WO2009136029A1 - Method for regenerating a post-treatment system by splitting up the richness - Google Patents
Method for regenerating a post-treatment system by splitting up the richness Download PDFInfo
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- WO2009136029A1 WO2009136029A1 PCT/FR2009/050559 FR2009050559W WO2009136029A1 WO 2009136029 A1 WO2009136029 A1 WO 2009136029A1 FR 2009050559 W FR2009050559 W FR 2009050559W WO 2009136029 A1 WO2009136029 A1 WO 2009136029A1
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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
- F01N3/02—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
- F01N3/023—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 using means for regenerating the filters, e.g. by burning trapped particles
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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
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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
- F01N9/002—Electrical control of exhaust gas treating apparatus of filter regeneration, e.g. detection of clogging
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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
- F02D41/024—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to increase temperature 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
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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
- F01N2560/025—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting O2, e.g. lambda sensors
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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
- F01N2560/08—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being a pressure sensor
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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
- F01N2610/03—Adding substances to exhaust gases the substance being hydrocarbons, e.g. engine fuel
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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
- F01N3/023—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 using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/0231—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 using means for regenerating the filters, e.g. by burning trapped particles using special exhaust apparatus upstream of the filter for producing nitrogen dioxide, e.g. for continuous filter regeneration systems [CRT]
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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
- F02D2200/0802—Temperature of the exhaust gas treatment apparatus
- F02D2200/0804—Estimation of the temperature of the exhaust gas treatment 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
- F02D2250/00—Engine control related to specific problems or objectives
- F02D2250/11—Oil dilution, i.e. prevention thereof or special controls according thereto
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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
- F02D41/1473—Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the regulation method
- F02D41/1475—Regulating the air fuel ratio at a value other than stoichiometry
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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
Definitions
- a method of regenerating a post-processing system by fractionating wealth is provided.
- the present invention generally relates to exhaust aftertreatment systems of an internal combustion engine, in particular a diesel engine, and, in particular, the regeneration of the after-treatment systems.
- a point is chosen. of engine operation favorable to the regeneration process.
- the regeneration is preceded by a heating phase of the system in order to obtain the minimum temperature above which it is effective.
- a first strategy uses preheating systems such as air pumps, electrical resistors, an additional injector to the exhaust, while another strategy optimizes the operation of the engine to increase the temperature of the exhaust gas.
- GB 2324052 A (Ford) discloses a method of regenerating a post-treatment system comprising a three-way catalyst and a nitrogen oxide trap connected in series, the nitrogen oxide trap.
- the method consists in controlling the richness of the air / fuel mixture of the engine during the temperature rise phase as a function of oxygen consumption and renewal cycles in the nitrogen oxide trap.
- a relatively poor mixture is injected for a time sufficient for the oxygen to be stored in the nitrogen oxide trap.
- a relatively rich mixture is then injected into the cylinders for a sufficient time so that the resulting excess fuel in the exhaust gas first reacts completely with the oxygen stored in the three - way catalyst, and then the surplus The remaining fuel passes through the three - way catalyst to react with the oxygen stored in the nitrogen oxide trap, thereby releasing heat and raising the temperature of the nitrogen oxide trap.
- This mode of operation should be maintained for approximately 5 minutes before the nitrogen oxide trap reaches the regeneration temperature.
- the engine must also be maintained in an operating mode in which excess fuel is obtained for a period of time long enough to purge the trap.
- US patent application 2005/0076637 discloses another type of regeneration method of an exhaust line in wherein a lean air / fuel mixture is introduced into the internal combustion engine by additionally injecting fuel into the combustion chamber of the engine after the primary injection.
- the richness of the air / fuel mixture of the engine is cyclically modulated during the temperature rise phase by following the oxygen consumption and renewal cycles in the catalyst.
- the probability of maintaining favorable purging conditions is inversely proportional to the heating time of the post-treatment system. Therefore, whatever the heating strategy used, the objective is to reach as quickly as possible the temperature from which the post-treatment system is effective in order to increase desulfurization opportunities and to limit the dilution of fuel in the oil.
- one method consists of injecting fuel into the combustion chamber, creating no torque, after the top dead center, while maintaining a richness (air mixture / fuel) below 1. Indeed, increasing the richness of the gases causes a rise in temperature and exotherm in the catalytic part of the post-treatment systems, due to the oxidation of the lean mixture reducers. (air / fuel ratio greater than 1).
- the aim of the invention is thus to accelerate the temperature rise of the aftertreatment systems present at the exhaust by acting directly on the richness of the gases leaving the engine.
- the object of the invention is therefore a regeneration method of a gas post-treatment system of an exhaust line of an internal combustion engine by raising the temperature of the post-treatment system to a maximum regeneration temperature.
- the richness of the air / fuel mixture is varied by implementing successive phases of injection of relatively rich and poor mixtures independently of the consumption and the renewal of oxygen in the exhaust line.
- the relatively rich mixture remains established for a time within a range of 0.5s to 2s, and the relatively poor mixture remains established during a time in the same interval from 0.5s to 2s. This time is previously defined, and does not require additional sensors that would add to the cost of production.
- the increase in richness of the mixture at each new cycle can be done for example by injecting fuel upstream of the post-treatment system.
- the invention also relates, in another aspect, to a gas post-treatment system of an exhaust line of an internal combustion engine comprising means for raising the temperature of the aftertreatment system to a regeneration temperature.
- this system comprises means for varying the richness of the air / fuel mixture and means for implementing successive phases of injection of relatively rich and poor mixtures regardless of consumption or renewal of oxygen in the exhaust line to raise the temperature of the aftertreatment system to the regeneration temperature.
- the system may comprise an additional fuel injector placed at the inlet of the gas aftertreatment system intended to increase the richness of the air / fuel mixture during a purge phase of the post-treatment system.
- the device comprises a temperature probe placed between the nitrogen oxide trap and the particle filter.
- the device comprises a temperature probe at the inlet of the post-treatment system.
- This temperature probe is placed between the additional injector and the nitrogen oxide trap, as close as possible to the trap, in the case of an additional injector enrichment system.
- the device of the invention comprises an oxygen probe placed at the outlet of the nitrogen oxide trap.
- This oxygen sensor placed downstream of the nitrogen oxide trap makes it possible to detect the purges of the trap and to check the state of said trap during onboard diagnostics.
- the device of the invention comprises an oxygen probe placed upstream of the nitrogen oxide trap.
- This oxygen sensor is also placed upstream of the additional injector in the case of a wealth increase by additional injector.
- This oxygen sensor which makes it possible to measure the fractionation of the richness of the air / fuel mixture upstream of the additional injector, makes it possible to construct a setpoint by estimation for the control relating to the operation of the nitrogen oxide trap.
- FIG. 1 illustrates the evolution of the temperature on the upstream face of a nitrogen oxide trap during a rich / poor transition of the exhaust gases of an internal combustion engine.
- FIG. 2 illustrates a post processing architecture implementing the regeneration method according to the invention.
- FIG. 4 represents curves of temperature and dilution of the fuel in the oil as a function of time, in the case of heating by rapid fractionation of the richness.
- FIG. 1 shows the temperature variation of a monolith (c 1), during a test phase, at low hourly volumetric speed, during a rich / poor transition.
- a monolith c 1
- Trp rich / poor transition
- the temperature of the monolith increases before decreasing towards the stabilized temperature of the lean state. This phase is exploited to increase the heating rate of the monolith.
- FIG. 2 represents an architecture according to the invention, designated by the general numerical reference 1, intended for the post-treatment of the exhaust gases and therefore intended to be placed at the outlet of an internal combustion engine 2.
- the exhaust gases are discharged through the aftertreatment system, which is composed of a nitrogen oxide trap 3 and a particulate filter 4.
- the temperature of the aftertreatment system is controlled at input by a first temperature sensor 5 and entering the particle filter with a last temperature probe 6.
- the state of the nitrogen oxide trap and therefore the need or not to regenerate the trap is controlled using an oxygen sensor 7 placed at the exit of the trap.
- the contamination of the particulate filter is controlled by means of a system for measuring the differential pressure 9 between the inlet of the particulate filter and its outlet.
- an additional fuel injector 10 is placed at the inlet of the nitrogen oxide trap in this example.
- the richness of the mixture can also be achieved by post-injection of fuel into the cylinders.
- the fractionation of the richness of the air / fuel mixture is measured with the aid of an oxygen probe 13 placed upstream of the nitrogen oxide trap 3 and the additional fuel injector 10.
- An electronic control unit 12 duly programmed ensures the control of the main injection system and, in particular, monitors the fouling of the after-treatment systems, that is to say the particle filter from the differential pressure prevailing on both sides. other of the filter.
- the filter temperature is raised to a regeneration temperature. This temperature rise is for example obtained by injecting an air / fuel mixture into the exhaust line by means of the injector 10.
- the temperature in a monolith begins to increase before decreasing towards the stabilized temperature of the lean state.
- the temperature rise is here obtained by exploiting this temperature increase phase preceding the lowering of the temperature in order to increase the heating rate of the filter.
- Figure 4 represents the temperature (c2 ') and dilution (c3') curves of the fuel in the oil as a function of time, in the case of fractionation heating according to the invention of the richness. It is noted that after 40s of heating, the temperature on the upstream face of the nitrogen oxide trap reaches 658 ° C. in fractional mode, whereas it reaches only 564 ° C. in constant richness mode, which represents a 96 ° C gain.
- the regeneration method which has just been described can be adapted to any post-treatment architecture provided with a nitrogen oxide trap, a particle filter, an additional injector, of a pre-treatment temperature probe and an input temperature sensor of the particulate filter, an oxygen sensor at the outlet of the nitrogen oxide trap, a differential pressure sensor at the particle filter, and an electronic control unit driving these elements.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Exhaust Gas After Treatment (AREA)
- Electrical Control Of Air Or Fuel Supplied To Internal-Combustion Engine (AREA)
- Processes For Solid Components From Exhaust (AREA)
Abstract
The invention relates to a method of regenerating a gas post-treatment system of an exhaust line 1 of an internal combustion engine 2 by increasing the temperature of the post-treatment system up to a regeneration temperature. During the increase in temperature, the richness of the air/fuel mixture is varied by implementing successive phases of injecting relatively rich and lean mixtures independently of the consumption or of the renewal of oxygen in the exhaust line.
Description
Procédé de régénération d'un système de post traitement par fractionnement de la richesse. A method of regenerating a post-processing system by fractionating wealth.
La présente invention concerne, d'une manière générale, les systèmes de post traitement des gaz d' échappement d'un moteur à combustion interne, notamment d'un moteur diesel, et, en particulier, la régénération des systèmes de post-traitement.The present invention generally relates to exhaust aftertreatment systems of an internal combustion engine, in particular a diesel engine, and, in particular, the regeneration of the after-treatment systems.
Afin de répondre à la baisse des seuils admis pour les émissions de gaz polluants des véhicules automobiles, des systèmes de post traitement des gaz de plus en plus complexes sont disposés dans la ligne d' échappement des moteurs à combustion interne. Ceux-ci permettent notamment de réduire les émissions de particules et d'oxydes d' azotes en plus du monoxyde de carbone et des hydrocarbures imbrûlés. Pour brûler complètement les polluants, ces systèmes de post traitement nécessitent de travailler à des températures élevées, ce qui n' est malheureusement pas le cas en régime normal du moteur.In order to meet the lower thresholds for emissions of gaseous pollutants from motor vehicles, increasingly complex aftertreatment systems are arranged in the exhaust line of internal combustion engines. These include reducing particulate and nitrogen oxide emissions in addition to carbon monoxide and unburned hydrocarbons. To completely burn the pollutants, these post-treatment systems require working at high temperatures, which is unfortunately not the case under normal engine conditions.
Lorsqu'on envisage une phase de régénération d'un filtre à particules pour éviter le colmatage de celui-ci, la désulfurisation d'un piège à oxyde d' azote, ou plus généralement le traitement de polluants à thermique élevée, on choisit un point de fonctionnement du moteur favorable au processus de régénération. La régénération est précédée d'une phase de chauffe du système dans le but d'obtenir la température minimale au dessus de laquelle il est efficace. Deux types de stratégies existent. Une première stratégie utilise des systèmes de préchauffage tels que des pompes à air, des résistances électriques, un injecteur additionnel à l' échappement, tandis qu'une autre stratégie optimise le fonctionnement du moteur pour augmenter la température des gaz d' échappement.
Par exemple, la demande de brevet GB 2324052 A (Ford) décrit un procédé de régénération d'un système de post traitement comprenant un catalyseur à trois voies et un piège à oxyde d' azote connectés en série, le piège à oxyde d' azote contenant des éléments de stockage pour l'oxygène. La méthode consiste à contrôler la richesse du mélange air/carburant du moteur lors de la phase d' élévation de température en fonction des cycles de consommation et de renouvellement d'oxygène dans le piège à oxyde d' azote. Un mélange relativement pauvre est injecté pendant un temps suffisant pour que l'oxygène soit emmagasiné dans le piège à oxyde d' azote. Un mélange relativement riche est ensuite injecté dans les cylindres pendant un temps suffisant afin que le surplus de carburant résultant dans les gaz d' échappement réagisse tout d' abord complètement avec l'oxygène emmagasiné dans le catalyseur à trois voies, puis pour que le surplus de carburant restant traverse le catalyseur à trois voies pour venir réagir avec l'oxygène emmagasiné dans le piège à oxyde d' azote, et ainsi dégager de la chaleur et élever la température du piège à oxyde d' azote. L 'amplitude de modulation du rapport air/carburant nécessaire pour cette opération est de l'ordre de λ = 0.1 et la fréquence doit être plus petite que 1 Hz.When considering a regeneration phase of a particulate filter to prevent clogging thereof, the desulfurization of a nitrogen oxide trap, or more generally the treatment of pollutants with a high temperature, a point is chosen. of engine operation favorable to the regeneration process. The regeneration is preceded by a heating phase of the system in order to obtain the minimum temperature above which it is effective. Two types of strategies exist. A first strategy uses preheating systems such as air pumps, electrical resistors, an additional injector to the exhaust, while another strategy optimizes the operation of the engine to increase the temperature of the exhaust gas. For example, GB 2324052 A (Ford) discloses a method of regenerating a post-treatment system comprising a three-way catalyst and a nitrogen oxide trap connected in series, the nitrogen oxide trap. containing storage elements for oxygen. The method consists in controlling the richness of the air / fuel mixture of the engine during the temperature rise phase as a function of oxygen consumption and renewal cycles in the nitrogen oxide trap. A relatively poor mixture is injected for a time sufficient for the oxygen to be stored in the nitrogen oxide trap. A relatively rich mixture is then injected into the cylinders for a sufficient time so that the resulting excess fuel in the exhaust gas first reacts completely with the oxygen stored in the three - way catalyst, and then the surplus The remaining fuel passes through the three - way catalyst to react with the oxygen stored in the nitrogen oxide trap, thereby releasing heat and raising the temperature of the nitrogen oxide trap. The amplitude of modulation of the air / fuel ratio necessary for this operation is of the order of λ = 0.1 and the frequency must be smaller than 1 Hz.
Ce mode d'opération doit être maintenu pendant approximativement 5 minutes avant que le piège à oxyde d' azote n' atteigne la température de régénération. Le moteur doit en outre être maintenu dans un mode de fonctionnement selon lequel un excédant de carburant est obtenu pendant une période de temps suffisamment longue pour purger le piège.This mode of operation should be maintained for approximately 5 minutes before the nitrogen oxide trap reaches the regeneration temperature. The engine must also be maintained in an operating mode in which excess fuel is obtained for a period of time long enough to purge the trap.
La demande de brevet US 2005/0076637 (Audi) décrit un autre type de procédé de régénération d'une ligne d' échappement dans
lequel on introduit un mélange air/carburant pauvre dans le moteur à combustion interne, en injectant de manière additionnelle du carburant dans la chambre de combustion du moteur après l'injection primaire. La richesse du mélange air/carburant du moteur est modulée cycliquement lors de la phase d' élévation de température en suivant les cycles de consommation et de renouvellement d'oxygène dans le catalyseur.US patent application 2005/0076637 (Audi) discloses another type of regeneration method of an exhaust line in wherein a lean air / fuel mixture is introduced into the internal combustion engine by additionally injecting fuel into the combustion chamber of the engine after the primary injection. The richness of the air / fuel mixture of the engine is cyclically modulated during the temperature rise phase by following the oxygen consumption and renewal cycles in the catalyst.
Par ailleurs, la probabilité de maintenir des conditions favorables de purge est inversement proportionnelle à la durée de chauffe du système de post traitement. De ce fait, quelque soit la stratégie de chauffe utilisée, l'objectif est d' atteindre le plus rapidement possible la température à partir de laquelle le système de post traitement est efficace afin d'augmenter les opportunités de désulfurisation et de limiter la dilution de carburant dans l'huile. Afin d'obtenir les conditions de richesse et de température nécessaires en amont du système, une méthode consiste à injecter du carburant dans la chambre de combustion, ne créant pas de couple, après le point mort haut, tout en maintenant une richesse (mélange air/carburant) en dessous de 1. En effet, le fait d' augmenter la richesse des gaz provoque une hausse de température et de l' exotherme dans la partie catalytique des systèmes de post traitement, due à l'oxydation des réducteurs en mélange pauvre (rapport air/carburant supérieur à 1 ). Le niveau de richesse (Ri = 0.99) est alors maintenu constant pendant la durée de chauffe. Dans la pratique, on constate avec cette méthode que les temps de chauffe d'un piège à oxyde d' azote sont trop élevés à faible régime et faibles charges, puisqu'ils sont de l'ordre de 50 à 100 secondes, ce qui n' est pas acceptable sur des profiles de roulage de type urbain et extra urbain puisqu'ils ne permettent pas de réaliser des désulfurisation efficaces et engendrent une forte dilution.
L 'invention vise ainsi à accélérer l' élévation de température des systèmes de post traitement présents à l' échappement en agissant directement sur la richesse des gaz en sortie du moteur.Moreover, the probability of maintaining favorable purging conditions is inversely proportional to the heating time of the post-treatment system. Therefore, whatever the heating strategy used, the objective is to reach as quickly as possible the temperature from which the post-treatment system is effective in order to increase desulfurization opportunities and to limit the dilution of fuel in the oil. In order to obtain the necessary conditions of richness and temperature upstream of the system, one method consists of injecting fuel into the combustion chamber, creating no torque, after the top dead center, while maintaining a richness (air mixture / fuel) below 1. Indeed, increasing the richness of the gases causes a rise in temperature and exotherm in the catalytic part of the post-treatment systems, due to the oxidation of the lean mixture reducers. (air / fuel ratio greater than 1). The level of richness (Ri = 0.99) is then kept constant during the heating period. In practice, it is found with this method that the heating times of a nitrogen oxide trap are too high at low speed and low loads, since they are of the order of 50 to 100 seconds, which is not acceptable on urban and extra-urban type rolling profiles since they do not make it possible to carry out effective desulfurization and generate a high dilution. The aim of the invention is thus to accelerate the temperature rise of the aftertreatment systems present at the exhaust by acting directly on the richness of the gases leaving the engine.
L 'invention a donc pour obj et, un procédé de régénération d'un système de post traitement de gaz d'une ligne d' échappement d'un moteur à combustion interne par élévation de la température du système de post traitement jusqu' à une température de régénération.The object of the invention is therefore a regeneration method of a gas post-treatment system of an exhaust line of an internal combustion engine by raising the temperature of the post-treatment system to a maximum regeneration temperature.
Selon une caractéristique générale de ce procédé, lors de l' élévation de température, on fait varier la richesse du mélange air/carburant en mettant en œuvre des phases successives d'injection de mélanges relativement riches et pauvres indépendamment de la consommation et du renouvellement d'oxygène dans la ligne d' échappement.According to a general characteristic of this process, during the rise in temperature, the richness of the air / fuel mixture is varied by implementing successive phases of injection of relatively rich and poor mixtures independently of the consumption and the renewal of oxygen in the exhaust line.
Avantageusement, pour chacun des cycles riche/pauvre de la phase d' élévation de température jusqu' à la température de régénération, le mélange relativement riche reste établit durant un temps compris dans un intervalle de 0,5s à 2s, et le mélange relativement pauvre reste établit durant un temps compris dans le même intervalle de 0,5s à 2s. Ce temps est préalablement définit, et ne nécessite pas de capteurs supplémentaires qui rajouteraient au coût de production.Advantageously, for each of the rich / poor cycles of the temperature rise phase up to the regeneration temperature, the relatively rich mixture remains established for a time within a range of 0.5s to 2s, and the relatively poor mixture remains established during a time in the same interval from 0.5s to 2s. This time is previously defined, and does not require additional sensors that would add to the cost of production.
Avantageusement, lors de cette montée en température, l' élévation de richesse du mélange à chaque nouveau cycle peut se faire par exemple en injectant du carburant en amont du système de post traitement.Advantageously, during this rise in temperature, the increase in richness of the mixture at each new cycle can be done for example by injecting fuel upstream of the post-treatment system.
On peut également élever la richesse du mélange air/carburant par post-injection de carburant dans le moteur, c 'est-à-dire en effectuant une injection retardée de carburant dans les cylindres du moteur, de sorte que ce carburant supplémentaire injecté ne soit pas
brûlé et contribue à l' élévation de richesse, et ainsi l'élévation de température.It is also possible to increase the richness of the air / fuel mixture by post-injection of fuel into the engine, that is to say by performing a delayed injection of fuel into the engine cylinders, so that this additional fuel injected is not burned and contributes to the rise of wealth, and thus the rise of temperature.
Selon un mode de mise en oeuvre, pour un point de fonctionnement moteur stabilisé à 1200 rpm / 4 bars, on fractionne la richesse en créneaux de richesse λ = 1 ,01 (pauvre) et de richesse λ =According to one embodiment, for a motor operating point stabilized at 1200 rpm / 4 bar, the wealth richness slices λ = 1, 01 (poor) and wealth λ = are split up.
0,95 (riche) de durée 1 seconde.0.95 (rich) of duration 1 second.
L 'invention a également pour objet, selon un autre aspect, un système de post traitement de gaz d'une ligne d' échappement d'un moteur à combustion interne comprenant des moyens pour élever la température du système de post traitement jusqu' à une température de régénération.The invention also relates, in another aspect, to a gas post-treatment system of an exhaust line of an internal combustion engine comprising means for raising the temperature of the aftertreatment system to a regeneration temperature.
Selon une caractéristique générale de ce système, celui-ci comprend des moyens pour faire varier la richesse du mélange air/carburant et des moyens pour mettre en oeuvre des phases successives d'injection de mélanges relativement riche et pauvre indépendamment de la consommation ou du renouvellement d'oxygène dans la ligne d' échappement pour élever la température du système de post traitement jusqu' à la température de régénération.According to a general characteristic of this system, it comprises means for varying the richness of the air / fuel mixture and means for implementing successive phases of injection of relatively rich and poor mixtures regardless of consumption or renewal of oxygen in the exhaust line to raise the temperature of the aftertreatment system to the regeneration temperature.
Avantageusement, le système peut comprendre un injecteur additionnel de carburant placé à l' entrée du système de post traitement des gaz destiné à augmenter la richesse du mélange air/carburant lors d'une phase de purge du système de post traitement.Advantageously, the system may comprise an additional fuel injector placed at the inlet of the gas aftertreatment system intended to increase the richness of the air / fuel mixture during a purge phase of the post-treatment system.
Selon une caractéristique de l'invention, le dispositif comprend une sonde de température placée entre le piège à oxyde d' azote et le filtre à particule.According to one characteristic of the invention, the device comprises a temperature probe placed between the nitrogen oxide trap and the particle filter.
Selon encore une autre caractéristique de l'invention, le dispositif comprend une sonde de température à l' entrée du système de post traitement.
Cette sonde de température est placé entre l'injecteur additionnel et le piège à oxydes d' azote, au plus près du piège, dans le cas d'un système d'élévation de richesse par injecteur additionnel.According to yet another characteristic of the invention, the device comprises a temperature probe at the inlet of the post-treatment system. This temperature probe is placed between the additional injector and the nitrogen oxide trap, as close as possible to the trap, in the case of an additional injector enrichment system.
On peut encore utiliser un système de mesure de la pression différentielle au niveau du filtre à particules destiné à contrôler l' état du filtre.It is also possible to use a system for measuring the differential pressure at the level of the particulate filter for controlling the state of the filter.
Avantageusement, le dispositif de l'invention comprend une sonde à oxygène placée à la sortie du piège à oxyde d'azote.Advantageously, the device of the invention comprises an oxygen probe placed at the outlet of the nitrogen oxide trap.
Cette sonde à oxygène placée en aval du piège à oxydes d' azote permet de détecter les fins de purge du piège et de vérifier l' état dudit piège lors de diagnostiques embarqués.This oxygen sensor placed downstream of the nitrogen oxide trap makes it possible to detect the purges of the trap and to check the state of said trap during onboard diagnostics.
Avantageusement, le dispositif de l'invention comprend une sonde à oxygène placée en amont du piège à oxyde d' azote.Advantageously, the device of the invention comprises an oxygen probe placed upstream of the nitrogen oxide trap.
Cette sonde à oxygène est également placée en amont de l' injecteur additionnel dans le cas d'une élévation de richesse par injecteur additionnel. Cette sonde à oxygène permettant une mesure du fractionnement de la richesse du mélange air/carburant en amont de l' injecteur supplémentaire, permet de construire une consigne par estimation pour la commande relative au fonctionnement du piège à oxydes d' azote.This oxygen sensor is also placed upstream of the additional injector in the case of a wealth increase by additional injector. This oxygen sensor, which makes it possible to measure the fractionation of the richness of the air / fuel mixture upstream of the additional injector, makes it possible to construct a setpoint by estimation for the control relating to the operation of the nitrogen oxide trap.
D ' autres avantages et caractéristiques de l'invention apparaîtront à l' examen de la description détaillée d'un mode de réalisation de l'invention nullement limitatif, et des dessins annexés, sur lesquels : -la figure 1 illustre l'évolution de la température sur la face amont d'un piège à oxyde d' azote lors d'une transition riche/pauvre des gaz d'échappement d'un moteur à combustion interne.Other advantages and features of the invention will appear on examining the detailed description of an embodiment of the invention which is in no way limitative, and the attached drawings, in which: FIG. 1 illustrates the evolution of the temperature on the upstream face of a nitrogen oxide trap during a rich / poor transition of the exhaust gases of an internal combustion engine.
-la figure 2 illustre une architecture de post traitement mettant en œuvre le procédé de régénération suivant l'invention.
-la figure 3 représente des courbes de température et de dilution du carburant dans l'huile en fonction du temps, dans le cas d'une chauffe classique à richesse constante λ = 1 ,01.FIG. 2 illustrates a post processing architecture implementing the regeneration method according to the invention. FIG. 3 represents curves of temperature and dilution of the fuel in the oil as a function of time, in the case of a conventional constant-rich heater λ = 1.0.
-la figure 4 représente des courbes de température et de dilution du carburant dans l'huile en fonction du temps, dans le cas d'une chauffe par fractionnement rapide de la richesse.FIG. 4 represents curves of temperature and dilution of the fuel in the oil as a function of time, in the case of heating by rapid fractionation of the richness.
Sur la figure 1 on a représenté la variation de température d'un monolithe (c l ), pendant une phase de test, à faible vitesse volumique horaire, lors d'une transition riche/pauvre. Lors de la transition riche/pauvre (Trp), la température du monolithe augmente avant de décroître vers la température stabilisée de l' état pauvre. Cette phase est exploitée afin d' accroître la vitesse de chauffe du monolithe.FIG. 1 shows the temperature variation of a monolith (c 1), during a test phase, at low hourly volumetric speed, during a rich / poor transition. During the rich / poor transition (Trp), the temperature of the monolith increases before decreasing towards the stabilized temperature of the lean state. This phase is exploited to increase the heating rate of the monolith.
En fractionnant rapidement la richesse en deux créneaux riches et pauvres, réchauffement du monolithe est optimisé, contrairement à un chauffage du système de post traitement réalisé à une richesse constante de l'ordre de λ = 0,99.By rapidly splitting the wealth into two rich and poor niches, monolith heating is optimized, unlike a heating of the post-treatment system carried out at a constant richness of the order of λ = 0.99.
Il est donc possible avec cette stratégie, de réduire de l'ordre de 50% le temps de chauffe dans des conditions de roulage difficiles, c' est-à-dire à bas régime et faible charge. On diminue ainsi le temps de chauffe et la dilution du carburant dans l'huile, optimisant ainsi la gestion globale des prestations dépollution / consommation et dilution de gazole dans l'huile.It is therefore possible with this strategy to reduce the heating time in the order of 50% under difficult driving conditions, that is to say at low speed and low load. This reduces the heating time and the dilution of the fuel in the oil, thus optimizing the overall management of benefits depollution / consumption and dilution of diesel in the oil.
La figure 2 représente une architecture selon l'invention, désignée par la référence numérique générale 1 , destinée au post traitement des gaz d'échappement et donc destinée à être placée à la sortie d'un moteur à combustion interne 2.FIG. 2 represents an architecture according to the invention, designated by the general numerical reference 1, intended for the post-treatment of the exhaust gases and therefore intended to be placed at the outlet of an internal combustion engine 2.
Comme on le voit, les gaz d' échappement sont évacués par le système de post traitement ici composé d'un piège à oxyde d' azote 3 et d'un filtre à particules 4. La température du système de post traitement est contrôlée à l' entrée par une première sonde de température 5 et à
l' entrée du filtre à particule grâce à une dernière sonde de température 6.As can be seen, the exhaust gases are discharged through the aftertreatment system, which is composed of a nitrogen oxide trap 3 and a particulate filter 4. The temperature of the aftertreatment system is controlled at input by a first temperature sensor 5 and entering the particle filter with a last temperature probe 6.
L ' état du piège à oxyde d' azote et donc le besoin ou non de régénérer le piège est contrôlé à l'aide d'une sonde à oxygène 7 placée à la sortie du piège. L ' encrassage du filtre à particules quant à lui est contrôlé grâce à un système de mesure de la pression différentielle 9 entre l' entrée du filtre à particules et sa sortie. Afin d' élever la richesse des gaz dans le système de post traitement, un injecteur additionnel de carburant 10 est placé à l' entrée du piège à oxyde d' azote dans cet exemple. L' élévation de richesse du mélange peut également être effectuée par post-injection de carburant dans les cylindres. Le fractionnement de la richesse du mélange air/carburant est mesurée à l' aide d'une sonde à oxygène 13 placée en amont du piège à oxydes d' azote 3 et de l'injecteur additionnel de carburant 10. Une unité de contrôle électronique 12 dûment programmée assure le contrôle du système d'injection principale et, en particulier, surveille l' encrassement des systèmes de post-traitement , c' est-à-dire du filtre à particules à partir de la pression différentielle régnant de part et d' autre du filtre. Lorsqu'il est détecté que le filtre doit être régénéré, il est procédé à une élévation de température du filtre jusqu' à une température de régénération. Cette élévation de température est par exemple obtenue en injectant un mélange air/carburant dans la ligne d' échappement au moyen de l'injecteur 10.The state of the nitrogen oxide trap and therefore the need or not to regenerate the trap is controlled using an oxygen sensor 7 placed at the exit of the trap. The contamination of the particulate filter is controlled by means of a system for measuring the differential pressure 9 between the inlet of the particulate filter and its outlet. In order to raise the richness of the gases in the aftertreatment system, an additional fuel injector 10 is placed at the inlet of the nitrogen oxide trap in this example. The richness of the mixture can also be achieved by post-injection of fuel into the cylinders. The fractionation of the richness of the air / fuel mixture is measured with the aid of an oxygen probe 13 placed upstream of the nitrogen oxide trap 3 and the additional fuel injector 10. An electronic control unit 12 duly programmed ensures the control of the main injection system and, in particular, monitors the fouling of the after-treatment systems, that is to say the particle filter from the differential pressure prevailing on both sides. other of the filter. When it is detected that the filter needs to be regenerated, the filter temperature is raised to a regeneration temperature. This temperature rise is for example obtained by injecting an air / fuel mixture into the exhaust line by means of the injector 10.
A faible vitesse volumique horaire, lors d'une transition riche/pauvre, la température dans un monolithe commence par augmenter avant de décroître vers la température stabilisée de l' état pauvre. Ainsi, l'élévation de température est ici obtenue en exploitant cette phase d' augmentation de température précédant l' abaissement de température afin d' accroître la vitesse de chauffe du filtre. En fractionnant rapidement la richesse en deux créneaux riches et pauvres
à la différence de la situation initiale où la chauffe du système de post traitement était réalisée à une richesse constante de l'ordre de λ = 0,99, r échauffement du monolithe est optimisé. Il est donc possible avec cette nouvelle stratégie, de réduire de l'ordre de 50% le temps de chauffe dans des conditions de roulage difficiles, c' est-à-dire à bas régime et faible charge. On diminue ainsi le temps de chauffe et la dilution du carburant dans l'huile, optimisant ainsi la gestion globale des prestations dépollution / consommation et dilution de gazole dans l'huile. Par exemple, sur un point de fonctionnement moteur stabilisé àAt low hourly volumetric velocity, during a rich / poor transition, the temperature in a monolith begins to increase before decreasing towards the stabilized temperature of the lean state. Thus, the temperature rise is here obtained by exploiting this temperature increase phase preceding the lowering of the temperature in order to increase the heating rate of the filter. By quickly splitting wealth into two rich and poor niches unlike the initial situation where the heating of the post-treatment system was carried out at a constant richness of the order of λ = 0.99, the heating of the monolith is optimized. It is therefore possible with this new strategy to reduce the heating time in the order of 50% under difficult driving conditions, that is to say at low speed and low load. This reduces the heating time and the dilution of the fuel in the oil, thus optimizing the overall management of benefits depollution / consumption and dilution of diesel in the oil. For example, on a motor operating point stabilized at
1200 rpm / 4 bars, on fractionne la richesse en créneaux de richesse λ= l ,01 (pauvre) et de richesse λ=0,95 (riche) de durée 1 seconde, contrairement à l' état de la technique où la régénération se produit traditionnellement avec une richesse constante des gaz d'échappement de valeur λ=l ,01 pendant toute la durée de chauffe du système de post traitement.1200 rpm / 4 bar, one splits the richness in slices of wealth λ = l, 01 (poor) and richness λ = 0.95 (rich) of duration 1 second, contrary to the state of the art where the regeneration is traditionally produced with a constant richness of the exhaust gas of value λ = 1.01 during the entire heating period of the post-treatment system.
La figure 3 présente les courbes de température (c2) et de dilution (c3) du carburant dans l'huile en fonction du temps, dans le cas d'une chauffe conventionnelle à richesse constante λ = 1 ,01 , tandis que la figure 4 représente les courbes de température (c2 ') et de dilution (c3 ') du carburant dans l'huile en fonction du temps, dans le cas d'une chauffe par fractionnement conforme à l'invention de la richesse. On constate qu' après 40s de chauffe, la température sur la face amont du piège à oxyde d' azote atteint 658°C en mode fractionnée, alors qu' elle n' atteint que 564°C en mode richesse constante, ce qui représente un gain de 96°C. Si l'on considère le temps de chauffe pour atteindre 564°C sur la face amont du piège à oxyde d' azote, il suffit de 23s en chauffe fractionnée au lieu de 40s à richesse constante soit un gain de 17s.
D 'un point de vue dilution de carburant dans l'huile, les courbes démontrent également un gain sur l'intégrale de la quantité de carburant post inj ecté. A l'iso température de chauffe, ici 564°C, la quantité cumulée de carburant post injecté n' est que de 313 cg.s/cp en mode fractionné au lieu de 363 cg.s/cp en chauffe à richesse constante, ce qui représente un gain de 15%.Figure 3 shows the temperature (c2) and dilution (c3) curves of the fuel in the oil as a function of time, in the case of conventional constant-rich heating λ = 1, 01, while Figure 4 represents the temperature (c2 ') and dilution (c3') curves of the fuel in the oil as a function of time, in the case of fractionation heating according to the invention of the richness. It is noted that after 40s of heating, the temperature on the upstream face of the nitrogen oxide trap reaches 658 ° C. in fractional mode, whereas it reaches only 564 ° C. in constant richness mode, which represents a 96 ° C gain. If one considers the heating time to reach 564 ° C on the upstream face of the nitrogen oxide trap, it is enough to 23s in fractional heating instead of 40s with constant wealth is a gain of 17s. From a fuel dilution point of view, the curves also show a gain on the integral of the amount of fuel injected. At the iso heating temperature, here 564 ° C, the cumulative amount of fuel post injected is only 313 cg s / cp in fractional mode instead of 363 cg s / cp heating constant wealth, this which represents a gain of 15%.
Ainsi, comme l'illustre les précédentes courbes, il faut moins de temps que pour l'art antérieur pour atteindre une même consigne de température, tout en injectant moins de carburant dans la post injection. On réduit ainsi la dilution de gazole dans l'huile et la consommation de carburant du véhicule automobile.Thus, as illustrated by the previous curves, it takes less time than for the prior art to achieve the same temperature setpoint, while injecting less fuel into the post injection. This reduces the diesel fuel dilution and the fuel consumption of the motor vehicle.
On notera que le procédé de régénération qui vient d' être décrit peut s ' adapter sur n'importe quelle architecture de post traitement dotée d'un piège à oxyde d'azote, d'un filtre à particule, d'un injecteur additionnel, d'une sonde de température avant traitement et d'une sonde de température d' entrée du filtre à particules, d'une sonde à oxygène à la sortie du piège à oxyde d'azote, d'un capteur différentiel de pression au niveau du filtre à particule, et d'une unité de contrôle électronique pilotant ces éléments.
It will be noted that the regeneration method which has just been described can be adapted to any post-treatment architecture provided with a nitrogen oxide trap, a particle filter, an additional injector, of a pre-treatment temperature probe and an input temperature sensor of the particulate filter, an oxygen sensor at the outlet of the nitrogen oxide trap, a differential pressure sensor at the particle filter, and an electronic control unit driving these elements.
Claims
1. Procédé de régénération d'un système de post traitement de gaz d'une ligne d' échappement ( 1 ) d'un moteur à combustion interne (2) par élévation de la température du système de post traitement jusqu' à une température de régénération, caractérisé par le fait que lors de l' élévation de température on fait varier la richesse d'un mélange air/carburant en mettant en œuvre des phases successives d'injection de mélanges relativement riches et pauvres indépendamment de la consommation ou du renouvellement d'oxygène dans la ligne d' échappement.A method of regenerating a gas aftertreatment system of an exhaust line (1) of an internal combustion engine (2) by raising the temperature of the aftertreatment system to a temperature of regeneration, characterized in that during the rise in temperature the richness of an air / fuel mixture is varied by implementing successive phases of injection of relatively rich and poor mixtures independently of the consumption or the renewal of oxygen in the exhaust line.
2. Procédé selon la revendication 1 , caractérisée par le fait que durant un temps compris dans un intervalle de 0,5s à 2s, le mélange relativement riche reste établit, et le mélange relativement pauvre reste établit durant un temps compris dans le même intervalle de 0,5s à2. Method according to claim 1, characterized in that for a time in a range of 0.5s to 2s, the relatively rich mixture remains established, and the relatively poor mixture remains established for a time in the same range of 0.5s to
2s, jusqu' à ce que ladite température de régénération soit atteinte.2s, until said regeneration temperature is reached.
3. Procédé selon l'une quelconque des revendications 1 à 2, caractérisé par le fait que l' élévation de richesse du mélange se fait en injectant du carburant en amont du système de post traitement. 3. Method according to any one of claims 1 to 2, characterized in that the richness increase of the mixture is done by injecting fuel upstream of the post-treatment system.
4. Procédé selon l'une quelconque des revendications 1 à 2, caractérisé par le fait que l'élévation de richesse du mélange se fait par post-injection de carburant dans le moteur.4. Method according to any one of claims 1 to 2, characterized in that the richness of the mixture is achieved by post-injection of fuel into the engine.
5. Procédé selon l'une quelconque des revendication 1 à 4, caractérisé par le fait que sur un point de fonctionnement moteur stabilisé à 1200 rpm / 4 bars, on fractionne la richesse en créneaux de richesse λ = 1 ,01 (pauvre) et de richesse λ = 0,95 (riche) de durée 1 seconde.5. Method according to any one of claims 1 to 4, characterized in that on a motor operating point stabilized at 1200 rpm / 4 bar, is divided wealth wealth wealth λ = 1, 01 (poor) and of richness λ = 0.95 (rich) of duration 1 second.
6. Dispositif de régénération d'un système de post traitement de gaz d'une ligne d' échappement ( 1 ) d'un moteur à combustion interne (2) comprenant des moyens pour élever la température du système de post traitement jusqu' à une température de régénération, caractérisé par le fait qu'il comprend des moyens pour faire varier la richesse du mélange air/carburant et des moyens pour mettre en oeuvre des phases successives d'injection de mélanges relativement riche et pauvre indépendamment de la consommation ou du renouvellement d'oxygène dans la ligne d' échappement pour élever la température du système de post traitement jusqu' à la température de régénération.6. Regeneration device for a gas post-treatment system of an exhaust line (1) of an internal combustion engine (2) comprising means for raising the temperature of the post-treatment system to a regeneration temperature, characterized in that it comprises means for varying the richness of the air / fuel mixture and means for carrying out successive phases of injection of relatively rich and poor mixtures regardless of the consumption or renewal of oxygen in the exhaust line to raise the temperature of the post-treatment system up to the regeneration temperature.
7. Dispositif selon la revendication 6, caractérisé par le fait qu'il comprend un injecteur additionnel de carburant ( 10) placé à l' entrée du système de post traitement des gaz ( 1 ) destiné à augmenter la richesse du mélange air/carburant lors d'une phase de purge du système de post traitement.7. Device according to claim 6, characterized in that it comprises an additional fuel injector (10) placed at the inlet of the aftertreatment system (1) for increasing the richness of the air / fuel mixture during a purge phase of the post-processing system.
8. Dispositif selon les revendications 6 et 7, caractérisé par le fait qu'il comprend une sonde de température (6) placée entre le piège à oxyde d' azote (3) et le filtre à particule (4).8. Device according to claims 6 and 7, characterized in that it comprises a temperature probe (6) placed between the nitrogen oxide trap (3) and the particle filter (4).
9. Dispositif selon l'une quelconque des revendications 6 à 8, caractérisé par le fait qu'il comprend une sonde de température (5) à l' entrée du système de post traitement. 9. Device according to any one of claims 6 to 8, characterized in that it comprises a temperature sensor (5) at the entrance of the post-treatment system.
10. Dispositif selon l'une quelconque des revendications 6 à 9, caractérisé en ce qu'il comprend un système de mesure de la pression différentielle (9) au niveau du filtre à particules (4) destiné à contrôler l' état du filtre.10. Device according to any one of claims 6 to 9, characterized in that it comprises a system for measuring the differential pressure (9) at the particle filter (4) for controlling the state of the filter.
1 1. Dispositif selon l'une quelconque des revendications 6 à 10, caractérisé en ce qu'il comprend une sonde à oxygène (7) placée à la sortie du piège à oxyde d' azote (3).1 1. Device according to any one of claims 6 to 10, characterized in that it comprises an oxygen sensor (7) placed at the outlet of the nitrogen oxide trap (3).
12. Dispositif selon l'une quelconque des revendications 6 à 1 1 , caractérisé en ce qu'il comprend une sonde à oxygène ( 13) placée en amont du piège à oxyde d' azote (3). 12. Device according to any one of claims 6 to 1 1, characterized in that it comprises an oxygen sensor (13) placed upstream of the nitrogen oxide trap (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09742227A EP2286073A1 (en) | 2008-05-07 | 2009-04-01 | Method for regenerating a post-treatment system by splitting up the richness |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0853043 | 2008-05-07 | ||
FR0853043A FR2930968B1 (en) | 2008-05-07 | 2008-05-07 | METHOD FOR REGENERATING A POST PROCESSING SYSTEM BY FRACTIONING WEALTH |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2009136029A1 true WO2009136029A1 (en) | 2009-11-12 |
Family
ID=40083556
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2009/050559 WO2009136029A1 (en) | 2008-05-07 | 2009-04-01 | Method for regenerating a post-treatment system by splitting up the richness |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2286073A1 (en) |
FR (1) | FR2930968B1 (en) |
WO (1) | WO2009136029A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110017197A (en) * | 2018-01-04 | 2019-07-16 | 罗伯特·博世有限公司 | Method for running the internal combustion engine with catalyst converter |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2786529A1 (en) * | 1998-12-01 | 2000-06-02 | Toyota Motor Co Ltd | Control of exhaust gas emission for direct injection diesel engine by reactivating particle filter |
FR2804170A1 (en) * | 2000-01-20 | 2001-07-27 | Peugeot Citroen Automobiles Sa | Particle filter regeneration system for Diesel engine includes a control command, which can change the injected fuel amount between two values, for initiating or maintaining the catalysis |
EP1477652A2 (en) * | 2003-05-15 | 2004-11-17 | Nissan Motor Company, Limited | Exhaust emission control system of internal combustion engine |
DE102004019660A1 (en) * | 2003-04-22 | 2005-01-27 | Mitsubishi Jidosha Kogyo K.K. | Exhaust gas purification device for an internal combustion engine |
EP1544428A1 (en) * | 2002-08-26 | 2005-06-22 | Hitachi, Ltd. | Apparatus and method for clarifying exhaust gas of diesel engine |
EP1662101A1 (en) * | 2004-11-19 | 2006-05-31 | Mitsubishi Jidosha Kogyo Kabushiki Kaisha | Exhaust emission control device of internal combustion engine |
DE102005059815A1 (en) * | 2005-12-09 | 2007-06-14 | Hyundai Motor Co. | Method and apparatus for controlling the regeneration of a simultaneous NOx-PM reduction device |
-
2008
- 2008-05-07 FR FR0853043A patent/FR2930968B1/en not_active Expired - Fee Related
-
2009
- 2009-04-01 WO PCT/FR2009/050559 patent/WO2009136029A1/en active Application Filing
- 2009-04-01 EP EP09742227A patent/EP2286073A1/en not_active Withdrawn
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2786529A1 (en) * | 1998-12-01 | 2000-06-02 | Toyota Motor Co Ltd | Control of exhaust gas emission for direct injection diesel engine by reactivating particle filter |
FR2804170A1 (en) * | 2000-01-20 | 2001-07-27 | Peugeot Citroen Automobiles Sa | Particle filter regeneration system for Diesel engine includes a control command, which can change the injected fuel amount between two values, for initiating or maintaining the catalysis |
EP1544428A1 (en) * | 2002-08-26 | 2005-06-22 | Hitachi, Ltd. | Apparatus and method for clarifying exhaust gas of diesel engine |
DE102004019660A1 (en) * | 2003-04-22 | 2005-01-27 | Mitsubishi Jidosha Kogyo K.K. | Exhaust gas purification device for an internal combustion engine |
EP1477652A2 (en) * | 2003-05-15 | 2004-11-17 | Nissan Motor Company, Limited | Exhaust emission control system of internal combustion engine |
EP1662101A1 (en) * | 2004-11-19 | 2006-05-31 | Mitsubishi Jidosha Kogyo Kabushiki Kaisha | Exhaust emission control device of internal combustion engine |
DE102005059815A1 (en) * | 2005-12-09 | 2007-06-14 | Hyundai Motor Co. | Method and apparatus for controlling the regeneration of a simultaneous NOx-PM reduction device |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110017197A (en) * | 2018-01-04 | 2019-07-16 | 罗伯特·博世有限公司 | Method for running the internal combustion engine with catalyst converter |
Also Published As
Publication number | Publication date |
---|---|
FR2930968A1 (en) | 2009-11-13 |
FR2930968B1 (en) | 2014-10-24 |
EP2286073A1 (en) | 2011-02-23 |
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