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JPS581609B2 - precision filter - Google Patents
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JPS581609B2 - precision filter - Google Patents

precision filter

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Publication number
JPS581609B2
JPS581609B2 JP52114830A JP11483077A JPS581609B2 JP S581609 B2 JPS581609 B2 JP S581609B2 JP 52114830 A JP52114830 A JP 52114830A JP 11483077 A JP11483077 A JP 11483077A JP S581609 B2 JPS581609 B2 JP S581609B2
Authority
JP
Japan
Prior art keywords
filter medium
perforated plate
filter
perforated
support surface
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP52114830A
Other languages
Japanese (ja)
Other versions
JPS5448382A (en
Inventor
鈴木精一
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.)
KYORITSU ENJINIARINGU KK
Original Assignee
KYORITSU ENJINIARINGU 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 KYORITSU ENJINIARINGU KK filed Critical KYORITSU ENJINIARINGU KK
Priority to JP52114830A priority Critical patent/JPS581609B2/en
Publication of JPS5448382A publication Critical patent/JPS5448382A/en
Publication of JPS581609B2 publication Critical patent/JPS581609B2/en
Expired legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 本発明は、液体や気体などの流体のための精密濾過器に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a microfilter for fluids such as liquids and gases.

金属製網を濾材として用いた清澄濾過器において、その
濾過精度の向上を図ろうとすれば、必然的にメッシュは
微細化してゆく。
In a clarifying filter using a metal mesh as a filter medium, if the filtration accuracy is to be improved, the mesh will inevitably become finer.

しかしながら、金網や濾過器の構造上、次のような解決
困難な相殺する条件としての問題点(1)〜(4)など
が派生して、メッシュの微細化したがって濾過性能の向
上に限界が生じてくる。
However, due to the structure of the wire mesh and filter, the following problems (1) to (4) arise as counterbalancing conditions that are difficult to solve, and there is a limit to the refinement of the mesh and therefore the improvement of filtration performance. It's coming.

(1)金網を微細化しようとする程(たとえば100ミ
クロンから数ミクロ冫へと高性能化する程)、濾過原液
の流れに対する抵抗は、大きくなる。
(1) The finer the wire mesh is made (for example, the higher the performance is from 100 microns to several microns), the greater the resistance to the flow of the filtration stock solution becomes.

したがって金網に与えられる圧力は上昇し、反面金網は
細線化して耐圧力は減少する。
Therefore, the pressure applied to the wire mesh increases, but on the other hand, the wire mesh becomes thinner and its pressure resistance decreases.

(2)金網を補強するためには、平滑面に透孔を穿設し
た補強板の上へ金網を重ねる方式が、単純には考えられ
る。
(2) In order to reinforce the wire mesh, a simple method that can be considered is to stack the wire mesh on top of a reinforcing plate with through holes drilled in its smooth surface.

しかしながら、この場合には金網が平滑面に密着して閉
塞され、有効濾過面積が減少してしまう。
However, in this case, the wire mesh comes in close contact with the smooth surface and is occluded, reducing the effective filtration area.

そこで、同一面積をとろうとすれば、大型化は避けられ
ない。
Therefore, if you try to have the same area, it is inevitable that you will increase the size.

(3)金網の端面の取扱い方、その組立て、分解、操作
中の濾液の漏れ防止などが難しく繁雑となる。
(3) It becomes difficult and complicated to handle the end face of the wire mesh, assemble it, disassemble it, and prevent leakage of filtrate during operation.

(4)濾過工程を実現する構成と、活性炭の吸着作用に
よる脱臭などのような粉体による処理プロセスを実現す
る構成とがそれぞれ単体で組合わされる場合、構成全体
が一層大型・複雑化してくる。
(4) When a configuration that implements a filtration process and a configuration that implements a treatment process using powder, such as deodorization through the adsorption effect of activated carbon, are combined individually, the entire configuration becomes even larger and more complex. .

本発明は、このような従来からの問題点に鑑みてなされ
たものであって、濾過性能の向上された精密濾過器を提
供することを主目的とする。
The present invention has been made in view of these conventional problems, and its main purpose is to provide a precision filter with improved filtration performance.

第1図は本発明の一実施例の断面図であり、第2図は第
1図に示される切断面線■−■からみた一部の断面図で
ある。
FIG. 1 is a cross-sectional view of one embodiment of the present invention, and FIG. 2 is a partial cross-sectional view taken along the section line (■--■) shown in FIG.

本件精密濾過器Fは、例えば200気圧以上で圧送され
る濾過原液を精密濾過するために用いられるものであり
、第1図の上方から下方へ、円形平板状多孔板1と、複
数枚の濾網2と、もう一つの円形平板状多孔板3とがこ
の順序で重積され、サンドイツチ状に構成される。
The precision filter F is used for precision filtering a filtration stock solution that is pumped under pressure of, for example, 200 atmospheres or more, and from the top to the bottom of FIG. The net 2 and another circular flat perforated plate 3 are stacked in this order to form a sandwich-like structure.

これらの部材1,2.3はすべてステンレス鋼製である
These members 1, 2.3 are all made of stainless steel.

濾過されるべき原液は矢符4のように圧送され、濾液は
多孔板1を経て第1図の上方へ流出する。
The stock solution to be filtered is pumped as indicated by the arrow 4, and the filtrate flows out through the perforated plate 1 upward in FIG.

この精密濾過器を逆洗洗浄するためには、第1図の上方
から下方に向けて矢符4とは逆方向に洗浄水を圧送する
In order to backwash the microfilter, wash water is pumped from the top to the bottom in the direction opposite to the arrow 4 in FIG.

多孔板1は高圧力で圧送される原水によって圧力を受け
る濾網2を平板状のままで支持して変形を防ぎうるに充
分な強度を有し、また多孔板3は逆洗洗浄時に高圧力で
圧送される洗浄水によって濾網2の変形を防ぐに充分な
強度を有する。
The perforated plate 1 has sufficient strength to support the filter net 2 which is pressurized by the raw water pumped under high pressure in a flat plate shape and prevent deformation. It has sufficient strength to prevent the filter net 2 from being deformed by the washing water pumped by the filter.

濾網2の網目の開きは微細であり、例えば50ミクロン
未満であってもよく、さらに0,1ミクロンから10ミ
クロン程度の孔径であってもよい。
The opening of the mesh of the filter net 2 may be fine, for example, less than 50 microns, and the pore size may be about 0.1 micron to 10 microns.

複数枚の濾網2の積層は各濾網2の織組織の方向が相互
に交差するように行なわれ、それによって網目または気
孔径が全面にわたって均一化される。
The plurality of filter nets 2 are stacked so that the weave directions of the filter nets 2 intersect with each other, thereby making the mesh or pore diameter uniform over the entire surface.

濾網2の積層枚数は濾過性能に応じて選ばれる。The number of laminated filter nets 2 is selected depending on the filtering performance.

多孔板1はその中央がくぼんで形成され、このくぼんだ
部分に濾網2および多孔板1よりも示径の多孔板3が収
められる。
The perforated plate 1 is formed with a recess at its center, and the filter net 2 and the perforated plate 3 having a diameter smaller than that of the perforated plate 1 are housed in this recessed part.

多孔板1の濾網2に対向する面は、その濾網2を支持す
る支持面5と、濾網2を多孔板3とともに固定する固定
面6とから成り、本件精密濾過器は後述の第6図および
第7図示の如κ使甲されてシールまたは多段化されるた
めの環状の外周部24を備える。
The surface of the perforated plate 1 facing the filter screen 2 consists of a support surface 5 that supports the filter screen 2, and a fixing surface 6 that fixes the filter screen 2 together with the perforated plate 3. As shown in FIGS. 6 and 7, it is provided with an annular outer circumferential portion 24 for sealing or multi-stage use.

濾網支持面5は、もう一つの多孔板3に形成される濾網
支持面11との間で濾過作用を行なうべき濾網2の部分
を変形させることなく支持し、そのために濾網2を収め
うるように凹状に形成され、また円周方向に同心の溝8
および放射状に延びる溝9が刻設される。
The filter net support surface 5 supports the portion of the filter net 2 that is to perform the filtration action between it and the filter net support surface 11 formed on another porous plate 3 without deforming it, and for this purpose, the filter net 2 is It is formed in a concave shape so that it can be accommodated, and also has a concentric groove 8 in the circumferential direction.
and radially extending grooves 9 are carved.

これ等の溝8,9の交差位置には円周方向および半径方
向に1つおきに多孔板1の厚さ方向に貫通する流体通過
孔10が穿設される。
At the intersections of these grooves 8 and 9, fluid passage holes 10 that penetrate in the thickness direction of the perforated plate 1 are bored every other in the circumferential direction and the radial direction.

これ等の溝8,9は比較的多数設けられ、それによって
多孔板1の支持面5と濾網2との接触面積は小さい。
A relatively large number of these grooves 8 and 9 are provided, so that the contact area between the support surface 5 of the perforated plate 1 and the filter screen 2 is small.

したがって濾網2の濾過面は閉塞されることはなく、有
効濾過面積が減少したり、圧力損失が不所望に大きくな
る恐れがない。
Therefore, the filtration surface of the filter net 2 is not blocked, and there is no possibility that the effective filtration area will be reduced or the pressure loss will be undesirably large.

しかして、支持面5は、矢符4の方向に流れる原液によ
って濾液が濾網2を通過する全面にわたって均一に支持
する働きをするとともに、濾網2を通過した濾液を多孔
板1め支持面5へ均−に集液するように働く。
Thus, the support surface 5 functions to uniformly support the entire surface of the filtrate passing through the filter screen 2 by the stock solution flowing in the direction of the arrow 4, and also serves to support the filtrate that has passed through the filter screen 2 to the perforated plate 1. It works to collect liquid evenly into 5.

多孔板1の固定面6,12には支持面5を外囲する2重
の環状の突起17.18が多孔板1の半径方向に間隔を
あけて設けられる。
Double annular projections 17 and 18 surrounding the support surface 5 are provided on the fixed surfaces 6 and 12 of the perforated plate 1 at intervals in the radial direction of the perforated plate 1.

突起17.18の幅は頂部になるにつれて先細状になっ
ている。
The width of the projections 17,18 tapers towards the top.

多孔板3は、多孔板1と同様に支持面11と固定面12
とを有し、支持面11には多数の環状溝13と多数の放
射状溝14とが形成され流体通過孔15がそれらの溝1
3.14の交差位置に設けられる。
Like the perforated plate 1, the perforated plate 3 has a support surface 11 and a fixed surface 12.
A large number of annular grooves 13 and a large number of radial grooves 14 are formed in the support surface 11, and the fluid passage holes 15 are formed in the grooves 1.
3.14 at the intersection.

多孔板3の固定面12には、突起17,18に対応して
2重の環状突起19.20が設けられる。
The fixed surface 12 of the perforated plate 3 is provided with double annular projections 19 and 20 corresponding to the projections 17 and 18.

第3図aは第2図の突起17.19の付近の拡大断面図
である。
FIG. 3a is an enlarged sectional view of the vicinity of projection 17.19 of FIG. 2.

第3図bは突起17.19によって濾網2に作用する圧
力分布を示す。
FIG. 3b shows the pressure distribution acting on the filter screen 2 by the projections 17,19.

第3図bの横軸は、多孔板1,3の半径方向を示し、縦
軸は濾網2に作用する圧力の大きさを示す。
The horizontal axis in FIG. 3b indicates the radial direction of the perforated plates 1 and 3, and the vertical axis indicates the magnitude of the pressure acting on the filter screen 2.

濾網2に作用する圧力分布は、突起17.19による濾
網2の圧縮幅すなわち多孔板1,3の半径方向の幅にわ
たって鋭い接面圧力分布を生じている。
The pressure distribution acting on the filter screen 2 produces a sharp contact pressure distribution over the compression width of the filter screen 2 by the protrusions 17.19, that is, the radial width of the perforated plates 1, 3.

このような鋭い圧力分布によって濾網2が王縮されるこ
とにより、その圧縮部分において支持面5,11から第
1図の左右方向に洩れる液体の流過が有効に防がれる。
Since the filter net 2 is compressed by such a sharp pressure distribution, liquid leaking from the support surfaces 5, 11 in the left and right directions in FIG. 1 at the compressed portions is effectively prevented.

多孔板1,3に穿設された流体通過孔10,15は、溝
8,9;13,14の幅よりも大きく形成され、それに
よって液体の果液および配液が円滑に行なわれる。
The fluid passage holes 10, 15 formed in the perforated plates 1, 3 are formed to be larger than the width of the grooves 8, 9; 13, 14, so that the liquid can be smoothly distributed.

流体通過孔10.15による液体の通過許容量は濾網2
の有効濾過面積の流量に比べて等しいかまたはより大き
くされ、それによって濾液の不所望な圧力損失が生じな
いようにされる。
The amount of liquid allowed to pass through the fluid passage hole 10.15 is the filter net 2.
is equal to or greater than the flow rate of the effective filtration area, thereby avoiding undesirable pressure losses of the filtrate.

再び第1図を参照して、多孔板1の突起18に連なる多
孔板1の軸線方向の内壁21と、この内壁21に対抗す
る多孔板3の外壁22との間の部分23には、濾網2の
周縁が挾圧され、多孔板1,3の突起17,18;19
,20に鋭い圧力分布が生じるように濾網2が圧縮され
たままでこの部分23において液密に溶接される。
Referring again to FIG. 1, a filter is provided in a portion 23 between an inner wall 21 of the perforated plate 1 in the axial direction that is connected to the protrusion 18 of the perforated plate 1 and an outer wall 22 of the perforated plate 3 that opposes this inner wall 21. The periphery of the net 2 is pinched, and the protrusions 17, 18; 19 of the perforated plates 1, 3
, 20, the filter screen 2 remains compressed and welded in a fluid-tight manner in this section 23.

この溶接によって支持面5,11に挾まれた濾網2の部
分から固定面6,12を経る外方への液体の洩れが完全
に防がれる。
This welding completely prevents liquid from leaking outward through the fixing surfaces 6, 12 from the portion of the filter screen 2 sandwiched between the supporting surfaces 5, 11.

多孔板1の環状の外周部24の上下両面は、切削・研磨
等によって平行かつ均一な平坦に仕上げてシールまたは
多段化のための便宜が図られる。
The upper and lower surfaces of the annular outer circumferential portion 24 of the perforated plate 1 are finished to be parallel and uniformly flat by cutting, polishing, etc. to facilitate sealing or multi-tiering.

外周部24は流体通過孔10.15の穿設された外面2
5.26よりも隆起して形成され、したがって後述の多
段化の場合において、液体を配液するように働く。
The outer periphery 24 has an outer surface 2 formed with fluid passage holes 10.15.
5.26, and therefore serves to distribute liquid in the case of multi-stage formation, which will be described later.

上述のように外周部24が平滑面に形成されることによ
って、本件濾過器が例えば多段化された場合において、
パッキン材が不要になるという優れた利点がある。
When the outer circumferential portion 24 is formed to have a smooth surface as described above, for example, when the present filter is multi-staged,
This has the great advantage of eliminating the need for packing material.

第4図は本発明の他の実施例の断面図である。FIG. 4 is a sectional view of another embodiment of the invention.

この実施例では同一形状の多孔板1a,3aを大きな力
で締付けるために多孔板1a,3aおよび濾網2aを共
通に貫通するボルト穴28が穿設されて三者1a,2a
,3aが一体的にねじ止めされる。
In this embodiment, in order to tighten the perforated plates 1a and 3a of the same shape with a large force, bolt holes 28 are drilled to commonly pass through the perforated plates 1a and 3a and the filter screen 2a.
, 3a are integrally screwed together.

これ等の部材1a,2a,3aの外周部分19aにおい
て三者が一体的に液密に溶接される,ボルト穴28を挿
通するボルト(図示せず)は第3図示の多孔板1a,3
aを相互に近接方向に締結してナットに螺合する。
These members 1a, 2a, 3a are integrally liquid-tightly welded at the outer circumferential portion 19a of the members 1a, 2a, 3a, and bolts (not shown) inserted through the bolt holes 28 are connected to the perforated plates 1a, 3 shown in the third figure.
A are fastened in a direction close to each other and screwed into a nut.

このボルトとナットとの組合せに代ってリベットであっ
てもよく、または第3図示の濾過器を多段に組合せて一
体的にする場合における多段濾過器を一体に締結する連
結ボルトであってもよい。
Rivets may be used in place of this combination of bolts and nuts, or connecting bolts may be used to fasten the multi-stage filters together in the case where the filters shown in the third figure are combined into one unit. good.

第5図は本発明のさらに他の実施例を示す。FIG. 5 shows yet another embodiment of the invention.

この実施例では前述のシールを行なうための突起17,
18;19,20にかわって、環状突起29、およびこ
の突起29に濾網2bを介して当接する環状凹部30と
が、多孔板1bおよび3bにそれぞれ形成される。
In this embodiment, a protrusion 17 for performing the above-mentioned sealing,
18; In place of 19 and 20, an annular projection 29 and an annular recess 30 that abuts the projection 29 via the filter screen 2b are formed on the perforated plates 1b and 3b, respectively.

突起29の外周面の曲率と凹部30の内周面の曲率とは
相互に異なっており、したがって濾網2bの圧縮幅にわ
たる接面圧力分布を鋭くすることができ、それによって
洩れ止めを確実に防ぐことができる。
The curvature of the outer circumferential surface of the protrusion 29 and the curvature of the inner circumferential surface of the recess 30 are different from each other, so that the contact surface pressure distribution over the compression width of the filter screen 2b can be sharpened, thereby ensuring leakage prevention. It can be prevented.

多孔板1b,3bは溶接によって締付けられてもよく、
またボルト穴31に挿通ずるボルトによって締付けられ
てもよく、また接着剤であってもよい。
The perforated plates 1b and 3b may be fastened together by welding,
Alternatively, it may be tightened with a bolt inserted into the bolt hole 31, or may be tightened with an adhesive.

多孔板1,1a,1b,3,3a,3bの支持面8,1
4には、全面にわたってローレット加工などによって極
めて多数の小さな凹凸を形成してもよく、それによって
支持面9,11は濾網2をきわめて多数の点で支持する
ことになり、濾液の流過抵抗を一層小さくすることがで
きる。
Support surfaces 8, 1 of perforated plates 1, 1a, 1b, 3, 3a, 3b
4 may be formed with a very large number of small irregularities by knurling or the like over the entire surface, so that the support surfaces 9 and 11 support the filter screen 2 at a very large number of points, which reduces the flow resistance of the filtrate. can be made even smaller.

このようなローレット加工などによる凹凸部分の底は共
通に連通しており、また流体通過孔10.15に連通し
ている。
The bottoms of the concave and convex portions formed by knurling or the like communicate in common, and also communicate with the fluid passage holes 10.15.

前述の濾網にかわってセラミック板、焼結金属板等の多
孔質濾材であってもよく、さらには平織、綾織等の織物
または不織布から成る濾布を用いてもよく、またガラス
、合成樹脂等から成ってもよい。
Instead of the above-mentioned filter net, a porous filter medium such as a ceramic plate or a sintered metal plate may be used, and a filter cloth made of woven fabric or non-woven fabric such as plain weave or twill weave may be used. It may also consist of

第6図は第1図の濾過器Fの一使用例を示す。FIG. 6 shows an example of the use of the filter F shown in FIG.

濾過器Fは液体の流過する管路40.41に介装され、
それらの管路40,41のフランジ42,43によって
装着される。
The filter F is interposed in the pipe line 40.41 through which the liquid flows,
They are attached by flanges 42, 43 of their conduits 40, 41.

こうして、きわめて簡易に既存の管路などへ本件濾過器
10を増付けることができる。
In this way, the present filter 10 can be added to an existing pipe line or the like very easily.

第7図は本発明の他の使用例を示す。FIG. 7 shows another example of use of the invention.

この濾過装置は、濾過性能を向上するために濾過器Fが
ユニットとしてたとえば3段に重ねられ、濾過原液流入
側と濾液流出側とには取付補助具44.45が設けられ
、これら部材F,44.45がボルトなどによって一体
的に組立てられる。
In this filtration device, the filters F are stacked as a unit in three stages, for example, in order to improve the filtration performance, and mounting aids 44 and 45 are provided on the filtration stock inflow side and the filtrate outflow side, and these members F, 44 and 45 are integrally assembled using bolts or the like.

一方の取付補助具44は、中央に透孔を有する円板44
aとその透孔に連通する短筒44bとから成り、短筒4
4bの開放端外周にはねじが刻設されて取付の便が図ら
れる。
One of the mounting aids 44 is a disc 44 having a through hole in the center.
a and a short tube 44b communicating with the through hole.
A screw is engraved on the outer periphery of the open end of 4b to facilitate installation.

他方の増付補助具45も同様に構成される。The other additional auxiliary tool 45 is similarly configured.

以上のように本発明によれば、濾網等の平板状濾材を平
板状多孔板によってサンドイツチし、それ等三者の周縁
が液密的に相互に一体的に固着されるので、高精度の濾
過が行なわれるとともに濾赦の漏出が防止される。
As described above, according to the present invention, a flat filter medium such as a filter net is sandwiched by a flat perforated plate, and the peripheral edges of the three members are integrally fixed to each other in a liquid-tight manner. Filtration is performed and leakage of the filter is prevented.

また、平板状多孔板は平板状濾材を全面にわたって小さ
い接触面によって支持することになるので、濾過抵抗が
大きい場合においても濾材は変形したり損傷することな
く確実に支持され、しかも有効濾過面積を閉塞すること
はなく、液体の圧力損失を不所望に高めたりすることは
ない。
In addition, since the flat perforated plate supports the flat filter medium over the entire surface with a small contact surface, the filter medium is reliably supported without deformation or damage even when the filtration resistance is large, and the effective filtration area is It does not block or undesirably increase liquid pressure losses.

さらに本件濾過器は平板状のユニットとして形成されう
るので、多様に組合せて単体で小形にブロック化するこ
とができるなど幾多の卓越した効果が奏される。
Furthermore, since the present filter can be formed as a flat unit, it can be combined in various ways and can be made into a small block by itself, and has many excellent effects.

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

第1図は本発明の一実施例の縦断面図、第2図は第1図
の切断面線■一■からみた図であり、濾網2は省略して
ある。 第3図aは第1図および第2図の突起17.19を示す
多孔板1,3の半径方向に沿う拡大断面図であり、第3
図bは突起17,19の圧力分布を示す図である。 第4図および第5図は本発明の他の実施例の一部をそれ
ぞれ示す断面図、第6図は未発明の一実施例の精密濾過
器の一使用態様を示す正面図、第7図は多段濾過を行な
う場合の本発明の一使用例の断面図である。 1,1a,1b,3,3a,3b・・・平板状多孔板、
2,2a,2b・・・濾網、5・・・支持面、6・・・
固定面、8,9,13,14・・・溝、10.15・・
・流体通過孔、17,18,19,20,29・・・シ
ール突起、30・・・シール凹部。
FIG. 1 is a longitudinal sectional view of an embodiment of the present invention, and FIG. 2 is a view taken from the section line 1-1 in FIG. 1, with the filter screen 2 omitted. FIG. 3a is an enlarged sectional view along the radial direction of the perforated plates 1, 3 showing the protrusions 17.19 of FIGS. 1 and 2;
FIG. b is a diagram showing the pressure distribution of the protrusions 17 and 19. 4 and 5 are sectional views showing a part of other embodiments of the present invention, FIG. 6 is a front view showing one mode of use of a precision filter according to an embodiment of the invention, and FIG. 7 1 is a cross-sectional view of an example of the use of the present invention when performing multi-stage filtration. 1, 1a, 1b, 3, 3a, 3b... flat perforated plate,
2, 2a, 2b... filter net, 5... support surface, 6...
Fixed surface, 8, 9, 13, 14... Groove, 10.15...
-Fluid passage hole, 17, 18, 19, 20, 29...Seal protrusion, 30...Seal recess.

Claims (1)

【特許請求の範囲】 1 精密濾過を行なうための50ミクロン未満の気孔径
を有する平板状濾材と、 前記濾材を両側から挾んでサンドイツチして補強する一
対の平板状多孔板であって、前記各多孔板は、前記濾材
に対向する濾材支持面とその濾材支持面を外囲する固定
面とを有し、前記濾材支持面には、前記多孔板の厚さ方
向に貫通した前記気孔径よりも大きい流体通過孔が穿設
され、かつ底が共通に連通しているとともに前記流体通
過孔に連通している凹凸が前記濾材支持面の全面にわた
って形成され、前記多孔板のいずれか一方の固定面には
、幅が頂部になるにつれて先細状になっているシール突
起部が環状に形成され、前記多孔板のいずれか他方の固
定面には、前記突起部に前記濾材を介して当接しかつ前
記濾材の圧縮幅にわたって鋭い接面圧力分布を生じて漏
れ止めに有効に働く環状のシール当接部が形成された、
そのような多孔板と、 前記濾材と前記多孔板とを一体的に固定する手段とを含
むことを特徴とする精密濾過器。
[Scope of Claims] 1. A flat filter medium having a pore diameter of less than 50 microns for performing precision filtration, and a pair of flat perforated plates sandwiching the filter medium from both sides and reinforcing it by sandwiching the filter medium, comprising: The perforated plate has a filter medium support surface that faces the filter medium and a fixed surface that surrounds the filter medium support surface, and the filter medium support surface has pores that are larger than the diameter of the pores that penetrate in the thickness direction of the perforated plate. A large fluid passage hole is bored therein, the bottom thereof is in common communication, and unevenness communicating with the fluid passage hole is formed over the entire surface of the filter medium supporting surface, and the fixing surface of either one of the perforated plates A seal protrusion is formed in an annular shape, the width of which tapers toward the top, and the seal protrusion is in contact with the protrusion via the filter medium and is provided on the other fixing surface of the perforated plate. An annular seal contact area is formed that produces a sharp contact pressure distribution over the compressed width of the filter medium and effectively prevents leakage.
A precision filter comprising: such a perforated plate; and means for integrally fixing the filter medium and the perforated plate.
JP52114830A 1977-09-24 1977-09-24 precision filter Expired JPS581609B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52114830A JPS581609B2 (en) 1977-09-24 1977-09-24 precision filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52114830A JPS581609B2 (en) 1977-09-24 1977-09-24 precision filter

Publications (2)

Publication Number Publication Date
JPS5448382A JPS5448382A (en) 1979-04-16
JPS581609B2 true JPS581609B2 (en) 1983-01-12

Family

ID=14647749

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52114830A Expired JPS581609B2 (en) 1977-09-24 1977-09-24 precision filter

Country Status (1)

Country Link
JP (1) JPS581609B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0630243Y2 (en) * 1987-12-14 1994-08-17 石川島播磨重工業株式会社 filter
JP7517490B1 (en) * 2023-02-07 2024-07-17 三菱マテリアル株式会社 Wire mesh laminated porous body and porous body-containing pipe
JP7517488B1 (en) * 2023-02-07 2024-07-17 三菱マテリアル株式会社 Wire mesh laminated porous body and porous body-containing pipe

Also Published As

Publication number Publication date
JPS5448382A (en) 1979-04-16

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