JPS60248215A - Purifying body for exhaust gas - Google Patents

Purifying body for exhaust gas

Info

Publication number
JPS60248215A
JPS60248215A JP10464384A JP10464384A JPS60248215A JP S60248215 A JPS60248215 A JP S60248215A JP 10464384 A JP10464384 A JP 10464384A JP 10464384 A JP10464384 A JP 10464384A JP S60248215 A JPS60248215 A JP S60248215A
Authority
JP
Japan
Prior art keywords
ceramic
exhaust gas
slit
porous
porous body
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
JP10464384A
Other languages
Japanese (ja)
Inventor
Fumio Odaka
文雄 小高
Hiroki Yamazaki
博貴 山崎
Keisuke Yamamoto
山本 慧介
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.)
Bridgestone Corp
Original Assignee
Bridgestone Corp
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 Bridgestone Corp filed Critical Bridgestone Corp
Priority to JP10464384A priority Critical patent/JPS60248215A/en
Publication of JPS60248215A publication Critical patent/JPS60248215A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a purifying body for exhaust gas causing cracks scarcely and having improved thermal characteristics by covering the external surface of a porous ceramic body with a nonporous ceramic film having at least one slit on the surface. CONSTITUTION:The purifying body 1 for exhaust gas is constituted of a cellular structure having three-dimensional network provided with internal communicating spaces. The purifying body consists of a porous ceramic body 2 formed to an approximately elliptic cylinder as a whole, and a nonporous ceramic film 3 covering the external surface of the porous ceramic body 2 forming two uncovered faces 2a, 2b respectively on two specified parts of the porous ceramic body 2. Slits 4 comprising recessed grooves are formed on the surface of the ceramic film 3. Preferred distance between each slit is 0.4-20cm, and preferred thickness of the ceramic film is 0.05-3mm., and preferred depth of the slit is >=1/10 basing on the thickness of the film.

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は内部連通空間を有する三次元網状のセー 1 
− ルlI造をなしたセラミック多孔体の外面部に非多孔質
のセラミック膜を前記セラミック多孔体外面部の所定の
2か所に開放面を形成するように一体に被覆してなる1
11ガス浄化体に関し、特に耐熱衝撃性、耐熱応力性を
白土させた排ガス浄化体に関する。 従来、排ガス浄化体として、内部連通空間をイ1する三
次元網状のセル構造をなしたセラミック多孔体を浄化担
体とづる排ガス浄化体が知られている。この浄化体はセ
ラミック多孔体の内部連通空間を排ガス通路とする一b
のであるが、この場合セラミック多孔体はその内部連通
空間を通過ηる排ガスのリークが生じないように排ガス
の入[1及び出口を形成する2か所を除いて外面部を被
覆する必要がある。このようなセラミック多孔体の外面
部の被覆方法としては、非多孔質のセラミック膜を用い
る方法があるが、非多孔質の1?ラミツク膜で外面部を
被覆(〕たセラミック多孔体は高揚のIJIガスが通過
することにより熱衝撃や熱応力を受け、非多孔質のセラ
ミック膜に容易にクラックが生じ、−2− ヒラミック膜の破壊に伴なって内部の三次元網状の1?
ル構造をなしたセラミック多孔体の破壊をも惹起すると
いう問題がある。このため急激な温度変化による熱衝撃
や温石の不均一性により発生Jる熱応力に対する強度を
上げるための対策として、セラミック多孔体とその被覆
ヒラミック膜との熱111服係数を小さくする材料或い
は配合前での対策が講じられているが、そのような対策
のみでは限度があるため更に耐熱衝撃性等の熱的性質を
向上させる新しい方法の開発が望まれる3゜本発明は、
上記事情に鑑みなされたもので、熱lI!i撃、熱応力
がかかって〜1;)セラミック多孔体の外面部を被覆J
−る非多孔質のセラミック膜にクラックが生じ勤<、熱
的性質の向上1ノだ排ガス浄化体を提供することを目的
どする。 即ち、本発明は上記目的を達成するため、内部連通空間
を有する三次元網状のセル4R造をなしたセラミック多
孔体の外面部に少なくども1本のスリンI〜を表面に設
(′Jた非多孔質のセラミック膜を前記セラミック多孔
体外面部の所定の2か所に聞−3− 放向を形成するように一体に被覆したーしのである、。 本発明に係る排ガス浄化体によれば、前記セラミック多
孔体外面部を被覆した非多孔質セラミック膜にスリット
を設けたことにより、高温の排ガスが繰返し通過するこ
とにより生じる温度変化にも良好に対応し、熱衝撃等に
よる急激な収縮又は膨張による変形を効果的に吸収して
、セラミック膜のクラックの発生を防止し、またかりに
セラミック膜にクラックが発生して・bスリン8部の軽
い亀裂に止まり、内部の三次元網状のセル構造をなした
セラミック多孔体部の破壊を確実に防止Jることができ
るものである。 以下、本発明につき図面を参照して更にWT t)く説
明する。 第1図及び第2図はそれぞれ本発明排ガス浄化体の一実
施例を示すもので、この排ガス浄化体1は、内部連通空
間を有する三次元網状のセル構造をなし、全体としてほ
ぼ楕円柱状に形成されたセラミック多孔体2と、このセ
ラミック多孔体2の所定の2か所(図面においては軸方
向両端面)に−4− 開放面2a、21+をそれぞれ形成するようにセラミッ
ク多孔体2の外面部に被覆された非多孔質のセラミック
膜3とから2Zるものであり、このセラミック膜3の表
面には凹溝状にスリット4が形成されているものである
。この排ガス浄化体1は一方の開hl!面2aが排ガス
入口、他方の開放面2bが11Fガス出口とイ(す、セ
ラミック多孔体2の内部連通空間が排ガス通路となるも
ので、前記排ガス人[](一方の開放面2a)からセラ
ミック多孔体2の内部連通空間に流入した排ガスはこの
内部連通空間を流れる間に処理され、処理された排ガス
は排ガス出1](他方の聞11¥而2h)から流出する
ものである。 この場合、第1図の実施例においてはスリットがIJ1
ガス進行方向(図中矢印へ方向)に沿って互に所定間隔
離間して複数本形成されている例であり、また第2図の
実施例はスリットが排ガスの進行方向に沿っ−C複数本
形成されていると共に、これらスリットと直角方向に(
即ち周方向に沿って)複数本形成され、格子状にスリッ
トが形成されて−5− いる例であり、このようなスリットの形成態様により、
セラミック膜3及びセラミック多孔体2のクラックをよ
り確実に防止することができるものであって、図示した
ようにスリットは少なくとも熱応力に対して直交する方
向に、即ち排ガスの進行方向に沿って形成することがク
ラック防止効果の点で優れているものである。 また、スリットは図示したJ:うに複数本形成すること
が好ましいが、この場合スリット間の間隔は0.4〜2
0CI11.特に1〜10c+nとすることが好ましい
、。 しかしながら、スリットは必ずしも複数本でな(でもよ
く、場合によっては1本でもよい。また、スリット形成
態様−す図示の実施例に制限されない。 なお、セラミック多孔体の外面部を被覆する非多孔質の
セラミック膜の厚さは排ガス浄化体の使用条件や製品用
途等により適宜な厚さを採用することができるが、通常
0.05〜3mm、特に0.2〜11ww1が好ましい
。また、スリットの深さは非多孔質セラミック膜の厚さ
の1/1o以−に、−6− 特に1/2〜9/10とすることが好ましい。この際、
スリット中として番まセラミック多孔体の大ぎさに応じ
適宜任意の
The present invention is a three-dimensional net-like sail having an internal communication space.
- A non-porous ceramic membrane is integrally coated on the outer surface of a ceramic porous body having a circular structure so as to form open surfaces at two predetermined locations on the outer surface of the ceramic porous body.
No. 11 relates to a gas purifying body, and particularly relates to an exhaust gas purifying body having a clay-like structure with thermal shock resistance and heat stress resistance. Conventionally, as an exhaust gas purifying body, an exhaust gas purifying body is known in which a porous ceramic body having a three-dimensional network cell structure with an internal communication space is used as a purifying carrier. This purifying body uses the internal communication space of the ceramic porous body as an exhaust gas passage.
However, in this case, it is necessary to cover the outer surface of the ceramic porous body except for the two places forming the exhaust gas inlet and outlet so that the exhaust gas passing through the internal communication space does not leak. . As a method of coating the outer surface of such a porous ceramic body, there is a method of using a non-porous ceramic membrane. A ceramic porous body whose outer surface is coated with a Lamic membrane is subject to thermal shock and thermal stress when high-intensity IJI gas passes through it, and cracks easily occur in the non-porous ceramic membrane. 1 of the three-dimensional network inside as a result of the destruction?
There is a problem in that it also causes destruction of the ceramic porous body having a pore structure. Therefore, as a measure to increase the strength against thermal shock caused by rapid temperature changes and thermal stress caused by non-uniformity of heated stones, materials or compounds that reduce the thermal coefficient of 111 of the ceramic porous body and its covering hyalmic membrane are used. Although the measures mentioned above have been taken, there are limits to these measures alone, so it is desired to develop new methods to further improve thermal properties such as thermal shock resistance.
This was done in view of the above circumstances, and it's hot! i impact, thermal stress is applied~1;) Coating the outer surface of the ceramic porous body
It is an object of the present invention to provide an exhaust gas purifying body which has improved thermal properties by preventing cracks from forming in a non-porous ceramic membrane. That is, in order to achieve the above object, the present invention provides at least one sulin I~ on the outer surface of a ceramic porous body having a three-dimensional network cell 4R structure having an internal communication space. A non-porous ceramic membrane is integrally coated at two predetermined locations on the outer surface of the ceramic porous body so as to form a diagonal. According to the exhaust gas purifying body according to the present invention, By providing slits in the non-porous ceramic membrane that covers the outer surface of the porous ceramic body, it can respond well to temperature changes caused by repeated passage of high-temperature exhaust gas, and can resist rapid contraction or expansion due to thermal shock, etc. It effectively absorbs the deformation caused by the ceramic membrane and prevents the occurrence of cracks in the ceramic membrane, and prevents cracks from occurring in the ceramic membrane. The present invention will be further explained below with reference to the drawings. FIGS. 1 and 2 each show an embodiment of the exhaust gas purifying body of the present invention. This exhaust gas purifying body 1 has a three-dimensional network cell structure with an internal communication space, and has an approximately elliptical cylinder shape as a whole. The outer surface of the ceramic porous body 2 is formed so as to form -4- open surfaces 2a and 21+ at two predetermined locations (both end faces in the axial direction in the drawing) of the ceramic porous body 2. A non-porous ceramic membrane 3 is coated on the surface of the ceramic membrane 3, and a groove-like slit 4 is formed on the surface of the ceramic membrane 3. This exhaust gas purifying body 1 has one open hl! The surface 2a is the exhaust gas inlet, and the other open surface 2b is the 11F gas outlet. The exhaust gas that has flowed into the internal communication space of the porous body 2 is treated while flowing through this internal communication space, and the treated exhaust gas flows out from the exhaust gas outlet 1] (the other side 11 and 2h). , in the embodiment of FIG. 1, the slit is IJ1
This is an example in which a plurality of slits are formed at a predetermined distance from each other along the gas traveling direction (in the direction of the arrow in the figure), and in the embodiment shown in FIG. At the same time, in the direction perpendicular to these slits (
In other words, this is an example in which a plurality of slits are formed (along the circumferential direction) and slits are formed in a lattice pattern.
Cracks in the ceramic membrane 3 and the ceramic porous body 2 can be more reliably prevented, and as shown in the figure, the slits are formed at least in the direction orthogonal to the thermal stress, that is, along the traveling direction of the exhaust gas. It is excellent in terms of crack prevention effect. In addition, it is preferable to form a plurality of slits as shown in the figure, but in this case, the interval between the slits is 0.4 to 2.
0CI11. In particular, it is preferably 1 to 10c+n. However, the number of slits is not necessarily plural (or may be one in some cases). Also, the slit formation mode is not limited to the illustrated embodiment. The thickness of the ceramic membrane can be selected depending on the usage conditions of the exhaust gas purifier and the product application, but it is usually 0.05 to 3 mm, preferably 0.2 to 11 ww1. The depth is preferably 1/10 or more, particularly 1/2 to 9/10, of the thickness of the non-porous ceramic membrane.
Depending on the size of the ceramic porous body, the slit can be set as appropriate.

【1】を採用することができるが、0.1〜
4關、特に0.5〜1111Wlとすることが好ましい
。 また、セラミック多孔体はセル膜のない軟質ポリウレタ
ンフォーム\にセラミック泥漿を付着さ11、これを焼
結することにより前記軟質ポリウレタンフォームを炭化
除去して+IL!造したものを用いることが好ましく、
このJ:うにレル膜のない軟質ポリウレタンフォームか
らセラミック多孔体を形成することににす、正十二面体
の稜の部分のみからなる筒形にセラミック多孔体が得ら
れ、これは空隙率が大きいので圧力10失が少ない状態
で排ガスが通過すると共に、内部連通空間が入り組んで
いるので、排ガスがこの内部連通空間を通過する際に格
子と確実に接触し、効率のよい処理が行なわれる。 ここで、セラミック多孔質の形状は図示したように楕円
柱状である場合に限られず、種々変更可= 7 − 能である。 また、前記セラミック多孔体の材質は使用条f1に応じ
て選定されるため特に制限されないが、アルミナ、ムラ
イト、ジルコン、ヂタン酸アルミニウム、リシアやコー
ジライト質を用いることが好ましい。この場合、非多孔
質[ラミック膜の材質としてもセラミック多孔体とほぼ
同様の材質のvつのを使用することがでさ゛る。 なお、本発明において、セラミック多孔体外面部にスリ
ン1へを設けた非多孔質のセラミック膜を被覆する方法
としては、特に制限されないが、例えば■セラミック多
孔体の外m1部にセラミック泥漿を塗り付け、泥漿が乾
燥する前に泥漿表面の所定箇所を物理的に掻き取り、ス
リン1−を没ける方法、■セラミック多孔体の外面部に
所定厚さにセラミック泥漿を塗りf1&プた後、形成す
べきスリットと同じ形状の部材(例えばネット)を乗せ
、次いで更にその−Fからセラミック泥漿をスプレーな
どでコーティングし、前記部材を除去してこの部材に相
応したスリン1〜を設ける方法、■セラミツー 8 − り多孔体の外面部に所定θさにセラミック泥漿を塗り付
番フた後、所定箇所にセラミック泥漿が付着しくrい撥
水剤(シリコーン油など)を塗布し、次いでセラミック
泥漿をコーティングして撥水剤ゆ布部に対応()てスリ
ットを設置−16方法など種々の方法を採用することが
できる。なお、このにうな方法でスリットを設けたセラ
ミック泥漿を乾燥、焼結づることにより、本発明の排ガ
ス浄化体を得ることができる。 以上説明1ノたように、本発明は内部連通空間を有する
三次元網状のセル構造をなしたセラミック多孔体の外面
部に少なくとも1本のスリットを表面に設けた非多孔質
のセラミック膜を前記セラミック多孔体外面部の所定の
2箇所に開放面を形成するように一体に被覆してなるの
で、耐熱衝撃性、耐熱応力性が向上し、排ガス浄化体に
対し温腹の変化(高温−室温)が繰返し生じても非多孔
質のセラミック膜にクラックが発生し難いものである。 例えば、セラミック膜にスリットを設けない場合には7
00℃でクラックが生じるのに対し、図示−9= の実施例の場合には900〜950 ℃までクラックが
発生しないものである。従って、本発明によればセラミ
ック多孔体に流入lノだ排ガスのリークをなくして排ガ
スを確実に処理することができる。 この点につき熱l1iv1.テストを実際に11なった
結果を次に示す。 [実施例、比較例] 楕円柱状のセル膜のない軟質ポリウレタンフォームにコ
ーディエライトを主成分とするセラミック泥漿を付着し
、乾燥、焼結して長径が280wnn。 短径が120mm、高さが60TIII11の楕円柱状
のセラミック多孔体を製)告すると共に、このセラミッ
ク多孔体の外周面を厚さ1論の非多孔質のセラミック膜
で被覆して試料とした。 この場合、試料としては実施例1として非多孔質のセラ
ミック膜の表面に第1図に示したようにスリットを形成
したちのくスリット幅1龍、スリットの間隔40+nm
)、実施VIJ2どして第2図に示したようにスリット
を形成したもの(スリット幅0.5n、スリットの間隔
10wm)及び比較例と−10− してスリットを形成しない−bのをイれぞれ用いた。 次に、上記試11を加熱jF内に入れ、50℃おきに温
度を上げ、R1(利に亀裂又は破損が起こるまで試験を
続けた。この場合、保持時間は約1時間とし、そのj像
室渇にht置した。結束を下表に示1゜
[1] can be adopted, but 0.1~
4, particularly preferably 0.5 to 1111 Wl. Moreover, the ceramic porous body is made by adhering ceramic slurry to a flexible polyurethane foam without a cell membrane 11, and by sintering this, the soft polyurethane foam is carbonized and removed, resulting in +IL! It is preferable to use a manufactured
This J: We decided to form a ceramic porous body from a flexible polyurethane foam that does not have a sea urchin membrane.A cylindrical ceramic porous body consisting only of the ridges of a regular dodecahedron was obtained, and this has a large porosity. Therefore, the exhaust gas passes through with less pressure loss, and since the internal communication space is intricate, the exhaust gas reliably contacts the grid when passing through the internal communication space, resulting in efficient processing. Here, the shape of the ceramic porous material is not limited to the elliptical columnar shape as shown in the figure, but can be changed in various ways. Further, the material of the ceramic porous body is not particularly limited as it is selected depending on the usage condition f1, but it is preferable to use alumina, mullite, zircon, aluminum ditanate, ricia, or cordierite. In this case, it is not possible to use a non-porous material (substantially the same material as the ceramic porous body) for the ramic membrane. In the present invention, there are no particular restrictions on the method for coating the outer surface of the ceramic porous body with the non-porous ceramic membrane provided with Surin 1, but for example, , A method of physically scraping a predetermined part of the slurry surface and submerging the Surin 1- before the slurry dries, ■ A method of applying ceramic slurry to a predetermined thickness on the outer surface of the ceramic porous body and then forming it. A method of placing a member having the same shape as the slit (for example, a net), then coating the -F with ceramic slurry by spraying, etc., removing the member, and providing Surin 1~ corresponding to this member, ■ Cerami Two 8 - After applying the ceramic slurry to the outer surface of the porous body at a predetermined angle and removing the number, apply a water repellent (silicone oil, etc.) to prevent the ceramic slurry from adhering to the specified location, and then coat the ceramic slurry. Various methods can be adopted, such as installing a slit corresponding to the water repellent area. The exhaust gas purifying body of the present invention can be obtained by drying and sintering the ceramic slurry provided with slits using this method. As explained above in Section 1, the present invention provides a non-porous ceramic membrane having at least one slit on the outer surface of a ceramic porous body having a three-dimensional network cell structure having an internal communication space. Since the outer surface of the ceramic porous body is integrally coated to form open surfaces at two predetermined locations, the thermal shock resistance and thermal stress resistance are improved, and the temperature difference (high temperature - room temperature) with respect to the exhaust gas purifying body is improved. Even if this occurs repeatedly, cracks are unlikely to occur in the non-porous ceramic membrane. For example, if there are no slits in the ceramic membrane, 7
While cracks occur at 00°C, in the case of Example -9= shown in the figure, cracks do not occur up to 900 to 950°C. Therefore, according to the present invention, it is possible to eliminate leakage of exhaust gas flowing into the ceramic porous body and to reliably treat the exhaust gas. Regarding this point, heat l1iv1. The actual test result of 11 is shown below. [Example, Comparative Example] Ceramic slurry containing cordierite as a main component was adhered to an elliptical cylinder-shaped flexible polyurethane foam without a cell membrane, dried and sintered to have a major axis of 280wnn. An elliptical ceramic porous body with a minor axis of 120 mm and a height of 60TIII11 was prepared, and the outer circumferential surface of this ceramic porous body was coated with a non-porous ceramic film having a thickness of 1 mm to prepare a sample. In this case, the sample used was Example 1, in which slits were formed on the surface of a non-porous ceramic membrane as shown in Figure 1.
), Example VIJ2 had slits formed as shown in Figure 2 (slit width 0.5n, slit spacing 10wm), and Comparative Example -10-b without slits. Each was used. Next, the above sample 11 was placed in a heated JF, and the temperature was increased in 50°C increments, and the test was continued until cracks or damage occurred in R1 (R1).In this case, the holding time was about 1 hour, and the J image was Placed in a dry room.The binding is shown in the table below.

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

第1図及び第2図はイれぞれこの発明の一実施例を示J
斜視図ぐある。 1・・・排ガス浄化体、2・・・セラミック多孔体。 2ay21)・・・間 1k 面、・ 3・・・非多孔質セラミック躾、4・・・スリット。 −11−
FIG. 1 and FIG. 2 each show an embodiment of the present invention.
There is a perspective view. 1... Exhaust gas purifying body, 2... Ceramic porous body. 2ay21)...between 1k surface, 3...non-porous ceramic base, 4...slit. -11-

Claims (1)

【特許請求の範囲】 1、内部連通空間を有する三次元網状のセル構造をなし
たセラミック多孔体の外面部に少なくとも1本のスリッ
トを表面に設()た非多孔質のセラミック膜を前記セラ
ミック多孔体外面部の所定の2か所に開放面を形成する
ように一体に被覆してなることを特徴とする1JIガス
浄化体。 2、非多孔質セラミック膜に設4−1だスリットの深さ
が前記セラミック膜の厚さの1/10以−1−である特
許請求の範囲第1項記載の排ガス浄化体。 3、複数本のスリットを互に0.2〜2Ocynずつ離
間して排ガス進行方向とほぼ同方向に形成した特許請求
の範囲第1項又は第2項記載の11[ガス浄化体。
[Claims] 1. A non-porous ceramic membrane having at least one slit on the outer surface of a ceramic porous body having a three-dimensional network cell structure having an internal communication space; 1. A 1JI gas purifying body, characterized in that the outer surface of the porous body is integrally coated to form open surfaces at two predetermined locations. 2. The exhaust gas purifying body according to claim 1, wherein the depth of the slit 4-1 provided in the non-porous ceramic membrane is 1/10 or more of the thickness of the ceramic membrane. 3. A gas purifying body according to claim 1 or 2, wherein the plurality of slits are spaced apart from each other by 0.2 to 2 ocyn and are formed in substantially the same direction as the exhaust gas traveling direction.
JP10464384A 1984-05-25 1984-05-25 Purifying body for exhaust gas Pending JPS60248215A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10464384A JPS60248215A (en) 1984-05-25 1984-05-25 Purifying body for exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10464384A JPS60248215A (en) 1984-05-25 1984-05-25 Purifying body for exhaust gas

Publications (1)

Publication Number Publication Date
JPS60248215A true JPS60248215A (en) 1985-12-07

Family

ID=14386130

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10464384A Pending JPS60248215A (en) 1984-05-25 1984-05-25 Purifying body for exhaust gas

Country Status (1)

Country Link
JP (1) JPS60248215A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5240480A (en) * 1992-09-15 1993-08-31 Air Products And Chemicals, Inc. Composite mixed conductor membranes for producing oxygen

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5240480A (en) * 1992-09-15 1993-08-31 Air Products And Chemicals, Inc. Composite mixed conductor membranes for producing oxygen

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