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JPH06272539A - Exhaust emission control device for internal combustion engine - Google Patents

Exhaust emission control device for internal combustion engine

Info

Publication number
JPH06272539A
JPH06272539A JP5057411A JP5741193A JPH06272539A JP H06272539 A JPH06272539 A JP H06272539A JP 5057411 A JP5057411 A JP 5057411A JP 5741193 A JP5741193 A JP 5741193A JP H06272539 A JPH06272539 A JP H06272539A
Authority
JP
Japan
Prior art keywords
absorbent
reducing agent
exhaust
fuel
light oil
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
JP5057411A
Other languages
Japanese (ja)
Other versions
JP3093905B2 (en
Inventor
Yasushi Araki
康 荒木
Shinya Hirota
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 JP05057411A priority Critical patent/JP3093905B2/en
Publication of JPH06272539A publication Critical patent/JPH06272539A/en
Application granted granted Critical
Publication of JP3093905B2 publication Critical patent/JP3093905B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • F01N3/10Exhaust 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
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/36Arrangements for supply of additional fuel
    • 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
    • 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
    • F01N5/00Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy
    • F01N5/02Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy the devices using heat
    • 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
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/03Adding substances to exhaust gases the substance being hydrocarbons, e.g. engine fuel
    • 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
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/10Adding substances to exhaust gases the substance being heated, e.g. by heating tank or supply line of the added substance
    • 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
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

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

PURPOSE:To enable the use of a liquid reducing agent for an NOx absorbent regenerating operation by solving problems of activity degradation and low temperature toxic damage of NOx absorbent caused by the deposition of ungasified component when the NOx absorbent is regenerated by the use of the liquid reducing agent. CONSTITUTION:An NOx absorbent 5 is disposed in an exhaust pipe 3 of an internal combustion engine and a reducing agent supply device 11 for supplying a liquid reducing agent like light oil is disposed in the upstream of the NOx absorbent 5. A heat exchange section 13a for preheating the liquid reducing agent with the heat of exhaust gas in the exhaust pipe is provided in a supply path 13 for supplying the reducing agent to a reducing agent injection valve 12 of the reducing agent supply device 11. Since the liquid reducing agent is gasified by the preheating section 13a, an amount of ungasified component reaching the NOx absorbent is reduced.

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を
行うガソリンエンジン等、大部分の運転領域においてリ
ーン空燃比の燃焼を行う内燃機関の排気中のNOX を効
果的に除去可能な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 internal combustion engine that burns at a lean air-fuel ratio in most operating regions such as a diesel engine and a gasoline engine that performs lean combustion. The present invention relates to an exhaust gas purification device that can effectively remove NO X in exhaust gas.

【0002】[0002]

【従来の技術】この種の排気浄化装置の例としては、例
えば特開昭62─106826号公報に開示されたもの
がある。同公報の装置は、ディーゼル機関の排気通路に
酸素の存在下でNOX を吸収する吸収剤(触媒)を配置
して排気中のNOX を吸収させ、該吸収剤のNOX 吸収
効率が低下したときに吸収剤への排気の流入を遮断して
吸収剤に気体状の還元剤を供給することにより、吸収剤
からNOX を放出させると共に放出されたNOXを還元
浄化するようにしたものである。
2. Description of the Related Art An example of this type of exhaust emission control device is disclosed in Japanese Patent Application Laid-Open No. 62-106826. The apparatus of this publication is to place the absorbent to absorb NO X in the presence of oxygen in an exhaust passage of a diesel engine (catalyst) to absorb the NO X in the exhaust gas, lowering the NO X absorption efficiency of the absorbent In such a case, when exhaust gas is blocked from flowing into the absorbent and a gaseous reducing agent is supplied to the absorbent, NO x is released from the absorbent and the released NO x is reduced and purified. Is.

【0003】[0003]

【発明が解決しようとする課題】上記特開昭62─10
6826号公報の排気浄化装置では、NOX 吸収剤から
のNOX の放出と還元浄化(以下「再生」という)を行
うために、水素等の気体状還元剤をNOX 吸収剤に供給
している。しかし、水素等気体状の還元剤は貯蔵に際し
て特別な容器を必要とする等、取扱が困難な問題があ
り、特に車両用内燃機関に使用する場合には種々の問題
を生じる。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
In the exhaust gas purification device of Japanese Patent No. 6826, a gaseous reducing agent such as hydrogen is supplied to the NO X absorbent in order to perform NO X release from the NO X absorbent and reduction purification (hereinafter referred to as “regeneration”). There is. However, a gaseous reducing agent such as hydrogen has a problem that it is difficult to handle, such as requiring a special container for storage, and causes various problems particularly when used in an internal combustion engine for vehicles.

【0004】従って、NOX 吸収剤の再生に用いる還元
剤としては、取扱が簡単な液体の還元剤を使用すること
が好ましい。また、補給、貯蔵の煩雑さをなくすために
は、できればガソリン、軽油等、当該車両の燃料をその
まま液体還元剤として使用することが望ましい。ところ
が、特に軽油等の液体燃料は沸点の異なる多くの成分を
含んでおり、排気温度が低いと気化しにくい成分も含ま
れている。このため、これらの液体燃料をそのままNO
X 吸収剤の上流側の排気通路に噴射した場合には、沸点
の高い成分は気化せずに排気流とともに霧状のままNO
X 吸収剤に到達してしまう場合がある。この場合NOX
吸収剤に到達した燃料は吸収剤表面に液状のまま付着
し、吸収剤表面を覆う層を形成する。
Therefore, it is preferable to use a liquid reducing agent which is easy to handle as the reducing agent used for regenerating the NO x absorbent. Further, in order to eliminate the complexity of replenishment and storage, it is desirable to use the fuel of the vehicle such as gasoline or light oil as it is as a liquid reducing agent, if possible. However, especially liquid fuels such as light oil contain many components having different boiling points, and also contain components that are difficult to vaporize when the exhaust temperature is low. For this reason, these liquid fuels are directly used for NO
When injected into the exhaust passage on the upstream side of the X absorbent, the component with a high boiling point is not vaporized and remains in a mist state with the exhaust flow.
It may reach the X absorbent. In this case NO X
The fuel that has reached the absorbent adheres to the absorbent surface in a liquid state and forms a layer covering the absorbent surface.

【0005】NOX 吸収剤表面に付着した液体燃料は、
吸収剤の温度がある程度高い場合には吸収剤の熱を受け
て気化し、還元剤としての作用を行う。しかし、燃料が
気化する際にNOX 吸収剤から気化熱相当の熱が奪われ
るため、NOX 吸収剤の温度が低下することになり、液
状のまま到達する燃料の量が多いとNOX 吸収剤の温度
が活性温度以下に低下してしてしまう場合がある。この
ため、軽油などの液体燃料を還元剤として使用すると、
NOX 吸収剤の活性が低下してNOX 浄化率の低下を生
じ、エミッションの悪化を招く問題が生じる恐れがあ
る。
The liquid fuel adhering to the surface of the NO x absorbent is
When the temperature of the absorbent is high to some extent, it receives the heat of the absorbent to be vaporized and acts as a reducing agent. However, since the evaporation heat considerable heat is lost from the NO X absorbent when the fuel is vaporized, will be the temperature of the NO X absorbent is lowered, NO X absorption and greater the amount of fuel to reach a liquid state The temperature of the agent may fall below the activation temperature. Therefore, if liquid fuel such as light oil is used as the reducing agent,
It decreases the activity of the NO X absorbent caused the reduction of the NO X purification rate, which may cause a problem leading to deterioration of the emission.

【0006】また、NOX 吸収剤の温度が燃料の気化温
度よりも低下すると吸収剤に付着した燃料はもはや気化
せずNOX 吸収剤の表面を覆ってしまい、有効表面積の
減少によりNOX の吸収、放出作用が阻害される、いわ
ゆるNOX 吸収剤の低温被毒の問題が生じる場合があ
る。上記のため、従来は軽油等の液体燃料を還元剤とし
て使用する場合には、排気通路にバーナ等を設けて液体
燃料を不完全燃焼させ、発生するHC、CO等のガスを
還元剤としてNOX 吸収剤に供給する必要があった。し
かし、排気通路にバーナ等を設けて燃焼を行うことは安
全上からも好ましくなく、また、バーナやその附帯設備
を排気通路に設けるため、構造が複雑になる等の問題が
あった。
Further, when the temperature of the NO x absorbent falls below the vaporization temperature of the fuel, the fuel adhering to the absorbent no longer vaporizes and covers the surface of the NO x absorbent, reducing the effective surface area and reducing the amount of NO x . absorption, release effect is inhibited, in some cases problems of cold poisoning called the NO X absorbent occurs. For the above reasons, conventionally, when liquid fuel such as light oil is used as a reducing agent, a burner or the like is provided in the exhaust passage to incompletely burn the liquid fuel and the generated gas such as HC or CO is used as the reducing agent. X absorbent had to be supplied. However, it is not preferable from a safety point of view to provide a burner or the like in the exhaust passage for combustion, and there is a problem that the structure becomes complicated because the burner and its auxiliary equipment are provided in the exhaust passage.

【0007】本発明は、上記の問題を解決し、軽油等の
液体燃料をNOX 吸収剤の還元剤として使用することの
できる内燃機関の排気浄化装置を提供する事を目的とし
ている。
An object of the present invention is to solve the above problems and to provide an exhaust gas purifying apparatus for an internal combustion engine which can use a liquid fuel such as light oil as a reducing agent for an NO X absorbent.

【0008】[0008]

【課題を解決するための手段】本発明によれば、リーン
空燃比の燃焼を行うことのできる内燃機関の排気通路
に、流入排気の空燃比がリーンのときにNOX を吸収し
流入排気の酸素濃度が低下したときに吸収したNOX
放出するNOX 吸収剤を配置し、排気中のNOXを吸収
させ、NOX 吸収後に前記NOX 吸収剤に液体還元剤を
供給してNOX 吸収剤から吸収したNOX を放出させる
と共に該NOX を還元浄化する内燃機関の排気浄化装置
において、前記NOX 吸収剤に供給する液体還元剤を予
熱する還元剤予熱手段を備え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 SUMMARY OF], in an exhaust passage of an internal combustion engine capable of performing combustion of the lean air-fuel ratio, the air-fuel ratio of the inflowing exhaust is absorbed inflowing exhaust the NO X when the lean oxygen concentration place the NO X absorbent to release the absorbed NO X when lowered, the NO X in the exhaust gas is absorbed, by supplying the liquid reducing agent to the the NO X absorbent after NO X absorbing NO X the NO X absorbed from the absorbent causes release in the exhaust purification system for an internal combustion engine to reduce and purify the NO X, characterized in that it comprises a reducing agent preheating means for preheating the supply liquid reducing agent to the the NO X absorbent An exhaust gas purification device for an internal combustion engine is provided.

【0009】[0009]

【作用】NOX 吸収剤上流側の排気通路に供給する液体
燃料は供給前に予熱手段により予熱されて気化するた
め、液状のままNOX 吸収剤に到達する液体燃料が減少
し、NOX 吸収剤の温度低下が防止される。このため、
NOX 吸収剤の活性低下や低温被毒の問題が生じない。
The liquid fuel supplied to the exhaust passage on the upstream side of the NO x absorbent is preheated and vaporized by the preheating means before being supplied, so that the liquid fuel that reaches the NO x absorbent in a liquid state is reduced and the NO x absorbent is absorbed. The temperature drop of the agent is prevented. For this reason,
There is no problem of reduced activity of the NO x absorbent and low temperature poisoning.

【0010】[0010]

【実施例】以下、添付図面を用いて本発明の実施例を説
明する。図1において、1はディーゼルエンジン、2は
エンジンの吸気管、3はエンジンの排気管を示す。ま
た、5は排気管3に接続された後述のNOX 吸収剤5で
ある。本実施例では、エンジン排気管3のNOX 吸収剤
5上流側には排気シャッターバルブ6が設けられてい
る。
Embodiments of the present invention will be described below with reference to the accompanying drawings. In FIG. 1, 1 is a diesel engine, 2 is an engine intake pipe, and 3 is an engine exhaust pipe. Reference numeral 5 is a NO x absorbent 5 which will be described later and is connected to the exhaust pipe 3. In this embodiment, an exhaust shutter valve 6 is provided on the upstream side of the NO x absorbent 5 in the engine exhaust pipe 3.

【0011】シャッターバルブ6は全開時の排気抵抗の
少ないバタフライ弁の形式であり、エンジンの通常運転
時には全開に保持されており、NOX 吸収剤5からのN
Xの再生操作時に所定開度まで閉弁され、排気管3を
絞ってNOX 吸収剤5を通過する排気ガス量を低減させ
る。7はシャッターバルブ6を開閉駆動する負圧アクチ
ュエータ等の適宜な形式のアクチュエータである。
[0011] The shutter valve 6 is in the form of exhaust resistance less butterfly valve fully open state during normal operation of the engine is held fully opened, N from the NO X absorbent 5
The valve is closed to a predetermined opening when the O X is regenerated, and the exhaust pipe 3 is throttled to reduce the amount of exhaust gas passing through the NO X absorbent 5. Reference numeral 7 is an actuator of an appropriate type such as a negative pressure actuator that drives the shutter valve 6 to open and close.

【0012】また、エンジン排気管3のシャッターバル
ブ6とNOX 吸収剤5との間には後述する還元剤供給装
置11が配置されており、NOX 吸収剤5の再生操作時
にNOX 吸収剤の上流側の排気管に還元剤を供給するよ
うになっている。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。ECU20はCPU、
RAM、ROM、及び入力ポート、出力ポートを相互に
双方向バスで接続した構成の、公知のディジタルコンピ
ュータからなり、エンジンの燃料噴射量制御等の基本制
御を行うほか、本実施例では排気シャッターバルブ6の
開閉制御と、還元剤供給装置11からの還元剤供給制御
とを行っている。これらの制御のためECU20の入力
ポートには、排気温度、エンジン回転数、アクセル開度
等の信号がそれぞれ図示しないセンサから入力されてい
る。
Further, the NO X absorbent when is disposed a reducing agent supply device 11 to be described later, the regenerating operation of the NO X absorbent 5 is provided between the shutter valve 6 and the NO X absorbent 5 of the engine exhaust pipe 3 The reducing agent is supplied to the exhaust pipe on the upstream side of. Reference numeral 20 in the drawing denotes an electronic control unit (ECU) of the engine 1. The ECU 20 is a CPU,
The RAM, the ROM, the input port, and the output port are connected to each other by a bidirectional bus, and are composed of known digital computers to perform basic control such as fuel injection amount control of the engine. In this embodiment, an exhaust shutter valve is also provided. The opening / closing control of 6 and the reducing agent supply control from the reducing agent supply device 11 are performed. For these controls, signals such as exhaust temperature, engine speed, accelerator opening, etc. are input to the input ports of the ECU 20 from sensors not shown.

【0013】NOX 吸収剤5は例えばアルミナ等の担体
を使用し、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
選ばれた少なくとも一つと、白金Pt のような貴金属と
が担持されている。このNOX 吸収剤5は流入する排気
の空燃比がリーンの場合にはNOX を吸収し、酸素濃度
が低下するとNOX を放出するNOX の吸放出作用を行
う。
As the NO x absorbent 5, for example, a carrier such as alumina is used, and on this carrier, an alkali metal such as potassium K, sodium Na, lithium Li, cesium Cs, or an alkaline earth such as barium Ba or calcium Ca is used. At least one selected from rare earths such as lanthanum La and yttrium Y, and a noble metal such as platinum Pt are supported. This the NO X absorbent 5 absorbs NO X in the case the air-fuel ratio of the exhaust gas flowing is lean, the oxygen concentration is carried out to absorbing and releasing action of the NO X that releases NO X when lowered.

【0014】なお、上述の排気空燃比とは、ここではN
X 吸収剤5の上流側の排気通路やエンジン燃焼室、吸
気通路等にそれぞれ供給された空気量の合計と燃料の合
計の比を意味するものとする。従って、NOX 吸収剤5
の上流側排気通路に燃料、還元剤または空気が供給され
ない場合には排気空燃比はエンジンの運転空燃比(エン
ジン燃焼室内の燃焼における空燃比)と等しくなる。
The above exhaust air-fuel ratio is N in this case.
O X absorbent upstream of 5 exhaust passage and the engine combustion chamber is intended to mean the ratio of the total sum and the fuel respectively supplied amount of air in the intake passage or the like. Therefore, NO x absorbent 5
When fuel, reducing agent or air is not supplied to the upstream side exhaust passage of, the exhaust air-fuel ratio becomes equal to the operating air-fuel ratio of the engine (air-fuel ratio in combustion in the engine combustion chamber).

【0015】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、通常運転時の排気空燃比はリーンであ
り、NOX 吸収剤5は排気中のNOX の吸収を行う。ま
た、還元剤供給装置11から排気中に還元剤が導入され
て酸素濃度が低下すると、NOX 吸収剤5は吸収した還
元剤の放出を行う。この吸放出作用の詳細なメカニズム
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7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。
In this embodiment, since the diesel engine is used, the exhaust air-fuel ratio during normal operation is lean, and the NO X absorbent 5 absorbs NO X in the exhaust. Further, when the reducing agent is introduced into the exhaust gas from the reducing agent supply device 11 and the oxygen concentration is reduced, the NO x absorbent 5 releases the absorbed reducing agent. There are some points where the detailed mechanism of this absorption / release action is not clear. However, it is considered that this absorbing / releasing action is performed by the mechanism shown in FIG. Next, this mechanism will be described by taking as an example the 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.

【0016】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7(A) に示され
るようにこれら酸素O2 がO2 - またはO2-の形で白金
Ptの表面に付着する。一方、流入排気中のNOは白金
Pt の表面上でこのO2 - またはO2-と反応し、NO2
となる(2NO+O2 →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7(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5内に
吸収される。
That is, when the inflow exhaust becomes considerably lean, the oxygen concentration in the inflow exhaust greatly increases, and as shown in FIG. 7 (A), the oxygen O 2 is in the form of O 2 or O 2 −. It adheres to the surface of platinum Pt. On the other hand, NO in the inflowing exhaust gas reacts with this O 2 or O 2 on the surface of platinum Pt to generate NO 2
(2NO + O 2 → 2NO 2 ). Next, a part of the generated NO 2 is oxidized on the platinum Pt, absorbed in the absorbent and bonded to the barium oxide BaO, and as shown in FIG.
As shown in ( 3 ), it diffuses into the absorbent in the form of nitrate ion NO 3 . In this way, NO X is absorbed in the NO X absorbent 5.

【0017】従って、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
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 の生成量が減少すると
反応が逆方向(NO3 - →NO2 )に進み、こうして吸
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。すなわち、流入排気中の酸素濃度が低下す
るとNOX 吸収剤5からNOX が放出されることにな
る。
Therefore, NO 2 is produced on the surface of platinum Pt as long as the oxygen concentration in the inflowing exhaust gas is high, and NO 2 is absorbed in the absorbent and the nitrate ion NO 3 unless the NO X absorption capacity of the absorbent is saturated. - is generated. In contrast the oxygen concentration decreases and the amount of NO 2 is reduced by reaction backward in the inflowing exhaust gas (NO 3 - → NO 2) proceeds to thus of the absorbent and nitrate ions NO 3 - is NO 2 Is released from the absorbent in the form of. That is, the oxygen concentration in the inflowing exhaust gas is released NO X from the NO X absorbent 5 when lowered.

【0018】一方、流入排気中にHC、CO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
- またはO2-と反応して酸化され、排気中の酸素を消費
して排気中の酸素濃度を低下させる。また、排気中の酸
素濃度低下によりNOX 吸収剤5から放出されたNO2
は図7(B) に示すように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。
On the other hand, when reducing components such as HC and CO are present in the inflowing exhaust gas, these components are oxygen O 2 on platinum Pt.
- or it is reacted with oxide and O 2-, lowering the oxygen concentration in the exhaust to consume oxygen in the exhaust. In addition, NO 2 released from the NO X absorbent 5 due to a decrease in oxygen concentration in the exhaust gas
Is reduced by reacting with HC and CO as shown in FIG. 7 (B). When NO 2 is no longer present on the surface of platinum Pt in this manner, NO 2 is released from the absorbent one after another.

【0019】すなわち、流入排気中のHC,COは、ま
ず白金Pt 上のO2 - またはO2-とただちに反応して酸
化され、次いで白金Pt 上のO2 - またはO2-が消費さ
れてもまだHC,COが残っていればこの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。NOX 吸収剤5のNOX
出、還元操作(再生操作)に使用する還元剤としては、
排気中で炭化水素や一酸化炭素等の還元成分を発生する
ものであれば良く、水素、一酸化炭素等の気体、プロパ
ン、プロピレン、ブタン等の液体又は気体の炭化水素、
ガソリン、軽油、灯油等の液体燃料等が使用できるが、
本実施例では前述のように貯蔵、補給等の際の煩雑さを
避けるためディーゼルエンジン1の燃料である軽油を還
元剤として使用している。
[0019] That is, HC in the inflowing exhaust gas, CO, first O 2 on the platinum Pt - immediately react with oxidized or O 2-, and then on the platinum Pt O 2 - or O 2- is consumed the HC, NO X discharged from the released NO X and the engine from the absorbent by CO is reduced even yet HC, any remaining CO is. As the reducing agent used for the NO x releasing and reducing operation (regenerating operation) of the NO x absorbent 5,
It is sufficient if it produces a reducing component such as hydrocarbon or carbon monoxide in exhaust gas, hydrogen, gas such as carbon monoxide, liquid or gaseous hydrocarbon such as propane, propylene, butane,
Liquid fuels such as gasoline, light oil, and kerosene can be used,
In this embodiment, as described above, light oil, which is the fuel of the diesel engine 1, is used as the reducing agent in order to avoid the complexity of storage, replenishment, and the like.

【0020】次に、図2を用いて本実施例の還元剤供給
装置11について説明する。前述のように軽油を還元剤
として使用する場合には軽油中の高沸点成分が液状のま
まNOX 吸収剤5に付着する問題が生じる。本実施例で
は以下に説明するように還元剤供給装置11から供給す
る軽油を予熱することにより上記の液体燃料の付着の問
題を解決している。
Next, the reducing agent supply device 11 of this embodiment will be described with reference to FIG. As described above, when light oil is used as the reducing agent, there arises a problem that the high boiling point components in the light oil adhere to the NO X absorbent 5 in a liquid state. In the present embodiment, as described below, the problem of the liquid fuel adhesion is solved by preheating the light oil supplied from the reducing agent supply device 11.

【0021】図2において、還元剤供給装置11は、排
気管3のNOX 吸収剤5上流側に配置された噴射弁12
を備えている。噴射弁12は、前述のECU20からの
制御信号に応じて開閉してNOX 吸収剤5上流側に還元
剤(軽油)を噴射し、NOX吸収剤5の再生操作を行
う。軽油はディーゼルエンジン1の燃料供給装置14か
ら、ECU20の制御信号に応じて開閉する遮断弁15
と燃料通路13とを介して噴射弁12に圧力供給され
る。本実施例では、燃料通路13は排気管3の周囲に巻
き回された熱交換部13aを備えており、排気管3内の
排気ガスの熱により、熱交換部13a内の軽油を予熱す
るようになっている。
In FIG. 2, the reducing agent supply device 11 includes an injection valve 12 disposed upstream of the NO x absorbent 5 in the exhaust pipe 3.
Is equipped with. Injection valve 12 injects a reducing agent (light oil) to the NO X absorbent 5 upstream opening and closing in response to a control signal from the above-mentioned ECU 20, performs the regenerating operation of the NO X absorbent 5. Light oil is supplied from the fuel supply device 14 of the diesel engine 1 to a shutoff valve 15 which opens and closes in response to a control signal from the ECU 20.
Pressure is supplied to the injection valve 12 through the fuel passage 13 and the fuel passage 13. In the present embodiment, the fuel passage 13 is provided with a heat exchange section 13a wound around the exhaust pipe 3 so that the heat of the exhaust gas in the exhaust pipe 3 preheats the light oil in the heat exchange section 13a. It has become.

【0022】本実施例では、NOX 吸収剤5の再生操作
が完了すると(すなわち、軽油の噴射を完了して噴射弁
12が閉弁すると)、ECU20の信号により遮断弁1
5が開弁する。これにより、噴射弁12までの燃料通路
13内には燃料供給装置14の出口圧力相当の圧力の軽
油が充填される。所定時間が経過すると遮断弁15は閉
弁され、遮断弁15と噴射弁12との間の燃料通路13
は両端を密閉された状態に保持される。
In this embodiment, when the regeneration operation of the NO x absorbent 5 is completed (that is, the injection of the light oil is completed and the injection valve 12 is closed), the shutoff valve 1 is triggered by a signal from the ECU 20.
5 opens. As a result, the fuel passage 13 up to the injection valve 12 is filled with light oil having a pressure equivalent to the outlet pressure of the fuel supply device 14. When a predetermined time has elapsed, the shutoff valve 15 is closed, and the fuel passage 13 between the shutoff valve 15 and the injection valve 12 is closed.
Is kept sealed at both ends.

【0023】燃料通路13内に保持された軽油は、次回
の再生操作が開始されるまでの間この密閉状態のまま熱
交換部13aを介して排気ガスの熱を受け、加熱され
る。このため、燃料通路内13内の軽油は温度が上昇す
るとともに、蒸気圧の上昇により圧力が上昇し、高温、
高圧の状態になる。 次いで、NOX 吸収剤5の再生条
件が成立するとECU20の信号により噴射弁12が開
弁する。これにより、燃料通路13内の高圧の軽油は噴
射弁12から排気通路3内に噴射される。軽油は燃料通
路13内で高温になり低沸点成分は既に気化している
が、液状のまま残っていた高沸点成分も、燃料通路13
内が噴射弁12の開弁により高圧状態から急激に減圧さ
れるため瞬時に気化する。このため、NOX 吸収剤5に
は気体状の軽油のみが供給され、軽油の液状成分の到達
による前述の問題が防止される。
The light oil held in the fuel passage 13 is heated by receiving the heat of the exhaust gas via the heat exchanging portion 13a in this sealed state until the next regeneration operation is started. Therefore, the temperature of the light oil in the fuel passage 13 rises, and the pressure rises due to the rise of the vapor pressure, so that the high temperature,
High pressure. Next, when the regeneration condition of the NO X absorbent 5 is satisfied, the injection valve 12 is opened by the signal of the ECU 20. As a result, the high pressure light oil in the fuel passage 13 is injected from the injection valve 12 into the exhaust passage 3. The light oil has a high temperature in the fuel passage 13 and the low-boiling point component has already vaporized, but the high-boiling point component that remains in the liquid state also remains in the fuel passage 13.
The inside is rapidly depressurized from the high pressure state due to the opening of the injection valve 12, so that it is instantly vaporized. Therefore, only the gaseous light oil is supplied to the NO x absorbent 5, and the above-mentioned problems due to the arrival of the liquid component of the light oil are prevented.

【0024】なお、上述の実施例では、燃料供給装置1
4と燃料通路13との間にECU20の信号に応じて開
閉する遮断弁15を設けているが、遮断弁15の代わり
に燃料通路13から燃料供給装置14への軽油の逆流を
防止する逆止弁を設けた構成としてもよい。この場合に
は、再生操作時に噴射弁12が開弁して燃料通路13内
の圧力が燃料供給圧力以下に低下すると逆止弁を通って
燃料供給装置14から燃料通路13内に自動的に軽油が
流入するため、遮断弁15の開閉操作が不要となる。
In the above embodiment, the fuel supply system 1
4 and the fuel passage 13 are provided with a shut-off valve 15 which opens and closes in response to a signal from the ECU 20, but instead of the shut-off valve 15, a non-return valve for preventing back flow of light oil from the fuel passage 13 to the fuel supply device 14. A valve may be provided. In this case, when the injection valve 12 is opened during the regeneration operation and the pressure in the fuel passage 13 drops below the fuel supply pressure, the fuel oil is automatically fed from the fuel supply device 14 into the fuel passage 13 through the check valve. Therefore, it is not necessary to open / close the shutoff valve 15.

【0025】なお、本実施例ではNOX 吸収剤5への軽
油供給量は遮断弁15と噴射弁12との間の燃料通路1
3の容積と、燃料供給装置14の燃料供給圧力により決
定される。また、本実施例では燃料通路13の熱交換部
13aは排気管3の周囲に設けられているが、図3に示
すように熱交換部13aを排気管3内に配置した構成と
すれば軽油を更に高温高圧の状態に保持することができ
る。
In this embodiment, the amount of light oil supplied to the NO x absorbent 5 is controlled by the fuel passage 1 between the shutoff valve 15 and the injection valve 12.
3 and the fuel supply pressure of the fuel supply device 14. Further, in the present embodiment, the heat exchange portion 13a of the fuel passage 13 is provided around the exhaust pipe 3, but if the heat exchange portion 13a is arranged in the exhaust pipe 3 as shown in FIG. Can be maintained in a high temperature and high pressure state.

【0026】次に、図4に本発明の別の実施例を示す。
本実施例では、燃料通路13の熱交換部13aは、排気
管3の周囲に形成された比較的容量の大きな容器の形式
とされている。また、熱交換部13aの下部には遮断弁
16を介して燃料回収通路17が接続されており、噴射
弁12は熱交換部13aの上部に接続されている。本実
施例では、熱交換部13a内の軽油が加熱され高温高圧
状態になると、軽油の気化した低沸点成分は熱交換部1
3aの上部にに充満し、下部には気化しない高沸点成分
が液体のまま滞留する。噴射弁12が開弁すると、熱交
換部13内の軽油が排気管3内に噴射されるが、噴射弁
12は熱交換部13aの上部に接続されているため噴射
弁12からは上部の気化した低沸点成分と、熱交換部1
3内の減圧により気化した高沸点成分のみが噴射され
る。このため、噴射弁12からは気体状の軽油のみが噴
射されるのでNOX 吸収剤5への液状成分の付着をより
確実に防止できる。
Next, FIG. 4 shows another embodiment of the present invention.
In this embodiment, the heat exchange portion 13a of the fuel passage 13 is in the form of a container formed around the exhaust pipe 3 and having a relatively large capacity. Further, a fuel recovery passage 17 is connected to a lower part of the heat exchange part 13a via a shutoff valve 16, and the injection valve 12 is connected to an upper part of the heat exchange part 13a. In the present embodiment, when the light oil in the heat exchange section 13a is heated to a high temperature and high pressure state, the vaporized low boiling point component of the light oil is transferred to the heat exchange section 1
A high-boiling component that fills the upper part of 3a and does not vaporize remains in the lower part as a liquid. When the injection valve 12 opens, the light oil in the heat exchange part 13 is injected into the exhaust pipe 3, but since the injection valve 12 is connected to the upper part of the heat exchange part 13a, the upper part of the injection valve 12 vaporizes. Low boiling point component and heat exchange part 1
Only the high boiling point component vaporized by the pressure reduction in 3 is injected. For this reason, since only the gaseous light oil is injected from the injection valve 12, it is possible to more reliably prevent the liquid component from adhering to the NO X absorbent 5.

【0027】なお、本実施例では再生操作完了後熱交換
部13a下部の遮断弁16が開弁され、熱交換部13a
内に液体のまま残留している高沸点成分が回収通路17
を介してエンジン燃料系統に回収されるとともに、上部
の遮断弁15が下部遮断弁16の開弁と同時に開き、燃
料供給装置14から熱交換部13aに軽油が供給されて
熱交換部13a内の軽油の入替えが行われる。上部の遮
断弁15は下部の遮断弁16が閉弁した後所定時間経過
後に閉弁し、その間に熱交換部13aに所定量の新しい
軽油が充填される。
In this embodiment, after the regeneration operation is completed, the shutoff valve 16 below the heat exchange section 13a is opened, and the heat exchange section 13a is opened.
The high boiling point component that remains as a liquid inside the recovery passageway 17
And the upper cutoff valve 15 opens simultaneously with the opening of the lower cutoff valve 16, and the light oil is supplied from the fuel supply device 14 to the heat exchange section 13a to collect the heat in the heat exchange section 13a. Light oil is replaced. The upper cutoff valve 15 is closed after a predetermined time has elapsed after the lower cutoff valve 16 was closed, and during that time, the heat exchange section 13a is filled with a predetermined amount of new light oil.

【0028】次に図5に本発明の更に別の実施例を示
す。本実施例では、還元剤供給装置11には前述の実施
例のような熱交換部は設けられておらず、噴射弁12下
流側の排気通路3に気化用蓄熱体18aを内蔵した予熱
室18が設けられている点が相違している。蓄熱体18
aはセラミック焼結材等の多孔質材料から構成され、図
6に示すように内部に排気流方向の通路19が形成され
ている。通路19は、下流側端部が閉塞された通路19
aと上流側端部が閉塞された通路19bとが交互に配置
されており、排気は通路19aから蓄熱体18aに流入
し、通路19a、19bとを隔てる壁面19cを通過し
て通路19bから流出するようになっている。
Next, FIG. 5 shows still another embodiment of the present invention. In the present embodiment, the reducing agent supply device 11 is not provided with the heat exchange portion as in the above-described embodiment, and the preheating chamber 18 in which the vaporization heat storage body 18a is built in the exhaust passage 3 on the downstream side of the injection valve 12 is provided. The difference is that is provided. Heat storage body 18
Reference symbol a is made of a porous material such as a ceramic sintered material, and as shown in FIG. 6, a passage 19 in the exhaust flow direction is formed inside. The passage 19 is a passage 19 whose downstream end is closed.
a and a passage 19b whose upstream end is closed are alternately arranged, and the exhaust gas flows into the heat storage body 18a from the passage 19a, passes through the wall surface 19c separating the passages 19a and 19b, and flows out from the passage 19b. It is supposed to do.

【0029】本実施例では、蓄熱体18aはNOX 吸収
剤5がNOX の吸収を行っている時に通過する排気ガス
により加熱され高温になる。NOX 吸収剤5の再生操作
時には、噴射弁12から噴射された霧状の軽油は排気と
ともに蓄熱体18aに流入する。この際、軽油の高沸点
成分は液状のまま蓄熱体18aに流入するが、排気が蓄
熱体18aの通路19aと19bとを隔てる壁面19c
を通過する際にトラップされるため、蓄熱体18aの下
流側のNOX 吸収剤5には排気と、軽油の気化成分のみ
が到達する。また、蓄熱体18aにトラップされた軽油
の高沸点成分は高温の蓄熱体18aから気化熱を奪って
気化するため、高沸点成分の気化に際してNOX 吸収剤
5の温度が低下することがない。また、排気温度が低い
場合は、蓄熱体18aにトラップされた軽油の高沸点成
分の一部は液状のまま蓄熱体18aに残留することにな
るが、エンジンの負荷が増大して排気温度が上昇したと
きに気化して蓄熱体18aから流出し、NOX 吸収剤5
の触媒作用により酸化されるため蓄熱体18aの排気通
路が閉塞したり、HC、CO等のエミッションが悪化す
ることはない。本実施例では、予熱室18の外部には断
熱材18bが設けられ、蓄熱体18aからの熱放散を防
止し、蓄熱体18aの高温を維持するように鳴ってい
る。
[0029] In this embodiment, the regenerator 18a becomes a high temperature is heated by the exhaust gas passing through when the NO X absorbent 5 is performing the absorption of NO X. During the regeneration operation of the NO x absorbent 5, the mist-like light oil injected from the injection valve 12 flows into the heat storage body 18a together with the exhaust gas. At this time, the high boiling point component of the light oil flows into the heat storage body 18a in a liquid state, but the exhaust wall surface 19c that separates the passages 19a and 19b of the heat storage body 18a.
Since it is trapped when passing through the exhaust gas, only the exhaust gas and the vaporized component of light oil reach the NO X absorbent 5 on the downstream side of the heat storage body 18a. Further, since the high boiling point component of the light oil trapped in the heat storage body 18a deprives the heat of vaporization from the high temperature heat storage body 18a and is vaporized, the temperature of the NO x absorbent 5 does not drop when the high boiling point component is vaporized. Further, when the exhaust gas temperature is low, a part of the high boiling point component of the light oil trapped in the heat storage material 18a remains in the heat storage material 18a in a liquid state, but the engine load increases and the exhaust gas temperature rises. When it does, it vaporizes and flows out from the heat storage body 18a, and the NO x absorbent 5
Since it is oxidized by the catalytic action of the above, the exhaust passage of the heat storage body 18a is not blocked, and the emissions of HC, CO, etc. do not deteriorate. In this embodiment, a heat insulating material 18b is provided outside the preheating chamber 18 to prevent heat from being dissipated from the heat storage body 18a and to keep the heat storage body 18a at a high temperature.

【0030】なお、上記に説明した実施例では、排気温
度が比較的低い場合には軽油の高沸点成分の一部が液状
のままNOX 吸収剤5に到達する場合が考えられるが、
上述のように到達する液体成分の量は僅かであり、ま
た、液体成分に先立って到達した気化成分の酸化反応に
よる発熱によりNOX 吸収剤5の温度が上昇しているた
めNOX 吸収剤5に到達した液体成分も速やかに気化
し、NOX 吸収剤5の活性低下や低温被毒を生じるには
至らない。
In the embodiment described above, when the exhaust temperature is relatively low, it is possible that a part of the high boiling point component of the light oil reaches the NO x absorbent 5 in a liquid state.
The amount of the liquid component to arrive as described above is small, also, the NO X absorbent and the temperature of the NO X absorbent 5 is raised by heat generated by the oxidation reaction of the vaporized component having reached prior to the liquid components 5 The liquid component that has reached the point (3) is also promptly vaporized, and the activity of the NO x absorbent 5 and low temperature poisoning do not occur.

【0031】[0031]

【発明の効果】本発明によれば、液体還元剤を用いてN
X 吸収剤の再生を行う場合に、NO X 吸収剤に供給す
る前に液体還元剤を予熱する手段を設けたことにより、
NOX吸収剤に液状のまま還元剤が到達することによる
NOX 吸収剤の活性低下や低温被毒の発生を防止し、液
体還元剤を用いて簡易な手段でNOX 吸収剤の再生操作
を行うことができる。
According to the present invention, N
OXNO when regenerating the absorbent XSupply to absorbent
By providing a means for preheating the liquid reducing agent before
NOXDue to the reducing agent reaching the absorbent in a liquid state
NOXPrevents the activity of the absorbent from decreasing and the occurrence of low temperature poisoning.
NO by simple means using body reducing agentXRegeneration operation of absorbent
It can be performed.

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

【図1】本発明の排気浄化装置の第一の実施例を示す図
である。
FIG. 1 is a diagram showing a first embodiment of an exhaust emission control device of the present invention.

【図2】図1の還元剤供給装置の構成の一例を示す図で
ある。
FIG. 2 is a diagram showing an example of a configuration of the reducing agent supply device of FIG.

【図3】図1の還元剤供給装置の構成の一例を示す図で
ある。
FIG. 3 is a diagram showing an example of a configuration of the reducing agent supply device of FIG.

【図4】図1の還元剤供給装置の構成の一例を示す図で
ある。
FIG. 4 is a diagram showing an example of a configuration of the reducing agent supply device of FIG.

【図5】本発明の排気浄化装置の第二の実施例を示す図
である。
FIG. 5 is a diagram showing a second embodiment of the exhaust emission control device of the present invention.

【図6】図5の蓄熱体の構成を示す図である。6 is a diagram showing a configuration of a heat storage body of FIG.

【図7】NOX 吸収剤のNOX 吸放出作用を説明する図
である。
FIG. 7 is a diagram illustrating the NO X absorption and release action of a NO X absorbent.

【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 5…NOX 吸収剤 6…シャッターバルブ 7…アクチュエータ 11…還元剤供給装置 12…噴射弁 13…燃料通路 13a…熱交換部 14…燃料供給装置 15…遮断弁 16…遮断弁 17…回収通路 18…予熱室 18a…蓄熱体 19…排気通路 20…ECUDESCRIPTION OF SYMBOLS 1 ... Diesel engine 2 ... Intake pipe 3 ... Exhaust pipe 5 ... NO X absorbent 6 ... Shutter valve 7 ... Actuator 11 ... Reducing agent supply device 12 ... Injection valve 13 ... Fuel passage 13a ... Heat exchange part 14 ... Fuel supply device 15 ... shut-off valve 16 ... shut-off valve 17 ... recovery passage 18 ... preheating chamber 18a ... heat storage body 19 ... exhaust passage 20 ... ECU

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 リーン空燃比の燃焼を行うことのできる
内燃機関の排気通路に、流入排気の空燃比がリーンのと
きにNOX を吸収し流入排気の酸素濃度が低下したとき
に吸収したNOX を放出するNOX 吸収剤を配置し、排
気中のNOXを吸収させ、NOX 吸収後に前記NOX
収剤に液体還元剤を供給してNOX 吸収剤から吸収した
NOX を放出させると共に該NOX を還元浄化する内燃
機関の排気浄化装置において、前記NOX 吸収剤に供給
する液体還元剤を予熱する還元剤予熱手段を備えたこと
を特徴とする内燃機関の排気浄化装置。
In an exhaust passage of claim 1 an internal combustion engine capable of performing combustion of the lean air-fuel ratio, the air-fuel ratio of the inflowing exhaust gas is the oxygen concentration of the inflowing exhaust absorbs NO X when the lean absorbed when reduced NO place the NO X absorbent to release the X, the NO X in the exhaust gas is absorbed to release the the NO X absorbent NO X which the liquid reducing agent is supplied and absorbed from the NO X absorbent in after NO X absorbent the in the exhaust purification device for an internal combustion engine NO X to reduce and purify the the NO X absorbent exhaust purification system of an internal combustion engine, characterized in that it comprises a reducing agent preheating means for preheating the supply liquid reducing agent together.
JP05057411A 1993-03-17 1993-03-17 Exhaust gas purification device for internal combustion engine Expired - Lifetime JP3093905B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05057411A JP3093905B2 (en) 1993-03-17 1993-03-17 Exhaust gas purification device for internal combustion engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05057411A JP3093905B2 (en) 1993-03-17 1993-03-17 Exhaust gas purification device for internal combustion engine

Publications (2)

Publication Number Publication Date
JPH06272539A true JPH06272539A (en) 1994-09-27
JP3093905B2 JP3093905B2 (en) 2000-10-03

Family

ID=13054910

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05057411A Expired - Lifetime JP3093905B2 (en) 1993-03-17 1993-03-17 Exhaust gas purification device for internal combustion engine

Country Status (1)

Country Link
JP (1) JP3093905B2 (en)

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JPH10212932A (en) * 1997-01-29 1998-08-11 Hino Motors Ltd Exhaust gas emission control device for internal combustion engine
AU702289B2 (en) * 1994-07-01 1999-02-18 Ivoclar Ag ZrO2-containing glass-ceramic
US6619035B2 (en) 2000-07-24 2003-09-16 Toyota Jidosha Kabushiki Kaisha Exhaust emission control device of internal combustion engine
JP2005283201A (en) * 2004-03-29 2005-10-13 Nissan Diesel Motor Co Ltd Water level meter mounting structure
WO2007077919A1 (en) * 2006-01-06 2007-07-12 Mitsui Engineering & Shipbuilding Co., Ltd. Method of denitration of exhaust gas and apparatus therefor
JP2007182804A (en) * 2006-01-06 2007-07-19 Hino Motors Ltd Exhaust emission control device
JP2009510323A (en) * 2005-09-30 2009-03-12 コリア・インスティチュート・オブ・エネルギー・リサーチ Exhaust gas heating device for internal combustion engine
WO2011000685A1 (en) * 2009-07-01 2011-01-06 Sulzer Chemtech Ag Device for cleaning exhaust gases containing nox
WO2012107637A1 (en) * 2011-02-10 2012-08-16 Wärtsilä Finland Oy Exhaust gas receiver, internal combustion engine and method for selective catalytic reduction
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AU702289B2 (en) * 1994-07-01 1999-02-18 Ivoclar Ag ZrO2-containing glass-ceramic
JPH10212932A (en) * 1997-01-29 1998-08-11 Hino Motors Ltd Exhaust gas emission control device for internal combustion engine
US6619035B2 (en) 2000-07-24 2003-09-16 Toyota Jidosha Kabushiki Kaisha Exhaust emission control device of internal combustion engine
JP2005283201A (en) * 2004-03-29 2005-10-13 Nissan Diesel Motor Co Ltd Water level meter mounting structure
JP2009510323A (en) * 2005-09-30 2009-03-12 コリア・インスティチュート・オブ・エネルギー・リサーチ Exhaust gas heating device for internal combustion engine
WO2007077919A1 (en) * 2006-01-06 2007-07-12 Mitsui Engineering & Shipbuilding Co., Ltd. Method of denitration of exhaust gas and apparatus therefor
JP2007182804A (en) * 2006-01-06 2007-07-19 Hino Motors Ltd Exhaust emission control device
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WO2011000685A1 (en) * 2009-07-01 2011-01-06 Sulzer Chemtech Ag Device for cleaning exhaust gases containing nox
CN102472142A (en) * 2009-07-01 2012-05-23 苏舍化学技术有限公司 Device For Cleaning Exhaust Gases Containing Nox
WO2012107637A1 (en) * 2011-02-10 2012-08-16 Wärtsilä Finland Oy Exhaust gas receiver, internal combustion engine and method for selective catalytic reduction
EP2673484B1 (en) 2011-02-10 2015-08-26 Wärtsilä Finland Oy Exhaust gas receiver, internal combustion engine and method for selective catalytic reduction
CN102733914A (en) * 2012-07-02 2012-10-17 中国第一汽车股份有限公司 Post-processing control unit of ammonia storage and supply in exhaust branch pipe afterheat manner
CN103437867A (en) * 2013-08-30 2013-12-11 东风商用车有限公司 Aerodynamic ammonia gas preparation and quantitative injection system
FR3027056A1 (en) * 2014-10-10 2016-04-15 Peugeot Citroen Automobiles Sa SELECTIVE CATALYTIC REDUCTION DEVICE
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CN109441598B (en) * 2018-12-29 2019-11-05 常州信息职业技术学院 A kind of motor-driven vehicle treatment apparatus and its control system

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