JPH0645510B2 - Inorganic oxide artificial fiber honeycomb structure and method for manufacturing the same - Google Patents
Inorganic oxide artificial fiber honeycomb structure and method for manufacturing the sameInfo
- Publication number
- JPH0645510B2 JPH0645510B2 JP1025520A JP2552089A JPH0645510B2 JP H0645510 B2 JPH0645510 B2 JP H0645510B2 JP 1025520 A JP1025520 A JP 1025520A JP 2552089 A JP2552089 A JP 2552089A JP H0645510 B2 JPH0645510 B2 JP H0645510B2
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- inorganic oxide
- weight
- honeycomb structure
- oxide artificial
- fiber
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、フイルター、触媒担体、吸着材として用いる
無機質酸化物人造繊維製のハニカム構造体に関する。TECHNICAL FIELD The present invention relates to a honeycomb structure made of an inorganic oxide artificial fiber used as a filter, a catalyst carrier, and an adsorbent.
セラミツク製のハニカム構造体としては、セラミツク粉
末を押し出し成形して焼結したもの、無機質酸化物人造
繊維のペーパーをダンボール紙と同様な方法で製造した
ものがある。As the honeycomb structure made of ceramic, there are a ceramic powder extruded and sintered, and an inorganic oxide artificial fiber paper manufactured by a method similar to that of cardboard paper.
セラミツク粉末で形成したものは、押し出しによつて隔
壁の厚さを薄くすることに制約がある為単位体積当たり
の表面積を広くするには限界があり、又隔壁の嵩密度を
小さくして空孔容積を大きくしようとすると、押し出し
の際に隔壁を欠けた部分を生ずるため空孔率の大きい隔
壁を有するハニカム構造体を製造出来ない。このため触
媒担体や、フイルター等の途に充分対応しうるものは得
られていない。The ceramic powder is limited in that the thickness of the partition wall can be reduced by extrusion, so there is a limit to increase the surface area per unit volume. If the volume is increased, a portion lacking the partition wall is generated during extrusion, so that the honeycomb structure having the partition wall having a large porosity cannot be manufactured. Therefore, a catalyst carrier, a filter, or the like that is not sufficiently compatible with the situation has not been obtained.
無機質酸化物人造繊維のペーパーは抄紙法によつて製造
されるため、通常は嵩密度が0.35g/cc以下であり、
嵩密度を高めるために然火物粉末を添加すると嵩密度が
大きくなり強度のあるものとなるが、耐スポーリング性
が小さくなり加熱鈴却を繰返し受けると寿命が極めて短
くなる。嵩密度の小さいペーパーを波形に折り曲げ平ら
な板と交互に重ねて接着して形成されたハニカム構造体
は、強度が極めて小さい。Since the paper of the inorganic oxide artificial fiber is manufactured by the papermaking method, the bulk density is usually 0.35 g / cc or less,
If fire powder is added to increase the bulk density, the bulk density becomes large and the strength becomes strong, but the spalling resistance becomes small and the life becomes extremely short when repeatedly subjected to heating bellows. The honeycomb structure formed by bending a paper having a low bulk density into a corrugated shape and alternately stacking the flat plates on each other and adhering the paper has extremely low strength.
従つて現在までのところ、単位体積当たりの表面積が大
きく、隔壁の嵩密度、空孔率を所望にでき強度並びに耐
スポーリング性を充分な無機質酸化物製のハニカム構造
体は提供されていない現状にある。Therefore, to date, a honeycomb structure made of an inorganic oxide having a large surface area per unit volume, a desired bulk density of partition walls, a desired porosity and sufficient strength and spalling resistance has not been provided. It is in.
本発明はこのような現状に鑑み、単位体積当たりの表面
積が大きく、隔壁の嵩密度、空孔率を所望にでき、強度
並びに耐スポーリング性の良好な無機質酸化物人造繊維
製のハニカム構造体を提供することを課題とする。In view of such circumstances, the present invention has a large surface area per unit volume, can have desired bulk density and porosity of partition walls, and has good strength and spalling resistance. The challenge is to provide.
本発明は無機質酸化物人造繊維に押し出し成形を適用す
ることにより、上記課題を解決出来る無機質酸化物人造
繊維製のハニカム構造体が得られることを見出したもの
である。The present invention has found that a honeycomb structure made of an artificial inorganic oxide fiber capable of solving the above problems can be obtained by applying extrusion molding to the artificial inorganic oxide fiber.
本発明は、80重量%以上が無機質酸化物人造繊維から
なり、セルを区画する隔壁の厚さが1.0〜0.1mmで
あり、該隔壁の嵩密度が1.8〜0.5g/ccで、セル一
つの開口断面積が1mm2以上であつて、無機質酸化物人
造繊維が無機結合剤で相互に結合されている押し出し成
形体からなる無機質酸化物人造繊維ハニカム構造、及び
繊維の70重量%以上のアスペクト比が10〜3000
で、アスペクト比10未満が30重量%以下であり、シ
ヨツト含有率が1重量%未満の無機質酸化物人造繊維を
無機質分中に87重量%以上と、無機結合剤と、水分以
外の全配合物100重量部に対して40〜60重量部の
水分とを含む混合物を押し出し成形し、乾燥焼成する無
機質酸化物人造繊維ハニカム構造体の製造方法、を課題
解決の手段とするものである。According to the present invention, 80% by weight or more is made of an inorganic oxide artificial fiber, the partition wall for partitioning the cell has a thickness of 1.0 to 0.1 mm, and the partition wall has a bulk density of 1.8 to 0.5 g / In cc, the open cross-sectional area of one cell is 1 mm 2 or more, and the inorganic oxide artificial fiber honeycomb structure is composed of an extruded body in which the inorganic oxide artificial fibers are bonded to each other by an inorganic binder. Aspect ratio of 10% or more by weight or more
And, an inorganic oxide artificial fiber having an aspect ratio of less than 10 is 30% by weight or less and a shot content of less than 1% by weight in an inorganic content of 87% by weight or more, an inorganic binder, and a total composition other than water. A method for manufacturing an inorganic oxide artificial fiber honeycomb structure, in which a mixture containing 40 to 60 parts by weight of water with respect to 100 parts by weight is extruded and dried and fired is used as a means for solving the problem.
本発明において、無機質酸化物人造繊維としては、ガラ
ス繊維、アルミナ繊維、シリカ維繊、シリカ−アルミナ
繊維、シリカ−アルミナ−ボリア繊維、ジルコニア繊維
等の概ね繊維径2〜12μmのものを用いる。繊維径が
太いものでは、繊維相互の結合点が少なくなるので、隔
壁を薄くした場合、強度が小さくなるので概ねこの程度
までの太さのものを用いるのが良い。又これらの無機質
酸化物人造繊維で一般に市販されている繊維は、最も細
いもので2μm程度である。これらは単独でも複数を混
合して用いても良い。In the present invention, as the inorganic oxide artificial fibers, glass fibers, alumina fibers, silica fibers, silica-alumina fibers, silica-alumina-boria fibers, zirconia fibers and the like having a general fiber diameter of 2 to 12 μm are used. If the diameter of the fiber is large, the number of bonding points between the fibers is small. Therefore, when the partition wall is thin, the strength becomes small. Therefore, it is preferable to use the thickness of about this level. The commercially available fibers of these inorganic oxide artificial fibers are about 2 μm in the thinnest fiber. These may be used alone or in combination of two or more.
本発明においてアスペクト比とは、繊維の径に対する繊
維の長さの比(繊維の長さ/繊維の径)をいう。ショッ
トとは溶融原料を繊維状とする過程で生じた粒状物で、
当業者では一般に212μmふるい残分でショット含有
率が表示される。In the present invention, the aspect ratio means the ratio of the fiber length to the fiber diameter (fiber length / fiber diameter). Shot is a granular material generated in the process of making the molten raw material into fibrous,
Those of ordinary skill in the art will generally indicate the shot content as a 212 μm sieve residue.
これらの無機質酸化物人造繊維は、成形を容易にするた
めのカルボキシメチルセルロース、メチルセルロース、
ポリビニルアルコール等の有機糊剤、ワツクス、パラフ
イン、ステアリン酸等の水エマルジヨン、黒鉛等の押し
出しを滑らかに行なえるようにするための滑剤、可塑剤
としての水、水の代わりに含水塩、アルコール、ケトン
等の水と同効物質も可塑剤として用い得るが水が最も経
済的である。These inorganic oxide artificial fibers are carboxymethyl cellulose, methyl cellulose, for facilitating molding,
Organic paste such as polyvinyl alcohol, wax, paraffin, water emulsion such as stearic acid, lubricant for smoothly extruding graphite, water as a plasticizer, water-containing salt instead of water, alcohol, Water and the same effect substances such as ketones can be used as a plasticizer, but water is the most economical.
グリセリン、アミン類、ポリエチレングリコール等の成
形乾燥時に成形体に可撓性と靭性を与えるための湿潤
剤、水ガラス、コロイダルシリカ、コロイダルアルミナ
等の無機結合剤、結合助剤としてタルク、ベントナイ
ト、窒化硼素、酸化マグネシウム等の粉末と混合しペー
スト状とし、ハニカム状に押し出し乾燥したあと、焼成
してハニカム構造体とする。Glycerin, amines, polyethylene glycol, etc., a wetting agent for imparting flexibility and toughness to the molded body during molding and drying, an inorganic binder such as water glass, colloidal silica, colloidal alumina, talc, bentonite, nitriding agent It is mixed with powder of boron, magnesium oxide or the like to form a paste, which is extruded into a honeycomb shape, dried, and then fired to obtain a honeycomb structure.
本発明無機質酸化物人造繊維ハニカム構造体において、
無機質酸化物人造繊維を87重量%以上とするのは、構
造体そのものを強度のあるものとするために繊維を交互
に結合する無機結合剤を配合する必要があり、繊維を1
00%とすることができないし使用する結合剤の種類に
よりその量が異なること、及びこの結合を強化するため
の結合助剤の添加量との合計量から繊維含有量の下限が
おのずから決まつてくるためである。In the inorganic oxide artificial fiber honeycomb structure of the present invention,
In order to make the structure itself strong, it is necessary to add an inorganic binder that alternately binds the fibers, in order to make the structure itself strong.
The lower limit of the fiber content is naturally determined from the fact that it cannot be set to 00% and the amount varies depending on the type of binder used, and the total amount with the addition amount of the binding aid for strengthening this binding. This is because of
又、結合剤と結合助剤との合計量が13重量%を超える
と耐スポーリング性が低下するようになり、無機質酸化
物人造繊維の耐スポーリング性を充分に利用できなくな
るようになるため、これらの合計量を13重量%までに
押さえる必要がある為である。Further, when the total amount of the binder and the binding aid exceeds 13% by weight, the spalling resistance is lowered, and the spalling resistance of the inorganic oxide artificial fiber cannot be fully utilized. This is because it is necessary to suppress the total amount of these to 13% by weight.
本発明無機質酸化物人造繊維ハニカム構造体において、
セルを区画する隔壁の厚さを0.1〜1.0mmとし、セ
ルの一つの開口断面積を1mm2以上としたのは、押し出
し金型製作可能下限が隔壁の厚さで0.1mmであり、セ
ルの一つの開口断面積で1mm2であることによる。セル
を区画する隔壁の厚さの上限を1mmとするのは、厚さを
1mmを超えて大きくすると単位体積当たりの表面積が小
さくなり、ハニカム構造体としての用途に適しないもの
となるからである。In the inorganic oxide artificial fiber honeycomb structure of the present invention,
The partition wall that divides the cell has a thickness of 0.1 to 1.0 mm, and the opening cross-sectional area of one cell is 1 mm 2 or more. Yes, because the cross-sectional area of one opening of the cell is 1 mm 2 . The reason why the upper limit of the thickness of the partition walls that define the cells is set to 1 mm is that if the thickness is increased to more than 1 mm, the surface area per unit volume becomes small, which makes it unsuitable for use as a honeycomb structure. .
隔壁の嵩密度を1.8〜0.5g/ccとするのは、0.5
g/cc未満では隔壁の空孔率は大きくなるが、取扱いに耐
える強度を有しなくなり、1.8g/ccを超えると無機質
酸化物人造繊維のアスペクト比が小さいものの比率が大
きくなるので、強度のあるものとするには繊維相互の接
点を結合する結合剤の量も増え、隔壁の空孔率が約25
%以下に低下しハニカム構造体としての用途に適しなく
なるからである。The partition wall bulk density of 1.8 to 0.5 g / cc is 0.5
If it is less than g / cc, the porosity of the partition wall becomes large, but it does not have the strength to withstand handling, and if it exceeds 1.8 g / cc, the ratio of the inorganic oxide artificial fiber having a small aspect ratio becomes large, so the strength is high. In order to achieve this, the amount of binder that bonds the contact points of the fibers also increases, and the porosity of the partition wall is about 25.
This is because it becomes less than 100% and becomes unsuitable for use as a honeycomb structure.
本発明ハニカム構造体の製造方法において、無機質酸化
物人造繊維として大部分がアスペクト比が10〜300
0のものを用いるのは、アスペクト比10未満では嵩密
度が1.8g/ccよりも大きいものとなり、3000を超
えるものでは押し出し成形が困難となる。又、アスペク
ト比10未満のものが30重量%を超えると嵩密度が
1.8g/ccを超えるようになるからである。In the method for manufacturing a honeycomb structure of the present invention, most of the inorganic oxide artificial fibers have an aspect ratio of 10 to 300.
If the aspect ratio is less than 10, the bulk density is greater than 1.8 g / cc, and if it exceeds 3000, extrusion molding becomes difficult. Also, if the aspect ratio is less than 10 and more than 30% by weight, the bulk density will exceed 1.8 g / cc.
又、シヨツトを含有する繊維ではシヨツト含有量が1重
量%を超えると、隔壁の嵩密度を大きくし、押し出し成
形機に詰まりを生ずるようになるので、1重量%未満好
ましくは0.5重量%未満とするのが良い。Further, in the case of fibers containing a shot, if the shot content exceeds 1% by weight, the bulk density of the partition walls becomes large and the extrusion molding machine becomes clogged, so less than 1% by weight, preferably 0.5% by weight. It is good to be less than.
押し出し材料は、ペースト状として押し出すことが必要
で、水分が多すぎるとペーストに成形性を与えるため
に、多量の糊剤の添加が必要となり、糊剤の添加量が多
いと焼成前の乾燥で収縮が大きくなるだけでなく、滑剤
として添加した油脂等の除去が困難となり焼成の際に亀
裂が発生し、嵩比重が0.5g/cc未満となり、少ないと
押し出しを円滑に行なえず隔壁の欠けたものが生ずるよ
うになるので、水分以外の全配合物100重量部に対し
て40〜60重量部の水分を含有せしめることが必要で
ある。The extruded material needs to be extruded as a paste, and if the water content is too high, the paste needs to be formed in a large amount in order to give the paste moldability. Not only does the shrinkage increase, but it becomes difficult to remove oils and fats added as a lubricant, cracks occur during firing, and the bulk density becomes less than 0.5 g / cc. Therefore, it is necessary to add 40 to 60 parts by weight of water to 100 parts by weight of the total composition other than water.
平均繊維径2.8μmのシリカ−アルミナ繊維のシヨツ
ト含有率を0.05重量%にまで低下せしめ、大部分の
アスペクト比を100〜200とし、アスペクト比10
未満が8重量%にしたもの(バルクa)と、同じ繊維を
大部分のアスペクト比を10〜50とし、アスペクト比
10未満が18重量%にしたもの(バルクb)とを用い
た。The shot content of silica-alumina fibers having an average fiber diameter of 2.8 μm was reduced to 0.05% by weight, most of the aspect ratios were set to 100 to 200, and the aspect ratio was set to 10
Was used in an amount of 8 wt% (bulk a), and most of the same fiber had an aspect ratio of 10 to 50 and an aspect ratio of less than 10 was 18 wt% (bulk b).
このバルクを下表に示す配合で撹拌機にて予備混合した
後、ニーダーにて充分混練し更にそれぞれの混合物を一
昼夜寝かしオーガー式真空押し出し機で押出し成形し
た。This bulk was premixed with a stirrer in the composition shown in the table below, thoroughly kneaded with a kneader, and each mixture was left to stand for 24 hours and extruded with an auger type vacuum extruder.
バルクaを用いた実施例1のものは、セル一個の開口寸
法が3×3mmの正方形で、隔壁厚さ0.5mm、外径約2
5×25mmの正方形に押出した。In Example 1 using the bulk a, each cell has a square shape having an opening size of 3 × 3 mm, a partition wall thickness of 0.5 mm, and an outer diameter of about 2 mm.
Extruded into a 5 × 25 mm square.
又、バルクbを用いた実施例2のものは、セル一個の開
口寸法が1.5×1.5mmの正方形で、隔壁厚さ0.2
mm、外径約26×26mmの正方形に押出した。In the second embodiment using the bulk b, the opening size of one cell is a square of 1.5 × 1.5 mm, and the partition wall thickness is 0.2.
mm, and an outer diameter of about 26 × 26 mm was extruded into a square.
この押出した成形体を乾燥脱脂後、電気炉にて200℃
/hrの昇温速度で1350℃まで昇温し、この温度に一
時間保持して焼成した。This extruded compact is dried and degreased and then heated in an electric furnace at 200 ° C.
The temperature was raised to 1350 ° C. at a heating rate of / hr, and the temperature was maintained for 1 hour for firing.
比較例1 中心粒径5μmのアルミナ粉末を表に示す配合で、焼成
温度を1650℃とした以外は実施例1、2と同様にし
てハニカム構造体を得た。Comparative Example 1 A honeycomb structure was obtained in the same manner as in Examples 1 and 2 except that the alumina powder having a central particle size of 5 μm was compounded as shown in the table and the firing temperature was 1650 ° C.
比較例2 平均繊維径2.8μmのシリカ−アルミナ繊維を長さ1
0mm以下にし、シヨツト含有率30重量%のバルクを8
0重量部と、木節粘土20重量部とを水5000重量部
に分散させ、これに有機バインダーとしてポリ酢酸ビニ
ルを添加した後、ポリアクリルアミドを添加して凝集処
理し、抄紙法で抄造し、厚さ約0.6mmのシートを作成
した。このシートを乾燥した後段ボール紙と同様にし
て、波のピツチ5mm、波高さ1.8mmの連続波形をつけ
たコルゲートシートと、平らなシートとを交互に重ね
て、1250℃で1時間焼成し、外形寸法約30×30
×30mmのハニカム構造体を得た。Comparative Example 2 A silica-alumina fiber having an average fiber diameter of 2.8 μm and a length of 1 was used.
0mm or less, 8% bulk with a shot content of 30% by weight
0 parts by weight and 20 parts by weight of kibushi clay were dispersed in 5000 parts by weight of water, and after adding polyvinyl acetate as an organic binder to this, polyacrylamide was added to perform coagulation treatment, and papermaking was performed by a papermaking method. A sheet having a thickness of about 0.6 mm was prepared. After drying this sheet, corrugated sheets with a continuous corrugation with a wave pitch of 5 mm and a wave height of 1.8 mm and a flat sheet are alternately laminated in the same manner as corrugated paper and baked at 1250 ° C. for 1 hour. , External dimensions approx. 30 x 30
A honeycomb structure with a size of 30 mm was obtained.
以上の配合と、得られたハニカム構造体の物性とを下記
の表に示す。The above composition and the physical properties of the obtained honeycomb structure are shown in the following table.
表において、隔壁嵩密度はg/cc、圧縮強度は開口方向kg
f/cm2、セル数は25mm角、耐スポーリング性は100
0℃と室温とを交互に10回上下した結果を示す。 In the table, partition bulk density is g / cc, compressive strength is in the opening direction kg.
f / cm 2 , cell number is 25 mm square, spalling resistance is 100
The results obtained by alternately moving up and down at 0 ° C. and room temperature 10 times are shown.
本発明によれば、単位体積当たりの表面積が大きく、隔
壁の嵩密度、空孔率を所望に出来、強度並びに耐スポー
リングの良好な無機質酸化物人造繊維製のハニカム構造
体を提供できる。Advantageous Effects of Invention According to the present invention, it is possible to provide a honeycomb structure made of an inorganic oxide artificial fiber, which has a large surface area per unit volume, can have desired bulk density and porosity of partition walls, and has good strength and spalling resistance.
Claims (2)
らなり、セルを区画する隔壁の厚さが1.0〜0.1mm
であり、該隔壁の嵩密度が1.8〜0.5g/ccで、セ
ルの一つの開口断面積が1mm2以上であつて、無機質酸
化物人造繊維が無機結合剤で相互に結合されている押し
出し成形体からなる無機質酸化物人造繊維ハニカム構造
体。1. 87% by weight or more is made of an inorganic oxide artificial fiber, and the partition wall partitioning the cell has a thickness of 1.0 to 0.1 mm.
The partition wall has a bulk density of 1.8 to 0.5 g / cc, one opening cross-sectional area of the cell is 1 mm 2 or more, and the inorganic oxide artificial fibers are bonded to each other with an inorganic binder. An inorganic oxide artificial fiber honeycomb structure consisting of an extruded body.
0〜3000で、アスペクト比10未満が30重量%以
下であり、シヨツト含有率が1重量%未満の無機質酸化
物人造繊維を無機質分中に87重量%以上と、無機結合
剤と、水分以外の全配合物100重量部に対して40〜
60重量部の水分とを含む混合物を押し出し成形し、乾
燥焼成する無機質酸化物人造繊維ハニカム構造体の製造
方法。2. Aspect ratio of 70% by weight or more of the fiber is 1
An inorganic oxide artificial fiber having an aspect ratio of 0 to 30 and an aspect ratio of less than 10 is 30% by weight or less and a shot content of less than 1% by weight in an inorganic content of 87% by weight or more, an inorganic binder, and a content other than water. 40 to 100 parts by weight of the total formulation
A method for producing an inorganic oxide artificial fiber honeycomb structure, which comprises extruding a mixture containing 60 parts by weight of water and drying and firing the mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1025520A JPH0645510B2 (en) | 1989-02-03 | 1989-02-03 | Inorganic oxide artificial fiber honeycomb structure and method for manufacturing the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1025520A JPH0645510B2 (en) | 1989-02-03 | 1989-02-03 | Inorganic oxide artificial fiber honeycomb structure and method for manufacturing the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02208263A JPH02208263A (en) | 1990-08-17 |
| JPH0645510B2 true JPH0645510B2 (en) | 1994-06-15 |
Family
ID=12168335
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1025520A Expired - Fee Related JPH0645510B2 (en) | 1989-02-03 | 1989-02-03 | Inorganic oxide artificial fiber honeycomb structure and method for manufacturing the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0645510B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006040874A1 (en) * | 2004-10-08 | 2006-04-20 | Ibiden Co., Ltd. | Honeycomb structure and process for producing the same |
| EP1951637A4 (en) * | 2005-11-16 | 2009-10-28 | Geo2 Technologies Inc | POROUS SUBSTRATE EXTRUSION SYSTEM |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006137161A1 (en) | 2005-06-24 | 2006-12-28 | Ibiden Co., Ltd. | Honeycomb structure body |
| WO2006137151A1 (en) * | 2005-06-24 | 2006-12-28 | Ibiden Co., Ltd. | Honeycomb structure and exhaust gas purifier |
| WO2006137163A1 (en) * | 2005-06-24 | 2006-12-28 | Ibiden Co., Ltd. | Honeycomb structure body |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60130419A (en) * | 1983-12-19 | 1985-07-11 | Taiho Kogyo Co Ltd | Cylindrical member manufacturing equipment |
-
1989
- 1989-02-03 JP JP1025520A patent/JPH0645510B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006040874A1 (en) * | 2004-10-08 | 2006-04-20 | Ibiden Co., Ltd. | Honeycomb structure and process for producing the same |
| KR100813445B1 (en) * | 2004-10-08 | 2008-03-13 | 이비덴 가부시키가이샤 | Honeycomb structure and process for producing the same |
| JPWO2006040874A1 (en) * | 2004-10-08 | 2008-05-15 | イビデン株式会社 | Honeycomb structure and manufacturing method thereof |
| US7939157B2 (en) | 2004-10-08 | 2011-05-10 | Ibiden Co., Ltd | Honeycomb structure and method for manufacturing the same |
| JP5161460B2 (en) * | 2004-10-08 | 2013-03-13 | イビデン株式会社 | Honeycomb structure and manufacturing method thereof |
| EP1951637A4 (en) * | 2005-11-16 | 2009-10-28 | Geo2 Technologies Inc | POROUS SUBSTRATE EXTRUSION SYSTEM |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02208263A (en) | 1990-08-17 |
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