JPH0598954A - Exhaust emission control system for internal combustion engine - Google Patents
Exhaust emission control system for internal combustion engineInfo
- Publication number
- JPH0598954A JPH0598954A JP28409691A JP28409691A JPH0598954A JP H0598954 A JPH0598954 A JP H0598954A JP 28409691 A JP28409691 A JP 28409691A JP 28409691 A JP28409691 A JP 28409691A JP H0598954 A JPH0598954 A JP H0598954A
- Authority
- JP
- Japan
- Prior art keywords
- nox
- exhaust gas
- absorbent
- bypass valve
- temperature
- 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
Links
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
- F01N3/0807—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
- F01N3/0828—Exhaust 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
- F01N3/0842—Nitrogen oxides
-
- 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
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
-
- 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
- F01N3/0807—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
- F01N3/0871—Regulation of absorbents or adsorbents, e.g. purging
- F01N3/0878—Bypassing absorbents or adsorbents
-
- 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
- F01N3/18—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 methods of operation; Control
- F01N3/20—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 methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2053—By-passing catalytic reactors, e.g. to prevent overheating
-
- 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
- F01N2250/00—Combinations of different methods of purification
- F01N2250/12—Combinations of different methods of purification absorption or adsorption, and catalytic conversion
-
- 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
- F01N2410/00—By-passing, at least partially, exhaust from inlet to outlet of apparatus, to atmosphere or to other device
- F01N2410/12—By-passing, at least partially, exhaust from inlet to outlet of apparatus, to atmosphere or to other device in case of absorption, adsorption or desorption of exhaust gas constituents
-
- 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
- F01N3/18—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 methods of operation; Control
- F01N3/20—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 methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、HCのほとんど出ない
内燃機関システムでも、また常時空燃比リーン域で運転
される内燃機関システムでも、NOx 吸収材とNOx 分
解触媒の組合せでNOx を浄化する内燃機関の排気浄化
装置に関する。BACKGROUND OF THE INVENTION The present invention purifies NOx using a combination of a NOx absorbent and a NOx decomposing catalyst, even in an internal combustion engine system that emits almost no HC, or in an internal combustion engine system that always operates in a lean air-fuel ratio range. The present invention relates to an exhaust emission control device for an internal combustion engine.
【0002】[0002]
【従来の技術】燃費の向上とCO2 排出量低減を一挙に
満足させるために、空燃比がリーン域で燃焼を行なうリ
ーンバーンエンジンの開発が進められ、一部実用化され
ている。2. Description of the Related Art A lean burn engine that burns in a lean region of an air-fuel ratio has been developed and partially put into practical use in order to improve fuel efficiency and reduce CO 2 emission all at once.
【0003】リーンバーンエンジンでの課題は、空燃比
リーン域の排気ガス中では、三元触媒がNOx 浄化能力
をほとんどもたないことから、空燃比リーン域の排気ガ
ス中でもNOx を浄化できるシステムを開発することで
ある。The problem with the lean burn engine is that the three-way catalyst has almost no NOx purification capability in the exhaust gas in the lean range of the air-fuel ratio, so a system capable of purifying NOx in the exhaust gas in the lean range of the air-fuel ratio is required. It is to develop.
【0004】空燃比リーン域でもNOx を浄化できる触
媒として、特開平1−139145号公報は、ゼオライ
トに遷移金属(Cu)をイオン交換して担持させた、い
わゆるリーンNOx 触媒を提案している。この触媒は、
HC存在下でNOx を還元できる。As a catalyst capable of purifying NOx even in a lean air-fuel ratio range, Japanese Patent Laid-Open No. 1-139145 proposes a so-called lean NOx catalyst in which a transition metal (Cu) is ion-exchanged and supported on zeolite. This catalyst is
NOx can be reduced in the presence of HC.
【0005】また、リーンバーンエンジンのNOx を浄
化するシステムとして、本出願人により先に、Ba−C
u−O系のNOx 吸収材と三元触媒との組合せから成る
排気浄化装置が提案されている。このシステムでは、空
燃比リーン域で低温でNOxをNOx 吸収材に吸蔵して
おき、空燃比がストイキになって排気ガス温が高温にな
ったときにNOx 吸収材にNOxを放出させ、この放出
させたNOx を下流の三元触媒で、空燃比ストイキ時に
あることを利用して、還元させるものであった。Further, as a system for purifying NOx of a lean burn engine, the applicant of the present invention has previously described Ba-C.
An exhaust gas purification device has been proposed which is composed of a combination of a uO-based NOx absorbent and a three-way catalyst. In this system, NOx is stored in the NOx absorbent at low temperature in the lean range of the air-fuel ratio, and when the air-fuel ratio becomes stoichiometric and the exhaust gas temperature becomes high, NOx is released to the NOx absorbent, and this release The NOx thus produced was reduced by the downstream three-way catalyst by utilizing the fact that the air-fuel ratio was stoichiometric.
【0006】[0006]
【発明が解決しようとする課題】しかし、リーンNOx
触媒には、NOx の還元にHCを必要とするので、HC
のほとんど出ないシステム、たとえば、ディーゼルエン
ジンの場合等には、燃焼を一部犠牲にしてHCを生成し
なければならず、折角のリーンバーンの燃費の向上とい
う効果を十分には引き出せないという問題がある。[Problems to be Solved by the Invention] However, lean NOx
The catalyst requires HC to reduce NOx, so HC
In the case of a system that does not generate much, for example, in the case of a diesel engine, it is necessary to generate HC by partially sacrificing combustion, and it is not possible to sufficiently bring out the effect of improving fuel efficiency of lean burn. There is.
【0007】また、NOx 吸収材と三元触媒の組合せの
システムには、常時、空燃比リーン域で運転されるよう
なエンジン、たとえばディーゼルエンジンでは、三元触
媒がNOx 浄化の働きをする機会をもつことができず、
NOx 吸収材が飽和した後はNOx がそのまま外部に流
れ出てしまうという問題がある。In addition, in a system of a combination of a NOx absorbent and a three-way catalyst, in an engine which is always operated in a lean region of the air-fuel ratio, such as a diesel engine, the three-way catalyst has an opportunity to perform NOx purification. I ca n’t hold it,
After the NOx absorbent is saturated, there is a problem that NOx flows out as it is.
【0008】本発明の目的は、HCのほとんど出ないエ
ンジンでも、また常時空燃比リーン域で運転されるエン
ジンでも、NOx を浄化し得る内燃機関の排気浄化装置
を提供することにある。It is an object of the present invention to provide an exhaust gas purification apparatus for an internal combustion engine which can purify NOx even in an engine that emits almost no HC and in an engine that always operates in a lean air-fuel ratio range.
【0009】[0009]
【課題を解決するための手段】上記目的は、本発明によ
れば、次の内燃機関の排気浄化装置によって達成され
る。すなわち、内燃機関の排気通路に設置された、所定
温度以下でNOx を吸収し該吸収したNOx を前記所定
温度を超える温度で放出するNOx 吸収材および該NO
x 吸収材より下流のNOx 分解触媒と、前記NOx 吸収
材および前記NOx 分解触媒をバイパスするバイパス通
路と、前記NOx 吸収材およびNOx分解触媒側に流れ
る排気ガス量と前記バイパス通路に流れる排気ガス量と
の割合を変えるバイパスバルブと、排気ガス温度が所定
温度を超えたときに、所定時間、前記NOx 吸収材およ
びNOx 分解触媒側に流れる排気ガス量を絞るように前
記バイパスバルブを制御するバイパスバルブ制御手段
と、を備えた内燃機関の排気浄化装置。According to the present invention, the above object is achieved by the following exhaust gas purification apparatus for an internal combustion engine. That is, the NOx absorbent installed in the exhaust passage of the internal combustion engine, which absorbs NOx at a predetermined temperature or lower and releases the absorbed NOx at a temperature higher than the predetermined temperature, and the NOx absorbent.
NOx decomposing catalyst downstream from the x absorbent, a bypass passage bypassing the NOx absorbing material and the NOx decomposing catalyst, an exhaust gas amount flowing to the NOx absorbent and the NOx decomposing catalyst side, and an exhaust gas amount flowing to the bypass passage. And a bypass valve for controlling the bypass valve so as to throttle the amount of exhaust gas flowing to the NOx absorbent and the NOx decomposition catalyst side for a predetermined time when the exhaust gas temperature exceeds a predetermined temperature. An exhaust emission control device for an internal combustion engine, comprising: a control unit.
【0010】[0010]
【作用】たとえばBa−Cu−O系のNOx 吸収材は、
所定温度(約500°C)以下で比較的長時間にわたっ
てNOx を吸蔵し、所定温度を超えると短時間でNOx
を放出する。また、上記NOx 分解触媒は、HCが非存
在下でも、空間速度が低いと、NOx をN2 とO2に分
解する。For example, the Ba-Cu-O-based NOx absorbent is
It occludes NOx for a relatively long time below a specified temperature (about 500 ° C), and when it exceeds the specified temperature, it will occlude in a short time.
To release. Further, the NOx decomposing catalyst decomposes NOx into N 2 and O 2 when the space velocity is low even in the absence of HC.
【0011】NOx 吸収材を車両の床下に配置している
ような場合には、通常運転時、エンジンからの排気ガス
は途中の排気管での放熱で500°C以下になるので、
NOx はNOx 吸収材に吸収され、外部への放出が抑制
される。加速時等、排気温度が上昇する時、NOx 吸収
材は所定温度を超え、それまで吸蔵したNOx を放出
し、短時間のうちに自身は再生される。放出されたNO
x は下流側のNOx 分解触媒に至り、そこでN2 とO2
に分解されるので、外部への放出が抑制される。When the NOx absorbent is placed under the floor of the vehicle, the exhaust gas from the engine during normal operation becomes 500 ° C. or less due to heat dissipation in the exhaust pipe on the way.
NOx is absorbed by the NOx absorbent, and its release to the outside is suppressed. When the exhaust gas temperature rises, such as during acceleration, the NOx absorbent exceeds a predetermined temperature, releases the NOx stored up to that point, and regenerates itself in a short time. NO released
x reaches the NOx decomposition catalyst on the downstream side, where N 2 and O 2
As it is decomposed into, the release to the outside is suppressed.
【0012】NOx 分解触媒は、Cu−ZSM−5、P
t/Al2 O3 、またはCo/Al2 O3 などから成
り、HC(還元剤)がなくても、低空間速度状態下でN
Ox を分解する。ディーゼルエンジンの空間速度SVは
高く、そのままではNOx 分解触媒のNOx 分解能力は
弱いから、排気高温時にはバイパスバルブでNOx吸収
材およびNOx 分解触媒側に流れる排気ガス量を絞って
低SVとする。この場合、バイパス通路側に流される排
気ガスはNOx を浄化されることなく排出されるが、こ
のような状態は短時間、たとえば10秒間、しか続かな
いから問題ない。The NOx decomposition catalyst is Cu-ZSM-5, P
It is composed of t / Al 2 O 3 or Co / Al 2 O 3, etc., and is N under low space velocity conditions even without HC (reducing agent).
Decomposes Ox. Since the space velocity SV of a diesel engine is high and the NOx decomposing catalyst has a weak NOx decomposing ability as it is, a bypass valve is used to reduce the amount of exhaust gas flowing to the NOx absorbent and the NOx decomposing catalyst side at high exhaust temperature to reduce the SV. In this case, the exhaust gas flowing to the side of the bypass passage is discharged without purifying NOx, but such a state lasts only for a short time, for example, 10 seconds, which causes no problem.
【0013】[0013]
【実施例】以下に、本発明に係る内燃機関の排気浄化装
置の一実施例を、図面を参照して説明する。図1に示す
ように、内燃機関(たとえば、ディーゼルエンジン)の
排気通路6には、NOx 吸収材2とその下流にNOx 分
解触媒4とが配置される。排気通路6には、NOx 吸収
材2およびNOx 分解触媒4をバイパスするように、バ
イパス通路8が設けられる。排気通路6とバイパス通路
8との分岐点には、NOx 吸収材2およびNOx 分解触
媒4側に流れる排気ガス量と、バイパス通路8に流れる
排気ガス量との割合を変えるバイパスバルブ10が設け
られる。バイパスバルブ10は、バイパスバルブ制御手
段12によって制御され、排気ガス温度Tが所定温度T
0 を超えたときに、所定時間、たとえば10秒間、NO
x 吸収材2およびNOx 分解触媒4側に流れる排気ガス
量が絞られる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of an exhaust gas purifying apparatus for an internal combustion engine according to the present invention will be described below with reference to the drawings. As shown in FIG. 1, an NOx absorbent 2 and a NOx decomposition catalyst 4 are arranged downstream of the NOx absorbent 2 in an exhaust passage 6 of an internal combustion engine (for example, a diesel engine). A bypass passage 8 is provided in the exhaust passage 6 so as to bypass the NOx absorbent 2 and the NOx decomposition catalyst 4. A bypass valve 10 is provided at a branch point between the exhaust passage 6 and the bypass passage 8 to change the ratio of the amount of exhaust gas flowing to the NOx absorbent 2 and the NOx decomposition catalyst 4 side to the amount of exhaust gas flowing to the bypass passage 8. .. The bypass valve 10 is controlled by the bypass valve control means 12 so that the exhaust gas temperature T is the predetermined temperature T.
When it exceeds 0 , NO for a predetermined time, for example, 10 seconds.
The amount of exhaust gas flowing to the x absorber 2 and the NOx decomposition catalyst 4 side is throttled.
【0014】図2は、具体的な系統図を示している。1
4は制御装置で、マイクロコンピュータから成る。バイ
パスバルブ制御手段12は制御装置14に記憶されたプ
ログラム中に、すなわち図3、図4のプログラム中に設
定されている手段から成る。制御装置14は、演算を実
行するセントラルプロセッサユニット(CPU)14
a、読出し専用のメモリであるリードオンリメモリ(R
OM)14b、一時記憶用のメモリであるランダムアク
セスメモリ(RAM)14bc、アナログ量をディジタ
ル量に変換するA/Dコンバータ14d、インプットイ
ンタフェース14e、アウトプットインタフェース14
f、を備えている。制御装置14には、さらに、後述す
るタイマ14gが接続されている。FIG. 2 shows a concrete system diagram. 1
Reference numeral 4 is a control device, which is composed of a microcomputer. The bypass valve control means 12 comprises means set in the program stored in the control device 14, that is, in the programs of FIGS. The control device 14 is a central processor unit (CPU) 14 that executes calculations.
a, read only memory (R
OM) 14b, random access memory (RAM) 14bc that is a memory for temporary storage, A / D converter 14d that converts an analog amount into a digital amount, an input interface 14e, an output interface 14
f. A timer 14g, which will be described later, is further connected to the control device 14.
【0015】排気通路6には、NOx 吸収材2の上流に
排気温センサ16が設置されており、その出力はA/D
コンバータ14dに入力され、演算における排気温Tと
して用いられる。またCPU14aの演算の指令は、ア
ウトプットインタフェース14fを介してバイパスバル
ブ10のアクチュエータに送られ、バイパスバルブ10
が制御される。An exhaust temperature sensor 16 is installed upstream of the NOx absorbent 2 in the exhaust passage 6, and its output is A / D.
It is input to the converter 14d and used as the exhaust temperature T in the calculation. Further, the calculation command of the CPU 14a is sent to the actuator of the bypass valve 10 via the output interface 14f, and the bypass valve 10
Is controlled.
【0016】上記装置において、NOx 吸収材2は、通
常運転時に排気ガス温度が約500°C以下になり、加
速時等に排気ガス温度が500°Cを超える排気通路部
分に配置される。このような排気通路部分は、図5に示
すように、通常、エンジン18から離れた、車両20の
床下部分である。図5にて、22はマフラを示してい
る。In the above apparatus, the NOx absorbent 2 is disposed in the exhaust passage portion where the exhaust gas temperature is about 500 ° C or less during normal operation and the exhaust gas temperature exceeds 500 ° C during acceleration or the like. Such an exhaust passage portion is usually an underfloor portion of the vehicle 20, which is separated from the engine 18, as shown in FIG. In FIG. 5, 22 indicates a muffler.
【0017】NOx 吸収材2は、所定温度(たとえば5
00°C)以下でNOx を吸収し、吸収したNOx を前
記所定温度を超える温度で放出する固体材から成り、こ
のような性質をもつNOx 吸収材として、アルカリ土類
と銅の複合酸化物(Ba−Cu−O系)、たとえばMn
O2 ・BaCuO2 がある。Ba−Cu−O系のNOx
吸収材2は、約500°C以下で、NOをNO2 の型に
し、それを安定してNOx 吸収材結晶構造の中に吸収で
きる。Ba−Cu−O系NOx 吸収材2は、約500°
Cを超える温度で、そのNO2 吸収能力を喪失し、それ
まで吸収していたNO2 を、吸収工程に比べてはるかに
速やかに、放出する性質をもつ。たとえば、数時間をか
けて吸収したものを約10秒間で放出する。The NOx absorbent 2 has a predetermined temperature (for example, 5
It is made of a solid material that absorbs NOx at a temperature of less than 00 ° C and releases the absorbed NOx at a temperature higher than the above-mentioned predetermined temperature. As a NOx absorbent having such properties, a composite oxide of alkaline earth and copper ( Ba-Cu-O system), for example, Mn
There are O 2 and BaCuO 2 . Ba-Cu-O-based NOx
At about 500 ° C. or below, the absorber 2 turns NO into NO 2 type and can stably absorb it into the NO x absorber crystal structure. The Ba-Cu-O-based NOx absorbent 2 is about 500 °
At temperatures in excess of C, the NO 2 lost absorption capacity, the NO 2 which has been absorbed far, far rapidly than the absorption step has a property of releasing. For example, what is absorbed over several hours is released in about 10 seconds.
【0018】上記のBa−Cu−O系NOx 吸収材2
は、たとえば、次のようにして作製される。 製作例1 白金入り 硝酸銅と硝酸Baを等モル比混合し、650°Cで4時
間空気中で焼成した。これを8硝酸白金中に浸漬し、白
金を担持した。その後500°Cで窒素気流中で焼成し
た。 製作例2 セリウム入り 硝酸銅と硝酸Baを等モル比混合し、650°Cで4時
間空気中で焼成した。これを硝酸セリウム溶液中に浸漬
し、セリウムを担持した。その後500°C空気流中で
焼成した。 モノリス化 上記焼成物の粉末を100部、シリカゾルを100部、
部水を10部混合したスラリーを調整し、コージェライ
ト製のモノリスをその中に浸漬した。引上げセルのつま
りをエア吹きで取り除き、250°Cで乾燥した。一連
の操作を数回繰り返した。その後、500°Cで焼成
し、NOx 吸収材2を得た。The above Ba-Cu-O-based NOx absorbent 2
Is produced, for example, as follows. Production Example 1 Platinum-containing copper nitrate and Ba nitrate were mixed in an equimolar ratio and calcined in air at 650 ° C. for 4 hours. This was immersed in platinum octanitrate to support platinum. Then, it was baked in a nitrogen stream at 500 ° C. Production Example 2 Copper nitrate containing cerium and Ba nitrate were mixed in an equimolar ratio, and the mixture was baked at 650 ° C. for 4 hours in air. This was immersed in a cerium nitrate solution to carry cerium. Then, it was fired in an air stream at 500 ° C. Monolithization 100 parts of the powder of the above fired product, 100 parts of silica sol,
A slurry was prepared by mixing 10 parts of partial water, and a monolith made of cordierite was immersed therein. The plugging cell was clogged with air and dried at 250 ° C. A series of operations was repeated several times. Then, it was baked at 500 ° C. to obtain a NOx absorbent 2.
【0019】また、図6は、Ba−Cu−O(Ba:C
u=1:13)NOx吸収材にNOx を供給した際の出
口ガスにおけるNO濃度と温度との特性を示している。
ただし、酸素非共存下で、空間速度は6000/時の場
合である。酸素共存下で試験すると図6のNOx 放出特
性は50−100°C右側にずれる。このことから、B
a−Cu−O系のNOx 吸収材は、空燃比がリーン域の
酸素過剰の排気中で、約500°Cを超える温度でNO
x を放出し、約500°C以下ではNOx を吸収するこ
とがわかる。また、空燃比をストイキまたはリッチにす
ると、酸素非共存下に近くなってNOx 放出特性が低温
側にずれ、NOx 放出は促進される。Further, FIG. 6 shows that Ba--Cu--O (Ba: C).
u = 1: 13) Shows the characteristics of NO concentration and temperature in the outlet gas when NOx is supplied to the NOx absorbent.
However, the space velocity is 6000 / hour in the absence of oxygen. When tested in the presence of oxygen, the NOx emission characteristics of FIG. 6 shift to the right at 50-100 ° C. From this, B
The a-Cu-O-based NOx absorbent is NO at a temperature exceeding about 500 ° C in exhaust gas with excess oxygen in the lean air-fuel ratio range.
It can be seen that x is released and NOx is absorbed below about 500 ° C. Further, when the air-fuel ratio is stoichiometric or rich, the NOx releasing characteristic shifts to the low temperature side due to the near non-oxygen coexistence, and the NOx releasing is promoted.
【0020】また、NOx 分解触媒4は、Cu−ZSM
−5、すなわちゼオライトZSM−5にCu等の遷移金
属をイオン交換して担持した触媒、またはアルミナAl
2 O3 に白金Ptを担持した触媒、またはアルミナにコ
バルトCoを担持した触媒などから成り、これらは何れ
も、NOxを、低空間速度で、炭化水素HC無しで、N
2 とO2 に分解できる。逆にHC量が多すぎるとHC被
毒を起してNOx 分解効率が低下し、また高空間速度で
はNOx 分解効率が悪い。したがって、NOx吸収材2
が高温域でNOx を放出しているときには、放出された
NOx を高効率で分解するために、NOx 分解触媒4の
単位面積あたりを流れる排気ガス流は低速(低空間速
度)でなければならず、このために、バイパスバルブ制
御手段12は、排気ガス高温時に、NOx 吸収材2およ
びNOx 分解触媒4側に流れる排気ガスを絞るように、
バイパスバルブ10を制御する。The NOx decomposition catalyst 4 is Cu-ZSM.
-5, that is, a catalyst in which a transition metal such as Cu is ion-exchanged and supported on zeolite ZSM-5, or alumina Al
It is composed of a catalyst in which platinum Pt is supported on 2 O 3 , a catalyst in which cobalt Co is supported on alumina, and the like, each of which contains NOx at a low space velocity and no hydrocarbon HC,
It can be decomposed into 2 and O 2 . On the contrary, if the amount of HC is too large, the poisoning of HC will occur and the NOx decomposition efficiency will decrease, and at high space velocity, the NOx decomposition efficiency will be poor. Therefore, the NOx absorbent 2
When releasing NOx in a high temperature range, the exhaust gas flow flowing per unit area of the NOx decomposing catalyst 4 must be low speed (low space velocity) in order to decompose the released NOx with high efficiency. For this reason, the bypass valve control means 12 throttles the exhaust gas flowing to the NOx absorbent 2 and the NOx decomposition catalyst 4 side when the exhaust gas temperature is high.
The bypass valve 10 is controlled.
【0021】図3、図4は、通常運転時はNOx をNO
x 吸収材2に吸収し、排気高温時にNOx 吸収材2にN
Ox を放出させるとともに排気ガス流を絞ってNOx 分
解触媒4にNOx を分解させるように、バイパスバルブ
10を制御するためのプログラムのフローチャートを示
している。これらのプログラムはROM14bに記憶さ
れており、CPU14aに読出されて演算が実行され
る。図3、図4のフローチャートは、一定時間間隔で割
込まれる。3 and 4 show that NOx is NO during normal operation.
The NOx absorbent 2 absorbs N when the exhaust temperature is high.
A flow chart of a program for controlling the bypass valve 10 so as to release Ox and throttle the exhaust gas flow to cause the NOx decomposition catalyst 4 to decompose NOx is shown. These programs are stored in the ROM 14b and are read by the CPU 14a to execute the calculation. The flowcharts of FIGS. 3 and 4 are interrupted at regular time intervals.
【0022】図3のフローにおいて、ステップ102
で、バイパスフラグ動作フラグFdbが1か否かが判定
される。Fdb=1が、バイパスフラグ10がNOx 吸
収材2およびNOx 分解触媒4側に流れる排気ガス量を
絞りバイパス通路8側にも排気ガスを流す場合に対応
し、Fdb=0が、排気ガスの全量がNOx 吸収材2お
よびNOx 分解触媒4側に流れている場合に対応する。In the flow of FIG. 3, step 102
Then, it is determined whether the bypass flag operation flag Fdb is 1 or not. Fdb = 1 corresponds to the case where the bypass flag 10 throttles the amount of exhaust gas flowing to the NOx absorbent 2 and the NOx decomposition catalyst 4 side and causes the exhaust gas to flow also to the bypass passage 8 side, and Fdb = 0 indicates the total amount of exhaust gas. Is flowing to the NOx absorbent 2 and the NOx decomposition catalyst 4 side.
【0023】ステップ102で、Fdb=1と判定され
た場合は、既にバイパスバルブ10が動作中であって、
ステップ104−110に通してバイパスバルブ動作を
行なう必要がないから、そのままリターンする。ステッ
プ102でFdb=1でないと判定された場合は、ステ
ップ104に進み、回転積算フラグFdgが1か否かを
判定する。Fdg=1は、NOx 吸収材2が再生された
後の積算時間SNeが所定時間SNeOを超えていず、
NOx 吸収材2が飽和していないことを意味し、Fdg
=0はNOx 吸収材2が飽和しているかあるいは飽和し
そうになっていることを意味する。If it is determined in step 102 that Fdb = 1, the bypass valve 10 is already in operation,
Since it is not necessary to perform the bypass valve operation through steps 104 to 110, the process directly returns. If it is determined in step 102 that Fdb = 1 is not satisfied, the process proceeds to step 104, and it is determined whether the rotation integration flag Fdg is 1. Fdg = 1 means that the integrated time SNe after the NOx absorbent 2 is regenerated does not exceed the predetermined time SNeO,
It means that the NOx absorbent 2 is not saturated, and Fdg
= 0 means that the NOx absorbent 2 is saturated or is about to be saturated.
【0024】ステップ104でFdg=1と判定された
場合は、NOx 吸収材2にNOx を放出させた後余り時
間が経過しておらず、NOx 吸収材2を再生する必要が
ないので、そのままリターンし、Fdg=1でないと判
定された場合はステップ106に進み、排気温Tが所定
温度T0 より高いか否かを判定する。ここで、T0 は、
NOx 吸収触媒2が、空燃比リーンの排気中で、NOx
を吸収する温度領域とNOx を放出する温度領域との境
目の温度であり、通常500°C近傍にある。When it is judged in step 104 that Fdg = 1, it is not necessary to regenerate the NOx absorbent 2 since no time has passed since the NOx absorbent 2 was released with NOx, and the process is returned as it is. If it is determined that Fdg = 1 is not established, the routine proceeds to step 106, where it is determined whether the exhaust temperature T is higher than the predetermined temperature T 0 . Where T 0 is
When the NOx absorption catalyst 2 is in the exhaust of lean air-fuel ratio, NOx
It is the temperature at the boundary between the temperature range that absorbs NOx and the temperature range that releases NOx, and is usually near 500 ° C.
【0025】ステップ104でTがT0 以下と判定され
た場合には、NOx 吸収材2はNOx を放出できる温度
にないから、そのままリターンし、TがT0 を超えると
判定された場合に、NOx 吸収材2が放出するNOx を
NOx 分解触媒4が高効率で分解できるようにバイパス
バルブ10を制御するために、ステップ108、110
へと進む。When it is determined in step 104 that T is equal to or less than T 0 , the NOx absorbent 2 is not at a temperature at which NOx can be released, and therefore, the routine returns as is, and when it is determined that T exceeds T 0 , In order to control the bypass valve 10 so that the NOx decomposition catalyst 4 can decompose NOx released by the NOx absorbent 2 with high efficiency, steps 108 and 110 are performed.
Go to.
【0026】ステップ108では、この経路を通るとき
にはバイパスバルブ10を動作させるので、バイパスバ
ルブ動作フラグFdbを1とおく。続いて、ステップ1
10に進み、バイパスバルブ10を動作させるととも
に、タイマ14gをONにする。バイパスバルブ10が
動作していることは、NOx 吸収材2およびNOx 分解
触媒4側に流れる排気ガス量を絞るようにバイパスバル
ブ10を操作することを意味する。In step 108, the bypass valve 10 is operated when passing through this route, so the bypass valve operation flag Fdb is set to 1. Then, step 1
10, the bypass valve 10 is operated and the timer 14g is turned on. The operation of the bypass valve 10 means that the bypass valve 10 is operated so as to reduce the amount of exhaust gas flowing to the NOx absorbent 2 and the NOx decomposition catalyst 4 side.
【0027】タイマ14gは、ON後約10秒後に、積
算エンジン回転数SNeを0にクリアするとともに、バ
イパスバルブ動作フラグFdbを0にクリアする。した
がって、タイマ14gは、バイパスバルブ10動作を約
10秒間継続させ、その間にNOx 吸収触媒2のNOx
放出を完了させ、NOx 放出が完了したであろうON後
10秒後に、Fdbを0にクリアする。上記において、
ステップ106、110、タイマ14gはバイパスバル
ブ制御手段12を構成する。The timer 14g clears the cumulative engine speed SNe to 0 and the bypass valve operation flag Fdb to 0 about 10 seconds after being turned on. Therefore, the timer 14g continues the operation of the bypass valve 10 for about 10 seconds, during which the NOx of the NOx absorption catalyst 2 is NOx.
The emission is completed, and Fdb is cleared to 0 10 seconds after the ON state when the NOx emission is supposed to be completed. In the above,
The steps 106 and 110 and the timer 14g constitute the bypass valve control means 12.
【0028】図3のルーチンから図4のルーチンへと割
込まれる。図4のルーチンは、図3のルーチンでNOx
吸収材2が再生されると、NOx 吸収材2が飽和する迄
はたとえ排気温TがT0 を超えてもバイパスバルブ10
を動作させないようにし、バイパス通路8を通って排気
ガスがNOx を浄化されることなく外部に流出される状
態が長時間続かないようにするためのルーチンである。The routine of FIG. 3 is interrupted by the routine of FIG. The routine of FIG. 4 is the same as the routine of FIG.
When the absorbent 2 is regenerated, the bypass valve 10 is kept until the NOx absorbent 2 is saturated even if the exhaust temperature T exceeds T 0.
Is a routine for preventing the exhaust gas from flowing through the bypass passage 8 to the outside without being purified of NOx for a long time.
【0029】ステップ202で、Fdb=1か否かを判
定する。タイマ14gON後約10秒後にはFdb=0
にクリアされるので、一定時間経過するまではFdb=
1でないため、ステップ204へと進み、NOx 吸収材
2の再生後の使用時間が、ルーチンへの割込み毎に積算
されていく。ステップ202でFdb=1と判定された
ときは、NOx 吸収材2が飽和寸前にあるので、そのま
まリターンして図3のルーチンへの次回の割込みに入っ
ていく。In step 202, it is determined whether Fdb = 1. About 10 seconds after turning on the timer 14g, Fdb = 0
Will be cleared to Fdb =
Since it is not 1, the routine proceeds to step 204, where the usage time after regeneration of the NOx absorbent 2 is accumulated for each interruption to the routine. When it is determined in step 202 that Fdb = 1, the NOx absorbent 2 is on the verge of saturation, and therefore the routine directly returns and enters the next interruption to the routine of FIG.
【0030】ステップ202でFdb=1と判定されて
ステップ204に進むと、エンジン回転積算SNeを積
算していき、ステップ206で、SNeが所定のエンジ
ン回転積算SNeOを超えたか否かを判定する。SNe
がSNeO以下なら、NOx吸収材2はまだ飽和してい
ないとみなしてよいから、ステップ212に進んでFd
g=1とおいて、図3の演算に備える。ステップ202
でSNeがSNeOを越えたと判定されると、ステップ
208、210に進みFdb=1、Fdg=1とおい
て、図3の演算に備える。When it is determined at step 202 that Fdb = 1 and the routine proceeds to step 204, the engine revolution integrated SNe is accumulated, and at step 206 it is determined whether SNe exceeds a predetermined engine revolution integrated SNeO. SNe
Is less than SNeO, it may be considered that the NOx absorbent 2 is not yet saturated, so the routine proceeds to step 212 and Fd
When g = 1, the preparation for the calculation in FIG. 3 is performed. Step 202
If it is determined that SNe has exceeded SNeO, the process proceeds to steps 208 and 210 to set Fdb = 1 and Fdg = 1 in preparation for the calculation of FIG.
【0031】つぎに、作用を説明する。通常運転時に
は、排気ガスの全量がNOx 吸収材2およびNOx 分解
触媒4側に流れている。この時は排気ガス温度はNOx
吸収材2の入口で500°C以下のため、排気ガス中の
NOx はNOx 吸収材2に吸収されていく。NOx 吸収
材2のNOx 吸収容量は、NOx 吸収材の容積にもよる
が、通常数時間連続してNOx を吸収できる程度にあ
る。数時間の連続運転の間には加速状態は繰返しあらわ
れ、その時には排気ガス温もNOx 吸収材2の入口で5
00°Cを超える。この高温状態ではNOx 吸収材2は
NOx を放出するので、これを利用してNOx吸収材2
の再生をはかる。すなわち、NOx 放出時には、NOx
分解触媒4が高効率のNOx 分解能力をもつように、バ
イパスバルブ10によってNOx 分解触媒4を流れる排
気ガス流を絞り、低空間速度とする。これによって、N
Ox 吸収材2から放出されたNOx はNOx 分解触媒4
で、高効率でN2 とO2 に分解される。Next, the operation will be described. During normal operation, the entire amount of exhaust gas flows to the NOx absorbent 2 and the NOx decomposition catalyst 4 side. At this time, the exhaust gas temperature is NOx
NOx in the exhaust gas is absorbed by the NOx absorbent 2 because it is 500 ° C or less at the inlet of the absorbent 2. Although the NOx absorption capacity of the NOx absorbent 2 depends on the volume of the NOx absorbent, it is usually such that it can absorb NOx continuously for several hours. During several hours of continuous operation, the accelerating condition appears repeatedly, and at that time, the exhaust gas temperature is 5 at the NOx absorbent 2 inlet.
Over 00 ° C. In this high temperature state, the NOx absorbent 2 releases NOx.
Try to play. That is, when releasing NOx, NOx
The bypass valve 10 restricts the exhaust gas flow flowing through the NOx decomposing catalyst 4 so that the decomposing catalyst 4 has a highly efficient NOx decomposing ability, so as to have a low space velocity. By this, N
The NOx released from the Ox absorbent 2 is the NOx decomposition catalyst 4
At high efficiency, it is decomposed into N 2 and O 2 .
【0032】NOx 吸収材2の再生、すなわち吸収NO
x の全量放出は、約10秒間、500°C以上の排気ガ
スを流すだけで達成される。この間は、排気ガスの一部
はバイパス通路8に流され、バイパス通路を通る排気ガ
スはNOx が分解されることなく外部へ排出されるが、
この状態は約10秒間と短いため、NOx 排出規制上、
問題にならない。Regeneration of the NOx absorbent 2, that is, absorbed NO
Full release of x is achieved by flowing exhaust gas above 500 ° C for about 10 seconds. During this time, a part of the exhaust gas is caused to flow into the bypass passage 8 and the exhaust gas passing through the bypass passage is discharged to the outside without decomposing NOx.
This state is as short as about 10 seconds, so due to NOx emission regulations,
It doesn't matter.
【0033】上記のNOx 吸収材2によるNOx の吸
収、および排気ガス高温時におけるNOx 分解触媒4に
よるNOx の分解は、HCの存在無しに行なわれること
ができ、しかも常時リーン域で運転される内燃機関、た
とえばディーゼルエンジンにおいても働くことができ
る。したがって、従来のリーンNOx 触媒や、NOx 吸
収材と三元触媒の組合せシステムが適用できない内燃機
関の排気システムのNOx浄化にも利用することができ
る。The absorption of NOx by the NOx absorbent 2 and the decomposition of NOx by the NOx decomposition catalyst 4 at high exhaust gas temperature can be performed without the presence of HC, and the internal combustion is always operated in the lean range. It can also work in engines, for example diesel engines. Therefore, it can also be used for NOx purification of an exhaust system of an internal combustion engine to which a conventional lean NOx catalyst or a combination system of a NOx absorbent and a three-way catalyst cannot be applied.
【0034】[0034]
【発明の効果】本発明によれば、内燃機関の排気通路に
NOx 吸収材とその下流にNOx 分解触媒を設け、NO
x 吸収材とNOx 分解触媒の両方をバイパスするバイパ
ス通路と、両通路への流量の割合を変えるバイパスバル
ブを設け、バイパスバルブ制御手段によって排気高温時
にNOx 吸収材およびNOx 分解触媒に流れる排気ガス
を絞るようにしたので、排気ガス中のHC量の多少また
は有無にかかわらず、かつ常時リーン域で運転されよう
とも、あるいはリーン域またはストイキの繰返しで運転
されようとも、効果的にNOx を浄化することができ
る。According to the present invention, the NOx absorbent and the NOx decomposition catalyst are provided downstream of the NOx absorbent in the exhaust passage of the internal combustion engine, and
A bypass passage that bypasses both the x-absorbent and the NOx-decomposing catalyst, and a bypass valve that changes the ratio of the flow rate to both passages are provided, and the exhaust gas flowing to the NOx-absorbing material and the NOx-decomposing catalyst at high exhaust temperature is provided by the bypass valve control means. Since it is throttled, it effectively purifies NOx regardless of whether the amount of HC in the exhaust gas is or not, and whether it is always operated in the lean range or is repeatedly operated in the lean range or stoichiometry. be able to.
【図1】本発明の一実施例に係る内燃機関の排気浄化装
置の系統図である。FIG. 1 is a system diagram of an exhaust gas purification device for an internal combustion engine according to an embodiment of the present invention.
【図2】図1よりさらに詳しい本発明実施例に係る内燃
機関の排気浄化装置の系統図である。FIG. 2 is a system diagram of an exhaust gas purification device for an internal combustion engine according to an embodiment of the present invention, which is more detailed than FIG.
【図3】図1で用いたNOx 吸収材の再生制御のフロー
チャートである。FIG. 3 is a flowchart of regeneration control of the NOx absorbent used in FIG.
【図4】NOx 吸収材の再生終了後一定時間SNeO経
過するまではNOx 再生ステップ106−110に入っ
ていかないようにするために各種フラグを制御するルー
チンのフローチャートである。FIG. 4 is a flowchart of a routine for controlling various flags so as not to enter NOx regeneration step 106-110 until a certain time SNeO has elapsed after the regeneration of the NOx absorbent is completed.
【図5】図1の内燃機関の排気浄化装置を車両に搭載し
た状態の概略側面図である。5 is a schematic side view of a state in which the exhaust emission control device for the internal combustion engine of FIG. 1 is mounted on a vehicle.
【図6】図1で用いたNOx 吸収材のNOx 吸収、放出
/排気温度特性図である。FIG. 6 is a NOx absorption / release / exhaust temperature characteristic diagram of the NOx absorbent used in FIG. 1.
2 NOx 吸収材 4 NOx 分解触媒 6 排気通路 8 バイパス通路 10 バイパスバルブ 12 バイパスバルブ制御手段 14 制御装置 16 排気温センサ 18 内燃機関 20 車両 22 マフラ 2 NOx absorbent 4 NOx decomposition catalyst 6 exhaust passage 8 bypass passage 10 bypass valve 12 bypass valve control means 14 control device 16 exhaust temperature sensor 18 internal combustion engine 20 vehicle 22 muffler
Claims (1)
温度以下でNOx を吸収し該吸収したNOx を前記所定
温度を超える温度で放出するNOx 吸収材および該NO
x 吸収材より下流のNOx 分解触媒と、 前記NOx 吸収材および前記NOx 分解触媒をバイパス
するバイパス通路と、 前記NOx 吸収材およびNOx 分解触媒側に流れる排気
ガス量と前記バイパス通路に流れる排気ガス量との割合
を変えるバイパスバルブと、 排気ガス温度が所定温度を超えたときに、所定時間、前
記NOx 吸収材およびNOx 分解触媒側に流れる排気ガ
ス量を絞るように前記バイパスバルブを制御するバイパ
スバルブ制御手段と、を備えたことを特徴とする内燃機
関の排気浄化装置。1. An NOx absorbent installed in an exhaust passage of an internal combustion engine, which absorbs NOx at a predetermined temperature or lower and releases the absorbed NOx at a temperature higher than the predetermined temperature, and the NOx.
NOx decomposition catalyst downstream from the x absorbent, a bypass passage bypassing the NOx absorbent and the NOx decomposition catalyst, an exhaust gas amount flowing to the NOx absorbent and the NOx decomposition catalyst side, and an exhaust gas amount flowing to the bypass passage. And a bypass valve that controls the bypass valve so that when the exhaust gas temperature exceeds a predetermined temperature, the amount of exhaust gas flowing to the NOx absorbent and the NOx decomposition catalyst side is throttled for a predetermined time. An exhaust emission control device for an internal combustion engine, comprising: a control means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28409691A JP2734838B2 (en) | 1991-10-04 | 1991-10-04 | Exhaust gas purification device for internal combustion engine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28409691A JP2734838B2 (en) | 1991-10-04 | 1991-10-04 | Exhaust gas purification device for internal combustion engine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0598954A true JPH0598954A (en) | 1993-04-20 |
JP2734838B2 JP2734838B2 (en) | 1998-04-02 |
Family
ID=17674163
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28409691A Expired - Lifetime JP2734838B2 (en) | 1991-10-04 | 1991-10-04 | Exhaust gas purification device for internal combustion engine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2734838B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1785607A1 (en) * | 2005-11-11 | 2007-05-16 | Bayerische Motoren Werke Aktiengesellschaft | Exhaust system for an internal combustion engine |
-
1991
- 1991-10-04 JP JP28409691A patent/JP2734838B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1785607A1 (en) * | 2005-11-11 | 2007-05-16 | Bayerische Motoren Werke Aktiengesellschaft | Exhaust system for an internal combustion engine |
Also Published As
Publication number | Publication date |
---|---|
JP2734838B2 (en) | 1998-04-02 |
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