1. Field of the Invention
The invention relates to an exhaust gas purification apparatus for an internal combustion engine and a method of controlling the same.
2. Description of the Related Art
Published Japanese Translation of PCT Application No. 2000-514911 (JP-A-2000-514911) describes a known combustor that brings an air-fuel mixture gas into contact with a catalyst to generate flames. The combustor includes a small catalyst that is able to electrically heat the catalyst and a large catalyst that is arranged downstream of the small catalyst in a direction in which the mixture gas flows. A mixture gas having a lean air-fuel ratio is continuously supplied to the electrically heated small catalyst to continuously generate flames downstream of the small catalyst. Then, the air-fuel ratio of the mixture gas is increased and the amount of the mixture gas is increased to continuously generate flames in the large catalyst.
In other words, in the above described combustor, a mixture gas having a lean air-fuel ratio is supplied to the small catalyst, so fuel is caused to burn with excessive air. This makes it possible to continuously generate flames. However, when fuel is supplied from a fuel supply valve to a small oxidation catalyst, the air-fuel ratio of exhaust gas that flows out from the small oxidation catalyst may be lean but is mostly rich. That is, exhaust gas flowing out from the small oxidation catalyst mostly contains excessive fuel.
Thus, as in the case of the above described combustor, when fuel is continuously caused to flow out from the small oxidation catalyst in order to continuously generate flames, not all fuel burns favorably because of insufficient air. Therefore, there is a problem that not only soot is generated but also a flame temperature does not sufficiently increase.
The inventors have been studied that, in order to increase the temperature of a catalyst, or the like, a small oxidation catalyst and a fuel supply valve are arranged in an engine exhaust passage, the small oxidation catalyst has a cross-sectional area smaller than the cross-sectional area of the engine exhaust passage, the fuel supply valve is used to supply fuel to the small oxidation catalyst, and then fuel is supplied from the fuel supply valve to the small oxidation catalyst to generate flames downstream of the small oxidation catalyst. As a result, to generate high-temperature flames without generating soot in the engine exhaust passage, it has been found that flames are intermittently generated by intermittently supplying fuel from the fuel supply valve.
A first aspect of the invention provides an exhaust gas purification apparatus for an internal combustion engine. The exhaust gas purification apparatus includes: a small oxidation catalyst that is arranged in an engine exhaust passage and that has a cross-sectional area smaller than a cross-sectional area of the engine exhaust passage, wherein portion of exhaust gas flowing in the engine exhaust passage flows through the small oxidation catalyst; a fuel supply valve that is arranged in the engine exhaust passage and that supplies fuel to the small oxidation catalyst; a determination unit that determines whether flames is generated by supplying fuel from the fuel supply valve; and a control unit that, when the determination unit determines that the flames is generated by supplying fuel from the fuel supply valve, intermittently supplies fuel from the fuel supply valve to the small oxidation catalyst to intermittently generate flames downstream of the small oxidation catalyst.
A second aspect of the invention provides a method of controlling an exhaust gas purification apparatus for an internal combustion engine. The exhaust gas purification apparatus includes a small oxidation catalyst and a fuel supply valve. The small oxidation catalyst is arranged in an engine exhaust passage and has a cross-sectional area smaller than a cross-sectional area of the engine exhaust passage. Portion of exhaust gas flowing in the engine exhaust passage flows through the small oxidation catalyst. The fuel supply valve is arranged in the engine exhaust passage and supplies fuel to the small oxidation catalyst. The method includes: determining whether flames is generated by supplying fuel from the fuel supply valve; and, when it is determined that the flames is generated by supplying fuel from the fuel supply valve, intermittently supplying fuel from the fuel supply valve to the small oxidation catalyst to intermittently generate flames downstream of the small oxidation catalyst.
According to the aspects of the invention, it is possible to generate high-temperature flames while suppressing generation of soot in the engine exhaust passage.
The features, advantages, and technical and industrial significance of this invention will be described in the following detailed description of example embodiments of the invention with reference to the accompanying drawings, in which like numerals denote like elements, and wherein:
On the other hand, the exhaust manifold 5 is connected to an inlet of an exhaust gas turbine 7b of the exhaust gas turbocharger 7, and an outlet of the exhaust gas turbine 7b is connected to an exhaust gas purification catalyst 13 via an exhaust pipe 12. The exhaust gas purification catalyst 13 has an oxidation function. A small oxidation catalyst 14 is arranged in an engine exhaust passage, that is, in the exhaust pipe 12, at a portion upstream of the exhaust gas purification catalyst 13. The small oxidation catalyst 14 has a volume smaller than that of the exhaust gas purification catalyst 13. Portion of exhaust gas flowing into the exhaust gas purification catalyst 13 flows through the small oxidation catalyst 14. A fuel supply valve 15 is arranged in the engine exhaust passage, that is, in the exhaust pipe 12, at a portion upstream of the small oxidation catalyst 14. The fuel supply valve 15 supplies fuel to the small oxidation catalyst 14.
In the embodiment shown in
The exhaust manifold 5 and the intake manifold 4 are connected to each other via an exhaust gas recirculation (hereinafter, referred to as EGR) passage 18. An electronically controlled EGR control valve 19 is arranged in the EGR passage 18. In addition, the cooling unit 20 is arranged around the EGR passage 18 to cool EGR gas that flows through the EGR passage 18. In the embodiment shown in
An electronic control unit 30 is formed of a digital computer, and includes 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, which are connected to one another via a bidirectional bus 31. A temperature sensor 25 is attached to the small oxidation catalyst 14. The temperature sensor 25 detects the temperature of the small oxidation catalyst 14. A differential pressure sensor 26 is attached to the particulate filter 16. The differential pressure sensor 26 detects a differential pressure before and after the particulate filter 16. Output signals of these temperature sensor 25, differential pressure sensor 26 and intake air amount detector 8 are input to the input port 35 through respective AD converters 37. A load sensor 41 is connected to an accelerator pedal 40. The load sensor 41 generates an output voltage in proportion to a depression amount L of the accelerator pedal 40. The output voltage of the load sensor 41 is input to the input port 35 via a corresponding one of the AD converter 37. In addition, a crank angle sensor 42 is connected to the input port 35. The crank angle sensor 42 generates an output pulse each time a crankshaft rotates, for example, by 15 degrees. On the other hand, the output port 36 is connected to each fuel injection valve 3, a step motor for driving the throttle valve 10, the EGR control valve 19 and the fuel pump 23 via corresponding driving circuits 38.
As is apparent from
On the other hand, as shown in
In the embodiment shown in
On the other hand, a catalyst carrier made of, for example, alumina is also supported on a base of the NOx occlusion catalyst 17 shown in
In the example shown in
If ratio between air and fuel (hydrocarbon) that are supplied into an engine intake passage, the combustion chambers 2 and the exhaust passage upstream of the NOx occlusion catalyst 17 is referred to as the air-fuel ratio of exhaust gas, the NOx absorbent 52 occludes NOx when the air-fuel ratio of exhaust gas is lean, and releases the occluded NOx when the concentration of oxygen in exhaust gas decreases, thus carrying out NOx absorbing/releasing action.
That is, taking the case where barium Ba is used as a component that constitutes the NOx absorbent 52 as an example, when the air-fuel ratio of exhaust gas is lean, that is, when the concentration of oxygen in exhaust gas is high, NO contained in the exhaust gas is oxidized to NO2 on the platinum Pt 51 as shown in
In contrast, when the air-fuel ratio of exhaust gas is rich or stoichiometric, the concentration of oxygen in exhaust gas decreases. Thus, reaction proceeds in the reverse direction (from NO3− to NO2) and, as a result, nitrate ions NO3− in the NOx absorbent 52 are released from the NOx absorbent 52 in the form of NO2. Subsequently, the released NOx is reduced by unburned HC or CO contained in exhaust gas.
In this way, when the air-fuel ratio of exhaust gas is lean, that is, when combustion takes place at a lean air-fuel ratio, NOx contained in exhaust gas is occluded into the NOx absorbent 52. However, when combustion continuously takes place at a lean air-fuel ratio, the NOx absorption capacity of the NOx absorbent 52 is saturated during then. As a result, NOx cannot be absorbed by the NOx absorbent 52. Then, in the present embodiment, by supplying fuel from the fuel supply valve 15 prior to saturation of the absorption capacity of the NOx absorbent 52, the air-fuel ratio of exhaust gas is temporarily made rich to release NOx from the NOx absorbent 52.
Incidentally, SOx, that is, SO2, is contained in exhaust gas. If the SO2 flows into the NOx occlusion catalyst 17, the SO2 is oxidized by the platinum Pt 51 to SO3. Subsequently, the SO3 is absorbed into the NOx absorbent 52 to be bonded with barium carbonate BaCO3 while being diffused in the NOx absorbent 52 in the form of sulfate ion SO42− to produce stable sulfate BaSO4. However, because the NOx absorbent 52 is strongly basic, the sulfate BaSO4 is stable and is difficult to be decomposed. If only the air-fuel ratio of exhaust gas is simply made rich, the sulfate BaSO4 remains as it is without decomposition. Thus, the NOx absorbent 52 contains increased sulfate BaSO4 as time elapses. As a result, as time elapses, the amount of NOx the NOx absorbent 52 can absorb decreases. That is, the NOx occlusion catalyst 17 experiences sulfur poisoning.
Incidentally, in this case, in a state where the temperature of the NOx occlusion catalyst 17 is increased to a SOx release temperature, which is higher than or equal to 600° C., when the air-fuel ratio of exhaust gas that flows into the NOx occlusion catalyst 17 is made rich, SOx is released from the NOx absorbent 52. Then, in the present embodiment, when the NOx occlusion catalyst 17 experiences sulfur poisoning, fuel is supplied from the fuel supply valve 15 to increase the temperature of the NOx occlusion catalyst 17 to the SOx release temperature. Thus, the air-fuel ratio of exhaust gas that flows into the NOx occlusion catalyst 17 is made rich to release SOx from the NOx occlusion catalyst 17.
In the embodiment shown in
Incidentally, because flow resistance is large inside the small oxidation catalyst 14, the amount of exhaust gas that flows through the small oxidation catalyst 14 is small. In addition, as oxidation reaction occurs in the small oxidation catalyst 14, gas expands inside the small oxidation catalyst 14. Thus, the amount of exhaust gas that flows through the small oxidation catalyst 14 further reduces. In addition, as the gas temperature increases due to oxidation reaction, the viscosity of gas increases. Thus, the amount of exhaust gas that flows through the small oxidation catalyst 14 further reduces. Hence, the flow rate of exhaust gas inside the small oxidation catalyst 14 is considerably lower than the flow rate of exhaust gas that flows inside the exhaust pipe 12.
In this way, because the flow rate of exhaust gas inside the small oxidation catalyst 14 is low, oxidation reaction is activated in the small oxidation catalyst 14. In addition, because the volume of the small oxidation catalyst 14 is small, the temperature of the small oxidation catalyst 14 rapidly increases to a considerably high temperature. At this time, as the temperature of the small oxidation catalyst 14 is higher than the ignition temperature of fuel, fuel flowing out from the small oxidation catalyst 14 ignites, and flames are generated downstream of the small oxidation catalyst 14 as indicated by H in
That is, as fuel is supplied from the fuel supply valve 15 to the small oxidation catalyst 14, portion of the supplied fuel is oxidized in the small oxidation catalyst 14. On the other hand, the remaining supplied fuel is decomposed, that is, reformed, into hydrocarbons having low molecular weight in the small oxidation catalyst 14. As a result, the reformed fuel flows out from the small oxidation catalyst 14. At this time, the air-fuel ratio of exhaust gas that flows out from the small oxidation catalyst 14 may be lean but is mostly rich. That is, exhaust gas flowing out from the small oxidation catalyst 14 at this time mostly contains excessive fuel.
At this time, when the temperature of the small oxidation catalyst 14 is higher than the ignition temperature, flames H are generated as shown in
Then, in the present embodiment shown in
As shown in
As shown in
Note that as described above, when fuel is supplied from the fuel supply valve 15 to the small oxidation catalyst 14, the air-fuel ratio of exhaust gas that flows out from the small oxidation catalyst 14 is rich. Thus, at the time of generating flames H, exhaust gas having a rich air-fuel ratio intermittently flows out from the small oxidation catalyst 14.
Next, a region in which flames H are generated will be described. In
When the oxidation catalyst 13, and the like, are not activated, it is necessary to increase the temperature of the oxidation catalyst 13, and the like, in order to activate the oxidation catalyst 13, and the like. In addition, to burn particulates accumulated on the particulate filter 16, it is necessary to increase the temperature of the particulate filter 16 to approximately 600° C. When SOx is released from the NOx occlusion catalyst 17 as well, it is necessary to increase the temperature of the NOx occlusion catalyst 17 to the SOx release temperature, which is higher than or equal to 600° C.
Note that
For releasing NOx or SOx from the NOx occlusion catalyst 17, when flames H are intermittently generated while the air-fuel ratio of exhaust gas is made rich, that is, when flames of a rich air-fuel ratio are intermittently generated, it is possible to considerably favorably release NOx or SOx from the NOx occlusion catalyst 17 and favorably reduce the released NOx or SOx. That is, because generated flames consume almost entire oxygen contained in exhaust gas, oxygen contained in the exhaust gas sharply reduces. Thus, NOx is rapidly released from the NOx occlusion catalyst 17. In addition, generated flames promote thermal decomposition to produce strongly active reduction components, such as HC, CO, and H2. Thus, NOx released from the NOx occlusion catalyst 17 is favorably reduced. The same applies to SOx.
In this way, when NOx or SOx is released from the NOx occlusion catalyst 17, it is desirable to intermittently generate flames of a rich air-fuel ratio. Thus, in the present embodiment, when NOx or SOx needs to be released from the NOx occlusion catalyst 17, flames of a rich air-fuel ratio are intermittently generated as much as possible.
Note that
Incidentally, when the small oxidation catalyst 14 is activated, it is possible to easily increase the temperature of the small oxidation catalyst 14 to 800° C. or above. Thus, as is apparent from
Then, in the present embodiment, when oxygen is insufficient to generate flames, secondary air is supplied from the secondary air supply device 45 into the engine exhaust passage. Specifically, when the engine is operating at an intermediate load or at a high load, the amount of secondary air necessary for adjusting the concentration of oxygen contained in exhaust gas to, for example, the oxygen concentration during light load or deceleration (with fuel injection) shown in
Supplying secondary air when oxygen is insufficient to generate flames in this way is carried out when the temperatures of the oxidation catalyst 13, particulate filter 16 and NOx occlusion catalyst 17 are increased. When secondary air is supplied at the time when NOx or SOx needs to be released from the NOx occlusion catalyst 17, there is a possibility that the air-fuel ratio of exhaust gas cannot be maintained at a rich air-fuel ratio. Thus, when oxygen is insufficient to generate flames at the time when NOx or SOx needs to be released from the NOx occlusion catalyst 17, no secondary air is supplied. In this case, no flame is generated to allow a rich air-fuel ratio.
That is, in the present embodiment, when NOx or SOx needs to be released from the NOx occlusion catalyst 17, it is determined whether the operating state of the engine is such that flames of a rich air-fuel ratio H can be generated. When NOx or SOx needs to be released from the NOx occlusion catalyst 17, and when the operating state of the engine is such that flames of a rich air-fuel ratio H can be generated, flames H are generated. In contrast, when the operating state of the engine is not such that flames of a rich air-fuel ratio H can be generated at the time when NOx or SOx needs to be released from the NOx occlusion catalyst 17, the air-fuel ratio of exhaust gas that flows into the NOx occlusion catalyst 17 is made rich without generating flames H.
Note that in this case, in the present embodiment, when the engine is operating at a light load or decelerating, it is determined that the operating state of the engine is such that flames of a rich air-fuel ratio can be generated. Thus, when the engine is operating at a light load or decelerating at the time when NOx or SOx needs to be released from the NOx occlusion catalyst 17, flames of a rich air-fuel ratio are generated.
Note that, as is apparent from
Next, fuel supply control executed in the present embodiment will be described with reference to
First, the case in which flames are intermittently generated to increase the temperatures of the oxidation catalyst 13, particulate filter 16 and NOx occlusion catalyst 17 will be described with reference to
Thus, in this case, exhaust gas temperature increasing control is carried out to increase the temperature of exhaust gas until the small oxidation catalyst 14 is activated, and, when the small oxidation catalyst 14 is activated, fuel is intermittently supplied from the fuel supply valve 15. The exhaust gas temperature increasing control is, for example, carried out by retarding the timing at which fuel is injected into each combustion chamber 2. Note that when oxygen is insufficient to generate flames, secondary air is supplied while fuel is being intermittently supplied, that is, while flame generation control is being carried out, as shown in
As flames are generated, the amount of fuel supply is increased, and the increased amount of fuel is intermittently supplied. At this time, that is, during rich flame generation control, flames of a rich air-fuel ratio are generated, and NOx is released from the NOx occlusion catalyst 17. Note that, when SOx is released from the NOx occlusion catalyst 17, the duration of the rich flame generation control is longer than the case shown in
In contrast, in step 62, when it is determined that ΣNOX is larger than NX, the process proceeds to step 63. In step 63, it is determined whether flames of a rich air-fuel ratio can be generated, that is, the engine is operating at a light load or decelerating. When it is determined that flames can be generated, the process proceeds step 64. In step 64, the process of intermittently generating flames of a rich air-fuel ratio H, that is, the fuel supply control shown in
In step 66, a differential pressure ΔP before and after the particulate filter 16 is detected by the differential pressure sensor 26. After that, in step 67, it is determined whether the differential pressure ΔP exceeds an allowable value PX. When ΔP is larger than PX, the process proceeds to step 68. In step 68, an amount of secondary air necessary for generating flames is calculated. Subsequently, in step 69, in order to regenerate the particulate filter 16, the process of intermittently generating flames H to increase the temperature of the particulate filter 16, that is, the fuel supply control shown in
Number | Date | Country | Kind |
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2008-215283 | Aug 2008 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB09/05319 | 4/22/2009 | WO | 00 | 1/14/2010 |