JPH10252452A - Reducing method of hazardous substance in exhaust gas from internal combustion engine provided with exhaust catalyst and device thereof - Google Patents

Reducing method of hazardous substance in exhaust gas from internal combustion engine provided with exhaust catalyst and device thereof

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Publication number
JPH10252452A
JPH10252452A JP10002281A JP228198A JPH10252452A JP H10252452 A JPH10252452 A JP H10252452A JP 10002281 A JP10002281 A JP 10002281A JP 228198 A JP228198 A JP 228198A JP H10252452 A JPH10252452 A JP H10252452A
Authority
JP
Japan
Prior art keywords
exhaust gas
secondary air
internal combustion
combustion engine
oxygen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10002281A
Other languages
Japanese (ja)
Inventor
Sven Behrens
シュフェン・ベーレンス
Steffen Franke
シュテフェン・フランケ
Horst Dr Harndorf
ホルスト・ハルンドルフ
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 JPH10252452A publication Critical patent/JPH10252452A/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
    • 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
    • F01N3/22Control of additional air supply only, e.g. using by-passes or variable air pump drives
    • 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
    • B01D53/22Separation 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 by diffusion
    • B01D53/229Integrated processes (Diffusion and at least one other process, e.g. adsorption, absorption)
    • 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
    • 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
    • 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
    • F01N3/2006Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating
    • 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
    • F01N3/206Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
    • 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
    • F01N3/30Arrangements for supply of additional air
    • F01N3/32Arrangements for supply of additional air using air pump
    • 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
    • F01N13/16Selection of particular materials
    • 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
    • F01N2610/1406Storage means for substances, e.g. tanks or reservoirs
    • 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)
  • Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Toxicology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce hazardous substances in exhaust gas effectively by providing at least one film (separation module) through which only oxygen molecules can permeate in a chamber and making oxygen rich to supply it to an internal combustion engine. SOLUTION: A secondary air pump 20 is provided as a reducing device of hazardous substances in exhaust gas in an internal combustion engine 10, and air 22 in which oxygen 22 is made rich is supplied to the secondary air pump 20. the air 22 in which oxygen is made rich is taken into from a pressure vessel and is mixed with ambient air in a mixer. An amount of air to be blown in is controlled by a secondary air blowing valve 30 which can be operated by an engine controller. The air 22 in which oxygen is made rich is supplied to this side of exhaust gas catalyst 52 in an exhaust pipe 50 of the internal combustion engine 10 through a pipe 40. The exothermic reaction occurs is the exhaust pipe 50 due to the supply of the air 22 in which oxygen is made rich, and the catalyst 52 is heated by the exothermic reaction to reduce hazardous substances in the exhaust gas effectively.

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,まず,内燃機関の
排気ガスに内燃機関の運転状態の関数として二次空気ポ
ンプにより二次空気が供給される,排気ガス触媒を備え
た内燃機関とくに自動車からの燃焼排気ガス内の有害物
質の低減方法に関するものである。
The present invention relates to an internal combustion engine provided with an exhaust gas catalyst, particularly an automobile, in which secondary air is supplied to the exhaust gas of the internal combustion engine by a secondary air pump as a function of the operating state of the internal combustion engine. The present invention relates to a method for reducing harmful substances in combustion exhaust gas from coal.

【0002】[0002]

【従来の技術】経験によると,試験(たとえばFTP7
5)において,最初の120秒間に内燃機関の一酸化炭
素(CO)および炭化水素(HC)の総エミッションの
約80%が放出される。この原因は,一方で低温機関に
おける混合物形成の不良および他方で運転温度にまだ達
していない触媒の転換率の不足である。したがって,こ
の問題を解決するために,触媒の始動時間すなわち触媒
がその作動温度に到達するまでの経過時間が短縮されな
ければならない。その理由は,これにより有害物質エミ
ッションの明らかな低減が達成されるからである。
2. Description of the Related Art Experience has shown that testing (eg, FTP7
In 5), approximately 80% of the total emissions of carbon monoxide (CO) and hydrocarbons (HC) are emitted during the first 120 seconds. This is due, on the one hand, to poor mixture formation in low-temperature engines and, on the other hand, to a lack of conversion of the catalyst which has not yet reached its operating temperature. Therefore, in order to solve this problem, the start-up time of the catalyst, that is, the elapsed time until the catalyst reaches its operating temperature, must be reduced. The reason is that this achieves a clear reduction of harmful substance emissions.

【0003】これは,たとえば触媒の手前で排気ガスに
二次空気ポンプまたは二次空気ブロアにより周囲空気が
供給されることにより達成可能である。このような内燃
機関の燃焼排気ガス内の有害物質の低減方法およびこの
方法を実行するための装置は,たとえばドイツ特許公開
第4141946号から既知である。この場合,内燃機
関の排気ガスに触媒の手前で,内燃機関の運転状態の関
数として,排気ガス温度を上昇させるために二次空気ポ
ンプにより二次空気が供給される。これは,たとえば燃
料リッチな暖機運転(燃料過剰)において,始動後短時
間,排気系統に触媒の手前で空気が吹き込まれることに
より行われる。この空気過剰は十分な温度レベルにおい
て排気系統内でHCおよびCOを酸化させ,これによ
り,より望ましい高い排気ガス温度を形成する。一方
で,このより高温の排気ガスは,触媒をその作動温度に
迅速に到達させるように働く。
This can be achieved, for example, by supplying the exhaust gas with ambient air by means of a secondary air pump or a secondary air blower before the catalyst. A method for reducing harmful substances in the combustion exhaust gas of such an internal combustion engine and a device for carrying out the method are known, for example, from DE-A 41 41 946. In this case, secondary air is supplied to the exhaust gas of the internal combustion engine by a secondary air pump in order to increase the exhaust gas temperature as a function of the operating state of the internal combustion engine, before the catalyst. This is performed, for example, in a fuel-rich warm-up operation (excess fuel) by blowing air into the exhaust system in front of the catalyst for a short time after starting. This excess air oxidizes HC and CO in the exhaust system at sufficient temperature levels, thereby creating a more desirable high exhaust gas temperature. On the other hand, this hotter exhaust gas serves to quickly bring the catalyst to its operating temperature.

【0004】さらに,吸い込まれたフレッシュエアに純
粋の酸素(O2)を混入することにより排気ガス温度の
上昇したがって触媒の始動時間の短縮が達成される方法
が既知である。
Furthermore, it is known to increase the exhaust gas temperature and thus reduce the catalyst start-up time by incorporating pure oxygen (O 2 ) into the fresh air that is drawn in.

【0005】このような内燃機関からの燃焼排気ガス内
の有害物質の低減方法およびこの方法を実行するための
装置がたとえばドイツ特許第4404681号から既知
である。この場合,室内に設けられた,酸素分子
(O2)に対してのみ透過可能な膜により吸込空気の酸
素(O2)のリッチ化が達成されるように設計されてい
る。
[0005] A method for reducing pollutants in the combustion exhaust gas from such internal combustion engines and a device for carrying out the method is known, for example, from DE 44 04 681 A1. In this case, it is designed such that the oxygen (O 2 ) of the intake air is enriched by a membrane provided only in the room and permeable only to oxygen molecules (O 2 ).

【0006】このような方法において,エンジン制御全
体がO2リッチな吸込空気により決定されなければなら
ないことが問題である。この理由から,機関制御の係合
の著しい増大が必要となる。結局,内燃機関の機関管理
全体が変更されなければならない。
A problem with such a method is that the entire engine control must be determined by the O 2 -rich intake air. For this reason, a significant increase in engine control engagement is required. Eventually, the overall engine management of the internal combustion engine must be changed.

【0007】[0007]

【発明が解決しようとする課題】したがって,できるか
ぎり簡単な技術的態様で触媒始動時間の短縮したがって
燃焼排気ガス内の有害物質の明らかな低減が可能な,冒
頭記載のタイプの排気ガス触媒を備えた内燃機関からの
燃焼排気ガス内の有害物質の低減方法を提供することが
本発明の課題である。
It is therefore possible to provide an exhaust gas catalyst of the type mentioned at the outset, which makes it possible to reduce the catalyst start-up time and thus reduce the harmful substances in the combustion exhaust gas in as simple a technical manner as possible. It is an object of the present invention to provide a method for reducing harmful substances in combustion exhaust gas from an internal combustion engine.

【0008】[0008]

【課題を解決するための手段】この課題は,本発明によ
り,冒頭記載のタイプの触媒を備えた内燃機関からの燃
焼排気ガス内の有害物質の低減方法において,供給され
る二次空気の酸素(O2)含有量が上昇されることによ
り解決される。供給される二次空気のO2含有量の上昇
により,すなわち触媒の手前における排気ガスのO2
ッチ化により,触媒の手前および触媒内における酸化条
件がきわめて有利な方法で改善され,これにより触媒始
動時間が短縮され,したがって燃焼排気ガス内の有害物
質の低減が達成される。さらに,吹き込まれる空気の酸
素含有量を上昇するとき,空気の容積流量を全体として
低減させることができることは有利である。これによ
り,機関排気ガスの冷却は低減され,これが同様に触媒
の始動時間を短縮させるように働くことはきわめて有利
である。
SUMMARY OF THE INVENTION The object of the present invention is to provide a method for reducing harmful substances in combustion exhaust gas from an internal combustion engine equipped with a catalyst of the type described at the outset, according to the invention. The problem is solved by increasing the (O 2 ) content. By increasing the O 2 content of the secondary air supplied, that is, by O 2 enrichment of the exhaust gas in front of the catalyst, the oxidation conditions in front and in the catalyst of the catalyst is improved in a very advantageous manner, thereby catalyst The start-up time is reduced, so that a reduction in the pollutants in the combustion exhaust gas is achieved. Furthermore, it is advantageous that the volumetric flow rate of the air can be reduced as a whole when the oxygen content of the blown air is increased. Hereby, the cooling of the engine exhaust gas is reduced, which advantageously also serves to reduce the start-up time of the catalyst.

【0009】純粋に原理的に,二次空気内の酸素含有量
を上昇させるために種々の方法が考えられる。
Purely in principle, various methods are conceivable for increasing the oxygen content in the secondary air.

【0010】たとえば,酸素は自動車に搭載されたガス
ボンベから取り出されて二次空気ポンプに供給されても
よい。
[0010] For example, oxygen may be taken out of a gas cylinder mounted on an automobile and supplied to a secondary air pump.

【0011】この場合,完全に消費された酸素圧縮ガス
ボンベは交換されるかまたは再充填されなければなら
ず,これは技術的におよび構造的にきわめて高い費用を
必要とする。
In this case, the completely consumed oxygen compressed gas cylinder must be replaced or refilled, which requires very high technical and structural costs.

【0012】したがって,とくに有利な実施態様は,O
2含有量を上昇するために,二次空気が,室内に設けら
れた,酸素分子に対してのみ透過可能な膜,いわゆる分
離モジュールを通過して供給されるように設計されてい
る。このように,車両に搭載されている分離モジュール
を用いて必要に応じて連続的にO2がリッチな二次空気
が発生されかつ排気ガスに供給されてもよい。したがっ
て,この場合,たとえば酸素圧縮ガスボンベ等が全く必
要なくなる。
[0012] Therefore, a particularly advantageous embodiment is O
2 In order to increase the content, the secondary air is designed to be supplied through a membrane provided only in the chamber, permeable only to oxygen molecules, a so-called separation module. In this manner, the O 2 -rich secondary air may be continuously generated and supplied to the exhaust gas as needed by using the separation module mounted on the vehicle. Therefore, in this case, for example, an oxygen compressed gas cylinder or the like is not required at all.

【0013】この方法の他のきわめて有利な実施態様
は,O2がリッチ化された二次空気が,分離モジュール
内で発生された後内燃機関の排気ガスに混合される前に
まず圧力タンク内に中間貯蔵され,後の運転サイクルに
おいて運転状態の関数として排気ガスに供給されるよう
に設計されている。このように,後に排気ガスに供給さ
れる二次空気の酸素のリッチ化は,二次空気の吹込みを
必要としない運転状態において,たとえば車両の全負荷
運転時に行われる。後の運転サイクルにおいて,たとえ
ば低温始動のときまたは暖機過程において,このとき中
間貯蔵されているO2がリッチ化された二次空気を排気
ガスに供給することができる。
Another very advantageous embodiment of the method is that the O 2 -enriched secondary air is first generated in a separation module and then mixed with the exhaust gas of the internal combustion engine before being mixed in the pressure tank. And is designed to be supplied to the exhaust gas as a function of the operating conditions in a later operating cycle. As described above, the enrichment of the oxygen of the secondary air to be supplied to the exhaust gas later is performed in an operation state in which the secondary air is not required to be blown, for example, during a full load operation of the vehicle. In a later operating cycle, for example during a cold start or during a warm-up process, the secondary air enriched with O 2, which is then stored intermediately, can be supplied to the exhaust gas.

【0014】膜は,たとえば膜を介してのO2分圧降下
を駆動力として必要とする混合物透過性セラミックから
構成されてもよい。したがって,有利な実施態様におい
ては,追加のブロアを使用しなくてもよいように,膜に
おいて必要な分圧降下が二次空気ポンプにより発生され
るように設計されている。
The membrane may, for example, be composed of a mixture-permeable ceramic which requires a driving force of O 2 partial pressure drop through the membrane. Therefore, in an advantageous embodiment, the required partial pressure drop in the membrane is designed to be generated by a secondary air pump, so that no additional blowers need be used.

【0015】さらに本発明は,排気ガス触媒の手前で内
燃機関の排気ガスに内燃機関の運転状態の関数として二
次空気ポンプにより二次空気が供給される前記二次空気
ポンプを含む,排気ガス触媒を備えた内燃機関とくに自
動車からの燃焼排気ガス内の有害物質の低減装置に関す
るものである。
[0015] The present invention further relates to an exhaust gas comprising a secondary air pump in which the secondary air is supplied to the exhaust gas of the internal combustion engine by a secondary air pump as a function of the operating state of the internal combustion engine before the exhaust gas catalyst. The present invention relates to an internal combustion engine equipped with a catalyst, and more particularly to a device for reducing harmful substances in combustion exhaust gas from automobiles.

【0016】この場合,これに関しては,できるだけ少
ない技術的費用で燃焼排気ガスからの有害物質のより有
効な低減を可能にする冒頭記載の種類の装置を提供する
ことが本発明の課題である。
In this case, it is the object of the present invention to provide a device of the type mentioned at the outset, which makes possible a more effective reduction of pollutants from the combustion exhaust gas with as little technical expenditure as possible.

【0017】この課題を解決するために,上記のタイプ
の排気ガス触媒を備えた内燃機関からの燃焼排気ガス内
の有害物質の低減装置において,それにより二次空気の
酸素(O2)のリッチ化が可能である本発明による手段
が設けられている。
In order to solve this problem, an apparatus for reducing harmful substances in combustion exhaust gas from an internal combustion engine equipped with an exhaust gas catalyst of the type described above, thereby enriching the secondary air with oxygen (O 2 ) Means according to the invention are provided which can be implemented.

【0018】有利な実施態様においては,この手段が,
室内に設けられた,酸素分子に対してのみ透過可能な少
なくとも1つの膜(分離モジュール)を含むように設計
されている。これにより,自動車上で酸素のリッチ化を
行うことが可能である。
In an advantageous embodiment, this means comprises:
It is designed to include at least one membrane (separation module) provided in the chamber and permeable only to oxygen molecules. This makes it possible to enrich oxygen on a vehicle.

【0019】分離モジュールが二次空気ポンプの下流側
に設けられているように設計されていることは有利であ
る。このようにして,二次空気ポンプにより形成される
圧力が,たとえば混合物透過性セラミックからなる膜に
おいてO2をリッチ化するために必要な,膜における分
圧降下の発生に使用されてもよい。
Advantageously, the separation module is designed to be provided downstream of the secondary air pump. In this way, the pressure formed by the secondary air pump, for example a mixture permeability O 2 in a membrane made of ceramics required to enrich, it may be used generated under partial pressure drop in the membrane.

【0020】内燃機関の後の運転サイクルに使用する目
的でO2がリッチ化された空気を貯蔵するために,O2
リッチ化された二次空気を一次的に貯蔵可能な圧力タン
クが分離モジュールの下流側に設けられている。
[0020] For O 2 in order to use the operating cycle after the internal combustion engine to store enriched air, O 2 is the enrichment is secondary air temporarily storable pressure tank isolation It is provided downstream of the module.

【0021】本発明の他の特徴および利点がいくつかの
実施態様の以下の説明ならびに図面から明らかである。
Other features and advantages of the invention will be apparent from the following description of several embodiments, as well as from the drawings.

【0022】[0022]

【発明の実施の形態】本発明による内燃機関10の燃焼
排気ガス内の有害物質の低減装置の第1の実施態様は二
次空気ポンプ20を含み,二次空気ポンプ20に22の
符号を有する矢印により記号で示された酸素がリッチ化
された周囲空気が供給される。この場合,酸素または酸
素がリッチ化された空気は,たとえば(図示されていな
い)圧力容器から取り入れられ,周囲空気の混合装置を
介して混入される。酸素が,たとえば,(図示されてい
ない)自動車に搭載された酸素容器から取り入れられる
か,または酸素が車両上でさらに以下に説明する方法で
発生されてもよい。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the apparatus for reducing harmful substances in the combustion exhaust gas of an internal combustion engine 10 according to the present invention includes a secondary air pump 20, and the secondary air pump 20 has a reference numeral 22. Ambient air enriched in oxygen, indicated by arrows, is supplied. In this case, oxygen or oxygen-enriched air is taken in, for example, from a pressure vessel (not shown) and is mixed in via an ambient air mixing device. Oxygen may be taken in, for example, from an oxygen container mounted on the vehicle (not shown), or oxygen may be generated on the vehicle in a manner described further below.

【0023】空気吹込量の制御は(図示されていない)
機関制御装置から操作可能な二次空気吹込弁30により
行われ,吹込空気の酸素成分に応じて機関制御装置によ
り設定される。この場合,それぞれ固定された混合比か
ら出発される。
Control of the amount of air blown (not shown)
This is performed by the secondary air injection valve 30 operable from the engine control device, and is set by the engine control device according to the oxygen component of the blown air. In this case, one starts with a fixed mixing ratio.

【0024】酸素がリッチ化された空気は配管40を介
して内燃機関10の排気管50に触媒52の手前で供給
される。
The oxygen-enriched air is supplied to the exhaust pipe 50 of the internal combustion engine 10 via the pipe 40 before the catalyst 52.

【0025】酸素がリッチ化された空気の供給により排
気管50内に発熱反応が発生し,この発熱反応は触媒を
加熱し,したがって触媒始動時間すなわちたとえば低温
始動において触媒がその作動温度に到達するまでの経過
時間を短縮させる。
The supply of oxygen-enriched air causes an exothermic reaction in the exhaust pipe 50 which heats the catalyst and thus reaches its operating temperature during the catalyst start-up time, for example, during a cold start. To reduce the elapsed time.

【0026】図2に示されている第2の実施態様におい
ては,第1の実施態様の要素と同じ要素には同じ符号が
付けられ,したがってこれらの説明に関しては第1の実
施態様に関する説明がそのまま参照される。第1の実施
態様とは異なり,図2に示す第2の実施態様において
は,二次空気ポンプ20の下流側に分離モジュール70
が設けられている。室内に設けられた,酸素分子に対し
てのみ透過可能な膜を含むこの分離モジュール70によ
り,吹込みのために必要な酸素がリッチ化された空気が
車両上で,しかも二次空気ブロア20を起動している間
のみ発生される。このようにして,二次空気ブロアが起
動されているときは常に,二次空気の酸素のリッチ化も
また同時に達成される。
In the second embodiment shown in FIG. 2, the same elements as those of the first embodiment are denoted by the same reference numerals, and therefore, the description of the first embodiment will be omitted. It is referred to as it is. In contrast to the first embodiment, in the second embodiment shown in FIG.
Is provided. By means of this separation module 70 which is provided in the room and comprises a membrane which is permeable only to oxygen molecules, the oxygen-enriched air required for blowing can be supplied to the vehicle and the secondary air blower 20 Only fired during startup. In this way, whenever the secondary air blower is activated, the oxygen enrichment of the secondary air is also achieved at the same time.

【0027】図3に示されている実施態様は,図2に示
されている実施態様とは,分離モジュール70の下流側
に圧力タンク80が設けられていることが異なり,この
圧力タンク80内に,後の運転サイクルにおいて,たと
えば内燃機関の低温始動過程において排気ガスに供給可
能なように,分離モジュール70により発生された,二
次空気がリッチ化された二次空気が中間貯蔵される。こ
の場合,二次空気ポンプは,二次空気の吹込みを全く必
要としない運転状態において起動されることは有利であ
る。二次空気ポンプは連続運転で使用されてもよい。
The embodiment shown in FIG. 3 is different from the embodiment shown in FIG. 2 in that a pressure tank 80 is provided on the downstream side of the separation module 70. In a later operating cycle, the secondary air enriched in the secondary air generated by the separation module 70 is temporarily stored so that it can be supplied to the exhaust gas, for example, during the cold start of the internal combustion engine. In this case, it is advantageous for the secondary air pump to be started in an operating state in which no secondary air is required. The secondary air pump may be used in continuous operation.

【0028】二次空気ポンプは,たとえば惰行運転にお
いてまたは自動車のブレーキ作動において過剰エネルギ
ーを有する運転サイクルにおいて起動されることが有利
である。これにより,とくに,酸素がリッチ化された空
気を発生するための燃料の多量消費が回避される。二次
空気吹込みは,二次空気ポンプを運転することなく二次
空気吹込弁30を介して制御しながら行ってもよい。酸
素がリッチ化された吹込空気を分離モジュール70内で
発生するために,種々のタイプの膜が使用可能である。
[0028] The secondary air pump is advantageously started in a driving cycle with excess energy, for example in coasting operation or in the braking of a motor vehicle. This avoids, in particular, the large consumption of fuel for generating oxygen-enriched air. The secondary air injection may be performed while operating via the secondary air injection valve 30 without operating the secondary air pump. Various types of membranes can be used to generate oxygen-enriched blowing air in the separation module 70.

【0029】たとえば二酸化ジルコニウム(ZrO2
からなるセラミック膜またはペロブスキー石(Pero
vskit)からなるセラミック膜が使用されてもよ
い。
For example, zirconium dioxide (ZrO 2 )
Ceramic membrane or perovski stone (Pero)
vskit) may be used.

【0030】二酸化ジルコニウムの場合,周囲空気から
の酸素の取得は,外部導体接続を介して膜の両側の間の
電流流れにより得られる,膜にかかる電圧差により行わ
れる。この場合,電圧を介してとくに追加の機械的ポン
プ仕事なしに,このようにして得られた酸素(O2)の
濃縮が達成される。この場合,電圧によりきわめて高い
圧力(>1020バール)を設定できるので,圧力タンク
80を充填するための追加の圧縮機は全く必要としな
い。
In the case of zirconium dioxide, the acquisition of oxygen from the surrounding air is effected by the voltage difference across the membrane, which is obtained by the current flow between the two sides of the membrane via an external conductor connection. In this case, the enrichment of the oxygen (O 2 ) thus obtained is achieved via the voltage, in particular without additional mechanical pumping work. In this case, no extra compressor is required to fill the pressure tank 80, since the voltage can set very high pressures (> 10 20 bar).

【0031】混合物透過性セラミック膜たとえばペロブ
スキー石(Perovskit)膜においては,膜を介
しての発生すべき酸素分圧降下が駆動力として働く。こ
の駆動力は二次空気ポンプ20により発生してもよい。
In a mixture permeable ceramic membrane, such as a Perovskiite membrane, the oxygen partial pressure drop to be generated through the membrane acts as a driving force. This driving force may be generated by the secondary air pump 20.

【0032】二酸化ジルコニウム膜のみでなく混合物透
過性膜もまた高温(>400°C)においてはじめて経
済的な使用に対して意味のある透過係数を示すので,こ
のような膜の加熱を簡単な方法で可能にするために,分
離モジュールはできるだけ排気管50の近くにまたは排
気管50内に設けられる。
The heating of such zirconium dioxide membranes, as well as the mixture permeable membranes, only at high temperatures (> 400 ° C.) has meaningful transmission coefficients for economical use, so that heating such membranes is a simple process. The separation module is provided as close to or within the exhaust pipe 50 as possible.

【0033】さらに,酸素のリッチ化はプラスチック膜
たとえばポリマー膜により達成することができる。この
ようなポリマー膜により40容積%以下の酸素含有量を
達成することができる。ポリマー膜を有する分離モジュ
ール70を作動させるために,分圧降下を発生させるた
めのポンプ仕事ないし圧縮仕事の形の機械的分離動力が
必要である。このポンプ仕事および圧縮仕事はたとえば
ポンプ/圧縮機とブレーキとの適切な結合によりブレー
キ作動の間に低下すべき運動エネルギーを利用して発生
してもよい。さらに,圧力降下を発生するために二次空
気ポンプ20を使用してもよい。
Furthermore, enrichment of oxygen can be achieved by a plastic film, for example, a polymer film. With such a polymer membrane, an oxygen content of 40% by volume or less can be achieved. In order to operate the separation module 70 with a polymer membrane, mechanical separation power in the form of a pumping or compression work for generating a partial pressure drop is required. This pumping and compression work may be generated, for example, by using the kinetic energy to be reduced during braking by a suitable coupling of the pump / compressor and the brake. Further, a secondary air pump 20 may be used to create a pressure drop.

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

【図1】本発明による排気ガス触媒を備えた内燃機関か
らの燃焼排気ガス内の有害物質の低減装置の第1の実施
態様の部分切取図である。
FIG. 1 is a partial cutaway view of a first embodiment of a device for reducing harmful substances in combustion exhaust gas from an internal combustion engine provided with an exhaust gas catalyst according to the present invention.

【図2】本発明による排気ガス触媒を備えた内燃機関か
らの燃焼排気ガス内の有害物質の低減装置の第2の実施
態様の部分切取図である。
FIG. 2 is a partial cutaway view of a second embodiment of the apparatus for reducing harmful substances in combustion exhaust gas from an internal combustion engine provided with an exhaust gas catalyst according to the present invention.

【図3】本発明による排気ガス触媒を備えた内燃機関か
らの燃焼排気ガス内の有害物質の低減装置の第3の実施
態様の部分切取図である。
FIG. 3 is a partial cutaway view of a third embodiment of the apparatus for reducing harmful substances in combustion exhaust gas from an internal combustion engine provided with an exhaust gas catalyst according to the present invention.

【符号の説明】[Explanation of symbols]

10 内燃機関 20 二次空気ポンプ 22 酸素がリッチ化された周囲空気 30 二次空気吹込弁 40 配管 50 排気管 52 排気ガス触媒 70 膜 80 圧力タンク DESCRIPTION OF SYMBOLS 10 Internal combustion engine 20 Secondary air pump 22 Ambient air enriched with oxygen 30 Secondary air injection valve 40 Piping 50 Exhaust pipe 52 Exhaust gas catalyst 70 Membrane 80 Pressure tank

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F01N 3/24 ZAB F01N 3/24 ZABF (72)発明者 シュテフェン・フランケ ドイツ連邦共和国 71701 シュヴィーベ ルディンゲン,ダンツィガー・シュトラー セ 2 (72)発明者 ホルスト・ハルンドルフ ドイツ連邦共和国 71701 シュヴィーベ ルディンゲン,アオエンヴェーク 25──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI F01N 3/24 ZAB F01N 3/24 ZABF (72) Inventor Steffen Franke Germany 71701 Schwiebbe Rudingen, Danziger Straße 2 (72 ) Inventor Horst Harndorf, Germany 71701 Schwiebe Rudingen, Aoenweg 25

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 内燃機関(10)の排気ガスに内燃機関
(10)の運転状態の関数として二次空気ポンプ(2
0)により二次空気が供給される,排気ガス触媒(5
2)を備えた内燃機関(10)とくに自動車からの燃焼
排気ガス内の有害物質の低減方法において,供給される
二次空気の酸素(O2)含有量が上昇されることを特徴
とする排気ガス触媒を備えた内燃機関からの燃焼排気ガ
ス内の有害物質の低減方法。
An exhaust gas of an internal combustion engine (10) is supplied to a secondary air pump (2) as a function of an operating state of the internal combustion engine (10).
0), secondary air is supplied by the exhaust gas catalyst (5
In the method for reducing harmful substances in combustion exhaust gas from an internal combustion engine (10), particularly from an automobile, the oxygen (O 2 ) content of the supplied secondary air is increased. A method for reducing harmful substances in combustion exhaust gas from an internal combustion engine provided with a gas catalyst.
【請求項2】 O2含有量を上昇するために,二次空気
が,室内に設けられた,酸素分子に対してのみ透過可能
な膜(分離モジュール70)を通過して供給されること
を特徴とする請求項1の方法。
2. In order to increase the O 2 content, secondary air is supplied through a membrane (separation module 70) provided only in the chamber and permeable only to oxygen molecules. The method of claim 1 wherein the method comprises:
【請求項3】 O2がリッチ化された二次空気が,内燃
機関(10)の排気ガスに混入される前にまず圧力タン
ク(80)内に中間貯蔵され,後の運転サイクルにおい
て運転状態の関数として排気ガスに供給されることを特
徴とする請求項1または2の方法。
3. The secondary air enriched in O 2 is first intermediately stored in a pressure tank (80) before being mixed with exhaust gas of an internal combustion engine (10), and the operating state is determined in a subsequent operation cycle. 3. The method according to claim 1, wherein the exhaust gas is supplied as a function of the exhaust gas.
【請求項4】 前記膜において必要な分圧降下が二次空
気ポンプ(20)により発生されることを特徴とする請
求項1ないし3のいずれかの方法。
4. The method as claimed in claim 1, wherein the required partial pressure drop in the membrane is generated by a secondary air pump (20).
【請求項5】 排気ガス触媒(52)の手前で内燃機関
(10)の排気ガスに内燃機関(10)の運転状態の関
数として二次空気ポンプ(20)により二次空気が供給
される前記二次空気ポンプ(20)を含む,排気ガス触
媒(52)を備えた内燃機関(10)とくに自動車から
の燃焼排気ガス内の有害物質の低減装置において,供給
される二次空気の酸素(O2)のリッチ化を可能にする
手段が設けられていることを特徴とする排気ガス触媒を
備えた内燃機関からの燃焼排気ガス内の有害物質の低減
装置。
5. The exhaust gas of the internal combustion engine (10) is supplied with secondary air by a secondary air pump (20) as a function of the operating state of the internal combustion engine (10) before the exhaust gas catalyst (52). In an internal combustion engine (10) equipped with an exhaust gas catalyst (52) including a secondary air pump (20), particularly in a device for reducing harmful substances in combustion exhaust gas from automobiles, the oxygen (O 2 ) A device for reducing harmful substances in combustion exhaust gas from an internal combustion engine equipped with an exhaust gas catalyst, wherein the device is provided with means for enabling the enrichment of 2 ).
【請求項6】 前記手段が,室内に設けられた,酸素分
子に対してのみ透過可能な少なくとも1つの膜(分離モ
ジュール70)を含むことを特徴とする請求項5の装
置。
6. The apparatus according to claim 5, wherein said means comprises at least one membrane (separation module 70) provided in the chamber and permeable only to oxygen molecules.
【請求項7】 前記分離モジュール(70)が前記二次
空気ポンプ(20)の下流側に設けられていることを特
徴とする請求項5または6の装置。
7. Apparatus according to claim 5, wherein the separation module is provided downstream of the secondary air pump.
【請求項8】 O2がリッチ化された二次空気を一時的
に貯蔵可能な圧力タンク(80)が分離モジュール(7
0)の下流側に設けられていることを特徴とする請求項
5ないし7のいずれかの装置。
8. A pressure tank (80) capable of temporarily storing O 2 -enriched secondary air is provided in a separation module (7).
The apparatus according to any one of claims 5 to 7, wherein the apparatus is provided downstream of (0).
JP10002281A 1997-03-15 1998-01-08 Reducing method of hazardous substance in exhaust gas from internal combustion engine provided with exhaust catalyst and device thereof Pending JPH10252452A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19710841.5 1997-03-15
DE19710841A DE19710841A1 (en) 1997-03-15 1997-03-15 Reduction of rich pollutant emissions from vehicular engines by supply of oxidant to exhaust gases

Publications (1)

Publication Number Publication Date
JPH10252452A true JPH10252452A (en) 1998-09-22

Family

ID=7823522

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (5)

Country Link
JP (1) JPH10252452A (en)
KR (1) KR19980080272A (en)
DE (1) DE19710841A1 (en)
FR (1) FR2760654B1 (en)
IT (1) IT1298311B1 (en)

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JP2006090324A (en) * 2004-09-25 2006-04-06 Robert Bosch Gmbh Method and device for operating particle filter arranged in exhaust region of internal combustion engine

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ITMI980398A1 (en) 1999-08-27
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KR19980080272A (en) 1998-11-25
FR2760654A1 (en) 1998-09-18
IT1298311B1 (en) 1999-12-20

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