JPH11276819A - Filter - Google Patents

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Publication number
JPH11276819A
JPH11276819A JP10081452A JP8145298A JPH11276819A JP H11276819 A JPH11276819 A JP H11276819A JP 10081452 A JP10081452 A JP 10081452A JP 8145298 A JP8145298 A JP 8145298A JP H11276819 A JPH11276819 A JP H11276819A
Authority
JP
Japan
Prior art keywords
filtration
precoat layer
tank
filtrate
precoat
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.)
Withdrawn
Application number
JP10081452A
Other languages
Japanese (ja)
Inventor
Hiroyuki Takeuchi
宏幸 竹内
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.)
FSK Corp
Original Assignee
FSK Corp
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 FSK Corp filed Critical FSK Corp
Priority to JP10081452A priority Critical patent/JPH11276819A/en
Publication of JPH11276819A publication Critical patent/JPH11276819A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To make the thickness of a precoat layer forming a filter column as uniform as possible and to reuse the precoating agent simply. SOLUTION: In a filter in which a filter column 2 which is formed from a casing of mesh structure and in which a precoat layer 21 comprising diatomaceous earth or the like is formed in advance is suspended/fitted from/to a partition wall 13 which partitions a cylindrical filter tank 1 into an upper part chamber 11 and a lower part chamber 12, the lower part of the tank 1 is formed to be a conical part 3 in which the inside diameter decreases downward, a filtrate supply pipe 4 is introduced from the side of the tank 1 to the inside, and the supply port 41 of the pipe 4 is opened toward the center of a tank formed in the conical part 3.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、研削液、切削液な
どを精密ろ過するために用いられるプレコート式ろ過カ
ラムを備えたろ過装置に関するものであって、特に、均
一なプレコート層が形成できるろ過装置の改良された構
造に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtration device provided with a precoat type filtration column used for precision filtration of a grinding fluid, a cutting fluid, etc., and more particularly to a filtration device capable of forming a uniform precoat layer. It relates to an improved structure of the device.

【0002】[0002]

【従来の技術】従来、研削液、切削液などを精密ろ過す
るためのろ過装置としては、例えば、図2に例示するよ
うに、円筒状のろ過槽1を上部室11と下部室12に仕
切る隔壁13に網目構造のケーシングからなるろ過カラ
ム2を垂下させて取り付け、そのろ過カラム2の表面に
は、ケイソウ土などを堆積させたプレコート層21を形
成して、ろ液を外側からこのプレコート層21を透過さ
せて、固形分を取り除く方式にろ過装置が用いられてい
る。
2. Description of the Related Art Conventionally, as a filtering device for finely filtering a grinding fluid, a cutting fluid, etc., for example, as shown in FIG. 2, a cylindrical filtration tank 1 is partitioned into an upper chamber 11 and a lower chamber 12. A filtration column 2 made of a mesh-shaped casing is attached to the partition wall 13 in a hanging manner, and a precoat layer 21 on which diatomaceous earth or the like is deposited is formed on the surface of the filtration column 2, and the filtrate is applied to the precoat layer from the outside. A filtration device is used in a system that removes solids by passing through the filter 21.

【0003】この方式のろ過装置の場合、前記ろ過カラ
ム2の外表面に均一なプレコート層21を形成すること
が高いろ過能力を維持する点から重要な事項となってい
る。そこで、プレコート層21を形成する操作について
図2によって説明すると、ろ過槽1の側壁に設けた供給
口14からプレコート剤を混合したろ液を下部室12に
送り込み、ろ液を上部室11へと透過させる際に、プレ
コート剤がろ過カラム2のケーシング表面に堆積するこ
とにより、プレコート層21が形成されるのである。
In the case of this type of filtration device, forming a uniform precoat layer 21 on the outer surface of the filtration column 2 is an important matter from the viewpoint of maintaining high filtration performance. Then, the operation of forming the precoat layer 21 will be described with reference to FIG. 2. The filtrate mixed with the precoat agent is sent to the lower chamber 12 from the supply port 14 provided on the side wall of the filtration tank 1, and the filtrate is transferred to the upper chamber 11. At the time of permeation, the precoat agent is deposited on the casing surface of the filtration column 2 to form the precoat layer 21.

【0004】このようにプレコート層21が形成される
ので、プレコート剤の供給口14に近い部分のプレコー
ト層が反対側に較べて厚さが厚く形成され、部分的に厚
さが不均一な状態になるという現象が見られた。このよ
うな不均一なプレコート層21では、薄い部分では微細
粒子を捕捉する機能が厚い部分より低いので、全体とし
てろ過精度が低下することになる。また、ろ過精度を高
めるため、プレコート剤を多量に供給してプレコート層
全体の厚さを大きくすると、ろ過抵抗が増大し、ろ過能
力が低下するという問題もあった。
[0004] Since the precoat layer 21 is formed in this manner, the precoat layer near the supply port 14 for the precoat agent is formed thicker than the opposite side, and the thickness is partially uneven. Phenomenon was seen. In such a non-uniform precoat layer 21, since the function of capturing fine particles is lower in a thin portion than in a thick portion, the filtration accuracy is reduced as a whole. In addition, when a large amount of a precoat agent is supplied to increase the thickness of the entire precoat layer in order to increase the filtration accuracy, there is a problem that the filtration resistance increases and the filtration ability decreases.

【0005】また、前記ろ過装置では、ろ過操作が進行
して、プレコート層上に捕捉固形分が多量に堆積して目
詰まりをおこすと、ろ過抵抗が異常に増大しろ過効率が
低下するため、このような堆積物を除去する操作を行
う。すなわち、ろ液の加圧を停止し、あるいはさらに逆
圧を加えるなどして、プレコート層を捕捉固形分ととも
に、ろ過カラムから脱落させる。その後、改めて前記し
た方法により新たなプレコート層を形成すればよい。
In the above-mentioned filtration device, if the filtration operation proceeds and a large amount of captured solids accumulates on the precoat layer to cause clogging, the filtration resistance increases abnormally and the filtration efficiency decreases. An operation for removing such deposits is performed. That is, the precoat layer is dropped from the filtration column together with the captured solids by stopping the pressurization of the filtrate or further applying a reverse pressure. Thereafter, a new precoat layer may be formed again by the above-described method.

【0006】この場合、前記の脱落させたプレコート剤
を再利用するには、ろ過槽1の下部室12下端の排出口
からプレコート剤を抜き出して、一旦、貯留してから改
めて、供給口14からろ液とともに供給して付着させる
という前記の方法を行う必要があった。
In this case, in order to reuse the dropped pre-coating agent, the pre-coating agent is withdrawn from the outlet at the lower end of the lower chamber 12 of the filtration tank 1, temporarily stored, and then renewed from the supply port 14. It was necessary to perform the above-mentioned method of supplying and attaching together with the filtrate.

【0007】[0007]

【発明が解決しようとする課題】本発明は、上記の問題
点を解決するためになされたものであり、ろ過カラムの
形成されるプレコート層の厚さを可及的に均一化できる
ろ過装置を提供する。さらに、ろ過操作中にプレコート
層を一旦、解体し、改めて再利用する際に、そのプレコ
ート剤をろ過槽から抜き出す必要がなく、簡単に再利用
することができるろ過装置を提供するものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a filtration apparatus capable of making the thickness of a precoat layer formed on a filtration column as uniform as possible. provide. Further, the present invention provides a filtration device which can be easily reused without the necessity of extracting the precoat agent from the filtration tank when the precoat layer is once disassembled and reused again during the filtration operation.

【0008】[0008]

【課題を解決するための手段】上記の問題を解決するた
めになされた本発明のろ過装置は、円筒形状のろ過槽内
に、プレコート層が形成され得るろ過カラムを配設した
ろ過装置であって、前記ろ過槽の下部を下方に縮径する
円錐形部分とし、ろ液供給管を前記ろ過槽内に導入し
て、その供給口を上方から前記円錐形部分のほぼ中心に
向けて開口させたことを特徴とするものである。さら
に、本発明が、前記円錐形部分の上方に向かう開き角度
が60〜90度である形態のろ過装置として好ましく具
体化することができる。
SUMMARY OF THE INVENTION The present invention has been made in order to solve the above-mentioned problems. The present invention provides a filtration apparatus in which a filtration column on which a precoat layer can be formed is disposed in a cylindrical filtration tank. The lower part of the filtration tank is a conical portion that is reduced in diameter downward, a filtrate supply pipe is introduced into the filtration tank, and the supply port is opened from above toward substantially the center of the conical part. It is characterized by having. Further, the present invention can be preferably embodied as a filtration device having an opening angle of 60 to 90 degrees toward the upper side of the conical portion.

【0009】[0009]

【発明の実施の形態】次に、本発明のろ過装置に係る実
施形態を図1を参照して説明する。図1において、本発
明のろ過装置は、円筒形状のろ過槽1内に、プレコート
層が形成され得るろ過カラム2を配設したろ過装置であ
って、具体的には、前記ろ過槽1を上部室11と下部室
12に仕切る隔壁13に網目構造のケーシングからなる
ろ過カラム2を垂下させて取り付けてある。この事例で
は、ろ過カラムの数は2本であるが、その所要数は目的
とするろ過能力などに応じて適宜選択される得るもので
ある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, an embodiment according to the present invention will be described with reference to FIG. In FIG. 1, the filtration device of the present invention is a filtration device in which a filtration column 2 on which a precoat layer can be formed is disposed in a cylindrical filtration tank 1. A filtration column 2 composed of a mesh-structured casing is attached to a partition 13 that partitions the chamber 11 and the lower chamber 12 from the casing 13. In this case, the number of filtration columns is two, but the required number can be appropriately selected according to the intended filtration capacity and the like.

【0010】そして、このろ過カラム2の表面には、予
めケイソウ土などからなるプレコート層21を形成して
おき、ろ液を外側からこのプレコート層21を透過させ
て、ろ過操作が行われる。このような構造においては、
従来のものと特に変わるところはない。
A precoat layer 21 made of diatomaceous earth or the like is formed on the surface of the filtration column 2 in advance, and a filtration operation is performed by allowing the filtrate to pass through the precoat layer 21 from the outside. In such a structure,
There is no particular difference from the conventional one.

【0011】本発明の特徴とするところは、前記ろ過槽
1の下部は、下方に向かって内径が縮小する円錐形部分
3に形成され、かつ、ろ液供給管4は、前記ろ過槽1の
側面から槽内部に導入したうえ、その供給口41を上方
から前記円錐形部分3のほぼ中心に向けて開口させた点
にある。
A feature of the present invention is that a lower portion of the filtration tank 1 is formed in a conical portion 3 whose inner diameter decreases downward, and a filtrate supply pipe 4 is provided in the filtration tank 1. The point is that the supply port 41 is introduced into the tank from the side, and the supply port 41 is opened from above toward substantially the center of the conical portion 3.

【0012】次に、このろ過装置により運転操作につい
て説明すると、先ず最初にプレコートを行うには、予め
ろ液を貯留しておく混合タンク7に所定量のプレコート
剤(主にけいそう土粉末を用いる)を投入し、ポンプ6
を作動させて、プレコート剤をろ液とともにろ液供給管
4を経由してろ過槽1に供給する。
Next, the operation of this filtration apparatus will be described. First, in order to perform pre-coating, a predetermined amount of pre-coating agent (mainly diatomaceous earth powder) is placed in a mixing tank 7 in which a filtrate is stored in advance. Use) and pump 6
Is operated to supply the precoat agent to the filtration tank 1 via the filtrate supply pipe 4 together with the filtrate.

【0013】ここで、この混合ろ液は、下部室12から
ろ過カラム2を通って上部室11に至り、上部排出口1
4から3方バルブ61を経て、混合タンク7へ還流する
ことになり、その際にプレコート剤がろ過カラム2の外
表面に堆積するのであるが、この場合、所定厚さのプレ
コート層21が形成されるまで混合ろ液を循環させれば
よい。
Here, the mixed filtrate flows from the lower chamber 12 through the filtration column 2 to the upper chamber 11, and the upper outlet 1
The mixture is refluxed from the four-way valve 61 to the mixing tank 7 through the three-way valve 61. At this time, the precoat agent is deposited on the outer surface of the filtration column 2. In this case, the precoat layer 21 having a predetermined thickness is formed. The mixed filtrate may be circulated until the mixture is discharged.

【0014】この場合、プレコート剤混合ろ液は、ろ液
供給管4の供給口41から前記ろ過槽1下部の円錐形部
分3のほぼ中心に向けて吐出されることになり、その水
流は周囲に向かって均等に広がり、かつ巻き上げられ
て、攪拌状態で上部のろ過カラム2の部分に到達するの
で、各ろ過カラム2のプレコート層21がむらなく形成
されるという利点が得られるのである。なお、ろ過カラ
ム2としては、所定の目開きの金網からなる円筒ケーシ
ングあるいは、不織布のようなろ過材を円筒状に成形し
た通常のろ過カラムが応用され得る。
In this case, the filtrate containing the precoating agent is discharged from the supply port 41 of the filtrate supply pipe 4 toward substantially the center of the conical portion 3 at the lower portion of the filtration tank 1, and its water flow is reduced. , And are wound up and reach the upper filtration column 2 under stirring, so that the advantage that the precoat layer 21 of each filtration column 2 is formed evenly is obtained. In addition, as the filtration column 2, a cylindrical casing made of a wire mesh having a predetermined mesh or a normal filtration column in which a filtering material such as a nonwoven fabric is formed into a cylindrical shape can be applied.

【0015】次いで、ろ過操作を行うには、3方バルブ
61を切り換えて、ろ過液をろ過液タンク8に送り込む
ようにするとともに、混合タンク7からのろ液を供給を
継続すればよい。このろ過運転が進行して、目詰まりな
どが生じたときには、次の操作により、その目詰まりを
解消してから、改めてプレコート層を形成して、運転を
再開することになる。
Next, in order to carry out the filtration operation, the three-way valve 61 is switched so that the filtrate is sent to the filtrate tank 8 and the supply of the filtrate from the mixing tank 7 is continued. When the filtration operation proceeds and clogging or the like occurs, the clogging is eliminated by the following operation, a precoat layer is formed again, and the operation is restarted.

【0016】先ず、ポンプ6の運転を停止して、ろ過カ
ラムに対するろ過圧力を解除し、プレコート層21をそ
の自重で解体、落下させる。また、必要に応じて、ろ過
カラム2の内側から圧力をかけるなどの逆圧により、プ
レコート層21を剥離させることもできる。かくして、
プレコート層は崩壊した状態で円錐形部分3の底部に滞
留することになる。
First, the operation of the pump 6 is stopped, the filtration pressure on the filtration column is released, and the precoat layer 21 is disassembled and dropped by its own weight. Further, if necessary, the precoat layer 21 can be peeled off by a reverse pressure such as applying a pressure from the inside of the filtration column 2. Thus,
The precoat layer will stay in the collapsed state at the bottom of the conical section 3.

【0017】ここで、3方バルブ61をプレコートライ
ンA側に切り換えて、ポンプ6の運転を再開すると、ろ
液供給管4の供給口41から吐出されるろ液水流が、滞
留している前記プレコート剤に衝突して、四方に分散し
ながらこれを巻き上げて、攪拌状態で上部のろ過カラム
2の部分に到達するので、如上の最初のプレコート層の
形成操作の場合と同様に、各ろ過カラム2のプレコート
層21がむらなく形成されるから、ろ過操作を再開する
ことができる。なお、滞留するプレコート剤の汚れが著
しい場合は、再使用できないので、円錐形部分3の底部
の排出バルブ5を開いて、ろ液とともに外部に抜き出し
て廃棄することになる。
Here, when the three-way valve 61 is switched to the precoat line A side and the operation of the pump 6 is resumed, the filtrate water flow discharged from the supply port 41 of the filtrate supply pipe 4 is retained. As it collides with the precoat agent and is wound up while being dispersed in all directions, and reaches the upper filtration column 2 in a stirring state, each filtration column is formed in the same manner as in the first precoat layer forming operation. Since the second precoat layer 21 is formed evenly, the filtration operation can be restarted. When the remaining precoat agent is extremely dirty, it cannot be reused. Therefore, the discharge valve 5 at the bottom of the conical portion 3 is opened, and the precoat agent is taken out together with the filtrate and discarded.

【0018】このように、本発明によれば、最初にプレ
コート層を形成する場合でも、また目詰まり対策後のプ
レコート層の形成においても、各ろ過カラムによる厚さ
むらが著しく改善されるので、ろ過精度が大幅に向上す
る、例えば、従来のケースでは粒径1μmの粒子の除去
率が90%程度であった場合に、これを100%にまで
向上することができることが分かった。
As described above, according to the present invention, even when the precoat layer is formed first, and also in the formation of the precoat layer after measures against clogging, the thickness unevenness of each filtration column is significantly improved. It has been found that the filtration accuracy can be greatly improved, for example, when the removal rate of particles having a particle diameter of 1 μm is about 90% in the conventional case, this can be improved to 100%.

【0019】なお、本発明では、前記円錐形部分の上方
に向かう開き角度が60〜90度である形態のろ過装置
として具体化するのが好適である。この開き角度が90
度を超えると、供給口41から吐出され上昇するろ液水
流によるプレコート剤の巻き込み作用が不十分となる。
また60度より小さい場合は、前記円錐形部分の上下長
さが大きくなり過ぎ好ましくない。
In the present invention, it is preferable to embody the filtering device in a form in which the opening angle of the conical portion upward is 60 to 90 degrees. This opening angle is 90
Exceeding the degree, the effect of entrainment of the precoat agent by the rising filtrate water flow discharged from the supply port 41 becomes insufficient.
If the angle is smaller than 60 degrees, the vertical length of the conical portion becomes too large, which is not preferable.

【0020】[0020]

【発明の効果】本発明のろ過装置は、以上に説明したよ
うに構成されているので、ろ過カラム上のプレコート層
の形成に際して、その厚さを均一化でき、結果、ろ過精
度を大幅に向上させることができた。また、ろ過操作中
にプレコート層を解体し、改めて再利用する際に、その
プレコート剤をろ過槽から抜き出す必要がなく、簡単に
再利用することができるから、ろ過装置の運転操作性が
改善されるという優れた効果がある。よって本発明は従
来の問題点を解消したろ過装置として、その工業的価値
は極めて大なるものがある。
As described above, the filtration device of the present invention is configured as described above, so that the thickness of the precoat layer on the filtration column can be made uniform when formed, and as a result, the filtration accuracy is greatly improved. I was able to. In addition, when the precoat layer is disassembled during the filtration operation and reused again, the precoat agent does not need to be extracted from the filtration tank and can be easily reused, so that the operability of the filtration device is improved. Has an excellent effect. Therefore, the present invention has a very large industrial value as a filtration device which has solved the conventional problems.

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

【図1】本発明のろ過装置を説明するための断面概念
図。
FIG. 1 is a conceptual cross-sectional view for explaining a filtration device of the present invention.

【図2】従来のろ過装置の要部断面略図。FIG. 2 is a schematic cross-sectional view of a main part of a conventional filtration device.

【符号の説明】[Explanation of symbols]

1 ろ過槽、11 上部室、12 下部室、13 隔
壁、2 ろ過カラム、21プレコート層、3 円錐形部
分、4 ろ液供給管、41 供給口。
DESCRIPTION OF SYMBOLS 1 Filtration tank, 11 upper chamber, 12 lower chamber, 13 partition, 2 filtration column, 21 precoat layer, 3 conical part, 4 filtrate supply pipe, 41 supply port.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】円筒形状のろ過槽内に、プレコート層が形
成され得るろ過カラムを配設したろ過装置であって、前
記ろ過槽の下部を下方に縮径する円錐形部分とし、ろ液
供給管を前記ろ過槽内に導入して、その供給口を上方か
ら前記円錐形部分のほぼ中心に向けて開口させたことを
特徴とするろ過装置。
1. A filter device comprising a cylindrical filtration tank provided with a filtration column on which a precoat layer can be formed, wherein a lower portion of the filtration tank is formed as a conical portion having a diameter reduced downward, and a filtrate is supplied. A filter device, wherein a pipe is introduced into the filtration tank, and a supply port thereof is opened from above toward substantially the center of the conical portion.
【請求項2】前記円錐形部分の上方に向かう開き角度が
60〜90度である請求項1に記載のろ過装置。
2. The filtering device according to claim 1, wherein an upward opening angle of the conical portion is 60 to 90 degrees.
JP10081452A 1998-03-27 1998-03-27 Filter Withdrawn JPH11276819A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10081452A JPH11276819A (en) 1998-03-27 1998-03-27 Filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10081452A JPH11276819A (en) 1998-03-27 1998-03-27 Filter

Publications (1)

Publication Number Publication Date
JPH11276819A true JPH11276819A (en) 1999-10-12

Family

ID=13746807

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10081452A Withdrawn JPH11276819A (en) 1998-03-27 1998-03-27 Filter

Country Status (1)

Country Link
JP (1) JPH11276819A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009207983A (en) * 2008-03-04 2009-09-17 Metawater Co Ltd Method for recovering phosphorus extract and apparatus for recovering phosphorus extract

Cited By (1)

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JP2009207983A (en) * 2008-03-04 2009-09-17 Metawater Co Ltd Method for recovering phosphorus extract and apparatus for recovering phosphorus extract

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