• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A method of managing an SCR catalyst system of an internal combustion engine having an SCR catalyst (30) and an SCR coated particle filter (20) upstream thereof. In order to inject liquid reducing agent for the SCR catalyst (30) and / or the SCR-coated particle filter (20), a first injection position upstream of the SCR-coated particle filter (20) is provided. the shape of a first metering device (40) and a second injection position upstream of the SCR catalyst (30) and downstream of the SCR-coated particle filter (20) in the form of a second metering device (50); the injection positions for injecting liquid reducing agent are chosen according to the operating states of the SCR catalyst system.
    公开号:FR3043429A1
    申请号:FR1660728
    申请日:2016-11-07
    公开日:2017-05-12
    发明作者:Alexander Franz；Andreas Fritsch
    申请人:Robert Bosch GmbH；
    IPC主号:
    专利说明:

    Field of invention
    The present invention relates to a method for managing an SCR catalyst system of an internal combustion engine, the system comprising at least one SCR catalyst upstream thereof and at least one SCR coated particle filter. The subject of the invention is also an SCR catalyst system for implementing the method and a computer program on a memory medium that can be read by a machine and an electronic control device for carrying out the method. . State of the art
    Methods and devices for managing an internal combustion engine are known, in particular a motor fitted to a motor vehicle whose exhaust gas system is equipped with an SCR catalyst (that is to say a catalytic selective reduction catalyst) for reducing the nitrogen oxides (NOx) contained in the exhaust gas of the internal combustion engine with a reducing agent to obtain nitrogen. In order to carry out the reaction, ammonia (NH 3) or, for example, formic acid is used as the reducing agent. The reducing agent or a component giving this agent is added to the exhaust gas upstream of the catalyst in the direction of passage of the exhaust gas; this consists for example in injecting reagents releasing ammonia NH3, in particular an aqueous solution of urea. The ammonia released in the exhaust gas line reacts at an appropriate temperature with the troublesome nitrogen oxides from combustion in the catalyst. The amount of aqueous urea solution required generally depends on the charge applied to the internal combustion engine and is appropriately injected into the exhaust gas line.
    Currently known SCR catalysts store ammonia NH3 on the surface of the catalyst. The conversion of the NOx nitrogen oxides in the SCR catalyst is all the more successful as the supply of reducing agent in the catalyst is important. As long as the NH 3 ammonia storage capacity in the SCR catalyst is not exhausted, the reducing agent, dosed in excess, is stored. For NH3 ammonia accumulation, the NH3 ammonia fill level expression is used. If less reducing agent is supplied than necessary for the conversion of nitrogen oxides instantaneously present in the exhaust gas, accumulated reducing agent is consumed to ensure the conversion of the nitrogen oxides and thus reduces the NH3 ammonia filling level.
    The currently known dosing strategies for SCR systems have a fill level control which adjusts the operating point as a set value of the ammonia NH3 fill level in the SCR catalyst and is example a temperature-dependent filling level setpoint. The operating point is chosen so that the ammonia filling level NH3 is sufficiently high to guarantee both the conversion rate of NOx nitrogen oxides and also to provide a buffer for absorbing the short peaks of NOx. nitrogen oxides NOx. In addition, the filling level must be kept as close as possible to the maximum storage capacity to prevent NH3 ammonia slipping into the system.
    In order to achieve higher conversion rates for the reduction of nitrogen oxides in the exhaust gas duct, systems with two separate SCR catalyst plants are already being used. Feeding the SCR catalyst plants, one behind the other, usually provides a reducing agent injection position upstream of the first SCR catalyst plant according to the direction of passage of the exhaust gas. Part of the reducing agent thus supplied is not consumed by the catalysis reaction in the first SCR catalyst plant and is not stored therein so that this portion of reducing agent supplied leaves the first plant of SCR catalysts in the form of an NH3 ammonia slip. This "NH 3 ammonia slip" supplies the second SCR catalyst plant with a reducing agent so that there will be enough reducing agent for the second SCR catalyst plant; this is, for example, described in DE 10 2011 085 952 A1. Such systems equipped with two SCR installations are controlled for the conduct of the process, in the usual way, with a split program; the quantities used for conducting the process are taken for each SCR installation, on known models of catalysts. SCR catalyst modeling can be implemented in existing automotive control devices and this modeling addresses both the NOx NOx conversion of the SCR catalyst and NH3 ammonia slip. To improve the relatively complicated and fragile double modeling, the document DE 10 2012 221 905 A1 describes a method for managing an SCR catalyst system equipped with two SCR installations whose dependence on the overall degree of efficiency desired for the SCR system is determined. dosing of the reducing agent upstream of the first SCR catalyst based on a model-based pre-order.
    Document DE 10 2013 217 169 A1 describes an exhaust gas aftertreatment method and system according to which, in the direction of passage of the exhaust gas, the system comprises an oxidation catalyst, a first catalyst installation SCR and a second SCR catalyst installation. Directly upstream of the first SCR catalyst plant, an injector introduces the reducing agent. If necessary, it can also have one or more other injectors distributed in the exhaust pipe and each of them is for example between the first SCR catalyst installation and the second SCR catalyst installation. The document describes a method of managing this aftertreatment exhaust aftertreatment system, a multiple of the reducing agent dosage required instantly. DESCRIPTION AND ADVANTAGES OF THE INVENTION The subject of the invention is a method for managing an SCR catalyst system of an internal combustion engine, the system comprising at least one SCR catalyst and at least one SCR coated particle filter. upstream, the method being characterized in that to inject liquid reducing agent for the SCR catalyst and / or the SCR-coated particle filter, a first injection position is provided upstream of the SCR-coated particulate filter under the form of a first metering device and a second injection position upstream of the SCR catalyst and downstream of the SCR-coated particle filter in the form of a second metering device, the injection positions for injection of the liquid reducing agent being chosen according to the operating states of the SCR catalyst system.
    In other words, the process according to the invention is based on an SCR catalyst system of an internal combustion engine comprising at least one SCR catalyst and at least one SCR-coated particle filter, upstream. The condition for the application of the process of the invention for managing such an SCR catalyst system consists in injecting the reducing agent in the liquid state for the SCR catalyst and / or for the SCR-coated particle filter under the as a first injection upstream of the SCR-coated particle filter by a first metering device and a second metering plant upstream of the SCR catalyst and downstream of the SCR-coated particle filter in the form of a second dosing system. According to the heart of the invention, to inject the liquid reducing agent, the injection positions are chosen, that is to say the injection by the first metering device and / or by the second metering device according to the invention. the operating states of the SCR catalyst system. This method allows a particularly advantageous conduct of such an SCR catalyst system which allows an optimum post-treatment of the exhaust gas while minimizing the consumption of reducing agent. In principle, the process according to the invention is not limited to an SCR catalyst system comprising a SCR catalyst and an SCR-coated particle filter upstream. Moreover, the process according to the invention can be applied to other SCR catalyst systems. For example, the process can be applied to an SCR catalyst system which, in place of the SCR-coated particle filter, comprises a conventional particle filter and in addition a conventional SCR catalyst installed upstream. This system also comprises a particulate filter, customary, and both upstream and downstream of the particulate filter, each time a conventional SCR catalyst. In the sense of the description of the invention given below, the particulate filter with the SCR catalyst installed upstream is synonymous with SCR coated particle filter, and the process is suitably adapted. The description given below also makes it possible to replace the SCR-coated particle filter with a conventional particulate filter preceded by an SCR catalyst. The reducing agent is preferably an aqueous solution of urea, for example a solution known under the trademark AdBlue. Correspondingly, other reducing agents for selective reduction in SCR catalyst plants can also be used. Dosing facilities can be customary dosing valves. The use of two injection positions for metering the reducing agent for SCR catalyst installations makes it possible to optimally operate such an SCR catalyst system. According to a particularly preferred development of the process of the invention, in an operating state in which the temperature of the SCR-coated particle filter is greater than a predefined threshold, the liquid reducing agent is injected mainly by the second injection position. i.e. the second dosing installation. The expression "mainly" means that the injection is mostly in each case more than 50% and also up to 100% by the second dosing installation insofar as the dosing systems operate independently of one another. the other. If the system is designed to control only one or the other dosing system, this means that, according to the method, the injection is done exclusively by the second dosing system. This embodiment of the process of the invention is based on the fact that, starting from a certain temperature of the SCR-coated particle filter, part of the ammonia NH3 to be assayed is oxidized in the SCR-coated particle filter. without being used for the conversion of nitrogen oxides. Therefore, it is very advantageous from the point of view of reducing agent consumption to switch in such cases to the second dosing system.
    In the operating state mentioned, in which the temperature of the SCR-coated particle filter is greater than a predefined threshold, it may notably be an operating state corresponding to a regeneration of the SCR-coated particle filter. Temperatures during regeneration of the SCR-coated particulate filter can reach up to 1000 ° C. in the particle filter, for example, so that there will be no conversion of nitrogen oxides in the particulate filter. . The emissions of NOx nitrogen oxides downstream of the SCR-coated particle filter are therefore very high during the regeneration of the particulate filter. The injection according to the invention of reducing agent downstream of the SCR-coated particle filter can also sufficiently supply the SCR catalyst downstream with sufficient reducing agent, so that the reduction of the nitrogen oxides in the SCR catalyst will be sufficient.
    According to a preferential development, at the start of the internal combustion engine, in particular of a cold start, the injection of the reducing agent is mainly done, that is to say essentially by the first metering device and the injection Reducing agent is also exclusively done by the first dosing system. This results from the fact that the upstream catalyst, ie the SCR-coated particle filter, is closer to the internal combustion engine and thus arrives more quickly at its operating temperature. Thus, the conversion of nitrogen oxides NOx in direct phase after the start of the internal combustion engine is mainly in the first catalyst SCR, that is to say in the particle filter SCR coating, so that it is advantageous to inject upstream of this SCR-coated particle filter.
    In the normal operating mode of the internal combustion engine, at least one phase is preferably injected by the second metering device because the SCR-coated particle filter is charged more slowly with carbon black if there is no no conversion of NOx nitrogen oxides in the SCR-coated particle filter. This so-called "NO2 effect" effect in the SCR-coated particle filter produces oxidation of the carbon black in the particulate filter which is thus consumed. This NO2 effect depends particularly on the concentration of NO2 nitrogen oxides in the particulate filter. If there is no conversion of NOx nitrogen oxides in the particulate filter, the NO2 oxide concentration increases in the particulate filter and burns the carbon black. Preferably, in the phases of normal operation, if the exhaust gas composition permits, it is preferable to inject the reducing agent only downstream of the SCR-coated particle filter.
    The control of the dosing plants in the context of the process of the invention distinguishes mainly two cases which depend on the practical realization of each of the SCR catalyst systems. In the first case, the two metering plants are not activated simultaneously because they are fed for example by a common pump. In this case, only the first dosing system or only the second dosing system is controlled. In the second case, the two dosing plants can be operated independently of one another so that one or the other dosing system or the two dosing systems will be controlled simultaneously, if necessary in accordance with a different report. The first case is particularly economical because, compared to the usual systems, only one metering installation is provided to supply the two SCR catalyst plants; here it is only an additional metering device, that is to say an additional metering valve or an additional injector with a pipe, for example with a T-shaped part. the method of the invention, we can then provide a control program by which one injects into the two metering facilities. If both dosing systems are controlled simultaneously, there will be no switching between the two dosing systems and the control of the different dosing states will be done in parallel.
    The following description firstly relates to the case in which the two dosing systems are not activated simultaneously. It is thus necessary to switch between the two dosing installations. In principle, this allows two states. In the state "dosing valve 1", the dosing is done by the first dosing system. In the state "dosing valve 2", the dosing is done by the second dosing system. An appropriate control program of the method of the invention makes it possible to activate a state machine with both states. Preferably, at the beginning of a driving cycle, that is to say after the starting of the internal combustion engine, the state "metering valve 1" is activated. Switching to the state "metering valve 2" can be done if it is ensured that the second metering installation is not faulty and if in addition at least one of the following conditions is fulfilled: there is regeneration of the SCR-coated particle filter and the temperature in the SCR-coated particle filter is greater than a predefined threshold T1 and the temperature in the SCR catalyst is higher than a predefined threshold T2; the temperature in the SCRF-coated particle filter is greater than a predefined threshold T3 and the temperature in the SCR catalyst is greater than a predefined threshold T4; the ammonia feed NH3 of the catalyst SCR is below a predefined threshold mNH3_1 and the difference between the ammonia feed NH3 of the particulate filter SCRF with respect to the reference value is smaller in amplitude than a predefined threshold dmNH3_l and the temperature in the catalyst SCR is below a predefined threshold T5 and the mass flow of NOx nitrogen oxides is below a threshold dmNOx_l; - the first dosing system is considered defective.
    The thresholds Tl-T5 above are defined as follows:
    Threshold T1 relates to a safety request for the SCR-coated particle filter; it describes the temperature at which ammonia begins to oxidize. Depending on the respective data of the system, the temperature T1 may for example be less than about 350 ° C.
    The temperature T2 corresponds to a safety interrogation for the SCR catalyst and it describes the temperature below which the urea can not be stored and does not decompose completely to ammonia. Depending on the respective data of the system, the temperature T1 is for example about 180 ° C.
    The temperature T3 is a temperature threshold for the SCR coated particle filter in normal operating mode; if this threshold is exceeded, ammonia NH3 begins to oxidize. Preferably, the temperature T3 is less than or equal to the temperature T1. Depending on the respective data of the system, the temperature T3 is for example at about 350 ° C.
    The temperature T4 corresponds to a temperature threshold of the SCR catalyst in normal operating mode, a threshold below which the urea can not be stored and does not decompose completely into ammonia. Preferably, the temperature T4 corresponds to the value of the temperature T2. Depending on the respective data of the system, the temperature T4 is for example about 180 ° C.
    The temperature T5 describes an optimum temperature for the SCR catalyst making it possible to arrive at high conversion rates. The optimum temperatures in practice depend on the respective embodiments of the catalyst, especially from the point of view of catalyst coating and volume. The optimum temperature is for example at about 225 ° C.
    According to another advantageous characteristic, it is switched back to the first metering device if it is not defective and if at least one of the following conditions is met: there is no regeneration of the particulate filter with SCRF coating and the temperature in the SCR catalyst is below a predefined threshold T6, the temperature in the SCRF coated particle filter being between the predefined thresholds T7 and T8; the difference of the ammonia feed NH3 of the SCRF coated particle filter differs from the set point by an amplitude greater than a predefined threshold dmNH3_2 and the temperature in the SCRF coated particle filter is between the predefined thresholds T9 and T10; the second dosing installation is considered defective.
    The thresholds T6-T10 above are defined to some extent as follows:
    The threshold T6 corresponds to the temperature of the SCR catalyst from which it is possible to have conversion decreases because the SCR catalyst, especially in comparison with the SCR-coated particle filter, is too cold. Depending on the data of the catalyst system, the temperature is for example at about 250 ° C.
    Temperatures T7 and T8 refer to the temperature limits for the SCR-coated particle filter between which good NOx conversion can be expected without oxidizing excess ammonia. Depending on the system data, the temperature T7 is for example about 180 ° C and T8 is for example about 350 ° C.
    Temperatures T9 and T10 are the temperature limits for the SCR-coated particle filter between which we will have a good conversion of NOx nitrogen oxides without oxidizing too much ammonia. The temperatures T9 and T10 may differ slightly from the temperatures T7 and T8 to optimize the switching sensitivity between the states "metering valve 1" and "metering valve 2" to avoid a switchover between these states. Depending on the data of the system, the temperature T9 will for example be of the order of 180 ° C and the temperature T10 will for example be of the order of 325 ° C.
    The temperature thresholds, the NH 3 ammonia feedstock and the mass flow rates are preferably adjusted according to operating parameters and / or the state and data of the SCR catalyst and / or the SCR-coated particle filter and are thus adapted to the practical realization of each system.
    The dmNH3_l and dmNH3_2 thresholds may be in particular in the form of characteristic curves depending on the respective temperature of the catalyst. Preferably, the threshold mNH3_1 depends in particular on the age of the catalyst. In a particularly advantageous manner, the different thresholds may, if necessary, depend on the temperature of the exhaust gas, the mass flow rates of nitrogen oxides NOx and the exhaust gas, the NO2 ratio, the state aging, fouling by black smoke and black-smoke charge and / or hydrocarbon catalyst installations. This is done for example using a field of characteristics to one or more dimensions.
    A particular advantage of the process is that for the SCR catalyst system with dosing systems, in case of failure of one of the two dosing plants, in case of failure of one of the dosing plants, the other plant of The dosage can inject the reducing agent, if necessary to completely ensure this injection, so that the exhaust gas post-treatment process will be guaranteed in the SCR catalysts.
    Preferably, the switching conditions mentioned above are unblocked with respect to each other.
    According to a preferred development of the method of the invention, after switching between the dosing plants, it is possible to block any other switching for a predefined duration T1. The predefined duration is for example in a range of a few seconds, for example this duration is between 5-20 s, for example this range corresponds to 10 s. This has the advantage that the blockage over time allows the hydraulic system to stabilize by damping.
    If the injection of the reducing agent is done by the first dosing system, the control of the system is preferably in the form of a model-based pre-control, in particular the nominal filling level of the particulate filters. The SCR coating reacts with the NH 3 ammonia feed of the SCR catalyst, in a manner comparable to the process known from DE 10 2012 221 905 A1. This can also be done if the injection is only preferentially and not completely by the first dosing system. If the injection is done completely or at least in large part by the second dosing system, the control functions can be split into the control program, especially from the point of view of the pre-control and the fill level controller. In this case, as in a conventional SCR system, the injection will be regulated according to the set filling level and the filling state regulator.
    According to a development of the SCR catalyst system in which the two dosing systems are controlled independently of one another and which can also be controlled simultaneously, there is no switching between the two dosing systems. In this embodiment of the catalyst system, the controls of the two states, that is to say for an injection by the first metering installation and for an injection by the second metering installation, can be done in parallel. The invention also relates to a catalyst system of an internal combustion engine, the system comprising at least one SCR catalyst and at least one SCR coated particle filter installed upstream. In order to inject liquid reducing agent for the SCR catalyst and / or for the SCR-coated particle filter, a first metering device is provided upstream of the SCR-coated particle filter and a second metering device upstream of the SCR-coated particle filter. SCR catalyst but downstream of the SCR coated particle filter, that is to say that this second installation is between the SCR coated particle filter and SCR catalyst. According to the invention, this SCR catalyst system is designed to perform the method described above.
    The SCR coated particle filter may be preceded by an oxidation catalyst. The SCR catalyst may be followed by a cleaning catalyst. The two dosing systems can be controlled independently of one another, or activated simultaneously because they are fed by a common pump providing the reducing agent. With regard to the characteristics of the SCR catalyst system, reference will be made to the description given above. The invention also relates to a computer program for implementing the steps of the method of the invention. The invention also relates to a machine readable memory medium on which is recorded the computer program and an electronic control device for carrying out the steps of the described method. Embodiment of the method of the invention in the form of a computer program or a machine-readable memory medium or an electronic control device has the particular advantage that the method of the invention It can thus be used by vehicles already manufactured which are equipped with an SCR catalyst system comprising two SCR catalyst installations and two dosing plants for the required reducing agent. This makes it possible to design existing vehicles for the process according to the invention and thus to use the advantages of the process.
    Description of embodiments
    The single figure shows schematically an embodiment of a catalyst system for implementing the method of the invention. The figure shows the exhaust gas ducting of a non-detailed internal combustion engine; this pipe is traversed by the exhaust gas in the direction of the arrow. The exhaust gas aftertreatment system comprises a Diesel DOC oxidation catalyst 10, followed by an SCR-coated particle filter (SCRF) 20. Then, downstream, there is an SCR catalyst (SCR) 30, itself followed by a cleaning catalyst CUC (not shown). Between the Diesel Oxidation Catalyst 10 and the SCR Coated Particulate Filter 20, there is a first metering device 40 for metering a liquid reducing agent solution. This metering device 40 is thus upstream of the SCRF particle filter 20. Downstream of the SCRF particle filter 20 and at the same time upstream of the SCR catalyst 30, there is a second metering device 50 for dosing the liquid solution. reducing agent. The metering devices 40 and 50 are customary dosing valves or injectors. The dosing installations 40 and 50 make it possible to introduce a solution of liquid reducing agent, for example an aqueous solution of urea (for example known under the trademark AdBlue) or a comparable reducing agent. Various sensors, in particular for NOx, NH3 components and temperatures, are provided. These sensors, not shown, provide signals for controlling the exhaust gas post-treatment process.
    The implementation of the method of the invention is not limited to such an installation. In principle, the invention can also be applied to other exhaust gas aftertreatment systems insofar as they comprise at least two SCR catalyst installations (for example the SCRF 20 and SCR 30 catalysts) as well as two metering plants for the necessary reducing agent, the first metering installation being upstream of the first SCR catalyst installation (for example the SCRF 20 installation) and the second metering installation being between the first SCR catalyst installation ( for example SCRF 20) and the second catalyst plant (for example SCR 30). The system is designed so that the two metering devices 40 can operate independently of one another or in the case of a more economical system, not to be operated simultaneously for example by being fed by a common pump.
    The operation according to the invention, of such a catalyst system SCR, can use a control program, for example a controller, with two states. In the state "metering valve 1", the dosage of the reducing agent is done with the first metering device 40 and in the state "metering valve 2", the dosage of the reducing agent is done by the second metering installation 50. At the beginning of a driving cycle, the state "metering valve 1" will be activated. It will switch to the state "metering valve 2" if the metering installation 50 is not defective and if in addition, one of the following conditions is met: it is in regeneration of the SCRF particle filter 20 and the The temperature in the SCRF filter 20 exceeds a threshold T1 and the temperature in the SCR filter 30 exceeds a threshold T2, the temperature in the SCRF coated particle filter 20 is greater than a threshold T3 and the temperature in the SCR catalyst 30 is greater at a threshold T4, the ammonia feed NH3 of the catalyst SCR 30 is lower than a threshold mNH3_1 and the difference of the charge of the particulate filter SCRF 20 with respect to a threshold is smaller in amplitude than a threshold dmNH3_l. The temperature in the catalyst SCR 30 exceeds a threshold T5 and the mass flow rate of nitrogen oxides NOx is below a threshold dmNOx_1, the metering device 40 is considered to be defective.
    There will be a feedback on the state "metering valve 2" if the metering system 40 is not defective and in addition, if one of the following conditions is met: the SCRF coated particle filter Is not in regeneration and the temperature in the SCR catalyst 30 is below a T6 threshold; the temperature in the SCRF particle filter 20 is between the thresholds T7 and T8, the difference of the ammonia feed NH3 of the SCRF particulate filter 20 with respect to a target charge is greater in amplitude at dmNH3_2 and the temperature in the SCRF filter 20 is between the thresholds T9 and T10.
    Preferably, all these switching conditions are without interference in time. In addition, it is advantageous, after a switching operation, to block other switching requests during a predetermined period T1 to allow the hydraulic system to be amortized.
    NOMENCLATURE OF MAIN ELEMENTS
    10 DOC Diesel Oxidation Catalyst
    20 SCR coated particle filter, SCRF filter
    30 SCR Catalyst 40 Dosing system 50 Dosing system
    权利要求:
    Claims (13)
    [1" id="c-fr-0001]
    1) Method for managing an SCR catalyst system of an internal combustion engine the SCR catalyst system comprising at least one SCR catalyst (30) and at least one SCR coated particle filter (20) upstream thereof, characterized in that for injecting liquid reducing agent for the SCR catalyst (30) and / or the SCR-coated particle filter (20), a first injection position is provided upstream of the SCR-coated particle filter (20) in the form of a first metering device (40) and a second injection position upstream of the SCR catalyst (30) and downstream of the SCR-coated particle filter (20) in the form of a second metering device (50), the injection positions for injecting liquid reducing agent are selected according to operating states of the SCR catalyst system.
    [0002]
    2) Method according to claim 1, characterized in that the SCR catalyst system comprises, in place of the SCR-coated particle filter (20), a particulate filter with a SCR catalyst installed upstream thereof.
    [0003]
    Method according to Claim 1 or Claim 2, characterized in that in a second state of operation in which the temperature of the SCR-coated particle filter (20) is greater than a predefined threshold, the agent is injected liquid reducer, mainly by the second metering device (50).
    [0004]
    Method according to one of Claims 1 to 3, characterized in that in an operating state in which the SCR-coated particulate filter (20) is regenerated, liquid reducing agent is essentially injected into the using the second dosing system (50).
    [0005]
    Process according to one of Claims 1 to 4, characterized in that at the start of the internal combustion engine, in particular in the case of cold start, the liquid reducing agent is injected essentially with the aid of the first dosing system (40).
    [0006]
    Process according to one of Claims 1 to 5, characterized in that, in the normal operating mode, at least one liquid reducing agent is injected per phase, preferably via the second dosing device (50).
    [0007]
    Process according to one of Claims 1 to 6, characterized in that, at the start of the internal combustion engine, an injection is made by the first dosing system (40) and the second dosing system ( 50) if the second metering device (50) is not defective and at least one of the following conditions is fulfilled: the SCR-coated particle filter (20) is regenerated and its temperature is greater than one predefined threshold T1 and the temperature in the catalyst SCR (30) is greater than a predefined threshold T2; the temperature in the SCRF-coated particle filter (20) is greater than a predefined threshold T3 and the temperature in the SCR catalyst (30) is greater than a predefined threshold T4; the NH 3 ammonia feedstock of the SCR catalyst (30) is less than a predefined threshold mNH3_1 and the difference between the ammonia feed NH3 of the SCRF particulate filter (20) with respect to the setpoint value is smaller in amplitude than a predefined threshold dmNH3_l and the temperature in the SCR catalyst (30) is below a predefined threshold T5 and the mass flow rate of nitrogen oxides NOx is below a threshold dmNOx_l; - The first metering device (40) is considered defective.
    [0008]
    Process according to Claim 7, characterized in that the first dosing system (40) is switched back to the first dosing device (40) if it is not defective and at least one of the conditions is met. The following is fulfilled: there is no regeneration of the SCRF-coated particle filter (20), the temperature in the SCR catalyst (30) is below a predefined threshold T6 and the temperature in the SCRF-coated particle filter (20) lies between the predefined thresholds T7 and T8; the difference of the ammonia feed NH3 of the SCRF coated particle filter (20) differs from the set point by an amplitude greater than a predefined threshold dmNH3_2 and the temperature in the SCRF coated particle filter (20) is included between the predefined thresholds T9 and T10; the second metering device (50) is considered defective.
    [0009]
    Method according to Claim 7 or Claim 8, characterized in that, after switching between the metering devices (40, 50), any subsequent switching is blocked for a predetermined period T1.
    [0010]
    Method according to one of Claims 1 to 9, characterized in that for injection by the first dosing system (40), the SCR catalyst system is controlled by a model-based pre-control.
    [0011]
    11 °) SCR catalyst system for an internal combustion engine comprising at least one SCR catalyst (30) and at least one SCR-coated particle filter (20) upstream, characterized in that to inject the reducing agent for the SCR catalyst (30) and / or the SCR-coated particle filter (20), it comprises a first metering device (40) upstream of the SCR-coated particle filter (20) and a second dosing (50) upstream of the SCR catalyst (30) and downstream of the SCR-coated particle filter (20), the SCR catalyst system being designed to perform a method according to one of claims 1 to 9.
    [0012]
    12 °) SCR catalyst system according to claim 11, characterized in that in place of the SCR-coated particle filter (20), it comprises a particle filter with upstream thereof, a catalyst SCR.
    [0013]
    13) A computer program adapted to perform the steps of a method according to one of claims 1 to 10 and a machine-readable memory medium comprising such a computer program as well as an electronic control device for executing the process steps according to one of claims 1 to 10.
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    同族专利:
    公开号 | 公开日
    US10145286B2|2018-12-04|
    US20170130628A1|2017-05-11|
    FR3043429B1|2021-09-17|
    DE102015221982A1|2017-05-24|
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    法律状态:
    2017-11-24| PLFP| Fee payment|Year of fee payment: 2 |
    2019-01-25| PLSC| Publication of the preliminary search report|Effective date: 20190125 |
    2019-11-21| PLFP| Fee payment|Year of fee payment: 4 |
    2020-11-19| PLFP| Fee payment|Year of fee payment: 5 |
    2021-11-19| PLFP| Fee payment|Year of fee payment: 6 |
    优先权:
    申请号 | 申请日 | 专利标题
    DE102015221982.8A|DE102015221982A1|2015-11-09|2015-11-09|Method for operating an SCR catalytic converter system of an internal combustion engine|
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