JPS63138113A - Catalyst converter for automobile - Google Patents

Catalyst converter for automobile

Info

Publication number
JPS63138113A
JPS63138113A JP61284058A JP28405886A JPS63138113A JP S63138113 A JPS63138113 A JP S63138113A JP 61284058 A JP61284058 A JP 61284058A JP 28405886 A JP28405886 A JP 28405886A JP S63138113 A JPS63138113 A JP S63138113A
Authority
JP
Japan
Prior art keywords
catalyst carrier
exhaust gas
catalytic converter
automobile
catalyst
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
JP61284058A
Other languages
Japanese (ja)
Inventor
Takayasu Okuno
奥野 隆寧
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP61284058A priority Critical patent/JPS63138113A/en
Publication of JPS63138113A publication Critical patent/JPS63138113A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Exhaust Gas After Treatment (AREA)

Abstract

PURPOSE:To enable provision of capacity characteristics being sufficient enough to allow satisfaction of given demand characteristics, by a method wherein a catalyst carrier is divided into a plurality of parts, and division catalyst carriers are differed in a ratio surface area from each other. CONSTITUTION:A catalyst converter body 1 is provided on both sides with exhaust gas outlet and inlet ports 3 and 2, and is connected to a flange 5 of an exhaust muffler 5 through a flange 4 formed to the one end part. A catalyst carrier serving as a means facilitating retension of exhaust gas is situated in the catalyst converter body 1. In this case, a catalyst carrier is formed such that a plurality of division catalyst carriers S1-Sn are properly combined together. Each of the catalyst carries S1-Sn is formed by ceramic to form a porous substance having continuous void three-dimensional skeleton structure, and the size of each pore of the porous substance and the number of the pores are differed from each other. This constitution enables provision of capacity characteristics being sufficient enough to allow satisfaction of given demand characteristics.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は自動車の排気ガス中に含まれる有害成分を効率
よく酸化或いは還元させて排気ガスを浄化するのに用い
られる触媒コンバーターの改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an improvement in a catalytic converter used to efficiently oxidize or reduce harmful components contained in automobile exhaust gas and purify the exhaust gas.

〔循来の技術〕[Circulating technology]

周知のとおり、自動車の排出ガス中の有害成分を浄化さ
せるための触媒コンバーターが用いられている。触媒コ
ンバーター内には排気ガスが接触する触媒担体が配され
ている。この触媒コンバーターに関して要求されること
は、第1には有害成分除去効率であり、第2には、エン
ジンの排気効率を阻害しない問題である。これらはほと
んど触媒担体に関係する。第1の点は触媒担体の比表面
積(表面積/体積)に関し、触媒コンバーター内に配さ
れる触媒担体の比表面積が大きくなればなるほどコンバ
ーター内を通過する排出ガスの単位流量あたりの触媒担
体の接触面積が太きなるので、排出ガスを十分にコンバ
ーター内に残留させることができ、その結果浄化のため
の化学反応を十分に行なわしめることができ、従って浄
化効率は向上する。しかし第2の点は触媒担体の比表面
積が大きくなればなるほど排出ガスと触媒担体との接触
面積が大きくなり、その結果流路抵抗が大きくなるので
排気効率は落ちる。即ち、有害成分除去効率と排気効率
とは第8図(A)に示すように略反比例の関係にある。
As is well known, catalytic converters are used to purify harmful components in automobile exhaust gas. A catalyst carrier is arranged inside the catalytic converter and comes into contact with the exhaust gas. The first requirement for this catalytic converter is the efficiency of removing harmful components, and the second requirement is that the exhaust efficiency of the engine is not inhibited. These mostly relate to catalyst supports. The first point concerns the specific surface area (surface area/volume) of the catalyst carrier. Since the area is large, the exhaust gas can remain sufficiently in the converter, and as a result, the chemical reaction for purification can be sufficiently carried out, and therefore the purification efficiency is improved. However, the second point is that as the specific surface area of the catalyst carrier becomes larger, the contact area between the exhaust gas and the catalyst carrier becomes larger, and as a result, the flow path resistance becomes larger and the exhaust efficiency decreases. That is, the harmful component removal efficiency and the exhaust efficiency are in a substantially inversely proportional relationship as shown in FIG. 8(A).

この場合縦軸を排気効率R1横軸を有害成分除去効率r
とする。
In this case, the vertical axis is exhaust efficiency R1, and the horizontal axis is harmful component removal efficiency r
shall be.

所で現在用いられている触媒コンバーターは、金属板錆
層型、全屈粒子型セラミックのハニカム構造体等の単一
の触媒担体を有するものの他、最近ではセラミック製連
続気泡三次元骨格構造多孔体で成る単一の触媒担体を有
するものも提案されている。このセラミック製連続気泡
三次元骨格構造多孔体は、軟質ウレタンフオームを所定
の気孔の大きさ、等を設定して発泡させ、必要な形状に
形成した後、この発泡ウレタンフオームに液状セラミッ
クを含浸させてから乾燥させ、最後にこれを焼いてウレ
タンフオームだけを除去して形成するものである。
The catalytic converters currently in use include those with a single catalyst carrier such as a metal plate rust layer type, a fully curved particle type ceramic honeycomb structure, and recently, ceramic open-cell porous bodies with a three-dimensional skeleton structure. It has also been proposed to have a single catalyst carrier consisting of: This porous ceramic open-cell three-dimensional skeleton structure is produced by foaming soft urethane foam with a predetermined pore size, forming it into the required shape, and then impregnating the foamed urethane foam with liquid ceramic. It is then dried and finally baked to remove only the urethane foam.

E記いずれの触媒コンバーターも基本的な有害成分除去
効率と排気効率の関係を(反比例関係)解決するもので
はないが、上記第1.2の点の相互関係に於いて排気効
率を可及的に阻害しないで最大限の有害成分除去効率を
得られるものとしては上記単一のセラミック製連続気泡
三次元骨格構造多孔体を触媒担体に用いた触媒コンバー
ターが最も秀れていることが判明している。
None of the catalytic converters described in E above solve the basic relationship between harmful component removal efficiency and exhaust efficiency (inversely proportional relationship), but they can improve exhaust efficiency as much as possible in the mutual relationship of point 1.2 above. It has been found that the catalytic converter using the single open-cell ceramic porous body with a three-dimensional framework structure as the catalyst carrier is the most excellent as a device that can obtain the maximum harmful component removal efficiency without impairing the There is.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで自動車側に求められる有害成分除去効率、排気
効率等の要求特性は各車種、使用条件、環境、法規制等
その他いろいろの条件によって異なる。これに対して各
車に適用される触媒コンバーター側の有する有害成分除
去効率、排気効率等の能力特性がある。
By the way, the required characteristics such as harmful component removal efficiency and exhaust efficiency required for automobiles differ depending on each vehicle type, usage conditions, environment, laws and regulations, and other various conditions. On the other hand, there are performance characteristics such as harmful component removal efficiency and exhaust efficiency that the catalytic converter side has that is applied to each car.

上記自動車側に求められる要求特性と触媒コンバーター
側の能力特性を可及的に一致させることが望ましい、而
して従来の触媒コンバーターは単一の又は単一層の触媒
担体としているためその能力特性は第8図(B)の点線
に示す様に一様に決まってしまう。ところが第8図(C
)に示すように自動車側に求められる要求特性の場合は
上述のとおり、車種、使用条件等に応じた要求特性(夫
々一点鎖線、二点鎖線で示す)を相互に満足する様に求
められることが多く、徒って最終的に求められる要求特
性(実線で示す)は第8図(D)に示す様に一様な特性
ではない。
It is desirable to match the performance characteristics of the catalytic converter as much as possible with the characteristics required for the automobile. As shown by the dotted line in FIG. 8(B), it is determined uniformly. However, in Figure 8 (C
) As mentioned above, in the case of the required characteristics required from the automobile side, the required characteristics (indicated by the dashed-dotted line and the dashed-double-dotted line, respectively) depending on the vehicle type, usage conditions, etc. must be mutually satisfied. As a result, the finally required characteristics (indicated by the solid line) are not uniform as shown in FIG. 8(D).

従って実際に自動車側の有害成分除去効率、排気効率の
要求特性と、各車に適用される触媒コンバーターの有す
る同様な能力特性とは一致しない場合が多く、自動車側
に求められる要求特性に対して応じられる触媒コンバー
ター側の能力特性にも限界が生じていた。この様な要求
特性と能力特性の差は自動車に対する様々な要求が増々
高水準になっている現在では拡大するばかりであり、早
急な改善かもとめられている。
Therefore, in many cases, the required characteristics of harmful component removal efficiency and exhaust efficiency on the automobile side do not match the similar performance characteristics of the catalytic converter applied to each car, and the required characteristics on the automobile side There was also a limit to the capacity characteristics of the catalytic converter that could be met. The difference between such required characteristics and performance characteristics is only widening now that various demands for automobiles are becoming higher and higher, and there is an urgent need for improvement.

ところで、現在最も秀れていると思われるセラミック製
連続気泡三次元骨格構造多孔体の単一触媒担体を用いて
も要求特性に応じて2つ以上の異なる能力特性を有する
様に単一に形成すれば、上記問題点を解決することがで
きる様に思われるがウレタンフオームの発泡段階で異な
った相のものを複層にできない等の技術的問題が残され
ており実施が困難となっている。
By the way, even if you use a single catalyst carrier made of open-celled ceramic porous material with a three-dimensional skeleton structure, which is considered to be the best at present, it is possible to form a single catalyst carrier that has two or more different performance characteristics depending on the required characteristics. Although it seems that the above problems can be solved by doing so, there remain technical problems such as the inability to form layers of different phases during the foaming stage of the urethane foam, making it difficult to implement. .

従って本発明の目的とするところは、■有害成分除去効
率と排気効率の相互関係に於いて極めて秀れた能力特性
を有するセラミック製連続気泡三次元骨格構造多孔体を
触媒担体として用いながら、自動車側に求められる上記
有害成分除去効率、排気効率等の要求特性ごとにどのよ
うな要求特性に対しても可及的に応じられる様な能力特
性を出せる触媒コンバーターを提供するにあり、■その
際、格別高度な技術を用いることなく容易に行え、且つ
低コストを実現することができる触媒コンバーターを提
供するにある。
Therefore, the object of the present invention is to: 1) provide an automotive vehicle using a porous ceramic open-cell three-dimensional framework structure as a catalyst carrier, which has extremely excellent performance characteristics in terms of the mutual relationship between harmful component removal efficiency and exhaust efficiency; Our objective is to provide a catalytic converter that can meet any required characteristics as much as possible, such as the above-mentioned harmful component removal efficiency and exhaust efficiency. The object of the present invention is to provide a catalytic converter that can be easily performed without using particularly advanced technology and can be realized at low cost.

〔問題点を解決する為の手段〕[Means for solving problems]

本発明は従来の問題点を解決すると共に、J:記目的を
達成する為以下の技術的手段を講じたものである。
The present invention solves the conventional problems and takes the following technical means to achieve the object described in J.

即ち、自動車の排気ガス導入口と排出口を有するコンバ
ーターケーシング本体と該本体内に配された単一の触媒
担体とから成る自動車用触媒コンバーターに於いて、上
記触媒担体はセラミック製連続気泡三次元骨格構造体で
構成され、この触媒担体は複数に分割されると共に各分
割単位触媒担体は孔隙の大きさ、単位長さ当りの孔の数
が相互に異なったものであり、適用される自動車の排気
効率要求特性や排気ガス中の有害成分の除去効率要求特
性に応じて、それらの要求特性を満足するような能力特
性を出せる上記分割単位触媒担体が組合わされて、内部
に配設されていることを特徴とする自動車用触媒コンバ
ーターである。而して個々の分割単位触媒担体の個々の
能力特性は、孔隙の大きさ、単位長さ当たりの孔の数、
厚さ等の因子によって決まるものである。
That is, in an automobile catalytic converter consisting of a converter casing main body having an exhaust gas inlet and an exhaust port, and a single catalyst carrier disposed within the main body, the catalyst carrier is a ceramic open-cell three-dimensional ceramic converter. Consisting of a skeletal structure, this catalyst carrier is divided into a plurality of parts, and each divided unit catalyst carrier has a different pore size and number of pores per unit length, depending on the automobile to which it is applied. According to the required characteristics of exhaust efficiency and the required characteristics of removal efficiency of harmful components in exhaust gas, the above-mentioned divided unit catalyst carriers that can provide performance characteristics that satisfy those required characteristics are combined and arranged inside. This is an automotive catalytic converter characterized by the following. Therefore, the individual performance characteristics of each divided unit catalyst carrier are determined by the pore size, the number of pores per unit length,
This is determined by factors such as thickness.

〔作用〕[Effect]

排気効率と有害成分除去効率との関係に於いて能力特性
が夫々異なる3つの分割単位触媒担体S、、s2  、
s3を用意する。これらの比表面積の関係はs、<s2
 <s3とする。ところで自動車側に一定の排気効率に
対する一定の有害成分除去効率を有する様な要求特性0
が求められているとき、上記夫々の分割単位触媒担体S
t  、S2+S3を夫々単一で触媒コンバーターに用
いたとき、第7図(A)、CB)に示す様に上記要求特
性0に一致するものがない場合、可及的に要求特性0に
近い能力特性を有するものを選択し、組合せる。この場
合第7図(B)に示す様にある範囲で分割単位担体S、
が、他の範囲で分割単位担体S3が要求特性0に近いの
でこの2つを選択し。
Three divided unit catalyst carriers S, s2, each having different performance characteristics in the relationship between exhaust efficiency and harmful component removal efficiency.
Prepare s3. The relationship between these specific surface areas is s, <s2
<s3. By the way, the required characteristics such as a certain harmful component removal efficiency for a certain exhaust efficiency on the automobile side are 0.
is required, each of the above divided unit catalyst carriers S
When t, S2+S3 are used alone in a catalytic converter, as shown in Figure 7 (A) and CB), if there is no one that matches the required characteristic 0 above, the required characteristic is as close to 0 as possible. Select and combine those with characteristics. In this case, as shown in FIG. 7(B), within a certain range, the dividing unit carrier S,
However, in other ranges, the divided unit carrier S3 has the required characteristic close to 0, so these two are selected.

組合せるとする。その結果、第7図(C)に示す様に自
動車側に求められる上記要求特性0に可及的に応じられ
る能力特性を出す触媒コンバーターが容易に得られる。
Let's combine them. As a result, as shown in FIG. 7(C), it is easy to obtain a catalytic converter that exhibits performance characteristics that meet the above-mentioned required characteristics 0 required for automobiles as much as possible.

かくして、第1図に示す様に上記分割単位触媒担体S1
.S2を配した触媒コンバータ一本体内部9に導入され
た排出ガスは先ず分割単位触媒担体SI内を次に分割単
位触媒担体S2内を通過していく、この分割単位触媒担
体SI+32は夫々に異なる比表面積を有するセラミッ
ク製連続気泡三次元骨格構造を有する多孔体であり、排
出ガスの流路は複雑に入りくんでおり、その為排出ガス
はこの中を乱流しながら通過していく。
Thus, as shown in FIG. 1, the divided unit catalyst carrier S1
.. Exhaust gas introduced into the main body interior 9 of the catalytic converter equipped with S2 first passes through the divided unit catalyst carriers SI and then through the divided unit catalyst carriers S2. It is a porous body with a three-dimensional skeleton structure made of open cells made of ceramic with a large surface area, and the exhaust gas flow path is complicated, so the exhaust gas passes through it in a turbulent flow.

この様な排出ガスが個々の所で受ける作用は個々の触媒
担体の性質が異なるので一様ではなく、単一の触媒コン
バーター内で排気効率と浄化効率との関係が多様に変化
しているのである。従って分割単位触媒担体の組合せを
かえることにより。
The effects that exhaust gas receives at each location are not uniform because the properties of each catalyst carrier are different, and the relationship between exhaust efficiency and purification efficiency changes in a variety of ways within a single catalytic converter. be. Therefore, by changing the combination of split unit catalyst carriers.

単一の触媒コンバーターとしては多様な排気効率に対す
る浄化効率の能力特性を有するものにでき、いかなる要
求特性にも応じられるようになる。
A single catalytic converter can have various exhaust efficiency and purification efficiency performance characteristics, and can meet any required characteristics.

即ち、自動車側に求められる一定の排気効率に対する一
定の浄化効率を有する様な要求特性に個々一致する能力
特性を有するものではないが、任意の能力特性を有する
ものを組合せることにより、触媒コンバーター全体とし
ての能力特性は、自動車側に求められる要求特性に応じ
られるものとなる。
In other words, the catalytic converter does not have performance characteristics that individually match the required characteristics such as having a certain purification efficiency for a certain exhaust efficiency required by the automobile, but by combining devices with arbitrary performance characteristics, it is possible to improve the catalytic converter. The performance characteristics as a whole will meet the required characteristics required by the automobile side.

〔実施例〕〔Example〕

以下本発明の好適なる実施例を図面に基づき詳述する。 Hereinafter, preferred embodiments of the present invention will be described in detail based on the drawings.

先ず第1図〜第4図に基づき第1実施例を説明する。First, a first embodiment will be explained based on FIGS. 1 to 4.

第1図に於いて、■は自動車用触媒コンバータ一本体を
示す、この触媒コンバータ一本体1は一方側に排出ガス
導入口3と他方側に排出ガス導出口2を有し、本体1の
端部l′に形成されたフランジ4にて自動車の排気マフ
ラー5のフランジ5′に連設されている。この場合触媒
コンバータ一本体1は着脱筒にするため上記連設する手
段としてナツト、ボルトを利用している。この連設部分
は図示しないシール手段が施されている。この様にして
コンバータ一本体lとマフラー5とが連通ずるとガス導
入口3から矢示7で示す様に排出ガスが導入され、コン
バータ一本体内部9に残留する間にガス中の有害成分例
えばCO,l(C,Noを図示しない空気導入手段によ
り導入された空気により酸化或いは還元され、続けて矢
示6に示す様に他方側のガス導出口2より排出される。
In Fig. 1, ■ indicates a main body of an automobile catalytic converter.This catalytic converter main body 1 has an exhaust gas inlet 3 on one side and an exhaust gas outlet 2 on the other side. A flange 4 formed at portion l' is connected to a flange 5' of an exhaust muffler 5 of an automobile. In this case, the catalytic converter main body 1 is made into a removable cylinder, so nuts and bolts are used as the connecting means. This continuous portion is provided with a sealing means (not shown). When the converter main body 1 and the muffler 5 communicate with each other in this manner, exhaust gas is introduced from the gas inlet 3 as shown by the arrow 7, and while it remains inside the converter main body 9, harmful components in the gas such as CO, l (C, No) are oxidized or reduced by the air introduced by an air introduction means (not shown), and are subsequently discharged from the gas outlet 2 on the other side as shown by arrow 6.

上記酸化或いは還元反応を十分に行なわしめ有害成分除
去効率(有害成分の浄化効率)を良くするためには、コ
ンバータ一本体1内部9にガスが残留しやすくするため
の手段が必要である。この手段として第1図に示す様に
コンバータ一本体l内部に触媒担体を設ける。該触媒担
体は単一のものではなく複数の分割単位触媒担体Sl 
 + 32  。
In order to sufficiently carry out the above oxidation or reduction reaction and improve the harmful component removal efficiency (harmful component purification efficiency), a means for making it easier for gas to remain inside the converter main body 1 is required. As a means for this purpose, a catalyst carrier is provided inside the converter main body l as shown in FIG. The catalyst carrier is not a single one but a plurality of divided unit catalyst carriers Sl.
+32.

・・−3nで構成されており、第1図では2つの分割単
位触媒担体s、、s2で構成した場合を示している。又
、各分割単位触媒担体s、、s2はセラミック製で第2
図(A)〜(C)に示す様に連続気泡三次元骨格構造を
有する多孔体であって、第3図に示す様に軟質ウレタン
フオームを発泡させる第一工程とこの発泡ウレタンフオ
ームを必要な形状に裁断する第2工程と、セラミック原
料を液状にする第3工程と、液状セラミック原料の粘度
を調整する第4工程と、この液状セラミック原料を上記
発泡ウレタンフオームに含浸させる第5工程と、液状セ
ラミック原料を乾燥させ固まらせる第6エ程と、固まっ
たセラミック原料を焼いて発泡ウレタンフオームを除去
する第7エ程を経て形成される。
...-3n, and FIG. 1 shows a case in which it is composed of two divided unit catalyst carriers s, , s2. In addition, each divided unit catalyst carrier s,, s2 is made of ceramic and the second
As shown in Figures (A) to (C), it is a porous body having an open-cell three-dimensional skeleton structure, and as shown in Figure 3, the first step is to foam a soft urethane foam, a second step of cutting into a shape, a third step of liquefying the ceramic raw material, a fourth step of adjusting the viscosity of the liquid ceramic raw material, a fifth step of impregnating the urethane foam with the liquid ceramic raw material, It is formed through a sixth step in which the liquid ceramic raw material is dried and solidified, and a seventh step in which the solidified ceramic raw material is baked to remove the urethane foam.

又、上記各分割単位触媒担体s、、s2は上記第1工程
の発泡条件或いは第4工程の粘度条件により第2図(A
)、(C)に示す様に孔隙10の大きさや単位長さ当た
りの孔数又は厚さが異なる様に形成されている。即ち、
個々の単位触媒担体は夫々比表面積が異なる。従って図
示しないが分割単位触媒担体s、、s2よりも大きな孔
隙或いは小さな孔隙を有するものや、単位長さ当たりの
孔数の多いもの或いは少ないもの即ち、比表面積の大き
いもの小さいものも形成可能である。
In addition, each of the divided unit catalyst carriers s, s2 has the same characteristics as shown in FIG. 2 (A) depending on the foaming conditions in the first step or the viscosity conditions in the fourth step.
) and (C), the holes 10 are formed to have different sizes, number of holes per unit length, or thickness. That is,
Each unit catalyst carrier has a different specific surface area. Therefore, although not shown in the drawings, it is also possible to form catalyst carriers with larger or smaller pores than the divided unit catalyst carriers s, s2, with more or fewer pores per unit length, that is, with larger or smaller specific surface areas. be.

と記触媒担体を構成する分割単位触媒担体s、、s2 
争・−3nの数、或いは各分割単位触媒担体をどれだけ
の比表面積を有するものにするかは自在に組合せること
が出来る。この場合適用される自動車側に求められる排
気効率要求特性、や排出ガス中の有害成分除去効率要求
特性に応じて、それらの要求特性を満足する能力特性を
出せるように組合せる。
Divided unit catalyst carriers s, , s2 constituting the catalyst carrier written as
The number of -3n or the specific surface area of each divided unit catalyst carrier can be freely combined. In this case, depending on the exhaust efficiency required characteristics required by the automobile to which the vehicle is applied and the required characteristics required for the removal efficiency of harmful components in exhaust gas, the combinations are made so as to produce performance characteristics that satisfy these required characteristics.

従って第1図に示す様に2つの比表面積の異なる分割単
位触媒担体s、、s2を組合せても要求特性に応じられ
ない場合には第4図に示す様に比表面積の異なる3つの
分割単位触媒担体SI+S2.S3を組合せて行うとい
うようにする。この場合側々の分割単位触媒担体s、、
s2  、s3の配列は何ら限定されるものではない、
又この実施例に於いては第1図及び第4図に示す様に個
々の分割単位触媒担体の間に空間8を設けている。
Therefore, if the required characteristics cannot be met even by combining two divided unit catalyst carriers s, , s2 with different specific surface areas as shown in FIG. 1, three divided units with different specific surface areas as shown in FIG. Catalyst carrier SI+S2. This is done in combination with S3. In this case the side split unit catalyst carriers s,
The arrangement of s2 and s3 is not limited in any way,
Further, in this embodiment, as shown in FIGS. 1 and 4, spaces 8 are provided between the individual divided unit catalyst carriers.

上記分割単位触媒担体s、、s2 、S3 φ・・Sn
は1記のとおり、セラミック製連続気泡三次元骨格構造
を有する多孔体で形成されているので、触媒コンバータ
一本体1内に導入された排出ガスが上記分割単位触媒担
体s、、s2  +33内を夫々通過するとき、複雑に
入りくんだ連通流路中を通過するため乱流を起こすが、
上記空間8を設けることにより、排出ガスの流れをいっ
たん整流することができ、次なる分割単位触媒担体にス
ムーズに移行させ、必要以上に排気効率を阻害しないよ
うにすることができる。
The above divided unit catalyst carriers s,, s2, S3 φ...Sn
As described in 1, since it is formed of a porous body having a three-dimensional skeleton structure of ceramic open cells, the exhaust gas introduced into the catalytic converter main body 1 flows through the divided unit catalyst carriers s, , s2 +33. When passing through each, it passes through a complicated communication channel, which causes turbulence.
By providing the space 8, the flow of the exhaust gas can be rectified once, and it can be smoothly transferred to the next divided unit catalyst carrier, so that the exhaust efficiency is not inhibited more than necessary.

上記空間8は上述した通り、自動車側に求められる要求
特性に応じて付加的に設けられるものであって絶対条件
ではない、又、上記分割単位触媒担体S I  + S
 2等を触媒コンバータ一本体l内に配設するときには
、しっかりと固定する必要があるが、この場合の固定方
法、或いは位置決め方法は特に制限されるものではなく
、図示しないが個々の分割単位触媒担体の間に金属0リ
ングを配し1位置決めを図ることで達成される。
As mentioned above, the space 8 is additionally provided according to the required characteristics required for the automobile, and is not an absolute condition.
When arranging the second unit in the catalytic converter main body l, it is necessary to securely fix it, but in this case, the fixing method or positioning method is not particularly limited. This is achieved by placing a metal O-ring between the carriers and positioning the carrier.

以下特許請求の範囲第2項に記載した第2の発明につい
ての好適なる第2実施例を第5.6図に基づき詳述する
A second preferred embodiment of the second invention described in claim 2 will be described in detail below with reference to FIG. 5.6.

第2実施例では第5図に示すように第1実施例に示した
触媒コンバータ一本体1の内部9に夫々比表面積の異な
る3つの分割単位触媒担体S1 。
In the second embodiment, as shown in FIG. 5, three divided unit catalyst carriers S1 each having a different specific surface area are provided inside 9 of the catalytic converter main body 1 shown in the first embodiment.

s2.s3を配設している。第1実施例に記したとおり
、この分割単位触媒担体の数、及び個々の分割単位触媒
担体の比表面積の差(孔隙の大きさ、単位長さあたりの
孔数等による。)を自在に選択し組合せることができる
s2. s3 is installed. As described in the first embodiment, the number of divided unit catalyst carriers and the difference in specific surface area of each divided unit catalyst carrier (depending on the size of the pores, the number of pores per unit length, etc.) can be freely selected. and can be combined.

さて第2実施例では、個々の分割単位触媒担体s、、s
2 +33の夫々の間に排出ガスの流量を制御する為の
銅を主成分とする材料でニッケル。
Now, in the second embodiment, the individual divided unit catalyst carriers s,, s
Nickel is a copper-based material for controlling the flow rate of exhaust gas between each of 2 and 33.

クロム、モリブデン等の合金製の金属製多孔板を設ける
。又、この金属多孔板はこれだけでも触媒担体の機能を
有する。
A metal perforated plate made of alloy such as chromium or molybdenum is provided. Moreover, this metal porous plate alone has the function of a catalyst carrier.

第5図は分割単位触媒担体s、、s2の間、及びS2+
S3の間に夫々11a 、 llbの2枚の金属多孔板
を設けた場合を示している。上記金属多孔板11a 、
 llbは第6図(A)、第6図(B)に示す様に夫々
、孔の大きさ、孔数が異なるものであり、図示しないが
上記金属多孔板11a、11b以外にも形成できる0個
々の分割単位触媒担体S1 。
Figure 5 shows the space between the divided unit catalyst carriers s, , s2, and S2+
A case is shown in which two metal porous plates 11a and llb are provided between S3. The metal porous plate 11a,
As shown in FIG. 6(A) and FIG. 6(B), llb has different hole sizes and numbers of holes, and although not shown, it can be formed other than the metal porous plates 11a and 11b. Individual split unit catalyst carrier S1.

s2.s3の間にいか様な金属多孔板を組合せるかは、
分割単位触媒担体を組合せる場合と同様適用される自動
車側に求められる排気効率、排出ガス中の有害成分除去
効率(浄化効率)等の要求特性に応じられる様な走力特
性を出せる様に組合せる。又、これらの金属多孔板11
a 、 llbを分割単位触媒担体S、、s2 、s3
の夫々の間に配する場合には第5図に示すように第1実
施例に示した空間8を設けることなく互いに接触する様
にする。
s2. What kind of metal perforated plate should be combined during s3?
Similar to the case of combining split unit catalyst carriers, combinations are made to produce running characteristics that meet the requirements of the automobile to which it is applied, such as exhaust efficiency and efficiency of removing harmful components from exhaust gas (purification efficiency). Ru. Moreover, these metal porous plates 11
a, llb are divided into unit catalyst carriers S,, s2, s3
5, they are placed in contact with each other without providing the space 8 shown in the first embodiment, as shown in FIG.

次に一連の動作を説明する°。Next, I will explain the series of operations.

排気効率と有害成分除去効率との関係に於いて能力特性
が夫々異なる3つの分割単位触媒担体s、、s2  +
53を用意する。第7図(B)の線図はこれを示したも
のである。これらの比表面積の関係はS !>S2 >
33とする。ところで自動車側に一定の排気効率に対す
る一定の有害成分除去効率を有する様な要求特性0が第
7図(A)のように求められているとき、上記夫々の分
割単位触媒担体s、、s2  、S3を夫々単一で触媒
コンバーターに用いたとき、第7図(A)、(B)に示
す様に上記要求特性Oに一致するものがない場合、可及
的に要求特性0に近い能力特性を有するものを選択し、
組合せる。この場合第7図(B)に示す様にある範囲で
分割単位担体S1が、他の範囲で分割単位担体S2が要
求特性0に近いのでこの2つを選択し、組合せる。その
結果、第7図CC’)に示す様に自動車側に求められる
上記要求特性0に可及的に応じられる触媒コンバーター
が容易に得られる。第7図(C)は、上記選択組合せの
結果の触媒コンバーター全体の能力線図である。
Three divided unit catalyst carriers s,, s2 + each having different performance characteristics in the relationship between exhaust efficiency and harmful component removal efficiency.
Prepare 53. The diagram in FIG. 7(B) shows this. The relationship between these specific surface areas is S! >S2>
33. By the way, when the required characteristic 0 such as having a certain harmful component removal efficiency for a certain exhaust efficiency on the automobile side is required as shown in FIG. When S3 is used alone in a catalytic converter, if there is no one that matches the above required characteristic O as shown in FIGS. 7(A) and (B), the performance characteristic is as close to the required characteristic 0 as possible. Select the one that has
Combine. In this case, as shown in FIG. 7(B), since the divided unit carrier S1 has the required characteristic close to 0 in a certain range and the divided unit carrier S2 has the required characteristic close to 0 in another range, these two are selected and combined. As a result, as shown in FIG. 7 CC'), a catalytic converter can be easily obtained that can meet the above-mentioned required characteristic 0 required for automobiles as much as possible. FIG. 7(C) is a performance diagram of the entire catalytic converter as a result of the above-mentioned selected combinations.

かくして、第1図に示す様に上記分割単位触媒担体S、
、S2を配した触媒コンバータ一本体1内部9に導入さ
れた排出ガスは先ず分割単位触媒担体SI内を次に分割
単位触媒担体S2内を通過していく、この分割単位触媒
担体s、、s2は夫々に異なる比表面積を有するセラミ
ック製連続気泡三次元骨格構造を有する多孔体であり、
排出ガスの流路は複雑に入りくんでおり、その為排出ガ
スはこの中を乱流しながら通過していく、このとき分割
単位触媒担体s、、s2との間に空間8が設けられてい
るときは、この空間8により排出ガスはいったん整流さ
れるので分割単位触媒担体S2への侵入がスムーズに行
なわれるが、この空間8のかわりに第2実施例に示す様
に金属多孔板11a等が配されている場合には、この金
属多孔板自体が触媒担体として排出ガスを残留させよう
と作用する。
Thus, as shown in FIG. 1, the divided unit catalyst carrier S,
, S2, the exhaust gas introduced into the interior 9 of the catalytic converter main body 1 first passes through the divided unit catalyst carriers SI and then through the divided unit catalyst carriers S2. is a porous body with a three-dimensional skeleton structure of ceramic open cells each having a different specific surface area,
The exhaust gas flow path is complicated, and therefore the exhaust gas passes through it in a turbulent flow. At this time, a space 8 is provided between the divided unit catalyst carriers s, s2. In this case, the exhaust gas is once rectified by this space 8, so that it can smoothly enter the divided unit catalyst carrier S2. When such a metal porous plate is provided, the metal porous plate itself acts as a catalyst carrier to allow the exhaust gas to remain.

この様な排出ガスが個々の所で受ける作用は個々の触媒
担体の性質が異なるので一様ではなく。
The effect that such exhaust gas receives at each location is not uniform because the properties of each catalyst carrier are different.

単一の触媒コンバーター内で排気効率と浄化効率との関
係が多様に変化しているのである。従って分割単位触媒
担体の組合せをかえることにより、単−の触媒コンバー
ターとしては多様な排気効率に対する浄化効率の能力特
性を有するものにでき、いかなる要求特性にも応じられ
るようになる。
The relationship between exhaust efficiency and purification efficiency changes in a variety of ways within a single catalytic converter. Therefore, by changing the combination of divided unit catalyst carriers, a single catalytic converter can have various performance characteristics of purification efficiency with respect to exhaust efficiency, and can meet any required characteristics.

即ち、自動車側に求められる一定の排気効率に対する一
定の浄化効率を有する様な要求特性に個々一致する能力
特性を有するものではないが、任意の能力特性を有する
ものを組合せることにより、触媒コンバーター全体とし
ての能力特性は、自動車側に求められる要求特性に応じ
られるものとなる。
In other words, the catalytic converter does not have performance characteristics that individually match the required characteristics such as having a certain purification efficiency for a certain exhaust efficiency required by the automobile, but by combining devices with arbitrary performance characteristics, it is possible to improve the catalytic converter. The performance characteristics as a whole will meet the required characteristics required by the automobile side.

〔発明の効果〕〔Effect of the invention〕

以上のことから判るとおり本発明によれば自動車側に求
められる一定の排気効率に対する一定の浄化効率(有害
成分除去効率)を有する様な要求特性に適正に応じられ
る能力特性を有する触媒コンバーターを提供することが
できる。
As can be seen from the above, the present invention provides a catalytic converter that has performance characteristics that can appropriately meet the required characteristics such as a certain purification efficiency (toxic component removal efficiency) for a certain exhaust efficiency required by an automobile. can do.

即ち、自動車に求められる排気効率、浄化効率等の要求
特性は種々の条件により、多様なものであり、他方触媒
コンバーターに用いる触媒担体として秀れたセラミック
製連続気泡三次元骨格構造を有する多孔体は技術的問題
から単一状で部分的に比表面積を異なるようにすること
は困難であったので一様な能力特性しか発揮することが
できなかった0本発明は従来の触媒コンバーターの単一
触媒担体を複数に分割し、個々の分割単位触媒担体を夫
々比表面積が異なるものとし、適用される自動車側に求
められる排気効率、有害成分除去効率等の要求特性を満
足する能力特性を出せる様に上記分割単位触媒担体を適
宜組合せるようにしたからである。
In other words, the characteristics required for automobiles, such as exhaust efficiency and purification efficiency, vary depending on various conditions.On the other hand, porous bodies made of ceramic with an open-cell three-dimensional skeleton structure are excellent as catalyst carriers for use in catalytic converters. Due to technical problems, it was difficult to vary the specific surface area in parts of a single catalytic converter, so only uniform performance characteristics could be exhibited. The catalyst carrier is divided into multiple parts, and each divided unit catalyst carrier has a different specific surface area, so that performance characteristics can be achieved that satisfy the required characteristics such as exhaust efficiency and harmful component removal efficiency required by the automobile to which it is applied. This is because the above-mentioned divided unit catalyst carriers are appropriately combined.

従って特に高度な技術を用いることなく容易に実施する
ことができるものである。而してこの分割単位触媒担体
の組合せの好適なものは、実験的に容易に求めることが
できるものである。更に特許請求の範囲第2項に記載し
た第2発明によれば上記側々の分割単位触媒担体の間に
金属多孔板を設ける様にしたので、複数の分割単位触媒
担体の組合せだけでは応じきれない特殊な要求特性が求
められたときでも金属多孔板を孔径、孔数等の異なるも
のにかえることにより、より多様な能力特性を発揮させ
ることができ、上記特殊な要求特性にも応じられる触媒
コンバーターを提供することができる。
Therefore, it can be easily implemented without using particularly advanced technology. A suitable combination of the divided unit catalyst carriers can be easily determined experimentally. Furthermore, according to the second invention described in claim 2, a metal porous plate is provided between the divided unit catalyst carriers on each side, so that the combination of a plurality of divided unit catalyst carriers alone cannot be used. Even when special required characteristics are required, by changing the metal porous plate to one with a different pore diameter, number of holes, etc., it is possible to exhibit more diverse performance characteristics, and the catalyst can meet the above-mentioned special required characteristics. converter can be provided.

このように、本発明は、予め能力特性の異なる分割単位
触媒担体を準備すればよく、予め究めつくした特定的な
もののみを用意する必要がないので、その生産も容易で
ある利点を併せもつものである。
As described above, the present invention has the advantage that it is easy to produce because it is only necessary to prepare split unit catalyst carriers with different performance characteristics in advance, and there is no need to prepare only specific ones that have been thoroughly investigated in advance. It is something.

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

添付図面第1図〜第7図は実施例であり、第1図〜第4
図は第1実施例、第5図〜第7図は第2実施例を示す図
であり、第1図は触媒コンバータ一本体を示す断面図、
第2図(A)は分割単位触媒担体のx−X線断面図、第
2図(B)は同部分の拡大図、第2図(C)は同Y−Y
線断面図、第3図は分割単位触媒担体の製造工程図、第
4図は触媒コンバータ一本体の他の例を示す断面図、第
5図は第2実施例に於ける触媒コンバータ一本体を示す
断面図、第6図(A)は金属多孔板を示すV−V線断面
図、第6図CB)は金属多孔板を示すW−W線断面図、
第7図(A)、は自動車側の要求特性線図、(B)は分
割単位触媒担体の能力特性線図、(C)は組合せを選択
した後の触媒コンバーター全体の能力特性線図、第8図
(A)は排気効率と有害成分除去効率が互いに反比例す
ることを説明する為の線図、第8図(B)は従来の単一
層の触媒担体の一様に決まる能力特性線図、第8図(C
)は自動車側の要求する特性が種々ある旨を示す線図、
第8図CD)は、木来求められるべき望ましい特性線図
の例を示した図であり、 尚、図中109.触媒コンバータ一本体、290.排ガ
ス導出口#9ミコF 389.排ガス導入口。 s、、S2  、S3  、、、分割単位触媒担体であ
る。 竿2園(A) 不2園(C) 竿3 閃 多孔体の触媒4gL、(本 基4 園 不5区 卒6区 (A) 阜6@ (B) 竿7医(A) *筈ゆ儲鮫呻 竿7因(C) 早8圀A 、耳肴へか降り動子 竿8阿C 肩害暗玲都幼平 手続?fi正書(方式) %式% 2 発明の名称 自動車用触媒コンバーター 3 補正をする者 事件との関係  特許出願人 住 所  静岡県磐田市寺谷新田35番地氏名 鈴木 
健次 4 代理人     〒220
The attached drawings Figures 1 to 7 are examples, and Figures 1 to 4 are examples.
The figure shows the first embodiment, and FIGS. 5 to 7 show the second embodiment, and FIG. 1 is a sectional view showing the main body of the catalytic converter.
Figure 2 (A) is a cross-sectional view taken along the line x-X of the divided unit catalyst carrier, Figure 2 (B) is an enlarged view of the same part, and Figure 2 (C) is the same
A line sectional view, FIG. 3 is a manufacturing process diagram of a divided unit catalyst carrier, FIG. 4 is a sectional view showing another example of a catalytic converter main body, and FIG. 5 is a catalytic converter main body in a second embodiment. 6(A) is a sectional view taken along the line V-V showing the perforated metal plate, FIG. 6 CB) is a sectional view taken along the line W-W showing the perforated metal plate,
Figure 7 (A) is a required characteristic diagram for the automobile, (B) is a performance characteristic diagram of the divided unit catalyst carrier, and (C) is a performance characteristic diagram of the entire catalytic converter after selecting the combination. Figure 8 (A) is a diagram to explain that exhaust efficiency and harmful component removal efficiency are inversely proportional to each other, Figure 8 (B) is a diagram of the performance characteristics uniformly determined for a conventional single-layer catalyst carrier, Figure 8 (C
) is a diagram showing that there are various characteristics required by automobiles,
Fig. 8 (CD) is a diagram showing an example of a desirable characteristic diagram to be obtained. Catalytic converter body, 290. Exhaust gas outlet #9 Miko F 389. Exhaust gas inlet. s, , S2 , S3 , , are divided unit catalyst carriers. Rod 2 Garden (A) Fu 2 Garden (C) Rod 3 Flash porous catalyst 4gL, (Basic 4 Garden Fu 5 Ward Graduation 6 Ward (A) Fu 6 @ (B) Rod 7 Doctor (A) *Shutyu Yusame moaning rod 7 reasons (C) Haya 8 Kuni A, moving to the earpiece 8 A C Shoulder harm anreito yohei procedure? fi official book (method) % formula % 2 Name of invention Automotive catalyst Converter 3 Relationship with the case of the person making the amendment Patent applicant Address: 35 Teratani Shinden, Iwata City, Shizuoka Prefecture Name: Suzuki
Kenji 4 Agent 〒220

Claims (2)

【特許請求の範囲】[Claims] (1)自動車の排気ガス導入口と排出口を有するコンバ
ーターケーシング本体と該本体内に配された触媒担体と
から成る自動車用触媒コンバーターであって、上記触媒
担体はセラミックス製連続気泡三次元骨格構造体で構成
され、この触媒担体は複数に分割されると共に各分割単
位触媒担体は孔隙の大きさ、単位長さ当りの孔の数が相
互に異なったものであり、適用される自動車の排気効率
要求特性や排気ガス中の有害成分の除去効率要求特性に
応じて、それらの要求特性を満足する能力特性を出せる
ように、上記分割単位触媒担体が組合わされて、内部に
配設されていることを特徴とする自動車用触媒コンバー
ター。
(1) An automotive catalytic converter consisting of a converter casing body having an exhaust gas inlet and an exhaust port, and a catalyst carrier disposed within the body, wherein the catalyst carrier has an open-cell three-dimensional skeletal structure made of ceramics. This catalyst carrier is divided into a plurality of parts, and each divided unit catalyst carrier has a different pore size and number of pores per unit length, and the exhaust efficiency of the automobile to which it is applied is different. In accordance with the required characteristics and the required characteristics for the removal efficiency of harmful components in exhaust gas, the divided unit catalyst carriers described above are combined and arranged internally so that the ability characteristics that satisfy those required characteristics can be obtained. An automotive catalytic converter featuring:
(2)自動車の排気ガス導入口と排出口を有するコンバ
ーターケーシング本体と該本体内に配された触媒担体と
から成る自動車用触媒コンバーターであって、上記触媒
担体はセラミック製連続気泡三次元骨格構造体で構成さ
れ、この触媒担体は複数に分割されると共に各分割単位
触媒担体は孔隙の大きさ、単位長さ当りの孔の数が相互
に異なったものであり、適用される自動車の排気効率要
求特性や排気ガス中の有害成分の除去要求特性に応じて
、それらの要求特性を満足する能力特性を出せるように
、上記分割単位触媒担体が組合わされて、内部に配設さ
れている自動車用触媒コンバーターに於いて、上記各分
割単位触媒担体の間には金属多孔板が配されていること
を特徴とする自動車用触媒コンバーター。
(2) A catalytic converter for an automobile consisting of a converter casing main body having an automobile exhaust gas inlet and an exhaust port, and a catalyst carrier disposed within the main body, the catalyst carrier having an open-cell three-dimensional skeletal structure made of ceramic. This catalyst carrier is divided into a plurality of parts, and each divided unit catalyst carrier has a different pore size and number of pores per unit length, and the exhaust efficiency of the automobile to which it is applied is different. According to the required characteristics and the required characteristics for removal of harmful components in exhaust gas, the above-mentioned divided unit catalyst carriers are combined and arranged inside so that the ability characteristics that satisfy those required characteristics can be obtained. A catalytic converter for an automobile, characterized in that a metal porous plate is disposed between each of the divided unit catalyst carriers.
JP61284058A 1986-11-28 1986-11-28 Catalyst converter for automobile Pending JPS63138113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61284058A JPS63138113A (en) 1986-11-28 1986-11-28 Catalyst converter for automobile

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61284058A JPS63138113A (en) 1986-11-28 1986-11-28 Catalyst converter for automobile

Publications (1)

Publication Number Publication Date
JPS63138113A true JPS63138113A (en) 1988-06-10

Family

ID=17673745

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61284058A Pending JPS63138113A (en) 1986-11-28 1986-11-28 Catalyst converter for automobile

Country Status (1)

Country Link
JP (1) JPS63138113A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015015619A1 (en) * 2013-08-01 2015-02-05 Miyashita Michiko Exhaust gas purification system

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5217615U (en) * 1975-07-23 1977-02-08
JPS574235A (en) * 1980-06-12 1982-01-09 Toru Mashida Catalytic device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5217615U (en) * 1975-07-23 1977-02-08
JPS574235A (en) * 1980-06-12 1982-01-09 Toru Mashida Catalytic device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015015619A1 (en) * 2013-08-01 2015-02-05 Miyashita Michiko Exhaust gas purification system
CN104968911A (en) * 2013-08-01 2015-10-07 宫下美智子 Exhaust gas purification system

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