![]() Method and apparatus for determining the minimum level of a reducing agent container in an SCR syste
专利摘要:
SUMMARY The invention relates to a method in SCR systems comprising a dosing unit (250) for supplying reducing agent to an exhaust duct (240) for exhaust gas purification and a container for reducing agent, comprising stepwise selecting (s310; s340) a limit level for reducing agent in saga container (205) for reducing agents. The method also includes the steps of determining (s320) a cooling demand of said dosage unit (250), and selecting (s340) a limit level for reducing agent in said container (205), based on said cooling demand. The invention also relates to a computer program product comprising program code (P) for a computer (200; 210; 400) for implementing a method according to the invention. The invention also relates to a device of an SCR system comprising a dosing unit (250) for supplying reducing agent to a single exhaust duct (240) for exhaust gas purification and a motor vehicle (100) equipped with the device. Figure 2 for publication 公开号:SE1050653A1 申请号:SE1050653 申请日:2010-06-21 公开日:2011-12-22 发明作者:Andreas Liljestrand;Per Bremberg;Daniel Arvidsson 申请人:Scania Cv Ab; IPC主号:
专利说明:
to cool the dosing unit by means of the reductant which, when cooled, flows from 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 metering valve to the container can be substantially constant. In today's vehicles, cooling of the dosing unit is ensured by having a fairly high minimum permissible volume of reducing agent in the container. In this case, cooling of the dosing unit can be ensured even at extreme external temperatures. A disadvantage of this technique is that a relatively large portion of the reducing agent held by the container cannot be used for dosing into the exhaust pipe for use in the SCR catalyst. In this case, said reducing agents will in practice to some extent constitute ballast, which in itself entails a number of negative effects, such as e.g. that the total load capacity of the vehicle is less than it could be, both in terms of weight and volume. urea solution to an exhaust system where the urea solution is pumped from a tank i describes a temperature-controlled injection system for sufficient mass flow to enable sufficient injection, and to cool an associated injector to a sufficiently low temperature. The cooling oil solution can be returned to the tank. The system includes a volume meter and temperature sensor in the tank. In the event of a deviation, the system can stop the circulation of the urea solution. This has the disadvantage that an undesired temperature can be obtained at the injector. Thus, there is a need to improve the present SCR system to reduce or eliminate the above mentioned drawbacks. 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. An object of the present invention is to provide a new and advantageous method for improving the performance of an SCR system, in which an available volume of reducing agent for dosing is optimized. Another object of the invention is to provide a new and advantageous device of an SCR system and a new and advantageous computer program for improving the performance of an SCR system. Another object of the invention is to provide a new and advantageous device of an SCR system and a new and advantageous computer program for improving the performance of an SCR system, in which an available volume of reducing agent for dosing is optimized. An object of the present invention is to provide a method and a device in an SCR system, wherein said method and device respectively provide a reduced risk of undesired functional degradation of components of the SCR system and / or a reduced risk of clogging of components, t .ex. a dosage unit, of the SCR system with respect to a reducing agent. A further object of the invention is to provide an alternative method in an SCR system and an alternative computer program in an SCR system and an alternative device of an SCR system. These objects are achieved by a method in SCR systems comprising a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification, according to claim 1. According to one aspect of the invention, there is provided a method of SCR system comprising a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification and a container for reducing agent, comprising the step of selecting a limit level for reducing agent in said reducing agent container. The method also includes the steps of determining a cooling requirement of said dosing unit, and of selecting a limit level for reducing agent in said container, on the basis of said cooling requirement. To ensure that the reducing agent in the container does not become too hot, to ensure efficient cooling of the dosing unit, the innovative method is provided, whereby a sufficient volume of reducing agent is selected. Hereby an optimization of a minimum desired volume of reducing agent can be provided. According to one aspect of the present invention, a variable minimum permissible volume of reducing agent is made possible in the container, which volume is determined on the basis of an actual cooling requirement of the dosing unit. An advantage of the present invention is that a volume of reducing agent available for dosing can be maximized. In a case where the SCR system is mounted on a motor vehicle, the load capacity can then be advantageously increased both in terms of weight and volume. Another advantage of the present invention is that the volume of the container can in some cases be optimized, such as e.g. made smaller, which can free up space for other components of the SCR system or other system mounted on the SCR system. Another advantage of the present invention is that the choice of residual volume strategy based on a region or climate in which the SCR system is normally operated can be provided. According to one aspect of the invention, it is possible to temporarily lower a limit value level, indicating a minimum desired volume of reducing agent in the container, in case it is deemed necessary to e.g. avoid automatic reduction of available torque of a motor of the SCR system. The method may comprise the steps of: - determining a prevailing temperature of said reducing agent in said container; and - determining said cooling demand of said dosage unit on the basis of said determined prevailing temperature of said reducing agent in said container. This gives the advantage of being able to determine said cooling need by means of a simple provider of a method with a small calculation model, which calculation complexity. The method may comprise the steps of: - determining a prevailing temperature of said reducing agent in said dosage unit; and - determining said cooling demand of said dosage unit on the basis of said established dosage unit. This gives the advantage of being able to determine said cooling demand prevailing temperature of said reducing agent in said by means of a simple calculation model, which provides a method with small calculation complexity. The method may comprise the step of: - determining said cooling demand of said dosing unit on the basis of at least one determined parameter selected from the group including: prevailing ambient temperature of said container, prevailing operating power of an engine of said SCR system, prevailing temperature of exhaust gases in said exhaust duct , and accumulated dosed amount of reducing agent. In this case, an improved basis can be provided to make it possible to determine said cooling needs with additional accuracy. The method may comprise the step of: - selecting said limit level for reducing agents in said container within a predetermined range. By introducing restrictions in the selection of said limit level, a safer procedure is achieved in order to reduce the risk of unwanted clogging of the dosing unit. A lower limit level for 3 or 5 reducing agents in the container. An upper limit level for reducing agents in reducing agents in the container can correspond to e.g. liters the container may correspond to a volume which is slightly less than a total volume of the container, such as e.g. 90% of the total volume. The method may comprise the step of: - continuously determining a cooling requirement of said dosing unit, and - selecting an updated limit level for reducing agent in said container, on the basis of said continuously determined cooling requirement. In this way a method is provided which has a rapid response to oscillating processes, such as e.g. during operation of the SCR system with strongly varying loads. The method may comprise the step of: - selecting an initial level of reducing agent in a reducing agent container, based on the performance of said SCR system and / or an imaginary future operation of the SCR system, average load of an engine of the SCR system and estimated maximum in terms of e.g. estimated load on the motor of the SCR system. This has the advantage of providing a method with shortened adaptation of said limit level of the reducing agent in the container, which also gives a more robust method. Said reducing agent may be a urea-based reducing agent. Said limit level for reducing agent in said container corresponds to a minimum desired volume of reducing agent in said container. The procedure is easy to implement in existing motor vehicles. Software in SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust 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 SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust purification and a container for reducing agent 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. Innovative procedure is thus cost effective, in components need to be installed in the vehicle. Required hardware is today Implementation of it especially since no additional sensors or already pre-arranged in the vehicle. The invention thus provides a cost-effective solution to the above problems. Software that includes program code in SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust purification can be easily updated or replaced. Furthermore, different parts of the software that include program code in SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust purification can be replaced independently of each other. This modular configuration is advantageous from a maintenance perspective. According to one aspect of the invention, there is provided an apparatus of SCR systems comprising a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification and a container for reducing agent, comprising means for selecting a limit level for reducing agent in said reducing agent container. The device also comprises means for determining a cooling need of said dosing unit, as well as means for selecting a limit level for reducing agent in said container, on the basis of said cooling need. The device may comprise: - means for determining a prevailing temperature of said reducing agent in said container; and - means for determining said cooling demand of said dosage unit on the basis of said determined prevailing temperature of said reducing agent in said container. The device may comprise: - means for determining a prevailing temperature of said reducing agent in said dosing unit; and means for determining said cooling demand of said dosage unit on the basis of said determined prevailing temperature of said reducing agent in said dosage unit. The device may comprise: - means for determining said cooling demand of said dosing unit on the basis of at least one determined parameter selected from the group including: prevailing ambient temperature of said container, prevailing operating power of an engine of said SCR system, prevailing temperature of exhaust gases in said exhaust duct, and accumulated dosed amount of reducing agent. The device may comprise: - means for selecting said limit level for reducing agents in said container within a predetermined range. The device may comprise: - means for continuously determining a cooling need of said dosing unit, and - means for selecting an updated limit level for reducing agents in said container, on the basis of said continuously determined cooling needs. The device may comprise: - means for selecting an initial limit level for reducing agent in a reducing agent container, based on the performance of said SCR system and / or an imaginary future operation of the SCR system, average load of an engine of the SCR system and estimated maximum in terms of e.g. estimated load on the motor of the SCR system. The above objects are also achieved with a motor vehicle which includes the features of the device of SCR systems which include a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification. The motor vehicle can be a truck, bus or car. According to one aspect of the invention, there is provided a computer program in SCR systems comprising a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas cleaning and a container for reducing agent, said computer program comprising program code stored on a computer readable medium to cause an electronic control unit or another computer connected to the electronic control unit to perform the steps according to any one 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 and incorporate within other further applications, modifications areas, 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 3a schematically illustrates a flow chart of a method, according to an embodiment of the invention; Figure 3b schematically illustrates in further detail a flow chart of a method, according to an embodiment of the invention; and Figure 4 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 with an engine 150 and 11 a trailer 112. The vehicle may 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 limited to SCR systems of motor vehicles. The innovative method of SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification and the innovative device of SCR systems comprising a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification according to an aspect of the invention are well suited for other platforms which includes 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 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 microway 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 emissions can e.g. be NOx gas. The terms "reductant" and "reducing agent" are used synonymously herein. Said reductant is according to an embodiment 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 the necessary adaptations, e.g. regarding temperature level where functional degradation for a given reductant is initiated, 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 an outflow of added reductant can be controlled. The pump 230 is arranged to pressurize the reductant 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 an exhaust duct 240 of an exhaust system (not shown in its entirety) of the vehicle 100. The exhaust duct 240 is arranged to direct exhaust gases from the engine 150 to an environment of the SCR system. More specifically, the dosing unit 250 is arranged to supply in a controlled manner a suitable amount of reductant to the exhaust duct 240 of the vehicle 100. According to this embodiment, an SCR catalyst (not shown) is arranged downstream of a position of the exhaust system where supply of the reductant is provided. 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 the exhaust duct which is arranged to direct exhaust gases from the internal combustion engine 150 of the vehicle 100 to the SCR catalyst. 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. the exhaust duct 240, muffler and SCR catalyst can then be led to the dosing unit 250. In the dosing unit, reducing agent present therein can be heated by said thermal energy. 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 itself sensitive to temperatures above a certain 120 degree exhaust duct 240, the muffler and the SCR catalyst of the vehicle 100 temperature value, such as e.g. Celsius. Since e.g. If this temperature value exceeds this, 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. It should be noted that the reductant present in the dosage unit 250 may be adversely affected at temperatures significantly lower than the 120 degrees Celsius indicated above. At temperatures exceeding e.g. 70 degrees the reducing agent becomes unstable, temperatures possibly crystallize and in the long run possibly cause Celsius to in order at slightly higher clogging of the dosing unit 250. 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. the metering unit 250 is cooled by a flow of the reductant as it is pumped through the metering unit 250 from the pump 230 to the container 205. A first control unit 200 is arranged for communication with a first temperature sensor 220 via a link 221. The first temperature sensor 220 is arranged to detect a prevailing temperature of the reductant in the dosing unit 250. The first temperature sensor 220 is arranged to continuously send signals to the first control unit 200 including information about a prevailing first temperature T1 of the reductant in the dosing unit 250. The first control unit 200 is arranged to calculate a cooling demand of the dosing unit 250 on the basis of the signals received from the first temperature sensor 220. The first control unit 200 is arranged for communication with the pump 230 via a link 231. The first control unit 200 is arranged to control operation of the pump 230 in order to e.g. regulate flows of the reductant within the subsystem 299. The first control unit 200 is arranged to control an operating power of the pump 230 by controlling the electric motor thereby. The first control unit 200 is arranged for communication with a second temperature sensor 280 via a link 281. The second temperature sensor 280 is arranged to detect a prevailing temperature T2 of the exhaust duct 240. The second temperature sensor 280 is arranged to continuously send signals to the first control unit 200 including information about a prevailing temperature of the exhaust duct 240. The first control unit 200 is arranged to calculate a prevailing temperature Test of the reductant in the dosing unit 250 on the basis of the signals received from the the second temperature sensor 280. The first control unit 200 is arranged to calculate a cooling demand of the dosing unit 250 on the basis of the signals received from the second temperature sensor 280. The first control unit 200 is arranged for communication with a third temperature sensor 290 via a link 291. The third temperature sensor 290 is arranged to detect a prevailing temperature T3 of the reductant in the container 205. The third temperature sensor 290 is arranged to continuously send signals to the first control unit 200 including information about a prevailing temperature of the reductant in the container 205. The first control unit 200 is arranged to calculate a cooling demand of the dosing unit 250 on the basis of the signals received from the third temperature sensor 290. The first control unit 200 is arranged for communication with a level sensor 260 via a link 261. The level sensor 260 is arranged to detect a prevailing volume of the reductant in the container 205. The level sensor 260 is arranged to continuously send signals to the first control unit 200 including information about a prevailing volume of the reductant in the container 205. The first control unit 200 is arranged to calculate a cooling demand of the dosing unit 250 on the basis of the signals received from the level travel sensor 260. The first control unit 200 is arranged for communication with the dosing unit 250 via a link 251. 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, on the basis of at least one of the signals received from the first temperature sensor 220, the second temperature sensor 280, the third temperature sensor 290 and the level sensor 260, to determine a cooling demand of the dosing unit 250, and to select a limit level for reducing agent in the container 205, on the basis of said cooling demand, in accordance with an aspect of the innovative process. A second control unit 210 is arranged for communication with the first control unit 200 via a link 201. 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. to determine a cooling need of dosing unit 250, and to select a limit level for reducing agent in the container 205, on the basis of said cooling need. 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. The subsystem 299 may also include a fourth temperature sensor (not shown) for detecting a prevailing ambient temperature T4 of said container 205 and sending a signal including this information to the first control unit 200. The first control unit 200 is arranged to determine a cooling need of said dosing unit 250 on the basis of the measured prevailing ambient temperature of said container 205. The subsystem 299 may also include determining means (not shown) for determining the accumulated dosed amount of reducing agent and sending a signal including this information to the first control unit 200. The first control unit 200 is arranged to determine a cooling need of said dosing unit 250 on the basis of the determined accumulated dosed amount of reducing agent. The subsystem 299 may also include determining means (not shown) for determining a prevailing operating power of a motor 150 of said SCR system and sending a signal including this information to the first control unit 200. The first control unit 200 is arranged to determine a cooling need of said dosing unit 250 on the basis of the determined operating power of the motor 150 of said SCR system. Figure 3a schematically illustrates a flow chart of a process in SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification and a container for reducing agent, according to a first method step s301. Step s301 includes the step of selecting a boundary level for an embodiment of the invention. The method comprises reducing agents in said reducing agent containers. The step s301 includes the steps of determining a cooling requirement of said dosing unit and 18 selecting a limit level for reducing agent in said container, on the basis of said cooling requirement. After step s301, the process is terminated. Figure 3b schematically illustrates a flow chart of a process in SCR systems including a dosing unit for supplying reducing agent to an exhaust duct for exhaust gas purification and a container for reducing agent, according to an embodiment of the invention. The method includes a first method step s310. Method step s310 includes the step of selecting an initial reducing agent limit value in the container 205. This limit value corresponds to a minimum desired residual volume of reducing agent in the container 205. This residual volume can be set based on how the SCR system is intended to operate in the future. In case the SCR system is mounted on a motor vehicle, this residual volume can be set on the basis of the vehicle's operating type and / or maximum engine power of the vehicle, and / or in which regional area the vehicle is intended to be used. The initial limit value for reducing agent in the container 205 can be set to a suitable value, such as e.g. 5, 10, 15 or 20 liters. After the process step s310, a subsequent process step s320 is performed. Method step s320 includes the step of determining a cooling need of the dosing unit 250. This can be done in a number of different ways. According to one example, only a measured temperature of the reducing agent in the container 205 is considered. According to one example, only a measured temperature of the reducing agent in the dosing unit 250 is considered. According to one example, a measured temperature of the reducing agent in the container 205 and a measured temperature of the reducing agent in the dosing unit 250 are considered. According to another example, parameters such as e.g. prevailing ambient temperature of the container 205, and / or prevailing operating power of the engine 105 of the SCR system, and / or prevailing temperature of exhaust gases in the exhaust duct 240 and / or accumulated metered amount of reducing agent is used to determine a cooling requirement of the metering unit 250. a subsequent procedure step s330 is performed. The process step s330 includes the step of determining whether to change the current reducing agent limit value in the container 205. This can be done in different ways. In cases where it is determined that the SCR system has been operated with a relatively high power for a certain time, and / or where it is determined that a temperature of the reductant, e.g. in the container 205, has increased to an undesirable level, the limit value of the reducing agent may need to be changed to ensure a required cooling of the dosing unit 250. According to an example, a temperature of the reducing agent in the container 205 should not exceed 50 degrees Celsius to avoid the reducing agent not is degraded functionally and in the long run completely or partially clog the dosing unit 250, even during normal operation. If it is determined that the current limit value for reducing agent in the container 205 is not to be changed, the procedure step s320 is performed again. If it is determined that the current limit value for reducing agent in the container 205 is to be changed, a subsequent process step s340 is performed. The process step s340 comprises the step of selecting, on the basis of said cooling demand, a limit level for reducing agent in said container. This limit level can be either higher or lower than a currently current limit level. It should be noted that the innovative method makes it possible to set an optimal limit level for reducing agent in the container 205 for each SCR system. According to one example, adaptation of an appropriate limit level of reducing agent in the container 205 may take a number of days or weeks. According to one example, a function is also provided in which a more short-term adaptation of an appropriate limit level for reducing agent in the container 205 is performed taking into account temporarily changed operating cases of the SCR system. After the procedure step s340, the procedure is terminated. Referring to Figure 4, there is shown a diagram of an embodiment of a device 400. The controllers 200 and 210 described with reference to Figure 2 may in one embodiment include the device 400. The device 400 includes a non-volatile memory 420, a data processing unit 410, and a read / write memory 450. The non-volatile memory 420 has a first memory portion 430 in which a computer program, such as an operating system, is stored to control the operation of the device 200. Further, the device 400 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 420 also has a second memory portion 440. A computer program P is provided which includes routines for determining a cooling need of said dosing unit. Program P includes routines for determining a prevailing temperature of said reducing agent in said container; and determining said cooling needs of said dosage unit reducing agents in said container. As an alternative, or a complement, on the basis of said prevailing temperature of said, the program P comprises routines for determining a prevailing temperature of said reducing agent in said dosage unit; and determining said cooling demand of said dosage unit on the basis of said determined prevailing temperature of said reducing agent in said dosage unit. The program P includes routines for determining said cooling demand of the dosing unit on the basis of at least one determined parameter selected from the group including: prevailing ambient temperature of said container 205, prevailing operating power of the engine 150 of said SCR system, prevailing temperature of exhaust gases in the exhaust duct 240, and accumulated dosed amount of reducing agent. The program P includes routines for selecting a limit level for reducing agents in said containers, on the basis of said cooling requirements. The program P can be stored in an executable manner or in a compressed manner in a memory 460 and / or in a read / write memory 450. When it is described that the data processing unit 410 performs a certain function, it is to be understood that the data processing unit 410 performs a certain part of the program which is stored in the memory 460, or a certain part of the program which is stored in the read / write memory 450. The data processing device 410 may communicate with a data port 499 via a data bus 415. The non-volatile memory 420 is intended for communication with the data processing unit 410 via a data bus 412. The separate memory 460 is intended to communicate with the data processing unit 410 via a data bus 411. the data processing unit 410 via a data bus 414. To the data port 499, e.g. links 201, 221, 231, 251, 261, 281 and 291 are connected (see Figure 2). The read / write memory 450 is arranged to communicate with When data is received on the data port 499, it is temporarily stored in the second memory part 440. When the received input data has been temporarily stored, the data processing unit 410 is prepared to perform code execution in a manner described above. According to one embodiment, signals received at the data port 499 comprise information about a prevailing temperature of said reducing agent in said container. According to one embodiment, signals received at the data port 499 comprise information about a prevailing temperature of said reducing agent in said dosing unit. The received signals on the data port 499 can be used by the device 400 to determine a cooling need of the dosing unit 250, and to select a limit level for reducing agent in said container 205, on the basis of said cooling need. Parts of the methods described herein may be performed by the device 400 by means of the data processing unit 410 running the program stored in the memory 460 or the read / write memory 450. When the device 400 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 in SCR systems comprising a dosing unit (250) for supplying reducing agent to an exhaust duct (240) for exhaust gas purification and a container for reducing agent, comprising the step of: - selecting (s310; s340) a limit level for reducing agent in said container ( 205) for reducing agents characterized by the steps of: - determining (s320) a cooling requirement of said dosing unit (250), and - selecting (s340) a limit level for reducing agents in said container (205), on the basis of said cooling requirements. [2] The method of claim 1, comprising the steps of: - determining a prevailing temperature of said reducing agent in said container (205); and - determining (s320) said cooling demand of said dosage unit (250) on the basis of said determined prevailing temperature of said reducing agent in said container (205). [3] A method according to claim 1 or 2, comprising the steps of: - determining an prevailing temperature of said reducing agent in said dosing unit (250): and - determining (s320) said cooling demand of said dosing unit (250) on the basis of said determined prevailing temperature of said reducing agent in said dosage unit (250). [4] A method according to any one of claims 1-3, comprising the step of: - determining (s320) said cooling demand of said dosing unit (250) on the basis of at least one determined parameter selected from the group including: in said container (205), operating power of an engine (150) of said SCR system, prevailing temperature prevailing ambient temperature prevailing of exhaust gases in said exhaust duct (240), and accumulated metered amount of reducing agent. [5] A method according to any one of the preceding claims, comprising the step of: - selecting (s340) said limit level for reducing agent in said container (205) within a predetermined range. [6] A method according to any one of the preceding claims, comprising the step of: - continuously determining (s320) a cooling demand of said dosing unit (250), and - selecting (s340) an updated limit level for reducing agents in said container (205), on the basis of said continuously determined cooling needs. [7] A method according to any one of the preceding claims, comprising the step of: - selecting (S310) an initial limit level for reducing agent in a container (205) for reducing agent, based on the performance of said SCR system and / or an imaginary future operation of SCR system, average load of one motor (150) of the SCR system and estimated maximum load of the motor (150) of the SCR system. as regards e.g. appreciated [8] A method according to any one of the preceding claims, wherein said reducing agent is a urea-based reducing agent. [9] A method according to any one of the preceding claims, wherein said limit level for reducing agent in said container (205) corresponds to a minimum desired volume of reducing agent in said container (205). [10] Apparatus of SCR systems comprising a dosing unit (250) for supplying reducing agent to an exhaust duct (240) for exhaust purification and a container for reducing agent, comprising: - means (200: 210; 400) for selecting a limit level for reducing agent in said container (205) for reducing agent, characterized by: - means (200; 210; 400) for determining a cooling need of said dosing unit (250), and - means (200; 210; 400) for select a limit level for reducing agent in said container (205), based on said cooling demand. [11] The device of claim 10, comprising: - means (290) for determining a reducing agent in said container (205); and prevailing temperature of said means (200; 210; 400) for determining said cooling demand of said dosage unit (250) on the basis of said determined prevailing temperature of said reducing agent in said container (205). [12] An apparatus according to claim 10 or 11, comprising: - means (220) for determining a reducing agent in said dosage unit (250); and prevailing temperature of said means (200; 210; 400) for determining said cooling demand of said dosage unit (250) on the basis of said determined prevailing temperature of said reducing agent in said dosage unit (250). [13] An apparatus according to any one of claims 10 to 12, comprising: - means (200; 210; 400) for determining said cooling demand of said dosing unit (250) on the basis of at least one determined parameter selected from the group comprising: prevailing ambient temperature of said container (205), prevailing operating power of an engine (150) of said SCR system, prevailing temperature of exhaust gases in said exhaust duct (240), and accumulated dosed amount of reducing agent. [14] Device according to any one of claims 10-13, comprising: - means (200; 210; 400) for selecting said limit level for reducing agent in said container (205) within a predetermined range. 10 15 20 25 30 26 [15] Device according to any one of claims 10-14, comprising: - means (200; 210; 400) for continuously determining a cooling need of said dosing unit (250), and - means (200; 210; 400) for selecting an updated limit level for reducing agents in said containers (205), on the basis of said continuously determined cooling requirements. [16] Device according to any one of claims 10-15, comprising: - means (200; 210; 400) for selecting an initial limit level for reducing agent in a container (205) for reducing agent, based on the performance of said SCR system and / or an imaginary future operation of the SCR system, in terms of e.g. estimated average load of one motor (150) of the SCR system and estimated maximum load of the motor (150) of the SCR system. [17] Device according to any one of claims 10-16, wherein said reducing agent is a urea-based reducing agent. [18] The device of any of claims 10-17, wherein said limit level of reducing agent in said container corresponds to a minimum desired volume of reducing agent in said container (205). [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 SCR systems comprising a dosing unit (205) for supplying reducing agent to an exhaust duct (240) for exhaust purification and a container for reducing agent, said computer program (P) comprising program code stored on a computer readable , medium for causing an electronic control unit (200; 400) or another computer (210; 400) connected to the electronic control unit (200; 400) to perform the steps according to any one 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; 400) or another computer (210; 400) connected to the electronic control unit (200; 400).
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同族专利:
公开号 | 公开日 EP2582940A1|2013-04-24| EP2582940B1|2017-08-30| BR112012031782A2|2016-11-01| JP2013531167A|2013-08-01| WO2011162684A1|2011-12-29| SE534974C2|2012-03-06| RU2013102498A|2014-07-27| RU2530679C2|2014-10-10| US20130133310A1|2013-05-30| CN102959193A|2013-03-06| EP2582940A4|2016-06-01| US9212581B2|2015-12-15|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US5522218A|1994-08-23|1996-06-04|Caterpillar Inc.|Combustion exhaust purification system and method| US6063350A|1997-04-02|2000-05-16|Clean Diesel Technologies, Inc.|Reducing nox emissions from an engine by temperature-controlled urea injection for selective catalytic reduction| US6279603B1|1998-10-01|2001-08-28|Ambac International|Fluid-cooled injector| US6814303B2|2002-04-03|2004-11-09|Cleaire Advanced Emission Controls|Fluid-cooled mount for an injector| US6941746B2|2002-11-21|2005-09-13|Combustion Components Associates, Inc.|Mobile diesel selective catalytic reduction systems and methods| JP3732493B2|2003-10-02|2006-01-05|日産ディーゼル工業株式会社|Engine exhaust purification system| US7776265B2|2004-03-18|2010-08-17|Cummins Filtration Ip, Inc.|System for diagnosing reagent solution quality| US7021047B2|2004-07-23|2006-04-04|General Motors Corporation|Diesel exhaust aftertreatment device regeneration system| DE102004050022B4|2004-10-13|2012-01-05|L'orange Gmbh|Device for cooling a nozzle for the metered injection of a reducing agent into the exhaust gas tract of an internal combustion engine| DE102005002318A1|2005-01-17|2006-07-27|Robert Bosch Gmbh|Exhaust gas aftertreatment process and device for this purpose| US8499739B2|2006-08-31|2013-08-06|Caterpillar Inc.|Injector having tangentially oriented purge line| JP4706660B2|2007-04-10|2011-06-22|株式会社デンソー|Reducing agent supply device| US8056326B2|2007-05-31|2011-11-15|Caterpillar Inc.|Regeneration device having cooled injection housing| US8096112B2|2007-09-28|2012-01-17|Caterpillar Inc.|Exhaust after-treatment system having a secondary tank| JP5001793B2|2007-11-13|2012-08-15|三菱ふそうトラック・バス株式会社|Exhaust purification device| JP5118460B2|2007-12-10|2013-01-16|三菱ふそうトラック・バス株式会社|Exhaust purification device|JP5609924B2|2012-07-02|2014-10-22|トヨタ自動車株式会社|Exhaust gas purification device for internal combustion engine| DE102016210262A1|2016-06-10|2017-12-14|Robert Bosch Gmbh|A method of emptying a reductant delivery system of an SCR catalyst| US11003804B2|2017-12-22|2021-05-11|Symbol Technologies, Llc|Container loading/unloading time estimation| CN112145261B|2020-08-05|2021-12-07|中船澄西船舶修造有限公司|Marine low-temperature self-cleaning urea cabin|
法律状态:
2022-01-25| NUG| Patent has lapsed|
优先权:
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申请号 | 申请日 | 专利标题 SE1050653A|SE534974C2|2010-06-21|2010-06-21|Method and apparatus for determining the minimum level of a reducing agent container in an SCR system based on the cooling needs of a dosing unit|SE1050653A| SE534974C2|2010-06-21|2010-06-21|Method and apparatus for determining the minimum level of a reducing agent container in an SCR system based on the cooling needs of a dosing unit| RU2013102498/06A| RU2530679C2|2010-06-21|2011-06-17|Method and device relevant to batchers cooling in scr systems| US13/704,724| US9212581B2|2010-06-21|2011-06-17|Method and device pertaining to cooling of dosing units of SCR systems| BR112012031782A| BR112012031782A2|2010-06-21|2011-06-17|method and device related to the cooling of metering units of scr systems| JP2013516529A| JP2013531167A|2010-06-21|2011-06-17|Method and device relating to cooling of the input unit of an SCR system| CN201180030669XA| CN102959193A|2010-06-21|2011-06-17|Method and device pertaining to cooling of dosing units of SCR systems| PCT/SE2011/050773| WO2011162684A1|2010-06-21|2011-06-17|Method and device pertaining to cooling of dosing units of scr systems| EP11798454.2A| EP2582940B1|2010-06-21|2011-06-17|Method and device pertaining to cooling of dosing units of scr systems| 相关专利
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