DE19731624A1 - Reversible rich regeneration of nitrogen@ oxide absorption catalyst - Google Patents
Reversible rich regeneration of nitrogen@ oxide absorption catalystInfo
- Publication number
- DE19731624A1 DE19731624A1 DE1997131624 DE19731624A DE19731624A1 DE 19731624 A1 DE19731624 A1 DE 19731624A1 DE 1997131624 DE1997131624 DE 1997131624 DE 19731624 A DE19731624 A DE 19731624A DE 19731624 A1 DE19731624 A1 DE 19731624A1
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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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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8696—Controlling the catalytic process
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9495—Controlling the catalytic process
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
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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—Regulation of absorbents or adsorbents, e.g. purging
- 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
- 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
- F02D41/1439—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the position of the sensor
- F02D41/1441—Plural sensors
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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
- F02D41/1446—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 exhaust temperatures
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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
- F01N2250/00—Combinations of different methods of purification
- F01N2250/12—Combinations of different methods of purification absorption or adsorption, and catalytic conversion
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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
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B1/00—Engines characterised by fuel-air mixture compression
- F02B1/02—Engines characterised by fuel-air mixture compression with positive ignition
- F02B1/04—Engines characterised by fuel-air mixture compression with positive ignition with fuel-air mixture admission into cylinder
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Exhaust Gas After Treatment (AREA)
- Electrical Control Of Air Or Fuel Supplied To Internal-Combustion Engine (AREA)
Abstract
Description
Die Erfindung betrifft ein Verfahren zur Überwachung und Steuerung der De-Sulfatierung bei NOx-Speicherkatalysatoren, die Brennkraftmaschinen vom Otto- oder Dieselmotortyp zur Abgasreinigung nachgeschaltet sind.The invention relates to a method for monitoring and controlling the de-sulfation NOx storage catalytic converters, the internal combustion engines of the Otto or diesel engine type Exhaust gas cleaning are downstream.
NOx-Speicherkatalysatoren werden während des Betriebs durch den im Kraftstoff enthaltenen Schwefel und dessen Einlagerung als Sulfat in dem NOx-Speicherkatalysator vergiftet, so daß die NOx-Aufnahme des Speicherkatalysators behindert oder insgesamt verhindert wird. Es ist daher in periodischen Abständen eine Entschwefelung bzw. eine De- Sulfatierung des NOx-Speicherkatalysators durchzuführen. Es ist bekannt, daß eine Schwefelvergiftung des NOx-Speicherkatalysators überwiegend oder vollständig reversibel ist, sofern in reduzierender Umgebung eine De-Sulfatierungs-Mindesttemperatur überschritten wird.NOx storage catalytic converters are activated during operation by the in the fuel contained sulfur and its storage as sulfate in the NOx storage catalyst poisoned so that the NOx uptake of the storage catalyst is hindered or overall is prevented. It is therefore periodic desulfurization or de- Carrying out sulfation of the NOx storage catalyst. It is known that a Sulfur poisoning of the NOx storage catalytic converter is largely or completely reversible is a minimum desulfation temperature in a reducing environment is exceeded.
Bei magerbetriebenen Ottomotoren kann in jedem Betriebszustand bei Inkaufnahme eines entsprechenden Mehrverbrauchs mit stöchiometrischem oder fetten Luft-Kraftstoff-Gemisch gefahren werden. Durch Maßnahmen wie eine Spätzündung des Motors ist überdies die Abgastemperatur in weiten Grenzen variierbar, so daß übliche De- Sulfatierungstemperaturen von ca. 650°C in nahezu jedem Kennfeldbereich eines Ottomotors erzielt werden können.In the case of lean-burn gasoline engines, one can be used in any operating state appropriate additional consumption with stoichiometric or rich air-fuel mixture be driven. Measures such as retarding the engine also Exhaust gas temperature can be varied within wide limits, so that usual de- Sulphation temperatures of approx. 650 ° C in almost every map area Otto engine can be achieved.
Derzeit bekannte NOx-Speicherkatalysatoren können oberhalb von ca. 550°C unter mageren Bedingungen kein NOx mehr einlagern und zeigen starke Alterungseffekte beim Überschreiten von ca. 800°C. Currently known NOx storage catalytic converters can drop below approx. 550 ° C no longer store NOx in lean conditions and show strong aging effects when Exceeding approx. 800 ° C.
Bei Dieselmotoren kann ein länger andauernder Betrieb mit λ < 1 wegen der damit verbundenen Minderleistung und der ansteigenden Partikelemissionen nicht durchgeführt werden.In diesel engines, longer-term operation with λ <1 can occur because of this associated underperformance and the increasing particle emissions not carried out become.
Der Erfindung liegt daher die Aufgabe zugrunde, ein Verfahren zur gesteuerten De- Sulfatierung von NOx-Speicherkatalysatoren und eine Vorrichtung zur Durchführung des Verfahrens zu schaffen, die eine geregelte Desulfatierung ohne Zerstörung des NOx- Speicherkatalysators auf einfache Weise ermöglichen.The invention is therefore based on the object of developing a method for controlled de- Sulfation of NOx storage catalysts and a device for performing the To create process that controlled desulfation without destroying the NOx Enable storage catalytic converter in a simple manner.
Diese Aufgabe wird durch das Verfahren nach Anspruch 1 und die Vorrichtung zur Durchführung des Verfahrens nach Anspruch 13 gelöst. Bevorzugte Ausgestaltungen der Erfindung sind Gegenstand der Unteransprüche.This object is achieved by the method according to claim 1 and the device for Implementation of the method according to claim 13 solved. Preferred embodiments of the Invention are the subject of the dependent claims.
Die vorliegende Erfindung betrifft ein Verfahren zur De-Sulfatierung eines einer
Brennkraftmaschine nachgeschalteten NOx-Speichers, das die folgenden Schritte aufweist:
The present invention relates to a method for de-sulfating a NOx accumulator connected downstream of an internal combustion engine, which has the following steps:
- a) Vorliegen der Notwendigkeit einer De-Sulfatierung des NOx-Speichers,a) existence of the need to de-sulfate the NOx storage,
- b) Einleiten und Durchführen einer abgastemperatursteigernden Maßnahme, mit der der NOx-Speicherkatalysator auf oberhalb einer vorbestimmten De-Sulfatierungstemperatur erhitzt wird,b) initiation and implementation of an exhaust gas temperature-increasing measure with which the NOx storage catalytic converter to above a predetermined desulphation temperature is heated
- c) De-Sulfatieren des NOx-Speichers durch Fettbetreiben des Motors, undc) de-sulfation of the NOx storage by operating the engine with grease, and
- d) Einleiten des Normalbetriebs der Brennkraftmaschine nach der Beendigung des De- Sulfatierungsschritts.d) initiation of normal operation of the internal combustion engine after the end of the de- Sulfation step.
Weiterhin wird die abgastemperatursteigernde Maßnahme so gesteuert, daß die Temperatur des NOx-Speicherkatalysators immer unterhalb der Alterungstemperatur des NOx-Speichers liegt. Vorzugsweise liegt die maximale NOx-Speichertemperatur um einen vorbestimmten Sicherheitsabstand unterhalb der Alterungstemperatur.Furthermore, the exhaust gas temperature increasing measure is controlled so that the temperature of the NOx storage catalyst always below the aging temperature of the NOx storage lies. The maximum NOx storage temperature is preferably around a predetermined one Safety distance below the aging temperature.
Bei einer Brennkraftmaschine des Typs Ottomotor wird der Motor nach dem Vorliegen (Erkennen) der Notwendigkeit einer Entschwefelung stöchiometrisch betrieben, bevor eine abgastemperatursteigernde Maßnahme eingeleitet wird. Die abgastemperatursteigernde Maßnahme kann durch Verstellen des Zündzeitpunktes auf einen späteren Zeitpunkt erzielt werden.In an internal combustion engine of the gasoline engine type, the engine is present (Recognize) the need for desulfurization operated stoichiometrically before one measure to increase exhaust gas temperature is initiated. The exhaust gas temperature increasing Measure can be achieved by adjusting the ignition timing to a later time become.
Vorzugsweise wird bei einer Brennkraftmaschine des Typs Ottomotor unmittelbar nach dem De-Sulfatierungsschritt ein Betrieb mit λ = 1 durchgeführt, bevor nach dem Unterschreiten eines vorbestimmten zweiten Sicherheitsabstandes zur Alterungsschwelle der Fett-Mager- Betrieb des Motors wieder aufgenommen wird. Vorzugsweise beträgt der zweite Sicherheitsabstand ca. 100°C.Preferably, in an internal combustion engine of the gasoline engine type, immediately after the De-sulfation step performed an operation with λ = 1 before falling below a predetermined second safety distance from the aging threshold of the fat-lean Operation of the engine is resumed. The second is preferably Safety distance approx. 100 ° C.
Ferner wird bei einer Brennkraftmaschine des Typs Dieselmotor nach der Erkennung der Notwendigkeit einer De-Sulfatierung zuerst eine NOx-Regeneration durchgeführt, bevor eine katalysatortemperatursteigernde Maßnahme eingeleitet wird. Die NOx-Regeneration wird durch einen Betrieb mit λ < 1 durchgeführt.Furthermore, in an internal combustion engine of the diesel engine type, after the detection of the Necessity of de-sulfation is carried out first before a NOx regeneration catalyst temperature-increasing measure is initiated. The NOx regeneration will performed by an operation with λ <1.
Vorzugsweise wird die katalysatortemperatursteigernde Maßnahme bei Dieselmotoren durch eine Verstellung des Spritzbeginnzeitpunkts, Änderung der EGR-Rate (Abgasrückführrate), Absenken des Ladedrucks, partielle Androsselung, kombinierter Fett-Mager-Betrieb, Einspritzen von Kraftstoff in die Abgasanlage vor dem Katalysator oder eine Nacheinspritzung bei CR-Motoren (common-Rail) durchgeführt. Ferner kann eine Anfettung beispielsweise durch Saugluftdrosselung und/oder EGR-Anhebung und/oder Nacheinspritzung und/oder Ladedrucksenkung erzielt werden.The measure to increase the catalyst temperature is preferably carried out in the case of diesel engines an adjustment of the injection start time, change of the EGR rate (exhaust gas recirculation rate), Lowering the boost pressure, partial throttling, combined fat-lean operation, Injecting fuel into the exhaust system in front of the catalytic converter or one Post-injection performed on CR engines (common rail). Furthermore, an enrichment for example by suction air throttling and / or EGR increase and / or Post-injection and / or boost pressure reduction can be achieved.
Bei Dieselmotoren wird der Motorennormalbetrieb unmittelbar nach Beendigung der De- Sulfatierung wieder aufgenommen.In the case of diesel engines, normal engine operation is started immediately after the Sulfation resumed.
Die Vorrichtung zur Durchführung des erfindungsgemäßen Verfahrens umfaßt eine Brennkraftmaschine mit nachgeschaltetem NOx-Speicher, wobei unmittelbar vor und nach dem NOx-Speicher jeweils ein Temperatursensor zur Messung der Abgastemperatur angeordnet ist.The device for carrying out the method according to the invention comprises a Internal combustion engine with downstream NOx storage, immediately before and after a temperature sensor for measuring the exhaust gas temperature is arranged.
Die Erfindung ist nachfolgend anhand der Zeichnungen erläutert, in denen: The invention is explained below with reference to the drawings, in which:
Fig. 1 schematisch die Vorrichtung zur Überwachung der De-Sulfatierung sowohl für einen Otto- als auch einen Dieselmotor zeigt, Fig. 1 schematically shows the device for monitoring the de-sulfation both a gasoline and a diesel engine,
Fig. 2 den schematischen Ablauf einer De-Sulfatierung beim Mager-Otto-Motor zeigt, und Fig. 2 shows the schematic sequence of a de-sulfation in the lean Otto engine, and
Fig. 3 schematisch den Desulfatierungsablauf beim Dieselmotor zeigt. Fig. 3 shows schematically the desulfation process in the diesel engine.
Fig. 1 zeigt die erfindungsgemäße Vorrichtung zur De-Sulfatierung einer Brennkraftmaschine bestehend aus einem Motor 1 sowie einer Abgasanlage 2, die einen NOx- Speicherkatalysator 3 sowie Temperaturfühler T1 und T2 aufweist, die unmittelbar vor und nach dem NOx-Speicherkatalysator 2 angeordnet sind. Aus der Figur ist erkennbar, daß der Temperaturfühler T1 die Abgastemperatur unmittelbar vor dem NOx-Speicher 3 mißt während der Temperaturfühler T2 die Abgastemperatur unmittelbar nach dem NOx-Speicher 3 mißt. Fig. 1, the device according to the invention shows for de-sulfation of an internal combustion engine comprising an engine 1 and an exhaust system 2, which includes a NOx storage catalyst 3, and temperature sensors T1 and T2, which are arranged immediately before and after the NOx storage catalyst 2. From the figure it can be seen that the temperature sensor T1 measures the exhaust gas temperature immediately upstream of the NOx storage 3, while the temperature sensor T2 measures the exhaust gas temperature immediately downstream of the NOx storage 3 .
Fig. 2 zeigt schematisch den Ablauf einer De-Sulfatierung am Mager-Otto-Motor 1. Dargestellt ist der zeitliche Ablauf gegenüber der Abgastemperatur sowie dem aktuellen λ- Wert. Dabei stellt die Kurve I den Verlauf der Temperatur am ersten Temperaturfühler T1, die Kurve II den Temperaturverlauf am zweiten Temperaturfühler T2 und Kurve III den Verlauf von λ dar. Fig. 2 shows schematically the sequence of a de-sulfation at the lean Otto-engine 1. The course of time in relation to the exhaust gas temperature and the current λ value is shown. Curve I represents the temperature curve at the first temperature sensor T1, curve II the temperature curve at the second temperature sensor T2 and curve III the curve of λ.
Aus dem üblichen alternierenden Fett-Mager-Betrieb heraus wird beim Vorliegen der Notwendigkeit eines Entschwefelungsvorgangs zunächst der Motor stöchiometrisch betrieben und eine abgastemperatursteigernde Maßnahme (Punkt A der Kurve III) - z. B. Spätzündung - eingeleitet, bis die Temperatur am Temperatursensor T1 vor dem Speicherkatalysator um einen Sicherheitsabstand (z. B. 50°) unter der Alterungsschwelle liegt, die ca. 800°C bei heute üblichen NOx-Speicherkatalysatoren beträgt.Out of the usual alternating fat-lean operation is when the The need to desulfurize the engine first stoichiometrically operated and an exhaust gas temperature increasing measure (point A of curve III) - z. B. Late ignition - initiated until the temperature at the temperature sensor T1 before the Storage catalytic converter by a safety distance (e.g. 50 °) below the aging threshold lies, which is approximately 800 ° C with today's conventional NOx storage catalysts.
Als Folge der steigenden Abgastemperatur und der möglicherweise zunehmenden Schadstoffmenge im Abgas nimmt die Temperatur am Temperatursensor T2 hinter dem NOx-Speicherkatalysator ebenfalls zu. Falls zu erkennen ist, daß durch die katalytische Reaktion im NOx-Speicherkatalysator die Alterungsschwelle überschritten wird beispielsweise durch zu schnellen Temperaturanstieg im Kurvenpunkt B der Kurve I, wird die abgastemperatursteigernde Maßnahme in ihrer Wirkung zurückgenommen (Punkt C der Kurve I). Die Gefahr einer internen Überhitzung des NOx-Speichers 3 ist wahrscheinlich wenn die Temperatur-Anstiegsgeschwindigkeit in der Nähe der Alterungsschwelle so hoch ist, daß ohne Änderung der abgastemperatursteigernden Maßnahme mit einem Überschreiten der Alterungsschwelle gerechnet werden muß.As a result of the rising exhaust gas temperature and the possibly increasing amount of pollutants in the exhaust gas, the temperature at the temperature sensor T2 behind the NOx storage catalytic converter also increases. If it can be seen that the aging threshold is exceeded by the catalytic reaction in the NOx storage catalytic converter, for example due to an excessively rapid temperature rise in curve point B of curve I, the effect of the exhaust gas temperature-increasing measure is reduced (point C of curve I). The risk of internal overheating of the NOx store 3 is likely if the temperature rise speed in the vicinity of the aging threshold is so high that the aging threshold must be exceeded without changing the exhaust gas temperature-increasing measure.
Wenn vor und nach dem NOx-Speicherkatalysator 3 die De-Sulfatierungs- Temperaturschwelle überschritten ist (Punkt D der Kurve II), wird der Motor 1 solange fett betrieben (von Punkt E bis Punkt F der Kurve III), bis die Sulfatbeladung sicher abgebaut worden ist. Dauer und Maß der Anfettung richten sich nach der errechneten oder geschätzten Schwefelbeladung. Im unmittelbaren Anschluß an die De-Sulfatierung (Punkt F der Kurve III) ist ein Magerbetrieb des Motors 1 unbedingt zu vermeiden, da wegen der hohen Katalysatortemperatur ohnehin noch kein NOx eingelagert wird und auf dem HC- und CO-gesättigten Träger die Zugabe von Sauerstoff zu einer sicheren Überschreitung der Altersschwelle zumindest in einem Teil des Speicherkatalysators 3 führen wird. Günstiger ist ein weiterer kurzfristiger Betrieb mit λ = 1, jedoch ohne abgastemperatursteigernde Maßnahmen, um ein allmähliches Absinken der Katalysatortemperatur herbeizuführen.If the desulphation temperature threshold is exceeded before and after the NOx storage catalytic converter 3 (point D of curve II), the engine 1 is operated richly (from point E to point F of curve III) until the sulphate load has been safely reduced is. The duration and extent of the enrichment depend on the calculated or estimated sulfur load. Immediately following the de-sulfation (point F of curve III), lean operation of engine 1 must be avoided, since no NOx is stored anyway due to the high catalyst temperature and the addition of oxygen on the HC and CO-saturated carrier will lead to a safe exceeding of the age threshold at least in part of the storage catalytic converter 3 . Another short-term operation with λ = 1 is more favorable, but without measures to increase the exhaust gas temperature, in order to bring about a gradual decrease in the catalyst temperature.
Erst nach Unterschreiten eines zweiten Sicherheitsabstandes (ca. 100 °) zur Alterungsschwelle hin (Punkt G der Kurve II) wird ein Fett-Mager-Betrieb des Motors 1 wieder zugelassen. Dabei kann möglicherweise im Speicher 3 kurzzeitig die NOx-Thermo- Desorptionsschwelle überschritten werden; bei den relativ niedrigen Abgastemperaturen magerer Ottomotor-Fahrzeuge ist jedoch anschließend mit einem raschen Unterschreiten der NOx-Thermo-Desorptionsschwelle zu rechnen.Only after falling below a second safety distance (approx. 100 °) towards the aging threshold (point G of curve II) is engine 1 lean operation again permitted. The NOx thermal desorption threshold may be exceeded briefly in memory 3 ; at the relatively low exhaust gas temperatures of lean Otto engine vehicles, however, a rapid drop below the NOx thermal desorption threshold is to be expected.
Fig. 3 zeigt den schematischen zeitlichen Ablauf einer De-Sulfatierung eines Dieselmotors 1. Die Bezeichnung der Kurven entspricht derjenigen der Fig. 2. Bei Dieselmotoren kann die Entschwefelung nicht in derselben Weise wie bei mageren Ottomotoren durchgeführt werden, da ein länger andauernder Betrieb mit λ < 1 wegen der Minderleistung und der ansteigenden Partikelemissionen nicht möglich ist. Daher wird mit Blick auf die NOx- Thermo-Desorptionsschwelle beim Erkennen der Notwendigkeit einer Entschwefelung zunächst eine NOx-Regeneration durchgeführt, so daß die Katalysatoraufheizung bei entleertem NOx-Speicher 3 erfolgt. Anschließend wird bei magerem Abgas eine katalysatortemperatursteigernde Maßnahme (Punkt A der Kurve III) ergriffen, beispielsweise durch Spritzbeginnverstellung, Änderung der EGR-Rate (Abgasrückführrate), Absenken des Ladedrucks, partielle Androsselung, kombinierter Fett-Mager-Betrieb, Einspritzen von Kraftstoff in die Abgasanlage vor dem Katalysator, Nacheinspritzung (nur bei Common-Rail- Motoren). Die Abgastemperatur des Temperatursensors T1 vor dem Katalysator 3 wird analog zu Mager-Otto-Motoren mit 50° Sicherheitsabstand zur Alterungsschwelle eingestellt. Fig. 3 shows the schematic timing of a de-sulfation of a diesel engine 1. The designation of the curves corresponds to that of FIG. 2. In diesel engines, desulfurization cannot be carried out in the same way as in lean gasoline engines, since long-term operation with λ <1 is not possible because of the underperformance and the increasing particle emissions. Therefore, with a view to the NOx thermal desorption threshold, a NOx regeneration is first carried out when the need for desulfurization is recognized, so that the catalyst is heated when the NOx store 3 is empty. If the exhaust gas is lean, a measure to increase the catalyst temperature (point A of curve III) is taken, for example by adjusting the start of injection, changing the EGR rate (exhaust gas recirculation rate), lowering the boost pressure, partial throttling, combined rich-lean operation, injecting fuel into the exhaust system before the catalytic converter, post-injection (only for common rail engines). The exhaust gas temperature of the temperature sensor T1 upstream of the catalytic converter 3 is set analogously to lean-gasoline engines with a 50 ° safety margin from the aging threshold.
Durch Überwachung der Abgastemperatur des Temperatursensors T2 hinter dem NOx- Speicher 3 wird wie beim Ottomotor sichergestellt, daß durch Oxidationsreaktionen auf der NOx-Speicheroberfläche keine Überhitzung stattfindet (Punkt B der Kurve II); gegebenenfalls wird durch teilweise Rücknahme der katalysatortemperatursteigernden Maßnahme (Punkt C der Kurve I) eine thermische Schädigung vermieden. Sobald die Temperatur nach dem Katalysator am Temperatursensor T2 die De-Sulfatierungsgrenze überschritten hat (Punkt D der Kurve II), wird die De-Sulfatierung durch Anfetten des Abgases eingeleitet (Punkt E der Kurve III). Dauer der Anfettung und der Wert von λ während der Fett-Phase richten sich wiederum nach der errechneten oder geschätzten Schwefelbeladung. Die Anfettung kann analog zur NOx-Regeneration, beispielsweise durch Saugluftdrosselung, EGR-Anhebung, Nacheinspritzung oder Ladedrucksendung erfolgen.By monitoring the exhaust gas temperature of the temperature sensor T2 behind the NOx accumulator 3 , it is ensured, as in the case of the gasoline engine, that there is no overheating due to oxidation reactions on the NOx accumulator surface (point B of curve II); if necessary, thermal damage is avoided by partially withdrawing the measure that increases the catalyst temperature (point C of curve I). As soon as the temperature after the catalyst at temperature sensor T2 has exceeded the de-sulfation limit (point D of curve II), de-sulfation is initiated by enriching the exhaust gas (point E of curve III). The duration of the enrichment and the value of λ during the fat phase in turn depend on the calculated or estimated sulfur loading. The enrichment can be carried out analogously to the NOx regeneration, for example by suction air throttling, EGR increase, post-injection or boost pressure transmission.
Nach Beendigung der De-Sulfatierung (Punkt F der Kurve III) kann kein längerer Betrieb mehr mit λ < 1 aufrechterhalten werden; es wird daher sofort wieder der normale Betriebsmodus eingestellt. Wegen der üblicherweise sehr niedrigen Abgastemperaturen bei Dieselmotoren und der resultierend raschen und starken Auskühlung ist trotz der nach der Entschwefelung auftretenden Oxidationsreaktionen nur eine kleine NOx-speicherinterne Temperaturspitze zu erwarten. After de-sulfation has ended (point F of curve III), no longer operation can take place more can be maintained with λ <1; it immediately becomes normal again Operating mode set. Because of the usually very low exhaust gas temperatures Diesel engines and the resulting rapid and strong cooling is despite the after Desulfurization occurring oxidation reactions only a small internal NOx storage Temperature peak to be expected.
11
Motor
engine
22nd
Abgasanlage
Exhaust system
33rd
NOx-Speicherkatalysator
T1 Temperaturfühler 1
T2 Temperaturfühler 2
I Temperaturverlauf T1
I Temperaturverlauf T2
II Verlauf λ
A Einleiten KTM
B Temperaturanstieg zu schnell
C Rücknahme KTM
D Überschreiten De-Sulfatierungstemperatur
E Einleiten De-Sulfatierung
F Ende De-Sulfatierung
G Fett-Mager-Betrieb
KTM Katalysatortemperatursteigernde Maßnahme
NOx storage catalytic converter
T1 temperature sensor 1
T2 temperature sensor 2
I temperature curve T1
I temperature curve T2
II course λ
A Initiate KTM
B Temperature rise too fast
C KTM withdrawal
D Exceeds the desulfation temperature
E Initiate de-sulfation
F End of de-sulfation
G Fat-lean operation
KTM catalyst temperature increasing measure
Claims (13)
- a) Vorliegen der Notwendigkeit einer Entschwefelung,
- b) Einleiten und Durchführen einer abgastemperatursteigernden Maßnahme, mit der der NOx-Speicherkatalysator (3) mindestens auf eine vorbestimmte De- Sulfatierungstemperatur erhitzt wird,
- c) De-Sulfatieren des NOx-Speichers durch Fettbetreiben der Brennkraftmaschine (1), und
- d) Einleiten des Normalbetriebs der Brennkraftmaschine (1) nach der Beendigung des De-Sulfatierungsschritts.
- a) the need for desulfurization,
- b) initiation and implementation of an exhaust gas temperature-increasing measure with which the NOx storage catalytic converter ( 3 ) is heated to at least a predetermined desulfurization temperature,
- c) De-sulfation of the NOx storage by operating the engine with grease ( 1 ), and
- d) initiating normal operation of the internal combustion engine ( 1 ) after the end of the de-sulfation step.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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DE1997131624 DE19731624A1 (en) | 1997-07-23 | 1997-07-23 | Reversible rich regeneration of nitrogen@ oxide absorption catalyst |
DE59807160T DE59807160D1 (en) | 1997-07-19 | 1998-07-09 | Method and device for monitoring the de-sulfation in NOx storage catalysts |
EP98112705A EP0892158B1 (en) | 1997-07-19 | 1998-07-09 | Method and device to monitor the desulphurization of NOx storage catalytic converters |
US09/119,498 US6164064A (en) | 1997-07-19 | 1998-07-20 | Method and arrangement for desulfurization of NOx reservoir catalysts |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1997131624 DE19731624A1 (en) | 1997-07-23 | 1997-07-23 | Reversible rich regeneration of nitrogen@ oxide absorption catalyst |
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Publication Number | Publication Date |
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DE19731624A1 true DE19731624A1 (en) | 1999-01-28 |
Family
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DE1997131624 Withdrawn DE19731624A1 (en) | 1997-07-19 | 1997-07-23 | Reversible rich regeneration of nitrogen@ oxide absorption catalyst |
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DE19910664A1 (en) * | 1999-03-11 | 2000-09-14 | Volkswagen Ag | Process for the de-sulfation of a NOx storage catalytic converter |
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DE19922962A1 (en) * | 1999-05-19 | 2000-11-23 | Daimler Chrysler Ag | Periodic desulfurization of a nitrogen oxide or sulfur oxide storage device in a vehicle I.C. engine comprises adjusting the storage air ratio by changing the secondary air amount introduced and/or the engine air ratio |
DE19923481A1 (en) * | 1999-05-21 | 2000-11-23 | Volkswagen Ag | Desulfurizing a nitrogen oxides storage catalyst arranged in the exhaust gas channel of an IC engine comprises adjusting the engine to a lean working modulus until a threshold value for lambda is reached in a first phase |
DE19926146A1 (en) * | 1999-06-09 | 2000-12-14 | Volkswagen Ag | Method for initiating and monitoring desulfurization of at least one NOx storage catalytic converter arranged in an exhaust gas duct of an internal combustion engine |
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WO2001009491A1 (en) * | 1999-07-28 | 2001-02-08 | Volkswagen Aktiengesellschaft | Method for regulating the exhaust gas temperature of a lean combustion engine during the desulphurization of a catalyst |
DE19952830A1 (en) * | 1999-11-02 | 2001-05-03 | Audi Ag | Process for exhaust gas aftertreatment by post-injection of fuel in a diesel internal combustion engine with a pre-catalytic converter and particle filter |
US6971230B1 (en) | 1999-11-02 | 2005-12-06 | Audi Ag | Method for the post-treatment of exhaust gases by subsequent injection of fuel in a diesel-type internal combustion engine provided with a pre-catalyst and a particle filter |
DE19959610A1 (en) * | 1999-12-10 | 2001-06-13 | Volkswagen Ag | Method for heating a catalytic converter, in particular in idle mode, of a lean-burn internal combustion engine of a vehicle |
DE10005473A1 (en) * | 2000-02-08 | 2001-08-09 | Bayerische Motoren Werke Ag | Process for operating an internal combustion engine comprises a multiple step process in which the nitrogen oxides emissions in the exhaust gas are initially continuously or intermittently measured after the nitrogen oxides storage catalyst |
DE10005473C2 (en) * | 2000-02-08 | 2002-01-17 | Bayerische Motoren Werke Ag | Method and device for desulfating a nitrogen oxide storage catalyst |
EP1134393A3 (en) * | 2000-03-17 | 2003-09-10 | Ford Global Technologies, Inc. | Method and apparatus for controlling a lean-burn engine |
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US6854266B2 (en) | 2000-08-11 | 2005-02-15 | Robert Bosch GmbH | Method for desulfurizing a storage medium |
WO2002014666A1 (en) * | 2000-08-11 | 2002-02-21 | Robert Bosch Gmbh | Method for desulfurizing a storage medium |
KR100795621B1 (en) * | 2000-08-11 | 2008-01-17 | 로베르트 보쉬 게엠베하 | Method for desulfurizing a storage |
US6637198B2 (en) | 2000-11-01 | 2003-10-28 | Daimlerchrysler Ag | Method for operating an emission control system having nitrogen oxide storage |
DE10153901B4 (en) * | 2001-10-12 | 2011-07-14 | Volkswagen AG, 38440 | Method and device for desulfurization of a diesel engine downstream NOx storage catalyst |
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