JP3071218B2 - Ceramic filter - Google Patents
Ceramic filterInfo
- Publication number
- JP3071218B2 JP3071218B2 JP2340581A JP34058190A JP3071218B2 JP 3071218 B2 JP3071218 B2 JP 3071218B2 JP 2340581 A JP2340581 A JP 2340581A JP 34058190 A JP34058190 A JP 34058190A JP 3071218 B2 JP3071218 B2 JP 3071218B2
- Authority
- JP
- Japan
- Prior art keywords
- ceramic
- support
- film
- membrane
- porous
- 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 - Fee Related
Links
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、ガス中や液体中の固体を分離捕獲するセラ
ミックスフィルターの改良に関する。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a ceramic filter for separating and capturing a solid in a gas or a liquid.
[従来の技術と課題] 周知の如く、半導体プロセスインラインガスフィルタ
ー等に使用される多孔質セラミックス分離膜としては、
アルミナ質の非対称膜が使用されている。この材料は、
もともとウラン原料のガス分離用として開発されたこと
から、大きなプラントにおける信頼性を確保するために
単純な形状即ち単チューブ形状のものから始まってい
る。この単チューブの形成方法としては押し出し成形が
適しており、後に開発された蓮根形状のチューブも同様
の成形技術によって作られている。[Prior art and problems] As is well known, a porous ceramics separation membrane used for a semiconductor process in-line gas filter or the like includes:
Alumina asymmetric membranes are used. This material is
Since it was originally developed for gas separation of uranium raw materials, it started with a simple shape, that is, a single tube shape, in order to ensure reliability in a large plant. Extrusion molding is suitable as a method for forming this single tube, and a lotus root-shaped tube developed later is also made by a similar molding technique.
ところで、単チューブ、蓮根状チューブのいずれにも
おいても、分離膜は穴の内側に形成されている。ここ
で、分離膜は支持体と同じ化学成分をもち、粒径の小さ
い粉体を焼結して形成されている。By the way, in both the single tube and the lotus root tube, the separation membrane is formed inside the hole. Here, the separation membrane has the same chemical composition as the support, and is formed by sintering a powder having a small particle size.
[発明が解決しようとする課題] しかしながら、単チューブ、蓮根状チューブともに、
全体の形は強度的機能を浮けもつ支持体材質となってお
り、分離膜は単チューブの内側あるいは蓮根状チューブ
の穴の内側に形成されているため、セラミック膜材料全
体の体積に比べて膜面積を大きくすることが困難であ
る。従って、膜面積を確保するためには、セラミック膜
材料が大きくなってしまい、その結果膜モジュールが大
きくなり、最終的には分離装置が大きくならざるを得な
い。[Problems to be Solved by the Invention] However, both the single tube and the lotus root tube,
The overall shape is made of a support material that has a strong function, and the separation membrane is formed inside the single tube or inside the hole of the lotus root tube, so the membrane is smaller than the volume of the entire ceramic membrane material. It is difficult to increase the area. Therefore, in order to secure the membrane area, the ceramic membrane material becomes large, and as a result, the membrane module becomes large, and eventually the separation device must be large.
また、チューブ形状のセラミック膜材料がセラミック
モジュールの概念まで規定することとなった。つまり、
1m弱の長さをもつモジュールが基本となり、小さい膜モ
ジュールはチューブを切断して膜材料とし、これにケー
シング、ガスケット等を付属して作られていた。そのた
め、モジュールの最小径は、セラミックチューブの太さ
によって制限されていた。Also, the ceramic film material in the form of a tube defines the concept of a ceramic module. That is,
Basically, a module with a length of less than 1 m was used, and a small membrane module was made by cutting a tube into a membrane material, and attached a casing, gasket, etc. Therefore, the minimum diameter of the module was limited by the thickness of the ceramic tube.
本発明は上記事情に鑑みてなされたもので、三次元網
目状構造を有する多孔質セラミックス支持体の一部を除
く骨格の表面に、この多孔質セラミックス支持体のもつ
細孔径よりも小さい細孔径をもつセラミック膜が複数層
形成され、しかもセラミックス支持体内部から複数層形
成されたセラミック膜表面に向って細孔径が内部から表
面にゆくに従って順次小さくなるように構成することに
より、単位面積当りの膜面積を大きくできるセラミック
フィルターを提供することを目的とする。The present invention has been made in view of the above circumstances, and has a pore diameter smaller than the pore diameter of the porous ceramic support on the surface of the skeleton excluding a part of the porous ceramic support having a three-dimensional network structure. A plurality of ceramic membranes having the following structure are formed, and the pore diameter is gradually reduced from the inside to the surface of the ceramic membrane formed from the ceramic support toward the surface of the multilayered ceramic membrane. It is an object of the present invention to provide a ceramic filter capable of increasing a film area.
[課題を解決するための手段] 本発明は、三次元網目状構造を有する多孔質セラミッ
クス支持体の一部を除く骨格の表面に、この多孔質セラ
ミックス支持体のもつ細孔径よりも小さい細孔径をもつ
セラミック膜が複数層形成され、しかもセラミックス支
持体内部から複数層形成されたセラミック膜表面に向っ
て細孔径が内部から表面にゆくに従って順次小さくなっ
ていることを特徴とするセラミックフィルターである。[Means for Solving the Problems] The present invention provides a porous ceramic support having a three-dimensional network structure on a surface of a skeleton excluding a part of the porous ceramic support having a pore size smaller than the pore size of the porous ceramic support. The ceramic filter is characterized in that a plurality of ceramic membranes having a plurality of layers are formed, and the pore diameter is gradually reduced from the inside to the surface from the inside of the ceramic support toward the surface of the ceramic membrane formed with the plurality of layers. .
本発明において、多孔質セラミックス支持体を三次元
網目構造とするために、セラミックススラリーを発泡さ
せて泡状とする技術を用いた。この技術によれば、網目
状セラミックスに欠陥が導入され難い。また、三次元網
目構造の支持体表面に膜を形成する際、膜にピンホール
等の欠陥が発生するのを回避するために、んセラミック
発泡成形体をバインダーを溶解する溶剤によって処理し
たり、または仮焼後薄いセラミックスリップに浸漬した
りして、網目を構成するセラミックス断面を実質的に円
形にすることが望ましい。なお、三次元網目構造のセラ
ミックス支持体は、通常ポリウレタンフォーム等の表面
にセラミックススリップを付着させて成形体を作り、こ
れを焼成することによりウレタンフォームを焼散してセ
ラミックス支持体のみとすることにより形成する。しか
し、この技術によれば、ウレタンが存在していた所が
穴となり,網目の強度を著しく低下させる、ウレタン
の表面に付着したセラミックススリップが乾燥し収縮す
る際発生するマイクロクラックを多くもっている、ウ
レタンが分解する際発生するガスによって網目にクラッ
クが発生する等、多くの欠陥をもっているため好ましく
ない。In the present invention, in order to form a porous ceramic support into a three-dimensional network structure, a technique of foaming a ceramic slurry to form a foam is used. According to this technique, it is difficult for defects to be introduced into the network ceramics. Further, when forming a film on the surface of the support having a three-dimensional network structure, in order to avoid occurrence of defects such as pinholes in the film, the ceramic foam molded body is treated with a solvent that dissolves a binder, Alternatively, it is preferable that the cross section of the ceramic constituting the mesh is made substantially circular by dipping in a thin ceramic slip after calcination. Note that a ceramic support having a three-dimensional network structure usually has a ceramic slip attached to the surface of a polyurethane foam or the like to form a molded body, which is then fired to burn off the urethane foam to form only the ceramic support. Is formed. However, according to this technique, the place where the urethane was present becomes a hole, significantly reducing the strength of the network, and has many micro cracks generated when the ceramic slip attached to the urethane surface dries and shrinks. Gases generated when urethane is decomposed have many defects such as cracks in the mesh, which is not preferable.
本発明において、セラミックス支持体を多孔質とする
のは、網目を構成するセラミックス支持体中をろ過後の
流体の流路とするためである。また、網目形状をなすセ
ラミックス支持体の材質は、強度と流体の透過抵抗から
決めることになる。In the present invention, the reason why the ceramic support is made porous is to make the inside of the ceramic support constituting the network a flow path of the fluid after filtration. Further, the material of the ceramic support having the mesh shape is determined based on the strength and the permeation resistance of the fluid.
本発明において、網目状構造体部分を流れた流体を集
めて流す流路の太い骨状構造体を網目状セラミックスと
組み合わせることも、単位面積当りの膜面積を大きく取
るのに効果的である。例えば、動物における血管系や植
物の葉のように細い流路を集めて太い流路にする。In the present invention, it is also effective to combine a mesh-like ceramic with a bone-like structure having a large flow path for collecting and flowing the fluid flowing through the network-like structure, in order to increase the membrane area per unit area. For example, thin channels such as the vasculature of an animal or leaves of a plant are collected into a thick channel.
本発明において、網目状の多孔質セラミックスに骨状
の多孔質セラミックスを組み合わせるには、予め加圧成
形その他の方法で骨状多孔質セラミックス素材を成形
し、加工、仮焼したものを、泡立て後に未乾燥の泡に挿
入し一体化するなどの方法により可能である。また、別
々に成形した泡成形体と骨成形体を加工し仮焼したもの
を組立て、泡を形成するためのスラリーで接合しても良
い。In the present invention, in order to combine the mesh-like porous ceramics with the bone-like porous ceramics, the bone-like porous ceramics material is previously molded by pressure molding or other methods, processed, calcined, and after bubbling. It is possible by a method such as insertion into an undried foam and integration. Alternatively, a separately molded foam compact and a bone compact may be processed and calcined, assembled, and joined with a slurry for forming foam.
本発明において、セラミックス支持体中に透過抵抗の
少ないような連通する気孔を導入する方法としては、比
較的粒径の大きい粒子と微粉とを配合し、粒径の大きい
粒子が焼結時に変形し難く、大粒子間に気孔が導入され
易いという性質を利用した方法でも良いし、他の方法で
も良い。In the present invention, as a method of introducing communicating pores having a low permeation resistance into the ceramic support, particles having a relatively large particle size and fine powder are blended, and the particles having a large particle size are deformed during sintering. It may be a method utilizing the property of being difficult to introduce pores between large particles, or may be another method.
本発明において、多孔質セラミックス支持体の表面に
この多孔質セラミックスのもつ細孔径よりも小さい細孔
径をもつセラミックス膜を形成する手段としては、公知
である浸漬法、つまりセラミックスを形成するセラミッ
クス微粒子を懸濁させた液体にセラミックス支持体を浸
漬し、多孔質の支持体中に液体を吸収し、懸濁している
セラミックス微粒子を支持体表面に付着させることによ
り可能である。ここで、セラミックス微粒子が支持体の
表面に付着するためには、支持体の気孔径と微粒子の径
の相対的関係が重要で、微粒子径が小さすぎると支持体
内部に侵入してしまう。また、支持体表面に付着した微
粒子層は、加熱して支持体に焼き付けることができる。
焼き付け条件は、微粒子の粒子成長度合、焼付け強度を
勘案して決められる。具体的には、焼付け温度が高くな
ると粒子成長が進行し微粒子による膜気孔径が大きくな
るとともに、支持体への焼付け強度が高くなる。一方、
焼付け温度が高すぎると、膜の収縮が進み、膜表面に地
割れ状のクラックが発生する。In the present invention, as a means for forming a ceramic film having a pore diameter smaller than the pore diameter of the porous ceramic on the surface of the porous ceramic support, a known immersion method, that is, fine ceramic particles forming the ceramic is used. This is possible by immersing the ceramic support in the suspended liquid, absorbing the liquid in the porous support, and attaching the suspended ceramic fine particles to the surface of the support. Here, in order for the ceramic fine particles to adhere to the surface of the support, the relative relationship between the pore diameter of the support and the diameter of the fine particles is important. If the diameter of the fine particles is too small, they will penetrate into the support. Further, the fine particle layer attached to the support surface can be heated and baked on the support.
The baking conditions are determined in consideration of the degree of particle growth of the fine particles and the baking strength. Specifically, as the baking temperature increases, the particle growth progresses, the pore diameter of the film due to the fine particles increases, and the baking strength to the support increases. on the other hand,
If the baking temperature is too high, shrinkage of the film proceeds, and ground cracks occur on the film surface.
なお、本発明に係るセラミックフィルターは、三次元
網目構造を有する多孔質セラミックス支持体の表面に、
この多孔質セラミックスのもつ細孔径よりも小さい径を
もつセラミック膜が形成された構成のものでもよい。ま
た、上記セラミックフィルターにおいて、三次元網目構
造を有する多孔質セラミック支持体中に、前記網目構造
体と同材質であり、かつ前記網目構造体の骨格部分より
も太い骨状構造を有し、網目構造体と骨状構造体の内部
が一体となって連通し、網目構造体と骨状構造体の表面
に形成されたセラミックフィルターの一部もしくは全て
の表面にフィルター膜が形成されていてもよい。Incidentally, the ceramic filter according to the present invention, the surface of the porous ceramic support having a three-dimensional network structure,
A configuration in which a ceramic film having a diameter smaller than the pore diameter of the porous ceramic is formed may be used. Further, in the ceramic filter, the porous ceramic support having a three-dimensional network structure has a bone-like structure made of the same material as the network structure and having a thickness larger than a skeleton portion of the network structure. The structure and the inside of the bone-like structure may integrally communicate with each other, and a filter membrane may be formed on a part or all of the surface of the ceramic filter formed on the surface of the mesh structure and the bone-like structure. .
[作用] 本発明によれば、単位面積当りの膜面積を大きくでき
るセラミックスフィルターが得られる。[Operation] According to the present invention, a ceramics filter capable of increasing the film area per unit area is obtained.
[実施例] 以下、本発明の一実施例について説明する。Example An example of the present invention will be described below.
(1)攪拌発泡; 平均粒径20μmのアルミナ粒子90重量部、一次粒径0.
2μmの高純度アルミナ粉10重量部、イオン交換水50重
量部、バインダーとしてメチルセルローズ5重量部、整
泡剤としてのステアリン酸アンモニウム5重量部、分散
剤ポリアクリル酸アンモニウム0.5重量部を攪拌機中に
投入し、攪拌発泡させた。(1) Agitated foaming; 90 parts by weight of alumina particles having an average particle diameter of 20 μm, and a primary particle diameter of 0.
10 parts by weight of 2 μm high-purity alumina powder, 50 parts by weight of ion-exchanged water, 5 parts by weight of methylcellulose as a binder, 5 parts by weight of ammonium stearate as a foam stabilizer, and 0.5 parts by weight of a dispersant ammonium polyacrylate are placed in a stirrer. It was charged and stirred and foamed.
(2)丸棒の形成; 平均粒径20μmのアルミナ粒子90重量部、一次粒径0.
2μmの高純度アルミナ粉10重量部、イオン交換水20重
量部、バインダーとしてメチルセルローズ5重量部をら
い潰機で混合し、40メッシュのナイロン篩を通して造粒
し、乾燥して造粒粉とした。次に、この造粒粉を50Kg/c
m2の圧力で加圧成形し、50mm×50mm×5mmの板状成形体
とした。次いで、この成形体を1200℃で1時間空気中で
加熱して仮焼体を得た後、これを機械加工して4φ×40
mmの丸棒とした。(2) Formation of a round bar; 90 parts by weight of alumina particles having an average particle size of 20 μm, and a primary particle size of 0.
10 parts by weight of 2 μm high-purity alumina powder, 20 parts by weight of ion-exchanged water, and 5 parts by weight of methylcellulose as a binder were mixed with a crusher, granulated through a 40-mesh nylon sieve, and dried to obtain a granulated powder. . Next, 50 kg / c
Pressure molding was performed at a pressure of m 2 to obtain a 50 mm × 50 mm × 5 mm plate-like molded body. Next, the molded body was heated in the air at 1200 ° C. for one hour to obtain a calcined body, which was then machined to obtain a 4 × 40
mm round bar.
(3)支持体の形成; 上記丸棒を上記泡の中に挿入し、同時に乾燥した。次
に、この乾燥体を加工して10φ×40mmの棒状とした。こ
の際、φ4の仮焼体の軸中心を加工中心とした。次い
で、この加工体を空気中1200℃、1時間焼成した後、水
素雰囲気中で1900℃、2時間焼成して支持体とした。こ
の支持体は、第1図に示す如く、中心部にφ3.9mmの太
い骨状構造部1、この骨造構造部1の周囲に太さ0.3mm
でセル径1mmの網目状構造部2が取り巻いている。セラ
ミックス材質は、気孔率30%、10μmの気孔径であっ
た。第2図は第1図のX−X線に沿う断面図、第3図は
第2図の部分拡大図である。なお、図において、骨状構
造部1の一端(X)側に膜3が形成され、他端(Y)に
は膜が形成されていない。また、4は骨状構造部1表面
の膜5と連通した網目状構造部2の表面の膜であり、網
目状構造部2の内部は気孔の大きい多孔体となってい
る。(3) Formation of support; The round bar was inserted into the foam and dried at the same time. Next, this dried body was processed into a rod shape of 10φ × 40 mm. At this time, the axis center of the calcined body of φ4 was set as the processing center. Next, the processed body was fired in air at 1200 ° C. for 1 hour, and then fired in a hydrogen atmosphere at 1900 ° C. for 2 hours to obtain a support. As shown in FIG. 1, the support has a thick bone-like structure 1 having a diameter of 3.9 mm at the center and a thickness of 0.3 mm around the bone structure 1.
And a mesh structure 2 having a cell diameter of 1 mm is surrounded. The ceramic material had a porosity of 30% and a pore diameter of 10 μm. FIG. 2 is a sectional view taken along line XX of FIG. 1, and FIG. 3 is a partially enlarged view of FIG. In the figure, the film 3 is formed on one end (X) side of the bone-like structure portion 1, and the film is not formed on the other end (Y). Reference numeral 4 denotes a film on the surface of the network structure 2 which communicates with the film 5 on the surface of the bone structure 1. The inside of the network structure 2 is a porous body having large pores.
次に、一次粒径1μm,凝集体の平均粒径3μmの高純
度アルミナ粉体3重量部をイオン交換水100重量部中に
分散したスリップに上記支持体を浸漬した後、室内に放
置して乾燥した。これを1500℃で2時間空気中で焼き付
け、膜が一層形成された支持体(成膜体)を得た。Next, the support was immersed in a slip obtained by dispersing 3 parts by weight of high-purity alumina powder having a primary particle diameter of 1 μm and an average particle diameter of aggregates of 3 μm in 100 parts by weight of ion-exchanged water. Dried. This was baked in air at 1500 ° C. for 2 hours to obtain a support (film-formed body) on which a single layer of film was formed.
次に、一次粒径0.2μm、凝集体の平均粒径1μmの
高純度アルミナ粉体1重量部をイオン交換水100重量部
中に分散したスリップに上記成膜体を浸漬し、乾燥した
後、1200℃で2時間空気中で焼き付けた。つづいて、こ
れの骨状構造部1端部をダイヤモンドグラインダーで加
工し、骨状構造部1端部の膜部分を除去した。ひきつづ
き、これを内径φ12mmのステンレス管に、テフロンガス
ケットを用いてセラミックスを固定した。このステンレ
ス管の一方から導入される空間はセラミックの外側空間
と導通させ、他の一方は膜を除去した管の内部空間と導
通させ、フィルターモジュールとした。Next, the above-mentioned film-formed body was immersed in a slip obtained by dispersing 1 part by weight of high-purity alumina powder having a primary particle diameter of 0.2 μm and an average particle diameter of aggregates of 1 μm in 100 parts by weight of ion-exchanged water, and then dried. Baking in air at 1200 ° C. for 2 hours. Subsequently, the end of the bone-like structure 1 was processed with a diamond grinder to remove the film portion at the end of the bone-like structure 1. Subsequently, ceramics were fixed to a stainless steel tube having an inner diameter of 12 mm using a Teflon gasket. The space introduced from one of the stainless steel tubes was connected to the outer space of the ceramic, and the other was connected to the inner space of the tube from which the membrane had been removed, to form a filter module.
このモジュールの外径はφ15mm、長さ50mm、体積9c
m3、膜面積238cm2であった。これに対し、従来のフィル
ターモジュールは、外径φ50mm、長さ70mm、体積137c
m3、膜面積は143cm2であった。The outer diameter of this module is φ15mm, length 50mm, volume 9c
m 3 and a membrane area of 238 cm 2 . In contrast, the conventional filter module has an outer diameter of 50 mm, a length of 70 mm, and a volume of 137 c.
m 3 , and the membrane area was 143 cm 2 .
なお、本発明のものは、アルミナセラミックスに限ら
ず、粉粒体を成形,焼結して作られる他成分のセラミッ
クスによっても作り得るものである。例えば、セラミッ
クス材質が、シリカ,ジルコニア,スピネル,ムライト
などの酸化物や窒化珪素,炭化珪素などの非酸化物でも
よい。It should be noted that the present invention is not limited to alumina ceramics, but can also be made of ceramics of other components made by molding and sintering a granular material. For example, the ceramic material may be an oxide such as silica, zirconia, spinel, or mullite, or a non-oxide such as silicon nitride or silicon carbide.
[発明の効果] 以上詳述した如く本発明によれば、三次元網目状構造
を有する多孔質セラミックス支持体の一部を除く骨格の
表面に、この多孔質セラミックス支持体のもつ細孔径よ
りも小さい細孔径をもつセラミックス膜が複数層形成さ
れ、しかもセラミックス支持体内部から複数層形成され
たセラミック膜表面に向って細孔径が内部から表面にゆ
くに従って順次小さくなる構成等を採用することによ
り、単位面積当りの膜面積を大きくできるセラミックフ
ィルターを提供できる。[Effects of the Invention] As described above in detail, according to the present invention, the surface of the skeleton excluding a part of the porous ceramic support having a three-dimensional network structure is larger than the pore diameter of the porous ceramic support. By adopting a structure in which a plurality of ceramic films having a small pore diameter are formed, and the pore diameter gradually decreases from the inside to the surface from the inside of the ceramic support toward the surface of the ceramic film formed of the plurality of layers, A ceramic filter capable of increasing the membrane area per unit area can be provided.
第1図は本発明の一実施例に係る支持体の略斜視図、第
2図は第1図のX−X線に沿う断面図、第3図は第2図
の部分拡大図である。 1……骨状構造部、2……網目状造部、3,4,5……膜。FIG. 1 is a schematic perspective view of a support according to one embodiment of the present invention, FIG. 2 is a sectional view taken along line XX of FIG. 1, and FIG. 3 is a partially enlarged view of FIG. 1 ... bone-like structure part, 2 ... mesh-like structure part, 3, 4, 5 ... membrane.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 武藤 唯義 神奈川県秦野市曽屋30番地 東芝セラミ ックス株式会社秦野工場内 (58)調査した分野(Int.Cl.7,DB名) B01D 39/20 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Tadayoshi Muto 30 Soya, Hadano-shi, Kanagawa Toshiba Ceramics Co., Ltd. Hadano Plant (58) Field surveyed (Int.Cl. 7 , DB name) B01D 39/20
Claims (1)
クス支持体の一部を除く骨格の表面に、この多孔質セラ
ミックス支持体のもつ細孔径よりも小さい細孔径をもつ
セラミック膜が複数層形成され、しかもセラミックス支
持体内部から複数層形成されたセラミック膜表面に向っ
て細孔径が内部から表面にゆくに従って順次小さくなっ
ていることを特徴とするセラミックフィルター。1. A plurality of ceramic films having pore diameters smaller than the pore diameter of the porous ceramics support are formed on the surface of the skeleton excluding a part of the porous ceramics support having a three-dimensional network structure. A ceramic filter, characterized in that the pore diameter gradually decreases from the inside toward the surface of the ceramic film having a plurality of layers formed from the inside of the ceramic support.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2340581A JP3071218B2 (en) | 1990-11-30 | 1990-11-30 | Ceramic filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2340581A JP3071218B2 (en) | 1990-11-30 | 1990-11-30 | Ceramic filter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04200704A JPH04200704A (en) | 1992-07-21 |
JP3071218B2 true JP3071218B2 (en) | 2000-07-31 |
Family
ID=18338370
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2340581A Expired - Fee Related JP3071218B2 (en) | 1990-11-30 | 1990-11-30 | Ceramic filter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3071218B2 (en) |
-
1990
- 1990-11-30 JP JP2340581A patent/JP3071218B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH04200704A (en) | 1992-07-21 |
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