DE102007041897B4 - Method and device for operating an internal combustion engine - Google Patents
Method and device for operating an internal combustion engine Download PDFInfo
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- DE102007041897B4 DE102007041897B4 DE102007041897A DE102007041897A DE102007041897B4 DE 102007041897 B4 DE102007041897 B4 DE 102007041897B4 DE 102007041897 A DE102007041897 A DE 102007041897A DE 102007041897 A DE102007041897 A DE 102007041897A DE 102007041897 B4 DE102007041897 B4 DE 102007041897B4
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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
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2066—Selective catalytic reduction [SCR]
- F01N3/208—Control of selective catalytic reduction [SCR], e.g. dosing of reducing agent
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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
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
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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
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/105—General auxiliary catalysts, e.g. upstream or downstream of the main catalyst
- F01N3/106—Auxiliary oxidation catalysts
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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
- F01N9/00—Electrical control of exhaust gas treating 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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/20—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a flow director or deflector
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/40—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a hydrolysis catalyst
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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
- F01N2560/00—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
- F01N2560/02—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
- F01N2560/021—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting ammonia NH3
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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
- F01N2560/00—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
- F01N2560/02—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
- F01N2560/026—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting NOx
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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
- F01N2570/18—Ammonia
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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
- F01N2610/00—Adding substances to exhaust gases
- F01N2610/02—Adding substances to exhaust gases the substance being ammonia or urea
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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
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Materials Engineering (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Verfahren zum Betreiben einer Brennkraftmaschine (14) mit einem SCR-System, das einen SCR-Katalysator (23) umfasst, bei dem
– ein Ammoniak-Beladungsgrad (NH3_LD) des SCR-Katalysators (23) ermittelt oder eingestellt wird,
– abhängig von zumindest einer Betriebsgröße der Brennkraftmaschine (14) ein aktueller Stickoxidgehalt (NOX_AV) eines Abgases der Brennkraftmaschine (14) ermittelt wird,
– abhängig von dem ermittelten aktuellen Stickoxidgehalt (NOX_AV) des Abgases ein Basissollwert (NH3_MASS_BAS) einer Ammoniakmediummasse ermittelt wird, die dem Abgastrakt zum Umwandeln des Stickoxids des Abgases zuzumessen ist,
– ein Sollwert (NH3_MASS_SP) der Ammoniakmediummasse so ermittelt wird, dass der Sollwert (NH3_MASS_SP) der Ammoniakmediummasse um den Basissollwert (NH3_MASS_BAS) der Ammoniakmediummasse schwingt und dass der schwingende Sollwert (NH3_MASS_SP) der Ammoniakmediummasse im Mittel dem ermittelten Basissollwert (NH3_MASS_BAS) der Ammoniakmediummasse zumindest näherungsweise entspricht,
– abhängig von dem ermittelten Sollwert (NH3_MASS_SP) der Ammoniakmediummasse zum Umsetzen des Sollwerts (NH3_MASS_SP) der Ammoniakmediummasse ein Stellsignal für ein Stellglied ermittelt wird, dessen Stellung sich auf eine...Method for operating an internal combustion engine (14) with an SCR system comprising an SCR catalytic converter (23), in which
An ammonia loading level (NH3_LD) of the SCR catalytic converter (23) is determined or set,
Depending on at least one operating variable of the internal combustion engine (14), a current nitrogen oxide content (NOX_AV) of an exhaust gas of the internal combustion engine (14) is determined,
Depending on the determined current nitrogen oxide content (NOX_AV) of the exhaust gas, a base setpoint value (NH3_MASS_BAS) of an ammonia medium mass is determined, which is to be assigned to the exhaust gas tract for converting the nitrogen oxide of the exhaust gas,
- A nominal value (NH3_MASS_SP) of the ammonia medium mass is determined such that the setpoint value (NH3_MASS_SP) of the ammonia medium mass oscillates around the nominal base value (NH3_MASS_BAS) of the ammonia medium mass and the oscillating nominal value (NH3_MASS_SP) of the ammonia medium mass is at least equal to the determined base setpoint value (NH3_MASS_BAS) of the ammonia medium mass approximates,
- Depending on the determined setpoint value (NH3_MASS_SP) of the ammonia medium mass for converting the setpoint value (NH3_MASS_SP) of the ammonia medium mass, an actuating signal for an actuator is determined, the position of which is based on a ...
Description
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Betreiben einer Brennkraftmaschine. Die Brennkraftmaschine hat ein SCR-System, das einen SCR-Katalysator umfasst. Abhängig von zumindest einer Betriebsgröße der Brennkraftmaschine wird ein aktueller Stickoxidgehalt eines Abgases der Brennkraftmaschine ermittelt. Abhängig von dem ermittelten aktuellen Stickoxidgehalt des Abgases wird ein Basissollwert einer Ammoniakmediummasse ermittelt. Die Ammoniakmediummasse ist dem Abgastrakt zum Umwandeln des Stickoxids des Abgases zuzumessen.The invention relates to a method and a device for operating an internal combustion engine. The internal combustion engine has an SCR system that includes an SCR catalyst. Depending on at least one operating variable of the internal combustion engine, a current nitrogen oxide content of an exhaust gas of the internal combustion engine is determined. Depending on the determined current nitrogen oxide content of the exhaust gas, a base target value of an ammonia medium mass is determined. The ammonia medium mass is to be metered to the exhaust tract for converting the nitrogen oxide of the exhaust gas.
Zur Reduzierung eines Stickoxidgehalts im Abgas einer Brennkraftmaschine kann eine Abgasnachbehandlung mit wässriger Harnstofflösung und einem SCR-Katalysator durchgeführt werden. Die wässrige Harnstofflösung kann auch als Harnstoff bezeichnet werden. Zur Abgasnachbehandlung wird die wässrige Harnstofflösung mit einer Flüssigkeitspumpe zu einem Harnstoffeinspritzventil gepumpt, das die Harnstofflösung stromaufwärts des SCR-Katalysators in einen Abgasstrom in einem Abgastrakt der Brennkraftmaschine zumisst. Die Harnstofflösung reagiert in dem heißen Abgasstrom zu Ammoniak und Kohlendioxid. In dem SCR-Katalysator reagiert dann der Ammoniak mit dem Stickoxidgemisch des Abgases zu Stickstoff und Wasser.To reduce a nitrogen oxide content in the exhaust gas of an internal combustion engine, an exhaust gas aftertreatment with aqueous urea solution and an SCR catalyst can be carried out. The aqueous urea solution may also be referred to as urea. For exhaust aftertreatment, the aqueous urea solution is pumped with a liquid pump to a urea injection valve which meters the urea solution upstream of the SCR catalyst into an exhaust gas stream in an exhaust tract of the internal combustion engine. The urea solution reacts in the hot exhaust stream to ammonia and carbon dioxide. In the SCR catalyst, the ammonia then reacts with the nitrogen oxide mixture of the exhaust gas to form nitrogen and water.
Die
Die
Die Aufgabe, die der Erfindung zugrunde liegt, ist, ein Verfahren und eine Vorrichtung zum Betreiben einer Brennkraftmaschine zu schaffen, die eine geeignete Beladung eines SCR-Katalysators mit Ammoniak für eine besonders effektive Abgasnachbehandlung mittels eines SCR-Systems der Brennkraftmaschine ermöglichen.The object underlying the invention is to provide a method and an apparatus for operating an internal combustion engine, which allow a suitable loading of an SCR catalyst with ammonia for a particularly effective exhaust aftertreatment by means of an SCR system of the internal combustion engine.
Die Aufgabe wird gelöst durch die Merkmale der unabhängigen Ansprüche. Vorteilhafte Ausgestaltungen der Erfindung sind in den Unteransprüchen angegeben.The object is solved by the features of the independent claims. Advantageous embodiments of the invention are specified in the subclaims.
Die Erfindung zeichnet sich aus durch ein Verfahren und eine Vorrichtung zum Betreiben einer Brennkraftmaschine. Die Brennkraftmaschine hat ein SCR-System, das einen SCR-Katalysator umfasst. Ein Ammoniakbeladungsgrad des SCR-Katalysators wird ermittelt oder eingestellt. Abhängig von zumindest einer Betriebsgröße der Brennkraftmaschine wird ein aktueller Stickoxidgehalt eines Abgases der Brennkraftmaschine ermittelt. Abhängig von dem ermittelten aktuellen Stickoxidgehalt des Abgases wird ein Basissollwert einer Ammoniakmediummasse ermittelt. Die Ammoniakmediummasse ist dem Abgastrakt zum Umwandeln des Stickoxids des Abgases zuzumessen. Ein Sollwert der Ammoniakmasse wird so ermittelt, dass der Sollwert der Ammoniakmediummasse um den Basissollwert der Ammoniakmediummasse schwingt und dass der schwingende Sollwert der Ammoniakmediummasse im Mittel dem ermittelten Basissollwert der Ammoniakmediummasse zumindest näherungsweise entspricht. Abhängig von dem ermittelten Sollwert der Ammoniakmediummasse wird zum Umsetzen des Sollwerts der Ammoniakmediummasse ein Stellsignal für ein Stellglied ermittelt, dessen Stellung sich auf eine tatsächlich zugemessene Ammoniakmediummasse auswirkt. Der Basissollwert der Ammoniakmediummasse wird abhängig von dem ermittelten beziehungsweise eingestellten Ammoniakbeladungsgrad ermittelt.The invention is characterized by a method and a device for operating an internal combustion engine. The internal combustion engine has an SCR system that includes an SCR catalyst. An ammonia loading level of the SCR catalyst is determined or adjusted. Depending on at least one operating variable of the internal combustion engine, a current nitrogen oxide content of an exhaust gas of the internal combustion engine is determined. Depending on the determined current nitrogen oxide content of the exhaust gas, a base target value of an ammonia medium mass is determined. The ammonia medium mass is to be metered to the exhaust tract for converting the nitrogen oxide of the exhaust gas. A target value of the ammonia mass is determined such that the desired value of the ammonia medium mass oscillates around the basic target value of the ammonia medium mass and that the oscillating nominal value of the ammonia medium mass corresponds at least approximately to the determined base target value of the ammonia medium mass. Depending on the determined nominal value of the ammonia medium mass, an actuating signal for an actuator is determined for converting the nominal value of the ammonia medium mass, whose position has an effect on an actually metered ammonia medium mass. The basic setpoint of the ammonia medium mass is determined as a function of the determined or adjusted ammonia loading level.
Die Betriebsgröße der Brennkraftmaschine umfasst beispielsweise eine Last, eine Drehzahl und/oder eine Verbrennungstemperatur bei einem Verbrennungsprozess der Brennkraftmaschine. Dass der Sollwert der Ammoniakmediummasse um den Basissollwert der Ammoniakmediummasse schwingt, bedeutet in diesem Zusammenhang, dass ein Verlauf des Sollwerts der Ammoniakmediummasse eine Schwingung um einen Verlauf des Basissollwerts der Ammoniakmediummasse vollzieht. Dass der schwingende Sollwert der Ammoniakmediummasse im Mittel dem ermittelten Basissollwert der Ammoniakmediummasse zumindest näherungsweise entspricht, bedeutet in diesem Zusammenhang, dass eine Mittelung des Verlaufs des Sollwerts der Ammoniakmediummasse einer Mittelung des Verlaufs des Basissollwerts der Ammoniakmediummasse zumindest näherungsweise entspricht. Der Ausdruck ”beziehungsweise” wird in dieser Patentanmeldung in seiner ursprünglichen Bedeutung verwendet. Somit verknüpft ”beziehungsweise” zwei Elemente einer mehrteiligen Aussage, wenn sich diese Elemente jeweils ausschließlich auf unterschiedliche vorher genannte Substantive beziehen.The operating variable of the internal combustion engine includes, for example, a load, a rotational speed and / or a combustion temperature a combustion process of the internal combustion engine. The fact that the desired value of the ammonia medium mass oscillates around the basic setpoint value of the ammonia medium mass means in this context that a profile of the nominal value of the ammonia medium mass carries out a vibration about a progression of the basic nominal value of the ammonia medium mass. The fact that the oscillating desired value of the ammonia medium mass on average at least approximately corresponds to the determined base setpoint value of the ammonia medium mass means in this context that an averaging of the profile of the nominal value of the ammonia medium mass at least approximately corresponds to an averaging of the course of the basic nominal value of the ammonia medium mass. The term "or" is used in this patent application in its original meaning. Thus, "or" combines two elements of a multi-part statement, if these elements relate exclusively to different previously mentioned nouns.
Das Ansteuern des Stellglieds mittels des ermittelten Stellsignals bewirkt im fehlerfreien Betrieb der Brennkraftmaschine, dass die tatsächlich zugemessene Ammoniakmediummasse während einer ersten Zeitdauer größer als die Ammoniakmediummasse ist, die zum Umwandeln des Stickoxids in dem Abgas benötigt wird, und dass während einer zweiten Zeitdauer die tatsächlich zugemessene Ammoniakmediummasse kleiner als die zum Umwandeln des Stickoxids benötigte Ammoniakmediummasse ist. Dies führt dazu, dass während der ersten Zeitdauer der Beladungsgrad des SCR-Katalysators zunimmt und dass während der zweiten Zeitdauer der Beladungsgrad des SCR-Katalysators abnimmt. Dies kann zu einer besonders effektiven Aufnahme des Ammoniaks durch den SCR-Katalysator und zu einem besonders effektiven Umwandeln des Stickoxids des Abgases mittels des Ammoniaks beitragen. Dies trägt zu einer besonders effektiven Abgasnachbehandlung des Abgases der Brennkraftmaschine mittels des SCR-Systems bei.The control of the actuator by means of the determined control signal causes the actual metered Ammoniamediummasse during a first period of time is greater than the Ammoniamediummasse that is needed to convert the nitrogen oxide in the exhaust gas, and that during a second period of time the actually metered Ammonia medium mass is smaller than the ammonia medium mass required for converting the nitrogen oxide. As a result, during the first period of time, the degree of loading of the SCR catalyst increases, and during the second period, the degree of loading of the SCR catalyst decreases. This can contribute to a particularly effective absorption of the ammonia by the SCR catalyst and to a particularly effective conversion of the nitrogen oxide of the exhaust gas by means of the ammonia. This contributes to a particularly effective exhaust aftertreatment of the exhaust gas of the internal combustion engine by means of the SCR system.
In einer vorteilhaften Ausgestaltung wird der Sollwert der Ammoniakmediummasse zunächst so ermittelt, dass der Sollwert der Ammoniakmediummasse zunächst größer als der Basissollwert der Ammoniakmediummasse ist. Anschließend wird der Sollwert der Ammoniakmediummasse so ermittelt, dass der Sollwert der Ammoniakmediummasse um den Basissollwert der Ammoniakmediummasse schwingt. Dies trägt dazu bei, dass zunächst der SCR-Katalysator mit genügend Ammoniak beladen wird, so dass in jedem Fall eine ausreichende Umwandlung der Stickoxide des Abgases möglich ist. Dies trägt dazu bei, dass die Abgasnachbehandlung mittels des SCR-Systems beispielsweise nach einem Motorstart der Brennkraftmaschine besonders schnell besonders effektiv ist.In an advantageous embodiment, the desired value of the ammonia medium mass is first determined so that the desired value of the ammonia medium mass is initially greater than the base setpoint of the ammonia medium mass. Subsequently, the desired value of the ammonia medium mass is determined so that the desired value of the ammonia medium mass oscillates around the basic target value of the ammonia medium mass. This contributes to the fact that initially the SCR catalyst is loaded with enough ammonia, so that in each case a sufficient conversion of the nitrogen oxides of the exhaust gas is possible. This contributes to the fact that the exhaust gas aftertreatment by means of the SCR system, for example after an engine start of the internal combustion engine, is particularly particularly particularly effective.
In einer weiteren vorteilhaften Ausgestaltung wird der Sollwert der Ammoniakmediummasse so ermittelt, dass der Sollwert der Ammoniakmediummasse solange größer als der Basissollwert der Ammoniakmediummasse ist, bis der Ammoniakbeladungsgrad des SCR-Katalysators größer als ein vorgegebener erster Schwellenwert ist oder bis der aktuelle Stickoxidgehalt des Abgases kleiner als ein vorgegebener zweiter Schwellenwert ist. Ferner wird der Sollwert der Ammoniakmediummasse so ermittelt, dass anschließend der Sollwert der Ammoniakmediummasse kleiner als der Basissollwert der Ammoniakmediummasse ist. Dies kann zu dem besonders effektiven Beladen des SCR-Katalysators und/oder zu einem besonders effektiven Umwandeln der Stickoxide des Abgases beitragen.In a further advantageous embodiment, the nominal value of the ammonia medium mass is determined such that the desired value of the ammonia medium mass is greater than the base target value of the ammonia medium mass until the ammonia loading level of the SCR catalyst is greater than a predefined first threshold value or until the current nitrogen oxide content of the exhaust gas is less than is a predetermined second threshold. Furthermore, the nominal value of the ammonia medium mass is determined so that subsequently the desired value of the ammonia medium mass is smaller than the basic nominal value of the ammonia medium mass. This can contribute to the particularly effective loading of the SCR catalyst and / or to a particularly effective conversion of the nitrogen oxides of the exhaust gas.
In einer weiteren vorteilhaften Ausgestaltung wird der Sollwert der Ammoniakmediummasse so ermittelt, dass der Sollwert der Ammoniakmediummasse so lange kleiner als der Basissollwert der Ammoniakmediummasse ist, bis der Ammoniakbeladungsgrad des SCR-Katalysators kleiner als ein vorgegebener dritter Schwellenwert ist oder bis der aktuelle Stickoxidgehalt des Abgases größer als ein vorgegebener vierter Schwellenwert ist. Ferner wird der Sollwert der Ammoniakmediummasse so ermittelt, dass anschließend der Sollwert der Ammoniakmediummasse größer als der Basissollwert der Ammoniakmediummasse ist. Dies kann zu einer besonders effektiven Umwandlung der Stickoxide des Abgases und/oder zu einem besonders effektiven Aufladen des SCR-Katalysators beitragen.In a further advantageous embodiment, the nominal value of the ammonia medium mass is determined so that the desired value of the ammonia medium mass is smaller than the base setpoint of the ammonia medium mass until the ammonia loading of the SCR catalyst is less than a predetermined third threshold or until the current nitrogen oxide content of the exhaust gas is greater is a predetermined fourth threshold. Furthermore, the nominal value of the ammonia medium mass is determined so that subsequently the desired value of the ammonia medium mass is greater than the basic nominal value of the ammonia medium mass. This can contribute to a particularly effective conversion of the nitrogen oxides of the exhaust gas and / or to a particularly effective charging of the SCR catalyst.
Ausführungsbeispiele der Erfindung sind im Folgenden anhand von schematischen Zeichnungen näher erläutert.Embodiments of the invention are explained in more detail below with reference to schematic drawings.
Es zeigen:Show it:
Elemente gleicher Konstruktion oder Funktion sind figurenübergreifend mit den gleichen Bezugszeichen gekennzeichnet.Elements of the same construction or function are identified across the figures with the same reference numerals.
Eine Brennkraftmaschine
In dem Zylinderkopf
Ferner ist dem Abgastrakt
Stromaufwärts des Harnstoffeinspritzventils
Falls die Brennkraftmaschine
Eine Steuereinrichtung
Die Sensoren sind beispielsweise ein Pedalstellungsgeber
Je nach Ausführungsform der Erfindung kann eine beliebige Untermenge der genannten Sensoren vorhanden sein oder es können auch zusätzliche Sensoren vorhanden sein.Depending on the embodiment of the invention, any subset of said sensors may be present, or additional sensors may be present.
Die Stellglieder sind beispielsweise die Drosselklappe
Auf einem Speichermedium der Steuereinrichtung
Das Programm wird vorzugsweise zeitnah einem Motorstart der Brennkraftmaschine
In einem Schritt S2 wird ein Beladungsgrad NH3_LD des SCR-Katalysators
Alternativ dazu kann in dem Schritt S2 der Beladungsgrad NH3_LD des SCR-Katalysators
In einem Schritt S3 wird ein aktueller Stickoxidgehalt NOX_AV des Abgases ermittelt. Der aktuelle Stickoxidgehalt NOX_AV kann beispielsweise mittels eines Stickoxidsensors stromabwärts des Gasauslassventils
In einem Schritt S4 wird ein Basissollwert NH3_MASS_BAS der Ammoniakmediummasse abhängig von dem Beladungsgrad NH3_LD des SCR-Katalysators
In einem Schritt S5 wird abhängig von dem ermittelten Basissollwert NH3_MASS_BAS der Ammoniakmediummasse ein Sollwert NH3_MASS_SP der Ammoniakmediummasse ermittelt. Vorzugsweise wird der Sollwert NH3_MASS_SP der Ammoniakmediummasse zunächst so ermittelt, dass der Sollwert NH3_MASS_SP der Ammoniakmediummasse größer als der Basissollwert NH3_MASS_BAS der Ammoniakmediummasse ist. Dies trägt dazu bei, dass zu Beginn der Abgasnachbehandlung der SCR-Katalysator
Ferner trägt dies der Erkenntnis Rechnung, dass während einer ersten Zeitdauer, während der der Ammoniak an dem SCR-Katalysator
Insbesondere können zum gezielten Variieren des Sollwerts NH3_MASS_SP der Ammoniakmediummasse Schritte S6 bis S11 abgearbeitet werden.In particular, steps S6 to S11 can be executed to selectively vary the nominal value NH3_MASS_SP of the ammonia medium mass.
In dem Schritt S6 wird überprüft, ob der Beladungsgrad NH3_LD des SCR-Katalysators
In dem Schritt S7, der zusätzlich oder alternativ zu dem Schritt S6 abgearbeitet wird, wird überprüft, ob der aktuelle Stickoxidgehalt NOX_AV kleiner als ein vorgegebener zweiter Schwellenwert THD_2 ist. Ist die Bedingung des Schritts S7 erfüllt, so wird die Bearbeitung in einem Schritt S8 fortgesetzt. Ist die Bedingung des Schritts S7 nicht erfüllt, so wird die Bearbeitung erneut in dem Schritt S7 oder in dem Schritt S6 fortgesetzt.In step S7, which is executed in addition to or as an alternative to step S6, it is checked whether the current nitrogen oxide content NOX_AV is less than a predefined second threshold value THD_2. If the condition of step S7 is satisfied, the processing is continued in step S8. If the condition of the step S7 is not satisfied, the processing is continued again in the step S7 or in the step S6.
In einem Schritt S8 wird der Sollwert NH3_MASS_SP der Ammoniakmediummasse abhängig von dem Basissollwert NH3_MASS_BAS vorzugsweise so ermittelt, dass der Sollwert NH3_MASS_SP der Ammoniakmediummasse kleiner als der Basissollwert NH3_MASS_BAS der Ammoniakmediummasse ist. Somit wird in dem Schritt S8 die zweite Zeitdauer eingeleitet, während der im Wesentlichen die Reaktion des im SCR-Katalysator
In einem Schritt S9 wird überprüft, ob der Ammoniakbeladungsgrad NH3_LD kleiner als ein vorgegebener dritter Schwellenwert THD_3 ist. Ist die Bedingung des Schritts S9 erfüllt, so wird die Bearbeitung in einem Schritt S11 fortgesetzt. Ist die Bedingung des Schritts S9 nicht erfüllt, so wird der Schritt S9 erneut abgearbeitet oder es wird ein Schritt S10 abgearbeitet.In a step S9, it is checked whether the ammonia loading degree NH3_LD is smaller than a predetermined third threshold value THD_3. If the condition of step S9 is satisfied, the processing is continued in step S11. If the condition of step S9 is not satisfied, step S9 is executed again or a step S10 is executed.
In dem Schritt S10 wird überprüft, ob der aktuelle Stickoxidgehalt NOX_AV größer als ein vorgegebener vierter Schwellenwert THD_4 ist. Ist die Bedingung des Schritts S10 erfüllt, so wird die Bearbeitung in einem Schritt S11 fortgesetzt. Ist die Bedingung des Schritts S10 nicht erfüllt, so wird der Schritt S10 erneut abgearbeitet oder es wird der Schritt S9 abgearbeitet. Der Schritt S10 kann zusätzlich oder alternativ zu dem Schritt S9 abgearbeitet werden.In step S10, it is checked whether the current nitrogen oxide content NOX_AV is greater than a predetermined fourth threshold value THD_4. If the condition of step S10 is satisfied, the processing is continued in step S11. If the condition of step S10 is not met, step S10 is executed again or step S9 is executed. The step S10 may be executed additionally or alternatively to the step S9.
In einem Schritt S11 kann das Programm zum Betreiben der Brennkraftmaschine
Die Schwellenwerte können konstant sein oder abhängig von zumindest einer der Betriebsgrößen der Brennkraftmaschine
Claims (5)
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US5785937A (en) * | 1994-08-10 | 1998-07-28 | Siemens Aktiengesellschaft | Method for the catalytic conversion of nitrogen oxides present in the exhaust gas of an internal-combustion engine |
US6017503A (en) * | 1996-07-25 | 2000-01-25 | Ngk Insulators, Ltd. | Method of removing NOx from exhaust gases |
US20050282285A1 (en) * | 2004-06-21 | 2005-12-22 | Eaton Corporation | Strategy for controlling NOx emissions and ammonia slip in an SCR system using a nonselective NOx/NH3 |
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DE4117143C2 (en) * | 1991-05-25 | 1995-04-20 | Daimler Benz Ag | Process for the selective catalytic reduction of nitrogen oxides in exhaust gases from automotive diesel engines |
US6427439B1 (en) * | 2000-07-13 | 2002-08-06 | Ford Global Technologies, Inc. | Method and system for NOx reduction |
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US5785937A (en) * | 1994-08-10 | 1998-07-28 | Siemens Aktiengesellschaft | Method for the catalytic conversion of nitrogen oxides present in the exhaust gas of an internal-combustion engine |
US6017503A (en) * | 1996-07-25 | 2000-01-25 | Ngk Insulators, Ltd. | Method of removing NOx from exhaust gases |
US20050282285A1 (en) * | 2004-06-21 | 2005-12-22 | Eaton Corporation | Strategy for controlling NOx emissions and ammonia slip in an SCR system using a nonselective NOx/NH3 |
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