JPH1110008A - Catalyst converter - Google Patents

Catalyst converter

Info

Publication number
JPH1110008A
JPH1110008A JP9168870A JP16887097A JPH1110008A JP H1110008 A JPH1110008 A JP H1110008A JP 9168870 A JP9168870 A JP 9168870A JP 16887097 A JP16887097 A JP 16887097A JP H1110008 A JPH1110008 A JP H1110008A
Authority
JP
Japan
Prior art keywords
cut
raised
catalytic converter
valley
waveform
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
JP9168870A
Other languages
Japanese (ja)
Inventor
Yasuhiro Mita
裕弘 三田
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.)
Marelli Corp
Original Assignee
Calsonic 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 Calsonic Corp filed Critical Calsonic Corp
Priority to JP9168870A priority Critical patent/JPH1110008A/en
Publication of JPH1110008A publication Critical patent/JPH1110008A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2330/00Structure of catalyst support or particle filter
    • F01N2330/30Honeycomb supports characterised by their structural details
    • F01N2330/38Honeycomb supports characterised by their structural details flow channels with means to enhance flow mixing,(e.g. protrusions or projections)

Abstract

PROBLEM TO BE SOLVED: To provide a catalytic convertor capable of improving exhaust gas purifying performance by avoiding the opening phenomenon of a core. SOLUTION: In a structure in which the honeycomb shaped core 3 formed by laminating the catalyst carriers 5 consisting of corrugated metallic thin plates to form cells at the laminated part is formed and arranged in a shell 2, plural numbers of grooves 6 in the cylindrical direction formed toward the cylindrical peripheral direction on the inner surface of the shell 2, the catalyst carrier 5 is engaged with the grooves 6 at the outer peripheral side of the core 3 in the laminated direction to restrict the mutual detachment of the catalyst carriers 5.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は自動車の排気系等に
設けられて、排気ガスを通過させることにより触媒反応
によって排気ガス中の有害成分を浄化する触媒コンバー
タに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a catalytic converter provided in an exhaust system or the like of an automobile and purifying harmful components in the exhaust gas through a catalytic reaction by passing the exhaust gas.

【0002】[0002]

【従来の技術】触媒コンバータの中には、例えば特開平
1−236948号公報に示されているように、金属薄
板からなる波形状の触媒担体を重ね合わせて、重ね合わ
せ部分にセルを形成したハニカム状のコアを外筒内に配
設して構成したものが知られている。
2. Description of the Related Art In a catalytic converter, for example, as shown in Japanese Patent Application Laid-Open No. 1-236948, a corrugated catalyst carrier made of a thin metal plate is overlapped to form a cell in the overlapped portion. There is known a structure in which a honeycomb core is provided in an outer cylinder.

【0003】[0003]

【発明が解決しようとする課題】前述のように波形状の
触媒担体を重ね合わせてハニカム状のコアを形成したも
のでは、波形状の触媒担体をうず巻状に巻回積層してハ
ニカム状のコアを形成したものとは異なり、排気ガスの
流入圧力で触媒担体が中心部分から後方へスパイラル状
に飛び出す所謂フィルムアウト現象を回避することはで
きるが、コアの入口側で排気ガスの圧力を受けることに
よって、重ね合わせた触媒担体相互が開離する所謂口開
き現象が生じ、特に、排気マニホールドに近接して設け
た場合にこの現象が顕著となって、排気ガスの浄化性能
が低下してしまう可能性がある。
As described above, in the case where the honeycomb core is formed by laminating the corrugated catalyst carriers, the honeycomb carrier is formed by winding the corrugated catalyst carriers in a spiral shape. Unlike the one in which the core is formed, it is possible to avoid a so-called film-out phenomenon in which the catalyst carrier jumps backward from the center portion in a spiral shape by the inflow pressure of the exhaust gas, but receives the pressure of the exhaust gas at the inlet side of the core. As a result, a so-called opening phenomenon in which the superposed catalyst carriers are separated from each other occurs, and particularly when the catalyst carriers are provided close to the exhaust manifold, the phenomenon becomes conspicuous, and the exhaust gas purification performance decreases. there is a possibility.

【0004】そこで、本発明は重ね合わせた波形状の触
媒担体相互がコア入口側の排気ガスの圧力で開離して口
開き現象が生じるのを回避することができて、排気ガス
の浄化性能を一段と向上することができる触媒コンバー
タを提供するものである。
Accordingly, the present invention can prevent the opening and closing phenomenon caused by the separation of the superposed corrugated catalyst carriers due to the pressure of the exhaust gas on the core inlet side, thereby improving the purification performance of the exhaust gas. An object of the present invention is to provide a catalytic converter that can be further improved.

【0005】[0005]

【課題を解決するための手段】請求項1の発明は、波形
成形した金属薄板からなる触媒担体を重ね合わせて、重
ね合わせ部分にセルを形成したハニカム状のコアを形成
し、このコアを外筒内に配設した構造において、前記外
筒の内面に、筒長方向の溝を筒周方向へ複数本形成し、
該溝に、前記コアの外周側で前記触媒担体が重ね合わせ
方向に係合し、触媒担体相互の開離を拘束したことを特
徴とする。
According to the first aspect of the present invention, a catalyst-shaped core made of corrugated metal sheets is overlapped to form a honeycomb-shaped core having cells formed in the overlapped portion. In the structure disposed in the cylinder, on the inner surface of the outer cylinder, a plurality of grooves in the cylinder length direction are formed in the cylinder circumferential direction,
The catalyst carrier is engaged with the groove in the overlapping direction on the outer peripheral side of the core, thereby restraining the catalyst carriers from being separated from each other.

【0006】請求項2の発明は、請求項1記載の触媒コ
ンバータであって、前記溝は、前記外筒の少なくともコ
アの入口側に設けられていることを特徴とする。
According to a second aspect of the present invention, there is provided the catalytic converter according to the first aspect, wherein the groove is provided at least on the inlet side of the core of the outer cylinder.

【0007】請求項3の発明は、請求項1又は2記載の
触媒コンバータであって、前記溝は、前記外筒の内面に
セレーションを設けて形成したことを特徴とする。
A third aspect of the present invention is the catalytic converter according to the first or second aspect, wherein the groove is formed by providing serrations on an inner surface of the outer cylinder.

【0008】請求項4の発明は、請求項1又は2記載の
触媒コンバータであって、前記溝は、前記外筒内に固着
した波板によって形成したことを特徴とする。
According to a fourth aspect of the present invention, there is provided the catalytic converter according to the first or second aspect, wherein the groove is formed by a corrugated plate fixed in the outer cylinder.

【0009】請求項5の発明は、請求項1〜4のいずれ
かに記載の触媒コンバータであって、前記溝は、表面に
触媒を担持させたことを特徴とする。
According to a fifth aspect of the present invention, there is provided the catalytic converter according to any one of the first to fourth aspects, wherein the groove carries a catalyst on a surface thereof.

【0010】請求項6の発明は、請求項1〜5のいずれ
かに記載の触媒コンバータであって、コアは、1枚の触
媒担体を波形方向にS字状に連続的に折り返して、ハニ
カム状に重ね合わせて構成したことを特徴とする。
According to a sixth aspect of the present invention, there is provided the catalytic converter according to any one of the first to fifth aspects, wherein the core is formed by continuously folding one catalyst carrier in an S-shape in a waveform direction to form a honeycomb. It is characterized in that it is configured by overlapping in a shape.

【0011】請求項7の発明は、請求項1〜6のいずれ
かに記載の触媒コンバータであって、触媒担体は波形の
山部に、該波形の山部と谷部とを形成する斜壁の途中位
置から逆方向に切起し形成した切起し谷部を波形の折り
目方向に複数個備えている一方、波形の谷部には、前記
斜壁の途中位置から逆方向に切起し形成した切起し山部
を波形の折り目方向に複数個備えていることを特徴とす
る。
According to a seventh aspect of the present invention, there is provided the catalytic converter according to any one of the first to sixth aspects, wherein the catalyst carrier has a sloping wall that forms a ridge and a valley of the waveform on the ridge of the waveform. While a plurality of cut and raised valleys cut and raised in the reverse direction from the middle position are provided in the fold direction of the waveform, the valleys of the waveform are cut and raised in the reverse direction from the middle position of the inclined wall. It is characterized in that a plurality of cut-and-raised ridges are provided in the direction of the fold of the waveform.

【0012】請求項8の発明は、請求項7記載の触媒コ
ンバータであって、切起し谷部と切起し山部は、触媒担
体の波形の山部と谷部とを形成する斜壁の中央位置から
切起し形成してあることを特徴とする。
According to an eighth aspect of the present invention, there is provided the catalytic converter according to the seventh aspect, wherein the cut and raised valley and the cut and raised ridge form a sloped wall that forms a corrugated peak and a valley of the catalyst carrier. Characterized by being cut and raised from the center position of.

【0013】請求項9の発明は、請求項7記載の触媒コ
ンバータであって、触媒担体の波形の山部と谷部とを形
成する斜壁の中央位置には、波形の折り目方向に沿って
棚部が形成され、各隣接する山部に形成した切起し谷部
と、谷部に形成した切起し山部とを、この棚部を境とし
て切起し形成して、隣接する切起し谷部と切起し山部の
各切起し止端間に波形方向に棚部幅の間隔を設定したこ
とを特徴とする。
According to a ninth aspect of the present invention, there is provided the catalytic converter according to the seventh aspect, wherein the center of the inclined wall forming the peak and the valley of the waveform of the catalyst carrier is formed along the direction of the fold of the waveform. A shelf is formed, and a cut-and-raised valley formed in each adjacent ridge and a cut-and-raised ridge formed in a valley are cut and raised with the shelf as a boundary to form an adjacent cut. An interval of a shelf width is set in a waveform direction between the cut and raised toes of the raised valley and the cut and raised ridge.

【0014】請求項10の発明は、請求項7〜9のいず
れかに記載の触媒コンバータであって、触媒担体の波形
の山部に形成した切起し谷部と、谷部に形成した切起し
山部とを、波形の折り目方向にオフセットして形成し
て、隣接する切起し谷部と切起し山部の各切起し止端間
に、波形の折り目に所要に間隔を設定したことを特徴と
する。
According to a tenth aspect of the present invention, there is provided the catalytic converter according to any one of the seventh to ninth aspects, wherein the cut-and-raised valley formed at the peak of the waveform of the catalyst carrier and the cut formed at the valley. The raised ridges are formed offset in the direction of the fold of the waveform, and a necessary space is formed between the adjacent raised and cut valleys and the cut and raised toes of the raised and raised ridges at the crease of the waveform. It is characterized by having been set.

【0015】[0015]

【発明の効果】請求項1の発明では、重ね合わせた触媒
担体相互を溝に係合させることによって触媒担体相互の
開離を拘束しているため、コアの入口側で排気ガスの流
入圧力によってコア中央部分等から触媒担体相互が開離
する口開き現象を防止することができ、多数のセルが集
合したハニカム形状の変形をなくして、排気ガスの浄化
性能を一段と向上することができる。
According to the first aspect of the present invention, the separation of the catalyst carriers is restricted by engaging the overlapped catalyst carriers with the grooves. The opening phenomenon in which the catalyst carriers are separated from each other from the center of the core or the like can be prevented, and the honeycomb shape in which a large number of cells are gathered can be prevented from being deformed, so that the exhaust gas purification performance can be further improved.

【0016】請求項2の発明では、請求項1の発明の効
果に加え、コアの入口側において触媒担体相互が開離す
る口開き現象を確実に防止することができる。
According to the invention of claim 2, in addition to the effect of the invention of claim 1, it is possible to reliably prevent the opening phenomenon in which the catalyst carriers are separated from each other on the inlet side of the core.

【0017】請求項3の発明では、請求項1又は2の発
明の効果に加え、触媒担体とセレーションによって強固
に係合させることによって口開き現象を確実に防止する
ことができる。又、外筒の内面を単に加工するだけで溝
を形成することができ、溝の形成が極めて容易である。
According to the third aspect of the present invention, in addition to the effects of the first or second aspect of the invention, the opening phenomenon can be reliably prevented by firmly engaging the catalyst carrier with the serration. Also, the grooves can be formed by simply processing the inner surface of the outer cylinder, and the formation of the grooves is extremely easy.

【0018】請求項4の発明では、請求項1又は2の発
明の効果に加え、波板によって触媒担体を係合させ、口
開き現象を確実に防止することができる。又、波板を外
筒内に固着するだけで溝を形成することができるため、
その設定位置等の自由度が増大する。
According to the invention of claim 4, in addition to the effect of the invention of claim 1 or 2, the catalyst carrier is engaged by the corrugated plate, and the opening phenomenon can be reliably prevented. Also, since the groove can be formed only by fixing the corrugated sheet in the outer cylinder,
The degree of freedom such as the set position increases.

【0019】請求項5の発明では、請求項1〜4のいず
れかの発明の効果に加え、溝の表面も触媒活性面として
利用することができるため、コアの外周側においても触
媒活性面積を著しく増大させ、排気ガスの浄化性能をよ
り向上させることができる。
According to the fifth aspect of the present invention, in addition to the effects of any one of the first to fourth aspects, the surface of the groove can also be used as a catalytically active surface. This significantly increases the exhaust gas purification performance.

【0020】請求項6によれば、請求項1〜8の効果に
加えて、1枚の触媒担体を波形方向にS字状に連続的に
折り返して、ハニカム状に重ね合わせてコアを構成して
いるため、コアを容易に構成することができると共に、
排気ガスの流入圧力で触媒担体が後方へ飛び出すフィル
ムアウト現象を防止することができる。
According to the sixth aspect, in addition to the effects of the first to eighth aspects, a core is formed by folding one catalyst carrier continuously in an S-shape in a waveform direction and overlapping in a honeycomb shape. Therefore, the core can be easily configured,
The film-out phenomenon in which the catalyst carrier jumps backward due to the inflow pressure of the exhaust gas can be prevented.

【0021】請求項7によれば、請求項1〜6の効果に
加えて、触媒担体は波形の山部に逆方向に切起し形成し
た切起し谷部を波形の折り目方向に複数個備えていると
共に、波形の谷部には逆方向に切起し形成した切起し山
部を波形の折り目方向に複数個備えているため、重ね合
わせた触媒担体相互間に形成されたセル相互で排気ガス
の流通を行わせることができ、排気ガスを触媒担体表面
の触媒に十分に接触させて触媒反応を活発に行わせるこ
とができることと併せて、切起し谷部と切起し山部の存
在によって隣接する触媒担体相互が密着するのを防止し
てセルを確保できるため、排気ガスの浄化性能を向上す
ることができる。
According to the seventh aspect, in addition to the effects of the first to sixth aspects, in addition to the effects of the first to sixth aspects, the catalyst carrier has a plurality of cut-and-raised valleys formed by cutting and raising in the direction opposite to the peak of the waveform in the direction of the fold of the waveform. In addition, the valleys of the corrugations are provided with a plurality of ridges which are formed in the opposite direction in the valleys of the corrugations. In addition to the fact that exhaust gas can be circulated, the exhaust gas can be brought into sufficient contact with the catalyst on the surface of the catalyst carrier and the catalytic reaction can be actively carried out, Since the cells can be secured by preventing the adjacent catalyst carriers from contacting each other due to the presence of the portion, the purification performance of the exhaust gas can be improved.

【0022】また、重ね合わせた触媒担体相互間に形成
されたセル相互で排気ガスの流通を行わせることができ
るので、全体で排気ガスの圧力分布を略均一化すること
ができて、コアの耐久性を向上することもできる。
Further, since the exhaust gas can be circulated between the cells formed between the superposed catalyst carriers, the pressure distribution of the exhaust gas can be made substantially uniform as a whole, and Durability can also be improved.

【0023】更に、切起し谷部と切起し山部とを形成す
ることによって、触媒担体の剛性を高めることもでき
る。
Further, by forming the cut and raised valleys and the cut and raised ridges, the rigidity of the catalyst carrier can be increased.

【0024】請求項8によれば、請求項7の効果に加え
て、切起し谷部と切起し山部を、触媒担体の波形の山部
と谷部とを形成する斜壁の中央位置から切起し形成して
あるから、前記切起し谷部と切起し山部の切起し開口面
積を大きくすることができて、セル相互の排気ガスの流
通性を向上することができる。
According to the eighth aspect, in addition to the effect of the seventh aspect, in addition to the effect of the seventh aspect, the cut and raised valley and the cut and raised ridge are formed at the center of the inclined wall which forms the corrugated peak and the valley of the catalyst carrier. Since the cut and raised portion is formed from the position, the cut and raised opening area of the cut and raised valley portion and the cut and raised portion can be increased, and the flow of exhaust gas between cells can be improved. it can.

【0025】また、触媒担体の波形の山部と切起し山部
および波形の谷部と切起し谷部とを同一の突出量にでき
て、触媒担体相互の密着を確実に防止することができ
る。
Further, it is possible to make the crests and cuts and ridges of the catalyst carrier and the valleys and cut and raise valleys of the waveform the same amount of protrusion, so that the close contact between the catalyst carriers is reliably prevented. Can be.

【0026】請求項9によれば、請求項7の効果に加え
て、切起し谷部と切起し山部は、触媒担体の波形の山部
と谷部とを形成する斜壁の中央位置に形成した棚部を境
として切起し形成してあるから、前記切起し谷部と切起
し山部の切起し開口面積を大きくすることができて、セ
ル相互の排気ガスの流通性を向上することができる。
According to the ninth aspect, in addition to the effect of the seventh aspect, the cut and raised valley and the cut and raised ridge are formed at the center of the inclined wall forming the corrugated peak and the valley of the catalyst carrier. Since the cut-and-raised portion is formed with the ledge formed at the position as a boundary, the cut-and-raised portion and the cut-and-raised portion can be increased in the opening area, and the exhaust gas between the cells can be increased. Distribution can be improved.

【0027】また、触媒担体の波形の山部と切起し山部
および波形の谷部と切起し谷部とを同一の突出量にでき
て、触媒担体相互の密着を確実に防止することができ
る。
Further, it is possible to make the corrugated peaks and ridges of the catalyst carrier and the corrugated valleys and cut and raised valleys the same amount of protrusion, thereby reliably preventing the catalyst carriers from sticking to each other. Can be.

【0028】更に、隣接する切起し谷部と切起し山部の
各切起し止端間には、波形方向に棚部幅の間隔が確保さ
れるため、熱膨脹率の差によって前記切起し止端間が裂
断するのを回避することがてきる。
Further, a gap of the width of the ledge is secured between the cut and raised toes of the adjacent cut and raised valleys and the cut and raised ridges. It is possible to avoid tearing between the raised ends.

【0029】請求項10によれば、請求項7〜9の効果
に加えて、切起し谷部と切起し山部の各切起し止端間に
は、波形の折り目方向に所要の間隔を設定してあるた
め、熱膨脹率の差によって前記切起し止端間が裂断する
のを確実に回避することができる。
According to the tenth aspect, in addition to the effects of the seventh to ninth aspects, a required space is provided between the cut and raised toes of the cut and raised valley and the cut and raised ridge in the crease direction of the waveform. Since the interval is set, it is possible to reliably prevent the cut-and-raised toe from being torn due to the difference in the thermal expansion coefficient.

【0030】[0030]

【発明の実施の形態】以下、本発明の実施形態を図面と
共に詳述する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0031】(第1実施形態)図1,2において、1は
触媒コンバータを示し、断面楕円形に形成した金属製の
外筒2と、外筒2内に配設したハニカム状のコア3とを
備えている。
(First Embodiment) In FIGS. 1 and 2, reference numeral 1 denotes a catalytic converter, which comprises a metal outer cylinder 2 formed in an elliptical cross section, and a honeycomb core 3 disposed in the outer cylinder 2. It has.

【0032】外筒2の両端部のディフューザ4は別体成
形してあり、これらディフューザ4,4は外筒2の両端
部内に嵌合して固定してある。
The diffusers 4 at both ends of the outer cylinder 2 are formed separately, and these diffusers 4 and 4 are fitted and fixed in both ends of the outer cylinder 2.

【0033】5は前記コア3を構成する触媒担体で、表
面に触媒を担持させたステンレス等の金属薄板をもって
波形に成形してあり、この実施形態では1枚の触媒担体
5を波形方向にS字状に連続的に折り返してハニカム状
に重ね合わせ、各重ね合わせ部分にセルを形成するよう
にしているが、複数枚の触媒担体5を積層してハニカム
状のコア3を構成することもできる。
Reference numeral 5 denotes a catalyst carrier constituting the core 3, which is formed into a corrugated shape by a thin metal plate such as stainless steel having a catalyst carried on the surface thereof. Although the cells are continuously folded in a letter shape and overlapped in a honeycomb shape to form cells in each overlapped portion, a plurality of catalyst carriers 5 may be stacked to form a honeycomb-shaped core 3. .

【0034】一方、本実施形態では、外筒2の内面に筒
長方向(図2左右方向)の溝6を筒周方向へ複数本形成
し、該溝6に前記コア3の外周側で触媒担体5の折返し
部5gが重ね合わせ方向(図1左右方向)に係合し、触
媒担体5相互の開離を拘束している。
On the other hand, in the present embodiment, a plurality of grooves 6 are formed in the inner surface of the outer cylinder 2 in the cylinder length direction (left and right directions in FIG. 2) in the cylinder circumferential direction. The folded portion 5g of the carrier 5 is engaged in the overlapping direction (the left-right direction in FIG. 1), and restricts the separation of the catalyst carriers 5 from each other.

【0035】前記溝6は、外筒2の少なくともコア3の
入口側に設けられるものであるが、本第1実施形態で
は、図2のようにコア3の入口側と出口側との双方に溝
6を設けている。
The groove 6 is provided at least on the inlet side of the core 3 of the outer cylinder 2. In the first embodiment, as shown in FIG. 2, both the inlet side and the outlet side of the core 3 are provided. A groove 6 is provided.

【0036】前記溝6は、図3のように外筒2の内面に
セレーション7を設けて形成したものである。そして、
各溝6の表面には触媒が担持されている。
The groove 6 is formed by providing a serration 7 on the inner surface of the outer cylinder 2 as shown in FIG. And
A catalyst is carried on the surface of each groove 6.

【0037】尚、前記溝6はコア3の中央側(図1の左
右中央側)において特に口開きが起こりやすいことに鑑
みれば、少なくともこの中央側において前記溝6により
触媒担体5を係合させるように構成することもできる。
In view of the fact that the groove 6 is particularly likely to open at the center of the core 3 (the center on the left and right in FIG. 1), the catalyst carrier 5 is engaged with the groove 6 at least on the center. It can also be configured as follows.

【0038】前記触媒担体5としては、図4,5又は図
6〜8に示すものが用いられている。
As the catalyst carrier 5, those shown in FIGS. 4, 5 or 6 to 8 are used.

【0039】これらの図に示す触媒担体5は、何れも波
形の山部5aに、該波形の山部5aと谷部5bとを形成
する斜壁5cの途中位置から逆方向に切起し形成した切
起し谷部5dを波形の折り目方向に複数個備えている一
方、波形の谷部5bには、斜壁5cの途中位置から逆方
向に切起し形成した切起し山部5eを波形の折り目方向
に複数個備えている。
Each of the catalyst carriers 5 shown in these figures is formed by cutting and raising in the opposite direction from the midway position of the inclined wall 5c forming the crest 5a and the valley 5b of the corrugation on the crest 5a of the corrugation. While a plurality of cut-and-raised valleys 5d are provided in the direction of the fold of the waveform, the valley 5b of the waveform has a cut-and-raised ridge 5e formed by being raised and raised in the opposite direction from an intermediate position of the inclined wall 5c. A plurality is provided in the fold direction of the waveform.

【0040】ここで、図4〜6に示す触媒担体5にあっ
ては、前記波形の各斜壁5cの中央位置に該波形の折り
目方向に沿って棚部5fを形成し、各隣接する山部5a
に形成した切起し谷部5dと、谷部5bに形成した切起
し山部5eとを、この棚部5fを境として切起し形成し
て、隣接する切起し谷部5dと切起し山部5eの各切起
し止端間に波形方向に棚部5fの幅の間隔S1 を設定し
てある。
Here, in the catalyst carrier 5 shown in FIGS. 4 to 6, a ledge 5f is formed at the center position of each sloping wall 5c of the corrugation along the fold direction of the corrugation, and each adjacent peak is formed. Part 5a
The cut-and-raised valley portion 5d formed in the valley portion 5b and the cut-and-raised ridge portion 5e formed in the valley portion 5b are cut and raised with the shelf portion 5f as a boundary, and cut with the adjacent cut-and-raised valley portion 5d. between the cut-and-raised toe of raised ridges 5e is set apart S 1 of the width of the shelf portion 5f in the waveform direction.

【0041】図4,5に示す例では山部5aと、これに
隣接する切起し谷部5dとを同一の長さに形成して、波
形の折り目方向に1ピンチずれた状態に規則性をもっ
て、形成してあり、また、図6に示す例では山部5aと
谷部5bおよび切起し谷部5d,切起し山部5eとを同
一の長さに形成して、隣接する山部5aと切起し山部5
e、および隣接する谷部5bと切起し谷部5dを、波形
の折り目方向に1ピッチずれた状態に規則性をもって形
成してあるが、隣接する前記切起し谷部5dと切起し山
部5eとをこのような規則を持たずに波形の折り目方向
にオフセットして形成して、これら隣接する切起し谷部
5dと切起し山部5eの各切起し止端間に、波形の折り
目方向に所要の間隔を設定するようにしてもよい。
In the example shown in FIGS. 4 and 5, the peak 5a and the cut-and-raised valley 5d adjacent to the peak 5a are formed to have the same length, and the regularity is set such that the pinch is shifted by one pinch in the fold direction of the waveform. In the example shown in FIG. 6, the peaks 5a and the valleys 5b, the cut-and-raised valleys 5d, and the cut-and-raised ridges 5e are formed to have the same length, and the adjacent peaks are formed. 5a
e, and the adjacent valleys 5b and the raised valleys 5d are regularly formed in a state shifted by one pitch in the fold direction of the waveform. The ridges 5e are formed in such a manner as to be offset in the fold direction of the waveform without such a rule, and between the adjacent cut-and-raised valleys 5d and the cut-and-raised toes of the cut-and-raised ridges 5e. Alternatively, a required interval may be set in the fold direction of the waveform.

【0042】図7,8に示す触媒担体5は、何れも隣接
する切起し谷部5dと切起し山部5eとを、波形の折り
目方向にオフセットして形成して、これら隣接する切起
し谷部5dと切起し山部5eの各切起し止端間に、波形
の折り目方向に所要の間隔S2 を設定してある。
The catalyst carrier 5 shown in FIGS. 7 and 8 is formed such that the adjacent cut and raised valleys 5d and the cut and raised ridges 5e are offset from each other in the direction of the fold of the waveform. between each cut-and-raised toe electromotive City valley 5d and-lifted crests 5e, it is set the required interval S 2 in the fold direction of the waveform.

【0043】図7に示す例では、切起し谷部5dと切起
し山部5eとを、例の斜壁5cの中央位置がそれぞれ逆
方向に切起し形成してあるが、図8に示す例では切起し
谷部5dを波形の谷部5bよも浅く、また、切起し山部
5eを波形の山部5aよりも低く形成することによっ
て、隣接する切起し谷部5dと切起し山部5eの各切起
し止端間に前述の波形の折り目方向の間隔S2 の他に、
波形方向に所要の間隔S3 が設定されるようにしてあ
る。
In the example shown in FIG. 7, the cut and raised valley portion 5d and the cut and raised ridge portion 5e are formed by cutting and raising the center position of the inclined wall 5c in the opposite direction. In the example shown in FIG. 5, the cut and raised valley 5d is formed shallower than the corrugated valley 5b, and the cut and raised valley 5e is formed lower than the corrugated ridge 5a, so that the adjacent cut and raised valley 5d is formed. other spacing S 2 of the fold direction of the aforementioned waveform between the cut-and-lifted toe of the cut-and-raised ridges 5e,
Required interval S 3 in the waveform direction are to be set.

【0044】次に、作用を説明する。通常では、触媒コ
ンバータ1にコア3よりも小径の図外の排気管から流入
する排気ガスは、入口側のディフューザ4の拡散作用に
よってコア3の入口側の略全面のセルに流入するように
はなるが、それでも該排気管から流入する排気ガスはコ
ア3の中心部に集中しやすく、該コア3の中央部分で重
ね合わせた触媒担体5の相互が開離する傾向となる。
又、この開離によって、触媒担体5の端面が変形し、或
いは触媒担体5が外筒2に対して斜めに傾いたりする傾
向となる。
Next, the operation will be described. Normally, the exhaust gas flowing into the catalytic converter 1 from an exhaust pipe (not shown) having a diameter smaller than that of the core 3 flows into a substantially entire cell on the inlet side of the core 3 by the diffusion action of the diffuser 4 on the inlet side. Nevertheless, the exhaust gas flowing from the exhaust pipe tends to concentrate at the center of the core 3, and the catalyst carriers 5 superposed at the center of the core 3 tend to be separated from each other.
Further, due to this separation, the end face of the catalyst carrier 5 tends to be deformed, or the catalyst carrier 5 tends to be inclined with respect to the outer cylinder 2.

【0045】ところが、前述のように、コア3の外周側
で触媒担体5の折返し部5gが溝6に係合するため、触
媒担体5の相互の開離が拘束され、コア3の入口側で排
気ガスの流入圧力によってコア3の中央部分から触媒担
体5の相互が開離する口開き現象・変形を防止すること
ができ、多数のセルが集合したハニカム形状の変形をな
くして排気ガスの浄化性能を向上することができる。
However, as described above, since the folded portion 5g of the catalyst carrier 5 engages with the groove 6 on the outer peripheral side of the core 3, mutual separation of the catalyst carriers 5 is restricted, and the catalyst carrier 5 is closed at the entrance side of the core 3. It is possible to prevent the opening and closing phenomenon in which the catalyst carriers 5 are separated from each other from the central portion of the core 3 by the inflow pressure of the exhaust gas, and to eliminate the deformation of the honeycomb shape in which a large number of cells are assembled, thereby purifying the exhaust gas. Performance can be improved.

【0046】又、本実施形態では、溝6をコア3の出口
側にも設けてあるため、前記口開き現象を防止すると共
に、コア3全体でその形状維持を行なうことができ、こ
の点からも排気ガスの浄化性能を向上することができ
る。
In this embodiment, since the groove 6 is also provided on the outlet side of the core 3, the opening phenomenon can be prevented and the shape of the entire core 3 can be maintained. Also, the exhaust gas purification performance can be improved.

【0047】さらに、通常では、コア3の口開き等の変
形が起こると、コア3の外周側と外筒2の内面との間に
隙間が形成され、この隙間からガスが後方側へ短絡的に
流れて(バイパス)、触媒と接することができずに浄化
性能を低下させる傾向となる。しかし、前述のように、
コア3の口開きを防止すると共に、溝6の内面にも触媒
が担持されているため、この部分でも十分に反応させる
ことができ、触媒活性面積が著しく向上して、この点か
らも排気ガスの浄化性能を向上することができる。
Further, normally, when deformation such as opening of the core 3 occurs, a gap is formed between the outer peripheral side of the core 3 and the inner surface of the outer cylinder 2, and gas is short-circuited to the rear side from this gap. And the purification performance tends to decrease because the catalyst cannot contact the catalyst. However, as mentioned above,
Since the opening of the core 3 is prevented and the catalyst is also carried on the inner surface of the groove 6, the reaction can be sufficiently performed even in this portion, and the catalyst active area is significantly improved. Purification performance can be improved.

【0048】セレーション7は外筒2の内面に対し突出
する形態となるため、外筒2の前後にディフューザ4を
嵌合させる時に、ディフューザ4をセレーション7に突
き当て、容易に位置決めることができる。
Since the serrations 7 project from the inner surface of the outer cylinder 2, when the diffusers 4 are fitted to the front and rear of the outer cylinder 2, the diffusers 4 can be abutted against the serrations 7 and positioned easily. .

【0049】次に、本実施形態では前述の触媒担体5と
して、図4〜8に示すように波形の山部5aに逆方向に
切起し形成した切起し谷部5dを波形の折り目方向に複
数個備えていると共に、波形の谷部5bに逆方向に切起
し形成した切起し山部5eを波形の折り目方向に複数個
備えたものを用いているため、重ね合わせた触媒担体5
の相互に形成されたセル相互で図4の矢印で示すように
排気ガスの流通を行わせることができ、従って、排気ガ
スを触媒担体5の表面の触媒に十分に接触させて触媒反
応を活発に行わせることができることと併せて、切起し
谷部5dと切起し山部5eの存在によって隣接する触媒
担体5の相互が密着するのを防止してセルを確保できる
ため、排気ガスの浄化性能を更に向上することができ
る。
Next, in the present embodiment, as the above-mentioned catalyst carrier 5, a cut-and-raised valley 5d formed by cutting and raising in the opposite direction to the corrugated peak 5a as shown in FIGS. And a plurality of cut-and-raised ridges 5e formed in the corrugated valley 5b in the opposite direction in the fold direction of the corrugation. 5
As shown by arrows in FIG. 4, the exhaust gas can flow between the cells formed mutually, so that the exhaust gas is sufficiently brought into contact with the catalyst on the surface of the catalyst carrier 5 to activate the catalytic reaction. In addition to the above, the presence of the cut and raised valley portion 5d and the cut and raised ridge portion 5e can prevent the adjacent catalyst carriers 5 from contacting each other and secure cells, so that the exhaust gas Purification performance can be further improved.

【0050】また、このように重ね合わせた触媒担体5
の相互間に形成されたセル相互で排気ガスの流通を行わ
せることができるので、コア3の全体で排気ガスの圧力
分布を略均一化することができて、コア3の耐久性を向
上することができる。
Further, the catalyst carriers 5 thus superposed are overlapped.
The exhaust gas can be circulated between the cells formed between the cores 3. Therefore, the pressure distribution of the exhaust gas can be made substantially uniform over the entire core 3, and the durability of the core 3 is improved. be able to.

【0051】更に、切起し谷部5dと切起し山部5eと
を形成することによって、触媒担体5自体の剛性を高め
ることができて、品質感および信頼性を高めることもで
きる。
Further, by forming the cut and raised valleys 5d and the cut and raised ridges 5e, the rigidity of the catalyst carrier 5 itself can be increased, and the sense of quality and reliability can be improved.

【0052】ここで、図4〜6に示した触媒担体5を用
いれば、切起し谷部5dと切起し山部5eを、触媒担体
5の波形の山部5aと谷部5bとを形成する斜壁5cの
中央位置に形成した棚部5fを境にして形成してあるか
ら、前記切起し谷部5dと切起し山部5eの切起し開口
面積を大きくすることができて、セル相互の排気ガスの
流通性を向上することができる。
Here, if the catalyst carrier 5 shown in FIGS. 4 to 6 is used, the cut-and-raised valley 5d and the cut-and-raised peak 5e are connected to the corrugated peak 5a and the valley 5b of the catalyst carrier 5. Since it is formed with the ledge 5f formed at the center position of the sloped wall 5c to be formed as a boundary, the cut and raised valley 5d and the cut and raised ridge 5e can have a larger opening area. As a result, the flow of exhaust gas between the cells can be improved.

【0053】また、触媒担体5の波形の山部5aと切起
し山部5eおよび波形の谷部5bと切起し谷部5dとを
同一の突出量にできて、触媒担体5の相互密着を確実に
防止することができる。
Further, the corrugated peaks 5a and the raised ridges 5e and the corrugated valleys 5b and the raised valleys 5d of the catalyst carrier 5 can be made to have the same protrusion amount, so that the catalyst carriers 5 are in close contact with each other. Can be reliably prevented.

【0054】更には、隣接する切起し谷部5dと切起し
山部5eの各切起し止め端間には、波形方向に棚部5f
の幅の間隔S1 が確保されるため、熱膨脹率の差によっ
て前記切起し止端間が製断するのを回避することができ
る。
Further, between the cut-and-raised ends of the adjacent cut-and-valley portions 5d and the cut-and-raised ridge portions 5e, the shelves 5f are arranged in the waveform direction.
The interval S 1 of the width of is ensured, may be between the cut-and-raised toe by the difference in thermal expansion rate to avoid to manufacturing cross.

【0055】また図7に示す触媒担体5を用いれば、前
記図4〜6に示したものを用いた場合と同様の排気浄化
性能が得られることは勿論、切起し谷部5dと切起し山
部5eの各切起し止端間には、波形の折り目方向に所要
の間隔S2 を設定してあるので、この場合も熱膨脹率の
差によって前記切起し止端間が製断するのを回避するこ
とができる。
When the catalyst carrier 5 shown in FIG. 7 is used, it is possible to obtain the same exhaust purification performance as when using the catalyst carrier shown in FIGS. and between each cut-and-raised toe of the mountain portion 5e, so the fold direction of the waveform is set a required distance S 2, between the cut-and-raised toe by the difference in thermal expansion rate in this case is Seidan Can be avoided.

【0056】更に、図8に示す触媒担体5を用いれば、
前記図7に示したものを用いた場合と略同様の排気浄化
性能が得られる他、切起し谷部5dと切起し山部5eの
各切起し止端間には、波形の折り目方向に所要の間隔S
2 と、波形方向に所要の間隔S3 とを設定してあるの
で、熱膨脹率の差による間切起し止端間の製断を確実に
回避するこができる。
Further, if the catalyst carrier 5 shown in FIG. 8 is used,
In addition to obtaining substantially the same exhaust purification performance as the case of using the one shown in FIG. 7, a wavy crease is provided between the cut and raised toes of the cut and raised valley 5d and the cut and raised ridge 5e. Required spacing S in the direction
2, because is set the required interval S 3 to the waveform direction can this be reliably avoid manufacturing cross between raised toe and chopped by the difference in thermal expansion coefficient.

【0057】(第2実施形態)図9は、本発明の第2実
施形態に係り、図3に対応した要部拡大断面図である。
尚、第1実施形態と対応した構成部分には同符号を付し
て説明し、また重複した説明は省略する。
(Second Embodiment) FIG. 9 is an enlarged sectional view of a main part corresponding to FIG. 3 according to a second embodiment of the present invention.
The components corresponding to those of the first embodiment are denoted by the same reference numerals, and the description thereof will not be repeated.

【0058】本実施形態においては、溝6を外筒2内に
固着した波板8によって形成している。波板8はステン
レス等によって成形されており、外筒2の内面に対し、
その各頂部8aがロウ付けや拡散接合等によって固着さ
れている。尚、波板8の端部はディフューザ4によって
閉塞され、波板8と外筒2との間を排気ガスが短絡的に
通過することはない。他の構成は第1実施形態と略同一
である。
In this embodiment, the groove 6 is formed by the corrugated plate 8 fixed in the outer cylinder 2. The corrugated sheet 8 is formed of stainless steel or the like.
The respective tops 8a are fixed by brazing, diffusion bonding, or the like. The end of the corrugated sheet 8 is closed by the diffuser 4, and the exhaust gas does not pass between the corrugated sheet 8 and the outer cylinder 2 in a short-circuit manner. Other configurations are substantially the same as those of the first embodiment.

【0059】従って、本実施形態においても、第1実施
形態と略同様な作用効果を奏することができる。又、本
実施形態では、外筒2と別体の波板8をロウ付け等によ
って固着するようにしたため、外筒2に対する波板8の
設定箇所の調整が容易であり、また排気ガスの流れ方向
においてその設置する個数も適宜選択することができ、
自由度が増大する。
Therefore, in the present embodiment, substantially the same functions and effects as those of the first embodiment can be obtained. Further, in the present embodiment, since the corrugated sheet 8 which is separate from the outer cylinder 2 is fixed by brazing or the like, it is easy to adjust the setting position of the corrugated sheet 8 with respect to the outer cylinder 2 and the flow of the exhaust gas. The number to be installed in the direction can also be appropriately selected,
The degree of freedom increases.

【0060】尚、前記各実施形態では、溝6をセル3の
入口側と出口側に設けているが、入口側にのみ設けるこ
ともできる。又、入口から出口全体に渡って設けること
もでき、更には口開きを防止することができるものであ
れば、入口よりも後方側に配置することも可能である。
Although the grooves 6 are provided on the inlet side and the outlet side of the cell 3 in each of the above embodiments, they may be provided only on the inlet side. Further, it can be provided from the entrance to the entire exit, and if it can prevent the opening, it can also be disposed behind the entrance.

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

【図1】本発明の第1実施形態を示す図2のA−A線に
沿う概略断面図である。
FIG. 1 is a schematic cross-sectional view showing a first embodiment of the present invention, taken along line AA of FIG. 2;

【図2】第1実施形態の全体構造を示す概略断面図であ
る。
FIG. 2 is a schematic sectional view showing the entire structure of the first embodiment.

【図3】第1実施形態に係る要部拡大断面図である。FIG. 3 is an enlarged sectional view of a main part according to the first embodiment.

【図4】各実施形態に用いられる触媒担体の斜視図であ
る。
FIG. 4 is a perspective view of a catalyst carrier used in each embodiment.

【図5】図4に示した触媒担体の説明図である。FIG. 5 is an explanatory view of the catalyst carrier shown in FIG.

【図6】触媒担体の異なる例を示す説明図である。FIG. 6 is an explanatory view showing a different example of a catalyst carrier.

【図7】触媒担体の異なる例を示す説明図である。FIG. 7 is an explanatory view showing another example of a catalyst carrier.

【図8】触媒担体の異なる例を示す説明図である。FIG. 8 is an explanatory view showing a different example of a catalyst carrier.

【図9】本発明の第2実施形態に係る要部拡大断面図で
ある。
FIG. 9 is an enlarged sectional view of a main part according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 触媒コンバータ 2 外筒 3 コア 5 触媒担体 5a 波形の山部 5b 波形の谷部 5c 斜壁 5d 切起し谷部 5e 切起し山部 5f 棚部 6 溝 7 セレーション 8 波板 DESCRIPTION OF SYMBOLS 1 Catalytic converter 2 Outer cylinder 3 Core 5 Catalyst carrier 5a Wave-shaped peak 5b Wave-shaped valley 5c Sloping wall 5d Cut and raised valley 5e Cut and raised ridge 5f Shelf 6 Groove 7 Serration 8 Corrugated plate

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 波形成形した金属薄板からなる触媒担体
を重ね合わせて、重ね合わせ部分にセルを形成したハニ
カム状のコアを形成し、このコアを外筒内に配設した構
造において、 前記外筒の内面に、筒長方向の溝を筒周方向へ複数本形
成し、 該溝に、前記コアの外周側で前記触媒担体が重ね合わせ
方向に係合し、触媒担体相互の開離を拘束したことを特
徴とする触媒コンバータ。
1. A structure in which a catalyst carrier made of a corrugated metal sheet is overlapped to form a honeycomb core having cells formed in the overlapped portion, and the core is disposed in an outer cylinder. On the inner surface of the cylinder, a plurality of grooves in the cylinder length direction are formed in the cylinder circumferential direction, and the catalyst carriers are engaged with the grooves in the overlapping direction on the outer peripheral side of the core to restrict the separation of the catalyst carriers. A catalytic converter characterized by the following.
【請求項2】 請求項1記載の触媒コンバータであっ
て、 前記溝は、前記外筒の少なくともコアの入口側に設けら
れていることを特徴とする触媒コンバータ。
2. The catalytic converter according to claim 1, wherein the groove is provided at least on an inlet side of a core of the outer cylinder.
【請求項3】 請求項1又は2記載の触媒コンバータで
あって、 前記溝は、前記外筒の内面にセレーションを設けて形成
したことを特徴とする触媒コンバータ。
3. The catalytic converter according to claim 1, wherein the groove is formed by providing serrations on an inner surface of the outer cylinder.
【請求項4】 請求項1又は2記載の触媒コンバータで
あって、 前記溝は、前記外筒内に固着した波板によって形成した
ことを特徴とする触媒コンバータ。
4. The catalytic converter according to claim 1, wherein the groove is formed by a corrugated plate fixed in the outer cylinder.
【請求項5】 請求項1〜4のいずれかに記載の触媒コ
ンバータであって、 前記溝は、表面に触媒を担持させたことを特徴とする触
媒コンバータ。
5. The catalytic converter according to claim 1, wherein the groove has a surface on which a catalyst is supported.
【請求項6】 請求項1〜5のいずれかに記載の触媒コ
ンバータであって、 コアは、1枚の触媒担体を波形方向にS字状に連続的に
折り返して、ハニカム状に重ね合わせて構成したことを
特徴とする触媒コンバータ。
6. The catalytic converter according to claim 1, wherein the core is formed by continuously folding one catalyst carrier in an S-shape in a waveform direction and overlapping the honeycomb in a honeycomb shape. A catalytic converter, comprising:
【請求項7】 請求項1〜6のいずれかに記載の触媒コ
ンバータであって、 触媒担体は波形の山部に、該波形の山部と谷部とを形成
する斜壁の途中位置から逆方向に切起し形成した切起し
谷部を波形の折り目方向に複数個備えている一方、波形
の谷部には、前記斜壁の途中位置から逆方向に切起し形
成した切起し山部を波形の折り目方向に複数個備えてい
ることを特徴とする触媒コンバータ。
7. The catalytic converter according to claim 1, wherein the catalyst carrier is formed on the corrugated peak from an intermediate position of a slope wall forming the corrugated peak and valley. While a plurality of cut and raised valleys are formed in the fold direction of the waveform, the cut and raised valleys are formed by cutting and raising in the opposite direction from the middle position of the inclined wall. A catalytic converter comprising a plurality of peaks in the direction of a fold of a waveform.
【請求項8】 請求項7記載の触媒コンバータであっ
て、 切起し谷部と切起し山部は、触媒担体の波形の山部と谷
部とを形成する斜壁の中央位置から切起し形成してある
ことを特徴とする触媒コンバータ。
8. The catalytic converter according to claim 7, wherein the cut-and-raised valley and the cut-and-raised ridge are cut from a center position of a slope wall forming a wave-shaped peak and a valley of the catalyst carrier. A catalytic converter characterized by being raised and formed.
【請求項9】 請求項7記載の触媒コンバータであっ
て、 触媒担体の波形の山部と谷部とを形成する斜壁の中央位
置には、波形の折り目方向に沿って棚部が形成され、各
隣接する山部に形成した切起し谷部と、谷部に形成した
切起し山部とを、この棚部を境として切起し形成して、
隣接する切起し谷部と切起し山部の各切起し止端間に波
形方向に棚部幅の間隔を設定したことを特徴とする触媒
コンバータ。
9. The catalytic converter according to claim 7, wherein a shelf is formed along a fold direction of the waveform at a center position of the inclined wall forming a peak and a valley of the waveform of the catalyst carrier. The cut-and-raised valley formed in each adjacent peak and the cut-and-raised ridge formed in the valley are cut and raised with this shelf as a boundary,
A catalytic converter characterized in that an interval of a shelf width is set in a waveform direction between adjacent cut and raised toes of a cut and raised valley and a cut and raised ridge.
【請求項10】 請求項7〜9のいずれかに記載の触媒
コンバータであって、 触媒担体の波形の山部に形成した切起し谷部と、谷部に
形成した切起し山部とを、波形の折り目方向にオフセッ
トして形成して、隣接する切起し谷部と切起し山部の各
切起し止端間に、波形の折り目に所要に間隔を設定した
ことを特徴とする記載の触媒コンバータ。
10. The catalytic converter according to claim 7, wherein a cut-and-raised valley formed at a peak of a waveform of the catalyst carrier, and a cut-and-raised peak formed at the valley. Are formed offset in the direction of the fold of the waveform, and a necessary interval is set between the cut and raised toes of the adjacent cut and raised valleys and the cut and raised ridges. And a catalytic converter.
JP9168870A 1997-06-25 1997-06-25 Catalyst converter Pending JPH1110008A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9168870A JPH1110008A (en) 1997-06-25 1997-06-25 Catalyst converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9168870A JPH1110008A (en) 1997-06-25 1997-06-25 Catalyst converter

Publications (1)

Publication Number Publication Date
JPH1110008A true JPH1110008A (en) 1999-01-19

Family

ID=15876099

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9168870A Pending JPH1110008A (en) 1997-06-25 1997-06-25 Catalyst converter

Country Status (1)

Country Link
JP (1) JPH1110008A (en)

Similar Documents

Publication Publication Date Title
US6190784B1 (en) Conical honeycomb body with longitudinal structures
JP3610720B2 (en) Metal catalyst carrier structure
JP2506909Y2 (en) Metal support matrix for exhaust gas purification catalyst
JP4570249B2 (en) Monolithic metal honeycomb body with variable number of ducts
JP3382626B2 (en) Metal sheet for metal catalyst carrier and metal catalytic converter using the same
US5567395A (en) Catalyst carrier for a catalytic converter for purifying an exhaust gas in an internal combustion engine
JPH06205984A (en) X-lap type metallic honeycomb body
JPH08158863A (en) Metal honeycomb body
JPH1110008A (en) Catalyst converter
JPH1162571A (en) Catalytic converter
JPH1113464A (en) Catalyst converter
JPH1113465A (en) Catalyst converter
JPH1113466A (en) Catalyst converter
JP3510590B2 (en) Wound metal carrier
JP3454018B2 (en) Structure of metal catalyst support
JPH1162568A (en) Metallic catalytic converter
KR100313037B1 (en) Catalytic Converter
JPH1113467A (en) Catalyst converter
JP3334059B2 (en) Exhaust gas purification catalyst carrier
JPH1150840A (en) Metallic catalyst converter
JPH1110007A (en) Catalyst carrier for catalytic converter
JPH10328572A (en) Catalytic converter
JPH08312339A (en) Exhaust emission control device
JP3717746B2 (en) Exhaust gas purification metal carrier and method for producing the same
JPH10331629A (en) Catalyst converter