JPH0422706A - catalytic converter - Google Patents
catalytic converterInfo
- Publication number
- JPH0422706A JPH0422706A JP2125162A JP12516290A JPH0422706A JP H0422706 A JPH0422706 A JP H0422706A JP 2125162 A JP2125162 A JP 2125162A JP 12516290 A JP12516290 A JP 12516290A JP H0422706 A JPH0422706 A JP H0422706A
- Authority
- JP
- Japan
- Prior art keywords
- engine
- bearer
- catalytic converter
- nox
- fuel ratio
- 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
- 230000003197 catalytic effect Effects 0.000 title claims description 17
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical group O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 9
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 7
- 229910052703 rhodium Inorganic materials 0.000 claims abstract description 7
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 6
- 239000000446 fuel Substances 0.000 abstract description 15
- 239000000203 mixture Substances 0.000 abstract description 14
- 239000003054 catalyst Substances 0.000 abstract description 8
- 239000000919 ceramic Substances 0.000 abstract description 2
- 229910052751 metal Inorganic materials 0.000 abstract description 2
- 239000002184 metal Substances 0.000 abstract description 2
- 230000004308 accommodation Effects 0.000 abstract 1
- 238000000746 purification Methods 0.000 description 7
- 230000001052 transient effect Effects 0.000 description 4
- 230000001133 acceleration Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust 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
- F01N3/24—Exhaust 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
- F01N3/28—Construction of catalytic reactors
- F01N3/2803—Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
- F01N3/2825—Ceramics
- F01N3/2828—Ceramic multi-channel monoliths, e.g. honeycombs
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Ceramic Engineering (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
[発明の目的〕
(産業上の利用分野)
本発明は希薄混合気あるいは理論空燃比の混合気が燃焼
されるエンジンから排出されるNOxの浄化効率をいず
れも高めることができる触媒コンバータに関する。[Detailed Description of the Invention] [Objective of the Invention] (Industrial Application Field) The present invention aims to improve the purification efficiency of NOx emitted from an engine in which a lean mixture or a mixture at a stoichiometric air-fuel ratio is burned. Regarding catalytic converters that can
(従来の技術)
エンジンの燃料消費率を向上させるための1つの方法と
して、希薄混合気をエンジンで燃焼させることが知られ
ている。このようなエンジンをリーンバーンエンジンと
いう。このようなリーンバーンエンジンから排出される
NOxを分解する触媒として第4図に示す浄化効率特性
曲線を有するCu/ゼオライト構造を有するリーンNO
X触媒が用いられていた。なお、Cu/ゼオライト構造
とはゼオライト構造というAI、Siよりなる結晶構造
にCuを担持した構造をいう。(Prior Art) It is known that one method for improving the fuel consumption rate of an engine is to combust a lean air-fuel mixture in the engine. This kind of engine is called a lean burn engine. As a catalyst for decomposing NOx emitted from such a lean burn engine, lean NOx having a Cu/zeolite structure having a purification efficiency characteristic curve shown in Fig. 4 is used.
X catalyst was used. Note that the Cu/zeolite structure refers to a structure in which Cu is supported on a crystal structure consisting of AI and Si, called a zeolite structure.
(発明が解決しようとする課8)
ところで、上記リーンバーンエンジンは定常運転時にお
いて希薄混合気をエンジンで燃焼させ、加速時等の過渡
運転時には理論空燃比の混合気をエンジンで燃焼させて
いる。(Question 8 to be solved by the invention) By the way, in the lean burn engine described above, during steady operation, the engine burns a lean air-fuel mixture, and during transient operation, such as during acceleration, the engine burns a mixture at a stoichiometric air-fuel ratio. .
しかし、従来のリーンNOX触媒をリーンバーンエンジ
ンの排気ガス浄化に用いた場合、加速時等の過渡運転時
に理論空燃比の混合気をエンジンで燃焼させるため、理
論空燃比付近で大量に排出されるNOxを完全に浄化す
ることはできなかった。これは、第4図に示すように、
従来のリーンNOX触媒のN Ox浄化効率は理論空燃
比近傍では50%程度であるためである。However, when a conventional lean NOx catalyst is used to purify the exhaust gas of a lean-burn engine, the engine burns a mixture at the stoichiometric air-fuel ratio during transient operations such as during acceleration, so a large amount of NOx is emitted near the stoichiometric air-fuel ratio. It was not possible to completely purify NOx. This is as shown in Figure 4.
This is because the NOx purification efficiency of the conventional lean NOx catalyst is about 50% near the stoichiometric air-fuel ratio.
本発明は上記の点に鑑みてなされたもので、その目的は
希薄混合気あるいは理論空燃比の混合気が燃焼されたエ
ンジンから排出されるNO,の浄化効率をいずれも高め
ることができる触媒コンバータを提供することにある。The present invention has been made in view of the above points, and its purpose is to provide a catalytic converter that can improve the purification efficiency of NO, which is emitted from an engine in which a lean mixture or a mixture at a stoichiometric air-fuel ratio is combusted. Our goal is to provide the following.
[発明の構成]
(課題を解決するための手段)
担体上に形成されたCu/ゼオライト構造等のウォッシ
ュコート層上にPt、Rh、Pd等の貴金属元素を単一
若しくは複数担持させるようにしたことを特徴とする触
媒コンバータである。[Structure of the invention] (Means for solving the problem) A single or multiple noble metal elements such as Pt, Rh, and Pd are supported on a wash coat layer such as a Cu/zeolite structure formed on a carrier. This is a catalytic converter characterized by the following.
(作用)
リーンバーンエンジンの定常運転時に排出されるNOx
はCu/ゼオライト構造の活性点で分解促進され、理論
空燃比で運転される過渡運転時では、エンジンから排出
されるHC,Co、N。(Function) NOx emitted during steady operation of a lean burn engine
is decomposed at active sites in the Cu/zeolite structure, and during transient operation at the stoichiometric air-fuel ratio, HC, Co, and N are discharged from the engine.
8をPt、Rh、Pd等の貴金属元素の活性点で、同時
に低減させるようにしている。8 at the active sites of noble metal elements such as Pt, Rh, and Pd.
(実施例)
以下図面を参照して本発明の一実施例に係わる触媒コン
バータについて説明する。第1図は担体上への担持状態
を示す断面図、第2図は触媒コンバータの軸方向に沿っ
た断面図、第3図は触媒コンバータの径方向に沿った断
面図である。(Example) A catalytic converter according to an example of the present invention will be described below with reference to the drawings. FIG. 1 is a sectional view showing the state of support on a carrier, FIG. 2 is a sectional view taken along the axial direction of the catalytic converter, and FIG. 3 is a sectional view taken along the radial direction of the catalytic converter.
まず、第2図において、11は触媒コンバータである。First, in FIG. 2, 11 is a catalytic converter.
この触媒コンバータ11は断面が円筒形をしており、そ
の外周は排気ガスが流入される吸入部12、触媒が収納
される容器部13、浄化された排気ガスが排出される吐
出部14により構成される。This catalytic converter 11 has a cylindrical cross section, and its outer periphery is composed of an intake section 12 into which exhaust gas flows, a container section 13 where a catalyst is housed, and a discharge section 14 from which purified exhaust gas is discharged. be done.
さらに、15はハニカム形状を有するセラミックあるい
は金属よりなる担体である。そして、担体15により4
方向が囲まれたセル16が軸方向に無数に形成されてい
る。Furthermore, 15 is a carrier made of ceramic or metal and having a honeycomb shape. Then, by the carrier 15, 4
A countless number of cells 16 are formed in the axial direction.
そして、上記担体15上の構造について第1図を参照し
て説明する。上記担体15上にはCu/ゼオライト構造
を有するウォッシュコート層21が形成されており、こ
のウォッシュコート層21にPt、Rh、Pdの貴金属
が複数担持されている。The structure on the carrier 15 will be explained with reference to FIG. 1. A washcoat layer 21 having a Cu/zeolite structure is formed on the carrier 15, and a plurality of noble metals such as Pt, Rh, and Pd are supported on this washcoat layer 21.
上記のように構成された触媒コンバータを用いることに
より、リーンバーンエンジンの定常運転時に排出される
NOxはウォッシュコート層21のCu/ゼオライト構
造の活性点で分解促進され、理論空燃比で運転される過
渡運転時では、エンジンから排出されるHC,Co、N
OxをPt、Rh、Pd等の貴金属元素の活性点で、同
時に低減させるようにしている。つまり、本発明の一実
施例に係わる触媒コンバータのNOx浄化効率は第4図
の実線で示すようになる。By using the catalytic converter configured as described above, NOx emitted during steady operation of the lean burn engine is accelerated in decomposition at the active sites of the Cu/zeolite structure of the washcoat layer 21, and the engine is operated at the stoichiometric air-fuel ratio. During transient operation, HC, Co, and N discharged from the engine
Ox is simultaneously reduced at the active sites of noble metal elements such as Pt, Rh, and Pd. In other words, the NOx purification efficiency of the catalytic converter according to one embodiment of the present invention is shown by the solid line in FIG.
なお、上記実施例ではウォッシュコート層21にPt、
Rh、Pd等の貴金属元素を複数担持するようにしたが
、それらのうち単一の貴金属元素を担持するようにして
も良い。In addition, in the above embodiment, the wash coat layer 21 includes Pt,
Although a plurality of noble metal elements such as Rh and Pd are supported, a single noble metal element may be supported.
[発明の効果]
以上詳述したように本発明によれば、希薄混合気あるい
は理論空燃比の混合気で燃焼されたエンジンから排出さ
れるN Oxの浄化効率をいずれも高めることができる
触媒コンバータを提供することができる。[Effects of the Invention] As detailed above, the present invention provides a catalytic converter that can improve the purification efficiency of NOx emitted from an engine burned with a lean mixture or a mixture with a stoichiometric air-fuel ratio. can be provided.
第1図は本発明の一実施例に係わる触媒コンバータの担
体上への担持状態を示す断面図、第2図は触媒コンバー
タの軸方向に沿った断面図、第3図は触媒コンバータの
径方向に沿った断面図、第4図はNOx浄化効率と空燃
比との関係を示す特性図である。
11・・触媒コンバータ、15・・・担体、21・・・
ウォッシュコート層。FIG. 1 is a cross-sectional view showing how a catalytic converter is supported on a carrier according to an embodiment of the present invention, FIG. 2 is a cross-sectional view along the axial direction of the catalytic converter, and FIG. 3 is a radial direction of the catalytic converter. 4 is a characteristic diagram showing the relationship between NOx purification efficiency and air-fuel ratio. 11...Catalytic converter, 15...Carrier, 21...
Washcoat layer.
Claims (1)
シュコート層上にPt,Rh,Pd等の貴金属元素を単
一若しくは複数担持させるようにしたことを特徴とする
触媒コンバータ。A catalytic converter characterized in that a single or multiple noble metal elements such as Pt, Rh, and Pd are supported on a washcoat layer such as a Cu/zeolite structure formed on a carrier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2125162A JPH0422706A (en) | 1990-05-15 | 1990-05-15 | catalytic converter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2125162A JPH0422706A (en) | 1990-05-15 | 1990-05-15 | catalytic converter |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0422706A true JPH0422706A (en) | 1992-01-27 |
Family
ID=14903413
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2125162A Pending JPH0422706A (en) | 1990-05-15 | 1990-05-15 | catalytic converter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0422706A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040002344A (en) * | 2002-09-06 | 2004-01-07 | 안호근 | The catalyst for selective catalytic reduction of NOx |
KR20040037724A (en) * | 2002-10-30 | 2004-05-07 | 현대자동차주식회사 | Particulate trap |
-
1990
- 1990-05-15 JP JP2125162A patent/JPH0422706A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040002344A (en) * | 2002-09-06 | 2004-01-07 | 안호근 | The catalyst for selective catalytic reduction of NOx |
KR20040037724A (en) * | 2002-10-30 | 2004-05-07 | 현대자동차주식회사 | Particulate trap |
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