EP1188915A2 - Method for regulating the regeneration of a NOx storage catalyst - Google Patents
Method for regulating the regeneration of a NOx storage catalyst Download PDFInfo
- Publication number
- EP1188915A2 EP1188915A2 EP01119751A EP01119751A EP1188915A2 EP 1188915 A2 EP1188915 A2 EP 1188915A2 EP 01119751 A EP01119751 A EP 01119751A EP 01119751 A EP01119751 A EP 01119751A EP 1188915 A2 EP1188915 A2 EP 1188915A2
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- Prior art keywords
- regeneration
- catalytic converter
- storage catalytic
- storage
- lambda
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0807—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
- F01N3/0828—Exhaust 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
- F01N3/0842—Nitrogen oxides
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/021—Introducing corrections for particular conditions exterior to the engine
- F02D41/0235—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
- F02D41/027—Introducing 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
- F02D41/0275—Introducing 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/14—Introducing closed-loop corrections
- F02D41/1438—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
- F02D41/1439—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the position of the sensor
- F02D41/1441—Plural sensors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/14—Introducing closed-loop corrections
- F02D41/1438—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
- F02D41/1444—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
- F02D41/146—Introducing 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/14—Introducing closed-loop corrections
- F02D41/1438—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
- F02D41/1444—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
- F02D41/146—Introducing 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
- F02D41/1463—Introducing 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D2200/00—Input parameters for engine control
- F02D2200/02—Input parameters for engine control the parameters being related to the engine
- F02D2200/08—Exhaust gas treatment apparatus parameters
- F02D2200/0808—NOx storage capacity, i.e. maximum amount of NOx that can be stored on NOx trap
Definitions
- the invention relates to a method for controlling a NO x regeneration of a NO x storage catalytic converter with the features mentioned in the preamble of claim 1.
- the same catalyst systems for cleaning an exhaust gas from internal combustion engines, it is known to arrange the same catalyst systems in the exhaust line, which decompose the pollutant components of the exhaust gas into less environmentally relevant products.
- the pollutant components are reducing agents such as carbon monoxide CO or incompletely burned hydrocarbons, they can, if there is sufficient oxygen, be oxidized to carbon dioxide and water in so-called oxidation catalysts. It is also known to convert nitrogen oxides NO x formed during the combustion process back to nitrogen using the reducing agents.
- reduction catalysts have been developed which, if the reducing agents are provided to a sufficient extent, allow the NO x to be converted almost completely.
- a mass flow of reducing agent as well as an extent of NO x formation during the combustion process depend strongly on the mixture ratios prevailing during the combustion. In phases of rich or stoichiometric operation, a largely complete implementation on the NO x is guaranteed. If, however, the system is switched to lean operation, the NO x reduction is reduced due to an excess of oxygen. Since lean operation has proven to be particularly economical, but high NO x emissions should be avoided for environmental reasons, NO x storage components have been developed to remedy this. Such storage components sorb NO x in phases of lean operation and store this as nitrate. When changing to rich or stoichiometric operation, the NO x is desorbed again.
- the catalyst component for reducing the NO x and the storage component can be combined to form a so-called NO x storage catalyst.
- a storage capacity of the NO x storage catalytic converter is naturally limited. Such a NO x storage catalytic converter must therefore be regenerated at regular intervals. The NO x regeneration takes place by changing to stoichiometric or rich operation, the stored nitrate being desorbed again as NO x and reduced to nitrogen on the catalyst component with the aid of the reducing agents.
- the NO x regeneration in NO x storage catalytic converter systems is initiated, for example, after reaching a predefined NO x loading state or after exceeding a predefined NO x concentration downstream of the NO x storage catalytic converter. If there is a need for regeneration, a mass flow of reducing agent is increased by a motor intervention, for example in the area of the throttle valves or the injection system. The increase is usually achieved by lowering a lambda value upstream of the NO x storage catalytic converter to a predetermined rich setpoint.
- the NO x regeneration is generally terminated when the lambda value, or a lambda proportional voltage correlating therewith, on a gas probe arranged downstream of the NO x storage catalytic converter exceeds a predetermined threshold value (regeneration termination voltage threshold).
- a predetermined threshold value (regeneration termination voltage threshold).
- Both the regeneration termination voltage threshold and the rich target value for lambda during NO x regeneration are defined in the prior art regardless of the catalytic converter state. This is associated with the risk that the NO x regeneration of aged, ie damaged, NO x storage catalytic converters is not carried out as required.
- very large reducing agent mass flows and low regeneration termination voltage thresholds only a partial regeneration of the NO x storage catalytic converter can be expected.
- the high reducing agent mass flow is only partially used for NO x regeneration and thus shortly after the start of the NO x regeneration, a slightly rich exhaust gas passes through the NO x storage catalytic converter and leads to the termination of the NO x regeneration.
- this object is achieved by the method for regulating a NO x regeneration of a NO x storage catalytic converter arranged in the exhaust line of a lean-burn internal combustion engine with the features mentioned in claim 1.
- a damage state of the NO x storage catalytic converter is detected and, depending on the damage condition, a reducing agent mass flow during the NO x regeneration and / or a regeneration termination voltage threshold of a determining lambda gas probe arranged downstream of the NO x storage catalytic converter are specified.
- the parameters determining the NO x regeneration can be adapted to the actual catalyst state and an almost complete NO x regeneration can be ensured.
- the damage state of the NO x storage catalytic converter is assessed on the basis of a current NO x storage capacity in comparison to an NO x storage capacity of an undamaged NO x storage catalytic converter.
- the NO x storage capacity can be determined using known models on the basis of the signals of the exhaust gas cleaning system provided by the sensors. Here, variables such as a current NO x loading state and a remaining NO x storage capacity can be taken into account.
- the regeneration termination voltage threshold can be increased. The former measure reduces the likelihood of reducing agent mass breakthroughs, since an almost complete conversion in the NO x storage catalytic converter is still ensured even at high space velocities of the exhaust gas. By increasing the regeneration termination voltage threshold, a higher NO x breakthrough emission can be tolerated in addition or in combination.
- the exhaust gas purification system 12 comprises at least one NO x storage catalytic converter 14 and a suitable sensor system for detecting operating parameters in the exhaust line 16.
- This sensor system includes downstream and upstream of the NO x Storage catalytic converter 14 arranged gas probes, here the lambda probes 18, 20 and a NO x sensitive measuring device 22.
- the signals provided by the sensors are fed into an engine control unit 24 imported and evaluated there using stored algorithms.
- About the Engine control unit 24 can then perform a control intervention to change the during a Combustion process of the internal combustion engine 10 prevailing conditions respectively.
- a throttle valve 26 in an intake duct is an example of an actuator here 28 shown.
- a change can then be made by changing a throttle valve angle Intake volume of the internal combustion engine 10 are influenced.
- interventions in the combustion process especially one not here shown injection system - by varying injection parameters, such as one Injection duration, injection angle, injection volume and the like. Procedure and Devices for carrying out such control interventions are well known and are therefore not explained in more detail here. All that remains to be said is that in this way, a reducing agent mass flow is specifically increased or decreased can be.
- the engine control unit 24 is also integrated into a control unit 30, with which one Adaptation of a regeneration termination voltage threshold and / or the Reductant mass flow depending on a catalyst state can. For this purpose, a corresponding algorithm is stored in the control unit 30.
- the Control unit 30 can of course also be implemented as an independent unit become.
- the catalyst state can also be quantified using a model and made available to the further process, for example, as a percentage degree of damage.
- a current NO x storage capacity that is to say the NO x mass, which can be maximally sorbed by the NO x storage catalytic converter 14, serves in particular as the evaluation criteria.
- the NO x storage capacity can in turn be determined with the aid of known models in which a NO x mass flow upstream of the NO x storage catalytic converter 14 is detected and a NO x breakthrough emission downstream of the NO x storage catalytic converter is checked.
- the current catalytic converter state can then be characterized, for example, as 85% of a fresh NO x storage catalytic converter.
- FIG. 2 shows, for a fresh and a damaged NO x storage catalytic converter 14, on the one hand a voltage curve at the downstream lambda probe 20 and on the other hand target values SV i for lambda upstream of the NO x storage catalytic converter 14 and regeneration termination voltage thresholds S i .
- the voltage curve at the lambda probe 20 during the NO x regeneration of a fresh NO x storage catalytic converter is given by the curve 40 (bold solid line) and for the already damaged NO x storage catalytic converter by the curve 42 (dashed line).
- the internal combustion engine 10 then changes to a rich working mode, so that the NO x storage catalytic converter 14 is subjected to an increased mass flow of reducing agent.
- the target specifications SV i which are specified during this rich regeneration phase of the internal combustion engine 10 by suitably influencing the actuators for the lambda value upstream of the NO x storage catalytic converter 14, are dependent on the catalytic converter state. The same applies to the regeneration termination voltage thresholds S i , when they reach lambda probe 20, lean operation of internal combustion engine 10 is resumed.
- a curve 44 shows the target profile of lambda during NO x regeneration of a fresh NO x storage catalytic converter 14 (double, solid line).
- the curve 40 for the voltage signal at the lambda probe 20 shows a rapid increase, which results from the sudden increase in the reducing agent breakthrough emission. If the voltage reaches a regeneration termination voltage threshold S 1 , for example at 650 mV (time T E, 1 ), the internal combustion engine 10 is switched back to lean operation.
- the mass flow of reducing agent is reduced. This is done by appropriately specifying a target specification SV 2 for the rich regeneration phase - here, for example, to a lambda value of approximately 0.92. As a result of this, the mass flow of reducing agent also drops, so that it can be prevented that a slightly rich exhaust gas passes through the NO x storage catalytic converter 14 shortly after the start of the NO x regeneration and that the NO x regeneration is possibly incompletely terminated. Furthermore, the regeneration termination voltage threshold S 2 is also raised for this catalyst state in the present case.
Abstract
Description
Die Erfindung betrifft ein Verfahren zur Regelung einer NOx-Regeneration eines NOx-Speicherkatalysators
mit den im Oberbegriff des Anspruchs 1 genannten Merkmalen.The invention relates to a method for controlling a NO x regeneration of a NO x storage catalytic converter with the features mentioned in the preamble of
Zur Reinigung eines Abgases von Verbrennungskraftmaschinen ist es bekannt, im Abgasstrang derselben Katalysatorsysteme anzuordnen, die die Schadstoffkomponenten des Abgases in weniger umweltrelevante Produkte zersetzen. Handelt es sich bei den Schadstoffkomponenten um Reduktionsmittel wie Kohlenmonoxid CO oder unvollständig verbrannte Kohlenwasserstoffe, so können diese, sofern ausreichend Sauerstoff vorhanden ist, in sogenannten Oxidationskatalysatoren zu Kohlendioxid und Wasser aufoxidiert werden. Weiterhin ist es bekannt, während des Verbrennungsprozesses gebildete Stickoxide NOx mit Hilfe der Reduktionsmittel wieder zu Stickstoff umzusetzen. Dazu sind Reduktionskatalysatoren entwickelt worden, die, sofern die Reduktionsmittel in einem ausreichenden Maße zur Verfügung gestellt werden, eine nahezu vollständige Umsetzung des NOx erlauben.For cleaning an exhaust gas from internal combustion engines, it is known to arrange the same catalyst systems in the exhaust line, which decompose the pollutant components of the exhaust gas into less environmentally relevant products. If the pollutant components are reducing agents such as carbon monoxide CO or incompletely burned hydrocarbons, they can, if there is sufficient oxygen, be oxidized to carbon dioxide and water in so-called oxidation catalysts. It is also known to convert nitrogen oxides NO x formed during the combustion process back to nitrogen using the reducing agents. For this purpose, reduction catalysts have been developed which, if the reducing agents are provided to a sufficient extent, allow the NO x to be converted almost completely.
Ein Reduktionsmittel-Massenstrom als auch ein Umfang der NOx-Bildung während des Verbrennungsprozesses hängen stark von den während der Verbrennung herrschenden Gemischverhältnissen ab. In Phasen fetten oder stöchiometrischen Betriebs ist eine weitestgehend vollständige Umsetzung am NOx gewährleistet. Wird allerdings in einen Magerbetrieb geschaltet, so wird wegen eines Sauerstoffüberschusses die NOx-Reduktion verringert. Da sich der Magerbetrieb als besonders verbrauchsgünstig erwiesen hat, aber eine hohe NOx-Emission aus umweltrelevanten Gründen vermieden werden soll, sind zur Abhilfe NOx-Speicherkomponenten entwickelt worden. Derartige Speicherkomponenten sorbieren in Phasen mageren Betriebs NOx und lagern dieses als Nitrat ein. Beim Wechsel in den fetten oder stöchiometrischen Betrieb erfolgt wieder eine Desorption des NOx. Die Katalysatorkomponente zur Reduktion des NOx und die Speicherkomponente können zu einem sogenannten NOx-Speicherkatalysator zusammengefasst werden. A mass flow of reducing agent as well as an extent of NO x formation during the combustion process depend strongly on the mixture ratios prevailing during the combustion. In phases of rich or stoichiometric operation, a largely complete implementation on the NO x is guaranteed. If, however, the system is switched to lean operation, the NO x reduction is reduced due to an excess of oxygen. Since lean operation has proven to be particularly economical, but high NO x emissions should be avoided for environmental reasons, NO x storage components have been developed to remedy this. Such storage components sorb NO x in phases of lean operation and store this as nitrate. When changing to rich or stoichiometric operation, the NO x is desorbed again. The catalyst component for reducing the NO x and the storage component can be combined to form a so-called NO x storage catalyst.
Eine Speicherkapazität des NOx-Speicherkatalysators ist naturgemäß begrenzt. Daher muss ein derartiger NOx-Speicherkatalysator in regelmäßigen Abständen regeneriert werden. Die NOx-Regeneration erfolgt durch Wechsel in den stöchiometrischen oder fetten Betrieb, wobei das eingelagerte Nitrat wieder als NOx desorbiert und an der Katalysatorkomponente mit Hilfe der Reduktionsmittel zu Stickstoff reduziert wird.A storage capacity of the NO x storage catalytic converter is naturally limited. Such a NO x storage catalytic converter must therefore be regenerated at regular intervals. The NO x regeneration takes place by changing to stoichiometric or rich operation, the stored nitrate being desorbed again as NO x and reduced to nitrogen on the catalyst component with the aid of the reducing agents.
Die NOx-Regeneration bei NOx-Speicherkatalysatorsystemen wird beispielsweise nach Erreichen eines vorgegebenen NOx-Beladungszustandes oder nach Überschreiten einer vorgegebenen NOx-Konzentration stromab des NOx-Speicherkatalysators eingeleitet. Besteht Regenerationsnotwendigkeit so wird durch einen motorischen Eingriff, beispielsweise im Bereich der Drosselklappen oder des Einspritzsystems, ein Reduktionsmittel-Massenstrom erhöht. Zumeist erfolgt die Erhöhung dadurch, dass ein Lambdawert vor dem NOx-Speicherkatalysator auf einen vorgegebenen fetten Sollwert abgesenkt wird. Die NOx-Regeneration wird im Allgemeinen dann abgebrochen, wenn der Lambdawert, oder eine damit korrelierende lambdaproportionale Spannung an einer stromab des NOx-Speicherkatalysators angeordneten Gassonde, einen vorgegebenen Schwellenwert übersteigt (Regenerationsabbruch-Spannungsschwelle). Sowohl die Regenerationsabbruch-Spannungsschwelle als auch der fette Sollwert für Lambda während der NOx-Regeneration werden im Stand der Technik unabhängig vom Katalysatorzustand festgelegt. Damit ist das Risiko verbunden, dass bei gealterten, das heißt beschädigten, NOx-Speicherkatalysatoren die NOx-Regeneration nicht bedarfsgerecht durchgeführt wird. So ist bei sehr großen Reduktionsmittel-Massenströmen und niedrigen Regenerationsabbruch-Spannungsschwellen nur mit einer Teilregeneration des NOx-Speicherkatalysators zu rechnen. Der hohe Reduktionsmittel-Massenstrom wird nur teilweise zur NOx-Regeneration genutzt und somit tritt bereits kurz nach Beginn der NOx-Regeneration ein leicht fettes Abgas durch den NOx-Speicherkatalysator und führt zum Abbruch der NOx-Regeneration.The NO x regeneration in NO x storage catalytic converter systems is initiated, for example, after reaching a predefined NO x loading state or after exceeding a predefined NO x concentration downstream of the NO x storage catalytic converter. If there is a need for regeneration, a mass flow of reducing agent is increased by a motor intervention, for example in the area of the throttle valves or the injection system. The increase is usually achieved by lowering a lambda value upstream of the NO x storage catalytic converter to a predetermined rich setpoint. The NO x regeneration is generally terminated when the lambda value, or a lambda proportional voltage correlating therewith, on a gas probe arranged downstream of the NO x storage catalytic converter exceeds a predetermined threshold value (regeneration termination voltage threshold). Both the regeneration termination voltage threshold and the rich target value for lambda during NO x regeneration are defined in the prior art regardless of the catalytic converter state. This is associated with the risk that the NO x regeneration of aged, ie damaged, NO x storage catalytic converters is not carried out as required. With very large reducing agent mass flows and low regeneration termination voltage thresholds, only a partial regeneration of the NO x storage catalytic converter can be expected. The high reducing agent mass flow is only partially used for NO x regeneration and thus shortly after the start of the NO x regeneration, a slightly rich exhaust gas passes through the NO x storage catalytic converter and leads to the termination of the NO x regeneration.
Aufgabe der vorliegenden Erfindung ist es daher, ein gattungsgemäßes Verfahren zur Verfügung zu stellen, mit dem eine bedarfsgerechte Durchführung der NOx-Regeneration unter Berücksichtigung des Katalysatorzustandes erfolgen kann.It is therefore an object of the present invention to provide a generic method with which the NO x regeneration can be carried out as required, taking into account the state of the catalyst.
Erfindungsgemäß wird diese Aufgabe durch das Verfahren zur Regelung einer NOx-Regeneration
eines im Abgasstrang einer magerlauffähigen Verbrennungskraftmaschine
angeordneten NOx-Speicherkatalysators mit den im Anspruch 1 genannten Merkmalen
gelöst. Dadurch, dass ein Schädigungszustand des NOx-Speicherkatalysators erfasst
und in Abhängigkeit von dem Schädigungszustand ein Reduktionsmittel-Massenstrom
während der NOx-Regeneration und/oder eine Regenerationsabbruch-Spannungsschwelle
einer stromab des NOx-Speicherkatalysators angeordneten,
ermittelnden Lambda-Gassonde vorgegeben werden, kann eine Anpassung der die NOx-Regeneration
bestimmenden Parameter an den tatsächlichen Katalysatorzustand
erfolgen und eine nahezu vollständige NOx-Regeneration sichergestellt werden.According to the invention, this object is achieved by the method for regulating a NO x regeneration of a NO x storage catalytic converter arranged in the exhaust line of a lean-burn internal combustion engine with the features mentioned in
Nach einer bevorzugten Ausgestaltung des Verfahrens wird der Schädigungszustand des NOx-Speicherkatalysators anhand einer aktuellen NOx-Speicherkapazität im Vergleich zu einer NOx-Speicherfähigkeit eines ungeschädigten NOx-Speicherkatalysators beurteilt. Die NOx-Speicherkapazität kann mit bekannten Modellen anhand der von der Sensorik bereitgestellten Signale des Abgasreinigungssystems ermittelt werden. Hierbei können Größen, wie ein aktueller NOx-Beladungszustand und eine verbleibende NOx-Speicherfähigkeit, berücksichtigt werden.According to a preferred embodiment of the method, the damage state of the NO x storage catalytic converter is assessed on the basis of a current NO x storage capacity in comparison to an NO x storage capacity of an undamaged NO x storage catalytic converter. The NO x storage capacity can be determined using known models on the basis of the signals of the exhaust gas cleaning system provided by the sensors. Here, variables such as a current NO x loading state and a remaining NO x storage capacity can be taken into account.
Mit zunehmendem Schädigungsgrad des NOx-Speicherkatalysators kann dann zum einen der Reduktionsmittel-Massenstrom durch Regelung des Lambdawertes vor dem NOx-Speicherkatalysator verändert werden, insbesondere der Lambdawert während der NOx-Regeneration in Richtung λ = 1 verschoben werden. Zum anderen kann die Regenerationsabbruch-Spannungsschwelle erhöht werden. Erstere Maßnahme mindert die Wahrscheinlichkeit für Reduktionsmittel-Massendurchbrüche, da selbst bei hohen Raumgeschwindigkeiten des Abgases noch eine nahezu vollständige Umsetzung in dem NOx-Speicherkatalysator sichergestellt ist. Durch die Anhebung der Regenerationsabbruch-Spannungsschwelle kann daneben oder in Kombination eine höhere NOx-Durchbruchsemission toleriert werden.As the degree of damage to the NO x storage catalytic converter increases, the reducing agent mass flow can then be changed by regulating the lambda value upstream of the NO x storage catalytic converter, in particular the lambda value can be shifted in the direction λ = 1 during NO x regeneration. On the other hand, the regeneration termination voltage threshold can be increased. The former measure reduces the likelihood of reducing agent mass breakthroughs, since an almost complete conversion in the NO x storage catalytic converter is still ensured even at high space velocities of the exhaust gas. By increasing the regeneration termination voltage threshold, a higher NO x breakthrough emission can be tolerated in addition or in combination.
Weitere bevorzugte Ausgestaltungen der Erfindung ergeben sich aus den übrigen, in den Unteransprüchen genannten Merkmalen.Further preferred refinements of the invention result from the others in the Characteristics mentioned subclaims.
Die Erfindung wird nachfolgend in einem Ausführungsbeispiel anhand der zugehörigen Zeichnungen näher erläutert. Es zeigen:
Figur 1- eine schematische Anordnung eines NOx-Speicherkatalysators im Abgasstrang einer magerlauffähigen Verbrennungskraftmaschine und
Figur 2- Spannungsverläufe einer Lambdasonde während einer NOx-Regeneration eines frischen und eines geschädigten NOx-Speicherkatalysators sowie Sollvorgaben für Lambda stromauf des NOx-Speicherkatalysators und Regenerationsabbruch-Spannungsschwellen.
- Figure 1
- a schematic arrangement of a NO x storage catalyst in the exhaust line of a lean-burn internal combustion engine and
- Figure 2
- Voltage curves of a lambda probe during a NO x regeneration of a fresh and a damaged NO x storage catalytic converter as well as target values for lambda upstream of the NO x storage catalytic converter and regeneration termination voltage thresholds.
Die Figur 1 zeigt in einer schematischen Anordnung eine magerlauffähige
Verbrennungskraftmaschine 10 mit einer Abgasreinigungsanlage 12. Die
Abgasreinigungsanlage 12 umfasst zumindest einen NOx-Speicherkatalysator 14 sowie
eine geeignete Sensorik zur Erfassung von Betriebsparametern im Abgasstrang 16.
Diese Sensorik beinhaltet stromab und stromauf des NOx-Speicherkatalysators 14
angeordnete Gassonden, hier die Lambdasonden 18, 20 sowie eine NOx-sensitive
Messeinrichtung 22.1 shows a schematic arrangement of a lean-burn
Die von der Sensorik bereitgestellten Signale werden in ein Motorsteuergerät 24
eingelesen und dort anhand hinterlegter Algorithmen bewertet. Über das
Motorsteuergerät 24 kann dann ein Regeleingriff zur Änderung der während eines
Verbrennungsvorganges der Verbrennungskraftmaschine 10 herrschenden Verhältnisse
erfolgen. Beispielhaft ist hier als Stellglied eine Drosselklappe 26 in einem Ansaugkanal
28 dargestellt. Über eine Änderung eines Drosselklappenwinkels kann dann ein
Ansaugvolumen der Verbrennungskraftmaschine 10 beeinflusst werden. Denkbar sind
auch Eingriffe in den Verbrennungsprozess - insbesondere über ein hier nicht
dargestelltes Einspritzsystem - durch Variation von Einspritzparametern, wie eine
Einspritzdauer, Einspritzwinkel, Einspritzvolumen und dergleichen. Verfahren und
Vorrichtung zur Durchführung derartiger Regeleingriffe sind hinlänglich bekannt und
werden daher an dieser Stelle nicht näher erläutert. Festzuhalten bleibt lediglich, dass
auf diese Weise auch ein Reduktionsmittel-Massenstrom gezielt erhöht oder erniedrigt
werden kann.The signals provided by the sensors are fed into an
Das Motorsteuergerät 24 ist ferner an eine Steuereinheit 30 integriert, mit der eine
Adaption einer Regenerationsabbruch-Spannungsschwelle und/oder des
Reduktionsmittel-Massenstroms in Abhängigkeit von einem Katalysatorzustand erfolgen
kann. Dazu ist in der Steuereinheit 30 ein entsprechender Algorithmus hinterlegt. Die
Steuereinheit 30 kann selbstverständlich auch als selbstständige Einheit verwirklicht
werden. The
Auch der Katalysatorzustand kann mit Hilfe eines Modells quantifiziert werden und
beispielsweise als prozentualer Schädigungsgrad dem weiteren Verfahren zur Verfügung
gestellt werden. Dazu dient als Beurteilungskriterien insbesondere eine aktuelle NOx-Speicherkapazität,
also die NOx-Masse, die maximal von dem NOx-Speicherkatalysator
14 sorbiert werden kann. Die NOx-Speicherkapazität kann wiederum mit Hilfe bekannter
Modelle, bei denen ein NOx-Massenstrom stromauf des NOx-Speicherkatalysators 14
erfasst sowie eine NOx-Durchbruchsemission stromab des NOx-Speicherkatalysators
überprüft wird, ermittelt werden. Letztendlich lässt sich dann der aktuelle
Katalysatorzustand beispielsweise als 85 % eines frischen NOx-Speicherkatalysators
charakterisieren.The catalyst state can also be quantified using a model and made available to the further process, for example, as a percentage degree of damage. A current NO x storage capacity, that is to say the NO x mass, which can be maximally sorbed by the NO x storage
Die Figur 2 zeigt für einen frischen und einen geschädigten NOx-Speicherkatalysator 14
zum einen einen Spannungsverlauf an der stromab liegenden Lambdasonde 20 und zum
anderen Sollvorgaben SVi für Lambda stromauf des NOx-Speicherkatalysators 14 und
Regenerationsabbruch-Spannungsschwellen Si. Der Spannungsverlauf an der
Lambdasonde 20 während der NOx-Regeneration eines frischen NOx-Speicherkatalysators
ist durch die Kurve 40 (fette durchgezogene Linie) und für den
bereits geschädigten NOx-Speicherkatalysator durch die Kurve 42 (gestrichelte Linie)
gegeben. Zunächst liegt für gealterte NOx-Speicherkatalysatoren zu einem Zeitpunkt TR
eine Regenerationsnotwendigkeit vor. Diese kann beispielsweise mit Hilfe der NOx-sensitiven
Messeinrichtung 22 in bekannter Weise anhand einer detektierten NOx-Durchbruchsemission
ermittelt werden. Anschließend wechselt die
Verbrennungskraftmaschine 10 in einen fetten Arbeitsmodus, so dass der NOx-Speicherkatalysator
14 mit einem erhöhten Reduktionsmittel-Massenstrom beaufschlagt
wird. Die Sollvorgaben SVi, die während dieser fetten Regenerationsphase der
Verbrennungskraftmaschine 10 durch geeignete Beeinflussung der Stellglieder für den
Lambdawert vor dem NOx-Speicherkatalysator 14 vorgegeben werden, sind abhängig
vom Katalysatorzustand. Ebenso verhält es sich mit den Regenerationsabbruch-Spannungsschwellen
Si, bei deren Erreichen an der Lambdasonde 20 wieder ein
Magerbetrieb der Verbrennungskraftmaschine 10 aufgenommen wird.FIG. 2 shows, for a fresh and a damaged NO x storage
Eine Kurve 44 zeigt den Sollverlauf von Lambda bei NOx-Regeneration eines frischen
NOx-Speicherkatalysators 14 (doppelte, durchgezogene Linie). Um die NOx-Regeneration
möglichst zügig durchzuführen, wird eine relativ niedrige Sollvorgabe SV1,
beispielsweise bei λ = 0,85, gewählt. Gegen Ende der NOx-Regeneration zeigt die Kurve
40 für das Spannungssignal an der Lambdasonde 20 einen rasanten Anstieg, der aus
dem schlagartigen Anstieg der Reduktionsmittel-Durchbruchsemission resultiert. Erreicht
die Spannung eine Regenerationsabbruch-Spannungsschwelle S1, beispielsweise bei
650 mV (Zeitpunkt TE,1), so wird die Verbrennungskraftmaschine 10 wieder in den
Magerbetrieb geschaltet.A
Ist der NOx-Speicherkatalysator 14 bereits geschädigt, so wird der Reduktionsmittel-Massenstrom
gemindert. Dies erfolgt durch entsprechende Festlegung einer Sollvorgabe
SV2 für die fette Regenerationsphase - hier beispielsweise auf einen Lambdawert von
zirka 0,92. Damit einhergehend sinkt auch der Reduktionsmittel-Massenstrom, so dass
verhindert werden kann, dass bereits kurz nach Beginn der NOx-Regeneration ein leicht
fettes Abgas durch den NOx-Speicherkatalysator 14 durchtritt und gegebenenfalls die
NOx-Regeneration unvollständig abgebrochen wird. Weiterhin wird im vorliegenden Fall
auch die Regenerationsabbruch-Spannungsschwelle S2 für diesen Katalysatorzustand
angehoben. Hierdurch verlängert sich zusätzlich die fette Regenerationsphase, so dass
eine nahezu vollständige NOx-Regeneration des NOx-Speicherkatalysators 14
sichergestellt ist und erst zu einem Zeitpunkt TE,2 ein Wechsel in den Magerbetrieb erfolgt
(Kurve 46; doppelte, gestrichelte Linie). If the NO x storage
- 1010
- VerbrennungskraftmaschineInternal combustion engine
- 1212
- Abgasreinigungsanlageemission control system
- 1414
- NOx-SpeicherkatalysatorNO x storage catalytic converter
- 1818
- Abgasstrangexhaust gas line
- 18, 2018, 20
- Lambdasondenlambda probes
- 2222
- NOx-sensitive MesseinrichtungNO x sensitive measuring device
- 2424
- MotorsteuergerätEngine control unit
- 2626
- Drosselklappethrottle
- 2828
- Ansaugkanalintake port
- 3030
- Steuereinheitcontrol unit
- 4040
- Kurve für den Spannungsverlauf während der NOx-Regeneration eines frischen NOx-SpeicherkatalysatorsCurve for the voltage curve during the NO x regeneration of a fresh NO x storage catalytic converter
- 4242
- Kurve für den Spannungsverlauf während der NOx-Regeneration eines beschädigten NOx-SpeicherkatalysatorsCurve for the voltage curve during the NO x regeneration of a damaged NO x storage catalytic converter
- 4444
- Kurve für die Sollvorgaben von Lambda während der NOx-Regeneration eines frischen NOx-SpeicherkatalysatorsCurve for the target values of lambda during the NO x regeneration of a fresh NO x storage catalytic converter
- 4646
- Kurve für die Sollvorgaben von Lambda während der NOx-Regeneration eines beschädigten NOx-SpeicherkatalysatorsCurve for the target values of lambda during the NO x regeneration of a damaged NO x storage catalytic converter
- SVi SV i
- Sollvorgabe für Lambda im fetten ArbeitsmodusTarget specification for lambda in rich working mode
- Si S i
- Regenerationsabbruch-SpannungsschwelleRegeneration termination voltage threshold
- TR T R
- Zeitpunkt des Vorliegens der RegenerationsnotwendigkeitTime of the need for regeneration
- TE,i T E, i
- Zeitpunkte des Vorliegens der Regenerationsabbruch-SpannungsschwellenTimes of the existence of the regeneration termination voltage thresholds
Claims (6)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10045610 | 2000-09-15 | ||
DE2000145610 DE10045610A1 (en) | 2000-09-15 | 2000-09-15 | Method for controlling a NOx regeneration of a NOx storage catalytic converter |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1188915A2 true EP1188915A2 (en) | 2002-03-20 |
EP1188915A3 EP1188915A3 (en) | 2004-01-07 |
EP1188915B1 EP1188915B1 (en) | 2005-11-16 |
Family
ID=7656276
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20010119751 Expired - Lifetime EP1188915B1 (en) | 2000-09-15 | 2001-08-28 | Method for regulating the regeneration of a NOx storage catalyst |
Country Status (2)
Country | Link |
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EP (1) | EP1188915B1 (en) |
DE (2) | DE10045610A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1475636A1 (en) * | 2003-05-07 | 2004-11-10 | DaimlerChrysler AG | A method of determining the concentration of a gas component in the exhaust gas of an internal combustion engine |
WO2008029256A3 (en) * | 2006-09-06 | 2008-05-22 | Toyota Motor Co Ltd | Air-fuel ratio control apparatus and air-fuel ratio control method for internal combustion engine |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102019200367A1 (en) * | 2019-01-15 | 2020-07-16 | Ford Global Technologies, Llc | Method for determining regeneration parameter values of a multiple LNT catalyst system and device for data processing |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0903479A2 (en) * | 1997-09-19 | 1999-03-24 | Toyota Jidosha Kabushiki Kaisha | An exhaust gas purification device for an internal combustion engine |
EP0928890A2 (en) * | 1998-01-10 | 1999-07-14 | Degussa Aktiengesellschaft | Method for operating an NOx storage catalytic converter |
WO1999035386A1 (en) * | 1998-01-09 | 1999-07-15 | Ford Global Technologies, Inc. | Method for regenerating a nitrogen oxide trap in the exhaust system of an internal combustion engine |
DE19918875A1 (en) * | 1998-04-27 | 1999-10-28 | Denso Corp | Air fuel ratio control system for lean burn engine with oxygen and nitrogen oxides storage catalysts |
-
2000
- 2000-09-15 DE DE2000145610 patent/DE10045610A1/en not_active Withdrawn
-
2001
- 2001-08-28 EP EP20010119751 patent/EP1188915B1/en not_active Expired - Lifetime
- 2001-08-28 DE DE50108067T patent/DE50108067D1/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0903479A2 (en) * | 1997-09-19 | 1999-03-24 | Toyota Jidosha Kabushiki Kaisha | An exhaust gas purification device for an internal combustion engine |
WO1999035386A1 (en) * | 1998-01-09 | 1999-07-15 | Ford Global Technologies, Inc. | Method for regenerating a nitrogen oxide trap in the exhaust system of an internal combustion engine |
EP0928890A2 (en) * | 1998-01-10 | 1999-07-14 | Degussa Aktiengesellschaft | Method for operating an NOx storage catalytic converter |
DE19918875A1 (en) * | 1998-04-27 | 1999-10-28 | Denso Corp | Air fuel ratio control system for lean burn engine with oxygen and nitrogen oxides storage catalysts |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1475636A1 (en) * | 2003-05-07 | 2004-11-10 | DaimlerChrysler AG | A method of determining the concentration of a gas component in the exhaust gas of an internal combustion engine |
WO2008029256A3 (en) * | 2006-09-06 | 2008-05-22 | Toyota Motor Co Ltd | Air-fuel ratio control apparatus and air-fuel ratio control method for internal combustion engine |
Also Published As
Publication number | Publication date |
---|---|
DE50108067D1 (en) | 2005-12-22 |
DE10045610A1 (en) | 2002-04-18 |
EP1188915A3 (en) | 2004-01-07 |
EP1188915B1 (en) | 2005-11-16 |
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