JP3443223B2 - Diesel engine exhaust purification system - Google Patents

Diesel engine exhaust purification system

Info

Publication number
JP3443223B2
JP3443223B2 JP32719595A JP32719595A JP3443223B2 JP 3443223 B2 JP3443223 B2 JP 3443223B2 JP 32719595 A JP32719595 A JP 32719595A JP 32719595 A JP32719595 A JP 32719595A JP 3443223 B2 JP3443223 B2 JP 3443223B2
Authority
JP
Japan
Prior art keywords
catalyst
reforming catalyst
hydrocarbon
reforming
exhaust gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP32719595A
Other languages
Japanese (ja)
Other versions
JPH09166014A (en
Inventor
信也 広田
雄二 榊原
保夫 高田
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
Toyota Central R&D Labs Inc
Original Assignee
Toyota Motor Corp
Toyota Central R&D Labs Inc
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, Toyota Central R&D Labs Inc filed Critical Toyota Motor Corp
Priority to JP32719595A priority Critical patent/JP3443223B2/en
Publication of JPH09166014A publication Critical patent/JPH09166014A/en
Application granted granted Critical
Publication of JP3443223B2 publication Critical patent/JP3443223B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • 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
    • F01N2240/00Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/30Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a fuel reformer
    • 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
    • F01N2610/08Adding substances to exhaust gases with prior mixing of the substances with a gas, e.g. air
    • 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
    • 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]

【発明の属する技術分野】本発明は、ディーゼルエンジ
ンの排気浄化装置に関する。
TECHNICAL FIELD The present invention relates to an exhaust emission control device for a diesel engine.

【0002】[0002]

【従来の技術】ディーゼルエンジンは、通常、燃料を空
気過剰状態で燃焼させるために、その排気ガス中には比
較的多くの窒素酸化物(以下、NOxと称する)が含ま
れている。有害なNOxを浄化するための装置として、
排気系に配置されたNOx触媒と、このNOx触媒の排
気上流側へアンモニア等の還元剤を供給する手段とを有
するものが公知である。
2. Description of the Related Art A diesel engine usually contains a relatively large amount of nitrogen oxides (hereinafter referred to as NOx) in its exhaust gas in order to burn fuel in an excess air state. As a device for purifying harmful NOx,
It is known to have a NOx catalyst arranged in the exhaust system and a means for supplying a reducing agent such as ammonia to the exhaust upstream side of the NOx catalyst.

【0003】特開平5−222923号公報に開示され
ているNOx浄化装置は、還元剤の車両搭載性を考慮し
て、ディーゼルエンジンの燃料と同様な軽油を還元剤と
して使用することが提案されている。軽油は、炭素数の
多い炭化水素を主成分とし沸点が高いものであるため
に、直接的にNOx触媒へ供給しても良好に気化せず、
十分にNOxを還元することができない。それにより、
この浄化装置では、軽油をNOx触媒へ供給する以前
に、ヒータにより加熱された改質触媒へ供給し、炭素数
の少ない炭化水素に改質されたものだけをNOx触媒の
排気上流側へ供給するようになっている。
In the NOx purifying device disclosed in Japanese Patent Laid-Open No. 5-222923, it has been proposed to use a light oil similar to a diesel engine fuel as a reducing agent in consideration of the vehicle mountability of the reducing agent. There is. Light oil does not vaporize well even if it is directly supplied to the NOx catalyst, because light oil has a high boiling point and contains hydrocarbons with a large number of carbon atoms.
It cannot sufficiently reduce NOx. Thereby,
In this purification device, light oil is supplied to the reforming catalyst heated by the heater before it is supplied to the NOx catalyst, and only the reformed hydrocarbon having a small carbon number is supplied to the exhaust gas upstream side of the NOx catalyst. It is like this.

【0004】[0004]

【発明が解決しようとする課題】前述の従来技術によっ
て、軽油を還元剤として使用することが可能となるが、
改質触媒を加熱するために、ヒータへ常時電力を供給す
る必要があり、このような新たな多大なエネルギが消費
される。
The above-mentioned prior art makes it possible to use light oil as a reducing agent.
In order to heat the reforming catalyst, it is necessary to constantly supply electric power to the heater, and such a large amount of new energy is consumed.

【0005】従って、本発明の目的は、新たな多大なエ
ネルギを消費することなく、軽油等の炭化水素系燃料を
炭化水素系還元剤に改質して、窒素酸化物を浄化するN
Ox触媒によって排気ガス中のNOxを良好に還元する
ことができるディーゼルエンジンの排気浄化装置を提供
することである。
Therefore, an object of the present invention is to purify nitrogen oxides by reforming a hydrocarbon fuel such as light oil into a hydrocarbon reducing agent without consuming a large amount of new energy.
An object of the present invention is to provide an exhaust emission control device for a diesel engine, which can favorably reduce NOx in exhaust gas with an Ox catalyst.

【0006】[0006]

【課題を解決するための手段】請求項1に記載の本発明
によるディーゼルエンジンの排気浄化装置は、機関排気
系に配置された窒素酸化物を浄化するためのNO触媒
と、排気ガスの熱により加熱され、炭化水素系燃料を炭
化水素系還元剤に改質するための改質触媒と、炭化水素
系燃料を前記改質触媒を介して前記NO触媒へ供給す
る炭化水素系燃料供給手段と、前記炭化水素系燃料供給
手段によって前記改質触媒へ供給された前記炭化水素系
燃料の一部を前記改質触媒で燃焼させるだけの空気を前
記改質触媒へ供給する空気供給手段、とを具備し、前記
改質触媒は大きな熱容量を有する前記NO 触媒により
取り囲まれ、前記改質触媒と排気ガスとの熱交換は前記
NO 触媒を介して行われることを特徴とする。
According to a first aspect of the present invention, there is provided an exhaust emission control device for a diesel engine, wherein an NO x catalyst for purifying nitrogen oxides arranged in an engine exhaust system and heat of exhaust gas. And a reforming catalyst for reforming the hydrocarbon-based fuel into a hydrocarbon-based reducing agent, and a hydrocarbon-based fuel supply means for supplying the hydrocarbon-based fuel to the NO X catalyst via the reforming catalyst. And an air supply means for supplying to the reforming catalyst air sufficient to burn a part of the hydrocarbon fuel supplied to the reforming catalyst by the hydrocarbon fuel supplying means to the reforming catalyst, And the above
The reforming catalyst uses the NO x catalyst having a large heat capacity.
The heat exchange between the reforming catalyst and the exhaust gas is surrounded by
It is characterized in that it is carried out via a NO X catalyst .

【0007】このディーゼルエンジンの排気浄化装置に
おいては、改質触媒が排気ガスの熱によって加熱され、
空気供給手段が改質触媒へ供給された炭化水素系燃料の
一部を改質触媒で燃焼させるだけの空気を改質触媒へ供
給するために、排気ガス温度が低くて改質触媒が炭化水
素系燃料を炭化水素系還元剤に改質可能な温度とならな
くても、改質触媒において炭化水素系燃料の一部が燃焼
し、この燃焼熱によって改質触媒が炭化水素系燃料を改
質可能な温度に維持される。また、改質触媒は大きな熱
容量を有するNO 触媒により取り囲まれており、改質
触媒と排気ガスとの熱交換はNO 触媒を介して行われ
るために、排気ガスの温度変化に対して改質触媒の温度
変化は小さく維持される。
In this exhaust emission control system for a diesel engine, the reforming catalyst is heated by the heat of the exhaust gas,
The exhaust gas temperature is low and the reforming catalyst is a hydrocarbon because the air supply unit supplies air to the reforming catalyst to burn only a portion of the hydrocarbon-based fuel supplied to the reforming catalyst to the reforming catalyst. Even if the temperature of the system fuel does not reach the level at which it can be reformed to the hydrocarbon reducing agent, a part of the hydrocarbon fuel burns in the reforming catalyst, and the heat of combustion causes the reforming catalyst to reform the hydrocarbon fuel. Maintained at possible temperature. Also, the reforming catalyst has a large heat
Surrounded by a NO x catalyst with capacity , reforming
The heat exchange between the catalyst and the exhaust gas is performed via the NO X catalyst.
In order to change the temperature of the exhaust gas, the temperature of the reforming catalyst
The changes are kept small.

【0008】また、請求項2に記載の本発明によるディ
ーゼルエンジンの排気浄化装置は、機関排気系に配置さ
れた窒素酸化物を浄化するためのNO触媒と、排気ガ
スの熱により加熱され、炭化水素系燃料を炭化水素系還
元剤に改質するための改質触媒と、炭化水素系燃料を前
記改質触媒を介して前記NO触媒へ供給する炭化水素
系燃料供給手段と、前記炭化水素系燃料供給手段によっ
て前記改質触媒へ供給された前記炭化水素系燃料の一部
を前記改質触媒で燃焼させるだけの空気を前記改質触媒
へ供給する空気供給手段、とを具備し、前記改質触媒は
大きな熱容量を有するカバーにより取り囲まれ、前記改
質触媒と排気ガスとの熱交換は前記カバーを介して行わ
れることを特徴とする。
According to a second aspect of the present invention, there is provided an exhaust emission control device for a diesel engine, wherein an NO x catalyst for purifying nitrogen oxides arranged in an engine exhaust system and an exhaust gas.
Reforming catalyst for reforming a hydrocarbon-based fuel into a hydrocarbon-based reducing agent, which is heated by the heat of fuel, and a hydrocarbon-based fuel for supplying the hydrocarbon-based fuel to the NO x catalyst via the reforming catalyst. Fuel supply means and air supply for supplying to the reforming catalyst air sufficient to burn a part of the hydrocarbon fuel supplied to the reforming catalyst by the hydrocarbon fuel supplying means with the reforming catalyst. Means, and the reforming catalyst comprises
It is surrounded by a cover with a large heat capacity,
Heat exchange between the high quality catalyst and the exhaust gas is performed through the cover.
Characterized in that it is.

【0009】このディーゼルエンジンの排気浄化装置に
おいては、改質触媒が排気ガスの熱によって加熱され、
空気供給手段が改質触媒へ供給された炭化水素系燃料の
一部を改質触媒で燃焼させるだけの空気を改質触媒へ供
するために、排気ガス温度が低くて改質触媒が炭化水
素系燃料を炭化水素系還元剤に改質可能な温度とならな
くても、改質触媒において炭化水素系燃料の一部が燃焼
し、この燃焼熱によって改質触媒が炭化水素系燃料を改
質可能な温度に維持される。また、改質触媒は大きな熱
容量を有するカバーにより取り囲まれており、改質触媒
と排気ガスとの熱交換はカバーを介して行われるため
に、排気ガスの温度変化に対して改質触媒の温度変化は
小さく維持される。
In this exhaust emission control system for a diesel engine, the reforming catalyst is heated by the heat of the exhaust gas,
Since the air supply means supplies the reforming catalyst with the air that burns part of the hydrocarbon fuel supplied to the reforming catalyst with the reforming catalyst, the temperature of the exhaust gas is low and the reforming catalyst is
The temperature must be high enough to reform the elementary fuel into a hydrocarbon-based reducing agent.
At least some of the hydrocarbon fuel burns in the reforming catalyst
The combustion heat causes the reforming catalyst to modify the hydrocarbon fuel.
Maintained at a temperature that allows quality. Also, the reforming catalyst has a large heat
Surrounded by a cover with capacity, reforming catalyst
And the heat exchange with the exhaust gas is done through the cover
In addition, the temperature change of the reforming catalyst with respect to the temperature change of the exhaust gas
Maintained small.

【0010】[0010]

【発明の実施の形態】図1は、本発明によるディーゼル
エンジンの排気浄化装置の第1実施形態を示す概略断面
図である。同図において、1はディーゼルエンジンの排
気通路である。排気通路1の拡管部1aには、排気ガス
中のNOxを浄化するためのNOx触媒2が配置されて
いる。このNOx触媒2は、熱容量の大きなコージェラ
イト又は炭化ケイ素(SiC)等のセラミックを基材と
して銅イオン交換ゼオライト(Cu−ZSM−5)等を
担持したものであり、炭化水素を還元剤として良好にN
Oxを還元するものである。このNOx触媒2は、その
中心に貫通穴2aを有している。
1 is a schematic sectional view showing a first embodiment of an exhaust emission control device for a diesel engine according to the present invention. In the figure, 1 is an exhaust passage of a diesel engine. A NOx catalyst 2 for purifying NOx in the exhaust gas is arranged in the expanded portion 1a of the exhaust passage 1. The NOx catalyst 2 has a large heat capacity such as cordierite or a ceramic such as silicon carbide (SiC) as a base material and supports copper ion-exchanged zeolite (Cu-ZSM-5) and the like, and is excellent in reducing hydrocarbon as a reducing agent. To N
It reduces Ox. The NOx catalyst 2 has a through hole 2a at its center.

【0011】本実施形態の排気浄化装置は、還元剤とし
ての炭化水素として、ディーゼルエンジンの燃料である
軽油を使用する。軽油の主成分は炭素数の多い炭化水素
であるために、その沸点が高く、そのままNOx触媒2
へ供給しても気化し難く、還元剤として良好に機能しな
い。従って、NOx触媒2へ供給する以前に、炭素数を
少なく改質する必要があり、そのための改質触媒3が、
NOx触媒2の貫通穴2aの排気下流側に配置されてい
る。
The exhaust emission control system of this embodiment uses light oil, which is a fuel for a diesel engine, as a hydrocarbon as a reducing agent. Since the main component of light oil is a hydrocarbon with a large number of carbon atoms, its boiling point is high and the NOx catalyst 2
It is difficult to vaporize even when supplied to and does not function well as a reducing agent. Therefore, before supplying to the NOx catalyst 2, it is necessary to reform with a small number of carbon atoms, and the reforming catalyst 3 for that needs to be reformed.
The NOx catalyst 2 is arranged on the exhaust downstream side of the through hole 2a.

【0012】改質触媒3は、NOx触媒2と同様な基材
に貴金属が担持された酸化触媒であり、所定温度以上で
活性化して軽油を改質するものである。改質触媒3の排
気下流側端面には、板部材4が配置されている。それに
より、NOx触媒2の貫通穴2aは閉鎖され、排気ガス
が貫通穴2aを通過しないようになっており、従って、
改質触媒3へは排気ガスが流入しない。改質触媒3とN
Ox触媒2とが接触している部分において、改質触媒3
からNOx触媒2へ還元剤が通過しないように遮蔽され
ている。又は、この部分には、改質触媒3からNOx触
媒2へ還元剤が通過し難くなるような構造が設けられて
いる。
The reforming catalyst 3 is an oxidation catalyst in which a noble metal is supported on the same base material as the NOx catalyst 2, and is activated at a temperature equal to or higher than a predetermined temperature to reform light oil. The plate member 4 is disposed on the exhaust downstream side end surface of the reforming catalyst 3. As a result, the through hole 2a of the NOx catalyst 2 is closed and the exhaust gas is prevented from passing through the through hole 2a.
Exhaust gas does not flow into the reforming catalyst 3. Reforming catalyst 3 and N
The reforming catalyst 3 is provided in a portion in contact with the Ox catalyst 2.
Is shielded from the NOx catalyst 2 so that the reducing agent does not pass therethrough. Alternatively, this portion is provided with a structure that makes it difficult for the reducing agent to pass from the reforming catalyst 3 to the NOx catalyst 2.

【0013】板部材4には、改質触媒3へ軽油及び空気
を供給するための供給管5が接続されている。供給管5
は、排気通路1の外部へ延在して二股に分岐し、その一
方が軽油供給量を制御するための第1制御弁5aを介し
て燃料ポンプ(図示せず)へ接続され、他方が空気供給
量を制御するための第2制御弁5bを介して空気ポンプ
(図示せず)へ接続されている。
A supply pipe 5 for supplying light oil and air to the reforming catalyst 3 is connected to the plate member 4. Supply pipe 5
Are branched into two branches extending to the outside of the exhaust passage 1, one of which is connected to a fuel pump (not shown) through a first control valve 5a for controlling the amount of light oil supply, and the other is air. It is connected to an air pump (not shown) via a second control valve 5b for controlling the supply amount.

【0014】20は、第1及び第2制御弁5a,5bを
制御するための制御装置であり、機関回転を検出するた
めの回転センサ21と、吸入空気量を検出するためのエ
アフローメータ22、及び排気通路1のNOx触媒2の
下流側に位置して排気ガスの温度を検出するための温度
センサ23等が接続されている。
Reference numeral 20 denotes a control device for controlling the first and second control valves 5a and 5b, which includes a rotation sensor 21 for detecting engine rotation, an air flow meter 22 for detecting intake air amount, A temperature sensor 23 for detecting the temperature of the exhaust gas is connected to the exhaust passage 1 on the downstream side of the NOx catalyst 2.

【0015】本実施形態において、改質触媒3は、NO
x触媒2によって取り囲まれ、板部材4によって排気ガ
スの流入が防止されている。従って、改質触媒3と排気
ガスとの間の熱交換は、大きな熱容量を有するNOx触
媒2を介して行われ、機関運転状態に応じて大きく変化
する排気ガス温度に対して、改質触媒の温度変化は小さ
く維持される。改質触媒3は、特に、NOx触媒2の各
部分のうちで、排気ガスの温度変化に対して最も影響さ
れ難い排気下流部分によって取り囲まれているために、
さらに温度変化は小さく維持される。
In the present embodiment, the reforming catalyst 3 is NO
It is surrounded by the x catalyst 2 and the inflow of exhaust gas is prevented by the plate member 4. Therefore, the heat exchange between the reforming catalyst 3 and the exhaust gas is performed via the NOx catalyst 2 having a large heat capacity, and the exhaust gas temperature of the reforming catalyst changes greatly with respect to the exhaust gas temperature that greatly changes according to the engine operating state. Temperature changes are kept small. Since the reforming catalyst 3 is surrounded by the exhaust downstream portion, which is the least affected by the temperature change of the exhaust gas, among the respective portions of the NOx catalyst 2,
Furthermore, the temperature change is kept small.

【0016】従って、改質触媒3の温度は、常に、ある
程度の温度以上となっている。それにより、供給管5か
ら改質触媒3へ軽油及び空気が供給されると、軽油の一
部が良好に燃焼を開始する。それにより、この燃焼熱に
よってさらに改質触媒3の温度が上昇し、改質触媒3が
残りの軽油を改質させるのに適した温度となり、残りの
軽油を確実に改質して気化させることが可能となる。こ
のように改質及び気化された軽油は、空気流によってN
Ox触媒2の排気上流側に移動して排気ガスと十分に混
合し、還元剤として、NOx触媒2において排気ガス中
のNOxを良好に還元させることが可能となる。
Therefore, the temperature of the reforming catalyst 3 is always above a certain temperature. As a result, when the light oil and the air are supplied from the supply pipe 5 to the reforming catalyst 3, a part of the light oil starts to burn well. As a result, the temperature of the reforming catalyst 3 further rises due to this combustion heat, and the reforming catalyst 3 reaches a temperature suitable for reforming the remaining light oil, and surely reforms and vaporizes the remaining light oil. Is possible. The light oil thus reformed and vaporized is N
It is possible to move to the upstream side of the exhaust gas of the Ox catalyst 2 and sufficiently mix with the exhaust gas, and as a reducing agent, the NOx in the exhaust gas can be favorably reduced in the NOx catalyst 2.

【0017】このように、改質触媒3を介してNOx触
媒2へ供給される軽油量は、排気ガス中に含まれるNO
xの量に対応させることが望ましい。図2は、機関回転
数N及び機関負荷としての単位回転数当たりの吸入空気
量Q/Nに対するNOxの発生量を示すマップである。
このように、機関運転状態に応じてNOx発生量が変化
するために、制御装置20は、回転センサ21及びエア
フローメータ22により検出される現在の機関回転数N
及び吸入空気量Qに基づき、現在のNOx発生量を把握
して、これに対応させた軽油量がNOx触媒2へ供給さ
れるように、また、改質触媒3で燃焼する軽油量も考慮
し、第1制御弁5aの開度を制御するようになってい
る。
As described above, the amount of light oil supplied to the NOx catalyst 2 through the reforming catalyst 3 depends on the NO contained in the exhaust gas.
It is desirable to correspond to the amount of x. FIG. 2 is a map showing the engine speed N and the generated amount of NOx with respect to the intake air amount Q / N per unit speed as the engine load.
As described above, since the NOx generation amount changes according to the engine operating state, the control device 20 controls the current engine speed N detected by the rotation sensor 21 and the air flow meter 22.
Also, based on the intake air amount Q, the present NOx generation amount is grasped so that the corresponding light oil amount is supplied to the NOx catalyst 2, and the light oil amount burned in the reforming catalyst 3 is also taken into consideration. The opening degree of the first control valve 5a is controlled.

【0018】また、改質触媒3へ供給される空気量は、
一部の軽油が改質触媒3で燃焼して改質触媒3の温度を
残りの軽油が改質触媒3で確実に改質及び気化されるよ
うに決定され、制御装置20は、この空気量が実現され
るように第2制御弁5bの開度を制御するようになって
いる。例えば、改質触媒に供給される軽油は、2000
ccのエンジンで通常走行においては約1cc/分であ
り、そのうちの約10%、すなわち0.1cc/分を改
質触媒で燃焼させるようになっている。この燃焼に必要
な空気は約1リットル/分であり、この量の空気が改質
触媒へ供給されるようになっている。
The amount of air supplied to the reforming catalyst 3 is
A part of the light oil is burned in the reforming catalyst 3 and the temperature of the reforming catalyst 3 is determined so that the remaining light oil is surely reformed and vaporized in the reforming catalyst 3, and the control device 20 controls the air amount. The opening degree of the second control valve 5b is controlled so that For example, the light oil supplied to the reforming catalyst is 2000
It is about 1 cc / min in normal running with a cc engine, and about 10% of that, that is, 0.1 cc / min, is burned by the reforming catalyst. The air required for this combustion is about 1 liter / minute, and this amount of air is supplied to the reforming catalyst.

【0019】NOx触媒2は、所定温度範囲を外れる
と、NOxを十分に還元することができない。従って、
制御装置20は、温度センサ23により検出されるNO
x触媒2下流側の排気ガス温度からNOx触媒2の温度
を推定し、これが所定範囲内にある時にだけ前述したよ
うに軽油及び空気を改質触媒3へ供給するようになって
いる。
The NOx catalyst 2 cannot sufficiently reduce NOx outside the predetermined temperature range. Therefore,
The control device 20 detects NO detected by the temperature sensor 23.
The temperature of the NOx catalyst 2 is estimated from the exhaust gas temperature on the downstream side of the x catalyst 2, and the light oil and air are supplied to the reforming catalyst 3 as described above only when the temperature is within a predetermined range.

【0020】図3は、本発明によるディーゼルエンジン
の排気浄化装置の第2実施形態を示す概略断面図であ
る。第1実施形態との違いについてのみ以下に説明す
る。本実施形態では、NOx触媒2’には貫通穴は設け
られていない。改質触媒3’は、拡管部1a’のNOx
触媒2’の排気上流側に配置されている。
FIG. 3 is a schematic sectional view showing a second embodiment of the exhaust emission control system for a diesel engine according to the present invention. Only the differences from the first embodiment will be described below. In this embodiment, the NOx catalyst 2'is not provided with a through hole. The reforming catalyst 3'is the NOx of the tube expansion portion 1a '.
It is arranged on the exhaust upstream side of the catalyst 2 '.

【0021】この改質触媒3’は球形状を有し、それに
軽油及び空気を供給するための供給管5’によって拡管
部1a’のほぼ中心に支持されている。また、改質触媒
3’の排気上流側半分を被うセラミック製のカバー6が
設けられている。このカバー6は、非常に大きな熱容量
を有している。
The reforming catalyst 3'has a spherical shape and is supported by a supply pipe 5'for supplying light oil and air to the reforming catalyst 3'at substantially the center of the pipe expanding portion 1a '. A ceramic cover 6 is provided to cover the exhaust upstream half of the reforming catalyst 3 '. This cover 6 has a very large heat capacity.

【0022】本実施形態において、改質触媒3’は、熱
容量の大きなカバー6によって取り囲まれ、また、この
カバー6によって排気ガスの流入が防止されている。従
って、第1実施形態と同様に、改質触媒3’と排気ガス
との間の熱交換は、大きな熱容量を有するカバー6を介
して行われ、機関運転状態に応じて大きく変化する排気
ガス温度に対して、改質触媒3’の温度変化は小さく維
持される。それにより、第1実施形態と同様に軽油及び
空気を改質触媒3’へ供給することによって、軽油は良
好に改質及び気化され、空気流及び排気ガス流によって
排気下流側に位置するNOx触媒2’へ供給される。
In the present embodiment, the reforming catalyst 3'is surrounded by a cover 6 having a large heat capacity, and the cover 6 prevents the inflow of exhaust gas. Therefore, as in the first embodiment, heat exchange between the reforming catalyst 3 ′ and the exhaust gas is performed via the cover 6 having a large heat capacity, and the exhaust gas temperature that greatly changes according to the engine operating state. On the other hand, the temperature change of the reforming catalyst 3'is kept small. As a result, by supplying light oil and air to the reforming catalyst 3'as in the first embodiment, the light oil is satisfactorily reformed and vaporized, and the NOx catalyst located on the exhaust downstream side by the air flow and the exhaust gas flow. 2'is supplied.

【0023】前述した二つの実施形態は、排気ガスの熱
によって改質触媒を軽油燃焼可能な温度にするものであ
る。軽油の一部を確実に燃焼させるために、改質触媒の
温度があまり低下しないように、改質触媒は熱容量の大
きな部材により取り囲まれるようになっている。しか
し、これは、本発明を限定するものではなく、例えば、
単に改質触媒を排気通路内に配置しても、又は、排気通
路外で隣接配置しても、排気ガス温度がかなり低くなる
特定機関運転状態を除き、改質触媒は排気ガスの熱によ
って軽油燃焼可能な温度となり、軽油の一部を燃焼させ
ることで、この燃焼熱により改質触媒の温度を軽油を良
好に改質させる温度に上昇させることができ、この燃焼
を繰り返すことによって改質触媒においてこの温度が維
持される。また、炭化水素系還元剤として軽油より沸点
の低い灯油等を使用すれば、改質触媒の温度がさらに低
くても空気供給により燃焼させることができる。
In the above-mentioned two embodiments, the reforming catalyst is brought to a temperature at which the light oil can be burned by the heat of the exhaust gas. In order to reliably burn a part of the light oil, the reforming catalyst is surrounded by a member having a large heat capacity so that the temperature of the reforming catalyst does not drop so much. However, this is not a limitation of the invention, for example:
Even if the reforming catalyst is simply placed inside the exhaust passage or adjacent to the outside of the exhaust passage, the reforming catalyst is light oil due to the heat of the exhaust gas except in the specific engine operating state where the exhaust gas temperature becomes considerably low. When the temperature reaches a temperature at which combustion is possible and a portion of the light oil is burned, the temperature of the reforming catalyst can be raised by this heat of combustion to a temperature at which the light oil can be well reformed. By repeating this combustion, the reforming catalyst This temperature is maintained at. If kerosene or the like having a lower boiling point than light oil is used as the hydrocarbon-based reducing agent, it can be burned by supplying air even if the temperature of the reforming catalyst is lower.

【0024】図4は、本発明によるディーゼルエンジン
の排気浄化装置の第3実施形態を示す概略断面図であ
る。第2実施形態との違いについてのみ以下に説明す
る。本実施形態では、改質触媒3”は、ケース7内に収
納されて排気通路1”の外部に配置されている。
FIG. 4 is a schematic sectional view showing a third embodiment of the exhaust purification system for a diesel engine according to the present invention. Only the differences from the second embodiment will be described below. In the present embodiment, the reforming catalyst 3 ″ is housed in the case 7 and arranged outside the exhaust passage 1 ″.

【0025】ケース7の一端部は、前述同様な供給管
5”が接続されている。ケース7の他端部に接続された
接続管7aは、吸気通路の拡管部1a”におけるNOx
触媒2”の排気上流側に延在している。ケース7の回り
には、電気ヒータ8が配置されている。
A supply pipe 5 "similar to that described above is connected to one end of the case 7. The connection pipe 7a connected to the other end of the case 7 is NOx in the expanded pipe portion 1a" of the intake passage.
It extends to the exhaust gas upstream side of the catalyst 2 ″. An electric heater 8 is arranged around the case 7.

【0026】制御装置20”は、前述同様、第1及び第
2制御弁5a”,5b”の開度制御を実施すると共に、
電気ヒータ8への通電を制御する。この制御は、機関始
動と同時に通電を開始して、改質触媒3”を軽油燃焼可
能な温度にした後は、通電を中止するようになってい
る。改質触媒3”が、一度、軽油燃焼可能な温度となる
と、それ以後は、前述同様、軽油の一部が燃焼して改質
触媒3”の温度を上昇させ、軽油を良好に改質可能な温
度とし、これが繰り返され、改質触媒3”がこの温度に
維持される。それにより、改質された軽油が、接続管7
aを介してNOx触媒2”へ供給されるようになってい
る。
The controller 20 "controls the opening of the first and second control valves 5a" and 5b "as described above, and
The energization of the electric heater 8 is controlled. In this control, the energization is started at the same time as the engine is started, and the energization is stopped after the reforming catalyst 3 ″ is brought to a temperature at which the light oil can be burned. When the combustible temperature is reached, as described above, a part of the light oil is burned to raise the temperature of the reforming catalyst 3 ″ to a temperature at which the light oil can be satisfactorily reformed, and this is repeated for reforming. The catalyst 3 "is maintained at this temperature. As a result, the modified light oil is connected to the connecting pipe 7
It is adapted to be supplied to the NOx catalyst 2 ″ via a.

【0027】前述した全ての実施形態において、改質触
媒において燃料を燃焼させるとカーボン等が生成され
て、改質触媒に目詰まりを発生させることがある。これ
を防止するために、定期的に供給管から空気のみを供給
することにより、このカーボンを燃焼させることができ
る。
In all the above-described embodiments, when the fuel is burned in the reforming catalyst, carbon or the like is generated, which may cause clogging of the reforming catalyst. In order to prevent this, it is possible to burn this carbon by periodically supplying only air from the supply pipe.

【0028】[0028]

【発明の効果】このように、請求項1に記載の本発明に
よるディーゼルエンジンの排気浄化装置によれば、改質
触媒が排気ガスの熱によって加熱され、空気供給手段が
改質触媒へ供給された炭化水素系燃料の一部を改質触媒
で燃焼させるだけの空気を改質触媒へ供給するために、
排気ガス温度が低くて改質触媒が炭化水素系燃料を炭化
水素系還元剤に改質可能な温度とならなくても、改質触
媒において炭化水素系燃料の一部が燃焼し、この燃焼熱
によって改質触媒を炭化水素系燃料を改質可能な温度に
維持することができる。また、改質触媒は大きな熱容量
を有するNO 触媒により取り囲まれており、改質触媒
と排気ガスとの熱交換はNO 触媒を介して行われるた
めに、排気ガスの温度変化に対して改質触媒の温度変化
は小さく維持されて、改質触媒の温度は常にある程度の
温度以上となっており、改質触媒において常に炭化水素
系燃料の一部を燃焼可能である。それにより、供給手段
が、この改質触媒を介して炭化水素系燃料をNO触媒
装置へ供給することにより、新たな多大なエネルギを消
費することなく、排気ガスの熱を利用して改質された炭
化水素系還元剤をNO触媒へ供給することができ、N
触媒における良好なNOの還元が実現される。
As described above, according to the exhaust gas purification apparatus for a diesel engine of the present invention as set forth in claim 1, the reforming catalyst is heated by the heat of the exhaust gas, and the air supply means is supplied to the reforming catalyst. In order to supply the reforming catalyst with air sufficient to burn a part of the hydrocarbon-based fuel with the reforming catalyst,
Even if the temperature of the exhaust gas is low and the reforming catalyst does not reach a temperature at which the hydrocarbon-based fuel can be reformed into the hydrocarbon-based reducing agent, part of the hydrocarbon-based fuel burns in the reforming catalyst, and the combustion heat Thus, the reforming catalyst can be maintained at a temperature at which the hydrocarbon fuel can be reformed. Also, the reforming catalyst has a large heat capacity.
And a reforming catalyst surrounded by a NO x catalyst having
The heat exchange between the exhaust gas and the exhaust gas is performed via the NO X catalyst.
Change the temperature of the reforming catalyst against the temperature change of the exhaust gas.
Is kept small and the temperature of the reforming catalyst is
The temperature is above the temperature, and hydrocarbons are always present in the reforming catalyst.
It is possible to burn part of the system fuel. As a result, the supply means supplies the hydrocarbon-based fuel to the NO X catalyst device via the reforming catalyst, and the heat of the exhaust gas is used for reforming without consuming a large amount of new energy. The hydrocarbon-based reducing agent thus generated can be supplied to the NO X catalyst,
A good NO X reduction on the O X catalyst is achieved.

【0029】また、請求項2に記載の本発明によるディ
ーゼルエンジンの排気浄化装置によれば、改質触媒が排
気ガスの熱によって加熱され、空気供給手段が改質触媒
へ供給された炭化水素系燃料の一部を改質触媒で燃焼さ
せるだけの空気を改質触媒へ供給するために、排気ガス
温度が低くて改質触媒が炭化水素系燃料を炭化水素系還
元剤に改質可能な温度とならなくても、改質触媒におい
て炭化水素系燃料の一部が燃焼し、この燃焼熱によって
改質触媒を炭化水素系燃料を改質可能な温度に維持する
ことができる。また、改質触媒は大きな熱容量を有する
カバーにより取り囲まれており、改質触媒と排気ガスと
の熱交換はカバーを介して行われるために、排気ガスの
温度変化に対して改質触媒の温度変化は小さく維持され
て、改質触媒の温度は常にある程度の温度以上となって
おり、改質触媒において常に炭化水素系燃料の一部を燃
焼可能である。それにより、供給手段が、この改質触媒
を介して炭化水素系燃料をNO触媒装置へ供給するこ
とにより、新たな多大なエネルギを消費することなく、
排気ガスの熱を利用して改質された炭化水素系還元剤を
NO触媒へ供給することができ、NO触媒における
良好なNOの還元が実現される。
Further, according to the exhaust gas purifying apparatus for a diesel engine of the present invention as defined in claim 2, the reforming catalyst is exhausted.
Exhaust gas is supplied to the reforming catalyst in order to supply the reforming catalyst with air which is heated by the heat of the gas and is burned by the reforming catalyst to a part of the hydrocarbon fuel supplied to the reforming catalyst by the air supply means.
At low temperature, the reforming catalyst returns hydrocarbon fuel to hydrocarbon fuel.
Even if it does not reach the temperature at which it can be reformed into the base material,
Part of the hydrocarbon fuel burns, and this combustion heat
Maintaining the reforming catalyst at a temperature at which hydrocarbon fuels can be reformed
be able to. Also, the reforming catalyst has a large heat capacity.
It is surrounded by a cover, and the reforming catalyst and exhaust gas
The heat exchange of the exhaust gas is carried out through the cover.
The temperature change of the reforming catalyst is kept small with respect to the temperature change.
Therefore, the temperature of the reforming catalyst is always above a certain level.
The reforming catalyst always burns part of the hydrocarbon fuel.
It can be baked. As a result, the supply means supplies the hydrocarbon-based fuel to the NO X catalyst device via the reforming catalyst, without consuming a large amount of new energy,
The using heat of exhaust gas reformed hydrocarbon reductant can be supplied to the NO X catalyst, reduction of good NO X in the NO X catalyst is achieved.

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

【図1】本発明によるディーゼルエンジンの排気浄化装
置の第1実施形態を示す概略断面図である。
FIG. 1 is a schematic sectional view showing a first embodiment of an exhaust emission control device for a diesel engine according to the present invention.

【図2】機関回転数及び機関負荷に対するNOx発生量
を示すマップである。
FIG. 2 is a map showing NOx generation amount with respect to engine speed and engine load.

【図3】本発明によるディーゼルエンジンの排気浄化装
置の第2実施形態を示す概略断面図である。
FIG. 3 is a schematic sectional view showing a second embodiment of an exhaust emission control device for a diesel engine according to the present invention.

【図4】本発明によるディーゼルエンジンの排気浄化装
置の第3実施形態を示す概略断面図である。
FIG. 4 is a schematic sectional view showing a third embodiment of the exhaust emission control system for a diesel engine according to the present invention.

【符号の説明】[Explanation of symbols]

1,1’,1”…排気通路 2,2’,2”…NOx触媒 3,3’,3”…改質触媒 4…板部材 5,5’,5”…供給管 6…カバー 8…電気ヒータ 20,20”…制御装置 23…温度センサ 1,1 ', 1 "... Exhaust passage 2,2 ', 2 "... NOx catalyst 3,3 ', 3 "... Reforming catalyst 4 ... Plate member 5,5 ', 5 "... Supply pipe 6 ... Cover 8 ... Electric heater 20, 20 "... Control device 23 ... Temperature sensor

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI F01N 3/24 B01D 53/34 ZAB ZAB 53/36 ZAB 3/36 ZAB 101A (72)発明者 高田 保夫 愛知県愛知郡長久手町大字長湫字横道41 番地の1 株式会社豊田中央研究所内 (56)参考文献 特開 平6−212952(JP,A) 特開 平7−127447(JP,A) 特開 平6−137138(JP,A) (58)調査した分野(Int.Cl.7,DB名) F01N 3/08 - 3/36 B01D 53/34 B01D 53/86 B01D 53/94 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI F01N 3/24 B01D 53/34 ZAB ZAB 53/36 ZAB 3/36 ZAB 101A (72) Inventor Yasuo Takada Nagakute Town, Aichi District, Aichi Prefecture 1 in 41, Yokomichi Yokomichi, Chuo Research Institute, Toyota Central Research Institute Co., Ltd. (56) Reference JP-A-6-212952 (JP, A) JP-A-7-127447 (JP, A) JP-A-6-137138 (JP, A) (58) Fields surveyed (Int.Cl. 7 , DB name) F01N 3/08-3/36 B01D 53/34 B01D 53/86 B01D 53/94

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 機関排気系に配置された窒素酸化物を浄
化するためのNO触媒と、排気ガスの熱により加熱さ
れ、炭化水素系燃料を炭化水素系還元剤に改質するため
の改質触媒と、炭化水素系燃料を前記改質触媒を介して
前記NO触媒へ供給する炭化水素系燃料供給手段と、
前記炭化水素系燃料供給手段によって前記改質触媒へ供
給された前記炭化水素系燃料の一部を前記改質触媒で燃
焼させるだけの空気を前記改質触媒へ供給する空気供給
手段、とを具備し、前記改質触媒は大きな熱容量を有す
る前記NO 触媒により取り囲まれ、前記改質触媒と排
気ガスとの熱交換は前記NO 触媒を介して行われる
とを特徴とするディーゼルエンジンの排気浄化装置。
1. A NO X catalyst arranged in an engine exhaust system for purifying nitrogen oxides, and a reformer for reforming a hydrocarbon-based fuel into a hydrocarbon-based reducing agent which is heated by heat of exhaust gas. Quality catalyst, and hydrocarbon-based fuel supply means for supplying a hydrocarbon-based fuel to the NO X catalyst via the reforming catalyst,
An air supply means for supplying to the reforming catalyst air sufficient to burn a part of the hydrocarbon fuel supplied to the reforming catalyst by the hydrocarbon fuel supplying means to the reforming catalyst. However , the reforming catalyst has a large heat capacity.
Surrounded by the NO X catalyst,
An exhaust emission control device for a diesel engine, characterized in that heat exchange with air gas is performed through the NO X catalyst .
【請求項2】 機関排気系に配置された窒素酸化物を浄
化するためのNO触媒と、排気ガスの熱により加熱さ
れ、炭化水素系燃料を炭化水素系還元剤に改質するため
の改質触媒と、炭化水素系燃料を前記改質触媒を介して
前記NO触媒へ供給する炭化水素系燃料供給手段と、
前記炭化水素系燃料供給手段によって前記改質触媒へ供
給された前記炭化水素系燃料の一部を前記改質触媒で燃
焼させるだけの空気を前記改質触媒へ供給する空気供給
手段、とを具備し、前記改質触媒は大きな熱容量を有す
るカバーにより取り囲まれ、前記改質触媒と排気ガスと
の熱交換は前記カバーを介して行われることを特徴とす
るディーゼルエンジンの排気浄化装置。
2. A NO X catalyst arranged in an engine exhaust system for purifying nitrogen oxides, and heated by heat of exhaust gas.
Is a reforming catalyst and a hydrocarbon fuel supply means for supplying hydrocarbon fuel through the reforming catalyst to the NO X catalyst for reforming hydrocarbon fuel to hydrocarbon-based reducing agent,
The air supply means for supplying only air to burn a portion of the hydrocarbon-based fuel supplied to the reforming catalyst in the reforming catalyst by the hydrocarbon-based fuel supply unit to the reforming catalyst, comprising a city However, the reforming catalyst has a large heat capacity.
Is surrounded by a cover, the reforming catalyst and exhaust gas
Exhaust gas purification device for a diesel engine, characterized in that heat exchange is performed via the cover .
JP32719595A 1995-12-15 1995-12-15 Diesel engine exhaust purification system Expired - Fee Related JP3443223B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32719595A JP3443223B2 (en) 1995-12-15 1995-12-15 Diesel engine exhaust purification system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32719595A JP3443223B2 (en) 1995-12-15 1995-12-15 Diesel engine exhaust purification system

Publications (2)

Publication Number Publication Date
JPH09166014A JPH09166014A (en) 1997-06-24
JP3443223B2 true JP3443223B2 (en) 2003-09-02

Family

ID=18196380

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32719595A Expired - Fee Related JP3443223B2 (en) 1995-12-15 1995-12-15 Diesel engine exhaust purification system

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Country Link
JP (1) JP3443223B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3565035B2 (en) * 1998-07-10 2004-09-15 三菱ふそうトラック・バス株式会社 NOx reduction system for combustion exhaust gas
DE10045607B4 (en) * 2000-09-15 2013-11-28 Volkswagen Ag Emission-reducing motor vehicle unit and corresponding method
KR100782134B1 (en) * 2007-01-03 2007-12-05 한국에너지기술연구원 Fuel and air feeding device for hydrocarbon reforming/combustion
JP2009138570A (en) * 2007-12-04 2009-06-25 Toyota Motor Corp Fuel reforming device
US7980061B2 (en) * 2008-03-04 2011-07-19 Tenneco Automotive Operating Company Inc. Charged air bypass for aftertreatment combustion air supply
JP5625257B2 (en) * 2009-04-13 2014-11-19 いすゞ自動車株式会社 Exhaust gas temperature riser
WO2012107949A1 (en) * 2011-02-07 2012-08-16 トヨタ自動車株式会社 Internal combustion engine

Also Published As

Publication number Publication date
JPH09166014A (en) 1997-06-24

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