JP3093905B2 - Exhaust gas purification device for internal combustion engine - Google Patents

Exhaust gas purification device for internal combustion engine

Info

Publication number
JP3093905B2
JP3093905B2 JP05057411A JP5741193A JP3093905B2 JP 3093905 B2 JP3093905 B2 JP 3093905B2 JP 05057411 A JP05057411 A JP 05057411A JP 5741193 A JP5741193 A JP 5741193A JP 3093905 B2 JP3093905 B2 JP 3093905B2
Authority
JP
Japan
Prior art keywords
absorbent
exhaust gas
exhaust
fuel
reducing agent
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
JP05057411A
Other languages
Japanese (ja)
Other versions
JPH06272539A (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 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 from exhaust energy
    • F01N5/02Exhaust or silencing apparatus combined or associated with devices profiting from 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

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 exhaust gas purifying apparatus for an internal combustion engine, such as a diesel engine or a lean-burn gasoline engine, which burns at a lean air-fuel ratio in most operating regions. of the NO X in the exhaust gas effectively removable it relates to an exhaust purification device.

【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 gas purifying apparatus is disclosed, for example, 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 By shutting off the inflow of exhaust gas into the absorbent and supplying a gaseous reducing agent to the absorbent, NO X is released from the absorbent and the released NO X is reduced and purified. It 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。
Problems to be Solved by the Invention
In the exhaust gas purifying apparatus disclosed in Japanese Patent No. 6826, a gaseous reducing agent such as hydrogen is supplied to the NO X absorbent in order to release NO X from the NO X absorbent and perform reduction purification (hereinafter referred to as “regeneration”). I have. However, the 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 especially when it is used for a vehicle internal combustion engine.

【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。
[0004] Thus, the reducing agent used for regeneration of the NO X absorbent, it is preferred that the handling is using a reducing agent simple liquid. In addition, in order to reduce 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 the liquid reducing agent. However, liquid fuel such as light oil in particular contains many components having different boiling points, and also contains components that are difficult to vaporize when the exhaust temperature is low. For this reason, these liquid fuels are
When injected into the exhaust passage on the upstream side of the X absorbent, components having a high boiling point do not evaporate and remain in the form of a mist together with the exhaust gas.
It may reach the X absorbent. In this case NO X
The fuel that has reached the absorbent adheres to the surface of the absorbent in a liquid state, and forms a layer covering the surface of the absorbent.

【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。
[0005] Liquid fuel adhering to the NO X absorbent surface,
When the temperature of the absorbent is high to some extent, the heat of the absorbent is vaporized by the heat of the absorbent to act 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 drop below the activation temperature. Therefore, when a liquid fuel such as light oil is used as a 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, it will cover the surface of the NO X absorbent fuel temperature is attached to the absorbent and lower than the vaporization temperature of the fuel no longer vaporization without the NO X absorbent, of the NO X by reduction of the effective surface area absorption, release effect is inhibited, in some cases problems of cold poisoning called the NO X absorbent occurs. For the above reasons, conventionally, when a liquid fuel such as light oil is used as a reducing agent, a burner or the like is provided in an exhaust passage to incompletely burn the liquid fuel, and the generated gas such as HC and CO is used as a reducing agent. It had to be supplied to the X absorbent. However, it is not preferable from the viewpoint of safety to provide a burner or the like in the exhaust passage from the viewpoint of safety, 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。
[0007] The present invention is intended to provide an exhaust purification system of an internal combustion engine which can solve the above problems, to use a liquid fuel such as light oil as the reducing agent of the NO X absorbent.

【0008】[0008]

【課題を解決するための手段】本発明によれば、流入す
る排気ガスの空燃比がリーンであるときにNO X を吸収
し、流入する排気ガス中の酸素濃度を低下させると吸収
したNO X を放出するNO X 吸収剤を機関排気通路内に
配置すると共に、機関運転中常時NO X 吸収剤に排気ガ
スを流通させておき、NO X 吸収剤に流入する排気ガス
がリーンのときにNO X 吸収剤に吸収されたNO X をN
X 吸収剤に流入する排気ガス中の酸素濃度が低下せし
められたときにNO X 吸収剤から放出するようにした内
燃機関の排気浄化装置において、前記NO X 吸収剤に液
体還元剤を供給してNO X 吸収剤に流入する排気ガス中
の酸素濃度を低下せしめることによりNO X 吸収剤に吸
収されているNO X をNO X 吸収剤から放出させると共
に、前記NO X 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, an inflow
Absorbed NO X when the air-fuel ratio of the exhaust gas that is lean
And reduce the oxygen concentration in the incoming exhaust gas
The the NO X absorbent in the engine exhaust passage that releases the NO X
With placing, always the NO X absorbent during the operation of the engine exhaust gas
Scan allowed to flow through the exhaust gas flowing into the NO X absorbent
N but the NO X absorbed in the NO X absorbent when the lean
Oxygen concentration in the exhaust gas flowing into the O X absorbent Shi lowered
Among which is adapted to release from the NO X absorbent when is because
In the exhaust purification system of combustion engine, the liquid in the the NO X absorbent
Exhaust gas which is supplied to the body reducing agent flowing into the NO X absorbent
Absorption in the NO X absorbent by allowed to lower the oxygen concentration
Co when releasing the NO X that is yield from the NO X absorbent
To, to preheat the supplied liquid reducing agent to the the NO X absorbent
An exhaust gas purification device for an internal combustion engine, provided with a reducing agent preheating means, 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。
[Action] for liquid fuel supplied to the exhaust passage of the NO X absorbent upstream vaporized is preheated by preheating means before supplying liquid fuel to reach the left the NO X absorbent liquid is reduced, NO X absorption The temperature drop of the agent is prevented. For this reason,
The NO X absorbent decreased activity or cold poisoning problem does not occur.

【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, reference numeral 1 denotes a diesel engine, 2 denotes an intake pipe of the engine, and 3 denotes an exhaust pipe of the engine. Reference numeral 5 denotes a NO X absorbent 5 described later connected to the exhaust pipe 3. In this embodiment, the the NO X absorbent 5 upstream of the engine exhaust pipe 3 and an exhaust shutter valve 6 is provided.

【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
O X is closed to the predetermined opening degree at the time of the regenerating operation, reduce the amount of exhaust gas passing through the the NO X absorbent 5 squeezing exhaust pipe 3. Reference numeral 7 denotes an appropriate type of actuator 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 the exhaust pipe. In the figure, reference numeral 20 denotes an electronic control unit (ECU) of the engine 1. The ECU 20 is a CPU,
A known digital computer having a configuration in which a RAM, a ROM, and an input port and an output port are connected to each other via a bidirectional bus, performs basic control such as fuel injection amount control of an engine, and in this embodiment, an exhaust shutter valve. 6 and the control of the supply of the reducing agent from the reducing agent supply device 11. For these controls, input ports of the ECU 20 are supplied with signals such as exhaust temperature, engine speed, and accelerator opening 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。
[0013] the NO X absorbent 5 uses a carrier such as alumina or the like, the carrier on, for example potassium K, sodium Na, alkali metal, barium Ba, alkaline earth such as calcium Ca, such as lithium Li, cesium Cs And at least one selected from rare earths such as lanthanum La and yttrium Y, and a noble metal such as platinum Pt. 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-described exhaust air-fuel ratio is defined as N
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 no fuel, reducing agent or air is supplied to the upstream exhaust passage of the engine, 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。
[0015] In this embodiment, since the diesel engine is used, the exhaust air-fuel ratio during normal operation is lean, NO X absorbent 5 performs absorption of the NO X in the exhaust gas. Also, when a reducing agent is introduced into the exhaust oxygen concentration is lowered, the release of the NO X absorbent 5 absorbs reducing agent performs a reducing agent supply device 11. The detailed mechanism of this absorption / release action is 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.

【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 inflowing exhaust gas becomes considerably lean, the oxygen concentration in the inflowing exhaust gas greatly increases, and as shown in FIG. 7A, the oxygen O 2 is converted into 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, and NO 2
(2NO + O 2 → 2NO 2 ). Next, a part of the generated NO 2 is absorbed in the absorbent while being oxidized on the platinum Pt, and is combined with the barium oxide BaO.
It is diffused in the absorbent in the form of nitrate ions NO 3 - as shown in the. 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。
Accordingly, as long as the oxygen concentration in the inflowing exhaust gas is high, NO 2 is generated on the surface of the platinum Pt, and as long as the NO x absorption capacity of the absorbent is not saturated, NO 2 is absorbed in the absorbent and nitrate ions NO 3 - is generated. 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 becomes NO 2 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, if reducing components such as HC and CO are present in the inflowing exhaust gas, these components become 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. Further, the NO 2 released from the NO X absorbent 5 due to a decrease in the 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 the platinum Pt, 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. The NO X absorbent 5 of the NO X emission, the reducing agent used for reduction operation (reproducing operation),
Any substance that generates a reducing component such as hydrocarbon or carbon monoxide in the exhaust gas may be used.Hydrogen, gas such as carbon monoxide, liquid or gaseous hydrocarbon such as propane, propylene, and butane,
Liquid fuels such as gasoline, light oil and kerosene can be used,
In this embodiment, light oil, which is the fuel of the diesel engine 1, is used as a reducing agent in order to avoid complications in storage and replenishment as described above.

【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. When used as a reducing agent to gas oil as described above causes a problem that high-boiling component in the diesel fuel from adhering to leave the NO X absorbent 5 in a liquid. In this embodiment, as described below, the problem of the adhesion of the liquid fuel 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。
[0021] In FIG. 2, the reducing agent supply device 11 is arranged in the NO X absorbent 5 upstream side of the exhaust pipe 3 injectors 12
It has. 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 a fuel supply device 14 of the diesel engine 1 to a shut-off valve 15 which opens and closes in response to a control signal from the ECU 20.
Pressure is supplied to the injection valve 12 via the fuel passage 13 and the fuel passage 13. In the present embodiment, the fuel passage 13 includes a heat exchange portion 13a wound around the exhaust pipe 3, and the heat of the exhaust gas in the exhaust pipe 3 preheats the light oil in the heat exchange portion 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。
[0022] In this embodiment, the regenerating operation of the NO X absorbent 5 is completed (i.e., the injection valve 12 to complete the injection of diesel fuel is closed), the shut-off valve by ECU20 signals 1
5 opens. Thus, 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. After a lapse of a predetermined time, the shutoff valve 15 is closed, and the fuel passage 13 between the shutoff valve 15 and the injection valve 12 is closed.
Are kept closed 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 through the heat exchange section 13a in this sealed state until the next regeneration operation is started. For this reason, the temperature of the light oil in the fuel passage 13 increases, and the pressure increases due to the increase of the vapor pressure.
High pressure condition. Then, the injection valve 12 by ECU20 signal when the reproduction condition is satisfied in the NO X absorbent 5 is opened. Accordingly, 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 components have already been vaporized.
The inside is rapidly reduced in pressure from the high pressure state by the opening of the injection valve 12, so that the gas instantaneously evaporates. Therefore, the NO X absorbent 5 only gaseous diesel fuel is supplied, the foregoing by the arrival of the liquid component of the diesel fuel problems 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 device 1
A shutoff valve 15 that opens and closes in response to a signal from the ECU 20 is provided between the fuel passage 4 and the fuel passage 13, but instead of the shutoff valve 15, a check valve that prevents backflow of light oil from the fuel passage 13 to the fuel supply device 14. It is good also as composition provided with a valve. In this case, when the injection valve 12 is opened during the regeneration operation and the pressure in the fuel passage 13 falls below the fuel supply pressure, light oil is automatically fed from the fuel supply device 14 into the fuel passage 13 through the check valve. , The opening and closing operation of the shut-off valve 15 becomes unnecessary.

【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 the present embodiment, the amount of light oil supplied to the NO X absorbent 5 depends on 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. In this embodiment, the heat exchange portion 13a of the fuel passage 13 is provided around the exhaust pipe 3. However, if the heat exchange portion 13a is arranged in the exhaust pipe 3 as shown in FIG. Can be maintained at a higher temperature and a higher pressure.

【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 the present embodiment, the heat exchange portion 13a of the fuel passage 13 is in the form of a container having a relatively large capacity formed around the exhaust pipe 3. 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 this embodiment, when the light oil in the heat exchange unit 13a is heated to a high-temperature and high-pressure state, the gasified low-boiling component of the light oil is removed from the heat exchange unit 1a.
A high boiling point component that fills the upper part of 3a and does not evaporate remains in the lower part as a liquid. When the injection valve 12 is opened, light oil in the heat exchange section 13 is injected into the exhaust pipe 3, but since the injection valve 12 is connected to the upper part of the heat exchange section 13 a, the upper part is vaporized from the injection valve 12. Low boiling point component and heat exchange unit 1
Only high-boiling components vaporized by the reduced pressure in 3 are injected. Thus, the adhesion of the liquid component into the NO X absorbent 5 since only gaseous diesel fuel is injected can be more reliably prevented from the injection valve 12.

【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 shut-off valve 16 below the heat exchange section 13a is opened, and the heat exchange section 13a is opened.
The high-boiling components remaining as liquid in the recovery passage 17
And the upper shutoff valve 15 is opened simultaneously with the opening of the lower shutoff valve 16, and light oil is supplied from the fuel supply device 14 to the heat exchange unit 13 a, and The replacement of light oil is performed. The upper shut-off valve 15 closes a predetermined time after the lower shut-off valve 16 closes, during which time the heat exchange unit 13a is filled with a predetermined amount of fresh 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。
FIG. 5 shows still another embodiment of the present invention. In this embodiment, the reducing agent supply device 11 is not provided with the heat exchange unit as in the above-described embodiment, and the preheating chamber 18 in which the heat storage body 18a for vaporization is built in the exhaust passage 3 downstream of the injection valve 12 is provided. Is provided. Heat storage 18
“a” is made of a porous material such as a ceramic sintered material, and has a passage 19 in the exhaust flow direction formed therein as shown in FIG. The passage 19 is a passage 19 whose downstream end is closed.
a and the 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.

【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なってい
[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. NO During X regenerating operation of the absorber 5, the atomized gas oil injected from the injection valve 12 flows into the regenerator 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 as it is in a liquid state, but the exhaust gas flows through the wall surface 19c separating the passages 19a and 19b of the heat storage body 18a.
Because it is trapped when passing through the, and exhaust in the NO X absorbent 5 on the downstream side of the regenerator 18a, only the vaporized component of the gas oil arrives. The high-boiling components of the gas oil trapped in the regenerator 18a in order to vaporize depriving heat of vaporization from the hot regenerator 18a, the temperature of the NO X absorbent 5 is not lowered during vaporization of high boiling components. When the exhaust gas temperature is low, a part of the high boiling point component of the light oil trapped in the heat storage element 18a remains in the heat storage element 18a in a liquid state, but the load on the engine increases and the exhaust temperature increases. It flows out vaporized by the regenerator 18a when, NO X absorbent 5
Therefore, the exhaust passage of the heat storage body 18a is not blocked, and the emission of HC, CO, etc. does not deteriorate. In this embodiment, the heat insulating material 18b is provided on the outside of the preheating chamber 18 to prevent heat dissipation from the regenerator 18a, it has been to maintain a high-temperature regenerator 18a
You .

【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。
[0030] In the embodiments described above, when the exhaust temperature is relatively low is considered is a case where part of the high-boiling components of the gas oil to reach the left the NO X absorbent 5 in a liquid,
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 liquid components reaching the even vaporized rapidly, does not lead to results in decreased activity or low poisoning of the NO X absorbent 5.

【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 is reduced by using a liquid reducing agent.
OXWhen regenerating the absorbent, NO XSupply to absorbent
Means to preheat the liquid reducing agent before
NOXDue to the fact that the reducing agent reaches the absorbent in a liquid state
NOXPrevents a decrease in the activity of the absorbent 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 the 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 gas purification 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 illustrating an example of a configuration of a reducing agent supply device in FIG. 1;

【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 illustrating an example of a configuration of a reducing agent supply device in FIG. 1;

【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 illustrating an example of a configuration of a reducing agent supply device in FIG. 1;

【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 view showing a second embodiment of the exhaust gas purification apparatus of the present invention.

【図6】図5の蓄熱体の構成を示す図である。FIG. 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 / release action of the 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…ECU1 ... diesel engine 2 ... intake pipe 3 ... exhaust pipe 5 ... NO X absorbent 6 ... shutter valve 7 ... actuator 11 ... reducing agent supply device 12 ... injection valves 13 ... fuel passage 13a ... heat exchange portion 14 ... Fuel supply device 15 ... Shutoff valve 16 ... Shutoff valve 17 ... Recovery passage 18 ... Preheating chamber 18a ... Regenerator 19 ... Exhaust passage 20 ... ECU

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭62−106826(JP,A) 実開 平4−54926(JP,U) 特許2600492(JP,B2) ──────────────────────────────────────────────────続 き Continuation of front page (56) References JP-A-62-106826 (JP, A) JP-A-4-54926 (JP, U) Patent 2600492 (JP, B2)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 流入する排気ガスの空燃比がリーンであ
るときにNO X を吸収し、流入する排気ガス中の酸素濃
度を低下させると吸収したNO X を放出するNO X 吸収
剤を機関排気通路内に配置すると共に、機関運転中常時
NO X 吸収剤に排気ガスを流通させておき、NO X 吸収
剤に流入する排気ガスがリーンのときにNO X 吸収剤に
吸収されたNO X をNO X 吸収剤に流入する排気ガス中
の酸素濃度が低下せしめられたときにNO X 吸収剤から
放出するようにした内燃機関の排気浄化装置において、 前記NO X 吸収剤に液体還元剤を供給してNO X 吸収剤
に流入する排気ガス中の酸素濃度を低下せしめることに
よりNO X 吸収剤に吸収されているNO X をNO X 吸収
剤から放出させると共に、前記NO X 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設けた ことを特
徴とする内燃機関の排気浄化装置。
An air-fuel ratio of an inflowing exhaust gas is lean.
Absorbs NO X in Rutoki, concentrated oxygen in the exhaust gas flowing
NO X absorbent to release the NO X absorbed to decrease the degree
Place the engine in the engine exhaust passage, and
The NO X absorbent allowed to flow through the exhaust gas, NO X absorption
The NO X absorbent when the exhaust gas flowing into the lean to agent
In the exhaust gas that flows the absorbed NO X into the NO X absorbent
From the NO X absorbent when the oxygen concentration was allowed to decrease
In the exhaust purification system of an internal combustion engine which is adapted to emit, the NO X absorbent by supplying a liquid reducing agent to the the NO X absorbent
To reduce the oxygen concentration in the exhaust gas flowing into the
NO X absorbed NO X absorbed in the more the NO X absorbent
Together to release from the dosage, supplied to the the NO X absorbent
An exhaust gas purification device for an internal combustion engine, further comprising a reductant preheating means for preheating a liquid reductant .
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 JPH06272539A (en) 1994-09-27
JP3093905B2 true 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)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6176091B1 (en) 1998-10-01 2001-01-23 Nkk Corporation Method and apparatus for preventing snow from melting and for packing snow in artificial ski facility
US7788905B2 (en) 2003-07-01 2010-09-07 Toyota Jidosha Kabushiki Kaisha Fuel fractionation method and fuel fractionation apparatus for internal combustion engine

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4423794C1 (en) * 1994-07-01 1996-02-08 Ivoclar Ag Glass ceramic containing Zr0¶2¶, process for its production and its use
JP3398558B2 (en) * 1997-01-29 2003-04-21 日野自動車株式会社 Internal combustion engine exhaust gas purification device
JP3613676B2 (en) 2000-07-24 2005-01-26 トヨタ自動車株式会社 Exhaust gas purification device for internal combustion engine
JP4519497B2 (en) * 2004-03-29 2010-08-04 Udトラックス株式会社 Water level gauge mounting structure
WO2007037652A1 (en) * 2005-09-30 2007-04-05 Korea Institute Of Energy Research Heating device for exhaust gas in 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
WO2011000685A1 (en) * 2009-07-01 2011-01-06 Sulzer Chemtech Ag Device for cleaning exhaust gases containing nox
FI20115130A0 (en) * 2011-02-10 2011-02-10 Waertsilae Finland Oy Exhaust tanks, internal combustion engine and an SCR procedure
CN102733914B (en) * 2012-07-02 2017-08-25 中国第一汽车股份有限公司 The aftertreatment control unit of the active matter storing and supplying ammonia of 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
FR3027056B1 (en) * 2014-10-10 2018-03-02 Psa Automobiles Sa. SELECTIVE CATALYTIC REDUCTION DEVICE
DE102016100284A1 (en) 2016-01-11 2017-07-13 Eberspächer Exhaust Technology GmbH & Co. KG Exhaust system for an internal combustion engine and method for operating an exhaust system
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

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6176091B1 (en) 1998-10-01 2001-01-23 Nkk Corporation Method and apparatus for preventing snow from melting and for packing snow in artificial ski facility
US7788905B2 (en) 2003-07-01 2010-09-07 Toyota Jidosha Kabushiki Kaisha Fuel fractionation method and fuel fractionation apparatus for internal combustion engine

Also Published As

Publication number Publication date
JPH06272539A (en) 1994-09-27

Similar Documents

Publication Publication Date Title
JP3093905B2 (en) Exhaust gas purification device for internal combustion engine
US5406790A (en) Exhaust gas purification device for an engine
JP2586738B2 (en) Exhaust gas purification device for internal combustion engine
JP2727906B2 (en) Exhaust gas purification device for internal combustion engine
JP2722987B2 (en) Exhaust gas purification device for internal combustion engine
JPH06336914A (en) Exhaust emission control device of internal combustion engine
JP2845080B2 (en) Exhaust gas purification device for internal combustion engine
JP3580180B2 (en) Exhaust gas purification device for internal combustion engine
JP2722988B2 (en) Exhaust gas purification device for internal combustion engine
JP3353650B2 (en) Catalyst poisoning regeneration equipment for internal combustion engines
JP3632274B2 (en) Exhaust gas purification device for internal combustion engine
JP2842135B2 (en) Exhaust gas purification device for internal combustion engine
JP2830669B2 (en) Exhaust gas purification device for internal combustion engine
JP2746029B2 (en) Exhaust gas purification device for internal combustion engine
JP2722985B2 (en) Exhaust gas purification device for internal combustion engine
JP2845071B2 (en) Exhaust gas purification device for internal combustion engine
JP2845068B2 (en) Exhaust gas purification device for internal combustion engine
JP3374780B2 (en) Exhaust gas purification device for internal combustion engine
JP3397175B2 (en) Exhaust gas purification device for internal combustion engine
JP3324475B2 (en) Exhaust gas purification device for internal combustion engine
JP2845052B2 (en) Exhaust gas purification device for internal combustion engine
JP3496557B2 (en) Exhaust gas purification device for internal combustion engine
JP2830655B2 (en) Exhaust gas purification device for internal combustion engine
JP2663807B2 (en) Exhaust gas purification device for internal combustion engine
JP2888111B2 (en) Exhaust gas purification device for internal combustion engine

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080728

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080728

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090728

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090728

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100728

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110728

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110728

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120728

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130728

Year of fee payment: 13