JP3881060B2 - Method for producing honeycomb solid catalyst - Google Patents
Method for producing honeycomb solid catalyst Download PDFInfo
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- JP3881060B2 JP3881060B2 JP20530796A JP20530796A JP3881060B2 JP 3881060 B2 JP3881060 B2 JP 3881060B2 JP 20530796 A JP20530796 A JP 20530796A JP 20530796 A JP20530796 A JP 20530796A JP 3881060 B2 JP3881060 B2 JP 3881060B2
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- solid catalyst
- honeycomb
- shaped solid
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- oxide
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- 239000011949 solid catalyst Substances 0.000 title claims description 28
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000012784 inorganic fiber Substances 0.000 claims description 24
- 239000011347 resin Substances 0.000 claims description 18
- 229920005989 resin Polymers 0.000 claims description 18
- 238000010304 firing Methods 0.000 claims description 13
- 238000001035 drying Methods 0.000 claims description 11
- 239000002243 precursor Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 5
- 238000000354 decomposition reaction Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000000758 substrate Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 4
- 239000002759 woven fabric Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 238000007598 dipping method Methods 0.000 claims 1
- 239000000835 fiber Substances 0.000 description 7
- 239000000919 ceramic Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000010409 thin film Substances 0.000 description 6
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 239000010408 film Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000004925 Acrylic resin Substances 0.000 description 3
- 229920000178 Acrylic resin Polymers 0.000 description 3
- 229910010413 TiO 2 Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 239000003365 glass fiber Substances 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 239000012702 metal oxide precursor Substances 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 239000004745 nonwoven fabric Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 150000004703 alkoxides Chemical class 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 229910001510 metal chloride Inorganic materials 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000004833 X-ray photoelectron spectroscopy Methods 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000004453 electron probe microanalysis Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229910052976 metal sulfide Inorganic materials 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
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- Catalysts (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、固体触媒を被覆した無機質繊維のハニカム状成形体の製造方法に関する。さらに詳しくは、乾燥、焼成の前に賦形処理を行なった無機質繊維を多段に積層配置することにより高い反応性を有しかつ比較的軽量なハニカム状固体触媒の製造方法を提供するものである。
【0002】
【従来の技術】
従来のハニカム状固体触媒としては、固体触媒を練り込んで焼成したセラミック製ハニカムが知られている。また、特開昭55−159842号公報に開示される通り、無機質繊維の不織布などを予め波状に成形した後に積層してハニカム状とする方法が知られている。
【0003】
【発明が解決しようとする課題】
しかしながら、前記の方法のうち焼結したセラミック製ハニカムでは、割れや欠け等の問題があった。さらに、形状保持のために重量が比較的大きくなるといった欠点を有していた。また、無機質繊維の不織布などを予め波形に成形したのち積層する方法では、ハニカムの寸法が波形成形機の大きさによって制限を受けるといった欠点があった。
本発明は、これらの従来技術の欠点を解消し、高い反応活性を有し、比較的軽量なハニカム状固体触媒の製造方法を提供することを目的としている。
【0004】
【課題を解決するための手段】
本発明者らは、前記欠点を解決するため鋭意研究の結果、酸化物を主成分とした無機質繊維体を、加熱により酸化物になる酸化物前駆体と有機物樹脂とを相溶性のある溶媒に溶解してなる溶液に浸漬した後に所望の筒状に整え、乾燥前、乾燥後、あるいは焼成前の何れかの時点で多段に積層配置することにより、比較的軽量なハニカム状固体触媒ができることを見いだし、本発明を完成させた。
即ち、請求項1記載のハニカム状固体触媒の製造方法は、組成式AOxで表される酸化物を主成分とした無機質繊維体からなる基材を、加熱によりBOyで表される触媒である酸化物になる酸化物前駆体と有機物樹脂とを相溶性のある溶媒に溶解してなる溶液に浸漬した後、乾燥、焼成することにより、前記基材に前記酸化物をA−O−B結合により被覆するハニカム状固体触媒の製造方法であって、無機質繊維体を所望の筒状に整えて乾燥した後に多段に積層配置して焼成するか、あるいは所望の筒状に整えて多段に積層配置した後に乾燥および焼成することを特徴とする。
また請求項2記載のハニカム状固体触媒の製造方法は、前記焼成時の温度を200〜600℃の範囲の温度とすることにより、残留有機物を除去し被覆された酸化物の触媒特性を発現させることを特徴とする。
また請求項3記載のハニカム状固体触媒の製造方法は、前記有機物樹脂を、200℃以上かつ前記焼成温度以下の分解温度を有する樹脂とすることにより、被覆された酸化物の脱落を小さくすることを特徴とする。
また請求項4記載のハニカム状固体触媒は、前記基材を無機質繊維布とすることにより、さらに軽量化を図り、加えて被覆される酸化物の担持量を増やすことを特徴とする。
また請求項5記載のハニカム状固体触媒の製造方法は、前記基材を酸化珪素を主成分とした無機質繊維スリーブとすることにより、酸化物薄膜と強固な結合を形成することを特徴とする。
【0005】
【発明の実施の形態】
前記酸化物を主成分とした無機質繊維体としては、織布、不織布、紙などが挙げられる。なかでも強度の点から目付け10〜900g/m2 の織布が好ましい。また、筒状の形状を達成するためには予め管状に編んだ繊維製品、即ち、無機質繊維スリーブを用いるとよい。
無機質繊維体の内径(mm)及び単重(g/m)は、いくらのものでも構わないが、取扱い性や酸化物の担持量の関係から、1〜100mm、1〜300g/m、特に15〜50mm、25〜130g/mが好ましい。
【0006】
また、繊維体を構成する無機質繊維の材質は、ガラスやセラミック等、主成分としてA=Si,Al,Ti,Zr等の酸化物を有するものであればよい。なかでも酸化物薄膜と強固な結合を形成できる酸化珪素を主成分とした無機質繊維が好ましい。ここでいう、酸化珪素を含む無機質繊維とは、例えば、石英ガラス、高石英ガラス、Eガラス、Cガラス、Sガラス、Aガラス等からなる繊維が挙げられるが、経済性からEガラス繊維が好ましい。
無機質繊維の平均繊維径は特に限定されるものではないが、製造可能でしかも繊維体に加工するのが容易であることから、0.1〜20ミクロンが好ましい。
【0007】
また、加熱により金属酸化物となる前駆体としては、金属アルコキシド、金属塩化物、金属硫化物、金属酢酸塩等が使用できるが、有機物樹脂との相溶性の関係から、アルコール類を相溶性溶媒とする場合は金属アルコキシド、水を相溶性溶媒とする場合は金属塩化物を選択することが好ましい。しかし、前駆体と有機物樹脂が相溶する場合はどの組み合わせを選択してもかまわない。
【0008】
また、有機物樹脂としてはアクリル系、オレフィン系等が一般的であるが、製造工程中の焼成工程で酸化分解することが必要であるため分解温度が200℃以上かつ焼成温度以下の樹脂で、さらに該金属酸化物前駆体との相溶性であればよく、モノマーの種類や分子量によって特に限定されるものではない。
【0009】
このようにして選定された有機物樹脂と金属酸化物前駆体の溶液に、無機質繊維体を浸漬し筒状に整えたのち、乾燥する。このとき、筒状に整えるために、金属、セラミック、プラスチック、木などの型を用いて成形するとよい。さらに成形に用いる型を目的の形状に合わせて円筒、角筒あるいは異形筒など筒状体としておき、有機物樹脂と酸化物前駆体の溶液に浸漬した無機質繊維体を、この型の外壁にかぶせて成形するか、あるいは内壁に密着させて成形するとよい。
【0010】
多段に積層配置する行程は、乾燥前、乾燥後、あるいは焼成前の何れでも可能である。ただし触媒機能に不要なバインダ等を使用したくない場合には、乾燥前に積層配置して、酸化物薄膜の焼結により筒状体相互間の結着を行うとよい。
【0011】
乾燥温度は相溶性溶媒の沸点により異なるが、40〜150℃の範囲で行うのが好ましい。次に、乾燥膜を焼成することにより、有機物樹脂や金属酸化物の前駆体を構成している有機残基を取り除く。この焼成で金属酸化物前駆体は金属酸化物に変化し、有機物樹脂は酸化分解されA−O−B結合を有する薄膜が得られる。加えて、薄膜の焼結作用で形状保持が可能となる。
【0012】
【実施例】
次に、より具体的な実施例を説明する。
無機質繊維体、酸化物触媒の前駆体材料および有機物樹脂などは前記条件を満たしておけば効果は同じである。そこで、代表として、無機質繊維体としてEガラス繊維スリーブ(主成分SiO2)、酸化物の前駆体としてチタンイソプロポキシド、有機物樹脂としてアクリル系樹脂(分解温度350℃)および相溶媒としてエチルアルコールの組み合わせを選んで説明する。
【0013】
(実施例1)
内径10mmφのEガラス繊維スリーブを、酸化物前駆体であるチタンイソプロポキシド10gとアクリル系樹脂10gをエチルアルコール180gに溶解した溶液に浸漬した。このスリーブを溶液から取り出し5mmφのセラミック製六角筒にかぶせた状態で多段に積層配置し、60℃で1時間乾燥して硬化させたのち、毎分1℃の速度で450℃まで昇温し、450℃で5時間保持することにより、有機物樹脂を完全に酸化分解し、同時にチタンイソプロポキシドもTiO2 の酸化物に変化させ、繊維上にTiO2 膜を形成しセラミック製六角筒を抜き取りハニカム状の固体触媒を作製した。
【0014】
このときの形状保持性は良好であった。また、TiO2 膜の厚さをSEMで確認したところ約0.3ミクロンであり、強固に付着していた。さらに、この膜についてEPMAおよびESCAにより分析を行ったところ、Si−O−Ti結合の存在が確認された。
【0015】
このハニカム状固体触媒を200mm×200mm×長さ500mmの反応槽内に配置し、NOx を100ppm含む350℃の空気を1リットル/分の速度で通過させ、さらにアンモニアを入口NOx 量に対して1:1となるように添加し、分解効率を測定した。その結果、出口ではNox 濃度は10ppm以下となり、触媒による反応が効率的に進行していることが確認された。
ここで図1は本実施例にしたがって作製されたハニカム状固体触媒1の外観図である。また、図2は前記ハニカム状固体触媒1を反応槽2内に配置したときのモデル図である。なお、図中3は反応物の流路を示す。
【0016】
【発明の効果】
このように、本発明によるハニカム状固体触媒は、繊維上にA−O−B結合を持つ層を有した薄膜を形成することにより形状保持性に優れており、さらに比較的軽量な触媒成形体を提供することができる。
【図面の簡単な説明】
【図1】本発明のハニカム状固体触媒の一例を示したものである。
【図2】本発明のハニカム状固体触媒の使用方法の一例を示したもので、ハニカム状固体触媒を反応槽内に配置したときのモデル図である。
【符号の説明】
1 ハニカム状固体触媒
2 反応槽
3 反応物の流路[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a manufacturing method of a honeycomb JoNaru form of inorganic fibers coated with a solid catalyst. More specifically, the present invention provides a method for producing a honeycomb-shaped solid catalyst having high reactivity and relatively light weight by laminating and arranging inorganic fibers subjected to shaping treatment before drying and firing in multiple stages. .
[0002]
[Prior art]
As a conventional honeycomb-shaped solid catalyst, a ceramic honeycomb obtained by kneading and firing a solid catalyst is known. Further, as disclosed in Japanese Patent Laid-Open No. 55-159842, there is known a method in which a nonwoven fabric of inorganic fibers or the like is previously formed into a wave shape and then laminated to form a honeycomb.
[0003]
[Problems to be solved by the invention]
However, among the above methods, the sintered ceramic honeycomb has problems such as cracking and chipping. In addition, there is a disadvantage that the weight is relatively large for maintaining the shape. Further, the method of laminating a nonwoven fabric of inorganic fibers or the like in advance after corrugation has a drawback that the dimensions of the honeycomb are limited by the size of the corrugating machine.
The object of the present invention is to eliminate these drawbacks of the prior art and to provide a method for producing a honeycomb-shaped solid catalyst having a high reaction activity and a relatively light weight.
[0004]
[Means for Solving the Problems]
As a result of diligent research to solve the above-mentioned drawbacks, the inventors have made an inorganic fiber body mainly composed of an oxide into a compatible solvent with an oxide precursor that becomes an oxide by heating and an organic resin. After being immersed in the dissolved solution, it is arranged into a desired cylinder shape, and a relatively lightweight honeycomb solid catalyst can be formed by arranging multiple layers at any time before drying, after drying, or before firing. As a result, the present invention has been completed.
That is, the method for producing a honeycomb-shaped solid catalyst according to claim 1 is an oxidation that is a catalyst represented by BOy by heating a substrate made of an inorganic fiber body mainly composed of an oxide represented by a composition formula AOx. After immersing in a solution obtained by dissolving an oxide precursor and an organic resin in a compatible solvent, drying and firing, the oxide is bonded to the substrate by AOB bond. A method for producing a honeycomb-shaped solid catalyst to be coated, in which inorganic fiber bodies are arranged in a desired cylindrical shape and dried and then laminated and fired in multiple stages, or arranged in a desired cylindrical shape and arranged in multiple stages. It is characterized by being dried and fired later.
Further, in the method for producing a honeycomb-shaped solid catalyst according to
The method for producing a honeycomb-shaped solid catalyst according to claim 3 , wherein the organic resin is a resin having a decomposition temperature not lower than 200 ° C. and not higher than the firing temperature, thereby reducing the falling off of the coated oxide. It is characterized by.
The honeycomb-shaped solid catalyst according to claim 4 is characterized in that the substrate is made of an inorganic fiber cloth to further reduce the weight and to increase the amount of oxide to be covered.
The method for producing a honeycomb-shaped solid catalyst according to claim 5 is characterized in that the substrate is an inorganic fiber sleeve mainly composed of silicon oxide to form a strong bond with the oxide thin film.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
Examples of the inorganic fiber body mainly composed of the oxide include woven fabric, nonwoven fabric, and paper. Among these, a woven fabric having a basis weight of 10 to 900 g / m 2 is preferable from the viewpoint of strength. In order to achieve a cylindrical shape, it is preferable to use a fiber product knitted in a tubular shape, that is, an inorganic fiber sleeve.
The inner diameter (mm) and the unit weight (g / m) of the inorganic fiber body may be any amount, but 1 to 100 mm, 1 to 300 g / m, especially 15 in terms of handling properties and oxide loading. -50 mm and 25-130 g / m are preferred.
[0006]
Moreover, the material of the inorganic fiber which comprises a fiber body should just have oxides, such as A = Si, Al, Ti, Zr, as main components, such as glass and a ceramic. Among these, inorganic fibers mainly composed of silicon oxide that can form a strong bond with the oxide thin film are preferable. Examples of the inorganic fiber containing silicon oxide include fibers made of quartz glass, high quartz glass, E glass, C glass, S glass, A glass, etc., but E glass fiber is preferable from the viewpoint of economy. .
The average fiber diameter of the inorganic fiber is not particularly limited, but is preferably 0.1 to 20 microns because it can be manufactured and easily processed into a fiber body.
[0007]
In addition, metal alkoxides, metal chlorides, metal sulfides, metal acetates, and the like can be used as precursors that become metal oxides upon heating, but alcohols are compatible solvents because of their compatibility with organic resins. In the case of using a metal alkoxide, and in the case of using water as a compatible solvent, it is preferable to select a metal chloride. However, when the precursor and the organic resin are compatible, any combination may be selected.
[0008]
As the organic resin, acrylic resin, olefin resin, etc. are generally used. However, since it is necessary to oxidatively decompose in the baking process in the manufacturing process, a resin having a decomposition temperature of 200 ° C. or higher and a baking temperature or lower It is only required to be compatible with the metal oxide precursor, and is not particularly limited by the type and molecular weight of the monomer.
[0009]
The inorganic fiber body is immersed in the solution of the organic resin and metal oxide precursor selected in this manner, and is then dried, and then dried. At this time, in order to arrange it into a cylindrical shape, it is preferable to mold using a mold such as metal, ceramic, plastic, and wood. Furthermore, the mold used for molding is made into a cylindrical body such as a cylinder, a square cylinder or a deformed cylinder according to the desired shape, and an inorganic fiber body immersed in a solution of an organic resin and an oxide precursor is placed on the outer wall of this mold. It is good to shape | mold or make it closely_contact | adhere to an inner wall.
[0010]
The step of stacking the layers in multiple stages can be performed before drying, after drying, or before firing . However, if it is not desired to use a binder or the like that is unnecessary for the catalytic function, it is preferable to stack the layers before drying and bond the cylindrical bodies together by sintering the oxide thin film.
[0011]
Although drying temperature changes with boiling points of a compatible solvent, it is preferable to carry out in 40-150 degreeC. Next, the organic residue constituting the precursor of the organic resin or metal oxide is removed by baking the dry film. By this firing, the metal oxide precursor is changed to a metal oxide, and the organic resin is oxidatively decomposed to obtain a thin film having an A—O—B bond. In addition, the shape can be maintained by the sintering action of the thin film.
[0012]
【Example】
Next, description more specific examples.
The inorganic fiber body, the precursor material of the oxide catalyst, the organic resin, and the like have the same effect as long as the above conditions are satisfied. Therefore, as a representative, E glass fiber sleeve (main component SiO 2 ) as an inorganic fiber body, titanium isopropoxide as an oxide precursor, acrylic resin (decomposition temperature 350 ° C.) as an organic resin, and ethyl alcohol as a compatibilizer. Select and explain a combination.
[0013]
Example 1
An E glass fiber sleeve having an inner diameter of 10 mmφ was immersed in a solution in which 10 g of titanium isopropoxide as an oxide precursor and 10 g of an acrylic resin were dissolved in 180 g of ethyl alcohol. The sleeve was taken out from the solution and placed in multiple stages in a state of being covered with a ceramic hexagonal cylinder of 5 mmφ, dried and cured at 60 ° C. for 1 hour, then heated to 450 ° C. at a rate of 1 ° C. per minute, By holding at 450 ° C. for 5 hours, the organic resin is completely oxidatively decomposed, and at the same time, titanium isopropoxide is changed to TiO 2 oxide, a TiO 2 film is formed on the fiber, and the ceramic hexagonal cylinder is pulled out to form a honeycomb. A solid catalyst was prepared.
[0014]
The shape retention at this time was good. Further, when the thickness of the TiO 2 film was confirmed by SEM, it was about 0.3 μm and adhered firmly. Furthermore, when this film was analyzed by EPMA and ESCA, the presence of Si—O—Ti bonds was confirmed.
[0015]
This honeycomb-shaped solid catalyst is placed in a reaction vessel having a size of 200 mm × 200 mm × length 500 mm, air at 350 ° C. containing 100 ppm of NO x is passed at a rate of 1 liter / min, and ammonia with respect to the amount of inlet NO x And the decomposition efficiency was measured. As a result, the No x concentration was 10 ppm or less at the outlet, and it was confirmed that the reaction by the catalyst was proceeding efficiently.
Here, FIG. 1 is an external view of a honeycomb-shaped solid catalyst 1 manufactured according to this embodiment. FIG. 2 is a model diagram when the honeycomb solid catalyst 1 is arranged in the
[0016]
【The invention's effect】
As described above, the honeycomb solid catalyst according to the present invention is excellent in shape retention by forming a thin film having a layer having an A-O-B bond on a fiber, and is a relatively lightweight catalyst molded body. Can be provided.
[Brief description of the drawings]
FIG. 1 shows an example of a honeycomb solid catalyst of the present invention.
FIG. 2 shows an example of a method for using the honeycomb solid catalyst of the present invention, and is a model diagram when the honeycomb solid catalyst is arranged in a reaction vessel.
[Explanation of symbols]
1 Honeycomb
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20530796A JP3881060B2 (en) | 1996-07-16 | 1996-07-16 | Method for producing honeycomb solid catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP20530796A JP3881060B2 (en) | 1996-07-16 | 1996-07-16 | Method for producing honeycomb solid catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1028874A JPH1028874A (en) | 1998-02-03 |
| JP3881060B2 true JP3881060B2 (en) | 2007-02-14 |
Family
ID=16504793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP20530796A Expired - Fee Related JP3881060B2 (en) | 1996-07-16 | 1996-07-16 | Method for producing honeycomb solid catalyst |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3881060B2 (en) |
-
1996
- 1996-07-16 JP JP20530796A patent/JP3881060B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH1028874A (en) | 1998-02-03 |
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