METHOD FOR OPERATING AN EXHAUST GAS AFTERTREATMENT DEVICE OF A MOTOR VEHICLE

Abstract

The present disclosure provides a method for operating an exhaust gas aftertreatment device for cleaning an exhaust gas flow of a motor vehicle with an internal combustion engine operated in normal mode with oxygen surplus. An oxygen store arranged downstream of an NOx storage catalyst of the exhaust gas aftertreatment device receives oxygen in normal mode, and during a regeneration mode emits oxygen for converting breakthrough hydrocarbons and/or carbon monoxide. The oxygen store is assigned to a particulate filter and/or an oxidation catalyst of the exhaust gas aftertreatment device. The particulate filter and/or the oxidation catalyst is arranged downstream of the NOx storage catalyst.

Claims

1. A method for operating an exhaust gas aftertreatment device for cleaning an exhaust gas flow of a motor vehicle with an internal combustion engine operated with oxygen surplus in normal mode, the method comprising: providing an oxygen store downstream of an NOx storage catalyst of the exhaust gas aftertreatment device, wherein the oxygen store receives oxygen in normal mode and during a regeneration mode emits oxygen for converting breakthrough hydrocarbons and/or carbon monoxide, wherein the oxygen store is assigned to at least one of a particulate filter and an oxidation catalyst of the exhaust gas aftertreatment device, and wherein at least one of the at least one particulate filter and the oxidation catalyst are arranged downstream of the NOx storage catalyst.

2. The method as claimed in claim 1, wherein a coating containing at least one of cerium dioxide and zirconium dioxide is used as an oxygen store.

3. The method as claimed in claim 1, wherein the regeneration mode is ended when a comparison of an oxygen value with a target oxygen value shows that the oxygen value is equal to or less than the target oxygen value.

4. The method as claimed in claim 3, wherein the oxygen value is determined using a model during regeneration mode.

5. The method as claimed in claim 3, wherein the oxygen value (O2LNT) is determined by temperature measurements indicative of at least one of temperature of the oxygen store, mass flow (m.sub.flow), and a lambda value (.sub.eng).

6. The method as claimed in claim 4, wherein the model is configured to determine aging effects of the exhaust gas aftertreatment device.

7. The method as claimed in claim 4, wherein the model is configured to provide a lambda simulation value (.sub.mod).

8. The method as claimed in claim 7, wherein the lambda simulation value (.sub.mod) is indicative of a lambda value (.sub.eng) downstream of the internal combustion engine, temperature, mass flow (m.sub.flow) and oxygen value (O2LNT).

9. The method as claimed in claim 7, wherein the model compares the lambda simulation value (.sub.mod) with a lambda value (.sub.meas) measured downstream of the NOx storage catalyst to provide age-induced tracking in the oxygen value (O2LNT).

10. The method as claimed in claim 9, wherein a duration of the regeneration mode is controlled by a control unit based on the age-induced tracking in the oxygen value (O2LNT) provided by the model.

11. An exhaust gas aftertreatment device for cleaning an exhaust gas flow of a motor vehicle with an internal combustion engine operated with oxygen surplus in normal mode, the exhaust gas aftertreatment device comprising: an oxygen store arranged downstream of an NOx storage catalyst of the exhaust gas aftertreatment device, wherein the oxygen store receives oxygen in normal mode and during a regeneration mode emits oxygen for converting at least one of breakthrough hydrocarbons and carbon monoxide, wherein the oxygen store is assigned to at least one of a particulate filter and an oxidation catalyst of the exhaust gas aftertreatment device, wherein at least one of the particulate filter and the oxidation catalyst are arranged downstream of the NOx storage catalyst.

12. The exhaust gas aftertreatment device as claimed in claim 11, wherein the oxygen store has a coating containing at least one of cerium dioxide and zirconium dioxide.

13. The exhaust gas aftertreatment device as claimed in claim 11, wherein the exhaust gas aftertreatment device is configured to end the regeneration mode when a comparison of an oxygen value measured downstream of the NOx storage catalyst with a target oxygen value shows that the oxygen value is equal to or less than the target oxygen value.

14. The exhaust gas aftertreatment device as claimed in claim 11, wherein a model for determining the oxygen value during regeneration mode is assigned to the exhaust gas aftertreatment device.

15. The exhaust gas aftertreatment device as claimed in claim 14, wherein the oxygen value (O2LNT) is determined by temperature measurements indicative of at least one of temperature of the oxygen store, mass flow (m.sub.flow), and a lambda value (.sub.eng).

16. The exhaust gas aftertreatment device as claimed in claim 14, wherein the model is configured to determine aging effects of the exhaust gas aftertreatment device.

17. The exhaust gas aftertreatment device as claimed in claim 14, wherein the model is configured to provide a lambda simulation value (.sub.mod).

18. The exhaust gas aftertreatment device as claimed in claim 17, wherein the lambda simulation value (.sub.mod) is indicative of a lambda value (.sub.eng) downstream of the internal combustion engine, temperature, mass flow (m.sub.flow) and oxygen value (O2LNT).

19. The exhaust gas aftertreatment device as claimed in claim 17, wherein the model compares the lambda simulation value (.sub.mod) with a lambda value (.sub.meas) measured downstream of the NOx storage catalyst to provide age-induced tracking in the oxygen value (O2LNT).

20. A motor vehicle with an exhaust gas aftertreatment device as claimed in claim 11.

Description

DRAWINGS

[0020] In order that the disclosure may be well understood, there will now be described various forms thereof, given by way of example, reference being made to the accompanying drawings, in which:

[0021] FIG. 1 is a block diagram showing an internal combustion engine and an exhaust gas aftertreatment device of a motor vehicle for performance of an exemplary form of a method according to the present disclosure;

[0022] FIG. 2 shows a correlation between temperature and oxygen storage capacity according to the teachings of the present disclosure;

[0023] FIG. 3 is a block diagram showing an internal combustion engine and the exhaust gas aftertreatment device of FIG. 1, and an assigned model for performance of a further exemplary form of a method according to the present disclosure; and

[0024] FIG. 4 shows various curves of breakthrough hydrocarbons and carbon monoxide according to the teachings of the present disclosure.

[0025] The drawings described herein are for illustration purposes only and are not intended to limit the scope of the present disclosure in any way.

DETAILED DESCRIPTION

[0026] The following description is merely exemplary in nature and is not intended to limit the present disclosure, application, or uses. It should be understood that throughout the drawings, corresponding reference numerals indicate like or corresponding parts and features.

[0027] FIG. 1 shows an internal combustion engine 4 and an exhaust gas aftertreatment device 6 of a motor vehicle 2.

[0028] The internal combustion engine 4 in the present exemplary form is a diesel engine, i.e. the diesel engine is operated in normal mode with an oxygen surplus (>1). By deviation, the internal combustion engine 4 may also be configured as a petrol engine in lean mode to increase the engine efficiency.

[0029] In the present exemplary form, the exhaust gas aftertreatment device 6 connected downstream of the internal combustion engine 4 in the exhaust gas flow direction has an NOx storage catalyst 8.

[0030] By deviation from the exemplary form shown in FIG. 1, the exhaust gas aftertreatment device 6 may comprise further components (not shown) for exhaust gas aftertreatment, such as e.g. a diesel oxidation catalyst (DOC) for removing carbon monoxide (CO) and hydrocarbons (C.sub.mH.sub.n) from the exhaust gas flow, an SCR or SCRF catalyst for selective catalytic reduction of nitrous oxides, a blocking catalyst for retention of ammonia (NH.sub.3) and/or a diesel particulate filter.

[0031] The NOx storage catalyst 8 is configured to store NOx (nitrous oxides). It has a structure with a suitable carrier with a noble metal catalyst such as platinum, and an NOx storage component e.g. an earth alkali metal such as barium.

[0032] The internal combustion engine 4 has an assigned control unit (not shown) which causes a switch from operation with oxygen surplus to a substoichiometric operation and vice versa, as will also be explained in more detail later. For this, the control unit has hardware and/or software components.

[0033] A particulate filter 10 is arranged downstream of the NOx storage catalyst 8. In the present exemplary form, the particulate filter 10 is formed as a diesel particulate soot filter for reducing the particles present in the exhaust gas. The particulate filter 10 is also known as a diesel particulate filter (DPF), corresponding to the particle origin, or a soot particulate filter (RPF), corresponding to the particle composition.

[0034] The particulate filter 10 downstream of the NOx storage catalyst 8, like the NOx storage catalyst 8, is arranged as close as possible to the internal combustion engine 4 in order to guarantee rapid heating of the NOx storage catalyst 8 and particulate filter 10, so that the two components are ready for operation quickly.

[0035] Furthermore, in the present exemplary form, an oxygen store 12 is provided which absorbs and temporarily stores oxygen during normal operation with a lean mixture, and emits oxygen during a regeneration mode with a rich mixture.

[0036] In the present exemplary form, the oxygen store 12 is assigned to the particulate filter 10 and formed by a coating which, in the present exemplary form, contains cerium dioxide (CeO.sub.2) and/or zirconium dioxide (ZrO.sub.2).

[0037] Reference is now made additionally to FIG. 2 which shows the correlation between the temperature T of the oxygen store 12 and its oxygen storage capacity S according to the present disclosure.

[0038] It is evident that in this example, the oxygen storage capacity S increases almost linearly with the temperature T in a temperature range from 150 C. to 500 C., and then increases further linearly with a smaller gradient from higher temperatures T.

[0039] Reference is now also made to FIG. 3 which shows the internal combustion engine 4 and the exhaust gas aftertreatment device 6 with the NOx storage catalyst 8 and particulate filter 10.

[0040] FIG. 3 furthermore shows that a model 14 is provided with which an oxygen value O2LNT of the exhaust gas aftertreatment device 6 can be determined, whichas will be explained in more detail belowis used to control a switch from a regeneration mode with a rich mixture to a normal mode with a lean mixture.

[0041] The model 14 links together measurement values for the temperature T, such as e.g. the exhaust gas temperature which is indicative of the temperature of the oxygen store 10, the mass flow m.sub.flow and the lambda value .sub.eng on the downstream side of the internal combustion engine 4, in order to determine a value representative of the oxygen value O2LNT as an output parameter, e.g. according to the following equation:

dO2LNT/dt=f1(1, <1, T, m.sub.flow, O2LNT).

[0042] Furthermore, the model 14 is configured to also provide a lambda simulation value .sub.mod which is compared with the lambda value .sub.meas measured downstream of the particulate filter 10, so that aging effects can be taken into account.

[0043] For this, the model 14 links together, as well as the measured values for the lambda value .sub.eng downstream of the internal combustion engine 4, the temperature T, the mass flow m.sub.flow and the oxygen value O2LNT, e.g. according to the following equation:

.sub.mod=f2(.sub.eng, m.sub.flow, O2LNT).

[0044] The model 14 may be implemented on a control unit (not shown), which for this has hardware and/or software components.

[0045] With additional reference now to FIG. 4, an exemplary form of a method according to the present disclosure for operating such an exhaust gas aftertreatment device 6 will now be described.

[0046] In normal mode, the internal combustion engine 4 is operated in the part load range with a lambda value of the supplied mixture which is greater than one, i.e. with an oxygen surplus. During normal mode, the NOx storage catalyst 8 absorbs nitrous oxides from the exhaust gas flow, and the oxygen store 12 absorbs oxygen from the exhaust gas flow which has passed through the NOx storage catalyst 8, and temporarily stores this until the oxygen store 12 is full (OSC full in FIG. 4). The particulate filter 10 removes soot particles from the exhaust gas flow.

[0047] In order to achieve a regeneration of the NOx storage catalyst 8, a regeneration mode R is performed. The duration and frequency of the regeneration mode R are determined by the control unit, e.g. as a function of the stored nitrous oxide quantity, the exhaust gas temperature, the exhaust gas mass flow and other parameters, and then initiated.

[0048] For this, the control unit actuates the internal combustion engine 2 such that the exhaust gas has a lambda value of less than one, in order to regenerate the NOx storage catalyst 8. For this, the control unit e.g. changes the time of fuel injection to achieve a late fuel injection, changes the ratio of the fuel quantity on main injection to the fuel quantity on post injection, changes the position of the throttle valve (air throttling), or increases the exhaust gas recirculation rate.

[0049] However, during regeneration mode R, the NOx storage catalyst 8 may not contain sufficient oxygen to convert completely all hydrocarbons and/or carbon monoxide leaving the NOx storage catalyst 8.

[0050] Such hydrocarbons and/or carbon monoxide leaving the NOx storage catalyst 8 are known as breakthrough hydrocarbons and/or carbon monoxide.

[0051] The breakthrough hydrocarbons and/or carbon monoxide reach the particulate filter 10 with the oxygen store 12. During the regeneration mode R, the oxygen store 12 emits the oxygen temporarily stored and thus allows conversion of the breakthrough hydrocarbons and/or carbon monoxide.

[0052] The control unit ends the regeneration mode R when a comparison of the oxygen value O2LNT with a predefined target oxygen value O2Targ shows that the oxygen value O2LNT is equal to or less than the target oxygen value O2Targ.

[0053] This provides that a sufficient minimum quantity of oxygen is available to convert the breakthrough hydrocarbons and/or carbon monoxide. If however the oxygen quantity is below this minimum level, the result is a rise in the hydrocarbon and carbon monoxide concentration, as indicated in FIG. 4.

[0054] The oxygen value O2LNT is determined using the model 14. Furthermore, the model 14 provides the lambda simulation value .sub.mod.

[0055] The lambda simulation value .sub.mod is compared with the lambda value .sub.meas measured downstream of the particulate filter 10, so that aging effects can be detected and taken into account. For this, the difference is formed between the measured lambda value .sub.meas and the lambda simulation value .sub.mod, and parameters of the model 14 adapted accordingly.

[0056] Aging effects, in particular of the oxygen store 12, may lead to slow reduction in the storage capacity of the oxygen store 12 and hence also in the oxygen content, which leads to a change in the measured lambda value .sub.meas.

[0057] Thus an age-induced tracking in the oxygen value O2LNT supplied by the model 14 is achieved, and operation with insufficient oxygen reserves is avoided. Aging leads to a reduction in the oxygen storage capacity of the oxygen store 12. Thus only a reduced oxygen quantity is available during regeneration mode. This leads to a shortening of the duration of the regeneration mode, because sufficient oxygen is available only for a shorter regeneration mode. Thus, a sufficient minimum quantity of oxygen is provided for converting breakthrough hydrocarbons and/or carbon monoxide.