Exhaust purification device of an internal combustion engine

The present invention relates to an exhaust purification device of an internal combustion engine.

Known in the art is an internal combustion engine arranging in an engine exhaust passage an NO x storing catalyst which stores NO x contained in exhaust gas when the air-fuel ratio of the inflowing exhaust gas is lean and releases stored NO x when the air-fuel ratio of the inflowing exhaust gas is a stoichiometric air-fuel ratio or rich, arranging downstream of the NO x storing catalyst an NO x selective reducing catalyst capable of selectively reducing the NO x in the exhaust gas with adsorbed ammonia, arranging upstream of the NO x storing catalyst a three-way catalyst, and temporarily switching the air-fuel ratio of the exhaust gas flowing into the three-way catalyst from lean to rich to release NO x from the NO x storing catalyst (see Japanese Patent Publication (A) No. 11-30117).

In this internal combustion engine, when the air-fuel ratio of the exhaust gas is temporarily switched from lean to rich to release NO x from the NO x storing catalyst, there are cases of a comparatively large amount of ammonia being generated at the three-way catalyst, and the ammonia not used for the reduction of the NO x at the NO x storing catalyst at this time flowing out from the NO x storing catalyst. In this case, the ammonia flowing out from the NO x storing catalyst is adsorbed on the NO x selective reducing catalyst.

On the other hand, in this internal combustion engine, there are cases of a slight amount of NO x not stored at the NO x storing catalyst flowing out from the NO x storing catalyst during normal operation wherein the exhaust gas is maintained at a lean air-fuel ratio. However, in this internal combustion engine, when NO x flows out from the NO x storing catalyst in this way, this NO x is reduced by the ammonia adsorbed on the NO x selective reducing catalyst. From another angle, the ammonia adsorbed on the NO x selective reducing catalyst is consumed to reduce the NO x and thereby removed from the NO x selective reducing catalyst.

However, in this internal combustion engine, the outflow of NO x from the NO x storing catalyst occurs in the general course of things. Accordingly, if a state of NO x not flowing out from the NO x storing catalyst continues, the ammonia adsorbed on the NO x selective reducing catalyst continues to be adsorbed on the NO x selective reducing catalyst without reacting with the NO x and being removed. As a result, the amount of adsorbed ammonia of the NO x selective reducing catalyst becomes saturated, therefore causing the problem of the ammonia generated each time the air-fuel ratio of the exhaust gas is made rich passing straight through the NO x selective reducing catalyst and being exhausted into the atmosphere.

An object of the present invention is to provide an exhaust purification device of an internal combustion engine capable of maintaining an NO x selective reducing catalyst at a state where it is able to adsorb ammonia at all times.

According to the present invention, there is provided an exhaust purification device of an internal combustion engine arranging in an engine exhaust passage an NO x storing catalyst which stores NO x contained in exhaust gas when an air-fuel ratio of an inflowing exhaust gas is lean and releases stored NO x when the air-fuel ratio of the inflowing exhaust gas is a stoichiometric air-fuel ratio or rich, and arranging in the engine exhaust passage downstream of the NO x storing catalyst downstream an NO x selective reducing catalyst capable of selectively reducing NO x in the exhaust gas with adsorbed ammonia, the air-fuel ratio of the exhaust gas flowing into the NO x storing catalyst being temporarily switched from lean to rich to release NO x from the NO x storing catalyst, wherein, just before the air-fuel ratio of the exhaust gas flowing into the NO x storing catalyst is temporarily switched from lean to rich to release NO x from the NO x storing catalyst, ammonia removal control for removing the ammonia adsorbed on the NO x selective reducing catalyst is executed.

In the present invention, the ammonia adsorbed on the NO x selective reducing catalyst is not removed in the general course of things, but removal control of ammonia is executed at predetermined periods, whereby the NO x selective reducing catalyst is maintained at a state where ammonia is able to be adsorbed at all times.

FIG. 1 is an overview of a compression ignition type internal combustion engine,

FIGS. 2A and 2B are cross-sectional views of a surface portion of an NO x storing catalyst,

FIG. 3 is a time chart of ammonia removing NO x feed control,

FIG. 4A is a view showing a map of a stored NO x amount NOXA,

FIG. 4B shows the relationship between NO x storage rate and NO x stored amount for different levels of catalyst degradation,

FIGS. 5A-5C are views showing the amount of reducing agent during rich processing,

FIGS. 6A and 6B are views showing an inflowing ammonia amount of an NO x selective reducing catalyst,

FIG. 7 is a flow chart for carrying out exhaust purification processing,

FIGS. 8A - 8C are views for explaining methods of removing adsorbed ammonia,

FIG. 9A is a view showing an ammonia saturated adsorption amount of an NO x selective reducing catalyst,

FIG. 9B shows a relationship between reducing agent amount and degree of richness for a plurality of reducing agent amounts,

FIG. 10 is a flow chart for carrying out exhaust purification processing,

FIG. 11 is a flow chart for carrying out exhaust purification processing,

FIG. 12 is an overview showing a different embodiment of a compression ignition type internal combustion engine,

FIGS. 13A and 13B are views for explaining rich processing etc. for checking a saturated adsorption amount of ammonia, and

FIG. 14 is a flow chart for carrying out check control checking the saturated adsorption amount of the ammonia.

FIG. 1 shows an overview of a compression ignition type internal combustion engine.

Referring to FIG. 1 , 1 indicates an engine body, 2 a combustion chamber of each cylinder, 3 an electronically controlled fuel injector for injecting fuel into each combustion chamber 2 , 4 an intake manifold, and 5 an exhaust manifold. The intake manifold 4 is connected through an intake duct 6 to the outlet of a compressor 7 a of an exhaust turbocharger 7 . The inlet of the compressor 7 a is connected to an air cleaner 9 via an intake air amount detector 8 . Inside the intake duct 6 is arranged a throttle valve 10 driven by a step motor. Further, around the intake duct 6 is arranged a cooling device 11 for cooling the intake air flowing through the inside of the intake duct 6 . In the embodiment shown in FIG. 1 , the engine cooling water is guided into the cooling device 11 . The engine cooling water cools the intake air.

On the other hand, the exhaust manifold 5 is connected to the inlet of an exhaust turbine 7 b of the exhaust turbocharger 7 , while the outlet of the exhaust turbine 7 b is connected to the inlet of an NO x storing catalyst 12 . The outlet of the NO x storing catalyst 12 is connected via an exhaust pipe 13 to an NO x selective reducing catalyst 14 able to selectively reduce the NO x in the exhaust gas by an ammonia when the air-fuel ratio of the exhaust gas is lean. This NO x selective reducing catalyst 14 is formed by for example ammonia absorption type Fe zealite.

The exhaust manifold 5 and the intake manifold 4 are interconnected through an exhaust gas recirculation (hereinafter referred to as an “EGR”) passage 15 , and an electronically controlled EGR control valve 16 is arranged in the EGR passage 15 . Further, around the EGR passage 15 is arranged a cooling device 17 for cooling the EGR gas flowing through the inside of the EGR passage 15 . In the embodiment shown in FIG. 1 , the engine cooling water is guided into the cooling device 17 . The engine cooling water cools the EGR gas. On the other hand, each fuel injector 3 is connected through a fuel feed tube 18 to a common rail 19 . This common rail 19 is connected to a fuel tank 21 via an electronically controlled variable discharge fuel pump 20 . Fuel stored in the fuel tank 21 is supplied to the common rail 19 by the fuel pump 20 and the fuel supplied into the common rail 19 is supplied through each fuel feed tube 18 to the fuel injector 3 .

An electronic control unit 30 is comprised of a digital computer provided with a read only memory (ROM) 32 , a random access memory (RAM) 33 , a microprocessor (CPU) 34 , an input port 35 , and an output port 36 all connected to each other by a bidirectional bus 31 .

A temperature sensor 22 for detecting the temperature of the NO x selective reducing catalyst 14 is attached to the NO x selective reducing catalyst 14 , and the output signals of the temperature sensor 22 and the intake air amount detector 8 are input through corresponding AD converters 37 to the input port 35 . Further, an accelerator pedal 40 has a load sensor 41 generating an output voltage proportional to the amount of depression L of the accelerator pedal 40 connected to it. The output voltage of the load sensor 41 is input through a corresponding AD converter 37 to the input port 35 . Further, the input port 35 has a crank angle sensor 42 generating an output pulse each time the crankshaft turns for example by 15 degrees connected to it. On the other hand, the output port 36 is connected through corresponding drive circuits 38 to the fuel injectors 3 , the step motor for driving the throttle valve 10 , EGR control valve 16 , and fuel pump 20 .

First, explaining the NO x storing catalyst 12 shown in FIG. 1 , a catalyst carrier comprised of for example alumina is carried on the NO x storing catalyst 12 , and FIGS. 2(A) , (B) schematically show the cross-section of the surface part of this catalyst carrier 45 . As shown in FIGS. 2(A) , (B), the catalyst carrier 45 carries a precious metal catalyst 46 diffused on its surface. Further, the catalyst carrier 45 is formed with a layer of an NO x absorbent 47 on its surface.

In this embodiment of the present invention, platinum Pt is used as the precious metal catalyst 46 . As the ingredient forming the NO x absorbent 47 , for example, at least one element selected from potassium K, sodium Na, cesium Cs, or another alkali metal, barium Ba, calcium Ca, or another alkali earth, lanthanum La, yttrium Y, or another rare earth is used.

If the ratio of the air and fuel (hydrocarbons) supplied to the engine intake passage, combustion chambers 2 , and exhaust passage upstream of the NO x storing catalyst 12 is referred to as the “air-fuel ratio of the exhaust gas”, the NO x absorbent 47 performs an NO x absorption and release action of storing the NO x when the air-fuel ratio of the exhaust gas is lean and releasing the stored NO x when the oxygen concentration in the exhaust gas falls.

That is, if explaining this taking as an example the case of using barium Ba as the ingredient forming the NO x absorbent 47 , when the air-fuel ratio of the exhaust gas is lean, that is, when the oxygen concentration in the exhaust gas is high, the NO contained in the exhaust gas is oxidized on the platinum Pt 46 such as shown in FIG. 2(A) to become NO 2 , then is absorbed in the NO x absorbent 47 and diffuses in the NO x absorbent 47 in the form of nitric acid ions NO 3 − while bonding with the barium carbonate BaCO 3 . In this way, the NO x is absorbed in the NO x absorbent 47 . So long as the oxygen concentration in the exhaust gas is high, NO 2 is produced on the surface of the platinum Pt 46 . So long as the NO x absorbing capability of the NO x absorbent 47 is not saturated, the NO 2 is absorbed in the NO x absorbent 47 and nitric acid ions NO 3 − are produced.

As opposed to this, if the air-fuel ratio of air fuel mixture in the combustion chamber 2 is made rich or the stoichiometric air-fuel ratio, since the oxygen concentration in the exhaust gas falls, the reaction proceeds in the reverse direction (NO 3 − →NO 2 ) and therefore the nitric acid ions NO 3 − in the NO x absorbent 47 are released from the NO x absorbent 47 in the form of NO 2 , as shown in FIG. 2(B) . Next, the released NO x is reduced by the unburned hydrocarbons or CO included in the exhaust gas. For example, when the released NO x is reduced by CO, the released NO x becomes N 2 and CO 2 , as shown in FIG. 2(B) .

In this way, when the air-fuel ratio of the exhaust gas is lean, that is, when burning fuel under a lean air-fuel ratio, the NO x in the exhaust gas is absorbed in the NO x absorbent 47 . However, if continuing to burn fuel under a lean air-fuel ratio, during that time the NO x absorbing capability of the NO x absorbent 47 will end up becoming saturated and therefore NO x will end up no longer being able to be absorbed by the NO x absorbent 47 . Therefore, in this embodiment according to the present invention, before the absorbing capability of the NO x absorbent 47 becomes saturated, the air-fuel ratio of the exhaust gas is temporarily made rich and thereby release the NO x from the NO x absorbent 47 .

In this regard, if the air-fuel ratio of the exhaust gas is made rich to release NO x from the NO x absorbent 47 , as shown in FIG. 2(B) , a portion of the CO reacts with the water H 2 O contained in the exhaust gas to produce H 2 . Next, this H 2 reacts with the N 2 produced from the NO 2 released from the NO x absorbent 47 and produces ammonia NH 3 . That is, if the exhaust gas is made rich to release NO x from the NO x absorbent 47 , ammonia NH 3 is produced at the NO x storing catalyst 12 . This ammonia NH 3 flows out from the NO x storing catalyst 12 and is adsorbed on the NO x selective reducing catalyst 14 .

If leaving this state as it is, the adsorbed ammonia amount of the NO x selective reducing catalyst 14 will become saturated. This creates the problem of the ammonia generated each time the air-fuel ratio of the exhaust gas is made rich ending up passing straight through the NO x selective reducing catalyst 14 . Therefore, in the present invention, to prevent the occurrence of such a problem, just before the air-fuel ratio of the exhaust gas flowing into the NO x storing catalyst 12 being temporarily switched from lean to rich to release NO x from the NO x storing catalyst 12 , ammonia removal control for removing the ammonia adsorbed on the NO x selective reducing catalyst 14 is executed.

Somewhat more specifically, in the embodiment according to the present invention, NO x flows out from the NO x storing catalyst 12 just before the air-fuel ratio of the exhaust gas becomes rich. This NO x removes ammonia adsorbed on the NO x selective reducing catalyst 14 . That is, in the embodiment according to the present invention, the above ammonia removal control comprises an ammonia removing NO x feed control which feeds the amount of NO x that is necessary to remove ammonia adsorbed on the NO x selective reducing catalyst 14 to the NO x selective reducing catalyst 14 while the air-fuel ratio of the exhaust gas is made lean.

FIG. 3 shows a time chart of this ammonia removing NO x feed control. Note that, in FIG. 3 , A/F indicates the air-fuel ratio of the exhaust gas, ND the amount of NO x flowing out from the NO x storing catalyst 12 , that is, the amount of the inflowing NO x flowing into the NO x selective reducing catalyst 14 , NH the amount of ammonia flowing out from the NO x storing catalyst 12 , that is, the amount of inflowing ammonia flowing into the NO x selective reducing catalyst 14 , NS the amount of stored NO x stored in the NO x storing catalyst 12 , and HS the amount of adsorbed ammonia absorbed on the NO x selective reducing catalyst 14 .

As shown in FIG. 3 , if the air-fuel ratio A/F of the exhaust gas is switched from lean to rich, NO x is released from the NO x storing catalyst 12 and, accordingly, the stored NO x amount NS drops rapidly. On the other hand, at this time, because ammonia is produced at the NO x storing catalyst 12 , the inflowing ammonia amount NH flowing into the NO x selective reducing catalyst 14 increases temporarily and, as a result, the adsorbed ammonia amount HS of the NO x selective reducing catalyst 14 increases. That is, in FIG. 3 , NSX indicates the stored NO x amount NS when the air-fuel ratio A/F of the exhaust gas is switched to rich.

Next, if the air-fuel ratio A/F of the exhaust gas is returned from rich to lean one once again, for some time after, the inflowing NO x amount will be near zero. That is, almost all the NO x contained in the exhaust gas is stored in the NO x storing catalyst 12 . Further, in this period, ammonia is not generated at the NO x storing catalyst 12 , accordingly, the inflowing ammonia amount NH is zero.

Next, if the NO x storage ability of the NO x storing catalyst 12 approaches saturation, the NO x storing catalyst 12 will become unable to store all of the NO x contained in the exhaust gas, and a portion of the NO x contained in the exhaust gas will pass straight through the NO x storing catalyst 12 . The amount of this NO x that passes through increases over time, and as a result, the inflowing NO x amount ND of the NO x selective reducing catalyst 14 increases over time. The ammonia adsorbed on the NO x selective reducing catalyst 14 is consumed to reduce this inflowing NO x , whereby the adsorbed ammonia amount HS decreases over time.

As shown in FIG. 3 , in the embodiment according to the present invention, the NO x passes straight through the NO x storing catalyst 12 until the adsorbed ammonia amount HS is zero. When the adsorbed ammonia amount HS is zero, the air-fuel ratio A/F of the exhaust gas is switched from lean to rich, whereby NO x ceases passing straight through the catalyst. That is, in the embodiment according to the present invention, when the amount of NO x passing straight through the NO x storing catalyst 12 becomes the amount necessary for removing ammonia adsorbed on the NO x selective reducing catalyst 14 under a lean air-fuel ratio of the exhaust gas, the air-fuel ratio of the exhaust gas is temporarily switched from lean to rich.

Next, referring to FIGS. 4 to 8 , a first embodiment according to the present invention will be explained.

In this first embodiment, there is provided an adsorbed ammonia amount estimating means for estimating an ammonia amount HS adsorbed on the NO x selective reducing catalyst 14 . The NO x necessary for removing all or a portion of the amount of adsorbed ammonia estimated by this adsorbed ammonia amount estimating means is fed to the NO x selective reducing catalyst 14 under a lean air-fuel ratio of the exhaust gas.

In this case, in this first embodiment, the above adsorbed ammonia amount estimating means estimates the amount of adsorbed ammonia based on the degree of richness and rich time when the air-fuel ratio of the exhaust gas is made rich to release NO x from the NO x storing catalyst 12 .

In this first embodiment, the pass-through amount of the NO x in the NO x storing catalyst 12 is calculated from the NO x amount exhausted per unit time from the engine and the NO x amount that the NO x storing catalyst 12 is able to store per unit time, that is, the NO x storage rate. That is, in this first embodiment, the NO x amount NOXA exhausted per unit time from the engine is stored as a function of the required torque TQ and engine speed N of the engine in the form of a map as shown in FIG. 4(A) in advance in the ROM 32 .

On the other hand, the NO x storage rate ΔNS of the NO x storing catalyst 12 is a function of the stored NO x amount NS of the NO x storing catalyst 12 . As shown in FIG. 4(B) , the NOX storage rate ΔNS falls as the stored NO x amount NS rises. Note that, at the FIG. 4(B) , a, b, c, and d show cases of differing degrees of degradation of the NO x storing catalyst 12 , wherein the relationship of these degrees of degradation is d>c>b>a. That is, the higher the degree of degradation, the more the NO x storage rate ΔNS drops. The relationship shown in FIG. 4(B) is stored in advance in the ROM 32 .

When the NO x storage rate ΔNS is higher in comparison to the exhausted NO x amount NOXA from the engine, all of the NOX exhausted from the engine is stored in the NO x storing catalyst 12 . As opposed to this, when the NO x storage rate ΔNS is lower in comparison to the NO x amount NOXA exhausted from the engine, only the amount of NO x corresponding to the NO x storage rate ΔNS in the NO x exhausted from the engine is stored in the NO x storing catalyst 12 , while the remaining NO x (=NOXA−ΔNS) passes straight through the NO x storing catalyst 12 . By this, the amount of NO x passing straight through can be calculated from the NO x amount NOXA exhausted from the engine and the NO x storage rate ΔNS.

On the other hand, when additional fuel is fed and the air-fuel ratio of the exhaust gas is made rich, a portion of this additional fuel is used to consume the oxygen in the exhaust gas and lower the air-fuel ratio from lean to the stoichiometric air-fuel ratio, whereas a small portion of the remaining additional fuel is used to produce ammonia, while the majority, that is, the portion shown by the shaded region in FIG. 5(A) is used as a reducing agent for reducing the NO x released from the NO x storing catalyst 12 . Accordingly, the amount Q of the reducing agent shown by the shaded region in FIG. 5(A) is determined from the stored NO x amount NSX ( FIG. 3 ) of when the air-fuel ratio of the exhaust gas is made rich. As shown in FIG. 5(B) , the amount Q of the reducing agent is proportional to the stored NO x amount NSX.

Changing the amount Q of the reducing agent requires changing either the degree of richness and the rich time shown in FIG. 5(A) or both. The first embodiment changes the rich time while maintaining the degree of richness constant so as to change the amount Q of the reducing agent. Accordingly, in the first embodiment, as shown in FIG. 5(C) , the rich time changes in proportion to the amount Q of the reducing agent.

FIGS. 6(A) and (B) show the relationship of the inflowing ammonia amount NH that is produced at the NO x storing catalyst 12 and flows into the NO x selective reducing catalyst 14 and the degree of richness and rich time shown in FIG. 5(A) . As shown in FIG. 6(A) , the inflowing ammonia amount NH exponentially increases as the degree of richness rises. On the other hand, as shown in FIG. 6(B) , the inflowing ammonia amount NH is proportional to the rich time. Accordingly, the inflowing ammonia amount NH, that is, the ammonia amount adsorbed on the NO x selective reducing catalyst 14 , can be estimated from the degree of richness and the rich time.

FIG. 7 shows the exhaust purification processing routine for executing the first embodiment. This routine is executed by interruption every predetermined period. In this first embodiment, the ammonia adsorption amount of the NO x selective reducing catalyst 14 is estimated, the target value X 0 of the NO x amount necessary to remove this adsorbed ammonia is calculated, and the amount of NO x according to this target value X 0 is fed to the NO x selective reducing catalyst 14 .

Referring to FIG. 7 , first, at step 50 , the NO x amount NOXA exhausted per unit time from the engine is calculated from the map shown in FIG. 4(A) . Next, at step 51 , the NO x storage rate ΔNS according to the stored NO x amount NS is calculated from the relationship shown in FIG. 4(B) . Next, at step 52 , it is judged if the exhausted NO x amount NOXA is larger than the NO x storage rate ΔNS. When NOXA>ΔNS, only the part of the exhausted NO x amount NOXA corresponding to the NOX storage rate ΔNS is stored in the NO x storing catalyst 12 , while the remaining NO x (NOXA-ΔNS) passes straight through the NO x storing catalyst 12 .

Accordingly, when it is judged at step 52 that NOXA>ΔNS, the routine proceeds to step 54 , where the NO x storage rate ΔNS is added to the stored NO x amount NS stored in the NO x storage catalyst 12 . Next, at step 55 , (NOXA-ΔNS) is added to the total value ΣNOX of the outflowing NO x amount passing straight through the NO x storing catalyst 12 and flowing out from the NO x storing catalyst 12 . Next, the routine proceeds to step 56 . On the other hand, when it is judged at step 52 that NOXA≦ΔNS, the routine proceeds to step 53 , where the exhausted NO x amount NOXA is added to the stored NO x amount NS, then the routine proceeds to step 56 .

At step 56 , it is judged if the total value ΣNOX of the outflowing NO x amount exceeds the target value X 0 necessary to remove the adsorbed ammonia. When the total value ΣNOX of the outflowing NO x amount exceeds the target value X 0 , the routine proceeds to step 57 , where the rich time is calculated based on the stored NO x amount NS at this time, that is, NSX. Next, at step 58 , rich processing to make the exhaust gas a rich air-fuel ratio is carried out. Next, at step 59 , NS and ΣNOX are cleared. Next, at step 60 , the inflowing ammonia amount NH, that is, the ammonia amount adsorbed on the NO x selective reducing catalyst 14 , is calculated based on the rich time. Next, at step 61 , the target value X 0 of the outflowing NO x amount necessary to remove the adsorbed ammonia is calculated.

FIGS. 8(A) , (B), and (C) show a number of methods of removing adsorbed ammonia. In FIGS. 8(A) , (B), and (C), the left NO x selective reducing catalyst 14 indicates the state of the adsorbed ammonia just before rich control making the exhaust gas a rich air-fuel ratio, whereas the right NO x selective reducing catalyst 14 indicates the state of the adsorbed ammonia after rich control. In the example shown in FIG. 8(A) , when rich control is carried out, the adsorbed ammonia reaches saturation and all of this adsorbed ammonia is removed just before rich control by the feeding of NO x .

On the other hand, in the example shown in FIG. 8(B) , when rich control is carried out, ammonia is adsorbed in a part of the adsorption region of the NO x selective reducing catalyst 14 and all of this adsorbed ammonia is removed just before rich control by the feeding of NO x . In the example shown in FIG. 8(C) , before rich control I and II, the feeding of NO x for removing ammonia is not carried out, but after the adsorbed ammonia reaches saturation, all of the adsorbed ammonia is removed before rich control III by the feeding of NO x .

FIG. 9 to FIG. 11 show a second embodiment keeping the adsorbed ammonia amount of the NO selective reducing catalyst 14 from exceeding the saturated adsorption amount of ammonia. That is, in FIG. 9(A) , the solid line MAX indicates the saturated adsorption amount of ammonia of the NO x selective reducing catalyst 14 . This saturated adsorption amount MAX drops as the temperature TC of the NO x selective reducing catalyst 14 rises.

In this second embodiment, the target ammonia amount NHO to be adsorbed on the NO x selective reducing catalyst 14 is predetermined. In the example shown in FIG. 9(A) , this target ammonia amount NHO is set to be an amount lower than the ammonia saturated adsorption amount MAX of the NO x selective reducing catalyst 14 by exactly a predetermined amount Z. Accordingly, this target ammonia amount NHO is a function of the catalyst temperature TC. As shown in FIG. 9(A) , when the catalyst temperature is TC 1 , the target ammonia amount becomes NHO 1 .

In this second embodiment, the ammonia amount generated during rich processing is controlled to the target ammonia amount NHO. Accordingly, in this second embodiment, the adsorbed ammonia amount will not exceed the saturated adsorption amount MAX. However, if the target value is set for the adsorbed ammonia amount in such a way, both the amount Q of the reducing agent for reducing the released NO x and the amount of generated ammonia must be controlled to the required amounts.

In this regard, as seen from FIG. 5(A) , the amount Q of the reducing agent is proportional to the product of the degree of richness and the rich time, while on the other hand, as can be seen from FIGS. 6(A) and (B), even if the reducing agent amount Q is the same, if changing the degree of richness and the rich time, the generated ammonia amount changes. FIG. 9(B) shows the relationship between a number of reducing agent amounts Q 1 to Q 5 , their generated ammonia amounts, that is, the inflowing ammonia amount NH flowing into the NO x selective reducing catalyst 14 , and their degrees of richness. Note that, the amount of reducing agent increases in the order of Q 1 , Q 2 , Q 3 , Q 4 , and Q 5 .

As can be seen from FIG. 9(B) , increasing the inflowing ammonia amount NH with respect to the same amount of reducing agent will require increasing the degree of richness. If the degree of richness is increased in this case, the rich time is shortened. That is, in this second embodiment, the degree of richness and the rich time of when the air-fuel ratio of the exhaust gas is made rich to release NO x from the NO x storing catalyst 12 are controlled to a degree of richness and a rich time capable of finishing the release action of NO x from the NO x storing catalyst 12 and of making the adsorbed ammonia amount of the NO x selective reducing catalyst 14 the target ammonia amount NHO.

FIG. 10 and FIG. 11 show an exhaust purification processing routine for executing the second embodiment. This routine is also executed by interruption every predetermined period.

Referring to FIG. 10 and FIG. 11 , first, at step 70 , the NO x amount NOXA exhausted per unit time from the engine is calculated from the map shown in FIG. 4(A) . Next, at step 71 , the NO x storage rate ΔNS based on the stored NO x amount NS is calculated from the relationship shown in FIG. 4(B) . Next, at step 72 , it is judged if the exhausted NO x amount NOXA is larger than the NO x storage rate ΔNS.

When it is judged at step 72 that NOXA>ΔNS, the routine proceeds to step 74 , where the NO x storage rate ΔNS is added to the stored NO x amount NS stored in the NO x storing catalyst 12 . Next, at step 75 , (NOXA-ΔNS) is added to the total value ΣNOX of the outflowing NO x amount passing straight through the NO x storing catalyst 12 and flowing out from the NO x storing catalyst 12 . Next, the routine proceeds to step 76 . On the other hand, if it is judged at step 72 that NOXA≦ΔNS, the routine proceeds to step 73 , where the exhausted NO x amount NOXA is added to the stored NO x amount NS, then the routine proceeds to step 76 .

At step 76 , it is judged if the total value ΣNOX of the outflowing NOX amount exceeds the target value X 0 necessary for removing the adsorbed ammonia of the target amount NHO. When the total value ΣNOX of the outflowing NO x amount exceeds the target value X 0 , the routine proceeds to step 77 , where the amount Q of the reducing agent necessary for reducing the NO x is calculated based on the stored NOX amount NS at this time, that is, the NSX. Next, at step 78 , the catalyst temperature TC detected by the temperature sensor 22 is read, then at step 79 , the target ammonia amount NHO based on the catalyst temperature TS is calculated.

Next, at step 80 , using the amount Q of the reducing agent and the target ammonia amount NHO, the degree of richness, that is, the rich air-fuel ratio, is calculated from the relationship shown in FIG. 9(B) , then, at step 81 , the rich time is calculated from the reducing agent amount Q and the degree of richness. Next, at step 82 , rich processing making the exhaust gas a rich air-fuel ratio is carried out. Next, at step 83 , NS and ΣNOX are cleared. Next, at step 84 , the target value X 0 of the outflowing NO x amount that is necessary for removing the adsorbed ammonia of the target amount NH 0 is calculated.

FIG. 12 shows a different embodiment of the compression ignition type internal combustion engine. In this embodiment, upstream and downstream of the NO x selective reducing catalyst 14 , there are provided an NO x sensor 23 for detecting the concentration of NO x flowing into the NO x selective reducing catalyst 14 and an NO x sensor 24 for detecting the concentration of NO x flowing out from the NO x selective reducing catalyst 14 . If ammonia is adsorbed on the NO x selective reducing catalyst 14 , the NO x flowing into the NO x selective reducing catalyst 14 is reduced by the adsorbed ammonia, whereby the NO x amount flowing out from the NO x selective reducing catalyst 14 decreases by exactly the amount that is used to remove the adsorbed ammonia in comparison to the NO x amount flowing into the NO x selective reducing catalyst 14 .

Accordingly, the adsorbed ammonia amount may be estimated from the difference in the NO x concentrations before and after the NO selective reducing catalyst 14 detected by the NO x sensors 23 and 24 . Accordingly, instead of estimating the adsorbed ammonia amount from the degree of richness and rich time during rich processing, the adsorbed ammonia may also be estimated from the output values of the pair of NO x sensors 23 and 24 .

FIG. 13 and FIG. 14 show an embodiment that detects the ammonia saturated adsorption amount MAX of the NO x selective reducing catalyst 14 from the difference in the NO x concentrations before and after the NO selective reducing catalyst 14 detected by the pair of NO x sensors 23 and 24 and corrects the target ammonia amount NHO based on this ammonia saturated adsorption amount MAX.

That is, in FIG. 13(A) , ND i indicates the inflowing NO x amount calculated from the output value of the NO x sensor 23 , while ND 0 indicates the outflowing NO x amount calculated from the output value of the NO x sensor 24 . At FIG. 13(A) , if rich processing, which is normally carried out at a timing shown by the broken line RS, is ceased, the inflowing NO x amount ND i continues to rise, and the outflowing NOX amount ND 0 rises rapidly until the inflowing NOX amount ND i if there is no longer adsorbed ammonia present.

In this case, the area shown by the shaded region in FIG. 13(A) indicates the ammonia adsorption amount, accordingly, the ammonia adsorption amount may be estimated from the output values of the pair of NO x sensors 23 and 24 . However, in this embodiment, in order to make the ammonia adsorption amount of the NO x selective reducing catalyst 14 reach saturation before detecting the ammonia saturated adsorption amount MAX so as to detect the ammonia saturated adsorption amount MAX, an amount of reducing agent of more than an amount necessary to release NO x from the NO x storing catalyst 12 is fed to the NO x storing catalyst 12 . In the example shown in FIG. 13(A) , as shown by RF, the air-fuel ratio A/F of the exhaust gas is continuously made rich multiple times.

If a large amount of reducing agent is fed in such a way, the area shown by the shaded region in FIG. 13(A) will indicate the ammonia saturated adsorption amount MAX. If the saturated adsorption amount curve used until now is the broken line curve in FIG. 13(B) and the ammonia saturated adsorption amount, which is detected when the catalyst temperature TC is TC 1 , is MAX 1 , the saturated adsorption amount curve is corrected to the solid line saturated adsorption amount curve. The saturated adsorption amount curve is corrected in such a way. If the saturated adsorption amount curve is corrected in such a way, the target ammonia amount NHO is corrected to be lower than the saturated adsorption amount curve by, for example, a predetermined value Z.

FIG. 14 shows the check control routine of the saturated adsorption amount of the ammonia. This check control routine is for example executed only once every time a vehicle is operated.

Referring to FIG. 14 , first, at step 90 , an instruction to execute a rich processing for check is sent. For example, an instruction making the air-fuel ratio A/F of the exhaust gas rich twice as shown by RF at FIG. 13(A) and prohibiting rich processing shown by the broken line RS is sent.

Next, at step 91 , the inflowing NO x amount ND 1 is calculated by multiplying the exhaust gas amount, that is, the intake air amount, with the NO x concentration detected by the NO x sensor 23 , next, at step 92 , the outflowing NO x amount ND 0 is calculated by multiplying the exhaust gas amount, that is, the intake air amount, with the NO x concentration detected by the NO x sensor 24 . Next, at step 93 , the difference ΔND (=ND i −ND 0 ) between the inflowing NO x amount ND i and the outflowing NO x amount ND 0 is calculated. Next, at step 94 , the difference ΔND is added to the integrated value ΣΔND.

Next, at step 95 , it is judged if the difference ΔND is in the process of decreasing. This difference ΔND (=ND i −ND 0 ), as can be seen from FIG. 13(A) , is initially zero, but gradually increases, then decreases. When the difference ΔND is not in the process of decreasing, the routine jumps to step 97 . At step 97 , it is waited until a predetermined unit time passes, then the routine returns to step 90 . On the other hand, when it is judged at step 95 that ΔND is in the process of decreasing, the routine proceeds to step 96 , where it is judged if the difference ΔND has become zero, that is, it is judged if the calculation of the consumed NO x amount corresponding to the shaded area in FIG. 13(A) is completed. If the difference ΔND is not zero, the routine proceeds to step 97 .

On the other hand, when it is judged at step 96 that the difference ΔND has become zero, that is, when the calculation of the consumed NO x amount corresponding to the shaded area in FIG. 13(A) is completed, the routine proceeds to step 98 , where the ammonia saturated adsorption amount MAX is calculated from the consumed NO x amount, and the saturated adsorption amount curve is corrected. Next, at step 99 , the target ammonia amount NHO is corrected. Next, at step 100 , after waiting for exactly a predetermined waiting time, the routine proceeds to step 101 . At step 101 , rich processing for releasing NO x shown by the RT in FIG. 13(A) is carried out, then the check control is ended.

List of Reference Numerals

4 . . . intake manifold

5 . . . exhaust manifold

7 . . . exhaust turbocharger

12 . . . NO x storing catalyst

14 . . . NO x selective reducing catalyst