JP2002256852A - Device for processing exhaust gas of internal combustion engine and vehicle mounted with the device - Google Patents

Device for processing exhaust gas of internal combustion engine and vehicle mounted with the device

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Publication number
JP2002256852A
JP2002256852A JP2002038018A JP2002038018A JP2002256852A JP 2002256852 A JP2002256852 A JP 2002256852A JP 2002038018 A JP2002038018 A JP 2002038018A JP 2002038018 A JP2002038018 A JP 2002038018A JP 2002256852 A JP2002256852 A JP 2002256852A
Authority
JP
Japan
Prior art keywords
exhaust gas
carrier element
internal combustion
combustion engine
reducing
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.)
Pending
Application number
JP2002038018A
Other languages
Japanese (ja)
Inventor
Walter Sarholz
ザールホルツ ヴァルター
Bernd Schumann
シューマン ベルント
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.)
Robert Bosch GmbH
Original Assignee
Robert Bosch GmbH
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 Robert Bosch GmbH filed Critical Robert Bosch GmbH
Publication of JP2002256852A publication Critical patent/JP2002256852A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9445Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
    • B01D53/9454Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific device
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9495Controlling the catalytic process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/21Mixing gases with liquids by introducing liquids into gaseous media
    • B01F23/213Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids
    • B01F23/2132Mixing gases with liquids by introducing liquids into gaseous media by spraying or atomising of the liquids using nozzles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20Jet mixers, i.e. mixers using high-speed fluid streams
    • B01F25/25Mixing by jets impinging against collision plates
    • 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
    • F01N13/00Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
    • 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
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • F01N3/033Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
    • F01N3/035Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
    • 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
    • F01N3/0814Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents combined with catalytic converters, e.g. NOx absorption/storage reduction catalysts
    • 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
    • F01N3/0821Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents combined with particulate filters
    • 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
    • F01N3/0842Nitrogen oxides
    • 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
    • F01N3/0871Regulation of absorbents or adsorbents, e.g. purging
    • 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
    • F01N3/28Construction of catalytic reactors
    • F01N3/2892Exhaust flow directors or the like, e.g. upstream of catalytic device
    • 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
    • F01N11/00Monitoring or diagnostic devices for exhaust-gas treatment apparatus, e.g. for catalytic activity
    • 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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/06Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for extinguishing sparks
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Analytical Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Biomedical Technology (AREA)
  • Toxicology (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a device for processing the exhaust gas of an internal combustion engine having a supplying unit for continuously supplying a carrier element and a reducing agent. SOLUTION: In the device for processing the exhaust gas of an internal combustion engine equipped with a supplying unit supplying the carrier element containing a catalyst activity substance for oxidizing and/or reducing several components of the exhaust gas, in particular, a ceramic carrier element and reducing agent, the separate region having the reducing condition and the oxidizing condition is provided.

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、排ガスの異なる成
分を酸化および/または還元するための触媒活性物質を
含む担体要素、殊にセラミック担体要素と還元剤を連続
的に供給するための供給ユニットとを備えた、内燃機関
の排ガスを処理するための装置に関する。
The present invention relates to a supply unit for continuously supplying a carrier element, in particular a ceramic carrier element, and a reducing agent containing a catalytically active substance for oxidizing and / or reducing different components of the exhaust gas. And a device for treating exhaust gas from an internal combustion engine.

【0002】[0002]

【従来の技術】知識レベルが進歩することに相応して、
健康および環境の保護のために、自動車の排ガスの放出
を規制する法律的な基準は絶えず厳しくなっている。こ
の基準を満たすために、例えば欧州特許第082641
1号明細書の記載によれば、内燃機関の希薄排ガス、即
ち空気比λ>1を有する排ガス触媒が使用され、この排
ガス触媒は、触媒活性の層の裏面上への炭化水素の別々
の供給管を有する。
2. Description of the Related Art As the level of knowledge progresses,
For the protection of health and the environment, legal standards regulating the emission of motor vehicle emissions are constantly becoming more stringent. To meet this criterion, for example, EP 0 864 1
According to the description of the specification, a lean exhaust gas of an internal combustion engine, that is to say an exhaust gas catalyst having an air ratio λ> 1, is used, which comprises a separate supply of hydrocarbons on the back side of the catalytically active layer. Has a tube.

【0003】相応して希薄で運転される内燃機関の場合
には、一酸化炭素放出量および燃料放出量だけは僅かで
あるが、しかし、NO放出量は比較的に高く、この場
合排ガスは、殊に窒素酸化物(NO)を含有し、この窒
素酸化物は、希薄な排ガス中で接触還元されることがで
きないかまたは僅かな反応速度でのみ還元されることが
できる。炭化水素の別々の供給により、還元比の形成が
可能になり、それによってNOの放出量の還元が可能
になり、この場合には、なかんずく窒素(N)または
二酸化炭素(CO)および水(HO)が形成され
る。
[0003] When the internal combustion engine is operated at lean correspondingly, only carbon monoxide emissions and fuel emissions but are slightly, but, NO X emissions is relatively high, the exhaust gas in this case , Especially nitrogen oxides (NO), which cannot be catalytically reduced in lean exhaust gases or can be reduced only at low reaction rates. Separate feeds of hydrocarbons allow for the formation of a reduction ratio, thereby reducing the emission of NO X , in which case nitrogen (N 2 ) or carbon dioxide (CO 2 ) and inter alia Water (H 2 O) is formed.

【0004】しかし、欧州特許第0826411号明細
書の記載の排ガス触媒の場合には、還元比は単に比較的
に大量の炭化水素の供給によって維持されうることは、
欠点である。それというのも、排ガスに対向した側から
酸素は、触媒活性層によって拡散しうるからである。N
の放出量の転移は、それによって著しく損なわれ
る。更に、大量の供給することができる炭化水素は、希
薄混合気燃焼エンジンの概念に不利な影響を及ぼす。
However, in the case of the exhaust gas catalysts described in EP 08 264 411, it is clear that the reduction ratio can be maintained merely by supplying a relatively large amount of hydrocarbons.
It is a disadvantage. This is because oxygen can diffuse through the catalytically active layer from the side facing the exhaust gas. N
O transfer of emission of X is significantly impaired thereby. In addition, the large supply of hydrocarbons has a detrimental effect on the concept of lean-burn engines.

【0005】[0005]

【発明が解決しようとする課題】これに対して、本発明
の課題は、担体要素と還元剤を連続的に供給するための
供給ユニットとを有する、内燃機関の排ガスを処理する
ための装置を提案することであり、この場合この装置
は、内燃機関の希薄排ガスのNOの放出量の転移を改
善し、同時に供給することができる還元剤の量は、明ら
かに減少される。
The object of the present invention, on the other hand, is to provide an apparatus for treating exhaust gas of an internal combustion engine, comprising a carrier element and a supply unit for continuously supplying a reducing agent. It is a proposal, in this case, that the device improves the transfer of the NO X emissions of the lean exhaust gas of the internal combustion engine, and the amount of reducing agent that can be supplied at the same time is significantly reduced.

【0006】[0006]

【課題を解決するための手段】この課題は、冒頭に記載
された装置から出発してによって請求項1記載の特徴部
の記載によって解決される。
This object is achieved by starting from the device described at the outset and by the characterizing features of claim 1.

【0007】従属請求項に記載された方法によって、本
発明の好ましい実施態様および他の形成が可能になる。
[0007] The preferred embodiments and other forms of the invention are made possible by the methods recited in the dependent claims.

【0008】それに応じて、内燃機関の排ガスを処理す
るための本発明による装置は、還元条件および酸化条
件、有利に希薄な空気比(λ>1)を有する別個の領域
が設けられていることを示す。
Accordingly, the device according to the invention for treating the exhaust gas of an internal combustion engine is provided with separate zones with reducing and oxidizing conditions, preferably with a lean air ratio (λ> 1). Is shown.

【0009】この種の装置を用いることにより、還元領
域内でNOの排ガス成分の変換が有利に可能になるこ
とが保証される。殊に、この場合には、相応して大きく
寸法決定可能な領域の本発明により調節可能な強力な還
元条件は、NOの放出量の本質的に良好な転移を生じ
る。
[0009] By using such a device, the conversion of exhaust gas components of the NO X is guaranteed to be advantageously possible in reducing the area. In particular, in this case, the strong reduction conditions which can be adjusted according to the invention in a correspondingly large scalable region result in an essentially good transfer of the NO X emissions.

【0010】それによって、供給することができる炭化
水素の量は、殊に内燃機関の燃料の形で明らかに減少さ
れることができ、このことは、燃料消費量の本質的な減
少、ひいては経済性および環境保護性の改善を運転され
る内燃機関に相応して導くことができる。本発明によれ
ば、この装置は、例えばオットーエンジンならびにディ
ーゼルエンジンに使用可能である。
As a result, the amount of hydrocarbons that can be supplied can be significantly reduced, especially in the form of fuel for the internal combustion engine, which leads to a substantial reduction in fuel consumption and thus economics. An improvement in the power and environmental protection can be guided correspondingly to the engine to be operated. According to the invention, the device can be used, for example, for Otto engines as well as for diesel engines.

【0011】この場合、別個の領域は、多種多様に形成
されていてもよいし、構成されていてもよい。こうし
て、例えば還元条件および/または酸化条件を有する多
数の別々の領域を実現させることができる。好ましく
は、還元条件を有する層状に形成された領域が設けられ
ている。それによって、有利に形成された界面を種々の
領域の分離のために変換することができることが可能に
なる。このために、原則的に場合によって分離層が設け
られていてもよい。この分離層は、例えばメンブラン、
フィルター層または類似物として実現させることができ
る。
In this case, the separate regions may be formed in various ways or may be formed. In this way, a large number of separate zones with, for example, reducing and / or oxidizing conditions can be realized. Preferably, a region formed in a layer having a reduction condition is provided. Thereby, it is possible that the advantageously formed interface can be transformed for the separation of various regions. For this purpose, a separating layer may in principle also be provided. This separation layer is, for example, a membrane,
It can be realized as a filter layer or the like.

【0012】また、界面は、異なる構造および/または
材料組成を有する領域を形成させることによって実現さ
れることができる。好ましくは、硝酸塩を形成させるた
めおよび/またはNOを蓄積するための物質が設けら
れており、したがって有利にNO排ガス成分は、硝酸
塩に変換される。それによって、殊に硝酸塩の固体表面
拡散および/または固体ばら積み拡散による窒素運搬
と、なかんずく気相拡散により行なわれる酸素運搬との
分離は、実現されうる。
[0012] Also, the interface can be realized by forming regions having different structures and / or material compositions. Preferably, materials for storing for forming nitrates and / or NO X is provided, thus advantageously NO X exhaust gas components are converted to nitrate. In this way, a separation of nitrogen transport, in particular by solid surface diffusion and / or solid bulk diffusion of nitrates, and in particular oxygen transport carried out by gas phase diffusion can be realized.

【0013】この場合、NOの運搬は、気相中で酸素
運搬と同様に妨害されるが、しかし、物質を用いて窒素
の気相とは無関係の固体運搬は、考えられうる限り有利
であるかまたはまたは本質的に有利である。硝酸塩とし
て吸収される窒素酸化物は、なかんずく固体拡散により
還元条件を有する領域内に到達し、この場合この硝酸塩
は、連続的に供給される還元剤と反応させることがで
き、それによって好ましくは窒素(N)に変換され
る。
In this case, the transport of NO X is impeded in the gas phase as well as the transport of oxygen, but the transport of solids independent of the gas phase of nitrogen using substances is as advantageous as possible. Some or essentially advantageous. The nitrogen oxides absorbed as nitrates reach, inter alia, in regions having reducing conditions by solid state diffusion, in which case the nitrates can be reacted with a continuously supplied reducing agent, whereby (N 2 ).

【0014】類似のガス拡散係数のために、例えば比較
的に簡単な酸素拡散限定によりNO の運搬は妨害され
るであろうし、したがって排ガスの一部分は、単に相応
する領域に到達し、それによって単にNOの放出量の
一部分だけが変換されうるであろう。しかし、本発明に
よれば、物質を用いることにより硝酸塩の形成によって
酸素の輸送は抑制され、同時に窒素の輸送は促進され、
このことは、別々の領域の形成の付加的な改善を生じ
る。
For similar gas diffusion coefficients, for example,
NO by simple oxygen diffusion limitation XTransport is disturbed
And thus a portion of the exhaust gas is simply
To reach the area whereXRelease of
Only a portion could be converted. However, in the present invention
According to the use of substances, by the formation of nitrates
Oxygen transport is suppressed, while nitrogen transport is promoted,
This results in additional improvements in the formation of separate areas
You.

【0015】好ましくは、硝酸塩を形成させるためおよ
び/またはNOを蓄積するための物質として、アルカ
リ土類金属酸化物、殊に酸化バリウム、酸化ストロンチ
ウムおよび/または酸化カルシウムおよび/またはアル
カリ金属酸化物または記載された酸化物の混合酸化物な
らびに酸化アルミニウム、酸化ジルコニウム、酸化ラン
タンおよび/または酸化セリウムの中の1つ以上の成分
が設けられている。
[0015] Preferably, as a substance for storing for forming nitrates and / or NO X, alkaline earth metal oxides, in particular barium oxide, strontium oxide and / or calcium oxide and / or alkali metal oxides Alternatively, a mixed oxide of the described oxides and one or more components of aluminum oxide, zirconium oxide, lanthanum oxide and / or cerium oxide are provided.

【0016】本発明の特殊な他の形成において、少なく
とも1つの触媒活性物質は、硝酸塩を形成させるためお
よび/またはNOを蓄積するための物質を含む。それ
によって、有利に還元条件を有する層状に形成された領
域を変換させることができ、本発明による装置を製造す
る場合には、硝酸塩を形成させるためおよび/またはN
を蓄積するための物質は、殊に炭化水素および一酸
化炭素の酸化のためおよびなかんずくNOの還元のた
めに、触媒活性物質、例えば白金、ルテニウム、パラジ
ウムまたは相応する金属の組合せ物に添加されることが
できる。
[0016] In another special form of the present invention, at least one catalytically active material comprises a material for storing for forming nitrates and / or NO X. This makes it possible to convert the layered regions which advantageously have reducing conditions and, in the case of producing the device according to the invention, to form nitrates and / or N 2
Materials for accumulating O X are in particular for the reduction for and inter alia NO X in the oxidation of hydrocarbons and carbon monoxide, the catalytic active material, such as platinum, ruthenium, palladium or corresponding combination of metal Can be added.

【0017】殊に、約0.1〜5μmの孔径により、こ
の場合には、約20〜500μmの細孔の長さが設けら
れており、なかんずく触媒活性物質の孔径および多孔度
を有利に調整することにより、酸素の拡散を制限するこ
とが可能になり、この場合には、反応帯域からの硝酸塩
還元の生成物、例えばCOおよびHOの除去は、云
うに値する程度に遮断される。
In particular, a pore size of about 0.1 to 5 μm, in this case a length of pores of about 20 to 500 μm, is provided, in particular to advantageously control the pore size and porosity of the catalytically active substance. By doing so, it is possible to limit the diffusion of oxygen, in which case the removal of products of nitrate reduction, such as CO 2 and H 2 O, from the reaction zone is blocked to a considerable extent. .

【0018】本発明の好ましい実施態様において、触媒
活性物質は、少なくとも担体の排ガスに対向した側に層
状で配置されている。それによって、好ましくは担体要
素の製造ならびに還元剤の連続的供給、ならびに還元条
件を有する層状領域の形成が変更されうる。
In a preferred embodiment of the invention, the catalytically active substances are arranged in layers at least on the side of the carrier facing the exhaust gas. Thereby, preferably the production of the carrier element and the continuous supply of the reducing agent, as well as the formation of the lamellar region with the reducing conditions, can be modified.

【0019】また、先に記載された物質に対して選択的
に、アンモニアを形成させるためおよび/またはアンモ
ニアを蓄積させるために相応する物質を用いてのアンモ
ニア蓄積体ならびに酸化剤の供給管を有する還元剤蓄積
体は、排ガスから離れた側から設けられていてもよい。
It also has a supply line for the ammonia accumulator and the oxidizing agent, using a corresponding substance for forming ammonia and / or for accumulating ammonia, selectively with respect to the substances described above. The reducing agent accumulator may be provided from a side remote from the exhaust gas.

【0020】有利に、排ガス分配器は、排ガス流の分配
のために設けられている。それによって、例えば個々の
排ガス分流の異なる後処理のために、排ガス流の好まし
い分配が実現可能であることが保証される。
Advantageously, an exhaust gas distributor is provided for the distribution of the exhaust gas stream. This ensures that a favorable distribution of the exhaust gas stream is feasible, for example, for different work-up of the individual exhaust gas streams.

【0021】本発明の特殊な他の実施態様において、少
なくとも1つの混合装置は、還元剤と排ガス分流との混
合のために設けられており、したがってこの排ガス分流
は、脂肪を含む空気比(λ<1)、有利に0.6〜0.
7の前記空気比を有している。それによって、好ましく
は脂肪を含んだ排ガス分流が供給ユニットにより、殊に
排ガスから離れた側で担体要素に供給可能であることが
可能になる。
In another particular embodiment of the invention, at least one mixing device is provided for the mixing of the reducing agent with the offgas stream, so that the offgas stream has a fat-to-air ratio (λ). <1), preferably 0.6-0.
And has an air ratio of 7. This makes it possible for the preferably waste gas stream containing fat to be supplied to the carrier element by the supply unit, in particular on the side remote from the exhaust gas.

【0022】触媒中への侵入前に還元剤と排ガス分流と
の混合により、カーボンブラックの形成、ひいては担体
要素の細孔の閉塞が阻止されることは好ましい。当該の
亀裂形成および細孔の閉塞は、排ガス触媒の場合に公知
技術水準によれば純粋な炭化水素の供給によって250
℃の通常の触媒温度で予想することができ、このこと
は、還元剤輸送の強力な妨害、ひいてはNOの放出量
の転移を生じる。
It is preferred that the mixing of the reducing agent and the offgas stream before entry into the catalyst prevents the formation of carbon black and thus the blockage of the pores of the support element. According to the prior art in the case of exhaust gas catalysts, the formation of cracks and the obstruction of the pores are, according to the state of the art, provided by pure hydrocarbon feeds.
At normal catalyst temperatures of ° C. this can be expected, which results in a strong disturbance of the transport of the reducing agent and thus a shift in the emission of NO X.

【0023】好ましくは、還元剤と混合される排ガス分
流は、単に全排ガス流の一部分を含み、したがって還元
条件、即ち脂肪を含む空気比(λ<1)を生じさせるた
めに、比較的に僅かな還元剤が供給されなければならな
い。
Preferably, the offgas stream mixed with the reducing agent comprises only a fraction of the total offgas stream and is therefore relatively low in order to produce reducing conditions, ie a fat-containing air ratio (λ <1). Must be supplied.

【0024】特に、制御ユニットは、還元剤の供給の制
御のために設けられている。それによって、内燃機関の
異なる運転条件で好ましくは還元剤の供給は、運転条件
に適合しうることが保証される。これは、殊に車両また
は類似物のための内燃機関の場合に有利である。
In particular, the control unit is provided for controlling the supply of the reducing agent. This ensures that the supply of the reducing agent, preferably at different operating conditions of the internal combustion engine, can be adapted to the operating conditions. This is particularly advantageous in the case of internal combustion engines for vehicles or the like.

【0025】本発明の特殊な他の実施態様において、制
御ユニットは、空気比λの測定のために少なくとも1つ
のセンサーを含み、したがって内燃機関の異なる運転条
件の際にも相応する排ガス分流中の空気比λを一定の値
に調節することができる。
In another particular embodiment of the invention, the control unit includes at least one sensor for measuring the air ratio λ, so that even in different operating conditions of the internal combustion engine, the control unit includes The air ratio λ can be adjusted to a constant value.

【0026】好ましくは、数多くの通路を有し、排ガス
分流を担体要素の異なる部分に供給するための少なくと
も1つの排ガス案内要素を有する管状担体要素が設けら
れており、この場合全ての部分は、多数の通路を含む。
それによって、担体要素への好ましい排ガス分流の供給
を変更することができることが可能になる。
Preferably, a tubular carrier element is provided which has a number of passages and at least one exhaust gas guiding element for supplying a split stream of exhaust gas to different parts of the carrier element, all parts comprising: Includes multiple passages.
This makes it possible to vary the supply of the preferred offgas stream to the carrier element.

【0027】それによって、同時に還元条件および希薄
な空気比を有する別個の領域を形成させるための界面
は、有利に拡大されていてもよい。原則的に本発明によ
る別個の領域間の当該界面を本質的に拡大することは、
好ましい。それというのも、それによって反応エダクト
ならびに反応生成物の物質の輸送、殊に物質流は、改善
することができるからである。
[0027] Thereby, the interface for simultaneously forming a separate region with reducing conditions and a lean air ratio may advantageously be enlarged. Essentially enlarging the interface between the discrete areas according to the invention essentially
preferable. This makes it possible to improve the transport of the reaction starting materials as well as the reaction product, in particular the material flow.

【0028】例えば、半径方向での円形、直線状および
/または複雑な帯域を相応する排ガス案内要素により形
成することは、なかんずく相応する供給ユニットとの組
合せで考えることができる。管状の担体要素は、円形、
楕円形、角張ったまたは比較可能な断面を有することが
でき、この場合には、場合により数多くの通路は、スリ
ット状および/または列状で配置されている。
For example, the formation of a circular, linear and / or complex zone in the radial direction by means of a corresponding exhaust gas guiding element can be envisaged, inter alia, in combination with a corresponding supply unit. The tubular carrier element is circular,
It can have an elliptical, angular or comparable cross-section, in which case a large number of passages are arranged in a slit and / or row.

【0029】好ましくは、供給ユニットは、担体要素の
中央帯域中に配置されており、この場合には、排ガス分
流をスリット状または列状に分布させるための溢流通路
が設けられている。それによって、例えば列および/ま
たはスリットは、有利に交互に異なる排ガス分流を貫流
させることができることが保証される。
[0029] The supply unit is preferably arranged in the central zone of the carrier element, in which case an overflow passage is provided for distributing the exhaust gas divergence in a slit-like or row-like manner. This ensures that, for example, the rows and / or the slits can advantageously alternately flow through different exhaust gas branches.

【0030】場合によっては、排ガス案内要素として配
合装置、例えば担体要素の個々の通路または多数の通路
のために相応する溢流通路、相応する栓または類似物を
有するかまたは有しない仕切板が設けられている。この
場合、相応して配置された溢流通路は、例えば仕切られ
たかまたは栓をされた通路への排ガス分流の分配を実現
させることができる。
If appropriate, a compounding device is provided as an exhaust gas guiding element, for example a partition plate with or without corresponding overflow passages, corresponding plugs or the like for individual or multiple passages of the carrier element. Have been. In this case, a correspondingly arranged overflow channel can provide, for example, a distribution of the exhaust gas stream to a partitioned or plugged channel.

【0031】担体要素の中央帯域中に供給ユニットを配
置することによって、排ガス分流の比較的に流れに有利
な分布を実現させることができる。例えば、脂肪を含む
空気比を有する排ガス分流は、溢流通路を介して担体要
素の外側領域内に流入する。場合によっては、希薄な空
気比を有する2つの排ガス分流は、相応する溢流通路に
より担体要素の中央領域内に流入し、この場合排ガス分
流は、有利に別個に担体要素をスリット状または列状に
貫流する。
By arranging the supply unit in the central zone of the carrier element, a relatively flow-favorable distribution of the offgas stream can be achieved. For example, an exhaust gas divergence having a fat-containing air ratio flows into the outer region of the carrier element via an overflow channel. In some cases, the two exhaust gas streams with lean air ratios flow into the central region of the carrier element by means of corresponding overflow channels, wherein the exhaust gas stream advantageously separates the carrier element into slits or rows. Flow through.

【0032】本発明の1つの実施例は、図に示されてお
り、以下、図面につき詳説する。
One embodiment of the present invention is shown in the drawings and will now be described in detail with reference to the drawings.

【0033】[0033]

【実施例】図1には、詳細には示されていない多孔質の
ガス透過性支持セラミックおよび触媒活性層を有するセ
ラミック担持触媒1が略示されており、この場合この触
媒活性層は、硝酸塩形成および/またはNO蓄積のた
めの物質を用いる公知の排ガス触媒技術からの排ガスの
異なる成分を酸化および還元するための触媒活性材料を
含む。セラミック担持触媒1には、分流3が垂直な通路
列の中央部分で供給管4を介して供給される。分流3
は、排ガス流5の一部分、例えば全排ガス流の5%未満
を有する。図4によれば、分流3に噴入装置8により還
元剤7が供給され、この場合この還元剤は、有利に内燃
機関の燃料に相当する。
FIG. 1 schematically shows a porous, gas-permeable supporting ceramic, not shown in detail, and a ceramic-supported catalyst 1 having a catalytically active layer, wherein the catalytically active layer comprises nitrate. using the formation and / or material for of the NO X storage containing catalytically active material for the oxidation and reduction of the different components of the exhaust gas from the well-known exhaust gas catalyst technology. A split stream 3 is supplied to the ceramic supported catalyst 1 via a supply pipe 4 at the center of a vertical row of passages. Shunt 3
Has a portion of the exhaust gas stream 5, for example less than 5% of the total exhaust gas stream. According to FIG. 4, the branch stream 3 is supplied with a reducing agent 7 by means of an injection device 8, which preferably corresponds to the fuel of the internal combustion engine.

【0034】セラミック担持触媒1は、図1によれば、
多数の小さな通路を有し、この場合には、分かり易く表
現するために、通路の数は、本質的に実際の触媒の場合
よりも少ない。図1の詳細に示された一部分から栓2を
認めることができ、この栓は、通路の端部を閉鎖する。
栓3は、脂肪を含んだ、即ち脂肪を含む空気比(λ<
1)、有利に0.6〜0.7の空気比を有する分流3が
供給管4によりセラミック担体の中央部で供給され、図
2によれば溢流開口によりスリットの全ての通路中に流
入することができるように配置されている。
According to FIG. 1, the ceramic supported catalyst 1
It has a large number of small passages, in which case the number of passages is essentially smaller than for a real catalyst, for the sake of clarity. A plug 2 can be seen from the part shown in detail in FIG. 1, which plug closes the end of the passage.
The plug 3 contains fat, that is, a fat-containing air ratio (λ <
1), a diverted stream 3, preferably having an air ratio of 0.6 to 0.7, is supplied at the center of the ceramic carrier by means of a supply pipe 4 and flows according to FIG. It is arranged to be able to.

【0035】図1によれば、排ガス流5は、セラミック
担体1の上部ならびに下部で開いた通路内に流入し、相
応する溢流開口9により相応するスリットのセラミック
体1の中央部分で通路内に流入する。それに応じて、希
薄、即ち希薄な空気比(λ>1)を有する排ガスを有す
る通路は、栓2との中央部分で緊密に閉鎖され、脂肪を
含む空気比(λ<1)を有するスリットの通路は、セラ
ミック担体1の上部ならびに下部で緊密に閉鎖されてい
る。
According to FIG. 1, the exhaust gas stream 5 flows into a passage which is open at the top and at the bottom of the ceramic carrier 1 and has a corresponding overflow opening 9 in the central part of the ceramic body 1 of the corresponding slit. Flows into. Correspondingly, the passage with the exhaust gas having a lean, ie lean, air ratio (λ> 1) is closed tightly in the central part with the plug 2 and has a slit with a fat-containing air ratio (λ <1). The passage is tightly closed at the top as well as at the bottom of the ceramic carrier 1.

【0036】図2には、図1に記載された線”2”−”
2”に沿っての断面が略示されている。この場合、栓2
ならびに溢流開口9の配置が明らかになる。図2に示さ
れた例示的なスリットの場合には、脂肪を含んだ分流3
は、スリットの全通路内に流入し、図3の記載によれ
ば、多孔質の支持セラミックの細孔を通じてセラミック
担体1の触媒層の裏面上に流れる。殊に、珪酸塩形成お
よび/またはNOX蓄積のために触媒層に添加された物
質は、脂肪を含む排ガス領域および化学量論的排ガス領
域が形成され、それによって窒素を比較的に高い変換率
で還元することができることが保証される。
FIG. 2 shows a line "2"-"described in FIG.
2 "is schematically shown in this case.
In addition, the arrangement of the overflow opening 9 becomes clear. In the case of the exemplary slit shown in FIG.
Flows into the entire passage of the slit and, according to the description in FIG. 3, flows through the pores of the porous supporting ceramic onto the back surface of the catalyst layer of the ceramic carrier 1. In particular, the substances added to the catalyst layer for the formation of silicates and / or for the accumulation of NOx result in the formation of fat-containing exhaust gas regions and stoichiometric exhaust gas regions, whereby nitrogen is converted at a relatively high conversion rate. It is guaranteed that it can be reduced.

【0037】付加的に、触媒層の狭い細孔ならびに反応
生成物および残留窒素の流れは、酸素の拡散を阻止し、
化学量論的反応領域および脂肪を含んだ反応領域の形成
を改善する。触媒層中への気相での窒素の供給は、それ
によって同様に阻止される。しかし、この物質は、気相
とは無関係に窒素酸化物の輸送を固体に結合した硝酸塩
拡散の形で保証する。相応する固体なしに支持される、
窒素の輸送は、酸素の輸送の抑制と結び付いて完全なN
変換を保証することはできない。
Additionally, the narrow pores of the catalyst layer and the flow of reaction products and residual nitrogen prevent oxygen diffusion,
Improves the formation of stoichiometric and fat-containing reaction zones. The supply of nitrogen in the gas phase into the catalyst layer is likewise prevented. However, this material guarantees the transport of the nitrogen oxides independently of the gas phase in the form of solid-bound nitrate diffusion. Supported without a corresponding solid,
Nitrogen transport is combined with suppression of oxygen transport and complete N
O X conversion can not be guaranteed.

【0038】図4には、脂肪を含む空気比(λ<1)を
有する分流3を発生させるために排ガス分配器10を有
する供給管4が示されている。供給管4は、この供給管
がセラミック担体1上に殆んど緊密に載置されているよ
うに取り付けられている。この場合、小さな漏れは、前
記装置の機能を損なわない。それというのも、分流3の
上記の空気比の場合には、この分流は、漏れが少なくて
も脂肪を含んだままであり、一方、排ガス流5は、相応
する漏れの場合でも希薄なままであるからである。希薄
な排ガス流5の簡単に高められたHC含量は、触媒によ
って十分に酸化される。
FIG. 4 shows a supply pipe 4 having an exhaust gas distributor 10 for generating a split stream 3 having a fat-containing air ratio (λ <1). The supply tube 4 is mounted such that the supply tube is placed almost tightly on the ceramic carrier 1. In this case, a small leak does not impair the function of the device. This is because, for the above-mentioned air ratio of the split stream 3, this split stream remains fat-containing with little leakage, while the exhaust gas stream 5 remains lean even with a corresponding leak. Because there is. The simply increased HC content of the lean exhaust gas stream 5 is fully oxidized by the catalyst.

【0039】更に、図4には、噴入装置8が示されてお
り、この場合噴霧される燃料7は、2つの混合板11、
12を用いて殆んど完全に排ガス分流3と混合される。
例えば、型LSUの市販のλゾンデ、即ちλゾンデ−ユ
ニバーサル(Lambdasonde-Universal)として形成され
ているセンサー13は、下流で混合板11、12に向か
って空気比λを測定する。詳細には図示されていない制
御ユニットを用いた場合には、例えば導入される燃料7
の量は、制御される。この場合には、例えば詳細には図
示されていないポンプが運転され、このポンプは、燃料
を燃料タンクから噴霧装置8に搬送し、この場合この噴
霧装置は、例えば噴霧ノズルとして形成されている。ま
た、本発明によれば、相応する別の噴霧装置ならびに混
合装置が実現可能である。
FIG. 4 also shows an injection device 8 in which the fuel 7 to be sprayed comprises two mixing plates 11,
12 is mixed almost completely with the offgas stream 3.
For example, a sensor 13 embodied as a commercially available λ sonde of the type LSU, ie a λ Sonde-Universal, measures the air ratio λ downstream towards the mixing plates 11, 12. If a control unit not shown in detail is used, for example,
Is controlled. In this case, for example, a pump (not shown in detail) is operated, which pumps the fuel from the fuel tank to a spray device 8, which is formed, for example, as a spray nozzle. According to the invention, further suitable spraying and mixing devices are also possible.

【0040】図5には、排ガス分配器10を有する供給
管4ならびに混合板12は、説明のために斜視図で記載
されている。更に、図5は、2つの案内板14および排
ガス管15の装置を認めることができる。例示的に、全
体の装置は、案内板14により内燃機関の排気管に溶接
される。
FIG. 5 shows the supply pipe 4 having the exhaust gas distributor 10 and the mixing plate 12 in a perspective view for explanation. FIG. 5 also shows the arrangement of the two guide plates 14 and the exhaust pipe 15. Illustratively, the entire device is welded to the exhaust pipe of the internal combustion engine by a guide plate 14.

【0041】図6には、理解しやすくするために、図5
に記載された全装置が付加的に正面図で示されている。
FIG. 6 shows FIG. 5 for easy understanding.
Are additionally shown in a front view.

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

【図1】詳細に示された一部分を含む、本発明によるセ
ラミック担持触媒を示す略示斜視図。
FIG. 1 is a schematic perspective view showing a ceramic supported catalyst according to the present invention, including parts shown in detail.

【図2】図1に記載された線”2”−”2”に沿って本
発明によるセラミック担持触媒を示す略示断面図。
FIG. 2 is a schematic sectional view showing the ceramic supported catalyst according to the present invention along the line “2”-“2” described in FIG. 1;

【図3】図1に記載された線”3”−”3”に沿って本
発明によるセラミック担持触媒を示す略示断面図。
FIG. 3 is a schematic sectional view showing the ceramic supported catalyst according to the present invention along the line “3”-“3” described in FIG. 1;

【図4】本発明による装置を示す略示断面図。FIG. 4 is a schematic sectional view showing an apparatus according to the present invention.

【図5】排ガス分配器を示す略示斜視図。FIG. 5 is a schematic perspective view showing an exhaust gas distributor.

【図6】排ガス分配器を示す略示斜視図。FIG. 6 is a schematic perspective view showing an exhaust gas distributor.

【符号の説明】[Explanation of symbols]

1 セラミック担持触媒、 2 栓、 3 分流、 4
供給管、 5 排ガス流、 6 ケーシング、 7
燃料、 8 噴霧装置、 9 溢流開口、 10 排ガ
ス分配器、 11 混合板、 12 混合板、 13
センサー、 14 案内板、 15 排ガス管
1 ceramic supported catalyst, 2 stoppers, 3 branch flow, 4
Supply pipe, 5 exhaust gas flow, 6 casing, 7
Fuel, 8 atomizing device, 9 overflow opening, 10 exhaust gas distributor, 11 mixing plate, 12 mixing plate, 13
Sensor, 14 guide plate, 15 exhaust pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 ベルント シューマン ドイツ連邦共和国 ルーテスハイム ダイ ムラーシュトラーセ 23 Fターム(参考) 3G091 AA17 AA18 AA28 AB06 AB09 BA14 CA16 CA27 DB10 EA34 FB10 FB12 GA06 GA10 GA24 GB01X GB01Y GB03Y GB04Y GB10X GB10Y GB15Y GB17X HA36 4D048 AA06 AB02 AC02 BB02 CC23 CC47 DA02 DA20  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Bernd Schumann Luthesheim Daimlerstrasse 23 F-term (reference) 3G091 AA17 AA18 AA28 AB06 AB09 BA14 CA16 CA27 DB10 EA34 FB10 FB12 GA06 GA10 GA24 GB01X GB01Y GB03Y GB04Y GB10X GB GB17X HA36 4D048 AA06 AB02 AC02 BB02 CC23 CC47 DA02 DA20

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 排ガス(5)の異なる成分を酸化および
/または還元するための触媒活性物質を含む担体要素、
殊にセラミック担体要素と還元剤(7)を連続的に供給
するための供給ユニット(4)とを備えた、内燃機関の
排ガスを処理するための装置において、還元条件および
酸化条件を有する別個の領域が設けられていることを特
徴とする、内燃機関の排ガスを処理するための装置。
1. A carrier element comprising a catalytically active substance for oxidizing and / or reducing different components of an exhaust gas (5),
In particular, in a device for treating the exhaust gas of an internal combustion engine, which comprises a ceramic carrier element and a supply unit (4) for continuously supplying a reducing agent (7), separate devices having reducing and oxidizing conditions are provided. Device for treating exhaust gas of an internal combustion engine, characterized in that it has an area.
【請求項2】 還元条件を有する層状に形成された領域
が設けられている、請求項1記載の装置。
2. The apparatus according to claim 1, wherein a layered region having a reducing condition is provided.
【請求項3】 硝酸塩を形成させるためおよび/または
NOを蓄積するための物質が設けられている、請求項
1または2記載の装置。
3. The device according to claim 1, wherein a substance for forming nitrates and / or accumulating NO X is provided.
【請求項4】 少なくとも1つの触媒活性物質が硝酸塩
を形成させるためおよび/またはNOを蓄積するため
の物質を含む、請求項1から3までのいずれか1項に記
載の装置。
4. The device according to claim 1, wherein the at least one catalytically active substance comprises a substance for forming nitrates and / or for accumulating NO X.
【請求項5】 触媒活性物質が少なくとも担体要素の排
ガスに対向した側に層状で配置されている、請求項1か
ら4までのいずれか1項に記載の装置。
5. The device as claimed in claim 1, wherein the catalytically active substance is arranged in a layer at least on the side of the carrier element facing the exhaust gas.
【請求項6】 排ガス分配器(10)が排ガス流(3、
5)の分配のために設けられている、請求項1から5ま
でのいずれか1項に記載の装置。
6. The exhaust gas distributor (10) comprises an exhaust gas stream (3,
6. The device according to claim 1, which is provided for the distribution of 5).
【請求項7】 少なくとも1つの混合装置(11、1
2)が還元剤(7)と排ガス分流(3)との混合のため
に設けられており、したがってこの排ガス分流(3)
は、空気比λ<1を有している、請求項1から6までの
いずれか1項に記載の装置。
7. At least one mixing device (11, 1).
2) is provided for mixing the reducing agent (7) with the exhaust gas divergence (3), so that this exhaust gas shunt (3)
Has an air ratio λ <1. 7.
【請求項8】 制御ユニットが還元剤供給量の制御のた
めに設けられている、請求項1から7までのいずれか1
項に記載の装置。
8. The method according to claim 1, wherein the control unit is provided for controlling the supply amount of the reducing agent.
The device according to item.
【請求項9】 制御ユニットが空気比λの測定のために
少なくとも1つのセンサー(13)を含む、請求項1か
ら8までのいずれか1項に記載の装置。
9. The device according to claim 1, wherein the control unit includes at least one sensor for measuring the air ratio λ.
【請求項10】 数多くの通路を有し、排ガス分流
(3、5)を担体要素の異なる部分に供給するための少
なくとも1つの排ガス案内要素(2)を有する管状担体
要素が設けられており、この場合全ての部分は、多数の
通路を含む、請求項1から9までのいずれか1項に記載
の装置。
10. A tubular carrier element having a number of passages and having at least one exhaust gas guiding element (2) for supplying an exhaust gas split stream (3, 5) to different parts of the carrier element is provided. 10. The device according to any one of the preceding claims, wherein all parts here comprise a number of passages.
【請求項11】 供給ユニット(4)が担体要素の中央
部分に配置されており、この場合上方流通路(9)が排
ガス分流(3、5)をスリット間に分配するかまたは列
状に分配するために設けられている、請求項1から10
までのいずれか1項に記載の装置。
11. The supply unit (4) is arranged in the central part of the carrier element, wherein the upper flow passage (9) distributes the exhaust gas divergence (3, 5) between the slits or in a line. Claims 1 to 10 provided for
The apparatus according to any one of the preceding claims.
【請求項12】 請求項1から11までのいずれか1項
に記載の装置が設けられていることを特徴とする車両。
12. A vehicle provided with the device according to claim 1. Description:
JP2002038018A 2001-02-17 2002-02-15 Device for processing exhaust gas of internal combustion engine and vehicle mounted with the device Pending JP2002256852A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10107548.0 2001-02-17
DE10107548 2001-02-17

Publications (1)

Publication Number Publication Date
JP2002256852A true JP2002256852A (en) 2002-09-11

Family

ID=7674449

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002038018A Pending JP2002256852A (en) 2001-02-17 2002-02-15 Device for processing exhaust gas of internal combustion engine and vehicle mounted with the device

Country Status (3)

Country Link
JP (1) JP2002256852A (en)
FR (1) FR2820989B1 (en)
IT (1) ITMI20020310A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010025112A (en) * 2008-07-21 2010-02-04 Friedrich Boysen Gmbh & Co Kg Exhaust system

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10242412A1 (en) * 2002-09-12 2004-03-25 Robert Bosch Gmbh Exhaust gas purification device for I.C. engines has a controllable feed unit for feeding auxiliary agents into regions of the channel structure of an exhaust gas post-treatment unit
DE10261620A1 (en) * 2002-12-27 2004-07-29 Volkswagen Ag Particulate filter with NOx storage catalytic converter function
DE102004050768A1 (en) * 2004-10-16 2006-04-20 Robert Bosch Gmbh Exhaust after-treatment device and method for operating an exhaust aftertreatment device
DE102008029761A1 (en) * 2008-06-25 2009-12-31 Volkswagen Ag Honey-comb structured exhaust gas cleaning body for use in exhaust gas system of internal combustion engine of motor vehicle, has walls permeable for reactants in partial areas such that reactant enters into flow channels through areas

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19546482A1 (en) * 1995-12-13 1997-06-26 Basf Ag Method for operating a cleaning system, a cleaning system and use thereof
JPH1076141A (en) * 1996-09-02 1998-03-24 Toyota Motor Corp Catalyst for purification of exhaust gas
DE19816323C1 (en) * 1998-04-11 1999-10-14 Dornier Gmbh Catalytic reduction of nitrogen oxides in vehicle exhaust gas
DE19938854C5 (en) * 1999-08-17 2006-12-28 Emitec Gesellschaft Für Emissionstechnologie Mbh Device for reducing the nitrogen oxide content in an exhaust gas of an internal combustion engine

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010025112A (en) * 2008-07-21 2010-02-04 Friedrich Boysen Gmbh & Co Kg Exhaust system
US8468802B2 (en) 2008-07-21 2013-06-25 Friedrich Boysen Gmbh & Co. Kg Exhaust gas system

Also Published As

Publication number Publication date
ITMI20020310A1 (en) 2003-08-18
FR2820989A1 (en) 2002-08-23
FR2820989B1 (en) 2005-02-25
ITMI20020310A0 (en) 2002-02-15

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