EP1365131B1 - Method for controling a NOx storage catalyst - Google Patents

Method for controling a NOx storage catalyst Download PDF

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Publication number
EP1365131B1
EP1365131B1 EP03090075A EP03090075A EP1365131B1 EP 1365131 B1 EP1365131 B1 EP 1365131B1 EP 03090075 A EP03090075 A EP 03090075A EP 03090075 A EP03090075 A EP 03090075A EP 1365131 B1 EP1365131 B1 EP 1365131B1
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EP
European Patent Office
Prior art keywords
regeneration
catalyst
storage catalyst
storage
process according
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EP03090075A
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German (de)
French (fr)
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EP1365131A2 (en
EP1365131A3 (en
Inventor
Hermann Dr. Hahn
Sören HINZE
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Volkswagen AG
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Volkswagen AG
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    • 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
    • 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
    • F01N13/009Exhaust 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 having two or more separate purifying devices arranged in series
    • 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
    • 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
    • F01N2430/00Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics
    • F01N2430/06Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics by varying fuel-air ratio, e.g. by enriching fuel-air mixture
    • 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
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/02Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
    • F01N2560/026Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting NOx
    • 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
    • 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
    • F02D2200/0802Temperature of the exhaust gas treatment apparatus
    • 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
    • F02D2200/0814Oxygen storage amount

Definitions

  • the invention relates to a method for controlling a NO x storage catalytic converter with the features mentioned in the preamble of claim 1.
  • the exhaust gas is passed over at least one catalyst, which performs a conversion of one or more pollutant components of the exhaust gas.
  • catalysts Different types of catalysts are known. Oxidation catalysts promote the oxidation of unburned hydrocarbons (HC) and carbon monoxide (CO), while reduction catalysts promote the reduction of nitrogen oxides (NO x ) of the exhaust gas.
  • 3-way catalysts are used to simultaneously catalyze the conversion of the three aforementioned components (HC, CO, NO X ).
  • NO x storage catalysts are used which, in addition to a catalytic component, contain an NO x reservoir which stores NO x in the form of nitrate in the lean operating phases.
  • intermediate fat regeneration phases at ⁇ ⁇ 1 where HC and CO are formed, which act as reducing agents, the nitrates are reduced to nitrogen N 2 .
  • the NO x storage catalytic converter is still a catalyst, for example, a 3-way catalyst upstream.
  • a regeneration period is fixed by means of a rich exhaust gas atmosphere.
  • the actual load state of the NO x storage catalytic converter and a current regeneration rate of the same can disadvantageously not be taken into account.
  • Such The procedure therefore involves the risk that the regeneration period is too short or too long, in the first case, an incomplete regeneration of the memory and in the second case unnecessary fuel consumption and emission of environmentally harmful reducing agents (HC and CO) is accepted.
  • the regeneration profile is monitored by means of a sensor system arranged downstream of the NO x storage catalytic converter in the form of a NO x sensor or a lambda probe which measures an oxygen content of the exhaust gas.
  • a decreasing proportion of oxygen in the exhaust gas indicates a reduced reduction agent conversion at the NO x reservoir and thus increasing proportions of the reducing agent in the exhaust gas.
  • the NO x regeneration is stopped, that is, the internal combustion engine is switched back to a lean operating mode as soon as the measured oxygen content falls below a predetermined limit value or a sensor voltage exceeds a corresponding limit voltage.
  • This method has the disadvantage that the sensor can only react if a certain reductant breakthrough already occurs.
  • the pipe between engine and catalyst at the end of the regeneration when the engine leaves the regeneration mode, still filled with rich exhaust gas. This contributes significantly to an increase in reductant breakdown at the regeneration end.
  • Various methods are known for initiating the regeneration of the NO x storage catalytic converter, which are usually based on stored behavior models of the NO x storage catalytic converter or on emission profiles measured, for example, by means of an NO x sensor. Especially in the latter case, it may be that the initiation of a regeneration is carried out exclusively on demand with a corresponding NO x breakthrough.
  • the NO x regenerations are performed such that the regeneration is terminated as soon as the signal of the downstream oxygen-sensitive sensor system reaches a certain threshold value or a behavioral model for the catalytic converter has determined the time of its complete emptying. Both methods are usually designed so that there is only a small breakthrough of reducing agent at the end of regeneration. In exceptional cases, a small excess of reducing agent can be tolerated for various reasons.
  • Nitrate storage phase proceeds with reduced efficiency, increasing fuel consumption and emission of pollutants.
  • the invention is therefore based on the object to provide a method for controlling a NO x storage catalyst available, which is optimized with respect to the lowest possible reducing agent emission compared to the prior art and which is too high saturation and thus a poorer regenerability of NO X - Storage catalyst avoids.
  • the first process step according to the invention which takes place at the beginning of a regeneration phase, ensures that the rich exhaust gases located at the end of a regeneration phase upstream of the NO x storage catalytic converter are optimal due to the definition of a combustion lambda which takes into account the diffusion rate of the oxygen-containing components of the catalyst coating
  • Regeneration of the NO x storage catalyst can be used, so that a reducing agent breakthrough is advantageously reduced.
  • the engine operating point, the exhaust gas mass flow and / or the catalyst state which can be determined by known methods, for example by means of a conversion factor, can be used to determine the combustion lambda.
  • the air-fuel mixture (combustion lambda) supplied for regeneration is not only determined at the beginning of the regeneration, but also varies during the regeneration, since the conditions for determining the combustion lambda may be variable after the regeneration begins. This variation can be carried out by known methods.
  • the predetermined threshold value for the saturation state of the NO x storage catalytic converter is determined in advance by suitable tests. This gives information about up to which load of the NO X storage catalytic converter the NO x regeneration with normal execution still leads to a sufficient conversion of all stored nitrogen oxides.
  • the current load value for the NO X storage catalyst is determined by balancing the NO X M levels before and after the NO X storage catalyst.
  • the signal of the NO x -sensitive measuring device for example, the signal of a second NO X -sensitive measuring device located in front of the NO x * storage catalytic converter or a corresponding modeling in the engine control unit can be used.
  • the threshold value may additionally be dependent on further factors, for example catalyst / exhaust gas temperature, exhaust gas mass flow, NO X mass flow, HC content of the lean exhaust gas and the like, which may have to be taken into account as correction values of the threshold value.
  • At least one next NO x regeneration can be explicitly extended.
  • An increased reductant breakthrough due to the more intensive regeneration is accepted.
  • the achievement of the threshold value can be used to deactivate the diagnosis of the catalytic converter or other functionalities evaluating the current storage capacity of the catalytic converter in the following period.
  • the withdrawal of this deactivation may, for example, be made dependent on a certain cumulative amount of reducing agent or a predetermined minimum number of regeneration processes.
  • the NO X -sensitive measuring device is a NOx sensor, which also provides an oxygen-dependent signal which can be used to monitor the regeration of the NO X storage catalytic converter. Otherwise, however, an additional oxygen-sensitive measuring device such as a lambda broadband or jump probe can be used to monitor the regeneration phase.
  • the internal combustion engine 10 shown in Figure 1 is downstream of an exhaust system 12.
  • the exhaust system 12 has an exhaust gas channel 14, in which a pre-catalyst arranged close to the engine 16 and a large-volume NO x storage 18 are located.
  • the exhaust gas channel 14 usually has various gas and / or temperature sensors (not shown here) for regulating the internal combustion engine 10.
  • an NO x sensor 20 is shown, which is arranged downstream of the NO x storage catalytic converter 18 and which supplies a signal U NOX for the proportion of NO x in the exhaust gas.
  • the NO x sensor 20 is equipped with a Lambdamessfunktion, so that in addition a dependent of an oxygen content of the exhaust gas signal U ⁇ is provided.
  • the signals U NOX and U ⁇ are transmitted to an engine control unit 22 in which they are digitized and further processed. Further, the operating state of the internal combustion engine 10 information related also found in the engine control unit 22.
  • a control unit 24 is also integrated. By means of the engine control unit 22 and the control unit 24, at least one operating parameter of the internal combustion engine 10, in particular an air-fuel mixture (combustion lambda) to be supplied, is influenced as a function of the signals U NOX and U ⁇ of the NO x sensor 20.
  • FIG. 2 shows the time profile of various parameters of the internal combustion engine 10 and of the exhaust system 12 during a NO x regeneration of the NO x storage catalytic converter 18, which takes place according to the prior art.
  • the internal combustion engine 10 is in a lean mode of operation in which it is supplied with an oxygen-rich air-fuel mixture with ⁇ M »1 (graph 100).
  • the exhaust gas contains an excess of nitrogen oxides NO x , which can not be completely converted by the precatalyst 16.
  • NO x is therefore stored in the NO x storage catalytic converter 18, whose NO x charge increases continuously to saturation NO XMAX (graph 102). Based on a suitable criterion, a NO x regeneration need is recognized at a time t A.
  • This may be, for example, a NO x breakthrough detected by the NO x sensor 20.
  • the internal combustion engine 10 is switched by influencing the engine control unit 22 in a rich operating mode with ⁇ F ⁇ 1. Due to the now increased mass flow the reducing agent CO and HC in the exhaust gas is desorbed in the NO x storage 18 stored NO X and reduced to nitrogen. A decrease in the NO x charge of the storage catalytic converter 18 (graph 102), however, is recorded only after a certain time delay after switching the internal combustion engine 10, since at time t A of the exhaust duct 14 is still filled with lean exhaust gas, which initially still the storage catalytic converter 18 must happen before the reducing agents reach it.
  • the course of the NO x regeneration is in the meantime tracked with the aid of the signal U ⁇ provided by the NO x sensor 20.
  • the signal U ⁇ (graph 104) behaves inversely proportional to an oxygen concentration of the exhaust gas downstream of the storage catalytic converter 18. As the reducing agents are consumed to an increasing extent as regeneration progresses, the signal U ⁇ of the NO X sensor 20 increases slowly. At a time t E , the signal U ⁇ reaches a predetermined threshold value U SE , whereupon the internal combustion engine 10 is usually switched back into a lean operating mode with ⁇ M »1.
  • the approach shown in Figure 3 is pursued according to the invention, wherein the time course of the same parameters as in Figure 2 and in addition the course of the signal U NOX (graph 108) of the NOx sensor 20 is shown for the NO X emissions.
  • the NO x emission increases sharply with increasing loading of the NO x storage catalytic converter 18, wherein at the time t A upon reaching a predetermined threshold value NO XSE , which is determined by balancing the NO x quantities before and after the NO x storage catalytic converter 18 and which is in relation to the saturation of the NO x storage 18, the regeneration of the NO x storage 18 is initiated.
  • the threshold NO XSE is determined experimentally in advance and gives the point at the NO X storage loading, in which a complete emptying of the NO X storage catalytic converter is still possible in a subsequent regeneration phase. After initiation of the regeneration, the NO x emission drops steeply and remains at a constantly low level.
  • the course of the NO x charge of the NO x storage catalytic converter 18-represented by graph 102- substantially corresponds to the course according to FIG. 2, since the loading and the discharge are subject to the same mechanisms. However, the graph 102 is at a lower level since the emptying begins at a lower loading condition and ends only at complete emptying.
  • the temperature of the storage catalytic converter 18 is determined at time t A and transmitted to the engine control unit 22, which subsequently the internal combustion engine 10 of a lean mode with ⁇ M »1 in a rich mode with ⁇ F ⁇ 1 switched, the determined catalyst temperature is used to establish an optimized combustion lambda.
  • a combustion lambda ⁇ F is set, which may be higher ( ⁇ FT1 ), lower ( ⁇ FT2 ) or equal to the combustion lambda ⁇ FT0 , without the evaluation of the temperature of the NO x Storage Catalyst 18 would have been adjusted.
  • a combustion lambda ⁇ F which takes into account at least the temperature of the NO x storage 18 as a relevant factor, it is ensured that at the time t E at the end of a regeneration phase before the NO x storage catalytic converter 18 fat exhaust gases are still for regeneration of the NO x storage 18 can be used. A reducing agent breakthrough can thus be significantly reduced. Comparing the graph of graph 106 with that in FIG. 2, which illustrates the concentrations of carbon monoxide CO and unburned hydrocarbons HC downstream of NO x storage catalyst 18, shows a large reduction in pollutant emission due to regeneration.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Electrical Control Of Air Or Fuel Supplied To Internal-Combustion Engine (AREA)

Abstract

Process for controlling a nitrogen oxides storage catalyst in an internal combustion engine comprises evaluating the actual catalyst behavior with respect to oxygen storage of the oxygen-containing component in the catalyst coating at the start of the regeneration of the storage catalyst, and/or regenerating the nitrogen oxides storage catalyst. Process for controlling a nitrogen oxides storage catalyst in an internal combustion engine comprises evaluating the actual catalyst behavior with respect to oxygen storage of the oxygen-containing component in the catalyst coating at the start of the regeneration of the storage catalyst, and/or regenerating the nitrogen oxides storage catalyst when a prescribed threshold value for the saturation state of the catalyst is reached or increasing the regeneration when the prescribed threshold value for the saturation state of the catalyst is reached neglecting introduction of a reducing agent.

Description

Die Erfindung betrifft ein Verfahren zur Steuerung eines NOX-Speicherkatalysators mit den im Oberbegriff des Anspruchs 1 genannten Merkmalen.The invention relates to a method for controlling a NO x storage catalytic converter with the features mentioned in the preamble of claim 1.

Zur Nachbehandlung von Abgasen von Verbrennungskraftmaschinen ist es allgemein üblich, das Abgas katalytisch zu reinigen. Dazu wird das Abgas über mindestens einen Katalysator geleitet, der eine Konvertierung einer oder mehrerer Schadstoffkomponenten des Abgases vornimmt. Es sind unterschiedliche Arten von Katalysatoren bekannt. Oxidationskatalysatoren fördern die Oxidation von unverbrannten Kohlenwasserstoffen (HC) und Kohlenmonoxid (CO), während Reduktionskatalysatoren eine Reduzierung von Stickoxiden (NOX) des Abgases unterstützen. Ferner werden 3-Wege-Katalysatoren verwendet, um die Konvertierung der drei vorgenannten Komponenten (HC, CO, NOX) gleichzeitig zu katalysieren. Die Verwendung eines 3-Wege-Katalysators ist jedoch nur möglich, wenn ein streng stöchiometrisches Luft-Kraftstoff-Verhältnis bei λ = 1 vorliegt.For the aftertreatment of exhaust gases from internal combustion engines, it is common practice to purify the exhaust gas catalytically. For this purpose, the exhaust gas is passed over at least one catalyst, which performs a conversion of one or more pollutant components of the exhaust gas. Different types of catalysts are known. Oxidation catalysts promote the oxidation of unburned hydrocarbons (HC) and carbon monoxide (CO), while reduction catalysts promote the reduction of nitrogen oxides (NO x ) of the exhaust gas. Furthermore, 3-way catalysts are used to simultaneously catalyze the conversion of the three aforementioned components (HC, CO, NO X ). However, the use of a 3-way catalyst is only possible if a strictly stoichiometric air-fuel ratio at λ = 1 is present.

Zur Optimierung des Verbrauchs von Kraftfahrzeugen werden unter anderem magerlauffähige Verbrennungskraftmaschinen eingesetzt. In einem verbrauchsgünstigen Magerbetrieb, bei dem die Verbrennungskraftmaschine mit Sauerstoffüberschuss, das heißt mit λ > 1, gefahren wird, ist eine vollständige 3-wege-katalytische Umsetzung von NOX nicht möglich. Bei derartigen Verbrennungskraftmaschinen werden daher NOX-Speicherkatalysatoren eingesetzt, die neben einer katalytischen Komponente einen NOX-Speicher enthalten, der in den mageren Betriebsphasen NOX in Form von Nitrat speichert. In zwischengeschalteten fetten Regenerationsphasen bei λ < 1, bei denen HC und CO gebildet werden, die als Reduktionsmittel wirken, werden die Nitrate zu Stickstoff N2 reduziert. Häufig ist dem NOX-Speicherkatalysator noch ein Katalysator, beispielsweise ein 3-Wege-Katalysator, vorgeschaltet.In order to optimize the consumption of motor vehicles, inter alia lean combustion engines are used. In a low-consumption lean operation, in which the internal combustion engine with oxygen excess, that is, with λ> 1, driven, a complete 3-way catalytic conversion of NO X is not possible. In such internal combustion engines, therefore, NO x storage catalysts are used which, in addition to a catalytic component, contain an NO x reservoir which stores NO x in the form of nitrate in the lean operating phases. In intermediate fat regeneration phases at λ <1, where HC and CO are formed, which act as reducing agents, the nitrates are reduced to nitrogen N 2 . Often the NO x storage catalytic converter is still a catalyst, for example, a 3-way catalyst upstream.

In einfachen Verfahren zur Steuerung des NOX-Speicherkatalysators wird eine Regenerationsdauer mittels einer fetten Abgasatmosphäre fest vorgegeben. Dabei kann nachteilhafterweise der tatsächliche Beladungszustand des NOX-Speicherkatalysators und eine aktuelle Regenerationsrate desselben nicht berücksichtigt werden. Eine solche Vorgehensweise birgt daher die Gefahr, dass die Regenerationsdauer zu kurz oder zu lang gewählt wird, wobei im ersten Fall eine unvollständige Regeneration des Speichers und im zweiten Fall ein unnötiger Kraftstoffmehrverbrauch sowie eine Emission umweltschädlicher Reduktionsmittel (HC und CO) in Kauf genommen wird.In simple methods for controlling the NO x storage catalytic converter, a regeneration period is fixed by means of a rich exhaust gas atmosphere. In this case, the actual load state of the NO x storage catalytic converter and a current regeneration rate of the same can disadvantageously not be taken into account. Such The procedure therefore involves the risk that the regeneration period is too short or too long, in the first case, an incomplete regeneration of the memory and in the second case unnecessary fuel consumption and emission of environmentally harmful reducing agents (HC and CO) is accepted.

Weiterhin sind Verfahren bekannt, bei denen mit Hilfe einer stromab des NOX-Speicherkatalysators angeordneten Sensorik in Form eines NOX-Sensors oder einer Lambda-Sonde, die einen Sauerstoffanteil des Abgases misst, der Regenerationsverlauf überwacht wird. Dabei zeigt ein sinkender Sauerstoffanteil im Abgas einen verminderten Reduktionsmittelumsatz am NOX-Speicher und somit steigende Anteile der Reduktionsmittel im Abgas an. Um Reduktionsmitteldurchbrüche zu vermeiden, wird die NOX-Regeneration abgebrochen, das heißt die Verbrennungskraftmaschine wieder in einen mageren Betriebsmodus umgeschaltet, sobald der gemessene Sauerstoffanteil einen vorgegebenen Grenzwert unterschreitet beziehungsweise eine Sensorspannung eine entsprechende Grenzspannung überschreitet. Dieses Verfahren ist mit dem Nachteil verbunden, dass der Sensor erst reagieren kann, wenn bereits ein gewisser Reduktionsmitteldurchbruch auftritt. Zudem ist bei diesen Verfahren das Rohr zwischen Motor und Katalysator am Ende der Regeneration, wenn der Motor den Regenerationsbetrieb verlässt, noch mit fettem Abgas gefüllt. Dies trägt deutlich zu einer Erhöhung des Reduktionsmitteldurchbruches am Regenerationsende bei.Furthermore, methods are known in which the regeneration profile is monitored by means of a sensor system arranged downstream of the NO x storage catalytic converter in the form of a NO x sensor or a lambda probe which measures an oxygen content of the exhaust gas. In this case, a decreasing proportion of oxygen in the exhaust gas indicates a reduced reduction agent conversion at the NO x reservoir and thus increasing proportions of the reducing agent in the exhaust gas. To avoid reducing agent breakthroughs, the NO x regeneration is stopped, that is, the internal combustion engine is switched back to a lean operating mode as soon as the measured oxygen content falls below a predetermined limit value or a sensor voltage exceeds a corresponding limit voltage. This method has the disadvantage that the sensor can only react if a certain reductant breakthrough already occurs. In addition, in these methods, the pipe between engine and catalyst at the end of the regeneration, when the engine leaves the regeneration mode, still filled with rich exhaust gas. This contributes significantly to an increase in reductant breakdown at the regeneration end.

Zur Einleitung der Regeneration des NOX-Speicherkatalysators sind verschiedene Verfahren bekannt, die üblicherweise auf abgelegten Verhaltensmodellen des NOX-Speicherkatalysators oder auf zum Beispiel mittels eines NOX-Sensors gemessenen Emissionsverläufen beruhen. Besonders im letztgenannten Fall kann es sein, dass die Einleitung einer Regeneration ausschließlich bedarfsgerecht bei entsprechendem NOX-Durchbruch durchgeführt wird. Wie bereits oben ausgeführt, werden die NOX-Regenerationen so durchgeführt, dass die Regeneration beendet wird, sobald das Signal der nachgeschalteten sauerstoffsensitiven Sensorik einen gewissen Schwellwert erreicht oder ein Verhaltensmodell für den Katalysator den Zeitpunkt seiner kompletten Leerung ermittelt hat. Beide Verfahren werden üblicherweise so ausgelegt, dass es nur zu einem geringen Durchbruch von Reduktionsmittel bei Regenerationsende kommt. In Ausnahmefällen kann ein kleiner Überschuss an Reduktionsmittel aus verschiedenen Gründen toleriert werden.Various methods are known for initiating the regeneration of the NO x storage catalytic converter, which are usually based on stored behavior models of the NO x storage catalytic converter or on emission profiles measured, for example, by means of an NO x sensor. Especially in the latter case, it may be that the initiation of a regeneration is carried out exclusively on demand with a corresponding NO x breakthrough. As already stated above, the NO x regenerations are performed such that the regeneration is terminated as soon as the signal of the downstream oxygen-sensitive sensor system reaches a certain threshold value or a behavioral model for the catalytic converter has determined the time of its complete emptying. Both methods are usually designed so that there is only a small breakthrough of reducing agent at the end of regeneration. In exceptional cases, a small excess of reducing agent can be tolerated for various reasons.

Bei dieser Verfahrensweise kann jedoch ein Speicherkatalysator mit sehr hohem Sättigungsgrad nicht vollständig geleert werden. Es verbleibt ein gewisser Restanteil an gespeicherten Nitraten in der Beschichtung. Die der Regenerationsphase nachfolgende Einspeicherphase von Nitraten läuft dann mit verringerter Effektivität ab, wodurch sich der Kraftstoffverbrauch und die Emission an Schadstoffen erhöht.In this procedure, however, a storage catalyst with a very high degree of saturation can not be completely emptied. There remains some residual amount of stored nitrates in the coating. The regeneration phase following Nitrate storage phase then proceeds with reduced efficiency, increasing fuel consumption and emission of pollutants.

Der Erfindung liegt daher die Aufgabe zugrunde, ein Verfahren zur Steuerung eines NOX-Speicherkatalysators zur Verfügung zu stellen, welches hinsichtlich einer möglichst geringen Reduktionsmittelemission gegenüber dem Stand der Technik optimiert ist und welches eine zu hohe Sättigung und damit eine schlechtere Regenerierbarkeit des NOX-Speicherkatalysators vermeidet.The invention is therefore based on the object to provide a method for controlling a NO x storage catalyst available, which is optimized with respect to the lowest possible reducing agent emission compared to the prior art and which is too high saturation and thus a poorer regenerability of NO X - Storage catalyst avoids.

Diese Aufgabe wird durch ein Verfahren mit den im Anspruch 1 genannten Merkmalen gelöst.This object is achieved by a method having the features mentioned in claim 1.

Das erfindungsgemäße Verfahren zur Steuerung eines NOX-Speicherkatalysators einer Brennkraftmaschine mit einer stromab des NOX-Speicherkatalysators angeordneten NOX-sensitiven Messeinrichtung sowie mit einer Motorsteuerungseinheit sieht vor, dass

  • (a) zu Beginn der Regeneration des NOX-Speicherkatalysators das aktuelle Katalysatorverhalten hinsichtlich einer Sauerstoffausspeicherung der sauerstoffhaltigen Komponenten in der Katalysatorbeschichtung auf der Basis der Katalysatortemperatur bewertet wird, wobei das zur Regeneration der Verbrennungskraftmaschine zugeführte Luft-Kraftstoff-Gemisch (Verbrennungslambda) in Abhängigkeit dieser Bewertung grundsätzlich festgelegt wird, und/oder
  • (b) bei Erreichen eines vorgegebenen Schwellwertes für den Sättigungszustand des NOX-Speicherkatalysators die Regeneration des NOX-Speicherkatalysators eingeleitet wird oder
  • (c) bei Überschreiten des vorgegebenen Schwellwertes für den Sättigungszustand des NOX-Speicherkatalysators mindestens die sich anschließende Regeneration unter Vernachlässigung eines Reduktionsmitteldurchbruches verlängert wird.
The method according to the invention for controlling an NO x storage catalytic converter of an internal combustion engine with an NO x -sensitive measuring device arranged downstream of the NO x storage catalytic converter and with an engine control unit provides that
  • (A) at the beginning of the regeneration of the NO x storage catalyst, the current catalyst behavior is evaluated in terms of oxygen storage of the oxygen-containing components in the catalyst coating on the basis of the catalyst temperature, wherein the regeneration of the internal combustion engine supplied air-fuel mixture (combustion lambda) in response Assessment is determined in principle, and / or
  • (B) upon reaching a predetermined threshold value for the saturation state of the NO x storage catalytic converter, the regeneration of the NO x storage catalyst is initiated or
  • (C) is extended when the predetermined threshold for the saturation state of the NO x storage catalytic converter is exceeded, at least the subsequent regeneration neglecting a reducing agent breakthrough.

Durch den ersten erfindungsgemäßen Verfahrensschritt, der zu Beginn einer Regenerationsphase erfolgt, wird gewährleistet, dass die am Ende einer Regenerationsphase vor dem NOX-Speicherkatalysator befindlichen fetten Abgase, aufgrund der Festlegung eines Verbrennungslambdas, das die Diffusionsgeschwindigkeit der sauerstoffhaltigen Komponenten der Katalysatorbeschichtung berücksichtigt, optimal zurThe first process step according to the invention, which takes place at the beginning of a regeneration phase, ensures that the rich exhaust gases located at the end of a regeneration phase upstream of the NO x storage catalytic converter are optimal due to the definition of a combustion lambda which takes into account the diffusion rate of the oxygen-containing components of the catalyst coating

Regeneration des NOX-Speicherkatalysators genutzt werden, so dass ein Reduktionsmitteldurchbruch vorteilhafterweise verringert wird. Weiterhin können der Motorbetriebspunkt, der Abgasmassenstrom und/oder der Katalysatorzustand, der über bekannte Verfahren, zum Beispiel mittels eines Konvertierungsfaktors, ermittelbar ist, zur Festlegung des Verbrennungslambdas herangezogen werden. Zur Bestimmung des Beginns einer Regenerationsphase wird vorzugsweise das NOX-Signal des NOX-Sensors und kein Zeitschema verwendet.Regeneration of the NO x storage catalyst can be used, so that a reducing agent breakthrough is advantageously reduced. Furthermore, the engine operating point, the exhaust gas mass flow and / or the catalyst state, which can be determined by known methods, for example by means of a conversion factor, can be used to determine the combustion lambda. To determine the beginning of a regeneration phase, it is preferable to use the NO x signal of the NO x sensor and no time scheme.

Nach einer besonders bevorzugten Ausführungsform des Verfahrens wird das zur Regeneration zugeführte Luft-Kraftstoff-Gemisch (Verbrennungslambda) nicht nur zu Beginn der Regeneration festgelegt, sondern auch während der Regeneration variiert, da die Bedingungen zur Festlegung des Verbrennungslambdas nach Beginn der Regeneration veränderlich sein können. Diese Variation kann mittels bekannter Verfahren durchgeführt werden.According to a particularly preferred embodiment of the method, the air-fuel mixture (combustion lambda) supplied for regeneration is not only determined at the beginning of the regeneration, but also varies during the regeneration, since the conditions for determining the combustion lambda may be variable after the regeneration begins. This variation can be carried out by known methods.

Durch die beiden weiteren Verfahrensschritte des Hauptanspruchs, die alternativ durchgeführt werden, wird eine Sättigung des NOX-Speicherkatalysators vermieden beziehungsweise werden deren Auswirkungen durch erfinderische Maßnahmen kompensiert. Daher kann in der Regel der NOX-Speicherkatalysator während der Regenerationsphase vollständig entladen werden.The two further method steps of the main claim, which are carried out alternatively, a saturation of the NO x storage catalyst is avoided or their effects are compensated by inventive measures. Therefore, as a rule, the NO x storage catalyst can be completely discharged during the regeneration phase.

Der vorgegebene Schwellwert für den Sättigungszustand des NOX-Speicherkatalysators wird vorab durch geeignete Versuche ermittelt. Dieser gibt Auskunft darüber, bis zu welcher Beladung des NOX-Speicherkatalysators die NOX-Regeneration mit normaler Durchführung noch zu einer hinreichenden Umsetzung aller gespeicherten Stickoxide führt.The predetermined threshold value for the saturation state of the NO x storage catalytic converter is determined in advance by suitable tests. This gives information about up to which load of the NO X storage catalytic converter the NO x regeneration with normal execution still leads to a sufficient conversion of all stored nitrogen oxides.

Der aktuelle Wert für die Beladung des NOX-Speicherkatalysators wird durch Bilanzierung der NOXM-engen vor und nach dem NOX-Speicherkatalysator ermittelt. Dazu kann neben dem Signal der NOX-sensitiven Messeinrichtung beispielsweise das Signal einer zweiten, vor dem NOX*Speicherkatalysator befindlichen NOX-sensitiven Messeinrichtung oder eine entsprechende Modellierung in der Motorsteuerungseinheit herangezogen werden. Der Schwellwert kann zusätzlich von weiteren Faktoren abhängig sein, zum Beispiel Katalysator-/Abgastemperatur, Abgasmassenstrom, NOX-Rohmassenstrom, HC-Gehalt des mageren Abgases und dergleichen, die gegebenenfalls als Korrekturgrößen des Schwellwertes zu berücksichtigen sind.The current load value for the NO X storage catalyst is determined by balancing the NO X M levels before and after the NO X storage catalyst. For this purpose, in addition to the signal of the NO x -sensitive measuring device, for example, the signal of a second NO X -sensitive measuring device located in front of the NO x * storage catalytic converter or a corresponding modeling in the engine control unit can be used. The threshold value may additionally be dependent on further factors, for example catalyst / exhaust gas temperature, exhaust gas mass flow, NO X mass flow, HC content of the lean exhaust gas and the like, which may have to be taken into account as correction values of the threshold value.

Wird nun im Fahrbetrieb ein zu diesem Schwellwert in Relation stehender Wert erreicht, so kann als vorbeugende Maßnahme eine Regeneration eingeleitet werden, obwohl dies von der Konvertierungsleistung her noch nicht erforderlich wäre. Auf diese Weise wird eine Sättigung des NOX-Speicherkatalysators verhindert.If a value in relation to this threshold value is reached while driving, a regeneration can be initiated as a preventive measure, even though this would not be necessary from the conversion performance. In this way, saturation of the NO x storage catalyst is prevented.

Alternativ kann mindestens eine nächste NOX-Regeneration explizit verlängert werden. Dabei wird ein erhöhter Reduktionsmitteldurchbruch aufgrund der intensiveren Regeneration in Kauf genommen.Alternatively, at least one next NO x regeneration can be explicitly extended. An increased reductant breakthrough due to the more intensive regeneration is accepted.

Des Weiteren kann das Erreichen des Schwellwertes dazu genutzt werden, die Diagnose des Katalysators oder sonstige die aktuelle Speicherfähigkeit des Katalysators bewertende Funktionalitäten im folgenden Zeitraum zu deaktivieren. Die Rücknahme dieser Deaktivierung kann zum Beispiel abhängig gemacht werden von einer gewissen kumulierten Reduktionsmittelmenge oder einer vorgegebenen Mindestanzahl von Regenerationsvorgängen.Furthermore, the achievement of the threshold value can be used to deactivate the diagnosis of the catalytic converter or other functionalities evaluating the current storage capacity of the catalytic converter in the following period. The withdrawal of this deactivation may, for example, be made dependent on a certain cumulative amount of reducing agent or a predetermined minimum number of regeneration processes.

Vorteilhafterweise ist die NOX-sensitive Messeinrichtung ein NOX-Sensor, der auch ein sauerstoffabhängiges Signal liefert, das zur Überwachung der Regeration des NOX-Speicherkatalysators verwendet werden kann. Ansonsten kann aber auch eine zusätzliche sauerstoffsensitive Messeinrichtung wie eine Lambda-Breitband- oder -Sprungsonde eingesetzt werden, um die Regenerationsphase zu überwachen.Advantageously, the NO X -sensitive measuring device is a NOx sensor, which also provides an oxygen-dependent signal which can be used to monitor the regeration of the NO X storage catalytic converter. Otherwise, however, an additional oxygen-sensitive measuring device such as a lambda broadband or jump probe can be used to monitor the regeneration phase.

Weitere bevorzugte Ausgestaltungen der Erfindung ergeben sich aus den übrigen, in den Unteransprüchen genannten Merkmalen.Further preferred embodiments of the invention will become apparent from the remaining, mentioned in the dependent claims characteristics.

Die Erfindung wird nachfolgend in Ausführungsbeispielen anhand der zugehörigen Zeichnungen näher erläutert. Es zeigen:

Figur 1
eine Prinzipdarstellung einer Verbrennungskraftmaschine mit einer Abgasanlage;
Figur 2
zeitliche Verläufe verschiedener Abgasparameter während einer herkömmlichen NOX-Regeneration;
Figur 3
zeitliche Verläufe verschiedener Abgasparameter während einer NOX-Regeneration im Anschluss an eine erfindungsgemäße Einleitung der Regeneration zur Verhinderung der Sättigung des Katalysators und
Figur 4
zeitliche Verläufe verschiedener Abgasparameter während einer NOX-Regeneration gemäß der vorliegenden Erfindung nach Festlegung eines Verbrennungslambdas zu Beginn der NOX-Regeneration .
The invention will be explained in more detail in embodiments with reference to the accompanying drawings. Show it:
FIG. 1
a schematic diagram of an internal combustion engine with an exhaust system;
FIG. 2
time histories of various exhaust gas parameters during a conventional NO x regeneration;
FIG. 3
temporal courses of various exhaust gas parameters during a NO x regeneration following an inventive initiation of the regeneration to prevent the saturation of the catalyst and
FIG. 4
Timing of various exhaust gas parameters during a NO x regeneration according to the present invention after establishing a combustion lambda at the beginning of the NO x regeneration.

Der in Figur 1 dargestellten Verbrennungskraftmaschine 10 ist eine Abgasanlage 12 nachgeordnet. Die Abgasanlage 12 weist einen Abgaskanal 14 auf, in dem ein motornah angeordneter Vorkatalysator 16 sowie ein großvolumiger NOX-Speicherkatalysator 18 befindlich sind. Neben dem Vorkatalysator 16 und dem NOX-Speicherkatalysator 18 weist der Abgaskanal 14 üblicherweise verschiedene, hier jedoch nicht dargestellte Gas- und/oder Temperatursensoren zur Regelung der Verbrennungskraftmaschine 10 auf. Dargestellt ist in Figur 1 lediglich ein NOX-Sensor 20, der stromab des NOX-Speicherkatalysators 18 angeordnet ist und der ein Signal UNOX für den Anteil von NOX im Abgas liefert. Der NOX-Sensor 20 ist mit einer Lambdamessfunktion ausgestattet, so dass zusätzlich ein von einem Sauerstoffanteil des Abgases abhängiges Signal Uλ bereitgestellt wird. Die Signale UNOX und Uλ werden an ein Motorsteuergerät 22 übermittelt, in welchem diese digitalisiert und weiterverarbeitet werden. Weitere, den Betriebszustand der Verbrennungskraftmaschine 10 betreffende Informationen finden ebenfalls Eingang in das Motorsteuergerät 22. In dem Motorsteuergerät 22 ist zudem eine Steuereinheit 24 integriert. Mittels des Motorsteuergeräts 22 und der Steuereinheit 24 wird mindestens ein Betriebsparameter der Verbrennungskraftmaschine 10, insbesondere ein zuzuführendes Luft-Kraftstoff-Gemisch (Verbrennungslambda), in Abhängigkeit der Signale UNOX und Uλ des NOX-Sensors 20 beeinflusst.The internal combustion engine 10 shown in Figure 1 is downstream of an exhaust system 12. The exhaust system 12 has an exhaust gas channel 14, in which a pre-catalyst arranged close to the engine 16 and a large-volume NO x storage 18 are located. In addition to the precatalyst 16 and the NO x storage catalytic converter 18, the exhaust gas channel 14 usually has various gas and / or temperature sensors (not shown here) for regulating the internal combustion engine 10. In FIG. 1, only an NO x sensor 20 is shown, which is arranged downstream of the NO x storage catalytic converter 18 and which supplies a signal U NOX for the proportion of NO x in the exhaust gas. The NO x sensor 20 is equipped with a Lambdamessfunktion, so that in addition a dependent of an oxygen content of the exhaust gas signal U λ is provided. The signals U NOX and U λ are transmitted to an engine control unit 22 in which they are digitized and further processed. Further, the operating state of the internal combustion engine 10 information related also found in the engine control unit 22. In the engine control unit 22, a control unit 24 is also integrated. By means of the engine control unit 22 and the control unit 24, at least one operating parameter of the internal combustion engine 10, in particular an air-fuel mixture (combustion lambda) to be supplied, is influenced as a function of the signals U NOX and U λ of the NO x sensor 20.

Figur 2 zeigt den zeitlichen Verlauf verschiedener Parameter der Verbrennungskraftmaschine 10 sowie der Abgasanlage 12 während einer NOX-Regeneration des NOX-Speicherkatalysators 18, die nach dem Stand der Technik erfolgt. Zunächst befindet sich die Verbrennungskraftmaschine 10 in einem mageren Betriebsmodus, in dem ihr ein sauerstoffreiches Luft-Kraftstoff-Gemisch mit λM » 1 zugeführt wird (Graph 100). In dieser Phase enthält das Abgas einen Überschuss an Stickoxiden NOX, die durch den Vorkatalysator 16 nicht vollständig konvertiert werden können. NOX wird daher in den NOX-Speicherkatalysator 18 eingelagert, dessen NOX-Beladung dabei kontinuierlich bis zur Sättigung NOXMAX zunimmt (Graph 102). Anhand eines geeigneten Kriteriums wird zu einem Zeitpunkt tA eine NOX-Regenerationsnotwendigkeit erkannt. Dies kann beispielsweise ein, durch den NOX-Sensor 20 detektierter NOX-Durchbruch sein. Infolgedessen wird die Verbrennungskraftmaschine 10 durch Einflussnahme des Motorsteuergerätes 22 in einen fetten Betriebsmodus umgeschaltet mit λF < 1. Infolge des nunmehr erhöhten Massenstroms der Reduktionsmittel CO und HC im Abgas wird das im NOX-Speicherkatalysator 18 eingelagerte NOX desorbiert und zu Stickstoff reduziert. Eine Abnahme der NOX-Beladung des Speicherkatalysators 18 (Graph 102) ist jedoch erst nach einer gewissen zeitlichen Verzögerung nach Umschaltung der Verbrennungskraftmaschine 10 zu verzeichnen, da zum Zeitpunkt tA der Abgaskanal 14 noch mit magerem Abgas gefüllt ist, welches zunächst noch den Speicherkatalysator 18 passieren muss, ehe die Reduktionsmittel diesen erreichen. Der Verlauf der NOX-Regeneration wird währenddessen mit Hilfe des von dem NOX-Sensor 20 bereitgestellten Signals Uλ verfolgt. Das Signal Uλ (Graph 104) verhält sich umgekehrt proportional zu einer Sauerstoffkonzentration des Abgases stromab des Speicherkatalysators 18. Da mit fortschreitender Regeneration die Reduktionsmittel in immer geringerem Ausmaß verbraucht werden, steigt das Signal Uλ des NOX-Sensors 20 langsam an. Zu einem Zeitpunkt tE erreicht das Signal Uλ einen vorgegebenen Schwellwert USE, woraufhin die Verbrennungskraftmaschine 10 üblicherweise wieder in einen mageren Betriebsmodus mit λM » 1 umgeschaltet wird. Zum Zeitpunkt des Regenerationsendes tE befindet sich jedoch noch Abgas mit einem hohen Reduktionsmittelanteil in dem Abgaskanal 14 zwischen der Verbrennungskraftmaschine 10 und dem Speicherkatalysator 18. Dieses durchströmt den Speicherkatalysator 18, der bis auf einen gewissen Restanteil gespeicherter Nitrate geleert ist, und gelangt unkonvertiert in die Umwelt. Der Verlauf der stromab des Katalysators gemessenen Konzentration von Kohlenmonoxid CO und unverbrannten Kohlenwasserstoffen HC (Graph 106) zeigt daher nach Regenerationsende tE noch einen unerwünscht hohen Anstieg. Der Graph 102 zeigt, dass nach der Regeneration im NOX-Speicherkatalysator 18 ein Rest an Nitraten verbleibt, so dass der Wert NOXMIN für die vollständige Entladung des NOX-Speicherkatalysators 18 nicht erreicht wird. Dies führt zu einer Verringerung der Effektivität der nachfolgenden Einlagerung von NOX, was wiederum einen erhöhten Kraftstoffverbrauch beziehungsweise eine höhere Emission von Schadstoffen bedingt.FIG. 2 shows the time profile of various parameters of the internal combustion engine 10 and of the exhaust system 12 during a NO x regeneration of the NO x storage catalytic converter 18, which takes place according to the prior art. First, the internal combustion engine 10 is in a lean mode of operation in which it is supplied with an oxygen-rich air-fuel mixture with λ M »1 (graph 100). In this phase, the exhaust gas contains an excess of nitrogen oxides NO x , which can not be completely converted by the precatalyst 16. NO x is therefore stored in the NO x storage catalytic converter 18, whose NO x charge increases continuously to saturation NO XMAX (graph 102). Based on a suitable criterion, a NO x regeneration need is recognized at a time t A. This may be, for example, a NO x breakthrough detected by the NO x sensor 20. As a result, the internal combustion engine 10 is switched by influencing the engine control unit 22 in a rich operating mode with λ F <1. Due to the now increased mass flow the reducing agent CO and HC in the exhaust gas is desorbed in the NO x storage 18 stored NO X and reduced to nitrogen. A decrease in the NO x charge of the storage catalytic converter 18 (graph 102), however, is recorded only after a certain time delay after switching the internal combustion engine 10, since at time t A of the exhaust duct 14 is still filled with lean exhaust gas, which initially still the storage catalytic converter 18 must happen before the reducing agents reach it. The course of the NO x regeneration is in the meantime tracked with the aid of the signal U λ provided by the NO x sensor 20. The signal U λ (graph 104) behaves inversely proportional to an oxygen concentration of the exhaust gas downstream of the storage catalytic converter 18. As the reducing agents are consumed to an increasing extent as regeneration progresses, the signal U λ of the NO X sensor 20 increases slowly. At a time t E , the signal U λ reaches a predetermined threshold value U SE , whereupon the internal combustion engine 10 is usually switched back into a lean operating mode with λ M »1. At the time of the regeneration end t E , however, there is still exhaust gas with a high proportion of reducing agent in the exhaust gas duct 14 between the internal combustion engine 10 and the storage catalytic converter 18. This flows through the storage catalytic converter 18, which is emptied of some stored nitrates, and enters the converter without conversion Environment. The course of the measured downstream of the catalyst concentration of carbon monoxide CO and unburned hydrocarbons HC (graph 106) therefore shows after regeneration end t E still an undesirably high increase. The graph 102 shows that after regeneration in the NO x storage catalyst 18, a residue of nitrates remains, so that the value NO XMIN for the complete discharge of the NO x storage 18 is not achieved. This leads to a reduction of the effectiveness of the subsequent storage of NO X , which in turn causes an increased fuel consumption or a higher emission of pollutants.

Um die Sättigung des NOX-Speicherkatalysators und die damit verbundene unvollständige Auslagerung der Nitrate in der Regenerationsphase zu verhindern, wird erfindungsgemäß der in Figur 3 dargestellte Ansatz verfolgt, wobei der zeitliche Verlauf der gleichen Parameter wie in Figur 2 und zusätzlich der Verlauf des Signals UNOX (Graph 108) des NOX-Sensors 20 für die NOX-Emission dargestellt ist. Die NOX-Emission steigt mit zunehmender Beladung des NOX-Speicherkatalysators 18 steil an, wobei zum Zeitpunkt tA bei Erreichen eines vorgegebenen Schwellwertes NOXSE, der durch Bilanzierung der NOX-Mengen vor und nach dem NOX-Speicherkatalysator 18 ermittelt wird und der in Relation zur Sättigung des NOX-Speicherkatalysators 18 steht, die Regeneration des NOX-Speicherkatalysators 18 eingeleitet wird. Der Schwellwert NOXSEwird vorab experimentell ermittelt und gibt den Punkt bei der NOX-Speicherbeladung an, bei dem bei einer nachfolgenden Regenerationsphase eine vollständige Entleerung des NOX-Speicherkatalysators noch möglich ist. Nach Einleitung der Regeneration fällt die NOX-Emission steil ab und verbleibt währenddessen auf konstant niedrigem Niveau. Der Verlauf der NOX-Beladung des NOX-Speicherkatalysators 18 - dargestellt durch Graph 102 - entspricht im Wesentlichen dem Verlauf gemäß Figur 2, da die Beladung und die Entleerung den gleichen Mechanismen unterliegen. Allerdings liegt der Graph 102 auf einem niedrigeren Niveau, da die Entleerung bei einem niedrigeren Beladungszustand beginnt und erst bei der vollständigen Entleerung endet.In order to prevent the saturation of the NO x storage catalyst and the associated incomplete removal of the nitrates in the regeneration phase, the approach shown in Figure 3 is pursued according to the invention, wherein the time course of the same parameters as in Figure 2 and in addition the course of the signal U NOX (graph 108) of the NOx sensor 20 is shown for the NO X emissions. The NO x emission increases sharply with increasing loading of the NO x storage catalytic converter 18, wherein at the time t A upon reaching a predetermined threshold value NO XSE , which is determined by balancing the NO x quantities before and after the NO x storage catalytic converter 18 and which is in relation to the saturation of the NO x storage 18, the regeneration of the NO x storage 18 is initiated. The threshold NO XSE is determined experimentally in advance and gives the point at the NO X storage loading, in which a complete emptying of the NO X storage catalytic converter is still possible in a subsequent regeneration phase. After initiation of the regeneration, the NO x emission drops steeply and remains at a constantly low level. The course of the NO x charge of the NO x storage catalytic converter 18-represented by graph 102-substantially corresponds to the course according to FIG. 2, since the loading and the discharge are subject to the same mechanisms. However, the graph 102 is at a lower level since the emptying begins at a lower loading condition and ends only at complete emptying.

Auch in Figur 4 werden zur Darstellung des erfindungsgemäßen Verfahrens die gleichen Parameter berücksichtigt wie bei der Figur 2. Zur Einleitung der Regeneration des NOX-Speicherkatalysators 18 wird zum Zeitpunkt tA die Temperatur des Speicherkatalysators 18 ermittelt und an das Motorsteuergerät 22 übermittelt, das anschließend die Verbrennungskraftmaschine 10 von einem mageren Betriebsmodus mit λM » 1 in einen fetten Modus mit λF < 1 umgeschaltet, wobei die ermittelte Katalysatortemperatur zur Festlegung eines optimierten Verbrennungslambdas herangezogen wird. In Abhängigkeit von der ermittelten Temperatur des NOX-Speicherkatalysators 18 wird ein Verbrennungslambda λF eingestellt, das höher (λFT1), niedriger (λFT2) oder gleich mit dem Verbrennungslambda λFT0 sein kann, das ohne die Bewertung der Temperatur des NOX-Speicherkatalysators 18 eingestellt worden wäre. Durch die Einstellung eines Verbrennungslambdas λF, das zumindest die Temperatur des NOX-Speicherkatalysators 18 als einen maßgeblichen Faktor berücksichtigt, wird gewährleistet, dass die zum Zeitpunkt tE am Ende einer Regenerationsphase vor dem NOX-Speicherkatalysator 18 befindlichen fetten Abgase noch zur Regeneration des NOX-Speicherkatalysators 18 genutzt werden können. Ein Reduktionsmitteldurchbruch kann somit deutlich verringert werden. Der Vergleich des Verlaufs des Graphen 106 mit dem in Figur 2, die die Konzentrationen von Kohlenmonoxid CO und unverbrannten Kohlenwasserstoffen HC stromab des NOX-Speicherkatalysators 18 darstellen, zeigt eine starke Verringerung der regenerationsbedingten Schadstoffemission.The same parameters as in FIG. 2 are also taken into account in FIG. 4 in order to illustrate the method according to the invention. To initiate the regeneration of the NO x storage catalytic converter 18, the temperature of the storage catalytic converter 18 is determined at time t A and transmitted to the engine control unit 22, which subsequently the internal combustion engine 10 of a lean mode with λ M »1 in a rich mode with λ F <1 switched, the determined catalyst temperature is used to establish an optimized combustion lambda. Depending on the determined temperature of the NO x storage catalytic converter 18, a combustion lambda λ F is set, which may be higher (λ FT1 ), lower (λ FT2 ) or equal to the combustion lambda λ FT0 , without the evaluation of the temperature of the NO x Storage Catalyst 18 would have been adjusted. By setting a combustion lambda λ F , which takes into account at least the temperature of the NO x storage 18 as a relevant factor, it is ensured that at the time t E at the end of a regeneration phase before the NO x storage catalytic converter 18 fat exhaust gases are still for regeneration of the NO x storage 18 can be used. A reducing agent breakthrough can thus be significantly reduced. Comparing the graph of graph 106 with that in FIG. 2, which illustrates the concentrations of carbon monoxide CO and unburned hydrocarbons HC downstream of NO x storage catalyst 18, shows a large reduction in pollutant emission due to regeneration.

BEZUGSZEICHENLISTELIST OF REFERENCE NUMBERS

1010
VerbrennungskraftmaschineInternal combustion engine
1212
Abgasanlageexhaust system
1414
Abgaskanalexhaust duct
1616
Vorkatalysatorprecatalyzer
1818
NOX-SpeicherkatalysatorNO X storage catalyst
2020
NOX-SensorNO x sensor
2222
MotorsteuergerätEngine control unit
2424
Steuereinheitcontrol unit
100100
Verbrennungslambdacombustion lambda
102102
NOX-Beladung des NOX-SpeicherkatalysatorsNO x charge of the NO x storage catalyst
104104
Signalverlauf (Uλ) der Lambdafunktion des NOX-SensorsSignal curve (U λ ) of the lambda function of the NO X sensor
106106
Reduktionsmittelgehalt im AbgasReducing agent content in the exhaust gas
108108
Signalverlauf (UNOX) der Lambdafunktion des NOX-SensorsSignal curve (U NOX ) of the lambda function of the NO X sensor
NOXMAX NO XMAX
Sättigungswert der NOX-Beladung des NOX-SpeicherkatalysatorsSaturation value of the NO x charge of the NO x storage catalyst
NOXMIN NO XMIN
Wert für vollständige Entladung des NOX-SpeicherkatalysatorsValue for complete discharge of the NO X storage catalytic converter
NOXSE NO XSE
Schwellwert zur Einleitung der NOX-RegenerationThreshold for the initiation of the NO x regeneration
tA t A
Regenerationsbeginnregeneration start
tE t E
Regenerationsenderegeneration end
UNOX U NOX
Signal des NOX-SensorsSignal from the NO X sensor
Uλ U λ
Signal der Lambdamessfunktion des NOX-SensorsSignal of the lambda measurement function of the NO X sensor
UλSE U λSE
Schwellwert zur Beendigung der NOX-RegenerationThreshold for ending the NO X regeneration
λM λ M
LambdamagerwertLambda lean value
λF, λFT0, λFT1, λFT2 λ F , λ FT0, λ FT1, λ FT2
LambdafettwertLambda fat value

Claims (10)

  1. Process for controlling an NOX regeneration of an NOX storage catalyst (18) downstream of an internal combustion engine (10), comprising an NOX-sensitive measuring device (20) arranged downstream of the NOX storage catalyst (18) and also comprising an engine control unit (24), the regeneration of the NOX storage catalyst (18) on attainment of a predefined threshold value (NOXSE) for the state of saturation of the NOX storage catalyst (18) being initiated by establishment of a rich air-fuel mixture (λF) of the internal combustion engine (10), characterized in that, at the start (tA) of the regeneration of the NOX storage catalyst (18), a current oxygen release behaviour of the oxygen-containing components in a catalyst coating of the NOX storage catalyst (18) on the basis of the catalyst temperature is evaluated and the rich air-fuel mixture (λF) supplied to the internal combustion engine (10) for regeneration is determined as a function at least of this evaluation.
  2. Process according to Claim 1, characterized in that, at the start (tA) of the regeneration of the NOX storage catalyst (18), the exhaust gas flow rate, the engine operating point and/or the catalyst state is additionally evaluated, and in that the rich air-fuel mixture (λF) is determined as a function of this evaluation.
  3. Process according to Claim 1 or 2, characterized in that the rich air-fuel mixture (λF) supplied for regeneration is additionally varied during the regeneration of the NOX storage catalyst (18).
  4. Process according to one of Claims 1 to 3, characterized in that the NOX-sensitive measuring device (20) used is an NOX sensor.
  5. Process according to one of Claims 1 to 3, characterized in that an oxygen-sensitive measuring device is also used in addition to the NOX-sensitive measuring device (20).
  6. Process according to Claim 5, characterized in that the oxygen-sensitive measuring device used is a λ broadband or step-response sensor.
  7. Process according to one of Claims 1 to 6, characterized in that catalyst/exhaust gas temperature, exhaust gas flow rate, untreated NOX flow rate, HC content of the lean exhaust gas are taken into account as correction factors of the threshold value (NOXSE).
  8. Process according to one of Claims 1 to 7, characterized in that the attainment of the threshold value (NOXSE) leads to the deactivation of the functionalities which assess the current storage capacity of the NOX storage catalyst (18).
  9. Process according to Claim 8, characterized in that the reversal of the deactivation is dependent upon a defined amount of reducing agent and/or a defined minimum number of regeneration operations.
  10. Process according to one of Claims 1 to 9, characterized in that the predefined threshold value (NOXSE) for the state of saturation of the NOX storage catalyst (18) is such that the regeneration leads to a conversion of all stored nitrogen oxides.
EP03090075A 2002-05-08 2003-03-20 Method for controling a NOx storage catalyst Expired - Lifetime EP1365131B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10221568 2002-05-08
DE10221568A DE10221568A1 (en) 2002-05-08 2002-05-08 Method for controlling a NO¶x¶ storage catalytic converter

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EP1365131A2 EP1365131A2 (en) 2003-11-26
EP1365131A3 EP1365131A3 (en) 2004-04-07
EP1365131B1 true EP1365131B1 (en) 2006-08-16

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10360072A1 (en) * 2003-12-20 2005-07-14 Audi Ag Exhaust system for an internal combustion engine of a vehicle, in particular of a motor vehicle
DE102004022814B4 (en) * 2004-05-08 2010-06-10 Audi Ag Method for operating a lean-running internal combustion engine of a vehicle, in particular of a motor vehicle

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0940570B1 (en) * 1998-01-09 2001-08-22 Ford Global Technologies, Inc. Method for regenerating a nitrogen oxide trap in the exhaust system of an internal combustion engine taking into account the exhaust gas mass flow
DE19851564C2 (en) * 1998-11-09 2000-08-24 Siemens Ag Method for operating and checking a NOx storage reduction catalytic converter of a lean-burn internal combustion engine
DE19929292A1 (en) * 1999-06-25 2000-12-28 Volkswagen Ag Control of the operating condition of motor vehicle internal combustion engine dependent upon the catalyst cell temperature uses set detected threshold levels to vary engine control parameters
DE19933712A1 (en) * 1999-07-19 2001-05-17 Volkswagen Ag Method for controlling an operating mode of an internal combustion engine

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DE10221568A1 (en) 2003-12-04
EP1365131A2 (en) 2003-11-26
EP1365131A3 (en) 2004-04-07
DE50304630D1 (en) 2006-09-28
ATE336650T1 (en) 2006-09-15

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