JPH11179157A - Electric heating catalytic apparatus - Google Patents
Electric heating catalytic apparatusInfo
- Publication number
- JPH11179157A JPH11179157A JP9357818A JP35781897A JPH11179157A JP H11179157 A JPH11179157 A JP H11179157A JP 9357818 A JP9357818 A JP 9357818A JP 35781897 A JP35781897 A JP 35781897A JP H11179157 A JPH11179157 A JP H11179157A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst carrier
- foil
- catalyst
- preliminary
- metal
- 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.)
- Withdrawn
Links
- 238000005485 electric heating Methods 0.000 title claims description 20
- 230000003197 catalytic effect Effects 0.000 title abstract 3
- 239000003054 catalyst Substances 0.000 claims abstract description 126
- 239000011888 foil Substances 0.000 claims abstract description 81
- 229910052751 metal Inorganic materials 0.000 claims abstract description 38
- 239000002184 metal Substances 0.000 claims abstract description 38
- 238000002485 combustion reaction Methods 0.000 claims abstract description 11
- 239000012041 precatalyst Substances 0.000 claims description 39
- 239000000919 ceramic Substances 0.000 claims description 21
- 239000000853 adhesive Substances 0.000 claims description 20
- 230000001070 adhesive effect Effects 0.000 claims description 20
- 238000010030 laminating Methods 0.000 claims description 14
- 239000012790 adhesive layer Substances 0.000 claims description 8
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 abstract description 10
- 238000005304 joining Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000005096 rolling process Methods 0.000 abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 238000010292 electrical insulation Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000004804 winding Methods 0.000 description 4
- 230000004913 activation Effects 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- 238000005219 brazing Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910001463 metal phosphate Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、金属箔を積層して
形成したメタル担体を触媒担体としてこれを通電発熱さ
せ、短時間に触媒活性温度に上昇できる構造を有する内
燃機関の排気ガス浄化用電気加熱触媒装置に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying exhaust gas of an internal combustion engine having a structure in which a metal carrier formed by laminating metal foils is used as a catalyst carrier to generate heat and to raise the catalyst activation temperature in a short time. The present invention relates to an electric heating catalyst device.
【0002】[0002]
【従来の技術】内燃機関の排気ガスを浄化するため、金
属箔を積層してハニカム体としたメタル担体に触媒を担
持させた触媒装置を内燃機関の排気ガス通路に配置し、
排気中のHC、CO、NO2 等を浄化している。しか
し、排気ガス浄化用触媒は、活性温度より低い温度では
排気ガス浄化能力が著しく低下するため、内燃機関の始
動時等、触媒の温度が低い間は、排気中の上記有害物
質、特にHC、CO物質が触媒により浄化されず、その
まま大気中に放出されるという問題を生じる。2. Description of the Related Art In order to purify exhaust gas of an internal combustion engine, a catalyst device in which a catalyst is carried on a metal carrier formed by stacking metal foils to form a honeycomb body is disposed in an exhaust gas passage of the internal combustion engine.
It purifies HC, CO, NO 2 and the like in the exhaust gas. However, since the exhaust gas purifying catalyst has a significantly reduced exhaust gas purifying ability at a temperature lower than the activation temperature, when the temperature of the catalyst is low, such as when the internal combustion engine is started, the harmful substances in the exhaust gas, especially HC, There is a problem that the CO substance is not purified by the catalyst and is released to the atmosphere as it is.
【0003】この問題を解決するために、予備触媒担体
として金属箔を積層したハニカム体を使用し、内燃機関
の始動時にこの予備触媒担体に電流を通すことにより、
金属触媒担体自体を発熱させて、短時間で触媒活性化温
度(300〜400℃)まで温度を上昇させるようにし
た電気加熱式触媒装置が提案されている。[0003] In order to solve this problem, a honeycomb body in which metal foils are laminated is used as a preliminary catalyst carrier, and an electric current is passed through the preliminary catalyst carrier when the internal combustion engine is started.
There has been proposed an electrically heated catalyst device in which a metal catalyst carrier itself is heated to raise the temperature to a catalyst activation temperature (300 to 400 ° C.) in a short time.
【0004】この電気加熱式触媒装置は、図5に示すよ
うに,排気ガス通路に接続されたケーシング内に通電加
熱予備触媒担体2と主触媒担体3を直列に配設してなる
もので、排気ガスは通電加熱予備触媒担体2において加
熱した触媒によって短時間で排気ガス浄化作用を発揮さ
せるとともに、後方の主触媒担体3についても触媒の昇
温を促進して排気ガス浄化効果を早期に発揮するように
構成されている。As shown in FIG. 5, the electric heating type catalyst device comprises an electrically heated pre-catalyst carrier 2 and a main catalyst carrier 3 arranged in series in a casing connected to an exhaust gas passage. Exhaust gas exerts an exhaust gas purifying action in a short time by the catalyst heated in the electrically heated pre-catalyst carrier 2, and also promotes an exhaust gas purifying effect of the rear main catalyst carrier 3 by promoting the temperature rise of the catalyst. It is configured to be.
【0005】ここで用いられる通電加熱予備触媒担体2
は、金属製の波箔4と平箔5を用い、その少なくとも一
方の表面に絶縁皮膜を形成し、該波箔4と平箔5を重ね
て中心電極6の周りに巻き回して得られる円筒状の金属
ハニカム体と、このハニカム体を内装した外筒8と、こ
の外筒に電気的に絶縁されつつ装着された外部電極9
と、この外部電極9と前記外筒8間に通電する電源(図
示せず)等から構成されている。中心電極6からの配線
は外部電極9に接続される。該波箔4と平箔5とは図6
に示すようなハニカム構造を形成し、該波箔4と平箔5
との間は表面に絶縁皮膜を有するために電気的に絶縁さ
れている。中心電極6と外筒8との間に電圧を付加して
予備触媒担体2に通電を開始すると、波箔4と平箔5と
にそれぞれ独立に電流が流れ、予備触媒担体の温度を上
昇させることができる。波箔4と平箔5との接触部の一
部を局部的にろう付け接合によって絶縁皮膜を破壊しつ
つ接合し、該接合点を通電抵抗発熱点として予備触媒担
体2を加熱する方法も採用されていた。[0005] The electrically heated pre-catalyst carrier 2 used here
Is a cylinder obtained by using a metal corrugated foil 4 and a flat foil 5, forming an insulating film on at least one surface thereof, laminating the corrugated foil 4 and the flat foil 5, and winding around a center electrode 6. Metal honeycomb body, an outer cylinder 8 containing the honeycomb body, and an external electrode 9 mounted on the outer cylinder while being electrically insulated.
And a power supply (not shown) for supplying electricity between the external electrode 9 and the outer cylinder 8. The wiring from the center electrode 6 is connected to the external electrode 9. The corrugated foil 4 and the flat foil 5 are shown in FIG.
To form a honeycomb structure as shown in FIG.
Are electrically insulated because they have an insulating film on the surface. When a voltage is applied between the center electrode 6 and the outer cylinder 8 to start energizing the pre-catalyst carrier 2, a current flows independently through the corrugated foil 4 and the flat foil 5, thereby increasing the temperature of the pre-catalyst carrier. be able to. A method is also used in which a part of the contact portion between the corrugated foil 4 and the flat foil 5 is joined while breaking the insulating film by local brazing to break down the insulating film, and the junction is heated as a heating resistance of the preliminary catalyst carrier 2. It had been.
【0006】予備触媒担体2における迅速な触媒の昇温
のためには、予備触媒担体の熱容量が小さい方が有利で
あり、予備触媒担体は長さを短くする必要がある。ま
た、予備触媒担体の波箔と平箔とは中心電極6と外筒8
の近傍を除いては接合されていない。このように長さが
短く、かつ部分的にしか接合されていないため、予備触
媒担体は排気ガスの流れる方向の剪断力に対して非常に
弱い構造となっており、剪断力を受けるといわゆるテレ
スコープ変形と呼ばれる変形を起しやすい。In order to quickly raise the temperature of the catalyst in the pre-catalyst carrier 2, it is advantageous that the heat capacity of the pre-catalyst carrier is small, and the length of the pre-catalyst carrier needs to be reduced. Further, the corrugated foil and the flat foil of the preliminary catalyst carrier are formed by the center electrode 6 and the outer cylinder 8.
Are not joined except for the vicinity. Since the length is short and only partially joined, the pre-catalyst carrier has a structure that is very weak against shearing force in the flow direction of the exhaust gas. Deformation called scope deformation is likely to occur.
【0007】予備触媒担体2を構成する金属箔は、その
うちの一部は絶縁皮膜を有していない場合が有り、また
平箔と波箔との接触部の一部をろう付け接合する場合も
あり、予備触媒担体2と主触媒担体3を密着して配置す
ると、予備触媒担体と主触媒担体とが導通して電気的絶
縁が破られるという問題がある。そのため、従来は、P
CT公開96/38657号公報(PCT/JP96/
01474)に開示されているように、このように剪断
力に対して弱い予備触媒担体を触媒装置に組み込むに際
し、予備触媒担体の下流側にリテーナ10を設け、この
リテーナ10とリテーナ支持環11によって予備触媒担
体2を支持する対策が行われていた(図5)。Some of the metal foils constituting the pre-catalyst carrier 2 may not have an insulating film, and some of the contact portions between the flat foil and the corrugated foil may be joined by brazing. In addition, when the pre-catalyst carrier 2 and the main catalyst carrier 3 are disposed in close contact with each other, there is a problem that the pre-catalyst carrier and the main catalyst carrier are conducted to break electrical insulation. Therefore, conventionally, P
CT Publication No. 96/38657 (PCT / JP96 /
As disclosed in US Pat. No. 01474), when such a pre-catalyst carrier that is weak against shearing force is incorporated into the catalyst device, a retainer 10 is provided downstream of the pre-catalyst carrier, and the retainer 10 and the retainer support ring 11 Measures have been taken to support the preliminary catalyst carrier 2 (FIG. 5).
【0008】[0008]
【発明が解決しようとする課題】リテーナを用いて予備
触媒担体を保持する従来の方法においては、リテーナを
触媒装置に組み込むための外筒の支持機構、リテーナへ
の予備触媒担体の支持機構などを必要とし、触媒装置の
コスト低減の障害となっていた。In a conventional method for holding a pre-catalyst carrier using a retainer, a support mechanism for an outer cylinder for incorporating the retainer into the catalyst device, a support mechanism for the pre-catalyst carrier on the retainer, and the like are provided. This necessitates a reduction in the cost of the catalyst device.
【0009】本発明は、予備触媒担体と主触媒担体とを
密着して配置することを可能にし、これらの問題を解決
することを目的とする。An object of the present invention is to make it possible to arrange a preliminary catalyst carrier and a main catalyst carrier in close contact with each other and to solve these problems.
【0010】[0010]
【課題を解決するための手段】本発明は、上記課題を解
決するためになされたものであり、その要旨とするとこ
ろは以下のとおりである。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and the gist thereof is as follows.
【0011】その第1は、表面に酸化皮膜を有する金属
箔を積層して形成した通電加熱予備触媒担体と、該予備
触媒担体の排気ガス下流側に金属箔を積層して形成した
通電加熱を行わない主触媒担体とを有する内燃機関の排
気ガス浄化用電気加熱触媒装置において、前記予備触媒
担体を構成する金属箔は少なくとも主触媒担体と接する
側の表面に酸化皮膜を有してなり、前記予備触媒担体と
前記主触媒担体とを空間を設けずに配設してなることを
特徴とする電気加熱触媒装置である。[0011] First, a current-carrying pre-catalyst carrier formed by laminating a metal foil having an oxide film on its surface, and a current-carrying heating formed by laminating a metal foil downstream of the pre-catalyst carrier on the exhaust gas side. In the electric heating catalyst device for purifying exhaust gas of an internal combustion engine having a main catalyst carrier that is not performed, the metal foil constituting the preliminary catalyst carrier has an oxide film on at least a surface in contact with the main catalyst carrier, An electric heating catalyst device wherein a preliminary catalyst carrier and the main catalyst carrier are arranged without providing a space.
【0012】予備触媒担体を構成する金属箔の少なくと
も主触媒担体と接する側の表面に酸化皮膜を有している
ため、主触媒担体との間に空間を設けずに配設しても絶
縁は破壊されず、予備触媒担体の電流流路が確保され
る。リテーナ等の複雑な支持機構が不要となり、触媒装
置のコストを低減することができる。Since the metal foil constituting the pre-catalyst carrier has an oxide film on at least the surface in contact with the main catalyst carrier, even if it is arranged without providing a space between the metal foil and the main catalyst carrier, the insulation is maintained. It is not destroyed, and the current flow path of the preliminary catalyst carrier is secured. A complicated support mechanism such as a retainer is not required, and the cost of the catalyst device can be reduced.
【0013】その第2は、表面に酸化皮膜を有する金属
箔を積層して形成した通電加熱予備触媒担体と、該予備
触媒担体の排気ガス下流側に金属箔を積層して形成した
通電加熱を行わない主触媒担体とを有する内燃機関の排
気ガス浄化用電気加熱触媒装置において、前記予備触媒
担体の下流端面、主触媒担体の上流端面の少なくとも一
方に絶縁性のセラミックス接着剤を塗布してなり、前記
予備触媒担体、該セラミックス接着剤層と前記主触媒担
体とを該順序で空間を設けずに配設してなることを特徴
とする電気加熱触媒装置である。The second is an energization heating pre-catalyst carrier formed by laminating a metal foil having an oxide film on the surface, and an energization heating formed by laminating the metal foil downstream of the pre-catalyst carrier on the exhaust gas side. In the electric heating catalyst device for purifying exhaust gas of an internal combustion engine having a main catalyst carrier which is not performed, at least one of a downstream end surface of the preliminary catalyst carrier and an upstream end surface of the main catalyst carrier is coated with an insulating ceramic adhesive. An electric heating catalyst device, wherein the preliminary catalyst carrier, the ceramic adhesive layer and the main catalyst carrier are arranged in this order without providing a space.
【0014】第1の発明は、予備触媒担体に印加する電
圧が20V以下であれば問題なく使用することができる
が、印加電圧が20Vを超えて高くなると予備触媒担体
を構成する箔の酸化皮膜が破壊されて絶縁不良を起すこ
とがある。第2の発明によれば、予備触媒担体と主触媒
担体との間に設けた絶縁性のセラミックス接着剤層1
は、十分な絶縁抵抗を持たせることが可能なので、印加
電圧が20Vを超える場合においても予備触媒担体と主
触媒担体とを密着して配置することが可能となった。The first invention can be used without any problem if the voltage applied to the pre-catalyst carrier is 20 V or less. However, if the applied voltage is higher than 20 V, the oxide film of the foil constituting the pre-catalyst carrier can be used. May be destroyed, resulting in poor insulation. According to the second invention, the insulating ceramic adhesive layer 1 provided between the preliminary catalyst carrier and the main catalyst carrier
Can provide sufficient insulation resistance, so that even when the applied voltage exceeds 20 V, the preliminary catalyst carrier and the main catalyst carrier can be closely arranged.
【0015】[0015]
【発明の実施の形態】本発明による通電加熱予備触媒担
体2は、予め表面に絶縁皮膜を形成した金属波箔4と金
属平箔5を重ねて中心電極6の周りに巻き回し、中心部
側から外周部にかけて巻き回した波箔4と平箔5にそれ
ぞれ沿った電流路を形成しながら円筒形に形成したもの
である。また、主触媒担体3は、金属波箔と金属平箔と
を重ねて巻き回し、該波箔と平箔との接触部を接合して
円筒形に形成したものである。本第1の発明においては
予備触媒担体2と主触媒担体3との間の電気的絶縁は、
予備触媒担体2を構成する波箔4と平箔5の表面の絶縁
皮膜によって行われる。絶縁皮膜は、波箔及び平箔を大
気中で高温加熱することで酸化膜を形成し、この酸化膜
を絶縁皮膜として使用することができる。酸化膜厚み
は、0.5μm以上であれば本発明の絶縁皮膜として有
効である。金属箔の表面に形成した酸化膜は、その一部
は除去することが可能であるが、少なくとも主触媒担体
と接する側の表面の酸化膜は、主触媒担体との電気絶縁
性保持のために確保することが必要である。BEST MODE FOR CARRYING OUT THE INVENTION A current-carrying pre-catalyst carrier 2 according to the present invention is obtained by laminating a metal corrugated foil 4 and a metal flat foil 5 each having an insulating film formed on the surface thereof in advance and winding them around a center electrode 6 so as to form a center side. It is formed in a cylindrical shape while forming current paths along the corrugated foil 4 and the flat foil 5 wound from the outer periphery to the outer periphery. The main catalyst carrier 3 is formed by laminating a metal corrugated foil and a metal flat foil, winding the same, and joining a contact portion between the corrugated foil and the flat foil to form a cylindrical shape. In the first invention, the electrical insulation between the preliminary catalyst carrier 2 and the main catalyst carrier 3 is as follows:
This is performed by the insulating film on the surface of the corrugated foil 4 and the flat foil 5 constituting the preliminary catalyst carrier 2. The insulating film forms an oxide film by heating the corrugated foil and the flat foil at a high temperature in the air, and this oxide film can be used as the insulating film. If the thickness of the oxide film is 0.5 μm or more, it is effective as the insulating film of the present invention. The oxide film formed on the surface of the metal foil can be partially removed, but at least the oxide film on the surface in contact with the main catalyst carrier is used for maintaining electrical insulation with the main catalyst carrier. It is necessary to secure.
【0016】本第2の発明において、予備触媒担体2の
下流端面、主触媒担体3の上流端面の少なくとも一方に
絶縁性のセラミックス接着剤を塗布する手段としては、
図3に示すようにペースト状の絶縁性セラミックス接着
剤13を充たした容器の液面に接着剤を塗布すべき触媒
担体端面を浅く浸して接着剤を塗布する方法、ペースト
状の絶縁性セラミックス接着剤を刷毛やスプレーで塗布
する方法を用いることができる。ペースト状のセラミッ
クス接着剤の粘性を調整することにより、触媒担体の端
面に付着する接着剤の量を調整することができる。In the second invention, means for applying an insulating ceramic adhesive to at least one of the downstream end face of the preliminary catalyst carrier 2 and the upstream end face of the main catalyst carrier 3 includes:
As shown in FIG. 3, a method in which the end surface of the catalyst carrier to be coated with the adhesive is shallowly immersed in the liquid surface of a container filled with the paste-like insulating ceramic adhesive 13 and the adhesive is applied, A method of applying the agent by brush or spray can be used. By adjusting the viscosity of the paste-like ceramic adhesive, the amount of the adhesive adhering to the end surface of the catalyst carrier can be adjusted.
【0017】触媒担体の端面に付着した接着剤は、自ら
の表面張力によって図4(b)に示す断面形状を有し、
乾燥により溶剤である水が蒸発することによって強固な
絶縁性のセラミックス接着剤層1を形成することができ
る。The adhesive adhered to the end face of the catalyst carrier has a sectional shape shown in FIG.
The strong insulating ceramic adhesive layer 1 can be formed by evaporating water as a solvent by drying.
【0018】絶縁性のセラミックス接着剤としては、接
着剤の熱膨張率が金属箔の熱膨張率(14×10-6/
℃)に近くて、熱応力により剥離しにくいものが好適で
あり、シリカ系、シリカ・アルミナ系の接着剤を用いる
ことができる。シリカ系接着剤としては、例えば商品名
「アロンセラミックC」があり、主成分(骨材)はシリ
カ、結合剤はアルカリ金属シリケート、耐熱温度120
0℃、熱膨張率13×10-6/℃であり、触媒担体の端
面への塗布厚みは10〜200μmが適切である。シリ
カ・アルミナ系接着剤としては、例えば商品名「スミセ
ラムS−208C」があり、主成分はシリカ・アルミ
ナ、結合剤はリン酸金属塩、耐熱温度1600℃、熱膨
張率11×10-6/℃である。As the insulating ceramic adhesive, the coefficient of thermal expansion of the adhesive is the coefficient of thermal expansion of the metal foil (14 × 10 −6 /
C.), which is difficult to peel off due to thermal stress, and a silica-based or silica-alumina-based adhesive can be used. As the silica-based adhesive, for example, there is a product name “Aron Ceramic C”, the main component (aggregate) is silica, the binder is an alkali metal silicate,
The temperature is 0 ° C., the coefficient of thermal expansion is 13 × 10 −6 / ° C., and the coating thickness on the end face of the catalyst carrier is suitably from 10 to 200 μm. As the silica-alumina adhesive, for example, there is a trade name "Sumiceram S-208C", the main component is silica-alumina, the binder is a metal phosphate, the heat-resistant temperature is 1600 ° C, and the thermal expansion coefficient is 11 × 10 -6 / ° C.
【0019】[0019]
【実施例】(実施例1)予備触媒担体2は、厚み30μ
m、幅10mmのアルミニウム含有ステンレス鋼平箔
と、該平箔をコルゲート加工した波箔とを用いて製造し
た。金属箔は、大気雰囲気酸化炉を通過させることによ
り、またはルーズにコイル状に巻いた金属箔を大気酸化
炉内に高温で保持することにより、表面に絶縁皮膜とし
て0.7μm厚みの酸化膜を形成した。大気酸化炉の雰
囲気温度は1200℃、保持時間は30分とし、酸化膜
厚み実績が0.7μmとなるように保持時間を調整し
た。酸化膜形成が完了した該波箔と平箔とを中心電極6
の周りに巻き回して予備触媒担体2を形成した。主触媒
担体3は、厚み30μm、幅100mmのアルミニウム
含有ステンレス鋼平箔と該平箔をコルゲート加工した波
箔とを巻き回し、該平箔と波箔との接触部をろう付け接
合することによって形成した。前記予備触媒担体2と主
触媒担体3とを相互の間に空間を設けずに配設し、その
外側に外筒8を設けることによって、図1に示す電気加
熱触媒装置を製造した。(Example 1) The preliminary catalyst carrier 2 has a thickness of 30 μm.
It was manufactured using aluminum-containing stainless steel flat foil having a width of 10 mm and a width of 10 mm, and corrugated corrugated foil. By passing the metal foil through an air atmosphere oxidation furnace, or by holding a loosely coiled metal foil at a high temperature in an air oxidation furnace, a 0.7 μm thick oxide film as an insulating film is formed on the surface. Formed. The atmosphere temperature of the atmospheric oxidation furnace was 1200 ° C., the holding time was 30 minutes, and the holding time was adjusted so that the actual oxide film thickness was 0.7 μm. The corrugated foil and the flat foil on which the oxide film formation is completed are
To form a preliminary catalyst carrier 2. The main catalyst carrier 3 is formed by winding an aluminum-containing stainless steel flat foil having a thickness of 30 μm and a width of 100 mm and a corrugated corrugated foil, and brazing the contact portion between the flat foil and the corrugated foil. Formed. By providing the preliminary catalyst carrier 2 and the main catalyst carrier 3 without providing any space between them, and providing the outer cylinder 8 outside thereof, the electric heating catalyst device shown in FIG. 1 was manufactured.
【0020】この電気加熱触媒装置を自動車の排気ガス
系統に配置し、エンジン始動時に予備触媒担体2の外部
電極9と外筒8との間に12Vのバッテリー電圧を印加
したところ、予備触媒担体2の加熱によって迅速な触媒
の昇温と排気ガスの浄化を行うことができた。排気量2
000ccのエンジンで排気ガス温度100〜900℃
の熱サイクル試験を行った結果、予備触媒担体2のテレ
スコープ状のずれや通電加熱機能の低下も認められなか
った。浄化性能については、従来のリテーナ方式と比較
し、予備触媒担体の昇温は主触媒担体への熱伝導がある
ためやや遅れるが、排気ガスを介した熱伝達による主触
媒担体の昇温が速くなり、浄化性能は従来のリテーナ方
式よりも向上した。When the electric heating catalyst device is arranged in an exhaust gas system of an automobile and a battery voltage of 12 V is applied between the outer electrode 9 and the outer cylinder 8 of the pre-catalyst carrier 2 at the time of starting the engine, the pre-catalyst carrier 2 As a result, the temperature of the catalyst was quickly raised and the exhaust gas was purified. Displacement 2
Exhaust gas temperature 100 ~ 900 ℃ with 000cc engine
As a result of conducting a heat cycle test, no telescope-like displacement of the pre-catalyst carrier 2 and no decrease in the electric heating function were observed. Regarding the purification performance, the temperature rise of the spare catalyst carrier is slightly delayed due to the heat conduction to the main catalyst carrier, but the temperature rise of the main catalyst carrier due to heat transfer through the exhaust gas is faster than that of the conventional retainer system. In other words, the purification performance was improved compared to the conventional retainer system.
【0021】一方、この電気加熱触媒装置の外部電極9
と外筒8との間に24Vの電圧を印加したところ、通電
のオン−オフを繰り返した場合に予備触媒担体と主触媒
担体との間で局部的な絶縁破壊が発生し、本実施例にお
いては24Vの電圧印加は適切ではないことがわかっ
た。On the other hand, the external electrode 9 of the electric heating catalyst device
When a voltage of 24 V is applied between the external catalyst 8 and the outer cylinder 8, a local dielectric breakdown occurs between the auxiliary catalyst carrier and the main catalyst carrier when the energization is repeatedly turned on and off. It was found that applying a voltage of 24 V was not appropriate.
【0022】(実施例2)予備触媒担体2は、実施例1
と同様のアルミニウム含有ステンレス鋼箔を用い、実施
例1と同様に表面に絶縁皮膜として0.7μm厚みの酸
化膜を形成し、該波箔と平箔とを中心電極6の周りに巻
き回して形成した。この予備触媒担体2の下流側端面に
セラミックス接着剤を塗布した。接着剤として、金属箔
の熱膨張率(14×10-6/℃)に近い熱膨張率を有す
るセラミックス接着剤としてアロンセラミックC(商品
名)を選定し、図3に示す方法で予備触媒担体の端面に
図4に示すような厚み30μmのセラミックス接着剤層
1を形成した。主触媒担体としては実施例1と同様のも
のを用いた。予備触媒担体2、セラミックス接着剤層1
と主触媒担体3とをこの順序で空間を設けずに配設し、
その外側に外筒8を設けることによって、図2に示す電
気加熱触媒装置を製造した。(Example 2) The pre-catalyst carrier 2 was prepared as described in Example 1.
Using the same aluminum-containing stainless steel foil as in Example 1, an oxide film having a thickness of 0.7 μm was formed as an insulating film on the surface as in Example 1, and the corrugated foil and flat foil were wound around the center electrode 6. Formed. A ceramic adhesive was applied to the downstream end face of the preliminary catalyst carrier 2. As the adhesive, Aron Ceramic C (trade name) was selected as a ceramic adhesive having a coefficient of thermal expansion close to the coefficient of thermal expansion (14 × 10 −6 / ° C.) of the metal foil. A ceramic adhesive layer 1 having a thickness of 30 μm as shown in FIG. The same main catalyst carrier as in Example 1 was used. Preliminary catalyst carrier 2, ceramic adhesive layer 1
And the main catalyst carrier 3 are arranged in this order without providing a space,
By providing the outer cylinder 8 on the outside, the electric heating catalyst device shown in FIG. 2 was manufactured.
【0023】この電気加熱触媒装置を自動車の排気ガス
系統に配置し、エンジン始動時に予備触媒担体2の外部
電極9と外筒8との間に24Vのバッテリー電圧を印加
したところ、予備触媒担体2と主触媒担体3との間の電
気的絶縁には支障は発生せず、予備触媒担体2の加熱に
よって迅速な触媒の昇温と排気ガスの浄化を行うことが
できた。実施例1と同様に熱サイクル試験における通電
加熱機能の低下は認められなかった。浄化性能について
は、印加電圧を24Vに上げた結果として、実施例1よ
りも更に良好な浄化性能を得ることができた。When the electric heating catalyst device is arranged in an exhaust gas system of an automobile, and a battery voltage of 24 V is applied between the external electrode 9 of the pre-catalyst carrier 2 and the outer cylinder 8 at the time of starting the engine, the pre-catalyst carrier 2 There was no problem in the electrical insulation between the catalyst carrier and the main catalyst carrier 3, and the heating of the preliminary catalyst carrier 2 enabled rapid temperature rise of the catalyst and purification of exhaust gas. As in Example 1, no decrease in the current heating function in the heat cycle test was observed. Regarding the purification performance, as a result of increasing the applied voltage to 24 V, a purification performance even better than that of Example 1 could be obtained.
【0024】[0024]
【発明の効果】表面に酸化皮膜を有する金属箔を積層し
て形成した通電加熱予備触媒担体と、該予備触媒担体の
排気ガス下流側に金属箔を積層して形成した通電加熱を
行わない主触媒担体とを有する内燃機関の排気ガス浄化
用電気加熱触媒装置において、前記予備触媒担体を構成
する金属箔のすべての表面に酸化皮膜を形成し、前記予
備触媒担体と前記主触媒担体とを空間を設けずに配設す
ることにより、リテーナを不要とすることができ、通電
加熱触媒装置の製造コストの低減を図るとともに浄化性
能の向上を実現することができた。更に、予備触媒担体
の下流端面、主触媒担体の上流端面の少なくとも一方に
絶縁性のセラミックス接着剤を塗布することにより、予
備触媒担体と主触媒担体との間の電気絶縁性をより良好
にし、予備触媒担体の印加電圧を高めることができた。According to the present invention, a current-carrying pre-catalyst carrier formed by laminating a metal foil having an oxide film on the surface and a current-carrying pre-catalyst formed by laminating a metal foil downstream of the pre-catalyst carrier on the exhaust gas side are not used. In the electric heating catalyst device for purifying exhaust gas of an internal combustion engine having a catalyst carrier, an oxide film is formed on all surfaces of a metal foil constituting the preliminary catalyst carrier, and the preliminary catalyst carrier and the main catalyst carrier are separated by a space. By arranging the heating device without providing the same, the need for a retainer can be eliminated, and the production cost of the electrically heated catalyst device can be reduced, and the purification performance can be improved. Furthermore, by applying an insulating ceramic adhesive to at least one of the downstream end face of the preliminary catalyst carrier and the upstream end face of the main catalyst carrier, the electrical insulation between the preliminary catalyst carrier and the main catalyst carrier is further improved, The voltage applied to the preliminary catalyst carrier could be increased.
【図1】本発明の電気加熱触媒装置を示す断面図であ
る。FIG. 1 is a sectional view showing an electric heating catalyst device of the present invention.
【図2】本発明の電気加熱触媒装置を示す断面図であ
る。FIG. 2 is a cross-sectional view showing an electric heating catalyst device of the present invention.
【図3】本発明の絶縁性のセラミックス接着剤を塗布す
る方法を示す概略図である。FIG. 3 is a schematic view showing a method for applying an insulating ceramic adhesive according to the present invention.
【図4】本発明のセラミックス接着剤層を有する予備触
媒担体の断面図であり、(a)は全体図、(b)は部分
詳細断面図である。FIGS. 4A and 4B are cross-sectional views of a pre-catalyst carrier having a ceramic adhesive layer according to the present invention, wherein FIG. 4A is an overall view and FIG.
【図5】従来の電気加熱触媒装置を示す図であり、
(a)は断面図、(b)は分解斜視図である。FIG. 5 is a view showing a conventional electric heating catalyst device;
(A) is a sectional view, and (b) is an exploded perspective view.
【図6】予備触媒担体の波箔と平箔との積層状況を示す
部分断面図である。FIG. 6 is a partial cross-sectional view showing a laminated state of a corrugated foil and a flat foil of a preliminary catalyst carrier.
1 セラミックス接着剤層 2 予備触媒担体 3 主触媒担体 4 波箔 5 平箔 6 中心電極 8 外筒 9 外部電極 10 リテーナ 11 リテーナ支持環 13 セラミックス接着剤 REFERENCE SIGNS LIST 1 ceramic adhesive layer 2 preliminary catalyst carrier 3 main catalyst carrier 4 corrugated foil 5 flat foil 6 center electrode 8 outer cylinder 9 external electrode 10 retainer 11 retainer support ring 13 ceramic adhesive
Claims (2)
て形成した通電加熱予備触媒担体と、該予備触媒担体の
排気ガス下流側に金属箔を積層して形成した通電加熱を
行わない主触媒担体とを有する内燃機関の排気ガス浄化
用電気加熱触媒装置において、前記予備触媒担体を構成
する金属箔は少なくとも主触媒担体と接する側の表面に
酸化皮膜を有してなり、前記予備触媒担体と前記主触媒
担体とを空間を設けずに配設してなることを特徴とする
電気加熱触媒装置。An electrically heated pre-catalyst carrier formed by laminating a metal foil having an oxide film on its surface, and a main body that is formed by laminating a metal foil downstream of the pre-catalyst carrier on the exhaust gas side and is not electrically heated. An electric heating catalyst device for purifying exhaust gas of an internal combustion engine having a catalyst carrier, wherein the metal foil constituting the preliminary catalyst carrier has an oxide film on at least a surface in contact with the main catalyst carrier, And the main catalyst carrier are arranged without providing a space.
て形成した通電加熱予備触媒担体と、該予備触媒担体の
排気ガス下流側に金属箔を積層して形成した通電加熱を
行わない主触媒担体とを有する内燃機関の排気ガス浄化
用電気加熱触媒装置において、前記予備触媒担体の下流
端面、主触媒担体の上流端面の少なくとも一方に絶縁性
のセラミックス接着剤を塗布してなり、前記予備触媒担
体、該セラミックス接着剤層と前記主触媒担体とを該順
序で空間を設けずに配設してなることを特徴とする電気
加熱触媒装置。2. A current-carrying pre-catalyst carrier formed by laminating a metal foil having an oxide film on the surface, and a current-carrying pre-catalyst formed by laminating a metal foil downstream of the pre-catalyst carrier on the exhaust gas side. An electric heating catalyst device for purifying exhaust gas of an internal combustion engine having a catalyst carrier, wherein at least one of a downstream end face of the preliminary catalyst carrier and an upstream end face of the main catalyst carrier is coated with an insulating ceramic adhesive, An electric heating catalyst device comprising a catalyst carrier, the ceramic adhesive layer and the main catalyst carrier arranged in this order without providing a space.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9357818A JPH11179157A (en) | 1997-12-25 | 1997-12-25 | Electric heating catalytic apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9357818A JPH11179157A (en) | 1997-12-25 | 1997-12-25 | Electric heating catalytic apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11179157A true JPH11179157A (en) | 1999-07-06 |
Family
ID=18456086
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9357818A Withdrawn JPH11179157A (en) | 1997-12-25 | 1997-12-25 | Electric heating catalytic apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11179157A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002248357A (en) * | 2001-02-27 | 2002-09-03 | Satoru Igarashi | Method for manufacturing plate type catalyst and plate type catalyst |
WO2022019108A1 (en) | 2020-07-20 | 2022-01-27 | 株式会社キャタラー | Exhaust gas purification catalyst system |
-
1997
- 1997-12-25 JP JP9357818A patent/JPH11179157A/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002248357A (en) * | 2001-02-27 | 2002-09-03 | Satoru Igarashi | Method for manufacturing plate type catalyst and plate type catalyst |
JP4650858B2 (en) * | 2001-02-27 | 2011-03-16 | 哲 五十嵐 | Method for producing plate-type catalyst and plate-type catalyst |
WO2022019108A1 (en) | 2020-07-20 | 2022-01-27 | 株式会社キャタラー | Exhaust gas purification catalyst system |
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