Method for Introducing Heat Into at Least One Component of an Exhaust-Gas Aftertreatment Device, Software and Open-Loop or Closed-Loop Control Device

Abstract

A method for introducing heat into at least one component of an exhaust-gas aftertreatment device of an internal combustion engine (15). The method involves at least partially reacting a partial flow of an exhaust-gas flow with fuel in a heated catalyst (2) and then feeding back the resulting product to the exhaust-gas flow, The amount of fuel fed to the heated catalyst and/or the partial flow fed to the heated catalyst is controlled, by open-loop or closed-loop control, in accordance with the exhaust-gas temperature upstream and/or downstream of the component. The amount of fuel fed to the heated catalyst and/or the partial flow fed to the heated catalyst is determined by means of at least one heated-catalyst characteristic map. A computer readable medium stores a signal sequence representing data suitable for transmission by means of a computer network, to an open-loop or closed-loop control device to carry out the above-described method.

Claims

1. Method for introducing heat into at least one component (11, 12, 13) of an exhaust-gas aftertreatment device (1) of an internal combustion engine (15), in which method a partial flow of an exhaust-gas flow is at least partially reacted with fuel in a heated catalyst (2) and fed back to the exhaust-gas flow, characterized in that the amount of fuel fed to the heated catalyst (2) and/or the partial flow fed to the heated catalyst (2) is controlled, by open-loop or closed-loop control, in accordance with the exhaust-gas temperature upstream and/or downstream of the component (11, 12, 13), and the amount of fuel fed to the heated catalyst (2) and/or the partial flow fed to the heated catalyst (2) being determined by means of at least one heated-catalyst characteristic map (35).

2. Method according to claim 1, characterized in that the exhaust-gas temperature upstream and/or downstream of the component (11, 12, 13) is detected using at least one temperature sensor (111, 112, 132).

3. Method according to claim 1, characterized in that the exhaust-gas temperature upstream and/or downstream of the component (11, 12, 13) is determined from an operating state of the internal combustion engine (15).

4. Method according to claim 3, characterized in that the operating state of the internal combustion engine is determined from currently applied characteristic map values or characteristic map ranges of an engine control unit (16).

5. Method according to claim 1, characterized in that the input variables (351) of the heated-catalyst characteristic map (35) are selected from the exhaust-gas mass flow of the internal combustion engine and/or the oxygen content of the raw exhaust gas of the internal combustion engine and/or at least one exhaust-gas temperature and/or a driving profile and/or a navigation destination and/or position data and/or the state of charge of at least one battery.

6. Method according to claim 5, characterized in that the exhaust-gas mass flow of the internal combustion engine (2) and/or the oxygen content of the raw exhaust gas of the internal combustion engine and/or at least one exhaust-gas temperature are determined by means of a first reference-controlled synthesizer.

7. Method according to claim 1, characterized in that the thermal power outputted by the heated catalyst (2) is determined from the fuel amount fed to the heated catalyst (2) and/or the partial flow fed to the heated catalyst (2) by means of a second reference-controlled synthesizer.

8. Method according to claim 1, characterized in that the heated catalyst (2) has at least a second operating state (52) in which the air ratio λ of the heated catalyst (2) is between about 0.75 and about 30 or between about 1.0 and about 10, and the heated catalyst (2) has at least a fourth operating state (54) in which the air ratio λ of the heated catalyst (2) is between about 0.05 and about 0.7.

9. Method according claim 1, characterized in that the partial flow is selected between about 3 kg/h and about 100 kg/h or between about 6 kg/h and about 80 kg/h.

10. Method according to claim 1, characterized in that the heated catalyst (2) contains at least one electrical heating device which, in a first operating state, is used to bring the heated catalyst (2) to an operating temperature at which supplied fuel can be at least partially reacted on the heated catalyst (2) and/or in that the heated catalyst (2) contains at least one electrical heating device which, in an eighth operating state, is used to heat a partial flow, fed to the heated catalyst (2), of the raw exhaust gas of the internal combustion engine (15).

11. Method according to claim 1, characterized in that the component (11, 12, 13) is selected from an oxidation catalyst (11) and/or a three-way catalyst and/or an SCR catalyst (13) and/or a particulate filter (12).

12. A non-transitory computer-readable medium having data stored thereon or signal sequence which represents data and is suitable for transmission by means of a computer network, wherein the data represents a computer program which carries out the method according to claim 1, when the computer program is executed on a microprocessor.

13. An open-loop or closed-loop control device (3), configured to carry out the method according to claim 1.

14. A method for introducing heat into an exhaust-gas aftertreatment device (1) connected to an internal combustion engine (15) which outputs an exhaust-gas flow, the exhaust-gas aftertreatment device (1) comprising one or more of an oxidation catalyst component (11), a particulate filter component (12) and an SCR system component (13), the method comprising: at least partially reacting a partial flow of the exhaust-gas flow with fuel in a heated catalyst (2) and feeding the reacted partial flow back into the exhaust-gas flow; controlling the amount of fuel fed to the heated catalyst (2) and/or the partial flow of exhaust-gas flow fed to the heated catalyst (2) based on an exhaust-gas temperature upstream and/or downstream of said one or more components (11, 12, 13) in accordance with an at least one heated-catalyst characteristic map (35).

15. The method according to claim 14, comprising determining the exhaust-gas temperature upstream and/or downstream of said one or more components (11, 12, 13) from an operating state of the internal combustion engine (15); wherein the operating state of the internal combustion engine is determined from currently applied characteristic map values or characteristic map ranges of an engine control unit (16).

16. The method according to claim 15, comprising: selecting input variables (351) of the heated-catalyst characteristic map (35) from one or more of: (i) exhaust-gas mass flow of the internal combustion engine; (ii) oxygen content of raw exhaust gas of the internal combustion engine; (iii) at least one exhaust-gas temperature; (iv) a driving profile; (v) a navigation destination; (vi) position data; and (vii) state of charge of at least one battery.

17. The method according to claim 16, characterized in that the exhaust-gas mass flow of the internal combustion engine (2) and/or the oxygen content of the raw exhaust gas of the internal combustion engine and/or at least one exhaust-gas temperature are determined by means of a first reference-controlled synthesizer.

18. The method according to claim 17, wherein: the partial flow is between kg/h and about 80 kg/h; and the heated catalyst (2) has a plurality of operating states, including at least: (i) a second operating state (52) in which an air ratio λ of the heated catalyst (2) is between 1.0 and about 10; (ii) and a fourth operating state (54) in which the air ratio λ of the heated catalyst (2) is between about 0.05 and about 0.7.

19. The method according to claim 18, wherein the heated catalyst (2) contains at least one electrical heating device which: in a first operating state, brings the heated catalyst (2) to an operating temperature at which supplied fuel can be at least partially reacted on the heated catalyst (2); and/or in an eighth operating state, heats the partial flow fed to the heated catalyst (2).

20. The method according to claim 19, comprising: determining an amount of thermal power outputted by the heated catalyst (2) from the fuel amount fed to the heated catalyst (2) and/or the partial flow fed to the heated catalyst (2) by means of a second reference-controlled synthesizer.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0029] The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.

[0030] The invention shall be explained in more detail below on the basis of drawings and exemplary embodiments without restricting the general concept of the invention. In the drawings:

[0031] FIG. 1 shows a first exemplary embodiment of an exhaust-gas aftertreatment device that can be used according to the invention.

[0032] FIG. 2 shows a second exemplary embodiment of an exhaust-gas aftertreatment device that can be used according to the invention.

[0033] FIG. 3 shows a block diagram of an open-loop or closed-loop control device according to the present invention.

[0034] FIG. 4 shows a structure chart of the method according to the invention in a first embodiment.

[0035] FIG. 5 shows a structure chart of the method according to the invention in a second embodiment.

[0036] FIGS. 6A, 6B and 6C show the use of the method according to the invention in a first exemplary embodiment.

[0037] FIGS. 7A, 7B and 7C show the use of the method according to the invention in a second exemplary embodiment.

DETAILED DESCRIPTION

[0038] A first exemplary embodiment of an exhaust-gas aftertreatment device 1 usable according to the invention is explained in more detail on the basis of FIG. 1. The exhaust-gas aftertreatment device 1 is connected to an internal combustion engine 15 via an exhaust-gas line. The internal combustion engine 15 can be a compression-ignition internal combustion engine or also a spark-ignition internal combustion engine of known design. The internal combustion engine 15 draws in ambient air and exothermically reacts it with supplied fuel. In the process, the internal combustion engine 15 outputs mechanical power. During the operation of the internal combustion engine 15, a raw exhaust gas is produced which, in addition to CO.sub.2 and H.sub.2O, can also contain pollutants, such as CHx, CO and/or NOx.

[0039] The raw exhaust gas is fed to the exhaust-gas aftertreatment device 1 by means of an exhaust-gas line. Optionally, a sensor system can be installed in the exhaust-gas line, for example a λ-probe for measuring the oxygen content of the raw exhaust gas. In the illustrated first exemplary embodiment, the exhaust-gas aftertreatment device 1 includes a first SCR system 13a and a second SCR system 13b. The SCR systems are each designed to catalytically reduce nitrogen oxides in the raw exhaust gas by adding a reducing agent. For this purpose, temperatures above 220° C., preferably above 250° C., are required.

[0040] A particulate filter 12 is located in the flow direction between the two SCR systems 13a and 13b. The particulate filter 12 is designed to retain fine dust or soot particles produced during the operation of the internal combustion engine 15. If the particulate filter 12 becomes clogged with increasing use, it can be temporarily heated to high temperatures under oxygen supply so that the embedded particles are oxidized and discharged in gaseous form.

[0041] In the first exemplary embodiment shown in FIG. 1, the first SCR system 13a and the particulate filter 12 are installed close to the engine so that the thermal energy of the raw exhaust gas is sufficient to bring these components up to operating temperature or keep them at operating temperature. The second SCR system 13b, on the other hand, is located further downstream in the exhaust-gas line so that it reaches the operating temperature only slowly and/or can cool below its operating temperature during the part-load operation of the internal combustion engine 15. Therefore, exhaust-gas purification is inadequate in part-load operation, which is referred to as emission slip in the sense of the present description.

[0042] In order to solve this problem, a heated catalyst 2 is located upstream of the second SCR system 13b. A partial flow of the raw exhaust gas flowing in the exhaust-gas line is fed to the heated catalyst 2. Furthermore, a fuel is fed to the heated catalyst, which is reacted with the exhaust gas or the residual oxygen contained in the exhaust gas. The heat generated in this process is fed back to the exhaust-gas line in the form of a hot gas and introduced into the second SCR system 13b. This additional heat introduction can take place both after a cold start and during a part-load operation, thus allowing rapid heating, on the one hand, and preventing cooling during operation, on the other hand. At full load or near full load operating conditions of the internal combustion engine, the heated catalyst 2 can be switched off.

[0043] With reference to FIG. 2, a second exemplary embodiment of an exhaust-gas aftertreatment device which can be used according to the invention is explained in more detail. Equal reference signs denote equal components of the invention, so that the following description is limited to the essential differences. FIG. 2 shows an oxidation catalyst 11 which is designed to post-oxidize oxidizable components of the raw exhaust gas, for example CO and/or CH.sub.x. A particulate filter 12 is disposed downstream of the oxidation catalyst, as described above. An SCR system, which is used in particular to reduce NO.sub.x, is disposed downstream of the particulate filter 12.

[0044] In the illustrated exemplary embodiment, the heated catalyst 2 is located upstream of the oxidation catalyst 11 and downstream of the internal combustion engine 15. During operation, a partial stream of the not previously purified raw exhaust gas from the internal combustion engine 15 is therefore supplied to the heated catalyst 2.

[0045] FIG. 2 further shows three temperature sensors 111, 112 and 132. The temperature sensors measure the exhaust-gas temperature at the inlet to the oxidation catalyst, at the outlet from the oxidation catalyst and at the outlet from the SCR system. These three temperature sensors should be understood as merely exemplary. In other embodiments of the invention, the number of temperature sensors used can be greater or less. In some cases, no temperature sensor at all can be used, as described above with reference to FIG. 1. In this case, the temperatures can be determined from the operating state of the internal combustion engine, for example with a reference-controlled synthesizer.

[0046] It should be noted that the exhaust-gas aftertreatment devices 1 shown in FIGS. 1 and 2 should be understood as merely exemplary. In other embodiments of the invention, other components can be used, for example three-way catalysts or storage catalysts. Likewise, individual components can be omitted. It is merely essential to the invention that at least one component 11, 12, 13 is present in the exhaust-gas aftertreatment device 1.

[0047] The object of the invention is to achieve the operating temperature of at least one component 11, 12, 13 rapidly and/or to maintain it at low exhaust-gas temperatures of the internal combustion engine 15, which can occur in particular in the lower partial load range. An exhaust-gas temperature upstream and/or downstream of the component can either be measured, as shown in FIG. 2, or determined from the operating state of the internal combustion engine. In this second case, too, the temperature is referred to as a “measured value” for the purposes of the present description, even if it has not been measured directly, for example by a thermocouple or a resistance thermometer.

[0048] The measured value of the temperature, its deviation from a predeterminable desired value, the heat capacity of the exhaust-gas line and upstream components of the exhaust-gas aftertreatment device, and the heat loss or gain of the raw exhaust gas on its way through the exhaust-gas aftertreatment device lead to a required thermal power of the heated catalyst 2 as control variable. This control variable can be influenced by the amount of fuel supplied to the heated catalyst 2 as well as the amount of exhaust gas supplied to the heated catalyst and, in some cases, the electrical energy supplied to the heated catalyst as reference variables. The reference variables in turn depend on the oxygen content of the raw exhaust gas, the exhaust-gas temperature and the exhaust-gas mass flow of the raw exhaust gas of the internal combustion engine 15. The exemplary embodiment of an open-loop or closed-loop control device 3 shown in FIG. 3 therefore uses a heated catalyst characteristic map 35. The heated catalyst characteristic map 35 is supplied with the temperatures and the oxygen content of the raw exhaust gas measured or determined via a first reference-controlled synthesizer from the data of the engine control unit 16. Likewise, measured values optionally read out from the engine control unit 16 are fed to the open-loop or closed-loop control device 3 by means of a digital data link 351. Thereafter, the open-loop or closed-loop control device 3 can read and set the reference variables with the aid of the heated catalyst characteristic map 35.

[0049] In some embodiments of the invention, further data can, in addition to the data from the motor control unit 16, be made available to the open-loop or closed-loop control device 3, which can then control the reference variables of the heated catalyst 2 more quickly or with greater accuracy, either under characteristic map control or also by calculation. This further data can be selected from a driving profile and/or a navigation destination and/or position data and/or the state of charge of a battery. For example, the heating power of the heated catalyst 2 can already be proactively reduced if it is known that the vehicle is about to drive up an incline and that a larger and also hotter exhaust-gas mass flow of the raw exhaust gas from the internal combustion engine is available as a result. Likewise, the heated catalyst can already be proactively activated at the end of an incline in order to prevent or reduce a drop in temperature of the component of the exhaust-gas aftertreatment device, which results from the fact that the internal combustion engine only operates at partial load or even in overrun mode when driving downhill. In the same way, position data can be used to define a base load range of the heated catalyst 2 since, for example in urban areas, a lower average load of the internal combustion engine 15 can be expected than during highway travel. Similarly, the operation of the vehicle in urban areas can indicate a higher dynamic range, whereas a more uniform load demand is placed on the internal combustion engine 15 during interurban travel. Finally, a navigation destination can also be used to control the heated catalyst 2, for example by stopping the regeneration of a particulate filter 12 shortly before reaching the driving destination or by postponing it until the vehicle reaches the city limit.

[0050] FIG. 4 shows a structure chart of a first embodiment of the method according to the invention. In the first embodiment, the heated catalyst 2 can be operated in seven different operating states, which are designated by the reference signs 51 to 57. The process control according to FIG. 4 should not be understood as meaning that the seven operating states are necessarily run through sequentially. On the contrary, at least one temperature is determined downstream of an oxidation catalyst, either directly by measurement or indirectly from the operating state of the internal combustion engine. Depending on the temperature and optionally further parameters, for example the operating time of the internal combustion engine, one of the illustrated operating states of the heated catalyst 2 is then selected. If the temperature at the outlet of the oxidation catalyst changes so that the applied operating state is no longer appropriate, the open-loop or closed-loop control device changes to another operating state on the basis of the temperature. In this case, a hysteresis can be used to avoid frequent changes in the operating state of the heated catalyst 2. The individual operating states are explained in more detail below.

[0051] The first operating state 51 denotes the start of the heated catalyst. For this purpose, the heated catalyst can first be preheated by supplying an exhaust-gas mass flow with an optional electric heating device until supplied fuel is converted exothermically on the heated catalyst and heats the heated catalyst further to its operating temperature.

[0052] In the second operating state 52, a comparatively large exhaust-gas mass flow of, for example, about 60 kg/h to about 100 kg/h is supplied to the heated catalyst. The heated catalyst is operated with an air ratio λ between about 0.75 and about 3.5 or between about 1.5 and about 2.5. This results in an almost complete conversion of the supplied fuel with the residual oxygen of the exhaust gas supplied to the heated catalyst 2. In some embodiments, the heated catalyst can deliver a thermal power of about 5 kW to about 20 kW in the form of a hot gas.

[0053] The third operating state 53 denotes an alternating operation in which cyclic switching occurs between a first sub-step 53a and a second sub-step 53b. In the first sub-step 53a, the operating conditions correspond approximately to the operation in the second method step 52. In the second sub-step 53b, the exhaust-gas mass flow is reduced by a factor of 10 to 25, for example to about 3 kg/h to about 10 kg/h, so that the heated catalyst is operated with an air ratio λ of between about 0.05 and about 0.5 or between about 0.1 and about 0.4. In the second sub-step 53b, the supplied fuel is thus not completely reacted, but is partially vaporized and partially converted into a synthesis gas, which is supplied to the oxidation catalyst via the exhaust-gas line. The heat supplied in the first substep 53a allows the synthesis gas to ignite at the oxidation catalyst where it can be converted exothermically so that a heating power of about 13 kW to about 20 kW is released directly at the oxidation catalyst.

[0054] The fourth method step 54 is similar to the second sub-step 53b of the third method step 53. However, the partial exhaust-gas flow supplied to the heated catalyst is greater and can be between about 5 kg/h and about 20 kg/h. The control can be such that a predeterminable proportion of the raw exhaust gas is passed through the heated catalyst. For example, between about 2 % and about 10 % or between about 3 % and about 8 % of the exhaust-gas flow of the internal combustion engine can be fed as a partial flow to the heated catalyst 2. In the fourth operating state 54, the heated catalyst can supply a thermal power of from about 10 kW to about 50 kW or from about 14 kW to about 36 kW in the form of an ignitable synthesis gas to the oxidation catalyst 11. Therefore, the fourth operating state 54 is particularly suitable for the rapid heating of the exhaust-gas aftertreatment device after a cold start and after the heated catalyst is started in the first method step 51 and some preconditioning of the exhaust-gas aftertreatment device has taken place in the second and third process steps 52 and 53.

[0055] After the exhaust-gas aftertreatment device is heated to a predeterminable desired temperature, the heated catalyst 2a can be cleaned in the fifth method step 55. For this purpose, the supplied partial flow is increased again, for example to about 50 kg/h to about 100 kg/h. The amount of fuel supplied can be reduced compared with the second method step 52, so that the heat released in the heated catalyst 2 is primarily used to oxidize and vaporize remaining deposits and residual fuel in order to prevent permanent deposits and contamination in the heated catalyst 2.

[0056] The sixth method step 56 is suitable for a warm-keeping operation, for example if the internal combustion engine 15 only produces low exhaust-gas temperatures in the low partial load range or if no fuel at all is supplied to the internal combustion engine in overrun operation. In the sixth method step 56, the thermal power of the heated catalyst can be between about 0 kW and about 10 kW. For this purpose, a comparatively small partial flow of about 5 kg/h to about 50 kg/h of the raw exhaust gas is supplied to the heated catalyst 2, while the heated catalyst is operated with an air ratio λ of between about 0.75 and about 3.5 or between about 1.5 and about 2.5.

[0057] If the heated catalyst 2 is permanently not required at high exhaust-gas temperatures, it can also be switched off in the seventh method step 57. In this case, no fuel is fed to the heated catalyst 2 so that the heated catalyst does not emit any heat even in the event that a partial flow of the exhaust gas permanently flows through the heated catalyst due to its installation situation.

[0058] In some embodiments of the invention, the method steps 51, 52, 53 and 54 are run through cyclically after a cold start, in each case switching to the next operating state when predeterminable temperature thresholds are reached. During continuous operation of the internal combustion engine, it is then possible to switch between the operating states 54, 55, 56 and 57 on the basis of the exhaust-gas temperature or the deviation of the desired temperature value of the oxidation catalyst from the actual value. The temperature limit values between the individual operating states can be provided with a hysteresis in order to avoid frequent undesired changes of the operating state.

[0059] With reference to FIG. 5, a structure chart of a second embodiment of the method according to the invention is explained in more detail. Equal components of the invention or equal operating states are provided with equal reference signs so that the following description is limited to the essential differences. After a cold start of the internal combustion engine or of the vehicle equipped therewith, the heated catalyst is started in the first method step 51.

[0060] As soon as the heated catalyst 2 has reached its operational readiness, the open-loop or closed-loop control device checks whether the exhaust-gas temperatures upstream and downstream of the oxidation catalyst 11 are above predeterminable limit values and whether the exhaust-gas mass flow of the raw exhaust gas exceeds a predeterminable minimum value. If this is the case, the fourth operating state with comparatively low partial flow and low air ratio can be started immediately, which allows rapid heating of the oxidation catalyst. If this is not the case, the component of the exhaust gas aftertreatment device is first preheated in catalytic burner mode according to the second operating state 52.

[0061] As soon as the heat front generated in the fourth method step 54 has penetrated all components of the exhaust-gas aftertreatment device and the temperature sensor 132 at the output of the SCR system also detects a value above a predeterminable limit value, the heated catalyst 2 is switched to warm-keeping operation according to the above described sixth operating state 56.

[0062] The process control according to FIG. 5 differs from the preceding control primarily in that the open-loop or closed-loop control device 3 of the heated catalyst 2 reads the operating data from the engine control unit 16 of the internal combustion engine 15 and, if necessary, uses further data, such as the remaining driving distance, the topography and the road class, to determine the required thermal power of the heated catalyst 2 in advance and, on the basis of the current and/or future operating conditions of the internal combustion engine, sets the respective optimum values for the partial flow and the fuel amount of the heated catalyst 2 using the heated-catalyst characteristic map 35. In this way, dead times of the control circuit can be eliminated so that the desired values of the temperature of the component of the exhaust-gas aftertreatment can be reached more quickly or the actual temperature fluctuates to a lesser extent.

[0063] FIGS. 6A, 6B and 6C shows the use of the method according to the invention in a first exemplary embodiment of a multistage control system according to FIG. 4. FIG. 6A shows the exhaust-gas mass flow of a raw exhaust gas in curve A on the left ordinate and the oxygen content of the exhaust gas in curve B on the right ordinate versus time in seconds. FIG. 6B shows on the same time axis the temperature of the temperature sensor 112 downstream of the oxidation catalyst 11 on the right ordinate in curve C and the output power of the heated catalyst in curve D on the left ordinate. FIG. 6B shows measured values for a desired value of 400° C. FIG. 6C shows similar measured values as FIG. 6B, but for a desired value of 280° C.

[0064] As can be seen from FIGS. 6A- 6C, the output power of the internal combustion engine 15 in the section shown from a WHTC cycle is not constant over time, but rather highly dynamic. Accordingly, the exhaust-gas mass flow and the oxygen content of the exhaust gas also change within a few seconds. As FIGS. 6B and 6C both show, the heated catalyst 2 can be controlled very rapidly with the open-loop or closed-loop control device according to the invention, so that the heat introduced by the heated catalyst largely compensates for the fluctuating heat introduced by the internal combustion engine, so that the output temperature downstream of the oxidation catalyst 11 only fluctuates to a small extent. The oxidation catalyst 11 can therefore always be used even in the part-load operation of the internal combustion engine. Emission slip does not occur.

[0065] FIGS. 7A, 7B and 7C describe the use of the method according to the invention in a second exemplary embodiment, namely the regeneration of a particulate filter 12. FIG. 7A shows the exhaust-gas mass flow in curve A.

[0066] FIG. 7B shows in curve F the exhaust-gas temperature of the raw exhaust gas downstream of the internal combustion engine. Curve C shows the temperature at the outlet of the oxidation catalyst or at the inlet of the particulate filter. FIG. 7C shows in curve E the CO content of the raw exhaust gas and in curve G the CH.sub.x content.

[0067] For the regeneration of the particulate filter 12, high exhaust-gas temperatures are required to oxidize the embedded particles and discharge them in gaseous form from the particulate filter 12. According to the prior art, the exhaust-gas temperature is raised, for this purpose, by internal engine measures, which leads to poor consumption and emission values during the regeneration.

[0068] As FIGS. 7A-7C show, switching on the heated catalyst 2 after about 60 seconds leads to a rapid increase in the exhaust-gas temperature from about 200° C. to about 600° C. The exhaust-gas temperature is kept constant by the heated catalyst within a narrow temperature range despite a dynamic load demand on the internal combustion engine and correspondingly fluctuating exhaust-gas mass flow of the raw exhaust gas over time. As curves E, F and G show, no further in-engine measures are required for regeneration, i.e. the temperature of the raw-exhaust gas remains below 250° C. at all times. Similarly, the pollutant emissions shown in curves E and G are not increased during the regeneration of the particulate filter, which is different from the prior art.

[0069] Of course, the invention is not limited to the illustrated embodiments. Therefore, the above description should not be considered limiting but explanatory. The below claims should be understood as meaning that a stated feature is present in at least one embodiment of the invention. This does not rule out the presence of further features. Where the claims and the above description define “first” and “second” embodiments, this designation is used to distinguish between two similar embodiments without determining a ranking order.