JPH112114A - Exhaust gas purification device for internal combustion engine - Google Patents

Exhaust gas purification device for internal combustion engine

Info

Publication number
JPH112114A
JPH112114A JP9154035A JP15403597A JPH112114A JP H112114 A JPH112114 A JP H112114A JP 9154035 A JP9154035 A JP 9154035A JP 15403597 A JP15403597 A JP 15403597A JP H112114 A JPH112114 A JP H112114A
Authority
JP
Japan
Prior art keywords
catalyst
nox
amount
way catalyst
exhaust gas
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.)
Granted
Application number
JP9154035A
Other languages
Japanese (ja)
Other versions
JP3449174B2 (en
Inventor
Yasuji Ishizuka
靖二 石塚
Masayoshi Nishizawa
公良 西沢
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.)
Nissan Motor Co Ltd
Original Assignee
Nissan Motor Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nissan Motor Co Ltd filed Critical Nissan Motor Co Ltd
Priority to JP15403597A priority Critical patent/JP3449174B2/en
Publication of JPH112114A publication Critical patent/JPH112114A/en
Application granted granted Critical
Publication of JP3449174B2 publication Critical patent/JP3449174B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • F01N3/0807Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
    • F01N3/0828Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents characterised by the absorbed or adsorbed substances
    • F01N3/0842Nitrogen oxides
    • 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
    • F01N13/00Exhaust or silencing apparatus characterised by constructional features
    • F01N13/009Exhaust or silencing apparatus characterised by constructional features having two or more separate purifying devices arranged in series
    • 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
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/16Oxygen

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (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)
  • Catalysts (AREA)

Abstract

(57)【要約】 【課題】NOx吸収触媒に対してリーン燃焼中に吸収さ
れたNOxを、空燃比が理論空燃比又はリッチに切り換
えられたときに効率良く還元処理させる。 【解決手段】NOx吸収触媒の上流側及び下流側にそれ
ぞれ三元触媒を配置する。そして、前記NOx吸収触媒
が担持するセリアの量をB、上流側の三元触媒が担持す
るセリアの量をA、下流側の三元触媒が担持するセリア
の量をCとしたときに、(A+B)/Cが略0.2 〜1.2
の範囲、より好ましくは、略0.2 〜0.6 の範囲になるよ
うに、NOx吸収触媒及び上流側の三元触媒における単
位体積当たりのセリア量を調整する。前記(A+B)/
Cの最大値を制限することで、酸素ストレージ能力が制
限され、NOx脱離時に同時に脱離する酸素量が減少
し、NOxが効率良く還元処理される。また、前記(A
+B)/Cの最小値を制限することで、理論空燃比での
NOx浄化能力の低下を回避できる。
(57) [PROBLEMS] To efficiently reduce NOx absorbed by a NOx absorption catalyst during lean combustion when the air-fuel ratio is switched to a stoichiometric air-fuel ratio or rich. A three-way catalyst is arranged on each of an upstream side and a downstream side of a NOx absorption catalyst. Then, assuming that the amount of ceria carried by the NOx absorption catalyst is B, the amount of ceria carried by the upstream three-way catalyst is A, and the amount of ceria carried by the downstream three-way catalyst is C, A + B) / C is approximately 0.2 to 1.2
, More preferably in the range of about 0.2 to 0.6, the amount of ceria per unit volume in the NOx absorption catalyst and the upstream three-way catalyst is adjusted. (A + B) /
By limiting the maximum value of C, the oxygen storage capacity is limited, the amount of oxygen released simultaneously with the release of NOx is reduced, and NOx is efficiently reduced. In addition, (A)
By limiting the minimum value of + B) / C, it is possible to avoid a decrease in the NOx purification ability at the stoichiometric air-fuel ratio.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、内燃機関の排気浄
化装置に関し、詳しくは、排気通路にNOx吸収触媒を
備えた内燃機関において、NOxの浄化率を向上させる
ための技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas purifying apparatus for an internal combustion engine, and more particularly to a technique for improving a NOx purifying rate in an internal combustion engine having a NOx absorbing catalyst in an exhaust passage.

【0002】[0002]

【従来の技術】従来から、排気空燃比がリーンであると
きに排気中のNOxを吸収し、排気空燃比が理論空燃比
(ストイキ)又はリッチであるときに前記吸収したNO
xを放出して還元処理するNOx吸収触媒(NOx吸収
還元型三元触媒)を備えた機関が知られている。
2. Description of the Related Art Conventionally, NOx in exhaust gas has been absorbed when the exhaust air-fuel ratio is lean, and the absorbed NOx has been absorbed when the exhaust air-fuel ratio is stoichiometric or rich.
2. Description of the Related Art There is known an engine equipped with a NOx absorption catalyst (NOx absorption reduction type three-way catalyst) that releases x and performs a reduction process.

【0003】また、上記NOx吸収触媒を備える排気浄
化装置において、NOx吸収触媒の上流側及び下流側に
三元触媒をそれぞれ備えるようにした構成も知られてい
る(特開平8−270440号公報等参照)。
[0003] Further, in an exhaust gas purifying apparatus provided with the above-mentioned NOx absorption catalyst, a configuration in which a three-way catalyst is provided on the upstream side and the downstream side of the NOx absorption catalyst, respectively, is also known (Japanese Patent Application Laid-Open No. Hei 8-270440). reference).

【0004】[0004]

【発明が解決しようとする課題】上記NOx吸収触媒で
は、燃焼混合気の空燃比がリーンからストイキ又はリッ
チに切り換えられ、排気空燃比がリッチ化し始めると、
それまでのリーン燃焼中に吸収していたNOxを脱離す
ることになり、この脱離したNOxはNOx吸収触媒の
三元層や後方の三元触媒で還元処理されることになる。
In the above NOx absorption catalyst, when the air-fuel ratio of the combustion air-fuel mixture is switched from lean to stoichiometric or rich, and the exhaust air-fuel ratio starts to become rich,
The NOx absorbed during the lean combustion up to that time is desorbed, and the desorbed NOx is reduced by the three-way layer of the NOx absorption catalyst or the three-way catalyst at the rear.

【0005】しかし、NOx吸収触媒やNOx吸収触媒
の上流側に配置される三元触媒には、触媒の酸素ストレ
ージ能力によってリーン燃焼中に多量の酸素が蓄積して
おり、この蓄積していた酸素の脱離によって空燃比が切
り換わっても触媒内及び触媒下流の排気空燃比はなかな
かリッチにならず、更に、NOxの還元に必要なHC,
COが前記リーン燃焼中に蓄積されていた酸素によって
酸化処理されてしまうため、NOx吸収触媒やNOx吸
収触媒の下流側に配置される三元触媒において効率良く
NOxを還元処理することができないという問題があっ
た。
[0005] However, a large amount of oxygen is accumulated in the NOx absorption catalyst or the three-way catalyst disposed upstream of the NOx absorption catalyst during lean combustion due to the oxygen storage capacity of the catalyst. Even when the air-fuel ratio is switched due to desorption of the exhaust gas, the exhaust air-fuel ratio in the catalyst and downstream of the catalyst does not easily become rich, and furthermore, HC,
Since CO is oxidized by the oxygen accumulated during the lean combustion, the NOx reduction catalyst or the three-way catalyst disposed downstream of the NOx absorption catalyst cannot efficiently reduce NOx. was there.

【0006】ここで、触媒内を早期にリッチ化させてN
Ox浄化率を向上させるには、大きなリッチスパイクを
与える必要があるが、この場合、燃費が悪化し、また、
HC,COの排出量を増大せさてしまうという問題が生
じる。触媒の酸素ストレージ能力は、触媒に担持される
主にセリアCeの量によって変化するが、従来、単位体
積当たりのセリア担持量は各触媒で略同等であって、要
求浄化性能に基づく触媒容量の設定によって各触媒のセ
リア担持量が決定されることになっており、上記のNO
x脱離時に同時に脱離される酸素の影響を考慮した設定
にはなっていなかった。
Here, the inside of the catalyst is enriched at an early
In order to improve the Ox purification rate, it is necessary to give a large rich spike, but in this case, the fuel efficiency deteriorates, and
There is a problem that the emission amount of HC and CO is increased. The oxygen storage capacity of the catalyst varies depending on the amount of ceria Ce mainly supported on the catalyst. Conventionally, the amount of ceria supported per unit volume is substantially the same for each catalyst, and the catalyst capacity based on the required purification performance is reduced. The ceria carrying amount of each catalyst is determined by the setting, and the above NO
The setting was not made in consideration of the influence of oxygen desorbed at the time of x desorption.

【0007】本発明は上記実情に鑑みなされたものであ
り、少なくともNOx吸収触媒とその下流に配置される
三元触媒とを備えてなる排気浄化装置において、空燃比
がリーンからストイキ又はリッチに切り換わってNOx
が脱離されるときのNOxの処理能力を向上させること
を目的とする。
The present invention has been made in view of the above circumstances, and in an exhaust gas purification apparatus including at least a NOx absorption catalyst and a three-way catalyst disposed downstream thereof, the air-fuel ratio is switched from lean to stoichiometric or rich. NOx instead
It is an object of the present invention to improve the processing capacity of NOx when NO is desorbed.

【0008】[0008]

【課題を解決するための手段】そのため請求項1記載の
発明は、排気空燃比がリーンであるときに排気中のNO
xを吸収し、排気空燃比が理論空燃比又はリッチである
ときに前記吸収したNOxを放出して還元処理するNO
x吸収触媒と、該NOx吸収触媒の下流側に配置された
三元触媒とを少なくとも備えてなる内燃機関の排気浄化
装置において、前記三元触媒が担持する酸素ストレージ
能力に寄与する成分の量に対して、前記三元触媒よりも
上流側の触媒が担持する前記成分の総量を略1.2 倍以下
に設定したことを特徴とする。
Therefore, according to the first aspect of the present invention, when the exhaust air-fuel ratio is lean, the NO
NO that absorbs x and releases the absorbed NOx when the exhaust air-fuel ratio is the stoichiometric air-fuel ratio or is rich.
In an exhaust gas purification apparatus for an internal combustion engine comprising at least an x-absorption catalyst and a three-way catalyst disposed downstream of the NOx absorption catalyst, the amount of a component contributing to the oxygen storage capacity carried by the three-way catalyst is reduced. On the other hand, the total amount of the components carried by the catalyst upstream of the three-way catalyst is set to be approximately 1.2 times or less.

【0009】かかる構成によると、NOx吸収触媒の上
流側に触媒が配置されない場合には、該NOx吸収触媒
が担持する酸素ストレージ能力に寄与する成分の量が、
NOx吸収触媒の下流側に配置される三元触媒が担持し
ている量の略1.2 倍以下になるように設定され、また、
NOx吸収触媒の上流側に触媒が配置される場合には、
該NOx吸収触媒における担持量とNOx吸収触媒の上
流側に配置された触媒における担持量との総量が、NO
x吸収触媒の下流側に配置される三元触媒が担持してい
る量の略1.2 倍以下になるように設定される。
According to such a configuration, when the catalyst is not arranged on the upstream side of the NOx absorption catalyst, the amount of the component contributing to the oxygen storage capacity carried by the NOx absorption catalyst becomes:
The amount is set to be approximately 1.2 times or less the amount carried by the three-way catalyst disposed downstream of the NOx absorption catalyst, and
When the catalyst is arranged on the upstream side of the NOx absorption catalyst,
The total amount of the amount supported on the NOx absorption catalyst and the amount supported on the catalyst disposed upstream of the NOx absorption catalyst is NO.
The amount is set to be approximately 1.2 times or less the amount carried by the three-way catalyst disposed downstream of the x-absorption catalyst.

【0010】一方、請求項2記載の発明は、排気空燃比
がリーンであるときに排気中のNOxを吸収し、排気空
燃比が理論空燃比又はリッチであるときに前記吸収した
NOxを放出して還元処理するNOx吸収触媒と、該N
Ox吸収触媒の下流側に配置された三元触媒とを少なく
とも備えてなる内燃機関の排気浄化装置において、前記
三元触媒が有する酸素ストレージ能力よりも、前記三元
触媒よりも上流側の触媒が有する酸素ストレージ能力を
低く設定したことを特徴とする。
On the other hand, the invention according to claim 2 absorbs NOx in the exhaust when the exhaust air-fuel ratio is lean, and releases the absorbed NOx when the exhaust air-fuel ratio is stoichiometric or rich. A NOx absorption catalyst to be reduced by
In an exhaust gas purification apparatus for an internal combustion engine comprising at least a three-way catalyst disposed downstream of the Ox absorption catalyst, a catalyst upstream of the three-way catalyst may be more upstream than the oxygen storage capacity of the three-way catalyst. The low oxygen storage capacity is set.

【0011】かかる構成によると、NOx吸収触媒の上
流側に触媒が配置されない場合には、該NOx吸収触媒
が担持する酸素ストレージ能力が、NOx吸収触媒の下
流側に配置される三元触媒よりも低く設定され、また、
NOx吸収触媒の上流側に触媒が配置される場合には、
該NOx吸収触媒及びNOx吸収触媒の上流側に配置さ
れた触媒における酸素ストレージ能力の総和が、NOx
吸収触媒の下流側に配置される三元触媒よりも低く設定
される。
According to this configuration, when the catalyst is not arranged on the upstream side of the NOx absorption catalyst, the oxygen storage capacity of the NOx absorption catalyst is higher than that of the three-way catalyst arranged on the downstream side of the NOx absorption catalyst. Set low,
When the catalyst is arranged on the upstream side of the NOx absorption catalyst,
The sum of the oxygen storage capacity of the NOx absorption catalyst and the catalyst disposed upstream of the NOx absorption catalyst is NOx
It is set lower than the three-way catalyst disposed downstream of the absorption catalyst.

【0012】請求項3記載の発明では、前記請求項2記
載の構成において、前記三元触媒が担持する酸素ストレ
ージ能力に寄与する成分の量に対して、前記三元触媒よ
りも上流側の触媒が担持する前記成分の総量を略0.6 倍
以下に設定する構成とした。かかる構成によると、前記
三元触媒が有する酸素ストレージ能力よりも前記三元触
媒よりも上流側の触媒が有する酸素ストレージ能力を低
くする設定を、酸素ストレージ能力に寄与する成分量の
比率で規定するものであって、かつ、特に好ましい範囲
を略0.6 倍以下として特定する。
According to a third aspect of the present invention, in the configuration of the second aspect, a catalyst upstream of the three-way catalyst with respect to an amount of a component contributing to the oxygen storage capacity carried by the three-way catalyst. Is set so that the total amount of the components carried by is set to approximately 0.6 times or less. According to this configuration, the setting for lowering the oxygen storage capacity of the catalyst upstream of the three-way catalyst than the oxygen storage capacity of the three-way catalyst is defined by the ratio of the component amounts that contribute to the oxygen storage capacity. And a particularly preferable range is specified as approximately 0.6 times or less.

【0013】請求項4記載の発明では、請求項1又は3
において、前記三元触媒が担持する酸素ストレージ能力
に寄与する成分の量に対して、前記三元触媒よりも上流
側の触媒が担持する前記成分の総量を略0.2 倍以上に設
定する構成とした。かかる構成によると、酸素ストレー
ジ能力に寄与する成分量の比率の最大値を規制する構成
において最小比率を略0.2 倍以上として、NOx吸収触
媒及び該NOx吸収触媒の上流側の触媒における酸素ス
トレージ能力の最低必要レベルの規定する。
According to the invention described in claim 4, claim 1 or 3
, The total amount of the components carried by the catalyst upstream of the three-way catalyst is set to be about 0.2 times or more the amount of the components contributing to the oxygen storage capacity carried by the three-way catalyst. . According to this configuration, in the configuration that regulates the maximum value of the ratio of the components contributing to the oxygen storage capacity, the minimum ratio is set to about 0.2 times or more, and the oxygen storage capacity of the NOx absorption catalyst and the catalyst on the upstream side of the NOx absorption catalyst is reduced. Specify the minimum required level.

【0014】請求項5記載の発明では、前記酸素ストレ
ージ能力に寄与する成分としてセリアCeの量を設定す
る構成とした。かかる構成によると、NOx吸収触媒及
び該NOx吸収触媒の上流側の触媒が担持するセリアC
eの量が、NOx吸収触媒の下流側の三元触媒が担持す
るセリアCeの量を基準として規制されることになる。
According to the fifth aspect of the invention, the amount of ceria Ce is set as a component contributing to the oxygen storage capacity. According to this configuration, the ceria C carried by the NOx absorption catalyst and the catalyst on the upstream side of the NOx absorption catalyst
The amount of e is regulated based on the amount of ceria Ce carried by the three-way catalyst downstream of the NOx absorption catalyst.

【0015】請求項6記載の発明では、前記NOx吸収
触媒の上流側にも三元触媒が配置される構成とした。か
かる構成によると、上流側から三元触媒,NOx吸収触
媒,三元触媒の順で触媒が配置され、下流側の三元触媒
を基準として、上流側の三元触媒及びNOx吸収触媒に
おける酸素ストレージ能力(酸素ストレージ能力に寄与
する成分(セリア)の量)が制限される。
In the invention according to claim 6, a three-way catalyst is disposed upstream of the NOx absorption catalyst. According to this configuration, the three-way catalyst, the NOx absorption catalyst, and the three-way catalyst are arranged in this order from the upstream side, and the oxygen storage in the upstream three-way catalyst and the NOx absorption catalyst is based on the downstream three-way catalyst. Capacity (the amount of component (ceria) that contributes to oxygen storage capacity) is limited.

【0016】請求項7記載の発明では、前記NOx吸収
触媒が、前記三元触媒よりもバリウムBaを多く含むこ
とで、バリウムBaをNOx吸収剤としてNOxの吸収
を行う構成とした。かかる構成によると、NOx吸収触
媒と下流側の三元触媒とが共にバリウムBaを担持する
構成であっても、NOx吸収触媒の方がNOx吸収を目
的としてより多くのバリウムBaを担持することで通常
の三元触媒とは区別されることになり、かかる区別に基
づいて各触媒の酸素ストレージ能力(酸素ストレージ能
力に寄与する成分(セリア)の量)が決定される。
In the invention according to claim 7, the NOx absorption catalyst contains barium Ba more than the three-way catalyst, so that NOx is absorbed using barium Ba as a NOx absorbent. According to such a configuration, even when both the NOx absorption catalyst and the downstream three-way catalyst carry barium Ba, the NOx absorption catalyst carries more barium Ba for the purpose of NOx absorption. The catalyst is distinguished from the ordinary three-way catalyst, and the oxygen storage capacity (the amount of the component (ceria) contributing to the oxygen storage capacity) of each catalyst is determined based on the distinction.

【0017】[0017]

【発明の効果】請求項1記載の発明によると、リーン燃
焼状態からストイキ或いはリッチに切り換えられたとき
に、NOx吸収触媒及び該NOx吸収触媒の上流側に配
置される触媒から脱離される酸素の量を必要充分に制限
でき、NOx吸収触媒及び下流側の三元触媒を早期にリ
ッチ化させて、NOx還元処理を効率良く行わせること
ができるという効果がある。
According to the first aspect of the present invention, when the state is switched from the lean combustion state to the stoichiometric or rich state, the amount of oxygen released from the NOx absorption catalyst and the catalyst disposed upstream of the NOx absorption catalyst is reduced. The amount can be limited to a necessary and sufficient amount, and the NOx absorption catalyst and the three-way catalyst on the downstream side can be enriched early so that the NOx reduction process can be efficiently performed.

【0018】請求項2記載の発明によると、NOx吸収
触媒の下流側の三元触媒における酸素ストレージ能力よ
りも、上流側のNOx還元触媒を含む触媒における酸素
ストレージ能力を低くすることで、リーン燃焼状態から
ストイキ或いはリッチに切り換えられてNOxが脱離さ
れるときに、同時に脱離される酸素の量を確実に制限で
き、以て、NOxの還元処理を効率的に行わせることが
できるという効果がある。
According to the second aspect of the present invention, the oxygen storage capacity of the catalyst including the NOx reduction catalyst on the upstream side is made lower than the oxygen storage capacity of the three-way catalyst on the downstream side of the NOx absorption catalyst, whereby lean combustion is performed. When the state is switched to stoichiometric or rich and NOx is desorbed, the amount of oxygen desorbed at the same time can be reliably limited, so that there is an effect that the NOx reduction process can be performed efficiently. .

【0019】請求項3記載の発明によると、リーン燃焼
状態からストイキ或いはリッチに切り換えられたとき
に、NOx吸収触媒及び該NOx吸収触媒の上流側に配
置される触媒から脱離される酸素の量を最も効果的に減
少させて、NOx還元処理を最も効率良く行わせること
ができるという効果がある。請求項4記載の発明による
と、NOxの脱離時に同時に脱離される酸素の量を制限
しつつ、通常のストイキ時における排気浄化性能を確保
できるという効果がある。
According to the third aspect of the invention, when the state is switched from the lean combustion state to the stoichiometric or rich state, the amount of oxygen desorbed from the NOx absorption catalyst and the catalyst disposed upstream of the NOx absorption catalyst is reduced. There is an effect that the NOx reduction processing can be performed most efficiently by reducing it most effectively. According to the invention described in claim 4, there is an effect that the exhaust gas purifying performance at the time of normal stoichiometry can be secured while limiting the amount of oxygen that is simultaneously desorbed when NOx is desorbed.

【0020】請求項5記載の発明によると、触媒に担持
されるセリアの量を調整することで、NOx還元処理を
効率良く行わせることができる酸素ストレージ能力の設
定が行えるという効果がある。請求項6記載の発明によ
ると、NOx還元触媒の上流側にも三元触媒を備えるこ
とで、始動時における排気浄化の促進を図りつつ、NO
x吸収触媒に吸収されたNOxの還元処理を効率良く行
わせることができるという効果がある。
According to the fifth aspect of the present invention, by adjusting the amount of ceria carried on the catalyst, there is an effect that the oxygen storage capacity for efficiently performing the NOx reduction treatment can be set. According to the sixth aspect of the present invention, the three-way catalyst is provided also on the upstream side of the NOx reduction catalyst, so that the exhaust gas purification at the time of starting is promoted, and
There is an effect that the reduction treatment of NOx absorbed by the x-absorption catalyst can be efficiently performed.

【0021】請求項7記載の発明によると、バリウムを
通常の三元触媒よりも多く含むことで、前記バリウムを
NOx吸収剤として用いてリーン燃焼時にNOxを吸収
するNOx吸収触媒を備える構成において、前記NOx
吸収触媒に吸収されたNOxの還元処理を効率良く行わ
せることができるという効果がある。
According to the seventh aspect of the present invention, there is provided a configuration including a NOx absorption catalyst that contains barium in an amount larger than that of a normal three-way catalyst and absorbs NOx during lean combustion by using the barium as a NOx absorbent. The NOx
There is an effect that the reduction treatment of NOx absorbed by the absorption catalyst can be efficiently performed.

【0022】[0022]

【発明の実施の形態】以下に本発明の実施の形態を説明
する。図1は、実施の形態における内燃機関のシステム
構成を示す図であり、機関1には、スロットル弁2で計
量された空気が吸引され、燃料噴射弁3から噴射される
燃料と前記吸入空気とが混合して混合気が形成される。
Embodiments of the present invention will be described below. FIG. 1 is a diagram showing a system configuration of an internal combustion engine according to an embodiment. In the engine 1, air measured by a throttle valve 2 is sucked, and fuel injected from a fuel injection valve 3 and the intake air are mixed. Are mixed to form an air-fuel mixture.

【0023】前記燃料噴射弁3は、吸気ポート部分に燃
料を噴射するものであっても良いし、また、燃焼室内に
直接燃料を噴射するものであっても良い。前記混合気
は、点火栓4による火花点火によって着火燃焼し、燃焼
排気は、排気通路5に介装された三元触媒(ライトオフ
触媒)6,NOx吸収触媒7,三元触媒8で浄化されて
大気中に排出される。
The fuel injection valve 3 may be one that injects fuel into the intake port or one that directly injects fuel into the combustion chamber. The air-fuel mixture is ignited and burned by spark ignition by the spark plug 4, and the combustion exhaust gas is purified by the three-way catalyst (light-off catalyst) 6, the NOx absorption catalyst 7, and the three-way catalyst 8 provided in the exhaust passage 5. Is released into the atmosphere.

【0024】前記三元触媒6,8は共にストイキ(理論
空燃比)雰囲気においてNOx,CO,HCを同時に浄
化する触媒であり、三元触媒6は始動時の排気浄化を目
的として排気マニホールドの直下に配置され、三元触媒
8は、NOx吸収触媒7と共に車両の床下部分に配置さ
れる。前記NOx吸収触媒7は、排気空燃比がリーンで
あるときに排気中のNOxを吸収し、排気空燃比が理論
空燃比又はリッチであるときに前記吸収したNOxを放
出して三元触媒層で還元処理する触媒(NOx吸収還元
型三元触媒)である。
The three-way catalysts 6 and 8 are both catalysts that simultaneously purify NOx, CO and HC in a stoichiometric (stoichiometric air-fuel ratio) atmosphere, and the three-way catalyst 6 is located immediately below an exhaust manifold for the purpose of purifying exhaust gas during startup. And the three-way catalyst 8 is arranged together with the NOx absorption catalyst 7 in the underfloor portion of the vehicle. The NOx absorption catalyst 7 absorbs NOx in the exhaust when the exhaust air-fuel ratio is lean, and releases the absorbed NOx when the exhaust air-fuel ratio is stoichiometric or rich, and the three-way catalyst layer This is a catalyst for reduction treatment (NOx absorption reduction type three-way catalyst).

【0025】前記NOx吸収触媒7及び三元触媒6,8
は、全てバリウムBaを担持するが、NOx吸収触媒7
は、バリウムBaをNOx吸収剤として用いるべく、三
元触媒8に担持されているバリウムBaの量に対して単
位体積当たり略2倍のバリウムBaを担持するものであ
り、前記バリウムBaの担持量によってNOx吸収触媒
と通常の三元触媒とに区別される。但し、NOx吸収剤
をバリウムBaに限定するものではない。
The NOx absorption catalyst 7 and the three-way catalysts 6, 8
All carry barium Ba, but the NOx absorption catalyst 7
Carries barium Ba per unit volume approximately twice as much as the amount of barium Ba supported on the three-way catalyst 8 in order to use barium Ba as the NOx absorbent. Thus, the catalyst is classified into a NOx absorption catalyst and a normal three-way catalyst. However, the NOx absorbent is not limited to barium Ba.

【0026】前記燃料噴射弁3による噴射時期・噴射
量、及び、点火栓4による点火時期等を制御するコント
ロールユニット9はマイクロコンピュータを含んで構成
され、各種センサからの検出信号に基づく演算処理によ
って、前記燃料噴射弁3に対して燃料噴射信号(噴射パ
ルス信号)を出力し、点火栓4(パワートランジスタ)
に対しては点火信号を出力する。
The control unit 9 for controlling the injection timing / injection amount of the fuel injection valve 3 and the ignition timing of the ignition plug 4 includes a microcomputer, and performs arithmetic processing based on detection signals from various sensors. A fuel injection signal (injection pulse signal) is output to the fuel injection valve 3, and an ignition plug 4 (power transistor) is output.
, An ignition signal is output.

【0027】前記燃料噴射信号の演算においては、運転
条件に応じて目標空燃比を決定し、該目標空燃比の混合
気が形成されるように燃料噴射量(噴射パルス幅)が演
算されるが、前記目標空燃比として理論空燃比(ストイ
キ)及びリッチ空燃比の他、リーン空燃比が設定される
構成となっている。尚、本願において、リッチ・リーン
はいずれも理論空燃比を基準とするものとする。
In the calculation of the fuel injection signal, a target air-fuel ratio is determined according to operating conditions, and a fuel injection amount (injection pulse width) is calculated so that a mixture of the target air-fuel ratio is formed. In addition, a lean air-fuel ratio is set as the target air-fuel ratio in addition to a stoichiometric air-fuel ratio (stoichiometric ratio) and a rich air-fuel ratio. In the present application, both rich and lean are based on the stoichiometric air-fuel ratio.

【0028】前記各種センサとしては、機関1の吸入空
気流量を検出するエアフローメータ10、前記スロットル
弁2の開度を検出するスロットルセンサ11などが設けら
れる他、コントロールユニット9には図示しないクラン
ク角センサからの回転信号等が入力される。前記NOx
吸収触媒7は、リーン燃焼時においてNOxを吸収し、
目標空燃比が理論空燃比(ストイキ)又はリッチに切り
換えられると、それまでに吸収していたNOxを脱離
し、該脱離されたNOxは、NOx吸収触媒7の三元触
媒層及び下流側の三元触媒8で還元処理される。
The various sensors include an air flow meter 10 for detecting the intake air flow rate of the engine 1, a throttle sensor 11 for detecting the opening of the throttle valve 2, and the like. A rotation signal or the like from the sensor is input. The NOx
The absorption catalyst 7 absorbs NOx during lean combustion,
When the target air-fuel ratio is switched to the stoichiometric air-fuel ratio (stoichiometric) or rich, the NOx absorbed so far is desorbed, and the desorbed NOx is removed from the three-way catalyst layer of the NOx absorption catalyst 7 and the downstream side. The reduction treatment is performed by the three-way catalyst 8.

【0029】ここで、リーン燃焼状態が継続すると、N
Ox吸収触媒7に対するNOxの吸収量が限界に達して
NOxをそれ以上に吸収できなくなり、機関1から排出
されたNOxがそのまま排出されるようになってしまう
ので、負荷,回転,空燃比などからNOxの吸収量を推
定し、限界に達しているものと推定されるときには強制
的に空燃比を一時的に理論空燃比又はリッチに制御する
ようになっている。
Here, if the lean combustion state continues, N
Since the amount of NOx absorbed by the Ox absorption catalyst 7 reaches the limit and NOx can no longer be absorbed, and NOx discharged from the engine 1 is directly discharged, the load, rotation, air-fuel ratio, etc. The NOx absorption amount is estimated, and when it is estimated that the limit has been reached, the air-fuel ratio is forcibly controlled temporarily to the stoichiometric air-fuel ratio or rich.

【0030】ところで、前記NOx吸収触媒7及び三元
触媒6,8は、いずれも酸素ストレージ能力に寄与する
成分としてセリアCeを担持し、リーン燃焼時には多く
の酸素を蓄積する。但し、酸素ストレージ能力に寄与す
る成分としてセリアCeを担持する構成に限定するもの
ではない。そして、空燃比がリーンから理論空燃比(ス
トイキ)又はリッチに切り換えられると、前記蓄積して
いた酸素が脱離することになり、NOx吸収触媒7及び
三元触媒8内で脱離した酸素の存在、及び、三元触媒6
及びNOx吸収触媒7から脱離して下流に流れる酸素の
存在によって、前記脱離されたNOxを還元処理するN
Ox吸収触媒7及び三元触媒8の雰囲気がなかなかリッ
チ化せず、NOxを効率良く還元処理できない。
The NOx absorption catalyst 7 and the three-way catalysts 6, 8 each carry ceria Ce as a component that contributes to the oxygen storage capacity, and accumulates a large amount of oxygen during lean combustion. However, the configuration is not limited to a configuration that supports ceria Ce as a component that contributes to the oxygen storage capacity. When the air-fuel ratio is switched from lean to the stoichiometric air-fuel ratio (stoichiometric) or rich, the stored oxygen is desorbed, and the oxygen desorbed in the NOx absorption catalyst 7 and the three-way catalyst 8 is removed. Presence and three-way catalyst 6
And a process for reducing the desorbed NOx by the presence of oxygen desorbed from the NOx absorption catalyst 7 and flowing downstream.
The atmospheres of the Ox absorption catalyst 7 and the three-way catalyst 8 are not easily enriched, so that NOx cannot be efficiently reduced.

【0031】そこで、本実施の形態では、各触媒6〜8
の酸素ストレージ能力に寄与する成分であるセリアCe
の単位体積当たりの量を以下のようにして設定してあ
る。従来のセリアCeの単位体積当たりの量は各触媒6
〜8共に略同程度であり、各触媒6〜8におけるセリア
の量は触媒容量によって決定されており、三元触媒6の
セリア量AとNOx吸収触媒7のセリア量Bとの合計
は、三元触媒8のセリアの量Cの略2.4 倍になってい
た。
Therefore, in the present embodiment, each of the catalysts 6 to 8
Ce, a component that contributes to the oxygen storage capacity of
Is set per unit volume as follows. The amount of the conventional ceria Ce per unit volume is 6 for each catalyst.
To 8 are substantially the same, the amount of ceria in each of the catalysts 6 to 8 is determined by the catalyst capacity, and the total of the ceria amount A of the three-way catalyst 6 and the ceria amount B of the NOx absorption catalyst 7 is 3 The amount of ceria in the original catalyst 8 was about 2.4 times the amount C.

【0032】上記設定に対し、三元触媒8のセリア量C
をそのままとした状態で、三元触媒6及びNOx吸収触
媒7におけるセリアの総量A+Bを減少させていき、三
元触媒8のセリア量Cに対する三元触媒6及びNOx吸
収触媒7におけるセリア総量A+Bの割合((A+B)
/C)を減少させていくと、図2に示すように、リーン
燃焼からストイキ(又はリッチ)に切り換えられたとき
のNOx排出量が減少することが実験的に確認された。
With respect to the above setting, the ceria amount C of the three-way catalyst 8
Is reduced, the total amount A + B of ceria in the three-way catalyst 6 and the NOx absorption catalyst 7 is reduced. Ratio ((A + B)
As shown in FIG. 2, it was experimentally confirmed that the NOx emission when switching from lean combustion to stoichiometric (or rich) was reduced as / C) was decreased.

【0033】尚、セリア量A+Bの減少は、単位体積当
たりのセリア量を減少させることで実現させる。これ
は、セリア量A+Bの減少によって、三元触媒6及びN
Ox吸収触媒7における酸素ストレージ能力が低下し、
リーン燃焼からストイキ(又はリッチ)に切り換えられ
ても、脱離する酸素量が少ないため、NOx吸収触媒7
及び三元触媒8内の雰囲気が比較的早くリッチ化して還
元雰囲気となり、NOxの還元が効率良く行われるため
である。
The reduction of the ceria amount A + B is realized by reducing the ceria amount per unit volume. This is because the three-way catalyst 6 and N
The oxygen storage capacity of the Ox absorption catalyst 7 decreases,
Even when switching from lean combustion to stoichiometric (or rich), the amount of desorbed oxygen is small.
The reason is that the atmosphere in the three-way catalyst 8 is enriched relatively quickly to become a reducing atmosphere, and NOx is efficiently reduced.

【0034】リーン燃焼からストイキ(又はリッチ)に
切り換えられたときのNOx排出量は、上記割合(A+
B)/Cが小さいほど減少するが(図2参照)、図3に
示すように、セリア量A+Bを減少させ過ぎると、通常
のストイキ燃焼状態におけるNOx浄化率が低下してN
Ox排出量を増大させてしまうことになり、前記ストイ
キでのNOx排出量を許容値内に抑制するためには、前
記割合の(A+B)/Cの下限を、略0.2 とする必要が
ある。
The NOx emission amount when switching from lean combustion to stoichiometric (or rich) is determined by the ratio (A +
B) As C / C decreases (see FIG. 2), as shown in FIG. 3, when the ceria amount A + B is excessively reduced, the NOx purification rate in the normal stoichiometric combustion state decreases and N
Since the amount of Ox emission increases, the lower limit of the ratio (A + B) / C needs to be set to about 0.2 in order to suppress the amount of NOx emission in the stoichiometric range within an allowable value.

【0035】一方、図4に示すように、所定の走行モー
ド時(例えば10−15モード時)において、リーン→スト
イキ切り換え時に排出されるNOx量と、ストイキ状態
で排出されるNOx量とを含むNOx排出量の総量は、
前記割合(A+B)/Cを従来の略2.4 から略1.2 まで
減少させれば必要充分に低減されることなり(例えば従
来量に対して半減)、略0.2 〜1.2 倍の範囲内に前記割
合(A+B)/Cを設定すれば、通常のストイキ燃焼時
のNOx排出量を増大させることなく、トータルでのN
Ox排出量を効果的に低減できる。
On the other hand, as shown in FIG. 4, in a predetermined traveling mode (for example, in the 10-15 mode), it includes the NOx amount discharged when switching from lean to stoichiometric and the NOx amount discharged in the stoichiometric state. The total amount of NOx emissions is
If the ratio (A + B) / C is reduced from approximately 2.4 to approximately 1.2 in the related art, the ratio can be sufficiently reduced (for example, halved with respect to the conventional amount). If (A + B) / C is set, the total amount of Nx can be reduced without increasing the amount of NOx emission during normal stoichiometric combustion.
Ox emissions can be effectively reduced.

【0036】前記割合(A+B)/Cを略1.2 から更に
減少させていくと、図2に示すように、略0.6 まではN
Ox脱離時のNOx排出量の低下が進むが、略0.6 以下
にしてもそれ以上にNOx量は低下しないので、最も効
率良くNOxを浄化できるのは、前記割合(A+B)/
Cを略0.2 〜0.6 の範囲内に設定した場合である。上記
のように、前記割合(A+B)/Cを略0.2 〜0.6 の範
囲内に設定した場合には、三元触媒8の酸素ストレージ
能力よりも、三元触媒6及びNOx吸収触媒8における
酸素ストレージ能力の総和を低くしたことになる。
As the ratio (A + B) / C is further reduced from approximately 1.2, as shown in FIG.
Although the amount of NOx emission at the time of Ox desorption progresses, even if it is approximately 0.6 or less, the NOx amount does not decrease any more. Therefore, NOx can be purified most efficiently by the ratio (A + B) /
This is the case where C is set within a range of approximately 0.2 to 0.6. As described above, when the ratio (A + B) / C is set in the range of approximately 0.2 to 0.6, the oxygen storage capacity of the three-way catalyst 6 and the NOx absorption catalyst 8 is more than the oxygen storage capacity of the three-way catalyst 8. This means that the sum of the abilities has been lowered.

【0037】尚、上記実施の形態では、NOx吸収触媒
7の上流側に三元触媒6を備える構成としたが、三元触
媒6を備えない構成であっても良く、この場合に、B/
Cの割合が略0.2 〜1.2 の範囲内、好ましくは、略0.2
〜0.6 の範囲内になるように、NOx吸収触媒7におけ
る単位体積当たりのセリア量を調整すれば良い。
In the above-described embodiment, the three-way catalyst 6 is provided upstream of the NOx absorption catalyst 7. However, the three-way catalyst 6 may not be provided.
The proportion of C is in the range of about 0.2 to 1.2, preferably about 0.2
The amount of ceria per unit volume in the NOx absorption catalyst 7 may be adjusted so as to fall within the range of 0.6.

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

【図1】実施の形態の内燃機関を示すシステム構成図。FIG. 1 is a system configuration diagram showing an internal combustion engine of an embodiment.

【図2】リーン→ストイキ切り換え時のNOx排出量と
セリア量の比率との相関を示す線図。
FIG. 2 is a graph showing a correlation between a NOx emission amount and a ceria amount ratio at the time of switching from lean to stoichiometric.

【図3】ストイキ燃焼時のNOx排出量とセリア量の比
率との相関を示す線図。
FIG. 3 is a graph showing a correlation between a NOx emission amount and a ceria amount ratio during stoichiometric combustion.

【図4】所定の走行モード時におけるNOx排出量とセ
リア量の比率との相関を示す線図。
FIG. 4 is a diagram showing a correlation between a NOx emission amount and a ceria amount ratio in a predetermined traveling mode.

【符号の説明】[Explanation of symbols]

1 内燃機関 2 スロットル弁 3 燃料噴射弁 4 点火栓 5 排気通路 6 三元触媒 7 NOx吸収触媒 8 三元触媒 9 コントロールユニット 10 エアフローメータ 11 スロットルセンサ DESCRIPTION OF SYMBOLS 1 Internal combustion engine 2 Throttle valve 3 Fuel injection valve 4 Spark plug 5 Exhaust passage 6 Three-way catalyst 7 NOx absorption catalyst 8 Three-way catalyst 9 Control unit 10 Air flow meter 11 Throttle sensor

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F01N 3/24 F01N 3/24 E B01D 53/36 101B 104A ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI F01N 3/24 F01N 3/24 E B01D 53/36 101B 104A

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】排気空燃比がリーンであるときに排気中の
NOxを吸収し、排気空燃比が理論空燃比又はリッチで
あるときに前記吸収したNOxを放出して還元処理する
NOx吸収触媒と、該NOx吸収触媒の下流側に配置さ
れた三元触媒とを少なくとも備えてなる内燃機関の排気
浄化装置において、 前記三元触媒が担持する酸素ストレージ能力に寄与する
成分の量に対して、前記三元触媒よりも上流側の触媒が
担持する前記成分の総量を略1.2 倍以下に設定したこと
を特徴とする内燃機関の排気浄化装置。
1. An NOx absorption catalyst for absorbing NOx in exhaust gas when the exhaust air-fuel ratio is lean, and releasing and reducing the absorbed NOx when the exhaust air-fuel ratio is stoichiometric or rich. An exhaust gas purification device for an internal combustion engine comprising at least a three-way catalyst disposed downstream of the NOx absorption catalyst, wherein the three-way catalyst carries an oxygen storage capacity, An exhaust gas purification apparatus for an internal combustion engine, wherein the total amount of the components carried by the catalyst upstream of the three-way catalyst is set to about 1.2 times or less.
【請求項2】排気空燃比がリーンであるときに排気中の
NOxを吸収し、排気空燃比が理論空燃比又はリッチで
あるときに前記吸収したNOxを放出して還元処理する
NOx吸収触媒と、該NOx吸収触媒の下流側に配置さ
れた三元触媒とを少なくとも備えてなる内燃機関の排気
浄化装置において、 前記三元触媒が有する酸素ストレージ能力よりも、前記
三元触媒よりも上流側の触媒が有する酸素ストレージ能
力を低く設定したことを特徴とする内燃機関の排気浄化
装置。
2. An NOx absorption catalyst for absorbing NOx in exhaust gas when the exhaust air-fuel ratio is lean, and releasing and reducing the absorbed NOx when the exhaust air-fuel ratio is stoichiometric or rich. An exhaust gas purification device for an internal combustion engine comprising at least a three-way catalyst disposed downstream of the NOx absorption catalyst, wherein the oxygen storage capacity of the three-way catalyst is more upstream than the three-way catalyst. An exhaust gas purification device for an internal combustion engine, wherein an oxygen storage capacity of a catalyst is set low.
【請求項3】前記三元触媒が担持する酸素ストレージ能
力に寄与する成分の量に対して、前記三元触媒よりも上
流側の触媒が担持する前記成分の総量を略0.6 倍以下に
設定したことを特徴とする請求項2記載の内燃機関の排
気浄化装置。
3. The total amount of the components carried by the catalyst upstream of the three-way catalyst is set to approximately 0.6 times or less the amount of the components contributing to the oxygen storage capacity carried by the three-way catalyst. 3. The exhaust gas purifying apparatus for an internal combustion engine according to claim 2, wherein:
【請求項4】前記三元触媒が担持する酸素ストレージ能
力に寄与する成分の量に対して、前記三元触媒よりも上
流側の触媒が担持する前記成分の総量を略0.2 倍以上に
設定したことを特徴とする請求項1又は3に記載の内燃
機関の排気浄化装置。
4. The total amount of the components carried by the catalyst upstream of the three-way catalyst is set to be about 0.2 times or more the amount of the components contributing to the oxygen storage capacity carried by the three-way catalyst. The exhaust gas purification apparatus for an internal combustion engine according to claim 1 or 3, wherein:
【請求項5】前記酸素ストレージ能力に寄与する成分と
してセリアCeの量を設定することを特徴とする請求項
1,3又は4に記載の内燃機関の排気浄化装置。
5. The exhaust gas purifying apparatus for an internal combustion engine according to claim 1, wherein an amount of ceria Ce is set as a component contributing to the oxygen storage capacity.
【請求項6】前記NOx吸収触媒の上流側にも三元触媒
が配置されることを特徴とする請求項1〜5のいずれか
1つに記載の内燃機関の排気浄化装置。
6. The exhaust gas purifying apparatus for an internal combustion engine according to claim 1, wherein a three-way catalyst is disposed upstream of the NOx absorption catalyst.
【請求項7】前記NOx吸収触媒が、前記三元触媒より
もバリウムBaを多く含むことで、バリウムBaをNO
x吸収剤としてNOxの吸収を行うことを特徴とする請
求項請求項1〜6のいずれか1つに記載の内燃機関の排
気浄化装置。
7. The NOx absorption catalyst contains more barium Ba than the three-way catalyst, so that barium Ba is reduced to NO.
The exhaust gas purifying apparatus for an internal combustion engine according to any one of claims 1 to 6, wherein NOx is absorbed as an x absorbent.
JP15403597A 1997-06-11 1997-06-11 Exhaust gas purification device for internal combustion engine Expired - Lifetime JP3449174B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15403597A JP3449174B2 (en) 1997-06-11 1997-06-11 Exhaust gas purification device for internal combustion engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15403597A JP3449174B2 (en) 1997-06-11 1997-06-11 Exhaust gas purification device for internal combustion engine

Publications (2)

Publication Number Publication Date
JPH112114A true JPH112114A (en) 1999-01-06
JP3449174B2 JP3449174B2 (en) 2003-09-22

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2342056A (en) * 1998-09-18 2000-04-05 Toyota Motor Co Ltd NOx trap with oxygen storage components for an i.c.e.
JP2001276622A (en) * 2000-03-31 2001-10-09 Isuzu Motors Ltd Nitrogen oxide storage reduction catalyst
US7344684B2 (en) 2003-07-30 2008-03-18 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Exhaust emission purifying catalyst device
US11652207B2 (en) 2009-09-18 2023-05-16 A123 Systems Llc High power electrode materials

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0597106B1 (en) 1991-10-14 1997-04-02 Toyota Jidosha Kabushiki Kaisha Exhaust and purification device for internal combustion engines

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2342056A (en) * 1998-09-18 2000-04-05 Toyota Motor Co Ltd NOx trap with oxygen storage components for an i.c.e.
GB2342056B (en) * 1998-09-18 2001-04-04 Toyota Motor Co Ltd An exhaust gas purification device for an internal combustion engine
US6499294B1 (en) 1998-09-18 2002-12-31 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification device for an internal combustion engine
JP2001276622A (en) * 2000-03-31 2001-10-09 Isuzu Motors Ltd Nitrogen oxide storage reduction catalyst
US7344684B2 (en) 2003-07-30 2008-03-18 Mitsubishi Jidosha Kogyo Kabushiki Kaisha Exhaust emission purifying catalyst device
US11652207B2 (en) 2009-09-18 2023-05-16 A123 Systems Llc High power electrode materials

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