JPS6014902A - Filtration apparatus - Google Patents

Filtration apparatus

Info

Publication number
JPS6014902A
JPS6014902A JP12507083A JP12507083A JPS6014902A JP S6014902 A JPS6014902 A JP S6014902A JP 12507083 A JP12507083 A JP 12507083A JP 12507083 A JP12507083 A JP 12507083A JP S6014902 A JPS6014902 A JP S6014902A
Authority
JP
Japan
Prior art keywords
tubular
fluororesin
filtration
ptfe
membrane
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.)
Pending
Application number
JP12507083A
Other languages
Japanese (ja)
Inventor
Fumio Matsuyama
文雄 松山
Kazuichi Tomita
富田 和一
Hiroshi Mano
弘 真野
Akihiko Isomura
磯村 昭彦
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP12507083A priority Critical patent/JPS6014902A/en
Priority to KR1019840003862A priority patent/KR870000603B1/en
Priority to DE19843425027 priority patent/DE3425027A1/en
Priority to US06/629,036 priority patent/US4539113A/en
Publication of JPS6014902A publication Critical patent/JPS6014902A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To obtain an apparatus having excellent removability of fine particles, filtration rate, chemical and heat resistances by using a porous membrane of polytetrafluoroethylene and a support of fluoroplastics having a specific shape, and making all parts of fluoroplastics. CONSTITUTION:A tubular filter body 8 is constituted by covering the outside of a tubular support of fluoroplastics with a tubular filtration membrane of polytetrafluoroethylene (PTFE) one end of which is closed, or inserting the filtration membrane into said support. And the tubular support 8 is arranged in a vessel of fluoroplastics which is constituted basically of outer vessels 5,6 and a supporting plate 7. A sheet-shaped porous PTFE made into a tubular form one end of which is closed is suitably used as the PTFE tubular filtration membrane. A porous molded tube obtained by sintering granular PTFE is suitable for the tubular support of fluoroplastics, since the molded tube is characteristically low in permeation resistance and difficult to deform.

Description

【発明の詳細な説明】 (技術分野) 本発明は全部品が弗素樹脂から成る、耐薬品性及び耐熱
性に優れた精密濾過装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Technical Field) The present invention relates to a precision filtration device that has excellent chemical resistance and heat resistance and has all parts made of fluororesin.

(発明の背景) 液体や気体中に含まれる微粒子を精密濾過により分離す
るための濾過装置は多数知られている力(耐薬品性、耐
熱性に優れた精密濾過装置についてはほとんど知られて
いない。従来、弗素樹脂製の濾過膜を用いた場合であっ
ても、濾過装置の他部分に耐薬品性、耐熱性の点で劣る
材料を使用したものが多く、それらの材料の性質で全体
が規制される結果となっている。また、シール材として
もゴムパツキンを用いたものがほとんどで耐薬品性の点
で特に問題が多い。更に濾過装置の単位体積当りの濾過
膜の面積が小さく、濾過流量を多くとることが困難であ
る場合が多い。
(Background of the invention) Many filtration devices are known for separating fine particles contained in liquids and gases by precision filtration (very little is known about precision filtration devices with excellent chemical and heat resistance). Conventionally, even when using a fluororesin filtration membrane, other parts of the filtration device often use materials with poor chemical resistance and heat resistance, and the properties of these materials affect the overall performance. In addition, most sealing materials use rubber gaskets, which poses particular problems in terms of chemical resistance.Furthermore, the area of the filtration membrane per unit volume of the filtration device is small, making it difficult to filtrate. In many cases, it is difficult to obtain a large flow rate.

するものである。It is something to do.

(発明の構成) 本発明の構成を実施例を入れて詳細に説明する。(Structure of the invention) The configuration of the present invention will be explained in detail by including examples.

本発明に於ける一端閉塞のポリテトラフルオロエチレン
(以下PTFEと略記する)管状濾過膜は、シー・ト状
又はチーーブ状のPTFE多孔質膜を一端閉塞の管状に
加工したものが適当である。孔径は通常0.01〜10
0μmのものから用途に応じて選択使用される。特に延
伸焼結法により製造されたシート状又はチーーブ状のP
TFE多孔質膜を一端閉塞の管状としたものが最適であ
る。延伸焼結法によりPTFE多孔質膜を製造するには
基本的には特公昭42−18560号に記載の方法が採
用される。この方法により製造されたPTFE多孔質膜
は、繊維と該繊維により互に連結された結節とから成る
ミクロ構造を有することが特徴であり、機械的強度が大
きく、微細で均一な孔径を有し、大きな気孔率のものも
製造可能であるため単位面積当りの濾過流量を大きくす
ることができ、濾過膜としては最適である。
The polytetrafluoroethylene (hereinafter abbreviated as PTFE) tubular filtration membrane with one end closed in the present invention is suitably a sheet-shaped or tube-shaped PTFE porous membrane processed into a tubular shape with one end closed. Pore diameter is usually 0.01-10
It is selected from those with a diameter of 0 μm depending on the purpose. In particular, sheet-like or cheese-like P produced by the stretch sintering method
A TFE porous membrane in the form of a tube with one end closed is optimal. Basically, the method described in Japanese Patent Publication No. 18560/1983 is employed to produce a porous PTFE membrane by the stretch sintering method. The PTFE porous membrane produced by this method is characterized by having a microstructure consisting of fibers and nodules interconnected by the fibers, and has high mechanical strength and fine and uniform pore diameters. Since it is possible to manufacture membranes with large porosity, the filtration flow rate per unit area can be increased, making them optimal as filtration membranes.

管状濾過膜とすることができる。PTFE ’多孔質膜
の接着はPTFE多孔質膜を重ね合せて加圧しなからP
TFEの融点(約327℃)以上に加熱することにより
達成される。またPTFE多孔質膜を重ね合せた間に他
の弗素樹脂のフィルム又は粉末を挿入し、加圧しながら
挿入された弗素樹脂の融点以上に加熱してPTFE多孔
質膜の孔内に該弗素樹脂を入り込ませることによっても
達成される。この目的に使用される弗素樹脂の例として
は、テトラフルオロエチレン〜ヘキサフルオロプロピレ
ン共重合体(FEP)、テトラフルオロエチレンルバー
フルオロアルキルビニルエーテル共li 合体(P F
A ) 、テトラフルオロエチレン−エチレン共M 合
体(ETF E)。
It can be a tubular filtration membrane. Adhesion of PTFE porous membranes is done by overlapping the PTFE porous membranes and applying pressure.
This is achieved by heating the melting point of TFE (approximately 327° C.) or higher. Alternatively, a film or powder of another fluororesin is inserted between the stacked PTFE porous membranes, and the fluororesin is heated to a temperature higher than the melting point of the inserted fluororesin under pressure to inject the fluororesin into the pores of the PTFE porous membrane. This can also be achieved by infiltration. Examples of fluororesins used for this purpose include tetrafluoroethylene-hexafluoropropylene copolymer (FEP), tetrafluoroethylene rubber fluoroalkyl vinyl ether copolymer (P F
A), Tetrafluoroethylene-ethylene co-M combination (ETF E).

ポリクロロトリフルオロエチレン(PCTFE)、ポリ
弗化ビニリデン(PVdF) 、ポリ弗化ビニル(PV
F)クロロトリフルオロエチレン〜エチレン共重合体又
はPFAを用いるのが適当である。
Polychlorotrifluoroethylene (PCTFE), polyvinylidene fluoride (PVdF), polyvinyl fluoride (PV
F) It is suitable to use chlorotrifluoroethylene-ethylene copolymer or PFA.

弗素樹脂管状支持体として適当なものはPTFE粒体の
焼結多孔成形管である。これはPTFE粒体を成形型の
中で加熱焼結することにより製造される、連通孔をもつ
成形体である。この成形体も第2図Aのように一端閉塞
しているものが適当である。通常0.1μm−1mmの
孔径を有するものが使用されるが、濾過膜より大きな孔
径を有するものを選択するのが透過抵抗を低くするに有
効である。この焼結多孔成形管は透過性が良好で変形し
にくい特徴を有するため支持体として特に有用なもので
ある。
A suitable fluororesin tubular support is a sintered porous tube of PTFE granules. This is a molded body with communicating holes that is manufactured by heating and sintering PTFE particles in a mold. This molded body is also suitably closed at one end as shown in FIG. 2A. Although those having a pore diameter of 0.1 μm to 1 mm are normally used, it is effective to select one having a pore diameter larger than that of the filtration membrane in order to lower the permeation resistance. This sintered porous molded tube has good permeability and is resistant to deformation, making it particularly useful as a support.

弗素樹脂孔あき管から成る層との積層体である。It is a laminate with layers made of perforated fluororesin tubes.

ここで弗素樹脂の網状成形品又は不織布は一過膜の有効
面積を多くとるためのものであり、その孔径は一過膜よ
り大きくすることが透過抵抗を低くするkめに要求され
る。弗素樹脂網状成形品は、網状に一体に成形されたも
のであってもよく、織物又は編物であってもよい。また
弗素樹脂孔あき管は通常弗素樹脂管ντ流路となる直径
0.5〜10mm程度の孔をあけた第2図Bのような構
造のものが。
Here, the fluororesin net-like molded product or nonwoven fabric is used to increase the effective area of the transient membrane, and the pore diameter thereof is required to be larger than that of the transient membrane in order to lower the permeation resistance. The fluororesin reticulated molded product may be integrally molded into a reticulated material, or may be a woven or knitted material. Further, the perforated fluororesin tube usually has a structure as shown in Fig. 2B, in which a hole with a diameter of about 0.5 to 10 mm is made to serve as the ντ flow path of the fluororesin tube.

用いられる。孔の形状は円形が一般的であるが他の形状
であっても差支えない。この弗素樹脂孔あき管の外表面
又は内表面に弗素樹脂の網状成形品又は不織布が配置さ
れる。管の外側から内側に濾過される外圧型装置の場合
には弗素樹脂孔あき管の外側に弗素樹脂の網状成形品又
は不織布が配置され(第2図C)、管の内側から外側に
濾過される内圧型装置の場合には弗素樹脂孔あき管の内
側に弗素樹脂の網状成形品又は不織布が配置される。
used. The shape of the hole is generally circular, but other shapes may be used. A fluororesin mesh molded product or nonwoven fabric is placed on the outer or inner surface of this perforated fluororesin tube. In the case of an external pressure type device that filters from the outside of the tube to the inside, a fluororesin mesh molded product or nonwoven fabric is placed on the outside of the perforated fluororesin tube (Fig. 2C), and the filter is filtered from the inside of the tube to the outside. In the case of an internal pressure type device, a fluororesin mesh molded product or nonwoven fabric is placed inside the perforated fluororesin tube.

これらの管状支持体の材料である弗素樹脂の例としては
、PTFE 、FEP 、PFA 、ETFE 、PC
TFE 、PVdF 。
Examples of the fluororesin that is the material for these tubular supports include PTFE, FEP, PFA, ETFE, and PC.
TFE, PVdF.

PVF 、 ECTFE等があげられる。特に耐熱耐薬
品性が要求される場合には、PTFE、FEP 、PF
A等が有効である。
Examples include PVF and ECTFE. In particular, when heat resistance and chemical resistance are required, PTFE, FEP, PF
A etc. are valid.

についても、管の外側から内側して濾過される外圧型装
置の場合には、PTFE管状濾過膜は弗素樹脂管状支持
体の外部に設けられ、逆に管の内側から外側に濾過され
る内圧型装置の場合には、PTFE管状濾過膜は弗素樹
脂管状支持体の内部に設けられる。このPTFE管状濾
過膜と弗素樹脂管状支持体との組合せが本発明の管状濾
過体を構成するものである。 ′ 様のものがあげられる。配置例を第3図に示し島第3図
に於て、弗素樹脂容器は基本的には外容器5及び6と支
持板7から構成され、Aの容器は流体の入口と出口を容
器の一方の側に設けたものであり、Bの容器は入口と出
口を容器の両側に設けたものである。8は管状−週休で
あり、その開放端は支持板7に固定シールされている。
In the case of an external pressure type device in which filtration is performed from the outside of the tube inward, the PTFE tubular filtration membrane is provided outside the fluororesin tubular support, whereas in the case of an internal pressure type device in which filtration is performed from the inside of the tube to the outside. In the case of the device, a PTFE tubular filtration membrane is mounted inside a fluororesin tubular support. The combination of this PTFE tubular filtration membrane and the fluororesin tubular support constitutes the tubular filtration body of the present invention. ’ can be mentioned. An arrangement example is shown in Fig. 3. In Fig. 3, the fluororesin container basically consists of outer containers 5 and 6 and a support plate 7, and the container A has the fluid inlet and outlet connected to one side of the container. The container B has an inlet and an outlet on both sides of the container. 8 is a tubular tube, the open end of which is fixedly sealed to the support plate 7;

第3図に於て、管の外側から内側へ濾過する場合は流体
の入口は9になり、出口は1oになる。逆に、管の内 
−側から外側へ濾過する場合には流体の入口は1oにな
り、出口は9になる。支持板70例としては第4図のよ
うな孔あき円板が一般的である。管状濾過体を支持板に
固定シールする方法の例としては、・テーパーねじによ
る方法や熱融着による方法あるいは両者の組合せが適当
であった。ここで熱融着には、樹脂の融点以上に熱した
治具で圧する方法、高周波誘尋加熱あるいは超音波によ
る方法等を含むものとする。また両者の接続部分に弗素
樹脂製の接続部品を用いてもよい。その例を第5図に示
した。第5図に於てAは接続部品の一例であり、Bは接
続部品と管状支持体を組合せた例である。
In FIG. 3, when filtering from the outside to the inside of the tube, the inlet of the fluid is 9 and the outlet is 1o. On the other hand, inside the tube
When filtering from the - side to the outside, the fluid inlet will be 1o and the outlet will be 9. As an example of the support plate 70, a perforated circular plate as shown in FIG. 4 is generally used. As examples of methods for fixing and sealing the tubular filter body to the support plate, a method using a tapered screw, a method using heat fusion, or a combination of the two were suitable. Here, the thermal fusion includes a method of pressing with a jig heated to a temperature higher than the melting point of the resin, a method of using high-frequency induction heating, ultrasonic waves, and the like. Further, a connecting part made of fluororesin may be used for the connecting portion between the two. An example is shown in FIG. In FIG. 5, A is an example of a connecting part, and B is an example of a combination of a connecting part and a tubular support.

管状−過膜は管状支持体又は接続部品にその開放端を熱
融着するか、固定ねじ部に挿入することによって端末シ
ールが可能であった。管状濾過体の閉塞端は容器の底(
第3図A)、あるいは適当な支持板(第3図B)で固定
される。また外容器と6図に示したようなはめ合せ構造
として両側から圧縮する方法は、特に有効であった。両
側から圧縮するには、金属製又は樹脂製のフランジ付容
器内にこの弗素樹脂容器を入れて圧縮するのが適当であ
った。この方法は容器の耐圧を増すという利点も有する
ものである。この場合も、流体に触れるのは弗素樹脂容
器だけであるので耐薬品性は何ら低下することはない。
The tubular membrane could be end-sealed by heat-sealing its open end to a tubular support or connecting piece, or by inserting it into a locking thread. The closed end of the tubular filter body is located at the bottom of the container (
Fig. 3A) or a suitable support plate (Fig. 3B). In addition, a method of compressing the outer container from both sides by forming a fitting structure as shown in FIG. 6 was particularly effective. In order to compress from both sides, it was appropriate to place the fluororesin container inside a flanged metal or resin container and compress it. This method also has the advantage of increasing the pressure resistance of the container. In this case as well, since only the fluororesin container comes into contact with the fluid, the chemical resistance does not deteriorate at all.

本発明に於て最も優れた実施例を以下に述べる。The most excellent embodiment of the present invention will be described below.

まず、PTFE管状濾過膜は、シート状のPTFE多一
孔質膜を一端閉塞の管状とした第1図Aに示したものが
最適であった。これはシート状のPTFE多孔質膜は、
最初からチューブ状に成形したPTFE多孔質膜より、
孔径が均一で、微細孔径とした場合でも気孔率が大きく
とれ、膜厚も薄くできるため、単位面積当りの濾過流量
の大きいものが得られるためである。弗素樹脂管状支持
体としてはPTFE粒体の焼結多孔成形管(第2図A)
が透過抵抗が低く、変形しにくい特徴を有し適当であっ
た。特に外圧型の装置に使用しに場合、外側からの圧力
に強く有効なものであった。PTFE管状濾過膜がこの
支持体の外部を覆う構造とした場合、第5図Aに示した
接続部品をPTFE以外の例えばFEP 、PFA等で
作り、PTFE粒体の焼結多孔成形管と第5図Bのよう
に接続し、更にその外部を覆うようにPTFE管状濾過
膜をかぶせた上膜の開口端を接続部品に熱融着した第5
図Cのような管状−濾過体が好適であった。
First, the most suitable PTFE tubular filtration membrane was the one shown in FIG. 1A, in which a sheet-like PTFE porous membrane was formed into a tubular shape with one end closed. This sheet-shaped PTFE porous membrane is
From a PTFE porous membrane formed into a tube shape from the beginning,
This is because even when the pore size is uniform and the pore size is fine, the porosity can be increased and the membrane thickness can be reduced, resulting in a large filtration flow rate per unit area. The fluororesin tubular support is a sintered porous molded tube of PTFE particles (Figure 2A).
It was suitable because it had low permeation resistance and was not easily deformed. Particularly when used in external pressure type equipment, it was highly effective against pressure from the outside. If the structure is such that a PTFE tubular filtration membrane covers the outside of this support, the connecting parts shown in FIG. Connect as shown in Figure B, and then cover the outside with a PTFE tubular filtration membrane, and heat-seal the open end of the upper membrane to the connecting part.
A tubular-filter as shown in Figure C was preferred.

(発明の効果) 本発明の濾過装置は、精密濾過膜として最も優れたPT
FE多孔質膜と特定形状の弗素樹脂支持体を用い、しか
も全部品が弗素樹脂から成るkめ、流体中の微粒子除去
性能、濾過流量、耐薬品性、耐熱性の優れた装置である
。従って、はとん1どあらゆる流体の精密濾過に利用で
き、従来−過が困難であった、腐食性あるいは高温の流
体をも効率良く処理することを可能とするものである。
(Effect of the invention) The filtration device of the present invention uses PT, which is the most excellent precision filtration membrane.
This device uses a porous FE membrane and a fluororesin support of a specific shape, and all parts are made of fluororesin, so it has excellent performance in removing particulates from fluids, filtration flow rate, chemical resistance, and heat resistance. Therefore, it can be used for precision filtration of just about any fluid, and can efficiently treat corrosive or high-temperature fluids that have been difficult to filter in the past.

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

状PTFE多孔質膜から製造した管状濾過膜の例を示す
図である。第2図AはPTFE粒体の焼結多孔成形管の
例を示す図であり、Bは弗素樹脂孔あき管の例を示す図
である。Cは弗素樹脂孔あき管の外側に弗素樹脂網が配
置された構造の管状支持体の例を示す図である。第3図
は濾過装置の例を示す断面図である。第4図は支持板の
例を示す図である。第5図Aは接続部品、Bは接続部品
と管状支持体の組合せ、Cは更にPTFE管状−過膜を
融着しに例を示す図である。第6図はシール方法の例を
示す図である。 l・・PTFE管状濾過膜開口端、2・・・接着部分、
8・・弗素樹脂孔あき管、4・・・・弗素樹脂網、5.
6・・・外容器、7・・・支持板、8・・・管状濾過体
、9.10・・・入口又は出口、11・・・シール部分
、12・・・融着部分、13・・・PTFE管状−過膜
。 ■1(2) 72図
FIG. 2 is a diagram showing an example of a tubular filtration membrane manufactured from a porous PTFE membrane. FIG. 2A is a diagram showing an example of a sintered porous tube made of PTFE particles, and FIG. 2B is a diagram showing an example of a fluororesin perforated tube. C is a diagram showing an example of a tubular support having a structure in which a fluororesin network is arranged on the outside of a perforated fluororesin tube. FIG. 3 is a sectional view showing an example of a filtration device. FIG. 4 is a diagram showing an example of the support plate. FIG. 5A shows a connection part, B shows a combination of a connection part and a tubular support, and FIG. 5C shows an example of a PTFE tubular-membrane welded together. FIG. 6 is a diagram showing an example of a sealing method. l... PTFE tubular filtration membrane open end, 2... adhesive part,
8. Fluororesin perforated pipe, 4. Fluororesin net, 5.
6... Outer container, 7... Support plate, 8... Tubular filter body, 9.10... Inlet or outlet, 11... Sealing part, 12... Fusion part, 13... - PTFE tubular-transmembrane. ■1(2) Figure 72

Claims (1)

【特許請求の範囲】 (11一端閉塞のポリテトラフルオロエチレンを状濾過
膜が弗素樹脂管状支持体の外部を覆うか又は内部に挿入
された構造の管状濾過体を、流体の入口及び出口を有す
る弗素樹脂容器内に配置したことを特徴とする濾過装置
。 (2)ポリテトラフルオロエチレン管状−過膜が0.0
1〜100μmの孔径を有することを特徴とする特許請
求の範囲第1項記載の濾過装置。 (3)ポリテトラフルオロエチレン管状濾過膜が、繊維
と該繊維により互に連結された結節とから成るミクロ構
造を有することを特徴とする特許請求ゝの範囲第1項記
載の濾過装置。 (4)弗素樹脂管状支持体がポリテトラフルオロエチレ
ン粒体の焼結多孔成形管であることを特徴とする特許請
求の範囲第1項記載の濾過装置。 (5)焼結多孔成形管が0.1μm〜1mmの孔径を有
することを特徴とする特許請求の範囲第4項記載の濾過
装置。 (6)弗素樹脂管状支持体が、濾過膜より大きな孔径を
有する弗素樹脂の網状成形品又は不織布から成る層と、
弗素樹脂孔あき管から成る層との積層体であり、かつ該
弗素樹脂網状成形品又は不織布4から成る層が濾過膜側
に配置されているこ゛とを特徴とする特許請求の範囲第
1項記載の濾過装置。 (7)弗素樹脂管状支持体が一端閉塞の形状であること
を特徴とする特許請求の範囲第1項記載の濾過装置。 を特徴とする特許請求の範囲第1項記載の濾過装置。
[Claims] (11) A tubular filtration body having a structure in which a polytetrafluoroethylene-shaped filtration membrane with one end closed covers the outside of a fluororesin tubular support or is inserted into the interior thereof, and has an inlet and an outlet for fluid. A filtration device characterized by being placed in a fluororesin container. (2) A polytetrafluoroethylene tubular filtration membrane of 0.0
The filtration device according to claim 1, having a pore diameter of 1 to 100 μm. (3) The filtration device according to claim 1, wherein the polytetrafluoroethylene tubular filtration membrane has a microstructure consisting of fibers and nodes interconnected by the fibers. (4) The filtration device according to claim 1, wherein the fluororesin tubular support is a sintered porous tube made of polytetrafluoroethylene particles. (5) The filtration device according to claim 4, wherein the sintered porous formed tube has a pore diameter of 0.1 μm to 1 mm. (6) a layer in which the fluororesin tubular support is made of a fluororesin net-shaped molded product or nonwoven fabric having a pore diameter larger than that of the filtration membrane;
Claim 1, characterized in that it is a laminate with a layer made of a perforated fluororesin tube, and the layer made of the fluororesin reticular molded product or the nonwoven fabric 4 is arranged on the filtration membrane side. filtration device. (7) The filtration device according to claim 1, wherein the fluororesin tubular support has a shape with one end closed. A filtration device according to claim 1, characterized in that:
JP12507083A 1983-07-08 1983-07-08 Filtration apparatus Pending JPS6014902A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP12507083A JPS6014902A (en) 1983-07-08 1983-07-08 Filtration apparatus
KR1019840003862A KR870000603B1 (en) 1983-07-08 1984-07-04 Filtering devices
DE19843425027 DE3425027A1 (en) 1983-07-08 1984-07-06 FLUORINE RESIN FILTER
US06/629,036 US4539113A (en) 1983-07-08 1984-07-09 Fluororesin filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12507083A JPS6014902A (en) 1983-07-08 1983-07-08 Filtration apparatus

Publications (1)

Publication Number Publication Date
JPS6014902A true JPS6014902A (en) 1985-01-25

Family

ID=14901075

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12507083A Pending JPS6014902A (en) 1983-07-08 1983-07-08 Filtration apparatus

Country Status (1)

Country Link
JP (1) JPS6014902A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5409515A (en) * 1992-01-14 1995-04-25 Daikin Industries, Ltd. Filter apparatus and filter element
JP2009066553A (en) * 2007-09-14 2009-04-02 Chung Yuan Christian Univ Method for forming tubular filtration film material and its apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5409515A (en) * 1992-01-14 1995-04-25 Daikin Industries, Ltd. Filter apparatus and filter element
JP2009066553A (en) * 2007-09-14 2009-04-02 Chung Yuan Christian Univ Method for forming tubular filtration film material and its apparatus

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