JPS61149218A - Filter element and preparation thereof - Google Patents

Filter element and preparation thereof

Info

Publication number
JPS61149218A
JPS61149218A JP59279291A JP27929184A JPS61149218A JP S61149218 A JPS61149218 A JP S61149218A JP 59279291 A JP59279291 A JP 59279291A JP 27929184 A JP27929184 A JP 27929184A JP S61149218 A JPS61149218 A JP S61149218A
Authority
JP
Japan
Prior art keywords
filter
fluororesin
item
cap
fused
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP59279291A
Other languages
Japanese (ja)
Other versions
JPH0696101B2 (en
Inventor
Tokuya Miyaki
宮木 徳彌
Akihisa Inoue
明久 井上
Taisuke Otsubo
大坪 泰輔
Yoshihiro Hori
堀 芳廣
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.)
Kurabo Industries Ltd
Kurashiki Spinning Co Ltd
Original Assignee
Kurabo Industries Ltd
Kurashiki Spinning Co Ltd
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 Kurabo Industries Ltd, Kurashiki Spinning Co Ltd filed Critical Kurabo Industries Ltd
Priority to JP59279291A priority Critical patent/JPH0696101B2/en
Priority to EP85116390A priority patent/EP0187358A3/en
Publication of JPS61149218A publication Critical patent/JPS61149218A/en
Priority to US07/077,031 priority patent/US5114508A/en
Publication of JPH0696101B2 publication Critical patent/JPH0696101B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a filter having no problem in chemical resistance and the elution of a metal and capable of withstanding high pressure, by forming a filter membrane made of a fluorocarbon resin into a cylindrical form while folding the same in a plated state and connecting caps made of a fluorocarbon resin to both end parts of the formed cylinder in a liquid-tight state by fusion bonding. CONSTITUTION:A filter membrane made of a tetrafluoroethylene resin having a thickness of 50-200mum and a pore size of 0.01-10mum is folded in a pleated state, in such a state both side surfaces thereof are held between reticulated supports made of a fluorocarbon resin, to form a cylindrical shape. Each end parts of this filter material 3 is engaged with a cap 7 and gradually inserted in the fluorocarbon resin for the end cap, which is melted under heating at temp. of the m.p. of the end cap or more in an end cap mold, to perform the integral fusion bonding of said end part 4 and the end cap 7. After the filter material 3 is sedimented in the resin up to a depth of 1-10mm, the mold is cooled.

Description

【発明の詳細な説明】 ti;♀町)、(7:λ哩鼾り四ヨ2〉」悶f]本発明
は全体がフッ素樹脂から形成されているフィルターエレ
メントおよびその製法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filter element entirely made of fluororesin and a method for manufacturing the same.

側来嫁−肛 近年、膜分離技術をベースとして空気、ガス、水、薬品
等の超清浄化技術が著るしく進展し、食品分野、半導体
分野等の各分野で11広く利用されパている。特に半導
体集積回路製造プロセスにおける微細加工技術分野で必
要とされる薬剤の清浄化技術については、空気、ガス、
水等の清浄化技術に比較して技術的対応か遅れており、
最近特に注目されている。製品の歩留り向上、高品質化
をはかる」―で、薬剤の高純度化が求められているにも
かかわらず、半導体集積回路製造メーカーおよび薬剤供
給メーカー共にその対応が遅れているのは、金属溶出の
少ない、耐薬品性の良いフィルター製品の開発が遅れて
いることが主要因のろつとしてあげられている。現在、
上記要求を満たずものとして、全フッ素樹脂製のフィル
ターが求められており、平膜の多段方式およびチューブ
ラ一方式の膜フィルターが開発されているが、有効シ濾
過面積が少なく、y過流景が少ないため、高粘度薬剤の
濾過および人里処理に問題があり、市場の要求を満たず
に至っていない。
In recent years, ultra-purification technology for air, gas, water, chemicals, etc. based on membrane separation technology has made remarkable progress and is now widely used in various fields such as food and semiconductors. . In particular, regarding cleaning technology for chemicals required in the field of microfabrication technology in the semiconductor integrated circuit manufacturing process,
Compared to water purification technology, technical response is delayed,
It has received particular attention recently. Although there is a demand for highly purified chemicals in order to improve product yield and quality, semiconductor integrated circuit manufacturers and drug supply manufacturers have been slow to respond to this demand due to metal leaching. The main reason for this is that the development of filter products with low chemical resistance and good chemical resistance has been delayed. the current,
In order to meet the above requirements, there is a need for filters made of all-fluoropolymer resin, and flat membrane multi-stage and tubular one-type membrane filters have been developed, but the effective filtration area is small and As a result, there are problems in the filtration and human processing of high viscosity drugs, which do not meet market requirements.

一方、フッ素樹脂の膜を用いたプリーツ状フィルターエ
レメントが開発されている。これは有効濾過面積が大き
く、耐薬品性にもかなり優れているが、フッ素樹脂の接
着が本来極めて困難であることから、フィルター膜以外
はフッ素以外の材料が使用されており、これが耐薬品性
や金属溶出等のネックとなり、満足すべき製品は得られ
ていない。
On the other hand, pleated filter elements using fluororesin membranes have been developed. This has a large effective filtration area and excellent chemical resistance, but since adhesion of fluororesin is inherently extremely difficult, materials other than fluorine are used except for the filter membrane, and this is due to its chemical resistance. This causes bottlenecks such as metal leaching and metal elution, and it is not possible to obtain a satisfactory product.

%F’Q(−解決しようとする問題点 上記半導体集積回路製造プロセスにおいて採用されるフ
ィルターは 0.01−10μと云った非常に微小な孔
を必要とし、フィルター膜自体は極めて強度が弱く、フ
ィルター製造時に苛酷な条件を採用することはできず、
かつまたフィルターエレメント各部材の接着は、単に接
着しているのみでは不可であり、完全なシール状態で密
着している必要がある。
%F'Q(-Problem to be solved The filters used in the above semiconductor integrated circuit manufacturing process require extremely small pores of 0.01-10μ, and the filter membrane itself has extremely low strength. Harsh conditions cannot be used when manufacturing filters,
Moreover, the adhesion of each member of the filter element cannot be achieved simply by adhesion, but must be in close contact with each other in a completely sealed state.

本発明はこの様な要請を満足する全フッ素樹脂製フィル
ターエレメントおよびその製造法を提供する。
The present invention provides a filter element made of all fluororesin and a method for manufacturing the same that satisfies such requirements.

即ち、本発明は第1図および第2図に示すごとくフッ素
樹脂製めフィルター膜(1)の両面に熱可塑性フッ素樹
脂製ネット状支持体(2)を重ねたザンドイッチ状シー
トをプリーツ状に折り曲げて円筒状にし、その両側縁部
を液密に融着した円筒形プリーツ状濾過材(3)、該シ
濾過材の両端部(4)の中央開口部(5)を残して該両
端部と液密に融着されている所定の形状を有するフッ素
樹脂製キャップ(7)(第1図では理解を容易にするた
め別々に示している)を備えた全フッ素樹脂製フィルタ
ーエレメントおよびその製法を提供する。
That is, as shown in FIGS. 1 and 2, the present invention involves folding a sandwich-like sheet in which a fluororesin filter membrane (1) is laminated with a thermoplastic fluororesin net-like support (2) on both sides into pleats. A cylindrical pleated filter material (3) is made into a cylindrical shape, and both edges of the filter material are liquid-tightly fused. An all-fluoropolymer filter element equipped with a fluororesin cap (7) having a predetermined shape that is fluid-tightly fused (separately shown in Figure 1 for ease of understanding) and its manufacturing method. provide.

本発明に用いるフィルター膜(1)は、フッ素樹脂製、
特に四フッ化エチレン樹脂(P T F E)製であり
、これは多孔性フッ素樹脂製補強材でラミネートされた
ものであってよく、この膜自体はY過膜として公知のも
のである。膜厚、孔径は処理液の種類、シ濾過目的によ
って任意に選定すればよいが通常、膜厚50〜200μ
、孔径0.01−10μのものを使用する。この膜は機
械的強度が弱く、またシ濾過圧によって容易に変形する
ため、プリーツ状を保持するため、両側面にフッ素樹脂
製ネット状支持体を重ねてはさみサンドイッチ状にして
使用する。このフィルター膜として、例えば特開昭58
−14919号公報に記載されているごとき、ガラス繊
維表面にフルオロエチレンポリマーを融着させたものは
、強度的には向上するが微小孔径のものが得られず、耐
薬品性、溶出金属等の点で十分でなく、本発明の目的に
そぐわないため使用できない。また、フィルター膜とキ
ャップの融着は高い挿入圧により行なわれている。この
様な挿入圧は、フィルター膜が全フッ素樹脂製の場合は
、フィルター膜が変形し、液密な融着ができないため採
用し得ない。
The filter membrane (1) used in the present invention is made of fluororesin,
In particular, it is made of polytetrafluoroethylene resin (PTFE), which may be laminated with a porous fluoropolymer reinforcement, and the membrane itself is known as a Y membrane. The membrane thickness and pore size can be arbitrarily selected depending on the type of processing liquid and the purpose of filtration, but usually the membrane thickness is 50 to 200μ.
, with a pore diameter of 0.01-10μ. Since this membrane has low mechanical strength and is easily deformed by filtration pressure, it is used in the form of a sandwich with fluororesin net-like supports placed on both sides to maintain its pleated shape. As this filter membrane, for example, JP-A-58
-14919, in which fluoroethylene polymer is fused to the surface of glass fibers, improves strength but does not have micropores, and has poor chemical resistance and eluted metals. It cannot be used because it is insufficient in this respect and does not meet the purpose of the present invention. In addition, the filter membrane and the cap are fused together using high insertion pressure. Such an insertion pressure cannot be used if the filter membrane is made of all-fluororesin because the filter membrane will be deformed and a liquid-tight fusion cannot be achieved.

フッ素樹脂製フィルター膜は、熱可塑性フッ素樹脂製ネ
ット支持体(2)でサンドイッチ状にはさむ。これは、
フィルター膜が全面積にわたって濾過に有効に働くため
のスペーサーであると同時にシ濾過圧による膜の変形を
防ぐ他、ネット支持体自体が融着材として作用するため
、膜側縁部の融着を完全にするために重要な役割を有す
る。フィルター膜の素材であるフッ素樹脂、特にPTF
Eは熱融着が非常に困難であり、模の強度も極めて弱い
ためにその両端部(4)をフッ素樹脂で液密に融着する
ことは困難であり、それか全フッ素樹脂製円筒状のプリ
ーツ状フィルターニレメン)・が、従来提供されていな
かった原因のろつと考えられる。
The fluororesin filter membrane is sandwiched between thermoplastic fluororesin net supports (2). this is,
It acts as a spacer for the filter membrane to work effectively over its entire area for filtration, and at the same time prevents the membrane from deforming due to filtration pressure.The net support itself acts as a fusing material, which prevents fusing at the side edges of the membrane. It has an important role to complete. Fluororesin, especially PTF, which is the material for filter membranes
E is very difficult to heat-seal and the strength of the pattern is extremely weak, so it is difficult to liquid-tightly fuse both ends (4) with fluororesin, or a cylindrical shape made of all-fluororesin. This is thought to be the reason why pleated filters (elmmen) were not provided in the past.

ネット支持体(2)の素材は四フッ化エチレンーパーフ
ルオロアルキルビニルエーテル共重合樹脂(P F A
)、四フッ化エチレンー六フッ化プロピレン共重合樹脂
(FEP)、エチレン−四フッ化エチレン共重合樹脂(
ETFE)、三フッ化塩化エチレン樹脂(PCTFE)
、エチレン−三フッ化塩化エチレノ共重合樹1IiiT
(ECTFE)、フヅ化ビニリデン樹脂(PVdP) 
、フッ化ビニル樹脂(PVF)、四フッ化エチレンー六
フッ化プロピレン−パーフルオロアルキルビニルエーテ
ル共重合樹脂(EPE)等の熱可塑性フッ素樹脂、含フ
ッ素熱可塑性エラストマーおよびその他の含フツ素共重
合樹脂が使用される。特に好ましくは、耐薬品性、耐熱
性の点でPFA、FEPSEPE、ET−FE、PCT
FE、ECTFE、特にPPA、FEP、EPEである
The material of the net support (2) is tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer resin (PFA
), tetrafluoroethylene-hexafluoropropylene copolymer resin (FEP), ethylene-tetrafluoroethylene copolymer resin (
ETFE), trifluorochloroethylene resin (PCTFE)
, ethylene-trifluorochloride ethylene copolymer tree 1IiiiT
(ECTFE), polyvinylidene resin (PVdP)
, thermoplastic fluororesins such as vinyl fluoride resin (PVF), tetrafluoroethylene-hexafluoropropylene-perfluoroalkyl vinyl ether copolymer resin (EPE), fluorine-containing thermoplastic elastomers, and other fluorine-containing copolymer resins. used. Particularly preferable are PFA, FEPSEPE, ET-FE, and PCT in terms of chemical resistance and heat resistance.
FE, ECTFE, especially PPA, FEP, EPE.

ネット支持体はフッ素樹脂繊維の平織布、融着不織布、
成形ネット、編物、パンチングシート等多孔性の素材で
あって、プリーツ状に折り曲げることのできる程度の可
撓性とシ濾過圧によって容易に形崩れしない程度の剛性
を有するものが望ましく、そのため、通常厚さ01〜1
0H1孔面積0.1〜5尻尻重程度のものを用いる。
The net support is plain woven fabric of fluororesin fiber, fused nonwoven fabric,
It is desirable to use porous materials such as molded nets, knitted fabrics, and punched sheets that are flexible enough to be folded into pleats and rigid enough not to easily lose their shape due to filtration pressure. Thickness 01~1
Use one with a 0H1 hole area of 0.1 to 5 butts.

フィルター膜はネット支持体でサンドイッチ状にはさみ
、これをプリーツ状に折り曲げて円筒状にし、両側縁部
を例えば、通常のインパルスシーラー等で液密に融着す
る。フィルター膜とネット支持体は多層構造をとっても
よい(例えば支持体−膜一支持体−膜−支持体)。
The filter membrane is sandwiched between net supports, folded into pleats to form a cylindrical shape, and both side edges are liquid-tightly fused using, for example, an ordinary impulse sealer. The filter membrane and the net support may have a multilayer structure (eg support-membrane-support-membrane-support).

両側縁部(8)の融着は第2図に示すごとくネット支持
体のろ側縁部を長くし、これを他の側縁部の外側にかぶ
せて一体に融着してもよく、第3図に示すごとく、両側
縁部間に熱可塑性フッ素樹脂シールテープ(9)をはさ
んで融着してもよい。また第4図に示すごとく熱可塑性
フン素樹脂製シールカバー(10)をかぶせて融着して
もよい。この様なシールテープやシールカバーとしては
耐薬品性と融着性に優れたPFASFEP、EPF、E
TFE、PCTFESECTr’E、特にPFA。
The both side edges (8) may be fused together by elongating the lower side edge of the net support and covering the outside of the other side edge and fusing them together as shown in Figure 2. As shown in Figure 3, a thermoplastic fluororesin sealing tape (9) may be sandwiched and fused between both side edges. Alternatively, as shown in FIG. 4, a seal cover (10) made of thermoplastic fluororesin may be covered and fused. For such seal tapes and seal covers, PFASFEP, EPF, and E, which have excellent chemical resistance and fusion properties, are used.
TFE, PCTFESECTTr'E, especially PFA.

FEP、EPE等か好ましい。第3図および第4図に示
す態様ではシールの耐圧性が向上する。
FEP, EPE, etc. are preferred. In the embodiments shown in FIGS. 3 and 4, the pressure resistance of the seal is improved.

以上のごとくして得られた濾過祠はその両端部(4)を
、液通過用開口部(5)を残して熱可塑性フッ素樹脂製
キャップ中に埋入融着させる。プリーツ状フィルターの
端部を溶融フッ素樹脂の入ったキャップ用金型中に急速
に押込もと、プリーツが座屈しプリーツ襞間に樹脂が浸
入しない。即ち、フィルター膜がフッ素樹脂中に埋入し
た状態にならない。従って不完全なシールしか得られず
耐圧性も不十分となる。
Both ends (4) of the filter cage obtained as described above are embedded and fused in a cap made of thermoplastic fluororesin, leaving openings (5) for liquid passage. When the ends of the pleated filter are rapidly pushed into a cap mold containing molten fluororesin, the pleats buckle and the resin does not penetrate between the pleat folds. That is, the filter membrane is not embedded in the fluororesin. Therefore, only an incomplete seal is obtained and the pressure resistance is insufficient.

本発明では−1−記濾過祠端部をキャップおよび所望な
らば、後述する多孔性中空円筒状コア材(シ戸液の取出
流路)と嵌合し、これをエンドキャップ用金型中でキャ
ップの溶融温度以」−に加熱し、溶融したエンドキャッ
プ用フッ素樹脂中に、該温度を維持したまま上記シ濾過
材端部を徐々に挿入し一体に融着させる。その際、濾過
材はエンドキャップが十分溶融するまでホルダーでゆる
く保持し、エンドキャップが十分溶融した段階でわずか
な荷重、例えば1〜100 g7CM″をかけ、加熱を
続けながら溶融したエンドキャップ中に徐々に沈降させ
る。押し込みに要する時間はキャップに用いる樹脂の溶
融粘度により異なるが、深さ11IIm当たり30秒以
」二、より好ましくは1分以上とする。
In the present invention, the end portion of the filtration house described in -1- is fitted with a cap and, if desired, a porous hollow cylindrical core material (a flow path for taking out the liquid), which will be described later, and this is placed in a mold for the end cap. The end portion of the filter material is gradually inserted into the melted fluororesin for the end cap while maintaining the temperature and fused together. At that time, the filter material is held loosely in a holder until the end cap is sufficiently melted, and when the end cap is sufficiently melted, a slight load, e.g. The cap is allowed to settle gradually.The time required for pushing the cap varies depending on the melt viscosity of the resin used for the cap, but is preferably at least 30 seconds per 11 II m depth, and more preferably at least 1 minute.

シ濾過材が所定の深さ、例えば1〜10!!I11.エ
ンドキャップの樹脂内に沈降した後、金型を冷却する。
The filter material has a predetermined depth, for example 1 to 10! ! I11. After settling into the resin of the end cap, the mold is cooled.

また一定速度で一過材端部を押し込んでもよい。Alternatively, the end portion of the temporary material may be pushed in at a constant speed.

押込速度は0.1〜6mi/分、より好ましくは0゜2
〜2mm1分である。この方法により、一過材端部のフ
ィルター膜の襞間にエンドキャップ樹脂が浸入し液密に
融着される。
The pushing speed is 0.1 to 6 mi/min, more preferably 0°2
~2 mm 1 minute. By this method, the end cap resin infiltrates between the folds of the filter membrane at the end of the temporary material and is fused in a liquid-tight manner.

また別の方法として、エンドキャップを金型中で予め溶
融し、これにシ濾過材端部を徐々に挿入することによっ
て融着させてもよい。その際、y過材端部の挿入により
エンドキャップの温度が低下した場合は、該キャップが
再び溶融温度に達するのを待って、一過材端部を前記速
度で抑圧挿入してもよく、また前述のごとく、一定の荷
重をかけてシ濾過材端部を押し込んでもよい。両端部に
融着させるキャップは両者共、中央開口部(6)を有し
ていてもよく、−・方が中央開口部を有し、他方が中央
開口部を有さないキャップであ−、でもよい。
Alternatively, the end cap may be pre-melted in a mold and the end cap may be fused by gradually inserting the end of the filter material therein. At this time, if the temperature of the end cap decreases due to the insertion of the end of the y-over material, wait until the cap reaches the melting temperature again, and then press and insert the end of the y-over material at the above speed, Further, as described above, the end portion of the filter material may be pushed in by applying a certain load. The caps to be fused to both ends may both have a central opening (6), one having a central opening and the other having no central opening; But that's fine.

キャップ底部の厚さは1.5mm以上、好ましくは3〜
8rlll+である。
The thickness of the bottom of the cap is 1.5mm or more, preferably 3~
It is 8rllll+.

キャップに使用するフッ素樹脂は前述のフッ素樹脂のい
ずれも使用し得るが、耐薬品性の点で、FEPlPFA
、EPElETFESPCTFEまたはECTFE、特
にFET’、 PFA、EPEが望ましい。PTFEは
、融着性に劣り、かつ溶融時の粘度が高い1こめ、一過
材端部を挿入し難く好ましくlよい。
As the fluororesin used for the cap, any of the aforementioned fluororesins can be used, but FEPlPFA is preferred in terms of chemical resistance.
, EPElETFESPCTFE or ECTFE, especially FET', PFA, EPE. PTFE is preferable because it has poor fusion properties and high viscosity when melted, and it is difficult to insert the ends of the temporary material.

前述の多孔性中空円筒状コア材は必須ではないが、外部
からシ濾過圧がかかる場合、−過材を保護するために用
いるのが好ましい。
Although the aforementioned porous hollow cylindrical core material is not essential, it is preferably used to protect the filtration material when filtration pressure is applied from the outside.

コア材も前述のフッ素樹脂のいずれも使用し得るが、耐
薬品性と耐熱性の点でPTFE、FEP。
Although any of the aforementioned fluororesins can be used for the core material, PTFE and FEP are preferred in terms of chemical resistance and heat resistance.

PFA、EPE、ETFE、PCTPESECTFE、
特にFEP、PPA、EPEが好ましく、特に端部シー
ルに使用した樹脂と同じものが好ましい。
PFA, EPE, ETFE, PCTPESECTFE,
Particularly preferred are FEP, PPA, and EPE, and particularly preferred is the same resin as used for the end seal.

本発明フィルターエレメントは所望ならばフッ素樹脂製
シリンダー状保護外筒を)濾過材の周囲にかぶせてもよ
い。この保護外筒は処理液が通過するよう多数の孔を有
するパネルから作ったものでよく、必らずしもフィルタ
ーエレメントと一体に融着させる必要はない。キャップ
の内側にはめ込んでもよく、外側に挿入してもよい。
If desired, the filter element of the present invention may be covered with a cylindrical protective sleeve made of fluororesin around the filter medium. The protective sleeve may be made from a panel with a number of holes for passage of the processing liquid and does not necessarily need to be fused together with the filter element. It may be fitted inside the cap or inserted outside.

保護外筒は用途によってはステンレス、ハステロイC1
X−アロイ、H−アロイ、ジュラニッケル等の材料を用
いてもよく、フッ素樹脂製とするにはフッ素樹脂、例え
ばPTFE、FEP、 EPESPFA、 ETT?4
1PCTFE、ECTFE。
The protective outer cylinder is made of stainless steel or Hastelloy C1 depending on the application.
Materials such as X-alloy, H-alloy, Dura nickel, etc. may be used, and to make it made of fluororesin, fluororesin, such as PTFE, FEP, EPESPFA, ETT? 4
1PCTFE, ECTFE.

特にPTr’ES1?EP、 El”E、PFA等を用
いればよい。
Especially PTr'ES1? EP, El"E, PFA, etc. may be used.

本発明フィルターエレメントは全体がフッ素樹脂製であ
り、耐薬品性、耐熱性に優れ、金属溶出等の問題がない
上、0.01μ〜10μ と云った非常に小さい粒子を
含む処理液のろ過が可能であり、従って半導体集積回路
製造工程等で使用される薬剤等の精製に特に有用である
The filter element of the present invention is entirely made of fluororesin, has excellent chemical resistance and heat resistance, does not have problems such as metal elution, and can filter processing liquids containing very small particles of 0.01μ to 10μ. Therefore, it is particularly useful for purifying drugs and the like used in semiconductor integrated circuit manufacturing processes.

寒覧鯉 PTFEフィルター膜(厚さ100μ、平均孔径0.1
μ、面積250X2000Im”)の上下4二EPEネ
ット支持体(平均厚さ 0,4龍、孔面積率50%、面
積250X2000ii’)を重ねサンドイッチ状にし
、これらのシートを波付けして襞数70のプリーツを成
形する。
Kanrankoi PTFE filter membrane (thickness 100μ, average pore diameter 0.1
42 upper and lower EPE net supports (average thickness 0.4mm, pore area ratio 50%, area 250x2000ii') with a diameter of 250x2000Im") were layered to form a sandwich, and these sheets were corrugated to form a fold with 70 folds. form the pleats.

プリーツを円筒状にし、両側縁部を重ねEPEフィルム
(巾5■、長さ250肩m1厚さ50μ)をその間には
さみ(第3図)、これを市販のインパルスシーラーで熱
シールし、円筒形プリーツ状Y過材を得た。この熱融着
部は完全に液密にシールされている。
Make the pleats into a cylinder, overlap the edges on both sides, sandwich an EPE film (width 5cm, length 250cm, thickness 50μ) between them (Fig. 3), heat seal this with a commercially available impulse sealer, and make it into a cylindrical shape. A pleated Y overlay material was obtained. This heat-sealed portion is completely liquid-tightly sealed.

次に上記Y過材の内孔にPFA製多孔性中空円筒状コア
材(外径36IIIri、内径30mm、長さ240M
R)を挿入し、一端を揃ろえてこれらと嵌合するEPE
製エンドキャップ(底の厚さ6■)を嵌め込み、これら
を金型に入れて加熱する。この際、前記濾過材はホルダ
ーでゆるく把持する。320°Cで20分加熱後、前記
−過材の上に200gの荷重をのせて一過材の下端部を
エンドキャップの溶融樹脂中にゆっくり浸入させる。約
10分で前記シ濾過材が5■降下したところで荷重を除
き、後冷却する。
Next, a porous hollow cylindrical core material made of PFA (outer diameter 36IIIri, inner diameter 30mm, length 240M) was inserted into the inner hole of the Y filter material.
R), align one end, and fit these EPEs.
These end caps (bottom thickness: 6 mm) are fitted, and these are placed in a mold and heated. At this time, the filter medium is held loosely by a holder. After heating at 320° C. for 20 minutes, a load of 200 g is placed on the sieve material, and the lower end of the sieve material is slowly immersed into the molten resin of the end cap. After about 10 minutes, when the filter material has dropped 5 cm, the load is removed and the filter is cooled down.

溶融樹脂が固化した後金型から取り出すとy過材端部の
フィルター膜の襞間にエンドキャップの樹脂が浸入し、
強固に融着していた。他端も同じ操作をくり返す。
When the molten resin is removed from the mold after it has solidified, the resin from the end cap will seep into the folds of the filter membrane at the end of the overfill material.
It was firmly fused. Repeat the same operation on the other end.

得られたフィルターエレメントはプリーツ側縁部、端部
およびキャップ部とも液密に強固に密着しており、リー
クも全くなく、5kg/cm”以上の高圧に耐え得るも
のであった。
The obtained filter element was in fluid tight contact with the pleat side edges, ends, and cap, had no leaks, and was able to withstand a high pressure of 5 kg/cm'' or more.

発明の効果 本発明のフィルターエレメントは素材が全てフッ素樹脂
で構成されており、耐薬品性、金属溶出等の問題がない
上、従来融着が困難とされていたフッ素樹脂を特殊な方
法によって液密に融着している。
Effects of the Invention The filter element of the present invention is made entirely of fluororesin, so there are no problems such as chemical resistance or metal elution, and the fluororesin, which was conventionally considered difficult to fuse, can be melted using a special method. It is tightly fused.

得られたフィルターエレメントはプリーツ側縁部、端部
およびキャップ部ども、液密に強固に密着しており、リ
ークは全くなく、しかも高圧に耐え得るものであった。
The obtained filter element had pleat side edges, ends, and cap portions that were tightly and liquid-tightly adhered to each other, had no leakage, and was able to withstand high pressure.

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

第1図は本発明フィルターエレメント (但し一過材と
キャップとは別々に分けて示しである)の模式図、第2
図〜第4図はプリーツ側縁部の融着様式を示す模式図で
ある。 (1)・フィルター膜、 (2)・・・ネット支持体、
(3)・−過材、    (4)・・・シ濾過材端部、
(5)・・・y過材端部の中央開口部、(6)・キャッ
プ中央開口部、 (7)・・・キャップ、(8)シ濾過
材側縁部、 (9)・・シールテープ、(lO)・シー
ルカバー。 /“
Figure 1 is a schematic diagram of the filter element of the present invention (however, the temporary material and the cap are shown separately);
Figures 4 to 4 are schematic diagrams showing the manner in which pleat side edges are fused. (1) Filter membrane, (2) Net support,
(3) - filter material, (4)... end of filter material,
(5)...Central opening at the end of the filter material, (6).Central opening of the cap, (7)...Cap, (8) Side edge of the filter material, (9)...Seal tape , (lO)・Seal cover. /“

Claims (1)

【特許請求の範囲】 1、フッ素樹脂製フィルター膜の両面に熱可塑性フッ素
樹脂製ネット支持体を重ねたサンドイッチ状シートをプ
リーツ状に折り曲げて円筒状にし、その両側縁部を液密
に融着し、円筒状にしたろ過材、該ろ過材の両端部の中
央開口部を残して該両端部と液密に融着されているフッ
素樹脂製キャップを備えた全フッ素樹脂製フィルターエ
レメント。 2、フィルター膜が四フッ化エチレン樹脂製である第1
項記載のフィルターエレメント。 3、フィルター膜の微細孔の径が0.01〜10μであ
る第10項記載のフィルターエレメント。 4、ネット支持体がPFA、FEP、EPE、ETFE
、PCTFEまたはECTFE製である第1項記載のフ
ィルターエレメント。 5、両側縁部をEPE、PFA、FEP製シールテープ
をはさんで融着した第1項記載のフィルターエレメント
。 6、キャップがFEP、PFA、EPE、ETFE、P
CTFEまたはECTFEである第1項記載のフィルタ
ーエレメント。 7、エレメントがさらにフッ素樹脂製のろ過材支持用コ
ア材を備えた第1項記載のフィルターエレメント。 8、エレメントがさらにフッ素樹脂製の保護外筒を備え
た第1項記載のフィルターエレメント。 9、フッ素樹脂製フィルター膜の両面に熱可塑性フッ素
樹脂製ネット支持体を重ねてプリーツ状に成形し、該プ
リーツを円筒状にして、隣接する両側縁部を液密に融着
し、得られた円筒形プリーツ状フィルターの端部を所望
によりフッ素樹脂製ろ過材支持用コア材と嵌合し、溶融
温度以上に保持した溶融フッ素樹脂製キャップ中に徐々
に挿入し、加熱融着させることを特徴とする全フッ素樹
脂製フィルターエレメントの製法。 10、フィルター膜が四フッ化エチレン樹脂製である第
9項記載の製法。 11、プリーツ状フィルター側縁部の融着に際し、側縁
部間に熱可塑性フッ素樹脂製融着用テープを挿入して行
なう第9項記載の製法。 12、ネット支持体がPFA、FEP、EPE、ETF
E、PCTFEまたはECTFEである第9項記載の製
法。 13、キャップがFEP、PFA、EPE、ETFE、
PCTFEまたはECTFEである第9項記載の製法。 14、キャップの少なくとも一方が中央開口部を有する
第9項記載の製法。 15、円筒状にしたプリーツ状フィルターの端部をキャ
ップ中に押し込むに際し、1分以上かけて行なう第9項
記載の方法。
[Claims] 1. A sandwich-like sheet in which a thermoplastic fluororesin net support is layered on both sides of a fluororesin filter membrane is folded into a cylindrical shape by pleating, and the edges on both sides are fused in a liquid-tight manner. An all-fluororesin filter element comprising a cylindrical filter medium and a fluororesin cap liquid-tightly fused to both ends of the filter medium, leaving a central opening at both ends. 2. The first filter membrane is made of tetrafluoroethylene resin
Filter element as described in section. 3. The filter element according to item 10, wherein the diameter of the micropores of the filter membrane is 0.01 to 10μ. 4. Net support is PFA, FEP, EPE, ETFE
, PCTFE or ECTFE. 5. The filter element according to item 1, in which both side edges are fused with sealing tape made of EPE, PFA, or FEP. 6. Cap is FEP, PFA, EPE, ETFE, P
2. The filter element according to claim 1, which is CTFE or ECTFE. 7. The filter element according to item 1, wherein the element further includes a core material for supporting the filter material made of fluororesin. 8. The filter element according to item 1, wherein the element further includes a protective outer cylinder made of fluororesin. 9. Thermoplastic fluororesin net supports are layered on both sides of a fluororesin filter membrane and formed into a pleat shape, the pleats are made into a cylindrical shape, and adjacent both side edges are fused in a liquid-tight manner. If desired, the end of the cylindrical pleated filter is fitted with a core material made of fluororesin for supporting the filtration material, and gradually inserted into a cap made of molten fluororesin kept at a temperature higher than the melting temperature, and then heated and fused. A unique manufacturing method for filter elements made of all-fluorine resin. 10. The method according to item 9, wherein the filter membrane is made of tetrafluoroethylene resin. 11. The manufacturing method according to item 9, wherein when fusing the side edges of the pleated filter, a thermoplastic fluororesin fusing tape is inserted between the side edges. 12. Net support is PFA, FEP, EPE, ETF
E, the method according to item 9, which is PCTFE or ECTFE. 13. The cap is FEP, PFA, EPE, ETFE,
The method according to item 9, which is PCTFE or ECTFE. 14. The manufacturing method according to item 9, wherein at least one of the caps has a central opening. 15. The method according to item 9, wherein the end of the cylindrical pleated filter is pushed into the cap for one minute or more.
JP59279291A 1984-12-24 1984-12-24 Filter element and its manufacturing method Expired - Fee Related JPH0696101B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP59279291A JPH0696101B2 (en) 1984-12-24 1984-12-24 Filter element and its manufacturing method
EP85116390A EP0187358A3 (en) 1984-12-24 1985-12-20 Filter element and its production
US07/077,031 US5114508A (en) 1984-12-24 1987-07-21 Filter element and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59279291A JPH0696101B2 (en) 1984-12-24 1984-12-24 Filter element and its manufacturing method

Publications (2)

Publication Number Publication Date
JPS61149218A true JPS61149218A (en) 1986-07-07
JPH0696101B2 JPH0696101B2 (en) 1994-11-30

Family

ID=17609119

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59279291A Expired - Fee Related JPH0696101B2 (en) 1984-12-24 1984-12-24 Filter element and its manufacturing method

Country Status (1)

Country Link
JP (1) JPH0696101B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04271815A (en) * 1991-02-27 1992-09-28 Fuji Photo Film Co Ltd Filtering method
JPH09187612A (en) * 1995-10-31 1997-07-22 Takasago Thermal Eng Co Ltd Gaseous impurity treating system and particle removing filter
WO2002004091A1 (en) * 2000-07-10 2002-01-17 Conad Co., Ltd. Method for manufacturing environment friendly air filter
JP2012529982A (en) * 2009-06-16 2012-11-29 マン ウント フンメル ゲゼルシャフト ミット ベシュレンクテル ハフツング CONNECTION ELEMENT FOR MULTILAYER MEDIUM, FILTER ELEMENT, AND METHOD FOR CONNECTING THIN LAYER MEDIUM
WO2020009207A1 (en) * 2018-07-06 2020-01-09 富士フイルム株式会社 Filter, filter manufacturing method, filtering device, chemical solution manufacturing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5739808A (en) * 1980-06-26 1982-03-05 Rabofua As Adjustable buisiness or work chair
JPS59119307U (en) * 1983-01-28 1984-08-11 株式会社土屋製作所 Filtration element for chemical filters

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5739808A (en) * 1980-06-26 1982-03-05 Rabofua As Adjustable buisiness or work chair
JPS59119307U (en) * 1983-01-28 1984-08-11 株式会社土屋製作所 Filtration element for chemical filters

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04271815A (en) * 1991-02-27 1992-09-28 Fuji Photo Film Co Ltd Filtering method
JPH09187612A (en) * 1995-10-31 1997-07-22 Takasago Thermal Eng Co Ltd Gaseous impurity treating system and particle removing filter
WO2002004091A1 (en) * 2000-07-10 2002-01-17 Conad Co., Ltd. Method for manufacturing environment friendly air filter
JP2012529982A (en) * 2009-06-16 2012-11-29 マン ウント フンメル ゲゼルシャフト ミット ベシュレンクテル ハフツング CONNECTION ELEMENT FOR MULTILAYER MEDIUM, FILTER ELEMENT, AND METHOD FOR CONNECTING THIN LAYER MEDIUM
WO2020009207A1 (en) * 2018-07-06 2020-01-09 富士フイルム株式会社 Filter, filter manufacturing method, filtering device, chemical solution manufacturing method
JPWO2020009207A1 (en) * 2018-07-06 2021-07-15 富士フイルム株式会社 Filter, filter manufacturing method, filtration device, chemical solution manufacturing method

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