EXHAUST ENGINE CLEANING SYSTEM

Description

Technical Field

[0001] The present disclosure relates to an exhaust purification system of an internal combustion engine.Background Art

[0002] The exhaust purification system of an internal combustion engine described in WO2014 / 118890A comprises an upstream side exhaust purification catalyst provided in an exhaust passage of the internal combustion engine, a downstream side exhaust purification catalyst provided at the downstream side of the upstream side exhaust purification catalyst in the direction of flow of exhaust in the exhaust passage, a downstream side air-fuel ratio sensor provided between the upstream side exhaust purification catalyst and the downstream side exhaust purification catalyst in the exhaust passage, and a control device able to control the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst as "air-fuel ratio control".

[0003] In the exhaust purification system described in WO2014 / 118890A, in the air-fuel ratio control, when the output air-fuel ratio of the downstream side air-fuel ratio sensor is a rich judged air-fuel ratio or less, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst is switched to an air-fuel ratio leaner than the stoichiometric air-fuel ratio (below, referred to as a "lean air-fuel ratio"). In addition, when the oxygen storage amount of the upstream side exhaust purification catalyst becomes a switching reference storage amount less than a maximum storable amount of oxygen or becomes greater, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst is switched to an air-fuel ratio richer than the stoichiometric air-fuel ratio (below, referred to as a "rich air-fuel ratio"). By executing such air-fuel ratio control, it is considered possible to keep NO X from flowing out from the upstream side exhaust purification catalyst.

[0004] By executing the above-mentioned air-fuel ratio control, NO X will never flow out from the upstream side exhaust purification catalyst, but unburned gas (HC, CO, etc.) will sometimes flow out. For this reason, unburned gas will periodically flow into the downstream side exhaust purification catalyst and the oxygen storage amount of the downstream side exhaust purification catalyst will gradually fall. On the other hand, in most internal combustion engines, the feed of fuel from a fuel injector is temporarily stopped during operation of the internal combustion engine in accordance with the engine operating state as "fuel cut control". If such fuel cut control is executed, the oxygen storage amount of the downstream side exhaust purification catalyst will increase up to the maximum storable amount of oxygen. Therefore, if fuel cut control is periodically executed, due to the above-mentioned air-fuel ratio control, even if the oxygen storage amount of the downstream side exhaust purification catalyst falls, it will never reach close to zero.

[0005] In this regard, depending on the engine operating state, sometimes fuel cut control is not executed for a long time period. In this case, the oxygen storage amount of the downstream side exhaust purification catalyst falls and finally the unburned gas which flows out from the upstream side exhaust purification catalyst ends up being unable to be sufficiently removed at the downstream side exhaust purification catalyst. Therefore, in the exhaust purification system described in WO2014 / 118890A, when the oxygen storage amount of the downstream side exhaust purification catalyst decreases, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst is continuously or intermittently set as the lean air-fuel ratio. Due to this, the oxygen storage amount of the upstream side exhaust purification catalyst reaches the maximum storable amount of oxygen and exhaust gas containing oxygen or NO X flows out from the upstream side exhaust purification catalyst. According to the exhaust purification system described in WO2014 / 118890A, as a result, it is considered possible to make the oxygen storage amount of the downstream side exhaust purification catalyst increase and restore the ability of the upstream side exhaust purification catalyst to purify the unburned gas. US 2015086428 A1 describes an abnormality diagnosis system of internal combustion engine.Summary of Disclosure

[0006] In this regard, if the oxygen storage amount of the downstream side exhaust purification catalyst falls to a certain extent or less, unburned HC is physically adsorbed on the surface of the precious metal carried on the downstream side exhaust purification catalyst (HC poisoning). If the downstream side exhaust purification catalyst suffers from such HC poisoning, the reactivity on the downstream side exhaust purification catalyst falls. Therefore, even if a large amount of oxygen or NO X flows into the downstream side exhaust purification catalyst, the oxygen or NO X is not sufficiently removed from the exhaust gas. Part flows out from the downstream side exhaust purification catalyst.

[0007] In the exhaust purification system described in WO2014 / 118890A, when the oxygen storage amount of the downstream side exhaust purification catalyst decreases, even after the oxygen storage amount of the upstream side exhaust purification catalyst reaches the maximum storable amount of oxygen, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst is set as the lean air-fuel ratio. For this reason, a large amount of oxygen or NO X flows out from the upstream side exhaust purification catalyst and therefore a large amount of oxygen or NO X flows into the downstream side exhaust purification catalyst. However, if the downstream side exhaust purification catalyst suffers from HC poisoning, the oxygen or NO X in the inflowing exhaust gas can no longer be fully removed. Part may flow out from the downstream side exhaust purification catalyst.

[0008] Therefore, an object of the present invention, in view of the above problem, is to provide an exhaust purification system of an internal combustion engine which can keep NO X from flowing out from the downstream side exhaust purification catalyst.

[0009] The present invention was developed in view of such a problem and substances are as follows.

[0010] (1) An exhaust purification system of an internal combustion engine is defined in claim 1. (2) The exhaust purification system of an internal combustion engine according to (1), wherein the control device is further configured not to execute the control for increasing NO X even if the oxygen storage amount of the downstream side catalyst is less than or equal to the limit storage amount when the temperature of the downstream side catalyst is less than a predetermined temperature. (3) The exhaust purification system of an internal combustion engine according to (1) or (2), wherein the control device is further configured not to execute the control for increasing NO X even if the oxygen storage amount of the downstream side catalyst is less than or equal to the limit storage amount when the oxygen storage amount of the downstream side catalyst is less than or equal to the limit storage amount. (4) The exhaust purification system of an internal combustion engine according to any one of (1) to (3), wherein the control device is further configured to control the air-fuel ratio of the exhaust gas flowing into the upstream side catalyst in the air-fuel ratio control so that the air-fuel ratio of the exhaust gas flowing out from the upstream side catalyst does not become greater than or equal to a constant lean judged air-fuel ratio leaner than the stoichiometric air-fuel ratio, and wherein the lean judged air-fuel ratio is a lean air-fuel ratio with a difference from the stoichiometric air-fuel ratio equal to the difference between the rich judged air-fuel ratio and the stoichiometric air-fuel ratio.

[0011] According to the present invention, it is possible to keep NO X from flowing out from the downstream side exhaust purification catalyst.Brief Description of Drawings

[0012] FIG. 1 is a view schematically showing an internal combustion engine of the present invention. FIG. 2 is a view showing a relationship between a sensor applied voltage and output current at different exhaust air-fuel ratios. FIG. 3 is a view showing a relationship between an exhaust air-fuel ratio and output current when making the sensor applied voltage constant. FIG. 4 is a time chart of an air-fuel ratio correction amount when executing air-fuel ratio control. FIG. 5 is a time chart of an air-fuel ratio correction amount and an output air-fuel ratio of the downstream side exhaust purification catalyst etc. FIG. 6A is a view schematically showing a surface of a carrier of a downstream side exhaust purification catalyst. FIG. 6B is a view schematically showing a surface of a carrier of a downstream side exhaust purification catalyst. FIG. 7 schematically shows a concentration of oxygen and NO X in exhaust gas, a concentration of unburned gas, and an air-fuel ratio of different parts in an exhaust passage. FIG. 8 is a view schematically showing a surface of a carrier of a downstream side exhaust purification catalyst. FIG. 9 is a time chart, similar to FIG. 5, of an air-fuel ratio correction amount and presence of NO X increasing control. FIG. 10 is a view showing a relationship between an ignition timing and a concentration of NO X and HC flowing out from an engine body. FIG. 11 is a view showing a relationship between an EGR amount and a concentration of NO X and HC flowing out from an engine body. FIG. 12 is a view showing a relationship between a selective injection rate of a cylinder fuel injector and port fuel injector and a concentration of NO X and HC flowing out from an engine body. FIG. 13 is a flow chart showing a control routine of control for setting a correction amount of the air-fuel ratio. FIG. 14 is a flow chart showing a control routine of processing for executing increasing control which judges the start of execution of NO X increasing control. FIG. 15 is a flow chart showing a control routine of processing for increasing NO X . Description of Embodiments

[0013] Below, referring to the drawings, embodiments of the present invention will be explained in detail. Note that, in the following explanation, similar components are assigned the same reference numerals.<Explanation of Internal Combustion Engine as a Whole>

[0014] FIG. 1 is a view which schematically shows an internal combustion engine in which an exhaust purification system according to a first embodiment of the present invention is used. Referring to FIG. 1, 1 indicates an engine body, 2 a cylinder block, 3 a piston which reciprocates in the cylinder block 2, 4 a cylinder head which is fastened to the cylinder block 2, 5 a combustion chamber which is formed between the piston 3 and the cylinder head 4, 6 an intake valve, 7 an intake port, 8 an exhaust valve, and 9 an exhaust port. The intake valve 6 opens and closes the intake port 7, while the exhaust valve 8 opens and closes the exhaust port 9.

[0015] As shown in FIG. 1, a spark plug 10 is arranged at a center part of an inside wall surface of the cylinder head 4, while a cylinder fuel injector 11 which directly injects and feeds fuel into a cylinder is arranged at a peripheral part of the inner wall surface of the cylinder head 4. In addition, a port fuel injector (an intake passage fuel injector) 12 which injects and feeds fuel into the intake port (i.e. intake passage) 7 is arranged at the periphery of the intake port 7. The spark plug 10 is configured to generate a spark in accordance with an ignition signal. Further, the cylinder fuel injector 11 and the port fuel injector 12 respectively inject a predetermined amount of fuel in accordance with an injection signal. Note that, according to some embodiments only one of the cylinder fuel injector 11 and the port fuel injector 12 may be provided. Further, in the present embodiment, as the fuel, gasoline with a stoichiometric air-fuel ratio of 14.6 is used. However, the internal combustion engine in which an exhaust purification system of the present invention is used may also use fuel other than gasoline and blended fuel including gasoline as the fuel.

[0016] The intake port 7 of each cylinder is connected to a surge tank 14 through a corresponding intake manifold 13, while the surge tank 14 is connected to an air cleaner 16 through an intake pipe 15. The intake port 7, intake manifold 13, surge tank 14, and intake pipe 15 form an intake passage. Further, inside the intake pipe 15, a throttle valve 18 which is driven by a throttle valve drive actuator 17 is arranged. The throttle valve 18 can be operated by the throttle valve drive actuator 17 to thereby change the aperture area of the intake passage.

[0017] On the other hand, the exhaust port 9 of each cylinder is connected to an exhaust manifold 19. The exhaust manifold 19 has a plurality of runners which are connected to the exhaust ports 9 and a collected part at which these runners are collected. The collected part of the exhaust manifold 19 is connected to an upstream side casing 21 which houses an upstream side exhaust purification catalyst 20. The upstream side casing 21 is connected through an exhaust pipe 22 to a downstream side casing 23 which houses a downstream side exhaust purification catalyst 24. The exhaust manifold 19 and the surge tank 14 are connected through a recirculation exhaust gas (hereinafter, referred to as "EGR gas") conduit 26 to each other. Inside the EGR gas conduit 26, an EGR control valve 27 is arranged. The exhaust port 9, exhaust manifold 19, upstream side casing 21, exhaust pipe 22, and downstream side casing 23 form an exhaust passage.

[0018] The electronic control unit (ECU) 31 is comprised of a digital computer which is provided with components which are connected together through a bidirectional bus 32 such as a RAM (random access memory) 33, ROM (read only memory) 34, CPU (microprocessor) 35, input port 36, and output port 37. In the intake pipe 15, an airflow meter 39 is arranged for detecting the flow rate of air flowing through the intake pipe 15. The output of this airflow meter 39 is input through a corresponding AD converter 38 to the input port 36. Further, at the collected part of the exhaust manifold 19, an upstream side air-fuel ratio sensor 40 is arranged which detects the air-fuel ratio of the exhaust gas flowing through the inside of the exhaust manifold 19 (that is, the exhaust gas flowing into the upstream side exhaust purification catalyst 20). In addition, in the exhaust pipe 22, a downstream side air-fuel ratio sensor 41 is arranged which detects the air-fuel ratio of the exhaust gas flowing through the inside of the exhaust pipe 22 (that is, the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 and flowing into the downstream side exhaust purification catalyst 24). The outputs of these air-fuel ratio sensors 40 and 41 are also input through the corresponding AD converters 38 to the input port 36.

[0019] Further, an accelerator pedal 42 is connected to a load sensor 43 generating an output voltage which is proportional to the amount of depression of the accelerator pedal 42. The output voltage of the load sensor 43 is input to the input port 36 through a corresponding AD converter 38. The crank angle sensor 44 generates an output pulse every time, for example, a crankshaft rotates by 15 degrees. This output pulse is input to the input port 36. The CPU 35 calculates the engine speed from the output pulse of this crank angle sensor 44. On the other hand, the output port 37 is connected through corresponding drive circuits 45 to the spark plugs 10, the cylinder fuel injector 11, the port fuel injector 12, and the throttle valve drive actuator 17. Note that the ECU 31 functions as a control device for controlling the internal combustion engine and the exhaust purification system.<Explanation of Exhaust Purification Catalyst>

[0020] The upstream side exhaust purification catalyst 20 and the downstream side exhaust purification catalyst 24 are three-way catalysts having oxygen storage abilities. Specifically, the exhaust purification catalysts 20 and 24 are three-way catalysts comprised of carriers made of ceramic on which precious metals having catalytic actions (for example, platinum (Pt)) and substances having oxygen storage abilities (for example, ceria (CeO 2 )) are carried. The three-way catalysts have the functions of simultaneously removing unburned HC, CO and NOX if the air-fuel ratios of the exhaust gas flowing into the three-way catalysts are maintained at the stoichiometric air-fuel ratio. In addition, when the exhaust purification catalysts 20 and 24 store certain extents of oxygen, even if the air-fuel ratios of the exhaust gas flowing into the exhaust purification catalysts 20 and 24 deviate slightly to the rich side or the lean side from the stoichiometric air-fuel ratio, the unburned HC, CO and NOX are simultaneously removed.

[0021] That is, if the three-way catalysts 20 and 24 have oxygen storage abilities, i.e., if the oxygen storage amounts of the exhaust purification catalysts 20 and 24 are smaller than the maximum storable oxygen amount, when the air-fuel ratios of the exhaust gas flowing into the exhaust purification catalysts 20 and 24 become somewhat leaner than the stoichiometric air-fuel ratio, the excess oxygen contained in the exhaust gas is stored in the exhaust purification catalysts 20 and 24. Due to this, the surfaces of the exhaust purification catalysts 20 and 24 are maintained at the stoichiometric air-fuel ratio. As a result, the surfaces of the exhaust purification catalysts 20 and 24 are simultaneously cleaned of unburned HC, CO and NOX. At this time, the air-fuel ratios of the exhaust gas discharged from the exhaust purification catalysts 20 and 24 become the stoichiometric air-fuel ratio.

[0022] On the other hand, if the exhaust purification catalysts 20 and 24 are in a state where they can release oxygen, i.e., if the oxygen storage amounts of the exhaust purification catalysts 20 and 24 are greater than zero, when the air-fuel ratios of the exhaust gas flowing into the exhaust purification catalysts 20 and 24 become somewhat richer than the stoichiometric air-fuel ratio, the insufficient amount of oxygen for reducing the exhaust gas contained in the exhaust gas is released from the exhaust purification catalysts 20 and 24. Due to this, in this case as well, the surfaces of the exhaust purification catalysts 20 and 24 are maintained at the stoichiometric air-fuel ratio. As a result, the surfaces of the exhaust purification catalysts 20 and 24 are simultaneously cleaned of unburned HC, CO and NO X . At this time, the air-fuel ratios of the exhaust gas flowing out from the exhaust purification catalysts 20 and 24 become the stoichiometric air-fuel ratio.

[0023] In this way, if the exhaust purification catalysts 20 and 24 store certain amounts of oxygen, even if the air-fuel ratios of the exhaust gas flowing into the exhaust purification catalysts 20 and 24 deviate somewhat to the rich side or the lean side from the stoichiometric air-fuel ratio, the unburned HC, CO and NOX are simultaneously removed, and the air-fuel ratios of the exhaust gas flowing out from the exhaust purification catalysts 20 and 24 become the stoichiometric air-fuel ratio.<Explanation of Air-Fuel Ratio Sensor>

[0024] Next, referring to FIGS. 2 and 3, the output characteristic of air-fuel ratio sensors 40 and 41 in the present embodiment will be explained. FIG. 2 is a view showing the voltage-current (V-I) characteristic of the air-fuel ratio sensors 40 and 41 of the present embodiment. FIG. 3 is a view showing the relationship between air-fuel ratio of the exhaust gas (below, referred to as "exhaust air-fuel ratio") flowing around the air-fuel ratio sensors 40 and 41 and output current I, when making the supplied voltage constant. Note that, in this embodiment, the air-fuel ratio sensor having the same configurations is used as both air-fuel ratio sensors 40 and 41.

[0025] As will be understood from FIG. 2, in the air-fuel ratio sensors 40 and 41 of the present embodiment, the output current I becomes larger the higher (the leaner) the exhaust air-fuel ratio. Further, the line V-I of each exhaust air-fuel ratio has a region substantially parallel to the V axis, that is, a region where the output current does not change much at all even if the supplied voltage of the sensor changes. This voltage region is called the "limit current region". The current at this time is called the "limit current". In FIG. 2, the limit current region and limit current when the exhaust air-fuel ratio is 18 are shown by W 18 and I 18 , respectively. Therefore, the air-fuel ratio sensors 40 and 41 can be referred to as "limit current type air-fuel ratio sensors".

[0026] FIG. 3 is a view which shows the relationship between the exhaust air-fuel ratio and the output current I when making the supplied voltage constant at about 0.45V. As will be understood from FIG. 3, in the air-fuel ratio sensors 40 and 41, the output current I varies linearly (proportionally) with respect to the exhaust air-fuel ratio such that the higher (i.e., the leaner) the exhaust air-fuel ratio, the greater the output current I from the air-fuel ratio sensors 40 and 41. In addition, the air-fuel ratio sensors 40 and 41 are configured so that the output current I becomes zero when the exhaust air-fuel ratio is the stoichiometric air-fuel ratio.

[0027] Note that, in the above example, as the air-fuel ratio sensors 40 and 41, limit current type air-fuel ratio sensors are used. However, as the air-fuel ratio sensors 40 and 41, it is also possible to use air-fuel ratio sensors that are not of the limit current type, as long as the output current varies linearly with respect to the exhaust air-fuel ratio. Further, the air-fuel ratio sensors 40 and 41 may have structures different from each other.<Basic Air Fuel Ratio Control>

[0028] Next, an outline of the basic air-fuel ratio control in the exhaust purification system of an internal combustion engine of the present embodiment will be explained. In the air-fuel ratio control of the present embodiment, the fuel feed amount from the fuel injectors 11 and 12 is controlled by feedback based on the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 so that the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 becomes the target air-fuel ratio. In other words, in the air-fuel ratio control of the present embodiment, the feedback control is performed based on the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 so that the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalysts 20 becomes the target air-fuel ratio. Note that, "output air-fuel ratio" means an air-fuel ratio corresponding to the output value of an air-fuel ratio sensor.

[0029] Furthermore, in the air-fuel ratio control of the present embodiment, a target air-fuel ratio is set based on the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 etc. Specifically, when the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 becomes the rich air-fuel ratio, the target air-fuel ratio is set to the lean set air-fuel ratio. As a result, the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalyst 20 also becomes the air-fuel ratio equal to a lean set air-fuel ratio. In this regard, the lean set air-fuel ratio is a predetermined air-fuel ratio which is a fixed value and is leaner by a certain amount than the stoichiometric air-fuel ratio (an air-fuel ratio serving as the center of control). For example, the lean set air-fuel ratio is approximately 14.65 to 16. Further, the lean set air-fuel ratio can be expressed as an air-fuel ratio obtained by adding the lean correction amount to the air-fuel ratio serving as the center of control (in the present embodiment, stoichiometric air-fuel ratio). Further, in the present embodiment, it is judged that the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 becomes the rich air-fuel ratio, when the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 becomes less than or equal to a rich judgement air-fuel ratio which is slightly richer than the stoichiometric air-fuel ratio (for example, 14.55).

[0030] If the target air-fuel ratio is changed to the lean set air-fuel ratio, the oxygen excess / deficiency of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is cumulatively added. The "oxygen excess / deficiency" means the amount of oxygen which becomes excessive or the amount of oxygen which becomes deficient (amount of excess unburned HC, CO etc. (below, also referred to as the "unburned gas")) when trying to make the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 the stoichiometric air-fuel ratio. In particular, when the target air-fuel ratio is the lean set air-fuel ratio, the exhaust gas flowing into the upstream side exhaust purification catalyst 20 becomes excessive in oxygen. This excess oxygen is stored in the upstream side exhaust purification catalyst 20. Therefore, the cumulative value of the oxygen excess / deficiency (below, also referred to as the "cumulative oxygen excess / deficiency") can be said to be the estimated value of the stored amount of oxygen OSA of the upstream side exhaust purification catalyst 20.

[0031] Note that the oxygen excess / deficiency is calculated based on the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 and the estimated value of the intake air amount to the inside of the combustion chamber 5 which is calculated based on the output of the airflow meter 39 etc. or the fuel feed amount of the fuel injectors 11, 12 etc. Specifically, the oxygen excess / deficiency OEDsc is, for example, calculated by the following formula (1): ODEsc = 0.23 * Qi * AFup − AFR where 0.23 indicates the concentration of oxygen in the air, Qi indicates the amount of fuel injection, and AFup indicates the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 and AFR indicates the air-fuel ratio serving as the center of control (in the present embodiment, basically stoichiometric air-fuel ratio).

[0032] If the cumulative oxygen excess / deficiency of the thus calculated oxygen excess / deficiency becomes greater than or equal to the predetermined switching reference value (corresponding to predetermined switching reference storage amount Cref), the target air-fuel ratio which had up to then been set to the lean set air-fuel ratio is set to a rich set air-fuel ratio. As the result, the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalyst 20 also becomes the air-fuel ratio equal to the rich set air-fuel ratio. The rich set air-fuel ratio is a predetermined air-fuel ratio which is a certain degree richer than the stoichiometric air-fuel ratio (air-fuel ratio serving as the center of control). For example, it is 14 to 14.55 or so. Further, the rich set air-fuel ratio can be expressed as an air-fuel ratio obtained by adding a negative air-fuel ratio correction amount from the air-fuel ratio serving as the center of control (in the present embodiment, stoichiometric air-fuel ratio). Note that, in the present embodiment, the difference between the rich set air-fuel ratio and the stoichiometric air-fuel ratio (rich degree) is less than or equal to the difference between the lean set air-fuel ratio and the stoichiometric air-fuel ratio (lean degree).

[0033] After this, when the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 again becomes the rich judgment air-fuel ratio or less, the target air-fuel ratio is again set to the lean set air-fuel ratio. After this, a similar operation is repeated. In this way, in the present embodiment, the target air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is alternately set to the lean set air-fuel ratio and the rich set air-fuel ratio. In other words, in the present embodiment, the air-fuel ratio of the exhaust gas flowing into the exhaust purification catalyst 20 is alternately switched to the lean air-fuel ratio and the rich air-fuel ratio.<Explanation of Air Fuel Ratio Control Using Time Chart>

[0034] Referring to FIG. 4, the operation explained above will be explained in detail. FIG. 4 is a time chart of the air-fuel ratio correction amount AFC, the output air-fuel ratio AFup of the upstream side air-fuel ratio sensor 40, the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20, the cumulative oxygen excess / deficiency ΣOEDsc of the exhaust gas flowing into the upstream side exhaust purification catalyst 20, the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41, the stored amount of oxygen OSAufc of the downstream side exhaust purification catalyst 24, the concentration of NO X in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20, and the concentration of HC, CO in the exhaust gas flowing out from the downstream side exhaust purification catalyst 24, when performing the air-fuel ratio control of the present embodiment.

[0035] Note that, the air-fuel ratio correction amount AFC is a correction amount relating to the target air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20. When the air-fuel ratio correction amount AFC is 0, the target air-fuel ratio is set to the air-fuel ratio equal to the air-fuel ratio serving as center of control (below, referred to as "control center air-fuel ratio") (in this embodiment, stoichiometric air-fuel ratio). When the air-fuel ratio correction amount AFC is a positive value, the target air-fuel ratio becomes an air-fuel ratio leaner than the control center air-fuel ratio (in this embodiment, a lean air-fuel ratio), and when the air-fuel ratio correction amount AFC is a negative value, the target air-fuel ratio becomes an air-fuel ratio richer than the control center air-fuel ratio (in this embodiment, a rich air-fuel ratio).

[0036] In the illustrated example, in the state before the time t 1 , the air-fuel correction amount AFC is set to the predetermined constant rich set correction amount AFCrich (corresponding to the rich set air-fuel ratio). That is, the target air-fuel ratio is set to a rich air-fuel ratio, and along with this, the output air-fuel ratio of the upstream side air-fuel ratio sensor 40 becomes a rich air-fuel ratio. Unburned gas and the like contained in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is purified by the upstream side exhaust purification catalyst 20, and along with this the stored amount of oxygen OSAsc gradually decreases in the upstream side exhaust purification catalyst 20. The amount of unburned gas and the like in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is decreased by the purification at the upstream side exhaust purification catalyst 20, and therefore the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 becomes substantially the stoichiometric air-fuel ratio. Further, since the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 becomes the rich air-fuel ratio, the amount of NO X exhausted from the upstream side exhaust purification catalyst 20 is reduced.

[0037] If the stored amount of oxygen OSAsc gradually decreases in the upstream side exhaust purification catalyst 20 , the stored amount of oxygen OSAsc approaches zero. Along with this, part of the unburned gas and the like flowing into the upstream side exhaust purification catalyst 20 starts to flow out without being purified by the upstream side exhaust purification catalyst 20. Due to this, the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 gradually falls and the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 reaches the rich judgment air-fuel ratio AFrich at the time t 1 .

[0038] In the present embodiment, when the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 becomes the rich judgment air-fuel ratio AFrich or less, to increase the stored amount of oxygen OSAsc, the air-fuel ratio correction amount AFC is switched to the predetermined constant lean set correction amount AFClean (corresponding to the lean set air-fuel ratio). Further, at this time, the cumulative oxygen excess / deficiency ΣOEDsc is reset to 0.

[0039] Note that, in the present embodiment, the air-fuel ratio correction amount AFC is switched after the output air-fuel ratio of the downstream side air-fuel ratio sensor 41 reaches the rich judgment air-fuel ratio. This is because even if the stored amount of oxygen of the upstream side exhaust purification catalyst 20 is sufficient, the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 is sometimes slightly offset from the stoichiometric air-fuel ratio. Conversely speaking, the rich judgment air-fuel ratio is set to an air-fuel ratio which the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 will never reach when the stored amount of oxygen of the upstream side exhaust purification catalyst 20 is sufficient.

[0040] When the target air-fuel ratio is switched to a lean air-fuel ratio at the time t 1 , the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 changes from the rich air-fuel ratio to the lean air-fuel ratio. If at the time t 1 the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 changes to the lean air-fuel ratio, the upstream side exhaust purification catalyst 20 increases in the stored amount of oxygen OSAsc. Further, along with this, the cumulative oxygen excess / deficiency ΣOEDsc also gradually increases.

[0041] Due to this, the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 changes to the stoichiometric air-fuel ratio, and the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 converges to the stoichiometric air-fuel ratio. At this time, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 becomes the lean air-fuel ratio, but there is sufficient leeway in the oxygen storage ability of the upstream side exhaust purification catalyst 20, and therefore the oxygen in the inflowing exhaust gas is stored in the upstream side exhaust purification catalyst 20 and the NO X is reduced and purified. Therefore, the exhaust amount of NOx from the upstream side exhaust purification catalyst 20 is reduced.

[0042] After this, if the upstream side exhaust purification catalyst 20 increases in stored amount of oxygen OSAsc, at the time t 2 , the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20 reaches the switching reference storage amount Cref. For this reason, the cumulative oxygen excess / deficiency ΣOEDsc reaches the switching reference value OEDref which corresponds to the switching reference storage amount Cref. In the present embodiment, if the cumulative oxygen excess / deficiency ΣOEDsc becomes the switching reference value OEDref or more, in order to suspend the storage of oxygen to the upstream side exhaust purification catalyst 20, the air-fuel ratio correction amount AFC is switched to the rich set air-fuel amount AFTrich. Therefore, the target air-fuel ratio is switched to a rich air-fuel ratio. Further, at this time, the cumulative oxygen excess / deficiency ΣOEDsc is reset to 0.

[0043] Note that switching reference storage amount Cref is set at a sufficiently small amount so that even if sudden acceleration of the vehicle causes an unintentional deviation of the air-fuel ratio etc., the oxygen storage amount OSAsc does not reach the maximum storable oxygen amount Cmax. For example, the switching reference storage amount Cref is set as 3 / 4 or less of the maximum storable oxygen amount Cmax when the upstream side exhaust purification catalyst 20 is still unused, preferably 1 / 2 or less, more preferably 1 / 5 or less. As a result, the air-fuel ratio correction amount AFC is switched to the rich set correction amount AFCrich before the output air-fuel ratio AFdwn reaches a lean judged air-fuel ratio slightly leaner than the stoichiometric air-fuel ratio (for example, 14.65. Lean air-fuel ratio where difference from stoichiometric air-fuel ratio is equal to difference between rich judged air-fuel ratio and stoichiometric air-fuel ratio). That is, the present air-fuel ratio control can be said to control the air-fuel ratio of the exhaust gas flowing into said upstream side catalyst so that the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 does not becomes equal to or greater than a certain lean judged air-fuel ratio.

[0044] If at the time t 2 switching the target air-fuel ratio to the rich air-fuel ratio, the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 changes from the lean air-fuel ratio to the rich air-fuel ratio. The exhaust gas flowing into the upstream side exhaust purification catalyst 20 contains unburned gas etc., so the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 gradually decreases. The discharge of NO X from the upstream side exhaust purification catalyst 20 at this time becomes substantially zero.

[0045] If the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 gradually decreases, at the time t 3 , in the same way as the time t 1 , the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 reaches the rich judged air-fuel ratio AFrich. Due to this, the air-fuel ratio correction amount AFC is switched to the lean set correction amount AFClean. After that, the cycle of the above-mentioned t 1 to t 3 is repeated.

[0046] As will be understood from the above explanation, according to the present embodiment, it is possible to constantly suppress the amount of NO X exhausted from the upstream side exhaust purification catalyst 20. That is, as long as performing the control explained above, the exhaust amount of NOx from the upstream side exhaust purification catalyst 20 can basically be nearly zero. Further, since the cumulative period for calculating the cumulative oxygen excess / deficiency ΣOEDsc is short, comparing with the case where the cumulative period is long, a possibility of error occurring is low. Therefore, NOx being exhausted from the upstream side exhaust purification catalyst 20 due to the calculation error in the cumulative oxygen excess / deficiency ΣOEDsc can be prevented.

[0047] Further, in general, if the stored amount of oxygen of the exhaust purification catalyst is maintained constant, the exhaust purification catalyst falls in oxygen storage ability. That is, it is necessary that the oxygen storage amount of the exhaust purification catalyst is varied in order to maintain the oxygen storage ability of the exhaust purification catalyst at a high level. On the other hand, according to the present embodiment, as shown in FIG. 4, the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20 constantly fluctuates up and down, and therefore the oxygen storage ability is kept from falling.

[0048] Note that, in the above embodiment, the air-fuel ratio correction amount AFC is maintained to the lean set correction amount AFClean in the time t 1 to t 2 . However, in this period, the air-fuel ratio correction amount AFC is not necessarily maintained constant, and can be set so as to vary, for example to be gradually reduced. Alternatively, in the period from the time t 1 to time t 2 , the air-fuel ratio correction amount AFC may be temporally set to a value lower than 0 (for example, the rich set correction amount, etc.).

[0049] Similarly, in the above embodiment, the air-fuel ratio correction amount AFC is maintained to the rich set correction amount AFCrich in the time t 2 to t 3 . However, in this period, the air-fuel ratio correction amount AFC is not necessarily maintained constant, and can be set so as to vary, for example to be gradually increased. Alternatively, in the period from the time t 2 to time t 3 , the air-fuel ratio correction amount AFC may be temporarily set to a value higher than 0 (for example, the lean set correction amount, etc.).

[0050] Note that, in the present embodiment, setting of the air-fuel ratio correction amount AFC, i.e., setting of the target air-fuel ratio, is performed by the ECU 31. Therefore, it can be said that when the air-fuel ratio of the exhaust gas detected by the downstream side air-fuel ratio sensor 41 becomes the rich judgment air-fuel ratio or less, the ECU 31 makes the target air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 the lean air-fuel ratio continuously or intermittently until the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20 is estimated to become greater than or equal to the switching reference storage amount Cref, and when the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20 is estimated to become greater than or equal to the switching reference storage amount Cref, the ECU 31 makes the target air-fuel ratio the rich air-fuel ratio continuously or intermittently until the air-fuel ratio of the exhaust gas detected by the downstream side air-fuel ratio sensor 41 becomes less than or equal to the rich judgment air-fuel ratio without the stored amount of oxygen OSAsc reaching the maximum storable oxygen amount Cmaxn.

[0051] More simply speaking, in the present embodiment, it can be said that the ECU 31 switches the target air-fuel ratio (i.e. the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20) to the lean air-fuel ratio when the air-fuel ratio detected by the downstream side air-fuel ratio sensor 41 becomes less than or equal to the rich judgment air-fuel ratio and switches the target air-fuel ratio (i.e. the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20) to the rich air-fuel ratio when the stored amount of oxygen OSAsc of the upstream side exhaust purification catalyst 20 becomes greater than or equal to the switching reference storage amount Cref.<Explanation of Air-Fuel Ratio Control Using Also Downstream Side Exhaust Purification Catalyst>

[0052] Further, in the present embodiment, in addition to the upstream side exhaust purification catalyst 20, a downstream side exhaust purification catalyst 24 is also provided. The oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 become a value near the maximum storable oxygen amount Cmax by fuel cut control performed at a particular frequency. For this reason, even if exhaust gas containing unburned gas flows out from the upstream side exhaust purification catalyst 20, the unburned gas is oxidized and purified at the downstream side exhaust purification catalyst 24.

[0053] Note that, "fuel cut control" means control which prevents fuel from being injected from the fuel injectors 11, 12 during operation of the internal combustion engine (that is, during rotation of the crankshaft), at the time of deceleration of the vehicle in which the internal combustion engine is mounted. If performing such control, a large amount of air flows into the two exhaust purification catalysts 20, 24.

[0054] In the example which is shown in FIG. 4, fuel cut control is performed before the time t 0 . For this reason, before the time t 1 , the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 is a value near the maximum storable oxygen amount Cmax. Further, before the time t 1 , the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 is maintained at substantially the stoichiometric air-fuel ratio. For this reason, the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 is maintained constant.

[0055] After that, in part of the times t 1 to t 2 , the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 becomes the rich air-fuel ratio. For this reason, in this period, exhaust gas containing unburned gas flows into the downstream side exhaust purification catalyst 24.

[0056] However, as explained above, the downstream side exhaust purification catalyst 24 stores a large amount of oxygen. For this reason, if the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains unburned gas, the stored oxygen enables the unburned gas to be removed by oxidation. Further, along with this, the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 decreases. However, at the times t 1 to t 2 , the unburned gas flowing out from the upstream side exhaust purification catalyst 20 does not become that great, so the decrease in oxygen storage amount OSAufc during this period is slight. For this reason, at the time t 1 to t 2 , the unburned gas flowing out from the upstream side exhaust purification catalyst 20 is all removed by reduction in the downstream side exhaust purification catalyst 24.

[0057] At the time t 3 on as well, at each predetermined time interval, in the same way as the case of the times t 1 to t 2 , unburned gas flows out from the upstream side exhaust purification catalyst 20. This outflowing unburned gas is basically removed by reduction by the oxygen which is stored in the downstream side exhaust purification catalyst 24.<Effect of Reduction of Oxygen Storage Amount of Downstream Side Exhaust Purification Catalyst>

[0058] In this regard, fuel cut control is executed at the time of deceleration of a vehicle having an internal combustion engine etc., and therefore is not necessarily executed at every predetermined time interval. For this reason, in this case, fuel cut control sometimes is not executed over a long time period. In such a case, if unburned gas repeatedly flows out from the upstream side exhaust purification catalyst 20, the oxygen storage amount OSCufc of the downstream side exhaust purification catalyst 24 decreases toward zero. This situation is shown in FIG. 5.

[0059] FIG. 5 is a time chart of an air-fuel ratio correction amount AFC and an output air-fuel ratio AFdwn of the downstream side exhaust purification catalyst 24 etc. In the example shown in FIG. 5, at the times t 0 to t 1 , fuel cut control (FC control) is executed. For this reason, the output air-fuel ratio AFup of the upstream side air-fuel ratio sensor 40 and the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 become extremely large values. In addition, the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 and oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 respectively become the maximum storable amount of oxygen Cmax.

[0060] After that, at the times t 1 to t 2 , the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 is reduced as "post-reset rich control". In post-reset rich control, the air-fuel ratio correction amount AFC is set to a post-reset rich correction amount richer in absolute value than the rich set correction amount AFCrich. Due to this, a large amount of unburned gas flows into the upstream side exhaust purification catalyst 20. Along with this, the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 gradually decreases.

[0061] After that, if the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 approaches zero, unburned gas starts to flow out from the upstream side exhaust purification catalyst 20. At the time t 2 , the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 reaches the rich judged air-fuel ratio AFrich. In the present embodiment, if, during post-reset rich control, the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 becomes less than or equal to the rich judged air-fuel ratio AFrich, the air-fuel ratio control explained using FIG. 4 is executed. Therefore, at the time t 2 , the air-fuel ratio correction amount AFC is switched to the lean set correction amount AFClean.

[0062] In the example shown in FIG. 5, at the time t 2 , fuel cut control is not executed. Therefore, due to the above-mentioned air-fuel ratio control, the target air-fuel ratio is repeatedly alternately set to the rich air-fuel ratio and lean air-fuel ratio. For this reason, exhaust gas of substantially stoichiometric air-fuel ratio flows into the downstream side exhaust purification catalyst 24. Periodically, exhaust gas containing a large amount of unburned gas flows in. If, in this way, exhaust gas containing a large amount of unburned gas periodically flows into the downstream side exhaust purification catalyst 24, the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 gradually decreases and the ability to remove unburned gas and NO X in the downstream side exhaust purification catalyst 24 falls. Below, referring to FIGS. 6A and 6B, the purification ability of the downstream side exhaust purification catalyst 24 will be explained.

[0063] FIGS. 6A and 6B schematically show the surface of the carrier of the downstream side exhaust purification catalyst 24. In the illustrated example, the carrier of the downstream side exhaust purification catalyst 24 carries platinum (Pt) as a precious metal having a catalytic action. Further, "O 2 NON-STORING" in the figure shows the region where oxygen is not stored at the substance having an oxygen storage ability carried at the carrier (below, referred to as "oxygen storing substance"), while "O 2 STORING" shows the region where oxygen is being stored at the oxygen storage substance. Further, in the example shown in FIGS. 6A and 6B, exhaust gas flows on the surface of the carrier in the direction shown by the arrow in the figure. Therefore, at the left side of FIGS. 6A and 6B, the upstream side of the downstream side exhaust purification catalyst 24 is shown

[0064] FIG. 6A shows the state where exhaust gas of a rich air-fuel ratio flows into the downstream side exhaust purification catalyst 24. In the example shown in FIG. 6A, oxygen is released from the oxygen storage substance at only part of the upstream side of the downstream side exhaust purification catalyst 24. Here, the exhaust gas contains unburned HC and CO. For this reason, in the region where the oxygen storage substance stores oxygen, oxygen stored at the oxygen storage substance is released and reacts with the unburned HC and CO on the platinum whereby water and carbon dioxide are produced. As a result, the unburned HC and CO in the exhaust gas are reduced and removed. On the other hand, in the region in which the oxygen storage substance does not store oxygen, oxygen is not released even if unburned HC is deposited on the platinum or surface of the carrier. As a result, in the region in which the oxygen storage substance does not store oxygen, the unburned HC is physically adsorbed on the surface of the carrier.

[0065] If unburned gas continues to flow to the downstream side exhaust purification catalyst 24, the oxygen stored at the oxygen storage substance is successively released. As a result, as shown in FIG. 6B, at most of the parts of the downstream side exhaust purification catalyst 24, the state becomes one where the oxygen storage substance releases oxygen. At only part of the downstream side, the state becomes one where the oxygen storage substance stores oxygen. As a result, as shown in FIG. 6B, if exhaust gas of a rich air-fuel ratio flows into the downstream side exhaust purification catalyst 24, a reaction occurs between the unburned HC and CO in the exhaust gas and the oxygen at only part of the region at the downstream side. At most of the parts of the downstream side exhaust purification catalyst 24, unburned HC is successively physically adsorbed on the platinum or on the surface of the carrier and the physically adsorbed unburned HC covers most of the surface of the platinum.

[0066] If, in this way, unburned HC covers the surface of the platinum, the platinum no longer exhibits a sufficient catalytic action. Therefore, even if unburned gas, NO X and / or oxygen is present around the platinum, the reaction speed becomes slower. As a result, in the region where unburned HC covers the surface of the platinum, the ability to remove unburned gas and NO X falls. Such a phenomenon is called "HC poisoning" of the exhaust purification catalyst. Furthermore, as will be understood from FIG. 6B, the region where HC poisoning occurs increases along with the decrease of the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24. Therefore, as shown in FIG. 5, the rate of removal of unburned gas or NO X in the downstream side exhaust purification catalyst 24 falls along with the decrease of the oxygen storage amount OSAufc if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 falls by a certain extent or more.

[0067] In this regard, the unburned gas or NO X in the exhaust gas discharged from the engine body is not completely removed at the upstream side exhaust purification catalyst 20 even if the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 is a suitable amount. This situation is shown in FIG. 7.

[0068] FIG. 7 schematically shows the concentration of oxygen and NO X in the exhaust gas, the concentration of unburned gas (unburned HC and CO), and the air-fuel ratio at different parts of the exhaust passage. FIG. 7 shows the case where the air-fuel ratio of the exhaust gas discharged from the engine body is a lean air-fuel ratio. As shown in FIG. 7, since the exhaust gas discharged from the engine body is a lean air-fuel ratio, the exhaust gas flowing through the inside of the exhaust manifold 19 contains a larger amount of oxygen and NO X compared with when the exhaust gas is a stoichiometric air-fuel ratio. In addition, the exhaust gas also contains unburned gas, though not that much.

[0069] If such exhaust gas flows into the upstream side exhaust purification catalyst 20, the oxygen in the exhaust gas is stored at the upstream side exhaust purification catalyst 20, and therefore the air-fuel ratio of the exhaust gas becomes the stoichiometric air-fuel ratio. In addition, at the upstream side exhaust purification catalyst 20, the unburned gas and NO X in the exhaust gas and oxygen react whereby the unburned gas and NO X are removed. However, at the upstream side exhaust purification catalyst 20, not all of the unburned gas and NO X in the exhaust gas is necessarily removed. Part flows out from the upstream side exhaust purification catalyst 20.

[0070] As a result, as shown in FIG. 7, the air-fuel ratio of the exhaust gas flowing through the inside of the exhaust pipe 22 becomes substantially the stoichiometric air-fuel ratio. This exhaust gas contains a small amount of unburned gas and a small amount of NO X and oxygen remaining in it. Therefore, exhaust gas of a stoichiometric air-fuel ratio containing unburned gas and NO X flows into the downstream side exhaust purification catalyst 24.

[0071] Here, as explained above, if the HC poisoning of the downstream side exhaust purification catalyst 24 proceeds, the ability of the downstream side exhaust purification catalyst 24 to remove unburned gas or NO X falls. For this reason, if the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains a large amount of unburned gas and NO X , sometimes these unburned gas and NO X cannot be completely removed. Therefore, as shown in FIG. 6B, when HC poisoning due to unburned HC occurs at the downstream side exhaust purification catalyst 24, it becomes necessary to remove the adsorbed unburned HC so as to restore the purification ability of the downstream side exhaust purification catalyst 24.<Suppression of HC Poisoning Due to Inflow of NO X >

[0072] In this regard, as shown in FIG. 6B, even if unburned HC partially covers the surface of the platinum at the downstream side exhaust purification catalyst 24, if the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains oxygen and / or NO X , the unburned HC will react with the oxygen and / or NO X . As a result, it is possible to remove unburned HC adsorbed at the carrier of the downstream side exhaust purification catalyst 24. This situation is shown in FIG. 8.

[0073] FIG. 8 is a view, similar to FIGS. 6A and 6B, schematically showing the surface of the carrier at the downstream side exhaust purification catalyst 24. In particular, in the example shown in FIG. 8, the case is shown where the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains NO X . If exhaust gas contains NO X in this way, the NO X in the exhaust gas reacts with the unburned HC adsorbed on the platinum of the downstream side exhaust purification catalyst 24 and, as a result, unburned HC on the platinum is removed.

[0074] However, as explained above, in this case, the purification ability falls, and therefore if the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains oxygen and NO X in large amounts, the inflowing NO X cannot be sufficiently removed. That is, the NO X in the inflowing exhaust gas ends up flowing out without being removed at the downstream side exhaust purification catalyst 24.

[0075] Here, as the method of making exhaust gas containing oxygen or NO X flow into the downstream side exhaust purification catalyst 24, it may be considered to maintain the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 at the lean air-fuel ratio even if the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 reaches substantially the maximum storable amount of oxygen Cmax. Due to this, the oxygen in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is not stored in the upstream side exhaust purification catalyst 20 but flows out as-is from the upstream side exhaust purification catalyst 20. Along with this, the NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 also flows out as-is from the upstream side exhaust purification catalyst 20. However, with such a method, the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains a large amount of oxygen and NO X . As a result, the oxygen and NO X are not sufficiently removed at the downstream side exhaust purification catalyst 24, and flow out from the downstream side exhaust purification catalyst 24. In particular, NO X is lower in reactivity with unburned HC as compared with oxygen, and therefore most of the NO X is not removed at the downstream side exhaust purification catalyst 24 but flows out from the downstream side exhaust purification catalyst 24.

[0076] In this regard, the oxygen contained in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is removed by the unburned gas contained in the inflowing exhaust gas or is stored in the upstream side exhaust purification catalyst 20. For this reason, so long as the oxygen storage amount OSA of the upstream side exhaust purification catalyst 20 does not reach the vicinity of the maximum storable amount of oxygen, regardless of the air-fuel ratio of the exhaust gas, even if the exhaust gas flowing into the upstream side exhaust purification catalyst 20 contains oxygen, not much oxygen will flow out from the upstream side exhaust purification catalyst 20. Therefore, when the oxygen storage amount OSA of the upstream side exhaust purification catalyst 20 does not reach the vicinity of the maximum storable amount of oxygen, even if the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is set to change somewhat to the lean side, that is, even if the amount of oxygen flowing into the upstream side exhaust purification catalyst 20 is increased, the amount of oxygen contained in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 does not change significantly.

[0077] On the other hand, the NO X contained in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is removed by the unburned gas contained in the inflowing exhaust gas. However, NO X is lower in reactivity with unburned gas compared with oxygen. For this reason, when both oxygen and NO X are present in the exhaust gas, the unburned gas first reacts with the oxygen. Therefore, NO X does not completely react at the upstream side exhaust purification catalyst 20, but partially remains. Further, NO X itself is not stored in the upstream side exhaust purification catalyst 20.

[0078] Due to such a property, both when the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is the lean air-fuel ratio and when it is the rich air-fuel ratio, if the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 becomes higher, the concentration of NO X in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 also becomes higher. That is, by making the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 higher, the concentration of NO X in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 can be raised. Further, such a phenomenon occurs when the oxygen storage amount OSA of the upstream side exhaust purification catalyst 20 is a suitable amount. For this reason, even if the concentration of NO X in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 becomes high, a large amount of NO X will never flow into the downstream side exhaust purification catalyst 24 such as when the oxygen storage amount OSA of the upstream side exhaust purification catalyst 20 reaches the vicinity of the maximum storable amount of oxygen Cmax and when oxygen or NO X cannot be sufficiently removed at the upstream side exhaust purification catalyst 20.<Control for Increasing NO X >

[0079] Therefore, in the present embodiment, when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes less than or equal to a predetermined limit storage amount smaller than the maximum storable amount of oxygen Cmax, the concentration of oxygen in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 is not allowed to increase, but the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 is caused to increase as "control for increasing NO X ". This will be explained referring to FIG. 9.

[0080] FIG. 9 is a time chart, similar to FIG. 5, of the air-fuel ratio correction amount AFC, presence of control for increasing NO X , etc. In the example shown in FIG. 9, in the same way as the example shown in FIG. 5, at the times t 0 to t 1 , fuel cut control is executed, while at the times t 1 to t 2 , post-reset rich control is executed. In addition, from the time t 2 onward, the air-fuel ratio control such as shown in FIG. 4 is executed.

[0081] As explained above, from the time t 2 onward, due to execution of air-fuel ratio control, the oxygen storage amount OSAsc of the downstream side exhaust purification catalyst 24 gradually decreases. In the example shown in FIG. 9, at the time t 10 , the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 becomes the rich judged air-fuel ratio AFrich or less and the air-fuel ratio correction amount AFC is switched from the rich set correction amount AFCrich to the lean set correction amount AFClean. At this time, exhaust gas of a rich air-fuel ratio flows out from the upstream side exhaust purification catalyst 20. Along with this, the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 is decreased. As a result, in the example shown in FIG. 9, at the time t 11 , the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 reaches the limit storage amount Clim.

[0082] In the present embodiment, if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes less than or equal to the limit storage amount Clim, the control for increasing NO X is started. Here, the limit storage amount Clim is set at an amount such that the HC poisoning of the downstream side exhaust purification catalyst 24 starts to advance if the above-mentioned air-fuel ratio control is executed after fuel cut control without executing control for increasing NO X . Specifically, the limit storage amount Clim is set at a value of 2 / 3 to 1 / 10 of the maximum storable amount of oxygen Cmax at the time before use, preferably a value within 1 / 2 to 1 / 7, more preferably a value within 1 / 3 to 1 / 5.

[0083] Note that, the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24, in the same way as the upstream side exhaust purification catalyst 20, is estimated based on the cumulative value ΣOEDufc of the oxygen excess / deficiency in the exhaust gas flowing into the downstream side exhaust purification catalyst 24. Further, the oxygen excess / deficiency OEDufc in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 is calculated by the following formula (2). OEDsc = 0.23 × Qi × AFdwn − AFS Here, AFdwn shows the output air-fuel ratio of the downstream side air-fuel ratio sensor 41, while AFS shows the stoichiometric air-fuel ratio.

[0084] Due to this, the amount of NO X flowing into the upstream side exhaust purification catalyst 20 is caused to increase. As a result, the amount of NO X flowing out from the upstream side exhaust purification catalyst 20 also increases. However, as explained later, in control for increasing NO X , the air-fuel ratio of the exhaust gas flowing into the upstream side exhaust purification catalyst 20 does not greatly fluctuate. Therefore, even after control for increasing NO X is started, the output air-fuel ratio AFup of the upstream side air-fuel ratio sensor 40 does not change significantly.

[0085] Further, even during control for increasing NO X , the above-mentioned air-fuel ratio control continues to be executed. Therefore, if, at the time t 12 , it is estimated that the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 has reached the switching reference storage amount Cref, that is, if the cumulative oxygen excess / deficiency ΣOEDufc of the exhaust gas flowing into the downstream side exhaust purification catalyst 24 reaches the switching reference value OEDref, the air-fuel ratio correction amount AFC is switched to the lean set air-fuel ratio AFClean.

[0086] After that, at the time t 13 after the elapse of a predetermined reference execution time from the time t 11 , the control for increasing NO X is terminated. The predetermined reference execution time is set to enable desorption of most of the unburned HC which had been adsorbed when HC poisoning causes unburned HC to be adsorbed on the platinum or carrier at the downstream side exhaust purification catalyst 24. Note that, the timing of end of the control for increasing NO X does not necessarily have to be judged based on the time of execution of control for increasing NO X . For example, control for increasing NO X may be ended when the total amount of flow of exhaust gas flowing into the downstream side exhaust purification catalyst 24 from when starting control for increasing NO X reaches a predetermined reference total amount of flow.

[0087] Even after the end of control for increasing NO X , the above-mentioned air-fuel ratio control continues to be executed. Therefore, if at the time t 14 the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 becomes the rich judged air-fuel ratio AFrich or less, the air-fuel ratio correction amount AFC is switched from the lean set correction amount AFClean to the rich set correction amount AFCrich. After that, if, at the time t 15 , it is estimated that the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 has reached the switching reference storage amount Cref, the air-fuel ratio correction amount AFC is switched to the lean set air-fuel ratio AFClean.<Effect of Control for Increasing NO X >

[0088] As will be understood from FIG. 9, in the present embodiment, when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes the limit storage amount Clim or less, that is, when HC poisoning of the downstream side exhaust purification catalyst 24 starts to advance, control for increasing NO X is started. If control for increasing NO X is started, the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increases. Here, as explained above, if the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increases, the concentration of NO X in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 increases. Therefore, the concentration of NO X in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 is increased. If the concentration of NO X in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 in this way is increased, in the downstream side exhaust purification catalyst 24, the NO X reacts not only with the unburned gas in the exhaust gas but also the unburned HC adsorbed on the platinum or carrier. As a result, it is possible to remove the unburned HC adsorbed on the platinum or carrier of the downstream side exhaust purification catalyst 24 and possible to clear HC poisoning of the downstream side exhaust purification catalyst 24. Therefore, as shown in FIG. 9 by the solid line, it is possible to limit or prevent a fall in the rate of removal of unburned gas or NO X of the downstream side exhaust purification catalyst 24 (note that, in the figure, the broken line shows the trend in the rate of removal of the case where no control for increasing NO X is executed).

[0089] Further, even during execution of control for increasing NO X , the above-mentioned air-fuel ratio control continues to be maintained. For this reason, the oxygen storage amount OSAsc of the upstream side exhaust purification catalyst 20 never reaches the vicinity of the maximum storable amount of oxygen Cmax. Therefore, the oxygen storage ability of the upstream side exhaust purification catalyst 20 is maintained and exhaust gas of a lean air-fuel ratio will not flow out from the upstream side exhaust purification catalyst 20. That is, the ability of the upstream side exhaust purification catalyst 20 to remove NO X is maintained as it is. Further, during execution of control for increasing NO X , the concentration of NO X in the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 increases, but not significantly. Therefore, during execution of control for increasing NO X , a large amount of NO X unable to be removed by the downstream side exhaust purification catalyst 24 will never flow into the downstream side exhaust purification catalyst 24. For this reason, it is possible to maintain the ability of the exhaust purification system to remove NO X .

[0090] Note that, in the above embodiment, after fuel cut control, when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes the limit storage amount or less, the control for increasing NO X is executed only once. However, even if executing the control for increasing NO X once to remove the unburned HC adsorbed at the downstream side exhaust purification catalyst 24, after that, again the unburned HC starts to be adsorbed at the downstream side exhaust purification catalyst 24. Therefore, the control for increasing NO X is preferably executed several times until fuel cut control is again executed.

[0091] When executing this control for increasing NO X several times, the second cycle of the control for increasing NO X is executed when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes less than or equal to a second limit storage amount smaller than the limit storage amount (below, referred to as "the first limit storage amount"). Further, the third cycle of the control for increasing NO X is executed when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes less than or equal to a third limit storage amount smaller than the second limit storage amount. In this way, when executing the control for increasing NO X several times, the control for increasing NOx is executed when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 reaches a limit storage amount smaller than the previous limit storage amount. Further, the difference of the first limit storage amount and the second limit storage amount and the difference of the second limit storage amount and the third limit storage amount are set so as to become smaller than the difference between the maximum storable amount of oxygen and the first limit storage amount.<Specific Example of Control for Increasing NO X >

[0092] Next, a specific example of control for increasing NO X will be explained. As one example of control for increasing NO X , advancing the timing of ignition of the air-fuel mixture by the spark plug 10 may be mentioned. FIG. 10 is a view showing the relationship between the timing of ignition by the spark plug 10 and the concentration of NO X and HC flowing out from the engine body. As will be understood from FIG. 10, even if changing the ignition timing, the concentration of unburned HC in the exhaust gas flowing out from the engine body does not change significantly. As opposed to this, if making the ignition timing advance, the concentration of NO X in the exhaust gas flowing out from the engine body becomes higher. This is because the more advanced the ignition timing, the more the combustion temperature of the air-fuel mixture in the combustion chamber 5 rises and thereby the more the amount of NO X in the exhaust gas increases.

[0093] Further, even if the ignition timing is changed in this way, the amounts of fuel injected by the fuel injectors 11, 12 are not changed, and therefore the air-fuel ratio of the air-fuel mixture in the combustion chamber 5 does not change. Therefore, the concentration of oxygen in the exhaust gas flowing out from the engine body basically does not change. Therefore, by making the ignition timing advance, the concentration of oxygen in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 does not increase. Only the concentration of NO X is increased.

[0094] Due to the above, in the first cycle of the control for increasing NO X , the timing of ignition of the air-fuel ratio by the spark plug 10 is advanced compared to when not executing the control for increasing NO X . Due to this, it is possible to make only the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increase without making the concentration of oxygen increase.

[0095] Further, as another example of the control for increasing NO X , it may be considered to decrease the amount of EGR. As shown in FIG. 1, the internal combustion engine of the present embodiment is provided with an EGR mechanism having an EGR gas conduit 26 and an EGR control valve 27. This EGR mechanism is used to feed part of the exhaust gas discharged from a combustion chamber 5 of the internal combustion engine again to the combustion chamber 5. In such an EGR mechanism, the concentration of NO X and HC flowing out from the engine body according to the amount of exhaust gas fed by the EGR mechanism to a combustion chamber 5 (amount of EGR) changes.

[0096] FIG. 11 is a view showing the relationship between the amount of EGR and the concentration of NO X and HC flowing out from the engine body. As will be understood from FIG. 11, if the amount of EGR is decreased, along with this, the concentration of unburned HC decreases or the concentration of NO X increases. This is because by decreasing the amount of EGR, the combustion temperature of the air-fuel mixture in the combustion chamber 5 rises and thereby the amount of NO X in the exhaust gas increases.

[0097] Further, even if changing the amount of EGR in this way, the ratio of air and fuel flowing into a combustion chamber 5 will not change, therefore the air-fuel ratio of the air-fuel mixture in the combustion chamber 5 will not change. Therefore, the concentration of oxygen in the exhaust gas flowing out from the engine body basically does not change. For this reason, by decreasing the amount of EGR, only the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increases without the concentration of oxygen being increased.

[0098] Due to the above, in the second cycle of control for increasing NO X , the amount of EGR is decreased compared with when not executing the control for increasing NO X . Due to this, it is possible to make only the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increase without making the concentration of oxygen increase.

[0099] As still another example of the control for increasing NO X , it may be considered to adjust the ratio of the amounts of fuel injection from the cylinder fuel injector 11 and the port fuel injector 12. Here, as shown in FIG. 1, the internal combustion engine of the present embodiment has, for each cylinder, a cylinder fuel injector 11 injecting and feeding fuel directly into a combustion chamber 5 and a port fuel injector 12 injecting and feeding fuel into an intake passage of the intake port 7 etc. In such an internal combustion engine, the concentration of NO X and HC flowing out from the engine body changes in accordance with the ratio of feed of fuel of the cylinder fuel injector 11 and the port fuel injector 12.

[0100] FIG. 12 is a view showing the relationship between the ratio of feed of fuel of the cylinder fuel injector 11 and the port fuel injector 12 (selective injection ratio) and the concentration of NO X and HC flowing out from the engine body. As will be understood from FIG. 12, if increasing the ratio of feed of fuel from the port fuel injector 12 from the state of injecting fuel from only the cylinder fuel injector 11 (in figure, DI: 100%), the concentration of unburned HC decreases and the concentration of NO X increases along with this. The reason why the concentration of NO X increases in this way is as follows: That is, if injecting fuel from the port fuel injector 12, the fuel and air are sufficiently mixed from injection of fuel until ignition. For this reason, in the combustion chamber 5, the air-fuel mixture is burned well. As a result, the combustion temperature of the air-fuel mixture rises. If the combustion temperature of the air-fuel mixture rises in this way, the amount of NO X in the exhaust gas increases along with this.

[0101] Further, even if changing the selective injection ratio in this way, the ratio of air and fuel fed into a combustion chamber 5 up until the time of combustion does not change, and therefore the air-fuel ratio of the air-fuel mixture in the combustion chamber 5 does not change. Therefore, the concentration of oxygen in exhaust gas flowing out from the engine body basically does not change. For this reason, the ratio of the amount of fuel injection from the port fuel injector 12 to the amount of fuel injection from the cylinder fuel injector 11, defined as the "intake passage injection ratio", is increased to thereby make only the concentration of NO X increase without making the concentration of oxygen in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increase.

[0102] From the above, in the third cycle of the control for increasing NO X , compared with when not executing the control for increasing NO X , the intake passage injection ratio is increased. Due to this, it is possible to make only the concentration of NO X in the exhaust gas flowing into the upstream side exhaust purification catalyst 20 increase without making the concentration of oxygen increase.<Condition for Execution of Control Increasing NO X >

[0103] In this regard, as explained above, if unburned HC is adsorbed on the downstream side exhaust purification catalyst 24, if exhaust gas containing NO X flows into the downstream side exhaust purification catalyst 24, the unburned HC and NO X will react and the unburned HC will be removed. Such a reaction between the unburned HC and NO X does not sufficiently occur if the temperature of the downstream side exhaust purification catalyst 24 is low. Therefore, from this viewpoint, in order for the above-mentioned control for increasing NO X to be executed, the temperature of the downstream side exhaust purification catalyst 24 has to be above a certain temperature. Conversely, when the temperature of the downstream side exhaust purification catalyst 24 is low, if control for increasing NO X is executed, there is a possibility that the NO X in the exhaust gas flowing into the downstream side exhaust purification catalyst 24 will end up flowing out as-is without being removed at the downstream side exhaust purification catalyst 24.

[0104] Therefore, in the present embodiment, a temperature sensor (not shown) which detects the temperature of the downstream side exhaust purification catalyst 24 is used to detect the temperature of the downstream side exhaust purification catalyst 24. Further, when the temperature of the downstream side exhaust purification catalyst 24 is less than a predetermined lower limit temperature, even if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes the limit storage amount Clim or less, control for increasing NOX is not executed. Here, the lower limit temperature is a temperature where the unburned HC adsorbed at the downstream side exhaust purification catalyst 24 and the NOX in the exhaust gas will not sufficiently react if the temperature of the downstream side exhaust purification catalyst 24 falls any further, for example, 500°C.

[0105] When, in this way, the temperature of the downstream side exhaust purification catalyst 24 is low, control for increasing NO X is not executed, and therefore it is possible to keep the NO X flowing into the downstream side exhaust purification catalyst 24 from ending up flowing out as-is without being removed at the downstream side exhaust purification catalyst 24.

[0106] Note that, when the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 becomes less than or equal to the limit storage amount Clim, if the temperature of the downstream side exhaust purification catalyst 24 is less than the lower limit temperature, the temperature of the downstream side exhaust purification catalyst 24 may also be raised as "temperature raising control". As the temperature raising control, for example, it may be considered to make the combustion air-fuel ratio the rich air-fuel ratio at part of the cylinders among the plurality of cylinders and make the combustion air-fuel ratio the lean air-fuel ratio at the remaining cylinders also known as "dither control".

[0107] Further, as explained above, during the control for increasing NO X , the exhaust gas flowing into the downstream side exhaust purification catalyst 24 contains NO X , but the concentration is basically not that high. However, for example, at the time of engine high load operation or the time of engine high speed operation, the amount of flow of exhaust gas discharged from the engine body becomes great and therefore the amount of flow of the exhaust gas flowing into the downstream side exhaust purification catalyst 24 becomes greater. If, in this way, the amount of flow of the exhaust gas flowing into the downstream side exhaust purification catalyst 24 becomes greater, even if the concentration of NO X in the exhaust gas is not that high, the amount of NO X flowing into the downstream side exhaust purification catalyst 24 per unit time increases. In this way, if a large amount of NO X flows into the downstream side exhaust purification catalyst 24 per unit time, part of the inflowing NO X will not react with the unburned HC adsorbed on the downstream side exhaust purification catalyst 24 but will end up flowing out from the downstream side exhaust purification catalyst 24.

[0108] Therefore, in the present embodiment, when the amount of flow of exhaust gas discharged from the engine body is a predetermined upper limit flow or more, even if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 is less than or equal to the limit storage amount Clim, control for increasing NO X is not executed. Here, the upper limit flow is the amount of flow of exhaust gas flowing into the downstream side exhaust purification catalyst 24at or above which, even if unburned HC is adsorbed on the downstream side exhaust purification catalyst 24, the NO X in the inflowing exhaust gas is no longer sufficiently removed, for example, is 10 g / s. Further, the amount of flow of exhaust gas discharged from the engine body is calculated or estimated based on the amount of flow of air detected by the air flow meter 39. The amount of flow of intake air detected by the air flow meter 39 may be used as-is as the amount of flow of exhaust gas discharged from the engine body.<Flow Chart of Processing for Setting Air-Fuel Ratio Correction Amount>

[0109] FIG. 13 is a flow chart showing the control routine for control for setting the air-fuel ratio correction amount. The illustrated control routine is performed by interruption at certain time intervals.

[0110] As shown in FIG. 13, first, at step S11, it is judged if the condition for calculation of the air-fuel ratio correction amount AFC stands. As the case where the condition for calculation of the air-fuel ratio correction amount AFC stands, being in the middle of normal control where feedback control is performed and, for example, not being in the middle of fuel cut control etc. may be mentioned. When at step S11 it is judged that the condition for calculation of the target air-fuel ratio stands, the routine proceeds to step S12.

[0111] At step S12, it is judged if the lean set flag Fl is set OFF. The lean set flag Fl is set ON when the air-fuel ratio correction amount AFC is set to the lean set correction amount AFClean and is set OFF in other cases. When at step S12 the lean set flag Fl is set OFF, the routine proceeds to step S13. At step S13, it is judged if the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 is less than or equal to the rich judged air-fuel ratio AFrich. If it is judged that the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 is larger than the rich judged air-fuel ratio AFrich, the routine proceeds to step S14. At step S14, the air-fuel ratio correction amount AFC is maintained as set to the rich set correction amount AFCrich, and the control routine is terminated.

[0112] On the other hand, if the oxygen storage amount OSA of the upstream side exhaust purification catalyst 20 is decreased and the air-fuel ratio of the exhaust gas flowing out from the upstream side exhaust purification catalyst 20 falls, at step S13, it is judged that the output air-fuel ratio AFdwn of the downstream side air-fuel ratio sensor 41 is the rich judged air-fuel ratio AFrich or less. In this case, the routine proceeds to step S15, where the air-fuel ratio correction amount AFC is switched to the lean set correction amount AFClean. Next, at step S16, the lean set flag Fl is set ON, then the control routine is terminated.

[0113] If the lean set flag Fl is set ON, at the next control routine, at step S12, it is judged that the lean set flag Fl is not set OFF, then the routine proceeds to step S17. At step S17, it is judged if the cumulative oxygen excess / deficiency ΣOED from when the air-fuel ratio correction amount AFC was switched to the lean set correction amount AFClean is smaller than the switching reference value OEDref. If it is judged that the cumulative oxygen excess / deficiency ΣOED is smaller than the switching reference value OEDref, the routine proceeds to step S18, where the air-fuel ratio correction amount AFC continues to be maintained as set to the lean set correction amount AFClean, then the control routine is terminated. On the other hand, if the oxygen storage amount of the upstream side exhaust purification catalyst 20 increases, at step S17, it is judged that the cumulative oxygen excess / deficiency ΣOED is greater than or equal to the switching reference value OEDref, and the routine proceeds to step S19. At step S19, the air-fuel ratio correction amount AFC is switched to the rich set correction amount AFCrich. Next, at step S20, the lean set flag Fl is reset OFF, then the control routine is terminated.<Flow Chart of Processing for Executing Increasing Control>

[0114] FIG. 14 is a flow chart showing a control routine of processing for executing increasing control judging the start of execution of control for increasing NO x . The illustrated control routine is executed by interruption at predetermined time intervals.

[0115] First, at step S31, it is judged if the execute flag Fd of the control for increasing NO x has become OFF. The execute flag Fd is set ON when the control for increasing NO x is executed and is set OFF when it is not executed. When control for increasing NO x is not being executed and therefore the execute flag Fd is OFF, the routine proceeds to step S32. At step S32, it is judged if the already executed flag Fe has become ON. The already executed flag Fe is set ON when control for increasing NO x is already being executed after fuel cut control was previously executed and is set OFF when control increasing NO x is still not being executed. Note that, the already executed flag Fe is reset to OFF if fuel cut control is executed.

[0116] If at step S32 it is judged that the already executed flag Fe is OFF, that is, if control for increasing NO x is still not executed after the previous fuel cut control, the routine proceeds to step S33. At step S33, it is judged that the cumulative oxygen excess / deficiency ΣOEDufc of the downstream side exhaust purification catalyst 24 after the end of fuel cut control has become greater than or equal to a first reference value OEDref1. That is, it can be said that at step S33 it is judged if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 has become the limit storage amount Clim or less. When at step S33 it is judged that the cumulative oxygen excess / deficiency ΣOEDufc of the downstream side exhaust purification catalyst 24 is smaller than the first reference value OEDref1, the oxygen storage amount OSAref1 of the downstream side exhaust purification catalyst 24 does not fall significantly. Therefore, the HC poisoning of the downstream side exhaust purification catalyst 24 also does not advance. Therefore, in this case, control for increasing NO x is not executed and the control routine is terminated. On the other hand, when at step S33 it is judged that the cumulative oxygen excess / deficiency ΣOEDufc to the downstream side exhaust purification catalyst 24 is greater than or equal to the first reference value OEDref1, the routine proceeds to step S34. At step S34, the execute flag Fd is set to ON. As a result, due to the processing for increasing NO x shown in FIG. 15, control for increasing NO x is started. Next, at step S35, the already executed flag Fe is set to ON, and the control routine is terminated.

[0117] In the control routine after the processing for increasing NO x ends, the already executed flag Fe is set to ON, and therefore the routine proceeds from step S32 to step S36. At step S36, after the end of the previous processing for increasing NO x , it is judged if the cumulative oxygen excess / deficiency ΣOEDufc to the downstream side exhaust purification catalyst 24 has become a second reference value OEDref2 or more. That is, at step S36, it can be said to be judged if the oxygen storage amount OSAufc of the downstream side exhaust purification catalyst 24 is less than or equal to the second limit storage amount or the third limit storage amount. Note that, the second reference value OEDref2 is a value smaller than the first reference value OEDref1 and is a value equal to the difference between the above-mentioned first limit storage amount and second limit storage amount.

[0118] If at step S36 the cumulative oxygen excess / deficiency ΣOEDufc at the downstream side exhaust purification catalyst 24 is smaller than the second reference value OEDref2, HC poisoning of the downstream side exhaust purification catalyst 24 does not advance. Therefore, in this case, the control for increasing NO x is not executed and the control routine is terminated. On the other hand, if at step S36 it is judged that the cumulative oxygen excess / deficiency ΣOEDufc at the downstream side exhaust purification catalyst 24 is greater than or equal to the second reference value OEDref2, the routine proceeds to step S37. At step S37, the execute flag Fd is turned ON and, as a result, control for increasing NO x is started by the processing for increasing NO x shown in FIG. 15.<Flow Chart of Processing for Increasing NO x >

[0119] FIG. 15 is a flow chart showing a control routine of processing for increasing NO x . The illustrated control routine is executed by interruption at predetermined time intervals.

[0120] First, at step S41, it is judged of a flag Fd for executing control for increasing NO x is ON. When it is judged the execute flag Fd is OFF, the control routine is terminated. On the other hand, when the execute flag Fd is set ON at steps S34 and S37 of FIG. 14, it is judged at step S41 that the execute flag Fd becomes ON and the routine proceeds to step S42. At step S42, the output of the temperature sensor detecting the temperature of the downstream side exhaust purification catalyst 24 is used as the basis to judge if the temperature Tcat of the downstream side exhaust purification catalyst 24 is greater than or equal to the lower limit temperature Tcref. When at step S42 it is judged that the temperature Tcat of the downstream side exhaust purification catalyst 24 is the lower limit temperature Tcref or more, the routine proceeds to step S43. At step S43, it is judged if the intake air amount Ga which is detected by the air flow meter 39 is greater than or equal to the upper limit flow amount Gref. When at step S43 it is judged that the intake air amount Ga is greater than or equal to the upper limit flow amount Gref, the routine proceeds to step S44.

[0121] At step S44, it is judged if the time T for execution of control for increasing NO x , that is, the elapsed time T from when the execute flag FD is turned ON (minus time during which control for increasing NO x is stopped) is greater than or equal to the reference time Tref. When little time has elapsed from when control for increasing NO x is started, it is judged that the execution time T is shorter than the reference time Tref and the routine proceeds to step S45. At step S45, control for increasing NO x is executed. Therefore, for example, compared with when not executing control for increasing NO x , the timing of ignition by the spark plug 10 is advanced. After that, the control routine is terminated.

[0122] On the other hand, if at step S42 it is judged that the temperature Tcat of the downstream side exhaust purification catalyst 24 is less than the lower limit temperature Tcref, if executing control for increasing NO x , there is a possibility of NO x flowing out from the downstream side exhaust purification catalyst 24, and therefore the routine proceeds from step S42 to step S48. Further, even if at step S43 it is judged that the intake air amount Ga is less than the upper limit flow amount Gref, if executing control for increasing NO x , there is a possibility of NO x flowing out from the downstream side exhaust purification catalyst 24, and therefore the routine proceeds from step S43 to step S48. At step S48, the control for increasing NO x is stopped. Therefore, for example, compared with when executing control for increasing NO x , the timing of ignition by the spark plug 10 is delayed. After that, the control routine is terminated.

[0123] After that, if the time for execution of control for increasing NO x becomes longer, at the next control routine, it is judged at step S44 that the time T for execution of control for increasing NO x is greater than or equal to the reference time Tref, and the routine proceeds to step S46. At step S46, the control for increasing NO x is terminated. Next, at step S47, the execute flag Fd is reset to OFF, then the control routine is terminated.

[0124] Although this invention has been described by way of the specific embodiments, this invention is not limited to the above embodiments. The invention is defined by the appended claims.

Claims

1. An exhaust purification system of an internal combustion engine comprising: an upstream side catalyst (20) provided in an exhaust passage of the internal combustion engine; a downstream side catalyst (24) provided at a downstream side from the upstream side catalyst (20) in the direction of exhaust flow in the exhaust passage; an upstream side air-fuel ratio sensor (40) provided in the exhaust passage at an upstream side from the upstream side catalyst (20); a downstream side air-fuel ratio sensor (41) provided between the upstream side catalyst (20) and the downstream side catalyst (24) in the exhaust passage; and a control device (31) configured to be able to control a fuel feed amount from a fuel injector of the internal combustion engine so that the output air-fuel ratio of the upstream side air-fuel ratio sensor (40) becomes a target air-fuel ratio, as air-fuel ratio control, wherein the target air-fuel ratio being set based on the output of the downstream side air-fuel ratio sensor (41), the control device (31) is further configured to: switch the target air-fuel ratio to a lean air-fuel ratio leaner than the stoichiometric air-fuel ratio when the output air-fuel ratio of the downstream side air-fuel ratio sensor (41) becomes less than or equal to a constant rich judged air-fuel ratio richer than the stoichiometric air-fuel ratio and switch the target air-fuel ratio to a rich air-fuel ratio richer than the stoichiometric air-fuel ratio when the oxygen storage amount (OSAsc) of the upstream side catalyst (20), calculated based on the output air-fuel ratio of the upstream side air-fuel sensor (40), and an intake air amount or the fuel feed amount from the fuel injector, becomes greater than or equal to a switching reference storage amount smaller than the maximum storable amount of oxygen in the air-fuel ratio control; the control device (31) is characterised in being configured to control for increasing NOx by causing the concentration of NOx in the exhaust gas flowing into the upstream side catalyst (20) to increase without causing the concentration of oxygen in the exhaust gas flowing into the upstream side catalyst (20) to increase, said control for increasing NOx being executed when the oxygen storage amount (OSAufc) of the downstream side catalyst (24), calculated based on the output air-fuel ratio of the downstream side air-fuel sensor (41), and the fuel feed amount from the fuel injector, becomes less than or equal to a predetermined limit storage amount (Clim) smaller than the maximum storable amount of oxygen during the air-fuel ratio control, wherein the control device (31) is further configured to: - when the exhaust purification system further comprises a spark plug (10) igniting an air-fuel mixture in a combustion chamber of the internal combustion engine, cause the timing of ignition of the air-fuel mixture by the spark plug (10) to advance and thereby increase the concentration of NOx in the exhaust gas flowing into the upstream side catalyst (20) in the control for increasing NOx, or - when the exhaust purification system further comprises an EGR mechanism feeding part of the exhaust gas discharged from a combustion chamber of the internal combustion engine to the combustion chamber, use the EGR mechanism to cause the amount of exhaust gas again fed to the combustion chamber decrease and thereby increase the concentration of NOx in exhaust gas flowing into the upstream side catalyst (20) in the control for increasing NOx, or when the exhaust purification system further comprises a cylinder fuel injector (11) directly injecting fuel into a combustion chamber; and an intake passage fuel injector (12) injecting fuel into an intake passage of the internal combustion engine, change a ratio of an amount of feed of fuel from the intake passage fuel injector (12) to an amount of feed of fuel from the cylinder fuel injector (11), defined as an intake passage injection ratio; and increase the intake passage injection rate and thereby increasing a concentration of NOx flowing into the upstream side catalyst (20) in the control for increasing NOx.

2. The exhaust purification system of an internal combustion engine according to claim 1, wherein the control device (31) is further configured so as not to execute the control for increasing NOx even if the oxygen storage amount of the downstream side catalyst (24) becomes less than or equal to the limit storage amount when the temperature of the downstream side catalyst (24) is less than a predetermined temperature.

3. The exhaust purification system of an internal combustion engine according to claim 1 or 2, wherein the control device (31) is further configured so as not to execute the control for increasing NOx even if the oxygen storage amount of the downstream side catalyst (24) becomes less than or equal to the limit storage amount when the oxygen storage amount of the downstream side catalyst (24) becomes less than or equal to the limit storage amount.

4. The exhaust purification system of an internal combustion engine according to any one of claims 1 to 3, wherein the control device (31) is further configured to control the air-fuel ratio of the exhaust gas flowing into the upstream side catalyst (20) in the air-fuel ratio control so that the air-fuel ratio of the exhaust gas flowing out from the upstream side catalyst (20) does not become greater than or equal to a constant lean judged air-fuel ratio or leaner than the stoichiometric air-fuel ratio, and wherein the lean judged air-fuel ratio is a lean air-fuel ratio with a difference from the stoichiometric air-fuel ratio equal to the difference between the rich judged air-fuel ratio and the stoichiometric air-fuel ratio.