73, 73B for respective discharge passages 72, 72B, 72C,
From 73C, it is possible to sequentially separate and collect liquids with small particle sizes of mixed foreign substances to liquids with large particle sizes of mixed foreign substances. In addition, by classifying mixed foreign substances by particle size as described above,
Changes in substances due to differences in particle size can be investigated. Next, Figure 8 shows an example of a jig used to efficiently and quickly fill the fine particle filtering material. The jig 100 includes a leak-proof cap 101 that fits into the rotating cylindrical body 1l and the inner cylindrical wall (third circular wall) 15 and covers the gap between them.
A leakage prevention tube 102 that fits into the outer cylindrical wall (fourth cylindrical wall) 16, a leakage prevention tube 102 that fits into the lower end of the connecting fitting 19, and connects the rotary cylindrical body 11, the inner cylindrical wall 15, the outer cylindrical wall 16, and the leakage prevention tube. Stable stand 103 supporting 102, said stable stand 10
3, a vibration table 104, a holding cylinder 105, etc.

治具100に遠心式自浄フィルタ1をセットして、振動
を加えながら枦過材8を押し込めば容易に充填できる.
Filling can be easily accomplished by setting the centrifugal self-cleaning filter 1 in the jig 100 and pushing in the filtering material 8 while applying vibration.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明にかかる遠心式自浄フィルタ付枦過装置
の縦断面図、第2図はその遠心式自洋フィルタの縦断面
図、第3図はその遠心式自浄フィルタの平断面図、第4
図はその円筒壁およびp材層の正面図、第5図はその正
面図、第6図および第7図はそれぞれ遠心式自浄フィル
タ付枦過装置を複数連結して用いる場合の組付け図、第
8図は微粒子状の枦過材を効率良く迅速に充填に用いる
治具の断面図である. 図中 A・・・遠心式自浄フィルタ付枦過裂置 1・・
・遠心式自浄フィルタ 2・・・回転筒 3・・・回転
装置 4・・・気密炉過槽 5・・・導入口 6・・・
排出口7・・・吐出口 8・・・炉過材 11・・・回
転円筒体 12・・・中実回転軸 l3・・・中空回転
筒 14・・・第二円筒壁 15・・・第三円筒聖16
・・・第四円筒壁14B、15B、16B・・・枦材層
 17・・・段付フランジ板 17A・・・押さえ板 
l8・・・段付ノランジ板 18A・・・シールリング
 19・・・連結金具43・・・液流ガイド 46・・
・着脱用フランジ板 71・・・吐出管 72・・・吐出路 74・・・加圧空気導入 路 代 理 人 石黒健二 第4図 第2図 第3図 15 14 第5図 第8図
FIG. 1 is a longitudinal cross-sectional view of a centrifugal self-cleaning filter-equipped filter according to the present invention, FIG. 2 is a vertical cross-sectional view of the centrifugal self-cleaning filter, and FIG. 3 is a plan cross-sectional view of the centrifugal self-cleaning filter. Fourth
The figure is a front view of the cylindrical wall and p-material layer, FIG. 5 is a front view, and FIGS. 6 and 7 are assembly diagrams when multiple centrifugal self-cleaning filters are connected and used. Figure 8 is a cross-sectional view of a jig used for efficiently and quickly filling fine-particle filtering material. In the diagram A...Centrifugal self-cleaning filter with over-split arrangement 1...
・Centrifugal self-cleaning filter 2...Rotating cylinder 3...Rotating device 4...Airtight furnace tank 5...Inlet 6...
Discharge port 7... Discharge port 8... Furnace filtration material 11... Rotating cylindrical body 12... Solid rotating shaft l3... Hollow rotating cylinder 14... Second cylindrical wall 15... No. Sancylindrical Saint 16
...Fourth cylindrical wall 14B, 15B, 16B...Brush material layer 17...Stepped flange plate 17A...Pressure plate
l8...Stepped norange plate 18A...Seal ring 19...Connecting fitting 43...Liquid flow guide 46...
- Attachment/detachment flange plate 71...Discharge pipe 72...Discharge path 74...Pressurized air introduction path Agent Kenji IshiguroFigure 4Figure 2Figure 3Figure 15 14 Figure 5Figure 8

Claims (1)

【特許請求の範囲】 1)同軸に配した三重以上の多重円筒壁を有する中空回
転体の遠心力発生面となる多重円筒壁各々に、内外連通
口を周設するとともに、該多重円筒壁の外周を網目が微
細な布またはろ材層などで覆い、前記中空回転体の下方
向回転軸部に吐出口を設けてなる遠心式自浄フィルタと
、 前記遠心式自浄フィルタを内蔵するとともに回転自在に
支持する気密ろ過槽と、 前記遠心式自浄フィルタを駆動するモータと、上方から
重力またはポンプにより加圧した被ろ過液を、前記気密
ろ過槽に導入する導入口と、ろ過作用により気密ろ過槽
内に増加する混在異物の排出口とからなる遠心式自浄フ
ィルタ付液体浄化装置において、 上記遠心式自浄フィルタは、上端を閉塞し、円筒壁に前
記内外連通口を周設し、下端に前記吐出口を設けてなる
回転円筒体を中心とし、 該回転円筒体の上下端部に外嵌する上部フランジ板と下
部フランジ板を螺合により固定し、前記多重円筒壁は、
分離独立した各円筒壁がシール材を介して前記上部フラ
ンジ板と下部フランジ板の間に固定され、上部フランジ
板を外すことにより各円筒壁は取外すことができ、 所定の隣合う外側円筒壁と内側円筒壁に、それぞれ微細
繊維群を硬質樹脂で連結強化してなる紐または帯を巻付
けて形成されるろ材層、または網目が微細な布等を固定
して、前記内外連通口を覆い、該外側円筒壁と内側円筒
壁の間に微粒子状物質を密封できる構造であり、 前記隣合う外側円筒壁と内側円筒壁の間に活性炭、珪藻
土、白土または粒子状多孔質セラミック等のろ過材ある
いはイオン交換樹脂等の粒子状物質を充填したことを特
徴とする遠心式自浄フィルタ付液体浄化装置。 2)前記気密ろ過槽は、遠心式自浄フィルタと同軸心の
円筒状で上下端が閉塞した形状を呈し、スクリュー羽根
状の液流ガイドが等間隔に斜下方向に向かって周設され
、遠心式自浄フィルタの回転により誘起される回転液流
により、下方向に向かう液流を発生する構造であり、気
密ろ過槽の下端部に混在異物の排出口が設けられている
ことを特徴とする請求項1に記載の遠心式自浄フィルタ
付液体浄化装置。 3)前記遠心式自浄フィルタの下方向回転軸部に設けた
吐出口には、吐出路が連結され、該吐出路に開閉バルブ
を取付けるとともに、吐出口と開閉バルブの間に、ポン
プにより加圧された空気を圧送する加圧空気導入路が開
閉バルブを介して接続されていることを特徴とする請求
項1または請求項2に記載の遠心式自浄フィルタ付液体
浄化装置。
[Scope of Claims] 1) In a hollow rotary body having three or more multiple cylindrical walls arranged coaxially, each of the multiple cylindrical walls serving as a centrifugal force generating surface is provided with an internal and external communication port, and the multiple cylindrical walls are A centrifugal self-cleaning filter whose outer periphery is covered with a cloth with a fine mesh or a filter medium layer, etc., and a discharge port is provided in the downward rotating shaft of the hollow rotating body; and a centrifugal self-cleaning filter in which the centrifugal self-cleaning filter is built-in and rotatably supported. a motor for driving the centrifugal self-cleaning filter; an inlet for introducing the liquid to be filtered pressurized by gravity or a pump from above into the airtight filtration tank; In a liquid purification device with a centrifugal self-cleaning filter, which is equipped with a centrifugal self-cleaning filter that has an outlet for discharging foreign matter that is increasing in number, the centrifugal self-cleaning filter has its upper end closed, the inner and outer communication ports provided around the cylindrical wall, and the discharge port provided at the lower end. An upper flange plate and a lower flange plate which are externally fitted to the upper and lower ends of the rotating cylindrical body are fixed by screwing around the provided rotating cylindrical body, and the multiple cylindrical wall is
Each separate and independent cylindrical wall is fixed between the upper flange plate and the lower flange plate via a sealing material, and each cylindrical wall can be removed by removing the upper flange plate, and the predetermined adjacent outer cylindrical wall and inner cylinder A filter layer formed by wrapping strings or bands made by connecting and reinforcing groups of fine fibers with hard resin, or cloth with a fine mesh, is fixed to the wall to cover the inner and outer communication ports, and It has a structure that can seal particulate matter between the cylindrical wall and the inner cylindrical wall, and a filter material such as activated carbon, diatomaceous earth, white clay, or granular porous ceramic or ion exchange material is installed between the adjacent outer cylindrical wall and the inner cylindrical wall. A liquid purification device with a centrifugal self-cleaning filter characterized by being filled with particulate matter such as resin. 2) The airtight filtration tank has a cylindrical shape coaxial with the centrifugal self-cleaning filter, with its upper and lower ends closed. A claim characterized in that the structure generates a downward liquid flow by a rotating liquid flow induced by the rotation of a self-cleaning filter, and a discharge port for mixed foreign matter is provided at the lower end of the airtight filtration tank. Item 1. The liquid purification device with a centrifugal self-cleaning filter according to item 1. 3) A discharge path is connected to the discharge port provided on the downward rotating shaft of the centrifugal self-cleaning filter, and an on-off valve is attached to the discharge path, and a pump applies pressure between the discharge port and the on-off valve. 3. The liquid purification device with a centrifugal self-cleaning filter according to claim 1 or 2, wherein the pressurized air introduction path for feeding the air under pressure is connected via an on-off valve.
JP30003989A 1989-11-17 1989-11-17 Liquid purifying apparatus equipped with centrifugal type self-purifying filter Granted JPH03161003A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30003989A JPH03161003A (en) 1989-11-17 1989-11-17 Liquid purifying apparatus equipped with centrifugal type self-purifying filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30003989A JPH03161003A (en) 1989-11-17 1989-11-17 Liquid purifying apparatus equipped with centrifugal type self-purifying filter

Publications (2)

Publication Number Publication Date
JPH03161003A true JPH03161003A (en) 1991-07-11
JPH0512006B2 JPH0512006B2 (en) 1993-02-17

Family

ID=17879963

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30003989A Granted JPH03161003A (en) 1989-11-17 1989-11-17 Liquid purifying apparatus equipped with centrifugal type self-purifying filter

Country Status (1)

Country Link
JP (1) JPH03161003A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004321893A (en) * 2003-04-23 2004-11-18 Maezawa Ind Inc Filtration apparatus
JP2011152488A (en) * 2010-01-26 2011-08-11 Panasonic Electric Works Co Ltd Centrifugal filter and water treatment apparatus using the same
CN110156197A (en) * 2019-07-03 2019-08-23 东莞市宇科机械科技有限公司 A kind of sewage-treatment plant and its application method of sewer outlet

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004321893A (en) * 2003-04-23 2004-11-18 Maezawa Ind Inc Filtration apparatus
JP4542749B2 (en) * 2003-04-23 2010-09-15 前澤工業株式会社 Filtration device
JP2011152488A (en) * 2010-01-26 2011-08-11 Panasonic Electric Works Co Ltd Centrifugal filter and water treatment apparatus using the same
CN110156197A (en) * 2019-07-03 2019-08-23 东莞市宇科机械科技有限公司 A kind of sewage-treatment plant and its application method of sewer outlet

Also Published As

Publication number Publication date
JPH0512006B2 (en) 1993-02-17

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