JPH0217209B2 - - Google Patents
Info
- Publication number
- JPH0217209B2 JPH0217209B2 JP55115697A JP11569780A JPH0217209B2 JP H0217209 B2 JPH0217209 B2 JP H0217209B2 JP 55115697 A JP55115697 A JP 55115697A JP 11569780 A JP11569780 A JP 11569780A JP H0217209 B2 JPH0217209 B2 JP H0217209B2
- Authority
- JP
- Japan
- Prior art keywords
- foam
- ceramic
- ceramic foam
- exhaust gas
- present
- 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.)
- Expired - Lifetime
Links
Landscapes
- Filtering Materials (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Description
【発明の詳細な説明】
本発明は自動車の内燃機関等より排出される排
気ガスを浄化するための排気ガス浄化用構造物に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an exhaust gas purifying structure for purifying exhaust gas discharged from an internal combustion engine of an automobile or the like.
従来はセラミツク製ハニカム構造体にコーテイ
ングを施し、しかる後酸化触媒を担持している
が、これを例えば排気ガス通路中に設けた場合、
排気ガスの流れ方向とハニカム構造体の貫通孔と
が同一方向となる為、通気抵抗が小さいが、壁と
の相互作用も小さくなる。従つて排気ガスと壁面
との間の物質移動が小さくなり、ふきぬけが起こ
つて排気ガスの浄化率が悪いという問題点があ
る。一方、セラミツク発泡体を用いたものがあ
る。これ、は多孔質であり、表面積が多く浄化率
は良いが、ハニカムに比較し振動等の機械的な力
に対して極めて弱いという問題点がある。 Conventionally, a ceramic honeycomb structure is coated and then an oxidation catalyst is supported, but when this is installed, for example, in an exhaust gas passage,
Since the flow direction of exhaust gas and the through holes of the honeycomb structure are in the same direction, ventilation resistance is small, but interaction with the wall is also small. Therefore, there is a problem in that the mass transfer between the exhaust gas and the wall surface is reduced, and bubbling occurs, resulting in a poor purification rate of the exhaust gas. On the other hand, there are some that use ceramic foam. This is porous, has a large surface area, and has a good purification rate, but has the problem that it is extremely weak against mechanical forces such as vibrations compared to honeycomb.
そこで、本発明は排気ガス浄化部をなす第1の
セラミツク発泡体と、第1のセラミツク発泡体の
外周に設けられ、第1のセラミツク発泡体の目の
粗さよりも密な第2のセラミツク発泡体とからな
り、さらに第1のセラミツク発泡体と、第2の発
泡体とを同時焼成することにより、機械的強度に
優れ、かつ浄化率も高い排気ガス浄化用構造体を
提供することを目的とする。 Therefore, the present invention provides a first ceramic foam forming an exhaust gas purifying section, and a second ceramic foam provided around the outer periphery of the first ceramic foam and having a denser mesh than the first ceramic foam. The object of the present invention is to provide an exhaust gas purifying structure which has excellent mechanical strength and a high purification rate by co-firing a first ceramic foam and a second foam. shall be.
以下本発明を具体的実施例により、詳細に説明
する。第1図において、この第1図はセラミツク
発泡体を示しており、第1のセラミツク発泡体よ
りなる目の粗い部分1とその外周を取巻き一体と
なつた第2のセラミツク発泡体よりなる非可撓性
の目の密な部分2とより構成されている。この目
の粗い部分1は内部連通空間を持つた三次元網状
のセル構造を有している。また目の密な部分2は
その連通空間が目づまりした構造になつている。
このセラミツク発泡体は、排気浄化部をなすその
目の粗い部分1に触媒を担持し、かつ金属ケース
内に支持要素を介して収納され、これにより排気
ガス浄化用構造物が構成される。 The present invention will be explained in detail below using specific examples. In Fig. 1, this figure shows a ceramic foam, which includes a coarse part 1 made of a first ceramic foam and a non-porous part 1 made of a second ceramic foam that surrounds the outer periphery and is integrated with the coarse part 1. It is composed of a flexible dense part 2. This coarse part 1 has a three-dimensional network cell structure with internal communication spaces. In addition, the densely woven portion 2 has a structure in which the communication space is clogged.
This ceramic foam supports a catalyst on its coarse part 1, which forms the exhaust purification section, and is housed in a metal case via a support element, thereby forming an exhaust gas purification structure.
次に、上記セラミツク発泡体の製造方法を説明
する。なお、便宜上、第1図に付した符号を使用
する。 Next, a method for producing the ceramic foam will be explained. Note that, for convenience, the reference numerals shown in FIG. 1 are used.
内部連通空間を有する三次元網状のセル構造を
持つた目の粗さ平均13メツシユの円柱状合成樹脂
発泡体1と、同セル構造の目の粗さ平均40メツシ
ユの板状合成樹脂発泡体2とを用意する。なお、
これら発泡体1,2は例えばポリウレタンフオー
ム等で構成してあり、第3図のごときセル構造に
なつており、樹脂骨格部と外部に通ずる内部連通
空間とを有している。今、第1の円柱状発泡体1
のまわりに、厚さ3mmの板状の第2の発泡体2を
とりまき、その端部をテープ等で止めておく。こ
れを、コージエライト粉末1500gとメチルセルロ
ース60gを水2500ml中に溶かしたコージエライト
スラリーの中に浸たした後、余分なスラリーは圧
縮エアーでふきとばす。そして、100℃で3時間
乾燥させる。上記操作を数回くりかえした後、
1300℃〜1480℃で5時間、第1の発泡体および第
2の発泡体を同時焼成する。これにより、発泡体
1,2は焼失し、これの骨格に付着していたコー
ジエライトが残ることになる。なお、セラミツク
材料としてはコージエライトの他にアルミナ、ム
ライト等がある。本方法により得られた構造体
は、発泡体1の部分ではそのメツシユが粗いた
め、スラリーが発泡体1の骨格のまわりだけに付
着してその通気孔の目づまりは起こしていないの
に対し、発泡体2ではそのメツシユが細かいため
スラリーは発泡体2の通気孔をほぼ全部塞いでし
まう。そのため、これを焼成すると、発泡体1の
部分と発泡体2の部分は見掛け密度が異なる。従
つて、より非可撓性の緻密な部分2が比較的強度
の弱い部分1を保持していることになり、振動等
の機械的強度に対しては著しく強くなる。また、
本方法では発泡体1,2を同時に含浸し、焼成し
ているから、組成的に均一になるため、熱膨張率
の差がほとんどなく、焼成品には変形やヒビ、割
れ等は認められなかつた。 A cylindrical synthetic resin foam 1 having a three-dimensional network cell structure with internal communication spaces and an average mesh size of 13 meshes, and a plate-shaped synthetic resin foam 2 with the same cell structure and an average mesh size of 40 meshes. Prepare. In addition,
These foams 1 and 2 are made of polyurethane foam, for example, and have a cell structure as shown in FIG. 3, having a resin skeleton and an internal communication space communicating with the outside. Now, the first cylindrical foam 1
A plate-shaped second foam 2 with a thickness of 3 mm is placed around the 3 mm, and the ends are secured with tape or the like. This was immersed in cordierite slurry made by dissolving 1500 g of cordierite powder and 60 g of methyl cellulose in 2500 ml of water, and then the excess slurry was blown off with compressed air. Then, dry at 100℃ for 3 hours. After repeating the above operation several times,
Co-fire the first foam and the second foam at 1300°C to 1480°C for 5 hours. As a result, the foams 1 and 2 are burned away, leaving the cordierite attached to their skeletons. In addition to cordierite, ceramic materials include alumina, mullite, and the like. In the structure obtained by this method, the mesh in the foam 1 part is rough, so the slurry adheres only around the skeleton of the foam 1 and does not clog the ventilation holes. Since the foam 2 has a fine mesh, the slurry closes almost all of the air holes in the foam 2. Therefore, when this is fired, the foam 1 portion and the foam 2 portion have different apparent densities. Therefore, the more inflexible and dense portion 2 holds the relatively weaker portion 1, and becomes significantly stronger against mechanical strength such as vibration. Also,
In this method, foams 1 and 2 are impregnated and fired at the same time, so the composition is uniform, so there is almost no difference in thermal expansion coefficient, and the fired product does not have any deformation, cracks, or cracks. Ta.
このようにして作つた本構造体の圧縮強度は軸
方向で150〜200Kg/cm2、径方向で50〜100Kg/cm2、
ななめ方向で10〜20Kg/cm2であつた。また、これ
らの構造体にPt−Rh触媒を担持したものを排気
ガス中に設置してNOx、CO、HC等の有害物質
を除去すると、従来のハニカム構造体に比較し
て、これらの成分のすべてにおいて約6割の体積
で同等の浄化率を得ることが出来た。これは発泡
セラミツクの3次元網目構造により触媒と排気ガ
スとの接触相互作用が大きくなるためである。 The compressive strength of this structure made in this way is 150 to 200 Kg/cm 2 in the axial direction, 50 to 100 Kg/cm 2 in the radial direction,
It was 10 to 20 kg/cm 2 in the diagonal direction. In addition, when these structures carrying Pt-Rh catalysts are installed in the exhaust gas to remove harmful substances such as NOx, CO, and HC, these components are reduced compared to conventional honeycomb structures. In all cases, the same purification rate could be obtained with a volume of about 60%. This is because the three-dimensional network structure of the foamed ceramic increases the contact interaction between the catalyst and the exhaust gas.
第2図は、4分割のセラミツク発泡体1を十字
柱状のセラミツク発泡体3で仕切り、かつこれら
の外周をセラミツク発泡体2で取巻いた本発明の
他の実施例を示すものである。この実施例におい
ては、4つのセラミツク発泡体1の見掛け密度は
略同一であるが、他のセラミツク発泡体2,3の
見掛け密度より粗くなつている。また、この他の
セラミツク発泡体2,3は互いに略同一の見掛密
度を持つている。本実施例によれば、セラミツク
発泡体1の強度が十字柱状のセラミツク発泡体2
の存在により、一層向上することになる。 FIG. 2 shows another embodiment of the present invention in which a four-part ceramic foam body 1 is partitioned by a cross-shaped ceramic foam body 3, and the outer periphery of these is surrounded by a ceramic foam body 2. In this example, the apparent densities of the four ceramic foams 1 are approximately the same, but are coarser than the apparent densities of the other ceramic foams 2 and 3. Further, the other ceramic foams 2 and 3 have approximately the same apparent density. According to this embodiment, the strength of the ceramic foam 1 is that the ceramic foam 2 has a cross pillar shape.
The presence of this will further improve the performance.
第4図は第1図の変形実施例であり、中心にセ
ラミツク発泡体4(平均18メツシユ)を設け、こ
の発泡体4の見掛け密度を外側の発泡体1よりも
密に発泡体2よりも粗にしたものである。この実
施例による構造物を自動車の排気管に取付けた際
には、その中心を通る排気ガス流速は若干低下せ
しめられ排気管内の流速分布がなくなるため、従
来のハニカム構造体に比べより小さい体積で同等
の浄化性能を得ることができる。なお、本発明の
構造物は外観が筒状であるが、種々の形状が考え
られる。 FIG. 4 shows a modified embodiment of FIG. 1, in which a ceramic foam 4 (18 meshes on average) is provided in the center, and the apparent density of the foam 4 is set to be denser than the outer foam 1 and higher than the foam 2. It is a rough version. When the structure according to this embodiment is attached to the exhaust pipe of a car, the exhaust gas flow velocity passing through the center is slightly reduced and the flow velocity distribution within the exhaust pipe is eliminated, so it has a smaller volume than a conventional honeycomb structure. Equivalent purification performance can be obtained. Although the structure of the present invention has a cylindrical appearance, various shapes are possible.
以上要するに、本発明によれば、従来のセラミ
ツク製ハニカム構造体に比べて吹抜け現象を回避
できるばかりでなく、第1のセラミツク発泡体よ
り目の粗さの密な非可撓性の第2のセラミツク発
泡体によつて振動等の機械的強度を大幅に向上さ
せることができる。さらにまた第1のセラミツク
発泡体と第2のセラミツク発泡体とを同一な組成
としているので、熱膨張率の差がなく、焼成品の
変形やヒビ、割れ等の発生を防止することができ
る。 In summary, according to the present invention, not only can the blow-through phenomenon be avoided compared to conventional ceramic honeycomb structures, but also the non-flexible second ceramic foam has a denser mesh than the first ceramic foam. Ceramic foam can significantly improve mechanical strength against vibrations, etc. Furthermore, since the first ceramic foam and the second ceramic foam have the same composition, there is no difference in coefficient of thermal expansion, and it is possible to prevent deformation, cracking, cracking, etc. of the fired product.
第1図は本発明の一実施例を示す斜視図、第2
図は本発明の他の実施例を示す斜視図、第3図は
第1図のセラミツク発泡体の詳細を示す斜視図、
第4図は本発明の更に他の実施例を示す斜視図で
ある。
1……目の粗い部分、2,3……目の密な部
分、4……目の粗さが1と2の中間の部分。
Fig. 1 is a perspective view showing one embodiment of the present invention;
FIG. 3 is a perspective view showing another embodiment of the present invention; FIG. 3 is a perspective view showing details of the ceramic foam shown in FIG. 1;
FIG. 4 is a perspective view showing still another embodiment of the present invention. 1... part with coarse mesh, 2, 3... part with dense mesh, 4... part with coarseness between 1 and 2.
Claims (1)
体と、 この第1のセラミツク発泡体の外周に形成さ
れ、 前記第1のセラミツク発泡体より目の粗さが密
である第2のセラミツク発泡体とからなり、 前記第1のセラミツク発泡体と前記第2のセラ
ミツク発泡体とは、同時焼成によつて一体的に形
成されていることを特徴とする排気ガス浄化用構
造物。[Scope of Claims] 1. A first ceramic foam constituting an exhaust gas purifying section; and a foam formed on the outer periphery of the first ceramic foam, the opening of which is denser than that of the first ceramic foam. an exhaust gas purifying structure, characterized in that the first ceramic foam and the second ceramic foam are integrally formed by co-firing. thing.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11569780A JPS5738919A (en) | 1980-08-21 | 1980-08-21 | Construction body for waste gas purification |
| US06/294,780 US4396565A (en) | 1980-08-21 | 1981-08-20 | Method for producing a filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11569780A JPS5738919A (en) | 1980-08-21 | 1980-08-21 | Construction body for waste gas purification |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5738919A JPS5738919A (en) | 1982-03-03 |
| JPH0217209B2 true JPH0217209B2 (en) | 1990-04-19 |
Family
ID=14668990
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11569780A Granted JPS5738919A (en) | 1980-08-21 | 1980-08-21 | Construction body for waste gas purification |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5738919A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58174217A (en) * | 1982-04-03 | 1983-10-13 | Ngk Spark Plug Co Ltd | Ceramic filter for removing combustible fine particle |
| JPS5948724U (en) * | 1982-09-20 | 1984-03-31 | トヨタ自動車株式会社 | Particulate collection material |
| JPS6125616A (en) * | 1984-07-12 | 1986-02-04 | Tatsuro Hayashi | Porous ceramic filtration body |
| JPH0317934Y2 (en) * | 1985-05-17 | 1991-04-16 |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5931694Y2 (en) * | 1978-05-15 | 1984-09-07 | 株式会社ブリヂストン | porous ceramic structure |
-
1980
- 1980-08-21 JP JP11569780A patent/JPS5738919A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5738919A (en) | 1982-03-03 |
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