专利摘要:
The method according to the invention manages the heating in a selective catalytic reduction system, SCR said, electrically heated and implanted in a vehicle with a combustion engine. According to the invention, the method comprises determining a heating power gain setpoint (G) from a plurality of variables, said plurality of variables including: - the temperature (TE) of the outside air , - the state of charge (SOC) of an electric vehicle battery, - the efficiency (EF) of the SCR system, and - the hygrometry (Hy) of the outside air.
公开号:FR3081506A1
申请号:FR1854357
申请日:2018-05-24
公开日:2019-11-29
发明作者:Fabien Denys;Thomas Le Tallec
申请人:PSA Automobiles SA;
IPC主号:
专利说明:

METHOD AND DEVICE FOR MANAGING HEAT IN AN ELECTRICALLY HEATED SCR SYSTEM [001] The invention relates generally to the reduction of polluting emissions of nitrogen oxides from a thermal engine vehicle equipped with a selective catalytic reduction system , says "SCR", electrically heated. More particularly, the invention relates to a method and a device for managing heating in an electrically heated SCR system installed in a vehicle with an internal combustion engine.
Vehicles with internal combustion engines are equipped with exhaust gas aftertreatment systems designed to reduce polluting emissions and comply with environmental standards. The reduction of nitrogen oxides (NOx) emissions is achieved by means of the SCR system, for "Selective Catalytic Reduction".
The conventional SCR system is dependent on the temperature of the exhaust gases which must be sufficient to effectively reduce NOx emissions. In certain vehicle life situations, such as when the engine is cold started and when driving at low speed in urban areas, this constraint on the temperature of the exhaust gases impacts the NOx reduction performance.
In order to overcome the above drawback, it is known to use an electrically heated SCR system. Such an SCR system allows optimum operating temperatures to be reached more quickly and thus allows increased efficiency in reducing NOx.
However, the electrical supply to the heating resistor included in the SCR system places significant demands on the vehicle's electrical supply network and induces significant energy consumption. Indeed, the electrical power required to supply the heating resistor can be of the order of a few hundred watts to more than 1 kW. The electrical supply to the heating resistor can disrupt the electrical supply network, causing voltage drops which can affect the supply of other electrical consumers. Furthermore, when the alternator of the on-board network is in an operating state preventing it from satisfying the electrical demand of the SCR system, the vehicle's energy storage means are stressed and undergo discharges. The repeated electrical demands of the SCR system lead to more charge / discharge phases of the energy storage means and affect the durability of the main vehicle battery which is generally of the conventional lead type.
By European patent EP2820263B1, it is known, in an electrically heated SCR system, to control the electrical supply of the heating element thereof with an activation / deactivation frequency which is determined as a function of an operating state of the SCR system, and this in order to avoid deposits liable to form on the heating element. The critical operating state in which deposits may appear is detected using one or more operating state quantities. The operating state quantity can be a temperature, an additive flow rate or an exhaust gas flow rate.
It is desirable to optimize the management of the heating in the electrically heated SCR system of a vehicle with an internal combustion engine, in order to minimize the energy consumption necessary and to obtain acceptable depollution performance under the different living conditions. of the vehicle.
According to a first aspect, the invention relates to a method for managing heating in a selective catalytic reduction system, electrically heated and installed in a vehicle with an internal combustion engine, comprising the determination of a heating power gain instruction. from a plurality of variables, said plurality of variables comprising:
the outside air temperature, the state of charge of a vehicle electric battery, the efficiency of the SCR system, and the humidity of the outside air.
According to a particular characteristic of the process, the heating power gain setpoint is determined by equality:
G = MIN [Gte, Gsoc, Gef, Ghy], in which G is the heating power gain setpoint and Gte, Gsoc, Gef, Ghy are intermediate heating power gain setpoints determined with maps from the plurality of variables.
According to another particular characteristic, the intermediate heating power gain setpoint Gte is determined from a first mapping as a function of said temperature (T E ) of the outside air.
According to yet another particular characteristic, the intermediate heating power gain setpoint Gsoc is determined from a second map as a function of the state of charge of the battery.
According to yet another particular characteristic, the intermediate heating power gain setpoint Gef is determined from a third map as a function of a temperature and an aging of the SCR system on which the efficiency of that depends -this.
According to yet another particular characteristic, the Ghy intermediate heating power gain setpoint is determined from a fourth map as a function of the humidity and the temperature of the outside air.
According to yet another particular characteristic, the intermediate heating power gain setpoint Ghy is obtained by adding a time increment to a first intermediate heating power gain setpoint value which is provided by the fourth map.
According to another aspect, the invention also relates to a device for managing heating in a selective catalytic reduction system, electrically heated and installed in a vehicle with an internal combustion engine. According to the invention, the device comprises an electronic control unit comprising a memory in which are stored program instructions for the implementation of the method as briefly described above.
The invention also relates to a selective catalytic reduction system, electrically heated and installed in a vehicle with an internal combustion engine, and a vehicle comprises such a selective catalytic reduction system.
Other advantages and characteristics of the present invention will appear more clearly on reading the detailed description below of several particular embodiments of the invention, with reference to the accompanying drawings, in which:
Fig.1 is a simplified diagram of an exhaust gas depollution system including an SCR system and a device according to the invention for the management of heating in the SCR system;
Fig.2 is a functional block diagram of the device according to the invention showing the control law applied in accordance with the method of the invention; and Figs. 3A to 3F show examples of curves of different sizes involved in the process of the invention, depending on the variables taken into account by it.
Referring to FIG. 1, the method according to the invention for managing the heating of the SCR system is implemented in an exhaust gas depollution system 1 shown here in a simplified manner.
The exhaust gas depollution system 1 is intended for the post-treatment of EG exhaust gases from a diesel-type heat engine in a vehicle.
As shown in Fig.1, the exhaust gas depollution system 1 here essentially comprises an oxidation catalyst 2, a compact device 3, electrically heated, selective catalytic reduction and filtering of soot particles and an ammonia conversion catalyst 4. These various functional depollution components are integrated into an LE gas exhaust line through which the EG exhaust gases flow. The NOx probes and the various other conventional sensors included in the LE gas exhaust line for controlling the exhaust gas depollution system 1 are not shown. An electronic control unit, referenced ECU, is also included in the exhaust gas depollution system 1 for the control thereof.
The oxidation catalyst 2 is typically a DOC type oxidation catalyst (for “Diesel Oxidation Catalyst” in English) incorporating a passive NOx accumulator, called PNA for Passive NOx Adsorber in English, which makes it possible to capture the NOx. The ammonia conversion catalyst 4, known as ASC for "Ammonia Slip Converter", has the function of reducing the amount of ammonia released by the LE exhaust system.
Depending on the applications, the compact device 3 may have different architectures. Two architectures 3a and 3b are shown diagrammatically in FIG. 1 by way of example.
The architectures 3a and 3b here both include, in their downstream part, a first bread 30 of the SCR type followed by a second bread 31 of the so-called “SDPF” type for “SCR on Diesel Particulate Filter” in English . The second bread 31 performs a double function of SCR catalyst and of particulate filter, by integrating an SCR catalytic layer, called "washcoat", in an impregnated form in a particle filter.
In their upstream part, the architectures 3a and 3b include the injector 31 which introduces an additive into the LE gas exhaust line for NOx reduction, such as an aqueous urea solution known under the brand AdBlue deposited. A mixing box 32, placed downstream of the injector 31, ensures the homogeneous mixing of the urea with the exhaust gases. In architecture 3a, an electrical heating resistor 33, placed before the injector 31, allows the heating of the exhaust gases upstream of it. In architecture 3a, another SCR 34 bread is provided, of the so-called “eSCR” type, which is placed between the mixing box 32 and the first SCR bread 30. The SCR 34 bread is an SCR catalyst incorporating a resistance electric heater.
The method according to the invention is implemented by means of a device 5 which manages the heating of the SCR system. It will be noted that the method and the device according to the invention are designed to operate in particular with the two types of architecture 3a and 3b described above.
The device 5 is typically implemented in the form of a software module which is resident in a memory ME of the electronic control unit ECU. Typically, the ECU is the engine control unit which is responsible for controlling the engine and its various functional components and accessories. The software module implementing the device 5 authorizes the implementation of the method according to the invention by the execution of program code instructions by a processor of the ECU unit.
As shown in FIG. 1, the device 5 manages the heating of the SCR system through a heating power gain instruction G and in association with an electrical supply unit 6. The electrical supply unit 6 is supplied by a supply voltage + V and supplies a variable electrical power P as output, which is determined by the heating power gain setpoint G. The electrical power supply unit 6 is, for example, of the switching type, with a switching cyclic ratio which is determined by the heating power gain setpoint G.
In this particular embodiment, the power supply unit 6 outputs the electrical power P, with P = G.Pmx, with Pmx being the maximum electrical power deliverable by the unit 6 and the setpoint of gain G varying between 0 and 1. The gain setpoint G adjusts the electrical power P supplied to the electrical heating resistance of the SCR system. The device 5 controls the heating of the SCR system as a function of the vehicle's living conditions, in order to reach the temperature required for the reduction of NOx, while satisfying the various constraints which apply to the vehicle and making best use of the electrical energy available.
The operation of the device 5 is now described in detail above with reference more particularly to Figs.2 and 3A to 3F.
The device 5 determines the setpoint for gaining heating power G by means of a control law which takes into account different variables representative of vehicle life conditions. The various variables taken into account notably include the outside temperature T E , the state of charge SOC of the electric battery of the vehicle, the efficiency EF of the SCR system and the outside hygrometry Hy.
According to the method of the invention, it is determined several intermediate setpoints for gaining heating power Gte, Gsoc, Gef, and Ghy from the variables T E , SOC, EF and Hy, using maps CATte, CATsoc, CATef and CAThy. The intermediate gain settings for heating power Gte, Gsoc, Gef, and Ghy each have a value which varies between 0 and 1. The MIN function [Gte, Gsoc, Gef, Ghy], represented in Fig. 2 by the block functional B1, is used to determine the heating power gain setpoint G as being equal to the intermediate heating power gain setpoint having the lowest value, namely, G = MIN [Gte, Gsoc, Gef, Ghy] .
CATte mapping is used to determine the intermediate gain setpoint Gte as a function of the outside temperature T E. By way of example, the curve in FIG. 3A shows the value assigned to the intermediate gain setpoint Gte as a function of the outside temperature T E. The intermediate gain setpoint Gte is here maximum, Gte = 1, for T e between -30 ° C and 40 ° C, and becomes zero, Ge = 0, for extreme temperatures T E s 50 ° C or T E < -40 ° C.
CATsoc mapping is used to determine the intermediate gain setpoint Gsoc according to the SOC state of charge, varying between 0% and 100%, of the vehicle's electric battery. The SOC state of charge of the battery must be managed in particular for safety reasons. A sufficient supply of electrical energy must remain available in the battery for the safety components of the vehicle. As an example, the curve in Fig. 3B shows the value assigned to the intermediate gain setpoint Gsoc as a function of the state of charge SOC. The intermediate gain setpoint Gsoc is here maximum, Gsoc = 1, for SOC> 70%, and becomes zero, Gsoc = 0, for SOC <50%.
CATef mapping is used to determine the intermediate gain setpoint Gef as a function of the efficiency EF of the SCR system. The temperature T S cr of the SCR bread and the aging AG of the SCR system are the inputs provided to the CATef mapping.
As the example of the curve in FIG. 3C shows, the efficiency EF of the SCR system is directly linked to the temperature T S cr thereof. With current SCR systems, the maximum efficiency (here EF = 95%) is generally obtained for a temperature T S cr of the order of 200 ° C. However, the EF efficiency of the SCR system depends on the aging of the SCR system. The CATef mapping makes it possible to simultaneously manage the temperature Tscr and the aging AG to determine the intermediate gain setpoint Gef. For example, the curve in Fig.3D shows, for a given aging, the value assigned to the intermediate gain setpoint Gef as a function of the temperature Tscr. The intermediate gain setpoint Gef is here maximum, Gef = 1, for Tscr 100 ° C, and becomes zero, (æf = 0, for Tscr S 200 ° C.
CAThy mapping is used to determine a first intermediate gain command Gany as a function of the hygrometry Hy and the outside temperature T E which are supplied as input.
In the method according to the invention, taking into account the humidity allows to manage the condensation of water in the LE exhaust line. This condensation of water can prove to be bothersome and even destructive for NOx probes, for example. The modulation of the heating power of the SCR system allows control of the condensation of water in the LE exhaust line. A Mollier diagram giving the quantity of water present in the outside air as a function of the outside temperature T E and the hygrometry Hy is typically used to carry out the CAThy mapping. It will be noted that this CAThy mapping will preferably be more precise than the CATte mapping in order to finely consider the variables T E and Hy in the temperature range from 10 ° C to 30 ° C.
For example, the curve in Fig.3E shows the value assigned to the first intermediate gain setpoint Gany as a function of the state of the outside temperature T E , for two hygrometry values Hy = 20 % and Hy = 80%. For Hy = 20%, the first intermediate gain setpoint Gany is here maximum, GaHY = 1, for T E s 30 ° C, and becomes zero,
GaHY = 0, for T E > 45 ° C. For Hy = 80%, the first intermediate gain command Gany is here maximum, GaHY = 1, for T E s 10 ° C, and becomes zero, GaiY = 0, for T E > 25 ° C.
The first intermediate gain command Gany provided by the CAT H mapping is then corrected with a time increment + IC, by means of the functional block B2, to obtain the intermediate gain command Ghy = Gany + IC. The time increment + IC is intended to gradually increase the value of the intermediate gain setpoint Ghy to a maximum value of 1, so as to take account of the evolution of water condensation with the operating time of the engine.
For example, the curve of Fig.3F shows the progressive increase, obtained by means of the time increment + IC, of the value of the intermediate gain setpoint Ghy, here starting from the points P20 and P80, at T E = 35 ° C, of the curves in FIG. 3E for the hygrometry values Hy = 20% and Hy = 80%, respectively. The maximum value of the intermediate gain setpoint Ghy is limited to 1.
The limitation to 1 of the maximum value of the intermediate gain setpoint Ghy is represented in FIG. 2 by the functional block B3 which receives as input the sum Gany + IC and the maximum value 1 and outputs the setpoint Ghy intermediate gain.
The functional block B4 receiving as input the heating power gain instruction G = MIN [Gte, Gsoc, Gef, Ghy] models the function performed by the power supply unit 6 which provides electrical heating power P = G. Pmx, with Pmx being the maximum electrical power deliverable by the unit 6.
In general, it will be noted that additional variables, not detailed here, may be taken into account by the device 5 in order to determine the heating power gain gain setpoint G. In addition, it will be noted that calibrations of inhibition can be added to the variables, so as to benefit from more flexibility in the control law determining the heating power gain setpoint G.
The invention is not limited to the particular embodiments which have been described here by way of example. A person skilled in the art, depending on the applications of the invention, can make various modifications and variants which fall within the scope of the appended claims.
权利要求:
Claims (10)
[1" id="c-fr-0001]
1. Method for managing heating in a selective catalytic reduction system (3), called SCR, electrically heated and installed in a vehicle with thermal engine, comprising the determination of a heating power gain setpoint (G) from a plurality of variables, said plurality of variables comprising:
the temperature (T E ) of the outside air, the state of charge (SOC) of an electric vehicle battery, the efficiency (EF) of the SCR system, and the hygrometry (Hy) of the outside air .
[2" id="c-fr-0002]
2. Method according to claim 1, characterized in that said heating power gain setpoint (G) is determined by equality:
G = MIN [Gte, Gsoc, Gef, Ghy], in which G is said heating power gain setpoint and Gte, Gsoc, Gef, Ghy are intermediate heating power gain setpoints determined with maps (CATte, CATsoc, CATef, CAThy) from said plurality of variables (TE, SOC, EF, Hy).
[3" id="c-fr-0003]
3. Method according to claim 1 or 2, characterized in that said intermediate heating power gain setpoint Gte is determined from a first map (CATte) as a function of said temperature (T E ) of the outside air .
[4" id="c-fr-0004]
4. Method according to any one of claims 1 to 3, characterized in that said intermediate heating power gain setpoint Gsoc is determined from a second map (CATsoc) as a function of said state of charge (SOC).
[5" id="c-fr-0005]
5. Method according to any one of claims 1 to 4, characterized in that said intermediate heating power gain setpoint Gef is determined from a third map (CATef) as a function of a temperature (T S cr ) and aging (AG) of the SCR system on which said efficiency (EF) depends.
[6" id="c-fr-0006]
6. Method according to any one of claims 1 to 5, characterized in that said intermediate heating power gain setpoint Ghy is determined from a fourth map (CAThy) as a function of said hygrometry (Hy) and said temperature (T E ) of the outside air.
[7" id="c-fr-0007]
7. Method according to claim 6, characterized in that said intermediate heating power gain setpoint Ghy is obtained by adding a time increment (+ IC) to a first value (G3hy) of intermediate heating power gain setpoint which is provided by said fourth mapping (CAThy).
[8" id="c-fr-0008]
8. Device for managing heating in a selective catalytic reduction system, electrically heated and installed in a vehicle with an internal combustion engine, characterized in that it comprises an electronic control unit (ECU) comprising a memory (MEM) in which are stored program instructions for implementing the method according to any one of claims 1 to 7.
[9" id="c-fr-0009]
9. Selective catalytic reduction system, electrically heated and installed in a vehicle with an internal combustion engine, characterized in that it comprises a heating management device (5) according to claim 8.
[10" id="c-fr-0010]
10. Vehicle comprising a selective catalytic reduction system according to claim 9.
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同族专利:
公开号 | 公开日
FR3081506B1|2020-04-24|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题
DE102011122413A1|2011-12-24|2013-06-27|Volkswagen Aktiengesellschaft|Method for operating ammonia storage system of selective catalytic reduction catalyzer of exhaust system of motor car, involves enabling operation of main storage for filling start storage and/or for ammonia supply of catalyzer|
WO2013127936A1|2012-03-02|2013-09-06|Emitec Gesellschaft Für Emissionstechnologie Mbh|Method for operating a heating catalyst|CN113513397A|2021-03-29|2021-10-19|广西玉柴机器股份有限公司|Method for controlling thermal management system based on environmental change and engine controller|
EP3904651A1|2020-04-29|2021-11-03|RENAULT s.a.s.|Method for managing the priming of a device for after-treatment of the exhaust gases of a motor vehicle|
法律状态:
2019-04-18| PLFP| Fee payment|Year of fee payment: 2 |
2019-11-29| PLSC| Search report ready|Effective date: 20191129 |
2020-04-22| PLFP| Fee payment|Year of fee payment: 3 |
2021-04-21| PLFP| Fee payment|Year of fee payment: 4 |
优先权:
申请号 | 申请日 | 专利标题
FR1854357|2018-05-24|
FR1854357A|FR3081506B1|2018-05-24|2018-05-24|METHOD AND DEVICE FOR MANAGING HEATING IN AN ELECTRICALLY HEATED SCR SYSTEM|FR1854357A| FR3081506B1|2018-05-24|2018-05-24|METHOD AND DEVICE FOR MANAGING HEATING IN AN ELECTRICALLY HEATED SCR SYSTEM|
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