WO2001051779A1 - METHOD AND DEVICE FOR CONTROL OF DESULPHURISATION OF AN NOx STORAGE CATALYST ARRANGED IN AN EXHAUST SYSTEM OF AN INTERNAL COMBUSTION ENGINE - Google Patents
METHOD AND DEVICE FOR CONTROL OF DESULPHURISATION OF AN NOx STORAGE CATALYST ARRANGED IN AN EXHAUST SYSTEM OF AN INTERNAL COMBUSTION ENGINE Download PDFInfo
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- WO2001051779A1 WO2001051779A1 PCT/EP2001/000249 EP0100249W WO0151779A1 WO 2001051779 A1 WO2001051779 A1 WO 2001051779A1 EP 0100249 W EP0100249 W EP 0100249W WO 0151779 A1 WO0151779 A1 WO 0151779A1
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- Prior art keywords
- desulfurization
- catalytic converter
- activity
- storage catalytic
- internal combustion
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Classifications
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- 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
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- 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
- F01N3/0871—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents using means for controlling, e.g. purging, the absorbents or adsorbents
- F01N3/0885—Regeneration of deteriorated absorbents or adsorbents, e.g. desulfurization of NOx traps
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- 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
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- 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
- F02D41/028—Desulfurisation of NOx traps or adsorbent
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- 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
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- 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
- F01N2570/00—Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
- F01N2570/04—Sulfur or sulfur oxides
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- 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
- F02D2200/0811—NOx storage efficiency
Definitions
- the invention relates to a method and a device for controlling a desulfurization of a NO x storage catalytic converter arranged in an exhaust gas duct of an internal combustion engine with the features mentioned in independent claims 1 and 13.
- aftertreat exhaust gases from internal combustion engines which are operated at least temporarily in a lean operating mode, with the aid of NO x storage catalytic converters.
- the NO x storage catalyst stores nitrogen oxides NO x , which in this phase are present in excess in the exhaust gas compared to reducing exhaust gas components, such as carbon monoxide or unburned hydrocarbons and therefore cannot be fully converted, in the form of nitrate.
- the storage catalytic converter is subjected to NO x regeneration at regular intervals or if the NO x storage capacity decreases, for which purpose the storage catalytic converter is charged with a rich exhaust gas atmosphere and a minimum catalytic converter temperature is set.
- the invention is based on the object of proposing a method for controlling desulfurization of a NO x storage catalytic converter, with the aid of which irreversible damage to the NO x storage catalytic converter can be identified and tracked.
- this object is achieved by a method and a device for controlling desulfurization of a NO x storage catalytic converter with the features mentioned in the independent claims.
- a NO x of the NO x -Speichermeditician - determined from a storage catalyst downstream of the NO x storage catalytic converter and the measured NO x concentration falls below a predetermined threshold value for the NO x activity of the NO x -Speicherkataiysators desulfurization with predeterminable Desulfurization parameters initiated.
- irreversible damage to the NO x storage catalytic converter is tracked on the basis of a desulfurization success and hard desulfurization is initiated if a predetermined damage limit value is exceeded, at least one desulfurization parameter being selected in accordance with a higher desulfurization efficiency, and further operation of the internal combustion engine from the level after hard desulfurization recovered NO x activity is made dependent. Carrying out the hard desulfurization ensures a quantitative sulfur output, even if previous ones
- Standard desulphurization should have been incomplete.
- the NO x storage activity recovered after the hard desulfurization can be directly correlated with an existing irreversible damage to the NO x storage catalytic converter. Consequently, permanent damage to the NO x storage catalytic converter which can no longer be tolerated can be recognized.
- the threshold value the lower value of which triggers a desulfurization
- the threshold value is reset after each desulfurization in such a way that it is proportional to an NO x starting activity of the NO x after the desulfurization has ended.
- Storage catalytic converter is.
- the damage limit value represents a minimum limit that cannot be undercut for ⁇ d Fe ⁇ O ⁇ storage efficiency td ar, the threshold value being greater than the damage limit value.
- the threshold value, the lower value of which triggers desulfurization is not varied.
- a desulfurization frequency increases with increasing irreversible damage to the catalyst, so that a predetermined maximum desulfurization frequency serves as the damage limit value.
- the damage limit value is specified as a lower limit of an initial NO x activity recovered after desulfurization.
- Desulfurization in particular hard desulfurization, is associated with higher fuel consumption and may influence the operating behavior of a vehicle. The initiation of desulfurization is therefore not desirable in every operating situation.
- An advantageous embodiment of the method therefore provides that, if the damage limit value is exceeded, lean operation of the internal combustion engine is first prohibited and hard desulfurization is only initiated when suitable, predetermined boundary conditions exist. This can be, for example, a minimum temperature of the NO x storage catalytic converter and / or a minimum vehicle speed that is maintained over a minimum period.
- the method according to the present invention provides that the further operation of the internal combustion engine after hard desulfurization is dependent on the desulfurization success, that is to say on the level of an initial NO x activity recovered after the desulfurization.
- a preferred embodiment provides that if after the end of hard desulfurization a recovered NO x starting activity corresponds almost completely or at least to a predetermined extent to that of a sulfur-free, NO x -free and undamaged NO x storage catalytic converter, lean operation of the internal combustion engine continues is allowed. In this case, it can be assumed that the loss of NO x storage activity observed before the hard desulfurization is due to sulfur storage and thus to incomplete, previous desulfurization and not to irreversible damage to the NO x storage catalyst. After a successful hard desulfurization measure, it is therefore further preferred that Adapt desulfurization parameters so adaptively that subsequent ones
- the device comprises means, for example a control unit, in which a procedure for controlling the process steps of the desulfurization of a NO x storage catalytic converter is stored in digital form.
- a control unit can advantageously be integrated in a mostly existing engine control unit.
- Figure 1 is a schematic diagram with an exhaust gas cleaning system
- FIG. 2 shows a time course of a NO x storage activity of a NO x .
- FIG. 3 shows a time course of a NO x storage activity of a NO x .
- FIG. 4 shows a flow chart of the method steps according to the invention in accordance with the exemplary embodiment shown in FIG. 2.
- FIG. 1 schematically shows an internal combustion engine 10 with a downstream exhaust line 12.
- a pre-catalytic converter 16 and an NO x storage catalytic converter 18 are arranged in an exhaust gas duct 14 of the exhaust line 12.
- the exhaust duct 14 also houses various instruments for recording selected operating parameters.
- the gas probes 20, 22 detect a concentration of a gas component in the exhaust gas.
- the gas probe 20 designed as a lambda probe serves to record an oxygen fraction after the internal combustion engine 10 and before the catalyst components 16, 18, while the NO x probe 22 measures a NO x concentration behind the NO x storage catalyst 18.
- the temperature sensors 24, 26 arranged in front of and behind the NO x storage catalytic converter 18 serve to determine a catalytic converter temperature.
- one or even both temperature sensors 24, 26 can be dispensed with and a temperature of the NO x storage catalytic converter can be derived empirically. All signals detected by the gas probes 20, 22 and the temperature sensors 24, 26 find their way into an engine control unit 28, where they are first digitized and then further processed in order to control an operating mode of the internal combustion engine 10.
- the engine control unit 28 regulates, for example, an air-fuel mixture to be fed into the internal combustion engine 10 by influencing a position of a throttle valve 30 in an intake pipe 32 and / or an exhaust gas recirculation device 34.
- the actuators 30, 34 shown by way of example can, for example, lean or an Fat mode for the internal combustion engine 10 can be set.
- a control unit 36 is also integrated in the engine control unit 28, in which a procedure for controlling the desulfurization of the NO x storage catalytic converter 18, which is explained in more detail below, is stored.
- the control unit 36 can also be implemented independently of the engine control unit 28.
- FIG. 2 shows the time course of a relative NO x activity NOA re
- the relative NO x activity denotes NOA re
- the NO x activity NOA itself here is the ratio of the NO x concentration measured behind the NO x storage catalytic converter 18 to the NO x probe 22 of the NO x concentration present in front of the NO x storage catalytic converter 18.
- the NO x concentration upstream of the NO x storage catalytic converter 18, that is to say the raw NO x emission, is preferably calculated by the engine control unit 28 on the basis of current operating parameters of the internal combustion engine 10. Alternatively, it can also be measured with a NO x probe arranged in front of the NO x storage catalytic converter 18 in the exhaust line 14. The calculation of the NO x activity NOA or the relative NO x activity NOA re
- the NO x storage catalytic converter 18 has the NO x activity NOA similar to that of a fresh catalytic converter, so that the relative NO x activity NOA re
- Falling below a first threshold value SW for the relative NO x activity triggers a first desulfurization 40 of the NO x storage catalytic converter 18 at the time t-
- a minimum temperature of the catalyst required for the desulfurization is set and the internal combustion engine 10 is operated in a rich operating mode in accordance with a lambda fat specification for a predetermined or regulated desulfurization period.
- a lambda fat specification for a predetermined or regulated desulfurization period.
- the rich-lean lambda specifications of the intervals, a switching frequency or a position of the rich-lean switching thresholds after the NO x storage catalytic converter 18 can be specified as additional desulfurization parameters.
- the position of the threshold value SW is redefined by the control unit 36 in accordance with a recovered relative NO x starting activity NOAMX, the threshold value SW preferably being proportional to the recovered NO x starting activity NOAMX.
- NOAMX a desulfurization NO x -Anfangsmodtician NOAMX corresponds with progressive operating time t less and less of a fresh NO x - storage catalyst and decreases with increasing aging of the catalyst.
- Reasons for this are, for example, incomplete desulfurization and / or irreversible thermal damage to the NO x storage catalytic converter 18.
- the threshold value SW As a result of the decreasing NO x starting activity NOAMX, the threshold value SW, the undershoot of which triggers desulfurization, is increasingly reduced.
- the cycles of the sulphurisation 38 and desulphurization 40 are repeated until the NO x activity NOA a not to be lower border threshold value, the Damage limit value SW
- the hard desulfurization is advantageously only initiated when predetermined boundary conditions, for example a minimum temperature of the NO x storage catalytic converter 18 and / or a minimum vehicle speed maintained over a minimum period, are present. In this way, the fuel consumption for the energetically extremely demanding hard desulfurization can be kept relatively low.
- the hard desulfurization 42 differs from the previous desulfurization 40 in that at least one of the desulfurization parameters mentioned (for example catalyst temperature, lambda, time specification) is selected in accordance with a higher desulfurization efficiency. For example, an extended desulfurization period and / or a lower lambda fat specification can be provided for the hard desulfurization 42.
- NOAMX different levels of NO x starting activities NOAMX are recovered after the hard desulfurization 42.
- the recovered NO x activity NOAMX corresponds approximately to that of a sulfur-free, undamaged catalyst.
- the catalytic converter 18 has practically no permanent damage and the previous loss of activity is due to incomplete, previous desulfurization 40.
- the hard desulfurization 42 does not completely restore the original NO x activity, but it does so to a considerable extent. This indicates the presence of irreversible damage to the catalyst but also incomplete desulfurization 40.
- both scenarios 44, 46 lean operation of the internal combustion engine 10 is still permitted, it being possible for a lower threshold value to be specified for the NO x starting activity NOAMX to be recovered.
- the desulfurization parameters for subsequent desulfurization are advantageously adaptively corrected such that improved subsequent desulfurization results can be expected.
- the correction of the desulfurization parameters is all the more important the less the irreversible damage to the NO x storage catalytic converter 18 and the higher the recovered NO x activity NOAMX after the hard desulfurization 42.
- hard desulfurization 42 is practically unsuccessful run. Extensive irreversible damage to the storage catalytic converter 18 must therefore be concluded here.
- the lean operation of the internal combustion engine 10 is finally blocked in this case.
- a warning display can also be provided, which informs a vehicle driver of the condition of the catalytic converter or indicates maintenance that becomes necessary.
- FIG. 3 A course of the relative NO x activity NOA re
- the threshold value SW for the NO x activity NOA is kept constant during the entire vehicle operation.
- the NO x starting activity NOAMX restored after desulfurization 40 decreases.
- the time interval ⁇ in which the NO x storage catalytic converter 18 stores sulfur in the lean mode of the internal combustion engine 10 until the threshold SW is reached becomes shorter and shorter. In other words, a frequency rises, with which desulfurization 40 becomes necessary.
- a criterion for recognizing the need for hard desulfurization 42 can consist in a predetermined maximum desulfurization frequency or in a lower threshold of an NO x starting activity NOAMX recovered after desulfurization. All other method features of this embodiment of the invention correspond to the features shown in FIG. 2 and are not to be explained again here.
- FIG. 4 shows a flow chart to explain the embodiment of the method shown in FIG. 2.
- the process sequence begins with step S1, in which the internal combustion engine 10 is subjected to a lean atmosphere, that is to say with a lambda value> 1.
- step S2 the calculation of the NO x activity NOA based on the measured NO x from the NO probe 22 takes place x - concentration downstream of the NO x storing catalyst 18.
- the NO x -Speichermeditician NOA is compared in step S3 with the threshold value SW , If the NO x activity NOA is above the threshold value SW, the method goes to step S1 and the internal combustion engine 10 continues to be operated in the lean mode.
- step S3 If, on the other hand, it is determined in step S3 that the threshold value SW has been reached or fallen below, the NO x activity NOA is compared with the damage limit value SW
- step S8 a query is made in step S8 as to whether the recovered NO x activity NOAMX is less than a predetermined threshold value SWMX. If this question is answered in the negative, a new threshold value SW is calculated in step S6 as a function of the NO x starting activity NOAMX, whereupon the lean operation is again permitted in step S1. If, on the other hand, the desulfurization success cannot be determined in step S8, the lean operation is finally blocked in step S9.
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Abstract
Description
Verfahren und Vorrichtung zur Steuerung einer Entschwefelung eines in einem Abgaskanal einer Verbrennungskraftmaschine angeordneten Method and device for controlling desulfurization in an exhaust gas duct of an internal combustion engine
NOx-SpeicherkatalysatorsNO x storage catalytic converter
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zur Steuerung einer Entschwefelung eines in einem Abgaskanal einer Verbrennungskraftmaschine angeordneten NOx-Speicherkatalysators mit den in den unabhängigen Ansprüchen 1 und 13 genannten Merkmalen.The invention relates to a method and a device for controlling a desulfurization of a NO x storage catalytic converter arranged in an exhaust gas duct of an internal combustion engine with the features mentioned in independent claims 1 and 13.
Es ist bekannt, eine Nachbehandlung von Abgasen von Verbrennungskraftmaschinen, die zumindest zeitweise in einem mageren Betriebsmodus betrieben werden, mit Hilfe von NOx-Speicherkatalysatoren zu betreiben. Während eines mageren Betriebsmodus lagert dabei der NOx-Speicherkatalysator Stickoxide NOx, die in dieser Phase gegenüber reduzierenden Abgasbestandteilen, wie Kohlenmonoxid oder unverbrannten Kohlenwasserstoffen, in einem Überschuß im Abgas vorhanden sind und daher nicht vollständig umgesetzt werden können, in Form von Nitrat ein. In regelmäßigen Abständen beziehungsweise bei einer nachlassenden NOx-Speicherfähigkeit wird der Speicherkatalysator einer NOx-Regeneration unterworfen, wofür der Speicherkatalysator mit einer fetten Abgasatmosphäre beaufschlagt und eine Mindest- Katalysatortemperatur eingestellt wird.It is known to aftertreat exhaust gases from internal combustion engines, which are operated at least temporarily in a lean operating mode, with the aid of NO x storage catalytic converters. During a lean operating mode, the NO x storage catalyst stores nitrogen oxides NO x , which in this phase are present in excess in the exhaust gas compared to reducing exhaust gas components, such as carbon monoxide or unburned hydrocarbons and therefore cannot be fully converted, in the form of nitrate. The storage catalytic converter is subjected to NO x regeneration at regular intervals or if the NO x storage capacity decreases, for which purpose the storage catalytic converter is charged with a rich exhaust gas atmosphere and a minimum catalytic converter temperature is set.
Neben der NOx-Absorption findet eine unerwünschte Einlagerung von Schwefeloxiden im NOx-Speicherkatalysator statt. Die Schwefeleinlagerung ist unter den Bedingungen einer NOx-Regeneration nicht reversibel, wodurch es zu einer zunehmenden Verschwefelung des Speicherkatalysators kommt, die eine NOx-Speicherkapazität herabsetzt. Darüber hinaus kann eine Agglomeration von Schwefel zu einer Bildung von Sulfatkörnern führen, die eine katalytische Aktivität des NOx-Speicherkatalysators irreversibel schädigen können. Die Entfernung solcher Sulfatkörner wird mit steigender Korngröße zunehmend schwieriger. Es ist daher bekannt, in regelmäßigen Abständen eine Entschwefelung des NOx-Speicherkatalysators durchzuführen, wobei der eingelagerte Schwefel bei Katalysatortemperaturen von über 650 °C und unter Beaufschlagung mit einer fetten Abgasatmosphäre hauptsächlich in Form von Schwefeldioxid SO2 und Schwefelwasserstoff H2S ausgetragen wird. Neben der irreversiblen Schädigung durch Sulfatkornbildung sind weitere dauerhafte Schädigungsarten bekannt, die zu einer nachlassenden Speicherkapazität des Katalysators beitragen. Hier ist in erster Linie eine thermische Schädigung von Bedeutung.In addition to the NO x absorption, there is an undesirable incorporation of sulfur oxides in the NO x storage catalytic converter. The sulfur storage is not reversible under the conditions of NO x regeneration, which leads to increasing sulfurization of the storage catalyst, which reduces the NO x storage capacity. In addition, an agglomeration of sulfur can lead to the formation of sulfate grains, which can irreversibly damage a catalytic activity of the NO x storage catalyst. The removal of such sulfate grains becomes increasingly difficult with increasing grain size. It is therefore known to carry out a desulfurization of the NO x storage catalyst at regular intervals, the stored sulfur being discharged mainly in the form of sulfur dioxide SO2 and hydrogen sulfide H2S at catalyst temperatures of over 650 ° C. and when exposed to a rich exhaust gas atmosphere. In addition to the irreversible damage caused by the formation of sulfate grains, other permanent types of damage are known which contribute to a reduction in the storage capacity of the catalyst. Thermal damage is of primary importance here.
Der Erfindung liegt die Aufgabe zugrunde, ein Verfahren zur Steuerung einer Entschwefelung eines NOx-Speicherkatalysators vorzuschlagen, mit dessen Hilfe eine irreversible Schädigung des NOx-Speicherkatalysators erkannt und verfolgt werden kann.The invention is based on the object of proposing a method for controlling desulfurization of a NO x storage catalytic converter, with the aid of which irreversible damage to the NO x storage catalytic converter can be identified and tracked.
Erfindungsgemäß wird diese Aufgabe durch ein Verfahren und eine Vorrichtung zur Steuerung einer Entschwefelung eines NOx-Speicherkatalysators mit den in den unabhängigen Ansprüchen genannten Merkmalen gelöst. Gemäß dem erfindungsgemäßen Verfahren wird eine NOx-Speicheraktivität des NOx- Speicherkatalysators aus einer stromab des NOx-Speicherkatalysators gemessenen NOx-Konzentration ermittelt und bei Unterschreitung eines vorgebbaren Schwellenwertes für die NOx-Aktivität des NOx-Speicherkataiysators eine Entschwefelung mit vorgebbaren Entschwefelungsparametern eingeleitet. Ferner wird anhand eines Entschwefelungserfolges eine irreversible Schädigung des NOx- Speicherkatalysators verfolgt und bei Überschreitung eines vorgegebenen Schädigungsgrenzwertes eine harte Entschwefelung eingeleitet, wobei mindestens ein Entschwefelungsparameter entsprechend einer höheren Entschwefelungswirksamkeit gewählt wird, und ein weiterer Betrieb der Verbrennungskraftmaschine von der Höhe einer nach der harten Entschwefelung wiedergewonnenen NOx-Aktivität abhängig gemacht wird. Die Durchführung der harten Entschwefelung gewährleistet einen quantitativen Schwefelaustrag, auch wenn vorausgegangeneAccording to the invention, this object is achieved by a method and a device for controlling desulfurization of a NO x storage catalytic converter with the features mentioned in the independent claims. According to the inventive method, a NO x of the NO x -Speicheraktivität - determined from a storage catalyst downstream of the NO x storage catalytic converter and the measured NO x concentration falls below a predetermined threshold value for the NO x activity of the NO x -Speicherkataiysators desulfurization with predeterminable Desulfurization parameters initiated. Furthermore, irreversible damage to the NO x storage catalytic converter is tracked on the basis of a desulfurization success and hard desulfurization is initiated if a predetermined damage limit value is exceeded, at least one desulfurization parameter being selected in accordance with a higher desulfurization efficiency, and further operation of the internal combustion engine from the level after hard desulfurization recovered NO x activity is made dependent. Carrying out the hard desulfurization ensures a quantitative sulfur output, even if previous ones
Standardentschwefelungen unvollständig abgelaufen sein sollten. Somit kann die nach der harten Entschwefelung wiedergewonnene NOx-Speicheraktivität direkt mit einer vorliegenden irreversiblen Schädigung des NOx-Speicherkatalysators korreliert werden. Folglich kann eine nicht mehr tolerierbare dauerhafte Schädigung des NOx- Speicherkatalysators erkannt werden.Standard desulphurization should have been incomplete. Thus, the NO x storage activity recovered after the hard desulfurization can be directly correlated with an existing irreversible damage to the NO x storage catalytic converter. Consequently, permanent damage to the NO x storage catalytic converter which can no longer be tolerated can be recognized.
Die Erfindung läßt verschiedene Verfahrensvarianten zur Vorgabe des Schädigungsgrenzwertes zu. Entsprechend einer bevorzugten Ausgestaltung wird der Schwellenwert, dessen Unterschreitung eine Entschwefelung auslöst, nach jeder Entschwefelung derart neu vorgegeben, daß er proportional zu einer nach Beendigung der Entschwefelung wiedergewonnenen NOx-Anfangsaktivität des NOx- Speicherkatalysators ist. In d esem Fall stellt der Schädigungsgrenzwert einen nicht zu unterschreitenden minimalen G re nzwe rt f ü r~ d Fe^O^Spe i cheräkti vifät Td a r, wobei der Schwellenwert größer ist als der Schädigungsgrenzwert. Gemäß einer alternativen Ausgestaltung wird der Schwellenwert, dessen Unterschreitung eine Entschwefelung auslöst, nicht variiert. Entsprechend dieser Variante nimmt mit zunehmender irreversibler Schädigung des Katalysators eine Entschwefelungsfrequenz zu, so daß als Schädigungsgrenzwert eine vorgegebene maximale Entschwefelungsfrequenz dient. Gemäß einer weiteren alternativen Ausgestaltung, bei der der Schwellenwert ebenfalls konstant ist, wird der Schädigungsgrenzwert als eine untere Grenze einer nach einer Entschwefelung wiedergewonnenen NOx-Anfangsaktivität angegeben.The invention permits various process variants for specifying the damage limit value. According to a preferred embodiment, the threshold value, the lower value of which triggers a desulfurization, is reset after each desulfurization in such a way that it is proportional to an NO x starting activity of the NO x after the desulfurization has ended. Storage catalytic converter is. In this case, the damage limit value represents a minimum limit that cannot be undercut for ~ d Fe ^ O ^ storage efficiency td ar, the threshold value being greater than the damage limit value. According to an alternative embodiment, the threshold value, the lower value of which triggers desulfurization, is not varied. According to this variant, a desulfurization frequency increases with increasing irreversible damage to the catalyst, so that a predetermined maximum desulfurization frequency serves as the damage limit value. According to a further alternative embodiment, in which the threshold value is also constant, the damage limit value is specified as a lower limit of an initial NO x activity recovered after desulfurization.
Die Durchführung einer Entschwefelung, insbesondere einer harten Entschwefelung, geht mit einem höheren Kraftstoffverbrauch einher und kann gegebenenfalls das Betriebsverhalten eines Fahrzeuges beeinflussen. Die Einleitung einer Entschwefelung ist somit nicht in jeder Betriebssituation erwünscht. Daher sieht eine vorteilhafte Ausführungsform des Verfahrens vor, daß bei Überschreitung des Schädigungsgrenzwertes zunächst ein Magerbetrieb der Verbrennungskraftmaschine verboten wird und eine harte Entschwefelung erst eingeleitet wird, wenn geeignete, vorgegebene Randbedingungen vorliegen. Dies kann etwa eine Mindesttemperatur des NOx-Speicherkatalysators und/oder eine über eine Mindestdauer eingehaltene Mindestfahrzeuggeschwindigkeit sein.Desulfurization, in particular hard desulfurization, is associated with higher fuel consumption and may influence the operating behavior of a vehicle. The initiation of desulfurization is therefore not desirable in every operating situation. An advantageous embodiment of the method therefore provides that, if the damage limit value is exceeded, lean operation of the internal combustion engine is first prohibited and hard desulfurization is only initiated when suitable, predetermined boundary conditions exist. This can be, for example, a minimum temperature of the NO x storage catalytic converter and / or a minimum vehicle speed that is maintained over a minimum period.
Das Verfahren gemäß der vorliegenden Erfindung sieht vor, den weiteren Betrieb der Verbrennungskraftmaschine nach einer harten Entschwefelung von dem Entschwefelungserfolg, das heißt von der Höhe einer nach der Entschwefelung wiedergewonnenen NOx-Anfangsaktivität, abhängig zu machen. Eine bevorzugte Ausgestaltung sieht vor, daß, wenn nach Beendigung einer harten Entschwefelung eine wiedergewonnene NOx-Anfangsaktivität nahezu vollständig oder in wenigstens einem vorgegebenen Umfang der eines schwefelfreien, NOx-freien und nicht geschädigten NOx-Speicherkatalysators entspricht, ein Magerbetrieb der Verbrennungskraftmaschine weiterhin zugelassen wird. In diesem Fall kann nämlich davon ausgegangen werden, daß der vor der harten Entschwefelung beobachtete Verlust der NOx-Speicheraktivität auf eine Schwefeleinlagerung und damit auf unvollständig abgelaufene, vorausgegangene Entschwefelungen zurückzuführen ist und nicht auf eine irreversible Schädigung des NOx-Speicherkatalysators. Nach einer erfolgreichen harten Entschwefelungsmaßnahme ist es daher ferner bevorzugt, die Entschwefelungsparameter derart adaptiv anzupassen, daß nachfolgendeThe method according to the present invention provides that the further operation of the internal combustion engine after hard desulfurization is dependent on the desulfurization success, that is to say on the level of an initial NO x activity recovered after the desulfurization. A preferred embodiment provides that if after the end of hard desulfurization a recovered NO x starting activity corresponds almost completely or at least to a predetermined extent to that of a sulfur-free, NO x -free and undamaged NO x storage catalytic converter, lean operation of the internal combustion engine continues is allowed. In this case, it can be assumed that the loss of NO x storage activity observed before the hard desulfurization is due to sulfur storage and thus to incomplete, previous desulfurization and not to irreversible damage to the NO x storage catalyst. After a successful hard desulfurization measure, it is therefore further preferred that Adapt desulfurization parameters so adaptively that subsequent ones
Entschwefelungen wirkungsvoller ablaufen.Desulphurization works more effectively.
Wenn dagegen eine harte Entschwefelung weitestgehend erfolglos abläuft und eine wiedergewonnene NOx-Anfangsaktivität nicht signifikant höher liegt als eine nach der letzten Entschwefelung vorliegende NOx-Anfangsaktivität, wird auf eine starke irreversible Schädigung des NOx-Speicherkatalysators geschlossen und ein Magerbetrieb der Verbrennungskraftmaschine eingeschränkt oder gesperrt, um die NOx-Emission geringzuhalten. Es ist ferner denkbar, einen Fahrzeugführer beispielsweise durch eine Wamanzeige von einer Wartungsnotwendigkeit des Katalysators in Kenntnis zu setzen.If, on the other hand, hard desulfurization is largely unsuccessful and an initial NO x activity recovered is not significantly higher than an initial NO x activity present after the last desulfurization, a strong irreversible damage to the NO x storage catalytic converter is concluded and lean operation of the internal combustion engine is restricted or locked to keep the NO x emissions low. It is also conceivable to inform a driver of a need for maintenance of the catalytic converter, for example by means of a warning.
Es weiterhin bevorzugt vorgesehen, daß die Vorrichtung Mittel umfaßt, beispielsweise eine Steuereinheit, in der eine Prozedur zur Steuerung der Verfahrensschritte der Entschwefelung eines NOx-Speicherkatalysators in digitaler Form abgelegt ist. Eine solche Steuereinheit kann vorteilhafterweise in ein zumeist vorhandenes Motorsteuergerät integriert sein.It is further preferably provided that the device comprises means, for example a control unit, in which a procedure for controlling the process steps of the desulfurization of a NO x storage catalytic converter is stored in digital form. Such a control unit can advantageously be integrated in a mostly existing engine control unit.
Weitere bevorzugte Ausgestaltungen der Erfindung ergeben sich aus den übrigen, in den Unteransprüchen genannten Merkmalen.Further preferred embodiments of the invention result from the other features mentioned in the subclaims.
Die Erfindung wird nachfolgend in Ausführungsbeispielen anhand der zugehörigen Zeichnungen näher erläutert. Es zeigen:The invention is explained in more detail below in exemplary embodiments with reference to the associated drawings. Show it:
Figur 1 eine Prinzipdarstellung mit einer Abgasreinigungsanlage undFigure 1 is a schematic diagram with an exhaust gas cleaning system and
Mitteln zur Steuerung der Entschwefelung eines NOx- Speicherkatalysators;Means for controlling the desulfurization of a NO x storage catalytic converter;
Figur 2 einen zeitlichen Verlauf einer NOx-Speicheraktivität eines NOx-FIG. 2 shows a time course of a NO x storage activity of a NO x .
Speicherkatalysators gemäß einer bevorzugten Ausgestaltung der Erfindung;Storage catalytic converter according to a preferred embodiment of the invention;
Figur 3 einen zeitlichen Verlauf einer NOx-Speicheraktivität eines NOx-FIG. 3 shows a time course of a NO x storage activity of a NO x .
Speicherkatalysators gemäß einer weiteren bevorzugten Ausführungsform der vorliegenden Erfindung und Figur 4 ein Ablaufdiagramm der erfindungsgemäßen Verfahrensschritte gemäß dem in Figur 2 dargestellten Ausführungsbeispiel.Storage catalyst according to a further preferred embodiment of the present invention and FIG. 4 shows a flow chart of the method steps according to the invention in accordance with the exemplary embodiment shown in FIG. 2.
Die Figur 1 zeigt in schematischer Weise eine Verbrennungskraftmaschine 10 mit einem nachgeschalteten Abgasstrang 12. In einem Abgaskanal 14 des Abgasstranges 12 ist ein Vorkatalysator 16 sowie ein NOx-Speicherkatalysator 18 angeordnet. Der Abgaskanal 14 beherbergt ferner verschiedene Instrumente zur Erfassung ausgewählter Betriebsparameter. So erfassen beispielsweise die Gassonden 20, 22 eine Konzentration einer Gaskomponente im Abgas. Im vorliegenden Beispiel dient die als Lambda-Sonde ausgestaltete Gassonde 20 einer Erfassung eines Sauerstoffanteils nach der Verbrennungskraftmaschine 10 und vor den Katalysatorkomponenten 16, 18, während die NOx-Sonde 22 eine NOx-Konzentration hinter dem NOx- Speicherkatalysator 18 mißt. Die vor und hinter dem NOx-Speicherkatalysator 18 angeordneten Temperatursensoren 24, 26 dienen der Ermittlung einer Katalysatortemperatur. Alternativ kann auf eine oder sogar auf beide Temperatursensoren 24, 26 verzichtet werden und eine Temperatur des NOx- Speicherkatalysators empirisch abgeleitet werden. Alle von den Gassonden 20, 22 und den Temperatursensoren 24, 26 erfaßten Signale finden Eingang in ein Motorsteuergerät 28, wo sie zunächst digitalisiert und dann weiterverarbeitet werden, um einen Betriebsmodus der Verbrennungskraftmaschine 10 zu steuern. Hierfür regelt das Motorsteuergerät 28 beispielsweise ein in die Verbrennungskraftmaschine 10 einzuspeisendes Luft-Kraftstoff-Gemisch, indem es eine Stellung einer Drosselklappe 30 in einem Ansaugrohr 32 beeinflußt und/oder eine Abgasrückführeinrichtung 34. Durch die exemplarisch aufgezeigten Stellglieder 30, 34 kann beispielsweise ein Mageroder ein Fettmodus für die Verbrennungskraftmaschine 10 eingestellt werden.FIG. 1 schematically shows an internal combustion engine 10 with a downstream exhaust line 12. A pre-catalytic converter 16 and an NO x storage catalytic converter 18 are arranged in an exhaust gas duct 14 of the exhaust line 12. The exhaust duct 14 also houses various instruments for recording selected operating parameters. For example, the gas probes 20, 22 detect a concentration of a gas component in the exhaust gas. In the present example, the gas probe 20 designed as a lambda probe serves to record an oxygen fraction after the internal combustion engine 10 and before the catalyst components 16, 18, while the NO x probe 22 measures a NO x concentration behind the NO x storage catalyst 18. The temperature sensors 24, 26 arranged in front of and behind the NO x storage catalytic converter 18 serve to determine a catalytic converter temperature. Alternatively, one or even both temperature sensors 24, 26 can be dispensed with and a temperature of the NO x storage catalytic converter can be derived empirically. All signals detected by the gas probes 20, 22 and the temperature sensors 24, 26 find their way into an engine control unit 28, where they are first digitized and then further processed in order to control an operating mode of the internal combustion engine 10. For this purpose, the engine control unit 28 regulates, for example, an air-fuel mixture to be fed into the internal combustion engine 10 by influencing a position of a throttle valve 30 in an intake pipe 32 and / or an exhaust gas recirculation device 34. The actuators 30, 34 shown by way of example can, for example, lean or an Fat mode for the internal combustion engine 10 can be set.
In das Motorsteuergerät 28 ist ferner eine Steuereinheit 36 integriert, in der eine Prozedur zur Steuerung der Entschwefelung des NOx-Speicherkatalysators 18, die nachfolgend näher erläutert wird, hinterlegt ist. Alternativ kann die Steuereinheit 36 auch unabhängig von dem Motorsteuergerät 28 realisiert werden.A control unit 36 is also integrated in the engine control unit 28, in which a procedure for controlling the desulfurization of the NO x storage catalytic converter 18, which is explained in more detail below, is stored. Alternatively, the control unit 36 can also be implemented independently of the engine control unit 28.
Die Figur 2 stellt den zeitlichen Verlauf einer relativen NOx-Aktivität NOAre| eines NOx- Speicherkatalysators 18 dar. Dabei bezeichnet die relative NOx-Aktivität NOAre| das Verhältnis der NOx-Aktivität NOA des vorliegenden NOx-Speicherkatalysators 18 zu der NOx-Aktivität eines NOx- und schwefelfreien und ungeschädigten NOx- Speicherkatalysators. Die NOx-Aktivität NOA selbst ist hier als Verhältnis der hinter dem NOx-Speicherkatalysator 18 mit der NOx-Sonde 22 gemessenen NOx-Konzentration zu der vor dem NOx-Speicherkatalysator 18 vorliegenden NOx-Konzentration definiert. Die NOx-Konzentration vor dem NOx-Speicherkatalysator 18, also die NOx-Rohemission, wird vorzugsweise von dem Motorsteuergerät 28 anhand aktueller Betriebsparameter der Verbrennungskraftmaschine 10 berechnet. Alternativ kann sie auch mit einer vor dem NOx-Speicherkatalysator 18 im Abgasstrang 14 angeordneten NOx-Sonde gemessen werden. Die Berechnung der NOx-Aktivität NOA beziehungsweise der relativen NOx-Aktivität NOAre| erfolgt in dem Motorsteuergerät 28, in dem auch die NOx-Aktivität des NOx- und schwefelfreien ungeschädigten NOx-Speicherkatalysators gespeichert ist. Zu Beginn eines Fahrzeugbetriebes weist der NOx-Speicherkatalysator 18 die NOx-Aktivität NOA ähnlich der eines frischen Katalysators auf, so daß die relative NOx-Aktivität NOAre| zunächst einen Wert nahe "1" annimmt. Im folgenden Verlauf kommt es zu einer zunehmenden Verschwefelung des Katalysators 18, so daß die relative NOx-Aktivität NOAre| zunehmend abfällt. Die Unterschreitung eines ersten Schwellenwertes SW für die relative NOx-Aktivität löst eine erste Entschwefelung 40 des NOx-Speicherkatalysators 18 zum Zeitpunkt t-| aus. Entsprechend den vorgegebenen Entschwefelungsparametern wird eine für die Entschwefelung notwendige Mindesttemperatur des Katalysators eingestellt und die Verbrennungskraftmaschine 10 über eine vorgegebene oder geregelte Entschwefelungsdauer in einem fetten Betriebsmodus entsprechend einer Lambda- Fettvorgabe betrieben. Zur Unterdrückung einer H2S-Emission ist bekannt, die Entschwefelung in Fett-Mager-Intervallen zu betreiben. In diesem Fall sind als zusätzliche Entschwefelungsparameter beispielsweise die Fett-Mager-Lambdavorgaben der Intervalle, eine Umschaltfrequenz beziehungsweise eine Lage der Fett-Mager- Umschaltschwellen nach dem NOx-Speicherkatalysator 18 vorgebbar. Nach Beendigung einer Entschwefelung 40 wird entsprechend einer wiedergewonnenen relativen NOx-Anfangsaktivität NOAMX die Lage des Schwellenwertes SW durch die Steuereinheit 36 neu festgelegt, wobei der Schwellenwert SW vorzugsweise proportional zur wiedergewonnenen NOx-Anfangsaktivität NOAMX ist. Die nach Beendigung einer Entschwefelung vorliegende NOx-Anfangsaktivität NOAMX entspricht mit fortschreitender Betriebsdauer t immer weniger der eines frischen NOx- Speicherkatalysators und sinkt mit zunehmender Alterung des Katalysators. Ursachen hierfür sind beispielsweise unvollständige Entschwefelungen und/oder irreversible thermische Schädigungen des NOx-Speicherkatalysators 18. Infolge der sich verringernden NOx-Anfangsaktivität NOAMX wird der Schwellenwert SW, dessen Unterschreitung eine Entschwefelung auslöst, zunehmend weiter herabgesetzt. Die Zyklen der Verschwefelung 38 und Entschwefelung 40 wiederholen sich solange, bis die NOx-Aktivität NOA einen nicht zu unterschreitenden unteren Schwellenwert, den Schädigungsgrenzwert SW|^, zum Zeitpunkt t5 erreicht. Die Unterschreitung des Schädigungsgrenzwertes SWJR führt zunächst zu einer Umschaltung der Verbrennungskraftmaschine 10 von einem mageren Betriebsmodus in einen stöchiometrischen oder fetten Betriebsmodus, um die NOx-Emission geringzuhalten. Die harte Entschwefelung wird vorteilhafterweise erst dann eingeleitet, wenn vorgegebene Randbedingungen, beispielsweise eine Mindesttemperatur des NOx- Speicherkatalysators 18 und/oder eine über eine Mindestdauer eingehaltene Mindestfahrzeuggeschwindigkeit, vorliegen. Auf diese Weise kann der Kraftstoffverbrauch für die energetisch äußerst anspruchsvolle harte Entschwefelung relativ geringgehalten werden. Die harte Entschwefelung 42 unterscheidet sich gegenüber den vorausgegangenen Entschwefelungen 40, indem mindestens einer der genannten Entschwefelungsparameter (zum Beispiel Katalysatortemperatur, Lambda, Zeitvorgabe) entsprechend einer höheren Entschwefelungswirksamkeit gewählt wird. Beispielsweise kann für die harte Entschwefelung 42 eine verlängerte Entschwefelungsdauer und/oder eine niedrigere Lambda-Fettvorgabe vorgesehen sein.FIG. 2 shows the time course of a relative NO x activity NOA re | of a NO x storage catalytic converter 18. The relative NO x activity denotes NOA re | the ratio of the NO x activity NOA of the present NO x storage catalytic converter 18 to the NO x activity of a NO x and sulfur-free and undamaged NO x storage catalytic converter. The NO x activity NOA itself here is the ratio of the NO x concentration measured behind the NO x storage catalytic converter 18 to the NO x probe 22 of the NO x concentration present in front of the NO x storage catalytic converter 18. The NO x concentration upstream of the NO x storage catalytic converter 18, that is to say the raw NO x emission, is preferably calculated by the engine control unit 28 on the basis of current operating parameters of the internal combustion engine 10. Alternatively, it can also be measured with a NO x probe arranged in front of the NO x storage catalytic converter 18 in the exhaust line 14. The calculation of the NO x activity NOA or the relative NO x activity NOA re | takes place in the engine control unit 28, in which the NO x activity of the NO x and sulfur-free undamaged NO x storage catalytic converter is stored. At the start of vehicle operation, the NO x storage catalytic converter 18 has the NO x activity NOA similar to that of a fresh catalytic converter, so that the relative NO x activity NOA re | initially assumes a value close to "1". In the following course, there is an increasing sulfurization of the catalyst 18, so that the relative NO x activity NOA re | increasingly falling. Falling below a first threshold value SW for the relative NO x activity triggers a first desulfurization 40 of the NO x storage catalytic converter 18 at the time t- | out. In accordance with the predetermined desulfurization parameters, a minimum temperature of the catalyst required for the desulfurization is set and the internal combustion engine 10 is operated in a rich operating mode in accordance with a lambda fat specification for a predetermined or regulated desulfurization period. In order to suppress H2S emission, it is known to carry out the desulfurization in fat-lean intervals. In this case, the rich-lean lambda specifications of the intervals, a switching frequency or a position of the rich-lean switching thresholds after the NO x storage catalytic converter 18 can be specified as additional desulfurization parameters. After a desulfurization 40 has ended, the position of the threshold value SW is redefined by the control unit 36 in accordance with a recovered relative NO x starting activity NOAMX, the threshold value SW preferably being proportional to the recovered NO x starting activity NOAMX. The present after completion of a desulfurization NO x -Anfangsaktivität NOAMX corresponds with progressive operating time t less and less of a fresh NO x - storage catalyst and decreases with increasing aging of the catalyst. Reasons for this are, for example, incomplete desulfurization and / or irreversible thermal damage to the NO x storage catalytic converter 18. As a result of the decreasing NO x starting activity NOAMX, the threshold value SW, the undershoot of which triggers desulfurization, is increasingly reduced. The cycles of the sulphurisation 38 and desulphurization 40 are repeated until the NO x activity NOA a not to be lower border threshold value, the Damage limit value SW | ^, reached at time t5. Falling below the damage limit value SWJR initially leads to the internal combustion engine 10 being switched from a lean operating mode to a stoichiometric or rich operating mode in order to keep the NO x emission low. The hard desulfurization is advantageously only initiated when predetermined boundary conditions, for example a minimum temperature of the NO x storage catalytic converter 18 and / or a minimum vehicle speed maintained over a minimum period, are present. In this way, the fuel consumption for the energetically extremely demanding hard desulfurization can be kept relatively low. The hard desulfurization 42 differs from the previous desulfurization 40 in that at least one of the desulfurization parameters mentioned (for example catalyst temperature, lambda, time specification) is selected in accordance with a higher desulfurization efficiency. For example, an extended desulfurization period and / or a lower lambda fat specification can be provided for the hard desulfurization 42.
In Abhängigkeit von einer vorliegenden irreversiblen Schädigung des NOx- Speicherkatalysators 18 werden unterschiedlich hohe NOx-Anfangsaktivitäten NOAMX nach der harten Entschwefelung 42 wiedergewonnen. In einem mit 44 bezeichneten Szenarium entspricht die wiedergewonnene NOx-Aktivität NOAMX annähernd der eines schwefelfreien ungeschädigten Katalysators. In diesem Fall kann davon ausgegangen werden, daß der Katalysator 18 praktisch keine dauerhaften Schädigungen aufweist und der vorausgegangene Aktivitätsverlust auf unvollständige, vorausgegangene Entschwefelungen 40 zurückzuführen ist. Im Szenarium 46 wird durch die harte Entschwefelung 42 zwar die ursprüngliche NOx-Aktivität nicht vollständig, aber in erheblichem Umfang wiederhergestellt. Dies deutet auf das Vorliegen von irreversiblen Schädigungen des Katalysators aber auch auf unvollständig abgelaufene Entschwefelungen 40 hin. In beiden Szenarien 44, 46 wird ein Magerbetrieb der Verbrennungskraftmaschine 10 weiterhin zugelassen, wobei für die wiederzugewinnende NOx-Anfangsaktivität NOAMX ein unterer Schwellenwert vorgegeben werden kann. Vorteilhafterweise werden in beiden Fällen 44, 46 die Entschwefelungsparameter für nachfolgende Entschwefelungen derart adaptiv korrigiert, daß verbesserte nachfolgende Entschwefelungserfolge erwartet werden können. Die Korrektur der Entschwefelungsparameter ist um so wichtiger, je geringer die irreversible Schädigung des NOx-Speicherkatalysators 18 und je höher die wiedergewonnene NOx-Aktivität NOAMX nach der harten Entschwefelung 42 ist. Entsprechend dem Szenario 48 ist die harte Entschwefelung 42 praktisch ohne Erfolg verlaufen. Hier muß also auf eine umfangreiche irreversible Schädigung des Speicherkatalysators 18 geschlossen werden. Um weitere NOx-Emissionen zu unterbinden, wird in diesem Fall der Magerbetrieb der Verbrennungskraftmaschine 10 endgültig gesperrt. Optional kann auch eine Warnanzeige vorgesehen sein, die einen Fahrzeugführer von dem Zustand des Katalysators in Kenntnis setzt beziehungsweise auf eine notwendig werdende Wartung hinweist.Depending on the irreversible damage to the NO x storage catalytic converter 18, different levels of NO x starting activities NOAMX are recovered after the hard desulfurization 42. In a scenario denoted by 44, the recovered NO x activity NOAMX corresponds approximately to that of a sulfur-free, undamaged catalyst. In this case it can be assumed that the catalytic converter 18 has practically no permanent damage and the previous loss of activity is due to incomplete, previous desulfurization 40. In scenario 46, the hard desulfurization 42 does not completely restore the original NO x activity, but it does so to a considerable extent. This indicates the presence of irreversible damage to the catalyst but also incomplete desulfurization 40. In both scenarios 44, 46, lean operation of the internal combustion engine 10 is still permitted, it being possible for a lower threshold value to be specified for the NO x starting activity NOAMX to be recovered. In both cases 44, 46, the desulfurization parameters for subsequent desulfurization are advantageously adaptively corrected such that improved subsequent desulfurization results can be expected. The correction of the desulfurization parameters is all the more important the less the irreversible damage to the NO x storage catalytic converter 18 and the higher the recovered NO x activity NOAMX after the hard desulfurization 42. In accordance with scenario 48, hard desulfurization 42 is practically unsuccessful run. Extensive irreversible damage to the storage catalytic converter 18 must therefore be concluded here. In order to prevent further NO x emissions, the lean operation of the internal combustion engine 10 is finally blocked in this case. Optionally, a warning display can also be provided, which informs a vehicle driver of the condition of the catalytic converter or indicates maintenance that becomes necessary.
Ein Verlauf der relativen NOx-Aktivität NOAre| entsprechend einer anderen bevorzugten Ausgestaltung der Erfindung ist in der Figur 3 dargestellt. Hier wird der Schwellenwert SW für die NOx-Aktivität NOA während des gesamten Fahrzeugbetriebes konstant gehalten. Mit einer zunehmenden Alterung des NOx-Speicherkatalysators 18 sinkt die nach einer Entschwefelung 40 wiederhergestellte NOx-Anfangsaktivität NOAMX. Infolgedessen wird das Zeitintervall τ, in dem der NOx-Speicherkatalysator 18 im Magermodus der Verbrennungskraftmaschine 10 bis zum Erreichen der Schwelle SW Schwefel einlagert, immer kürzer. Mit anderen Worten: Es steigt eine Frequenz, mit der eine Entschwefelung 40 notwendig wird. Ein Kriterium zum Erkennen des Notwendigwerdens einer harten Entschwefelung 42 kann in einer vorgegebenen maximalen Entschwefelungsfrequenz bestehen oder aber auch in einer unteren Schwelle einer nach einer Entschwefelung wiedergewonnenen NOx-Anfangsaktivität NOAMX. Alle weiteren Verfahrensmerkmale dieser Ausführungsform der Erfindung entsprechen den in Figur 2 dargestellten Merkmalen und sollen hier nicht nochmals erläutert werden.A course of the relative NO x activity NOA re | according to another preferred embodiment of the invention is shown in Figure 3. Here the threshold value SW for the NO x activity NOA is kept constant during the entire vehicle operation. With increasing aging of the NO x storage catalytic converter 18, the NO x starting activity NOAMX restored after desulfurization 40 decreases. As a result, the time interval τ in which the NO x storage catalytic converter 18 stores sulfur in the lean mode of the internal combustion engine 10 until the threshold SW is reached becomes shorter and shorter. In other words, a frequency rises, with which desulfurization 40 becomes necessary. A criterion for recognizing the need for hard desulfurization 42 can consist in a predetermined maximum desulfurization frequency or in a lower threshold of an NO x starting activity NOAMX recovered after desulfurization. All other method features of this embodiment of the invention correspond to the features shown in FIG. 2 and are not to be explained again here.
Die Figur 4 zeigt ein Ablaufdiagramm zur Erläuterung der in Figur 2 dargestellten Ausführungsform des Verfahrens. Der Verfahrensablauf beginnt mit dem Schritt S1 , in dem die Verbrennungskraftmaschine 10 mit einer mageren Atmosphäre, das heißt mit einem Lambdawert > 1 , beaufschlagt wird. Im Schritt S2 erfolgt die Berechnung der NOx-Aktivität NOA auf Grundlage der von der NOx-Sonde 22 gemessenen NOx- Konzentration hinter dem NOx-Speicherkatalysator 18. Die NOx-Speicheraktivität NOA wird im Schritt S3 mit dem Schwellenwert SW verglichen. Liegt die NOx-Aktivität NOA über dem Schwellenwert SW geht das Verfahren in Schritt S1 über und die Verbrennungskraftmaschine 10 wird weiterhin in dem Magermodus betrieben. Wird dagegen im Schritt S3 festgestellt, daß der Schwellenwert SW erreicht beziehungsweise unterschritten wurde, erfolgt im Schritt S4 der Vergleich der NOx- Aktivität NOA mit dem Schädigungsgrenzwert SW|R. Ist der Schädigungsgrenzwert SW|R noch nicht erreicht oder unterschritten, wird im Schritt S5 eine Entschwefelung mit den vorgegebenen Entschwefelungsparametern eingeleitet. Nach Beendigung der Entschwefelung wird im Schritt S6 die wiedergewonnenene NOx-Aktivität NOAMX ermittelt und der Schwellenwert SW in Abhängigkeit von der ermittelten Anfangsaktivität NOAMX neu berechnet. Wird auf der anderen Seite im Schritt S4 festgestellt, daß die NOx-Aktivität NOA den Schädigungsgrenzwert SW|R erreicht oder unterschritten hat, so wird im Schritt S7 eine harte Entschwefelung eingeleitet. Nach Beendigung der harten Entschwefelung erfolgt im Schritt S8 die Abfrage, ob die wiedergewonnene NOx- Aktivität NOAMX kleiner als ein vorgegebener Schwellenwert SWMX ist. Wird diese Frage verneint, erfolgt im Schritt S6 die Berechnung eines neuen Schwellenwertes SW in Abhängigkeit von der NOx-Anfangsaktivität NOAMX, woraufhin der Magerbetrieb im Schritt S1 wieder zugelassen wird. Kann dagegen im Schritt S8 der Entschwefelungserfolg nicht festgestellt werden, so wird der Magerbetrieb im Schritt S9 endgültig gesperrt. FIG. 4 shows a flow chart to explain the embodiment of the method shown in FIG. 2. The process sequence begins with step S1, in which the internal combustion engine 10 is subjected to a lean atmosphere, that is to say with a lambda value> 1. In step S2, the calculation of the NO x activity NOA based on the measured NO x from the NO probe 22 takes place x - concentration downstream of the NO x storing catalyst 18. The NO x -Speicheraktivität NOA is compared in step S3 with the threshold value SW , If the NO x activity NOA is above the threshold value SW, the method goes to step S1 and the internal combustion engine 10 continues to be operated in the lean mode. If, on the other hand, it is determined in step S3 that the threshold value SW has been reached or fallen below, the NO x activity NOA is compared with the damage limit value SW | R in step S4. If the damage limit value SW | R has not yet been reached or fallen below, a desulfurization with the predetermined desulfurization parameters is initiated in step S5. After completing the Desulphurization, the recovered NO x activity NOAMX is determined in step S6 and the threshold value SW is recalculated as a function of the determined initial activity NOAMX. If, on the other hand, it is determined in step S4 that the NO x activity NOA has reached or fallen below the damage limit value SW | R, hard desulfurization is initiated in step S7. After hard desulfurization has ended, a query is made in step S8 as to whether the recovered NO x activity NOAMX is less than a predetermined threshold value SWMX. If this question is answered in the negative, a new threshold value SW is calculated in step S6 as a function of the NO x starting activity NOAMX, whereupon the lean operation is again permitted in step S1. If, on the other hand, the desulfurization success cannot be determined in step S8, the lean operation is finally blocked in step S9.
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP01902302A EP1252419B1 (en) | 2000-01-15 | 2001-01-11 | Method and device for control of desulphurisation of a nox storage catalyst arranged in an exhaust system of an internal combustion engine |
| AU2001230174A AU2001230174A1 (en) | 2000-01-15 | 2001-01-11 | Method and device for control of desulphurisation of an nox storage catalyst arranged in an exhaust system of an internal combustion engine |
| JP2001551959A JP4619603B2 (en) | 2000-01-15 | 2001-01-11 | Method and apparatus for controlling desulfurization of NOx storage catalyst disposed in an exhaust gas passage of an internal combustion engine |
| DE50108667T DE50108667D1 (en) | 2000-01-15 | 2001-01-11 | METHOD AND DEVICE FOR CONTROLLING DISCHARGE OF A NOX MEMORY CATALYST ARRANGED IN AN EXHAUST CHANNEL OF AN INTERNAL COMBUSTION ENGINE |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE2000101432 DE10001432A1 (en) | 2000-01-15 | 2000-01-15 | Method and device for controlling desulphurization of a NO¶x¶ storage catalytic converter arranged in an exhaust gas duct of an internal combustion engine |
| DE10001432.1 | 2000-01-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2001051779A1 true WO2001051779A1 (en) | 2001-07-19 |
Family
ID=7627577
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2001/000249 Ceased WO2001051779A1 (en) | 2000-01-15 | 2001-01-11 | METHOD AND DEVICE FOR CONTROL OF DESULPHURISATION OF AN NOx STORAGE CATALYST ARRANGED IN AN EXHAUST SYSTEM OF AN INTERNAL COMBUSTION ENGINE |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP1252419B1 (en) |
| JP (1) | JP4619603B2 (en) |
| CN (1) | CN1185405C (en) |
| AU (1) | AU2001230174A1 (en) |
| DE (2) | DE10001432A1 (en) |
| ES (1) | ES2256197T3 (en) |
| WO (1) | WO2001051779A1 (en) |
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| US7493755B2 (en) | 2004-06-23 | 2009-02-24 | Peugeot Citroen Automobiles Sa | System for assisting the regeneration of depollution means for a motor vehicle engine |
| US7694511B2 (en) | 2004-06-23 | 2010-04-13 | Peugeot Citroen Automobiles Sa | System for controlling depollution means regeneration |
| EP1766214B1 (en) * | 2004-06-23 | 2011-03-16 | Peugeot Citroën Automobiles S.A. | System for assisting the regeneration of depollution means for a motor vehicle engine |
| EP2980377A1 (en) * | 2014-08-01 | 2016-02-03 | Toyota Jidosha Kabushiki Kaisha | Exhaust gas purification apparatus for internal combustion engine |
| EP2868885A4 (en) * | 2012-06-19 | 2017-01-18 | Toyota Jidosha Kabushiki Kaisha | Exhaust purification device for internal combustion engine |
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| DE10114456B4 (en) * | 2000-04-07 | 2011-03-31 | Volkswagen Ag | Apparatus and method for coordinating exhaust gas-relevant measures |
| DE10102132B4 (en) * | 2001-01-18 | 2009-12-10 | Volkswagen Ag | Method and device for desulphurizing a NOx storage catalytic converter |
| DE10115962B4 (en) * | 2001-03-27 | 2009-03-05 | Volkswagen Ag | Process for the desulfurization of an arranged in the exhaust line of an internal combustion engine NOx storage catalyst |
| DE10249609B4 (en) * | 2002-10-18 | 2011-08-11 | Volkswagen AG, 38440 | Method for controlling a NOx storage catalytic converter |
| FR2862703B1 (en) * | 2003-11-25 | 2006-02-24 | Peugeot Citroen Automobiles Sa | A NOX TRAP DESULFATATION SYSTEM FOR MOTOR VEHICLE ENGINE |
| US7481046B2 (en) * | 2005-02-28 | 2009-01-27 | Ford Global Technologies, Llc | Method of desulfating a NOx storage and conversion device |
| JP4404073B2 (en) * | 2006-06-30 | 2010-01-27 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP2009024505A (en) * | 2007-07-17 | 2009-02-05 | Toyota Motor Corp | Exhaust purification device |
| CN113482752B (en) * | 2021-07-02 | 2022-06-24 | 东风商用车有限公司 | Packaging method of diesel engine post-processing packaging unit |
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Also Published As
| Publication number | Publication date |
|---|---|
| JP2003519744A (en) | 2003-06-24 |
| EP1252419A1 (en) | 2002-10-30 |
| ES2256197T3 (en) | 2006-07-16 |
| DE10001432A1 (en) | 2001-08-16 |
| DE50108667D1 (en) | 2006-04-06 |
| EP1252419B1 (en) | 2006-01-11 |
| AU2001230174A1 (en) | 2001-07-24 |
| CN1185405C (en) | 2005-01-19 |
| CN1395648A (en) | 2003-02-05 |
| JP4619603B2 (en) | 2011-01-26 |
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