KR20010060412A - Fabrication Method of Al2O3/Al Foam Filter - Google Patents

Fabrication Method of Al2O3/Al Foam Filter Download PDF

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KR20010060412A
KR20010060412A KR1019990059909A KR19990059909A KR20010060412A KR 20010060412 A KR20010060412 A KR 20010060412A KR 1019990059909 A KR1019990059909 A KR 1019990059909A KR 19990059909 A KR19990059909 A KR 19990059909A KR 20010060412 A KR20010060412 A KR 20010060412A
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foam filter
filter
ceramic
alumina
foam
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KR1019990059909A
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Korean (ko)
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정두화
정한남
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신현준
재단법인 포항산업과학연구원
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    • 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
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/01Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
    • C04B35/16Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
    • C04B35/18Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay rich in aluminium oxide
    • C04B35/185Mullite 3Al2O3-2SiO2
    • 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
    • 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
    • C04B38/0051Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof characterised by the pore size, pore shape or kind of porosity
    • 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
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/80After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only ceramics
    • C04B41/81Coating or impregnation
    • C04B41/85Coating or impregnation with inorganic materials
    • C04B41/88Metals

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Filtering Materials (AREA)

Abstract

PURPOSE: A method for preparing an alumina/aluminium foam filter is provided, to improve the abrasion resistance and strength of the foam filter, thereby allowing the filter to be used after the dust is removed mechanically. CONSTITUTION: The method comprises the steps of dipping the ceramic filter comprising silicate-based oxides into the molten aluminium maintained at the temperature of 800-1,100 deg.C, to obtain the alumina/aluminium foam filter by the exchange reaction. Preferably the pore rate of the strut of the foam filter is less than 20% to allow the exchange reaction to be occurred. The ceramic foam is commonly prepared by coating an urethane foam filter with the ceramic slurry which comprises silica, kaolin, clay, mullite or their mixtures; and drying and sintering it.

Description

알루미나/알루미늄 폼 필터 제조 방법{Fabrication Method of Al2O3/Al Foam Filter}Fabrication Method of Al2O3 / Al Foam Filter

본 발명은 세라믹 폼 필터에 관한 것으로, 특히 강도와 내마모성이 우수한 알루미나/알루미늄 복합체의 세라믹 폼 필터를 제조하는 방법에 관한 것이다.The present invention relates to a ceramic foam filter, and more particularly, to a method of manufacturing a ceramic foam filter of an alumina / aluminum composite having excellent strength and wear resistance.

일반적으로 세라믹 필터는 지르코니아(ZrO2), 탄화규소(SiC), 알루미나(Al2O3) 등의 세라믹 분말을 슬러리(slurry) 상태로 만들고, 여기에 우레탄 폼 필터(urethane foam filter)를 넣었다 빼냄으로써 세라믹 슬러리를 우레탄 폼에 코팅시키고, 그 후에 건조 및 소성 과정을 거쳐서 내부에 있는 우레탄을 연소시켜 지주(strut)에 기공을 가지며 내열성과 내마모성이 우수한 세라믹 폼 필터를 제조한다.In general, ceramic filters are made of a slurry made of ceramic powders such as zirconia (ZrO 2 ), silicon carbide (SiC), and alumina (Al 2 O 3 ), and a urethane foam filter is put therein. The ceramic slurry is coated on the urethane foam, and then, after drying and firing, the urethane is combusted to prepare a ceramic foam filter having pores in the strut and having excellent heat resistance and wear resistance.

그러나, 이러한 세라믹 폼 필터는 세라믹 재료를 이용하기 때문에 내열성과 내마모성은 우수하지만 파괴인성이 약하기 때문에 기계적 충격에 대한 저항성은 약한 결점이 있다.However, since the ceramic foam filter uses a ceramic material, it is excellent in heat resistance and abrasion resistance, but weak in fracture toughness, and thus weak in resistance to mechanical impact.

따라서, 폼 필터에 집진된 분진을 기계적으로 진동시켜 분리하고자 할 때 폼필터는 강한 기계적 충격을 받게 되어 재사용할 수 없는 문제점이 있다.Therefore, when trying to separate the dust collected in the foam filter by mechanical vibration, the foam filter is subjected to a strong mechanical shock, there is a problem that can not be reused.

본 발명은 상술한 문제점을 해결하기 위한 것으로서, 그 목적은 내마모성과 기계적인 충격이 강한 분진 제거용 필터를 제조함으로써, 필터에 집진된 분진을 기계적 충격으로 털어낸 후에도 반복 사용할 수 있는 세라믹 폼 필터를 제공하는 것이다.SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and an object thereof is to manufacture a filter for dust removal having strong wear resistance and mechanical impact, thereby providing a ceramic foam filter which can be repeatedly used even after shaking off dust collected on the filter by mechanical impact. To provide.

상기와 같은 목적을 달성하기 위하여, 본 발명은 규산염계 산화물로 구성된 세라믹 폼 필터에 있어서, 상기 세라믹 폼 필터를 800 ~ 1100℃로 유지된 용융 알루미늄 용탕속에 침적시켜 치환 반응시킴으로써 알루미나/알루미늄 복합체의 폼 필터를 제조하는 것을 특징으로 한다.In order to achieve the above object, the present invention is a ceramic foam filter composed of a silicate-based oxide, the ceramic foam filter is deposited in a molten aluminum molten aluminum kept at 800 ~ 1100 ℃ by substitution reaction by foaming the alumina / aluminum composite It is characterized by producing a filter.

상기 치환 반응이 가능하게 하기 위해서는 폼 필터의 지주(strut)의 기공율이 20% 미만으로 하는 것이 바람직하다.In order to enable the substitution reaction, the porosity of the strut of the foam filter is preferably less than 20%.

이하, 본 발명을 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail.

본 발명은 실리카(silica), 카올린(kaoline), 점토, 뮬라이트(mullite) 등의 규산염계 산화물로 구성된 세라믹 슬러리를 우레탄 폼 필터에 코팅시킨 후, 건조, 소성 과정을 거쳐 세라믹 폼 필터를 제조하고, 이 세라믹 폼 필터를 프리폼(preform)으로 사용하여 800 ~ 1100℃로 유지된 용융 알루미늄 용탕속에 침적시켜 치환 반응시킴으로써 알루미나/알루미늄 복합체의 폼 필터를 제조한다.The present invention is coated with a urethane foam filter of a ceramic slurry composed of silicate-based oxides such as silica (silica), kaoline (clay), clay, mullite (mullite), and then dried and calcined to prepare a ceramic foam filter, Using this ceramic foam filter as a preform, a foam filter of an alumina / aluminum composite was prepared by immersing in a molten aluminum molten metal kept at 800 to 1100 ° C. for substitution reaction.

상기 치환 반응은 규산염계 산화물로 구성된 세라믹 폼 필터의 실리카(SiO2)가 알루미늄과 치환하여 알루미나가 형성되는 것이다. 여기서 알루미늄을 사용한 것은 용융점이 낮아 용융탕을 만들기 쉽고, 규산에 대한 반응성이 높으며, 생성된 알루미나가 내마모성과 내충격성이 강하기 때문이다.In the substitution reaction, silica (SiO 2 ) of a ceramic foam filter composed of a silicate oxide is substituted with aluminum to form alumina. Aluminum is used here because it is easy to make a molten bath with a low melting point, high reactivity with silicic acid, and the resulting alumina has high abrasion resistance and impact resistance.

따라서, 상기 용융 알루미늄과의 치환 반응에 이용되는 프리폼인 세라믹 폼 필터는 규산염계 산화물로 이루어져야 하며, 통상의 방법으로 제조되는 것이면 사용될 수 있다.Therefore, the ceramic foam filter, which is a preform used for the substitution reaction with the molten aluminum, should be made of a silicate-based oxide, and can be used as long as it is manufactured by a conventional method.

또한, 치환 반응이 가능케 하기 위해서는 폼 필터를 구성하는 지주(strut)의 입자간 공극율이 20% 미만이어야 한다. 이는 지주의 기공율이 20% 이상이면 알루니마/알루미늄의 복합체 형성이 어려워지기 때문이다.In addition, in order to enable the substitution reaction, the interparticle porosity of the strut constituting the foam filter should be less than 20%. This is because the formation of the alumina / aluminum complex becomes difficult when the porosity of the pillar is 20% or more.

그리고, 프리폼인 규산염계 폼 필터를 용융 알루미늄과 치환 반응시 반응 온도는 800 ~ 1100℃가 적당하며, 반응 시간은 세라믹 폼 필터의 크기나, 세라믹 폼 필터를 구성하는 지주의 크기에 따라 결정되기 때문에 한정할 수 없다.When the silicate foam filter, which is a preform, is substituted with molten aluminum, a reaction temperature of 800-1100 ° C. is appropriate, and the reaction time is determined by the size of the ceramic foam filter or the size of the pillars constituting the ceramic foam filter. It cannot be limited.

상기 반응 온도를 800℃ 이상으로 한정하는 이유는 알루미늄의 용융 온도인 660℃와 치환 반응에 소요되는 시간을 고려한 것이다. 즉, 800℃ 이하에서는 규산염계 산화물에 포함된 실리카는 다음의 반응에 의해 알루미나화될 수 있으나, 반응 시간이 많이 소요되며 생성되는 알루미나의 결정이 안정한 알파 알루미나로 생성되지 않기 때문이다.The reason for limiting the reaction temperature to 800 ° C. or more is to consider 660 ° C., which is the melting temperature of aluminum, and the time required for the substitution reaction. That is, below 800 ° C., the silica included in the silicate-based oxide may be alumina by the following reaction, but it takes a long time and the crystals of the resulting alumina are not produced as stable alpha alumina.

3SiO2+ 4Al → 2Al2O3+ 3Si3SiO 2 + 4Al → 2Al 2 O 3 + 3Si

또한, 치환 반응의 온도를 1100℃ 이하로 한정한 이유는 반응에 사용되는 용융 알루미늄의 표면 산화를 최소화시키기 위함이다. 이는 용융 알루미늄 용탕의 표면은 대기 중에 노출되기 때문에 표면층의 알루미늄은 산소와 접촉하여 알루미나화 되면서 견고한 산화물 층을 형성하게 된다. 이렇게 형성된 알루미나 소결층은 폼 필터의 치환 반응 후 형성된 알루미나/알루미늄 폼 필터를 취출하는 작업에 방해물이 될 뿐만 아니라 반응물로 이용되는 알루미늄의 소모량이 많아져서 바람직하지 않다.In addition, the reason for limiting the temperature of the substitution reaction to 1100 ° C or less is to minimize the surface oxidation of the molten aluminum used in the reaction. This is because the surface of the molten aluminum molten metal is exposed to the atmosphere so that the aluminum in the surface layer contacts with oxygen to alumina to form a solid oxide layer. The alumina sintered layer thus formed is not only an obstacle to the operation of taking out the alumina / aluminum foam filter formed after the substitution reaction of the foam filter, but also the consumption of aluminum used as a reactant is not preferable.

이와 같이 반응성이나 작업성을 고려할 때 적합한 치환 반응의 온도는 1000℃ 정도이다.Thus, in consideration of reactivity and workability, the temperature of a suitable substitution reaction is about 1000 degreeC.

한편, 반응시 사용하는 알루미늄의 형상과 구성 성분은 특별히 한정하지 않으나 용융시 대기중의 산화성을 고려하여 괴상의 알루미늄을 사용하는 것이 바람직하며, 순도는 높을 수록 좋다.On the other hand, the shape and constituents of aluminum used in the reaction are not particularly limited, but it is preferable to use agglomerated aluminum in consideration of oxidizing property in the atmosphere during melting, and the higher the purity, the better.

이하, 실험 테이터를 참조로 하여 본 발명에 따른 바람직한 일 실시예를 설명한다.Hereinafter, a preferred embodiment of the present invention will be described with reference to experimental data.

실시예Example

하기 표 1에서와 같이 용융 실리카 분말 또는 뮬라이트 분말을 알루미나 포트에서 24시간 볼밀링하여 얻은 슬러리에 우레탄 폼을 침적시켜 세라믹을 코팅시켰다. 그리고, 세라믹이 코팅된 우레탄 폼을 전기로에서 탈지 및 소성시켜 세라믹 프리폼(preform)을 제조하였다.As shown in Table 1, a ceramic foam was coated by depositing urethane foam on a slurry obtained by ball milling a fused silica powder or a mullite powder in an alumina pot for 24 hours. The ceramic coated urethane foam was degreased and fired in an electric furnace to prepare a ceramic preform.

이와 같이 제조된 프리폼을 750 ~ 1200℃의 온도 범위에서 용융 알루미늄과3시간 반응시켜 알루미나/알루미늄 복합체의 폼필터를 제조하였다.The preform thus prepared was reacted with molten aluminum at a temperature range of 750 to 1200 ° C. for 3 hours to prepare a foam filter of an alumina / aluminum composite.

실험 No.Experiment No. 프리폼의 특성Preform Characteristics 금속Al과의 반응온도(℃)Reaction temperature with metal Al (℃) 알루미나/알루미늄복합체 제조특성Manufacturing Characteristics of Alumina / Aluminum Composites 복합체의 특성Characteristics of the complex 세라믹 폼필터의 구성Composition of Ceramic Foam Filter 폼필터지주의기공율(%)Foam filter column porosity (%) 생성두께(mm/hr)Thickness (mm / hr) 복합체의제조Manufacture of Complex 복합체의 특성Characteristics of the complex 파괴인성(Mpa·m1/2)Fracture Toughness (Mpa · m 1/2 ) 실시예 1Example 1 뮬라이트Mullite 33 800800 2.02.0 양호Good 고강도 고내마모High strength and high wear resistance 77 실시예 2Example 2 뮬라이트Mullite 33 10001000 2.52.5 양호Good 고강도 고내마모High strength and high wear resistance 77 실시예 3Example 3 실리카Silica 22 10001000 3.03.0 양호Good 고강도 고내마모High strength and high wear resistance 77 비교예 1Comparative Example 1 뮬라이트Mullite 33 750750 0.10.1 반응성 미흡Poor reactivity 내마모성 부족 저강도Lack of wear resistance -- 비교예 2Comparative Example 2 뮬라이트Mullite 33 12001200 2.52.5 불량Bad 취출곤란 Al 표면산화Blown out Al surface oxidation 77 비교예 3Comparative Example 3 뮬라이트Mullite 2525 10001000 0.10.1 미반응Unreacted 제조 곤란Manufacturing difficulty -- 비교예 4Comparative Example 4 뮬라이트Mullite 1~21 ~ 2 -- -- -- 분진 제거시 파괴Destruction when removing dust 33

상기 표 1에 나타난 바와 같이, 본 발명에 따라 제조된 시편 1 내지 3은 반응성이 양호하였으며, 복합체의 강도와 내마모성도 우수하였다.As shown in Table 1, the specimens 1 to 3 prepared according to the present invention had good reactivity, and also excellent strength and wear resistance of the composite.

이러한 실시예 1 내지 3의 결과에 반해, 비교예 1 내지 4의 결과는 다음과 같다.In contrast to the results of Examples 1 to 3, the results of Comparative Examples 1 to 4 are as follows.

비교예 1과 2는 세라믹 프리폼과 용융 알루미늄과의 반응시 반응 온도가 본 발명의 범위를 벗어난 것으로, 비교예 1은 750℃의 낮은 온도로 인해 반응성이 부족하여 복합체의 생성 두께가 0.1 mm/hr로 미흡하고, 생성된 알루미나도 안정한 상이 아니기 때문에 강도가 부족하였다.In Comparative Examples 1 and 2, the reaction temperature of the reaction between the ceramic preform and the molten aluminum is beyond the scope of the present invention. The strength was insufficient because the alumina produced was not a stable phase.

그리고, 비교예 2는 온도가 1200℃로 높아 치환 반응은 충분히 이루어져 생성 두께가 2.5 mm/hr로 되지만, 용융 알루미늄의 표면에 산화가 심하여 두꺼운 알루미나층의 생성으로 제조된 알루미나/알루미늄 복합체를 취출하는 데 어려움이 있다.In Comparative Example 2, although the temperature was high at 1200 ° C., the substitution reaction was sufficiently performed, resulting in a thickness of 2.5 mm / hr. Have difficulty.

한편, 비교예 3은 프리폼인 뮬라이트 폼 필터 지주의 기공율이 25%로 높아서 용융 알루미늄과의 반응성이 부족하여 복합체의 제조가 어려웠다.On the other hand, in Comparative Example 3, the porosity of the mullite foam filter post, which is a preform, was high at 25%, so the reactivity with molten aluminum was insufficient, making it difficult to manufacture a composite.

그리고, 비교예 4는 종래의 뮬라이트 폼 필터의 파괴인성을 나타낸 것으로, 본 발명 범위의 알루미나/알루미늄 복합체 폼 필터에 비해 파괴 인성이 약함을 알 수 있었다.And, Comparative Example 4 shows the fracture toughness of the conventional mullite foam filter, it was found that the fracture toughness is weak compared to the alumina / aluminum composite foam filter of the present invention range.

이와 같이 본 발명은 내마모성이 우수하고 기계적 충격에 대한 저항성이 강한 알루미나/알루미늄 복합체 폼 필터를 제조함으로써, 폼 필터에 집진된 분진을 분리한 후 재사용할 수 있다.As described above, the present invention can prepare alumina / aluminum composite foam filter having excellent abrasion resistance and strong resistance to mechanical impact, so that dust collected on the foam filter can be separated and reused.

Claims (2)

규산염계 산화물로 구성된 세라믹 폼 필터에 있어서,In a ceramic foam filter composed of a silicate oxide, 상기 세라믹 폼 필터를 800 ~ 1100℃로 유지된 용융 알루미늄 용탕속에 침적시켜 치환 반응에 의해 알루미나/알루미늄 복합체를 형성하는 것을 특징으로 하는 알루미나/알루미늄 폼 필터 제조 방법.The ceramic foam filter is immersed in a molten aluminum molten metal maintained at 800 ~ 1100 ℃ to form an alumina / aluminum composite by a substitution reaction. 제 1 항에 있어서, 상기 폼 필터의 지주(strut)의 기공율을 20% 미만으로 하는 것을 특징을 하는 알루미나/알루미늄 폼 필터 제조 방법.The method of claim 1, wherein the porosity of the strut of the foam filter is less than 20%.
KR1019990059909A 1999-12-21 1999-12-21 Fabrication Method of Al2O3/Al Foam Filter KR20010060412A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847220A (en) * 1986-09-17 1989-07-11 Lanxide Technology Company, Lp Method of making ceramic composites
US5214011A (en) * 1991-08-30 1993-05-25 Bfd, Incorporated Process for preparing ceramic-metal composite bodies
WO1996001738A1 (en) * 1994-07-11 1996-01-25 Ast Holding, Ltd. Method and apparatus for applying a heatable composition
US5728638A (en) * 1996-08-21 1998-03-17 Bfd, Inc. Metal/ceramic composites containing inert metals
KR20000037521A (en) * 1998-12-01 2000-07-05 최지호 Alpha-al2o3/beta-al2o3/al/si composite and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847220A (en) * 1986-09-17 1989-07-11 Lanxide Technology Company, Lp Method of making ceramic composites
US5214011A (en) * 1991-08-30 1993-05-25 Bfd, Incorporated Process for preparing ceramic-metal composite bodies
WO1996001738A1 (en) * 1994-07-11 1996-01-25 Ast Holding, Ltd. Method and apparatus for applying a heatable composition
US5728638A (en) * 1996-08-21 1998-03-17 Bfd, Inc. Metal/ceramic composites containing inert metals
KR20000037521A (en) * 1998-12-01 2000-07-05 최지호 Alpha-al2o3/beta-al2o3/al/si composite and preparation method thereof

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