JPH06392A - Metallic catalyst carrier - Google Patents
Metallic catalyst carrierInfo
- Publication number
- JPH06392A JPH06392A JP4166218A JP16621892A JPH06392A JP H06392 A JPH06392 A JP H06392A JP 4166218 A JP4166218 A JP 4166218A JP 16621892 A JP16621892 A JP 16621892A JP H06392 A JPH06392 A JP H06392A
- Authority
- JP
- Japan
- Prior art keywords
- plate
- flat plate
- corrugated
- catalyst carrier
- metal 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Catalysts (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、自動車,産業用車両等
の触媒コンバータに用いられるメタル触媒担体に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a metal catalyst carrier used in a catalytic converter for automobiles, industrial vehicles and the like.
【0002】[0002]
【従来の技術】一般に、自動車の排気系には、排気ガス
を浄化するため、触媒コンバータが配置されており、こ
の触媒コンバータ内には、例えば、特開平2−2808
42号公報に開示されるようなメタル触媒担体が収容さ
れている。2. Description of the Related Art Generally, a catalytic converter is arranged in an exhaust system of an automobile in order to purify exhaust gas. In the catalytic converter, for example, Japanese Patent Laid-Open No. 2-2808 is used.
The metal catalyst carrier as disclosed in Japanese Patent Laid-Open No. 42 is accommodated.
【0003】図4は、この種のメタル触媒担体を示すも
ので、このメタル触媒担体は、図5に示すように、金属
製の波板11と平板13とを交互に重ね、円形形状に多
重に巻回した後、楕円形状に押し潰すことにより形成さ
れる。FIG. 4 shows a metal catalyst carrier of this kind. As shown in FIG. 5, this metal catalyst carrier is composed of corrugated plates 11 and flat plates 13 made of metal, which are alternately superposed on each other to form a circular shape. It is formed by crushing into an elliptical shape after being wound into.
【0004】そして、波板11と平板13との接触部
が、ろう付け,拡散接合等により相互に固定された後、
例えば、図6に示すように、筒状容器15内に収容され
て用いられる。After the contact portions between the corrugated plate 11 and the flat plate 13 are fixed to each other by brazing, diffusion bonding, etc.,
For example, as shown in FIG. 6, it is used by being housed in a cylindrical container 15.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、このよ
うなメタル触媒担体では、波板11と平板13とに繰り
返し作用する熱応力により、平板13が往々にして破損
するという問題があった。However, in such a metal catalyst carrier, there has been a problem that the flat plate 13 is often damaged by thermal stress repeatedly acting on the corrugated plate 11 and the flat plate 13.
【0006】本発明者は、かかる従来の問題を解決する
ために鋭意研究した結果、従来のメタル触媒担体では、
図7に示すように、波板11と平板13との板厚が同一
の板厚tであるため、波状に成形され比較的変形自在な
波板11に比較して平板13の剛性が大きく、波板11
に比較して平板13に多大な熱応力が作用するためであ
ることを見出した。The present inventor has conducted extensive studies in order to solve such conventional problems, and as a result, in the conventional metal catalyst carrier,
As shown in FIG. 7, since the corrugated plate 11 and the flat plate 13 have the same plate thickness t, the rigidity of the flat plate 13 is larger than that of the corrugated plate 11 which is formed in a wave shape and is relatively deformable. Corrugated sheet 11
It was found that a large thermal stress acts on the flat plate 13 as compared with the above.
【0007】すなわち、メタル触媒担体に高温の排気ガ
スが流入すると、波板11および平板13が高温にな
り、図6に矢符で示したように、外側に向けて熱応力が
発生するが、筒状容器15の温度は、波板11および平
板13の温度に比較して低いため、筒状容器15の熱膨
張は、比較的小さく、この結果、波板11と平板13と
の熱膨張が筒状容器15により阻止され、波板11と平
板13との熱応力が緩和される。That is, when hot exhaust gas flows into the metal catalyst carrier, the corrugated plate 11 and the flat plate 13 become hot, and thermal stress is generated toward the outside as shown by arrows in FIG. Since the temperature of the tubular container 15 is lower than the temperatures of the corrugated plate 11 and the flat plate 13, the thermal expansion of the tubular container 15 is relatively small, and as a result, the thermal expansion of the corrugated plate 11 and the flat plate 13 is small. It is blocked by the cylindrical container 15, and the thermal stress between the corrugated plate 11 and the flat plate 13 is relieved.
【0008】ところが、従来のメタル触媒担体では、波
状に成形されている波板11に比較して平板13の剛性
が大きいため、波板11と平板13とに発生する熱応力
が、波板11に比較して、平板13において非常に大き
くなり、この結果平板13が破損し易くなる。However, in the conventional metal catalyst carrier, the rigidity of the flat plate 13 is higher than that of the corrugated plate 11 formed in a corrugated shape, so that the thermal stress generated between the corrugated plates 11 and 13 is generated. In comparison with the above, the flat plate 13 becomes very large, and as a result, the flat plate 13 is easily damaged.
【0009】なお、特開平2−280842号公報に開
示されるメタル触媒担体では、図8に示すように、波板
11と平板13とからなるメタル触媒担体17と、筒状
容器15との間に、波板11と平板13より板厚の充分
に大きい補強波板19を配置しているが、これは、波板
11と平板13との熱膨張を筒状容器15により直接阻
止することなく、比較的弾性変形自在な補強波板19を
介して阻止し、補強波板19により波板11と平板13
との熱膨張を吸収し、波板11と平板13とに発生する
熱応力を低減しようとするものである。In the metal catalyst carrier disclosed in Japanese Unexamined Patent Publication No. 2-280842, as shown in FIG. 8, between the metal catalyst carrier 17 including the corrugated plate 11 and the flat plate 13 and the cylindrical container 15. The reinforcing corrugated plate 19 having a plate thickness sufficiently larger than that of the corrugated plate 11 and the flat plate 13 is arranged in the above, but this does not directly prevent the thermal expansion of the corrugated plate 11 and the flat plate 13 by the tubular container 15. , The corrugated plate 11 and the flat plate 13 are blocked by the reinforcing corrugated plate 19 which is relatively elastically deformable.
It is intended to absorb the thermal expansion of and to reduce the thermal stress generated in the corrugated plate 11 and the flat plate 13.
【0010】本発明は、上記のような問題を解決すべく
なされたもので、平板の破損する虞れを従来より大幅に
低減することができるメタル触媒担体を提供することを
目的とする。The present invention has been made to solve the above problems, and an object of the present invention is to provide a metal catalyst carrier capable of significantly reducing the risk of plate damage.
【0011】[0011]
【課題を解決するための手段】本発明に係わるメタル触
媒担体は、金属製の波板と平板とを交互に積層してなる
メタル触媒担体において、前記平板の板厚を、前記波板
の板厚より小さくしてなるものである。A metal catalyst carrier according to the present invention is a metal catalyst carrier in which metal corrugated plates and flat plates are alternately laminated, and the plate thickness of the flat plate is the plate thickness of the corrugated plate. It is made smaller than the thickness.
【0012】[0012]
【作用】本発明のメタル触媒担体では、平板の板厚を波
板の板厚より小さくしたので、平板の剛性が小さくな
り、平板が熱変形し易くなり、熱応力が波板に伝達され
ることで平板の応力が緩和され、波板,平板の熱変形が
筒状容器により阻止されることにより、熱応力は緩和さ
れ、破断を防止できる。In the metal catalyst carrier of the present invention, the thickness of the flat plate is made smaller than that of the corrugated plate, so that the rigidity of the flat plate is reduced, the flat plate is easily thermally deformed, and the thermal stress is transmitted to the corrugated plate. As a result, the stress of the flat plate is relieved, and the thermal deformation of the corrugated plate and the flat plate is prevented by the tubular container, whereby the thermal stress is relieved and breakage can be prevented.
【0013】[0013]
【実施例】以下、本発明の詳細を図面に示す実施例につ
いて説明する。図1は、本発明のメタル触媒担体の一実
施例を示しており、このメタル触媒担体は、金属製の波
板31と平板33とを、楕円形状に巻回し、多重に積層
して形成されている。Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 shows an embodiment of the metal catalyst carrier of the present invention. This metal catalyst carrier is formed by winding a metal corrugated plate 31 and a flat plate 33 in an elliptical shape and stacking them in multiple layers. ing.
【0014】そして、メタル触媒担体は、楕円形状の筒
状容器35内に収容されている。しかして、この実施例
では、図2に示すように、平板33の板厚 tf が、波板
31の板厚 tw より小さくされている。The metal catalyst carrier is housed in an elliptic cylindrical container 35. Therefore, in this embodiment, as shown in FIG. 2, the plate thickness t f of the flat plate 33 is smaller than the plate thickness t w of the corrugated plate 31.
【0015】なお、平板33の板厚 tf は、波板31の
板厚 tw の0.5〜0.9倍とするのが望ましい。この
実施例では、平板33の板厚 tf は、40μmとされ、
波板31の板厚 t w は、50μmとされている。The plate thickness t of the flat plate 33 isfOf the corrugated plate 31
Thickness twIt is desirable to set it to 0.5 to 0.9 times. this
In the embodiment, the plate thickness t of the flat plate 33 isfIs 40 μm,
Thickness t of corrugated sheet 31 wIs 50 μm.
【0016】また、波板31と平板33との接触部は、
ろう付け,拡散接合等により相互に固定されている。以
上のように構成されたメタル触媒担体では、平板33の
板厚 tf を、波板31の板厚 tw より小さくしたので、
平板33の剛性が小さくなり、平板33の熱変形が筒状
容器35により阻止されることにより平板33に発生す
る熱応力が小さくなり、この結果、平板33の破損する
虞れを従来より大幅に低減することができる。The contact portion between the corrugated plate 31 and the flat plate 33 is
They are fixed to each other by brazing, diffusion bonding, etc. In the metal catalyst carrier configured as described above, since the plate thickness t f of the flat plate 33 is made smaller than the plate thickness t w of the corrugated plate 31,
The rigidity of the flat plate 33 is reduced, the thermal deformation of the flat plate 33 is prevented by the tubular container 35, and the thermal stress generated in the flat plate 33 is reduced. It can be reduced.
【0017】すなわち、従来のメタル触媒担体では、波
板と平板との板厚が同一の板厚であるため、波状に成形
されている波板に比較して平板の剛性が非常に大きいた
め、波板と平板との熱膨張が筒状容器により阻止される
ことなく波板と平板とに発生する熱応力が、波板に比較
して、平板において非常に大きくなっていたが、この実
施例のメタル触媒担体では、平板33の板厚を、波板3
1の板厚より小さくしたので、平板33の剛性が小さく
なり、平板33の熱膨張が筒状容器35により阻止され
ることにより平板33に発生する熱応力が小さくなり、
平板33の破損する虞れを従来より大幅に低減すること
ができる。That is, in the conventional metal catalyst carrier, since the corrugated plate and the flat plate have the same plate thickness, the rigidity of the flat plate is very large as compared with the corrugated plate which is formed in a wavy shape. The thermal stress generated in the corrugated plate and the flat plate without the thermal expansion of the corrugated plate and the flat plate being blocked by the cylindrical container was extremely large in the flat plate as compared with the corrugated plate. In the metal catalyst carrier of, the thickness of the flat plate 33 is
Since the thickness of the flat plate 33 is smaller than that of No. 1, the rigidity of the flat plate 33 is small, and the thermal stress generated in the flat plate 33 is small because the thermal expansion of the flat plate 33 is blocked by the cylindrical container 35.
The risk of breakage of the flat plate 33 can be significantly reduced as compared with the related art.
【0018】一方、平板33が熱変形し易くなるため、
波板31の熱変形が筒状容器35により阻止されること
により波板31に発生する熱応力が大きくなるが、波板
31は、平板33に比較して弾性変形し易いため破損す
る虞れはない。On the other hand, since the flat plate 33 is easily deformed by heat,
Although the thermal deformation of the corrugated plate 31 is prevented by the tubular container 35, the thermal stress generated in the corrugated plate 31 becomes large, but the corrugated plate 31 is more likely to be elastically deformed than the flat plate 33, and thus may be damaged. There is no.
【0019】すなわち、平板33の板厚を、波板31の
板厚より小さくすることにより、波板31と平板33と
に熱応力をより均等に分散することが可能となる。図3
は、上述したメタル触媒担体の熱サイクル試験の結果を
示すもので、横軸には、平板33の板厚 tf が、縦軸に
は、負荷した熱サイクルの回数がとられている。That is, by making the plate thickness of the flat plate 33 smaller than the plate thickness of the corrugated plate 31, it becomes possible to more evenly distribute the thermal stress between the corrugated plate 31 and the flat plate 33. Figure 3
Shows the result of the thermal cycle test of the above-mentioned metal catalyst carrier. The horizontal axis shows the plate thickness t f of the flat plate 33, and the vertical axis shows the number of loaded thermal cycles.
【0020】なお、この試験では、波板31の板厚 tw
は、全て50μmであった。図から、平板33の板厚
が、波板31の板厚と同一、すなわち、平板33の板厚
が50μmで、波板31の板厚が50μmのメタル触媒
担体では、図のa点に示すように、150回の熱サイク
ルで平板33に破断が生じているが、上述した平板33
の板厚が、波板31の板厚より小さい、すなわち、平板
33の板厚が、40μmで、波板31の板厚が50μm
のメタル触媒担体では、図のb点に示すように、200
回の熱サイクルで平板33に破断が生じていることがわ
かる。In this test, the corrugated plate 31 has a plate thickness t w
Were all 50 μm. From the figure, in the case of the metal catalyst carrier in which the plate thickness of the flat plate 33 is the same as the plate thickness of the corrugated plate 31, that is, the plate thickness of the flat plate 33 is 50 μm and the plate thickness of the corrugated plate 31 is 50 μm, it is shown at point a in the figure. As described above, the flat plate 33 is fractured after 150 thermal cycles.
Of the corrugated plate 31 is smaller than that of the corrugated plate 31, that is, the plate thickness of the flat plate 33 is 40 μm and the plate thickness of the corrugated plate 31 is 50 μm.
In the case of the metal catalyst carrier of No. 2, 200
It can be seen that the flat plate 33 is fractured by the heat cycles.
【0021】すなわち、この実施例のメタル触媒担体で
は、50回の熱サイクルに対応する分だけ寿命が向上し
ている。一方、平板33の板厚が、波板31の板厚より
大きい、すなわち、平板33の板厚が150μmで、波
板31の板厚が50μmのメタル触媒担体では、図のc
点に示すように、10回程度の熱サイクルで平板33に
破断が生じており、寿命が非常に短いことがわかる。That is, in the metal catalyst carrier of this embodiment, the life is improved by the amount corresponding to 50 heat cycles. On the other hand, the plate thickness of the flat plate 33 is larger than the plate thickness of the corrugated plate 31, that is, the plate thickness of the flat plate 33 is 150 μm and the plate thickness of the corrugated plate 31 is 50 μm.
As shown by the points, the flat plate 33 is fractured after about 10 thermal cycles, and it can be seen that the life is very short.
【0022】なお、本発明において、平板33の板厚 t
f を、波板31の板厚 tw の0.5〜0.9倍とするの
が望ましいのは、0.5倍未満では、平板33の強度が
小さくなり、メタル触媒担体の形状を充分に保つことが
困難になり、一方、0.9倍を越える時には、剛性が大
きいため充分な効果を得ることができないとの理由によ
る。In the present invention, the plate thickness t of the flat plate 33 is
It is desirable to set f to be 0.5 to 0.9 times the plate thickness t w of the corrugated plate 31. If it is less than 0.5 times, the strength of the flat plate 33 will be small and the shape of the metal catalyst carrier will be sufficient. It is difficult to maintain the above value. On the other hand, when it exceeds 0.9 times, the sufficient effect cannot be obtained due to the high rigidity.
【0023】なお、以上述べた実施例では、波板31と
平板33とを巻回してなるメタル触媒担体に本発明を適
用した例について述べたが、本発明は、かかる実施例に
限定されるものではなく、例えば、所定形状に切断され
た波板と平板とを単に重ねて積層してなるメタル触媒担
体等にも同様に適用できることは勿論である。In the above-mentioned embodiment, the example in which the present invention is applied to the metal catalyst carrier formed by winding the corrugated plate 31 and the flat plate 33 is described, but the present invention is limited to such an embodiment. It is needless to say that the present invention can be similarly applied to, for example, a metal catalyst carrier or the like in which a corrugated plate cut into a predetermined shape and a flat plate are simply stacked and laminated.
【0024】[0024]
【発明の効果】以上述べたように、本発明のメタル触媒
担体では、平板の板厚を、波板の板厚より小さくしたの
で、平板の熱変形が筒状容器により阻止されることによ
り平板に発生する熱応力が小さくなり、平板の破損する
虞れを従来より大幅に低減することができるという利点
がある。As described above, in the metal catalyst carrier of the present invention, the plate thickness of the flat plate is made smaller than that of the corrugated plate, so that the flat plate is prevented from being thermally deformed by the cylindrical container. There is an advantage that the thermal stress generated in the plate is reduced and the risk of the flat plate being broken can be greatly reduced compared to the conventional case.
【図1】本発明のメタル触媒担体の一実施例を示す断面
図である。FIG. 1 is a sectional view showing an embodiment of a metal catalyst carrier of the present invention.
【図2】図1の波板と平板とを拡大して示す断面図であ
る。FIG. 2 is an enlarged sectional view showing the corrugated plate and the flat plate of FIG.
【図3】図1のメタル触媒担体の熱サイクル試験結果を
示す説明図である。FIG. 3 is an explanatory diagram showing a result of a thermal cycle test of the metal catalyst carrier of FIG.
【図4】従来のメタル触媒担体を示す斜視図である。FIG. 4 is a perspective view showing a conventional metal catalyst carrier.
【図5】波板と平板とを巻回している状態を示す斜視図
である。FIG. 5 is a perspective view showing a state in which a corrugated plate and a flat plate are wound.
【図6】図4のメタル触媒担体を筒状容器内に収容した
状態を示す説明図である。FIG. 6 is an explanatory view showing a state where the metal catalyst carrier of FIG. 4 is housed in a cylindrical container.
【図7】図4の波板と平板とを拡大して示す断面図であ
る。7 is an enlarged sectional view showing the corrugated plate and the flat plate of FIG.
【図8】従来の金属触媒コンバータを示す説明図であ
る。FIG. 8 is an explanatory view showing a conventional metal catalytic converter.
31 波板 33 平板 31 corrugated plate 33 flat plate
Claims (1)
を交互に積層してなるメタル触媒担体において、前記平
板(33)の板厚を、前記波板(31)の板厚より小さ
くしてなることを特徴とするメタル触媒担体。1. A metal catalyst carrier comprising metal corrugated plates (31) and flat plates (33) alternately laminated, wherein the plate thickness of the flat plates (33) is the same as the plate thickness of the corrugated plates (31). A metal catalyst carrier characterized by being made smaller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4166218A JPH06392A (en) | 1992-06-24 | 1992-06-24 | Metallic catalyst carrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4166218A JPH06392A (en) | 1992-06-24 | 1992-06-24 | Metallic catalyst carrier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06392A true JPH06392A (en) | 1994-01-11 |
Family
ID=15827303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4166218A Pending JPH06392A (en) | 1992-06-24 | 1992-06-24 | Metallic catalyst carrier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06392A (en) |
-
1992
- 1992-06-24 JP JP4166218A patent/JPH06392A/en active Pending
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