JP3459937B2 - Metal carrier for exhaust gas purification catalyst - Google Patents

Metal carrier for exhaust gas purification catalyst

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Publication number
JP3459937B2
JP3459937B2 JP06243992A JP6243992A JP3459937B2 JP 3459937 B2 JP3459937 B2 JP 3459937B2 JP 06243992 A JP06243992 A JP 06243992A JP 6243992 A JP6243992 A JP 6243992A JP 3459937 B2 JP3459937 B2 JP 3459937B2
Authority
JP
Japan
Prior art keywords
carrier
exhaust gas
temperature
metal
honeycomb body
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 - Lifetime
Application number
JP06243992A
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Japanese (ja)
Other versions
JPH05309277A (en
Inventor
登志広 ▲高田▼
泰 石川
充蔵 柴田
俊和 中川
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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Publication date
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Priority to JP06243992A priority Critical patent/JP3459937B2/en
Publication of JPH05309277A publication Critical patent/JPH05309277A/en
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Publication of JP3459937B2 publication Critical patent/JP3459937B2/en
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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
    • 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)

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)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、内燃機関から排出され
る排気ガスを浄化する排気ガス浄化触媒用メタル担体に
関し、詳しくはメタル担体の構造の改良に関するもので
ある。 【0002】 【従来の技術】例えば自動車エンジンからの排ガスを浄
化するための排ガス浄化触媒として、セラミック製ある
いは金属製のハニカム体に活性アルミナなどの担持層を
形成し、その担持層に白金やロジウムなどの触媒金属を
担持させたものが多く用いられている。ところが触媒金
属は、約300℃より低い温度では触媒活性が得られな
いという現実がある。そのためエンジン始動直後などに
は触媒担体の温度が低く、排ガスの熱により300℃以
上に加熱されるまでの間は有害物質がほとんど浄化され
ぬまま排出されるという問題があった。 【0003】このような不具合を改善するために、セラ
ミックスより熱伝導率が高く昇温特性に優れた金属製の
メタル担体が主流となりつつある。また、例えば実開昭
63−141632号公報や実開平2−83320号公
報などには、排ガス上流側には体積の小さなメタルハニ
カム体を配置し、下流側にセラミックス製あるいはメタ
ル製のハニカム体を配置したタンデム型担体構造が開示
されている。このように上流側の担体の熱容量を小さく
することで、上流側の担体の温度を速やかに上昇させる
ことができる。また低温活性の高い触媒金属を上流側の
担体に多く担持させるなど、触媒設計の自由度も向上す
る。 【0004】ところで排気ガスは流路の外周側では流路
壁からの放熱などが生じるために、流路内では軸中心程
温度が高いという温度分布が生じている。さらに温度が
高い軸中心では触媒反応が進行し反応熱が発生するた
め、軸中心部と外周部との温度差が一段と拡がってしま
う。したがってメタル担体においても、軸中心側は昇温
特性に優れるが外周側では温度の上昇が遅く、担体の径
方向で初期の浄化性能にばらつきが生じるという不具合
がある。 【0005】そこで実開昭63−63521号公報など
には、複数のメタルハニカム体をそれぞれ間隔を隔てて
配置し、それぞれのハニカム体の流路の方向が互いに異
なるようにしたタンデム型担体が開示されている。この
担体では、それぞれの分割担体間に空間を有しているた
め、前段の分割担体で整流された排気ガスはその空間で
乱流となって攪拌混合され、さらに隣接する分割担体が
互いに異なる方向の流路を有するため、攪拌混合が一層
促進される。したがって下流側の分割担体に流入する排
気ガスの温度が均一となるので、浄化性能のばらつきが
防止される。 【0006】 【発明が解決しようとする課題】ところが上記したタン
デム型の担体構造においては、分割担体の間の空間部で
は排気ガスが直接外筒と接触することとなり、外筒から
の放熱が大きいという問題がある。また空間部で乱流と
なっても、軸中心側の高温排気ガスが外周側に移行する
のであるから、外周側の排気ガス温度が上昇し結果的に
外筒への放熱を助長することとなっている。したがって
熱損失が生じ、下流側の分割担体の昇温性能が向上せず
浄化性能の向上の妨げとなっていた。 【0007】また下流側の分割担体の昇温は排気ガスか
らの熱伝導のみに依存し、触媒反応熱によっても加熱さ
れた上流側の分割担体自体の熱は下流側の分割担体の昇
温には殆ど寄与していない。そればかりか空間部の断熱
作用により、上流側の分割担体の温度が上昇しすぎて熱
劣化しやすいという問題もある。さらに複数のハニカム
体を外筒内に装着する必要があり、生産性の面で不具合
がある。 【0008】なお、生産性の問題点を解決するものとし
て、1枚の平板に複数の波板を間隔を隔てて並べた状態
で巻回した構造も前記公報に開示されている。しかしこ
の構造では、空間部は平板のみがロール状に巻回され排
気ガスの径方向の移動が困難であるので、乱流化の効果
を得にくい。また上流側の熱は平板を介して下流側に伝
熱されるため、分割担体とした効果が半減する。さらに
熱容量も大きい。これらの理由により、初期の浄化性能
に劣るという不具合がある。 【0009】本発明はこのような事情に鑑みてなされた
ものであり、外筒への放熱を低減するとともに排気ガス
流を乱流化でき、かつ熱容量を小さくして昇温特性を向
上させることを目的とする。 【0010】 【課題を解決するための手段】上記課題を解決する本発
明の排気ガス浄化触媒用メタル担体は、平板と波板を重
ねてロール状に巻回されたハニカム体とハニカム体を保
持する外筒と、からなる排気ガス浄化触媒用メタル担体
において、平板及び波板の少なくとも一方は平板及び波
板の長手方向に対して傾斜しながら略巻回方向に延びる
貫通孔群のみをもち、ハニカム体の隣接する複数のハニ
カム通路が貫通孔群を介して螺旋状に連通し、貫通孔群
はハニカム体の内周から外周まで螺旋状に延びている
とを特徴とする。 【0011】貫通孔群を構成する貫通孔の径は、1〜5
mmが好ましい。径が1mm未満では貫通孔の形成が困
難であり、径が5mmを超えると軸中心側の高温排気ガ
スが外周側へ移行する程度が大きくなり過ぎるため好ま
しくない。 【0012】 【作用】本発明のメタル担体では、複数のハニカム通路
が貫通孔群を介して螺旋状に連通している。したがって
貫通孔を通じて排気ガスが出入することにより、排気ガ
スの径方向への移動が可能となり、排気ガス流の乱流化
を図ることができる。そして貫通孔群により上流側と下
流側の熱伝導面積を調整し、上流側の発熱量が下流側へ
奪熱される熱量を制御することにより、上流側の昇温と
下流側の昇温特性を制御している。また上流側から出た
排気ガスが、下流側へ流入する前に拡散する程度を調整
している。すなわち、貫通孔の数が多い程下流側による
奪熱量は少なく上流側の昇温は良好となり、また軸方向
に長く穿孔される程、上流側を出た排気ガスの拡散は多
くなり排気ガスのピーク温度が低くなる。このため実用
上は上記の現象を考慮して、適正な条件で貫通孔を設け
る必要がある。 【0013】また従来のタンデム型の担体のような空間
部が存在しないので、外筒部への放熱が少なく昇温が速
やかに行われる。 【0014】 【発明の効果】すなわち本発明のメタル担体によれば、
始動初期の上流側の昇温が早く、かつ下流側の温度も速
やかに上昇する。したがって初期の浄化性能が向上し、
かつ局部的な過熱が防止されるため劣化が防止され長期
間使用することができる。また複数のハニカム体を用い
ることなくタンデム型の担体と同等の作用効果を得るこ
とができ、生産性に優れている。 【0015】 【実施例】以下、参考例と実施例及び比較例により具体
的に説明する。 (参考例1) 図1に本発明の一参考例のメタル担体を示す。このメタ
ル担体は、ハニカム体1と、ハニカム体1を収納する外
筒2とから構成されている。 【0016】ハニカム体1は、図2に示すように、Fe
−20Cr−5Al−REM(Y,La等)などの耐熱
鋼から50μmの厚さに形成された幅100mmの箔状
の平板10と、その平板10をコルゲート加工して形成
された波板11とからなり、平板10と波板11とを重
ねて直径90mmのロール状に巻回して形成されてい
る。 【0017】この平板10及び波板11の幅方向中央部
には、それぞれ幅20mmの帯状に多数の貫通孔12が
一端から他端まで全体に穿設されている。したがって得
られたハニカム体1には、長さ方向の中央部分16の幅
20mmの部分に、外周から中心部まで貫通孔12の群
が存在している。ハニカム体1は、平板10と波板11
とが重ねられて巻回された後、フェライト系合金などか
らなる板厚1.5mmの外筒2に挿入される。そして、
4×10 -4Torrの真空下、1300℃で60分加熱され
ることにより、拡散接合およびロウ付け接合されて一体
化されている。なお、ロウ付けの場合、ロウ材の供給塗
布方法は公知の方法により行った。 【0018】本参考例のメタル担体は白金等の触媒用貴
金属を担持された後、図1に示すように軸方向が排気ガ
ス流と平行となるように触媒コンバータとして配置され
る。ここで上流側部分14は貫通孔12の多い中央部分
16を介して下流側部分15と連続している。したがっ
て貫通孔12内の排気ガスの断熱作用により、上流側部
分14の熱は全体が一体型の従来の担体に比べて下流側
部分15に伝熱されにくく、上流側部分14は速やかに
昇温する。しかし貫通孔12の周囲では平板10及び波
板11は連続しているため、空間部をもつタンデム型の
担体に比べれば伝熱は速やかに行われ、下流側部分15
の昇温特性も優れている。 【0019】また中央部分16では、図3に示すように
複数のハニカム通路13が貫通孔12を介して連通して
いる。したがってハニカム通路13内を流れる排気ガス
は、貫通孔12を出入可能であり、乱流化による温度の
均一化を図ることができる。これにより下流側部分15
の昇温が均一となり、下流側部分15における浄化性能
の局部的なばらつきを防止することができる。 【0020】そして外筒2と直接的に接触する排気ガス
量は、空間部をもつ従来のタンデム型担体に比べて極め
て少ない。したがって外筒2への無駄な放熱が抑制さ
れ、下流側部分15の昇温がさらに促進される。すなわ
ち本参考例のメタル担体によれば、下流側部分15の昇
温特性に特に優れている。これを実証するために、本
考例のメタル担体に常法により活性アルミナ担持層を形
成し、さらに常法により白金とロジウムからなる触媒金
属を担持させて触媒とし、自動車ガソリンエンジンの排
気系に装着した。そして始動後30秒時点における下流
側部分15の中心部分の温度を測定し、結果を表1に示
す。 【0021】なお貫通孔12の径の影響を知るために、
貫通孔12の孔径を10mm,5mm,1mmの3水準
としてそれぞれメタル担体を形成し、それぞれについて
上記温度を測定した。 (比較例1) 貫通孔12をもたないこと以外は参考例と同様のメタル
担体を選び、同様に参考例の測定位置と同様の位置にて
温度を測定した結果を表1に示す。 (比較例2) 比較例1と同様の材質からなる一対の50mm長のハニ
カム体を20mmの間隔を隔てて列設したタンデム型の
担体を選び、下流側のハニカム体の中央の温度を同様に
測定した結果を表1に示す。 【0022】 【表1】表1より、貫通孔12をもつ参考例1の担体は、貫通孔
をもたない比較例に比べて下流側部分の昇温特性に優れ
ていることが明らかである。また孔径が大きいほどその
効果が大きくなる傾向があることもわかる。 【0023】一方比較例1の担体では、下流側部分の昇
温特性が劣っているが、これは熱容量が大きいことに起
因するものと考えられる。また比較例2のタンデム型担
体では、空間部の存在により下流側担体への伝熱が妨げ
られたこと、及び外筒からの放熱が大きいことに起因す
るものと考えられる。上記参考例では、貫通孔12群は
平板10及び波板11の中央部分に一筋の帯状に設けた
が、平行に複数筋設けてもよい。(実施例1) 本発明の一実施例のメタル担体は、 図4又は図5に示す
ように、平板及び波板の長手方向に対して傾斜するよう
貫通孔12群を設ける。これらの場合は、貫通孔12
群によって上流側及び下流側に区分することは困難とな
るが、貫通孔12群の帯はメタル担体に螺旋状に形成さ
れ乱流化の効果が一層向上する。 (参考例2) 図6に第2の参考例のメタル担体を示す。このメタル担
体では、外径D1 =86mm、長さB1 =100mmの
ハニカム体1が、厚さt2 =2mm、外径D2=90m
m、長さB2 =100mmの外筒2に収納されている。 【0024】ハニカム体1はFe−20Cr−5Al系
で、厚さ50μm、幅100mmの平板10と、平板1
0が波高さ1.2mm、波ピッチ2.4mmにコルゲー
ト加工された波板11が中心軸の周りに巻回されて形成
されている。平板10及び波板11に加工前の平板に
は、事前に端面からb1 =20mmの箇所に、直径d1
=1mmの貫通孔12が図7のようにピッチp1 =3m
mで長手方向に設けられている。したがって貫通孔群の
存在位置では、平板及び波板の断面積は周方向に約33
%削減されている。 【0025】このメタル担体を、排気ガスがAの方向か
ら流入するように、エンジン排気系に取り付け、浄化程
度のパラメータとしてメタル担体の中心部で入口より1
0mmの位置X1 及び40mmの位置X2 における昇温
状況を測定評価した。また比較として図8に示すような
上流側担体3と下流側担体4とをもつ従来のタンデム担
体を同様に取り付け、参考例のメタル担体に相当する箇
所(X1 ,X2 )の昇温状況を測温比較した。エンジン
始動15秒、30秒後の測温結果を表2に示す。 【0026】 【表2】以上のように、本参考例のメタル担体の上流側測温点X
1 はタンデム担体に比べて昇温速度は遅いが、下流側測
温点X2 の昇温は遙かに良好で30秒後には浄化性能が
発揮できる温度に到達している。一方、タンデム担体に
おいては上流側担体3の昇温は早いが、排気ガスの浄化
を左右する下流側担体4の昇温は遅くて30秒経過して
も浄化可能温度に到達していない。 【0027】 【0028】
DETAILED DESCRIPTION OF THE INVENTION [0001] BACKGROUND OF THE INVENTION 1. Field of the Invention
Metal catalyst carrier for exhaust gas purification catalyst that purifies exhaust gas
In particular, it is concerned with improving the structure of metal carriers.
is there. [0002] 2. Description of the Related Art For example, exhaust gas from an automobile engine is purified.
As a catalyst for purifying exhaust gas
Or a supporting layer made of activated alumina etc. on a metallic honeycomb body.
Formed and a catalytic metal such as platinum or rhodium
What is carried is often used. However, catalyst gold
The genus does not provide catalytic activity below about 300 ° C.
There is a reality that it is. Therefore, immediately after starting the engine, etc.
Means that the temperature of the catalyst carrier is low, and
Most of the harmful substances are purified until heated up.
There was a problem of being discharged as it was. In order to improve such a problem, a
Made of metal with higher thermal conductivity and better temperature rise characteristics than mix
Metal carriers are becoming mainstream. Also, for example,
No. 63-141632 and Japanese Utility Model No. 2-83320
According to reports, small-sized metal honeycombs
A cam body is placed, and a ceramic or meta
Discloses a tandem-type carrier structure with a honeycomb body made of
Have been. Thus, the heat capacity of the carrier on the upstream side is reduced.
To quickly raise the temperature of the carrier on the upstream side
be able to. In addition, catalyst metal with high low-temperature activity is
Improve the degree of freedom in catalyst design, such as by supporting a large amount on a carrier
You. [0004] By the way, the exhaust gas passes through the flow path on the outer peripheral side of the flow path.
Due to heat radiation from the wall, etc.
There is a temperature distribution where the temperature is high. And the temperature
At the high center of the axis, the catalytic reaction proceeds and generates heat of reaction.
The temperature difference between the shaft center and the outer periphery
U. Therefore, even with metal carriers, the temperature rises at the center of the shaft.
Excellent characteristics, but the temperature rise is slow on the outer circumference,
That the initial purification performance varies depending on the direction
There is. Accordingly, Japanese Utility Model Application Laid-Open No. 63-63521 discloses
Has multiple metal honeycomb bodies separated by an interval
And the direction of the flow path of each honeycomb body is different from each other.
A tandem-type carrier is disclosed. this
The carrier has a space between each divided carrier.
Therefore, the exhaust gas rectified by the former divided carrier
The mixture is stirred and mixed in turbulence, and the adjacent divided carriers
Since the flow paths are different from each other, stirring and mixing are further improved.
Promoted. Therefore, the exhaust flowing into the downstream split carrier
Since the gas temperature becomes uniform, variations in purification performance
Is prevented. [0006] However, the above-mentioned tan
In the dem-type carrier structure, the space between the divided carriers
Exhaust gas comes into direct contact with the outer cylinder,
There is a problem that heat dissipation is large. Also, turbulence in the space
High temperature exhaust gas at the shaft center shifts to the outer periphery
Therefore, the temperature of the exhaust gas on the outer peripheral side rises and consequently
It is to promote heat radiation to the outer cylinder. Therefore
Heat loss occurs, and the temperature rise performance of the downstream carrier is not improved
This hindered improvement in purification performance. [0007] The temperature rise of the divided carrier on the downstream side is caused by exhaust gas.
Heat only by the heat of catalytic reaction.
The heat of the upstream divided carrier itself rises and rises in the downstream divided carrier.
Little contribution to temperature. Not only that, but also the insulation of the space
Due to the action, the temperature of the upstream split carrier rises too much,
There is also a problem that it is easily deteriorated. More honeycombs
Body needs to be mounted inside the outer cylinder, which is a problem in productivity
There is. It is assumed that the problem of productivity is solved.
, A state in which multiple corrugated sheets are arranged on a single flat plate at intervals
Is also disclosed in the publication. But this
In this structure, only the flat plate is wound in a roll shape
Since the gas is difficult to move in the radial direction, the effect of turbulence
Difficult to obtain. Heat on the upstream side is transferred to the downstream side via the flat plate.
Because of heating, the effect of the split carrier is reduced by half. further
Large heat capacity. For these reasons, the initial purification performance
There is a problem that it is inferior. The present invention has been made in view of such circumstances.
It reduces exhaust heat to the outer cylinder and
The flow can be made turbulent and the heat capacity is reduced to improve the temperature rise characteristics.
The purpose is to make it better. [0010] [MEANS FOR SOLVING THE PROBLEMS]
Ming's metal carrier for exhaust gas purification catalysts consists of flat and corrugated plates.
The honeycomb body wound in a roll shape
Metal carrier for exhaust gas purification catalyst, comprising an outer cylinder
, At least one of the flat plate and the corrugated plate
Extends substantially in the winding direction while tilting with respect to the longitudinal direction of the plate
Through hole grouponlyHaving a plurality of honeycombs adjacent to each other in the honeycomb body.
Cam passage spirally communicates through through holes, Through-hole group
Extends spirally from the inner circumference to the outer circumference of the honeycomb bodyThis
And features. The diameter of the through-holes constituting the through-hole group is 1 to 5
mm is preferred. If the diameter is less than 1 mm, it is difficult to form through holes.
If the diameter exceeds 5 mm, the high-temperature exhaust gas
Is too large to move to the outer circumference.
Not good. [0012] According to the metal carrier of the present invention, a plurality of honeycomb passages are provided.
Through the group of through holesSpirallyCommunicating. Therefore
Exhaust gas enters and exits through the through hole,
Turbulence in the exhaust gas flow
Can be achieved. And the upstream and lower by the through-hole group
Adjusts the heat transfer area on the upstream side, so that the calorific value on the upstream side is
By controlling the amount of heat deprived, the upstream temperature rise and
It controls the temperature rise characteristics on the downstream side. Also came out from the upstream side
Adjusts the degree to which exhaust gas diffuses before flowing downstream
are doing. That is, the larger the number of through holes, the more downstream
The amount of heat loss is small, the temperature rise on the upstream side is good, and
The longer the hole is drilled, the more the exhaust gas that has exited the upstream
And the peak temperature of the exhaust gas decreases. For this reason practical
Above, through holes are provided under appropriate conditions in consideration of the above phenomenon
Need to be Further, a space like a conventional tandem-type carrier is provided.
No heat radiation to the outer cylinder
Will be done promptly. [0014] According to the metal carrier of the present invention,
The temperature rise on the upstream side at the beginning of startup is fast, and the temperature on the downstream side is also fast.
It rises quickly. Therefore, the initial purification performance is improved,
Also, since local overheating is prevented, deterioration is prevented and long-term
Can be used for a while. Also, using multiple honeycomb bodies
Can achieve the same effect as a tandem-type carrier without
It has excellent productivity. [0015] [Embodiment]Reference Example, Example, and Comparative ExampleMore specific
Will be explained. (Reference example1) FIG. 1 shows one embodiment of the present invention.Reference example1 shows a metal carrier. This meta
The honeycomb carrier has a honeycomb body 1 and an outer housing for housing the honeycomb body 1.
And a cylinder 2. As shown in FIG. 2, the honeycomb body 1 is made of Fe
Heat resistance of -20Cr-5Al-REM (Y, La etc.)
100mm wide foil formed from steel to a thickness of 50μm
And a flat plate 10 formed by corrugating the flat plate 10
And the corrugated sheet 11 is overlapped.
It is formed by winding into a roll with a diameter of 90 mm.
You. The central part in the width direction of the flat plate 10 and the corrugated plate 11
Has a large number of through-holes 12 in a 20 mm wide strip shape.
It is entirely drilled from one end to the other. Therefore gain
The width of the central portion 16 in the length direction is
A group of through-holes 12 from the outer periphery to the center at a portion of 20 mm
Exists. The honeycomb body 1 includes a flat plate 10 and a corrugated plate 11.
After being wound with overlapping, ferrite alloy etc.
Is inserted into the outer cylinder 2 having a thickness of 1.5 mm. And
4 × 10 -FourHeated at 1300 ° C for 60 minutes under vacuum of Torr
Diffusion bonding and brazing bonding
Has been In the case of brazing, supply coating of brazing material
Cloth was performed by a known method. BookReference exampleMetal support is precious for catalysts such as platinum
After the metal is supported, the exhaust gas is directed in the axial direction as shown in FIG.
Is arranged as a catalytic converter so that it is parallel to the
You. Here, the upstream portion 14 is a central portion having many through holes 12.
The portion 16 is continuous with the downstream portion 15 through the portion 16. Accordingly
The heat insulation effect of the exhaust gas in the through hole 12 causes
The heat of the minute 14 is on the downstream side compared to the whole carrier
The heat is not easily transferred to the portion 15, and the upstream portion 14 is quickly
Raise the temperature. However, the flat plate 10 and the wave
Since the plate 11 is continuous, a tandem type having a space is provided.
The heat transfer is performed faster than the carrier, and the downstream portion 15
Is also excellent in temperature rise characteristics. In the central portion 16, as shown in FIG.
The plurality of honeycomb passages 13 communicate with each other through the through holes 12.
I have. Therefore, the exhaust gas flowing in the honeycomb passage 13
Can move in and out of the through-hole 12, and the temperature of the
Uniformity can be achieved. Thus, the downstream portion 15
And the purification performance of the downstream portion 15 becomes uniform.
Can be prevented from being locally varied. Exhaust gas that comes into direct contact with the outer cylinder 2
The volume is extremely high compared to a conventional tandem carrier with a space.
Less. Therefore, unnecessary heat radiation to the outer cylinder 2 is suppressed.
Thus, the temperature rise of the downstream portion 15 is further promoted. Sand
ChimotoReference exampleAccording to the metal carrier of FIG.
Especially excellent in temperature characteristics. To demonstrate this, a bookthree
ExampleActivated alumina support layer is formed on metal carrier
And platinum and rhodium catalyst in the usual manner
Metal as a catalyst for the emission of automobile gasoline engines.
It was attached to the air system. And 30 seconds after starting
The temperature of the central part of the side part 15 was measured, and the results are shown in Table 1.
You. In order to know the influence of the diameter of the through hole 12,
The hole diameter of the through hole 12 is 3 levels of 10mm, 5mm, 1mm
Each form a metal carrier, and for each
The temperature was measured. (Comparative Example 1) Except that it does not have a through hole 12Reference exampleMetal similar to
Choose a carrier and do the sameReference exampleAt the same position as the measurement position
Table 1 shows the results of measuring the temperature. (Comparative Example 2) A pair of 50 mm long honey made of the same material as in Comparative Example 1.
A tandem type with cam bodies arranged at intervals of 20 mm
Select the carrier and set the temperature at the center of the downstream honeycomb body in the same manner.
Table 1 shows the measurement results. [0022] [Table 1]From Table 1, it has a through-hole 12.Reference example1 carrier is a through hole
Excellent in temperature rise characteristics of the downstream part compared to the comparative example without
It is clear that Also, the larger the hole diameter,
It can also be seen that the effect tends to increase. On the other hand, the carrier of Comparative Example 1
Inferior temperature characteristics are caused by large heat capacity.
It is thought that it causes. In addition, the tandem bearing of Comparative Example 2
In the body, the presence of the space prevents heat transfer to the downstream carrier
And the large heat dissipation from the outer cylinder
It is considered to be. In the above reference example, the group of through holes 12 is
It was provided in the center part of the flat plate 10 and the corrugated plate 11 in a strip shape.
However, a plurality of lines may be provided in parallel.(Example 1) The metal carrier of one embodiment of the present invention is Shown in FIG. 4 or FIG.
So that it is inclined with respect to the longitudinal direction of the flat plate and the corrugated plate.
ToA group of through holes 12 is provided.In these cases, the through holes 12
It is difficult to distinguish upstream and downstream by groups.
However, the band of the group of through-holes 12 is spirally formed on the metal carrier.
The effect of turbulence is further improved. (Reference Example 2) FIG. 6 shows a metal carrier of a second reference example. This metal bearing
In the body, the outer diameter D1= 86mm, length B1= 100mm
The honeycomb body 1 has a thickness tTwo= 2mm, outer diameter DTwo= 90m
m, length BTwo= 100 mm. The honeycomb body 1 is made of an Fe-20Cr-5Al-based material.
A flat plate 10 having a thickness of 50 μm and a width of 100 mm;
0 is corrugated to wave height 1.2mm and wave pitch 2.4mm
Formed corrugated sheet 11 wound around center axis
Have been. For flat plate 10 and corrugated plate 11 before processing
Is b1= 20 mm, diameter d1
= 1 mm through holes 12 with pitch p as shown in FIG.1= 3m
m in the longitudinal direction. Therefore, the through hole group
In the existing position, the cross-sectional area of the flat plate and corrugated plate is about 33 in the circumferential direction.
% Has been reduced. When the exhaust gas is directed in the direction of A,
Into the exhaust system of the engine so that
One parameter from the entrance at the center of the metal carrier as a parameter of degree
0mm position X1And the position X at 40 mmTwoHeating in
The situation was measured and evaluated. For comparison, as shown in FIG.
A conventional tandem carrier having an upstream carrier 3 and a downstream carrier 4
Attach the body in the same way,Reference exampleEquivalent to the metal carrier of
Place (X1, XTwo) Was compared. engine
Table 2 shows the temperature measurement results 15 seconds and 30 seconds after the start. [0026] [Table 2]As mentioned above, the bookReference exampleTemperature measuring point X on the upstream side of the metal carrier
1Has a slower heating rate than the tandem carrier,
Hot point XTwoTemperature rise is much better and after 30 seconds the purification performance
The temperature that can be used has been reached. On the other hand, tandem carriers
In this case, the temperature of the upstream carrier 3 rises quickly, but the exhaust gas is purified.
The temperature rise of the downstream carrier 4 which affects
Has not reached the purifying temperature. [0027] [0028]

【図面の簡単な説明】 【図1】本発明の一参考例のメタル担体を一部破断して
示す斜視図である。 【図2】図1に用いたハニカム体の展開斜視図である。 【図3】図1の要部拡大断面図である。 【図4】実施例1のメタル担体の、平板の平面図であ
る。 【図5】実施例1の他の態様を示し、平板の平面図であ
る。 【図6】参考例2のメタル担体の断面図である。 【図7】参考例2のメタル担体に用いた平板の要部平面
図である。 【図8】従来のタンデム担体の断面図である。 【符号の説明】 1:ハニカム体 2:外筒
10:平板 11:波板 12:貫通孔
13:ハニカム通路 14:上流側部分 15:下流側部分
16:中央部分
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view showing a metal carrier according to a reference example of the present invention, partially cut away. FIG. 2 is an exploded perspective view of the honeycomb body used in FIG. FIG. 3 is an enlarged sectional view of a main part of FIG. FIG. 4 is a plan view of a flat plate of the metal carrier of Example 1. FIG. 5 is a plan view of a flat plate, showing another mode of the first embodiment. FIG. 6 is a cross-sectional view of a metal carrier of Reference Example 2. FIG. 7 is a plan view of a main part of a flat plate used for a metal carrier of Reference Example 2. FIG. 8 is a sectional view of a conventional tandem carrier. [Description of Signs] 1: Honeycomb body 2: Outer cylinder
10: flat plate 11: corrugated plate 12: through hole
13: honeycomb passage 14: upstream portion 15: downstream portion
16: Central part

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中川 俊和 愛知県東海市東海町5丁目3番地 新日 本製鐵株式會社 名古屋製鐵所内 (56)参考文献 特開 昭63−134061(JP,A) 特開 平3−174221(JP,A) 特開 平4−260443(JP,A) 特開 平2−273546(JP,A) 実開 昭63−141633(JP,U) 実開 昭63−126029(JP,U) 実開 平3−26321(JP,U) 実開 平4−53448(JP,U) 国際公開91/001178(WO,A1) (58)調査した分野(Int.Cl.7,DB名) B01J 21/00 - 38/74 B01D 53/94 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Toshikazu Nakagawa 5-3 Tokai-cho, Tokai-city, Aichi Prefecture Inside Nippon Steel Corporation Nagoya Works (56) References JP-A-63-134061 (JP, A JP-A-3-174221 (JP, A) JP-A-4-260443 (JP, A) JP-A-2-273546 (JP, A) JP-A 63-141633 (JP, U) JP-A 63-141633 126029 (JP, U) JP-A-3-26321 (JP, U) JP-A-4-53448 (JP, U) WO 91/001178 (WO, A1) (58) Fields investigated (Int. Cl. 7) B01J 21/00-38/74 B01D 53/94

Claims (1)

(57)【特許請求の範囲】 【請求項1】 平板と波板を重ねてロール状に巻回され
たハニカム体と該ハニカム体を保持する外筒と、からな
る排気ガス浄化触媒用メタル担体において、該平板及び
該波板の少なくとも一方は該平板及び該波板の長手方向
に対して傾斜しながら略巻回方向に延びる貫通孔群のみ
をもち、該ハニカム体の隣接する複数のハニカム通路が
該貫通孔群を介して螺旋状に連通し、該貫通孔群は該ハ
ニカム体の内周から外周まで螺旋状に延びていることを
特徴とする排気ガス浄化触媒用メタル担体。
(57) [Claim 1] A metal carrier for an exhaust gas purifying catalyst, comprising a honeycomb body wound on a flat sheet and a corrugated sheet and wound into a roll, and an outer cylinder holding the honeycomb body. Wherein at least one of the flat plate and the corrugated plate has only a group of through holes extending in a substantially winding direction while being inclined with respect to the longitudinal direction of the flat plate and the corrugated plate, and is adjacent to the honeycomb body. A plurality of honeycomb passages spirally communicate with each other through the through hole group, and the through hole group
A metal carrier for an exhaust gas purifying catalyst, which spirally extends from an inner periphery to an outer periphery of a honeycomb body .
JP06243992A 1992-03-18 1992-03-18 Metal carrier for exhaust gas purification catalyst Expired - Lifetime JP3459937B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06243992A JP3459937B2 (en) 1992-03-18 1992-03-18 Metal carrier for exhaust gas purification catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06243992A JP3459937B2 (en) 1992-03-18 1992-03-18 Metal carrier for exhaust gas purification catalyst

Publications (2)

Publication Number Publication Date
JPH05309277A JPH05309277A (en) 1993-11-22
JP3459937B2 true JP3459937B2 (en) 2003-10-27

Family

ID=13200237

Family Applications (1)

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3215866B2 (en) 1999-03-26 2001-10-09 名古屋大学長 Method for producing metal carrier used for exhaust gas purification catalyst
JP3932798B2 (en) 2000-11-15 2007-06-20 日産自動車株式会社 Metal carrier
CN1320260C (en) * 2002-08-16 2007-06-06 排放技术有限公司 Metal honeycomb body consisting of at least partially perforated sheet metal layers
US7083860B2 (en) 2002-08-16 2006-08-01 Emitec Gesellschaft Fuer Emissionstechnologie Mbh Metallic honeycomb body having at least partially perforated sheet-metal layers
DE102006005788A1 (en) * 2006-02-07 2007-08-09 Umicore Ag & Co. Kg Catalyst with improved light-off behavior
JP5279284B2 (en) 2008-01-30 2013-09-04 株式会社キャタラー Punching metal carrier catalyst for exhaust gas purification
JP5199291B2 (en) * 2010-02-03 2013-05-15 新日鉄住金マテリアルズ株式会社 Catalyst carrier
DE102016215289B4 (en) * 2016-08-16 2022-12-29 Vitesco Technologies GmbH Honeycomb body for exhaust aftertreatment
JP6742457B1 (en) * 2019-02-05 2020-08-19 株式会社キャタラー Metal base material for exhaust gas purification and exhaust gas purification apparatus using the same

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