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JP3470104B2 - Ceramic fiber filter - Google Patents
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JP3470104B2 - Ceramic fiber filter - Google Patents

Ceramic fiber filter

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Publication number
JP3470104B2
JP3470104B2 JP2001034744A JP2001034744A JP3470104B2 JP 3470104 B2 JP3470104 B2 JP 3470104B2 JP 2001034744 A JP2001034744 A JP 2001034744A JP 2001034744 A JP2001034744 A JP 2001034744A JP 3470104 B2 JP3470104 B2 JP 3470104B2
Authority
JP
Japan
Prior art keywords
filter
filter medium
pleated
ceramic
ceramic fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2001034744A
Other languages
Japanese (ja)
Other versions
JP2002233726A (en
Inventor
加久夫 植田
勉 松山
康男 矢島
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.)
Shinryo Corp
Original Assignee
Shinryo Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shinryo Corp filed Critical Shinryo Corp
Priority to JP2001034744A priority Critical patent/JP3470104B2/en
Publication of JP2002233726A publication Critical patent/JP2002233726A/en
Application granted granted Critical
Publication of JP3470104B2 publication Critical patent/JP3470104B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明はセラミックファイバ
ー(セラミック繊維)を利用したフィルタの構造に関
し、特に原子力関連施設の焼却設備の排ガス処理に用い
るのに適したフィルタに関する。 【0002】 【従来の技術】原子力関連施設の焼却設備では、燃焼排
ガス中の放射性物質を環境へ放出しないために、排ガス
処理系統に高性能エアフィルタ(HEPAフィルタ)を
設置するのが一般的であるが、HEPAフィルタはすす
やダストが多いと短期間で目詰まりするので、前段に除
去効率の高い除塵装置が必要となる。現在、除塵装置と
しては、セラミックフィルタと呼ばれる高温フィルタ
(セラミック粉末を焼結し円筒形にした濾材を用いたフ
ィルタ)が多く採用されている。 【0003】しかしながら、セラミックフィルタには次
のような多くの問題点がある。 1)セラミックフィルタで使用する濾材はコーディエラ
イトやシリコンカーバイドなどのセラミック粉末を、焼
結温度1200〜1600℃程度で、円筒形に焼結した
ものである。このため、フィルタ表面に堆積した未燃分
燃焼による熱衝撃・起動と停止によるガス温度変動で生
じる熱衝撃・逆洗によるガス温度変動で生じる熱衝撃な
どによって、割れや強度低下が発生する。 【0004】2)セラミックフィルタで使用する濾材は
セラミック粉末を円筒形に焼結したものなので、構造上
圧力損失が大きくなる。そのため、動力負荷が大きくな
る。逆洗を行うとフィルタ差圧が初期の状態まで回復し
なくなる。 3)セラミックフィルタに使用されるSiCが高価であ
る。使用中にセラミックフィルタが割れて濾過効果が失
われる可能性を否定できないため、原子力施設では、予
防保全の観点から年次点検でフィルタの全数交換が必要
となっている。濾材単価が高いのでランニングコストが
非常に高い。また、使用済みフィルタは2次廃棄物とな
り、その処理が問題となる。 4)フィルタの差圧上昇が早く逆洗間隔が短いため、焼
却運転中に逆洗する必要がある。 5)焼却運転中の逆洗は系内負圧制御の外乱となる。 6)セラミックファイバー(セラミック繊維)を利用し
たフィルタは、強度上の問題から逆洗ができないため、
交換頻度が多くなり、ランニングコストが高くなる。 【0005】特開平9−285710号「セラミックフ
ィルタ、その製造法及びそれを用いた装置」には、熱衝
撃によるセラミックスの破壊を防止し信頼性を高めるた
めに、多孔質セラミックスをセラミックス発熱体で複合
化する手法と、それを用いた脱塵装置が記載されてい
る。特開平9−38432号「セラミックフィルター」
には、濾過効率にすぐれ、濾過速度の速いセラミックフ
ィルターとして、不純物を含有した液体の導入側開口と
排出側開口とを交互に封止したハニカム構造体からなる
セラミックフィルターが記載されている。特開平7−6
0037号「セラミックフィルタ素材及びその製造方
法」には、セラミック繊維を抄造した支持母材の片側面
にセラミック粒子層を形成したセラミックフィルタ素材
とその製造方法が記載されている。 【0006】 【発明が解決しようとする課題】本発明の目的は、従来
のセラミックフィルタの欠点を除去した新規な構造のフ
ィルタを提供することであり、特に割れの発生がなく、
効率的な逆洗を可能とし、ランニングコストを低下させ
た高温フィルタを提供することにある。 【0007】 【課題を解決するための手段】本発明によるセラミック
ファイバーフィルタはその第1の態様において、アルミ
ナとシリカをそれぞれ約50%包含させた繊維状のセラ
ミックファイバーを補強用芯線とともに平織りした濾材
を形成し、この濾材を波形に折り曲げてプリーツ構造に
成形したプリーツ状濾材と、前記プリーツ状濾材の波形
の隙間に挿入された金属製のセパレータと、前記プリー
ツ状濾材と前記金属製セパレータを収納する外板とを備
え、前記プリーツ状濾材の波形の裏側に当接する前記金
属製セパレータの頂部(先端側)にはR(半径状曲が
り)加工が施されており、プリーツ構造により濾過面積
を大きくとると共に濾材の折り目に熱応力が集中しない
ようにしたことを特徴としている。 【0008】 【作用】本発明では、芯線(例えばSUS製)入りセラ
ミックファイバーをプリーツ構造に成形し、濾過面積を
大きくとることによって、コンパクト、低圧損で安価な
高温フィルタを提供する。プリーツ状の濾材は従来のセ
ラミックフィルタの濾材のように割れるおそれがなく、
物理的条件による寿命が長くなり、信頼性が高くなる。
また、濾材が芯線入りのプリーツ構造をしているので濾
過面積が大きくなり、濾過通過速度が低くなって、圧力
損失が小さくなる。従来のセラミックフィルタのように
SiCを必要としないので、濾材コストが低減される。 【0009】濾材部の形状保持と構造体の強度をアップ
させるために金属製セパレータが配置されるが、金属製
セパレータとして金網セパレータを使用すれば、濾材表
面に付着した粉塵等の効果的な逆洗が可能となる。ま
た、長期間、高温雰囲気下に暴露されることで濾材部の
折り目が熱劣化し損傷することが考えられるが、金属製
セパレータや金網セパレータの頂部(先端側)にはR
(半径状曲がり)加工が施されるので、折り目に熱応力
が集中するのを避けることができる。 【0010】本発明によるセラミックファイバーフィル
タはその変形例として、アルミナとシリカをそれぞれ約
50%包含させた繊維状のセラミックファイバーを補強
用芯線とともに平織りした濾材を形成し、この濾材を波
形に折り曲げてプリーツ構造に成形したプリーツ状濾材
と、前記プリーツ状濾材の波形の各折り目部分の裏側に
挿入された丸棒形の金属製セパレータと、前記丸棒形金
属製セパレータの端部を支持する金属製枠材とを備え、
プリーツ構造により濾過面積を大きくとったことを特徴
としている。 【0011】本発明によるセラミックファイバーフィル
タは、これらの工夫を行うことで、効率的な逆洗が可能
となる。フィルタ本体は、一例として、重量が約30k
g、外形寸法が約300×300×600mm程度にな
る。セラミックファイバーの仕様としては、最高使用温
度が1200℃、化学成分がアルミナとシリカを各50
%程度である。以下、本発明による好適な実施形態を添
付図面を参照しながら説明する。 【0012】 【発明の実施の形態】図1A〜Bは本発明の第1の好適
な実施例によるセラミックファイバーフィルタの濾材部
分10を表しており、プリーツ状の濾材12と、金属製
のセパレータ14とを備えている。プリーツ状の濾材1
2は、アルミナとシリカをそれぞれ約50%包含させた
繊維状のセラミックファイバーを補強用芯線とともに平
織りした濾材を形成し、この濾材を波形に折り曲げてプ
リーツ構造に成形されている。プリーツ状濾材12の波
形の隙間に金属製のセパレータ14が挿入されている。
図1の例では、セパレータ14は金属部材で構成され、
補強材として作用する。かくして、このようなプリーツ
構造により濾材12の濾過面積が大きくなっている。 【0013】排ガスは図1Aの矢印Gの方向からフィル
タ濾材部10へと送り込まれ、図1Bに示すように、セ
ラミックファイバーからなる濾材12に粉塵Fが付着し
て捕捉される。このときの通過速度は、例えば約2cm
/s程度である。図1Bにおいて、濾材12の波形の折
り目の裏側に当接する金属製セパレータの頂部14a
は、濾材の波形の折り目に熱応力が集中しないように
加工がなされている。 【0014】図2A〜Cは、セラミックファイバーフィ
ルタ濾材部10を外板16,18に収納したセラミック
ファイバーフィルタ組立体20を構成した応用例を表し
ている。外板16,18は端部を折り返し、折り返し部
22,24の表面は相手側フランジ面(図示せず)との
シール面になるようにパッキンが付着させられている。
このパッキンはセラミック製が望ましい。フィルタ濾材
部10には、熱応力による変形を防止するために耐熱性
を有する部材、例えばSUS310Sなどで作られた補
強材26が取り付けられている。フィルタ濾材部10の
濾材はセラミックファイバー製で、セパレータは耐熱性
を有する部材、例えばSUS310Sなどの金属で作ら
れている。排ガスは、図2Aにおいて上側の折り返し部
22内から下側の折り返し部24内へと矢印Gの方向に
流れて、放射性粉塵が濾過される。フィルタ20の外形
寸法は、幅Wが約300mm、奥行きDが約300m
m、高さHが600mm程度になる。 【0015】図2Bは、他の実施例によるフィルタ30
の横断面を表しており、この例ではセラミックファイバ
ー製の濾材32と、金属製の金網からなるメッシュセパ
レータ34で構成されている。メッシュセパレータ34
の山頂部は濾材32の波形の折り目と形状が一致するよ
うにR(曲がり)が付けられている。逆洗エアが矢印S
の方向から流されると、逆洗エアはメッシュセパレータ
34を通過して濾材32の表面に均一に吹きつけること
になるから、濾材の表面に付着した粉塵Fが確実に払い
落とされるようになる。 【0016】図2Cは、さらに他の実施例によるフィル
タ40の横断面を表しており、この例ではセラミックフ
ァイバー製の濾材42と、濾材42の波形の各折り目部
分に裏側から当接して支える丸棒形の補強材44と、補
強材44の端部を固定する丸棒形の枠材46とで構成さ
れている。丸棒形の補強材44は濾材42の折り目部分
が熱により劣化して折り曲げられるのを防止する働きを
する。逆洗エアが矢印Sの方向から流されると、逆洗エ
アは丸棒形の補強材44の間の大きな隙間を流れること
になるので、逆洗効果が高く、濾材42の表面に付着し
た粉塵Fが確実に払い落とされるようになる。 【0017】他の実施例として、濾材の波形に沿うよう
に波型成型されたセパレータを使用してもよい。 【0018】 【発明の効果】以上詳細に説明した如く、本発明のセラ
ミックファイバーフィルタによれば、従来のセラミック
フィルタの多くの欠点を除去した新規な構造のフィルタ
が提供され、特に熱衝撃による割れの発生がなく、圧力
損失が小さくなって、効率的な逆洗が可能となり、ラン
ニングコストが低下するなど、その技術的効果には極め
て顕著なものがある。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter structure using ceramic fiber (ceramic fiber), and more particularly, to a filter structure suitable for use in an exhaust gas treatment of an incineration facility of a nuclear facility. Regarding filters. 2. Description of the Related Art Generally, incinerators of nuclear facilities are equipped with a high-performance air filter (HEPA filter) in an exhaust gas treatment system in order to prevent radioactive substances in combustion exhaust gas from being released to the environment. However, the HEPA filter becomes clogged in a short period of time if there is a large amount of soot and dust, so that a dust removal device having a high removal efficiency is required at the preceding stage. At present, a high-temperature filter called a ceramic filter (a filter using a filter material obtained by sintering a ceramic powder into a cylindrical shape) is often used as a dust removing device. [0003] However, ceramic filters have many problems as follows. 1) The filter medium used in the ceramic filter is obtained by sintering ceramic powder such as cordierite or silicon carbide into a cylindrical shape at a sintering temperature of about 1200 to 1600 ° C. For this reason, cracks and a decrease in strength occur due to thermal shock caused by unburned combustion accumulated on the filter surface, thermal shock caused by gas temperature fluctuation caused by starting and stopping, thermal shock caused by gas temperature fluctuation caused by backwashing, and the like. [0004] 2) Since the filter medium used in the ceramic filter is obtained by sintering ceramic powder into a cylindrical shape, the pressure loss is large due to its structure. Therefore, the power load increases. When the backwash is performed, the filter differential pressure does not recover to the initial state. 3) SiC used for the ceramic filter is expensive. Since it is undeniable that the filtering effect may be lost due to cracking of the ceramic filter during use, it is necessary for nuclear facilities to replace all filters at annual inspections from the viewpoint of preventive maintenance. The running cost is very high because the unit price of the filter medium is high. Also, the used filter becomes secondary waste, and its disposal poses a problem. 4) Since the differential pressure of the filter rises quickly and the backwash interval is short, it is necessary to backwash during the incineration operation. 5) Backwash during incineration operation is a disturbance of negative pressure control in the system. 6) Filters using ceramic fibers (ceramic fibers) cannot be backwashed due to strength issues.
Frequent replacements increase running costs. Japanese Patent Application Laid-Open No. 9-285710, entitled "Ceramic Filter, Method for Producing the Same, and Apparatus Using the Same" discloses that a porous ceramic is heated with a ceramic heating element in order to prevent the destruction of the ceramic due to thermal shock and to enhance reliability. A method of compounding and a dust removing device using the method are described. JP-A-9-38432 "Ceramic filter"
Discloses a ceramic filter having a honeycomb structure in which openings for introducing and discharging a liquid containing impurities are alternately sealed as a ceramic filter having excellent filtration efficiency and a high filtration speed. JP-A-7-6
No. 0037 “Ceramic filter material and method for producing the same” describes a ceramic filter material in which a ceramic particle layer is formed on one side of a supporting base material formed from ceramic fibers and a method for producing the same. SUMMARY OF THE INVENTION An object of the present invention is to provide a filter having a novel structure which eliminates the drawbacks of the conventional ceramic filter, and in particular, does not cause cracks.
An object of the present invention is to provide a high-temperature filter which enables efficient backwashing and reduces running costs. According to a first aspect of the present invention, there is provided a ceramic fiber filter in which a fibrous ceramic fiber containing about 50% of alumina and silica is plain woven together with a reinforcing core wire. A pleated filter medium formed by bending the filter medium into a waveform and forming a pleated structure, a metal separator inserted into a gap between the waveforms of the pleated filter medium, and storing the pleated filter medium and the metal separator And a metal plate that abuts against the back side of the corrugation of the pleated filter medium.
At the top (tip side) of the metal separator, R
The pleated structure increases the filtration area and does not concentrate thermal stress on the folds of the filter media.
It is characterized in that the the like. According to the present invention, a compact, low-pressure-drop, inexpensive high-temperature filter is provided by molding a ceramic fiber containing a core wire (for example, made of SUS) into a pleated structure and increasing the filtration area. Pleated filter media has no risk of cracking like conventional ceramic filter media,
Longer life due to physical conditions and higher reliability.
In addition, since the filter medium has a pleated structure including a core wire, the filtration area increases, the filtration passage speed decreases, and the pressure loss decreases. Since no SiC is required unlike the conventional ceramic filter, the cost of the filter medium is reduced. A metal separator is disposed in order to maintain the shape of the filter medium portion and increase the strength of the structure. However, if a metal mesh separator is used as the metal separator, it is possible to effectively prevent dust and the like adhering to the surface of the filter medium. Washing becomes possible. In addition, it is considered that the folds of the filter media may be thermally degraded and damaged due to long-term exposure to a high-temperature atmosphere .
R on the top (tip side) of the separator or wire mesh separator
(Radial bending) processing is performed, so thermal stress
Can be avoided. As a modification of the ceramic fiber filter according to the present invention, as a modification, a filter medium is formed by weaving a fibrous ceramic fiber containing about 50% each of alumina and silica together with a reinforcing core wire, and this filter medium is folded into a waveform. Pleated filter material formed into a pleated structure, a round bar-shaped metal separator inserted on the back side of each fold portion of the corrugation of the pleated filter material, and a metal plate supporting an end of the round bar-shaped metal separator With frame material,
The pleated structure has a large filtering area. The ceramic fiber filter according to the present invention enables efficient backwashing by taking these measures. The filter body weighs about 30k as an example.
g, the external dimensions are about 300 × 300 × 600 mm. As for the specifications of the ceramic fiber, the maximum operating temperature is 1200 ° C, and the chemical components are alumina and silica 50 each.
%. Hereinafter, preferred embodiments according to the present invention will be described with reference to the accompanying drawings. 1A and 1B show a filter medium portion 10 of a ceramic fiber filter according to a first preferred embodiment of the present invention, in which a pleated filter medium 12 and a metal separator 14 are shown. And Pleated filter media 1
No. 2 forms a filter medium in which fibrous ceramic fibers each containing about 50% of alumina and silica are plain-woven together with a reinforcing core wire, and this filter medium is bent into a waveform to form a pleated structure. A metal separator 14 is inserted in the corrugated gap of the pleated filter medium 12.
In the example of FIG. 1, the separator 14 is formed of a metal member,
Acts as a reinforcement. Thus, the filtering area of the filter medium 12 is increased by such a pleated structure. The exhaust gas is fed into the filter medium section 10 from the direction of arrow G in FIG. 1A, and as shown in FIG. 1B, the dust F adheres to and is captured by the filter medium 12 made of ceramic fiber. The passing speed at this time is, for example, about 2 cm.
/ S. In FIG. 1B, the top portion 14a of the metal separator abutting against the back side of the fold of the corrugation of the filter medium 12
, As thermal stresses in the folds of the filter medium of the waveform is not concentrated R
Processing has been done. FIGS. 2A to 2C show an application example in which a ceramic fiber filter assembly 20 in which a ceramic fiber filter medium portion 10 is housed in outer plates 16 and 18 is formed. The ends of the outer plates 16 and 18 are folded back, and packing is adhered so that the surfaces of the folded portions 22 and 24 become a sealing surface with a mating flange surface (not shown).
This packing is preferably made of ceramic. A member having heat resistance, for example, a reinforcing member 26 made of SUS310S or the like is attached to the filter medium portion 10 in order to prevent deformation due to thermal stress. The filter medium of the filter medium section 10 is made of ceramic fiber, and the separator is made of a heat-resistant member, for example, a metal such as SUS310S. The exhaust gas flows in the direction of arrow G from the inside of the upper folded portion 22 to the inside of the lower folded portion 24 in FIG. 2A, and the radioactive dust is filtered. The external dimensions of the filter 20 are such that the width W is about 300 mm and the depth D is about 300 m
m and height H are about 600 mm. FIG. 2B shows a filter 30 according to another embodiment.
In this example, a filter medium 32 made of ceramic fiber and a mesh separator 34 made of a metal wire mesh are used. Mesh separator 34
R (bent) is provided so that the top of the mark has the same shape as the fold of the waveform of the filter medium 32. Backwash air is arrow S
, The backwash air passes through the mesh separator 34 and is sprayed uniformly on the surface of the filter medium 32, so that the dust F adhered to the surface of the filter medium is reliably removed. FIG. 2C shows a cross section of a filter 40 according to still another embodiment. In this example, a filter medium 42 made of ceramic fiber and a circle supporting the corrugated portions of the filter medium 42 from behind are supported. It comprises a bar-shaped reinforcing member 44 and a round bar-shaped frame member 46 for fixing an end of the reinforcing member 44. The round bar-shaped reinforcing member 44 functions to prevent the fold portion of the filter medium 42 from being deteriorated and bent by heat. When the backwash air flows in the direction of the arrow S, the backwash air flows through a large gap between the round bar-shaped reinforcing members 44, so that the backwash effect is high, and the dust adhering to the surface of the filter medium 42 is high. F will surely be paid off. As another embodiment, a separator corrugated so as to follow the waveform of the filter medium may be used. As described in detail above, according to the ceramic fiber filter of the present invention, there is provided a filter having a novel structure which eliminates many disadvantages of the conventional ceramic filter, and particularly, a crack caused by thermal shock. The technical effect is extremely remarkable, for example, there is no occurrence, the pressure loss is reduced, efficient backwashing is possible, and the running cost is reduced.

【図面の簡単な説明】 【図1】本発明におけるプリーツ状の濾材とセパレータ
の構造を表す斜視図である。 【図2】本発明によるセラミックファイバーフィルタの
組立体と断面構造を表す斜視図である。 【符号の説明】 10 フィルタ濾材部 20,30,40 セラミックファイバーフィルタ 12,32,42 プリーツ状濾材 14,34 セパレータ 16,18 外板 22,24 外板折り返し部 26 補強材 44 補強材 46 枠材
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view showing a structure of a pleated filter medium and a separator in the present invention. FIG. 2 is a perspective view showing an assembly and a sectional structure of a ceramic fiber filter according to the present invention. DESCRIPTION OF SYMBOLS 10 Filter media part 20, 30, 40 Ceramic fiber filter 12, 32, 42 Pleated filter media 14, 34 Separator 16, 18 Outer plate 22, 24 Outer plate folded portion 26 Reinforcement 44 Reinforcement 46 Frame material

───────────────────────────────────────────────────── フロントページの続き (72)発明者 矢島 康男 東京都新宿区北新宿1丁目8番1号 株 式会社忍足研究所内 (56)参考文献 特開 昭57−61997(JP,A) 特開 昭61−28415(JP,A) 特開 昭63−287522(JP,A) 特開 昭50−106854(JP,A) 特開 平1−224019(JP,A) 特開 平6−79119(JP,A) 実開 昭50−111776(JP,U)   ────────────────────────────────────────────────── ─── Continuation of front page    (72) Inventor Yasuo Yajima               1-8-1 Kita Shinjuku, Shinjuku-ku, Tokyo               Shikinari Institute                (56) References JP-A-57-61997 (JP, A)                 JP-A-61-28415 (JP, A)                 JP-A-63-287522 (JP, A)                 JP-A-50-106854 (JP, A)                 JP-A 1-224019 (JP, A)                 JP-A-6-79119 (JP, A)                 50-111776 (JP, U)

Claims (1)

(57)【特許請求の範囲】 【請求項1】 アルミナとシリカをそれぞれ約50%包
含させた繊維状のセラミックファイバーを補強用芯線と
ともに平織りした濾材を形成し、この濾材を波形に折り
曲げてプリーツ構造に成形したプリーツ状濾材と、 前記プリーツ状濾材の波形の隙間に挿入された金属製セ
パレータと、 前記プリーツ状濾材と前記金属製セパレータを収納する
外板とを備え、前記プリーツ状濾材の波形の裏側に当接する前記金属製
セパレータの頂部には半径状曲がり加工が施されてお
り、 プリーツ構造により濾過面積を大きくとると共に濾材の
折り目に熱応力が集中しないようにしたことを特徴とす
るセラミックファイバーフィルタ。
(57) [Claims 1] A filter medium is formed by weaving a fibrous ceramic fiber containing about 50% each of alumina and silica together with a reinforcing core wire in a plain weave, and this filter medium is bent into a corrugated form to be pleated. a pleated filter medium formed into structures, and metal separators which are inserted into the gap of the pleated filter medium wave, and an outer plate housing the metal separator and the pleated filter medium, the pleated filter medium wave The metal that comes in contact with the back side of the
The top of the separator has a radial bend.
Ri, filter media with a large filtration area by pleated structure
A ceramic fiber filter characterized in that thermal stress is not concentrated on the fold .
JP2001034744A 2001-02-13 2001-02-13 Ceramic fiber filter Expired - Lifetime JP3470104B2 (en)

Priority Applications (1)

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JP2001034744A JP3470104B2 (en) 2001-02-13 2001-02-13 Ceramic fiber filter

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Application Number Priority Date Filing Date Title
JP2001034744A JP3470104B2 (en) 2001-02-13 2001-02-13 Ceramic fiber filter

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JP3470104B2 true JP3470104B2 (en) 2003-11-25

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JP3677598B2 (en) * 2001-12-25 2005-08-03 新菱冷熱工業株式会社 Ceramic fiber filter to prevent bypass leakage
KR100653431B1 (en) * 2005-03-29 2006-12-01 주식회사 코캣 Chemical filter using metal compound and manufacturing method thereof
JP2007050342A (en) * 2005-08-18 2007-03-01 Toray Ind Inc filter
JP4699340B2 (en) * 2006-11-16 2011-06-08 日東電工株式会社 Filter unit
JP5747844B2 (en) * 2012-03-07 2015-07-15 清水建設株式会社 Filler, filler unit, and air purifier
JP6808562B2 (en) * 2017-04-05 2021-01-06 株式会社エフテック Spacer for pleated type filter
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CN112933762B (en) * 2021-03-05 2025-09-05 苏州兆和空气系统股份有限公司 A glass fiber filter element for oil mist purification

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108697960A (en) * 2015-11-13 2018-10-23 W.L.戈尔及同仁股份有限公司 Supporting member for filtering pleated media

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