JP3288558B2 - Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performance - Google Patents
Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performanceInfo
- Publication number
- JP3288558B2 JP3288558B2 JP23638995A JP23638995A JP3288558B2 JP 3288558 B2 JP3288558 B2 JP 3288558B2 JP 23638995 A JP23638995 A JP 23638995A JP 23638995 A JP23638995 A JP 23638995A JP 3288558 B2 JP3288558 B2 JP 3288558B2
- Authority
- JP
- Japan
- Prior art keywords
- foil
- honeycomb
- thick
- joined
- thin
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 229910052751 metal Inorganic materials 0.000 title claims description 32
- 239000002184 metal Substances 0.000 title claims description 32
- 239000003054 catalyst Substances 0.000 title claims description 24
- 238000010792 warming Methods 0.000 title claims description 3
- 238000000746 purification Methods 0.000 title description 20
- 239000011888 foil Substances 0.000 claims description 151
- 241000264877 Hippospongia communis Species 0.000 claims description 81
- 238000005304 joining Methods 0.000 claims description 14
- 238000004804 winding Methods 0.000 claims description 6
- 238000010030 laminating Methods 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 description 11
- 229910001220 stainless steel Inorganic materials 0.000 description 9
- 239000010935 stainless steel Substances 0.000 description 9
- 239000000969 carrier Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 230000002093 peripheral effect Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000001133 acceleration Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000003111 delayed effect Effects 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910001122 Mischmetal Inorganic materials 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
Landscapes
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、自動車や自家発電
機等の内燃機関の排気ガスを浄化する触媒用メタル担体
に関する。The present invention relates to a catalyst for the metal responsible body for purifying exhaust gas of an internal combustion engine such as an automobile or a private power generator
About the.
【0002】[0002]
【従来の技術】自動車の排ガス規制が強化される趨勢に
おいて、排気ガスの浄化用触媒の基体として従来のセラ
ミックハニカムに代わり、多くの利点を持つメタル担体
が使用されることが多くなった。これはメタル担体のハ
ニカムが50μm程度の薄い耐熱ステンレス鋼箔で構成
されてその熱容量が小さいため、エンジン始動後の昇温
が早く、触媒反応の開始が早くなること、また、耐熱性
が高いためエンジンのより近傍に装着し得るので、より
高い温度の排気ガスが利用でき、全体としての排気ガス
浄化率が向上することなどの利点がある理由による。通
常、このメタル担体は、図3に示す如く、波箔7と平箔
8とを重ねて巻回して形成したハニカム体を耐熱ステン
レス鋼製の外筒1に挿入して相互にろう付け或いは抵抗
溶接により接合して構成される。2. Description of the Related Art With the trend of stricter exhaust gas regulations for automobiles, metal carriers having many advantages have been increasingly used instead of conventional ceramic honeycombs as the base of exhaust gas purifying catalysts. This is because the honeycomb of the metal carrier is made of a thin heat-resistant stainless steel foil of about 50 μm and its heat capacity is small, so that the temperature rise after engine start is fast, the start of catalytic reaction is quick, and the heat resistance is high. Because it can be mounted closer to the engine, higher temperature exhaust gas can be used, and there are advantages such as improvement of the overall exhaust gas purification rate. Normally, as shown in FIG. 3, a honeycomb body formed by overlapping and winding a corrugated foil 7 and a flat foil 8 is inserted into a heat-resistant stainless steel outer cylinder 1 and brazed or resisted to each other, as shown in FIG. It is configured by welding.
【0003】また、メタル担体を構成するハニカム体の
箔厚を小さくすることにより、熱容量が小さくなる上、
径方向への熱伝導が下がってヒートスポットが生じやす
くなるため、触媒反応の開始が早くなることも知られて
いる。例えば、特開平6ー99076号公報には、この
性質を利用してメタル担体を前後2段に分割し、ガスの
入側のハニカム体の箔厚を出側のものより薄くする技術
が開示されている。[0003] Further, by reducing the foil thickness of the honeycomb body constituting the metal carrier, the heat capacity is reduced, and
It is also known that the heat transfer in the radial direction is reduced and a heat spot is easily generated, so that the start of the catalytic reaction is accelerated. For example, Japanese Unexamined Patent Publication No. Hei 6-99076 discloses a technique in which a metal carrier is divided into two stages by utilizing this property, and the thickness of the honeycomb body on the gas inlet side is made thinner than that on the outlet side. ing.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、最近の
自動車エンジンのコンピュータ制御の進歩により、エン
ジンブレーキ状態では燃料をカットするため、一時的に
排気ガスの温度が低下する。熱容量の小さいメタル担体
では、このときの触媒の温度が触媒反応温度以下にまで
下がり、次に浄化すべき排気ガスが流入したときに触媒
反応の開始が遅れる欠点がある。However, due to recent advances in computer control of automobile engines, the temperature of the exhaust gas temporarily drops because the fuel is cut off in the engine braking state. A metal carrier having a small heat capacity has a disadvantage that the temperature of the catalyst at this time drops to a temperature lower than the catalyst reaction temperature, and the start of the catalyst reaction is delayed when the next exhaust gas to be purified flows.
【0005】本発明は、このような従来のメタル担体の
問題点を解決し、温度が下がりにくく、触媒の暖気性能
および保温性能の著しい向上を図ることができるメタル
担体を提供することを目的とする。[0005] The present invention provides such problems to solve in the conventional metal carrier, the temperature is hardly lowered, metal <br/> responsible body capable of achieving a significant improvement in the warm-up performance and the insulation performance of the catalyst The purpose is to do.
【0006】[0006]
【課題を解決するための手段】本発明の要旨は次の通り
である。 (1)波箔と平箔とを重ねて巻回して形成したハニカム
体を外筒に挿入して相互に接合してなる排ガス浄化触媒
用メタル担体において、担体の中心軸から半径の55〜
85%以内の円柱部分のハニカムを20〜40μm厚の
箔で構成すると共に、それより外側の円筒部分のハニカ
ムを50〜200μm厚の箔で構成し、ハニカム体の薄
箔部は少なくともガス入側端面部において平箔と波箔を
接合したことを特徴とする暖気性能と保温性能に優れた
排ガス浄化触媒用メタル担体。 (2)薄箔のハニカムと厚箔のハニカムの少なくともガ
ス入側端面部付近において、平箔と波箔とが相互に接合
され、薄箔のハニカム部と厚箔のハニカム部間は前記接
合部以外の部分で接合されてなる(1)記載のメタル担
体。 (3)ハニカム体の薄箔部はガス入側端面部で平箔と波
箔を接合し、厚箔部ではガス出側端面部またはその近傍
で接合し、かつ薄箔部の最外周部2〜5層においてはガ
ス入側端面から厚箔部の接合部にわたって接合し、薄箔
部と厚箔部は厚箔部の接合部で接合したことを特徴とす
る(1)記載のメタル担体。The gist of the present invention is as follows. (1) In a metal carrier for an exhaust gas purifying catalyst in which a honeycomb body formed by laminating and winding a corrugated foil and a flat foil is inserted into an outer cylinder and joined to each other, a radius of 55 to 55 mm from the center axis of the carrier is obtained.
The honeycomb of cylindrical section within 85% as well as consists of foil 20~40μm thickness, it more honeycomb outer cylindrical portion constituted by a foil of 50~200μm thickness, the honeycomb body thin
The foil part should be flat foil and corrugated foil at least on the gas entry side end face.
Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performance characterized by being joined . ( 2 ) The flat foil and the corrugated foil are joined to each other at least in the vicinity of the gas inlet side end face of the thin foil honeycomb and the thick foil honeycomb, and the above-mentioned joint is formed between the thin foil honeycomb part and the thick foil honeycomb part. The metal carrier according to (1), which is joined at a portion other than the above. ( 3 ) The thin foil portion of the honeycomb body joins the flat foil and the corrugated foil at the gas entry side end surface, the thick foil portion joins at or near the gas exit side end surface, and the outermost peripheral portion 2 of the thin foil portion. The metal carrier according to (1), wherein in the first to fifth layers, the metal foil carrier is joined from the gas inlet side end face to the joining portion of the thick foil portion, and the thin foil portion and the thick foil portion are joined at the joining portion of the thick foil portion.
【0007】このように配置された、中心軸に近い部分
の薄箔ハニカムは熱容量が小さいため、エンジン始動後
の昇温が速く、触媒反応の開始が早い。一旦触媒反応が
開始すると、この部分の反応による発熱量が大きいた
め、外周部に配置された熱容量の大きな厚箔のハニカム
部分も加熱されて、反応に加わるようになって、反応に
よる発熱によってこの部分もさらに高温になる。しかる
後にエンジンブレーキ状態になったとき、中心軸に近い
部分の薄箔ハニカム部は排気ガスによって冷却されて温
度の降下が早いが、外周部の厚箔ハニカム部は熱容量が
大きいため冷却は遅い。その後エンジンは加速状態にな
ったとき、外周部のハニカム部の温度が高いため触媒反
応がいち早く開始して発熱する。この発熱により中心軸
に近い薄箔ハニカムが加熱され、もともと熱容量が小さ
いことも相まって昇温が急速に行なわれ触媒反応が比較
的早期に開始される。すなわち本発明担体では、エンジ
ン始動時は薄箔ハニカムが、エンジンブレーキ後の加速
時には厚箔ハニカムがいち早く触媒反応を開始して発熱
することにより他の部分の昇温を早め、全体としての反
応効率を高める。[0007] Since the thin-walled honeycomb arranged near the central axis has a small heat capacity, the temperature rise after the engine is started is fast, and the catalytic reaction is started quickly. Once the catalytic reaction starts, since the calorific value of the reaction in this part is large, the honeycomb part of the thick foil having a large heat capacity arranged on the outer peripheral part is also heated and starts to participate in the reaction, and the heat generated by the reaction causes this to occur. The parts also get hotter. Thereafter, when the engine is brought into the brake state, the thin-walled honeycomb portion near the center axis is cooled by the exhaust gas, and the temperature drops quickly, but the thick-walled honeycomb portion on the outer peripheral portion has a large heat capacity, so that cooling is slow. Thereafter, when the engine is in an accelerated state, the temperature of the honeycomb portion on the outer peripheral portion is high, so that the catalytic reaction starts quickly and generates heat. Due to this heat generation, the thin foil honeycomb near the central axis is heated, and due to the originally small heat capacity, the temperature rises rapidly and the catalytic reaction starts relatively early. That is, in the carrier of the present invention, when the engine is started, the thin-walled honeycomb rapidly starts the catalytic reaction during the acceleration after engine braking and generates heat, thereby accelerating the temperature rise in other parts, thereby increasing the overall reaction efficiency. Enhance.
【0008】本発明において薄箔ハニカムの半径を全ハ
ニカムの半径の55〜85%とした理由は、55%未満
ではエンジン始動後の触媒反応の立ち上りが遅く、また
85%超ではエンジンブレーキ後の加速時の触媒反応の
立ち上りが遅くなるからである。また、薄箔の厚さを2
0〜40μmに限定した理由は20μm未満ではハニカ
ムの機械的な強度が充分に得られず破壊し易く、40μ
m超ではエンジン始動後の触媒反応の立上りがやや遅く
なるからである。さらに厚箔の厚さを50〜200μm
と限定した理由は、50μm未満では保温力が充分でな
く、エンジンブレーキによっての冷却がやや早く、次の
加速時の触媒反応の立ち上りが遅くなり、200μm超
では熱容量が大き過ぎて昇温が遅くなるうえこの部分の
排気抵抗が上がってガスの流入率が悪くなるからであ
る。In the present invention, the reason why the radius of the thin foil honeycomb is set to 55 to 85% of the radius of the entire honeycomb is that if the radius is less than 55%, the catalytic reaction after the start of the engine is started slowly. This is because the rise of the catalytic reaction during acceleration is delayed. In addition, the thickness of the thin foil is 2
The reason for limiting the thickness to 0 to 40 μm is that if the thickness is less than 20 μm, the mechanical strength of the honeycomb cannot be sufficiently obtained and the honeycomb is easily broken.
If it exceeds m, the rise of the catalytic reaction after the start of the engine is slightly delayed. Further, the thickness of the thick foil is 50 to 200 μm
The reason for the limitation is that if the thickness is less than 50 μm, the heat retention is not sufficient, the cooling by the engine brake is slightly faster, the rise of the catalytic reaction at the next acceleration is slow, and if it exceeds 200 μm, the heat capacity is too large and the temperature rise is slow. In addition, the exhaust resistance of this portion increases, and the gas inflow rate deteriorates.
【0009】接合構造についてハニカム体の薄箔部は、
少なくともガス入側端面付近では平箔と波箔が接合され
るべきであるとした理由は、20〜40μmの厚みの場
合には、ガス入側端面付近の平箔と波箔が接合されてい
ないと流入する排気ガスによって箔材が振動して箔がち
ぎれ飛ぶからである。一方、箔厚が50〜200μmの
厚みの場合には、箔の剛性が高いため、ガス入側端面付
近の平箔と波箔の接合がなされていなくても、箔がちぎ
れ飛ぶことはない。また、薄箔ハニカムと厚箔ハニカム
が前記の接合部以外の部分で相互に接合されるべきであ
るとした理由は、厚箔ハニカムに比べて薄箔ハニカムの
機械的強度が低いため、排ガスの入側端面付近の両ハニ
カム内の接合部で両ハニカムが接合されていると、ハニ
カム内での温度分布の消長により熱応力〜歪が生じた場
合に薄箔ハニカムにこの応力〜歪が集中して、薄箔ハニ
カムが早期に破壊するからである。Regarding the joining structure, the thin foil portion of the honeycomb body is
The reason that the flat foil and the corrugated foil should be joined at least near the gas entry side end face is that the flat foil and the corrugated foil near the gas entry side end face are not joined in the case of a thickness of 20 to 40 μm. This is because the foil material vibrates due to the exhaust gas flowing in and the foil is torn off. On the other hand, when the foil thickness is 50 to 200 μm, since the foil has high rigidity, even if the flat foil and the corrugated foil near the gas entry side end face are not joined, the foil does not break off. In addition, the reason that the thin foil honeycomb and the thick foil honeycomb should be joined to each other at a portion other than the above-mentioned joint portion is that the mechanical strength of the thin foil honeycomb is lower than that of the thick foil honeycomb, so that the exhaust gas If both honeycombs are joined at the joints in both honeycombs near the entry side end face, if thermal stress ~ strain occurs due to the variation of the temperature distribution in the honeycomb, this stress ~ strain concentrates on the thin foil honeycomb This is because the thin foil honeycomb is destroyed early.
【0010】[0010]
【発明の実施の形態】以下、図面によって本発明の実施
態様を説明する。図1は本発明に係るメタル担体の一例
を示すもので、ステンレス鋼製の外筒1内に、ステンレ
ス箔製の平箔及び波箔を重ね合わせて巻回して構成した
ハニカム体を装入している。このハニカム体は、その外
周部付近には50〜200μm厚の平箔及び波箔で形成
した厚箔ハニカム2と、その内側に20〜40μm厚の
平箔及び波箔で形成した薄箔ハニカム3にて構成され
る。これら厚箔ハニカム2と薄箔ハニカム3の比率は、
薄箔ハニカム3の半径を全ハニカム半径の55〜85%
の範囲とする。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 shows an example of a metal carrier according to the present invention, in which a honeycomb body formed by superposing and winding a flat foil and a corrugated foil made of stainless steel in an outer cylinder 1 made of stainless steel is loaded. ing. This honeycomb body has a thick foil honeycomb 2 formed of a flat foil and a corrugated foil having a thickness of 50 to 200 μm near the outer peripheral portion thereof, and a thin foil honeycomb 3 formed of a flat foil and a corrugated foil having a thickness of 20 to 40 μm inside thereof. It is composed of The ratio between the thick foil honeycomb 2 and the thin foil honeycomb 3 is as follows:
The radius of the thin foil honeycomb 3 is 55 to 85% of the total honeycomb radius.
Range.
【0011】また、このように構成されたハニカム体の
ガス入側端面部分4,4′(図の斜線部分)は、平箔と
波箔とが相互に接合され、更に、厚箔ハニカム2と薄箔
ハニカム3間は、この平箔と波箔の接合部分以外の箇
所、例えば、ガス出側端面部分5で接合されると共に、
外筒1と厚箔ハニカム2との接合部6は、前記の平箔と
波箔とが接合されたガス入側端面部分4′と平箔と波箔
とが接合されていない部分にまたがって設けている。外
筒1と厚箔ハニカム2との接合箇所は、図示以外の任意
の箇所でも差支えない。The gas inlet side end face portions 4 and 4 '(shaded portions in the figure) of the honeycomb body having the above-mentioned structure have flat foils and corrugated foils joined to each other. The thin foil honeycombs 3 are joined at a portion other than the joining portion between the flat foil and the corrugated foil, for example, at the gas outlet side end face portion 5, and
The joint 6 between the outer cylinder 1 and the thick foil honeycomb 2 extends over the gas inlet side end face portion 4 'where the flat foil and the corrugated foil are joined, and the portion where the flat foil and the corrugated foil are not joined. Provided. The joint between the outer cylinder 1 and the thick foil honeycomb 2 may be any other than shown.
【0012】また、本発明の実施態様としては多くのバ
リエーションが可能である。例えば、図4、5に示す接
合構造では、厚箔部の平箔と波箔の接合部をガス出側〜
その近傍には位置している。本発明では極薄箔を用いる
ため、高温での熱疲労破壊が生じ易く、これを防止する
ためには図6〜図9に示す接合構造、即ち、ハニカム体
の薄箔部3はガス入側端面部で平箔と波箔を接合し、厚
箔部2ではガス出側端面部またはその近傍で接合し、か
つ薄箔部の最外周部2〜5層においてはガス入側端面か
ら厚箔部の接合部にわたって接合し、薄箔部と厚箔部は
厚箔部の接合部で接合した構造をとることが有効であ
る。特に、薄箔部で30μm程度の厚さの箔を用いた
り、厚箔部で50μm程度の厚さの箔を用いる場合は、
これらの接合構造をとることが望ましい。Further, many variations of the embodiment of the present invention are possible. For example, in the joining structure shown in FIGS.
It is located near it. In the present invention, since an ultra-thin foil is used, thermal fatigue fracture at a high temperature is apt to occur. To prevent this, the joining structure shown in FIGS. The flat foil and the corrugated foil are joined at the end face part, the thick foil part 2 is joined at or near the gas discharge end face part, and the outermost peripheral part of the thin foil part is the thick foil from the gas entry side end face in 2 to 5 layers. It is effective to form a structure in which the thin foil portion and the thick foil portion are joined at the joining portion of the thick foil portion. In particular, when using a foil having a thickness of about 30 μm in the thin foil portion or using a foil having a thickness of about 50 μm in the thick foil portion,
It is desirable to adopt these joining structures.
【0013】次に、図2にしたがって本発明のメタル担
体の製造過程を説明する。図2に示すように、巻取り軸
(図示せず)の周りに渦巻状に平箔および波箔を重ね合
わせて巻回してハニカム体を製造するが、この製作過程
は特に従来のものと変わるところはない。本発明ではこ
のハニカム体の途中で、部分的に箔の厚みを変更する必
要があるため、図示の如く、予め巻回前に先行する薄手
の平箔8aおよび波箔7aの後端に、厚さの異なる、即
ち厚手の平箔8bおよび波箔8bの先端を重ねてスポッ
ト溶接9等で固定しておき、継続して巻回すればよい。
なお、平箔、波箔同士の接続部は、特に制限するもので
はなく、任意に位置をずらしても問題はない。勿論、波
箔については事前に同一のピッチ寸法に波付け加工を施
すことが必要である。Next, the manufacturing process of the metal carrier of the present invention will be described with reference to FIG. As shown in FIG. 2, a honeycomb body is manufactured by winding a flat foil and a corrugated foil spirally around a winding shaft (not shown) to manufacture a honeycomb body. This manufacturing process is particularly different from the conventional one. There is no place. In the present invention, it is necessary to partially change the thickness of the foil in the middle of the honeycomb body. Therefore, as shown in FIG. In other words, the ends of the thick flat foil 8b and the corrugated foil 8b may be overlapped and fixed by spot welding 9 or the like, and then continuously wound.
The connection between the flat foil and the corrugated foil is not particularly limited, and there is no problem even if the position is arbitrarily shifted. Of course, the corrugated foil needs to be corrugated to the same pitch size in advance.
【0014】このようにして目標とするハニカム体半径
の中心から55〜85%以内の円柱部分のハニカムを2
0〜40μm厚の箔でつくり、その外側に位置する円筒
部分の残りのハニカムを50〜200μm厚の箔でつく
り、所望のハニカム体を製作する。また、後行の箔の仕
様は、先行の箔に無関係に選択することができるので、
必要に応じて箔厚のみならず、材質を変えたり、或いは
波箔の波高さやピッチを任意に変化させて製作すること
も可能である。In this way, the honeycomb of the cylindrical portion within 55 to 85% from the center of the target honeycomb body radius is set to 2
It is made of a foil having a thickness of 0 to 40 μm, and the remaining honeycomb of the cylindrical portion located outside the foil is made of a foil having a thickness of 50 to 200 μm to produce a desired honeycomb body. Also, the specification of the subsequent foil can be selected regardless of the preceding foil,
If necessary, not only the foil thickness but also the material can be changed, or the wave height and pitch of the corrugated foil can be arbitrarily changed.
【0015】[0015]
(実施例1)20Cr−5Al−0.3Nb−0.08
Yの組成からなる30μm厚のステンレス鋼箔製の平箔
と波箔を重ね合わせて巻回し、70mmφ×100mm長の
ハニカムを作製した。また、このハニカムの外側に20
Cr−5Al−0.05Ti−0.08REM(REM
はCe、La、ミッシュメタル)の組成からなる120
μm厚の平箔と波箔を重ね合わせて巻回し、100mmφ
×100mm長のハニカム体を作製し、103mmφ×1.
5厚×102mm長のステンレス鋼製外筒の中に装入し
た。薄箔・厚箔それぞれのハニカム体のガス入側端面か
ら20mmの長さまで平箔と波箔をろう付け接合し、薄箔
ハニカム/厚箔ハニカム/外筒相互の接合は、ガス出側
端部の30mmの長さにわたってろう付けを行った。比較
例として厚箔と同一組成の52μm厚の箔を用いて10
0mmφ×100mm長のハニカムを作製し、ステンレス鋼
製の外筒に装入して、ハニカムの入側端面から20mmは
平箔と波箔を相互に接合し、ハニカム/外筒間はガス出
側の30mmについてろう付け接合を行った。これら二つ
のメタル担体はγ−Al2 O3 のウォッシュコートを行
い、Pt、Ph、Pbの貴金属触媒を担持した。(Example 1) 20Cr-5Al-0.3Nb-0.08
A flat foil made of a Y composition and made of stainless steel foil having a thickness of 30 μm and a corrugated foil were overlapped and wound to produce a honeycomb having a length of 70 mmφ × 100 mm. In addition, 20 outside the honeycomb
Cr-5Al-0.05Ti-0.08REM (REM
Is composed of Ce, La, and misch metal).
A flat foil and a corrugated foil with a thickness of μm are stacked and wound, and
A honeycomb body having a length of 100 mm and a length of 103 mmφ × 1.
It was charged into a stainless steel outer cylinder having a thickness of 5 × 102 mm. The flat foil and the corrugated foil are brazed to a length of 20 mm from the gas entry side end face of the thin foil / thick foil honeycomb body, and the thin foil honeycomb / thick honeycomb / outer cylinder is joined at the gas exit end. Was brazed over a length of 30 mm. As a comparative example, a 10 μm thick foil having the same composition as the thick foil was used.
A honeycomb having a length of 0 mmφ × 100 mm is prepared and inserted into a stainless steel outer cylinder, and a flat foil and a corrugated foil are bonded to each other for 20 mm from the entrance end face of the honeycomb, and a gas outlet side is formed between the honeycomb and the outer cylinder. Of 30 mm was brazed. These two metal supports were subjected to wash coating of γ-Al 2 O 3 and supported Pt, Ph and Pb noble metal catalysts.
【0016】これらのメタル担体を排気量2000ccの
エンジンのエキゾーストマニホールド直下に装着し、エ
ンジン始動後回転数1500rpm 、吸気圧−58KPa に
保ったまま30秒後の排出ガスをメタル担体の入側と出
側から採取し、HCの浄化率を測定した。その結果、本
発明担体による触媒装置はすでに63%の浄化率を示し
たが、比較例のものは41%の浄化率にしか達していな
かった。These metal carriers are mounted directly below the exhaust manifold of an engine with a displacement of 2000 cc. After the engine is started, the exhaust gas is discharged from the inlet side of the metal carriers after 30 seconds while maintaining the rotation speed at 1500 rpm and the intake pressure of -58 KPa. The sample was collected from the side, and the purification rate of HC was measured. As a result, the catalyst device using the carrier of the present invention had already shown a purification rate of 63%, while that of the comparative example had reached a purification rate of only 41%.
【0017】(実施例2)実施例1で製作した本発明担
体と比較例の担体に触媒を担持したものについて、排気
量2000ccのエンジンのエキゾーストマニホールドか
ら1mの長さの排気ガス管を介してそのガス出側に上記
触媒装置を装着した。エンジン始動後回転数2000rp
m 、吸入圧−41KPa の運転状態で10分以上放置し
て、該触媒装置のHC浄化率が90%近傍で安定したの
を確認した後、エンジンを急停止した。それと同時にエ
ンジンブレーキ状態を想定してエキゾーストマニホール
ド直下から常温の大気を毎分20リットルの割りで5秒
間流して、該触媒装置を冷却し、その後空気を止めてエ
ンジンを始動して、再度回転数2000rpm 、吸入圧−
41KPa に調整して15秒後の排気ガスをサンプリング
して、HCの浄化率を測定した。その結果、本発明担体
による触媒装置では、浄化率が82%でほぼ以前の浄化
率に復帰していたが、比較例のものの浄化率は48%と
未だ低かった。(Example 2) The carrier of the present invention produced in Example 1 and the carrier of Comparative Example in which a catalyst was carried were passed through an exhaust gas pipe having a length of 1 m from an exhaust manifold of an engine having a displacement of 2000 cc. The catalyst device was mounted on the gas outlet side. 2000rpm after engine start
The engine was abruptly stopped after it was confirmed that the HC purification rate of the catalyst device was stabilized at around 90% after being left for 10 minutes or more at an operating condition of suction pressure of -41 KPa. At the same time, assuming the engine braking condition, an atmosphere at room temperature was allowed to flow for 5 seconds at a rate of 20 liters per minute from immediately below the exhaust manifold to cool the catalyst device, then the air was stopped and the engine was started. 2000rpm, suction pressure-
The exhaust gas was adjusted to 41 KPa and sampled after 15 seconds, and the HC purification rate was measured. As a result, in the catalyst device using the carrier of the present invention, the purification rate was 82% and returned to almost the previous purification rate, but the purification rate of the comparative example was still low at 48%.
【0018】(実施例3)20Cr−5Al−0.3N
b−0.08Yの組成からなる20μm厚のステンレス
鋼箔製の平箔と波箔を重ね合わせて巻回し、54mmφ×
90mm長のハニカムを作り、これらの箔の外周の終端部
に、20Cr−5Al−0.05Ti−0.08REM
の組成からなる52μm厚の箔の平箔と波箔をそれぞれ
溶接して繋ぎ、前記ハニカムの外側に巻回を続け、7
8.5mmφ×90mm長のハニカムを作製した。この際、
ハニカム断面で図8と図9の斜線部に相当するところの
波箔の頂部にろう材のバインダーとなるPVAの液を塗
布した。これらのハニカムを内径78mmφのステンレス
薄板製の外筒に圧入し、さらに両端面からろう粉をふり
かけ、両図の斜線部のところがそれぞれ接合部になるよ
うに2種類のメタル担体を製作した。Example 3 20Cr-5Al-0.3N
A flat foil and a corrugated foil made of a stainless steel foil having a composition of b-0.08Y and having a thickness of 20 μm are superposed and wound, and 54 mmφ ×
A 90 mm long honeycomb was made and 20Cr-5Al-0.05Ti-0.08REM was added to the end of the outer periphery of these foils.
The flat foil and the corrugated foil having a thickness of 52 μm each having the composition of
A honeycomb having a size of 8.5 mmφ × 90 mm was manufactured. On this occasion,
A PVA liquid serving as a binder of a brazing material was applied to the top of the corrugated foil corresponding to the hatched portions in FIGS. 8 and 9 in the honeycomb cross section. These honeycombs were press-fitted into an outer cylinder made of a stainless steel sheet having an inner diameter of 78 mmφ, and solder powder was sprinkled from both end surfaces to produce two types of metal carriers such that the hatched portions in both figures became the joining portions.
【0019】これら2種類のメタル担体を真空熱処理炉
でろう付け処理し、実施例1と同様にウォッシュコート
をした後、貴金属触媒を担持した。さらに排気量が25
00ccのV6エンジンのフロント側に図8の構造のもの
を、リヤ側に図9のものを取り付け、実施例1と同様の
条件でエンジン始動30秒後のHCの浄化率を測定し
た。その結果フロント側とリヤ側はそれぞれ69%、7
2%の浄化率を示した。These two types of metal carriers were brazed in a vacuum heat treatment furnace, washed and coated in the same manner as in Example 1, and supported with a noble metal catalyst. In addition, the displacement is 25
8 was attached to the front side of a 00 cc V6 engine, and the one shown in FIG. 9 was attached to the rear side. The HC purification rate was measured 30 seconds after engine startup under the same conditions as in Example 1. As a result, the front and rear sides were 69% and 7% respectively.
It showed a purification rate of 2%.
【0020】比較例として同一寸法で中心から最外周ま
での箔(後者の成分)が全て40μm厚のメタル担体2
個を同様にして装着して、同様の条件でHCの浄化率を
測定した。その結果フロント側とリヤ側はそれぞれ44
%、47%の浄化率を示した。As a comparative example, a metal carrier 2 having the same dimensions and a foil from the center to the outermost periphery (the latter component) all having a thickness of 40 μm
The individual pieces were mounted in the same manner, and the purification rate of HC was measured under the same conditions. As a result, the front and rear sides are 44
%, 47%.
【0021】(実施例4)実施例3と同様にしてV6エ
ンジンに2種の本発明担体を装着し、実施例2と同様に
して触媒を一旦暖気して浄化能が90%になってからエ
ンジンを停止し、エキゾーストマニホールドから空気を
5秒間流して触媒を若干冷却し、再度エンジンを始動さ
せ15秒後のHCの浄化能を測定した。その結果本発明
例のものは、フロント側とリヤ側が76%、78%の浄
化能を示した。(Embodiment 4) Two types of carriers of the present invention were mounted on a V6 engine in the same manner as in Embodiment 3, and after the catalyst was once warmed up to 90% in purification ability in the same manner as in Embodiment 2, The engine was stopped, air was allowed to flow from the exhaust manifold for 5 seconds to slightly cool the catalyst, the engine was started again, and the HC purification ability after 15 seconds was measured. As a result, in the case of the present invention, the front side and the rear side exhibited a purifying ability of 76% and 78%.
【0022】比較例として同一寸法で中心から最外周ま
での箔(後者の成分)が全て40μm厚のメタル担体2
個をV6エンジンに装着して、同様にしてメタル担体を
一旦暖気してエンジンを停止し、冷却空気を流してから
再度エンジンを始動し15秒後のHCの浄化率を測定し
た。その結果フロント側とリヤ側はそれぞれ39%、4
3%の浄化率を示した。As a comparative example, a metal carrier 2 having the same dimensions and a foil from the center to the outermost periphery (the latter component) all having a thickness of 40 μm was used.
Each was mounted on a V6 engine. Similarly, the metal carrier was once warmed up, the engine was stopped, cooling air was flown, and then the engine was started again. After 15 seconds, the HC purification rate was measured. As a result, the front and rear sides were 39% and 4% respectively.
It showed a purification rate of 3%.
【0023】[0023]
【発明の効果】以上の実施例にも示すように、本発明は
エンジン始動後の触媒の暖気性能に優れ、かつエンジン
ブレーキ中の触媒の保温性能に優れる触媒装置を可能に
するメタル担体を提供するもので、自動車等触媒装置の
浄化効率を向上させ、環境浄化に貢献するものである。As shown in the above embodiments, the present invention provides a metal carrier which enables a catalyst device having excellent catalyst warm-up performance after engine start and excellent catalyst heat retention performance during engine braking. It improves the purification efficiency of catalytic devices such as automobiles and contributes to environmental purification.
【図1】本発明担体の構造の一例を示す断面図。FIG. 1 is a sectional view showing an example of the structure of the carrier of the present invention.
【図2】本発明に係るメタル担体に用いるハニカム体を
製造する過程を示す説明図。FIG. 2 is an explanatory view showing a process of manufacturing a honeycomb body used for a metal carrier according to the present invention.
【図3】メタル担体の概要を示す斜視図。FIG. 3 is a perspective view showing an outline of a metal carrier.
【図4】本発明担体の構造の他の一例を示す断面図。FIG. 4 is a sectional view showing another example of the structure of the carrier of the present invention.
【図5】本発明担体の構造の更に他の一例を示す断面
図。FIG. 5 is a sectional view showing still another example of the structure of the carrier of the present invention.
【図6】本発明担体の構造の更に他の一例を示す断面
図。FIG. 6 is a sectional view showing still another example of the structure of the carrier of the present invention.
【図7】本発明担体の構造の更に他の一例を示す断面
図。FIG. 7 is a sectional view showing still another example of the structure of the carrier of the present invention.
【図8】本発明担体の構造の更に他の一例を示す断面
図。FIG. 8 is a sectional view showing still another example of the structure of the carrier of the present invention.
【図9】本発明担体の構造の更に他の一例を示す断面
図。FIG. 9 is a sectional view showing still another example of the structure of the carrier of the present invention.
1 外筒 2 厚箔ハニカム 3 薄箔ハニカム 4,4′ ハニカム内の接合部 5 ハニカムの接合部 6 厚箔ハニカムと外筒との接合部 7a 薄手の波箔 7b 厚手の波箔 8a 薄手の平箔 8b 厚手の平箔 9 スポット溶接部 DESCRIPTION OF SYMBOLS 1 Outer cylinder 2 Thick-honeycomb 3 Thin-foil honeycomb 4,4 'Joining part in a honeycomb 5 Joining part of a honeycomb 6 Joint part between a thick-foil honeycomb and an outer cylinder 7a Thin corrugated foil 7b Thick corrugated foil 8a Thin flat foil 8b thick flat foil 9 spot welds
フロントページの続き (72)発明者 大谷 忠幸 愛知県東海市東海町5−3 新日本製鐵 株式会社 名古屋製鐵所内 (72)発明者 太田 仁史 愛知県東海市東海町5−3 新日本製鐵 株式会社 名古屋製鐵所内 (56)参考文献 特開 平5−220405(JP,A) 特開 平2−253826(JP,A)Continuation of the front page (72) Inventor Tadayuki Otani 5-3 Tokaicho, Tokai City, Aichi Prefecture Nippon Steel Corporation Nagoya Works (72) Inventor Hitoshi Ota 5-3 Tokaicho, Tokai City, Aichi Prefecture Nippon Steel Corporation Nagoya Works, Ltd. (56) References JP-A-5-220405 (JP, A) JP-A-2-253826 (JP, A)
Claims (3)
ハニカム体を外筒に挿入して相互に接合してなる排ガス
浄化触媒用メタル担体において、担体の中心軸から半径
の55〜85%以内の円柱部分のハニカムを20〜40
μm厚の箔で構成すると共に、それより外側の円筒部分
のハニカムを50〜200μm厚の箔で構成し、ハニカ
ム体の薄箔部は少なくともガス入側端面部において平箔
と波箔を接合したことを特徴とする暖気性能と保温性能
に優れた排ガス浄化触媒用メタル担体。In a metal carrier for an exhaust gas purifying catalyst, a honeycomb body formed by laminating and winding a corrugated foil and a flat foil is inserted into an outer cylinder and joined to each other, a radius of 55 mm from a center axis of the carrier is obtained. Up to 85% of cylindrical honeycombs within 20 to 40%
μm with constituted by foil thickness, it more honeycomb outer cylindrical portion constituted by a foil of 50~200μm thick, honeycomb
The thin foil part of the rubber body is a flat foil at least on the gas entry side end face.
Metal carrier for exhaust gas purifying catalyst with excellent warming performance and heat retention performance, characterized by joining with corrugated foil .
くともガス入側端面部付近において、平箔と波箔とが相
互に接合され、薄箔のハニカム部と厚箔のハニカム部間
は前記接合部以外の部分で接合されてなる請求項1記載
のメタル担体。2. A flat foil and a corrugated foil are joined to each other at least in the vicinity of an end face portion on the gas entry side of the thin foil honeycomb and the thick foil honeycomb, and the gap between the thin foil honeycomb part and the thick foil honeycomb part is the same. 2. The metal carrier according to claim 1, wherein the metal carrier is joined at a portion other than the joining portion.
平箔と波箔を接合し、厚箔部ではガス出側端面部または
その近傍で接合し、かつ薄箔部の最外周部2〜5層にお
いてはガス入側端面から厚箔部の接合部にわたって接合
し、薄箔部と厚箔部は厚箔部の接合部で接合したことを
特徴とする請求項1記載のメタル担体。3. The thin foil portion of the honeycomb body is formed by joining a flat foil and a corrugated foil at an end face on a gas inlet side, and a thick foil portion is joined at or near an end face on a gas exit side, and the outermost periphery of the thin foil portion. 2. The metal according to claim 1, wherein the second to fifth layers are joined from the gas inlet side end surface to the joining portion of the thick foil portion, and the thin foil portion and the thick foil portion are joined at the joining portion of the thick foil portion. Carrier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23638995A JP3288558B2 (en) | 1995-02-23 | 1995-09-14 | Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performance |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3480495 | 1995-02-23 | ||
JP7-34804 | 1995-02-23 | ||
JP23638995A JP3288558B2 (en) | 1995-02-23 | 1995-09-14 | Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performance |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08290064A JPH08290064A (en) | 1996-11-05 |
JP3288558B2 true JP3288558B2 (en) | 2002-06-04 |
Family
ID=26373651
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---|---|---|---|
JP23638995A Expired - Fee Related JP3288558B2 (en) | 1995-02-23 | 1995-09-14 | Metal carrier for exhaust gas purification catalyst with excellent warming performance and heat retention performance |
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JP (1) | JP3288558B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011050924A (en) * | 2009-09-04 | 2011-03-17 | Mitsubishi Motors Corp | Exhaust gas cleaning device |
JP5534208B2 (en) * | 2010-09-02 | 2014-06-25 | 三菱自動車工業株式会社 | Exhaust gas purification device for internal combustion engine |
-
1995
- 1995-09-14 JP JP23638995A patent/JP3288558B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH08290064A (en) | 1996-11-05 |
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