JP2005169273A - Filtering device having pleat filter united with housing - Google Patents

Filtering device having pleat filter united with housing Download PDF

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JP2005169273A
JP2005169273A JP2003413082A JP2003413082A JP2005169273A JP 2005169273 A JP2005169273 A JP 2005169273A JP 2003413082 A JP2003413082 A JP 2003413082A JP 2003413082 A JP2003413082 A JP 2003413082A JP 2005169273 A JP2005169273 A JP 2005169273A
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liquid
cylindrical portion
passage
cylindrical
filtrate
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JP4503276B2 (en
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Fumio Nozaki
文雄 野崎
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Entegris Inc
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Mykrolis Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To solve the defect that a liquid to be filtered is likely to be wasted since the amount of the remaining liquid increases at the finishing stage of filtration due to a large volume of an occupied flow passage in conventional filtering devices housing pleat filters in containers, especially in a filtering device for filtering a small amount of the liquid to be filtered. <P>SOLUTION: A filtering device is provided with a cylindrical part having a cylindrical inside space with both ends opened , an annular pleat filter (a filer membrane is bent in a pleat shape and formed in a cylinder shape) inserted into the inside space in contact with the inner wall of the above cylindrical part and with the top and bottom end surfaces sealed with tight liquid, a perforated core supporting the inner peripheral surface of the pleat filter, a lower cover body and an upper cover body connected respectively to both of the ends of the cylindrical part with the tight liquid, a supply passage of the liquid to be filtered communicating with the inner surface of a housing, a supply opening of the liquid to be filtered connected to the supply passage, a discharge passage of the filtrate communicating with the inside passage of the perforated core, and a discharge opening of the filtrate connected to the discharge passage. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は液体を濾過する技術に関するもので、特に少量の液体を濾過するのに適し、被濾過液を効率よく濾過するためのハウジング一体型のプリーツフィルタを使用した濾過装置に関する。   The present invention relates to a technique for filtering a liquid, and more particularly to a filtration apparatus using a pleated filter integrated with a housing, which is suitable for filtering a small amount of liquid and efficiently filters a liquid to be filtered.

液体の濾過、特に半導体産業等の高価な薬液の濾過においては、1リットル前後といった少量の濾過を行うことが多く、濾過後の残液体においても回収率を上げる必要性が高くなっている。
特に、高い精度を要求される濾過操作においては、捕捉される粒子の大きさも次第に微細な領域になってきており、これに対する技術もより高度なものが求められて、現在では対象粒子の径は0.02μmの捕捉性能が要求されるようになってきている。
従来の濾過システムで一次側の液残量を最小にすることを第一の目的とする場合は、ディスクフィルタ(多孔支持ディスクに円板状の多孔質膜フィルタを支持させたもの)を円筒状の容器に納めたものを使用しているが、従来の構造では容器の寸法に対するディスクフィルタの濾過面積が相対的に小さいので、その小さい濾過面積に起因して処理時間が長くなる傾向があった。すなわち、円板状のフィルタの濾過面積は、外径の二乗に比例した濾過面積しか得ることができない。
この対策として、2枚以上のディスクフィルタを重畳した積層フィルタ(スタックフィルタ)とすることにより、一枚のディスクフィルタの濾過面積の積層数倍の濾過面積を得ることができ、処理時間を短縮することが可能であるが、その場合積層フィルタを収納する容器の内面とディスクフィルタ外径の間、並びに積層したディスクフィルタ同士の間に液体通路がそれぞれ必要になるので一次側流路容積及び二次側流路容積が加算されて一枚のディスクフィルタに必要な容積が積層数に応じて大きくなる。このため少量の濾過の場合、濾過作業終了時に容器内に残留している液体残量が大きい問題となる。
In the filtration of liquids, particularly in the case of expensive chemical solutions such as in the semiconductor industry, a small amount of filtration such as about 1 liter is often performed, and the need to increase the recovery rate of the remaining liquid after filtration is also increasing.
In particular, in filtration operations that require high accuracy, the size of captured particles is gradually becoming a finer area, and there is a demand for more advanced technology for this. A trapping performance of 0.02 μm has been required.
When the primary purpose is to minimize the remaining amount of liquid on the primary side in a conventional filtration system, a disk filter (a disk-shaped porous membrane filter supported on a porous support disk) is cylindrical. However, in the conventional structure, the filtration area of the disk filter relative to the dimensions of the container is relatively small, so the processing time tends to be longer due to the small filtration area. . That is, the filtration area of the disk-shaped filter can only obtain a filtration area proportional to the square of the outer diameter.
As a countermeasure, by using a laminated filter (stack filter) in which two or more disk filters are superposed, a filtration area that is several times as many as the filtration area of one disk filter can be obtained, and the processing time is shortened. In this case, a liquid passage is required between the inner surface of the container for housing the laminated filter and the outer diameter of the disk filter, and between the laminated disk filters. By adding the side channel volume, the volume required for one disk filter increases according to the number of layers. Therefore, in the case of a small amount of filtration, there is a problem that the remaining amount of liquid remaining in the container at the end of the filtration operation is large.

他方、濾過膜をひだ状に折り込み円筒状に配置したいわゆるプリーツフィルタを容器に収納したフィルタ装置では、同程度の大きさの容器に対して、濾過面積をディスクフィルタの場合に比して遙かに大きく設定することが可能となり、処理時間の短縮される利点があり、また広範な濾過操作の要求に対応することができるが、処理液体の残留量に対する構造上の不利益がある。
すなわち、プリーツフィルタでは所望の処理液量を規定時間内での処理を考える場合、流路容積をあまり増大させないで濾過面積を増大でき、また圧力損失を最小にすることができる。しかし、このタイプの構造設計においてもプリーツフィルタとハウジングの間には、通常プリーツフィルタの内外周面を支持するための、液体を流通させる多数の開口を有する内側多孔円筒(コア)及び外側多孔円筒(スリーブ)を必要とし、コアには内部通路をスリーブと円筒状容器(ハウジング)との間には液体通路のための空間を形成する必要がある(例えば特許文献1)。これらの通路は、濾過処理の終点で液体を加圧濾過しきれずに残留する液体のよどみになり、そのまま残留液空間を形成するという不利益を生じることになる。
少量の濾過操作において、濾過精度、処理液体の容器内部残留量の最小化を計ろうとすると処理時間が長くなり、濾過精度と処理時間の短縮を計ると容器内部残留量が増え濾過操作の効率を低下させてしまうことになる。
On the other hand, in a filter device in which a so-called pleated filter, in which a filtration membrane is folded in a pleated shape and stored in a container, is stored in a container, the filtration area is much larger than that of a disk filter for a container of the same size. However, there is an advantage that the processing time is shortened, and it is possible to meet a wide range of filtration operation requirements, but there is a structural disadvantage with respect to the remaining amount of the processing liquid.
That is, in the case of considering processing of a desired amount of processing liquid within a specified time in the pleated filter, the filtration area can be increased without increasing the flow volume so much, and the pressure loss can be minimized. However, even in this type of structural design, an inner porous cylinder (core) and an outer porous cylinder having a large number of openings through which liquid flows are usually provided between the pleated filter and the housing to support the inner and outer peripheral surfaces of the pleated filter. (Sleeve) is required, and an internal passage must be formed in the core, and a space for a liquid passage must be formed between the sleeve and the cylindrical container (housing) (for example, Patent Document 1). These passages become the stagnation of the remaining liquid because the liquid cannot be filtered under pressure at the end of the filtration process, resulting in the disadvantage of forming a residual liquid space as it is.
In a small amount of filtration operation, the processing time becomes longer when trying to minimize the filtration accuracy and the residual amount of processing liquid inside the container, and when the filtration accuracy and processing time are shortened, the residual amount inside the container increases and the efficiency of the filtering operation increases. It will be reduced.

特開平5−111622号明細書JP-A-5-111622

そこで、本発明が解決しようとする課題は、濾過精度の向上と処理時間の短縮を可能とするプリーツ型のフィルタでありながらも、容器内部残留量を最小にとどめることができるフィルタ装置を簡単な構造で提供することにある。   Therefore, the problem to be solved by the present invention is a simple filter device capable of minimizing the residual amount inside the container even though it is a pleated filter that can improve the filtration accuracy and shorten the processing time. There is to provide in structure.

本発明は、上記課題を、両端が開放された円筒状の内部空間を設けた円筒部と、前記内部空間に前記円筒部の内壁に直接接触した状態で挿入され上下端面が液密に封止されている円環状のプリーツフィルタ(フィルタ膜をプリーツ状に折り曲げ円筒状に形成したもの)と、前記プリーツフィルタの内周面を支持する多孔コアと、前記円筒部の両端とそれぞれ液密に接合されていて前記円筒部と共に液密ハウジングを構成する下側蓋体及び上側蓋体と、前記円筒部の下端部から前記プリーツフィルタのプリーツ間に通じる被濾過液分配路と、該分配路に通じる被濾過液供給路と、前記供給路へ接続された被濾過液供給口と、前記多孔コアの内部通路に通じる濾過液排出路と、前記排出路に接続された濾液排出口と、よりなる濾過装置により解決する。
この構成によると、プリーツフィルタとハウジングの外周壁を構成する円筒部の内壁面との間には特許文献1のような外側多孔円筒(スリーブ)もその外側の被濾過液供給通路も存在せず、その分だけ被濾過液体が占有する空間が減じるので、濾過残量が減じる。本発明では被濾過液が供給通路を介して直接プリーツフィルタの外側からプリーツ間に供給されるが、実験によると格別の流動抵抗の増加もなく一定の濾過量に対する濾過時間は従来のプリーツフィルタによる濾過装置と変わらないことが判明している。
The present invention solves the above-described problem by inserting a cylindrical portion having a cylindrical inner space open at both ends, and the upper and lower end surfaces of the inner space are sealed in a liquid-tight manner while being in direct contact with the inner wall of the cylindrical portion. Annular pleated filter (filter membrane is folded into a pleat and formed into a cylindrical shape), a porous core that supports the inner peripheral surface of the pleated filter, and both ends of the cylindrical portion are liquid-tightly joined. A lower lid body and an upper lid body that form a liquid-tight housing together with the cylindrical portion, a liquid distribution passage to be filtered that communicates between the pleats of the pleated filter from the lower end portion of the cylindrical portion, and the distribution passage. Filtration comprising a filtrate supply path, a filtrate supply port connected to the supply path, a filtrate discharge path leading to the internal passage of the porous core, and a filtrate discharge port connected to the discharge path Solve by equipment That.
According to this configuration, neither the outer porous cylinder (sleeve) nor the outside to-be-filtered liquid supply passage as in Patent Document 1 exists between the pleated filter and the inner wall surface of the cylindrical portion constituting the outer peripheral wall of the housing. Since the space occupied by the liquid to be filtered is reduced by that amount, the remaining amount of filtration is reduced. In the present invention, the liquid to be filtered is directly supplied between the pleats from the outside of the pleat filter via the supply passage. According to the experiment, the filtration time for a constant filtration amount is not limited by the conventional pleated filter without any particular increase in flow resistance. It has been found that it is no different from a filtration device.

本発明の1つの形態によると、前記被濾過液供給口は前記下側蓋体に設けられ、前記濾液排出口は前記上側蓋体に設けられている。この形態では、円筒部及び上下蓋体の構造が単純になり、樹脂成形金型が単純化され、濾過装置の製造が安価及び容易になる。   According to one aspect of the present invention, the filtrate supply port is provided in the lower lid, and the filtrate discharge port is provided in the upper lid. In this form, the structure of the cylindrical portion and the upper and lower lids is simplified, the resin molding die is simplified, and the manufacture of the filtration device is inexpensive and easy.

本発明の他の形態によると、前記被濾過液供給口は前記円筒部に設けられ、前記濾液排出口は前記上側蓋体に設けられている。この形態は樹脂成形金型の製造がやや複雑になるが、被濾過液体の供給が水平方向に行うことが可能となるので、場合により有利である。   According to another aspect of the invention, the filtrate supply port is provided in the cylindrical portion, and the filtrate discharge port is provided in the upper lid. Although this form makes the production of the resin mold somewhat complicated, it is advantageous in some cases because the liquid to be filtered can be supplied in the horizontal direction.

本発明の他の1つの形態によると前記円筒部の内周面の下端側は前記下側開放端に向けて末広状のテーパ面を有し、前記分配路が前記テーパ面と前記円筒状プリーツフィルタの外周面とにより画成されている。この形態によると、液体はプリーツフィルタの全てのプリーツ間に容易に分配され濾過効率が上がる。   According to another embodiment of the present invention, the lower end side of the inner peripheral surface of the cylindrical portion has a divergent tapered surface toward the lower open end, and the distribution path is formed between the tapered surface and the cylindrical pleat. It is defined by the outer peripheral surface of the filter. According to this configuration, the liquid is easily distributed among all the pleats of the pleated filter and the filtration efficiency is increased.

本発明の更に他の形態によると、前記下側蓋体は前記円筒部の内径よりも大きい内径を有する円環部を備えたカップ状部材であり、前記円筒部の下端外周は前記円環部に間隙を以て重畳する薄肉部を有し、該薄肉部には貫通孔が形成され、前記分配路が前記間隙と前記貫通孔とにより構成されている。この形態によると液体は上記間隙から前記貫通した通液溝を通って容易にプリーツフィルタの全外周面に供給され、それによりプリーツ間に容易に分配される。一方前記薄肉部下端はプリーツフィルタの下端部を支持することができる。   According to still another embodiment of the present invention, the lower lid is a cup-shaped member having an annular portion having an inner diameter larger than the inner diameter of the cylindrical portion, and the outer periphery of the lower end of the cylindrical portion is the annular portion. And a through-hole is formed in the thin-walled portion, and the distribution path is constituted by the gap and the through-hole. According to this embodiment, the liquid is easily supplied from the gap through the penetrating groove, to the entire outer peripheral surface of the pleated filter, and thereby easily distributed between the pleats. On the other hand, the lower end of the thin portion can support the lower end of the pleated filter.

本発明の他の好ましい形態では、前記プリーツフィルタの底部端縁部と前記多孔コアの底面と前記円筒部の底面は一枚の円板状プラスチックシートで封着されている。これによるとプリーツフィルタの底面が容易に封着でき、また被処理液の供給通路がプリーツフィルタ下側キャップとプラスチックシートとの間に形成され、液体のプリーツフィルタ外周部への一様な分配が可能になる。同様に前記プリーツフィルタの上部端縁部の封着にもプラスチックシートを介在させると封着が容易となる。   In another preferred embodiment of the present invention, the bottom edge of the pleated filter, the bottom surface of the porous core, and the bottom surface of the cylindrical portion are sealed with a single disc-shaped plastic sheet. According to this, the bottom surface of the pleated filter can be easily sealed, and a supply passage for the liquid to be processed is formed between the lower cap of the pleated filter and the plastic sheet, so that the liquid can be uniformly distributed to the outer periphery of the pleated filter. It becomes possible. Similarly, the sealing of the upper edge portion of the pleated filter is facilitated by interposing a plastic sheet.

本発明の他の好ましい形態では、前記多孔コアの内部通路及び多孔部が占める容積は多孔コアの全体の容積の50%以下に制限される。これにより残留液量を更に減少させることができる。この場合プリーツフィルタの内周面からの濾液の流通を良くするために前記多孔通路は上流側が広く内部通路側が狭い流路断面積を有することが望ましい。   In another preferred embodiment of the present invention, the volume occupied by the internal passage and the porous portion of the porous core is limited to 50% or less of the total volume of the porous core. Thereby, the residual liquid amount can be further reduced. In this case, in order to improve the flow of the filtrate from the inner peripheral surface of the pleated filter, the porous passage desirably has a flow passage cross-sectional area that is wide on the upstream side and narrow on the internal passage side.

本発明の好ましい他の形態では、円筒部の内周面の上端側は上側開放端に向けて末広状のテーパ面を有し、該テーパ面と円筒状プリーツフィルタの外周面とによりガス収集路を画成し、円筒部または上側蓋体にガスベント通路と、それに連絡するガスベント口とを設ける。好ましくはさらに、前記円筒部に前記被濾過液供給通路から前記ガスベント通路に接続する他のガスベント通路を設ける。この形態では被処理液体中の溶存ガスやバブルの分離除去が可能となる。   In another preferred embodiment of the present invention, the upper end side of the inner peripheral surface of the cylindrical portion has a tapered surface that is divergent toward the upper open end, and the gas collecting path is formed by the tapered surface and the outer peripheral surface of the cylindrical pleated filter. And a gas vent passage and a gas vent port communicating therewith are provided in the cylindrical portion or the upper lid. Preferably, further, another gas vent passage connected from the filtrate supply passage to the gas vent passage is provided in the cylindrical portion. In this form, it is possible to separate and remove dissolved gas and bubbles in the liquid to be treated.

この発明は、上記の通り小型小容量のものとするため、重要な方策としてスリーブをなくし、流路を狭めたものである。そのため、プリーツの各ひだに被濾過液が満遍なく行き渡るような構造を採用したものである。
本発明の第1の形態では、
(1)円筒部の構造
円筒部の形状を両端が開口した形にする。円筒部は円筒状に形成されたプリーツフィルタを直接保持するような内径を有する。被濾過液のほぼ均一な分配供給を行うための分配路を提供するために、(a)円筒部の下端部は下側蓋体の周壁の内径よりも小径を有し、且つ大きい貫通口を有する薄肉部を有することにより、下側蓋体の内周面との環状の被濾過液分配路を形成し、被濾過液をプリーツフィルタの下端からプリーツ間に容易に供給できる通液路とするか、または(b)円筒部の下端部の内周面は開放端に向けて末広状に拡大するテーパ面を有することにより、円筒状プリーツフィルタの外周面との間に被濾過液分配路を形成することが望ましい。
また、被濾過液に溶存するガスを排出する手段として、円筒部の内周上端側を開放端に向けて末広がりに拡大するテーパ面とにすることが望ましい。これによりテーパ面と円筒状のプリーツフィルタの外周面との間にガス収集路が形成され、ガスベント通路を通じてガスベント孔に導くことができる。
(2)下側蓋体の構造
上記(1)の(a)の場合には、薄肉部の周りに、薄肉部の通液路を経てプリーツフィルタプリーツ間に円滑に被濾過液を供給・分配するための供給流路を提供するために、下側蓋体は前記薄肉部よりも径の大きい内径と、前記円筒部の下端部に溶着できる大きさの外形を有するカップ状の部材として構成される。カップ状部材の上端縁は円筒部の下端縁に溶着される。上記(1)の(b)の場合には、筒部のテーパ面とプリーツフィルタの間の分配路に被濾過液供給路が連通していればよい。
(3)コアの構造
従来の単なる多孔筒体でなく、極力内容量を減らした円柱状構成であることが必要であり、このため内部通路と多孔部の容積を多孔コアの容積の50%以下に抑制することが望まれる。
(4)融着補助フィルム
また部品点数を減らすため、プリーツフィルタの上下端部を溶着により封着する際にコア上下端を同時に溶着することが必要である。この手段としてディスク状プラスチックフィルムをコアの少なくとも下端面(さらに上端面での封着に使用する場合には環状プラスチックフィルム)とプリーツフィルタの下端面(好ましくはさらに上端面)に当てた状態で封着することが望ましい。
Since the present invention has a small size and a small capacity as described above, the sleeve is eliminated and the flow path is narrowed as an important measure. For this reason, a structure in which the liquid to be filtered spreads evenly over each pleat of the pleat is adopted.
In the first aspect of the present invention,
(1) Structure of the cylindrical portion The cylindrical portion is shaped so that both ends are open. The cylindrical portion has an inner diameter that directly holds the pleated filter formed in a cylindrical shape. In order to provide a distribution path for performing substantially uniform distribution and supply of the liquid to be filtered, (a) the lower end portion of the cylindrical portion has a smaller diameter than the inner diameter of the peripheral wall of the lower lid, and a large through hole is provided. By having the thin-walled portion, an annular filtered liquid distribution path is formed with the inner peripheral surface of the lower lid, and the liquid to be filtered can be easily supplied from the lower end of the pleated filter between the pleats. Or (b) the inner peripheral surface of the lower end of the cylindrical portion has a tapered surface that expands toward the open end, thereby providing a liquid distribution path to be filtered between the outer peripheral surface of the cylindrical pleated filter. It is desirable to form.
Further, as a means for discharging the gas dissolved in the liquid to be filtered, it is desirable that the inner peripheral upper end side of the cylindrical portion has a tapered surface that expands toward the open end. Thereby, a gas collection path is formed between the tapered surface and the outer peripheral surface of the cylindrical pleated filter, and can be led to the gas vent hole through the gas vent passage.
(2) Structure of the lower lid In the case of (a) in (1) above, the liquid to be filtered is smoothly supplied and distributed between the pleated filter pleats around the thin wall portion through the liquid passage of the thin wall portion. In order to provide a supply flow path, the lower lid is configured as a cup-shaped member having an inner diameter larger in diameter than the thin-walled portion and an outer shape that can be welded to the lower end portion of the cylindrical portion. The The upper edge of the cup-shaped member is welded to the lower edge of the cylindrical portion. In the case of (b) in (1) above, it is only necessary that the filtrate supply path communicates with the distribution path between the tapered surface of the cylindrical portion and the pleated filter.
(3) Core structure It is necessary to have a columnar structure with a reduced internal capacity as much as possible, instead of a conventional simple porous cylinder. For this reason, the volume of the internal passage and the porous part is 50% or less of the volume of the porous core. It is desirable to suppress it.
(4) Auxiliary fusion film In order to reduce the number of parts, it is necessary to weld the upper and lower ends of the core simultaneously when the upper and lower ends of the pleated filter are sealed by welding. As a means for this, the disc-shaped plastic film is sealed in a state where it is applied to at least the lower end surface of the core (or an annular plastic film when used for sealing at the upper end surface) and the lower end surface (preferably further the upper end surface) of the pleated filter. It is desirable to wear.

本発明の第2の形態では、
(1)円筒部の構造
第1の形態と同様に、円筒部の形状を両端が開口した形にする。円筒部は円筒状に形成されたプリーツフィルタを直接保持するような内径を有する。上下蓋体は板状に形成され、円筒部はこれら上下蓋体に溶着される。被濾過液をプリーツフィルタの下端部からプリーツ間に容易に供給できるようにするために、円筒部の内周下端側を下端開放端へ向けて末広がりに拡大するテーパ面にし、それによりテーパ面と円筒状のプリーツフィルタの外周面との間に被濾過液のための分配路を形成する。この分配路を円筒部に設けた被濾過液供給路をへて被濾過液供給口に連絡する。供給路は円筒状のプリーツフィルタの外周面に対して接線方向に設けることにより、被濾過液は供給路からプリーツフィルタの外周面に接線方向から入り、前記テーパ面とプリーツフィルタの外周面との間の分配路に沿って全てのプリーツ間にほぼ一様に分配される。
(2)下側蓋体の構造
下側蓋体は単純な板状のものでよく、前記円筒部の下端部に溶着できる大きさの外形を有する。
(3)コアの構造
実施例1の場合と同様に構成する。
(4)溶着補助フィルム
なお、フィルタの上下端部を溶着により封着する際にコアの上下端部も同時に溶着することが必要である。この補助手段として接着を助けるディスク状プラスチックフィルムをコアの下端面とプリーツフィルタの下端面に当て、環状のプラスチックフィルムをコアの上端面とプリーツフィルタの上端面に当てた状態で封着することが望ましい。場合によりさらに円筒部と蓋体の間までこれらのフィルムを延長しても良い。
In the second aspect of the present invention,
(1) Structure of cylindrical portion As in the first embodiment, the shape of the cylindrical portion is made open at both ends. The cylindrical portion has an inner diameter that directly holds the pleated filter formed in a cylindrical shape. The upper and lower lids are formed in a plate shape, and the cylindrical portion is welded to these upper and lower lids. In order to allow the liquid to be filtered to be easily supplied between the pleats from the lower end portion of the pleated filter, the inner peripheral lower end side of the cylindrical portion is a tapered surface that expands toward the lower end open end, thereby forming a tapered surface. A distribution path for the liquid to be filtered is formed between the outer peripheral surface of the cylindrical pleated filter. The distribution path is connected to the filtrate supply port through the filtrate supply path provided in the cylindrical portion. By providing the supply path in a tangential direction with respect to the outer peripheral surface of the cylindrical pleated filter, the liquid to be filtered enters the outer peripheral surface of the pleated filter from the supply path from the tangential direction, and the tapered surface and the outer peripheral surface of the pleated filter are Almost evenly distributed among all pleats along the distribution path between them.
(2) Structure of lower lid body The lower lid body may be a simple plate-like one and has an outer shape that can be welded to the lower end portion of the cylindrical portion.
(3) Core structure The configuration is the same as that in the first embodiment.
(4) Welding auxiliary film In addition, when sealing the upper and lower ends of a filter by welding, it is necessary to also weld the upper and lower ends of a core simultaneously. As an auxiliary means, a disc-shaped plastic film that assists adhesion may be applied to the lower end surface of the core and the lower end surface of the pleated filter, and the annular plastic film may be sealed in contact with the upper end surface of the core and the upper end surface of the pleated filter. desirable. In some cases, these films may be further extended between the cylindrical portion and the lid.

以下図面を参照して本発明の濾過装置の好ましい実施例を説明する。なお、本発明の容器部を構成する構造部材である円筒部、上下蓋体、多孔コア、及び機能部材であるプリーツフィルタの各材質は耐食性、耐薬品性、耐熱性等を考慮して使用目的に応じて各種の合成樹脂から製作できるが、特許文献1等により周知であり、またプリーツフィルタの構造と製造方法も特許文献1等により周知であることから本書ではここでは詳しく説明しないので、同文献を参照されたい。また理解を容易にするために各実施例において同一又は類似の部材は同一の参照符号により示し、相違部分は別に説明する。   Preferred embodiments of the filtration device of the present invention will be described below with reference to the drawings. In addition, each material of the cylindrical part which is the structural member constituting the container part of the present invention, the upper and lower lids, the porous core, and the pleated filter which is the functional member is used in consideration of corrosion resistance, chemical resistance, heat resistance, etc. However, since the structure and the manufacturing method of the pleated filter are well known from Patent Document 1, etc., they will not be described in detail here. See literature. In order to facilitate understanding, the same or similar members are denoted by the same reference numerals in each embodiment, and different portions will be described separately.

図1は本発明の実施例1による濾過装置を示し、(a)は正面立断面図、(b)は平面図、及び(c)は底面図である。
この実施例による濾過装置1は、両端が開放され円筒状の内部空間を設けた円筒部3と、前記内部空間に円筒部3の内壁面39(図2)に接触した状態で挿入され上下端縁部が液密に封止されている円筒状のプリーツフィルタ5と、前記プリーツフィルタ5の内周面を支持する、多数の開口を有する多孔コア7と、前記円筒部3の上下両端とそれぞれ液密に接合されている下側蓋体9及び上側蓋体11とを含み、円筒部3、上下蓋体9、11は一緒になって液密ハウジング又は液密容器を形成している。
1A and 1B show a filtering device according to a first embodiment of the present invention, in which FIG. 1A is a front elevation sectional view, FIG. 1B is a plan view, and FIG. 1C is a bottom view.
The filtration device 1 according to this embodiment is inserted into the inner space in contact with an inner wall surface 39 (FIG. 2) of the cylindrical portion 3 having both ends open and provided with a cylindrical inner space. A cylindrical pleated filter 5 whose edge is liquid-tightly sealed, a porous core 7 having a large number of openings for supporting the inner peripheral surface of the pleated filter 5, and upper and lower ends of the cylindrical portion 3 respectively. The lower lid body 9 and the upper lid body 11 are joined in a liquid-tight manner, and the cylindrical portion 3 and the upper and lower lid bodies 9 and 11 together form a liquid-tight housing or a liquid-tight container.

下側蓋体9には被濾過液供給口15が設けられ、供給口15は、下側蓋体9の内面に沿って広がる被濾過液供給路13を経て、円筒部3の下端に設けた薄肉部33の外周面と下側蓋体9の環状部19の内周面との間に形成された環状の分配路21に通じている。この分配路21はその円周方向に配置された複数の開口35を経てプリーツフィルタ5のプリーツ間に通じている。供給路13は、多孔コア7及びプリーツフィルタ5の下端面を下側蓋体9の内底面から離間させることによって形成されており、それにより被濾過液(供給液)をプリーツフィルタ5の周部に一様に分配することが出来る。この形態では、多孔コア7及びプリーツフィルタ5の下端面を無孔のディスク状プラスチックフィルム6により気密に閉鎖する。プラスチックフィルムは溶着される部材の接着を助ける部材から製作する。さらに、下側蓋体9の供給路13の容積を減じるため、前記環状部19の内面の底部と、多孔コア7及びプリーツフィルタ5の下端面を無孔のディスク状プラスチックフィルム6により気密に閉鎖された面とを密着させることもできる。すなわち、この場合前記環状部19の内面の底部には、この底部に設けられた供給口15から放射状に分配路21方向に複数の溝を設けてもよい。なお、下側蓋体9にはさらに場合により供給路13に通じる残液排出口17が設けられることがある。
下側蓋体9はカップ状に形成されており、その環状部19は円筒部3よりも薄肉に形成され、それによりプリーツフィルタ5の下端の薄肉部33の外周を取り囲んで、環状分配流路21を形成している。円筒部3の下端に設けた開口35を有する薄肉部33は単純な円筒体でも良いが、より好ましくは図示のようにテーパ部として構成することにより、円滑な被濾過液の供給を行うことができる。この薄肉部33の内周面は円筒部3の内周面の一部を構成しプリーツフィルタ5の下端部を支持している。さらに薄肉部33は上記のディスク状プラスチックフィルムと一体に溶着され、被濾過液の供給が開口35を通してプリーツフィルタの外周に一様に分配されるようにしている。
The lower lid body 9 is provided with a filtrate supply port 15, and the supply port 15 is provided at the lower end of the cylindrical portion 3 through the filtrate supply path 13 extending along the inner surface of the lower lid body 9. It communicates with an annular distribution path 21 formed between the outer peripheral surface of the thin portion 33 and the inner peripheral surface of the annular portion 19 of the lower lid 9. The distribution path 21 communicates between the pleats of the pleat filter 5 through a plurality of openings 35 arranged in the circumferential direction. The supply path 13 is formed by separating the lower end surfaces of the porous core 7 and the pleat filter 5 from the inner bottom surface of the lower lid body 9, thereby allowing the liquid to be filtered (supply liquid) to flow around the pleated filter 5. Can be uniformly distributed. In this embodiment, the lower end surfaces of the porous core 7 and the pleated filter 5 are hermetically closed with a non-porous disc-shaped plastic film 6. The plastic film is made from a member that helps adhere the members to be welded. Further, in order to reduce the volume of the supply passage 13 of the lower lid 9, the bottom of the inner surface of the annular portion 19 and the lower end surfaces of the porous core 7 and the pleated filter 5 are hermetically closed by a non-porous disc-shaped plastic film 6. It is also possible to make a close contact with the finished surface. That is, in this case, a plurality of grooves may be provided at the bottom of the inner surface of the annular portion 19 in the direction of the distribution path 21 from the supply port 15 provided at the bottom. The lower lid 9 may further be provided with a residual liquid discharge port 17 that leads to the supply path 13 in some cases.
The lower lid body 9 is formed in a cup shape, and the annular portion 19 is formed thinner than the cylindrical portion 3, thereby surrounding the outer periphery of the thin portion 33 at the lower end of the pleated filter 5, 21 is formed. The thin portion 33 having the opening 35 provided at the lower end of the cylindrical portion 3 may be a simple cylindrical body, but more preferably, it is configured as a tapered portion as shown in FIG. it can. The inner peripheral surface of the thin portion 33 constitutes a part of the inner peripheral surface of the cylindrical portion 3 and supports the lower end portion of the pleated filter 5. Further, the thin portion 33 is welded integrally with the disk-shaped plastic film, so that the supply of the liquid to be filtered is uniformly distributed to the outer periphery of the pleated filter through the opening 35.

一方、上側蓋体11には、多孔コア7の内部通路23に通じる濾過液排出路25と、排出路25に接続された濾液排出口27が設けられている。
好ましくは上側蓋体11と円筒部3との接合部には円環状ベント通路29が形成され、このベント通路はベント口31に接続されている。後述のようにベント通路29は被濾過液供給通路13及びプリーツフィルタ5の周部へ連通されており、被濾過液中に溶存し或いはバブルで存在するガスを排出する。
On the other hand, the upper lid body 11 is provided with a filtrate discharge passage 25 that communicates with the internal passage 23 of the porous core 7 and a filtrate discharge port 27 that is connected to the discharge passage 25.
Preferably, an annular vent passage 29 is formed at the joint between the upper lid 11 and the cylindrical portion 3, and this vent passage is connected to the vent port 31. As will be described later, the vent passage 29 communicates with the filtrate supply passage 13 and the peripheral portion of the pleated filter 5, and discharges the gas dissolved in the filtrate or present as bubbles.

図2は実施例1による濾過装置の容器の一部を構成するための円筒部を示し、(a)は正面立断面図及び(b)は底面図である。
図1(a)及び図2に示すように、円筒部3の内面39はプリーツフィルタ5を直接支持するための支持面となる。また円筒部3は下端に薄肉部33を備え、薄肉部33には円周方向に延びる3個(一般に複数)の細長い開口35を有する。開口が張る角度αは出来るだけ大きくし(例えば100°)流動抵抗を出来るだけ下げることが望ましい。また既述のようにこの薄肉部33により環状分配路21が形成される。
円筒部3にはその壁部を垂直に貫通するベント通路41が設けられ、下端は被濾過液供給通路13または環状分配路21に接続し、上端は環状ガスベント通路29の下側部分に接続されている。更にガスベントを良好にするために円筒部3の内周面の上端側は上端に向けて末広がりに角度βで拡大するテーパ面8を有することによりプリーツフィルタ5の外周面とテーパ面8との間にガス収集路を形成している。このガスベント通路29の一部は横通路45によりこのガス収集路に通じており、プリーツフィルタ5の外周上部に溜まるガスを引き出す。
図1のように円筒部3の上端縁43は上側蓋体11の周部に溶着されており、下端縁37は下側蓋体9の環状部19の上端縁に溶着されている。ここでも環状の溶着補助プラスチックフィルムを使用することにより融着及び封着を容易にすることが望ましい。
FIG. 2 shows a cylindrical portion for constituting a part of the container of the filtration device according to the first embodiment, wherein (a) is a front elevational sectional view and (b) is a bottom view.
As shown in FIGS. 1A and 2, the inner surface 39 of the cylindrical portion 3 serves as a support surface for directly supporting the pleated filter 5. The cylindrical portion 3 includes a thin portion 33 at the lower end, and the thin portion 33 has three (generally plural) elongated openings 35 extending in the circumferential direction. It is desirable that the angle α at which the opening is stretched is as large as possible (for example, 100 °) to reduce the flow resistance as much as possible. Further, as described above, the annular distribution path 21 is formed by the thin portion 33.
The cylindrical portion 3 is provided with a vent passage 41 that vertically penetrates the wall portion, the lower end is connected to the filtrate supply passage 13 or the annular distribution passage 21, and the upper end is connected to the lower portion of the annular gas vent passage 29. ing. Further, in order to improve the gas vent, the upper end side of the inner peripheral surface of the cylindrical portion 3 has a taper surface 8 that widens toward the upper end and expands at an angle β, so that the gap between the outer peripheral surface of the pleat filter 5 and the taper surface 8 is increased. A gas collection path is formed in the area. A part of the gas vent passage 29 is connected to the gas collection path by a lateral passage 45 and draws out the gas accumulated on the outer periphery of the pleated filter 5.
As shown in FIG. 1, the upper edge 43 of the cylindrical portion 3 is welded to the peripheral portion of the upper lid body 11, and the lower edge 37 is welded to the upper edge of the annular portion 19 of the lower lid body 9. Again, it is desirable to facilitate fusion and sealing by using an annular welding assist plastic film.

図3は実施例1による濾過装置の多孔コアを示し、(a)は正面立断面図、(b)は正面立面図、(c)図3のc−c断面図、及び(d)は平面図である。
図1(a)及び図3を参照して多孔コア7の詳細を説明するに、多孔コア7の外周面はプリーツフィルタ5の内周面を支持すると共に、フィルタ5を透過した濾液を排出するために内部通路23に通ずる放射状に設けられ、多孔コアの多孔を構成する通路47を有する。廃液の効率を上げるために通路47はそれぞれ図3(c)のように外側に向けて末広の扇形になっている。扇形の角度γはプリーツフィルタ5の支持に支障のない範囲で出来るだけ大きくする。また同じ目的で多孔コア7の外周面には円周方向に延びて通路47に通じる浅い凹入部49が形成されている。
この例で注意すべきはプリーツフィルタを使用する通常の濾過装置における内部通路よりも内部通路23や、流路47が極端に小さいことである。これは残留液を極力減じるためである。好ましくは内部通路23と多孔通路47の総合容積は多孔コア7の全容積の50%以下、更に好ましくは30%以下、一層に好ましくは15%以下である。図3の例では約10%程度である。ただし充分な流量を確保できることを要するが、実施例では全く問題がない。
FIG. 3 shows a porous core of the filtration device according to Example 1, (a) is a front elevational sectional view, (b) is a front elevational view, (c) a cc sectional view of FIG. It is a top view.
The details of the porous core 7 will be described with reference to FIGS. 1A and 3. The outer peripheral surface of the porous core 7 supports the inner peripheral surface of the pleated filter 5 and discharges the filtrate that has passed through the filter 5. Therefore, it has a passage 47 which is provided in a radial pattern so as to communicate with the internal passage 23 and constitutes a porous core. In order to increase the efficiency of the waste liquid, each of the passages 47 has a fan shape that is wide toward the outside as shown in FIG. The fan-shaped angle γ is made as large as possible within a range that does not hinder the support of the pleated filter 5. For the same purpose, a shallow recessed portion 49 extending in the circumferential direction and communicating with the passage 47 is formed on the outer peripheral surface of the porous core 7.
It should be noted in this example that the internal passage 23 and the flow passage 47 are extremely smaller than the internal passage in a normal filtration apparatus using a pleated filter. This is to reduce the residual liquid as much as possible. Preferably, the total volume of the internal passage 23 and the porous passage 47 is 50% or less of the total volume of the porous core 7, more preferably 30% or less, and even more preferably 15% or less. In the example of FIG. 3, it is about 10%. However, although it is necessary to ensure a sufficient flow rate, there is no problem at all in the embodiment.

プリーツフィルタ5は周知であり例えば特許文献1に記載された方法で多孔質濾過膜の両面に不織布又はネット支持シートを重畳させ、プリーツ状にひだ折りして円筒状にし、両側縁を重畳封着することにより構成する。   The pleated filter 5 is well known, for example, by a method described in Patent Document 1, a nonwoven fabric or a net support sheet is superimposed on both sides of a porous filtration membrane, folded into a pleat shape into a cylindrical shape, and both side edges are overlap-sealed. It is constituted by doing.

図1(a)を参照して上記の構造により濾過装置の組立の一例を説明するに、多孔コア7の周りに、円筒状にしたプリーツフィルタ5を被せ、さらに円筒部3をその外側に被せ、次いでそれらの上端を加熱し、上側蓋体11の溶融した内面に溶着冷却する。このとき溶着を助けるために環状のプラスチックフィルムを使用しても良い。これによりプリーツフィルタ5の上縁は完全に液密に封着されると共に、その他の部材は一体になる。
次いで多孔コア7、プリーツフィルタ5及び円筒部3の下端面に融着可能な円板状の合成樹脂フィルム6を重ね熱融着する。
次いでこの半製品に下側蓋体9を被せ、円筒部3の下端縁37とカップ状の上端縁43とを熱融着して接合する。このとき溶着を助けるためにディスク状のプラスチックフィルムを使用しても良い。
Referring to FIG. 1 (a), an example of assembling a filtering device with the above structure will be described. A porous pleat filter 5 is covered around a porous core 7, and a cylindrical portion 3 is further covered on the outside. Then, their upper ends are heated and welded and cooled to the melted inner surface of the upper lid 11. At this time, an annular plastic film may be used to assist welding. As a result, the upper edge of the pleated filter 5 is completely liquid-tightly sealed and the other members are integrated.
Next, a disc-shaped synthetic resin film 6 that can be fused to the lower end surface of the porous core 7, the pleated filter 5, and the cylindrical portion 3 is laminated and heat-sealed.
Next, the lower lid body 9 is put on the semi-finished product, and the lower end edge 37 of the cylindrical portion 3 and the cup-shaped upper end edge 43 are bonded by heat fusion. At this time, a disk-shaped plastic film may be used to assist welding.

動作
図1はこの実施例による完成した濾過装置であり、排出口17は閉鎖されているものとする。被濾過液体は供給口15から導入され、供給路13により半径方向に流動し、環状の分配流路21に流れ、円筒部3の下端薄肉部33の開口35からプリーツフィルタ5の下端外周部、次いでプリーツ間に分流して上方に流れ、それにつれてプリーツフィルタ5の多孔質濾過膜を透過し、通路47、内部通路23、及び排出路25を経て排出口27に精製濾液として回収される。ゲル等や固形粒子はフィルタの外面に捕捉される。一方溶存ガスや気泡は供給通路13の環状の分配流路21から、ベント通路41、及び環状のベント通路29を経てベント口31に排出される。またプリーツフィルタ5の周辺から上昇するガスは横通路45から環状ベント通路29に引き出される。
Operation FIG. 1 is a completed filtering device according to this embodiment, and the outlet 17 is closed. The liquid to be filtered is introduced from the supply port 15, flows in the radial direction through the supply path 13, flows into the annular distribution flow path 21, and flows from the opening 35 of the lower end thin portion 33 of the cylindrical portion 3 to the lower end outer peripheral portion of the pleated filter 5. Subsequently, the flow is divided between the pleats and flows upward, and permeates through the porous filtration membrane of the pleat filter 5, and is collected as a purified filtrate in the discharge port 27 through the passage 47, the internal passage 23, and the discharge passage 25. Gels and solid particles are trapped on the outer surface of the filter. On the other hand, dissolved gas and bubbles are discharged from the annular distribution passage 21 of the supply passage 13 to the vent port 31 through the vent passage 41 and the annular vent passage 29. Gas rising from the periphery of the pleat filter 5 is drawn out from the lateral passage 45 to the annular vent passage 29.

本発明の際立った特徴は、プリーツフィルタ5が円筒部3の内面に直接接していること、及び供給液がプリーツフィルタ5の外周下端部から直接プリーツの間に分配供給されることである。これにより流路の濾過装置に占める容積割合が従来よりも遙かに抑制され、濾過装置内の残液量が小さくなることである。またガスベントが円筒部3の内表面のテーパ面8の存在により円滑に行われる。   The distinguishing features of the present invention are that the pleat filter 5 is in direct contact with the inner surface of the cylindrical portion 3 and that the supply liquid is distributed and supplied directly from the lower end of the outer periphery of the pleat filter 5 to the pleats. As a result, the volume ratio of the flow path to the filtration device is much more suppressed than in the past, and the amount of residual liquid in the filtration device is reduced. Further, the gas vent is smoothly performed by the presence of the tapered surface 8 on the inner surface of the cylindrical portion 3.

図4は本発明の変形例を示す。この実施例は、より少量の被濾過液を処理するための濾過装置を示し、多孔コア7、プリーツフィルタ5、及び円筒部3の高さが何れも実施例1のものよりも低くなっている。その他の構成及び動作は実施例1と同様である。   FIG. 4 shows a modification of the present invention. This embodiment shows a filtration device for processing a smaller amount of the liquid to be filtered, and the heights of the porous core 7, the pleat filter 5, and the cylindrical portion 3 are all lower than those of the first embodiment. . Other configurations and operations are the same as those in the first embodiment.

この実施例は被濾過液供給口とガスベント口が濾過装置の側部に配置される例である。
図5において、(a)は正面立断面図、(b)は平面図、(c)は立断面図である。この実施例による濾過装置1は、円筒部3と、円筒部3の内壁に接触した状態で挿入され上下端縁部が液密に封止されている円筒状のプリーツフィルタ5と、前記プリーツフィルタ5の内周面を支持する多数の開口を有する多孔コア7と、前記円筒部3の両端とそれぞれ液密に接合されている下側蓋体9及び上側蓋体11とを含み、円筒部3、上下蓋体9、11は一緒になって液密ハウジング又は液密容器を形成している。以上の構成は実施例1〜2のものと同様である。
In this embodiment, the liquid supply port and the gas vent port are arranged on the side of the filtration device.
5A is a front elevational sectional view, FIG. 5B is a plan view, and FIG. 5C is an elevational sectional view. The filtration device 1 according to this embodiment includes a cylindrical part 3, a cylindrical pleat filter 5 inserted in contact with the inner wall of the cylindrical part 3 and whose upper and lower edges are sealed in a liquid-tight manner, and the pleated filter 5 includes a porous core 7 having a large number of openings that support the inner peripheral surface of the cylinder 5, and a lower lid body 9 and an upper lid body 11 that are liquid-tightly joined to both ends of the cylindrical portion 3. The upper and lower lids 9 and 11 together form a liquid-tight housing or liquid-tight container. The above structure is the same as that of Examples 1-2.

しかし、この例では下側蓋体9には被濾過液供給口はなく、単にハウジングの下端部を閉鎖しているだけである。代わりに被濾過液供給口15は、円筒部3の下側部分に設けられ、被濾過液供給路51に連通している。この供給路51は円筒部3を貫通し内端がプリーツフィルタ5の下側部分の外周面の接線方向に開口している。円筒部3の内周下端部は下側開放端に向けて末広がりに拡大する角度δのテーパ面10が形成されている。これによりプリーツフィルタ5の外周面とテーパ面10との間に被濾過液のための分配路が形成される。この角度δは液体の分配供給に支障がない範囲でできるだけ小さくしそれにより分配路の容積を減じる。例えばδとして5〜20度、例えば10度が使用できる。一方、ベント口31は円筒部3の上側部分に設けられ、ベント通路53に連通している。同様に円筒部3の上端側内周面に沿って角度βのテーパ面8を設けてプリーツフィルタ5の外周面との間にガス収集路を形成し、ベント通路53に連通させる。角度βもガスベントに支障のない範囲例えば5〜20度が使用できる。
また、円筒部3の下端部は実施例1のような被濾過液の分配路を有さず、単に下側蓋体9に溶着されているだけである。
多孔コア7の構造は図3で説明したものと実質的に同一であり、プリーツフィルタ5の構成も同様である。
好ましくは多孔コア7とプリーツフィルタ5の上下端面には、環状及びディスク状プラスチックフィルムをそれぞれ介在させて上下端板との溶着を助けても良い。
However, in this example, the lower lid body 9 does not have a filtrate supply port, and merely closes the lower end of the housing. Instead, the filtrate supply port 15 is provided in the lower part of the cylindrical portion 3 and communicates with the filtrate supply path 51. The supply path 51 passes through the cylindrical portion 3 and has an inner end opened in a tangential direction of the outer peripheral surface of the lower portion of the pleated filter 5. A lower end portion of the inner periphery of the cylindrical portion 3 is formed with a tapered surface 10 having an angle δ that expands toward the lower open end. As a result, a distribution path for the liquid to be filtered is formed between the outer peripheral surface of the pleated filter 5 and the tapered surface 10. This angle δ is made as small as possible without impeding the liquid distribution supply, thereby reducing the volume of the distribution path. For example, 5 to 20 degrees, for example, 10 degrees can be used as δ. On the other hand, the vent port 31 is provided in the upper part of the cylindrical portion 3 and communicates with the vent passage 53. Similarly, a tapered surface 8 having an angle β is provided along the inner peripheral surface on the upper end side of the cylindrical portion 3 to form a gas collection path with the outer peripheral surface of the pleated filter 5 and communicate with the vent passage 53. The angle β can also be used within a range that does not hinder gas venting, for example, 5 to 20 degrees.
Further, the lower end portion of the cylindrical portion 3 does not have the distribution path for the liquid to be filtered as in the first embodiment, and is merely welded to the lower lid body 9.
The structure of the porous core 7 is substantially the same as that described in FIG. 3, and the configuration of the pleated filter 5 is also the same.
Preferably, annular and disc-shaped plastic films may be interposed between the upper and lower end surfaces of the porous core 7 and the pleated filter 5 to assist welding with the upper and lower end plates.

この実施例による濾過装置の動作において、被濾過液体は供給口15から導入され、供給路51によりプリーツフィルタ5の外周部に接線方向から流入し、円筒部の内面のテーパ面10により形成される分配路からプリーツ間に分流して上方に流れ、それにつれてプリーツフィルタ5の多孔質濾過膜を透過し、通路47、内部通路23、及び排出路25を経て排出口27に精製濾液として回収される。ゲル等や固形粒子はフィルタの外面に捕捉される。一方溶存ガスや気泡はプリーツフィルタ5の外周面とテーパ面8との間に形成されたガス収集路に沿って上昇し、ベント通路53を経てベント口31に排出される。
この例でも、従来のような多数の開口を有する外側多孔円筒状支持体及びその周りの通路が存在しないので、液体流路の容積が従来のプリーツフィルタを使用した濾過装置に比べて大幅に減少し、少量濾過の場合に濾過装置内の残留液の量を大幅に減少することが出来る。
In the operation of the filtration device according to this embodiment, the liquid to be filtered is introduced from the supply port 15, flows into the outer peripheral portion of the pleated filter 5 from the tangential direction through the supply path 51, and is formed by the tapered surface 10 on the inner surface of the cylindrical portion. From the distribution path, it is divided between the pleats, flows upward, and permeates through the porous filtration membrane of the pleat filter 5, and is collected as a purified filtrate in the discharge port 27 through the passage 47, the internal passage 23, and the discharge passage 25. . Gels and solid particles are trapped on the outer surface of the filter. On the other hand, dissolved gas and bubbles rise along a gas collection path formed between the outer peripheral surface of the pleated filter 5 and the tapered surface 8, and are discharged to the vent port 31 through the vent passage 53.
Even in this example, since there is no outer porous cylindrical support body having a large number of openings and a passage around it, the volume of the liquid flow path is greatly reduced as compared with a conventional filtration device using a pleated filter. In the case of a small amount of filtration, the amount of residual liquid in the filtration device can be greatly reduced.

図6を参照するに、この実施例は、実施例1(図1〜3)において、被濾過液分配路を実施例3(図5)と同様に形成したものである。この例では図1と同様な被濾過液供給路13に連通する被濾過液分配路は円筒部3の内周面の下側開放端に形成された末広状のテーパ面10により形成される。   Referring to FIG. 6, in this embodiment, the liquid distribution path in Example 1 (FIGS. 1 to 3) is formed in the same manner as in Example 3 (FIG. 5). In this example, the filtrate distribution path communicating with the filtrate supply path 13 similar to that in FIG. 1 is formed by a divergent tapered surface 10 formed at the lower open end of the inner peripheral surface of the cylindrical portion 3.

図1は本発明の実施例1による濾過装置を示し、(a)は正面立断面図、(b)は平面図、及び(c)は底面図である。1A and 1B show a filtering device according to a first embodiment of the present invention, in which FIG. 1A is a front elevational sectional view, FIG. 1B is a plan view, and FIG. 1C is a bottom view. 図2は実施例1による濾過装置の容器の一部を構成するための円筒部を示し、(a)は正面立断面図及び(b)は底面図である。FIG. 2 shows a cylindrical portion for constituting a part of the container of the filtration device according to the first embodiment, wherein (a) is a front elevational sectional view and (b) is a bottom view. 図3は実施例1による濾過装置の多孔コアを示し、(a)は正面立断面図、(b)は正面立面図、(c)図3のc−c断面図、及び(d)は平面図である。FIG. 3 shows a porous core of the filtration device according to Example 1, (a) is a front elevational sectional view, (b) is a front elevational view, (c) a cc sectional view of FIG. It is a top view. 本発明の実施例2による濾過装置を示す正面立断面図である。It is front elevation sectional drawing which shows the filtration apparatus by Example 2 of this invention. 本発明の実施例3により濾過装置を示し、(a)は正面立断面図、(b)は平面図、及び(c)立断面図である。The filtration apparatus is shown by Example 3 of this invention, (a) is front elevation sectional drawing, (b) is a top view, (c) It is elevation sectional drawing. 本発明の実施例4による濾過装置を示す正面立断面図である。It is front elevation sectional drawing which shows the filtration apparatus by Example 4 of this invention.

符号の説明Explanation of symbols

1 濾過装置
3 円筒部
5 プリーツフィルタ
7 多孔コア
8 テーパ面
9 下側蓋体
10 テーパ面
11 上側蓋体
13 被濾過液供給路
15 供給口
17 残液排出口
19 環状部
21 分配路(分配流路)
23 内部通路
25 排出路
27 排出口
29 ベント通路
31 ベント口
33 薄肉部
35 開口
37 下端縁
39 内壁面
41 ベント通路
43 上端縁
45 横通路
51 供給路
53 ベント通路
DESCRIPTION OF SYMBOLS 1 Filtration apparatus 3 Cylindrical part 5 Pleated filter 7 Porous core 8 Tapered surface 9 Lower lid body 10 Tapered surface 11 Upper lid body 13 Filtration liquid supply path 15 Supply port 17 Residual liquid discharge port 19 Annular part 21 Distribution path (distribution flow) Road)
23 internal passage 25 discharge passage 27 discharge port 29 vent passage 31 vent port 33 thin portion 35 opening 37 lower end edge 39 inner wall surface 41 vent passage 43 upper end edge 45 lateral passage 51 supply passage 53 vent passage

Claims (9)

両端が開放された円筒状の内部空間を設けた円筒部と、前記内部空間に前記円筒部の内壁に直接接触した状態で挿入され上下端縁部が液密に封止されている円筒状のプリーツフィルタと、前記プリーツフィルタの内周面を支持する多数の開口を有する多孔コアと、前記円筒部の両端とそれぞれ液密に接合されていて前記円筒部と共に液密ハウジングを構成する下側蓋体及び上側蓋体と、前記円筒部の下端部から前記プリーツフィルタのプリーツ間に通じる被濾過液分配路と、前記分配路に通じる被濾過液供給路と、前記供給路へ接続された被濾過液供給口と、前記多孔コアの内部通路に通じる濾過液排出路と、前記排出路に接続された濾液排出口と、よりなる濾過装置。 A cylindrical portion having a cylindrical inner space with both ends open, and a cylindrical portion that is inserted into the inner space in a state of direct contact with the inner wall of the cylindrical portion and whose upper and lower edge portions are liquid-tightly sealed. A pleat filter, a porous core having a large number of openings for supporting the inner peripheral surface of the pleat filter, and a lower lid that is liquid-tightly joined to both ends of the cylindrical portion and constitutes a liquid-tight housing together with the cylindrical portion A body and an upper lid, a filtered liquid distribution path that communicates between the pleats of the pleat filter from a lower end of the cylindrical section, a filtered liquid supply path that communicates with the distribution path, and a filtered medium connected to the supply path A filtration apparatus comprising: a liquid supply port; a filtrate discharge passage that communicates with an internal passage of the porous core; and a filtrate discharge port connected to the discharge passage. 前記被濾過液供給口は前記下側蓋体に設けられ、前記濾液排出口は前記上側蓋体に設けられている請求項1に記載の濾過装置。 The filtration apparatus according to claim 1, wherein the filtrate supply port is provided in the lower lid body, and the filtrate discharge port is provided in the upper lid body. 前記被濾過液供給口は前記円筒部に設けられ、前記濾液排出口は前記上側蓋体に設けられている請求項1に記載の濾過装置。 The filtration device according to claim 1, wherein the filtrate supply port is provided in the cylindrical portion, and the filtrate discharge port is provided in the upper lid. 前記円筒部の内周面の下端側は前記下側開放端に向けて末広状に拡大するテーパ面を有し、前記分配路が前記テーパ面と前記円筒状プリーツフィルタの外周面とにより画成されている請求項1〜3のいずれかに記載の濾過装置。 The lower end side of the inner peripheral surface of the cylindrical portion has a tapered surface that expands toward the lower open end, and the distribution path is defined by the tapered surface and the outer peripheral surface of the cylindrical pleated filter. The filtration device according to any one of claims 1 to 3. 前記下側蓋体は前記円筒部の内径よりも大きい内径を有する円環部を備えたカップ状部材であり、前記円筒部の下端外周は前記円環部に間隙を持って重畳する薄肉部を有し、該薄肉部には貫通孔が形成され、前記分配路が前記間隙と前記貫通孔とにより構成されている請求項1〜3のいずれかに記載の濾過装置。 The lower lid is a cup-shaped member having an annular part having an inner diameter larger than the inner diameter of the cylindrical part, and the outer periphery of the lower end of the cylindrical part has a thin part that overlaps the annular part with a gap. The filtration device according to claim 1, wherein a through hole is formed in the thin portion, and the distribution path is configured by the gap and the through hole. 前記プリーツフィルタの底部端縁部と前記多孔コアの底面と前記円筒部の底面は一枚の円板状プラスチックシートで封着されている請求項1〜5のいずれかに記載の濾過装置。 The filtration device according to any one of claims 1 to 5, wherein a bottom edge of the pleated filter, a bottom surface of the porous core, and a bottom surface of the cylindrical portion are sealed with a single disc-shaped plastic sheet. 前記多孔コアの内部通路及び多孔通路が占める容積は多孔コアの全体の容積の50%以下である請求項1〜6のいずれかに記載の濾過装置。 The filtration apparatus according to any one of claims 1 to 6, wherein the volume occupied by the internal passage and the porous passage of the porous core is 50% or less of the entire volume of the porous core. 前記円筒部の内周面の上端側は前記上側開放端に向けて末広状に拡大するテーパ面を有し、該テーパ面と前記円筒状プリーツフィルタの外周面とによりガス収集路を画成し、前記円筒部または前記上側蓋体にガスベント通路と、それに連絡するガスベント口とを設けた請求項1〜7のいずれかに記載の濾過装置。 The upper end side of the inner peripheral surface of the cylindrical portion has a tapered surface that expands toward the upper open end, and a gas collection path is defined by the tapered surface and the outer peripheral surface of the cylindrical pleated filter. The filtration device according to any one of claims 1 to 7, wherein a gas vent passage and a gas vent port communicating with the cylindrical portion or the upper lid are provided. 前記円筒部に前記被濾過液供給通路から前記ガスベント通路に接続する他のガスベント通路を設けた請求項8に記載の濾過装置。 The filtration device according to claim 8, wherein another gas vent passage connected to the gas vent passage from the filtrate supply passage is provided in the cylindrical portion.
JP2003413082A 2003-12-11 2003-12-11 Filtration device having housing-integrated pleat filter Expired - Fee Related JP4503276B2 (en)

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JP2009541031A (en) * 2006-06-21 2009-11-26 インテグリス・インコーポレーテッド System and method for liquid filtration with reduced hold-up volume
CN116871097A (en) * 2023-09-07 2023-10-13 杭州智和净化科技有限公司 Upper air inlet dry type paint mist collecting box

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CN116871097B (en) * 2023-09-07 2023-11-21 杭州智和净化科技有限公司 Upper air inlet dry type paint mist collecting box

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