JPH02229515A - Ceramic filter for filtration of molten metal and its manufacturing method - Google Patents

Ceramic filter for filtration of molten metal and its manufacturing method

Info

Publication number
JPH02229515A
JPH02229515A JP2002669A JP266990A JPH02229515A JP H02229515 A JPH02229515 A JP H02229515A JP 2002669 A JP2002669 A JP 2002669A JP 266990 A JP266990 A JP 266990A JP H02229515 A JPH02229515 A JP H02229515A
Authority
JP
Japan
Prior art keywords
manufacturing
slurry
filter
ceramic
foam material
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
JP2002669A
Other languages
Japanese (ja)
Inventor
Werner Kallisch
ヴェルナー カリッシュ
Reiner Stotzel
ライナー ステッツェル
Rolf Reitzscher
ロルフ リーツシャー
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.)
Georg Fischer AG
Original Assignee
Georg Fischer AG
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 Georg Fischer AG filed Critical Georg Fischer AG
Publication of JPH02229515A publication Critical patent/JPH02229515A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22CFOUNDRY MOULDING
    • B22C9/00Moulds or cores; Moulding processes
    • B22C9/08Features with respect to supply of molten metal, e.g. ingates, circular gates, skim gates
    • B22C9/086Filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/20Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
    • B01D39/2068Other inorganic materials, e.g. ceramics
    • B01D39/2093Ceramic foam
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/06Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by burning-out added substances by burning natural expanding materials or by sublimating or melting out added substances
    • C04B38/0615Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof by burning-out added substances by burning natural expanding materials or by sublimating or melting out added substances the burned-out substance being a monolitic element having approximately the same dimensions as the final article, e.g. a porous polyurethane sheet or a prepreg obtained by bonding together resin particles
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/02Refining by liquating, filtering, centrifuging, distilling, or supersonic wave action including acoustic waves
    • C22B9/023By filtering
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/04Additives and treatments of the filtering material
    • B01D2239/0471Surface coating material
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00612Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00793Uses not provided for elsewhere in C04B2111/00 as filters or diaphragms
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Geology (AREA)
  • Metallurgy (AREA)
  • Structural Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Acoustics & Sound (AREA)
  • Physics & Mathematics (AREA)
  • Manufacturing & Machinery (AREA)
  • Filtering Materials (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
  • Filtration Of Liquid (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は、耐熱性セラミックを基材とする開放セル型発
泡構造体を含み、かつ、溶湯の質流方向と交差する一対
の質流面と、ほぼ質流方向に向けて延在する少なくとも
一つの外周側面とを具える溶湯ろ過用セラミックフィル
タに関し、特に、有機発泡材料に高粘度スラリー状のセ
ラミックを含浸させて乾燥させた後、加熱を行って有機
発泡材料を除去すると共に残余のセラミックを焼成し、
さらに、所要に応じて乾燥後に耐火材料で事後の表面処
理を施して成る溶湯ろ過用セラミックフィルタに関する
ものである。さらに、本発明は上記セラミックフィルタ
の製造方法に関するものでもある。
[Detailed Description of the Invention] [Technical Field] The present invention includes an open cell foam structure made of a heat-resistant ceramic as a base material, and has a pair of mass flow surfaces that intersect with the mass flow direction of molten metal, and approximately Regarding a ceramic filter for molten metal filtration comprising at least one outer circumferential side surface extending in the mass flow direction, in particular, the ceramic filter is impregnated with a ceramic in the form of a high viscosity slurry into an organic foam material, dried, and then heated. The organic foam material is removed and the remaining ceramic is fired,
Furthermore, the present invention relates to a ceramic filter for filtrating molten metal which is subjected to surface treatment with a refractory material after drying as required. Furthermore, the present invention also relates to a method of manufacturing the above ceramic filter.

〔従来技術〕[Prior art]

上述の構成を有するセラミックフィルタは従来既知であ
り、製造すべき鋳造製品からスラグ、砂および耐火材料
等の不純物の混入を排除するために鋳造業界において慣
用されている。
Ceramic filters of the above-mentioned construction are known in the art and are commonly used in the foundry industry to exclude impurities such as slag, sand and refractory materials from the cast products to be manufactured.

通常、開放セル型の発泡構造を有するセラミックフィル
タを製造するに際しては、例えばポリウレタンフォーム
のような有機発泡材料にセラミック材料の低粘度スラリ
ーを含浸させ、あるいは高粘度スラリーを含浸させた後
にローラ対により余剰のスラリーを押出す。低粘度スラ
リーを用いる場合、セラミック材料は、発泡構造体全体
に亘ってほぼ均等に分配される。他方、高粘度スラIJ
一を用いる場合には、発泡材料の圧密硬度、ローラ間隙
およびスラリーのレオロジー的特性に応じて、発泡構造
体内部に、またはローラを通過する搬送方向と平行な側
面に沿ってスラリー質量の堆積を生じる傾向が認められ
ている。
Normally, when manufacturing a ceramic filter having an open cell foam structure, an organic foam material such as polyurethane foam is impregnated with a low viscosity slurry of ceramic material, or after being impregnated with a high viscosity slurry, a pair of rollers is used. Push out excess slurry. When using a low viscosity slurry, the ceramic material is distributed approximately evenly throughout the foam structure. On the other hand, high viscosity slug IJ
Depending on the consolidation hardness of the foam material, the roller gap and the rheological properties of the slurry, the slurry mass can be deposited inside the foam structure or along the sides parallel to the direction of conveyance past the rollers. There is a recognized tendency for this to occur.

所要のろ過作用を確実に達成するため、フィルタには、
溶湯に対する優れた耐熱性および機械的強度を付与する
必要がある。既知のフィルタにおいては、注湯に依存し
て所定の割合で溶渦中でのセラミックの破損・侵食が絶
えず生じる。かかる破損・侵食は、特に、溶湯の貫流方
向に向けて延在する側面が対応するローラを通過する際
に材料の集積密度が増加する場合であっても当該側面の
領域で、並びに外部に向けて開放した発泡構造体の中空
橋絡部で生じるものである。この中空橋絡部は、スラリ
ーを含浸させた発泡材料を次の処理位置まで搬送する過
程でスラリーの一部が再び除去され、発泡材料の焼成処
理の間に発生する蒸気圧によりセル橋絡部に生じるスリ
ット状の開口に由来するものである。
To ensure that the desired filtration action is achieved, the filter is
It is necessary to provide excellent heat resistance and mechanical strength against molten metal. In known filters, the ceramic is constantly damaged and eroded in the melt at a certain rate depending on the pouring. Such damage/erosion can occur in particular in the area of the side surfaces extending in the direction of flow of the molten metal, even if the accumulation density of the material increases as they pass through the corresponding rollers, as well as towards the outside. This occurs at the hollow bridging portion of the foam structure that is opened. During the process of conveying the foamed material impregnated with slurry to the next processing position, part of the slurry is removed again, and the cell bridge is formed by the vapor pressure generated during the firing process of the foamed material. This originates from the slit-like openings that occur in the.

国際公開第W0 82/03339号公報には、耐熱性
セラミック材料を基材とする開放セル型発泡構造のセラ
ミックフィルタが記載されいる。この既知のセラミック
フィルタは、有機発泡材料に高粘度のセラミック材料の
スラリーを含浸させ、引続いて乾燥、加熱および力焼を
行って発泡性材料を除去することにより製造されるもの
である。この場合、余剰のスラリーは、含浸処理を施し
た発泡材料がローラ対におけるローラ間隙を通過する際
に押出して除去する。さらに、フィルタの表面に露出し
たセル橋絡部を破損から確実に保護するために、乾燥お
よび含浸処理を施した発泡材料の表面にセラミック材料
のスラリーを更に含浸させる。その場合、フィルタの耐
熱性は向上する。しかし、この追加的な含浸は、一方で
は、露出したセル橋絡邪のみならず、その下方のフィル
タ領域にもフィルタの透過度を損なう追加的なスラリー
層が形成される点で不利であり、他方では、多くの実施
例において十分な強度が得られず、特に溶湯の落差が増
大すると不十分な強度に由来して依然として破損および
侵食や傾向が認やられている。
International Publication No. WO 82/03339 describes a ceramic filter having an open cell foam structure and having a heat-resistant ceramic material as a base material. This known ceramic filter is manufactured by impregnating an organic foam material with a slurry of highly viscous ceramic material, followed by drying, heating and firing to remove the foamable material. In this case, the excess slurry is extruded and removed when the impregnated foam material passes through the roller gap in the roller pair. Furthermore, in order to reliably protect the cell bridges exposed on the surface of the filter from damage, the surface of the dried and impregnated foam material is further impregnated with a slurry of ceramic material. In that case, the heat resistance of the filter is improved. However, this additional impregnation is disadvantageous in that, on the one hand, an additional slurry layer is formed not only in the exposed cell bridging but also in the filter area below it, impairing the filter's permeability; On the other hand, in many embodiments sufficient strength is not obtained, and a tendency to breakage and erosion is still observed due to insufficient strength, especially as the head of the molten metal increases.

〔発明の開示〕[Disclosure of the invention]

本発明の課題は、溶湯に対する機械的および熱的安定性
および耐久性に優れた前述の形式のセラミックフィルタ
を提案することにある。
The object of the present invention is to propose a ceramic filter of the type mentioned above which has excellent mechanical and thermal stability and durability against molten metal.

この課題を解決するため、本発明によるセラミックフィ
ルタは、溶湯の貫流方向に向けて延在する少なくとも一
つの外周側面の全面に、厚みが0.5〜3 mmの耐火
材料から成る閉鎖層を形成したことを特徴とするもので
ある。
In order to solve this problem, the ceramic filter according to the present invention forms a closed layer made of a refractory material with a thickness of 0.5 to 3 mm on the entire surface of at least one outer peripheral side surface extending in the flow direction of the molten metal. It is characterized by the fact that

上述の構成を有するフィルタは、周囲の側面領域におい
て閉鎖したフレームを形成することが可能となる。その
際、特に、貫流面における開放セル橋絡部は、フィルタ
の透過性を損なわない被覆層により閉鎖される。
A filter with the above-mentioned configuration makes it possible to form a closed frame in the surrounding side areas. In particular, the open cell bridges on the flow-through surface are closed off with a covering layer that does not impair the permeability of the filter.

製造すべきフィルタの寸法に合わせた有機発泡材料にお
ける周囲の側面領域は、底面が円形または長円形のフィ
ルタの場合、筒状外周面である。
The peripheral lateral area of the organic foam material adapted to the dimensions of the filter to be produced is a cylindrical outer circumferential surface in the case of filters with a circular or oblong base.

この側面領域に耐火性材料を発泡材料に被着することに
より、当該領域における周方向の全長に亘り厚みが0.
5〜3 mmの閉鎖層が形成される。発泡構造体の貫流
面における開放セル橋絡部は、耐火材料による被覆事後
処理を施すことができる。
By applying a fire-resistant material to the foam material in this side region, the thickness is reduced to 0.000000 over the entire circumferential length of this region.
A closure layer of 5-3 mm is formed. The open cell bridges on the flow-through side of the foam structure can be subsequently coated with a refractory material.

開放セル僑絡部は0.1〜l m+nの厚みで被覆する
のが好適であり、特に単位面積当たりの被覆質量は40
〜400 mg/cイとなる。
It is preferable to coat the open cell part with a thickness of 0.1 to lm+n, and in particular, the coating mass per unit area is 40
~400 mg/c.

側面の閉鎖層は、開放したセル橋絡部の被覆と同様に、
含浸に用いるものと同一のセラミックスラリーから形成
するのが好ましい。ここで使用される材料としては、例
えば、主成分がAl20,よりなる物質またはケイ線石
、ムライトもしくはシャモット等、耐火性に優れ、特に
アルミニウムを多く含有する既知の物質が挙げられる。
The lateral closure layer, as well as the covering of the open cell bridges,
Preferably, it is formed from the same ceramic slurry used for impregnation. The materials used here include, for example, substances whose main component is Al20, or known substances which are excellent in fire resistance and contain a particularly large amount of aluminum, such as sillimanite, mullite, or chamotte.

使用するスラリーの粘性は、2Orpmの回転速度下で
IXIO’〜2xlO’ cpsとするのが有利である
。場合によっては、開放セル橋絡部の閉鎖層および/ま
たは被覆層を形成するため、含漫に用いたスラリーの代
わりに、異種の耐火性材料から成るスラリー、または例
えば水ガラス、シリカゾル、樹脂、燐酸塩アルミニウム
、酸化ジルコン塩化物、珪酸塩エチルのような空気で結
合する耐火性材料を用いることができる。
Advantageously, the viscosity of the slurry used is between IXIO' and 2xlO' cps at a rotation speed of 2 Orpm. In some cases, slurries of different refractory materials, such as water glass, silica sols, resins, Air-bonded refractory materials such as aluminum phosphate, zirconium oxide chloride, and ethyl silicate can be used.

〔発明を実施するための最良の形態〕[Best mode for carrying out the invention]

以下、本発明を図示の実施例について一層具体的に説明
する。
Hereinafter, the present invention will be described in more detail with reference to the illustrated embodiments.

第1図は焼成前のフィルタ素材の断面を示すものであり
、同フィルタ素材は発泡性ポリウレタンのような有機材
料から成る発泡構造体lを具えている。発泡構造体1は
、例えば順次相互に隣接する4つの周方向側面2と、相
互に離間して平行に配置される一対の端面(貫流面)3
とを有する直方体形状に形成する。次いで、発泡構造体
1には高粘度スラリー状のセラミック材料4を含浸させ
る。後述するように、全ての側面2には耐火材料から成
る0.5〜3 mmの厚みの閉鎖層5を形成する。
FIG. 1 shows a cross-section of the filter material before firing, which includes a foamed structure l of an organic material such as foamed polyurethane. The foam structure 1 includes, for example, four circumferential side surfaces 2 that are adjacent to each other in sequence, and a pair of end surfaces (through-flow surfaces) 3 that are spaced apart and arranged in parallel.
It is formed into a rectangular parallelepiped shape having Next, the foamed structure 1 is impregnated with a ceramic material 4 in the form of a high viscosity slurry. As will be described later, all side surfaces 2 are provided with a closing layer 5 made of a refractory material and having a thickness of 0.5 to 3 mm.

この耐火材料は、特に発泡構造体に含浸させたものと同
一のスラリー状セラミック材料により構成する。さらに
、質流面3の開放セル橋絡部6には耐火材料から成る被
覆層7を形成する。この被覆層7も、発泡構造体1に含
浸させたものと同一のスラリー状セラミック材料により
構成する。焼成を行うと発泡構造体1が燃尽すると共に
、スラリー状をなしていたセラミック材料が硬化する。
This refractory material consists in particular of the same slurry ceramic material with which the foam structure is impregnated. Further, a coating layer 7 made of a refractory material is formed on the open cell bridging portion 6 of the flow surface 3. This coating layer 7 is also made of the same slurry ceramic material with which the foamed structure 1 is impregnated. When fired, the foamed structure 1 is burned out and the ceramic material in the form of slurry is hardened.

第2a図および第2b図に示すように、側面2の領域に
閉鎖層5を形成するためには、スラリーを含浸させた発
泡構造体lに、発泡構造体1と同一の底面形状を有する
スタンパ8によって所定時間に亘り圧力を負荷する。そ
の結果、第2a図に示すように、余剰のスラリーが側面
2の領域に達し、側面2上に部分的にビード状をなして
集中する。発泡構造体1から圧力を除荷すべくスタンパ
8を持ち上げると、全面が閉鎖されたスラリーのフレー
ムが形成される。これは、周側面2における余剰スラリ
ーのビードが、圧力の緩和時に周側面2上に均等に分布
するに至るためである。次に、スラリーを含浸させた発
泡構造体1を乾燥させて焼成し、焼成前または焼成後に
被覆層7を形成する。
As shown in FIGS. 2a and 2b, in order to form a closure layer 5 in the area of the side surface 2, a foam structure l impregnated with slurry is stamped with a stamper having the same bottom shape as the foam structure 1. 8 to apply pressure for a predetermined period of time. As a result, the excess slurry reaches the region of the side surface 2 and is concentrated thereon in the form of a partial bead, as shown in FIG. 2a. When the stamper 8 is lifted to release the pressure from the foam structure 1, a frame of slurry closed on all sides is formed. This is because the beads of excess slurry on the circumferential side 2 become evenly distributed on the circumferential side 2 when the pressure is relieved. Next, the foamed structure 1 impregnated with the slurry is dried and fired, and the coating layer 7 is formed before or after firing.

第3図に示すように、発泡構造体1は、スラリーを含浸
させた後に開放ベルト対9に通しても良い。すなわち、
スラリーを含浸させた発泡構造体1をベルト対9の間で
押圧することにより、余剰のスラリーを側面2まで押出
して側面上にビードを形成する。発泡構造体lがベルト
対9を通過すると圧力が除荷されるので、スラリーのビ
ードは両側の側面2上で均等に分布するに至り、両側に
一対の閉鎖層5が形成される。
As shown in FIG. 3, the foamed structure 1 may be passed through a pair of open belts 9 after being impregnated with the slurry. That is,
By pressing the foamed structure 1 impregnated with the slurry between the belt pair 9, excess slurry is pushed out to the side surface 2 and a bead is formed on the side surface. As the foam structure 1 passes through the pair of belts 9, the pressure is released so that the beads of slurry become evenly distributed on both sides 2, forming a pair of closure layers 5 on both sides.

第4図に示す実施例においては、スラリーを含浸させて
乾燥した発泡構造体1を水平搬送装置10により搬送し
、垂直軸線を有するローラ対11を通過させることによ
り閉鎖層5を形成する。ローラ対11により発泡構造体
1における一対の側面2に耐火材料、スラリーまたは空
気で結合する材料を塗布し、かつ、所定の深さまで多孔
質の発泡構造体内に侵入させる。その際、ドクターブレ
ードまたはドクターロール等を使用することにより、ロ
ーラ表面に可及的に均一な厚みの塗布材料層を形成する
In the embodiment shown in FIG. 4, the foamed structure 1 impregnated with slurry and dried is transported by a horizontal transport device 10 and passed through a pair of rollers 11 having a vertical axis to form a closure layer 5. A refractory material, slurry or air bonding material is applied to a pair of side surfaces 2 of the foam structure 1 by a pair of rollers 11 and penetrated into the porous foam structure to a predetermined depth. At that time, by using a doctor blade, a doctor roll, or the like, a coating material layer with as uniform a thickness as possible is formed on the roller surface.

閉鎖層5を形成する上記工程を第3図に示す工程に引続
いて行うと、全ての外側面2に閉鎖層5を形成すること
ができる。もっとも、全ての側面2に閉鎖層5を形成す
るためには、第4図に示す装置を二組順次に配置すると
共に、各装置間で発泡構造体1を90゜回転させる構成
としても良い。
If the above step of forming the closure layer 5 is performed subsequent to the step shown in FIG. 3, the closure layer 5 can be formed on all the outer surfaces 2. However, in order to form the closure layer 5 on all the side surfaces 2, two sets of devices shown in FIG. 4 may be sequentially arranged, and the foamed structure 1 may be rotated by 90 degrees between each device.

閉鎖層5を形成する更に別の方法として、発泡構造体1
の側面2に適当な気孔率を有する発泡材料から成る別の
層を接着するか、または微細な接着材m維東を側面2上
に設けることも可能である。
As yet another method of forming the closure layer 5, the foam structure 1
It is also possible to glue a further layer of foamed material with a suitable porosity to the side surface 2 or to provide a fine adhesive material on the side surface 2.

このような発泡構造体1にスラリーを含浸させると、外
側面領域における微細な気孔(空隙)がスラリーで充た
された状態に保持されるため、閉鎖層5を容易に形成す
ることが可能となる。
When such a foamed structure 1 is impregnated with slurry, the fine pores (voids) in the outer surface area are kept filled with the slurry, so that the closed layer 5 can be easily formed. Become.

第4図に示す方法は、既に焼成処理を施したフィルタの
外側面2に空気で結合する耐火材料から成る閉鎖層5を
設ける場合にも適用し得るものである。
The method shown in FIG. 4 can also be applied to the provision of a closure layer 5 of air-bonded refractory material to the outer surface 2 of a filter which has already been subjected to a firing treatment.

更に、第4図に示す方法は、乾燥後の焼成を行う前にス
ラリーを含浸させることにより、または焼成後に空気で
結合する耐火性材料の層を設けることにより被覆層7を
形成する際にも応用できる。
Furthermore, the method shown in FIG. 4 can also be used when forming the covering layer 7 by impregnating it with a slurry before performing the post-drying firing, or by providing a layer of air-bonded refractory material after the firing. Can be applied.

発泡セラミックフィルタを用いることにより溶湯(例え
ば鋳造設備においては溶融した球状黒鉛鋳鉄またはねず
み鋳鉄等)のろ過を行うと、フィルタには溶湯の貫流に
より熱応力のみならず静荷重も急激に作用する。熱応力
の程度は、セラミックフィルタの製造に用いられるスラ
リーの組成および特性に多分に依存する。
When a foamed ceramic filter is used to filter molten metal (for example, molten spheroidal graphite cast iron or gray cast iron in casting equipment), not only thermal stress but also static load acts rapidly on the filter due to the flow of molten metal. The degree of thermal stress is highly dependent on the composition and properties of the slurry used to manufacture the ceramic filter.

安定性および耐久性に影響を及ぼす他の要因は、フィル
タの積層面(接合面)の形状並びに構造上の制約による
フィルタの特異な形状である。後者は、本発明の構成に
より、溶湯の質流率に不所望の悪影響を及ぼすことなく
、顕著に改善することができる。
Other factors that affect stability and durability are the shape of the laminated surfaces (joint surfaces) of the filter and the unique shape of the filter due to structural constraints. The latter can be significantly improved by the configuration of the present invention without undesirably affecting the mass flow rate of the molten metal.

すなわち、本発明によるフィルタは、従来のものと対比
して使用時に遥かに大きな負荷(落差および圧力木頭)
を作用させることができる。この事実は、以下に説明す
る構成を有する試験装置を用いて実証されている。
That is, the filter according to the invention has a much higher load (head and pressure head) in use compared to the conventional one.
can be made to work. This fact has been demonstrated using a test device having the configuration described below.

第5図に示した試験装置は液状材料を受容するタンクI
2を含み、同クンク12の底部はプラグ13により閉鎖
される。タンク12の下側には、適宜規格等級のメッシ
ュ15を有するフィルタ受け部材14を配置し、この受
け部材により例えば5Q+nm X 5Qmm X22
mmの供試フィルタ16を支持する。タンク12および
受け部材l4の間には、例えば一部17’  が所定の
長さだけ延長可能な注湯管l7を配置する。供試フィル
タ16をメッシュ15上に装着し、プラグ13を抜いて
供試フィルタ16に所定量の溶湯を負荷すると共に質流
させるものである。
The test apparatus shown in Figure 5 consists of a tank I receiving liquid material.
2, the bottom of which is closed by a plug 13. A filter receiving member 14 having a mesh 15 of an appropriate standard grade is arranged on the lower side of the tank 12, and with this receiving member, for example, 5Q+nm x 5Qmm
A test filter 16 of mm is supported. Between the tank 12 and the receiving member l4, there is disposed a pouring pipe l7 whose portion 17' can be extended by a predetermined length, for example. The test filter 16 is mounted on the mesh 15, the plug 13 is removed, and a predetermined amount of molten metal is loaded onto the test filter 16 and is allowed to flow.

第5図に示した試験装置により、ねずみ鋳鉄を溶湯とし
て使用して、本発明によるセラミックフィルタを従来技
術による比較例のセラミックフィルタと比較した。本発
明によるセラミックフィルタは、所定寸法に形成され、
周囲の閉鎖層5の厚みを2mm ,被覆層7の厚みを0
. 5mmとしたものである。他方、比較例のセラミッ
クフィルタは、閉鎖層5および被覆層7が形成されて右
らず、スラリーの含浸処理のみにより製造したものであ
って、本発明によるものと実質的に同一の寸法および貫
流抵抗を有するものである。両フィルタにおける重量ス
ペクトルはほぼ同一であった。更に、両フィルタは同一
の炉程に置かれた。その結果は、次表に示すとおりであ
る。
The ceramic filter according to the present invention was compared with a comparative example ceramic filter according to the prior art using the test apparatus shown in FIG. 5 using gray cast iron as the molten metal. The ceramic filter according to the present invention is formed with predetermined dimensions,
The thickness of the surrounding closing layer 5 is 2 mm, and the thickness of the covering layer 7 is 0.
.. It is set to 5 mm. On the other hand, the ceramic filter of the comparative example was manufactured only by slurry impregnation treatment without forming the closure layer 5 and the covering layer 7, and had substantially the same dimensions and flow through as the one according to the present invention. It has resistance. The weight spectra in both filters were almost identical. Additionally, both filters were placed in the same furnace. The results are shown in the table below.

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

第1図は焼成前のセラミックフィルタを一部破断して示
す拡大断面図、 第2a図および第2b図は、それぞれ周囲の閉鎖層を形
成する方法の実施例を示す説明図、 第3図および第4
図は、それぞれ一対の側縁領域に閉鎖層を形成する方法
の実施例を示す説明図、第5図はセラミックフィルタの
試験装置の構成を示す正面図である。 l・・・発泡構造体 2・・・周方向側面 3・・・質流面(端面) 4・・・スラリー状セラミック材料 5・・・閉鎖層 6・・・開放セル橋絡部 7・・・被覆層 8・・・スタンパ 9・・・ベルト対 10・・・搬送装置 12・・・タンク 13・・・プラグ 14・・・フィルタ受け部材 15・・・メッシュ 16・・・供試フィルタ 17・・・注腸管 特 許 出 願 人 ゲオルグ フィッシャー アクチェンゲゼルシャフト
FIG. 1 is an enlarged cross-sectional view showing a partially broken ceramic filter before firing; FIGS. 2a and 2b are explanatory diagrams showing an example of the method for forming a surrounding closure layer; FIGS. Fourth
The figures are explanatory diagrams showing an example of a method for forming a closure layer on a pair of side edge regions, respectively, and FIG. 5 is a front view showing the configuration of a ceramic filter testing apparatus. l... Foamed structure 2... Circumferential side surface 3... Mass flow surface (end face) 4... Slurry ceramic material 5... Closed layer 6... Open cell bridging portion 7... - Covering layer 8... Stamper 9... Belt pair 10... Conveying device 12... Tank 13... Plug 14... Filter receiving member 15... Mesh 16... Sample filter 17 ... Enema tube patent applicant Georg Fischer Akchengesellschaft

Claims (1)

【特許請求の範囲】 1、耐熱性セラミックを基材とする開放セル型発泡構造
体を含み、かつ、溶湯の貫流方向と交差する一対の貫流
面(3)と、ほぼ貫流方向に向けて延在する少なくとも
一つの外周側面(2)とを具える溶湯ろ過用セラミック
フィルタであって、有機発泡材料(1)に高粘度スラリ
ー状のセラミック(4)を含浸させて乾燥させた後、加
熱を行って有機発泡材料(1)を除去すると共に残余の
セラミック (4)を焼成し、さらに、所要に応じて乾燥後に耐火材
料で事後の表面処理を施して成るものにおいて、前記側
面(2)の全面に、厚みが0.5〜3mmの耐火材料か
ら成る閉鎖層(5)を形成したことを特徴とするセラミ
ックフィルタ。 2、請求項1記載のセラミックフィルタにおいて、貫流
面(3)において開放する有機発泡材料(1)のセル橋
絡部を、耐火材料から成る被覆層(7)により閉鎖した
ことを特徴とするセラミックフィルタ。 3、請求項1または2に記載のセラミックフィルタにお
いて、被覆層(7)の厚みは、0.1〜1mmとしたこ
とを特徴とするセラミックフィルタ。 4、請求項1〜3のいずれか一項に記載のセラミックフ
ィルタにおいて、閉鎖層(5)および/または被覆層(
7)を形成する耐火材料は、有機発泡材料(1)に含浸
させるスラリー状のセラミックと同一材料としたことを
特徴とするセラミックフィルタ。 5、請求項1〜4のいずれか一項に記載のセラミックフ
ィルタを製造する方法であって、製造すべきフィルタの
寸法に対応させて成形した有機発泡材料(1)に耐熱性
セラミック材料から成る高粘度スラリーを含浸させてか
ら乾燥を行い、加熱およびカ焼を行って発泡材料を除去
すると共に所要に応じて耐火材料で事後の表面処理を施
すものにおいて、発泡材料の周側面領域で耐火材料を発
泡材料に被着し、該領域の周方向における全長に亘って
厚みが0.5〜3mmの閉鎖層を形成することを特徴と
する製造方法。 6、請求項5記載の製造方法において、事後の表面処理
として、発泡構造体の貫流面で開放したセル橋絡部に耐
火材料を施して被覆層を形成することを特徴とする製造
方法。 7、請求項5または6に記載の製造方法において、前記
セル橋絡部の被覆層は、厚さ0.1〜1mmおよび単位
面積当たりの質量40〜400mg/cm^2として施
すことを特徴とする製造方法。 8、請求項5〜7のいずれか一項に記載の製造方法にお
いて、スラリーを含浸させた有機発泡材料を、これと同
一の底面形状を有するスタンパにより押圧した後、発泡
材料から圧力を除負することを特徴とする製造方法。 9、請求項5〜7のいずれか一項に記載の製造方法にお
いて、スラリーを含浸させた有機発泡材料を、余剰のス
ラリーを押し出すために、開放ベルト対の間を通過させ
ることを特徴とする製造方法。 10、請求項5〜7のいずれか一項に記載の製造方法に
おいて、含浸に際して閉鎖スラリー層を形成することに
より、有機発泡材料の側面における気孔率を低下させる
ことを特徴とする製造方法。 11、請求項10記載の製造方法において、有機発泡材
料の周側面に閉鎖スラリー層の厚さに対応したより低い
気孔率の発泡材料を被着することにより、該側面におけ
る気孔率を低下させることを特徴とする製造方法。 12、請求項10記載の製造方法において、有機発泡材
料の周側面に微細な紡糸ヤーンを被着することにより、
該側面における気孔率を低下させることを特徴とする製
造方法。 13、請求項5〜7のいずれか一項に記載の製造方法に
おいて、スラリーを含浸させて乾燥した未焼成の発泡材
料を、少なくとも垂直軸線を有するローラ対の間に通し
、該ローラ対により高粘度スラリーを発泡材料の側面に
塗布すると共に所定の深さで発泡材料中に侵入させるこ
とを特徴とする製造方法。 14、請求項5〜7のいずれか一項に記載の製造方法に
おいて、焼成したフィルタを、少なくとも垂直軸線を有
するローラ対の間に通し、該ローラ対により空気で結合
する耐火性手段を塗布すると共に所定の深さでフィルタ
中に侵入させることを特徴とする製造方法。 15、請求項5〜14のいずれか一項に記載の製造方法
において、スラリーを含浸させて乾燥した未焼成の発泡
材料を、垂直軸線を有するローラ対の間に通し、その際
に発泡材料における開放セル橋絡部を高粘度スラリーに
より被覆することを特徴とする製造方法。 16、請求項5〜15のいずれか一項に記載の製造方法
において、焼成したフィルタを、垂直軸線を有するロー
ラ対の間に通し、その際に発泡材料における開放セル橋
絡部を空気で結合する耐火性手段により被覆することを
特徴とする製造方法。
[Scope of Claims] 1. It includes an open-cell foamed structure made of heat-resistant ceramic as a base material, and has a pair of flow-through surfaces (3) that intersect with the flow-through direction of the molten metal, and that extends substantially in the flow-through direction. A ceramic filter for filtrating molten metal comprising at least one outer circumferential side surface (2) in which an organic foam material (1) is impregnated with a ceramic (4) in the form of a high viscosity slurry, dried, and then heated. The organic foamed material (1) is removed and the remaining ceramic (4) is fired, and if necessary, after drying, the surface is treated with a refractory material. A ceramic filter characterized in that a closing layer (5) made of a refractory material with a thickness of 0.5 to 3 mm is formed on the entire surface. 2. The ceramic filter according to claim 1, wherein the cell bridging portion of the organic foam material (1) that is open at the flow-through surface (3) is closed by a coating layer (7) made of a refractory material. filter. 3. The ceramic filter according to claim 1 or 2, wherein the thickness of the coating layer (7) is 0.1 to 1 mm. 4. In the ceramic filter according to any one of claims 1 to 3, the closure layer (5) and/or the covering layer (
A ceramic filter characterized in that the refractory material forming (7) is the same material as the slurry-like ceramic impregnated into the organic foam material (1). 5. A method for manufacturing a ceramic filter according to any one of claims 1 to 4, wherein the organic foam material (1) is formed from a heat-resistant ceramic material and is molded to correspond to the dimensions of the filter to be manufactured. Where the foamed material is impregnated with a highly viscous slurry and then dried, heated and calcined to remove the foamed material and optionally subsequently surface treated with a refractory material, the refractory material is applied in the peripheral side area of the foamed material. A manufacturing method characterized in that a closed layer having a thickness of 0.5 to 3 mm is formed over the entire length of the region in the circumferential direction. 6. The manufacturing method according to claim 5, wherein, as a subsequent surface treatment, a refractory material is applied to the open cell bridging portions on the flow-through surface of the foam structure to form a coating layer. 7. The manufacturing method according to claim 5 or 6, wherein the coating layer of the cell bridging portion is applied with a thickness of 0.1 to 1 mm and a mass of 40 to 400 mg/cm^2 per unit area. manufacturing method. 8. In the manufacturing method according to any one of claims 5 to 7, after pressing the organic foam material impregnated with the slurry with a stamper having the same bottom shape as the stamper, the pressure is removed from the foam material. A manufacturing method characterized by: 9. The manufacturing method according to any one of claims 5 to 7, characterized in that the organic foam material impregnated with the slurry is passed between a pair of open belts in order to extrude excess slurry. Production method. 10. The manufacturing method according to any one of claims 5 to 7, characterized in that the porosity on the side surface of the organic foam material is reduced by forming a closed slurry layer during impregnation. 11. In the manufacturing method according to claim 10, the porosity on the side surface of the organic foam material is reduced by depositing a foam material with a lower porosity corresponding to the thickness of the closed slurry layer on the peripheral side surface of the organic foam material. A manufacturing method characterized by: 12. In the manufacturing method according to claim 10, by applying fine spun yarn to the peripheral side of the organic foam material,
A manufacturing method characterized by reducing the porosity on the side surface. 13. In the manufacturing method according to any one of claims 5 to 7, the unfired foamed material impregnated with the slurry and dried is passed between a pair of rollers having at least a vertical axis, and A manufacturing method characterized in that a viscous slurry is applied to the side surface of a foamed material and penetrated into the foamed material at a predetermined depth. 14. A manufacturing method according to any one of claims 5 to 7, in which the fired filter is passed between a pair of rollers having at least a vertical axis, by which a pneumatically bonded refractory means is applied. A manufacturing method characterized by making the filter penetrate into the filter at a predetermined depth. 15. The manufacturing method according to any one of claims 5 to 14, in which the unfired foamed material impregnated with the slurry and dried is passed between a pair of rollers having a vertical axis, whereby the A manufacturing method characterized by coating an open cell bridge portion with a high viscosity slurry. 16. A manufacturing method according to any one of claims 5 to 15, in which the fired filter is passed between a pair of rollers having a vertical axis, the open cell bridges in the foam material being bonded with air. A manufacturing method characterized by coating with a fire-resistant means.
JP2002669A 1989-01-11 1990-01-11 Ceramic filter for filtration of molten metal and its manufacturing method Pending JPH02229515A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH80/89A CH679746A5 (en) 1989-01-11 1989-01-11
CH00080/89-4 1989-01-11

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Publication Number Publication Date
JPH02229515A true JPH02229515A (en) 1990-09-12

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ID=4178808

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AR (1) AR243093A1 (en)
AT (1) AT396875B (en)
AU (1) AU624465B2 (en)
BE (1) BE1002969A5 (en)
BR (1) BR9000098A (en)
CA (1) CA2007450A1 (en)
CH (1) CH679746A5 (en)
DD (1) DD291480A5 (en)
DK (1) DK6290A (en)
ES (1) ES2019014A6 (en)
FI (1) FI900143L (en)
FR (1) FR2641475B1 (en)
GB (1) GB2227185B (en)
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IL (1) IL92973A0 (en)
IT (1) IT1238156B (en)
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013530029A (en) * 2010-03-19 2013-07-25 フォセコ インターナショナル リミテッド Manufacturing method of heat-resistant filter
US8802003B2 (en) 2010-03-19 2014-08-12 Foseco International Limited Method for the production of a refractory filter
US9518307B2 (en) 2010-03-19 2016-12-13 Foseco International Limited Method for the production of a refractory filter

Also Published As

Publication number Publication date
AU4773690A (en) 1990-07-19
NO900129D0 (en) 1990-01-10
ATA288689A (en) 1993-05-15
IL92973A0 (en) 1990-09-17
FI900143A7 (en) 1990-07-12
FR2641475A1 (en) 1990-07-13
NO175874B (en) 1994-09-12
NL9000009A (en) 1990-08-01
DD291480A5 (en) 1991-07-04
CH679746A5 (en) 1992-04-15
DK6290A (en) 1990-07-12
AT396875B (en) 1993-12-27
DK6290D0 (en) 1990-01-10
NO175874C (en) 1994-12-21
SE9000055L (en) 1990-07-12
FI900143L (en) 1990-07-12
BR9000098A (en) 1991-10-08
ES2019014A6 (en) 1991-05-16
MX173465B (en) 1994-03-07
AR243093A1 (en) 1993-07-30
KR900011502A (en) 1990-08-01
GB9000617D0 (en) 1990-03-14
HU900107D0 (en) 1990-05-28
YU250189A (en) 1990-12-31
GB2227185B (en) 1993-03-10
CA2007450A1 (en) 1990-07-11
PT92846A (en) 1990-07-31
FR2641475B1 (en) 1992-09-18
IT9019040A0 (en) 1990-01-10
FI900143A0 (en) 1990-01-10
AU624465B2 (en) 1992-06-11
NO900129L (en) 1990-07-12
BE1002969A5 (en) 1991-10-08
IT1238156B (en) 1993-07-09
ZA90198B (en) 1990-10-31
GB2227185A (en) 1990-07-25
IT9019040A1 (en) 1991-07-10

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