JPH04260443A - Catalyst carrier - Google Patents
Catalyst carrierInfo
- Publication number
- JPH04260443A JPH04260443A JP3041263A JP4126391A JPH04260443A JP H04260443 A JPH04260443 A JP H04260443A JP 3041263 A JP3041263 A JP 3041263A JP 4126391 A JP4126391 A JP 4126391A JP H04260443 A JPH04260443 A JP H04260443A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst carrier
- exhaust gas
- plate
- catalyst
- flat plate
- 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.)
- Withdrawn
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 46
- 239000002184 metal Substances 0.000 claims description 4
- 238000000746 purification Methods 0.000 abstract description 7
- 238000009826 distribution Methods 0.000 abstract description 6
- 230000002093 peripheral effect Effects 0.000 abstract description 6
- 238000004804 winding Methods 0.000 abstract description 2
- 238000010030 laminating Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/30—Honeycomb supports characterised by their structural details
- F01N2330/38—Honeycomb supports characterised by their structural details flow channels with means to enhance flow mixing,(e.g. protrusions or projections)
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は車両の排気ガス浄化触媒
等を担持する触媒担体に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a catalyst carrier for supporting an exhaust gas purifying catalyst for a vehicle.
【0002】0002
【従来の技術】図4において、エンジンEの排気管4に
は途中に排気ガス浄化装置が設けてあり、該装置は大径
としたケ−ス41内に、排気ガス浄化用の三元触媒等を
担持したハニカム状の触媒担体3を配設したものである
。触媒担体3は、板面に触媒を担持した金属製の波板と
平板を積層してなり、平板により閉鎖された波板空間内
を気流流路としてこれを流通する排気ガスを触媒により
浄化する。2. Description of the Related Art In FIG. 4, an exhaust gas purification device is provided in the middle of an exhaust pipe 4 of an engine E. This device includes a three-way catalyst for exhaust gas purification in a case 41 having a large diameter. A honeycomb-shaped catalyst carrier 3 supporting the like is disposed. The catalyst carrier 3 is made of a laminated metal corrugated plate with a catalyst supported on the plate surface and a flat plate, and the exhaust gas flowing through the corrugated plate space closed by the flat plate is purified by the catalyst as an air flow path. .
【0003】0003
【発明が解決しようとする課題】ところで、触媒担体で
の圧損を小さくするために、既述の如く触媒担体3の外
径は排気管4の径よりも大きくしてあるが、かかる担体
3における流速分布を調べると、図5に示す如く、担体
内周部での流速vは排気ガスの慣性等のために大きいが
外周部では小さく、大径としたことが圧損低下に有効に
寄与していないとともに、外周部の気流流路に設けた触
媒が有効に利用されていない。[Problems to be Solved by the Invention] By the way, in order to reduce the pressure loss in the catalyst carrier, the outer diameter of the catalyst carrier 3 is made larger than the diameter of the exhaust pipe 4 as described above. When examining the flow velocity distribution, as shown in Figure 5, the flow velocity v at the inner periphery of the carrier is large due to the inertia of the exhaust gas, but it is small at the outer periphery, indicating that the large diameter contributes effectively to reducing the pressure drop. In addition, the catalyst provided in the air flow path at the outer periphery is not effectively utilized.
【0004】本発明はかかる課題を解決するもので、触
媒担体における流速分布を均一にして圧損を低減すると
ともに、触媒の有効利用により効率的な浄化作用を発揮
する触媒担体を提供することを目的とする。[0004] The present invention is intended to solve these problems, and aims to provide a catalyst carrier that reduces pressure loss by uniformizing the flow velocity distribution in the catalyst carrier, and that exhibits an efficient purification effect by effectively utilizing the catalyst. shall be.
【0005】[0005]
【課題を解決するための手段】本発明の構成を説明する
と、板面に触媒を担持した金属製の波板1(図1)と平
板2を交互に積層して、波板1空間内を気流流路Pとす
る触媒担体3を構成して、該触媒担体3を気体流通管4
の一部に形成した大径部41内に収納するとともに、上
記波板1および平板2の板面に、気体を流通せしめる多
数の小孔11,21を形成したものである。[Means for Solving the Problems] To explain the structure of the present invention, corrugated metal plates 1 (FIG. 1) and flat plates 2 each having a catalyst supported on their plate surfaces are laminated alternately, and the space inside the corrugated plates 1 is covered. A catalyst carrier 3 is configured as an air flow path P, and the catalyst carrier 3 is connected to a gas flow pipe 4.
The corrugated plate 1 and the flat plate 2 are housed in a large diameter portion 41 formed in a part thereof, and a large number of small holes 11 and 21 are formed in the plate surfaces of the corrugated plate 1 and the flat plate 2 to allow gas to flow therethrough.
【0006】かかる構成において、大径部41内に設け
た触媒担体3では、気体流通管4の小径一般部より気体
が流入する内周部で流速は速くかつ圧力が高い。しかし
て、内周に位置する気流流路Pと外周に位置する気流流
路Pで圧力差を生じ、波板1および平板2の上記小孔1
1,12を経て気体が内周部の気流流路Pより外周部の
気流流路Pへ流出する。しかして、気体流速は触媒担体
3全体で平均化され、担体3流通時の気流圧損が低減せ
しめられるとともに、全ての触媒が等しく気体に作用し
て効率的な触媒機能が実現される。In this configuration, in the catalyst carrier 3 provided in the large diameter portion 41, the flow velocity is faster and the pressure is higher in the inner peripheral portion where gas flows than in the small diameter general portion of the gas flow pipe 4. Therefore, a pressure difference is generated between the airflow channel P located on the inner periphery and the airflow channel P located on the outer periphery, and the small holes 1 of the corrugated plate 1 and the flat plate 2
1 and 12, the gas flows out from the air flow path P in the inner circumference to the air flow path P in the outer circumference. Thus, the gas flow rate is averaged over the entire catalyst carrier 3, reducing the air flow pressure loss during the flow of the carrier 3, and all the catalysts act equally on the gas, achieving an efficient catalytic function.
【0007】[0007]
【実施例】図1において、気体流通管たるエンジン排気
管4は途中を拡径して大径の円筒ケ−ス41となし、該
ケ−ス41内に触媒担体3が配設してある。触媒担体3
は板面に触媒を担持した金属製波板1と平板2を、後述
する方法で巻回積層したもので、その外径は上記ケ−ス
41の内周壁に摺動可能に接する程度の大きさとしてあ
る。平板2で挟まれた波板1空間は気流流路Pとなって
おり、これを通過する間に排気ガスは触媒によって浄化
される。上記波板1および平板2には排気流の流通を許
す多数の小孔11,21が設けてある。[Embodiment] In FIG. 1, an engine exhaust pipe 4, which is a gas flow pipe, has its diameter enlarged in the middle to form a large diameter cylindrical case 41, and a catalyst carrier 3 is disposed inside the case 41. . Catalyst carrier 3
The metal corrugated plate 1 and the flat plate 2, each carrying a catalyst on their plate surfaces, are wound and laminated in a manner described later, and the outer diameter is large enough to slidably contact the inner circumferential wall of the case 41. It's sato. The space of the corrugated plate 1 sandwiched between the flat plates 2 forms an air flow path P, and the exhaust gas is purified by the catalyst while passing through this. The corrugated plate 1 and the flat plate 2 are provided with a large number of small holes 11 and 21 that allow exhaust flow to flow therethrough.
【0008】ケ−ス41の下流側開口にはこれを閉鎖す
るように円形のストッパ板5が設けられ、該ストッパ板
5の外周はフランジ部でケ−ス41内周に溶接等により
固定されるとともに、板面には上記小孔11,21と同
程度の径の多数の小孔51が形成してある。上記触媒担
体3は、図2に示す如く、多数の小孔11,21を形成
した波板1と平板2を、回転する芯金6に重ねて巻き取
ることにより、全体として略円形状に積層されている。A circular stopper plate 5 is provided at the downstream opening of the case 41 to close the opening, and the outer periphery of the stopper plate 5 is fixed to the inner periphery of the case 41 at a flange portion by welding or the like. In addition, a large number of small holes 51 having the same diameter as the small holes 11 and 21 are formed in the plate surface. As shown in FIG. 2, the catalyst carrier 3 is made by stacking a corrugated plate 1 and a flat plate 2, each having a large number of small holes 11 and 21, around a rotating core 6 and winding them up in a generally circular shape. has been done.
【0009】かかる構造の触媒担体3において、排気管
4よりケ−ス41内に排気ガスが流入すると、担体3の
内周部には慣性等により大きな流速で排気ガスが流入し
、圧力が上昇する。この圧力上昇により触媒担体3の内
周部と外周部の気流流路Pの間に圧力差を生じ、排気ガ
スの一部が波板1および平板2の上記小孔11,21を
経て外方の気流流路Pへ流入する(図3)。この結果、
担体3全体の排気ガス流速分布が均一化され、流通時の
圧損が低減される。また外周部を含めて担体3全体の触
媒が排気ガスの浄化に寄与するから効率的な浄化作用が
発揮される。In the catalyst carrier 3 having such a structure, when exhaust gas flows into the case 41 from the exhaust pipe 4, the exhaust gas flows into the inner periphery of the carrier 3 at a high flow velocity due to inertia, and the pressure increases. do. This pressure increase creates a pressure difference between the air flow path P on the inner circumference and the outer circumference of the catalyst carrier 3, and a part of the exhaust gas flows outward through the small holes 11 and 21 of the corrugated plate 1 and the flat plate 2. (Fig. 3). As a result,
The exhaust gas flow velocity distribution throughout the carrier 3 is made uniform, and pressure loss during circulation is reduced. Further, since the catalyst in the entire carrier 3 including the outer peripheral portion contributes to the purification of exhaust gas, an efficient purification effect is exhibited.
【0010】なお、高温の排気ガスが通過すると、外気
に触れる触媒担体3の最外周部では大きな温度勾配を生
じるが、ケ−ス41と触媒担体3の膨張率の差は、触媒
担体3がケ−ス41内で摺動伸縮可能であることにより
吸収され、応力発生により剥がれや亀裂等を生じること
はない。[0010] When high-temperature exhaust gas passes through, a large temperature gradient occurs at the outermost portion of the catalyst carrier 3 that is exposed to the outside air, but the difference in expansion rate between the case 41 and the catalyst carrier 3 is due to Since it can be slid and expanded and contracted within the case 41, it is absorbed, and no peeling or cracking occurs due to stress generation.
【0011】[0011]
【発明の効果】以上の如く本発明の触媒担体によれば、
排気ガス等の流通抵抗を小さく抑えることができるとと
もに、効率的な触媒作用が実現される。[Effects of the Invention] As described above, according to the catalyst carrier of the present invention,
The flow resistance of exhaust gas, etc. can be kept low, and efficient catalytic action can be realized.
【図1】触媒担体設置部の排気管の分解断面図である。FIG. 1 is an exploded sectional view of an exhaust pipe in a catalyst carrier installation part.
【図2】触媒担体の製造方法を示す斜視図である。FIG. 2 is a perspective view showing a method for manufacturing a catalyst carrier.
【図3】触媒担体内の流速分布を示す図である。FIG. 3 is a diagram showing the flow velocity distribution within the catalyst carrier.
【図4】エンジン排気系の部分断面平面図である。FIG. 4 is a partially sectional plan view of the engine exhaust system.
【図5】従来の触媒担体内の流速分布を示す図である。FIG. 5 is a diagram showing flow velocity distribution within a conventional catalyst carrier.
1 波板 11 小孔 2 平板 21 小孔 3 触媒担体 4 排気管(気体流通管) 41 ケ−ス(大径部) 5 ストッパ板 1 Corrugated plate 11 Small hole 2 Flat plate 21 Small hole 3 Catalyst carrier 4 Exhaust pipe (gas flow pipe) 41 Case (large diameter part) 5 Stopper plate
Claims (1)
平板を交互に積層して、波板空間内を気流流路とする触
媒担体を構成して、該触媒担体を気体流通管の一部に形
成した大径部内に収納するとともに、上記波板および平
板の板面に、気流を流通せしめる多数の小孔を形成した
ことを特徴とする触媒担体。Claim 1: A catalyst carrier is constructed by alternately stacking metal corrugated plates and flat plates each carrying a catalyst on the plate surface, and the corrugated plate space serves as an air flow path, and the catalyst carrier is connected to a gas flow pipe. A catalyst carrier characterized in that the catalyst carrier is housed in a large diameter portion formed in a part of the corrugated plate and the flat plate, and has a large number of small holes formed in the plate surfaces of the corrugated plate and the flat plate to allow airflow to flow therethrough.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3041263A JPH04260443A (en) | 1991-02-12 | 1991-02-12 | Catalyst carrier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3041263A JPH04260443A (en) | 1991-02-12 | 1991-02-12 | Catalyst carrier |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04260443A true JPH04260443A (en) | 1992-09-16 |
Family
ID=12603567
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3041263A Withdrawn JPH04260443A (en) | 1991-02-12 | 1991-02-12 | Catalyst carrier |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04260443A (en) |
-
1991
- 1991-02-12 JP JP3041263A patent/JPH04260443A/en not_active Withdrawn
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19980514 |