JPH06254403A - Exhaust gas purification device - Google Patents
Exhaust gas purification deviceInfo
- Publication number
- JPH06254403A JPH06254403A JP5038841A JP3884193A JPH06254403A JP H06254403 A JPH06254403 A JP H06254403A JP 5038841 A JP5038841 A JP 5038841A JP 3884193 A JP3884193 A JP 3884193A JP H06254403 A JPH06254403 A JP H06254403A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- catalyst
- pipe
- heat storage
- gas purifying
- 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
Links
- 238000000746 purification Methods 0.000 title abstract description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 83
- 238000005338 heat storage Methods 0.000 claims description 40
- 239000011232 storage material Substances 0.000 claims description 34
- 229910052751 metal Inorganic materials 0.000 claims description 17
- 239000002184 metal Substances 0.000 claims description 17
- 229910001220 stainless steel Inorganic materials 0.000 claims description 10
- 239000010935 stainless steel Substances 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 abstract description 7
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052782 aluminium Inorganic materials 0.000 abstract description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 5
- 230000002093 peripheral effect Effects 0.000 abstract description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 2
- GPNDARIEYHPYAY-UHFFFAOYSA-N palladium(ii) nitrate Chemical compound [Pd+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O GPNDARIEYHPYAY-UHFFFAOYSA-N 0.000 abstract description 2
- 238000004904 shortening Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 12
- 238000001816 cooling Methods 0.000 description 5
- 230000000630 rising effect Effects 0.000 description 5
- 230000001965 increasing effect Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 101150065537 SUS4 gene Proteins 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Exhaust Gas After Treatment (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、排ガス浄化触媒に係
り、特に自動車排気ガスをはじめ、各種産業、例えば化
学プラント等から排出される排ガス中の各種炭化水素、
一酸化炭素等燃焼可能な有害物質を除去するための排ガ
ス浄化触媒に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying catalyst, and particularly to various kinds of hydrocarbons in exhaust gas discharged from various industries such as automobile exhaust gas, for example, chemical plants.
The present invention relates to an exhaust gas purifying catalyst for removing combustible harmful substances such as carbon monoxide.
【0002】[0002]
【従来の技術】近年、自動車の排ガス規制はますます強
くなっており、排ガス浄化触媒の性能の向上が強く求め
られている。内燃機関を動力源とする自動車の排ガス浄
化触媒としては、例えばセラミックハニカム触媒が知ら
れている。ところで、自動車や発電機のようにコールド
スタートを避けることができない機関は、エンジンの温
度が運転開始から燃料の着火温度に到達するまでの間、
前記エンジンに供給された燃料は不完全燃焼し易い。ま
た、排ガス浄化触媒が十分な高温に到達していないの
で、触媒を通過する排ガスは実質的に処理されずに大気
に放出されることになる。従ってこのようなコールドス
タートする機関では、起動時に多量の未燃有害成分が排
出され易くなる。この傾向は排ガス浄化触媒として熱伝
導率が低いセラミックハニカム触媒を用いた場合にさら
に強くなる。2. Description of the Related Art In recent years, exhaust gas regulations of automobiles have become more and more strict, and improvement in performance of exhaust gas purifying catalysts has been strongly demanded. A ceramic honeycomb catalyst is known as an exhaust gas purifying catalyst for an automobile using an internal combustion engine as a power source, for example. By the way, in the case of engines such as automobiles and generators where cold start is unavoidable, the temperature of the engine can be increased from the start of operation to the ignition temperature of fuel.
The fuel supplied to the engine is prone to incomplete combustion. Moreover, since the exhaust gas purifying catalyst has not reached a sufficiently high temperature, the exhaust gas passing through the catalyst is discharged to the atmosphere without being substantially processed. Therefore, in such a cold-start engine, a large amount of unburned harmful components are easily discharged at the time of startup. This tendency becomes even stronger when a ceramic honeycomb catalyst having a low thermal conductivity is used as the exhaust gas purifying catalyst.
【0003】一方、このような弊害を防止するために、
熱伝導率が高い金属ハニカム触媒が開発されている。図
3は、従来の金属ハニカム触媒の斜視図である。図にお
いて、波状の金属板と平板状の金属板とを重合わせて渦
巻き状に巻いたハニカム触媒担体に触媒成分を担持した
金属ハニカム触媒が示されている。このような金属ハニ
カム触媒は熱伝導率が高く、起動時から触媒活性が発現
する温度に到達するまでの所要時間が短くなる。またこ
のような金属ハニカム触媒に電極を内蔵した自己発熱可
能な触媒は、運転開始直後の触媒温度を急激に上昇させ
ることによって起動時から触媒活性が発現するまでの所
要時間を著しく短縮することができるので、運転開始直
後の排ガス浄化性能を改善することができるものとして
注目されている。On the other hand, in order to prevent such an adverse effect,
Metal honeycomb catalysts with high thermal conductivity have been developed. FIG. 3 is a perspective view of a conventional metal honeycomb catalyst. In the figure, there is shown a metal honeycomb catalyst in which a catalyst component is carried on a honeycomb catalyst carrier in which a corrugated metal plate and a flat metal plate are superposed and spirally wound. Such a metal honeycomb catalyst has a high thermal conductivity, and the time required from starting to reaching the temperature at which the catalyst activity is exhibited becomes short. In addition, such a self-heatable catalyst in which an electrode is built into the metal honeycomb catalyst can significantly reduce the time required from the start-up to the manifestation of catalytic activity by rapidly increasing the catalyst temperature immediately after the start of operation. Therefore, it is attracting attention as being able to improve the exhaust gas purification performance immediately after the start of operation.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上記金
属ハニカム触媒は、熱伝導率が高いという特性の逆特性
としてエンジン停止後の冷却速度が速いという問題があ
り、一旦停止した後の2度目のエンジン起動時に再びコ
ールトスタート状態となり、起動、停止を繰り返す、例
えば自動車の排ガス浄化触媒としては満足できるもので
はなかった。However, the above-mentioned metallic honeycomb catalyst has a problem that the cooling rate after the engine is stopped is high as a characteristic opposite to the characteristic that the thermal conductivity is high, and therefore the second engine after the engine is stopped once is stopped. At the time of start-up, it becomes a cold start state again, and starts and stops repeatedly. For example, it is not satisfactory as an exhaust gas purifying catalyst for automobiles.
【0005】一方、電極を内蔵した金属ハニカム触媒は
触媒活性が発現するまでの所要時間を短縮するために、
数百アンペアもの電流が必要となり、電気系統およびバ
ッテリの負担が過大になるという問題がある。本発明の
目的は、上記従来技術の問題点を解決し、2度目からの
起動時において、エネルギの補給を要することなく、起
動時から触媒の活性が発現するまでの所要時間を大幅に
短縮し、起動時の排ガス浄化性能を効果的に向上させる
ことができる排ガス浄化触媒を提供することにある。On the other hand, a metal honeycomb catalyst having a built-in electrode is intended to shorten the time required for the catalytic activity to be exhibited.
A current of several hundred amperes is required, and there is a problem that the electric system and the battery are overloaded. An object of the present invention is to solve the above-mentioned problems of the prior art, and to significantly shorten the time required from the start to the activation of the catalyst without the need to replenish energy when starting from the second time. An object of the present invention is to provide an exhaust gas purifying catalyst that can effectively improve the exhaust gas purifying performance at startup.
【0006】[0006]
【課題を解決するための手段】上記目的は、触媒基材の
中心部に蓄熱材を充填するか、または蓄熱効果を有する
材料を充填することによって達成することができる。す
なわち、本願の第1の発明は、波状の金属板と平板状の
金属板とからなるハニカム触媒担体に触媒活性成分を担
持した排ガス浄化触媒において、前記ハニカム触媒担体
の中心部に密閉容器を配置し、該密閉容器内に蓄熱材料
を充填したことを特徴とする排ガス浄化触媒に関する。The above object can be achieved by filling the central portion of the catalyst substrate with a heat storage material or a material having a heat storage effect. That is, the first invention of the present application is an exhaust gas purifying catalyst in which a catalytically active component is supported on a honeycomb catalyst carrier composed of a corrugated metal plate and a flat metal plate, and a hermetically sealed container is arranged at the center of the honeycomb catalyst carrier. The present invention also relates to an exhaust gas purifying catalyst, characterized in that the closed container is filled with a heat storage material.
【0007】第2の発明は、波状のステンレス鋼板と平
板状のステンレス鋼板とを重合わせて渦巻き状に巻いた
ハニカム触媒担体に触媒活性成分を担持した排ガス浄化
触媒において、前記ハニカム触媒担体の中心部に密閉可
能なパイプを配置し、該パイプ内に蓄熱材料を充填した
ことを特徴とする排ガス浄化触媒に関する。A second aspect of the present invention is an exhaust gas purifying catalyst comprising a honeycomb catalyst carrier in which a corrugated stainless steel plate and a flat stainless steel plate are superposed and spirally wound to carry a catalytically active component. The exhaust gas purifying catalyst is characterized in that a pipe that can be sealed is arranged in a portion, and the pipe is filled with a heat storage material.
【0008】[0008]
【作用】金属ハニカム触媒の中心部に蓄熱材料を充填し
て蓄熱機能をもたせることにより、エンジン停止後も高
温が維持され、第2回目からの起動時における触媒の活
性が発現する温度に到達するまでの所要時間が短縮する
ので、例えば自動車エンジンから排出される、未燃分を
大量に含む起動時の排ガスが浄化され易くなる。また、
蓄熱材料を密閉容器内に充填したことにより、該密閉容
器の外側部分が放熱抑制部材として作用するので、より
高い蓄熱効果が得られる。[Function] By filling the central portion of the metal honeycomb catalyst with a heat storage material so as to have a heat storage function, the high temperature is maintained even after the engine is stopped, and the temperature reaches the temperature at which the catalyst activity is exhibited at the time of starting from the second time. Since the time required up to is shortened, it becomes easier to purify the exhaust gas discharged from the automobile engine at the time of startup, which contains a large amount of unburned components. Also,
By filling the heat storage material in the airtight container, the outer portion of the airtight container acts as a heat radiation suppressing member, so that a higher heat storage effect can be obtained.
【0009】本発明において、ハニカム触媒担体の中央
部に配置される密閉容器としては、例えば蓄熱材充填パ
イプが使用されるが、パイプの径は触媒の活性低下を生
じない程度であれば特に限定されない。すなわち触媒活
性が低下する許容範囲を10%程度とすれば、パイプ径
は、触媒の有効断面積の約10%程度とすることができ
る。従って、例えば金属ハニカム触媒の直径を70〜1
00mmとすると、前記蓄熱材充填パイプの許容直径
は、25mm前後となる。In the present invention, for example, a heat storage material-filled pipe is used as the closed container arranged in the central portion of the honeycomb catalyst carrier, but the diameter of the pipe is not particularly limited as long as the activity of the catalyst is not deteriorated. Not done. That is, the pipe diameter can be set to about 10% of the effective cross-sectional area of the catalyst if the allowable range for the catalyst activity to fall is set to about 10%. Therefore, for example, the diameter of the metal honeycomb catalyst is 70 to 1
When the length is 00 mm, the allowable diameter of the heat storage material filled pipe is about 25 mm.
【0010】本発明において蓄熱材料とは、例えば比熱
および比重が大きく、しかも物理的強度の大きいものが
好ましく、例えば、鋳鉄、ジルコニア、サーメット等の
いわゆる蓄熱材が使用される。また、蓄熱効果を高める
材料として、例えば発泡材のように、微小な空間を多数
有する多孔質の材料を使用することもできる。本発明に
おいてハニカム触媒担体は、波状のステンレス鋼薄板と
平板状のステンレス鋼薄板とを組み合わせて渦巻き状に
巻いたものが好適に使用されるが、その構造、例えばセ
ル数、薄板の厚み等は特に限定されない。また金属の種
類もステンレス以外のものであってもよい。また密閉容
器である蓄熱材充填パイプの材質は、前記ハニカム触媒
担体と同種のものを使用することが好ましく、例えば、
ステンレスが使用される。In the present invention, the heat storage material is preferably one having a large specific heat and a large specific gravity and a large physical strength, for example, a so-called heat storage material such as cast iron, zirconia or cermet is used. Further, as a material for enhancing the heat storage effect, a porous material having a large number of minute spaces, such as a foam material, can be used. In the present invention, the honeycomb catalyst carrier is preferably used by spirally winding a corrugated stainless steel thin plate and a flat plate-shaped stainless steel thin plate, and its structure, for example, the number of cells, the thickness of the thin plate, etc. There is no particular limitation. Further, the type of metal may be other than stainless steel. Further, the material of the heat storage material filled pipe which is a closed container, it is preferable to use the same kind of the honeycomb catalyst carrier, for example,
Stainless steel is used.
【0011】本発明において、ハニカム触媒担体に加熱
手段、例えば加熱電極を設けることが好ましい。これに
よって2度目以降の起動時だけでなく、第1回目の起動
時および長期間休止した後の起動時において、触媒活性
が発現するまでの時間を短縮することができる。なお、
本発明において、蓄熱材料を充填する密閉容器、例えば
パイプの径を比較的大きくすることにより、ハニカム触
媒における触媒自身の熱容量を相対的に小さくすること
ができるので、触媒の昇温速度が速くなるという副次的
効果が得られる。また、密閉容器に充填する蓄熱材料の
重量は、全触媒重量の20〜40%程度であることが好
ましく、これによって十分な蓄熱効果が得られる。蓄熱
材料を充填するパイプの直径を、上記したように、触媒
径の25%程度とすれば、例えば蓄熱材として比重6の
ものを密に充填したとしても、その重量は全触媒重量の
20〜40%の範囲内とすることができる。In the present invention, it is preferable to provide the honeycomb catalyst carrier with heating means, for example, a heating electrode. As a result, not only at the second and subsequent startups, but also at the first startup and the startup after a long period of rest, it is possible to shorten the time until the catalytic activity is expressed. In addition,
In the present invention, the heat capacity of the catalyst itself in the honeycomb catalyst can be made relatively small by relatively increasing the diameter of the closed container filled with the heat storage material, for example, the pipe, so that the temperature rising rate of the catalyst becomes faster. The secondary effect is obtained. In addition, the weight of the heat storage material filled in the closed container is preferably about 20 to 40% of the total weight of the catalyst, whereby a sufficient heat storage effect can be obtained. If the diameter of the pipe filled with the heat storage material is about 25% of the catalyst diameter as described above, even if the heat storage material having a specific gravity of 6 is densely packed, the weight of the pipe is 20 to 20% of the total weight of the catalyst. It can be within the range of 40%.
【0012】[0012]
【実施例】次に本発明を実施例によりさらに詳細に説明
する。図1は、本発明の一実施例を示す説明図、図2
は、そのII−II線矢視方向断面図である。この排ガス浄
化触媒が図3の従来技術と異なる点は、渦巻き状の金属
ハニカム触媒本体1の中心部に密閉容器として蓄熱材充
填パイプ2を配置し、該蓄熱材充填パイプ2に蓄熱材3
を充填した点である。EXAMPLES Next, the present invention will be described in more detail by way of examples. 1 is an explanatory view showing an embodiment of the present invention, FIG.
FIG. 11 is a sectional view taken along line II-II of FIG. This exhaust gas purifying catalyst is different from the conventional technique of FIG. 3 in that a heat storage material filling pipe 2 is arranged as a closed container in the center of a spiral metal honeycomb catalyst body 1, and the heat storage material 3 is placed in the heat storage material filling pipe 2.
Is the point filled.
【0013】実施例1 直径25mm、肉厚0.5mm、長さ130mmのSU
S304製の蓄熱材充填パイプ2に、両面にアルミニウ
ムを溶射した厚さ0.2mm、幅100mmのSUS4
30製の平板4の一端をろう付けし、次いで前記蓄熱材
充填パイプ2と平板4との間に、エキスパンド加工した
後、アルミニウムを溶射し、コルゲート加工して山谷高
さを約2.5mmとした、厚さ0.2mm、幅100m
mのSUS430製の波板5を巻き込んで、渦巻き状に
巻き、最外周を平板4どうしが重なるようにろう付けし
て直径80mm、長さ100mmのハニカム構造体とし
た。なお、このハニカム構造体の見かけ容積は470m
lである。次にこのハニカム構造体を一旦800℃で熱
処理してアルミニウム溶射層を酸化物化した後、活性ア
ルミナをウオッシュコートし、その後550℃で焼成し
た。その後、硝酸パラジウム水溶液に浸漬してパラジウ
ム含有量が約1g/lになるように調製し、乾燥した
後、最終的に再度550℃で焼成した。次いで中心部の
蓄熱材充填パイプ2に蓄熱材として直径1mmのジルコ
ニアボールを充填し、その後、該パイプ2の両端をSU
S304製の蓋でろう付けして排ガス浄化触媒とした。Example 1 SU having a diameter of 25 mm, a wall thickness of 0.5 mm and a length of 130 mm
A heat storage material filled pipe 2 made of S304, SUS4 having a thickness of 0.2 mm and a width of 100 mm formed by spraying aluminum on both surfaces.
One end of a flat plate 4 made of 30 is brazed and then expanded between the heat storage material filled pipe 2 and the flat plate 4 and then sprayed with aluminum and corrugated to a height of about 2.5 mm. Thickness 0.2mm, width 100m
m corrugated sheet 5 made of SUS430 was wound, wound in a spiral shape, and brazed so that the outermost circumferences of the flat plates 4 overlap each other to obtain a honeycomb structure having a diameter of 80 mm and a length of 100 mm. The apparent volume of this honeycomb structure is 470 m.
It is l. Next, this honeycomb structure was once heat-treated at 800 ° C. to oxide the aluminum sprayed layer, wash-coated with activated alumina, and then fired at 550 ° C. Then, it was immersed in an aqueous solution of palladium nitrate to prepare a palladium content of about 1 g / l, dried, and finally calcined again at 550 ° C. Then, a zirconia ball having a diameter of 1 mm is filled as a heat storage material into the heat storage material-filled pipe 2 in the central portion, and then both ends of the pipe 2 are SU
The exhaust gas purifying catalyst was brazed with an S304 lid.
【0014】本実施例によれば、中心部に蓄熱材3を充
填したパイプ2を配置したことにより、蓄熱効果が得ら
れ、例えば自動車のエンジンを停止した後の冷却時にお
ける温度低下を小さくすることができるので、再起動時
の排ガス浄化率が向上する。またエンジン停止後の冷却
時における触媒への水分の付着を防止することができる
ので、再起動時に水分の蒸発に伴う潜熱による熱量損失
を回避することができる。According to the present embodiment, the pipe 2 filled with the heat storage material 3 is arranged in the central portion, so that the heat storage effect is obtained and, for example, the temperature drop during cooling after the engine of the automobile is stopped is reduced. Therefore, the exhaust gas purification rate at the time of restart is improved. Further, since it is possible to prevent moisture from adhering to the catalyst during cooling after the engine is stopped, it is possible to avoid heat loss due to latent heat due to evaporation of moisture during restart.
【0015】実施例2 排ガス浄化触媒の外周部の平板4に通電用電極として厚
さ1mmのSUS430からなる平板を溶接した以外は
前記実施例1と同様にして排ガス浄化触媒を構成した。
この排ガス浄化触媒は、中心部の蓄熱材充填パイプ2と
前記外周部の電極との間に電流を通して発熱させること
ができる。両電極間の電気抵抗は0.07Ωであった。Example 2 An exhaust gas purifying catalyst was constructed in the same manner as in Example 1 except that a flat plate made of SUS430 having a thickness of 1 mm was welded to the flat plate 4 on the outer peripheral portion of the exhaust gas purifying catalyst as an energizing electrode.
The exhaust gas purifying catalyst can generate heat by passing an electric current between the heat storage material filled pipe 2 in the central portion and the electrode in the outer peripheral portion. The electric resistance between both electrodes was 0.07Ω.
【0016】本実施例によれば、通電用電極を設けた排
ガス浄化触媒の中心部に蓄熱材を充填したことにより、
起動時から触媒活性が発現するまでの昇温時間を著しく
短縮することができる。昇温時間の短縮はそのまま電力
使用量の低減につながり、バッテリおよび電気系統への
負担を軽減することができる。また本実施例によれば、
触媒中心部に配置した蓄熱材充填パイプ2の径を比較的
大きくしたことにより、従来の通電型触媒でみられたよ
うな、発熱と放熱とのアンバランスに起因する触媒中心
部と外周部との温度差が極めて小さくなり、通電時の触
媒温度は半径方向で均一になり易くなる。従って、触媒
性能が均一に発揮され、排ガス浄化率が向上する。According to the present embodiment, the exhaust gas purifying catalyst provided with the current-carrying electrode is filled with the heat storage material in the central portion,
It is possible to remarkably shorten the temperature rising time from the start-up to the manifestation of catalytic activity. The shortening of the temperature raising time directly leads to the reduction of the amount of electric power used, and the burden on the battery and the electric system can be reduced. Further, according to this embodiment,
By relatively increasing the diameter of the heat storage material-filled pipe 2 arranged in the center of the catalyst, the catalyst center and the outer periphery due to the imbalance between heat generation and heat radiation, as seen in the conventional energization type catalyst, are formed. The temperature difference is extremely small, and the catalyst temperature during energization tends to be uniform in the radial direction. Therefore, the catalyst performance is uniformly exhibited, and the exhaust gas purification rate is improved.
【0017】比較例1 中心部の蓄熱材充填パイプ2に蓄熱材を充填しなかった
以外は上記実施例1と同様にして排ガス浄化触媒を構成
した。実施例1、2および比較例1の排ガス浄化触媒を
それぞれ自動車エンジンの排ガスラインに接続し、一定
の条件で30分間運転し、次いでエンジンを停止し、3
0分後に再び同様の条件でエンジンを起動して排ガス浄
化触媒の昇温冷却曲線を求めた。ただし、実施例2の排
ガス浄化触媒の性能試験においては、エンジン起動と同
時に両電極間に12Vの電圧を30秒間負荷させて触媒
を加熱した。Comparative Example 1 An exhaust gas purifying catalyst was constructed in the same manner as in Example 1 except that the heat storage material-filled pipe 2 in the central portion was not filled with the heat storage material. The exhaust gas purifying catalysts of Examples 1 and 2 and Comparative Example 1 were each connected to an exhaust gas line of an automobile engine, operated for 30 minutes under a constant condition, and then the engine was stopped.
After 0 minutes, the engine was started again under the same conditions, and the temperature rising / cooling curve of the exhaust gas purifying catalyst was obtained. However, in the performance test of the exhaust gas purifying catalyst of Example 2, a voltage of 12 V was applied between both electrodes for 30 seconds at the same time when the engine was started to heat the catalyst.
【0018】試験結果を図4に示す。図4において、実
施例1および2は、比較例1に較べてエンジン停止後の
冷却速度が遅く、またエンジン再起動後の昇温速度が速
いこと、特に実施例2の昇温速度が著しく速いことが分
かる。通常の排ガス浄化用三元触媒の活性が発現する温
度は250〜400℃であることから、本実施例の排ガ
ス浄化触媒は、2回目からの起動時において触媒活性が
発現する温度に到達するまでの所要時間を従来技術の1
/2〜1/4に短縮することができる。The test results are shown in FIG. 4, in Examples 1 and 2, the cooling rate after the engine is stopped is slower than that in Comparative Example 1, and the temperature rising rate after the engine is restarted is high. Particularly, the temperature rising rate in Example 2 is remarkably high. I understand. Since the temperature at which the activity of a normal three-way catalyst for exhaust gas purification is expressed is 250 to 400 ° C., the exhaust gas purification catalyst of the present example until the temperature at which the catalytic activity is expressed is reached at the time of starting from the second time. The time required for
It can be shortened to / 2-1 / 4.
【0019】[0019]
【発明の効果】本願の請求項1記載の発明によれば、排
ガス浄化触媒の中心部に蓄熱材を充填した密閉容器を配
置したことにより、起動停止を繰り返す装置において、
2回目からの起動時における触媒活性が発現するまでの
所要時間を大幅に短縮することができるので、運転開始
初期の排ガス浄化性能を向上させることができる。According to the invention described in claim 1 of the present application, in the apparatus in which the start and stop is repeated by disposing the closed container filled with the heat storage material in the center of the exhaust gas purifying catalyst,
Since the time required for the catalyst activity to appear at the second and subsequent startups can be significantly shortened, the exhaust gas purification performance at the initial stage of operation can be improved.
【0020】本願の請求項2記載の発明によれば、波状
のステンレス鋼薄板と平板状のステンレス鋼薄板とから
なるハニカム触媒担体に触媒活性成分を担持した排ガス
浄化触媒の中心部に蓄熱材充填パイプを配置し、該パイ
プ内に蓄熱材料を充填したことにより、起動停止を繰り
返す装置、例えば自動車エンジンの2回目からの起動時
における運転開始初期の排ガス浄化性能を向上させるこ
とができる。According to the invention of claim 2 of the present application, the heat storage material is filled in the central portion of the exhaust gas purifying catalyst in which the catalytically active component is carried on the honeycomb catalyst carrier composed of the corrugated stainless steel thin plate and the flat plate-shaped stainless steel thin plate. By disposing the pipe and filling the heat storage material in the pipe, it is possible to improve the exhaust gas purification performance at the beginning of the operation at the time of starting the device that repeats the start and stop, for example, the automobile engine from the second time.
【図1】本発明の一実施例を示す排ガス浄化触媒の説明
図。FIG. 1 is an explanatory diagram of an exhaust gas purifying catalyst showing an embodiment of the present invention.
【図2】図1のII−II線矢視方向断面図。FIG. 2 is a sectional view taken along the line II-II of FIG.
【図3】従来技術を示す斜視図。FIG. 3 is a perspective view showing a conventional technique.
【図4】排ガス浄化触媒の性能試験の結果を示す図。FIG. 4 is a view showing a result of a performance test of an exhaust gas purifying catalyst.
1…金属ハニカム触媒本体、2…蓄熱材充填パイプ、3
…蓄熱材、4…平板、5…波板。1 ... Metal honeycomb catalyst body, 2 ... Heat storage material filling pipe, 3
... Heat storage material, 4 ... Flat plate, 5 ... Corrugated plate.
Claims (2)
るハニカム触媒担体に触媒活性成分を担持した排ガス浄
化触媒において、前記ハニカム触媒担体の中心部に密閉
容器を配置し、該密閉容器内に蓄熱材料を充填したこと
を特徴とする排ガス浄化触媒。1. An exhaust gas purifying catalyst comprising a catalytically active component supported on a honeycomb catalyst carrier comprising a corrugated metal plate and a flat metal plate, wherein a hermetically sealed container is arranged at the center of the honeycomb catalyst carrier. An exhaust gas purifying catalyst having a heat storage material filled therein.
レス鋼板とを重合わせて渦巻き状に巻いたハニカム触媒
担体に触媒活性成分を担持した排ガス浄化触媒におい
て、前記ハニカム触媒担体の中心部に密閉可能なパイプ
を配置し、該パイプ内に蓄熱材料を充填したことを特徴
とする排ガス浄化触媒。2. An exhaust gas purifying catalyst in which a catalytically active component is supported on a honeycomb catalyst carrier, which is formed by superposing a corrugated stainless steel plate and a flat stainless steel plate and wound in a spiral shape, and can be hermetically sealed at the center of the honeycomb catalyst carrier. An exhaust gas purifying catalyst, characterized in that a simple pipe is arranged and a heat storage material is filled in the pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5038841A JPH06254403A (en) | 1993-02-26 | 1993-02-26 | Exhaust gas purification device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5038841A JPH06254403A (en) | 1993-02-26 | 1993-02-26 | Exhaust gas purification device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06254403A true JPH06254403A (en) | 1994-09-13 |
Family
ID=12536434
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5038841A Pending JPH06254403A (en) | 1993-02-26 | 1993-02-26 | Exhaust gas purification device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06254403A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100471590B1 (en) * | 2002-04-25 | 2005-03-08 | 박종후 | Metallic monoliths substrate of 3-way catalytic converter |
US20110048388A1 (en) * | 2009-09-03 | 2011-03-03 | Ngk Insulators, Ltd. | Heat accumulation element |
JP2011147855A (en) * | 2010-01-20 | 2011-08-04 | Calsonic Kansei Corp | Electrically heating catalyst device and method for producing the same |
WO2024062718A1 (en) * | 2022-09-22 | 2024-03-28 | 日鉄ケミカル&マテリアル株式会社 | Metal honeycomb body, honeycomb unit, catalytic converter, method for manufacturing honeycomb unit, method for manufacturing catalytic converter, and method for manufacturing metal honeycomb body |
-
1993
- 1993-02-26 JP JP5038841A patent/JPH06254403A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100471590B1 (en) * | 2002-04-25 | 2005-03-08 | 박종후 | Metallic monoliths substrate of 3-way catalytic converter |
US20110048388A1 (en) * | 2009-09-03 | 2011-03-03 | Ngk Insulators, Ltd. | Heat accumulation element |
EP2293002A2 (en) | 2009-09-03 | 2011-03-09 | NGK Insulators, Ltd. | Heat Accumulation Element |
JP2011147855A (en) * | 2010-01-20 | 2011-08-04 | Calsonic Kansei Corp | Electrically heating catalyst device and method for producing the same |
WO2024062718A1 (en) * | 2022-09-22 | 2024-03-28 | 日鉄ケミカル&マテリアル株式会社 | Metal honeycomb body, honeycomb unit, catalytic converter, method for manufacturing honeycomb unit, method for manufacturing catalytic converter, and method for manufacturing metal honeycomb body |
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