• 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:
    SUMMARY The invention relates to a method in SCR systems for exhaust gas purification, comprising the steps of determining a need to, after switching off a medium and the step of predicting a temperature course of exhaust gas flow, cool a dosing unit for reducing agent reducing agent, at least a part of said SCR system as a basis for determining the said needs. The invention also relates to a computer program product comprising program code (P) for a computer (200; 210) for implementing a method according to the invention. The invention also relates to a device and a motor vehicle equipped with the device. Figure 2 for publication
    公开号:SE1050642A1
    申请号:SE1050642
    申请日:2010-06-21
    公开日:2011-12-22
    发明作者:Andreas Liljestrand；Per Bremberg；Ulf Carlsson；Lars Eriksson；Erik Gustafsson
    申请人:Scania Cv Ab；
    IPC主号:
    专利说明:

    the container via the pump and the dosing unit back to the container. In this way an active cooling of the dosing unit is provided. The return flow from the dosing valve to the container can be substantially constant and is currently not controlled or regulated by means of valves or similar units intended for the purpose.
    Since the dosing unit is currently arranged at the exhaust system of the vehicle, which exhaust system during operation of the vehicle is heated depending on e.g. load, the dosing unit risks overheating. Overheating of the dosing unit may result in degradation of the same consideration functionality, which may result in a degraded performance thereof.
    The dosing unit today comprises electrical components, some of which include a circuit board. Said circuit boards can e.g. be arranged to control the dosing of AdBlue to the exhaust system of the vehicle. These electrical components are sensitive to high temperatures for several reasons. Excessive temperatures of the dosing unit can result in degradation of the electrical components, which can lead to costly repairs at a service workshop. Furthermore, the reductant present in the dosage unit can at least partially crystallize at too high temperatures, which can lead to clogging of the dosage unit. It is therefore of the utmost importance that the temperature of the dosing unit of the SCR system does not exceed a critical temperature.
    Cooling of the dosing unit of an SCR system in vehicles today takes place continuously during ordinary operation of the vehicle as the reductant is circulated within the SCR system manner. on the above Cooling of the dosing unit during operation of the vehicle today works satisfactorily.
    After operation of the vehicle, there is a stored amount of thermal energy in mainly the exhaust system caused by said operation. This thermal energy can be led to the dosing unit from e.g. a muffler and the SCR catalyst for the dosing unit, which can be heated to a temperature exceeding a critical value thereof.
    When the vehicle is switched off and thus after the exhaust gas flow in the exhaust system is switched off, the dosing unit for the reductant is currently cooled by means of said reductant in the same way as during ordinary operation for a predetermined time, such as e.g. 30 minutes.
    This action is associated with certain disadvantages. As an example, a relatively large amount of energy is required to drive the pump in the SCR system after switching off the vehicle. In the event that a vehicle battery drives the pump of the SCR system, this may be discharged or reach an undesirably low degree of discharge.
    Another disadvantage of cooling the dosing unit in the same way as during ordinary operation is that the pump of the SCR system generates disturbing noise, which e.g. a driver of the vehicle may find it annoying, especially in the event that the driver is to sleep in the cab after a driving session, or where the driver is in the immediate vicinity of the vehicle.
    Thus, there is a need to improve the current cooling process of the dosing unit in the SCR system after the vehicle has been switched off in order to reduce or eliminate the above-mentioned disadvantages.
    SUMMARY OF THE INVENTION An object of the present invention is to provide a new and advantageous method for improving the performance of an SCR system.
    Another object of the invention is to provide a new and advantageous device and a new and advantageous computer program for improving the performance of an SCR system.
    An object of the present invention is to provide a new and advantageous method for effecting cooling of a dosing unit of an SCR system after shutting off an exhaust gas flow therein.
    Another object of the invention is to provide a new and advantageous device and a new and advantageous computer program for effecting cooling of a dosing unit of an SCR system after switching off an exhaust gas flow in the SCR system.
    A further object of the invention is to provide a method, an apparatus and a computer program for reducing the risk of a dosing unit in an SCR system overheating after shutting off an exhaust gas flow in the SCR system.
    A further object of the invention is to provide an alternative method, an alternative device and an alternative computer program for reducing the risk of a dosing unit in an SCR system overheating after shutting off an exhaust gas flow in the SCR system.
    These objects are achieved with a method for in SCR systems for exhaust gas purification according to claim 1.
    According to one aspect of the invention, there is provided a method of SCR exhaust gas purification system, comprising the steps of: - determining a need to, after shutting off an exhaust stream, cooling a reducing agent metering unit by reducing agent, and - predicting a temperature course of at least a portion in said SCR systems as a basis for determining said needs.
    By providing a calculation model which is arranged to calculate a future maximum temperature of the dosing unit which will be achieved, given stored energy of different parts of the SCR system at the shut-off of the exhaust gas flow, a reduced influence of the SCR system can be achieved.
    The calculation model is arranged to sample temperatures of different parts of the SCR system in the immediate time before and / or after switching off the exhaust gas flow and can on this basis predict whether the dosing unit will reach temperatures that are too high, at which temperatures the dosing unit could be damaged. In the event that it is determined that an excessively high temperature of the dosage unit is likely to be reached, cooling by means can be maintained at any suitable level. In the event that it is determined that an excessive dosing unit for reducing agent reducing agent high temperature of the dosing unit with high probability will not be reached, cooling of the reducing agent dosing unit by means of reducing agent can be switched off automatically. In this case, the number of occasions which involves continued cooling of the dosing unit for reducing agent by means of reducing agent when switching off the exhaust gas flow can be reduced, which is advantageous from several aspects. For example. unnecessary use of electrical energy to drive a supply device for said reducing agent in the SCR system is avoided.
    The method may further comprise the step of predicting whether a predetermined temperature of the dosing unit will be reached after said shut-off of exhaust gas flow. By predicting a temperature course of the dosing unit, operation of the reducing device supply device in the SCR system can be controlled in an optimal way, taking into account the use of electrical energy. By predicting a temperature course of the dosing unit, and automatically determining whether continued operation of the feeding device should cease, unnecessary cooling of the dosing unit can be avoided.
    Said predetermined temperature may be a functionally critical temperature for the dosing unit. Said function-critical temperature is a temperature at which e.g. electronic components of the dosing unit may be damaged to the extent that its functionality is degraded or eliminated. By setting said predetermined temperature to a suitable value, a robust method is provided to reduce the risk of a dosing unit in an SCR system overheating after switching off an exhaust flow in the SCR system.
    Said at least a portion of said SCR systems may include any of an SCR catalyst, a muffler, the dosage unit or the reducing agent. In particular, it is advantageous to predict a temperature course of the dosing unit. In cases where a temperature course is predicted for other components of the SCR system, such as e.g. The predicted temperature profile of the dosing unit can be modeled on the SCR catalyst or silencer on the basis thereof. Said prediction of the temperature course of said at least a part of said SCR system thus enables indirect determination of a future temperature of the dosing unit. In particular, an indirect determination of a future maximum temperature of the dosing unit is made possible. Said prediction of the temperature course may include consideration of reheating effects of at least a part of the SCR system. Depending on how the SCR system has been operated, different amounts of thermal energy may be stored in different parts of the SCR system. This thermal energy can be led to the dosing unit even after switching off the exhaust gas flow. According to one aspect of the invention, reheating effects are taken into account when modeling a temperature course of the dosing unit.
    The method may further comprise the step of predicting said temperature course of at least a part of said SCR system by means of a calculation model predetermined. The parameter configuration may be an arbitrary parameter configuration, including a parameter configuration. including e.g. a prevailing temperature of the SCR catalyst and / or a prevailing temperature of the muffler and / or a prevailing temperature of the reducing agent or dosage unit.
    The step of determining said need may be performed before said shutdown of exhaust flow, or the step of determining said need may be performed after said shutdown of exhaust flow. By determining said need before shutting off the exhaust flow, a decision to interrupt cooling of the dosing unit can be made earlier than if the step of determining said need is performed after said shutting off of exhaust flow. By determining the said need after shutting off the exhaust flow, a decision to interrupt cooling of the dosing unit can be made on the basis of a more updated basis compared to if said need is determined before shutting off the exhaust flow.
    Said reducing agent may be a fluid solution comprising urea.
    The procedure is easy to implement in existing motor vehicles. Software in an SCR system for exhaust gas purification according to the invention can be installed in a control unit of the vehicle in the manufacture thereof. A buyer of the vehicle can thus be given the opportunity to choose the function of the procedure as an option.
    Alternatively, software including program code for performing the innovative procedure of an SCR exhaust purification system may be installed in a control unit of the vehicle when upgrading at a service station. In this case, the software can be loaded into a memory in the control unit. Implementation of the innovative procedure is thus cost-effective, especially since no additional components or subsystems need to be installed in the vehicle. The required hardware is already present in the vehicle today. The invention thus provides a cost-effective solution to the above problems.
    Software comprising program code for determining a need to, after shutting off an exhaust flow, cool a dosing unit for reducing agent by means of reducing agent, and predict a temperature course of at least a part of said SCR system as a basis for determining said need, according to one aspect of the invention, can be easily updated or replaced. Furthermore, different parts of the software that include program code to perform the innovative procedure can be replaced independently. This modular configuration is advantageous from a maintenance perspective.
    According to one aspect of the invention, there is provided an apparatus including an SCR system for exhaust gas purification. The device comprises means for determining a need to, after switching off an exhaust gas flow, cool a dosing unit for reducing agent by means of reducing agent, and means for predicting a temperature course of at least a part of said SCR system as a basis for determining said need.
    The device may further comprise means for predicting whether a predetermined temperature of the dosing unit will be reached after said shut-off of exhaust gas flow. Said predetermined temperature may be a functionally critical temperature for the dosing unit.
    Said at least a portion of said SCR systems may include any of an SCR catalyst, a muffler, the dosage unit or the reducing agent.
    Said prediction of temperature course of said at least a part of said SCR system can enable indirect determination of a future temperature of the dosing unit.
    Said prediction of the temperature course may include consideration of reheating effects of at least a part of the SCR system.
    The device may further comprise means for predicting said temperature course of at least a part of said SCR system by means of a calculation model including a predetermined parameter configuration.
    The means for determining said need may be arranged to determine said need before said shutdown of exhaust flow, or where the means for determining said need are arranged to determine said need after said shutdown of exhaust flow.
    The above objects are also achieved with a motor vehicle incorporating the features of the device including an SCR system. The motor vehicle can be a truck, bus or car.
    An advantage of the present invention is that the time as a control unit of the vehicle does not have to be activated as often or as long as before to monitor and control the supply device for the reducing agent.
    According to one aspect of the invention, there is provided an arbitrary platform which includes a device with an SCR system, such as e.g. a watercraft.
    The watercraft can be of any kind, such as e.g. a motorboat, a ship, a ferry or a ship.
    According to one aspect of the invention, there is provided a computer program in an SCR system for exhaust gas purification, said computer program comprising program code stored on a computer readable medium for causing an electronic control unit or another computer connected to the electronic control unit to perform the steps of any of claims 1-9.
    According to one aspect of the invention, there is provided a computer program product comprising a program code stored on a computer readable medium for performing the method steps of any of claims 1-9, when said computer program is run on an electronic control unit or another computer connected to the electronic control unit. . Advantages of the invention will become apparent to those skilled in the art from the following details, as well as additional objects, and novel features of the present invention through the practice of the invention. While the invention is described below, it should be understood that the invention is not limited to the specific details described. Those skilled in the art having access to the teachings herein will recognize additional applications, modifications, and incorporations within other fields which are within the scope of the invention. SUMMARY DESCRIPTION OF THE DRAWINGS For a more complete understanding of the present invention and further objects and advantages thereof, reference is now made to the following detailed description which is to be read in conjunction with the accompanying drawings in which like reference numerals refer to like parts in the various figures, and in which: 1 schematically illustrates a vehicle, according to an embodiment of the invention; Figure 2 schematically illustrates a subsystem of the vehicle shown in Figure 1, according to an embodiment of the invention; Figure 3 schematically illustrates a subsystem of the vehicle shown in Figure 1, according to an embodiment of the invention; Figure 4a schematically illustrates a flow chart of a method, according to an embodiment of the invention; Figure 4b schematically illustrates in further detail a flow chart of a method, according to an embodiment of the invention; and Figure 5 schematically illustrates a computer, according to an embodiment of the invention.
    DETAILED DESCRIPTION OF THE FIGURES Referring to Figure 1, a side view of a vehicle 100 is shown. The exemplary vehicle 100 consists of a tractor 110 and a trailer 112.
    The vehicle can be a heavy vehicle, such as a truck or a bus. The vehicle can alternatively be a car. It should be noted that the invention is suitable for application to any SCR system and is not sold limited to SCR systems of motor vehicles. The innovative method and the innovative device according to an aspect of the invention are well suited for platforms which include an SCR system other than motor vehicles, such as e.g. watercraft.
    The watercraft can be of any kind, such as e.g. motorboats, ships, ferries or ships.
    The innovative method and the innovative device according to an aspect of the invention are also well suited for e.g. systems including industrial motors and / or motor-driven industrial robots and / or a stationary motor.
    The innovative method and the innovative device according to an aspect of the invention are also well suited for different types of power plants, such as e.g. an electric power plant comprising a diesel generator.
    The innovative method and the innovative device are well suited for an arbitrary motor system which includes a motor and an SCR system, such as e.g. at a locomotive or other platform.
    The innovative method and device are well suited for an arbitrary system that includes a NOX generator and an SCR system.
    Here, the term "link" refers to a communication link which may be a physical line, such as an optoelectronic communication line, or a non-physical line, such as a wireless connection, for example a radio or microwave link.
    Here, the term "lead" refers to a passage for holding and transporting a fl uid, such as e.g. a reductant in liquid form. The conduit can be a tube of 12 arbitrary dimensions. The conduit may consist of any suitable material, such as e.g. plastic, rubber or metal.
    Here, the terms "reductant" or "reducing agent" refer to an agent used to react with certain emissions in an SCR system. These "reductant" "reducing agents" are used synonymously herein. Said reductant is according to an emissions can e.g. be NOx gas. The terms and execution so-called AdBlue. Of course, other types of reductants can be used.
    Here, AdBlue is mentioned as an example of a reductant, but a person skilled in the art realizes that the innovative method and the innovative device can be realized for other types of reductants, with necessary adaptations, such as e.g. adjustments to the adequate freezing point for selected reductants, in control algorithms for executing software code in accordance with the innovative procedure.
    Referring to Figure 2, a subsystem 299 of the vehicle 100 is shown.
    The subsystem 299 is arranged in the tractor 110. The subsystem 299 may form part of an SCR system. According to this example, the subsystem 299 consists of a container 205 which is arranged to hold a reductant. The container 205 is arranged to contain a suitable amount of reductant and is further arranged to be able to be refilled if necessary. The container can hold e.g. 75 or 50 liters of reductant.
    A first conduit 271 is provided to direct the reductant to a pump 230 from the container 205. The pump 230 may be any suitable pump. The pump 230 may be a diaphragm pump comprising at least one filter. The pump 230 is arranged to be driven by means of an electric motor. The pump is 230 arranged to pump up the reductant from the container 205 via the first line 271 and via a second line 272 supply said reductant to a dosing unit 250.
    The dosing unit 250 comprises an electrically controlled dosing valve, by means of which a flow of reductant added to the exhaust system can be controlled. The pump 230 reductant is arranged to pressurize in the second line 272. The dosing unit 250 is arranged with a throttling unit, against which said pressure of the reductant is built up in the subsystem 299.
    The dosing unit 250 is arranged to supply said reductant to a 100. The dosing unit 250 is arranged to supply in a controlled manner an appropriate amount of exhaust system (not shown) to the vehicle. More specifically, the reductant is to an exhaust system of the vehicle 100. According to this embodiment, an SCR catalyst is (not shown) arranged downstream of a position of the exhaust system where supply of the reductant is effected. The amount of reductant supplied to the exhaust system is intended to be used in a conventional manner in the SCR catalyst to reduce the amount of unwanted emissions in a known manner.
    The dosing unit 250 is arranged at e.g. an exhaust pipe arranged to direct exhaust gases from an internal combustion engine (not shown) of the vehicle 100 to the SCR catalyst. The exhaust system may include a muffler (not shown) arranged in any conventional manner. The dosing unit 250 is arranged in thermal contact with the exhaust system of the vehicle 100. This means that thermal energy is stored in e.g. an exhaust pipe, muffler and SCR catalyst can then be led to the dosing unit. The dosing unit 250 comprises an electronic control card, which is 200.
    The dosing unit 250 also comprises plastic and / or rubber components, arranged to handle communication with a control unit which may melt or be otherwise adversely affected at excessive temperatures.
    The dosing unit 250 is sensitive to temperatures above a certain temperature value, such as e.g. 120 degrees Celsius. Since e.g. the exhaust pipe, muffler and SCR catalytic converter of the vehicle 100 exceed this temperature value, there is a risk that the dosing unit may overheat during operation of the vehicle or after operation of the vehicle unless cooling is provided. A third conduit 273 is provided between the metering unit 250 and the container 205. The third conduit 273 is arranged to return a certain amount of the reductant fed to the metering valve 250 to the container 205. With this configuration advantageous cooling of the metering unit 250 is provided. In this way, the dosing unit 250 is cooled by a fate of the reductant as it is pumped through the dosing unit 250 from the pump 230 to the container 205.
    A first coolant line 281 is provided to hold and transport coolant for an engine of the vehicle 100. The first coolant line 281 is partially disposed in the container 205 to heat the reductant present therein in the event that the reductant is cooled. According to this example, the first coolant line 281 is arranged to direct coolant heated by the vehicle's engine in a closed circuit through the container 205, via the pump 230 and a second coolant line 282 back to the engine of the vehicle 100.
    According to one embodiment, the first coolant line 281 is configured with a substantially U-shaped portion present in the container 205, as schematically shown in Figure 2. With this configuration, an improved heating of the reductant in the container 205 is provided when the reductant has too low a temperature to operate. in a desirable manner. It should be noted that the first coolant line 281 may be configured in any suitable manner. In case the reductant has a temperature exceeding a predetermined value, heating of the reductant by means of the coolant can be deactivated automatically.
    A first control unit 200 is the temperature sensor 220 via a link 293. The temperature sensor 220 is arranged arranged for communication with one to detect a prevailing temperature of the reductant where the sensor is mounted. According to this embodiment, the temperature sensor 220 is arranged at a bottom of the substantially U-shaped configuration of the first coolant line 281.
    The temperature sensor 220 is arranged to continuously send signals to the first control unit 200 including information about a prevailing temperature of the reductant. According to an alternative, the dosing unit 250 is for detecting a prevailing temperature of the temperature sensor reductant there. The temperature sensor 220 is arranged to detect a prevailing temperature of the reductant at a suitable position within the subsystem 299, which detected temperature can form the basis for calculating a temperature course of the dosing unit to enable to suitably control operation of the pump 230 to cool the dosing unit by said flow of reductant.
    The first control unit 200 is arranged for communication with the pump 230 via a link 292. The first control unit 200 is arranged to control operation of the pump 230 in order to e.g. regulating a pressure in the line 272. Thereby, a return flow of the reductant from the dosing unit 250 to the container 205 can be described as a function of a pressure of the reductant upstream of the dosing unit 250. The first control unit 200 is arranged to regulate a prevailing temperature of the dosing unit. pump 230.
    The first control unit 200 is arranged for communication with the dosing unit 250 via a link 291. The first control unit 200 is arranged to control operation of the dosing unit 250 in order to e.g. regulating the supply of the reductant to the exhaust system of the vehicle 100. The first control unit 200 is arranged to control the operation of the dosing unit 250 in order to e.g. regulate re-supply of the reductant to the container 205.
    According to one embodiment, the first control unit 200 is arranged to control operation of the pump 230 on the basis of the signals received from the temperature sensor, including information on a prevailing temperature of the reductant at an arbitrary position of the SCR system. In particular, the first control unit 16 200 according to a means arranged to, on the basis of the received signals comprising a prevailing temperature of the reductant at the area of the temperature sensor 220, intermittently control operation of the pump 230 with reduced power compared to ordinary operation after shutting off an exhaust gas flow from the engine.
    A second control unit 210 is arranged for communication with the first control unit 200 via a link 290. The second control unit 210 may be detachably connected to the first control unit 200. The second control unit 210 may be a control unit external to the vehicle 100. The second control unit 210 may be arranged to perform the innovative method steps according to the invention. The second control unit 210 can be used to upload software to the first control unit 200, in particular software for performing the innovative method. The second control unit 210 may alternatively be arranged for communication with the first control unit 200 via an internal network in the vehicle. The second control unit 210 may be arranged to perform substantially similar functions as the first control unit 200, such as e.g. calculating a value for future maximum temperature of the dosing unit on the basis of the received signals comprising a prevailing temperature of the reductant and controlling operation of the pump 230 in any suitable manner on the basis of the calculated temperature value. The second control unit 210 may be arranged to determine a need to, after switching off an exhaust flow, cool a dosing unit for reducing agent by means of reducing agent, and to predict a temperature course of at least a part of said SCR system as a basis for determining said need.
    It should be noted that the innovative method can be performed by the first control unit 200 or the second control unit 210, or by both the first control unit 200 and the second control unit 210.
    According to the embodiment schematically illustrated with reference to Figure 2, the first control unit 200 is arranged to control operation of the pump 230 with 17 reduced power compared to ordinary operation after shutting off an exhaust flow from the engine in such a way that, where applicable, an amount required electrical energy to cool the dosing unit 250 to a safety-critical temperature is reduced compared to the prior art.
    Figure 3 schematically illustrates a subsystem 399 of the vehicle 100.
    Subsystem 399 includes certain components described above with reference to Figure 2, such as e.g. the first control unit 200, the second control unit 210 and the temperature sensor 220 for detecting a prevailing temperature of the reductant in the container 205.
    The subsystem 399 includes a temperature sensor 310 which is arranged to measure a prevailing temperature of exhaust gases in an exhaust system upstream of the SCR catalyst. The temperature sensor 310 is arranged for communication with the first control unit via a link 311. The temperature sensor 310 is arranged to continuously send signals including information about a prevailing temperature of the exhaust stream to the first control unit 200 via the link 311. According to one embodiment, the first control unit 200 is arranged to estimating a prevailing temperature of the SCR catalyst on the basis of the received signals including information on a prevailing temperature of the exhaust stream.
    The subsystem 399 includes a temperature sensor 320 which is arranged to measure a prevailing temperature of the SCR catalyst. The temperature sensor 320 is arranged for communication with the first control unit via a link 321.
    The temperature sensor 320 is arranged to continuously send signals including information about a prevailing temperature of the SCR catalyst to the first control unit 200 via the link 321.
    The subsystem 399 includes a temperature sensor 330 which is arranged to measure a prevailing temperature of the dosing unit 250. The temperature sensor 330 is arranged for communication with the first control unit via a link 18 331. The temperature sensor 330 is arranged to continuously send signals including information about a prevailing temperature of the dosing unit 250 to the first control unit 200 via the link 331.
    The subsystem 399 includes a flow sensor 340 which is arranged to measure a prevailing flow of the reductant in the SCR system. The flow sensor 340 is can be arranged at any position of the SCR system, such as e.g. at line 273 downstream of the dosing unit 250. The flow sensor 340 is arranged for communication with the first control unit via a link 341.
    The flow sensor 340 is arranged to continuously send signals including information of a prevailing flow of the reductant to the first control unit 200 via the link 341.
    The signals sent by the sensors 310, 320, 330, 340 and 220, respectively, can be used by the first control unit to model a temperature profile of the dosing unit 250 according to an aspect of the invention. According to one embodiment, the first control unit 200 is arranged to model a temperature variation of the dosing unit 250 on the basis of the information of at least one of the signals received from the sensors 310, 320, 330, 340 and 220, respectively.
    Figure 4a schematically illustrates a flow chart of a method in SCR systems for exhaust gas purification, according to an embodiment of the invention. The method comprises a first method step s401. Step s401 comprises the step of determining a need to, after switching off an exhaust gas flow, cooling a dosing unit for reducing agent by means of reducing agent, and the step of predicting a temperature course of at least a part of said SCR system as a basis for determining said need. After step s401, the process is terminated.
    Figure 4b schematically illustrates a flow chart of a method in SCR systems for exhaust gas purification, according to an embodiment of the invention. The method comprises a first method step s410. Method step s410 includes the step of shutting off an exhaust gas flow from an internal combustion engine of the vehicle 100. At this time, the metering unit 250 is cooled in an ordinary manner, i.e. with the operating power of the pump 230 needed to maintain substantially the same cooling flow of the dosing unit as in ordinary operation.
    Shut-off of the exhaust gas flow is achieved by shutting down the engine of 100. After s410, a process step s415 is performed. the vehicle process step following future temperature course of the dosing unit 250 by means of a calculation model The process step s415 includes the step of calculating one which is stored in the first control unit 200 or the second control unit 210.
    The calculation of the temperature course can take place on the basis of one or a number of arbitrary parameters, such as e.g. a prevailing temperature of the SCR catalyst of the vehicle, a prevailing temperature of the reductant, a flow of the reductant in the SCR system, a prevailing temperature of a muffler of the vehicle, a prevailing temperature of the dosing unit 250, temperature of an exhaust gas flow before switching it off and / or a parameter associated with estimated vehicle load for a certain period of time before shutting off said exhaust flow. The calculation model is arranged to calculate a prevailing amount of stored energy in different parts of the SCR system in order to calculate on the basis thereof and thereby predict a temperature course of the dosing valve 250 as a basis for determining a need to cool the dosing unit 250.
    By calculating a future temperature course of the dosing unit 250, it can also be determined what maximum temperature the dosing unit 250 can reach in the event that cooling thereof does not continue or is interrupted after the shut-off of the exhaust gas flow. By determining a modeled value for a maximum future temperature of the dosing unit 250, operation of the pump 230 can be optimally controlled on the basis thereof. After the process step s415, a subsequent process step s420 is performed.
    Process step s420 includes the step of evaluating whether there is a continuing need to cool the dosage unit by a flow of the reductant in the SCR system. The step of determining whether there is a need to continue said cooling can take place on the basis of the determined modeled value for maximum future temperature of the dosing unit 250. According to an example, it is determined whether a continued cooling need exists on the basis of the signals from at least one of the sensor 220, the sensor 310, the sensor 320, the sensor 330, the sensor 340, which signals include information in accordance with what has been described above with reference to Figure 3. If there is no further cooling need, the process is terminated. If there is a continued cooling demand, a subsequent procedure step s430 is performed.
    The method step s430 includes the step of influencing the operation of the pump 230 in such a way that the pump is operated intermittently and / or with reduced operating power compared to ordinary operation. According to one embodiment, the pump 230 is operated intermittently with a predetermined interval configuration. According to one embodiment, the pump 230 is operated intermittently with an operating power corresponding to ordinary operation. According to one embodiment, the pump 230 is operated intermittently with a reduced operating power compared to an operating power used to maintain a cooling flow of the dosing unit 250 during ordinary operation. After the process step s430, a subsequent process step s440 is performed.
    Process step s440 includes the step of evaluating whether there is a continuing need to continue cooling the dosage unit by a flow of the reductant in the SCR system. The step of determining whether there is a need to continue said cooling can take place on the basis of an updated modeled value for maximum future temperature of the dosing unit 250. According to one embodiment, the calculation model is arranged to continuously update a determined modeled value for the future maximum temperature of the dosing unit 250. Calculation of an updated value for said maximum temperature can be performed in essentially the same way as described e.g. with reference to procedure step s415. According to an example, 21 is determined whether a continued cooling demand exists on the basis of the signals from at least one of the sensor 220, the sensor 310, the sensor 320, the sensor 330, the sensor 340, which signals comprise information as described above with reference to Figure 3. If it is determined that there is no continued cooling demand, the procedure is terminated. If it is determined that there is a continuing need for cooling, operation of the pump 230 continues in an arbitrary manner to ensure efficient cooling of the dosing unit 250. Eg. the pump 230 can continue to be operated intermittently, possibly even with reduced operating power compared to ordinary operation.
    Referring to Figure 5, there is shown a diagram of an embodiment of a device 500. The controllers 200 and 210 described with reference to Figure 2 may in one embodiment include the device 500. The device 500 includes a non-volatile memory 520, a data processing unit 510, and a read / write memory 550. The non-volatile memory 520 has a first memory portion 530 in which a computer program, such as an operating system, is stored to control the operation of the device 200. Further, the device 500 includes a bus controller, a serial communication port , I / O means, an A / D converter, a time and date input and transfer unit, an event counter and an interrupt controller (not shown). The non-volatile memory 520 also has a second memory portion 540.
    A computer program P is provided which comprises routines for determining a need to, after switching off an exhaust flow, cool a dosing unit for by means of temperature course of at least a part of said SCR system as reducing agent reducing agent, and to predict a basis for determining said need. , according to the innovative procedure.
    The program P includes routines for predicting whether a predetermined temperature of the dosing unit will be reached after said shut-off of exhaust gas flow. The program P may be stored in an executable manner or in a compressed manner in a memory 560 and / or in a read / write memory 550. 22 When it is described that the data processing unit 510 performs a certain function, it should be understood that the data processing unit 510 performs a certain part of the program which is stored in the memory 560, or a certain part of the program which is stored in the read / write memory 550.
    The data processing device 510 can communicate with a data port 599 via a data bus 515. The non-volatile memory 520 is intended for communication with the data processing unit 510 via a data bus 512. The separate memory 560 is intended to communicate with the data processing unit 510 via a data bus 511. the data processing unit 510 via a data bus 514. To the data port 599, e.g. links 311, 321, 331, 341, 293 and 290 are connected (see Figure 3).
    The read / write memory 550 is arranged to communicate with When data is received on the data port 599, it is temporarily stored in the second memory part 540. When the received input data has been temporarily stored, the data processing unit 510 is prepared to perform code execution in a manner described above. According to one embodiment, signals received at the data port 599 include information of a prevailing temperature of an SCR catalyst of the vehicle 100. According to one embodiment, signals received at the data port 599 include information of a prevailing temperature of the reductant in the SCR system. data port 599 information about a prevailing flow of the reductant, e.g. According to one embodiment, signals received on line 273. According to one embodiment, signals received on data port 599 include information about a prevailing temperature of the metering unit 250 of the SCR system. According to one embodiment, signals received at the data port 599 include information about a prevailing temperature of an exhaust flow in the exhaust system of the vehicle 100.
    The received signals on the data port 599 can be used by the device 500 to determine, by means of a calculation model stored in the device 500, a need to, after switching off an exhaust gas flow, cool a dosing unit for reducing agent by means of reducing agent, predict a temperature course of at least a part of said SCR system as a basis for determining said needs.
    Parts of the methods described herein may be performed by the device 500 by means of the data processing unit 510 running the program stored in the memory 560 or the read / write memory 550. When the device 500 runs the program, the methods described herein are executed.
    The foregoing description of the preferred embodiments of the present invention has been provided for the purpose of illustrating and describing the invention. It is not intended to be exhaustive or to limit the invention to the variations described. Obviously, many modifications and variations will occur to those skilled in the art. The embodiments were selected and described to best explain the principles of the invention and its practical applications, thereby enabling those skilled in the art to understand the invention for various embodiments and with the various modifications appropriate to the intended use.
    权利要求:
    Claims (22)
    [1]
    A method of SCR system for exhaust gas purification, comprising the steps of: - determining a need to, after switching off an exhaust gas flow, cool a dosing unit (250) for reducing agents by means of reducing agents, characterized by the step of: - predicting a temperature course of at least one part of said SCR system as a basis for determining said needs.
    [2]
    The method of claim 1, further comprising the step of: - predicting whether a predetermined temperature of the metering unit (250) will be reached after said shutdown of exhaust gas flow.
    [3]
    The method of claim 2, wherein said predetermined temperature is a functionally critical temperature for the dosage unit (250).
    [4]
    A process according to any one of the preceding claims, wherein said at least a portion of said SCR system comprises some of an SCR catalyst, a muffler, the dosage unit (250) or the reducing agent.
    [5]
    A method according to any one of the preceding claims, wherein said prediction of temperature course of said at least a part of said SCR system enables indirect determination of a future temperature of the dosing unit (250).
    [6]
    A method according to any one of the preceding claims, wherein said prediction of the temperature course involves consideration of reheating effects of at least a part of the SCR system.
    [7]
    A method according to any one of the preceding claims, further comprising the step of: - predicting said temperature course of at least a part of said SCR system by means of a calculation model including a predetermined parameter configuration.
    [8]
    A method according to claim 7, wherein the step of determining said need is performed before said shutdown of exhaust flow, or the step of determining said need is performed after said shutdown of exhaust flow.
    [9]
    A method according to any one of the preceding claims, wherein said reducing agent is a fluid solution comprising urea.
    [10]
    Device comprising an SCR system for exhaust gas purification, comprising: - means (200; 210; 500) for determining a need to, after switching off an exhaust gas flow, cool a dosing unit (250) for reducing agents by means of reducing agents, characterized by - means (200; 210; 500) for predicting a temperature course of at least a part of said SCR systems as a basis for determining said needs.
    [11]
    The device of claim 10, further comprising: - means (200; 210; 500) for predicting whether a predetermined temperature of the dosing unit will be reached after said shut-off of exhaust gas fl.
    [12]
    The device of claim 11, wherein said predetermined temperature is a functionally critical temperature of the dosage unit (250).
    [13]
    The device of any of claims 10-12, wherein said at least a portion of said SCR system includes some of an SCR catalyst, a muffler, the dosage unit (250) or the reducing agent. 10 15 20 25 30 26
    [14]
    Device according to any one of claims 10-13, wherein said prediction of temperature course of said at least a part of said SCR system future temperature of enables indirect determination of a dosing unit (250).
    [15]
    Device according to any one of claims 10-14, wherein said prediction of the temperature course includes consideration of reheating effects of at least a part of the SCR system.
    [16]
    An apparatus according to any one of claims 10-15, further comprising: - means (200; 210; 500) for predicting said temperature course of at least a part of said SCR system by means of a calculation model including a predetermined parameter configuration.
    [17]
    The device according to claim 16, wherein the means for determining said need is arranged to determine said need before said shut-off of exhaust flow, or wherein the means for determining said need are arranged to determine said need after said shut-off of exhaust flow.
    [18]
    The device of any of claims 10-17, wherein said reducing agent is a fluid solution comprising urea.
    [19]
    A motor vehicle (100; 110) comprising a device according to any one of claims 10-18.
    [20]
    The motor vehicle (100; 110) according to claim 19, wherein the motor vehicle is something of a truck, bus or passenger car.
    [21]
    A computer program (P) in an SCR system for exhaust gas purification, wherein said computer program (P) comprises program code stored on a computer readable medium for causing an electronic control unit (200; 500) or another computer (210). 500 connected to the electronic control unit (200; 500) for performing the steps of any of claims 1-9.
    [22]
    A computer program product comprising a program code stored on a computer readable medium for performing the method steps of any of claims 1-9, when said computer program is run on an electronic control unit (200; 500) or another computer (210; 500) connected to the electronic control unit (200; 500).
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    同族专利:
    公开号 | 公开日
    SE537642C2|2015-09-08|
    US20130186069A1|2013-07-25|
    EP2582941A1|2013-04-24|
    CN103109054A|2013-05-15|
    EP2582941A4|2016-02-17|
    US9222385B2|2015-12-29|
    WO2011162688A1|2011-12-29|
    RU2013102539A|2014-07-27|
    RU2548326C2|2015-04-20|
    EP2582941B1|2018-03-21|
    BR112012032239A2|2020-09-01|
    JP2013534587A|2013-09-05|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1050642A|SE537642C2|2010-06-21|2010-06-21|Method and apparatus for cooling a reducing agent dosing unit|SE1050642A| SE537642C2|2010-06-21|2010-06-21|Method and apparatus for cooling a reducing agent dosing unit|
    PCT/SE2011/050783| WO2011162688A1|2010-06-21|2011-06-20|Method and device pertaining to cooling of dosing units of scr systems|
    RU2013102539/06A| RU2548326C2|2010-06-21|2011-06-20|Method and device relevant to batching modules cooling in scr systems|
    CN2011800357051A| CN103109054A|2010-06-21|2011-06-20|Method and device pertaining to cooling of dosing units of SCR systems|
    JP2013516530A| JP2013534587A|2010-06-21|2011-06-20|Method and apparatus relating to cooling of the input unit of a selective catalytic reduction system|
    BR112012032239-7A| BR112012032239A2|2010-06-21|2011-06-20|method and device for cooling dosing units of scr systems|
    US13/704,743| US9222385B2|2010-06-21|2011-06-20|Method and device pertaining to cooling of dosing units of SCR systems|
    EP11798458.3A| EP2582941B1|2010-06-21|2011-06-20|Method and device pertaining to cooling of dosing units of scr systems|
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