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JP2830652B2 - Exhaust gas purification device for internal combustion engine - Google Patents
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JP2830652B2 - Exhaust gas purification device for internal combustion engine - Google Patents

Exhaust gas purification device for internal combustion engine

Info

Publication number
JP2830652B2
JP2830652B2 JP26389292A JP26389292A JP2830652B2 JP 2830652 B2 JP2830652 B2 JP 2830652B2 JP 26389292 A JP26389292 A JP 26389292A JP 26389292 A JP26389292 A JP 26389292A JP 2830652 B2 JP2830652 B2 JP 2830652B2
Authority
JP
Japan
Prior art keywords
nox
exhaust gas
exhaust
absorbent
oxygen
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.)
Expired - Lifetime
Application number
JP26389292A
Other languages
Japanese (ja)
Other versions
JPH06117220A (en
Inventor
康 荒木
信也 広田
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP26389292A priority Critical patent/JP2830652B2/en
Publication of JPH06117220A publication Critical patent/JPH06117220A/en
Application granted granted Critical
Publication of JP2830652B2 publication Critical patent/JP2830652B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Combined Controls Of Internal Combustion Engines (AREA)
  • Exhaust Gas After Treatment (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は内燃機関の排気浄化装置
に関し、詳細にはディーゼルエンジンや希薄燃焼ガソリ
ンエンジン等のように大部分の領域でリーン空燃比の燃
焼を行う内燃機関の排気中のNOxを効率的に除去する
排気浄化装置に関する。
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 an exhaust gas purifying apparatus for an internal combustion engine which burns at a lean air-fuel ratio in most areas such as a diesel engine and a lean burn gasoline engine. The present invention relates to an exhaust gas purification device that efficiently removes NOx.

【0002】[0002]

【従来の技術】リーン空燃比の燃焼を行う内燃機関の排
気中のNOx浄化方法に例としては、特開昭62−10
6826号公報に記載されたものがある。同公報の方法
では、ディーゼルエンジンの排気通路に、酸素存在下で
NOxを酸化吸収する触媒を配置し、触媒のNOx吸収
効率が低下した時点で触媒への排気流入を遮断して触媒
に還元剤を導入することにより吸収したNOxを放出さ
せると共に還元浄化している。
2. Description of the Related Art An example of a method for purifying NOx in exhaust gas of an internal combustion engine performing combustion at a lean air-fuel ratio is disclosed in Japanese Patent Application Laid-Open No. 62-10 / 1987.
There is one described in Japanese Patent No. 6826. According to the method disclosed in the publication, a catalyst that oxidizes and absorbs NOx in the presence of oxygen is disposed in an exhaust passage of a diesel engine, and when the NOx absorption efficiency of the catalyst is reduced, the inflow of exhaust gas to the catalyst is cut off and the reducing agent Is introduced to release the absorbed NOx and to purify by reduction.

【0003】[0003]

【発明が解決しようとする課題】前記特開昭62−10
6826号公報では、酸素を多量に含む排気の触媒への
流入を遮断して触媒に還元剤を導入することにより触媒
部分の酸素濃度を低下させて触媒からのNOxの放出と
還元浄化を行っている。しかし、上記公報の方法では、
触媒からのNOx放出及び浄化を行う際に触媒への排気
流入を遮断する必要があり、機関運転中にNOxの放
出、浄化を行うためには排気系に複数のNOx吸収触媒
を並列配置して順次切換えて排気流入を遮断し、放出、
浄化を行う必要がある。このため、上記方法では複数の
排気系が必要となり、装置の複雑化や車両への搭載性の
悪化を生じる恐れがある。
The above-mentioned Japanese Patent Application Laid-Open No. 62-10 / 1987.
Japanese Patent No. 6826 discloses that the exhaust gas containing a large amount of oxygen is blocked from flowing into the catalyst and a reducing agent is introduced into the catalyst to lower the oxygen concentration in the catalyst portion to release NOx from the catalyst and perform reduction purification. I have. However, in the method of the above publication,
When releasing and purifying NOx from the catalyst, it is necessary to shut off the inflow of exhaust gas to the catalyst. To release and purify NOx during operation of the engine, a plurality of NOx absorption catalysts are arranged in parallel in the exhaust system. Switching sequentially to shut off the exhaust inflow, release,
It is necessary to purify. For this reason, in the above method, a plurality of exhaust systems are required, and there is a possibility that the device becomes complicated and the mountability to a vehicle is deteriorated.

【0004】一方、触媒への排気流入を遮断せずに還元
剤の導入のみによって触媒からのNOxの放出、浄化を
行えば、上述の排気系の複雑化は防止できるものの、大
量の酸素を含む排気の流入下で触媒を還元雰囲気に保持
するためには触媒から放出されるNOxの放出、還元に
必要な量に加え、流入する排気中の酸素を消費して還元
雰囲気を生成するために大量の還元剤が必要となる。こ
のため還元剤の消費量が増大し、特に燃料油を還元剤と
して使用する場合には燃費が悪化する問題を生じる。
On the other hand, if NOx is released and purified from the catalyst only by introducing a reducing agent without interrupting the flow of exhaust gas into the catalyst, the above-mentioned complicated exhaust system can be prevented, but a large amount of oxygen is contained. In order to maintain the catalyst in a reducing atmosphere under the flow of exhaust gas, in addition to the amount required for the release and reduction of NOx released from the catalyst, a large amount of oxygen is used to generate a reducing atmosphere by consuming oxygen in the inflowing exhaust gas. Requires a reducing agent. For this reason, the consumption of the reducing agent increases, and a problem arises that fuel efficiency deteriorates, especially when fuel oil is used as the reducing agent.

【0005】本発明は、上記問題に鑑み、排気系の構成
を複雑化することなく、しかも還元剤の消費量の増大を
生じることなくリーン空燃比の排気中のNOxを除去可
能な排気浄化装置を提供することを目的としている。
SUMMARY OF THE INVENTION In view of the above problems, the present invention provides an exhaust gas purifying apparatus capable of removing NOx in exhaust gas having a lean air-fuel ratio without complicating the structure of an exhaust system and without increasing the consumption of a reducing agent. It is intended to provide.

【0006】[0006]

【課題を解決するための手段】本発明によれば、少くと
も大部分の運転領域でリーン空燃比の燃焼を行う内燃機
関の排気浄化装置であって、機関の排気通路に排気空燃
比がリーンのときにNOxを吸収し、排気酸素濃度が低
下すると吸収したNOxを放出するNOx吸収剤を配置
し、所定の運転条件下で排気中に還元剤を導入すること
により排気酸素濃度を低下させ前記吸収剤からNOxを
放出させると共に放出されたNOxを還元浄化する排気
浄化装置において、前記還元剤導入時に前記NOx吸収
剤に流入する排気中の酸素を消費して前記NO X 吸収剤
からのNO X 放出時の還元剤消費量を低減する酸素消費
手段を設けたことを特徴とする内燃機関の排気浄化装置
が提供される。
According to the present invention, there is provided an exhaust purification system for an internal combustion engine which burns at a lean air-fuel ratio in at least most of the operating range, wherein the exhaust air-fuel ratio is reduced in an exhaust passage of the engine. A NOx absorbent that absorbs NOx at the time of release and releases the absorbed NOx when the exhaust oxygen concentration is lowered is arranged, and a reducing agent is introduced into the exhaust under predetermined operating conditions to lower the exhaust oxygen concentration to reduce the exhaust oxygen concentration. in the exhaust purifying apparatus reduces and purifies the released NOx with the release of NOx from the absorbent, the the NO X absorbent to consume oxygen in the exhaust gas flowing into the NOx absorbent when the reducing agent introduced
Exhaust purification system of an internal combustion engine, characterized in that the provided oxygen consumption means for reducing the reducing agent consumption during NO X emission from is provided.

【0007】[0007]

【作用】酸素消費手段は、排気中への還元剤導入時に予
めNOx吸収剤に流入する排気中の酸素を消費し、排気
酸素濃度を低減する。このため、NOx吸収剤への酸素
流入が減少し、排気の流入を継続したままであっても還
元雰囲気の生成に必要な還元剤の量が低減される。
When the reducing agent is introduced into the exhaust gas, the oxygen consuming means consumes the oxygen in the exhaust gas flowing into the NOx absorbent in advance, thereby reducing the exhaust oxygen concentration. For this reason, the inflow of oxygen into the NOx absorbent is reduced, and the amount of the reducing agent required to generate the reducing atmosphere is reduced even when the inflow of exhaust gas is continued.

【0008】[0008]

【実施例】以下、本発明の排気浄化装置をディーゼルエ
ンジンに適用した例について説明する。図1は本発明の
第一の実施例を示す図である。図1において1はディー
ゼルエンジン本体、2はエンジン吸気管、3はエンジン
排気管、4はエンジン燃焼室に燃料を噴射する燃料噴射
弁である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, an example in which the exhaust emission control device of the present invention is applied to a diesel engine will be described. FIG. 1 is a diagram showing a first embodiment of the present invention. In FIG. 1, 1 is a diesel engine main body, 2 is an engine intake pipe, 3 is an engine exhaust pipe, and 4 is a fuel injection valve for injecting fuel into an engine combustion chamber.

【0009】本実施例においては、吸気管2にはシャッ
ターバルブ6が設けられている。シャッターバルブ6は
全開時に抵抗の少ない例えばバタフライ型弁とされ、通
常運転時には全開に保持されており、後述の吸収剤から
のNOx放出操作時に閉弁され、吸気管2を絞り、エン
ジン1に吸入される空気量を低減する。7は後述のEC
U20からの信号を受けてシャッターバルブ6を開閉駆
動するソレノイド、負圧アクチュエータ等の適宜な形式
のアクチュエータである。
In this embodiment, the intake pipe 2 is provided with a shutter valve 6. The shutter valve 6 is, for example, a butterfly valve having a small resistance when fully opened, and is kept fully open during normal operation. The shutter valve 6 is closed when NOx is released from the absorbent, which will be described later. Reduce the amount of air that is generated. 7 is EC described later
An appropriate type of actuator, such as a solenoid or a negative pressure actuator, that drives the shutter valve 6 to open and close in response to a signal from U20.

【0010】一方、エンジン排気管3には排気中に含ま
れるカーボンや可溶性有機成分(SOF)等の微粒子
(ディーゼルパティキュレート)を捕集するパティキュ
レートフィルタ11とケーシング内に収容されたNOx
吸収剤15が配置されている。また、図に20で示すの
はエンジン1の電子制御ユニット(ECU)である。E
CU20はCPU21、RAM22、ROM23及び入
力ポート24、出力ポート25を相互に双方向バス26
で接続した構成のディジタルコンピュータから成り、燃
料噴射弁4からの燃料噴射量制御等のエンジンの基本制
御を行っている。またECU20は、後述のNOx吸収
剤15からのNOxの放出、パティキュレートフィルタ
11の再生等の制御をも行っており、これらの制御のた
めECU20の入力ポート24にはエンジン回転数信
号、アクセル開度信号がそれぞれ図示しないセンサから
入力されている他、パティキュレートフィルタ11入口
に設けられた排気温度センサ17から排気温度信号が入
力されている。また、ECU20の出力ポート25は燃
料噴射弁4とシャッターバルブアクチュエータ7とに接
続され、燃料噴射量やシャッターバルブ6の開閉動作等
の制御を行っている。
On the other hand, the engine exhaust pipe 3 has a particulate filter 11 for collecting fine particles (diesel particulate) such as carbon and soluble organic components (SOF) contained in the exhaust gas, and NOx contained in a casing.
An absorbent 15 is provided. In addition, what is indicated by 20 in the figure is an electronic control unit (ECU) of the engine 1. E
The CU 20 connects the CPU 21, the RAM 22, the ROM 23, the input port 24, and the output port 25 to each other through a bidirectional bus 26.
A basic computer control such as control of the amount of fuel injected from the fuel injection valve 4 is performed. The ECU 20 also controls the release of NOx from a NOx absorbent 15, which will be described later, and the regeneration of the particulate filter 11. For these controls, an input port 24 of the ECU 20 provides an engine speed signal, an accelerator opening signal, and the like. The temperature signals are input from sensors (not shown), and an exhaust temperature signal is input from an exhaust temperature sensor 17 provided at the entrance of the particulate filter 11. The output port 25 of the ECU 20 is connected to the fuel injection valve 4 and the shutter valve actuator 7, and controls the fuel injection amount, the opening / closing operation of the shutter valve 6, and the like.

【0011】パティキュレートフィルタ11は通常、セ
ラミック等の耐熱性を有する濾材から形成され、排気中
のパティキュレートを濾過、捕集する。従ってフィルタ
11内には時間と共に捕集されたパティキュレートが蓄
積されるため、定期的に再生を行い捕集したパティキュ
レートを除去する必要がある。通常、このフィルタの再
生は、フィルタに捕集されたパティキュレートを着火温
度(約600℃)以上に加熱し、熱焼させることにより
行う。前述のようにパティキュレートはカーボンやSO
F等からなるため、条件によっては燃焼によりCO等の
還元性のガスを発生する。本実施例では、後述のように
NOx吸収剤からのNOx放出操作時に、シャッターバ
ルブ6を閉弁し燃料噴射量の増量を行うことにより排気
温度をパティキュレート着火温度以上に上昇させてフィ
ルタ11に捕集したパティキュレートを燃焼させる。こ
れにより排気中の酸素がパティキュレート燃焼に消費さ
れ排気酸素濃度が低下すると共にパティキュレート燃焼
によりCO,CO2 等の還元性ガスが発生し、NOx吸
収剤に供給される。
The particulate filter 11 is usually formed of a heat-resistant filter material such as ceramics, and filters and collects particulates in exhaust gas. Therefore, the collected particulates accumulate in the filter 11 over time, so that it is necessary to periodically regenerate and remove the collected particulates. Normally, regeneration of the filter is performed by heating the particulates collected by the filter to an ignition temperature (about 600 ° C.) or higher and burning it. As mentioned above, particulates are carbon or SO
Since it is composed of F or the like, depending on the conditions, a reducing gas such as CO is generated by combustion. In the present embodiment, as described later, at the time of the NOx releasing operation from the NOx absorbent, the exhaust valve temperature is raised to the particulate ignition temperature or higher by closing the shutter valve 6 and increasing the fuel injection amount so that the filter 11 is operated. Burn the collected particulates. As a result, the oxygen in the exhaust gas is consumed by the particulate combustion, the exhaust oxygen concentration is reduced, and the particulate combustion generates a reducing gas such as CO or CO 2 , which is supplied to the NOx absorbent.

【0012】ケーシング内に収容されているNOx吸収
剤15は例えばアルミナを担体とし、この担体上に例え
ばカリウムK、ナトリウムNa、リチウムLi、セシウ
ムCsのようなアルカリ金属、バリウムBa、カルシウ
ムCaのようなアルカリ土類、ランタンLa、イットリ
ウムYのような希土類から選ばれた少くとも一つと、白
金Ptのような貴金属とが担持されている。
The NOx absorbent 15 housed in the casing uses, for example, alumina as a carrier, and on the carrier, for example, an alkali metal such as potassium K, sodium Na, lithium Li, and cesium Cs, barium Ba, and calcium Ca. And at least one selected from rare earths such as alkaline earth, lanthanum La and yttrium Y, and a noble metal such as platinum Pt.

【0013】このNOx吸収剤15は流入する排気空燃
比がリーンのときにはNOxを吸収し、流入する排気中
の酸素濃度が低下すると吸収したNOxを放出するNO
xの吸放出作用を行う。ここで上述の排気空燃比とは、
NOx吸収剤15の上流側の排気通路やエンジン燃焼
室、吸気通路等に供給された空気量合計と燃料合計との
比をいうものとする。従って、NOx吸収剤15の上流
側排気通路に燃料又は空気が供給されない場合には排気
空燃比はエンジン燃焼室内の燃焼における空燃比と等し
くなる。なお、本実施例では、ディーゼルエンジンが使
用されているため、通常運転時は排気空燃比はリーンで
あり、NOx吸収剤15は排気中のNOxを吸収する。
また、後述の操作により排気中の酸素濃度が低下すると
NOx吸収剤15は吸収したNOxを放出することにな
る。
The NOx absorbent 15 absorbs NOx when the inflowing exhaust air-fuel ratio is lean, and releases the absorbed NOx when the oxygen concentration in the inflowing exhaust gas decreases.
x has a function of absorbing and releasing. Here, the above-mentioned exhaust air-fuel ratio is
It refers to the ratio of the total amount of air supplied to the exhaust passage, the engine combustion chamber, the intake passage and the like upstream of the NOx absorbent 15 to the total fuel. Therefore, when no fuel or air is supplied to the exhaust passage on the upstream side of the NOx absorbent 15, the exhaust air-fuel ratio becomes equal to the air-fuel ratio in combustion in the engine combustion chamber. In this embodiment, since a diesel engine is used, the exhaust air-fuel ratio is lean during normal operation, and the NOx absorbent 15 absorbs NOx in the exhaust.
Further, when the oxygen concentration in the exhaust gas is reduced by an operation described later, the NOx absorbent 15 releases the absorbed NOx.

【0014】NOx吸収剤15の上記NOx吸放出作用
の詳細については明らかでない部分もある。しかし、こ
の吸放出作用は図2に示すようなメカニズムで行われて
いるものと考えられる。次にこのメカニズムについて担
体上に白金PtおよびバリウムBaを担持させた場合を
例にとって説明するが他の貴金属、アルカリ金属,アル
カリ土類、希土類を用いても同様なメカニズムとなる。
The details of the NOx absorbing / releasing action of the NOx absorbent 15 are not clear in some parts. However, it is considered that this absorption / release action is performed by a mechanism as shown in FIG. Next, this mechanism will be described by taking as an example a case where platinum Pt and barium Ba are supported on a carrier, but the same mechanism can be obtained by using other noble metals, alkali metals, alkaline earths and rare earths.

【0015】即ち、流入排気がかなりリーンになると流
入排気中の酸素濃度が大巾に増大し、図2(A)に示さ
れるようにこれら酸素O2 がO2 - の形で白金Ptの表
面に付着する。一方、流入排気ガス中のNOは白金Pt
の表面上でO2 - と反応し、NO2 となる(2NO+O
2 →2NO2 )。次いで生成されたNO2 の一部は白金
Pt上で酸化されつつ吸収剤内に吸収されて酸化バリウ
ムBaOと結合しながら図2(A)に示されるように硝
酸イオンNO3 - の形で吸収剤内に拡散する。このよう
にしてNOxがNOx吸収剤15内に吸収される。
That is, when the inflow exhaust gas becomes considerably lean, the oxygen concentration in the inflow exhaust gas greatly increases, and as shown in FIG. 2 (A), the oxygen O 2 is converted into O 2 − in the form of O 2 − on the surface of the platinum Pt. Adheres to On the other hand, NO in the inflowing exhaust gas is platinum Pt.
On the surface of the reacts with the O 2 - and becomes NO 2 (2NO + O
2 → 2NO 2 ). Next, a part of the produced NO 2 is absorbed in the absorbent while being oxidized on the platinum Pt, and is absorbed in the form of nitrate ion NO 3 as shown in FIG. 2A while being combined with barium oxide BaO. Diffuses into agent. In this manner, NOx is absorbed in the NOx absorbent 15.

【0016】流入排気中の酸素濃度が高い限り白金Pt
の表面でNO2 が生成され、吸収剤のNOx吸収能力が
飽和しない限りNO2 が吸収剤内に吸収されて硝酸イオ
ンNO3 - が生成される。これに対して流入排気中の酸
素濃度が低下してNO2 の生成量が低下すると反応が逆
方向(NO3 - →NO2 )に進み、斯くして吸収剤内の
硝酸イオンNO3 - がNO2 の形で吸収剤から放出され
る。即ち、流入排気中の酸素濃度が低下するとNOx吸
収剤15からNOxが放出されることになる。
As long as the oxygen concentration in the inflow exhaust gas is high, platinum Pt
NO 2 is produced on the surface of, as long as NO 2 to NOx absorption ability of the absorbent is not saturated is absorbed nitrate ions NO 3 in the absorbent - is produced. On the other hand, when the oxygen concentration in the inflowing exhaust gas decreases and the amount of generated NO 2 decreases, the reaction proceeds in the reverse direction (NO 3 → NO 2 ), and thus the nitrate ion NO 3 in the absorbent is converted. It is released from the absorbent in the form of NO 2. That is, when the oxygen concentration in the inflow exhaust gas decreases, NOx is released from the NOx absorbent 15.

【0017】一方、このとき流入排気中に未燃HC,C
O等の還元成分が存在するとこれらの成分は白金Pt上
の酸素O2 - と反応して酸化される。また排気中の酸素
濃度低下により吸収剤15から放出されたNO2 は図2
(B)に示すように未燃HC,COと反応して還元され
る。このようにして白金Ptの表面上にNO2 が存在し
なくなると吸収剤から次から次へとNO2 が放出され
る。従って流入排気ガス中の未燃HC,CO成分が増加
すると短時間のうちにNOx吸収剤15からNOxが放
出される還元されることになる。
On the other hand, at this time, unburned HC, C
These ingredients when the reducing component is present in the O such oxygen O 2 on the platinum Pt - is oxidized by reacting with. The NO 2 released from the absorbent 15 due to the decrease in the oxygen concentration in the exhaust gas is shown in FIG.
As shown in (B), it is reduced by reacting with unburned HC and CO. In this way, when NO 2 is no longer present on the surface of platinum Pt, NO 2 is released from the absorbent one after another. Therefore, when the unburned HC and CO components in the inflowing exhaust gas increase, NOx is released from the NOx absorbent 15 and reduced in a short time.

【0018】即ち、流入排気中の未燃HC,COは、ま
ず白金Pt上のO2 - とただちに反応して酸化せしめら
れ、次いで白金Pt上のO2 - が消費されてもまだ未燃
HC,COが残っていればこの未燃HC,COによって
吸収剤から放出されたNOxおよび機関から排出された
NOxが還元される。従って、エンジン運転中にNOx
の放出、還元を行うために必要な還元剤の量は、(1)
排気中の酸素濃度を充分に低下させるのに必要な量と、
(2)白金Pt上のO2 - を消費するのに必要な量及
び、(3)吸収剤15から放出された全NOx及びエン
ジンから排出された全NOxを還元するのに必要な量の
和となる。 ところでディーゼルエンジンの排気には多
量の酸素が含まれているため、排気中の酸素濃度を充分
に低下させるための還元剤の量(上記(1))は極めて
多量になり還元剤の消費量が多くなる。本実施例では以
下の操作を行うことにより予め排気中の酸素を消費して
排気中の酸素濃度を低下させて上記(1)に要する還元
剤の量を低減しているのである。
[0018] That is, the unburned HC in the inflowing exhaust gas, CO, first O 2 on the platinum Pt - immediately reacts been oxidized, and then the platinum Pt on the O 2 - are still unburned HC be consumed , CO remains, the unburned HC and CO reduce NOx released from the absorbent and NOx discharged from the engine. Therefore, during engine operation, NOx
The amount of reducing agent required to release and reduce
The amount needed to sufficiently reduce the oxygen concentration in the exhaust,
(2) O 2 on the platinum Pt - amount needed to consume and, (3) the sum of the amount required to reduce all the NOx discharged from the entire NOx and engine released from the absorbent 15 Becomes By the way, since the exhaust gas of a diesel engine contains a large amount of oxygen, the amount of the reducing agent ((1) above) for sufficiently lowering the oxygen concentration in the exhaust gas is extremely large, and the consumption amount of the reducing agent is large. More. In this embodiment, by performing the following operation, the oxygen in the exhaust gas is consumed in advance to lower the oxygen concentration in the exhaust gas, thereby reducing the amount of the reducing agent required for the above (1).

【0019】図3は、図1の実施例の排気浄化装置にお
けるNOx吸収剤15の放出還元動作のフローチャート
を示す。本放出還元動作はECU20により制御され
る。図3、ステップ31はNOx吸収剤15のNOx放
出還元操作実行のための条件が成立しているか否かの判
定を示す。上記実行条件は(1)エンジン排気温度が所
定値以上であること;(2)車両が減速運転中であるこ
と;等である。
FIG. 3 shows a flowchart of the operation of releasing and reducing the NOx absorbent 15 in the exhaust gas purifying apparatus of the embodiment shown in FIG. This release / reduction operation is controlled by the ECU 20. FIG. 3, step 31 shows a determination as to whether or not conditions for executing the NOx release / reduction operation of the NOx absorbent 15 are satisfied. The execution conditions are (1) that the engine exhaust temperature is equal to or higher than a predetermined value; (2) that the vehicle is in deceleration operation;

【0020】上記(1)で排気温度は排気管3の排気温
度センサ17からECU20に入力される。ここで、排
気温度の上記所定値は、NOx吸収剤15の温度がNO
x放出、還元のための活性温度以上になる排気温度とさ
れる。また、上記(2)の車両減速中であることの判断
はエンジン回転数が所定値以上であり、かつアクセル開
度が全閉であることに基づいて行われる。NOxの放出
還元操作を車両減速運転中にのみ行うのは、後述のよう
に放出還元時にはシャッターバルブ6を閉じてエンジン
吸気を絞る必要があるため、これによりトルクショック
が生じることを防止するためである。
In the above (1), the exhaust gas temperature is input to the ECU 20 from the exhaust gas temperature sensor 17 of the exhaust pipe 3. Here, the above-mentioned predetermined value of the exhaust gas temperature is such that the temperature of the NOx absorbent 15 is NO.
The exhaust temperature is equal to or higher than the activation temperature for x release and reduction. Further, the determination (2) that the vehicle is being decelerated is made based on the fact that the engine speed is equal to or higher than the predetermined value and the accelerator opening is fully closed. The reason why the NOx release / reduction operation is performed only during the vehicle deceleration operation is to prevent the occurrence of torque shock because it is necessary to close the shutter valve 6 and reduce the engine intake during release / reduction as described later. is there.

【0021】上記放出、還元実行条件が成立している場
合には、ステップ32,33でパティキュレートフィル
タ11の再生を行う。すなわち、ステップ32でシャッ
ターバルブ6を閉弁してエンジン吸入空気量を低下させ
ると共にステップ33では燃料噴射量の増量を行ない、
排気温度をパティキュレート着火温度(約600℃)以
上に昇温させる。
If the conditions for executing the discharge and reduction are satisfied, the particulate filter 11 is regenerated in steps 32 and 33. That is, in step 32, the shutter valve 6 is closed to reduce the engine intake air amount, and in step 33, the fuel injection amount is increased.
The temperature of the exhaust gas is raised to the particulate ignition temperature (about 600 ° C.) or higher.

【0022】これによりパティキュレートフィルタ11
では捕集された排気微粒子の燃焼が開始される。ディー
ゼルエンジンの通常運転時の排気空燃比は大幅なリーン
であるがシャッターバルブ閉弁による吸入空気量の低下
と燃料噴射量との増量とを行うことにより排気空燃比は
リッチ側に移行し、排気中の未燃HC,CO等の成分が
大幅に増大する。また、上記によりパティキュレートフ
ィルタ11に捕集されたカーボン等の排気微粒子が燃焼
を開始するため排気中の酸素が燃焼に消費されて排気の
酸素濃度が更に低下すると共にカーボン等の燃焼により
CO等が発生するため、排気中の未燃HC,CO等の還
元成分は更に増加し、NOx吸収剤15でのNOx放
出、還元の条件が整う。
Thus, the particulate filter 11
Then, the combustion of the collected exhaust fine particles is started. Although the exhaust air-fuel ratio during normal operation of the diesel engine is significantly lean, the exhaust air-fuel ratio shifts to the rich side by reducing the intake air amount due to the closing of the shutter valve and increasing the fuel injection amount. Components such as unburned HC and CO therein greatly increase. In addition, since the exhaust particulates such as carbon collected by the particulate filter 11 start burning as described above, the oxygen in the exhaust is consumed by the combustion, and the oxygen concentration in the exhaust further decreases. Is generated, the reducing components such as unburned HC and CO in the exhaust further increase, and the conditions of NOx release and reduction in the NOx absorbent 15 are established.

【0023】またNOx吸収剤15は温度が高い程吸収
したNOxを放出し易くなる特性を有し、一般的にはパ
ティキュレートフィルタ11の着火温度である600℃
以上ではNOx放出速度が極めて大きくなる。従って本
実施例のようにパティキュレートフィルタ11の燃焼再
生と同時にNOx吸収剤15からのNOx放出還元を行
うことにより短時間でNOx吸収剤15からのNOxの
放出と還元とを完了することができる。
The NOx absorbent 15 has a characteristic that the higher the temperature is, the easier it is to release the absorbed NOx, and the NOx absorbent 15 generally has an ignition temperature of the particulate filter 11 of 600 ° C.
Above, the NOx release speed becomes extremely high. Therefore, the release and reduction of NOx from the NOx absorbent 15 can be completed in a short time by performing the NOx release and reduction from the NOx absorbent 15 at the same time as the combustion regeneration of the particulate filter 11 as in the present embodiment. .

【0024】なお、ステップ31で放出還元条件が成立
していない場合、及び放出還元操作実行中にステップ3
1の条件が成立しなくなった場合には、ステップ34,
35でシャッターバルブの開弁と燃料噴射増量の中止が
行われ、エンジンは通常の運転状態に復帰する。上述の
ように本実施例では、パティキュレートフィルタ11の
再生操作によりNOx吸収剤15でのNOx放出、還元
を開始させるようにしたことにより、(1)NOx吸収
剤に流入する排気中の酸素濃度低減と、(2)排気中の
CO,HC等の還元成分増大、及び(3)排気温度上昇
によるNOx放出還元時間の短縮、とを同時に達成して
いる。
It should be noted that if the discharge reduction condition is not satisfied in step 31, or if the discharge reduction operation is being performed, step 3
If condition 1 is no longer satisfied, step 34,
At 35, the shutter valve is opened and the fuel injection increase is stopped, and the engine returns to the normal operation state. As described above, in the present embodiment, the NOx release and reduction by the NOx absorbent 15 are started by the regeneration operation of the particulate filter 11, thereby (1) the oxygen concentration in the exhaust gas flowing into the NOx absorbent. At the same time, the reduction and (2) the increase of the reducing components such as CO and HC in the exhaust gas and (3) the reduction of the NOx emission reduction time due to the increase in the exhaust gas temperature are achieved.

【0025】なお、上述の実施例では、シャッターバル
ブ6の閉弁と燃料噴射量増量とによる排気温度上昇のみ
でパティキュレートの着火を行っているが、パティキュ
レートフィルタ11に着火用電気ヒータを設け、排気昇
温と併用して着火を促進するようにしても良い。次に図
4に、本発明の第二の実施例を示す。図4においても図
1と同じ参照符号は同一の要素を示している。本実施例
においては、パティキュレートフィルタ11入口には燃
料油を用いたバーナ12が設けられている点で図1の実
施例と相違している。すなわち、本実施例では、パティ
キュレートフィルタ11再生時にシャッターバルブ6を
閉弁すると共にバーナ12で燃料油を燃焼させることに
より排気の昇温を行い、エンジンへの燃料噴射量増量は
行なわない。本実施例によれば、パティキュレートフィ
ルタ11の排気微粒子捕集量が少なく、パティキュレー
トフィルタ11での排気昇温が充分でないような場合で
もバーナ12への燃料供給量を増大することにより排気
昇温と酸素消費とが達成できるため、NOx吸収剤15
でのNOx放出還元操作実施タイミングがパティキュレ
ートフィルタ11の排気微粒子捕集量に影響されない利
点がある。なお、この実施例においてもパーナ12から
発生する未燃HC,COがNOxの還元剤として作用す
ることは図1の実施例と同様である。
In the above-described embodiment, the particulate ignition is performed only by the exhaust gas temperature rise due to the closing of the shutter valve 6 and the increase of the fuel injection amount. However, the particulate filter 11 is provided with an electric heater for ignition. Alternatively, the ignition may be promoted in combination with the exhaust gas heating. Next, FIG. 4 shows a second embodiment of the present invention. 4, the same reference numerals as those in FIG. 1 denote the same elements. This embodiment is different from the embodiment of FIG. 1 in that a burner 12 using fuel oil is provided at the entrance of a particulate filter 11. That is, in the present embodiment, when the particulate filter 11 is regenerated, the temperature of the exhaust gas is increased by closing the shutter valve 6 and burning the fuel oil with the burner 12, and the fuel injection amount to the engine is not increased. According to the present embodiment, even when the amount of exhaust particulates collected by the particulate filter 11 is small and the exhaust gas temperature in the particulate filter 11 is not sufficient, the amount of fuel supplied to the burner 12 is increased to increase the exhaust gas. Since the temperature and oxygen consumption can be achieved, the NOx absorbent 15
There is an advantage that the timing of performing the NOx release / reduction operation in the above is not affected by the amount of exhaust particulate collected by the particulate filter 11. In this embodiment, unburned HC and CO generated from the parner 12 act as NOx reducing agents as in the embodiment shown in FIG.

【0026】図5は本発明の第三の実施例を示す。本実
施例では、図1,図4の実施例のパティキュレートフィ
ルタを設けず、排気通路に燃料油を用いたバーナ12と
着火用のグローヒータ13とを配置し、バーナ12の燃
焼によりNOx吸収剤15でのNOx放出、還元を行
う。すなわち、本実施例では、パティキュレートフィル
タ11での燃焼による酸素消費と還元成分の発生、及び
排気昇温の全ての作用をシャッターバルブ6の閉弁とバ
ーナ12の燃焼のみにより行っている。これによりNO
x吸収剤15でのNOx放出還元操作のタイミングを自
由に設定することができる利点がある。
FIG. 5 shows a third embodiment of the present invention. In this embodiment, the particulate filter of the embodiment shown in FIGS. 1 and 4 is not provided, and a burner 12 using fuel oil and a glow heater 13 for ignition are arranged in an exhaust passage. NOx release and reduction at 15 are performed. That is, in the present embodiment, all the effects of the oxygen consumption and the generation of the reducing component due to the combustion in the particulate filter 11 and the exhaust gas temperature rise are performed only by closing the shutter valve 6 and burning the burner 12. This makes NO
There is an advantage that the timing of the NOx release / reduction operation in the x absorbent 15 can be freely set.

【0027】次に図6に本発明の第四の実施例を示す。
本実施例ではNOx吸収剤15の上流側の排気管、好ま
しくは排気マニホルド直下流に小容量の酸化触媒28を
配置している。触媒28は熱容量の小さいメタル担体を
使用し、活性温度の低い、例えば高Pt担持品が好適で
ある。本実施例では、酸化触媒28により酸素消費と排
気温度上昇とを行う。
FIG. 6 shows a fourth embodiment of the present invention.
In this embodiment, a small-capacity oxidation catalyst 28 is disposed on the exhaust pipe on the upstream side of the NOx absorbent 15, preferably immediately downstream of the exhaust manifold. As the catalyst 28, a metal carrier having a small heat capacity is used, and a product having a low activation temperature, for example, a high Pt-supported product is suitable. In the present embodiment, the oxygen consumption and the exhaust gas temperature are increased by the oxidation catalyst 28.

【0028】すなわち、NOx吸収剤15でのNOx放
出還元操作の実行条件が成立した場合吸気管2のシャッ
ターバルブ6を閉弁すると共にエンジンの燃料噴射量を
増量し、空燃比を大幅にリッチ側に移行させる。これに
より排気中の未燃HC,CO等の成分が増大し、触媒2
8で酸化反応が生じて排気中の酸素が消費されると共に
反応熱により排気温度が上昇する。また、触媒28は小
容量であるため、燃料噴射量増量により生じた排気中の
未燃HC,COの一部しか消費することはできず、残り
の大部分の未燃HC,CO成分は触媒28を通過してN
Ox吸収剤15に到達し、放出されたNOxの還元剤と
して使用される。
That is, when the execution condition of the NOx release / reduction operation with the NOx absorbent 15 is satisfied, the shutter valve 6 of the intake pipe 2 is closed, the fuel injection amount of the engine is increased, and the air-fuel ratio is greatly increased. Move to As a result, components such as unburned HC and CO in the exhaust gas increase, and the catalyst 2
At 8, an oxidation reaction occurs, oxygen in the exhaust gas is consumed, and the exhaust gas temperature rises due to reaction heat. Further, since the catalyst 28 has a small capacity, only a part of the unburned HC and CO in the exhaust gas generated by the increase in the fuel injection amount can be consumed, and most of the remaining unburned HC and CO components are removed from the catalyst. N after passing 28
It reaches the Ox absorbent 15 and is used as a reducing agent for the released NOx.

【0029】本実施例では、触媒28として酸化触媒を
用いているが、前述のようにNOx吸収剤は酸化触媒と
しての機能を有しているため、触媒28の代わりに小容
量のNOx吸収剤を用いることも可能である。このよう
に触媒28の代わりに小容量のNOx吸収剤を配置する
こととすれば、下流に配置したNOx吸収剤と合わせて
全体としてNOx処理能力を増大させることができる。
In this embodiment, an oxidation catalyst is used as the catalyst 28. However, as described above, the NOx absorbent has a function as an oxidation catalyst. Can also be used. By arranging a small-capacity NOx absorbent instead of the catalyst 28 as described above, the NOx treatment capacity can be increased as a whole together with the NOx absorbent arranged downstream.

【0030】なお、上述の実施例においては、いずれも
NOx放出還元時に吸気管2のシャッターバルブ6を閉
じて吸入空気量を減少させているが、例えば、これらの
場合に排気再循環(EGR)を併用すれば排気中の酸素
量低減のうえで一層効果がある。また、上述の実施例
は、ディーゼルエンジンについてのみ説明したが、本発
明は希薄燃焼を行うガソリンエンジン(リーンバーンエ
ンジン)等にも適用可能である。
In each of the above-mentioned embodiments, the shutter valve 6 of the intake pipe 2 is closed to reduce the amount of intake air during NOx release and reduction. For example, in these cases, exhaust gas recirculation (EGR) is performed. When used together, it is more effective in reducing the amount of oxygen in the exhaust gas. Although the above-described embodiment has been described only for a diesel engine, the present invention is also applicable to a gasoline engine (lean burn engine) that performs lean combustion.

【0031】[0031]

【発明の効果】上述のように、本発明によれば、NOx
吸収剤の上流側に排気中の酸素を消費する手段を配置
し、NOxの放出、還元操作時に排気中の酸素濃度を予
め低下させるようにしたことにより、還元剤の所要量の
増大を防止することができる。
As described above, according to the present invention, NOx
Means for consuming oxygen in the exhaust gas are arranged upstream of the absorbent, and the concentration of oxygen in the exhaust gas is reduced in advance during the NOx release and reduction operations, thereby preventing the required amount of the reducing agent from increasing. be able to.

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

【図1】本発明の第一の実施例を示す図である。FIG. 1 is a diagram showing a first embodiment of the present invention.

【図2】NOxの吸放出作用を説明するための図であ
る。
FIG. 2 is a diagram for explaining a NOx absorption / release operation.

【図3】図1の実施例におけるNOxの放出、還元操作
を説明するフローチャートである。
FIG. 3 is a flowchart illustrating a NOx releasing and reducing operation in the embodiment of FIG. 1;

【図4】本発明の第二の実施例を示す図である。FIG. 4 is a diagram showing a second embodiment of the present invention.

【図5】本発明の第三の実施例を示す図である。FIG. 5 is a diagram showing a third embodiment of the present invention.

【図6】本発明の第四の実施例を示す図である。FIG. 6 is a diagram showing a fourth embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…ディーゼルエンジン 2…吸気管 3…排気管 6…吸気シャッターバルブ 11…パティキュレートフィルタ 12…バーナー 15…NOx吸収剤 17…排気温度センサ 20…電子制御ユニット 28…酸化触媒 DESCRIPTION OF SYMBOLS 1 ... Diesel engine 2 ... Intake pipe 3 ... Exhaust pipe 6 ... Intake shutter valve 11 ... Particulate filter 12 ... Burner 15 ... NOx absorbent 17 ... Exhaust temperature sensor 20 ... Electronic control unit 28 ... Oxidation catalyst

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F01N 3/08 - 3/28──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) F01N 3/08-3/28

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 少くとも大部分の運転領域でリーン空燃
比の燃焼を行う内燃機関の排気浄化装置であって、機関
の排気通路に排気空燃比がリーンのときにNOxを吸収
し、排気酸素濃度が低下すると吸収したNOxを放出す
るNOx吸収剤を配置し、所定の運転条件下で排気中に
還元剤を導入することにより排気酸素濃度を低下させ前
記吸収剤からNOxを放出させると共に放出されたNO
xを還元浄化する排気浄化装置において、 前記還元剤導入時に前記NOx吸収剤に流入する排気中
の酸素を消費して前記NO X 吸収剤からのNO X 放出時
の還元剤消費量を低減する酸素消費手段を設けたことを
特徴とする内燃機関の排気浄化装置。
An exhaust purification system for an internal combustion engine that performs combustion at a lean air-fuel ratio in at least most of an operating region, wherein NOx is absorbed in an exhaust passage of the engine when the exhaust air-fuel ratio is lean, and exhaust gas oxygen is exhausted. A NOx absorbent that releases the absorbed NOx when the concentration is reduced is arranged, and a reducing agent is introduced into the exhaust gas under predetermined operating conditions to lower the exhaust oxygen concentration to release NOx from the absorbent and release the NOx. NO
In the exhaust purifying apparatus reduces and purifies x, when NO X released from the the NO X absorbent to consume oxygen in the exhaust gas flowing into the NOx absorbent when the reducing agent introduced
An exhaust gas purifying apparatus for an internal combustion engine, comprising an oxygen consuming means for reducing the amount of reducing agent consumed .
JP26389292A 1992-10-01 1992-10-01 Exhaust gas purification device for internal combustion engine Expired - Lifetime JP2830652B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26389292A JP2830652B2 (en) 1992-10-01 1992-10-01 Exhaust gas purification device for internal combustion engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26389292A JP2830652B2 (en) 1992-10-01 1992-10-01 Exhaust gas purification device for internal combustion engine

Publications (2)

Publication Number Publication Date
JPH06117220A JPH06117220A (en) 1994-04-26
JP2830652B2 true JP2830652B2 (en) 1998-12-02

Family

ID=17395710

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26389292A Expired - Lifetime JP2830652B2 (en) 1992-10-01 1992-10-01 Exhaust gas purification device for internal combustion engine

Country Status (1)

Country Link
JP (1) JP2830652B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3797125B2 (en) * 2001-03-15 2006-07-12 いすゞ自動車株式会社 Exhaust gas purification device and regeneration control method thereof
JP2011001849A (en) * 2009-06-17 2011-01-06 Hitachi Constr Mach Co Ltd Exhaust gas treatment device for diesel engine

Also Published As

Publication number Publication date
JPH06117220A (en) 1994-04-26

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