JPH1066880A - Production of metallic catalyst carrier of catalyst convertor for vehicle - Google Patents

Production of metallic catalyst carrier of catalyst convertor for vehicle

Info

Publication number
JPH1066880A
JPH1066880A JP8228127A JP22812796A JPH1066880A JP H1066880 A JPH1066880 A JP H1066880A JP 8228127 A JP8228127 A JP 8228127A JP 22812796 A JP22812796 A JP 22812796A JP H1066880 A JPH1066880 A JP H1066880A
Authority
JP
Japan
Prior art keywords
metal
catalyst carrier
core
metal catalyst
thin 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.)
Pending
Application number
JP8228127A
Other languages
Japanese (ja)
Inventor
Tamotsu Sugimoto
保 杉本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Marelli Corp
Original Assignee
Calsonic Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Calsonic Corp filed Critical Calsonic Corp
Priority to JP8228127A priority Critical patent/JPH1066880A/en
Publication of JPH1066880A publication Critical patent/JPH1066880A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/28Construction of catalytic reactors
    • F01N3/2803Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
    • F01N3/2807Metal other than sintered metal
    • F01N3/281Metallic honeycomb monoliths made of stacked or rolled sheets, foils or plates
    • F01N3/2814Metallic honeycomb monoliths made of stacked or rolled sheets, foils or plates all sheets, plates or foils being corrugated
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2330/00Structure of catalyst support or particle filter
    • F01N2330/30Honeycomb supports characterised by their structural details
    • F01N2330/38Honeycomb supports characterised by their structural details flow channels with means to enhance flow mixing,(e.g. protrusions or projections)
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Catalysts (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

PROBLEM TO BE SOLVED: To contrive reduction of production cost in comparison with the conventional practice by unnecessitating joining of a thin plate made of metal and performing continuous catalyst fitting and drying. SOLUTION: A long-sized beltlike metallic thin plate consisting of a flat plate is continuously supplied to a pair of corrugate working gears in which a plurality of gears are laminated to form pairs are engaged with one another. The metallic thin plate is formed into a corrugated shape consisting of a plurality of crest parts and trough parts so that the crest parts and the trough parts of the adjacent metallic thin plates 19 do not become the same phase at time of lamination. Thereafter, the metallic thin plate 19 is continuously supplied into a catalyst tank 29 to stick a catalyst on the front and the rear thereof. After the metallic thin plate 19 is continuously supplied into a drying furnace and burned, it is laminated in a multiplex state to form a core and the core is pressed into an outer cylinder made of metal.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は車両用触媒コンバー
タに用いる金属触媒担体の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a metal catalyst carrier used for a catalytic converter for a vehicle.

【0002】[0002]

【従来の技術】従来、車両排気系には、排ガスを浄化す
る触媒コンバータが装着されているが、触媒コンバータ
に用いる触媒担体として、昨今、Fe−Cr−Al系フ
ェライトステンレス箔材(20Cr−5Al−La−F
e)等の金属製薄板からなる金属触媒担体が広く用いら
れている。
2. Description of the Related Art Conventionally, a catalytic converter for purifying exhaust gas has been mounted in a vehicle exhaust system. Recently, as a catalyst carrier used for the catalytic converter, an Fe-Cr-Al ferrite stainless steel foil material (20Cr-5Al) has been used. -La-F
Metal catalyst supports made of a thin metal plate such as e) are widely used.

【0003】そして、斯かる金属触媒担体の製造方法と
して、従来、以下の如き製造方法が知られている。先
ず、第一の製造方法は、金属製薄板からなる帯状の波板
と平板を交互に重ね、これらを多重に巻回して断面円形
或いは断面楕円形状のコアを形成した後、これを金属製
の外筒内に圧入して外筒全体をダイス等で絞り、そし
て、波板と平板の相対移動をなくすために、高温雰囲気
中で波板と平板及びコアの外周と外筒との間を拡散接合
するものである。
[0003] As a method for producing such a metal catalyst carrier, the following production method is conventionally known. First, in the first manufacturing method, a band-shaped corrugated sheet made of a thin metal plate and a flat plate are alternately stacked, and these are wound in multiple layers to form a core having a circular or elliptical cross section. Press into the outer cylinder, squeeze the entire outer cylinder with a die, etc., and diffuse between the outer periphery of the corrugated sheet and the flat plate and the core and the outer cylinder in a high temperature atmosphere to eliminate relative movement between the corrugated sheet and the flat plate. It is to join.

【0004】そして、上記コアに貴金属触媒の担持処理
を施し、外筒の両端部にディフューザを溶着して触媒コ
ンバータが製造されている。尚、金属触媒の担持処理と
して、外筒内のコアに白金等の金属触媒を含有するウォ
ッシュコート溶液(例えば、γアルミナと添加剤及び金
属触媒を成分とする溶液)を流し込んで、波板と平板の
表面にウォッシュコート層と称する薄い塗膜を形成する
方法が広く用いられている。
[0004] A catalytic converter is manufactured by subjecting the core to a treatment for supporting a noble metal catalyst and welding a diffuser to both ends of the outer cylinder. In addition, as a treatment for supporting the metal catalyst, a washcoat solution containing a metal catalyst such as platinum (for example, a solution containing γ-alumina, an additive and a metal catalyst as components) is poured into the core in the outer cylinder, and the corrugated sheet is formed. A method of forming a thin coating film called a washcoat layer on the surface of a flat plate is widely used.

【0005】又、第二の金属触媒担体の製造方法は、金
属製薄板からなる帯状の波板と平板を定尺に裁断して、
これらを交互に積層してコアを成形していくものであ
り、第三の製造方法は、金属製薄板からなる帯状の波板
をつづら折りし乍ら、定尺に裁断した平板を各折り目毎
に挿入してコアを成形していくもので、これらの製造方
法にあっても、コアを金属製の外筒内に圧入し、そし
て、波板と平板及びコアの外周と外筒とを拡散接合させ
てコアに貴金属触媒の担持処理を施した後、外筒の両端
部にディフューザを溶着して触媒コンバータが製造され
ている。
In a second method for producing a metal catalyst carrier, a strip-shaped corrugated sheet made of a thin metal plate and a flat plate are cut to a fixed size.
These are alternately laminated to form a core, and the third manufacturing method is to squeeze a band-shaped corrugated sheet made of a thin metal plate while cutting a flat plate cut to a fixed size for each fold. In these manufacturing methods, the core is pressed into a metal outer cylinder, and the corrugated plate and the flat plate, and the outer periphery of the core and the outer cylinder are diffusion-bonded. After the core is subjected to a precious metal catalyst loading treatment, diffusers are welded to both ends of the outer cylinder to produce a catalytic converter.

【0006】[0006]

【発明が解決しようとする課題】このように、従来の金
属触媒担体は、波板と平板を多重に積層して排ガスが通
過するセルが形成されているが、平板を使用する分だけ
重量が重く、又、波板は高温の排ガスによる熱応力を吸
収できるが平板は熱応力を吸収し難く、更に波板と平板
の接合箇所に応力歪みが発生して破断や脱落を引き起こ
す虞があった。
As described above, in the conventional metal catalyst carrier, a cell through which exhaust gas passes is formed by laminating a corrugated plate and a flat plate in multiple layers. The corrugated sheet is heavy and can absorb the thermal stress caused by the high temperature exhaust gas, but the flat plate does not easily absorb the thermal stress. .

【0007】そして、波板と平板との接合が不十分であ
ると、フィルムアウトが発生して金属触媒担体の破損に
繋がる虞も指摘されている。又、上述の如く波板と平板
を多重に積層した金属触媒担体にあっては、図11に示
すように表面張力によってウォッシュコート溶液が多く
付着したフィレット1が波板3と平板5との接合部に形
成され、斯かるフィレット1は全塗布量の30〜40%
に相当するが、このフィレット1は何ら浄化性能の向上
に寄与するものではなく、ウォッシュコート溶液が無駄
になっているのが実情であった。
[0007] It has also been pointed out that insufficient bonding between the corrugated sheet and the flat sheet may cause film-out and damage to the metal catalyst carrier. In the case of the metal catalyst carrier in which the corrugated plate and the flat plate are multiplexed as described above, the fillet 1 to which a large amount of the wash coat solution adheres due to the surface tension as shown in FIG. And the fillet 1 is 30 to 40% of the total applied amount.
However, this fillet 1 did not contribute to the improvement of the purification performance at all, and the fact was that the wash coat solution was wasted.

【0008】更に又、いずれの製造方法に於ても、波板
と平板の2種類の金属製薄板が必要となると共に、第二
の積層式の製造方法にあっては、波板と平板を何十枚も
定尺に裁断しなければならず、又、第三のつづら折り構
造の金属触媒担体にあっては、各折り目毎に平板を挿入
しなければならないため作業が煩雑であった。加えて、
これらの製造方法にあっては、金属製薄板の波付け(波
板の成形)→コアの成形(波板と平板の巻回,つづら折
り等)→金属触媒担体アッセンブリ(外筒へのコアの挿
入,拡散接合)→触媒付け(コアへの貴金属触媒の担持
処理)→触媒の乾燥(焼成)といった多くの工程を要
し、然も、触媒付けや乾燥を金属触媒担体1個毎に行わ
なければならないために大型の乾燥炉(焼成炉)が必要
となる等、工程数が多く金属触媒担体の製造コストが高
価になってしまう欠点があった。
Further, in any of the manufacturing methods, two kinds of metal thin plates, ie, a corrugated plate and a flat plate are required, and in the second lamination type manufacturing method, the corrugated plate and the flat plate are used. Dozens of sheets had to be cut to a fixed size, and in the case of the third metal catalyst carrier having a self-folding structure, a flat plate had to be inserted for each fold, so that the operation was complicated. in addition,
In these manufacturing methods, corrugation of a thin metal plate (forming of a corrugated sheet) → forming of a core (winding of a corrugated sheet and a flat plate, zigzag folding, etc.) → metal catalyst carrier assembly (insertion of a core into an outer cylinder) , Diffusion bonding) → catalyzing (processing of loading the precious metal catalyst on the core) → drying (firing) of the catalyst is required. Of course, catalyzing and drying must be performed for each metal catalyst carrier. For this reason, a large drying furnace (firing furnace) is required because of this, and there is a disadvantage that the number of steps is large and the production cost of the metal catalyst carrier is high.

【0009】又、特開平5−138040号公報には、
金属触媒担体の製造に当たり金属製薄板の接合を不要と
するため、図12に示すように一枚の金属製薄板をコル
ゲート加工して、波形7が所定のピッチで連続する複数
列9a,9b,9c,9dに区画成形すると共に、各列
9a,9b,9c,9dの位相を隣接する相互間でずら
してこれを多重に巻回していく金属触媒担体の製造方法
が開示されている。
Japanese Patent Application Laid-Open No. 5-138040 discloses that
In order to eliminate the necessity of joining the metal thin plates in the production of the metal catalyst carrier, a single metal thin plate is corrugated as shown in FIG. 12 to form a plurality of rows 9a, 9b, A method for manufacturing a metal catalyst carrier is disclosed in which a plurality of rows 9a, 9b, 9c, and 9d are formed while being sectioned, and the phases of the rows 9a, 9b, 9c, and 9d are shifted between adjacent ones.

【0010】而して、斯かる波板11を用いた金属触媒
担体にあっては、平板が不要となるため金属触媒担体全
体の軽量化が可能となり、その結果、低熱容量となって
昇温時間が短縮できると共に、熱応力の吸収に優れ破断
や脱落を引き起こす虞もないし、積層された波形7の端
部が相互に噛み合って波板11の相対移動が防止される
ため、フィルムアウト現象が生ずることもない。
[0010] In the metal catalyst carrier using the corrugated sheet 11, no flat plate is required, so that the weight of the entire metal catalyst carrier can be reduced, and as a result, the heat capacity becomes low and the temperature rises. In addition to being able to shorten the time, it is excellent in absorbing thermal stress and there is no possibility of causing breakage or falling off, and the ends of the laminated corrugations 7 mesh with each other to prevent the relative movement of the corrugated plate 11, so that the film-out phenomenon occurs. Nothing happens.

【0011】然し乍ら、上記波板11を用いた金属触媒
担体の製造方法にあっても、依然としてコアへの貴金属
触媒の担持処理や乾燥を金属触媒担体毎に行っているの
が実情であった。本発明は斯かる実情に鑑み案出された
もので、金属製薄板の接合を不要とすると共に、連続的
な触媒付けや乾燥を行うことによって従来に比し製造コ
ストの低廉化を図った車両用触媒コンバータの金属触媒
担体の製造方法を提供することを目的とする。
However, even in the method for manufacturing a metal catalyst carrier using the corrugated plate 11, the fact is that the supporting treatment and drying of the noble metal catalyst on the core are still performed for each metal catalyst carrier. The present invention has been devised in view of the above circumstances, and is a vehicle that eliminates the need for joining thin metal plates, and achieves a lower manufacturing cost compared to the conventional vehicle by performing continuous catalysting and drying. It is an object of the present invention to provide a method for producing a metal catalyst carrier of a catalytic converter for use.

【0012】[0012]

【課題を解決するための手段】斯かる目的を達成するた
め、請求項1に係る車両用触媒コンバータの金属触媒担
体の製造方法は、複数枚のギヤを積層して対となるギヤ
を互いに噛合させた一対のコルゲート加工ギヤに、平板
からなる長尺な帯状の金属製薄板を連続的に供給して、
当該金属製薄板を、積層時に隣接する金属製薄板同士の
山部と谷部が同位相とならないように複数の山部と谷部
とからなる波形形状に成形した後、当該金属製薄板を触
媒槽内に連続的に供給してその表裏に触媒を付着し、次
いで、斯かる金属製薄板を乾燥炉に連続的に供給して焼
成した後、これを多重に積層して断面円形状又は断面ト
ラック形状のコアを成形し、当該コアを金属製の外筒内
に圧入することを特徴とする。
According to a first aspect of the present invention, there is provided a method for manufacturing a metal catalyst carrier for a catalytic converter for a vehicle, wherein a plurality of gears are stacked and a pair of gears mesh with each other. To a pair of corrugated processing gears, a long strip-shaped metal thin plate made of a flat plate was continuously supplied,
After forming the metal sheet into a corrugated shape including a plurality of peaks and valleys so that the peaks and valleys of adjacent metal sheets do not have the same phase during lamination, the metal sheet is catalyzed. After continuously supplying the inside of the tank and attaching the catalyst to the front and back thereof, and then continuously supplying such a thin metal plate to a drying furnace and firing it, laminating the multiple layers to form a circular cross section or a cross section A track-shaped core is formed, and the core is pressed into a metal outer cylinder.

【0013】そして、請求項2に係る発明は、請求項1
記載の金属触媒担体の製造方法に於て、金属製薄板をつ
づら折りして多重に積層してコアを成形することを特徴
とし、請求項3に係る発明は、請求項1記載の金属触媒
担体の製造方法に於て、金属製薄板を定尺に裁断し、こ
れを順次積層してコアを成形することを特徴とする。
The invention according to claim 2 is based on claim 1
In the method for producing a metal catalyst support according to the above aspect, the core is formed by folding a metal thin plate by staking and multiply laminating the core. The manufacturing method is characterized in that a metal thin plate is cut into a fixed size, and the laminated thin plates are sequentially laminated to form a core.

【0014】又、請求項4に係る発明は、請求項1記載
の金属触媒担体の製造方法に於て、金属製薄板を多重に
巻回してコアを成形するものである。
According to a fourth aspect of the present invention, in the method for producing a metal catalyst carrier according to the first aspect, a core is formed by winding multiple thin metal plates.

【0015】(作用)各請求項に係る発明によれば、一
対のコルゲート加工ギヤに平板からなる長尺な帯状の金
属製薄板を連続的に供給して、当該金属製薄板を複数の
山部と谷部とからなる波形形状に成形した後、当該金属
製薄板を触媒槽内に連続的に供給してその表裏に触媒を
付着し、次いで、斯かる金属製薄板を乾燥炉に連続的に
供給して焼成した後、これを多重に積層してコアを成形
し、そして、このコアを外筒内に圧入することで金属触
媒担体が製造される。
(Effects) According to the invention of each claim, a long band-shaped thin metal plate made of a flat plate is continuously supplied to a pair of corrugated gears, and the thin metal plate is formed into a plurality of peaks. And a valley, the metal sheet is continuously fed into the catalyst tank to attach the catalyst to the front and back, and then the metal sheet is continuously fed to a drying furnace. After supplying and firing, the core is formed by laminating the cores in multiple layers, and the core is pressed into an outer cylinder to produce a metal catalyst carrier.

【0016】そして、斯様に製造された金属触媒担体
は、積層された各金属製薄板の山部と谷部の端部が相互
に噛み合って、金属製薄板相互の相対移動を防止する。
In the metal catalyst carrier thus manufactured, the ends of the ridges and valleys of the laminated metal thin plates mesh with each other to prevent relative movement between the metal thin plates.

【0017】[0017]

【発明の実施の形態】以下、本発明の実施形態を図面に
基づき詳細に説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0018】図1は請求項1及び請求項2に係る発明の
一実施形態によって製造された車両用触媒コンバータの
金属触媒担体を示し、当該金属触媒担体13は、断面ト
ラック形状の金属製の外筒15と、当該外筒15内に圧
入されたコア17とからなり、コア17はFe−Cr−
Al合金等からなる一枚の帯状の金属製薄板19を図2
の如くつづら折りして横方向に順次積層した構造となっ
ている。
FIG. 1 shows a metal catalyst carrier of a vehicular catalytic converter manufactured according to one embodiment of the invention according to claims 1 and 2. The metal catalyst carrier 13 is made of a metal having a track-shaped cross section. A cylinder 15 and a core 17 pressed into the outer cylinder 15, and the core 17 is made of Fe—Cr—
FIG. 2 shows a strip-shaped metal thin plate 19 made of an Al alloy or the like.
And the layers are sequentially laminated in the horizontal direction.

【0019】而して、上記金属製薄板19は、図3に示
すようにルーバーコルゲート加工によって、同一の長さ
Lからなる複数の山部21と谷部23が、夫々、排ガス
Gの流れ方向に対し斜め方向へ1/2L宛ずらして順次
隣接,配置された波形形状に形成されており、本実施形
態は、斯様に複数の山部21と谷部23を斜め方向へ所
定の規則性を以って順次配置することで、図4の如くつ
づら折りして積層された金属製薄板19相互の山部21
と谷部23が同位相とならず、対向する山部21同士が
当接してセルの目つぶれが生じないようになっている。
As shown in FIG. 3, a plurality of peaks 21 and valleys 23 having the same length L are formed in the metal thin plate 19 by louver corrugation as shown in FIG. Are formed in a waveform shape that is sequentially shifted and shifted by 1/2 L in the diagonal direction, and in the present embodiment, the plurality of peaks 21 and valleys 23 are formed in a predetermined regularity in the diagonal direction. 4, the metal thin plates 19 are folded in a zigzag as shown in FIG.
The valleys 23 and the valleys 23 do not have the same phase, and the opposing ridges 21 are in contact with each other so that the cells are not blinded.

【0020】尚、図4に示すように上記山部21と谷部
23は同一の長さLを以って成形され、そして、排ガス
Gの流れ方向に対し斜め方向へ1/2L宛ずらして順次
配置されているため、金属製薄板19の両端部に配置さ
れた略半数の山部21′と谷部23′は、他の山部21
や谷部23の1/2Lの長さとされている。その他、図
3中、符号25で表示する太線部分は山部21や谷部2
3を区画する平坦部である。
As shown in FIG. 4, the peaks 21 and the valleys 23 are formed to have the same length L, and are shifted by 1/2 L obliquely to the flow direction of the exhaust gas G. Almost half of the ridges 21 ′ and valleys 23 ′ arranged at both ends of the metal thin plate 19 are
The length of the valley 23 is 1 / 2L. In addition, in FIG. 3, a thick line portion indicated by reference numeral 25 is a peak portion 21 or a valley portion 2.
3 is a flat part.

【0021】本実施形態に於ける金属触媒担体13はこ
のように構成されており、当該金属触媒担体13は、請
求項1及び請求項2に係る発明方法の一実施形態によっ
て以下の如く製造される。図示しないが、先ず、複数枚
のギヤを積層して対となるギヤを互いに噛合させた一対
のコルゲート加工ギヤに、平板からなる長尺な帯状の金
属製薄板を連続的に供給して、図3で既述した波形形状
の金属製薄板19を順次成形していく。
The metal catalyst carrier 13 in the present embodiment is configured as described above. The metal catalyst carrier 13 is manufactured as follows by one embodiment of the method according to the first and second aspects of the present invention. You. Although not shown, first, a long band-like thin metal plate made of a flat plate is continuously supplied to a pair of corrugated gears in which a plurality of gears are stacked and a pair of gears mesh with each other. The corrugated metal thin plates 19 described in 3 are sequentially formed.

【0022】次いで、図5に示すように白金等の金属触
媒を含有する従来周知のウォッシュコート溶液27を貯
留した触媒槽29内に上記金属製薄板19を連続的に通
過させて、金属製薄板19の表裏にウォッシュコート溶
液27を付着させる。尚、図5中、31,33は金属製
薄板19のガイドローラで、金属製薄板19は約3秒程
度でウォッシュコート溶液27内を通過するように各ガ
イドローラ31,33で案内されている。
Next, as shown in FIG. 5, the metal thin plate 19 is continuously passed through a catalyst tank 29 in which a conventionally known wash coat solution 27 containing a metal catalyst such as platinum is stored. The washcoat solution 27 is attached to the front and back of the substrate 19. In FIG. 5, 31 and 33 are guide rollers for the metal thin plate 19, and the metal thin plate 19 is guided by the guide rollers 31 and 33 so as to pass through the washcoat solution 27 in about 3 seconds. .

【0023】この後、表裏にウォッシュコート溶液27
が付着した金属製薄板19を乾燥炉に連続的に供給して
これを焼成することで、図6に示すように金属製薄板1
9の表裏に薄いウォッシュコート層35が形成される。
そして、斯かる金属製薄板19を図2の如くつづら折り
して、これを横方向に順次積層し乍ら金属製薄板19を
所定寸法で裁断して断面トラック形状のコア17を順次
成形していく。そして、成形されたコア17を夫々金属
製の外筒15内に圧入することで、図1の如き金属触媒
担体13が製造されることとなる。
After that, wash coat solution 27
By continuously supplying the metal thin plate 19 to which the metal is adhered to the drying furnace and firing it, as shown in FIG.
9, a thin washcoat layer 35 is formed on the front and back.
Then, the metal thin plate 19 is folded in a zigzag as shown in FIG. 2, and the metal thin plate 19 is cut into a predetermined size while sequentially laminating the metal thin plates 19 to sequentially form the core 17 having a track-shaped cross section. . Then, each of the molded cores 17 is press-fitted into the outer cylinder 15 made of metal, whereby the metal catalyst carrier 13 as shown in FIG. 1 is manufactured.

【0024】而して、この後、外筒15の両端部にディ
フューザを溶着して触媒コンバータが製造されるが、図
7に示す触媒コンバータ37のように外筒15内にディ
フューザ39,41を挿入,溶着して、その挿入側端部
39a,41aの板厚でコア17の排ガス流入側端部1
7aと排ガス流出側端部17bの周縁部を夫々保持させ
たり、或いは又、図8に示すようにディフューザ41の
挿入側端部に環状のフランジ43を内方に設けて、当該
フランジ43でコア17の排ガス流出側端部17bの周
縁部を保持させれば、外筒15に対するコア17の位置
決めが可能である。
Thereafter, a diffuser is welded to both ends of the outer cylinder 15 to produce a catalytic converter. However, the diffusers 39 and 41 are provided in the outer cylinder 15 as in a catalytic converter 37 shown in FIG. Inserted and welded, and the exhaust gas inflow side end 1 of the core 17 is formed with the thickness of the insertion side end 39a, 41a.
7a and the peripheral edge of the exhaust gas outflow end 17b, respectively, or alternatively, as shown in FIG. The core 17 can be positioned with respect to the outer cylinder 15 by holding the peripheral edge of the exhaust gas outflow end 17 b of the core 17.

【0025】そして、上述の如く製造された金属触媒担
体13によれば、積層された各金属製薄板19の山部2
1と谷部23の端部が相互に噛み合って、金属製薄板1
9相互の相対移動を防止する。又、上記金属触媒担体1
3を用いた図7の触媒コンバータ37にあっては、ディ
フューザ39,41の挿入側端部39a,41aがコア
17の両端部17a,17bに夫々当接して、外筒15
に対するコア17全体のズレや積層した金属製薄板19
相互のズレを防止することとなる。
According to the metal catalyst carrier 13 manufactured as described above, the peaks 2 of each of the laminated metal thin plates 19 are formed.
1 and the ends of the valleys 23 are engaged with each other,
9 Prevent relative movement of each other. In addition, the metal catalyst carrier 1
7, the insertion-side ends 39a, 41a of the diffusers 39, 41 abut against both ends 17a, 17b of the core 17, respectively.
Of the core 17 as a whole and the laminated metal sheet 19
Mutual displacement is prevented.

【0026】このように、本実施形態に係る金属触媒担
体の製造方法は、金属触媒担体13の製造に当たり、平
板からなる長尺な帯状の金属製薄板からルーバーコルゲ
ート加工によって図3の如き金属製薄板19を連続的に
成形し、次いで、図5の如くこれを触媒槽29に連続的
に供給して触媒付けを行い、この後、セル17を成形し
て外筒15内に圧入することを特徴としており、製造工
程に於て、従来の如き金属製薄板19同士及び外筒15
とコア17との拡散接合が不要となって工程数が軽減
し、然も、コア17の成形前の金属製薄板19に触媒付
けと乾燥が連続的に行えるので、コアへの貴金属触媒の
担持処理を金属触媒担体毎に行っていた従来例に比し、
極めて安価に金属触媒担体13を製造することが可能と
なる。
As described above, in the method for manufacturing the metal catalyst carrier according to the present embodiment, the metal catalyst carrier 13 is manufactured by louver corrugating a long strip-shaped metal thin plate made of a metal plate as shown in FIG. The thin plate 19 is continuously formed and then continuously supplied to the catalyst tank 29 as shown in FIG. 5 to perform catalysis. Thereafter, the cell 17 is formed and pressed into the outer cylinder 15. In the manufacturing process, metal thin plates 19 and outer cylinder 15
The diffusion bonding between the core 17 and the core 17 becomes unnecessary, and the number of steps is reduced. In addition, the catalyst can be continuously applied to the thin metal plate 19 before the core 17 is formed, and the noble metal catalyst can be supported on the core. Compared to the conventional example where the treatment was performed for each metal catalyst carrier,
It becomes possible to manufacture the metal catalyst carrier 13 at extremely low cost.

【0027】又、従来、一枚の波板をつづら折りして金
属触媒担体を成形するには、折り目毎に平板を挿入して
セルを形成しなければならず、然も、斯かる波板を一枚
で巻回したり積層していくと、波板の山部と谷部が同位
相となる部分が存在するため、山部と谷部が重なり合っ
てセルの目つぶれや表面積の減少が生じ、通気抵抗や触
媒による排気浄化作用が著しく悪化してしまう欠点があ
った。
Conventionally, in order to form a metal catalyst carrier by folding a single corrugated sheet, a flat plate must be inserted at each fold to form a cell. When winding or laminating with a single sheet, there are parts where the peaks and valleys of the corrugated sheet have the same phase, so the peaks and valleys overlap and the blindness and surface area of the cell decrease, There is a drawback that the ventilation resistance and the exhaust gas purifying action of the catalyst are significantly deteriorated.

【0028】而して、その対策としては、二枚の波板を
逆向きで合わせて巻回したり、積層の場合は一枚宛逆位
相となるように裏返す必要があったが、本実施形態によ
れば、一枚の金属製薄板19を単につづら折りしていく
だけでコア17が製造でき、然も、従来のように折り目
毎に平板を挿入してセルを形成していく必要がないた
め、製造された金属触媒担体13にセルの目つぶれが発
生することもないし、図11の如きフィレット1が形成
されることもない。
As a countermeasure, it is necessary to wind two corrugated sheets together in the opposite direction, or to turn the two corrugated sheets upside down so that one sheet is in opposite phase. According to this, the core 17 can be manufactured by simply folding a single metal thin plate 19, and needless to say, it is not necessary to insert a flat plate for each fold to form cells as in the conventional case, The produced metal catalyst carrier 13 does not suffer from blinding of cells, nor does the fillet 1 as shown in FIG. 11 be formed.

【0029】そして、斯様に平板が不要となって金属触
媒担体13の軽量化が図られるため、これを用いた触媒
コンバータ37は低熱容量となって昇温時間が短縮でき
ると共に、熱応力の吸収に優れ破断や脱落を引き起こす
虞もないし、金属触媒担体13は、積層した金属製薄板
19の山部21や谷部23の端部が相互に噛み合って金
属製薄板19の相対移動が防止されるため、フィルムア
ウト現象が生ずることもない。
Since the metal catalyst carrier 13 is reduced in weight by eliminating the need for such a flat plate, the catalytic converter 37 using the metal catalyst carrier 13 has a low heat capacity, can reduce the time required for temperature rise, and can reduce the thermal stress. The metal catalyst carrier 13 is excellent in absorption and there is no danger of breaking or falling off, and the metal catalyst carrier 13 is prevented from moving relative to the metal thin plate 19 because the ends of the peaks 21 and the valleys 23 of the stacked metal thin plates 19 mesh with each other. Therefore, the film-out phenomenon does not occur.

【0030】ところで、上述したように本実施形態で
は、表裏にウォッシュコート層35を設けた金属製薄板
19を図2の如くつづら折りするので、その折り目部分
に若干のウォッシュコート層35の剥離が生ずる虞があ
る。然し乍ら、従来、この種の金属触媒担体13にあっ
ては、斯かる部位での触媒作用はあまり期待できるもの
ではないため、折り目部分の若干のウォッシュコート層
35の剥離は何ら触媒コンバータ37の排ガス浄化性能
に支障を来すことはない。
As described above, in the present embodiment, the metal thin plate 19 provided with the washcoat layer 35 on the front and back is folded in a zigzag as shown in FIG. 2, so that the peeling of the washcoat layer 35 slightly occurs at the fold. There is a fear. However, in the case of the metal catalyst carrier 13 of this type, since the catalytic action at such a portion is not so expected, any peeling of the wash coat layer 35 at the fold portion does not cause any exhaust gas of the catalytic converter 37. There is no hindrance to purification performance.

【0031】尚、上記実施形態では、触媒付けを行った
金属製薄板19を図2の如くつづら折りしてコア17を
成形したが、図9に示す請求項1及び請求項3の一実施
形態のように、図5に示す触媒付けを終えた金属製薄板
19を定尺に裁断し、これを順次積層してコア17を成
形してもよいし、又、図示しないが、請求項1及び請求
項4の一実施形態のように、図5に示す触媒付けを終え
た金属製薄板19を多重に巻回してコアを成形してもよ
く、これらの各実施形態によっても、所期の目的を達成
することが可能である。
In the above-described embodiment, the core 17 is formed by folding the thin metal plate 19 to which the catalyst has been applied, as shown in FIG. 2, but according to the first and third embodiments shown in FIG. As described above, the metal thin plate 19 after the catalyzing shown in FIG. 5 is cut into a fixed length, and these are sequentially laminated to form the core 17. As in the embodiment of item 4, the core may be formed by winding the metal thin plate 19 having been catalyzed as shown in FIG. 5 in multiple layers, and the intended purpose may be achieved by each of these embodiments. It is possible to achieve.

【0032】又、金属触媒担体を成形する金属製薄板は
上記金属製薄板19に限定されるものではなく、平板か
らなる長尺な帯状の金属製薄板をコルゲート加工ギヤに
連続的に供給して、図10に示す金属製薄板45のよう
に各谷部47に同一の長さMからなる山部49を、夫
々、排ガスGの流れ方向に対し斜め方向へその長さM宛
ずらして順次隣接,配置した波形に成形して、積層され
た金属製薄板45相互の対向する山部49同士が当接し
てセルの目つぶれが生じないようなものを使用してもよ
いし、更に又、図12に示す従来の金属製薄板11を用
いることも可能である。
Further, the metal sheet for forming the metal catalyst carrier is not limited to the above-mentioned metal sheet 19, and a long strip-shaped metal sheet made of a flat plate is continuously supplied to the corrugating gear. As shown in FIG. 10, a ridge portion 49 having the same length M is successively adjacent to each valley portion 47 in a diagonal direction to the flow direction of the exhaust gas G like a metal thin plate 45 shown in FIG. It may be formed into a corrugated shape so that the opposed metal peaks 49 of the laminated metal thin plates 45 do not come into contact with each other so that the cells are not blinded. It is also possible to use a conventional metal thin plate 11 shown in FIG.

【0033】[0033]

【発明の効果】以上述べたように、各請求項に係る金属
触媒担体の製造方法によれば、コアを成形する金属製薄
板同士の接合が不要となって工程数が軽減し、然も、コ
ア成形前の金属製薄板に触媒付けと乾燥が連続的に行え
るので、コアへの貴金属触媒の担持処理を金属触媒担体
毎に行っていた従来例に比し、極めて安価に金属触媒担
体を製造することが可能となった。
As described above, according to the method for manufacturing a metal catalyst carrier according to each claim, it is not necessary to join the metal thin plates forming the core, and the number of steps is reduced. The catalyst can be continuously applied to the thin metal plate before core molding and drying, so the metal catalyst carrier is manufactured at extremely low cost compared to the conventional case where the processing of loading the noble metal catalyst on the core is performed for each metal catalyst carrier. It became possible to do.

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

【図1】請求項1及び請求項2に係る製造方法の一実施
形態によって製造された金属触媒担体の全体斜視図であ
る。
FIG. 1 is an overall perspective view of a metal catalyst carrier manufactured by one embodiment of a manufacturing method according to claims 1 and 2.

【図2】図1に示す金属触媒担体の製造方法の一工程図
である。
FIG. 2 is a process chart of the method for producing the metal catalyst carrier shown in FIG.

【図3】図1に示す金属触媒担体の製造に用いる金属製
薄板の部分斜視図である。
FIG. 3 is a partial perspective view of a metal thin plate used for manufacturing the metal catalyst carrier shown in FIG.

【図4】図1の金属触媒担体の製造時に於ける金属製薄
板の積層状態を示す説明図である。
FIG. 4 is an explanatory diagram showing a state of lamination of metal thin plates at the time of manufacturing the metal catalyst carrier of FIG. 1;

【図5】図1に示す金属触媒担体の製造方法の一工程図
である。
FIG. 5 is a process chart of the method for producing the metal catalyst carrier shown in FIG.

【図6】図1に示す金属触媒担体の製造方法の一工程図
である。
FIG. 6 is a process chart of the method for producing the metal catalyst carrier shown in FIG.

【図7】図1に示す金属触媒担体を用いた触媒コンバー
タの要部断面図である。
FIG. 7 is a sectional view of a main part of a catalytic converter using the metal catalyst carrier shown in FIG.

【図8】図1に示す金属触媒担体を用いた触媒コンバー
タの変形例の要部拡大断面図である。
8 is an enlarged sectional view of a main part of a modified example of the catalytic converter using the metal catalyst carrier shown in FIG.

【図9】請求項1及び請求項3に係る製造方法の一実施
形態の一工程図である。
FIG. 9 is a process chart of one embodiment of the manufacturing method according to claims 1 and 3;

【図10】金属製薄板の変形例の部分斜視図である。FIG. 10 is a partial perspective view of a modified example of a metal thin plate.

【図11】従来の金属触媒担体の要部断面図である。FIG. 11 is a sectional view of a main part of a conventional metal catalyst carrier.

【図12】従来の金属製薄板の部分斜視図である。FIG. 12 is a partial perspective view of a conventional metal thin plate.

【符号の説明】[Explanation of symbols]

13 金属触媒担体 15 外筒 17 コア 19,45 金属製薄板 21,21′,49 山部 23,23′,47 谷部 27 ウォッシュコート溶液 29 触媒槽 35 ウォッシュコート層 37 触媒コンバータ 39,41 ディフューザ 43 フランジ DESCRIPTION OF SYMBOLS 13 Metal catalyst carrier 15 Outer cylinder 17 Core 19, 45 Metal thin plate 21, 21 ', 49 Mountain part 23, 23', 47 Valley part 27 Wash coat solution 29 Catalyst tank 35 Wash coat layer 37 Catalytic converter 39, 41 Diffuser 43 Flange

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B21D 47/00 B21D 47/00 C F01N 3/28 301 F01N 3/28 301P ──────────────────────────────────────────────────の Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI Technical display location B21D 47/00 B21D 47/00 C F01N 3/28 301 F01N 3/28 301P

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 複数枚のギヤを積層して対となるギヤを
互いに噛合させた一対のコルゲート加工ギヤに、平板か
らなる長尺な帯状の金属製薄板を連続的に供給して、当
該金属製薄板を、積層時に隣接する金属製薄板(19,
45)同士の山部(21,21′,49)と谷部(2
3,23′,47)が同位相とならないように複数の山
部(21,21′,49)と谷部(23,23′,4
7)とからなる波形形状に成形した後、当該金属製薄板
(19,45)を触媒槽(29)内に連続的に供給して
その表裏に触媒を付着し、次いで、斯かる金属製薄板
(19,45)を乾燥炉に連続的に供給して焼成した
後、これを多重に積層して断面円形状又は断面トラック
形状のコア(17)を成形し、当該コア(17)を金属
製の外筒(15)内に圧入することを特徴とする車両用
触媒コンバータの金属触媒担体の製造方法。
An elongated strip-shaped thin metal plate made of a flat plate is continuously supplied to a pair of corrugated gears in which a plurality of gears are stacked and a pair of gears mesh with each other. When laminating, the adjacent metal sheet (19,
45) peaks (21, 21 ', 49) and valleys (2)
3, 23 ', 47) and a plurality of peaks (21, 21', 49) and valleys (23, 23 ', 4) so that they do not have the same phase.
7), the metal thin plates (19, 45) are continuously supplied into the catalyst tank (29) to attach the catalyst to the front and back surfaces thereof, and then the metal thin plates (19, 45) are formed. (19, 45) is continuously supplied to a drying furnace and fired, and then laminated in multiple layers to form a core (17) having a circular or track-shaped cross section, and the core (17) is made of metal. A method for manufacturing a metal catalyst carrier for a catalytic converter for a vehicle, wherein the metal catalyst carrier is press-fitted into an outer cylinder (15).
【請求項2】 コア(17)は、金属製薄板(19,4
5)をつづら折りして多重に積層して成形されることを
特徴とする請求項1記載の車両用触媒コンバータの金属
触媒担体の製造方法。
2. The core (17) is made of a metal sheet (19, 4).
5. The method for manufacturing a metal catalyst carrier of a catalytic converter for a vehicle according to claim 1, wherein the metal catalyst carrier is formed by folding and severing 5).
【請求項3】 コア(17)は、金属製薄板(19,4
5)を定尺に裁断し、これを順次積層して成形されるこ
とを特徴とする請求項1記載の車両用触媒コンバータの
金属触媒担体の製造方法。
3. The core (17) is made of a metal sheet (19, 4).
5. The method for producing a metal catalyst carrier for a catalytic converter for a vehicle according to claim 1, wherein 5) is cut into a fixed size, and is sequentially laminated and molded.
【請求項4】 コア(17)は、金属製薄板(19,4
5)を多重に巻回して成形されることを特徴とする請求
項1記載の車両用触媒コンバータの金属触媒担体の製造
方法。
4. The core (17) is made of a metal sheet (19, 4).
5. The method for producing a metal catalyst carrier of a catalytic converter for a vehicle according to claim 1, wherein 5) is formed by winding multiple times.
JP8228127A 1996-08-29 1996-08-29 Production of metallic catalyst carrier of catalyst convertor for vehicle Pending JPH1066880A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8228127A JPH1066880A (en) 1996-08-29 1996-08-29 Production of metallic catalyst carrier of catalyst convertor for vehicle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8228127A JPH1066880A (en) 1996-08-29 1996-08-29 Production of metallic catalyst carrier of catalyst convertor for vehicle

Publications (1)

Publication Number Publication Date
JPH1066880A true JPH1066880A (en) 1998-03-10

Family

ID=16871645

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8228127A Pending JPH1066880A (en) 1996-08-29 1996-08-29 Production of metallic catalyst carrier of catalyst convertor for vehicle

Country Status (1)

Country Link
JP (1) JPH1066880A (en)

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