JP2003519744A - Method and apparatus for controlling desulfurization of a NOx storage catalyst disposed in an exhaust gas passage of an internal combustion engine - Google Patents

Method and apparatus for controlling desulfurization of a NOx storage catalyst disposed in an exhaust gas passage of an internal combustion engine

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Publication number
JP2003519744A
JP2003519744A JP2001551959A JP2001551959A JP2003519744A JP 2003519744 A JP2003519744 A JP 2003519744A JP 2001551959 A JP2001551959 A JP 2001551959A JP 2001551959 A JP2001551959 A JP 2001551959A JP 2003519744 A JP2003519744 A JP 2003519744A
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Prior art keywords
desulfurization
storage catalyst
activity
internal combustion
combustion engine
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JP4619603B2 (en
Inventor
ポット,エッケハルト
ハーン,ハーマン
ヒインツェ,ゼーレン
ツィルマー,ミカエル
ラング,アクセル
シュルツ,フランク
ドルックハンマー,イエンズ
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フォルクスワーゲン・アクチェンゲゼルシャフト
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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
    • F01N3/0807Exhaust 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
    • F01N3/0885Regeneration of deteriorated absorbents or adsorbents, e.g. desulfurization of NOx traps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/021Introducing corrections for particular conditions exterior to the engine
    • F02D41/0235Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/021Introducing corrections for particular conditions exterior to the engine
    • F02D41/0235Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
    • F02D41/027Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to purge or regenerate the exhaust gas treating apparatus
    • F02D41/0275Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to purge or regenerate the exhaust gas treating apparatus the exhaust gas treating apparatus being a NOx trap or adsorbent
    • F02D41/028Desulfurisation of NOx traps or adsorbent
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/146Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/146Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration
    • F02D41/1463Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration of the exhaust gases downstream of exhaust gas treatment apparatus
    • 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
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/04Sulfur or sulfur oxides
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D2200/00Input parameters for engine control
    • F02D2200/02Input parameters for engine control the parameters being related to the engine
    • F02D2200/08Exhaust gas treatment apparatus parameters
    • F02D2200/0811NOx storage efficiency

Abstract

(57)【要約】 本発明はNO貯蔵触媒の下流に配設され、排気ガス中のNO濃度に依存して信号を送る少なくとも1個のNOゾンデを使用して、内燃機関の排気ガス通路に配設されたNO貯蔵触媒の脱硫を制御するための方法及び装置に関する。NO貯蔵触媒(18)の下流で測定されたNOX濃度からNO貯蔵触媒(18)のNOX活性(NOA)を決定し、NO貯蔵触媒(18)のNOX活性(NOA)の所定の閾値(SW)を下回るときは、所定の脱硫パラメータにより脱硫を開始し、脱硫成績に基づいてNO貯蔵触媒(18)の不可逆的劣化を決定し、所定の劣化限界値(SWIR)を超えるときは強力脱硫を開始し、その場合高い脱硫効果に相当する少なくとも1つの脱硫パラメータが選択され、内燃機関10のその後の運転を、強力脱硫の後に回復したNOX初期活性(NOAMX)の高さに依存させる。 (57) Abstract: The present invention is disposed downstream of the NO X storage catalyst, using at least one of the NO X sonde depending on the concentration of NO X in the exhaust gas and sends a signal, the exhaust gas of the internal combustion engine The present invention relates to a method and an apparatus for controlling the desulfurization of a NO X storage catalyst disposed in a gas passage. NO X storage catalyst (18) the NO X storage NO X catalyst activity (18) (NOA) were determined from the NO X concentration measured downstream of, NO X storage NO X catalyst activity (18) of (NOA) when below a predetermined threshold value (SW), to start the desulfurization by a predetermined desulfurization parameters, based on the desulfurization performance to determine the irreversible deterioration of the NO X storage catalyst (18), a predetermined degradation limit (SW IR) the initiates a strong desulfurization when more than at least one of desulfurization parameters are selected corresponding to the case high desulfurizing effect, the subsequent operation of the internal combustion engine 10, the recovered NO X initial activity after a strong desulfurization (NOAMX) Depend on height.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】 本発明は独立請求項1及び13で挙げた特徴を有する、内燃機関の排気ガス通
路に配設されたNO貯蔵触媒の脱硫の制御のための方法及び装置に関する。
The present invention relates to a method and a device for controlling the desulfurization of a NO X storage catalyst arranged in the exhaust gas passage of an internal combustion engine, having the features recited in independent claims 1 and 13.

【0002】 少なくとも一時的に希薄燃焼運転モードで運転される内燃機関の排気ガスをN
貯蔵触媒の助けにより運転する後処理が知られている。その際、希薄燃焼運
転モード時に、この段階で窒素酸化物NOxは、還元性排気ガス成分例えば一酸
化炭素又は未燃焼炭化水素に比して排気ガス中に過量で存在し、従って、NO 貯蔵触媒は、完全に転化されない窒素酸化物NOXを硝酸塩の形で貯蔵する。N
Ox貯蔵能力が低下した場合には、規則的間隔で、貯蔵触媒にNOX再生が行わ
れる。そのために貯蔵触媒にリッチな排気ガス雰囲気を送り込み、最低触媒温度
を調整する。
The exhaust gas of an internal combustion engine that is operated in a lean burn operation mode at least temporarily is
O X aftertreatment be operated with the aid of the storage catalyst is known. At this time, the lean-burn operation mode, the nitrogen oxides NOx in this stage is present in excess in the exhaust gas as compared with the reducing exhaust gas components such as carbon monoxide or unburned hydrocarbons, thus, NO X storage catalyst, the fully not converted nitrogen oxides nO X stored in the form of nitrates. N
When the Ox storage capacity is lowered, at regular intervals, NO X regeneration is performed in the storage catalyst. Therefore, a rich exhaust gas atmosphere is sent to the storage catalyst to adjust the minimum catalyst temperature.

【0003】 NO貯蔵触媒ではNOXの吸収のほかに、硫黄酸化物の望ましくない蓄積が
起こる。硫黄の蓄積はNOX再生の条件下で不可逆的であるから、貯蔵触媒の硫
化が増加し、NO貯蔵能力が低下する。したがって、硫黄の凝集が硫酸塩粒子
の形成を招き、NO貯蔵触媒の触媒活性を不可逆的に劣化する恐れがある。こ
のような硫酸塩粒子の除去は粒子の大きさが増すにつれてますます難しくなる。
そこで規則的間隔でNO貯蔵触媒の脱硫を行い、その際650℃を超える触媒
温度でリッチな排気ガス雰囲気を送り込んで、蓄積された硫黄を主として二酸化
硫黄SO2及び硫化水素H2Sの形で排出することが知られている。
In addition to the absorption of NO X , NO X storage catalysts also have an undesired accumulation of sulfur oxides. Since the accumulation of sulfur is irreversible under the conditions of the NO X regeneration, sulfide increased the storage catalyst, NO X storage capacity is lowered. Therefore, the aggregation of sulfur may lead to the formation of sulfate particles, which may irreversibly deteriorate the catalytic activity of the NO X storage catalyst. Removal of such sulfate particles becomes increasingly difficult as the particle size increases.
Therefore, the NO X storage catalyst is desulfurized at regular intervals, at which time a rich exhaust gas atmosphere is fed at a catalyst temperature of over 650 ° C, and the accumulated sulfur is mainly formed into sulfur dioxide SO 2 and hydrogen sulfide H 2 S. It is known to be discharged in.

【0004】 硫酸塩粒子の形成による不可逆的な劣化のほかに、触媒の貯蔵能力の低下を招
くその他の恒久的な種類の劣化が知られている。この場合第一に重要なのは熱的
劣化である。
In addition to irreversible degradation due to the formation of sulfate particles, other permanent types of degradation leading to a loss of storage capacity of the catalyst are known. In this case, thermal degradation is of primary importance.

【0005】 本発明の根底にあるのは、NO貯蔵触媒の不可逆的劣化を識別し、追跡する
ことができるNO貯蔵触媒の脱硫の制御方法を提案するという課題である。
[0005] Underlying the present invention is to identify the irreversible deterioration of the NO X storage catalyst, a problem is proposed a method for controlling the desulphurization of the NO X storage catalyst which can be tracked.

【0006】 本発明に基づきこの課題は独立請求項に挙げた特徴を有する、NO貯蔵触媒
の脱硫の制御のための方法及び装置によって解決される。本発明方法によればN
貯蔵触媒の下流で測定されたNO濃度からNO貯蔵触媒のNOX貯蔵活
性を決定し、NO貯蔵触媒のNO活性が所定の閾値を下回るときは、所定の
脱硫パラメータにより脱硫を開始する。また脱硫成績に基づきNO貯蔵触媒の
不可逆的劣化を追跡し、所定の劣化限界値を超えるときは強力な脱硫を開始し、
その際高い脱硫効果に相当する少なくとも1つの脱硫パラメータが選定され、内
燃機関の以後の運転を強力脱硫の後に回復したNO活性の高さに依存させる。
たとえ、先行する標準脱硫が不完全に終わった場合でも、強力脱硫の実施は定量
的硫黄排出を可能にする。こうして強力脱硫の後に回復したNOX貯蔵活性を、
NO貯蔵触媒の現在の不可逆的劣化に直接相関させることができる。その結果
NO貯蔵触媒のもはや許容されない恒久的な劣化を識別することができる。
According to the invention, this problem is solved by a method and a device for controlling the desulfurization of NO X storage catalysts having the features recited in the independent claims. According to the method of the present invention, N
O X determine the NO X storage activity of the NO X storage catalyst from NO X concentration measured downstream of the storage catalyst, when the NO X activity of the NO X storage catalyst falls below a predetermined threshold, desulfurization by a predetermined desulfurization parameters To start. Also, irreversible deterioration of the NO X storage catalyst is tracked based on the desulfurization performance, and when the predetermined deterioration limit value is exceeded, strong desulfurization is started,
At least one desulfurization parameter corresponding to a high desulfurization effect is then selected, which makes the subsequent operation of the internal combustion engine dependent on the high NO X activity recovered after strong desulfurization.
Even if the preceding standard desulfurization is incomplete, the implementation of heavy desulfurization allows quantitative sulfur emissions. Thus, the NO x storage activity recovered after strong desulfurization is
It can be directly correlated to the current irreversible deterioration of the NO X storage catalyst. As a result, permanent deterioration of the NO X storage catalyst which is no longer acceptable can be identified.

【0007】 本発明によれば劣化限界値の設定のための種々の変法が可能である。好ましい
実施形態では、閾値は脱硫の終了後に回復したNO貯蔵触媒のNO初期活性
に比例するように、脱硫のつど設定され、これを下回ると脱硫が起動される。こ
の場合劣化限界値はNOX貯蔵活性の下回ってはならない最低限界値であり、閾
値は劣化限界値より大きい。代替実施形態によれば、下回ると脱硫を起動する閾
値は不変である。この変法では触媒の不可逆的劣化が増すにつれて脱硫頻度が増
加するから、劣化限界値として所定の最大脱硫頻度が利用される。閾値も同じく
一定である別の代替実施形態では、劣化限界値は脱硫後に回復したNO初期活
性の下限とされる。
According to the invention, various variants are possible for setting the deterioration limit value. In a preferred embodiment, the threshold to be proportional to the NO X initial activity of the NO X storage catalyst recovered after the end of the desulfurization, is set each time the desulfurization, the desulfurization is activated below which. In this case, the deterioration limit value is the lowest limit value that must not be lower than the NO X storage activity, and the threshold value is larger than the deterioration limit value. According to an alternative embodiment, the threshold below which desulfurization is triggered remains unchanged. In this modified method, the desulfurization frequency increases as the irreversible deterioration of the catalyst increases, so a predetermined maximum desulfurization frequency is used as the deterioration limit value. Threshold in another alternative embodiment which is also a constant, degradation limit is the lower limit of the NO X initial activity was recovered after desulfurization.

【0008】 脱硫、特に強力脱硫の実施は高い燃料消費を伴い、場合によっては車両の運転
挙動に影響することがある。従っていかなる運転状況でも脱硫の開始が望ましい
という訳ではない。そこで本方法の有利な実施形態は、劣化限界値を超えたとき
にまず内燃機関の希薄燃焼運転を禁止し、適当な所定の周辺条件が存在するとき
に初めて強力脱硫を開始する。この周辺条件は例えばNO貯蔵触媒の最低温度
及び/又は最小時間のあいだ順守する最低車速である。
The implementation of desulfurization, in particular heavy desulfurization, is associated with high fuel consumption and in some cases can influence the driving behavior of the vehicle. Therefore, it is not desirable to start desulfurization under any operating conditions. Thus, an advantageous embodiment of the method first inhibits lean burn operation of the internal combustion engine when the deterioration threshold is exceeded and only initiates strong desulfurization when suitable predetermined ambient conditions are present. The boundary conditions is the lowest speed for compliance between the minimum temperature and / or minimum time eg NO X storage catalyst.

【0009】 本発明に係る方法は、強力脱硫の後に内燃機関のさらなる運転を脱硫成績、即
ち脱硫後に回復したNOX初期活性の高さに依存させるものである。好ましい実
施形態は、強力脱硫の終了後に回復したNO初期活性がほぼ完全に又は少なく
とも硫黄とNOXのない無傷のNO貯蔵触媒の所定の範囲で適合するならば、
内燃機関の希薄燃焼運転が引き続き許容されるように構成されている。この場合
、つまり強力脱硫の前に観察されたNOX貯蔵活性の損失が硫黄の蓄積即ち不完
全に終わった先行の脱硫に原因し、NO貯蔵触媒の不可逆的劣化によるもので
ないからである。従って有効な強力脱硫処理の後は、さらに後続の脱硫が効果的
に行われるように脱硫パラメータを適応させることが好ましい。
[0009] The method of the present invention are those which depend a further operation of the internal combustion engine after a strong desulfurization desulfurization performance, i.e. the height of the NO X initial activity was recovered after desulfurization. A preferred embodiment is that if the NO X initial activity recovered after the end of the strong desulfurization is nearly complete or at least within a given range of sulfur and NO X- free intact NO X storage catalysts.
The lean-burn operation of the internal combustion engine is configured to continue to be permitted. In this case, that is, loss of the observed NO X storage activity prior strong desulfurized cause desulfurization of the preceding ended in accumulation i.e. incomplete sulfur, because not due irreversible deterioration of the NO X storage catalyst. Therefore, it is preferable to adjust the desulfurization parameters so that the subsequent desulfurization is effectively performed after the effective strong desulfurization treatment.

【0010】 これに対して強力脱硫がほとんど効果がなく、回復したNOX初期活性が最後
の脱硫の後のNO初期活性よりさほど高くないならば、NO貯蔵触媒の激し
い不可逆的劣化が推定され、NOX放出を少なくするために、内燃機関の希薄燃
焼運転が制限又は遮断される。また警報表示器により車両運転者に触媒の保守の
必要性を知らせることも考えられる。
On the other hand, if the strong desulfurization has little effect and the recovered NO x initial activity is not much higher than the NO x initial activity after the last desulfurization, a severe irreversible deterioration of the NO x storage catalyst is presumed. Therefore, the lean burn operation of the internal combustion engine is limited or cut off in order to reduce NO X emission. It is also conceivable to inform the vehicle driver of the necessity of catalyst maintenance by an alarm indicator.

【0011】 また装置はNO貯蔵触媒の脱硫処理の制御手順がデジタル形式で保存された
手段、例えば制御ユニットを具備するように構成することが好ましい。このよう
な制御ユニットはたいてい現存するエンジン制御装置に組込むことが好ましい。
It is also preferable that the apparatus is configured to include means, for example, a control unit, in which the control procedure of the desulfurization treatment of the NO X storage catalyst is stored in digital form. Such control units are often preferably incorporated into existing engine control systems.

【0012】 本発明のその他の好適な実施形態は従属請求項に挙げたその他の特徴で明らか
である。
Other preferred embodiments of the invention are apparent from the other features recited in the dependent claims.

【0013】 次に本発明の実施例を付属する図面に基づき詳述する。[0013]   Next, embodiments of the present invention will be described in detail with reference to the accompanying drawings.

【0014】 図1は内燃機関10及び後置された排気ガス系統12の概要を示す。排気ガス
系統12の排気ガス通路14に予備触媒16とNO貯蔵触媒18が配設されて
いる。また排気ガス通路14は選択された運転パラメータの検出のための種々の
計器を内蔵する。例えばガスゾンデ20、22は排気ガス中のガス成分の濃度を
検出する。本例ではラムダゾンデとして設計されたガスゾンデ20が内燃機関1
0の後方かつ触媒部品16、18の手前の酸素分の検出のために使用され、一方
、NOXゾンデ22はNO貯蔵触媒18の後方のNO濃度を測定する。NO
貯蔵触媒18の前後に配設された温度ゾンデ24、26は触媒温度の検出のた
めに使用される。代案として一方又は両方の温度ゾンデ24、26を廃止し、N
貯蔵触媒の温度を経験的に導き出すこともできる。ガスゾンデ20、22及
び温度ゾンデ24、26が検出したすべての信号は、エンジン制御装置28に入
力され、そこでまずデジタル化され、その上で内燃機関10の運転モードの制御
のためにさらに処理される。このためにエンジン制御装置28は例えば吸気管3
2のスロットル弁30の位置及び/又は排気ガス返送装置34を調節することに
よって、内燃機関10に供給される空燃混合気を調整する。例示した操作部30
、34によって例えば内燃機関10のリーン又はリッチモードを調整することが
できる。
[0014]   FIG. 1 shows an outline of an internal combustion engine 10 and an exhaust gas system 12 which is installed downstream. Exhaust gas
Pre-catalyst 16 and NO in the exhaust gas passage 14 of the system 12XWith the storage catalyst 18
There is. In addition, the exhaust gas passage 14 is provided with various types of exhaust gas for detecting selected operating parameters.
Built-in instrument. For example, gas sondes 20 and 22 show the concentration of gas components in exhaust gas.
To detect. In this example, a gas sonde 20 designed as a lambda sonde is an internal combustion engine 1
Used for the detection of oxygen content behind 0 and in front of the catalytic components 16, 18, while
, NOXSonde 22 is NOXNO behind storage catalyst 18XMeasure the concentration. NO
XTemperature probes 24 and 26 arranged before and after the storage catalyst 18 detect the catalyst temperature.
Used for As an alternative, one or both of the temperature sondes 24 and 26 may be eliminated and N
OXIt is also possible to empirically derive the temperature of the storage catalyst. Gassonde 20, 22 and
All signals detected by the temperature probe and temperature sonde 24, 26 enter the engine controller 28.
Input, where it is first digitized and then the operating mode of the internal combustion engine 10 is controlled.
Is further processed for. For this purpose, the engine control unit 28 is provided with, for example, the intake pipe 3
To adjust the position of the second throttle valve 30 and / or the exhaust gas return device 34.
Therefore, the air-fuel mixture supplied to the internal combustion engine 10 is adjusted. Illustrated operation unit 30
, 34 for adjusting the lean or rich mode of the internal combustion engine 10, for example.
it can.

【0015】 また下記で詳述するNO貯蔵触媒の脱硫の制御手順を格納した制御ユニット
36がエンジン制御装置28に組込まれている。代わりに、制御ユニット36を
エンジン制御装置28から独立に実現することもできる。
A control unit 36, which stores a desulfurization control procedure for the NO X storage catalyst, which will be described in detail below, is incorporated in the engine control device 28. Alternatively, the control unit 36 can be realized independently of the engine control 28.

【0016】 図2はNO貯蔵触媒18の相対NO活性NOArelの時間的経過を示す。
その際、相対NO活性NOArelはこのNO貯蔵触媒18のNO活性NO
Aと、NOXと硫黄のない無傷のNO貯蔵触媒のNO活性との比を表す。こ
の場合NO活性NOA自体はNO貯蔵触媒18の後方でNOXゾンデ22が
測定したNO濃度とNO貯蔵触媒18の前方のNO濃度の比と定義される
。NO貯蔵触媒18の前方のNO濃度即ちNOX粗放出は、とりわけエンジ
ン制御装置28により内燃機関10の実際運転パラメータに基づいて算定される
。代わりに、NO貯蔵触媒18の前方の排気ガス系統14に配設されたNO ゾンデで測定することもできる。NO活性NOA又は相対NO活性NOAre l の計算はエンジン制御装置28で行なわれる。エンジン制御装置28にはNO
及び硫黄を含まない無傷のNO貯蔵触媒のNO活性NOAも記憶されてい
る。車両運転の初めにNO貯蔵触媒18は新鮮な触媒と同様なNO活性NO
Aを有するから、相対NO活性NOArelは差当り“1”に近い値をとる。そ
の後の過程で触媒18の硫化が増加するから、相対NO活性NOArelが次第
に低下する。相対NO活性の最初の閾値SWを下回ると、時点t1でNO
蔵触媒18の最初の脱硫が起動される。所定の脱硫パラメータに従って脱硫に必
要な最低触媒温度が調整され、内燃機関10は所定の又は調整された脱硫時間の
あいだ空気過剰率リッチ設定に相当するリッチ運転モードで運転される。H2
放出を抑制するために、脱硫をリッチ・リーン・インターバルで操作することが
知られている。この場合補助脱硫パラメータとして例えば各インターバルのリッ
チ・リーン空気過剰率設定、切換え頻度又はNO貯蔵触媒18の後方のリッチ
・リーン切換え状態を設定することができる。脱硫40の終了後に回復した相対
NO初期活性NOAMXに従って、閾値SWの位置を新たに制御ユニット36
によって確定する。その場合閾値SWは回復したNO初期活性NOAMXに比
例することが好ましい。脱硫終了後のNO初期活性NOAMXは、運転時間t
の進行につれて新鮮なNO貯蔵触媒に次第に対応しなくなり、触媒の老化とと
もに低下する。その原因は例えばNO貯蔵触媒18の不完全な脱硫及び/又は
不可逆的な熱的劣化である。NO初期活性NOAMXの低下の結果、それを下
回れば脱硫が開始される閾値SWがますます低下する。時点t5にNOX活性NO
Aが、下回ってはならない下限値、劣化限界値SWIRに到達するまで、硫化38
と脱硫40のサイクルが繰返される。劣化限界値SWIRを下回ると、NO放出
を少なくするために、まず内燃機関10がリーン運転モードから化学量論的又は
リッチ運転モードに切換えられる。所定の周辺条件、例えばNO貯蔵触媒18
の最低温度及び/又は最小時間のあいだ順守する最低車速が現われたときに、初
めて強力脱硫を開始することが好ましい。エネルギー的に極めて問題が多い強力
脱硫のための燃料消費をこうして比較的少なくすることができる。強力脱硫42
は先行する脱硫40と比較して、上記の脱硫パラメータ(例えば触媒温度、空気
過剰率、時間設定)の少なくとも1つが高い脱硫効果に対応するように選定され
ることが相違する。例えば強力脱硫42のために長い脱硫時間及び/又は低い空
気過剰率リッチ設定を指定することができる。
[0016]   2 is NOXRelative NO of storage catalyst 18XActive NOArelShows the time course of.
At that time, relative NOXActive NOArelIs this NOXNO of storage catalyst 18XActive NO
A and NOXAnd intact NO without sulfurXNO of storage catalystXRepresents the ratio to activity. This
If NOXActive NOA itself is NOXNO behind the storage catalyst 18XSonde 22
Measured NOXConcentration and NOXNO in front of the storage catalyst 18XDefined as the ratio of concentrations
. NOXNO in front of the storage catalyst 18XConcentration ie NOXCoarse emission is especially
Calculated by the engine control device 28 based on actual operating parameters of the internal combustion engine 10.
. Instead, NOXNO disposed in the exhaust gas system 14 in front of the storage catalyst 18X It can also be measured with a sonde. NOXActive NOA or relative NOXActive NOAre l Is calculated by the engine control unit 28. NO for the engine control unit 28
XAnd intact NO containing no sulfurXNO of storage catalystXActive NOA is also remembered
It NO at the beginning of vehicle operationXThe storage catalyst 18 has the same NO as the fresh catalyst.XActive NO
Relative NO because it has AXActive NOArelTakes a value close to "1" per difference. So
Since the sulfurization of the catalyst 18 increases in the later process, the relative NOXActive NOArelDepends on
Fall to. Relative NOXBelow the initial activation threshold SW, time t1And NOXSavings
The first desulfurization of the stored catalyst 18 is started. Required for desulfurization according to prescribed desulfurization parameters
The required minimum catalyst temperature is adjusted so that the internal combustion engine 10 has a predetermined or adjusted desulfurization time.
Meanwhile, the engine is operated in the rich operation mode corresponding to the excess air ratio rich setting. H2S
It is possible to operate desulfurization at rich lean intervals to control emissions.
Are known. In this case, as the auxiliary desulfurization parameter, for example, the
Chi-lean excess air ratio setting, switching frequency or NOXRich behind the storage catalyst 18
・ The lean switching state can be set. Relatives recovered after the end of desulfurization 40
NOXAccording to the initial active NOAMX, the position of the threshold value SW is newly changed to the control unit 36.
Confirm by. In that case, the threshold value SW has recovered to NO.XCompared to initial active NOAMX
It is preferable to exemplify. NO after desulfurizationXThe initial activation NOAMX is the operating time t
NO as the progress ofXIt gradually becomes less compatible with stored catalysts,
It will decrease. The cause is NO, for example.XIncomplete desulfurization and / or storage catalyst 18
It is irreversible thermal deterioration. NOXAs a result of the decrease in initial active NOAMX,
If it turns, the threshold value SW at which desulfurization starts is further decreased. Time tFiveNOXActive NO
A is a lower limit value that must not fall below, deterioration limit value SWIRUntil it reaches 38
And the desulfurization 40 cycle is repeated. Deterioration limit value SWIRBelow, NOXrelease
First, the internal combustion engine 10 is changed from the lean operation mode to the stoichiometric or
It is switched to the rich operation mode. Predetermined peripheral conditions, such as NOXStorage catalyst 18
When the lowest vehicle speed that complies with the minimum temperature and / or the minimum time of
It is preferable to start strong desulfurization. Powerful with enormous energy problems
Fuel consumption for desulfurization can thus be relatively low. Strong desulfurization 42
Compared to the preceding desulfurization 40, the desulfurization parameters described above (eg catalyst temperature, air
At least one of (excess ratio, time setting) is selected to correspond to a high desulfurization effect.
Is different. Long desulfurization time and / or low emptyness due to high strength desulfurization 42, for example.
You can specify the overkill rich setting.

【0017】 NO貯蔵触媒18のこの不可逆的劣化に依存して強力脱硫の後に様々な高さ
のNO初期活性NOAMXが回復される。44で示すシナリオでは、回復され
たNO活性NOAMXは硫黄を含まない無傷の触媒にほぼ相当する。この場合
触媒18は事実上恒久的劣化がなく、先行する活性損失は不完全な先行する脱硫
40に原因すると想定することができる。シナリオ46では強力脱硫42によっ
て初期のNOX活性が完全にではなく、かなりの程度回復される。このことは触
媒の不可逆的な劣化があり、脱硫40が不完全であったことを示唆する。いずれ
のシナリオ44、46でも内燃機関10の希薄燃焼運転が引き続き許容され、回
復されるNO初期活性NOAMXに対しより下の閾値を設定することができる
。いずれの場合44、46も以後の脱硫成績の改善が期待されるように、後続の
脱硫のための脱硫パラメータを適応修正することが好ましい。NO貯蔵触媒1
8の不可逆的劣化が少なく、強力脱硫42の後の回復したNOX活性NOAが高
ければ、それだけ脱硫パラメータの修正が重要である。シナリオ48によれば、
強力脱硫42は実際上効果がなかった。従ってこの場合は貯蔵触媒18の広範な
不可逆的劣化を推定しなければならない。以後のNO放出を制止するために、
この場合は内燃機関10の希薄燃焼運転が最終的に遮断される。車両運転者に触
媒の状態を知らせ、又は必要な保守を指示する警報表示器をオプションとして設
けることもできる。
Due to this irreversible deterioration of the NO X storage catalyst 18, various heights of NO X initially active NOAMX are recovered after strong desulfurization. In the scenario shown in 44, NO X activity NOAMX the recovered corresponds substantially intact catalyst containing no sulfur. In this case, the catalyst 18 has virtually no permanent deterioration and it can be assumed that the preceding loss of activity is due to an incomplete preceding desulfurization 40. The initial of the NO X activity by a strong desulfurization 42 In scenario 46 completely Nide not be large extent recovered. This suggests that there was an irreversible deterioration of the catalyst and the desulfurization 40 was incomplete. Any lean burn operation scenarios 44,46 even the internal combustion engine 10 is subsequently permitted, can be set more thresholds below to NO X initial activity NOAMX be recovered. In either case 44 or 46, it is preferable to adaptively modify the desulfurization parameters for the subsequent desulfurization so that the subsequent improvement of the desulfurization performance is expected. NO X storage catalyst 1
Less 8 irreversible degradation of, the higher the recovered NO X activity NOA after strong desulfurization 42, it is important to fix the much desulfurization parameters. According to scenario 48,
Strong desulfurization 42 was practically ineffective. Therefore, in this case, extensive irreversible deterioration of the storage catalyst 18 must be estimated. In order to stop the subsequent NO X emission,
In this case, the lean burn operation of the internal combustion engine 10 is finally cut off. An alarm indicator may be optionally provided to inform the vehicle driver of the condition of the catalyst or to indicate necessary maintenance.

【0018】 本発明の別の好適な実施形態に相当する相対NO活性NOArelの経過を図
3に示す。この場合は全車両運転中にNOX活性NOAの閾値SWが一定に保た
れる。NO貯蔵触媒18の老化が増すにつれて、脱硫40の後に回復するNO 初期活性NOAMXが低下する。その結果内燃機関10のリーンモードでNO 貯蔵触媒18が閾値SWに到達するまで硫黄を蓄積する期間τがますます短く
なる。換言すれば、脱硫40が必要になる頻度が増加する。強力脱硫42の必要
性の認識の基準は、所定の最大脱硫頻度又は脱硫後に回復されたNO初期活性
NOAMXの下限値である。本発明のこの実施形態のその他の方法上の特徴はす
べて図2に示した特徴に相当するから、ここで改めて説明しない。
[0018]   Relative NO corresponding to another preferred embodiment of the present inventionXActive NOArelThe progress of
3 shows. In this case, NO while all vehicles are operating.XThe threshold value SW of the active NOA is kept constant
Be done. NOXNO recovers after desulfurization 40 as the aging of storage catalyst 18 increases X Initially active NOAMX decreases. As a result, NO in the lean mode of the internal combustion engine 10 X The period τ for accumulating sulfur until the storage catalyst 18 reaches the threshold value SW becomes shorter and shorter.
Become. In other words, the frequency with which desulfurization 40 is required increases. The need for strong desulfurization 42
The criterion for the recognition of sex is the specified maximum desulfurization frequency or NO recovered after desulfurization.XInitial activity
It is the lower limit of NOAMX. Other method features of this embodiment of the invention are:
Since all of them correspond to the features shown in FIG. 2, they will not be described again here.

【0019】 図4は図2に示した本方法の実施形態の説明のための流れ図を示す。手順は段
階S1で始まる。ここで内燃機関10にリーン大気、即ちラムダ値>1が送り込
まれる。段階S2では、NO貯蔵触媒18の後方でNOゾンデ22が測定し
たNO濃度に基づきNOX活性NOAの計算が行われる。段階S3でNO
蔵活性NOAが閾値SWと比較される。NO活性NOAが閾値SWより高けれ
ば、プロセスは段階S1に移行し、内燃機関10は引き続きリーンモードで運転
される。これに対して閾値SWに到達したか又はそれを下回ったことが段階S3
で確認されれば、段階4でNO活性NOAと劣化限界値SWIRの比較が行なわ
れる。劣化限界値SWIRにまだ到達していないか又は下回るならば、段階S5で
所定の脱硫パラメータにより脱硫が開始される。脱硫の終了後、回復したNO 活性NOAMXが段階S6で決定され、決定された初期活性NOAMXに応じて
閾値SWが新たに計算される。他方、段階S4でNO活性NOAが劣化限界値
SWIRに到達したか又はそれを下回ったことが確認されると、段階S7で強力脱
硫が開始される。強力脱硫の終了後段階S8で、回復したNO活性NOAMX
が所定の閾値SWMXより小さいか否かが問われる。この問いが否定されるなら
ば、段階S6でNO初期活性NOAMXに関連して新たな閾値SWの計算が行
われ、それに基づいて段階S1で希薄燃焼運転が再び許容される。ところが段階
S8で脱硫の成果が確認できなければ、段階S9で希薄燃焼運転が最終的に遮断
される。
FIG. 4 shows a flow chart for explaining the embodiment of the method shown in FIG. The procedure starts in step S1. Here, a lean atmosphere, that is, a lambda value> 1 is sent to the internal combustion engine 10. In step S2, calculating of the NO X activity NOA basis to the NO X concentration NO X sonde 22 is measured at the rear of the NO X storage catalyst 18 is performed. In step S3, the NO X storage active NOA is compared with the threshold value SW. If the NO X active NOA is higher than the threshold value SW, the process moves to step S1 and the internal combustion engine 10 is continuously operated in the lean mode. On the other hand, when the threshold value SW is reached or falls below the threshold value, step S3
If confirmed in step 4, the NO x active NOA is compared with the deterioration limit value SW IR in step 4. If the deterioration limit value SW IR has not yet been reached or falls below, the desulfurization is started in step S5 with predetermined desulfurization parameters. After the desulfurization is completed, the recovered NO X active NOAMX is determined in step S6, and the threshold value SW is newly calculated according to the determined initial active NOAMX. On the other hand, if it is confirmed in step S4 that the NO X active NOA reaches or falls below the deterioration limit value SW IR , strong desulfurization is started in step S7. NO X active NOAMX recovered in step S8 after completion of strong desulfurization
Is smaller than a predetermined threshold value SWMX. If this question is denied, a new threshold value SW is calculated in connection with the NO X initial activation NOAMX in step S6, on the basis of which the lean burn operation is again permitted in step S1. However, if the desulfurization result cannot be confirmed in step S8, the lean burn operation is finally shut off in step S9.

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

【図1】NO貯蔵触媒の脱硫の制御のための手段および排気ガス浄化設備
の原理図である。
FIG. 1 is a principle diagram of a means for controlling desulfurization of an NO X storage catalyst and an exhaust gas purification facility.

【図2】本発明の好適な実施形態に基づくNO貯蔵触媒のNO貯蔵活性
の時間的経過の図である。
FIG. 2 is a diagram of the NO X storage activity over time of a NO X storage catalyst according to a preferred embodiment of the present invention.

【図3】本発明の別の好適な実施形態に基づくNO貯蔵触媒のNO貯蔵
活性の時間的経過の図である。
FIG. 3 is a diagram of the NO X storage activity over time of a NO X storage catalyst according to another preferred embodiment of the present invention.

【図4】図2に示した実施例に基づく本発明に係る手順の流れ図である。4 is a flow chart of a procedure according to the present invention based on the embodiment shown in FIG.

【符号の説明】[Explanation of symbols]

10 内燃機関 18 NO貯蔵触媒 NOA NO活性 NOAMX NO初期活性 SW 閾値 SWIR 劣化限界値10 Internal combustion engine 18 NO X storage catalyst NOA NO X activity NOAMX NO X initial activity SW threshold SW IR deterioration limit value

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F02D 45/00 314 F02D 45/00 314Z (81)指定国 EP(AT,BE,CH,CY, DE,DK,ES,FI,FR,GB,GR,IE,I T,LU,MC,NL,PT,SE,TR),AE,A G,AL,AM,AU,AZ,BA,BB,BG,BR ,BY,BZ,CA,CN,CR,CU,CZ,DM, DZ,EE,GD,GE,GH,GM,HR,HU,I D,IL,IN,IS,JP,KE,KG,KP,KR ,KZ,LC,LK,LR,LS,LT,LV,MA, MD,MG,MK,MN,MW,MX,MZ,NO,N Z,PL,RO,RU,SD,SG,SI,SK,SL ,TJ,TM,TR,TT,TZ,UA,UG,US, UZ,VN,YU,ZA,ZW (72)発明者 ヒインツェ,ゼーレン ドイツ連邦共和国 38114 ブラウンシュ ヴァイグ,アイッヒタルシュトラーセ 4 アー. (72)発明者 ツィルマー,ミカエル ドイツ連邦共和国 ジックテ 38173 イ ム シュロトモーゲン 18 (72)発明者 ラング,アクセル ドイツ連邦共和国 38302 ウォルフェン ビュッテル,ネルケンウエグ 29 (72)発明者 シュルツ,フランク ドイツ連邦共和国 フォルドルフ 38533, ローゼンガルテン 35 (72)発明者 ドルックハンマー,イエンズ ドイツ連邦共和国 38108 ブラウンシュ ヴァイグ,ウイッヒルンシュトラーセ 47 ベー. Fターム(参考) 3G084 BA09 DA10 EA11 EB12 EC03 FA27 FA28 FA29 3G091 AA02 AA11 AB06 BA11 BA14 CB01 DA01 DA02 DB10 DB11 EA18 EA33 EA34 FB10 FB12 FC02 HA08 HA36 HA37 HA42 HB05 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F02D 45/00 314 F02D 45/00 314Z (81) Designated country EP (AT, BE, CH, CY, DE, DK, ES, FI, FR, GB, GR, IE, IT, LU, MC, NL, PT, SE, TR), AE, AG, AL, AM, AU, AZ, BA, BB, BG, BR , BY, BZ, CA, CN, CR, CU, CZ, DM, DZ, EE, GD, GE, GH, GM, HR, HU, ID, IL, IN, IS, JP, KE, KG, KP, KR, KZ, LC, LK, LR, LS, LT, LV, MA, MD, MG, MK, MN, MW, MX, MZ, NO, NZ, PL, R , RU, SD, SG, SI, SK, SL, TJ, TM, TR, TT, TZ, UA, UG, US, UZ, VN, YU, ZA, ZW (72) Inventor Hiinze, Zellen Federal Republic of Germany 38114 Braunschweig, Eichtalstraße 4 Ar. (72) Inventor Zilmer, Michael Gicte 38173, Federal Republic of Germany 18173 Im Schrotmogen 18 (72) Inventor, Lang, Axel German Republic 38302 Wolfen Buttel, Nerkenweg 29 (72) Inventor, Schulz, Frank Fordolf, Federal Republic of Germany 38533, Rosengarten 35 (72) Inventor Drukkhammer, Yens 3838 Germany Braunschweig, Wiehlungstrasse 47 B. F term (reference) 3G084 BA09 DA10 EA11 EB12 EC03 FA27 FA28 FA29 3G091 AA02 AA11 AB06 BA11 BA14 CB01 DA01 DA02 DB10 DB11 EA18 EA33 EA34 FB10 FB12 FC02 HA08 HA36 HA37 HA42 HB05

Claims (15)

【特許請求の範囲】[Claims] 【請求項1】NOX貯蔵触媒の下流に配設され、排気ガス中のNOX濃度に従
って信号を送る少なくとも1個のNOXゾンデを使用して、内燃機関の排気ガス
通路に配設されたNOX貯蔵触媒の脱硫を制御するための方法において、 a)NO貯蔵触媒(18)の下流で測定されたNOX濃度からNO貯蔵触媒
(18)のNOX活性(NOA)を決定し、 b)NO貯蔵触媒(18)のNOX活性(NOA)が所定の閾値(SW)を下
回るときは、所定の脱硫パラメータにより脱硫を開始し、 c)脱硫成績に基づきNO貯蔵触媒(18)の不可逆的劣化を決定し、所定の
劣化限界値(SWIR)を超えるときは、強力脱硫を開始し、これにより高い脱硫
効果に相当する少なくとも1つの脱硫パラメータが選択され、 d)内燃機関のその後の運転を、強力脱硫の後に回復したNOX初期活性(NO
AMX)の高さに依存させる ことを特徴とする方法。
Is disposed downstream of claim 1] NO X storage catalyst, using at least one of the NO X sonde transmits a signal in accordance with concentration of NO X in the exhaust gas, disposed in an exhaust gas passage of an internal combustion engine a method for controlling a desulphurization of the NO X storage catalyst, a) NO X storage catalyst (18) downstream in NO X determine the activity (NOA) of the NO X storage catalyst from the measured NO X concentration (18) of B) When the NO x activity (NOA) of the NO x storage catalyst (18) is below a predetermined threshold value (SW), desulfurization is started with a predetermined desulfurization parameter, and c) the NO x storage catalyst (based on the desulfurization performance ( 18) irreversible deterioration is determined, and when a predetermined deterioration limit value (SW IR ) is exceeded, strong desulfurization is started, whereby at least one desulfurization parameter corresponding to a high desulfurization effect is selected, and d) internal combustion After the institution The operation was recovered after a strong desulfurization NO X initial activity (NO
AMX) height dependent.
【請求項2】閾値(SW)が脱硫の終了後に回復したNO貯蔵触媒(18
)のNOX初期活性(NOAMX)に比例するように、脱硫のつど閾値(SW)
を設定し、劣化限界値(SWIR)がNO活性(NOA)の下回ってはならない
最小限界値であって、閾値(SW)が劣化限界値(SWIR)より大きいことを特
徴とする請求項1に記載の方法。
2. A NO X storage catalyst (18) whose threshold value (SW) is restored after the end of desulfurization.
), The threshold value (SW) of desulfurization is proportional to the NOX initial activity (NOAMX).
And the deterioration limit value (SW IR ) is a minimum limit value that must not be lower than the NO X activity (NOA), and the threshold value (SW) is larger than the deterioration limit value (SW IR ). The method according to Item 1.
【請求項3】閾値(SW)が不変であるとき、劣化限界値(SWIR)が所定
の最大脱硫頻度であることを特徴とする請求項1に記載の方法。
3. Process according to claim 1, characterized in that when the threshold value (SW) is unchanged, the deterioration limit value (SW IR ) is a predetermined maximum desulfurization frequency.
【請求項4】閾値(SW)が不変であるとき、劣化限界値(SWIR)が脱硫
後に回復したNO初期活性(NOAMX)の所定の下限であることを特徴とす
る請求項1に記載の方法。
4. The deterioration limit value (SW IR ) is a predetermined lower limit of NO X initial activity (NOAMX) recovered after desulfurization when the threshold value (SW) is unchanged. the method of.
【請求項5】劣化限界値(SWIR)を超えたとき、まず内燃機関(10)の
希薄燃焼運転を制限又は禁止し、所定の周辺条件例えばNO貯蔵触媒(18)
の最低温度及び/又は最小時間の間、順守する最低車速が成立するときに初めて
強力脱硫を開始することを特徴とする上記請求項のいずれか1つに記載の方法。
5. When the deterioration limit value (SW IR ) is exceeded, first, lean combustion operation of the internal combustion engine (10) is limited or prohibited, and predetermined ambient conditions such as a NO x storage catalyst (18).
The method according to any one of the preceding claims, characterized in that strong desulfurization is started only when the minimum vehicle speed to be observed is established during the minimum temperature and / or the minimum time.
【請求項6】強力脱硫の終了後に回復したNO初期活性(NOAMX)が
ほぼ完全に又は少なくとも所定の範囲で、硫黄とNOXのない無傷のNO貯蔵
触媒(18)に相当するならば、内燃機関(10)の希薄燃焼運転が引き続き許
容されることを特徴とする上記請求項のいずれか1つに記載の方法。
6. If the initial NO X activity (NOAMX) recovered after the end of strong desulfurization corresponds almost completely or at least to a certain extent to a sulfur and NO X- free intact NO X storage catalyst (18). A method as claimed in any one of the preceding claims, characterized in that a lean burn operation of the internal combustion engine (10) is still allowed.
【請求項7】強力脱硫の終了後に回復したNO初期活性(NOAMX)が
ほぼ完全に又は少なくとも所定の範囲で、硫黄とNOXのない無傷のNO貯蔵
触媒(18)に相当するならば、後続の脱硫が効果的に行われるように、脱硫パ
ラメータを調整することを特徴とする上記請求項のいずれか1つに記載の方法。
7. A strong desulfurization of restored NO X initial activity after completion (NOAMX) is almost completely or at least in a predetermined range, if corresponding to the intact of the NO X storage catalyst without sulfur and NO X (18) The method according to any one of the preceding claims, characterized in that the desulfurization parameters are adjusted so that the subsequent desulfurization takes place effectively.
【請求項8】強力脱硫の終了後に回復したNO初期活性(NOAMX)が
直接先行する脱硫の後より著しく高くなければ、NO貯蔵触媒(18)の激し
い不可逆的劣化を推定し、内燃機関(10)の希薄燃焼運転を制限又は遮断する
ことを特徴とする上記請求項のいずれか1つに記載の方法。
8. If the NO X initial activity (NOAMX) recovered after the end of the strong desulfurization is not significantly higher than that after the immediately preceding desulfurization, a severe irreversible deterioration of the NO X storage catalyst (18) is estimated and the internal combustion engine A method according to any one of the preceding claims, characterized in that the lean burn operation of (10) is limited or interrupted.
【請求項9】NO貯蔵触媒(18)のNO活性(NOA)がNO貯蔵
触媒(18)の下流で測定したNOX濃度と、測定した又は内燃機関(10)の
実際の運転パラメータに基づいて計算したNO貯蔵触媒(18)上流のNOX
濃度との比に相当することを特徴とする上記請求項のいずれか1つに記載の方法
And NO X concentration NO X activity (NOA) was measured downstream of the NO X storage catalyst (18) according to claim 9 NO X storage catalyst (18), the actual operating parameters of the measured or engine (10) NO X storage catalyst (18) upstream of the NO X calculated based on the
Method according to any one of the preceding claims, characterized in that it corresponds to the ratio with the concentration.
【請求項10】NO活性(NOA)がNO貯蔵触媒(18)の後方で測
定したNOX濃度と、硫黄のない無傷のNO貯蔵触媒(18)に基づきモデル
化したNO濃度の比であることを特徴とする上記請求項のいずれか1つに記載
の方法。
10. NO X activity (NOA) and the NO X concentrations measured behind of the NO X storage catalyst (18), of the NO X concentrations modeled based on intact of the NO X storage catalyst without sulfur (18) Method according to any one of the preceding claims, characterized in that it is a ratio.
【請求項11】脱硫パラメータがNO貯蔵触媒(18)の脱硫温度、空気
過剰率リッチ設定(Lambda−Fettvorgabe)及び脱硫時間であ
ることを特徴とする上記請求項のいずれか1つに記載の方法。
11. The desulfurization parameter according to claim 1, wherein the desulfurization parameters are a desulfurization temperature, an excess air ratio rich setting (Lambda-Fettvorgabe) and a desulfurization time of the NO X storage catalyst (18). Method.
【請求項12】制御されたリッチ・リーン脱硫(Fett−Mager−E
ntschwefelung)の場合は、リッチ・リーン空気過剰率設定(Fe
tt−Mager−Lambdavorgaben)、切換え頻度及びNO
蔵触媒(18)の後方のリッチ・リーン切換え限界(Fett−Mager−U
mschaltschwellen)の状態が補助脱硫パラメータであることを
特徴とする上記請求項のいずれか1つに記載の方法。
12. Controlled rich lean desulfurization (Fett-Manager-E).
In the case of ntschwefung, the rich / lean excess air ratio setting (Fe
tt-Mager-Lambdavorgaben), behind the rich lean switching limit switching frequency and NO X storage catalyst (18) (Fett-Mager- U
Method according to any one of the preceding claims, characterized in that the state of mschaltschwellen) is an auxiliary desulfurization parameter.
【請求項13】NOX貯蔵触媒の下流に配設され、排気ガス中のNOX濃度に
従って信号を送る少なくとも1個のNOXゾンデを使用して、内燃機関の排気ガ
ス通路に配設されたNOX貯蔵触媒の脱硫を制御するための装置において、下記
の手順、即ち (a)NO貯蔵触媒(18)の下流で測定されたNOX濃度からNO貯蔵触
媒(18)のNOX活性(NOA)を決定し、 (b)NO貯蔵触媒(18)のNOX活性(NOA)の所定の閾値(SW)を
下回るときは、所定の脱硫パラメータにより脱硫を開始し、 (c)脱硫成績に基づきNO貯蔵触媒(18)の不可逆的劣化を決定し、所定
の劣化限界値(SWIR)を超えるときは強力な脱硫を開始し、その際高い脱硫効
果に相当する少なくとも1つの脱硫パラメータが選択され、 (d)強力脱硫の後に回復したNOX活性(NOAMX)のレベルに従って内燃
機関のその後の運転に関して決定すること を遂行し得る手段が設けられていることを特徴とする装置。
13. is disposed downstream of the NO X storage catalyst, using at least one of the NO X sonde transmits a signal in accordance with concentration of NO X in the exhaust gas, disposed in an exhaust gas passage of an internal combustion engine an apparatus for controlling the desulphurization of the NO X storage catalyst, the following procedure, namely (a) NO X storage NO X catalyst activity NO X storage catalyst from NO X concentration measured downstream of (18) (18) (NOA) is determined, and (b) when it falls below a predetermined threshold value (SW) of the NO X activity (NOA) of the NO X storage catalyst (18), desulfurization is started with a predetermined desulfurization parameter, and (c) desulfurization The irreversible deterioration of the NO X storage catalyst (18) is determined based on the results, and when the predetermined deterioration limit value (SW IR ) is exceeded, strong desulfurization is started, and at this time, at least one desulfurization corresponding to a high desulfurization effect is achieved. The parameter is selected, ( apparatus characterized by means capable of performing determining with respect to the subsequent operation of the internal combustion engine according to the level of d) was recovered after a strong desulfurization NO X activity (NOAMX) is provided.
【請求項14】上記の手段がNO貯蔵触媒(18)の脱硫処理の制御手順
をデジタル形式で格納した制御ユニット(36)を具備することを特徴とする請
求項13に記載の装置。
14. Apparatus according to claim 13, characterized in that said means comprises a control unit (36) storing in digital form the control procedure for the desulfurization treatment of the NO X storage catalyst (18).
【請求項15】制御ユニット(36)がエンジン制御装置(28)に組込ま
れていることを特徴とする請求項14に記載の方法。
15. A method according to claim 14, characterized in that the control unit (36) is integrated in the engine control (28).
JP2001551959A 2000-01-15 2001-01-11 Method and apparatus for controlling desulfurization of NOx storage catalyst disposed in an exhaust gas passage of an internal combustion engine Expired - Fee Related JP4619603B2 (en)

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DE2000101432 DE10001432A1 (en) 2000-01-15 2000-01-15 Control of desulfurization of nitrogen oxides storage catalyst in IC engine exhaust system using sensor downstream from catalyst to determine its activity and desulfurization of catalyst if this falls below threshold value
PCT/EP2001/000249 WO2001051779A1 (en) 2000-01-15 2001-01-11 METHOD AND DEVICE FOR CONTROL OF DESULPHURISATION OF AN NOx STORAGE CATALYST ARRANGED IN AN EXHAUST SYSTEM OF AN INTERNAL COMBUSTION ENGINE

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