专利摘要:
SUMMARY The invention relates to a method in an SCR system for purifying exhaust gases from an engine (150), comprising a dosing unit (250) for supplying a reducing agent to an exhaust duct (240), comprising stepwise determining (s340) whether an undesired temperature level of the saw dosing unit (250) is present. The method also comprises the step of, if said undesired temperature level is determined to exist, removing (s360) reducing agent from said dosing unit (250) by adding said reducing agent to said exhaust duct (240). 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 of an SCR system and a motor vehicle (100) equipped with the device. Figure 2 for publication
公开号:SE1050651A1
申请号:SE1050651
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:

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.
During operation of the SCR system, thermal energy is stored in the exhaust system. This thermal energy can be transferred to e.g. the dosage unit.
During certain operating cases, where a cooling flow for the dosing unit is insufficient, there is a risk that the dosing unit is functionally degraded, overheated and permanently damaged, or even completely breaks down. Even at temperatures that are not critical for hardware in the SCR system, there is a risk that the reductant therein is adversely affected by excessive temperatures, whereby crystal formation of the reductant can be caused by clogging of e.g. dosage unit as a result.
WO 2009/020541 describes a system for discharging a reducing substance from an injection system. The system has a heater connected to an injector, where the purpose of the heater e.g. is to vaporize the substance from the injector to avoid blockages in the injection system. However, the heater is space consuming and its operation is associated with costs regarding development, installation, monitoring during operation and maintenance.
WO 2008/006840 describes a system for storing and supplying an additive in an exhaust system.
There is a need to improve the current SCR system 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.
An object of the present invention is to provide a new and advantageous method for improving the performance of an SCR system, where a cooling flow of a dosing unit is missing or insufficient.
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, where a cooling flow of a dosing unit is missing or insufficient.
An object of the present invention is to provide a method in an SCR system, which method provides a reduced risk of undesired functional degradation of components of the SCR system and / or a reduced risk of clogging of components, e.g. 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 for exhaust gas purification, according to claim 1.
According to one aspect of the invention, there is provided a method of an SCR system for purifying exhaust gases from an engine, comprising a metering unit for supplying a reducing agent to an exhaust duct, comprising the step of determining whether an undesired temperature level of said metering unit (250) is present. The method also comprises the step of, if said undesired temperature level is determined to exist, removing reducing agents from said dosing unit by adding said reducing agents to said exhaust duct.
This reduces the risk of formation of by-products of the reducing agent in the lead to operational disturbances, such as e.g. error codes in control system. These by-products would be the dosage unit. These by-products could otherwise also mean that emissions of the SCR system are not reduced to the desired extent.
Said determination of whether said undesired temperature level is present can be performed after switching off an exhaust gas flow. In operating cases where the motor of the SCR system is switched off after operation with a high power output, an evacuation of heated reducing agent in the dosing unit can contribute to lowering an undesirably high temperature of the dosing unit.
The method may comprise the step of continuously cooling said dosage unit by means of a flow of said reducing agent. By combining continuous cooling of the dosing unit by means of said reducing agent and dosing of heated reducing agent of the dosing unit into the exhaust duct, positive synergy effects are obtained, which lead to improved cooling of the dosing unit, especially after the engine of the SCR system has been switched off.
The method may comprise the step of intermittently removing reducing agents from said dosing unit by adding said reducing agents to said exhaust duct. By intermittently removing reducing agents, a heat transfer between the dosage unit and the reducing agent can be allowed under controlled conditions. In this way, an energy value of the reductant can be increased. At appropriate times, at least a portion of the heated reductant of the metering unit may be metered into the exhaust duct of the SCR system.
The amount of reducing agent removed should be so limited that a not too large amount of reducing agent is supplied to the exhaust duct, in particular after switching off an exhaust feed at the exhaust duct. At a start-up of the SCR system, the exhaust duct will be heated and help to vaporize the amount of reducing agent removed for use with the SCR catalyst in a conventional manner.
Said undesired temperature level may be within a predetermined range, e.g. within 80-130 degrees Celsius. Said undesired temperature level can be selected as a reducing agent. The appropriate value depending on the characteristics of the process in question may include the step of continuously determining a prevailing temperature of the dosing unit, in order to continuously determine whether a reliable process is hereby performed in an SCR system, where calculations of undesired temperature level of a dosing unit are present. of the amount to be removed can be performed on relevant input data.
The method may include the step of calculating an amount of reducing agent to be removed on the basis of a prevailing temperature of the dosage unit.
In this case, an optimized amount of a reducing agent can be removed from the dosing unit into the exhaust duct. The calculated amount of reducing agent can be dosed at a set appropriate time. The calculated amount of reducing agent can be dosed intermittently as appropriate.
The method may comprise the step of removing a predetermined amount of reducing agent from said dosage unit. The predetermined amount of reducing agent can be substantially any available heated reducing agent at the dosage unit. This step has the advantage that a less computationally heavy variant is provided.
The method may comprise the step of removing reducing agent from said dosage unit by means of existing pressurization of the reducing agent in the dosage unit. Said existing pressurization can be effected by a pump of the SCR system. According to an alternative embodiment, said reducing agent can be removed by means of a self-pressure of the SCR system.
Said reducing agent may be a urea-based reducing agent, such as e.g. AdBlue.
According to one aspect of the invention, there is provided an apparatus of an SCR system for purifying exhaust gases from an engine, comprising a dosing unit for supplying a reducing agent to an exhaust duct, comprising means for determining whether an undesired temperature level of a dosing unit is present, and means for that, if said undesired temperature level of said dosing unit is determined to exist, remove reducing agents from said dosing unit by adding said reducing agents to said exhaust duct.
Said determination of whether said undesired temperature level exists can be performed after shutting off an exhaust de fate.
The device may comprise means for continuously cooling said dosage unit by means of a flow of said reducing agent.
The device may comprise means for intermittently removing reducing agent from said dosing unit by supplying said reducing agent to said exhaust duct.
The device may comprise means for continuously determining a prevailing temperature of a dosing unit, for continuously determining whether an undesired temperature level of a dosing unit is present.
The device may comprise means for calculating an amount of reducing agent to be removed on the basis of a prevailing temperature of the dosing unit.
The device may comprise means for removing a predetermined amount of reducing agent from said dosage unit.
The device may comprise means for removing reducing agents from said by means of the existing dosing unit. dosing unit pressurization of the reducing agent for the above purposes is also achieved with a motor vehicle incorporating the features of the device of an SCR system described herein.
The motor vehicle can be a truck, bus or car.
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 1-10.
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 1-10, when said computer program is run on an electronic control unit or another computer connected to the electronic control unit. The procedure is easy to implement in existing motor vehicles. Software in SCR systems for exhaust gas purification according to the invention can be installed in a control unit of the vehicle in the manufacture of the same. 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 method of SCR exhaust purification system can 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 Required hardware is already present in the vehicle today. The invention sensors or components need to be installed in the vehicle. thus provides a cost-effective solution to the above problems.
Software that includes program code for SCR exhaust gas cleaning systems can be easily updated or replaced. Furthermore, different parts of the software that include program code in SCR systems for exhaust gas purification can be replaced independently advantageously from one of the other. This modular configuration is a maintenance perspective. 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 illustrates a computer, Figure 4 schematically 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 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 an SCR system and the innovative device of a device according to an aspect of the invention are well suited for platforms involving 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.
IO The innovations of an SCR system and the innovative device of a 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 innovation of an SCR system and the innovative device of a 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 innovation of an SCR system and the innovative device of a 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 pipe can be a pipe of any dimension. 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 the necessary adaptations, e.g. regarding temperature level where functional degradation for a given reductant 11 is initiated, in control algorithms for executing software code in accordance with the innovative method.
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. 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 a 100.
The exhaust duct 240 is arranged to direct exhaust gases from the engine 150 to an exhaust duct 240 of an exhaust system (not shown) of the vehicle surrounding 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. According to a variant, the amount of reductant supplied to the exhaust system is intended to be used in a conventional manner in the SCR catalyst in order to reduce the amount of undesired emissions in a known manner. According to one aspect of the invention, where applicable, the metered amount of reductant is not primarily intended for use directly in the SCR catalyst, but for entraining thermal energy from the metering unit 250 to the exhaust duct 240.
The dosing unit 250 is arranged at the exhaust duct 240 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. The reductant present in the dosing unit 250 is also heated.
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 degrees Celsius. the exhaust duct 240, the muffler and the SCR catalyst of the vehicle 100 temperature value, such as e.g. Since e.g. If this temperature value exceeds, there is a risk that the dosing unit may overheat during operation of the vehicle or after operation of the vehicle if cooling is not 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, Celsius can possibly crystallize at slightly higher 13 temperatures and in the long run possibly cause 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 dosing unit 250 is cooled by a flow of the reductant as it is pumped through the dosing unit 250 from the pump 230 to the container 205. Cooling of the dosing unit, by means of a return flow of the third line, can also be used after the vehicle has been switched off and the exhaust flow in the exhaust duct has ceased. If this cooling proves to be insufficient for the dosing unit 250, the innovative method can be advantageously used, including the step of evacuating at least a part of reducing agent heated in the dosing unit 250 to the exhaust duct 240.
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 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 dosing unit 250.
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 the prevailing temperature T2 of the exhaust duct 240.
The first control unit 200 is arranged to calculate a prevailing temperature 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 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. According to an example, the first control unit 200 is arranged to control 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 that, on the basis of the signals received from the first temperature sensor 220 and / or the second temperature sensor 280, if necessary, i.e. in determining that an undesired temperature level of said dosage unit is present, remove reducing agents from said dosage unit by adding said reducing agents to said exhaust duct, in accordance with one aspect of the innovative method.
In particular, according to an embodiment, the first control unit 200 is arranged to, on the basis of the signals received from the first temperature sensor 220 and / or the second temperature sensor 280, calculate, if necessary, an amount of reducing agent to be removed on the basis of a prevailing temperature of the dosing unit. in accordance with one 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. determining whether an undesired temperature level of the dosing unit 250 is present, and if said undesired temperature level is present, dosing an appropriate amount of reducing agent of the dosing unit into the exhaust duct 240. The innovative procedure may be performed by the first control unit 200 or the second control unit 210, or by both the the first control unit 200 and the second control unit 210.
Figure 3a schematically illustrates a flow chart of a method of an SCR system for purifying exhaust gases from an engine, comprising a dosing unit for supplying a reducing agent to an exhaust duct, according to first method step s301. Step s301 includes the steps of determining whether an embodiment of the invention. The method comprises an undesired temperature level of said dosing unit is present, and if said undesired temperature level is determined to be present, removing reducing agents from said dosing unit by adding said reducing agents to said exhaust duct. After step s301, the process is terminated.
Figure 3b schematically illustrates a flow chart of a process in an SCR system for purifying exhaust gases from the engine 150, comprising the dosing unit 250 for supplying a reducing agent to the exhaust duct 240, according to an embodiment of the invention. The method comprises a first method step s310. The process step s310 includes the step of determining a prevailing temperature of the dosing unit 250. This is done by directly measuring the prevailing temperature at the dosing unit 250. In process step s310 a first temperature value T1 representing a saving temperature of the dosing unit 250 is measured.
Method step s320 includes the step of determining an estimated prevailing temperature of the dosing unit 250 indirectly. This is done by measuring the temperature at a component other than the dosing unit 250 of the SCR system. In process step s310, a second temperature value T2 of a component other than the dosing unit 250 is measured. By means of the measured temperature T2, a first estimated prevailing temperature T1est of the dosing unit 250 can be determined. estimated prevailing temperature T2est of the dosing unit 250 is determined According to an alternative, a second can be (calculated) by means of a calculation model which has parameters other than temperature of a component of the SCR system as input value. Such an input parameter can e.g. be a prevailing load of the motor 150. It should be noted that steps s310 and s320 can be performed substantially simultaneously, or in reverse order. It should also be pointed out that according to one embodiment it is possible to use only the measured temperature T1 of the dosing unit 250 to determine a maximum temperature value Tmax as below. In some cases it is advantageous to use both the measured temperature T1 and at least one of the estimated prevailing temperatures T1est and T2est to determine a maximum temperature value Tmax as below as a more robust process is thereby obtained. After the process step s320, a subsequent process step s330 is performed.
Process step s330 includes the step of comparing the determined first temperature T1 and at least one of the estimated prevailing temperatures T1est and T2est of the dosing unit 250. After the process step s330, a subsequent process step s340 is performed. The process step s340 comprises the step of selecting the highest value of the values on the basis of a result of said comparison between the determined first temperature T1 and at least one of the estimated prevailing temperatures T1est and T2est. This highest temperature value is also called Tmax.
Method step s340 also includes the step of determining whether an undesired temperature level of the dosage unit is present, adding reducing agent therein. This can be done by a comparison with a limit value the dosing unit 250 is arranged that to an exhaust duct Tth, such as a predetermined temperature value, e.g. 70 or 100 degrees Celsius, depending on the type of reductant used in the SCR system.
If Tmax is greater than or equal to Tth, it can be determined that an undesired temperature level of the dosage unit is present. If Tmax is less than Tth, it can be determined that an undesired temperature level of the dosage unit does not exist. After the process step s340, a subsequent process step s350 is performed.
According to an alternative embodiment, as described above, it can be determined whether an undesired temperature level of the dosing unit 250 exists on the basis of only the measured temperature T1 of the dosing unit. According to this embodiment, a less complex method is provided, according to an aspect of the invention.
The process step s350 includes the step of, on the basis of the selected value Tmax, calculating an amount of reducing agent to be removed from the dosing unit 250. This can be performed by means of stored calculation models. In this case, a suitable dosage configuration can be determined, e.g. regarding the amount of reducing agent to be removed at the respective different times. After the process step s350, a subsequent process step s360 is performed. The process step s360 comprises the step of, on the basis of the selected value Tmax, taking a measure for influencing the temperature of the dosing unit 250. In this case, a fixed amount of reducing agent is removed at a suitable time. It appears here that a number of different amounts of reducing agent can be dosed at the respective fixed time. After the procedure step s360, 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 the presence of an undesired temperature level in a dosing unit for supplying reducing agent to an exhaust duct. The program P comprises routines for, when the presence of an undesired temperature level of the dosing unit 250 is determined, removing reducing agents from the dosing unit 250 by supplying said reducing agents to the exhaust duct 240, according to an aspect of the innovative method. The program P includes routines for continuously determining a prevailing temperature of the dosing unit, for continuously determining whether an undesired temperature level of a dosing unit is present. Program P includes routines for calculating an amount of reducing agent to be removed based on a prevailing temperature of the dosage unit. The program P comprises routines for continuously cooling the dosing unit 250 by means of a flow of said reducing agent. The program P comprises routines for intermittently removing reducing agents from said dosing unit by supplying said reducing agents to said exhaust duct.
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 and 281 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 include information about a first measured temperature T1 of the dosing unit 250. According to one embodiment, signals received at the data port 499 include information about a second measured temperature T2 of a component of the SCR system in addition to the dosing unit 250. The received signals at the data port 499 can be used by the device 400 to remove, where applicable, reducing agents from the dosing unit 250 of the SCR system.
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 (23)
[1]
A method of an SCR system for purifying exhaust gases from an engine (150), comprising a dosing unit (250) for supplying a reducing agent to an exhaust duct (240), comprising the step of: - determining (s340) whether an undesired temperature level in said dosing unit (250), characterized by the step of: - if said undesired temperature level is determined to exist, remove (s360) reducing agent from said dosing unit (250) by supplying said reducing agent to said exhaust duct (240).
[2]
A method according to claim 1, wherein said determining whether said undesired temperature level is present is performed after shutting off an exhaust gas fl.
[3]
A method according to claim 1 or 2, comprising the step of continuously cooling said dosage unit (250) by means of a flow of said reducing agent.
[4]
A method according to any one of claims 1-3, comprising the step of intermittently removing (s360) reducing agent from said dosing unit (250) by supplying said reducing agent to said exhaust duct (240).
[5]
A method according to any one of the preceding claims, wherein said undesired temperature level is within a predetermined range, e.g. within 80-130 degrees Celsius.
[6]
A method according to any one of the preceding claims, comprising the step of: - continuously determining a prevailing temperature of the dosing unit (250), to continuously determine whether an undesired temperature level of the dosing unit (250) is present. 10 15 20 25 30 22
[7]
A method according to any one of the preceding claims, comprising the step of: - calculating (s350) an amount of reducing agent to be removed on the basis of a prevailing temperature of the dosing unit (250).
[8]
A method according to any one of the preceding claims, comprising the step of: - removing (s360) a predetermined amount of reducing agent from said dosing unit (250) to said exhaust duct.
[9]
A method according to any one of the preceding claims, comprising the step of: - removing (s360) reducing agent from said dosing unit by means of existing pressurization of the reducing agent in the dosing unit (250).
[10]
10. A reducing agent process is a urea-based reducing agent. any of the preceding claims, wherein said
[11]
An apparatus of an SCR system for purifying exhaust gases from an engine (150), comprising a dosing unit (250) for supplying a reducing agent to an exhaust duct (240), comprising: - means (200; 210; 400) for determining whether there is an undesired temperature level of a dosing unit (250), characterized by: - means (200; 210; 400) for removing said reducing agent from said dosing unit (250) if said undesired temperature level of said dosing unit (250) is present by to supply said reducing agent to said exhaust duct (240).
[12]
The device of claim 11, wherein said determining whether said undesired temperature level is present is performed after shutting off an exhaust fl fate.
[13]
An apparatus according to claim 11 or 12, comprising: means (230) for continuously cooling said dosage unit (250) by means of a flow of said reducing agent.
[14]
Device according to any one of claims 11-13, comprising: - means (200; 210; 400) for intermittently removing reducing agent from said dosing unit (250) by supplying said reducing agent to said exhaust duct (240). 11-14, where the temperature level is within a predetermined range, e.g. within 80-130 degrees
[15]
Device according to any one of claims undesired Celsius.
[16]
Device according to any one of claims 11-15, comprising: - means (200; 210; 400) for continuously determining a prevailing temperature of the dosing unit (250), for continuously determining the presence of an undesired temperature level of the dosing unit (250).
[17]
Device according to any one of claims 11-16, comprising: - means (200; 210; 400) for calculating an amount of reducing agent to be removed on the basis of a prevailing temperature of the dosing unit (250).
[18]
Device according to any one of claims 11-17, comprising: - means (200; 210; 400) for removing a predetermined amount of reducing agent from said dosing unit (250).
[19]
Device according to any one of claims 11-18, comprising: - means (200; 210; 400) for removing reducing agent from said reducing agent in dosing unit by means of existing pressurization of the dosing unit (250).
[20]
Motor vehicle (100: 110) comprising a device according to any one of claims 11-19. 10 15 24
[21]
A motor vehicle (100; 110) according to claim 20, wherein the motor vehicle is something of a truck, bus or passenger car.
[22]
A computer program (P) in an SCR exhaust purification system, said computer program (P) comprising program code stored on a computer readable medium to cause 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 1-10.
[23]
A computer program product comprising a program code stored on a computer readable medium for performing the method steps of any of claims 1-10, when said computer program is run on an electronic control unit (200; 400) or another computer (210; 400) connected to it (200; 400). electronic control unit
类似技术:
公开号 | 公开日 | 专利标题
SE1050642A1|2011-12-22|Device including an SCR system and a method of an SCR system
EP2582946B1|2018-10-31|Method pertaining to air removal from a dosing system at an scr system and an scr system
SE1050648A1|2011-12-22|Method of SCR system and device of SCR system
SE1250768A1|2014-01-06|SCR system and procedure of an SCR system
SE1050651A1|2011-12-22|Method of SCR system and device of SCR system
SE1050639A1|2011-12-22|Device including an SCR system and a method of an SCR system
SE1050646A1|2011-12-22|Process of an HC dosing system and an HC dosing system
SE1050024A1|2011-07-15|Apparatus and method for heating a reductant in a SCR system of a motor vehicle
SE538382C2|2016-06-07|Method of heating a reducing agent in an SCR system and determining suitability for circulation of said reducing agent in said SCR system
SE1150789A1|2013-03-01|A method of detecting reducing agent crystals in an SCR system and corresponding SCR system
SE1050653A1|2011-12-22|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
SE1050647A1|2011-12-22|Device comprising an HC dosing system and a method of an HC dosing system
SE536920C2|2014-10-28|SCR system for exhaust gas purification and method for cooling the metering unit in such an SCR system
SE1050643A1|2011-12-22|Device comprising an HC dosing system and a method of an HC dosing system
SE1050649A1|2011-12-22|Method of HC dosing system and device of HC dosing system
SE1250265A1|2013-09-21|Procedure for an SCR system and an SCR system
SE1050652A1|2011-12-22|Method of HC dosing system and device of HC dosing system
SE1050644A1|2011-12-22|Device comprising an HC dosing system and a method of an HC dosing system
同族专利:
公开号 | 公开日
CN103003540A|2013-03-27|
EP2582945A4|2014-12-17|
US9399940B2|2016-07-26|
JP2013529750A|2013-07-22|
RU2013102526A|2014-07-27|
BR112012032547A2|2016-11-22|
US20130111883A1|2013-05-09|
EP2582945B1|2019-06-12|
SE536318C2|2013-08-20|
WO2011162699A1|2011-12-29|
EP2582945A1|2013-04-24|
CN103003540B|2015-08-12|
RU2545264C2|2015-03-27|
引用文献:
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JP3718208B2|2003-10-02|2005-11-24|日産ディーゼル工業株式会社|Engine exhaust purification system|
JP4240025B2|2005-09-02|2009-03-18|トヨタ自動車株式会社|Exhaust purification equipment|
CN101506482A|2006-07-13|2009-08-12|因勒纪汽车系统研究公司|System and process for storing an additive and injecting it into the exhaust gases of an engine|
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JP4906525B2|2007-01-26|2012-03-28|ボッシュ株式会社|Clogging determination device for reducing agent injection valve and clogging determination method for reducing agent injection valve|
US8006482B2|2007-03-02|2011-08-30|Caterpillar Inc.|Method of purging fluid injector by heating|
US8484947B2|2007-03-02|2013-07-16|Caterpillar Inc.|Fluid injector having purge heater|
US7958721B2|2007-06-29|2011-06-14|Caterpillar Inc.|Regeneration system having integral purge and ignition device|
US8281570B2|2007-08-09|2012-10-09|Caterpillar Inc.|Reducing agent injector having purge heater|
JP5139765B2|2007-10-12|2013-02-06|ボッシュ株式会社|Control device and control method for reducing agent supply system|
JP4453739B2|2007-10-24|2010-04-21|トヨタ自動車株式会社|Control method of addition valve|
WO2010003424A1|2008-07-07|2010-01-14|Grundfos Nonox A/S|Dosing system for use in an exhaust system of a combustion engine|
JP4986973B2|2008-10-23|2012-07-25|三菱ふそうトラック・バス株式会社|Exhaust purification device|
US8291926B2|2009-02-20|2012-10-23|Caterpillar Inc.|Reductant dosing system having anti-aeration device|
CN104806328B|2009-06-18|2017-06-16|康明斯知识产权公司|For the equipment, system and method for reductant line heating control|CN107250499B|2015-03-06|2019-12-13|康明斯排放处理公司|System and method for purging an exhaust reductant delivery system|
US9670818B2|2015-08-07|2017-06-06|Caterpillar Inc.|Air-assist dosing system having priming detection|
US9664083B2|2015-08-14|2017-05-30|Cummins Emission Solutions Inc.|Virtual reductant level sensor|
US20160282167A1|2016-06-08|2016-09-29|Caterpillar Inc.|System and method of operator indication for filling reductant tank|
RU172263U1|2016-09-20|2017-07-03|Общество с ограниченной ответственностью "Газпром добыча Уренгой"|Wiring "pump urea dispenser - electronic engine control unit" selective catalytic recovery of the vehicle|
法律状态:
2022-01-25| NUG| Patent has lapsed|
优先权:
申请号 | 申请日 | 专利标题
SE1050651A|SE536318C2|2010-06-21|2010-06-21|Method and apparatus for removing reducing agent from a metering unit of an SCR system|SE1050651A| SE536318C2|2010-06-21|2010-06-21|Method and apparatus for removing reducing agent from a metering unit of an SCR system|
PCT/SE2011/050797| WO2011162699A1|2010-06-21|2011-06-20|Method and device pertaining to dosing unit of scr system|
CN201180035558.8A| CN103003540B|2010-06-21|2011-06-20|The method and apparatus relevant with the feeder unit of SCR system|
BR112012032547A| BR112012032547A2|2010-06-21|2011-06-20|method and device related to the scr system dosing unit|
JP2013516541A| JP2013529750A|2010-06-21|2011-06-20|Method and device relating to the input unit of an SCR system|
EP11798469.0A| EP2582945B1|2010-06-21|2011-06-20|Method and device pertaining to dosing unit of scr system|
RU2013102526/06A| RU2545264C2|2010-06-21|2011-06-20|Process and device related with scr system batcher|
US13/805,024| US9399940B2|2010-06-21|2011-06-20|Method and device pertaining to dosing unit of SCR system|
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