WO2013153611A1 - Internal combustion engine control device - Google Patents
Internal combustion engine control device Download PDFInfo
- Publication number
- WO2013153611A1 WO2013153611A1 PCT/JP2012/059725 JP2012059725W WO2013153611A1 WO 2013153611 A1 WO2013153611 A1 WO 2013153611A1 JP 2012059725 W JP2012059725 W JP 2012059725W WO 2013153611 A1 WO2013153611 A1 WO 2013153611A1
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- WIPO (PCT)
- Prior art keywords
- injection
- cylinder
- fuel
- amount
- catalyst
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/021—Introducing corrections for particular conditions exterior to the engine
- F02D41/0235—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
- F02D41/027—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to purge or regenerate the exhaust gas treating apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/30—Controlling fuel injection
- F02D41/3094—Controlling fuel injection the fuel injection being effected by at least two different injectors, e.g. one in the intake manifold and one in the cylinder
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/101—Three-way catalysts
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Definitions
- the present invention relates to a technical field of a control device for an internal combustion engine suitable for recovering an exhaust purification catalyst installed in an exhaust path from sulfur poisoning.
- the exhaust purification catalyst installed in the exhaust path adsorbs sulfur contained as impurities in the fuel to the noble metal added to the catalyst and poisons the sulfur.
- sulfur poisoning the activity of the catalyst is remarkably lost, and the original exhaust purification action of the catalyst cannot be obtained. Therefore, various sulfur poisoning recovery controls have been proposed for desorbing sulfur from the catalyst. Yes.
- sulfur is oxidized inside the cylinder or in the exhaust path and is adsorbed to the catalyst as SOx (sulfur oxide), and the desorption of sulfur simply means reduction of sulfur.
- Patent Document 1 discloses sulfur poisoning recovery control in a lean NOx catalyst.
- the exhaust gas purification apparatus for an internal combustion engine disclosed in Patent Document 1 includes an H 2 (hydrogen) sensor upstream of the lean NOx catalyst, and rich combustion in the cylinder is controlled based on the output value of the H 2 sensor. It is the composition which becomes. That is, it is configured that the H 2 concentration of the catalyst inflow gas is F / B controlled to a rich combustion control amount, and an appropriate amount of hydrogen can be supplied at the time of sulfur poisoning recovery.
- H 2 hydrogen
- Patent Document 2 discloses a technique for raising the temperature of the catalyst by controlling some cylinders to be rich in the air-fuel ratio and the remaining cylinders to be air-fuel ratio lean.
- Patent Document 3 discloses a configuration in which H 2 is supplied by an H 2 supply means mounted upstream of the catalyst when the amount of sulfur accumulated in the NOx catalyst exceeds a predetermined value.
- Patent Document 4 a CO 2 adsorbent, an H 2 generation catalyst, and a NOx catalyst are arranged in an exhaust system of a lean combustion engine, and CO is supplied to the H 2 generation catalyst, which is generated by an aquatic gas shift reaction.
- a configuration in which H 2 is sent as a reducing agent to the NOx catalyst is disclosed.
- Patent Document 5 discloses a lean NOx catalyst system, and in an internal combustion engine capable of controlling in-cylinder combustion, when NOx catalyst is regenerated, post-injection timing is performed at a timing when the dehydrogenation reaction and cracking reaction repel each other.
- the structure to perform is disclosed.
- combustion on the rich side of the air-fuel ratio is a disadvantageous control from the viewpoint of exhaust emission, apart from the reduction of sulfur and NOx, and is also economically disadvantageous in that it leads to a deterioration in fuel consumption. Control. Therefore, it is not reasonable to perform rich combustion in the dark cloud on the safe side (in this case, that is, on the side where the amount of hydrogen generated increases) for the purpose of reducing only sulfur.
- the present invention has been made in view of the above-described circumstances, and provides an internal combustion engine control device capable of recovering a catalyst from sulfur poisoning while suppressing an increase in cost and deterioration of exhaust emission and fuel consumption. This is the issue.
- an internal combustion engine control apparatus is capable of in-cylinder injection of a cylinder, an exhaust purification catalyst installed in an exhaust path connected to the cylinder, and fuel into the cylinder.
- the internal combustion engine according to the present invention is a concept that encompasses an engine that can convert thermal energy generated when an air-fuel mixture containing fuel is burned into kinetic energy and take it out.
- a catalyst is provided, and at least an in-cylinder injection device is provided as a fuel injection device.
- the number of cylinders, the cylinder arrangement, the fuel type, the fuel injection mode, the intake / exhaust system configuration, the valve train configuration, the combustion system, the presence / absence of the supercharger, and the excess The manner of supply is not limited in any way.
- the exhaust purification catalyst according to the present invention is a concept encompassing various types of catalysts that can be provided in the exhaust path of an internal combustion engine.
- a three-way catalyst for example, a lean NOx catalyst (also referred to as a NOx storage reduction catalyst).
- Practical forms such as oxidation catalyst.
- the catalyst is poisoned by sulfur contained as an impurity in the fuel according to the actual operation period of the internal combustion engine. Since sulfur poisoning of the catalyst reduces the catalytic activity, it is necessary to desorb sulfur from the catalyst at the appropriate timing (that is, to recover the catalyst from sulfur poisoning). It should be noted that “appropriate timing” does not necessarily mean that a condition that defines such timing is determined in advance. In practice, it is effective to take this kind of recovery measure at a timing when the degree of sulfur poisoning can be considered to have exceeded the prescribed level, but there is no recovery measure for sulfur poisoning or measures to suppress sulfur poisoning. It is effective regardless of the level of sulfur poisoning.
- the control device for an internal combustion engine promotes the generation of hydrogen in the cylinder by changing the injection mode of the in-cylinder injection device, so that recovery from sulfur poisoning of the catalyst, or sulfur of the catalyst It is configured to prevent adsorption.
- the in-cylinder injection device Is changed so that the homogeneity of the air-fuel mixture formed inside the cylinder is lowered.
- the first control means controls the in-cylinder injection device according to the changed injection mode.
- the “injection mode” refers to, for example, the number of injections, the injection timing, the injection period, or the like, and a control amount that can change the homogeneity of the air-fuel mixture.
- the internal combustion engine further includes a port injection device in addition to the in-cylinder injection device, it can suitably include an injection ratio between the in-cylinder injection amount and the port injection amount.
- the in-cylinder injection device directly injects fuel into the cylinder, and therefore, compared with a port injection device that injects fuel into the intake port, for example, fuel loss due to port adhesion or the like does not occur, but more fuel and intake gas. Requires a long premixing period.
- the fuel injection timing in the in-cylinder injection device is set between the intake top dead center and the bottom dead center as a preferred embodiment, although it depends on conditions. That is, by performing fuel injection before the start of the compression stroke, sufficient premixing of the fuel and the cylinder intake gas in the compression stroke is achieved.
- the injection timing can be a suitable example of the “injection mode” according to the present invention.
- hydrogen generation in the cylinder (not all need to occur in the cylinder, and may include what is generated in the exhaust path after being discharged from the cylinder) is mainly a water gas shift reaction (CO + H 2 O ⁇ H 2 + CO 2 ) And steam reforming reaction (HC + H 2 O ⁇ H 2 + CO). That is, by promoting the generation of unburned or incombustible substances such as CO or HC inside the cylinder, the generation of hydrogen in the cylinder or the exhaust path can be promoted. Therefore, by changing the mode of in-cylinder injection so as to reduce the homogeneity of the air-fuel mixture, the generation of hydrogen can be favorably promoted in the cylinder or the exhaust path.
- such a change in the injection mode requires a change in the fuel injection amount for each cylinder determined to maintain the theoretical air fuel ratio or the target air fuel ratio by, for example, various known air fuel ratio F / B controls. do not do. Therefore, the exhaust path and the air-fuel ratio of the catalyst are not greatly affected by such a change in the injection mode.
- the catalyst is recovered from sulfur poisoning without increasing the cost and exhaust emission and fuel consumption are deteriorated, or the accumulation of sulfur on the catalyst is suppressed. Is possible.
- the changing means changes the fuel injection timing to the retard side with respect to the standard time as the injection mode (second term).
- the homogeneity of the air-fuel mixture can be reduced, and hydrogen generation inside the cylinder, the exhaust path or the catalyst can be favorably promoted. I can do it.
- the “standard time” means the injection time under the same conditions when measures for recovery or suppression of such sulfur poisoning are not required. If the standard timing is determined so as to optimize the fuel consumption of the internal combustion engine, the retard of the injection timing, that is, the deterioration of the fuel consumption can be caused. Compared with the technical idea of generating hydrogen, the difference in the amount of fuel consumption occurs, but the effect is very small. In that sense, it can be said that deterioration of fuel consumption is sufficiently suppressed.
- the internal combustion engine includes a port injection device capable of performing a port injection of fuel to the cylinder, and the changing means includes the port injection as the injection mode.
- the fuel injection amount and the fuel injection amount and ratio of the in-cylinder injection are changed so that the fuel injection amount of the in-cylinder injection increases, and the control means changes the changed injection ratio.
- the in-cylinder injection device and the port injection device are controlled according to (3rd item).
- the port injection can maintain the homogeneity of the air-fuel mixture better than the in-cylinder injection. It is known that the cold startability can be improved by doing so.
- the ratio of the in-cylinder injection amount to the port injection amount with respect to a certain required injection amount can be a suitable control amount that gives controllability to the homogeneity.
- the injection ratio is controlled as an injection aspect of the in-cylinder injection device. More specifically, the injection ratio is changed so that the in-cylinder injection amount is larger than a standard value (for example, the in-cylinder injection amount under the same condition when S poison recovery is not considered). Accordingly, the generation of hydrogen in the cylinder or the exhaust path can be favorably promoted.
- a standard value for example, the in-cylinder injection amount under the same condition when S poison recovery is not considered.
- first estimation means for estimating the amount of sulfur accumulated in the catalyst, and for recovering the catalyst from the sulfur poisoning from the estimated amount of accumulation.
- Second estimating means for estimating a required amount or required concentration of hydrogen, and the changing means changes the injection mode in accordance with the estimated required amount or required concentration (fourth term).
- the amount of sulfur deposition on the catalyst is estimated by the first estimating means.
- the “deposition amount” means an accumulation amount.
- the adhesion amount, the adsorption amount, and the deposition amount You may replace it with a poisonous amount.
- the accumulation amount is determined in advance experimentally with internal combustion engine operating parameters that may include at least part of the engine speed, intake pressure, accelerator opening, intake air amount, throttle opening, load factor, and fuel injection amount. It may be estimated based on the correlation between the operating parameter and the amount of sulfur production, which is established empirically or theoretically.
- the amount of sulfur or sulfur oxide (SOx) discharged per unit time in the exhaust path of the internal combustion engine may be integrated, and the accumulation amount may be estimated from this integrated value.
- the relationship between the integrated value and the actual accumulation amount that is, not all of the sulfur or sulfur oxide discharged from the cylinder is deposited on the catalyst
- the relationship is further referred to. May be.
- the second estimating means recovers the catalyst from sulfur poisoning from the amount of accumulation estimated by the first estimating means (including the concept of suppressing sulfur poisoning by suppressing the adsorption of sulfur to the catalyst).
- the apparatus further comprises third estimation means for estimating the amount of hydrogen generated in the cylinder, and the changing means includes the estimated required amount or A period for changing the injection mode may be determined based on the required concentration and the estimated generation amount (Section 5).
- the configuration is such that the amount of hydrogen produced by changing the injection mode is estimated in this way, it is possible to generate an appropriate amount of hydrogen according to the required amount or the required concentration estimated by the second estimating means. Therefore, sulfur poisoning of the catalyst or adsorption of sulfur to the catalyst can be efficiently prevented.
- the estimation of the hydrogen generation amount by the third estimation means is preferably performed in advance experimentally, empirically, or theoretically for each injection mode changed by the changing unit. This can be suitably realized by associating the generation amount or the concentration of. In short, if such a relationship is held as a control map that can be referred to, the third estimation means can estimate the generation amount relatively easily.
- the cooling water temperature specifying means for specifying the cooling water temperature of the internal combustion engine is provided, and the third estimating means generates the estimated generation according to the specified cooling water temperature.
- the amount may be corrected (Section 6).
- ⁇ ⁇ Hydrogen generated in the cylinder under one injection mode change condition varies depending on the engine warm-up state of the internal combustion engine.
- the combustion state of the cylinder worsens as engine warm-up becomes insufficient, such as during cold start. That is, even if the uniformity of the air-fuel mixture is constant, the amount of hydrogen produced tends to increase by the amount that the engine is in a relatively cooled state.
- the “specific” according to the present invention is comprehensive including not only detection by a detection unit such as a sensor but also acquisition of a sensor value from this type of detection unit or estimation based on an operating condition of the internal combustion engine. It is a concept.
- control apparatus includes catalyst temperature specifying means for specifying the temperature of the catalyst, and air-fuel ratio specifying means for specifying an air-fuel ratio in the exhaust path, wherein the changing means includes When the specified air-fuel ratio is richer than the stoichiometric air-fuel ratio by a predetermined value or more and the temperature of the specified catalyst is lower than the predetermined value, the homogeneity inside the cylinder is reduced. The injection mode of the in-cylinder injection device is changed (Seventh Item).
- the catalyst temperature (in short, the catalyst bed temperature) is specified by the catalyst temperature specifying means.
- the air-fuel ratio in the exhaust path is specified by the air-fuel ratio specifying means.
- the air-fuel ratio of the internal combustion engine is often F / B controlled to the theoretical air-fuel ratio or a target air-fuel ratio in the vicinity thereof by air-fuel ratio F / B control as described above, for example, power performance is required.
- the air-fuel ratio is controlled to be rich for promoting the temperature rise of the catalyst or for other reasons.
- the amount of sulfur adsorbed on the catalyst becomes high. From the viewpoint of actively avoiding sulfur poisoning of the catalyst, it is effective to actively generate hydrogen under such conditions.
- the changing means changes the injection mode of the in-cylinder injection device so that the homogeneity inside the cylinder is lowered. It is the composition to do. In other words, such a condition is adopted as an example of “when reducing sulfur deposited on the catalyst” according to the present invention.
- FIG. 1 is a schematic configuration diagram conceptually showing a configuration of an engine system according to an embodiment of the present invention. It is a schematic block diagram which represents notionally the structure of the fuel supply apparatus in the engine system of FIG. It is a schematic block diagram which represents notionally the structure of the high pressure pump in the fuel supply apparatus of FIG. 2 is a flowchart of S poison recovery control executed by an ECU in the engine system of FIG. 1.
- FIG. 5 is a conceptual diagram of an H2 request amount map referred to in S poison recovery control of FIG. 4. It is a figure which illustrates the relationship between the injection ratio and the amount of H2 generation in the engine system of FIG. It is a conceptual diagram of the correction coefficient in the S poison recovery control of FIG.
- FIG. 1 is a schematic configuration diagram conceptually showing the configuration of the engine system 10.
- an engine system 10 is mounted on a vehicle (not shown) and includes an ECU 100 and an engine 200.
- the ECU 100 is an electronic control unit that includes a CPU, a ROM, a RAM, and the like and is configured to be able to control the operation of the engine system 10, and is an example of the “control device for an internal combustion engine” according to the present invention.
- the ECU 100 is configured to be able to execute S poisoning recovery control described later in accordance with a control program stored in the ROM.
- the ECU 100 is an example of each of “changing means”, “first control means”, “first estimating means”, “second estimating means”, “third estimating means”, and “specifying means” according to the present invention. Although it is an integrated electronic control unit that can function, the physical, mechanical, and electrical configuration of each means according to the present invention is not limited to this, and each means includes, for example, a plurality of ECUs, You may comprise as various computer systems, such as various processing units, various controllers, or a microcomputer apparatus.
- Engine 200 is an in-line four-cylinder gasoline engine that is an example of an “internal combustion engine” according to the present invention.
- the engine 200 includes a plurality of cylinders 201 accommodated in a cylinder block CB.
- the cylinders 201 are arranged in the depth direction of the drawing, and only one cylinder 201 is shown in FIG. 1.
- the combustion chamber formed in the cylinder 201 is provided with a piston 202 that reciprocates in the vertical direction in the figure in accordance with the explosive force accompanying the combustion of the air-fuel mixture.
- the reciprocating motion of the piston 202 is converted into the rotational motion of the crankshaft 204 via the connecting rod 203 and is used as power for the vehicle on which the engine 200 is mounted.
- crank position sensor 205 capable of detecting the rotational position (ie, crank angle) of the crankshaft 204 is installed.
- the crank position sensor 205 is electrically connected to the ECU 100, and the detected crank angle is referred to the ECU 100 at a constant or indefinite period.
- the crank position sensor 205 is used for calculation of the engine speed NE or other control. It becomes the composition which is done.
- air sucked from the outside is purified by a cleaner (not shown) and then guided to a common intake pipe 206 for each cylinder.
- the intake pipe 206 is provided with a throttle valve 207 that can adjust the amount of intake air that is the amount of intake air.
- the throttle valve 207 is configured as a kind of electronically controlled throttle valve whose driving state is controlled by a throttle valve motor (not shown) electrically connected to the ECU 100.
- the ECU 100 basically drives and controls the throttle valve motor so as to obtain a throttle opening corresponding to an accelerator opening Ta detected by an unillustrated accelerator position sensor. However, the ECU 100 can also adjust the throttle opening without intervention of the driver's intention through the operation control of the throttle valve motor.
- the intake air appropriately adjusted by the throttle valve 207 is sucked into the cylinder through the intake port 208 corresponding to each cylinder 201 when the intake valve 209 is opened.
- the intake valve 209 is configured such that its opening / closing timing is defined according to the cam profile of a cam 210 having a substantially elliptical shape in cross section as shown in the figure.
- the cam 210 is fixed to an intake camshaft (reference number omitted) connected to the crankshaft 204 via power transmission means such as a cam sprocket or a timing chain. Therefore, the opening / closing phase of the intake valve 209 is uniquely related to the rotation phase of the crankshaft 204 (ie, the crank angle) in one fixed state.
- the fixed state between the intake cam 210 and the intake camshaft varies depending on the hydraulic pressure of the control oil supplied by the hydraulic drive device 211. More specifically, the intake cam 210 is connected to the intake cam shaft via a wing-like member called a vane, and the rotational phase between the vane and the intake cam shaft is applied to the hydraulic chamber of the hydraulic drive device 211. The configuration changes according to the hydraulic pressure applied. Therefore, the rotational phase between the intake cam 210 fixed to the vane and the intake camshaft also changes according to the hydraulic pressure.
- the hydraulic drive device 211 is in a state of being electrically connected to the ECU 100, and the ECU 100 can change the opening / closing timing of the intake valve 209 through the control of the hydraulic drive device 211.
- variable valve apparatus can take is not limited to the thing of this embodiment.
- the intake valve 209 may be a so-called electromagnetically driven valve (cam-by-wire) that is electromagnetically driven by a solenoid actuator or the like.
- the intake pipe 206 is provided with an air flow meter 212 capable of detecting the intake air amount Ga.
- the air flow meter 212 is electrically connected to the ECU 100, and the detected intake air amount Ga is referenced by the ECU 100 at a constant or indefinite period.
- the intake air guided to the intake port 208 is mixed with the port injection fuel injected from the PFI (Port Fuel Injector) 342 in which a part of the injection valve is exposed to the intake port 208 and mixed with the above-described fuel. It becomes a mixture.
- the PFI 342 is one element that constitutes the fuel supply device 300 described later with reference to FIG.
- a part of a spark plug (not shown) of an ignition device 213 that is a spark ignition device is exposed.
- the air-fuel mixture compressed in the compression stroke of the engine 200 is ignited and burned by the ignition operation of the spark plug.
- the ignition device 213 is electrically connected to the ECU 100, and the ignition timing of the ignition device 213 is controlled by the ECU 100.
- the air-fuel mixture that has undergone a combustion reaction in the combustion chamber is opened and closed by an exhaust valve 215 that is driven to open and close by the cam profile of the exhaust cam 214 that is indirectly connected to the crankshaft 204 in the exhaust stroke following the combustion stroke.
- the exhaust port 216 is discharged.
- the exhaust port 216 is connected to one end of an EGR pipe 217.
- the other end of the EGR pipe 217 is connected to an intake manifold (reference numeral omitted) located on the upstream side of the intake port 208, and a part of the exhaust can be returned to the intake system as EGR gas.
- the EGR amount that is the supply amount of EGR gas is controlled by an EGR valve 218 installed in the EGR pipe 217.
- the EGR valve 218 is an electromagnetically driven valve that controls the opening and closing of the valve by the electromagnetic force of the solenoid, and the valve opening degree is controlled by the control of the ECU 100 electrically connected to the drive device that controls the excitation state of the solenoid. It becomes the composition which is done.
- the EGR pipe 217 is connected to the exhaust port 216.
- the EGR pipe 217 collects exhaust ports 216 of a plurality of cylinders 201 on the downstream side of the exhaust port 216, and will be described later. It may be connected to an exhaust manifold leading to 219.
- the EGR pipe 217 and the EGR valve 218 constitute an HPL (High Pressure Pressure Loop) EGR device.
- HPL High Pressure Pressure Loop
- the configuration of the EGR device is not limited to this, and for example, a three-way catalyst 220 described later is used. It may be an LPL (Low Pressure Loop) EGR device that extracts exhaust gas from the downstream side.
- the exhaust pipe 219 is connected to the exhaust port 216 of each cylinder.
- the exhaust pipe 214 is an example of an “exhaust path” according to the present invention.
- the exhaust pipe 219 is provided with a three-way catalyst 220 as an example of the “exhaust purification catalyst” according to the present invention.
- the three-way catalyst 215 is a known catalyst device in which a noble metal such as platinum is supported on a catalyst carrier.
- the three-way catalyst 215 emits exhaust gas by causing the oxidative combustion reaction of HC and CO and the reduction reaction of nitrogen oxide NOx to proceed substantially simultaneously. It can be purified.
- an air-fuel ratio sensor 221 capable of detecting the input side air-fuel ratio A / Fin that is the air-fuel ratio of the catalyst inflow gas flowing into the three-way catalyst 220 is installed.
- the air-fuel ratio sensor 221 is, for example, a limiting current type wide-area air-fuel ratio sensor provided with a diffusion resistance layer.
- the air-fuel ratio sensor 221 is a sensor that outputs an output voltage value Vafin corresponding to the input-side air-fuel ratio A / Fin that is the air-fuel ratio of the exhaust (catalyst inflow gas) upstream of the three-way catalyst 220. That is, the air-fuel ratio sensor 221 employs a configuration in which the input-side air-fuel ratio A / Fin is indirectly detected by a voltage value having a unique relationship with the input-side air-fuel ratio A / Fin.
- the output voltage value Vafin matches the reference output voltage value Vst when the input side air-fuel ratio A / Fin is the stoichiometric air-fuel ratio.
- the output voltage value Vafin is lower than the reference output voltage value Vst when the input side air-fuel ratio A / Fin is on the air-fuel ratio rich side, and when the input-side air-fuel ratio A / Fin is on the air-fuel ratio lean side. It becomes higher than the reference output voltage value Vst. That is, the output voltage value Vafin continuously changes with respect to the change of the input side air-fuel ratio A / Fin.
- the air-fuel ratio sensor 221 is electrically connected to the ECU 100, and the detected output voltage value Vafin is referred to by the ECU 100 at a constant or indefinite period.
- an O 2 sensor 222 that can detect the downstream oxygen concentration Coxs that is the oxygen concentration of the catalyst exhaust gas that has passed through the three-way catalyst 220 is installed.
- the O 2 sensor 222 is a known electromotive force type oxygen concentration sensor (that is, a concentration cell type oxygen concentration sensor using stabilized zirconia).
- the O 2 sensor 222 is a sensor that outputs an output voltage value Voxs corresponding to the downstream oxygen concentration Coxs. That is, the O 2 sensor 222 adopts a configuration in which the oxygen concentration is indirectly detected by a voltage value having a unique relationship with the oxygen concentration.
- the output voltage value Voxs of the O 2 sensor 222 is a reference when the air-fuel ratio of the catalyst exhaust gas is the stoichiometric air-fuel ratio (in other words, when the downstream oxygen concentration Coxs is the reference oxygen concentration Coxsb corresponding to the stoichiometric air-fuel ratio). It corresponds to the output voltage value Voxsb (for example, about 0.5V).
- the output voltage value Voxs is higher than the reference output voltage value Voxsb when the air-fuel ratio of the catalyst exhaust gas is on the air-fuel ratio rich side with respect to the stoichiometric air-fuel ratio, and when the air-fuel ratio is also on the air-fuel ratio lean side. It becomes lower than the reference output voltage value Voxsb.
- the output voltage value Voxs of the O 2 sensor 222 is a decrease in the air-fuel ratio (ie, oxygen concentration). With a decrease in Coxs), it increases relatively linearly and substantially linearly to a maximum output voltage value Voxsmax (for example, about 0.9 V) corresponding to the rich-side detection limit air-fuel ratio. In the air-fuel ratio region on the rich side with respect to the rich-side detection limit air-fuel ratio, the output voltage value Voxs is substantially constant at the maximum output voltage value Voxsmax.
- the output voltage value Voxs of the O 2 sensor 222 increases the air-fuel ratio (that is, the oxygen concentration Coxs increases).
- a minimum output voltage value Voxsmin for example, about 0.1 V
- the output voltage value Voxs is substantially constant at the minimum output voltage value Voxsmin.
- the O 2 sensor 222 is electrically connected to the ECU 100, and the detected output voltage value Voxs is referred to by the ECU 100 at a constant or indefinite period.
- a water temperature sensor 223 capable of detecting a cooling water temperature Tw, which is a temperature of cooling water (LLC) circulated and supplied to cool the engine 200, is installed in a water jacket installed so as to surround the cylinder block CB. It is arranged.
- the water temperature sensor 223 is electrically connected to the ECU 100, and the detected cooling water temperature Tw is referred to by the ECU 100 at a constant or indefinite period.
- Engine 200 includes DFI (Direct Fuel Injector) 362 capable of in-cylinder fuel injection in addition to PFI 342. A part of the injection valve of the DFI 362 is exposed to the combustion chamber of the cylinder 201.
- the DFI 362 and the PFI 342 constitute a fuel supply device 300.
- FIG. 2 is a schematic configuration diagram conceptually showing the fuel supply device 300.
- symbol shall be attached
- the fuel supply apparatus 300 includes a fuel tank 310, a feed pipe 320, a feed pump 330, a port injection system 340, a high-pressure pump 350, and an in-cylinder injection system 360.
- the fuel tank 310 is a tank for storing fuel (in this embodiment, gasoline).
- the feed pipe 320 is a metal tubular member having one end connected to the fuel tank 310 and the other end connected to the port injection system 340 and the in-cylinder injection system 360.
- the feed pump 330 is provided in the vicinity of the fuel tank 310 in the feed pipe 320.
- the feed pump 330 is an electric pump device configured to pump fuel from the fuel tank 310 and supply the fuel to the feed pipe 320 at a desired fuel discharge speed (discharge amount per hour).
- the fuel discharged from the feed pump 330 is a low-pressure fuel having a predetermined feed pressure Pfd.
- the fuel discharge speed of the feed pump 330 is controlled by a drive device (not shown) that is electrically connected to the ECU 100.
- the feed pump 330 can variably control the feed pressure Pfd that is the fuel pressure in the feed pipe 320 through the control of the fuel discharge speed.
- the port injection system 340 includes a low pressure delivery 341, a plurality of PFIs 342, and a feed pressure sensor 343.
- the low pressure delivery 341 is a buffer configured to accumulate a certain amount of low pressure fuel having a feed pressure Pfd.
- the PFI 342 is a fuel injection device as an example of the “port injection device” according to the present invention connected to the low pressure delivery 341. As described above, the fuel injection valve of the PFI 342 is exposed to the intake port 208 of each cylinder, and an amount of port injection fuel Fpi determined by the valve opening period of the fuel injection valve and the feed pressure Pfd is injected into the intake port 208 as spray. It is configured to be possible.
- the feed pressure sensor 343 is a sensor configured to be able to detect the feed pressure Pfd of the low-pressure fuel described above.
- the feed pressure sensor 343 is electrically connected to the ECU 100, and the detected feed pressure Pfd is referred to by the ECU 100 at a constant or indefinite period.
- the high-pressure pump 350 is a mechanical pump device interposed between the feed pump 330 and the in-cylinder injection system 360.
- FIG. 3 is a schematic configuration diagram conceptually showing the configuration of the high-pressure pump 350.
- symbol shall be attached
- the high-pressure pump 350 includes an electromagnetic metering valve 351, a suction valve 352, a cylinder 353, a plunger 354, a pressurizing chamber 355, a cam 356, a discharge valve 357, and a high-pressure pipe 358.
- the electromagnetic metering valve 351 is an electromagnetic on-off valve that is provided on the feed pipe 320 connected to the feed pump 330 and adjusts the flow rate of the low-pressure fuel delivered by the feed pump 320.
- the flow rate of the low-pressure fuel pumped up from the fuel tank 310 by the feed pump 320 is adjusted by the electromagnetic metering valve 351 and supplied to the pressurizing chamber 355 to which one end of the feed pipe 320 is connected.
- the electromagnetic metering valve 351 is electrically connected to the ECU 100, and the drive duty that defines the valve opening period is controlled by the ECU 100.
- Plunger 354 is a pressurizing member installed in cylinder 353, and a rod-like member connected to the lower end is fixed to intake camshaft ICS of engine 200 and rotates in conjunction with the rotation of intake camshaft ICS.
- TDC Top Death Center
- BDC Bottom Dead center
- the pressurizing chamber 355 is a space defined by the inner wall portion of the cylinder 353 and the upper end portion of the plunger 354, and is a space whose volume changes in accordance with the reciprocation of the plunger 354 described above.
- the fuel metered by the electromagnetic metering valve 351 is sucked into the pressurizing chamber by pushing the suction valve 352 open when the plunger 354 moves from the TDC to the BDC in the cylinder 353 (that is, during the decompression period).
- the pressurized fuel is configured to push open the discharge valve 357 to be supplied to the high-pressure pipe 358 and to be pumped to the high-pressure delivery 361 connected to the high-pressure pipe 358.
- the driving load is uniquely related to the open state of the electromagnetic metering valve 351. That is, if the valve opening period of the electromagnetic metering valve 351 is long, more fuel is introduced into the pressurizing chamber 355, and the driving load of the high pressure pump 350 is increased accordingly.
- the high-pressure pump 350 exemplified here is an example of a high-pressure pump device in a cylinder injection system that directly injects fuel into the cylinder, and of course, other known modes can be adopted.
- the in-cylinder injection system 360 includes a high-pressure delivery 361, a plurality of DFIs 362, and a high-pressure sensor 363.
- the high-pressure delivery 361 is a buffer configured to be able to store a certain amount of high-pressure fuel having a fuel pressure Ph (Ph> Pfd).
- the DFI 362 is a fuel injection device that is connected to the high pressure delivery 361 and is an example of the “in-cylinder injection device” according to the present invention. As described above, the fuel injection valve of the DFI 362 is exposed to the combustion chamber of each cylinder, and the amount of in-cylinder injection fuel Fdi determined by the opening period of the fuel injection valve and the fuel pressure Ph is sprayed into the combustion chamber of the cylinder 201. It is configured to be jettable.
- the DFI 362 includes an electromagnetic valve that operates based on a command supplied from the ECU 100, and a nozzle (both not shown) that injects fuel when the electromagnetic valve is energized.
- the solenoid valve is configured to be able to control the communication state between the pressure chamber to which the high-pressure fuel accumulated in the high-pressure delivery 361 is applied and the low-pressure passage connected to the pressure chamber.
- the pressure chamber and the low-pressure passage are sometimes communicated with each other, and the pressure chamber and the low-pressure passage are shut off from each other when energization is stopped.
- the nozzle has a built-in needle that opens and closes the nozzle hole, and the fuel pressure in the pressure chamber urges the needle in the valve closing direction (direction in which the nozzle hole is closed). Accordingly, when the pressure chamber communicates with the low pressure passage by energizing the electromagnetic valve and the fuel pressure in the pressure chamber decreases, the needle rises in the nozzle and opens (opens the nozzle hole), thereby causing the high pressure delivery 361. High-pressure fuel supplied from the nozzle is injected from the injection hole. Further, when the pressure chamber and the low pressure passage are cut off from each other by stopping energization of the solenoid valve and the fuel pressure in the pressure chamber rises, the needle is lowered in the nozzle and closed, thereby terminating the injection.
- the injection ratio Rinj which is the ratio of the port injection fuel Fpi and the in-cylinder injection fuel Fdi, can be freely controlled between the PFI 342 and the DFI 362.
- the fuel injection amount Q of one cylinder 201 is the sum of the port injection amount Qpfi that is the fuel injection amount of the PFI 342 and the in-cylinder injection amount Qdfi that is the fuel injection amount of the DFI 362.
- the fuel injection amount Q is controlled by the ECU 100 by air-fuel ratio F / B control that is always executed during the operation period of the engine 200.
- the air-fuel ratio F / B control according to the present embodiment includes a main F / B control and a sub F / B control.
- the main F / B control is control of the fuel injection amount so that the input side air-fuel ratio A / Fin obtained based on the output voltage value Vafin of the air-fuel ratio sensor 221 converges to the input side target air-fuel ratio A / Fintg. is there.
- the sub F / B control is a control for correcting the output voltage value Vafin of the air-fuel ratio sensor 221 or the input side target air-fuel ratio A / Fintg so that the output voltage value Voxs of the O 2 sensor 222 converges to the target output voltage value Voxstg. is there.
- the target air-fuel ratio is an air-fuel ratio that optimizes the exhaust purification action of the three-way catalyst 220, and is, for example, a theoretical air-fuel ratio.
- this target air-fuel ratio may be changed as appropriate according to the required performance of the engine 200, etc., as long as it is allowed in consideration of emissions and fuel consumption, and may be changed as appropriate.
- the ECU 100 determines the above-described injection division ratio Rinj according to a predetermined standard.
- the injection ratio Rinj is usually a value experimentally, empirically, or theoretically determined in advance so that the fuel consumption of the engine 200 is best (this value is appropriately referred to as “standard injection ratio Rinjb” thereafter). Control).
- S poison recovery control The gasoline used for the engine 200 often contains sulfur.
- the sulfur in the fuel is likely to be combined with oxygen in the cylinder 201 or in the exhaust pipe 219 to become sulfur oxide (SOx).
- SOx sulfur oxide
- the sulfur oxide is easily chemically combined with the noble metal of the three-way catalyst 220, and the three-way catalyst 220 is gradually sulfur poisoned (S poison) during the operation period of the engine 200.
- S (sulfur) poisoning recovery control is executed by the ECU 100 in order to recover the three-way catalyst 220 from sulfur poisoning.
- FIG. 4 is a flowchart of the S poison recovery control.
- the ECU 100 acquires the S accumulation amount Dsf of the three-way catalyst 220 (step S101).
- the S deposition amount Dsf is the amount of sulfur deposited on the three-way catalyst 220 during the period from the end of the previous S poison recovery control to the present, and “the amount of sulfur deposition on the catalyst” according to the present invention. It is an example.
- the S accumulation amount Dsf is repeatedly calculated by the ECU 100 in a control routine different from the S poison recovery control, and stored in a rewritable memory such as a RAM with appropriate updating. That is, in the process of executing the S accumulation amount Dsf, the ECU 100 functions as an example of the “first estimation unit” according to the present invention.
- the ECU 100 estimates the S accumulation amount Dsf from the accumulated fuel consumption amount ⁇ Q, which is a value obtained by accumulating the fuel injection amount Q, which is the sum of the port injection amount Qpfi and the in-cylinder injection amount Qdfi, for each cycle of each cylinder. It is assumed that the sulfur content in the unit fuel is given as an initial value in advance.
- the ECU 100 calculates the S accumulation amount Dsf by multiplying the accumulated fuel consumption amount ⁇ Q at that time by a predetermined accumulation rate ⁇ .
- This deposition rate ⁇ is a correction coefficient that represents the ratio of sulfur deposited on the three-way catalyst 220 out of the sulfur discharged to the exhaust pipe 219, and experimentally, empirically, or theoretically, engine speed NE in advance.
- the load factor KL (that is, the ratio of the amount of fresh air sucked into the cylinder 201 to the physical maximum value) is stored in the control map as a parameter.
- the higher the engine speed NE and the larger the load factor KL the weaker the accumulation rate ⁇ tends to decrease.
- such an estimation mode of the S accumulation amount Dsf is an example, and various known modes can be applied to the calculation of the S deposition amount.
- step S102 determines whether the acquired S accumulation amount Dsf is larger than the reference value Dsfth (step S102).
- the reference value Dsfth is determined in advance experimentally, empirically, or theoretically as a value that reduces the purification efficiency of the three-way catalyst 220 to a predetermined level or more due to S poisoning.
- step S102: NO the ECU 100 returns the process to step S101.
- step S102 when the S accumulation amount Dsf is larger than the reference value Dsfth (step S102: YES), the ECU 100 executes the processing after step S103, assuming that the three-way catalyst 220 needs to be recovered from sulfur poisoning.
- step S103 the ECU 100 calculates an H2 (hydrogen) demand amount Nh2.
- the required H2 amount Nh2 is a required amount of hydrogen that needs to be generated in each cylinder 201 in order to recover the sulfur poisoning of the three-way catalyst 220, and according to the present invention, “for recovering the catalyst from sulfur poisoning” This is an example of “required amount of hydrogen”.
- the ECU 100 refers to the H2 request amount map stored in the ROM when calculating the H2 request amount Nh2.
- the H2 request amount map will be described with reference to FIG.
- FIG. 5 is a conceptual diagram of the H2 request amount map.
- the H2 requirement amount Nh2 and the S deposition amount Dsf are represented on the vertical axis and the horizontal axis, respectively.
- the H2 requirement amount Nh2 has a linear relationship with the S deposition amount Dsf.
- the relationship illustrated in FIG. 5 is digitized and stored in the H2 request amount map, and when calculating the H2 request amount Nh2, the ECU 100 acquires the S accumulation acquired in step S101 from the H2 request amount map. A value corresponding to the amount Dsf is selected (note that such a selection process is also an example of calculation).
- the ECU 100 changes the injection division ratio Rinj from the above-described standard injection ratio Rinjb to the injection division ratio Rinjh2 for sulfur poisoning recovery (step S104).
- FIG. 6 is a diagram illustrating the relationship between the ejection division ratio Rinj and the H2 generation amount Gh2.
- the vertical axis and the horizontal axis respectively represent the H2 generation amount Gh2 and the spray distribution ratio Rinj.
- the injection ratio Rinj in the present embodiment is defined as Qpfi / (Qpfi + Qdfi). The larger the value (left side in the figure), the larger the port injection amount Qpfi, and the smaller the value (right side in the figure), the in-cylinder injection. The quantity Qdfi increases.
- the H2 generation amount Gh2 increases in a quadratic function as the injection ratio Rinj decreases (that is, the in-cylinder injection amount Qdfi increases). Note that the characteristics shown in the figure are characteristics when the air-fuel ratio of the cylinder is the stoichiometric air-fuel ratio (14.6).
- the injection ratio Rinjh2 for recovery from sulfur poisoning may be a value smaller than the standard injection ratio Rinjb, and there is no need to have a clear guideline for the determination.
- the H2 generation amount Gh2 is not sufficiently large, the time during which the ejection ratio Rinj deviates from the standard ejection ratio Rinjb becomes longer, and thus is set to an appropriate value experimentally in advance.
- a configuration in which one ejection ratio Rinjh2 is selected from a plurality of options according to the magnitude of the H2 request amount Nh2 may be adopted.
- the ECU 100 acquires a correction coefficient for the H2 generation amount Gh2 (step S105).
- the correction coefficient will be described with reference to FIG. FIG. 7 is a conceptual diagram of the correction coefficient.
- the correction coefficient is a function of the cooling water temperature Tw. That is, the correction coefficient is set to be larger than 1 in the temperature region where the coolant temperature Tw is lower than the warm-up completion determination value Tww. This is because in the unwarmed state, the combustion in the cylinder 201 is worse than after the warm-up is completed.
- the ECU 100 determines the basic H2 generation amount according to the injection ratio Rinjh2 for recovery from sulfur poisoning, the correction coefficient, and the engine of the engine 200.
- the instantaneous H2 generation amount Gh2m is calculated based on the rotational speed NE and the load factor KL (that is, has a unique relationship with the gas discharge amount per unit time), and the instantaneous H2 generation amount Gh2m is integrated ( Step S106).
- the ECU 100 acquires the time integration value ⁇ Gh2m of the instantaneous H2 generation amount Gh2m (step S107).
- the time integrated value ⁇ Gh2m means the amount of hydrogen produced up to the present after the change of the injection ratio Rinj.
- step S108 the ECU 100 determines whether or not the acquired time integration value ⁇ Gh2m is larger than the previously calculated H2 request amount Nh2 (step S108). If ⁇ Gh2m is equal to or less than Nh2 (step S108: NO), the process returns to step S105.
- step S108 When it is determined in step S108 that ⁇ Gh2m is larger than Nh2 (step S108: YES), the ECU 100 clears the S accumulation amount Dsf (step S109), and returns the injection division ratio Rinj to the standard injection division ratio Rinjb. (Step S110), the process returns to Step S101.
- the S poison recovery control is executed as described above.
- the S poison recovery control when the S accumulation amount Dsf of the three-way catalyst 220 exceeds the reference value Dsfth, the injection as the injection mode of the DFI 362 that is the in-cylinder injection device
- the division ratio Rinj is changed from the standard injection division ratio Rinjb for optimally maintaining fuel efficiency to the injection division ratio Rinjh2 for recovery from sulfur poisoning.
- the injection ratio Rinjh2 for recovery from sulfur poisoning is an injection ratio in which the in-cylinder injection amount Qdfi is larger than the standard injection ratio Rinjb.
- the desorption of sulfur is promoted by the H2 generated in the cylinder 201. .
- FIG. 8 is a flowchart of the S poison recovery control according to the second embodiment of the present invention.
- the same reference numerals are given to the same portions as those in FIG. 4, and the description thereof will be omitted as appropriate.
- the ECU 100 changes the in-cylinder injection timing Tdfi from the standard in-cylinder injection timing Tdfi to the in-cylinder injection timing Tdfih2 for sulfur poisoning recovery (step S103). S201).
- FIG. 9 is a diagram illustrating the relationship between the in-cylinder injection timing Tdfi and the H2 generation amount Gh2.
- the vertical axis and the horizontal axis represent the H2 generation amount Gh2 and the in-cylinder injection timing Tdfi, respectively.
- the in-cylinder injection timing Tdfi is a crank angle at which the DFI 362 starts fuel injection.
- the H2 generation amount Gh2 increases as the in-cylinder injection timing Tdfi moves toward the retard side (the right side in the figure). Note that the illustrated characteristics are characteristics after the engine 200 is completely warmed up.
- the standard in-cylinder injection timing Tdfib is between the intake top dead center TDCi and the intake bottom dead center BDCi, and the end of the intake stroke and the entire compression stroke are provided for premixing of fuel and intake gas. Yes.
- the in-cylinder injection timing Tdfi is changed to the retarded angle side, it is difficult to ensure a period during which the in-cylinder injected fuel is sufficiently mixed with the intake gas, and the homogeneity of the air-fuel mixture decreases.
- the H2 generation amount Gh2 increases as in the case of the spray distribution ratio Rinj.
- the in-cylinder injection timing Tdfi for recovery from sulfur poisoning may be a value retarded from the standard in-cylinder injection timing Tdfib. It is not necessary. However, if the H2 generation amount Gh2 is not sufficiently large, the time during which the in-cylinder injection timing Tdfi deviates from the standard in-cylinder injection timing Tdfi becomes long, and thus is set to an appropriate value experimentally in advance. At this time, one in-cylinder injection timing Tdfih2 may be selected from a plurality of options according to the magnitude of the H2 request amount Nh2.
- the instantaneous H2 generation amount Gh2m is integrated (step S106) in the same way as when the injection ratio Tinj is switched.
- the H2 generation amount Gh2 that is a calculation reference of the instantaneous H2 generation amount Gh2m is different from the case where the injection ratio Rinj is switched.
- Step S106 and subsequent steps are the same as in the first embodiment up to step S109.
- the S accumulation amount Dsf is cleared (step S109)
- the in-cylinder injection timing Tdfi is returned to the standard in-cylinder injection timing Tdfib (step S202). )
- the process returns to step S101.
- the S poison recovery control according to the second embodiment is executed as described above.
- the hydrogen in the cylinder 201 is controlled by the retard control of the in-cylinder injection timing Tdfi, similarly to the injection ratio Rinj according to the first embodiment.
- production can be accelerated
- the S poison recovery control is executed. It was.
- FIG. 10 is a flowchart of the S adsorption suppression control according to the third embodiment.
- the same reference numerals are given to the same portions as those in FIG. 4, and the description thereof will be omitted as appropriate.
- the ECU 100 detects that the input side air-fuel ratio A / Fin detected by the air-fuel ratio sensor 221 is shifted to a rich side by a predetermined amount or more with respect to the theoretical air-fuel ratio (hereinafter, such an air-fuel ratio is referred to as “rich air-fuel ratio”. It is determined whether the catalyst bed temperature Tcat, which is the temperature of the three-way catalyst 220, is less than the reference value Tcatth (referred to as “fuel ratio”) (step S301).
- the ECU 100 When the input side air-fuel ratio A / Fin is a rich air-fuel ratio and the catalyst bed temperature Tcat is lower than the reference value Tcatth (step S301: YES), the ECU 100 generates the injection ratio Rinj as H2 as in the first embodiment. It changes to the injection division ratio Rinjh2 for use (step S104).
- step S301 When the spray distribution ratio Rinj is changed, the process returns to step S301.
- the change of the injection ratio Rinj is continued until the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth.
- step 301: NO When the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth (step 301: NO), the ECU 100 returns the injection ratio Rinj to the standard injection ratio Rinjb ( In step S110, the process returns to step S301.
- the S adsorption suppression control is executed as described above.
- FIG. 11 is a diagram illustrating the relationship between the catalyst bed temperature Tcat and the S adsorption amount of the three-way catalyst 220 under a rich air-fuel ratio.
- FIG. 11 is a characteristic diagram when the air-fuel ratio is a rich air-fuel ratio.
- step S301 the catalyst bed temperature Tcat is acquired, and the catalyst bed temperature Tcat is calculated after the latest IG on timing in a control routine different from the S poison recovery control. Is estimated based on Specifically, a control map indicating the relationship between the accumulated fuel consumption and the catalyst bed temperature Tcat is stored in advance in the ROM, and the ECU 100 acquires a temperature value corresponding to the accumulated fuel consumption from the control map. As a result, the catalyst bed temperature Tcat is estimated. In addition, when a temperature sensor is arrange
- FIG. 12 is a flowchart of the S adsorption suppression control according to the fourth embodiment.
- the same reference numerals are given to the same portions as those in FIGS. 8 and 10, and the description thereof is omitted as appropriate.
- step S301 when the input side air-fuel ratio A / Fin is a rich air-fuel ratio and the catalyst bed temperature Tcat is lower than the reference value Tcatth (step S301: YES), in-cylinder injection is performed as in the second embodiment.
- the timing Tdfi is changed to the in-cylinder injection timing Tdfih2 for generating H2 (step S201).
- step S301 When the in-cylinder injection timing Tdfi is changed, the process returns to step S301.
- the change in the in-cylinder injection timing Tdfi is continued until the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth.
- step 301: NO When the input side air-fuel ratio A / Fin is not a rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth (step 301: NO), the ECU 100 returns the in-cylinder injection time Tdfi to the standard time Tdfib (step step (S202), the process returns to step S301.
- the S adsorption suppression control according to the fourth embodiment is executed as described above.
- the in-cylinder injection timing Tdfi is changed to the in-cylinder injection timing Tdfih2 for generating H2 in the same manner as the injection dividing ratio Rinj for changing the injection ratio Rinjh2 for generating H2 in the third embodiment.
- the amount of H2 generated in the cylinder is increased. If the amount of H2 generated increases, it is possible to prevent sulfur from being deposited on the three-way catalyst 220 itself. That is, the S poisoning of the catalyst can be actively recovered.
- the present invention is not limited to the above-described embodiment, and can be appropriately changed without departing from the gist or concept of the invention that can be read from the claims and the entire specification, and the control of the internal combustion engine accompanying such a change.
- the apparatus is also included in the technical scope of the present invention.
- the present invention can be applied to sulfur poisoning recovery control of a catalyst in an internal combustion engine.
- 10 engine system, 100 ... ECU, 200 ... engine, CB ... Cylinder block, 201 ... cylinder, 212 ... intake port injector, 219 ... exhaust pipe, 220 ... three-way catalyst, 221 ... air-fuel ratio sensor, 222 ... O 2 sensor .
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Description
本発明は、排気経路に設置された排気浄化用の触媒を硫黄被毒から回復させるにあたって好適な、内燃機関の制御装置の技術分野に関する。 The present invention relates to a technical field of a control device for an internal combustion engine suitable for recovering an exhaust purification catalyst installed in an exhaust path from sulfur poisoning.
排気経路に設置される排気浄化用の触媒は、燃料中に不純物として含有される硫黄が触媒に添加される貴金属に吸着して硫黄被毒する。硫黄被毒した状態では、触媒の活性が著しく失われ、触媒本来の排気浄化作用を得られないことから、従来、触媒から硫黄を脱離させるための各種の硫黄被毒回復制御が提案されている。尚、硫黄は、気筒内部又は排気経路で酸化してSOx(硫黄酸化物)として触媒に吸着することが多く、硫黄の脱離とは、端的には、硫黄の還元を意味する。 The exhaust purification catalyst installed in the exhaust path adsorbs sulfur contained as impurities in the fuel to the noble metal added to the catalyst and poisons the sulfur. In the state of sulfur poisoning, the activity of the catalyst is remarkably lost, and the original exhaust purification action of the catalyst cannot be obtained. Therefore, various sulfur poisoning recovery controls have been proposed for desorbing sulfur from the catalyst. Yes. In many cases, sulfur is oxidized inside the cylinder or in the exhaust path and is adsorbed to the catalyst as SOx (sulfur oxide), and the desorption of sulfur simply means reduction of sulfur.
例えば、特許文献1には、リーンNOx触媒における硫黄被毒回復制御が開示されている。特許文献1に開示された内燃機関の排気浄化装置は、リーンNOx触媒上流側にH2(水素)センサを配し、当該H2センサの出力値に基づいて、筒内のリッチ燃焼が制御される構成となっている。即ち、触媒流入ガスのH2濃度をリッチ燃焼の制御量にF/B制御する構成となっており、硫黄被毒回復時に適切な量の水素を供給可能であるとされている。 For example, Patent Document 1 discloses sulfur poisoning recovery control in a lean NOx catalyst. The exhaust gas purification apparatus for an internal combustion engine disclosed in Patent Document 1 includes an H 2 (hydrogen) sensor upstream of the lean NOx catalyst, and rich combustion in the cylinder is controlled based on the output value of the H 2 sensor. It is the composition which becomes. That is, it is configured that the H 2 concentration of the catalyst inflow gas is F / B controlled to a rich combustion control amount, and an appropriate amount of hydrogen can be supplied at the time of sulfur poisoning recovery.
また、特許文献2には、一部の気筒を空燃比リッチに、残余の気筒を空燃比リーンに制御することによって、触媒の昇温を図る技術も開示されている。 Further, Patent Document 2 discloses a technique for raising the temperature of the catalyst by controlling some cylinders to be rich in the air-fuel ratio and the remaining cylinders to be air-fuel ratio lean.
また、特許文献3には、NOx触媒の硫黄蓄積量が所定値を超えた場合に、触媒上流に搭載されたH2供給手段によりH2を供給する構成が開示されている。 Patent Document 3 discloses a configuration in which H 2 is supplied by an H 2 supply means mounted upstream of the catalyst when the amount of sulfur accumulated in the NOx catalyst exceeds a predetermined value.
また、特許文献4には、希薄燃焼エンジンの排気系に、CO2吸着材とH2生成触媒とNOx触媒とを配し、H2生成触媒にCOを供給し、水生ガスシフト反応により生成されたH2を還元剤としてNOx触媒に送り込む構成が開示されている。 Further, in Patent Document 4, a CO 2 adsorbent, an H 2 generation catalyst, and a NOx catalyst are arranged in an exhaust system of a lean combustion engine, and CO is supplied to the H 2 generation catalyst, which is generated by an aquatic gas shift reaction. A configuration in which H 2 is sent as a reducing agent to the NOx catalyst is disclosed.
また、特許文献5には、リーンNOx触媒システムであって、筒内燃焼を制御可能な内燃機関において、NOx触媒再生時は、ポスト噴射時期を脱水素反応とクラッキング反応とが反発するタイミングで実施する構成が開示されている。 Further, Patent Document 5 discloses a lean NOx catalyst system, and in an internal combustion engine capable of controlling in-cylinder combustion, when NOx catalyst is regenerated, post-injection timing is performed at a timing when the dehydrogenation reaction and cracking reaction repel each other. The structure to perform is disclosed.
上述したように硫黄(S)の脱離には多様なアプローチが存在する。中でも、還元能力が極めて高い水素(H2)による硫黄の還元は、触媒を昇温させて還元反応の促進を図る二次的なプロセスを必ずとも必要としない点において、極めて有効である。 As described above, there are various approaches to sulfur (S) desorption. Among them, the reduction of sulfur with hydrogen (H2) having a very high reducing ability is extremely effective in that it does not necessarily require a secondary process in which the catalyst is heated to promote the reduction reaction.
しかしながら、硫黄被毒回復のために、例えば水素添加弁等の水素供給手段を排気経路に別途付加する構成とすることは、製造コストの面からすると望ましくない。 However, in order to recover sulfur poisoning, it is not desirable from the viewpoint of manufacturing cost to add a hydrogen supply means such as a hydrogen addition valve to the exhaust path separately.
また、改質触媒等により触媒で水素を生成する構成としても、触媒における改質反応に、実使用に耐え得る可制御性を与えることは一般的に難しい。それに加えて、改質反応による水素の生成量にも限界があり、必ずしもその時点で必要とされる量を供給し得る保証はない。これは、硫黄の還元を促進する目的から、何らかの手法(例えば、気筒間で空燃比インバランスを生じさせる等の手法)により触媒床温を上昇させたとしても根本的に変わらない。 In addition, even in a configuration in which hydrogen is generated by a catalyst using a reforming catalyst or the like, it is generally difficult to give controllability that can withstand actual use for the reforming reaction in the catalyst. In addition, the amount of hydrogen produced by the reforming reaction is limited, and there is no guarantee that the amount required at that time can be supplied. Even if the catalyst bed temperature is raised by some method (for example, a method of generating an air-fuel ratio imbalance between cylinders) for the purpose of promoting the reduction of sulfur, this does not change fundamentally.
一方、上述したように、リッチ燃焼により、ある程度の可制御性を伴って水素を生成する構成において、触媒上流側に水素濃度センサを配し、水素を必要量だけ触媒に供給する技術思想は、一見有用である。 On the other hand, as described above, in a configuration in which hydrogen is generated with a certain degree of controllability by rich combustion, a technical idea of providing a hydrogen concentration sensor upstream of the catalyst and supplying only a necessary amount of hydrogen to the catalyst is as follows: At first glance it is useful.
しかしながら、実践的見地に立つと、現実的制約に律束された車両搭載を前提とした場合において、この種の用途に十分な性能を発揮し得る水素センサは存在しない。 However, from a practical standpoint, there is no hydrogen sensor that can exhibit sufficient performance for this type of application when it is assumed that the vehicle is mounted with realistic constraints.
また、空燃比リッチ側での燃焼(リッチ燃焼)は、硫黄やNOxの還元は別として、排気エミッションの観点からは不利な制御であり、また燃費の悪化を招く点において経済的にも不利な制御である。従って、硫黄の還元のみを目的として、リッチ燃焼を闇雲に安全側(この場合、即ち、水素の生成量が多くなる側)で行うことは合理的でない。 In addition, combustion on the rich side of the air-fuel ratio (rich combustion) is a disadvantageous control from the viewpoint of exhaust emission, apart from the reduction of sulfur and NOx, and is also economically disadvantageous in that it leads to a deterioration in fuel consumption. Control. Therefore, it is not reasonable to perform rich combustion in the dark cloud on the safe side (in this case, that is, on the side where the amount of hydrogen generated increases) for the purpose of reducing only sulfur.
このように、従来、触媒を硫黄被毒から回復させるための多様な構成又は制御が提案されてはいても、各々一長一短であり、排気エミッション、燃費及びコスト等を含む多様な要求を満たしつつ触媒を硫黄被毒から回復させる制御は、実は未だに存在しない。 Thus, even though various configurations or controls for recovering the catalyst from sulfur poisoning have been proposed in the past, each has its advantages and disadvantages, while satisfying various requirements including exhaust emission, fuel consumption, cost, etc. There is actually no control to recover from sulfur poisoning.
本発明は、上述した事情に鑑みてなされたものであり、コストの増加並びに排気エミッション及び燃費の悪化を抑制しつつ触媒を硫黄被毒から回復させることが可能な内燃機関の制御装置を提供することを課題とする。 The present invention has been made in view of the above-described circumstances, and provides an internal combustion engine control device capable of recovering a catalyst from sulfur poisoning while suppressing an increase in cost and deterioration of exhaust emission and fuel consumption. This is the issue.
上述した課題を解決するため、本発明に係る内燃機関の制御装置は、気筒と、前記気筒に繋がる排気経路に設置された排気浄化用の触媒と、前記気筒に対する燃料の筒内噴射が可能な筒内噴射装置とを備えた内燃機関を制御する、内燃機関の制御装置であって、前記触媒に堆積する硫黄を減少させる場合において、前記気筒の内部における混合気の均質度が低下するように前記筒内噴射装置の噴射態様を変更する変更手段と、前記変更された噴射態様に従って前記筒内噴射装置を制御する第1制御手段とを具備することを特徴とする(第1項)。 In order to solve the problems described above, an internal combustion engine control apparatus according to the present invention is capable of in-cylinder injection of a cylinder, an exhaust purification catalyst installed in an exhaust path connected to the cylinder, and fuel into the cylinder. A control device for an internal combustion engine that controls an internal combustion engine including an in-cylinder injection device, and in the case where sulfur accumulated in the catalyst is reduced, the homogeneity of the air-fuel mixture in the inside of the cylinder is reduced. A change means for changing the injection mode of the in-cylinder injection device and a first control means for controlling the in-cylinder injection device according to the changed injection mode (first item).
本発明に係る内燃機関は、燃料を含む混合気が燃焼する際に生じる熱エネルギを運動エネルギに変換して取り出し可能な機関を包括する概念であって、特に、その排気経路に排気浄化用の触媒を備え、また燃料の噴射装置として少なくとも筒内噴射装置を備える。係る概念の範囲において、本発明に係る内燃機関における、気筒数、気筒配列、燃料種別、燃料の噴射態様、吸排気系の構成、動弁系の構成、燃焼方式、過給器の有無及び過給態様等は如何様にも限定されない趣旨である。 The internal combustion engine according to the present invention is a concept that encompasses an engine that can convert thermal energy generated when an air-fuel mixture containing fuel is burned into kinetic energy and take it out. A catalyst is provided, and at least an in-cylinder injection device is provided as a fuel injection device. Within the scope of the concept, in the internal combustion engine according to the present invention, the number of cylinders, the cylinder arrangement, the fuel type, the fuel injection mode, the intake / exhaust system configuration, the valve train configuration, the combustion system, the presence / absence of the supercharger, and the excess The manner of supply is not limited in any way.
本発明に係る排気浄化用の触媒とは、内燃機関の排気経路に備わり得る各種の触媒を包括する概念であり、好適な一例として、例えば、三元触媒、リーンNOx触媒(NOx吸蔵還元触媒とも称される)、酸化触媒等の実践的形態を採る。 The exhaust purification catalyst according to the present invention is a concept encompassing various types of catalysts that can be provided in the exhaust path of an internal combustion engine. As a suitable example, for example, a three-way catalyst, a lean NOx catalyst (also referred to as a NOx storage reduction catalyst). Practical forms such as oxidation catalyst.
触媒は、内燃機関の実稼動期間に応じて、燃料中に不純物として含有される硫黄により被毒する。触媒の硫黄被毒は触媒活性を低下させるから、然るべきタイミングで触媒から硫黄を脱離する(即ち、触媒を硫黄被毒から回復させる)必要がある。尚、「然るべきタイミング」とは、必ずしもそのようなタイミングを規定する条件が事前に決定されていることを意味しない。実践的には、硫黄被毒の度合いが所定レベルを超えたとみなされ得るタイミングでこの種の回復措置を講じることは有効であるが、硫黄被毒の回復措置、或いは硫黄被毒の抑制措置は、硫黄被毒のレベルに拠らず有効である。 The catalyst is poisoned by sulfur contained as an impurity in the fuel according to the actual operation period of the internal combustion engine. Since sulfur poisoning of the catalyst reduces the catalytic activity, it is necessary to desorb sulfur from the catalyst at the appropriate timing (that is, to recover the catalyst from sulfur poisoning). It should be noted that “appropriate timing” does not necessarily mean that a condition that defines such timing is determined in advance. In practice, it is effective to take this kind of recovery measure at a timing when the degree of sulfur poisoning can be considered to have exceeded the prescribed level, but there is no recovery measure for sulfur poisoning or measures to suppress sulfur poisoning. It is effective regardless of the level of sulfur poisoning.
硫黄被毒した触媒から硫黄(或いは硫黄酸化物)を脱離させるにあたって、水素はその極めて高い還元能力から有効であることが知られている。本発明に係る内燃機関の制御装置は、筒内噴射装置の噴射態様を変更することにより、気筒における水素の生成を促進し、もって触媒の硫黄被毒からの回復、或いは、触媒への硫黄の吸着阻止を図る構成となっている。 In desorbing sulfur (or sulfur oxides) from a sulfur poisoned catalyst, hydrogen is known to be effective due to its extremely high reducing ability. The control device for an internal combustion engine according to the present invention promotes the generation of hydrogen in the cylinder by changing the injection mode of the in-cylinder injection device, so that recovery from sulfur poisoning of the catalyst, or sulfur of the catalyst It is configured to prevent adsorption.
即ち、本発明に係る内燃機関の制御装置によれば、触媒に堆積する硫黄を減少させる場合(堆積した硫黄を脱離する場合も、吸着を防止する場合も含まれる)において、筒内噴射装置の噴射態様が、気筒内部に形成される混合気の均質度が低下するように変更される。第1制御手段は、この変更された噴射態様に従って筒内噴射装置を制御する。 That is, according to the control apparatus for an internal combustion engine according to the present invention, in the case of reducing the sulfur accumulated on the catalyst (including the case where the accumulated sulfur is desorbed and the adsorption is prevented), the in-cylinder injection device Is changed so that the homogeneity of the air-fuel mixture formed inside the cylinder is lowered. The first control means controls the in-cylinder injection device according to the changed injection mode.
ここで、「噴射態様」とは、例えば、噴射回数、噴射時期又は噴射期間等を指し、混合気の均質度を変化させ得る制御量を指す。また、後述するように内燃機関が筒内噴射装置に加えて更にポート噴射装置を備えるのであれば、筒内噴射量とポート噴射量との噴き分け比率を好適に含み得る。 Here, the “injection mode” refers to, for example, the number of injections, the injection timing, the injection period, or the like, and a control amount that can change the homogeneity of the air-fuel mixture. In addition, as will be described later, if the internal combustion engine further includes a port injection device in addition to the in-cylinder injection device, it can suitably include an injection ratio between the in-cylinder injection amount and the port injection amount.
筒内噴射装置は、気筒内部に直接燃料を噴射するため、例えば吸気ポートに燃料を噴射するポート噴射装置と較べると、ポート付着等による燃料損失が生じない反面、燃料と吸入ガスとの、より長い予混合期間を必要とする。例えば、筒内噴射装置における燃料の噴射時期は、条件にもよるが、好適な一形態として吸気上死点と下死点との間に設定される。即ち、圧縮行程の開始以前に燃料噴射を行うことによって、圧縮行程での燃料と筒内吸入ガスとの十分な予混合を図るのである。 The in-cylinder injection device directly injects fuel into the cylinder, and therefore, compared with a port injection device that injects fuel into the intake port, for example, fuel loss due to port adhesion or the like does not occur, but more fuel and intake gas. Requires a long premixing period. For example, the fuel injection timing in the in-cylinder injection device is set between the intake top dead center and the bottom dead center as a preferred embodiment, although it depends on conditions. That is, by performing fuel injection before the start of the compression stroke, sufficient premixing of the fuel and the cylinder intake gas in the compression stroke is achieved.
従って、逆に言えば、この噴射時期を遅角側に制御すれば、混合気の均質度(明確な定量的指標として検出される必要はない)を低下させることもまた可能となる。即ち、噴射時期は、本発明に係る「噴射態様」の好適な一例となり得る。 Therefore, conversely, if the injection timing is controlled to the retard side, the homogeneity of the air-fuel mixture (which need not be detected as a clear quantitative index) can also be reduced. That is, the injection timing can be a suitable example of the “injection mode” according to the present invention.
ここで、気筒における水素生成(全てが気筒で生じる必要はなく、気筒から排出された後に排気経路で生成されるものを含み得る)は、主として、水性ガスシフト反応(CO+H2O→H2+CO2)及び水蒸気改質反応(HC+H2O→H2+CO)による。即ち、気筒内部でCO或いはHC等の未燃物或いは不燃物の生成を促進することによって、気筒、或いは排気経路での水素の生成を促進することが出来る。従って、筒内噴射の態様を、混合気の均質度を低下させる方向に変更することによって、気筒、或いは排気経路において水素の生成を好適に促進することが出来るのである。 Here, hydrogen generation in the cylinder (not all need to occur in the cylinder, and may include what is generated in the exhaust path after being discharged from the cylinder) is mainly a water gas shift reaction (CO + H 2 O → H 2 + CO 2 ) And steam reforming reaction (HC + H 2 O → H 2 + CO). That is, by promoting the generation of unburned or incombustible substances such as CO or HC inside the cylinder, the generation of hydrogen in the cylinder or the exhaust path can be promoted. Therefore, by changing the mode of in-cylinder injection so as to reduce the homogeneity of the air-fuel mixture, the generation of hydrogen can be favorably promoted in the cylinder or the exhaust path.
ここで特に、このような噴射態様の変更は、例えば公知の各種空燃比F/B制御等により理論空燃比或いは目標空燃比に維持すべく決定される気筒毎の燃料噴射量の変更を必要としない。従って、排気経路及び触媒の空燃比は、このような噴射態様の変更に大きく影響されることはない。 Here, in particular, such a change in the injection mode requires a change in the fuel injection amount for each cylinder determined to maintain the theoretical air fuel ratio or the target air fuel ratio by, for example, various known air fuel ratio F / B controls. do not do. Therefore, the exhaust path and the air-fuel ratio of the catalyst are not greatly affected by such a change in the injection mode.
即ち、本発明に係る内燃機関の制御装置によれば、コストの増加並びに排気エミッション及び燃費の悪化を招くことなく触媒を硫黄被毒から回復させる、或いは、触媒への硫黄の堆積を抑制することが出来るのである。 That is, according to the control device for an internal combustion engine according to the present invention, the catalyst is recovered from sulfur poisoning without increasing the cost and exhaust emission and fuel consumption are deteriorated, or the accumulation of sulfur on the catalyst is suppressed. Is possible.
本発明に係る内燃機関の制御装置の一の態様では、前記変更手段は、前記噴射態様として、前記燃料の噴射時期を標準時期に対して遅角側に変更する(第2項)。 In one aspect of the control apparatus for an internal combustion engine according to the present invention, the changing means changes the fuel injection timing to the retard side with respect to the standard time as the injection mode (second term).
この態様によれば、噴射時期を標準時期に対して遅角側に変更することによって、混合気の均質度を低下させ、気筒内部、排気経路或いは触媒での水素生成を好適に促進することが出来る。 According to this aspect, by changing the injection timing to the retard side with respect to the standard timing, the homogeneity of the air-fuel mixture can be reduced, and hydrogen generation inside the cylinder, the exhaust path or the catalyst can be favorably promoted. I can do it.
尚、「標準時期」とは、このような硫黄被毒の回復又は抑制を目的とした措置を必要としない場合の同一条件における噴射時期を意味する。尚、標準時期が、内燃機関の燃費を最適値とすべく決定されている場合、噴射時期の遅角は、即ち燃費の悪化を招き得るが、従来のように空燃比をリッチ化することにより水素を生成する技術思想と較べると、消費燃料量に歴然たる差が生ずるところ、その影響は極めて小さくて済む。そのような意味においては、燃費の悪化は十分に抑制されると言える。 The “standard time” means the injection time under the same conditions when measures for recovery or suppression of such sulfur poisoning are not required. If the standard timing is determined so as to optimize the fuel consumption of the internal combustion engine, the retard of the injection timing, that is, the deterioration of the fuel consumption can be caused. Compared with the technical idea of generating hydrogen, the difference in the amount of fuel consumption occurs, but the effect is very small. In that sense, it can be said that deterioration of fuel consumption is sufficiently suppressed.
本発明に係る内燃機関の制御装置の他の態様では、前記内燃機関は、前記気筒に対する燃料のポート噴射が可能なポート噴射装置を具備し、前記変更手段は、前記噴射態様として、前記ポート噴射の燃料噴射量と前記筒内噴射の燃料噴射量と比率である噴き分け比率を、前記筒内噴射の燃料噴射量が多くなるように変更し、前記制御手段は、前記変更された噴き分け比率に従って前記筒内噴射装置及び前記ポート噴射装置を制御する(第3項)。 In another aspect of the control apparatus for an internal combustion engine according to the present invention, the internal combustion engine includes a port injection device capable of performing a port injection of fuel to the cylinder, and the changing means includes the port injection as the injection mode. The fuel injection amount and the fuel injection amount and ratio of the in-cylinder injection are changed so that the fuel injection amount of the in-cylinder injection increases, and the control means changes the changed injection ratio. The in-cylinder injection device and the port injection device are controlled according to (3rd item).
燃料噴射装置としてポート噴射装置を備えた構成においては、筒内噴射よりもポート噴射の方が混合気の均質度を良好に維持し得る点から、例えば、冷間始動時等においてポート噴射を利用すること等により、冷間始動性を向上させ得ることが知られている。 In the configuration provided with the port injection device as the fuel injection device, the port injection can maintain the homogeneity of the air-fuel mixture better than the in-cylinder injection. It is known that the cold startability can be improved by doing so.
ここで、このように筒内噴射とポート噴射との間で燃料と吸入ガスとの混合性が異なり得る点からすると、ある要求噴射量に対する筒内噴射量とポート噴射量との比率、即ち、噴き分け比率は、均質度に可制御性を与える好適な制御量となり得る。 Here, from the point that the mixability of the fuel and the intake gas can be different between the in-cylinder injection and the port injection, the ratio of the in-cylinder injection amount to the port injection amount with respect to a certain required injection amount, that is, The spray ratio can be a suitable control amount that gives controllability to the homogeneity.
この態様によれば、筒内噴射装置の噴射態様として、係る噴き分け比率が制御される。より具体的には、標準値(例えば、S被毒回復を考慮しない場合の同一条件における筒内噴射量)よりも筒内噴射量が多くなるように噴き分け比率が変更される。従って、気筒、或いは排気経路での水素の生成が好適に促進され得る。 According to this aspect, the injection ratio is controlled as an injection aspect of the in-cylinder injection device. More specifically, the injection ratio is changed so that the in-cylinder injection amount is larger than a standard value (for example, the in-cylinder injection amount under the same condition when S poison recovery is not considered). Accordingly, the generation of hydrogen in the cylinder or the exhaust path can be favorably promoted.
本発明に係る内燃機関の制御装置の他の態様では、前記触媒における硫黄の堆積量を推定する第1推定手段と、前記推定された堆積量から前記触媒を前記硫黄被毒から回復させるための水素の要求量又は要求濃度を推定する第2推定手段とを具備し、前記変更手段は、前記推定された要求量又は要求濃度に応じて前記噴射態様を変更する(第4項)。 In another aspect of the control apparatus for an internal combustion engine according to the present invention, first estimation means for estimating the amount of sulfur accumulated in the catalyst, and for recovering the catalyst from the sulfur poisoning from the estimated amount of accumulation. Second estimating means for estimating a required amount or required concentration of hydrogen, and the changing means changes the injection mode in accordance with the estimated required amount or required concentration (fourth term).
この態様によれば、第1推定手段により触媒における硫黄の堆積量が推定される。尚、「堆積量」とは、厳密には堆積した量を意味するが、触媒に対する硫黄の被毒プロセス(触媒に応じて必ずしも一義的でない)に応じて、例えば、付着量、吸着量及び被毒量と置き替えてもよい。 According to this aspect, the amount of sulfur deposition on the catalyst is estimated by the first estimating means. Strictly speaking, the “deposition amount” means an accumulation amount. However, depending on the poisoning process of sulfur to the catalyst (which is not necessarily unambiguous depending on the catalyst), for example, the adhesion amount, the adsorption amount, and the deposition amount. You may replace it with a poisonous amount.
触媒における硫黄の堆積量を推定するにあたっては、公知の各種方法を適用可能である。例えば、堆積量は、機関回転数、吸気圧、アクセル開度、吸入空気量、スロットル開度、負荷率及び燃料噴射量の少なくとも一部を含み得る内燃機関の運転パラメータと、予め実験的に、経験的に又は理論的に構築された、当該運転パラメータ及び硫黄生成量の相互関係とに基づいて推定されてもよい。この際、内燃機関の排気経路に単位時間当たりに排出される硫黄又は硫黄酸化物(SOx)の量が積算され、この積算値から堆積量が推定されてもよい。また、この積算値と実際の堆積量との関係(即ち、気筒から排出される硫黄又は硫黄酸化物の全てが触媒に堆積する訳ではない)が明らかである場合には、当該関係が更に参照されてもよい。 In estimating the amount of sulfur deposited on the catalyst, various known methods can be applied. For example, the accumulation amount is determined in advance experimentally with internal combustion engine operating parameters that may include at least part of the engine speed, intake pressure, accelerator opening, intake air amount, throttle opening, load factor, and fuel injection amount. It may be estimated based on the correlation between the operating parameter and the amount of sulfur production, which is established empirically or theoretically. At this time, the amount of sulfur or sulfur oxide (SOx) discharged per unit time in the exhaust path of the internal combustion engine may be integrated, and the accumulation amount may be estimated from this integrated value. In addition, when the relationship between the integrated value and the actual accumulation amount (that is, not all of the sulfur or sulfur oxide discharged from the cylinder is deposited on the catalyst) is clear, the relationship is further referred to. May be.
一方、第2推定手段は、第1推定手段により推定される堆積量から、触媒を硫黄被毒から回復させる(触媒への硫黄の吸着を抑制させることによって硫黄被毒を抑制する概念を含む)ための水素の要求量又は要求濃度を推定する。尚、このような要求量又は要求濃度は、触媒の硫黄被毒を幾らかなり回復させる効能を有する限りにおいて、必ずしも触媒に堆積した硫黄の全てを脱離させ得る量でなくてもよい。但し、推定された堆積量に相当する硫黄を全て除去するために必要な水素量を理論的に求めることは可能であり、また、噴射態様の変更により生じさせた水素のうち実際に触媒での硫黄脱離に供され得る水素の割合等を補正係数として実験的に求めることも出来る。 On the other hand, the second estimating means recovers the catalyst from sulfur poisoning from the amount of accumulation estimated by the first estimating means (including the concept of suppressing sulfur poisoning by suppressing the adsorption of sulfur to the catalyst). Estimate the required amount or concentration of hydrogen for It should be noted that such a required amount or required concentration does not necessarily have to be an amount capable of desorbing all of the sulfur deposited on the catalyst as long as it has an effect of considerably recovering the sulfur poisoning of the catalyst. However, it is possible to theoretically determine the amount of hydrogen required to remove all the sulfur corresponding to the estimated deposition amount, and among the hydrogen generated by changing the injection mode, The proportion of hydrogen that can be used for sulfur desorption can also be experimentally determined as a correction coefficient.
この態様によれば、噴射態様の変更を要する期間に一定の指針を与えることが出来、噴射態様の変更により生成される水素が不足する或いは過剰になる等といった懸念を緩和することが出来る。 According to this aspect, it is possible to give a certain guideline during a period that requires the change of the injection mode, and to alleviate the concern that the hydrogen generated by the change of the injection mode is insufficient or excessive.
尚、このように第1及び第2推定手段を備えた態様においては、前記気筒における水素の生成量を推定する第3推定手段を更に具備し、前記変更手段は、前記推定された要求量又は要求濃度と前記推定された生成量とに基づいて前記噴射態様を変更する期間を決定してもよい(第5項)。 In the aspect provided with the first and second estimation means as described above, the apparatus further comprises third estimation means for estimating the amount of hydrogen generated in the cylinder, and the changing means includes the estimated required amount or A period for changing the injection mode may be determined based on the required concentration and the estimated generation amount (Section 5).
このように噴射態様の変更による水素の生成量が推定される構成とすれば、第2推定手段により推定された要求量又は要求濃度に応じた適切な量の水素を生成することが出来る。従って、触媒の硫黄被毒を、或いは触媒への硫黄の吸着を効率的に防止することが出来る。 If the configuration is such that the amount of hydrogen produced by changing the injection mode is estimated in this way, it is possible to generate an appropriate amount of hydrogen according to the required amount or the required concentration estimated by the second estimating means. Therefore, sulfur poisoning of the catalyst or adsorption of sulfur to the catalyst can be efficiently prevented.
尚、第3推定手段による水素の生成量の推定は、好適には、予め実験的に、経験的に又は理論的に、変更手段により変更される噴射態様毎に、噴射態様の変更量と水素の生成量又は濃度とを対応付けておくことにより好適に実現され得る。端的には、このような関係を参照可能な制御マップとして保持しておけば、第3推定手段は、比較的に簡便に生成量を推定することが出来る。 The estimation of the hydrogen generation amount by the third estimation means is preferably performed in advance experimentally, empirically, or theoretically for each injection mode changed by the changing unit. This can be suitably realized by associating the generation amount or the concentration of. In short, if such a relationship is held as a control map that can be referred to, the third estimation means can estimate the generation amount relatively easily.
尚、第3推定手段を備えた態様では、前記内燃機関の冷却水温を特定する冷却水温特定手段を具備し、前記第3推定手段は、前記特定された冷却水温に応じて前記推定される生成量を補正してもよい(第6項)。 In the aspect including the third estimating means, the cooling water temperature specifying means for specifying the cooling water temperature of the internal combustion engine is provided, and the third estimating means generates the estimated generation according to the specified cooling water temperature. The amount may be corrected (Section 6).
一の噴射態様の変更条件において気筒で生成される水素は、内燃機関の機関暖機状態により変化する。端的には、冷間始動時等、機関暖機が不十分である程、気筒の燃焼状態は悪化する。即ち、混合気の均一度が一定であっても、機関が相対的冷却状態にある分だけ、水素の生成量は増加傾向となる。 水 素 Hydrogen generated in the cylinder under one injection mode change condition varies depending on the engine warm-up state of the internal combustion engine. In short, the combustion state of the cylinder worsens as engine warm-up becomes insufficient, such as during cold start. That is, even if the uniformity of the air-fuel mixture is constant, the amount of hydrogen produced tends to increase by the amount that the engine is in a relatively cooled state.
従って、冷却水温特定手段により特定される冷却水温に応じて、第3推定手段が推定する水素の生成量を補正することによって、より正確に水素の生成量を推定することが可能となる。 Therefore, by correcting the hydrogen generation amount estimated by the third estimation means in accordance with the cooling water temperature specified by the cooling water temperature specifying means, it becomes possible to estimate the hydrogen generation amount more accurately.
尚、本発明に係る「特定」とは、センサ等の検出手段による検出等に加え、この種の検出手段からのセンサ値の取得や内燃機関の運転条件等に基づいた推定等を含む包括的概念である。 The “specific” according to the present invention is comprehensive including not only detection by a detection unit such as a sensor but also acquisition of a sensor value from this type of detection unit or estimation based on an operating condition of the internal combustion engine. It is a concept.
本発明に係る内燃機関の制御装置の他の態様では、前記触媒の温度を特定する触媒温度特定手段と、前記排気経路における空燃比を特定する空燃比特定手段とを具備し、前記変更手段は、前記特定された空燃比が理論空燃比に対して所定値以上リッチ側にあり且つ前記特定された触媒の温度が所定値未満である場合において、前記気筒の内部における均質度が低下するように前記筒内噴射装置の噴射態様を変更する(第7項)。 In another aspect of the control apparatus for an internal combustion engine according to the present invention, the control apparatus includes catalyst temperature specifying means for specifying the temperature of the catalyst, and air-fuel ratio specifying means for specifying an air-fuel ratio in the exhaust path, wherein the changing means includes When the specified air-fuel ratio is richer than the stoichiometric air-fuel ratio by a predetermined value or more and the temperature of the specified catalyst is lower than the predetermined value, the homogeneity inside the cylinder is reduced. The injection mode of the in-cylinder injection device is changed (Seventh Item).
この態様によれば、触媒温度特定手段により触媒の温度(端的には触媒床温)が特定される。また、空燃比特定手段により排気経路における空燃比が特定される。 According to this aspect, the catalyst temperature (in short, the catalyst bed temperature) is specified by the catalyst temperature specifying means. The air-fuel ratio in the exhaust path is specified by the air-fuel ratio specifying means.
内燃機関の空燃比は、例えば上述したように空燃比F/B制御により理論空燃比又はその近傍の目標空燃比にF/B制御されることが多いが、例えば、動力性能が要求される、触媒の昇温を促進する或いは更に他の理由から、リッチ空燃比に制御されることも多い。 The air-fuel ratio of the internal combustion engine is often F / B controlled to the theoretical air-fuel ratio or a target air-fuel ratio in the vicinity thereof by air-fuel ratio F / B control as described above, for example, power performance is required. In many cases, the air-fuel ratio is controlled to be rich for promoting the temperature rise of the catalyst or for other reasons.
一方で、リッチ空燃比下において触媒床温が所定値(例えば、概ね500~600℃付近)未満となる温度領域では、触媒への硫黄の吸着量が高くなる。触媒の硫黄被毒を能動的に回避する観点からは、このような条件下において、積極的に水素を生成するのが効果的である。 On the other hand, in a temperature range where the catalyst bed temperature is lower than a predetermined value (for example, approximately around 500 to 600 ° C.) under a rich air-fuel ratio, the amount of sulfur adsorbed on the catalyst becomes high. From the viewpoint of actively avoiding sulfur poisoning of the catalyst, it is effective to actively generate hydrogen under such conditions.
この態様によれば、空燃比が所定以上リッチであり且つ触媒床温が所定値未満である場合において、気筒の内部における均質度が低下するように変更手段が筒内噴射装置の噴射態様を変更する構成となっている。言い換えれば、このような条件が、本発明に係る「触媒に堆積する硫黄を減少させる場合」の一例として採用される。 According to this aspect, when the air-fuel ratio is richer than the predetermined value and the catalyst bed temperature is lower than the predetermined value, the changing means changes the injection mode of the in-cylinder injection device so that the homogeneity inside the cylinder is lowered. It is the composition to do. In other words, such a condition is adopted as an example of “when reducing sulfur deposited on the catalyst” according to the present invention.
従って、触媒への硫黄の吸着を能動的に回避し、触媒の硫黄被毒を防ぐ、或いはその進行を遅滞させることが可能となる。 Therefore, it is possible to actively avoid sulfur adsorption on the catalyst, prevent sulfur poisoning of the catalyst, or delay its progress.
本発明のこのような作用及び他の利得は次に説明する実施形態から明らかにされる。 Such an operation and other advantages of the present invention will be clarified from embodiments described below.
<発明の実施形態>
以下、図面を参照して、本発明の各種実施形態について説明する。
<Embodiment of the Invention>
Hereinafter, various embodiments of the present invention will be described with reference to the drawings.
<第1実施形態>
<実施形態の構成>
始めに、図1を参照し、本発明の一実施形態に係るエンジンシステム10の構成について説明する。ここに、図1は、エンジンシステム10の構成を概念的に表してなる概略構成図である。
<First Embodiment>
<Configuration of Embodiment>
First, the configuration of an
図1において、エンジンシステム10は、図示せぬ車両に搭載され、ECU100及びエンジン200を備える。
1, an
ECU100は、CPU、ROM及びRAM等を備え、エンジンシステム10の動作を制御可能に構成された電子制御ユニットであり、本発明に係る「内燃機関の制御装置」の一例である。ECU100は、ROMに格納された制御プログラムに従って、後述するS被毒回復制御を実行可能に構成されている。
The
尚、ECU100は、本発明に係る「変更手段」、「第1制御手段」、「第1推定手段」、「第2推定手段」、「第3推定手段」、「特定手段」の夫々一例として機能し得る一体の電子制御ユニットであるが、本発明に係るこれら各手段の物理的、機械的及び電気的な構成はこれに限定されるものではなく、これら各手段は、例えば複数のECU、各種処理ユニット、各種コントローラ或いはマイコン装置等各種コンピュータシステム等として構成されていてもよい。
The
エンジン200は、本発明に係る「内燃機関」の一例たる直列4気筒ガソリンエンジンである。
図1において、エンジン200は、シリンダブロックCBに収容される複数の気筒201を備える。尚、図1において、気筒201は紙面奥行き方向に配列しており、図1においては一の気筒201のみが示されている。
1, the
エンジン200において、気筒201の内部に形成された燃焼室には、混合気の燃焼に伴う爆発力に応じて図示上下方向に往復運動を生じるピストン202を備える。ピストン202の往復運動は、コネクティングロッド203を介してクランクシャフト204の回転運動に変換され、エンジン200を搭載する車両の動力として利用される構成となっている。
In the
クランクシャフト204の近傍には、クランクシャフト204の回転位置(即ち、クランク角)を検出可能なクランクポジションセンサ205が設置されている。このクランクポジションセンサ205は、ECU100と電気的に接続されており、検出されたクランク角は、一定又は不定の周期でECU100に参照され、例えば、エンジン回転数NEの算出や、その他の制御に供される構成となっている。
In the vicinity of the
エンジン200において、外部から吸入された空気は、図示せぬクリーナにより浄化された後、各気筒について共通の吸気管206に導かれる。吸気管206には、この吸入空気の量である吸入空気量を調節可能なスロットルバルブ207が配設されている。このスロットルバルブ207は、ECU100と電気的に接続された不図示のスロットルバルブモータによってその駆動状態が制御される、一種の電子制御式スロットルバルブとして構成されている。
In the
ECU100は、基本的には不図示のアクセルポジションセンサにより検出されるアクセル開度Taに応じたスロットル開度が得られるようにスロットルバルブモータを駆動制御する。但し、ECU100は、スロットルバルブモータの動作制御を介してドライバの意思を介在させることなくスロットル開度を調整することも可能である。
The
スロットルバルブ207により適宜調量された吸入空気は、気筒201の各々に対応する吸気ポート208を経由して、吸気弁209の開弁時に気筒内部に吸入される。吸気弁209は、図示するように断面視略楕円形状を有するカム210のカムプロファイルに応じてその開閉時期が規定される構成となっている。
The intake air appropriately adjusted by the
一方、このカム210は、例えばカムスプロケットやタイミングチェーン等の動力伝達手段を介してクランクシャフト204に連結された吸気カム軸(符号省略)に固定されている。従って、吸気弁209の開閉位相は、クランクシャフト204の回転位相(即ち、クランク角)と、一の固定状態において一義的な関係にある。
On the other hand, the
ここで、この吸気カム210と吸気カム軸との固定状態は、油圧駆動装置211により供給される制御油の油圧により変化する。より具体的には、吸気カム210は、ベーンと呼ばれる翼状部材を介して吸気カム軸に連結されており、このベーンと吸気カム軸との回転位相は、油圧駆動装置211が有する油圧室に印加される油圧に応じて変化する構成となっている。従って、ベーンに固定された吸気カム210と吸気カム軸との回転位相もまた、当該油圧に応じて変化する。油圧駆動装置211は、ECU100と電気的に接続された状態にあり、ECU100は、油圧駆動装置211の制御を介して、吸気弁209の開閉時期を変化させることが出来る。
Here, the fixed state between the
尚、可変動弁装置の採り得る形態は、本実施形態のものに限定されない。例えば、吸気弁209は、ソレノイドアクチュエータ等により電磁的に駆動される、所謂電磁駆動弁(カム・バイワイヤ)であってもよい。
In addition, the form which a variable valve apparatus can take is not limited to the thing of this embodiment. For example, the
尚、吸気管206には、吸入空気量Gaを検出可能なエアフローメータ212が配設されている。エアフローメータ212は、ECU100と電気的に接続されており、検出された吸入空気量Gaは、ECU100により一定又は不定の周期で参照される構成となっている。
The
吸気ポート208に導かれた吸入空気は、吸気ポート208に噴射弁の一部が露出してなるPFI(Port Fuel Injector:吸気ポート噴射装置)342から噴射されたポート噴射燃料と混合されて前述の混合気となる。尚、PFI342は、後に図3を参照して説明する燃料供給装置300を構成する一要素である。
The intake air guided to the
エンジン200の燃焼室には火花点火装置である点火装置213の点火プラグ(符号省略)の一部が露出している。エンジン200の圧縮行程において圧縮された混合気は、この点火プラグの点火動作により着火し燃焼する仕組みとなっている。点火装置213は、ECU100と電気的に接続されており、点火装置213の点火時期は、ECU100により制御される構成となっている。
In the combustion chamber of the
一方、燃焼室において燃焼反応を生じた混合気は、燃焼行程に引き続く排気行程において、クランクシャフト204と間接的に連結された排気カム214のカムプロファイルにより開閉駆動される排気弁215の開弁時に、排気ポート216に排出される。
On the other hand, the air-fuel mixture that has undergone a combustion reaction in the combustion chamber is opened and closed by an
排気ポート216には、EGR管217の一端部が連結されている。EGR管217は、吸気ポート208の上流側に位置する吸気マニホールド(符号省略)にその他端部が連結されており、排気の一部をEGRガスとして吸気系に戻すことが出来る。
The
EGRガスの供給量たるEGR量は、EGR管217に設置されたEGR弁218により制御される。EGR弁218は、ソレノイドの電磁力により弁の開閉を制御する電磁駆動弁であり、当該ソレノイドの励磁状態を制御する駆動装置と電気的に接続されたECU100の制御により、その弁開度が制御される構成となっている。尚、図1では、EGR管217が排気ポート216に連結されているが、EGR管217は、排気ポート216よりも下流側において、複数の気筒201の排気ポート216を集約して後述する排気管219に導く排気マニホールドに連結されていてもよい。
The EGR amount that is the supply amount of EGR gas is controlled by an
本実施形態においては、EGR管217とEGR弁218とにより、HPL(High Pressure Loop)EGR装置が構成されるが、EGR装置の構成はこれに限定されず、例えば、後述する三元触媒220の下流側から排気を取り出すLPL(Low Pressure Loop)EGR装置であってもよい。
In this embodiment, the
各気筒の排気ポート216には、排気管219が連結されている。排気管214は、本発明に係る「排気経路」の一例である。
The
排気管219には、本発明に係る「排気浄化用の触媒」の一例たる三元触媒220が設置される。三元触媒215は、触媒担体に白金等の貴金属が担持された公知の触媒装置であり、HC及びCOの酸化燃焼反応と、窒素酸化物NOxの還元反応とを略同時に進行させることによって排気を浄化可能に構成される。
The
排気管219における三元触媒220の上流側には、三元触媒220に流入する触媒流入ガスの空燃比である入力側空燃比A/Finを検出可能な空燃比センサ221が設置されている。空燃比センサ221は、例えば、拡散抵抗層を備えた限界電流式広域空燃比センサである。
On the upstream side of the three-
空燃比センサ221は、三元触媒220の上流側の排気(触媒流入ガス)の空燃比である入力側空燃比A/Finに応じた出力電圧値Vafinを出力するセンサである。即ち、空燃比センサ221は、入力側空燃比A/Finと一義的な関係を有する電圧値により間接的に入力側空燃比A/Finを検出する構成を採る。
The air-
この出力電圧値Vafinは、入力側空燃比A/Finが理論空燃比である時に基準出力電圧値Vstに一致する。また、この出力電圧値Vafinは、入力側空燃比A/Finが空燃比リッチ側にある場合に基準出力電圧値Vstより低くなり、入力側空燃比A/Finが空燃比リーン側にある場合に基準出力電圧値Vstより高くなる。即ち、出力電圧値Vafinは、入力側空燃比A/Finの変化に対して連続的に変化する。空燃比センサ221は、ECU100と電気的に接続されており、検出された出力電圧値Vafinは、ECU100により一定又は不定の周期で参照される構成となっている。
The output voltage value Vafin matches the reference output voltage value Vst when the input side air-fuel ratio A / Fin is the stoichiometric air-fuel ratio. The output voltage value Vafin is lower than the reference output voltage value Vst when the input side air-fuel ratio A / Fin is on the air-fuel ratio rich side, and when the input-side air-fuel ratio A / Fin is on the air-fuel ratio lean side. It becomes higher than the reference output voltage value Vst. That is, the output voltage value Vafin continuously changes with respect to the change of the input side air-fuel ratio A / Fin. The air-
排気管219における三元触媒220の下流側には、三元触媒220を通過した触媒排出ガスの酸素濃度である下流側酸素濃度Coxsを検出可能なO2センサ222が設置されている。O2センサ222は、周知の起電力式酸素濃度センサ(即ち、安定化ジルコニアを用いた濃淡電池型の酸素濃度センサ)である。
On the downstream side of the three-
O2センサ222は、下流側酸素濃度Coxsに応じた出力電圧値Voxsを出力するセンサである。即ち、O2センサ222は、酸素濃度と一義的な関係を有する電圧値により間接的に酸素濃度を検出する構成を採る。 The O 2 sensor 222 is a sensor that outputs an output voltage value Voxs corresponding to the downstream oxygen concentration Coxs. That is, the O 2 sensor 222 adopts a configuration in which the oxygen concentration is indirectly detected by a voltage value having a unique relationship with the oxygen concentration.
O2センサ222の出力電圧値Voxsは、触媒排出ガスの空燃比が理論空燃比である場合(言い換えれば、下流側酸素濃度Coxsが理論空燃比に相当する基準酸素濃度Coxsbである場合)に基準出力電圧値Voxsb(例えば、約0.5V程度)に一致する。また、出力電圧値Voxsは、触媒排出ガスの空燃比が理論空燃比に対し空燃比リッチ側にある場合に基準出力電圧値Voxsbよりも高くなり、同じく空燃比が空燃比リーン側にある場合に基準出力電圧値Voxsbよりも低くなる。 The output voltage value Voxs of the O 2 sensor 222 is a reference when the air-fuel ratio of the catalyst exhaust gas is the stoichiometric air-fuel ratio (in other words, when the downstream oxygen concentration Coxs is the reference oxygen concentration Coxsb corresponding to the stoichiometric air-fuel ratio). It corresponds to the output voltage value Voxsb (for example, about 0.5V). The output voltage value Voxs is higher than the reference output voltage value Voxsb when the air-fuel ratio of the catalyst exhaust gas is on the air-fuel ratio rich side with respect to the stoichiometric air-fuel ratio, and when the air-fuel ratio is also on the air-fuel ratio lean side. It becomes lower than the reference output voltage value Voxsb.
具体的には、触媒排出ガスの空燃比が、理論空燃比とリッチ側検出限界空燃比との間にある場合、O2センサ222の出力電圧値Voxsは、空燃比の減少(即ち、酸素濃度Coxsの減少)に伴って、係るリッチ側検出限界空燃比に相当する最大出力電圧値Voxsmax(例えば、約0.9V程度)まで比較的急峻に、略線形に増加する。リッチ側検出限界空燃比よりもリッチ側の空燃比領域において、出力電圧値Voxsは最大出力電圧値Voxsmaxで略一定となる。 Specifically, when the air-fuel ratio of the catalyst exhaust gas is between the stoichiometric air-fuel ratio and the rich detection limit air-fuel ratio, the output voltage value Voxs of the O 2 sensor 222 is a decrease in the air-fuel ratio (ie, oxygen concentration). With a decrease in Coxs), it increases relatively linearly and substantially linearly to a maximum output voltage value Voxsmax (for example, about 0.9 V) corresponding to the rich-side detection limit air-fuel ratio. In the air-fuel ratio region on the rich side with respect to the rich-side detection limit air-fuel ratio, the output voltage value Voxs is substantially constant at the maximum output voltage value Voxsmax.
また、触媒排出ガスの空燃比が、理論空燃比とリーン側検出限界空燃比との間にある場合、O2センサ222の出力電圧値Voxsは、空燃比の増加(即ち、酸素濃度Coxsの増加)に伴って、係るリーン側検出限界空燃比に相当する最小出力電圧値Voxsmin(例えば、約0.1V程度)まで比較的急峻に、略線形に減少する。リーン側検出限界空燃比よりもリーン側の空燃比領域において、出力電圧値Voxsは最小出力電圧値Voxsminで略一定となる。 When the air-fuel ratio of the catalyst exhaust gas is between the stoichiometric air-fuel ratio and the lean side detection limit air-fuel ratio, the output voltage value Voxs of the O 2 sensor 222 increases the air-fuel ratio (that is, the oxygen concentration Coxs increases). ) To a minimum output voltage value Voxsmin (for example, about 0.1 V) corresponding to the lean-side detection limit air-fuel ratio, it decreases relatively linearly and substantially linearly. In the air-fuel ratio region leaner than the lean-side detection limit air-fuel ratio, the output voltage value Voxs is substantially constant at the minimum output voltage value Voxsmin.
O2センサ222は、ECU100と電気的に接続されており、検出された出力電圧値Voxsは、ECU100により一定又は不定の周期で参照される構成となっている。
The O 2 sensor 222 is electrically connected to the
エンジン200において、シリンダブロックCBを取り囲むように設置されたウォータジャケットには、エンジン200を冷却するために循環供給される冷却水(LLC)の温度である冷却水温Twを検出可能な水温センサ223が配設されている。水温センサ223は、ECU100と電気的に接続されており、検出された冷却水温Twは、ECU100により一定又は不定の周期で参照される構成となっている。
In the
エンジン200は、PFI342に加えて、燃料を筒内噴射可能なDFI(Direct Fuel Injector:筒内噴射装置)362を備える。DFI362の噴射弁は、その一部が気筒201の燃焼室に露出している。DFI362は、PFI342と共に、燃料供給装置300を構成する。
ここで、図2を参照し、燃料供給装置300の構成について説明する。ここに、図2は、燃料供給装置300を概念的に表してなる概略構成図である。尚、同図において、既出の各図と重複する箇所については同一の符号を付してその説明を適宜省略することとする。
Here, the configuration of the
図3において、燃料供給装置300は、燃料タンク310、フィード管320、フィードポンプ330、ポート噴射システム340、高圧ポンプ350及び筒内噴射システム360を備える。
3, the
燃料タンク310は、燃料(本実施形態ではガソリン)を貯留するタンクである。 The fuel tank 310 is a tank for storing fuel (in this embodiment, gasoline).
フィード管320は、一端部が燃料タンク310に連結され、他端部がポート噴射システム340及び筒内噴射システム360に連結された金属製の管状部材である。フィードポンプ330は、このフィード管320における燃料タンク310近傍に設けられている。
The feed pipe 320 is a metal tubular member having one end connected to the fuel tank 310 and the other end connected to the
フィードポンプ330は、燃料タンク310から燃料を汲み上げ、フィード管320に所望の燃料吐出速度(時間当たりの吐出量)で燃料を供給可能に構成された電動ポンプ装置である。フィードポンプ330から吐出される燃料は、所定のフィード圧Pfdを有する低圧燃料である。フィードポンプ330の燃料吐出速度は、ECU100と電気的に接続された不図示の駆動装置により制御される。尚、フィードポンプ330は、この燃料吐出速度の制御を介して、フィード管320内の燃圧であるフィード圧Pfdを可変に制御することが出来る。
The
ポート噴射システム340は、低圧デリバリ341と複数のPFI342とフィード圧センサ343とを含んで構成される。
The
低圧デリバリ341は、フィード圧Pfdを有する低圧燃料を一定量蓄積可能に構成されたバッファである。
The
PFI342は、低圧デリバリ341に連結された本発明に係る「ポート噴射装置」の一例たる燃料噴射装置である。PFI342の燃料噴射弁は、先述したように各シリンダの吸気ポート208に露出しており、燃料噴射弁の開弁期間及びフィード圧Pfdにより定まる量のポート噴射燃料Fpiを吸気ポート208に噴霧として噴射可能に構成されている。
The
フィード圧センサ343は、上述した低圧燃料のフィード圧Pfdを検出可能に構成されたセンサである。フィード圧センサ343は、ECU100と電気的に接続されており、検出されたフィード圧Pfdは、ECU100により一定又は不定の周期で参照される構成となっている。
The
高圧ポンプ350は、フィードポンプ330と筒内噴射システム360との間に介装された機械式ポンプ装置である。
The high-
ここで、図3を参照し、高圧ポンプ350の構成について説明する。ここに、図3は、高圧ポンプ350の構成を概念的に表してなる概略構成図である。尚、同図において、既出の各図と重複する箇所については同一の符号を付してその説明を適宜省略することとする。
Here, the configuration of the high-
図3において、高圧ポンプ350は、電磁調量弁351、吸入弁352、シリンダ353、プランジャ354、加圧室355、カム356、吐出弁357及び高圧管358を備える。
3, the high-
電磁調量弁351は、フィードポンプ330へ繋がるフィード管320上に設けられ、フィードポンプ320により送出された低圧燃料の流量を調節する電磁開閉弁である。フィードポンプ320により燃料タンク310から汲み上げられた低圧燃料は、この電磁調量弁351によりその流量が調節され、フィード管320の一端部が接続された加圧室355へ供給される。電磁調量弁351は、ECU100と電気的に接続されており、その開弁期間を規定する駆動デューティが、ECU100により制御される構成となっている。
The
プランジャ354は、シリンダ353内に設置された加圧部材であり、下端部に接続されたロッド状部材が、エンジン200の吸気カムシャフトICSに固定され且つ吸気カムシャフトICSの回転に連動して回転する、先述した吸気カム210のカムプロフィールに従って図中上下方向に往復運動するのに伴い、その上端部が図示TDC(Top Death Center:上死点)と図示BDC(Bottom Death Center:下死点)との間で往復運動する構成となっている。
加圧室355は、シリンダ353の内壁部分と、プランジャ354の上端部分とによって規定される空間であり、プランジャ354の前述した往復運動に伴って、その容積が変化する空間である。
The pressurizing
電磁調量弁351により調量された燃料は、プランジャ354がシリンダ353内をTDCからBDCへ向かって移動する際(即ち、減圧期)に、吸入弁352を押し開いて加圧室に吸入される。その後、プランジャ354がシリンダ353内をBDCからTDCへ向かって移動する際(即ち、加圧期)に、プランジャ354によって加圧室355内部の燃料が圧縮(即ち、加圧)される。加圧された燃料は、吐出弁357を押し開いて高圧管358に供給され、高圧管358に接続された高圧デリバリ361へと圧送される構成となっている。
The fuel metered by the
ここで、このようにエンジン200の機関運動に連動して加圧動作が行われる機械式ポンプ装置においては、駆動負荷が電磁調量弁351の開弁状態と一義的関係となる。即ち、電磁調量弁351の開弁期間が長ければ、その分多くの燃料が加圧室355に導入されることとなり、高圧ポンプ350の駆動負荷はその分上昇する。
Here, in the mechanical pump device in which the pressurizing operation is performed in conjunction with the engine motion of the
尚、ここに例示する高圧ポンプ350は、気筒内に燃料を直接噴射する筒内噴射システムにおける高圧ポンプ装置の一例であり、無論公知の他の態様を採り得る。
The high-
図2に戻り、筒内噴射システム360は、高圧デリバリ361と複数のDFI362と高圧センサ363とを含んで構成される。
2, the in-
高圧デリバリ361は、燃圧Ph(Ph>Pfd)を有する高圧燃料を一定量蓄積可能に構成されたバッファである。
The high-
DFI362は、高圧デリバリ361に連結された、本発明に係る「筒内噴射装置」の一例たる燃料噴射装置である。DFI362の燃料噴射弁は、先述したように各気筒の燃焼室に露出しており、燃料噴射弁の開弁期間及び燃圧Phにより定まる量の筒内噴射燃料Fdiを気筒201の燃焼室に噴霧として噴射可能に構成されている。
The
ここで、DFI362の構成について補足する。DFI362は、ECU100から供給される指令に基づいて作動する電磁弁と、この電磁弁への通電時に燃料を噴射するノズル(いずれも不図示)とを備える。当該電磁弁は、高圧デリバリ361に蓄積された高圧燃料が印加される圧力室と、当該圧力室に接続された低圧側の低圧通路との間の連通状態を制御可能に構成されており、通電時に当該圧力室と低圧通路とを連通させると共に、通電停止時に当該圧力室と低圧通路とを相互に遮断する構成となっている。
Here, we will supplement the configuration of DFI362. The
一方、ノズルは、噴孔を開閉するニードルを内蔵し、圧力室の燃料圧力がニードルを閉弁方向(噴孔を閉じる方向)に付勢している。従って、電磁弁への通電により圧力室と低圧通路とが連通し、圧力室の燃料圧力が低下すると、ニードルがノズル内を上昇して開弁する(噴孔を開く)ことにより、高圧デリバリ361より供給された高圧燃料が噴孔より噴射される。また、電磁弁への通電停止により圧力室と低圧通路とが相互に遮断されて圧力室の燃料圧力が上昇すると、ニードルがノズル内を下降して閉弁することにより、噴射が終了する。
On the other hand, the nozzle has a built-in needle that opens and closes the nozzle hole, and the fuel pressure in the pressure chamber urges the needle in the valve closing direction (direction in which the nozzle hole is closed). Accordingly, when the pressure chamber communicates with the low pressure passage by energizing the electromagnetic valve and the fuel pressure in the pressure chamber decreases, the needle rises in the nozzle and opens (opens the nozzle hole), thereby causing the
燃料供給装置300では、後述するように、PFI342とDFI362との間で、ポート噴射燃料Fpiと筒内噴射燃料Fdiとの比率である噴き分け比率Rinjを自由に制御することが出来る。
In the
<実施形態の動作>
<空燃比F/B制御の概要>
エンジン200において、一の気筒201の燃料噴射量Qは、PFI342の燃料噴射量であるポート噴射量QpfiとDFI362の燃料噴射量である筒内噴射量Qdfiとの総和である。この燃料噴射量Qは、ECU100により、エンジン200の稼動期間について常時実行される空燃比F/B制御により制御される。本実施形態に係る空燃比F/B制御は、メインF/B制御とサブF/B制御とから構成される。
<Operation of Embodiment>
<Outline of air-fuel ratio F / B control>
In the
メインF/B制御は、空燃比センサ221の出力電圧値Vafinに基づいて得られる入力側空燃比A/Finが入力側目標空燃比A/Fintgに収束するようになされる燃料噴射量の制御である。
The main F / B control is control of the fuel injection amount so that the input side air-fuel ratio A / Fin obtained based on the output voltage value Vafin of the air-
サブF/B制御は、O2センサ222の出力電圧値Voxsが目標出力電圧値Voxstgに収束するように空燃比センサ221の出力電圧値Vafin又は入力側目標空燃比A/Fintgを補正する制御である。
The sub F / B control is a control for correcting the output voltage value Vafin of the air-
メインF/B制御及びサブF/B制御を含む空燃比F/B制御が実行されると、三元触媒220の内部の空燃比を目標空燃比に収束させることが出来る。目標空燃比とは、三元触媒220の排気浄化作用が最適化される空燃比であって、例えば、理論空燃比である。無論、この目標空燃比は、エミッションや燃費を勘案して許容される範囲で、エンジン200の要求性能等に応じて適宜変更されてもよく、また実際に適宜変更される。
When the air-fuel ratio F / B control including the main F / B control and the sub F / B control is executed, the air-fuel ratio inside the three-
尚、このような触媒上下流の空燃比相当値に基づいたフィードバック制御は、従来各種のものが提案されており、ここでは、説明の煩雑化を防ぐ目的からこれ以上の詳細については割愛することとする。 Various types of feedback control based on the values corresponding to the air / fuel ratios upstream and downstream of the catalyst have been proposed in the past. Here, further details are omitted for the purpose of preventing complication of explanation. And
空燃比F/B制御において、気筒201毎に燃料噴射量Qが決定されると、ECU100は、所定の基準に従って上述した噴き分け比率Rinjを決定する。尚、噴き分け比率Rinjは、通常、予め実験的に、経験的に又は理論的に定められた、エンジン200の燃費が最良となる値(この値を、これ以降適宜「標準噴き分け比率Rinjb」と称する)に制御される。
In the air-fuel ratio F / B control, when the fuel injection amount Q is determined for each
<S被毒回復制御の詳細>
エンジン200に使用されるガソリンには、多寡はあれ硫黄が含まれることが多い。この燃料中の硫黄は、気筒201内部において、或いは排気管219において、酸素と結びついて硫黄酸化物(SOx)となり易い。硫黄酸化物は、三元触媒220の貴金属と化学的に結び付き易く、エンジン200の稼動期間において、三元触媒220は徐々に硫黄被毒(S被毒)する。エンジンシステム10では、この三元触媒220を硫黄被毒から回復させるために、ECU100により、S(硫黄)被毒回復制御が実行される。
<Details of S poison recovery control>
The gasoline used for the
ここで、図4を参照し、S被毒回復制御の詳細について説明する。ここに、図4は、S被毒回復制御のフローチャートである。 Here, the details of the S poison recovery control will be described with reference to FIG. FIG. 4 is a flowchart of the S poison recovery control.
図4において、ECU100は、三元触媒220のS堆積量Dsfを取得する(ステップS101)。S堆積量Dsfとは、前回のS被毒回復制御が終了してから現在に至る期間において、三元触媒220に堆積した硫黄の量であり、本発明に係る「触媒における硫黄の堆積量」の一例である。
In FIG. 4, the
S堆積量Dsfは、ECU100が、S被毒回復制御とは別の制御ルーチンで繰り返し演算しており、RAM等の書き換え可能なメモリに適宜更新を伴いつつ記憶している。即ち、S堆積量Dsfを実行する過程において、ECU100は、本発明に係る「第1推定手段」の一例として機能する。
The S accumulation amount Dsf is repeatedly calculated by the
ECU100は、ポート噴射量Qpfiと筒内噴射量Qdfiとの総和である燃料噴射量Qを、各気筒の各サイクルについて積算した値である積算燃料消費量ΣQからS堆積量Dsfを推定する。尚、予め単位燃料中の硫黄含有量は初期値として与えられているものとする。ECU100は、その時点の積算燃料消費量ΣQに対し、所定の堆積率σを乗じることによってS堆積量Dsfを算出する。
The
この堆積率σは、排気管219に排出された硫黄のうち三元触媒220に堆積する硫黄の比率を表す補正係数であり、予め実験的に、経験的に又は理論的に、機関回転数NE及び負荷率KL(即ち、気筒201に吸入された新気量の物理的最大値に対する割合である)をパラメータとして制御マップに格納されている。定性的には、機関回転数NEが高い程、また、負荷率KLが大きい程、堆積率σは弱減少傾向となる。尚、このようなS堆積量Dsfの推定態様は、一例であり、S堆積量の算出には公知の各種態様を適用可能である。
This deposition rate σ is a correction coefficient that represents the ratio of sulfur deposited on the three-
ECU100は、取得したS堆積量Dsfが基準値Dsfthよりも大きいか否かを判定する(ステップS102)。基準値Dsfthは、予め実験的に、経験的に又は理論的に、三元触媒220の浄化効率がS被毒により所定以上に低下する値として決定されている。S堆積量Dsfが基準値Dsfth以下である場合(ステップS102:NO)、ECU100は、処理をステップS101に戻す。
ECU100 determines whether the acquired S accumulation amount Dsf is larger than the reference value Dsfth (step S102). The reference value Dsfth is determined in advance experimentally, empirically, or theoretically as a value that reduces the purification efficiency of the three-
一方、S堆積量Dsfが基準値Dsfthよりも大きい場合(ステップS102:YES)、ECU100は、三元触媒220に硫黄被毒回復の必要性があるものとして、ステップS103以降の処理を実行する。
On the other hand, when the S accumulation amount Dsf is larger than the reference value Dsfth (step S102: YES), the
ステップS103において、ECU100は、H2(水素)要求量Nh2を算出する。H2要求量Nh2は、三元触媒220の硫黄被毒回復のために各気筒201で生成させる必要がある水素量の要求量であり、本発明に係る「触媒を硫黄被毒から回復させるための水素の要求量」の一例である。
In step S103, the
ECU100は、H2要求量Nh2を算出するにあたって、ROMに格納されたH2要求量マップを参照する。ここで、図5を参照し、H2要求量マップについて説明する。ここに、図5は、H2要求量マップの概念図である。
The
図5において、縦軸及び横軸に夫々H2要求量Nh2及びS堆積量Dsfが表される。図示するように、H2要求量Nh2は、S堆積量Dsfとリニアな関係を有する。H2要求量マップには、図5に例示される関係が数値化されて格納されており、ECU100は、H2要求量Nh2を算出するにあたって、H2要求量マップから、ステップS101で取得されたS堆積量Dsfに対応する値を選択する(尚、このような選択処理も算出の一例であるとする)構成となっている。
In FIG. 5, the H2 requirement amount Nh2 and the S deposition amount Dsf are represented on the vertical axis and the horizontal axis, respectively. As shown in the figure, the H2 requirement amount Nh2 has a linear relationship with the S deposition amount Dsf. The relationship illustrated in FIG. 5 is digitized and stored in the H2 request amount map, and when calculating the H2 request amount Nh2, the
図4に戻り、H2要求量Nh2が算出されると、ECU100は、噴き分け比率Rinjを、上述した標準噴き分け比率Rinjbから硫黄被毒回復用の噴き分け比率Rinjh2に変更する(ステップS104)。
Returning to FIG. 4, when the required H2 amount Nh2 is calculated, the
ここで、図6を参照し、噴き分け比率Rinjと気筒201のH2生成量との関係について説明する。ここに、図6は、噴き分け比率RinjとH2生成量Gh2との関係を例示する図である。
Here, with reference to FIG. 6, the relationship between the injection ratio Rinj and the H2 generation amount of the
図6において、縦軸及び横軸に夫々H2生成量Gh2及び噴き分け比率Rinjが表される。本実施形態における噴き分け比率Rinjは、Qpfi/(Qpfi+Qdfi)と定義されており、値が大きい程(図示左側)、ポート噴射量Qpfiが多くなり、値が小さい程(図示右側)、筒内噴射量Qdfiが多くなる。 6, the vertical axis and the horizontal axis respectively represent the H2 generation amount Gh2 and the spray distribution ratio Rinj. The injection ratio Rinj in the present embodiment is defined as Qpfi / (Qpfi + Qdfi). The larger the value (left side in the figure), the larger the port injection amount Qpfi, and the smaller the value (right side in the figure), the in-cylinder injection. The quantity Qdfi increases.
図示するように、H2生成量Gh2は、噴き分け比率Rinjが小さくなる(即ち、筒内噴射量Qdfiが増える)程、二次関数的に増加する。尚、図示の特性は、気筒の空燃比が理論空燃比(14.6)である場合の特性であるとする。 As illustrated, the H2 generation amount Gh2 increases in a quadratic function as the injection ratio Rinj decreases (that is, the in-cylinder injection amount Qdfi increases). Note that the characteristics shown in the figure are characteristics when the air-fuel ratio of the cylinder is the stoichiometric air-fuel ratio (14.6).
図4に戻り、硫黄被毒回復用の噴き分け比率Rinjh2は、極端な事例としては、標準噴き分け比率Rinjbよりも小さい値であればよく、その決定に明確な指針は必ずしもなくてよい。但し、H2生成量Gh2が十分に大きくないと、噴き分け比率Rinjが標準噴き分け比率Rinjbから乖離する時間が長くなるので、予め実験的に適当な値に定められている。この際、H2要求量Nh2の大小に応じて複数の選択肢の中から一の噴き分け比率Rinjh2が選択される構成としてもよい。 Referring back to FIG. 4, as an extreme case, the injection ratio Rinjh2 for recovery from sulfur poisoning may be a value smaller than the standard injection ratio Rinjb, and there is no need to have a clear guideline for the determination. However, if the H2 generation amount Gh2 is not sufficiently large, the time during which the ejection ratio Rinj deviates from the standard ejection ratio Rinjb becomes longer, and thus is set to an appropriate value experimentally in advance. At this time, a configuration in which one ejection ratio Rinjh2 is selected from a plurality of options according to the magnitude of the H2 request amount Nh2 may be adopted.
一方、硫黄被毒回復用の噴き分け比率Rinjh2が決定されると、ECU100は、H2生成量Gh2の補正係数を取得する(ステップS105)。ここで、図7を参照し、補正係数について説明する。ここに、図7は、補正係数の概念図である。
On the other hand, when the injection division ratio Rinjh2 for recovery from sulfur poisoning is determined, the
図7において、補正係数は冷却水温Twの関数である。即ち、冷却水温Twが、暖機完了判定値Tww未満となる温度領域において、補正係数は1より大きく設定される。これは、未暖機状態では、気筒201内部の燃焼が暖機完了後と較べて悪化するからである。
In FIG. 7, the correction coefficient is a function of the cooling water temperature Tw. That is, the correction coefficient is set to be larger than 1 in the temperature region where the coolant temperature Tw is lower than the warm-up completion determination value Tww. This is because in the unwarmed state, the combustion in the
図4に戻り、H2生成量Gh2の補正係数を取得すると、ECU100は、硫黄被毒回復用の噴き分け比率Rinjh2に応じた、基本となるH2生成量と、この補正係数と、エンジン200の機関回転数NE及び負荷率KL(即ち、単位時間当たりのガス排出量と一義的な関係を有する)とに基づいて、瞬時H2生成量Gh2mを算出すると共に、この瞬時H2生成量Gh2mを積算する(ステップS106)。
Returning to FIG. 4, when the correction coefficient for the H2 generation amount Gh2 is acquired, the
続いて、ECU100は、この瞬時H2生成量Gh2mの時間積算値ΣGh2mを取得する(ステップS107)。尚、時間積算値ΣGh2mは、噴き分け比率Rinj変更後現在に至るまでの水素の生成量を意味する。
Subsequently, the
時間積算値ΣGh2mが取得されると、ECU100は、この取得された時間積算値ΣGh2mが、先に算出されたH2要求量Nh2より大きいか否かを判定する(ステップS108)。ΣGh2mがNh2以下であれば(ステップS108:NO)、処理はステップS105に戻される。
When the time integration value ΣGh2m is acquired, the
ステップS108において、ΣGh2mがNh2より大きい旨が判定されると(ステップS108:YES)、ECU100は、S堆積量Dsfをクリアし(ステップS109)、噴き分け比率Rinjを標準噴き分け比率Rinjbに復帰させて(ステップS110)、処理をステップS101に戻す。S被毒回復制御は以上のように実行される。
When it is determined in step S108 that ΣGh2m is larger than Nh2 (step S108: YES), the
このように、本実施形態に係るS被毒回復制御によれば、三元触媒220のS堆積量Dsfが基準値Dsfthを超えた場合に、筒内噴射装置であるDFI362の噴射態様としての噴き分け比率Rinjが、燃費を最適に維持するための標準噴き分け比率Rinjbから、硫黄被毒回復用の噴き分け比率Rinjh2へ変更される。
Thus, according to the S poison recovery control according to the present embodiment, when the S accumulation amount Dsf of the three-
硫黄被毒回復用の噴き分け比率Rinjh2は、標準噴き分け比率Rinjbと較べて筒内噴射量Qdfiが多くなる噴き分け比率であるため、標準噴き分け比率Rinjbが選択される場合と較べて気筒201における混合気の均質度が低下し、燃焼状態が相対的に悪化して気筒201で水素が生成される三元触媒220では、この気筒201で生成されたH2により硫黄の脱離が促進される。
The injection ratio Rinjh2 for recovery from sulfur poisoning is an injection ratio in which the in-cylinder injection amount Qdfi is larger than the standard injection ratio Rinjb. In the three-
一方、噴き分け比率Rinjは、気筒毎に要求される燃料噴射量Qには影響を与えない。従って、エンジン200全体としては、燃料噴射量は要求値に維持され、燃費の悪化が生じることがない。即ち、本実施形態に係るS被毒回復制御によれば、コストの増加並びにエミッション及び燃費の悪化を招くことなく三元触媒220を硫黄被毒から回復させることが出来る。
<第2実施形態>
次に、図8を参照し、本発明の第2実施形態に係るS被毒回復制御について説明する。ここに、図8は、本発明の第2実施形態に係るS被毒回復制御のフローチャートである。尚、同図において、図4と重複する箇所には同一の符号を付してその説明を適宜省略することとする。
On the other hand, the injection ratio Rinj does not affect the fuel injection amount Q required for each cylinder. Therefore, for the
<Second Embodiment>
Next, S poison recovery control according to the second embodiment of the present invention will be described with reference to FIG. FIG. 8 is a flowchart of the S poison recovery control according to the second embodiment of the present invention. In the figure, the same reference numerals are given to the same portions as those in FIG. 4, and the description thereof will be omitted as appropriate.
図8において、H2要求量Nh2が算出されると(ステップS103)、ECU100は、筒内噴射時期Tdfiを標準筒内噴射時期Tdfibから硫黄被毒回復用の筒内噴射時期Tdfih2に変更する(ステップS201)。
In FIG. 8, when the required H2 amount Nh2 is calculated (step S103), the
ここで、図9を参照し、筒内噴射時期Tdfiと気筒201のH2生成量との関係について説明する。ここに、図9は、筒内噴射時期TdfiとH2生成量Gh2との関係を例示する図である。
Here, the relationship between the in-cylinder injection timing Tdfi and the H2 generation amount of the
図9において、縦軸及び横軸に夫々H2生成量Gh2及び筒内噴射時期Tdfiが表される。筒内噴射時期Tdfiは、DFI362が燃料噴射を開始するクランク角である。
9, the vertical axis and the horizontal axis represent the H2 generation amount Gh2 and the in-cylinder injection timing Tdfi, respectively. The in-cylinder injection timing Tdfi is a crank angle at which the
図示するように、H2生成量Gh2は、筒内噴射時期Tdfiが遅角側(図示右側)へ向かう程増加する。尚、図示の特性は、エンジン200の完全暖機後の特性であるとする。
As shown in the figure, the H2 generation amount Gh2 increases as the in-cylinder injection timing Tdfi moves toward the retard side (the right side in the figure). Note that the illustrated characteristics are characteristics after the
標準筒内噴射時期Tdfibは、吸気上死点TDCiと吸気下死点BDCiとの間にあり、吸気行程の終期と圧縮行程全てが燃料と吸入ガスとの予混合に供される構成となっている。これに対し、筒内噴射時期Tdfiを遅角側に変更すると、筒内噴射された燃料が吸入ガスと十分に混合される期間が担保され難くなり、混合気の均質度が低下する。その結果、噴き分け比率Rinjの場合と同様に、H2生成量Gh2が増加するのである。 The standard in-cylinder injection timing Tdfib is between the intake top dead center TDCi and the intake bottom dead center BDCi, and the end of the intake stroke and the entire compression stroke are provided for premixing of fuel and intake gas. Yes. On the other hand, if the in-cylinder injection timing Tdfi is changed to the retarded angle side, it is difficult to ensure a period during which the in-cylinder injected fuel is sufficiently mixed with the intake gas, and the homogeneity of the air-fuel mixture decreases. As a result, the H2 generation amount Gh2 increases as in the case of the spray distribution ratio Rinj.
図8に戻り、硫黄被毒回復用の筒内噴射時期Tdfiは、極端な事例としては、標準筒内噴射時期Tdfibよりも遅角側の値であればよく、その決定に明確な指針は必ずしもなくてよい。但し、H2生成量Gh2が十分に大きくないと、筒内噴射時期Tdfiが標準筒内噴射時期Tdfibから乖離する時間が長くなるので、予め実験的に適当な値に定められている。この際、H2要求量Nh2の大小に応じて複数の選択肢の中から一の筒内噴射時期Tdfih2が選択される構成としてもよい。 Returning to FIG. 8, in an extreme case, the in-cylinder injection timing Tdfi for recovery from sulfur poisoning may be a value retarded from the standard in-cylinder injection timing Tdfib. It is not necessary. However, if the H2 generation amount Gh2 is not sufficiently large, the time during which the in-cylinder injection timing Tdfi deviates from the standard in-cylinder injection timing Tdfi becomes long, and thus is set to an appropriate value experimentally in advance. At this time, one in-cylinder injection timing Tdfih2 may be selected from a plurality of options according to the magnitude of the H2 request amount Nh2.
このように硫黄被毒回復用の筒内噴射時期Tdfih2が定められると、噴き分け比率Tinjを切り替えた場合と同様に瞬時H2生成量Gh2mの積算処理(ステップS106)が行われる。尚、この場合、瞬時H2生成量Gh2mの算出基準となるH2生成量Gh2は、噴き分け比率Rinjを切り替えた場合と異なる。 When the in-cylinder injection timing Tdfih2 for sulfur poisoning recovery is determined in this way, the instantaneous H2 generation amount Gh2m is integrated (step S106) in the same way as when the injection ratio Tinj is switched. In this case, the H2 generation amount Gh2 that is a calculation reference of the instantaneous H2 generation amount Gh2m is different from the case where the injection ratio Rinj is switched.
ステップS106以降は、ステップS109まで第1実施形態と同様であり、S堆積量Dsfがクリアされると(ステップS109)、筒内噴射時期Tdfiが標準筒内噴射時期Tdfibに復帰させられ(ステップS202)、処理はステップS101に戻される。第2実施形態に係るS被毒回復制御は以上のように実行される。 Step S106 and subsequent steps are the same as in the first embodiment up to step S109. When the S accumulation amount Dsf is cleared (step S109), the in-cylinder injection timing Tdfi is returned to the standard in-cylinder injection timing Tdfib (step S202). ), The process returns to step S101. The S poison recovery control according to the second embodiment is executed as described above.
以上説明したように、本実施形態に係るS被毒回復制御によれば、第1実施形態に係る噴き分け比率Rinjと同様に、筒内噴射時期Tdfiの遅角制御により、気筒201での水素生成を促進し、三元触媒220のS被毒を好適に回復させることが出来る。
<第3実施形態>
第1及び第2実施形態では、三元触媒220のS堆積量Dsfが所定値を超えた場合、即ち、三元触媒220がある程度S被毒したことを検知してS被毒回復制御が実行された。しかしながら、予め三元触媒220へのS吸着が生じ易い条件が既知であれば、触媒のS堆積量に応じた制御とは別に、積極的にこのS吸着を抑制することも効果的である。第3実施形態では、図10を参照し、このような趣旨に基づいたS吸着抑制制御について説明する。ここに、図10は、第3実施形態に係るS吸着抑制制御のフローチャートである。尚、同図において、図4と重複する箇所には同一の符号を付してその説明を適宜省略することとする。
As described above, according to the S poison recovery control according to the present embodiment, the hydrogen in the
<Third Embodiment>
In the first and second embodiments, when the S accumulation amount Dsf of the three-
図10において、ECU100は、空燃比センサ221により検出される入力側空燃比A/Finが、理論空燃比に対して所定以上リッチ側にずれており(以下、このような空燃比を「リッチ空燃比」と称する)、且つ、三元触媒220の温度である触媒床温Tcatが基準値Tcatth未満であるか否かを判定する(ステップS301)。
In FIG. 10, the
入力側空燃比A/Finがリッチ空燃比であり且つ触媒床温Tcatが基準値Tcatth未満である場合(ステップS301:YES)、ECU100は、第1実施形態と同様に噴き分け比率RinjをH2生成用の噴き分け比率Rinjh2に変更する(ステップS104)。
When the input side air-fuel ratio A / Fin is a rich air-fuel ratio and the catalyst bed temperature Tcat is lower than the reference value Tcatth (step S301: YES), the
噴き分け比率Rinjが変更されると、処理はステップS301に戻される。噴き分け比率Rinjの変更は、入力側空燃比A/Finがリッチ空燃比でなくなるか、又は触媒床温Tcatが基準値Tcatth以上となるまで継続される。 When the spray distribution ratio Rinj is changed, the process returns to step S301. The change of the injection ratio Rinj is continued until the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth.
入力側空燃比A/Finがリッチ空燃比でなくなるか、又は触媒床温Tcatが基準値Tcatth以上となると(ステップ301:NO)、ECU100は、噴き分け比率Rinjを標準噴き分け比率Rinjbに戻し(ステップS110)、処理をステップS301に戻す。S吸着抑制制御は以上のように実行される。
When the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth (step 301: NO), the
ここで、このようなS吸着抑制制御の意義について、図11を参照して説明する。ここに、図11は、リッチ空燃比下における触媒床温Tcatと三元触媒220のS吸着量との関係を例示する図である。尚、図11は、空燃比がリッチ空燃比である場合の特性図である。
Here, the significance of such S adsorption suppression control will be described with reference to FIG. FIG. 11 is a diagram illustrating the relationship between the catalyst bed temperature Tcat and the S adsorption amount of the three-
図11に示すように、リッチ空燃比下においては、触媒床温Tcatが500~600℃付近の基準値よりも低温側にある場合に、高いS吸着量を示す。従って、このような条件下で噴き分け比率RinjをH2生成用の噴き分け比率Rinjh2に変更してH2生成量を増大させれば、三元触媒220に硫黄が堆積すること自体を防止することが出来る。即ち、能動的に触媒のS被毒を回復させることが出来るのである。
As shown in FIG. 11, under the rich air-fuel ratio, when the catalyst bed temperature Tcat is lower than the reference value in the vicinity of 500 to 600 ° C., a high S adsorption amount is shown. Therefore, if the injection ratio Rinj is changed to the injection ratio Rinjh2 for generating H2 and the amount of H2 generation is increased under such conditions, it is possible to prevent sulfur from being deposited on the three-
尚、ステップS301では、触媒床温Tcatが取得されるが、触媒床温Tcatは、最新のIGオンタイミング以降、S被毒回復制御とは別の制御ルーチンにおいて、当該タイミング以降の積算燃料消費量に基づいて推定される。具体的には、積算燃料消費量と触媒床温Tcatとの関係を表す制御マップが予めROMに格納されており、ECU100は、当該制御マップから、積算燃料消費量に対応する温度値を取得することによって触媒床温Tcatを推定する。尚、三元触媒220に温度センサが配置される場合には、当該温度センサの検出値が使用されてもよい。
<第4実施形態>
第3実施形態に係るS吸着抑制制御は、第1実施形態と第2実施形態との関係と同様に、筒内噴射時期Tdfiの変更によっても実現され得る。ここで、図12を参照し、本発明の第4実施形態として、このようなS吸着抑制制御について説明する。ここに、図12は、第4実施形態に係るS吸着抑制制御のフローチャートである。尚、同図において、図8及び図10と重複する箇所には同一の符号を付してその説明を適宜省略することとする。
In step S301, the catalyst bed temperature Tcat is acquired, and the catalyst bed temperature Tcat is calculated after the latest IG on timing in a control routine different from the S poison recovery control. Is estimated based on Specifically, a control map indicating the relationship between the accumulated fuel consumption and the catalyst bed temperature Tcat is stored in advance in the ROM, and the
<Fourth embodiment>
The S adsorption suppression control according to the third embodiment can be realized by changing the in-cylinder injection timing Tdfi, similarly to the relationship between the first embodiment and the second embodiment. Here, with reference to FIG. 12, such S adsorption suppression control will be described as a fourth embodiment of the present invention. FIG. 12 is a flowchart of the S adsorption suppression control according to the fourth embodiment. In the figure, the same reference numerals are given to the same portions as those in FIGS. 8 and 10, and the description thereof is omitted as appropriate.
図12において、ECU100は、入力側空燃比A/Finがリッチ空燃比であり且つ触媒床温Tcatが基準値Tcatth未満である場合(ステップS301:YES)、第2実施形態と同様に筒内噴射時期TdfiをH2生成用の筒内噴射時期Tdfih2に変更する(ステップS201)。 In FIG. 12, when the input side air-fuel ratio A / Fin is a rich air-fuel ratio and the catalyst bed temperature Tcat is lower than the reference value Tcatth (step S301: YES), in-cylinder injection is performed as in the second embodiment. The timing Tdfi is changed to the in-cylinder injection timing Tdfih2 for generating H2 (step S201).
筒内噴射時期Tdfiが変更されると、処理はステップS301に戻される。筒内噴射時期Tdfiの変更は、入力側空燃比A/Finがリッチ空燃比でなくなるか、又は触媒床温Tcatが基準値Tcatth以上となるまで継続される。 When the in-cylinder injection timing Tdfi is changed, the process returns to step S301. The change in the in-cylinder injection timing Tdfi is continued until the input side air-fuel ratio A / Fin is no longer the rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth.
入力側空燃比A/Finがリッチ空燃比でなくなるか、又は触媒床温Tcatが基準値Tcatth以上となると(ステップ301:NO)、ECU100は、筒内噴射時Tdfiを標準時期Tdfibに戻し(ステップS202)、処理をステップS301に戻す。第4実施形態に係るS吸着抑制制御は以上のように実行される。
When the input side air-fuel ratio A / Fin is not a rich air-fuel ratio or the catalyst bed temperature Tcat becomes equal to or higher than the reference value Tcatth (step 301: NO), the
第4実施形態においては、第3実施形態において噴き分け比率RinjをH2生成用の噴き分け比率Rinjh2に変更するのと同様に、筒内噴射時期TdfiがH2生成用の筒内噴射時期Tdfih2に変更され、筒内のH2生成量が増量される。H2生成量が増大すれば、三元触媒220に硫黄が堆積すること自体を防止することが出来る。即ち、能動的に触媒のS被毒を回復させることが出来るのである。
In the fourth embodiment, the in-cylinder injection timing Tdfi is changed to the in-cylinder injection timing Tdfih2 for generating H2 in the same manner as the injection dividing ratio Rinj for changing the injection ratio Rinjh2 for generating H2 in the third embodiment. As a result, the amount of H2 generated in the cylinder is increased. If the amount of H2 generated increases, it is possible to prevent sulfur from being deposited on the three-
本発明は、上述した実施形態に限られるものではなく、請求の範囲及び明細書全体から読み取れる発明の要旨或いは思想に反しない範囲で適宜変更可能であり、そのような変更を伴う内燃機関の制御装置もまた本発明の技術的範囲に含まれるものである。 The present invention is not limited to the above-described embodiment, and can be appropriately changed without departing from the gist or concept of the invention that can be read from the claims and the entire specification, and the control of the internal combustion engine accompanying such a change. The apparatus is also included in the technical scope of the present invention.
本発明は、内燃機関における触媒の硫黄被毒回復制御に適用可能である。 The present invention can be applied to sulfur poisoning recovery control of a catalyst in an internal combustion engine.
10…エンジンシステム、100…ECU、200…エンジン、CB…シリンダブロック、201…気筒、212…吸気ポートインジェクタ、219…排気管、220…三元触媒、221…空燃比センサ、222…O2センサ。 10 ... engine system, 100 ... ECU, 200 ... engine, CB ... Cylinder block, 201 ... cylinder, 212 ... intake port injector, 219 ... exhaust pipe, 220 ... three-way catalyst, 221 ... air-fuel ratio sensor, 222 ... O 2 sensor .
Claims (7)
前記気筒に繋がる排気経路に設置された排気浄化用の触媒と、
前記気筒に対する燃料の筒内噴射が可能な筒内噴射装置と
を備えた内燃機関を制御する、内燃機関の制御装置であって、
前記触媒に堆積する硫黄を減少させる場合において、前記気筒の内部における混合気の均質度が低下するように前記筒内噴射装置の噴射態様を変更する変更手段と、
前記変更された噴射態様に従って前記筒内噴射装置を制御する第1制御手段と
を具備することを特徴とする内燃機関の制御装置。 Cylinders,
An exhaust purification catalyst installed in an exhaust passage connected to the cylinder;
A control device for an internal combustion engine, comprising: an in-cylinder injection device capable of in-cylinder injection of fuel into the cylinder;
Change means for changing the injection mode of the in-cylinder injection device so as to reduce the homogeneity of the air-fuel mixture inside the cylinder when reducing sulfur accumulated in the catalyst;
A control device for an internal combustion engine, comprising: first control means for controlling the in-cylinder injection device in accordance with the changed injection mode.
ことを特徴とする請求の範囲第1項に記載の内燃機関の制御装置。 The control device for an internal combustion engine according to claim 1, wherein the changing means changes the fuel injection timing to a retard side with respect to a standard timing as the injection mode.
前記変更手段は、前記噴射態様として、前記ポート噴射の燃料噴射量と前記筒内噴射の燃料噴射量と比率である噴き分け比率を、前記筒内噴射の燃料噴射量が多くなるように変更し、
前記制御手段は、前記変更された噴き分け比率に従って前記筒内噴射装置及び前記ポート噴射装置を制御する
ことを特徴とする請求の範囲第1項又は第2項に記載の内燃機関の制御装置。 The internal combustion engine includes a port injection device capable of port injection of fuel to the cylinder,
The changing means changes, as the injection mode, an injection ratio that is a ratio of the fuel injection amount of the port injection and the fuel injection amount of the in-cylinder injection so that the fuel injection amount of the in-cylinder injection increases. ,
The control device for an internal combustion engine according to claim 1 or 2, wherein the control means controls the in-cylinder injection device and the port injection device in accordance with the changed injection ratio.
前記推定された堆積量から前記触媒を前記硫黄被毒から回復させるための水素の要求量又は要求濃度を推定する第2推定手段と
を具備し、
前記変更手段は、前記推定された要求量又は要求濃度に応じて前記噴射態様を変更する
ことを特徴とする請求の範囲第1項に記載の内燃機関の制御装置。 First estimating means for estimating the amount of sulfur deposited on the catalyst;
Second estimation means for estimating a required amount or a required concentration of hydrogen for recovering the catalyst from the sulfur poisoning from the estimated amount of deposition, and
The control device for an internal combustion engine according to claim 1, wherein the changing means changes the injection mode according to the estimated required amount or required concentration.
前記変更手段は、前記推定された要求量又は要求濃度と前記推定された生成量とに基づいて前記噴射態様を変更する期間を決定する
ことを特徴とする請求の範囲第4項に記載の内燃機関の制御装置。 Further comprising third estimating means for estimating the amount of hydrogen produced in the cylinder;
5. The internal combustion engine according to claim 4, wherein the changing unit determines a period for changing the injection mode based on the estimated required amount or concentration and the estimated generated amount. Engine control device.
前記第3推定手段は、前記特定された冷却水温に応じて前記推定される生成量を補正する
ことを特徴とする請求の範囲第5項に記載の内燃機関の制御装置。 Comprising cooling water temperature specifying means for specifying the cooling water temperature of the internal combustion engine,
The control apparatus for an internal combustion engine according to claim 5, wherein the third estimating means corrects the estimated generation amount in accordance with the specified cooling water temperature.
前記排気経路における空燃比を特定する空燃比特定手段と
を具備し、
前記変更手段は、前記特定された空燃比が理論空燃比に対して所定値以上リッチ側にあり且つ前記特定された触媒の温度が所定値未満である場合において、前記気筒の内部における均質度が低下するように前記筒内噴射装置の噴射態様を変更する
ことを特徴とする請求の範囲第1項に記載の内燃機関の制御装置。 A catalyst temperature specifying means for specifying the temperature of the catalyst;
Air-fuel ratio specifying means for specifying the air-fuel ratio in the exhaust path,
The changing means has a degree of homogeneity inside the cylinder when the specified air-fuel ratio is richer than a stoichiometric air-fuel ratio by a predetermined value or more and the temperature of the specified catalyst is less than a predetermined value. The control device for an internal combustion engine according to claim 1, wherein the injection mode of the in-cylinder injection device is changed so as to decrease.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004068624A (en) * | 2002-08-01 | 2004-03-04 | Nissan Motor Co Ltd | Exhaust gas purification apparatus and method for internal combustion engine |
| JP2005337127A (en) * | 2004-05-27 | 2005-12-08 | Toyota Motor Corp | Internal combustion engine |
| JP2006242124A (en) * | 2005-03-04 | 2006-09-14 | Toyota Motor Corp | Exhaust gas purification device for internal combustion engine |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004068624A (en) * | 2002-08-01 | 2004-03-04 | Nissan Motor Co Ltd | Exhaust gas purification apparatus and method for internal combustion engine |
| JP2005337127A (en) * | 2004-05-27 | 2005-12-08 | Toyota Motor Corp | Internal combustion engine |
| JP2006242124A (en) * | 2005-03-04 | 2006-09-14 | Toyota Motor Corp | Exhaust gas purification device for internal combustion engine |
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