JPS6233511A - Centrifugal self-cleaning filter apparatus - Google Patents

Centrifugal self-cleaning filter apparatus

Info

Publication number
JPS6233511A
JPS6233511A JP60173497A JP17349785A JPS6233511A JP S6233511 A JPS6233511 A JP S6233511A JP 60173497 A JP60173497 A JP 60173497A JP 17349785 A JP17349785 A JP 17349785A JP S6233511 A JPS6233511 A JP S6233511A
Authority
JP
Japan
Prior art keywords
filter
cylindrical
filtered
rotating
liquid
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
JP60173497A
Other languages
Japanese (ja)
Other versions
JPH0582242B2 (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 JP60173497A priority Critical patent/JPS6233511A/en
Publication of JPS6233511A publication Critical patent/JPS6233511A/en
Publication of JPH0582242B2 publication Critical patent/JPH0582242B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To improve the filtration efficiency of the titled apparatus and to prevent the rediffusion of foreign matter mixed in a liq. to be filtered into the liq. by providing a cylindrical filter of specified structure which is submerged in the liq. to be filtered and used, a rotor, a means for rotating the rotor, a sealing member and a dust collecting means. CONSTITUTION:A cylindrical filter A is connected to a pump, the filter A is submerged in a liq. to be filtered, the pump is started, rotors 3 and 4 are rotated, sealing members 14, 15, 17 and 18 are pressed on a rotating shaft part to seal the shaft, the pressure is maintained thereafter and filtration proceeds. Meanwhile, the filtrate present in the region between a blade 5 and the inner peripheral surface of the filter A is passed through the mesh of a filter medium 2 and again pushed back to the filter vessel 30 along with the rotation and due to the blade 5 which is embedded in the peripheral edge part of the rotors 3 and 4 at a specified setting angle. Consequently, the self cleaning of the filter A is performed. Moreover, the rediffusion of foreign matter mixed in the liq. to be filtered and which has been released from the surface of the filter medium 2 into the liq. is prevented.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、濾材表面に沈積しようとする流体中の混在異
物を、濾過操作中に自動的に除去させることのできる遠
心式自浄フィルタ装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a centrifugal self-cleaning filter device that can automatically remove mixed foreign matter in a fluid that tends to deposit on the surface of a filter medium during a filtration operation. .

[従来の技術] ポンプを使用して圧送される流体の流路に除塵用フィル
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。この種のフィルタとして
は回転ドラムの外周面に濾布を巻きつけたものとか、フ
レーム体に濾材を張設したもの、あるいは一端が封止さ
れた短筒状の金網製フィルタエレメントの開口端にカー
トリッジ式の取付用基部を接合させたものなどが使われ
てきた。
[Prior Art] It is common practice in all industrial fields to simultaneously transport fluid and remove foreign matter mixed in the fluid by interposing a dust removal filter in the flow path of the fluid being pumped using a pump. It is widely practiced. This type of filter consists of a filter cloth wrapped around the outer circumferential surface of a rotating drum, a filter material stretched over a frame, or a short cylindrical wire mesh filter element with one end sealed. Those with a cartridge-type mounting base joined together have been used.

[発明が解決しようとする問題点] 上記の如き従来の除塵用フィルタは、濾過すべき流体中
に混在する異物の粒径が小さければ小さい程網目の細か
い濾材を必要とし、殊に異物混入量が多い場合には短期
間でil!Uの表面に異物が堆積して濾過能力が著しく
低下するので、甚だしい時間と労力の浪費を伴うフィル
タの洗浄作業を頻繁に繰返さなければならず、生産性の
低下の一要因をなしていた。
[Problems to be Solved by the Invention] In the conventional dust removal filter as described above, the smaller the particle size of the foreign matter mixed in the fluid to be filtered, the finer the filter medium is required. If there are many cases, il in a short period of time! Since foreign matter accumulates on the surface of the U and the filtration ability is significantly reduced, the cleaning operation of the filter must be repeated frequently, which involves a tremendous waste of time and labor, and is one of the causes of reduced productivity.

本発明は、濾過作業中に濾材表面に沈積しようとする被
濾過液中の異物を自動的に排除させるための機構を備え
た、いわば自浄式の流体源適用フィルタを提供すること
を目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a so-called self-cleaning filter that can be applied to a fluid source and is equipped with a mechanism for automatically removing foreign substances in a liquid to be filtered that tend to deposit on the surface of a filter medium during filtration work. .

[問題点を解決するための手段] 上記目的を達成するために本発明の遠心式自浄フィルタ
装置は、中空筒体の周壁面に濾材を取付けると共に、筒
軸部にポンプの吸入口への連通手段を設けた筒状フィル
タと、前記筒状フィルタの内周面に接して回転し、該回
転方向に向かって前記内周面に対して末広がりの取付は
角度を有する複数個のブレードを植設した回転体と、該
回転体の回動手段と、前記筒状フィルタの内空部を外気
から遮断するために前記筒軸部に設けられたシール部材
と、前記濾材の表面から遠心力により剥離された被濾過
液中の混入異物が液中に再拡散されることを防ぐための
集塵手段とを備えてなり、前記筒状フィルタを被濾過液
中に浸漬させて使用する構成を採用した。
[Means for Solving the Problems] In order to achieve the above object, the centrifugal self-cleaning filter device of the present invention has a filter medium attached to the peripheral wall surface of the hollow cylinder, and a cylinder shaft that communicates with the suction port of the pump. A cylindrical filter provided with a means, and a plurality of blades that rotate in contact with the inner circumferential surface of the cylindrical filter and have an angle to the inner circumferential surface in the direction of rotation. a rotary body, a rotating means for the rotary body, a sealing member provided on the cylindrical shaft portion for insulating the inner space of the cylindrical filter from outside air, and peeling from the surface of the filter medium by centrifugal force. and a dust collection means for preventing foreign matter mixed in the filtered liquid from being re-diffused into the liquid, and the cylindrical filter is used by being immersed in the filtered liquid. .

[作用および発明の効果] 筒状フィルタの筒軸部に設けである連通手段を配管によ
ってポンプの吸入口に接続させたうえ、フィルタを被濾
過液中に浸漬しポンプを起動させると共に回転体を回動
させると、ポンプの吸引力によって筒状フィルタ内空部
は一瞬にして減圧されるために、筒状フィルタの内外の
圧力差によってシール部材が回転軸部に押圧されて軸封
状態がもたらされ、以後はこの圧力差が維持されて濾過
が進行する− 一方回転体の周縁部に特定の取付角度をもって植設され
たブレードが筒状フィルタの内周面に沿って回転するの
に伴って、このブレードと筒状フィルタの内周面に挟ま
れた領域に存在する濾過液はブレードによって圧縮作用
力と遠心作用力を受けるために、濾材の網目をくぐり扱
けて再び濾過槽に押し戻される。この時網目に吸着され
ていた被濾過液中の侵入異物は網目から押し出されて脱
落し、フィルタの自己浄化作用が営まれる。
[Operation and Effects of the Invention] The communication means provided on the cylindrical shaft of the cylindrical filter is connected to the suction port of the pump via piping, and the filter is immersed in the liquid to be filtered to start the pump and at the same time, the rotating body is started. When it is rotated, the pressure inside the cylindrical filter is instantly reduced by the suction force of the pump, so the sealing member is pressed against the rotating shaft due to the pressure difference between the inside and outside of the cylindrical filter, and the shaft sealing state is maintained. From then on, this pressure difference is maintained and filtration progresses. On the other hand, as the blades, which are installed at a specific angle on the periphery of the rotating body, rotate along the inner circumferential surface of the cylindrical filter. The filtrate existing in the area sandwiched between the blade and the inner peripheral surface of the cylindrical filter is subjected to compressive force and centrifugal force by the blade, so it can be handled through the mesh of the filter medium and pushed back into the filtration tank. It will be done. At this time, the foreign matter in the liquid to be filtered that has been adsorbed by the mesh is pushed out from the mesh and falls off, allowing the filter to perform its self-cleaning action.

従って従来の濾過装置の如く濾過運転中に急速に起こる
濾材の目詰りの状態を除くために、頻繁に濾材の洗浄作
業を行わなければならないという不都合が解消され、濾
過効率が著しく向上する。
Therefore, the inconvenience of having to frequently wash the filter medium in order to remove the clogging of the filter medium that rapidly occurs during filtration operation, which is the case with conventional filtration devices, is eliminated, and the filtration efficiency is significantly improved.

[実施例] 以下に付図に示す実施例に基づいて本発明の構成を具体
的に説明する。
[Example] The structure of the present invention will be specifically described below based on the example shown in the attached drawings.

第1図ないし第4図に描かれた本発明による第1実施例
装置の説明図において、Aは筒状フィルタ、1は筒状フ
ィルタAのケーシングであって、閉鎖された内空部を有
しくill材を準気密材料とみなせば)金属ないしは合
成樹脂製の偏平な筒体をなしている。1aはフィルタケ
ーシング1の周壁面に一定の間隔を隔てて設けられた縦
長のスリット群であって、このスリット状間口には濾材
2が張設されている。濾材2は濾布や様々なメツシュの
金網などからなる帯状体をなしており、筒状フィルタへ
の外周面に巻きつけられている。3と4は筒状フィルタ
Aのケーシング1の内空部にあって、その頂面と底面に
それぞれ接して配設された回転体、7は円盤状をなす回
転体3の回転軸であって中空筒体をなしており、ベアリ
ング10を介してケーシング1の頂壁面の筒軸部に形成
させたポンプ吸入口への連通手段としての軸受筒13内
に嵌着されている。8は同じく円盤状をなす回転体4の
回転軸であって、ベアリングボール9を介してケーシン
グ1の底壁面の筒軸部に設けた凹み状受座に嵌入されて
いる。
In the explanatory diagrams of the first embodiment of the device according to the present invention shown in FIGS. 1 to 4, A is a cylindrical filter, and 1 is a casing of the cylindrical filter A, which has a closed inner space. If we consider ill material to be a semi-airtight material, it is a flat cylindrical body made of metal or synthetic resin. Reference numeral 1a denotes a group of vertically elongated slits provided at regular intervals on the peripheral wall surface of the filter casing 1, and the filter medium 2 is stretched across the slit-like openings. The filter medium 2 is a band-like body made of filter cloth or various mesh wire gauze, and is wrapped around the outer peripheral surface of the cylindrical filter. 3 and 4 are rotary bodies disposed in the inner space of the casing 1 of the cylindrical filter A, in contact with the top and bottom surfaces thereof, respectively; 7 is a rotating shaft of the disc-shaped rotary body 3; It is a hollow cylindrical body, and is fitted through a bearing 10 into a bearing cylinder 13 that serves as a means for communicating with a pump suction port formed in the cylinder shaft portion of the top wall surface of the casing 1 . Reference numeral 8 denotes a rotating shaft of the rotating body 4, which is also disk-shaped, and is fitted through a bearing ball 9 into a recessed seat provided in the cylindrical shaft portion of the bottom wall surface of the casing 1.

5は上下一対の回転体3および4の相対向する周縁部に
架は渡すようにして取付けられた複数個のブレードであ
って、第2図に描かれたように巾方向に円弧形状を有す
る帯状板をなし、ボルト6によって両端部をそれぞれ回
転体3と4に固定されている。11は回転軸7の回動用
ブーりである。
Reference numeral 5 denotes a plurality of blades that are attached to the opposing peripheral edges of the pair of upper and lower rotating bodies 3 and 4 so that the rack crosses over the blades, and has an arc shape in the width direction as shown in FIG. It forms a band-shaped plate, and its both ends are fixed to the rotating bodies 3 and 4 by bolts 6, respectively. Reference numeral 11 denotes a rotary boot for rotating the rotating shaft 7.

12は回転体3の中空状回転軸7内に挿入された、ポン
プの吸入口に接続される配管の一端部分であり、回転軸
7の下端面から突出してケーシング1内に位置するその
先端にはフランジ状部12aが形成されている。20は
中空回転軸γ内に配管12を支持させるためのベアリン
グである。14と15は中空状回転軸7とこの内空部に
挿通されているポンプへの配管12との間の大気に導通
している空隙をケーシング1の内空部から遮断するため
の第1のシール部材であり、17と18は軸受筒13と
その内空部に挿通された回転軸7との間の大気と連通状
態にある空隙をケーシング1の内空部から遮断するため
の第2のシール部材であって、これら両シール部材は回
転軸1の下端部・近傍の部分図としての第3図および第
1図の(ロ)−(ロ)断面図としてての第4図によって
理解されるようにゴム弾性材からなる2つの半円筒体を
組合わせて短筒体を形作らせた如き構成を備えた内側シ
ール部材14(17)と同様な構成を備えた外側シール
部材15(18)とを、つき合わせ個所が円周方向に互
いに90°へたたるようにして同軸的且つ幾分の間隔を
へだてて嵌合させた如き構成を備えている。16と19
はそれぞれ第1と第2シール部材の固定用止め環である
Reference numeral 12 denotes one end portion of a pipe inserted into the hollow rotating shaft 7 of the rotary body 3 and connected to the suction port of the pump. A flange-shaped portion 12a is formed. 20 is a bearing for supporting the pipe 12 within the hollow rotating shaft γ. Reference numerals 14 and 15 indicate a first opening for blocking the air gap communicating with the atmosphere between the hollow rotating shaft 7 and the pump pipe 12 inserted into the inner space of the casing 1. Seal members 17 and 18 are second sealing members for blocking the air gap between the bearing sleeve 13 and the rotating shaft 7 inserted into the inner space, which is in communication with the atmosphere, from the inner space of the casing 1. These two seal members are understood from FIG. 3, which is a partial view of the lower end and vicinity of the rotating shaft 1, and FIG. 4, which is a sectional view taken along line (B)-(B) of FIG. The outer seal member 15 (18) has the same structure as the inner seal member 14 (17), which has a structure in which two semi-cylindrical bodies made of rubber elastic material are combined to form a short cylinder. and are fitted together coaxially and with some distance between them so that their abutting points are angled at 90° from each other in the circumferential direction. 16 and 19
are retaining rings for fixing the first and second seal members, respectively.

シール部材14と15および17と18は共に弾力性と
機械的強度殊に耐摩耗性にすぐれたウレタンゴムや弗素
ゴムなどで作られており、常態においては垂直な筒壁面
をなすように形作られているが、配管12を通じてポン
プの吸引ツノがケーシング1内に及ぼされると、濾材2
の通気抵抗によってケーシング1の内空部は大気圧に対
して減圧状態となり、シール部材14と15は大気圧に
押されてその内径が拡張され、外周面が配管12のフラ
ンジ状部12aの周縁立ち上がり部分12bの内周面に
向って押しつけられることによって前述の如きシール部
材としての役目を果たす。同様にシール部材17と18
の外周面は回転体3の頂面に形成されている円環状突出
部3aの内周面に大気圧によって押しつけられることに
よってその役目を果たす。30は筒状フィルタAを内部
に組込んだ濾過槽であって被濾過液の注入口30aと排
出口30bを備えている。
The seal members 14 and 15 and 17 and 18 are both made of urethane rubber, fluorine rubber, etc., which have excellent elasticity and mechanical strength, especially wear resistance, and are normally shaped to form a vertical cylindrical wall surface. However, when the suction horn of the pump is applied into the casing 1 through the piping 12, the filter medium 2
Due to the ventilation resistance, the inner space of the casing 1 becomes depressurized with respect to the atmospheric pressure, and the seal members 14 and 15 are pushed by the atmospheric pressure and their inner diameters are expanded, so that the outer peripheral surface becomes the peripheral edge of the flange-shaped portion 12a of the pipe 12. By being pressed toward the inner circumferential surface of the rising portion 12b, it functions as a sealing member as described above. Similarly, seal members 17 and 18
The outer circumferential surface of the rotating body 3 fulfills its role by being pressed against the inner circumferential surface of the annular projection 3a formed on the top surface of the rotating body 3 by atmospheric pressure. 30 is a filtration tank incorporating a cylindrical filter A therein, and is provided with an inlet 30a and an outlet 30b for the liquid to be filtered.

第5図は上記実施例装置の使用方法を例示した、濾過シ
ステムの構成図であって、21は回転体3および4の回
動用の無段変速モータまたは無段変速機を出力軸に接続
させた定速回転型モータ、22はVベルト、23はモー
タ制御箱、40は濾過用ポンプ、31は被濾過液、32
はポンプ40の吐出口配管、33は濾過済み液の貯槽、
34は濾過槽30の前置タンク、35と37および36
は濾過槽30と前置タンク34とを結ぶ配管および送液
ポンプである。
FIG. 5 is a configuration diagram of a filtration system illustrating how to use the above-mentioned embodiment device, and 21 is a continuously variable speed motor or continuously variable transmission for rotating the rotating bodies 3 and 4 connected to the output shaft. 22 is a V-belt, 23 is a motor control box, 40 is a filtration pump, 31 is a liquid to be filtered, 32
is a discharge port pipe of the pump 40, 33 is a storage tank for filtered liquid,
34 is a pre-tank of the filtration tank 30, 35, 37 and 36
are piping and a liquid pump that connect the filtration tank 30 and the pre-tank 34.

次に上記実施例装置の作動について説明する。Next, the operation of the above embodiment device will be explained.

装置を第5図に例示されたようにセットし、ポンプ40
の吐出口部に取付けたこの図では省かれている吐出バル
ブを絞り込んだ状態のもとに、ポンプ40の駆動用モー
タを起動させると同時に回転体3および4の回動用無段
変速モータ21を低速で始動させる。筒状フィルタA内
が濾過液で満たされておらずまた濾材2の網目が極めて
細かい場合には、あらかじめ筒状フィルタAの内空部を
濾過液で満たしておく。
Set up the apparatus as illustrated in FIG.
With the discharge valve (not shown in this figure) installed at the discharge port of the pump 40 in a closed state, the motor for driving the pump 40 is started, and at the same time, the continuously variable speed motor 21 for rotating the rotors 3 and 4 is started. Start at low speed. If the inside of the cylindrical filter A is not filled with filtrate and the mesh of the filter medium 2 is extremely fine, the inner space of the cylindrical filter A is filled with the filtrate in advance.

濾材2による被濾過液中の混入異物の除去能力は、濾材
2の網目に混入異物がある程度沈着して網目が狭められ
ることによって向上されるので、幾分かの異物沈着はむ
しろ好ましい。装置の起動後、モータ21の制御装置を
操作して回転体3および4を第2図に矢印(ハ)で示さ
れた方向に向けて次第に回転数を高めていくと、回転体
3の周縁部には筒状フィルタのケーシング1の内周面に
近接させるようにして、且つこの内周面に漸近するよう
な取付角度をもってブレード5が植設されているので、
ポンプ40の吸引力によってケーシング1内に吸入され
た濾過液の内、このブレード5とケーシング1の内壁面
との間に形成されたクサビ状空隙に存在する濾過液は矢
印(ニ)で示された如くこのクサビ状空隙に押し込まれ
るような作用“力を受けることになって液圧が上昇し、
遂には矢印すで描かれているように濾材2の網目からケ
ーシング1の外側に向けて押し出されるに到る。そして
この時網目に詰っていた異物もまた網目から押し出され
て脱落し、いわばフィルタの自浄作用が営まれることに
なる。回転体3の回転数が更に上昇すれば、ブレード5
の表面に生ずる遠心作用力が上記の液体の押圧作用力に
付加されることとなって自浄作用は一段と高められる。
The ability of the filter medium 2 to remove foreign substances from the liquid to be filtered is improved when the foreign substances are deposited to some extent on the mesh of the filter medium 2 and the mesh is narrowed, so some amount of foreign substance deposition is rather preferable. After starting the device, the control device of the motor 21 is operated to direct the rotating bodies 3 and 4 in the direction shown by the arrow (c) in FIG. 2 and gradually increase the rotation speed. Since the blade 5 is installed in the section so as to be close to the inner circumferential surface of the casing 1 of the cylindrical filter, and at an installation angle that approaches the inner circumferential surface asymptotically,
Among the filtrate sucked into the casing 1 by the suction force of the pump 40, the filtrate existing in the wedge-shaped gap formed between the blade 5 and the inner wall surface of the casing 1 is indicated by an arrow (d). As the fluid is forced into this wedge-shaped gap, the fluid pressure increases.
Eventually, it is pushed out from the mesh of the filter medium 2 toward the outside of the casing 1, as indicated by the arrow. At this time, the foreign matter that was stuck in the mesh is also pushed out and falls out, so that the filter performs a self-cleaning action. If the rotation speed of the rotating body 3 increases further, the blade 5
Since the centrifugal force generated on the surface of the liquid is added to the pressing force of the liquid, the self-cleaning effect is further enhanced.

しかし前述の如く濾材2の表面への異物の幾分かの沈積
を許容して異物の除去能力を高めることは望ましいが、
一方では濾過作業の効率化という要求もあるので、濾過
済み液体中の異物残存量をチェックしながら、回転体3
の回転数を調節し、同時に吐出バルブの開度も変化させ
て筒状フィルタのケーシング1内に吸入される濾過液量
とポンプ40からの吐出量とのバランスを計る。吐出バ
ルブを開きすぎるとケーシング1内への濾過液の補給が
追いつかず、ポンプ40は空転することになる。
However, as mentioned above, it is desirable to allow some of the foreign matter to settle on the surface of the filter medium 2 to increase the foreign matter removal ability;
On the other hand, there is also a demand for more efficient filtration work, so while checking the amount of foreign matter remaining in the filtered liquid,
The amount of filtrate sucked into the casing 1 of the cylindrical filter and the amount discharged from the pump 40 are balanced by adjusting the rotation speed of the pump 40 and at the same time changing the opening degree of the discharge valve. If the discharge valve is opened too much, the filtrate cannot be replenished into the casing 1, and the pump 40 will idle.

濾過効果と吐出量との兼ね合いで回転体3の最適回転数
が決定された後は同一条件のもとて操業する限り、この
決定回転数と吐出バルブ開度に装置の作動状態を固定さ
せて置けば、濾材2の表面に被濾過液中の混入異物が次
第に沈積して経時的に濾過効率が低下する不都合を来た
すことなく、安定した濾過作業を継続させることができ
る。
After the optimum rotation speed of the rotating body 3 has been determined based on the balance between the filtration effect and the discharge amount, the operating state of the device is fixed at this determined rotation speed and the discharge valve opening as long as it is operated under the same conditions. If this is done, it is possible to continue stable filtration work without causing the inconvenience that foreign matter in the liquid to be filtered gradually accumulates on the surface of the filter medium 2 and the filtration efficiency decreases over time.

次に上記実施例に示された構成を備えたテスト装置を使
って、回転体3を回転させた場合と回転させなかった場
合の装置の濾過能力(吐出量)の経時変化を比較したい
くつかの実験の結果を、各実験条件の一覧表としての表
1と、これらの各々の実験について求めたポンプ吐出量
対運転時間の相関グラフとして第10図ないし第13図
を参照しなから説明する。各グラフには同一条件のもと
て5回繰返して行われた実験の測定値をプロットし、こ
のプロットの分布領域を帯状斜線領域として(イ)〜(
ト)の如く表示した。
Next, using a test device having the configuration shown in the above example, some comparisons were made of changes over time in the filtration capacity (discharge amount) of the device when the rotating body 3 was rotated and when it was not rotated. The results of this experiment will be explained with reference to Table 1, which is a list of each experimental condition, and Figures 10 to 13, which are graphs showing the correlation between pump discharge amount and operating time obtained for each of these experiments. . In each graph, measured values from experiments conducted five times under the same conditions are plotted, and the distribution area of this plot is defined as a band-shaped diagonal area (A) to (
It was displayed as follows.

表1のNo、1の実験結果を図示した第10図において
回転体3を回転させなかった場合には、帯状グラフ(ロ
)にみられるように、装置の作動直後から吐出量は減少
の一途をたどり、約4分後に半減し、8分後には1/1
0程度に低落しているのに対して回転体3を200rp
mで回転させた場合にはグラフ(イ)に描かれているよ
うに10分経過後においても目立った吐出量の低下はみ
られず、本発明装置の濾過性能の卓抜さが明確に読み取
れる。
In Fig. 10, which shows the experimental results of No. 1 in Table 1, when the rotating body 3 was not rotated, the discharge amount continued to decrease immediately after the device was activated, as seen in the band graph (b). It decreased by half after about 4 minutes, and by 1/1 after 8 minutes.
The rotation speed of rotating body 3 is 200 rpm while the rotation speed has decreased to about 0.
When rotated at m, as shown in graph (A), there was no noticeable drop in the discharge amount even after 10 minutes, and the outstanding filtration performance of the device of the present invention can be clearly seen.

第2および第3の実験は、第1の実験に混入異物として
使われた鉄粉に較べてはるかに濾材2に目詰りを生じさ
せやすい紙バルブを用いたので、濾材2の自浄作用の効
果は第11図と第12図にそれぞれ明らかなように回転
体3を回転させた場合と回転させない場合のグラフ(ハ
)と(ニ)および(ホ)と(へ)とでは極端なまでに経
時下降曲線の傾度が相違している。
The second and third experiments used paper valves, which are much more likely to clog the filter medium 2 than the iron powder used as the foreign material in the first experiment, so the effect of the self-cleaning action of the filter medium 2 was evaluated. As is clear from Fig. 11 and Fig. 12, respectively, graphs (C) and (D) and (E) and (E) when the rotating body 3 is rotated and when it is not rotated have extremely large changes over time. The slopes of the downward curves are different.

第4の実験は回転体3の回転数と吐出量以外は第3の実
験と同一のテスト条件に保たせて回転数と濾過性能の相
関性を求めるべく行ったものである。そのテスト結果を
まとめた第13図にみられるように、回転体3の回転数
がaoorpm時には10分経過後にもグラフAにみら
れるように目立った濾過能力の低下は認められず、40
0rpm時のグラフBもグラフAに較べてさして相違が
なく ioorpm時のグラフDに到って始めて5分経
過後に濾過性能は運転開始時の80%内外にまで低下す
るものの以後はほぼこの能力水準に維持されており、回
転数零時のグラフ(ト)とは較ぶべくもないことが示さ
れている。勿論回転体3の最適回転数は濾過条件の相違
する毎に変動するが、いくつかの実験結果を総合的に勘
案すれば、200〜400rpHの範囲においてすこぶ
る有効な濾材の自浄効果を生ずるものと解される。勿論
それ以上に回転数を上げれば更に幾分かの性能向上が期
待される。
The fourth experiment was conducted under the same test conditions as the third experiment, except for the rotation speed of the rotating body 3 and the discharge amount, in order to determine the correlation between the rotation speed and the filtration performance. As shown in Fig. 13, which summarizes the test results, when the rotation speed of the rotating body 3 is aoorpm, no noticeable decrease in filtration capacity is observed even after 10 minutes as seen in graph A, and 40
Graph B at 0 rpm is not much different from graph A. After 5 minutes of reaching graph D at ioorpm, the filtration performance drops to around 80% of what it was at the start of operation. It is shown that there is no comparison with the graph (g) when the rotation speed is zero. Of course, the optimum rotational speed of the rotating body 3 varies depending on the filtration conditions, but if several experimental results are taken into consideration, it is concluded that a very effective self-cleaning effect of the filter medium is produced in the range of 200 to 400 rpm. be understood. Of course, if the rotation speed is increased beyond that, it is expected that the performance will improve somewhat.

上記の第1実施例装置では、濾材表面から剥離されて濾
過槽内に次第に堆積してくる被濾過液中の混入異物の除
去手段が示されていないので、次に第1実施例装置に混
入異物の除去用集塵手段を付設した、第2実施例装置に
ついて第6図ないし第9図を参照しながら説明する。
In the device of the first embodiment described above, there is no means for removing foreign matter mixed in the liquid to be filtered, which is peeled off from the surface of the filter medium and gradually accumulated in the filtration tank. A second embodiment of the apparatus equipped with a dust collecting means for removing foreign matter will be described with reference to FIGS. 6 to 9.

50は回転フィルタAの自浄作用によって濾材2の表面
から除去された被濾過液中の異物が濾過槽30内に再拡
散してしまうことを防止するための集塵ケースであって
、頂面が解放された筒状容器としての形状を備えており
、その内周面には、円周の174よりやや短い円弧長さ
を有するスクリュー羽根状の4枚の液流ガイド部材51
が円周方向に等間隔を保って斜め下向き方向に取付けら
れている。
Reference numeral 50 denotes a dust collection case for preventing foreign matter in the liquid to be filtered removed from the surface of the filter medium 2 by the self-cleaning action of the rotary filter A from re-diffusion into the filter tank 30. It has the shape of an open cylindrical container, and on its inner peripheral surface are four liquid flow guide members 51 in the shape of screw blades having an arc length slightly shorter than the circumference 174.
are mounted diagonally downward at equal intervals in the circumferential direction.

回転体1はこれらの液流ガイド部材51に包囲された状
態のもとに集塵ケース50内に配置され、ケース50の
底壁面には沈積してくる異物の排出川底孔50aが複数
個設けられている。50bはケース50の外周面に形成
されたフランジ状部であって、濾過液槽30の底板30
dの中心部に穿ったケース50の嵌着用穴の口縁部に係
止させた状態のもとにボルト53を用いて底板30dに
固定されている。
The rotating body 1 is placed in a dust collection case 50 in a state surrounded by these liquid flow guide members 51, and a plurality of bottom holes 50a are provided on the bottom wall surface of the case 50 to discharge foreign matter that accumulates. It is being 50b is a flange-shaped portion formed on the outer circumferential surface of the case 50, and is a flange-shaped portion formed on the outer peripheral surface of the case 50, and is
It is fixed to the bottom plate 30d using bolts 53 while being engaged with the edge of the fitting hole of the case 50 drilled in the center of the case 50.

55は集塵ケース50の解放された頂面を覆いかくずよ
うにして中空回転軸7に嵌着させた回転蓋体であって、
集塵ケース内に堆積する異物が上方に舞い上がるのを防
止する。この回転蓋体は極めて偏平な逆ろうと形状を備
えており、その円錐面には半径方向に多数のスリット5
5aが設けられている。そしてこのスリット55aの長
手方向の両側壁面aは第8図に描かれているように、回
転蓋体55の回転方向に向って上向きの斜面をなしてい
るので、蓋体55の回転に伴って、集塵ケース50の外
側にあってこのスリット55aの前面に位置する被濾過
液は斜面aによる衝突を受けることになり、衝突エネル
ギーを受は取った液は斜面に沿って下降流に転じて集塵
ケース50内に流入させられる。従ってこのような液流
ガイド機能を有するスリット状間口55aの働ぎによっ
て、ケース50内に次第に堆積されて来る濾過異物が液
の動きに伴われて浮上し、集塵ケース50の外にのがれ
出て再び被濾過液中に拡散してしまう不都合の発生が防
止される。
Reference numeral 55 denotes a rotary lid body fitted onto the hollow rotary shaft 7 so as to cover the open top surface of the dust collection case 50,
To prevent foreign matter accumulating in a dust collection case from flying upward. This rotary lid has an extremely flat inverted funnel shape, and its conical surface has many slits 5 in the radial direction.
5a is provided. As shown in FIG. 8, both side walls a of the slit 55a in the longitudinal direction are sloped upward in the direction of rotation of the rotary lid 55, so that as the lid 55 rotates, The liquid to be filtered, which is located outside the dust collection case 50 and in front of this slit 55a, will be collided with the slope a, and the liquid that has received the collision energy will turn into a downward flow along the slope. The dust is allowed to flow into the dust collection case 50. Therefore, due to the function of the slit-shaped opening 55a having such a liquid flow guide function, the filtration foreign matter that has gradually accumulated inside the case 50 floats up with the movement of the liquid, and is prevented from coming out of the dust collecting case 50. This prevents the inconvenience of leaking out and diffusing into the filtered liquid again.

一旦ケース50内に吸入された被濾過液のうち、部材2
の網目をくぐり扱は得なかった過剰分はケース50の頂
部周縁と回転蓋体55の外周縁との隙間すを通過して濾
過槽30内の自由空間にもどされるが、この還流に随伴
される異物の量はわずかである。
Of the liquid to be filtered once sucked into the case 50, the member 2
The excess amount that has not passed through the mesh passes through the gap between the top periphery of the case 50 and the outer periphery of the rotary lid 55 and is returned to the free space within the filtration tank 30, but is accompanied by this reflux. The amount of foreign matter involved is small.

55は回転蓋体55の取付用筒体、56は取付ボルトで
ある。
55 is a cylinder for mounting the rotary lid 55, and 56 is a mounting bolt.

60は回転フィルタAの濾材2表面から遠心作用力によ
って剥落させられ、次第に集塵ケース50内に堆積して
くる被濾過液中の混入異物を装置の外部に導き出すため
の縦型スクリューコンベアのケーシングである。61は
内蔵された縦向きスクリュー、62はスクリュー610
回転軸、63と64はそれぞれ回転軸62の上側ボール
軸受と下側ベアリング、65はスクリュー61を回転軸
62に固定させるためのボルト、66はケーシング60
の液漏れ防止用シール材、61はシール材66の抑圧固
定用中空ボルト、そして69はスクリュー61の駆動用
モータの取付はベースである。ケーシング60はその上
端部に設けた7ランジ状部を固定用ボルト68によって
集塵ケース50の底面に結合させている。
Reference numeral 60 denotes a casing of a vertical screw conveyor for guiding foreign matter contained in the liquid to be filtered, which is peeled off from the surface of the filter medium 2 of the rotary filter A by centrifugal force and gradually accumulated in the dust collection case 50, to the outside of the device. It is. 61 is a built-in vertical screw, 62 is a screw 610
The rotating shaft, 63 and 64 are the upper ball bearing and lower bearing of the rotating shaft 62, respectively, 65 is a bolt for fixing the screw 61 to the rotating shaft 62, and 66 is the casing 60.
61 is a hollow bolt for suppressing and fixing the sealing material 66, and 69 is a base on which a driving motor for the screw 61 is mounted. The casing 60 has seven flange-shaped portions provided at its upper end that are coupled to the bottom surface of the dust collection case 50 with fixing bolts 68.

70は縦型スクリューコンベアによって集塵ケース50
の底部から排出させた異物を水平方向に移送させるため
の横型スクリューコンベアのケーシングであり、71は
内蔵された横置ぎスクリュー、72−はスクリュー71
の回転軸、73は軸受筒、74はベアリング、75は軸
シール用パツキン、76はパツキン75の押圧固定用中
空ボルトである。コンベアケーシング70の異物導入ロ
ア0aは縦型コンベアケーシング60の底部排出口に接
続されている。77は横型コンベアケーシングの排出ロ
ア0bに嵌着させた排出口の延長用ゴムホースまたは配
管である。
70 is a dust collection case 50 by a vertical screw conveyor.
This is the casing of a horizontal screw conveyor for horizontally transporting foreign matter discharged from the bottom of the conveyor, 71 is a built-in horizontal screw, and 72- is a screw 71.
, 73 is a bearing cylinder, 74 is a bearing, 75 is a shaft seal packing, and 76 is a hollow bolt for pressing and fixing the packing 75. The foreign matter introduction lower Oa of the conveyor casing 70 is connected to the bottom discharge port of the vertical conveyor casing 60. 77 is a rubber hose or piping for extending the discharge port fitted to the discharge lower 0b of the horizontal conveyor casing.

第9図は第2実施例装置の使用状況を例示した濾過シス
テムの構成図であって、80は縦型スクリューコンベア
の駆動用モータ、81はモータ80の作動制御箱、82
は軸継手である。90は横型スラリ1−コンベアの駆動
用モータ、91はモータ90の作動制御箱、92は軸継
手である。他の符号は前記のそれと共通している。
FIG. 9 is a configuration diagram of a filtration system illustrating the usage of the second embodiment device, in which 80 is a driving motor for a vertical screw conveyor, 81 is an operation control box for the motor 80, and 82
is a shaft coupling. 90 is a drive motor for the horizontal slurry 1 conveyor, 91 is an operation control box for the motor 90, and 92 is a shaft joint. Other symbols are the same as those described above.

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

第1図ないし第5図は本発明による第1実施例装置の説
明図であって、第1図は装置の側断面図、第2図は第1
図の(イ)−(イ)断面図、第3図は第1図の部分図、
第4図は第1図の(ロ)−(ロ)断面図、第5図は装置
の使用状況の例示図である。 第6図ないし第9図は第2実施例装置の説明図であり、
第6図は装置の側断面図、第7図は第6図の(ホ)−(
ホ)断面図、第8図は回転蓋体の部分上面図とその(へ
)−(へ)断面図、第9図は装置の使用状況の例示図で
ある。 第10図ないし第13図は第1実施例装置とほぼ同一の
構造のテスト装置について、回転体3および4の回転の
有無と濾過能力との相対性を求めた実、験データである
。 図中 A・・・筒状フィルタ 1・・・筒状フィルタの
ケーシング 2・・・濾材 3.4・・・回転体 5・
・・ブレード 7・・・中空回転軸(連通手段)14.
15.17.18・・・シール部材 30・・・濾過槽
 50・・・集塵ケース 55・・・回転蓋体 60.
70・・・コンベアのケーシング 40・・・ポンプ
1 to 5 are explanatory diagrams of a first embodiment of the device according to the present invention, in which FIG. 1 is a side sectional view of the device, and FIG. 2 is a first embodiment of the device.
(A)-(A) sectional view in the figure, Figure 3 is a partial view of Figure 1,
FIG. 4 is a sectional view taken along line (b)-(b) of FIG. 1, and FIG. 5 is an illustrative view of the usage status of the apparatus. 6 to 9 are explanatory diagrams of the second embodiment device,
FIG. 6 is a side sectional view of the device, and FIG. 7 is a (E)-(
e) sectional view; FIG. 8 is a partial top view of the rotary lid body and a cross-sectional view thereof; FIG. 10 to 13 show actual experimental data for determining the relativity between the presence or absence of rotation of the rotating bodies 3 and 4 and the filtration capacity for a test device having almost the same structure as the device of the first embodiment. In the figure A...Tubular filter 1...Casing of the cylindrical filter 2...Filtering medium 3.4...Rotating body 5.
...Blade 7...Hollow rotating shaft (communication means) 14.
15.17.18 Seal member 30 Filtration tank 50 Dust collection case 55 Rotating lid body 60.
70...Conveyor casing 40...Pump

Claims (1)

【特許請求の範囲】 1)中空筒体の周壁面に濾材を取付けると共に、筒軸部
にポンプの吸入口への連通手段を設けた筒状フィルタと
、 前記筒状フィルタの内周面に接して回転し、該回転方向
に向かつて前記内周面に対して末広がりの取付け角度を
有する複数個のブレードを植設した回転体と、 該回転体の回動手段と、 前記筒状フィルタの内空部を外気から遮断するために前
記筒軸部に設けられたシール部材と、前記濾材の表面か
ら遠心力により剥離された被濾過液中の混入異物が液中
に再拡散されることを防ぐための集塵手段とを備えてな
り、 前記筒状フィルタを被濾過液中に浸漬させて使用するこ
とを特徴とする遠心式自浄フィルタ装置。 2)前記シール部材は、前記回転軸部の軸受に嵌着させ
たゴム弾性材製の短筒状体からなり、前記圧力差によつ
て筒径が拡張されることによつて回転軸に圧接されて前
記空隙が封鎖されるように構成されていることを特徴と
する特許請求の範囲第1項記載の遠心式自浄フィルタ装
置。 3)前記集塵手段は、前記筒状フィルタを包囲して設け
られた筒状集塵ケースと、該集塵ケースの頂面開口を覆
うようにして前記回転体の回転軸に嵌着させた回転蓋体
と、前記集塵ケースの底面開口部に接続させた、前記混
入異物の排出用コンベアとを備えてなり、前記回転蓋体
には被濾過液を前記集塵ケース内に流入させるための、
液流ガイド機能を有する開口が設けられていることを特
徴とする特許請求の範囲第1項または第2項記載の遠心
式自浄フィルタ装置。
[Scope of Claims] 1) A cylindrical filter in which a filter medium is attached to the peripheral wall surface of a hollow cylindrical body and a means for communicating with the suction port of the pump is provided in the cylindrical shaft portion; a rotating body having a plurality of blades installed therein, the blades rotating in the direction of rotation and having a mounting angle that widens towards the inner circumferential surface in the direction of rotation; a rotating means for the rotating body; A sealing member provided on the cylindrical shaft portion to isolate the empty space from outside air, and a sealing member provided on the cylindrical shaft portion to prevent foreign matter in the liquid to be filtered separated from the surface of the filter medium by centrifugal force from being re-diffused into the liquid. 1. A centrifugal self-cleaning filter device, comprising: a dust collecting means for filtration, wherein the cylindrical filter is used by being immersed in a liquid to be filtered. 2) The sealing member is made of a short cylindrical body made of rubber elastic material that is fitted into the bearing of the rotating shaft, and is pressed against the rotating shaft by expanding the diameter of the cylinder due to the pressure difference. 2. The centrifugal self-cleaning filter device according to claim 1, wherein the centrifugal self-cleaning filter device is configured such that the air gap is closed by closing the air gap. 3) The dust collection means includes a cylindrical dust collection case provided surrounding the cylindrical filter, and a cylindrical dust collection case that is fitted onto the rotating shaft of the rotating body so as to cover the top opening of the dust collection case. A rotary lid body and a conveyor for discharging the mixed foreign matter connected to a bottom opening of the dust collection case, and the rotary lid body is configured to cause the liquid to be filtered to flow into the dust collection case. of,
The centrifugal self-cleaning filter device according to claim 1 or 2, characterized in that the centrifugal self-cleaning filter device is provided with an opening having a liquid flow guiding function.
JP60173497A 1985-08-06 1985-08-06 Centrifugal self-cleaning filter apparatus Granted JPS6233511A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60173497A JPS6233511A (en) 1985-08-06 1985-08-06 Centrifugal self-cleaning filter apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60173497A JPS6233511A (en) 1985-08-06 1985-08-06 Centrifugal self-cleaning filter apparatus

Publications (2)

Publication Number Publication Date
JPS6233511A true JPS6233511A (en) 1987-02-13
JPH0582242B2 JPH0582242B2 (en) 1993-11-18

Family

ID=15961609

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60173497A Granted JPS6233511A (en) 1985-08-06 1985-08-06 Centrifugal self-cleaning filter apparatus

Country Status (1)

Country Link
JP (1) JPS6233511A (en)

Also Published As

Publication number Publication date
JPH0582242B2 (en) 1993-11-18

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