JP5334637B2 - Metal carrier for exhaust gas purification catalyst - Google Patents
Metal carrier for exhaust gas purification catalyst Download PDFInfo
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- JP5334637B2 JP5334637B2 JP2009065015A JP2009065015A JP5334637B2 JP 5334637 B2 JP5334637 B2 JP 5334637B2 JP 2009065015 A JP2009065015 A JP 2009065015A JP 2009065015 A JP2009065015 A JP 2009065015A JP 5334637 B2 JP5334637 B2 JP 5334637B2
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- 229910052751 metal Inorganic materials 0.000 title claims description 94
- 239000002184 metal Substances 0.000 title claims description 94
- 239000003054 catalyst Substances 0.000 title claims description 56
- 238000000746 purification Methods 0.000 title claims description 25
- 239000000463 material Substances 0.000 claims description 19
- 238000004080 punching Methods 0.000 claims description 11
- 229910001220 stainless steel Inorganic materials 0.000 description 12
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 10
- 239000010935 stainless steel Substances 0.000 description 10
- 238000005219 brazing Methods 0.000 description 9
- 238000005452 bending Methods 0.000 description 7
- 239000011888 foil Substances 0.000 description 5
- 239000010410 layer Substances 0.000 description 5
- 229910052759 nickel Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000000969 carrier Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000005304 joining Methods 0.000 description 2
- -1 20Cr-5Al Substances 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910004625 Ce—Zr Inorganic materials 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 229910000963 austenitic stainless steel Inorganic materials 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000003584 silencer Effects 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
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- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Description
本発明は、内燃機関から排出される排ガスを浄化するための触媒に使用するメタル担体及び当該担体を使用した排ガス浄化触媒に関する。 The present invention relates to a metal carrier used as a catalyst for purifying exhaust gas discharged from an internal combustion engine, and an exhaust gas purification catalyst using the carrier.
内燃機関の排ガス浄化用触媒は高温の排ガスに曝されるため、触媒担体の材質として、耐熱性のセラミックス等が使用されている。しかしながら、このようなセラミックス担体は機械的な衝撃に弱く、使用につれ圧力損失が増大するという問題がある。このような観点から、強度が高く、圧力損失が少ない触媒が要求される自動二輪車においては、耐熱性ステンレス等を材料としたメタル担体が一般的に用いられている。 Since the exhaust gas purifying catalyst of the internal combustion engine is exposed to high temperature exhaust gas, heat-resistant ceramics or the like is used as the material of the catalyst carrier. However, such a ceramic carrier is vulnerable to mechanical shock, and there is a problem that pressure loss increases with use. From such a viewpoint, a metal carrier made of heat-resistant stainless steel or the like is generally used in a motorcycle that requires a catalyst having high strength and low pressure loss.
メタルハニカム担体は、一般的に、耐熱合金を用いた平箔と波箔とを交互に巻き回して円筒形のハニカム体とし、このハニカム体を円筒形の金属製の外筒に装入した後ロウ付け等の手段によってこれらを接合することにより製造される。しかしながら、このような従来のメタルハニカム担体は、ハニカム体を構成する金属箔が薄いためエンジンから発生する失火に耐えられず、一部が溶けて外筒からハニカム体が脱落する虞がある。 Generally, a metal honeycomb carrier is formed by alternately winding flat foil and corrugated foil using a heat-resistant alloy into a cylindrical honeycomb body, and after inserting the honeycomb body into a cylindrical metal outer cylinder It is manufactured by joining them by means such as brazing. However, such a conventional metal honeycomb carrier cannot withstand the misfire generated from the engine because the metal foil constituting the honeycomb body is thin, and a part of the metal honeycomb carrier may melt and fall off from the outer cylinder.
標準的なメタルハニカム担体よりも高耐久性のものも開発されているが厳しい冷熱耐久要件を満たすことができず、通常のメタルハニカム担体と同様に脱落する場合がある。 A material having higher durability than a standard metal honeycomb carrier has been developed. However, it cannot meet strict cooling and heat durability requirements, and may fall off like a normal metal honeycomb carrier.
特開2008−190505号では、金属製のパイプ型触媒が開示されている。当該触媒は、エキゾーストパイプ(エキゾーストパイプ)又はサイレンサー内に、メタルハニカム担体の代わりに、あるいはメタルハニカム担体とともに配置することができる。 Japanese Patent Application Laid-Open No. 2008-190505 discloses a metal pipe-type catalyst. The catalyst can be arranged in an exhaust pipe (exhaust pipe) or silencer instead of the metal honeycomb carrier or together with the metal honeycomb carrier.
かかるパイプ型触媒が所定の浄化性能を達成するためにはある程度のパイプの長さが要求される。これは、ガス流速が速い場合、未反応の排ガスが排出され、その結果触媒性能が低下するためである。しかしながら、パイプをより長くすると、搭載性の点で問題がある。一方、触媒断面を広くすることで流速を下げることはできるが、排ガス処理量と触媒容量との関係で、スペースベロシティー(SV:空間速度)が増大し、その結果未反応ガスが増加する。 In order for such a pipe-type catalyst to achieve a predetermined purification performance, a certain length of pipe is required. This is because when the gas flow rate is high, unreacted exhaust gas is discharged, and as a result, the catalyst performance decreases. However, if the pipe is made longer, there is a problem in terms of mountability. On the other hand, although the flow velocity can be lowered by widening the catalyst cross section, the space velocity (SV: space velocity) increases due to the relationship between the exhaust gas treatment amount and the catalyst capacity, and as a result, the unreacted gas increases.
更に、特開平9−317452号公報で開示されているような、外筒パイプ内に小径のパイプを複数組み込んだタイプの触媒は、外筒内に小径パイプを組み付ける上で問題がある。特に、ロウ付けにより両者を接合する場合、隙間が許されないため、非常に高い寸法精度がパイプの製造に要求される。このようなパイプとして一般的な電縫管を使用することも考えられるが、外径サイズの自由度が低い電縫管は、縮径、拡管等の二次加工を必要とするため、コストアップを免れることはできない。 Further, a catalyst of a type in which a plurality of small diameter pipes are incorporated in the outer cylinder pipe as disclosed in JP-A-9-317452 has a problem in assembling the small diameter pipe in the outer cylinder. In particular, when the two are joined by brazing, a gap is not allowed, so that a very high dimensional accuracy is required for the manufacture of the pipe. Although it is conceivable to use general ERW pipes as such pipes, ERW pipes with a low degree of freedom in outer diameter size require secondary processing such as diameter reduction and pipe expansion, which increases costs. Can't escape.
本発明の目的は、従来の排ガス浄化触媒用担体と比較して、耐久性、排ガス浄化性能、搭載性の観点で優れた排ガス浄化用メタル担体及び当該担体を用いたメタル担体触媒を提供することにある。 An object of the present invention is to provide a metal carrier for exhaust gas purification that is superior in terms of durability, exhaust gas purification performance, and mountability compared to conventional exhaust gas purification catalyst carriers, and a metal carrier catalyst using the carrier. It is in.
本発明者がかかる課題について鋭意検討した結果、従来のメタルハニカム担体で使用されている金属箔よりも厚い金属板を、タービンで使用されているような羽根のように外筒内に多数配置することで、耐溶損性、排ガス浄化性能及び搭載性が大幅に向上した排ガス浄化触媒が得られることを見出し、本発明を完成するに至った。 As a result of intensive studies on the problem by the inventor, a large number of metal plates thicker than the metal foil used in the conventional metal honeycomb carrier are arranged in the outer cylinder like blades used in a turbine. As a result, it was found that an exhaust gas purification catalyst having greatly improved melting resistance, exhaust gas purification performance and mountability can be obtained, and the present invention has been completed.
即ち、本発明は、以下の発明を包含する。
[1]金属製のパイプの内側に、複数枚の金属製湾曲板及び/又は金属製平面板から成るユニットを1又は複数個配置した排ガス浄化用メタル担体であって、前記板が前記パイプの横断面の中央部から前記パイプの内壁面にかけて略等角度間隔で放射状に配置されていることを特徴とする排ガス浄化触媒用メタル担体。
[2]前記板がそれぞれ略U字型又はV字型の形状をしており、前記パイプの横断面の中央部から二手に分かれるように配置されていることを特徴とする、[1]に記載の排ガス浄化触媒用メタル担体。
[3]前記板にパンチング孔が設けられていることを特徴とする、[1]又は[2]に記載の排ガス浄化触媒用メタル担体。
[4]前記金属製パイプがエキゾーストパイプであり、複数個の前記ユニットが当該エキゾーストパイプ内に所定の間隔を空けて配置されている、[1]〜[3]のいずれかに記載の排ガス浄化触媒用メタル担体。
[5][1]〜[4]のいずれかに記載のメタル担体を基材としたことを特徴とする、排ガス浄化用メタル担体触媒。
That is, the present invention includes the following inventions.
[1] An exhaust gas purifying metal carrier in which one or a plurality of units composed of a plurality of metal curved plates and / or metal flat plates are arranged inside a metal pipe, the plate being the pipe of the pipe A metal carrier for an exhaust gas purifying catalyst, wherein the metal carrier is arranged radially at substantially equal angular intervals from a central portion of a transverse section to an inner wall surface of the pipe.
[2] The plate according to [1], wherein each of the plates has a substantially U-shape or V-shape, and is arranged so as to be divided into two hands from a central portion of a cross section of the pipe. The metal carrier for exhaust gas purification catalysts as described.
[3] The metal carrier for an exhaust gas purification catalyst according to [1] or [2], wherein the plate is provided with a punching hole.
[4] The exhaust gas purification according to any one of [1] to [3], wherein the metal pipe is an exhaust pipe, and the plurality of units are arranged in the exhaust pipe at predetermined intervals. Metal carrier for catalyst.
[5] A metal carrier catalyst for purifying exhaust gas, characterized in that the metal carrier according to any one of [1] to [4] is used as a base material.
本発明によると、従来よりも耐溶損性、排ガス浄化性能及び搭載性に優れた排ガス浄化触媒用メタル担体及び当該担体を用いた排ガス浄化触媒を提供することが可能となる。具体的には、本発明のメタル担体は、薄い金属箔を使用する従来のメタルハニカム担体と異なり、厚い金属板を使用することができるため、耐久性が大幅に向上する。そして、従来のパイプ型触媒と比較して排ガス流との接触面積が多いため、高性能化も実現される。 ADVANTAGE OF THE INVENTION According to this invention, it becomes possible to provide the exhaust gas purification catalyst using the metal support | carrier for exhaust gas purification catalysts and the said carrier which were excellent in melt | dissolution resistance, exhaust gas purification performance, and mountability conventionally. Specifically, unlike the conventional metal honeycomb carrier using a thin metal foil, the metal carrier of the present invention can use a thick metal plate, so that the durability is greatly improved. And since the contact area with an exhaust gas flow is large compared with the conventional pipe type catalyst, high performance is also realized.
複数個のチューブを外筒内に配置した従来のチューブ型触媒は、径方向に自由度が無く、組み付けの際に困難を伴い、また、強度も十分でない。一方、本発明のメタル担体のように湾曲板から構成されるユニットは、パイプ内に挿入する際廻しながら挿入されるためパイプ内に組み付けるのも容易なだけでなく、金属板がその弾性により元の形状に戻ろうとするため(スプリングバック)、十分な剛性も確保できるというメリットがある。更に、スプリングバック現象を活用することができる本発明のメタル担体は、湾曲板の曲率を変えることで外筒径の異なる様々なパイプに対応することができるというメリットもある。 A conventional tube-type catalyst in which a plurality of tubes are arranged in an outer cylinder has no degree of freedom in the radial direction, is difficult to assemble, and has insufficient strength. On the other hand, a unit composed of a curved plate like the metal carrier of the present invention is not only easy to assemble in the pipe because it is inserted while being inserted into the pipe, but the metal plate is also elastic due to its elasticity. There is a merit that sufficient rigidity can be secured because it tries to return to the shape (spring back). Furthermore, the metal carrier of the present invention that can utilize the springback phenomenon has an advantage that it can be applied to various pipes having different outer cylinder diameters by changing the curvature of the curved plate.
本発明は、金属製のパイプの内側に、複数枚の金属製湾曲板及び/又は金属製平面板から成るユニットを1又は複数個配置した排ガス浄化用メタル担体であって、前記板が前記パイプの横断面の中央部から前記パイプの内壁面にかけて略等角度間隔で放射状に配置されていることを特徴とする排ガス浄化触媒用メタル担体、を提供する。 The present invention is an exhaust gas purifying metal carrier in which one or a plurality of units comprising a plurality of metal curved plates and / or metal flat plates are arranged inside a metal pipe, wherein the plate is the pipe. An exhaust gas purifying catalyst metal carrier, characterized in that it is arranged radially at substantially equal angular intervals from the center of the cross section to the inner wall surface of the pipe.
本発明のメタル担体を構成するパイプとして、メタルハニカム担体で通常使用されている金属製の外筒、例えばSUS436等のステンレス製の円柱状の外筒等を使用することができる。その他、エキゾーストパイプ又はマフラーを前記パイプとして使用してもよい。 As the pipe constituting the metal carrier of the present invention, a metal outer cylinder usually used in a metal honeycomb carrier, for example, a stainless steel cylindrical outer cylinder such as SUS436 can be used. In addition, an exhaust pipe or a muffler may be used as the pipe.
パイプ内に挿入される前記ユニットは、複数枚の金属製湾曲板及び/又は金属製平面板を略等角度間隔で前記パイプの横断面の中央部から前記パイプの内壁面にかけて放射状に配置して成る。例えば、パイプの中央部から12枚の金属板が放射状に等間隔で配置される場合、各金属板の角度間隔は約30度毎となる。金属板の枚数及び配置される角度間隔は、製造コスト、所望とする強度、排ガス浄化性能等の観点から適宜調節される。これは、板材が多いと、板材を中央部で集合・接合する際の位置を決めるのが煩雑であり、また、中央部のガス流通部面積が狭くなるためである。従って、板材枚数は、限定しないが、3〜20枚が好ましい。 The unit inserted into the pipe is formed by arranging a plurality of metal curved plates and / or metal plane plates radially at substantially equal angular intervals from the center of the cross section of the pipe to the inner wall surface of the pipe. Become. For example, when twelve metal plates are radially arranged from the center of the pipe at equal intervals, the angular interval of each metal plate is about every 30 degrees. The number of metal plates and the angular interval at which they are arranged are appropriately adjusted from the viewpoints of manufacturing cost, desired strength, exhaust gas purification performance, and the like. This is because if there are many plate materials, it is complicated to determine the position when the plate materials are gathered and joined at the central portion, and the area of the gas circulation portion at the central portion becomes narrow. Accordingly, the number of plate members is not limited, but 3 to 20 sheets are preferable.
使用する金属板の材質は、限定しないが、一般的なメタルハニカム担体で使用されている金属、例えば熱容量が低く、且つ耐熱性、耐圧性等に優れているステンレス鋼、耐熱鋼が好ましい。更に、熱膨張率が低いほど、歪み難いため、本発明で使用する金属板として好ましい。かかるステンレス鋼の例としては、フェライト系ステンレス、オーステナイト系ステンレス等の鋼材がある。これらのステンレスの中でも、フェライト系(例えばSUS430系、436系等)が好ましい。 The material of the metal plate to be used is not limited, but a metal used in a general metal honeycomb carrier, for example, stainless steel or heat resistant steel having a low heat capacity and excellent heat resistance and pressure resistance is preferable. Furthermore, since the lower the coefficient of thermal expansion, the less likely it is to distort, it is preferable as the metal plate used in the present invention. Examples of such stainless steel include steel materials such as ferritic stainless steel and austenitic stainless steel. Among these stainless steels, ferrite type (for example, SUS430 type, 436 type etc.) is preferable.
上記ステンレスの他、抗酸化性の高い材料、例えば20Cr−5Alのような鋼材や、SUS340のようなステンレスでもよい。 In addition to the above stainless steel, a material having high antioxidant property, for example, a steel material such as 20Cr-5Al, or a stainless steel such as SUS340 may be used.
前記ユニットは、図2(a)〜(c)に示すように、所定の大きさの金属製切板を折り曲げ、これらの切板を多数組み合わて末端で接合することにより構成することができる。折り曲げの回数は特に限定されない。図2(d)のように、湾曲板を使用してユニットを構成してもよい。湾曲板の曲率は、パイプ内に配置した後のスプリングバックを考慮して適宜決定することができる。尚、曲率が大きいほど、パイプの横断面の中央部からその内壁面に到達するまでの長さが必要となるものの、それに伴い表面積が増大するため、結果として触媒性能が向上する。一方、曲率を小さくすると、パイプ内の排ガス流れの自由度が増大し、エンジン性能(背圧)が向上する。これらの切板は、前記パイプの横断面の中央部から前記パイプの内壁面にかけて略等角度間隔で放射状に配置される。図3のように、切板の一部に切り込みを入れ、これらを折り重ねることで図1に記載のようなユニットを作ることもできる。切板の代わりに一枚の円板を出発材料とすることもできる(図4)。この場合、円板の中央部から一定の角度毎に分離しないように切り込みを入れ、これらを一片ずつねじり、あるいは曲げることで所望の形状のユニットを作ることができる。 As shown in FIGS. 2A to 2C, the unit can be configured by bending a metal cut plate having a predetermined size and joining a number of these cut plates together at the end. The number of times of bending is not particularly limited. As shown in FIG. 2D, the unit may be configured using a curved plate. The curvature of the curved plate can be determined as appropriate in consideration of the springback after being placed in the pipe. In addition, although the length until it reaches the inner wall surface from the center part of the cross section of a pipe is needed, the surface area increases in connection with it, so that a catalyst performance improves as a curvature is large. On the other hand, when the curvature is reduced, the degree of freedom of the exhaust gas flow in the pipe is increased, and the engine performance (back pressure) is improved. These cut plates are arranged radially at substantially equal angular intervals from the center of the cross section of the pipe to the inner wall surface of the pipe. As shown in FIG. 3, it is possible to make a unit as shown in FIG. 1 by cutting a part of the cut plate and folding them. Instead of a cut plate, a single disc can be used as a starting material (FIG. 4). In this case, it is possible to make a unit having a desired shape by making cuts so as not to be separated from the central portion of the disk at certain angles and twisting or bending them one by one.
別の態様において、一枚の切板を折り曲げて略U字型又はV字型に成型し、これを前記パイプの横断面の中央部から二手に分かれるようにパイプ内に複数個配置してもよい(図5)。 In another aspect, one cut plate may be bent and formed into a substantially U shape or V shape, and a plurality of the cut plates may be arranged in the pipe so as to be separated from the center of the cross section of the pipe. Good (FIG. 5).
図2(c)、(d)及び図3(c)、(d)に記載のメタル担体は、作りやすさの点で優れている。しかし、使用する切板の枚数が多くなると、担体の中心部付近に各羽根の交点が集中し、その結果当該中心部付近で排ガスが流れる余地が少なくなる虞がある。また、この中心部をロウ材で固定すると、中心部付近での排ガス流れは更に阻害される。そのため、中心部付近の排ガス流れの悪化を防ぐ観点からは、図4(b)、(c)に記載のメタル担体を採用することも好ましい。一方、図4(b)、(c)に記載のメタル担体は、各板を固定する点が少ない。従って、耐久性などを考慮すると、パイプ内に固定するための点が多い図5(c)、(d)に記載のメタル担体を採用することも好ましい。更に、後述するとおり、上記担体にパンチング孔を設けて排ガス浄化性能を向上させることも好ましい。 The metal carriers described in FIGS. 2 (c) and 2 (d) and FIGS. 3 (c) and 3 (d) are excellent in terms of ease of production. However, when the number of cutting plates to be used increases, the intersections of the blades concentrate near the center of the carrier, and as a result, there is a possibility that the room for exhaust gas to flow near the center is reduced. Moreover, if this center part is fixed with a brazing material, the exhaust gas flow in the vicinity of the center part is further hindered. Therefore, it is also preferable to employ the metal carrier described in FIGS. 4B and 4C from the viewpoint of preventing deterioration of the exhaust gas flow near the center. On the other hand, the metal carrier described in FIGS. 4B and 4C has few points for fixing each plate. Therefore, in consideration of durability and the like, it is also preferable to employ the metal carrier described in FIGS. 5C and 5D, which has many points for fixing in the pipe. Furthermore, as described later, it is also preferable to provide punching holes in the carrier to improve the exhaust gas purification performance.
パイプ内に複数個のユニットを所定の間隔置きに多段に配置してもよい(図6)。このように複数個のユニットが多段に配置されると、ユニット間に生じる空間が排ガス流に乱れを生じさせ、排ガスとユニット表面に担持される触媒成分との接触が増大し、その結果排ガス浄化性能が向上するため好ましい。更に、円弧状に曲がっているパイプを使用する場合にも、奥行きの短いユニットを複数パイプ内に配置することもある(図7)。 A plurality of units may be arranged in multiple stages at predetermined intervals in the pipe (FIG. 6). When a plurality of units are arranged in multiple stages in this way, the space created between the units causes disturbance in the exhaust gas flow, increasing the contact between the exhaust gas and the catalyst component supported on the unit surface, and as a result, exhaust gas purification. This is preferable because the performance is improved. Furthermore, when using a pipe bent in an arc shape, a unit having a short depth may be arranged in a plurality of pipes (FIG. 7).
同一の形状のユニットを複数パイプ内に配置し、あるいは各ユニット内の金属板の曲げ方向を変えることで、ユニット毎に金属板の配置の位相をずらすこともできる(図8)。位相をずらすことで、排ガスの吹き抜けを防ぐことができ、その結果排ガス浄化性能が向上する。 By arranging units of the same shape in a plurality of pipes or changing the bending direction of the metal plate in each unit, the phase of the arrangement of the metal plate can be shifted for each unit (FIG. 8). By shifting the phase, the exhaust gas can be prevented from being blown out, and as a result, the exhaust gas purification performance is improved.
熱容量を低下させて触媒を早期に活性化させるために、前記ユニットを構成する金属板にパンチング孔を設けることが好ましい。このようなパンチング穴は、触媒内に流入する排ガスの拡散性を向上させ、それにより排ガス成分と触媒活性成分との接触性も増大させることができる。当該パンチング穴の個々のサイズは特に限定されない。尚、金属板の厚さよりも小さい直径のパンチ穴は通常量産に適していない。図9にパンチング孔が設けられたメタル担体触媒の一例を示す。当該パンチング孔は千鳥抜きされたものでもよい。 In order to reduce the heat capacity and activate the catalyst early, it is preferable to provide punching holes in the metal plate constituting the unit. Such punching holes can improve the diffusibility of the exhaust gas flowing into the catalyst, thereby increasing the contact between the exhaust gas component and the catalytically active component. The individual size of the punching hole is not particularly limited. Note that punch holes having a diameter smaller than the thickness of the metal plate are usually not suitable for mass production. FIG. 9 shows an example of a metal-supported catalyst provided with punching holes. The punching holes may be staggered.
前記ユニットは回転させながらパイプ内に挿入され、組付けられる。当該組み付け後、ロウ材、例えばニッケルロウが塗布される。あるいは、当該ユニットの周囲にニッケルロウ材を塗布した後パイプ内に挿入してもよい。パイプ内に組み付けられた前記ユニットを高温で処理してパイプの内壁とユニットとを互いに接合させることにより、本発明のメタル担体を調製することができる。 The unit is inserted into the pipe while being rotated and assembled. After the assembly, a brazing material such as nickel brazing is applied. Alternatively, a nickel brazing material may be applied around the unit and then inserted into the pipe. The metal carrier of the present invention can be prepared by treating the unit assembled in the pipe at a high temperature to join the inner wall of the pipe and the unit to each other.
排ガス浄化用メタル担体触媒
本発明のメタル担体触媒は、上述のメタル担体を用いて作製される。本発明はメタル担体自体に特徴を有するものであるため、メタル担体上に形成される触媒コート層には任意の成分が含まれうる。本発明のメタル担体触媒における触媒コート層は、従来使用されている方法、例えば含浸法、ウォッシュコート法などにより、メタル担体に触媒貴金属を担持させることでセル通路内に形成することができる。用途によっては、当該触媒コート層は、その他の触媒金属、あるいはアルカリ金属又はアルカリ土類金属などのNOx吸蔵材を含んでもよい。尚、当該触媒コート層は単層に限定されず、複数の層で構成することもできる。また、その厚さは特に限定されない。
Exhaust gas purification metal carrier catalyst The metal carrier catalyst of the present invention is produced using the above-mentioned metal carrier. Since the present invention is characterized by the metal carrier itself, the catalyst coat layer formed on the metal carrier may contain arbitrary components. The catalyst coat layer in the metal carrier catalyst of the present invention can be formed in the cell passage by supporting a catalyst noble metal on the metal carrier by a conventionally used method such as an impregnation method or a wash coat method. Depending on the application, the catalyst coat layer may include other catalyst metals or NOx occlusion materials such as alkali metals or alkaline earth metals. The catalyst coat layer is not limited to a single layer, and may be composed of a plurality of layers. Moreover, the thickness is not specifically limited.
以下の実施例を用いて、本発明を更に具体的に説明する。尚、本発明はこれらの実施例に限定されるものではない。 The present invention will be described more specifically with reference to the following examples. The present invention is not limited to these examples.
(実施例1)
幅23mm、全長90mmのステンレス板を12枚準備し、これらを曲率半径が約R13となるように円弧状にそれぞれ湾曲させた。約30度間隔で12枚の湾曲板の末端を集合させ、ニッケルロウ付けにて接合することで、メタル担体用のユニットを形成させた。当直径42.7mm、全長90mmのステンレス製の外筒内に当該ユニットを廻しながら挿入し、ニッケルロウ付けで接合させた。このメタル担体に触媒材料(Al2O3:57.6%、Ce−Zr酸化物:32.4%(CeO2:27.5%)、バインダー:5.8%、Pt:3.6%、Rh:0.7%)を36g/m2塗布し、焼成焼付けを行うことで本発明のメタル担体触媒を作成した。
Example 1
Twelve stainless steel plates having a width of 23 mm and a total length of 90 mm were prepared, and each was curved in an arc shape so that the radius of curvature was approximately R13. The ends of 12 curved plates were gathered at intervals of about 30 degrees and joined by nickel brazing to form a unit for a metal carrier. The unit was inserted into a stainless steel outer cylinder having a diameter of 42.7 mm and a total length of 90 mm, and joined by nickel brazing. Catalyst material (Al 2 O 3 : 57.6%, Ce-Zr oxide: 32.4% (CeO 2 : 27.5%), binder: 5.8%, Pt: 3.6% , Rh: 0.7%) was applied at 36 g / m 2 and baked and baked to prepare the metal carrier catalyst of the present invention.
(実施例2)
幅23mm、全長30mmのステンレス板を12枚準備し、これらを曲率半径が約R13となるように円弧状にそれぞれ湾曲させ、実施例1と同様にメタル担体用のユニットを2個形成させた。当直径42.7mm、全長90mmのステンレス製の外筒内に、前記ユニットの一方を廻しながら入りガス側に挿入し、他方のユニットを、湾曲板の位相が逆になるように出ガス側に挿入し、これらをニッケルロウ付けで接合させた(図6)。このように調製したメタル担体に、実施例1と同様の条件で触媒材料を塗布し、焼成焼付けを行うことで本発明のメタル担体触媒を作成した。
(Example 2)
Twelve stainless steel plates having a width of 23 mm and a total length of 30 mm were prepared and curved in an arc shape so that the radius of curvature was approximately R13, and two units for metal carriers were formed in the same manner as in Example 1. Insert one side of the unit into the stainless steel outer cylinder with a diameter of 42.7 mm and a total length of 90 mm, and insert it into the gas side while turning the other unit. They were inserted and joined by nickel brazing (FIG. 6). The metal carrier catalyst of the present invention was prepared by applying the catalyst material to the metal carrier thus prepared under the same conditions as in Example 1 and performing baking and baking.
(実施例3)
パンチング孔を設けた点を除き、実施例2と同様の手法によりメタル担体触媒を作成した(図9)。
(Example 3)
A metal-supported catalyst was prepared in the same manner as in Example 2 except that punching holes were provided (FIG. 9).
(比較例1)
パイプ触媒
直径42.7mm、全長90mmのパイプの内面に、実施例1と同様の条件で触媒材料を塗布し、焼成焼付けを行った。
(Comparative Example 1)
Pipe catalyst A catalyst material was applied to the inner surface of a pipe having a diameter of 42.7 mm and a total length of 90 mm under the same conditions as in Example 1 and baked.
(比較例2)
マルチチューブ触媒
直径42.7mm、全長90mmのパイプの内面及び合計3本の直径18mm、全長90mmのパンチングパイプの内面に実施例1と同様の条件で触媒材料を塗布し、焼成焼付けを行った。
(Comparative Example 2)
Multi-tube catalyst A catalyst material was applied to the inner surface of a pipe having a diameter of 42.7 mm and a total length of 90 mm and the inner surface of a total of three punching pipes having a diameter of 18 mm and a total length of 90 mm under the same conditions as in Example 1, followed by firing and baking.
(比較例3)
ハニカム触媒
直径42.7mm、直径90mm、セル密度100cpsiのメタルハニカム担体の内面に、実施例1と同様の条件で触媒材料を塗布し、焼成焼付けを行った。
(Comparative Example 3)
Honeycomb Catalyst A catalyst material was applied to the inner surface of a metal honeycomb carrier having a diameter of 42.7 mm, a diameter of 90 mm, and a cell density of 100 cpsi under the same conditions as in Example 1 and baked.
1 メタル担体
2 パイプ
3 湾曲板
4 パンチング孔
1
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JPH0632186Y2 (en) * | 1988-04-26 | 1994-08-24 | カルソニック株式会社 | Metal catalyst carrier |
JPH04103819A (en) * | 1990-08-24 | 1992-04-06 | Usui Internatl Ind Co Ltd | Exhaust gas purification device |
JPH06343876A (en) * | 1993-06-08 | 1994-12-20 | Yamaha Motor Co Ltd | Device for purifying exhaust gas of internal combustion engine |
WO1999064732A1 (en) * | 1998-06-09 | 1999-12-16 | Asec Manufacturing Partnership | Exhaust pipe catalytic device |
JP2001145835A (en) * | 1999-11-19 | 2001-05-29 | Suzuki Motor Corp | Metallic catalyst and its manufacturing method |
BRPI0418042A (en) * | 2003-12-26 | 2007-04-17 | Sakura Kogyo Kk | core part of a catalytic exhaust gas device, and methods for manufacturing it and for inserting and fixing a core part in a catalytic exhaust gas device |
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CN109414674B (en) * | 2016-05-23 | 2021-08-27 | 庄信万丰股份有限公司 | Expandable core device |
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