Evaluating method for NO.sub.x eliminating catalyst, an evaluating apparatus therefor, and an efficiency controlling method therefor

Abstract

In order to prevent a catalyst for an internal combustion engine from experiencing decreased efficiency by deterioration after long time use of the catalyst, the decreased efficiency of the catalyst is determined, and the internal engine is controlled based on results of the determination so as to maintain high efficiency of the catalyst. The catalyst is installed in an exhaust pipe of the engine. Sensors for detecting conditions of exhaust gas both at a upstream side and a downstream side of the catalyst are provided, respectively. As for the sensor, for example, an oxygen sensor whose output varies stepwise at .lambda.=1, or a sensor whose output varies in proportion to air-fuel ratio can be used. Detected values of the sensors are taken into a control unit, catalyst efficiency and deteriorating degree of the catalyst are estimated by comparison of the detected values, and the engine is controlled so that the catalyst efficiency is maximized. A preferable exhaust gas cleaning characteristics of the catalyst can be maintained because the decreased efficiency of the catalyst is determined exactly and the engine is controlled so as to prevent the catalyst from experiencing decrease efficiency.

Description

BACKGROUND AND SUMMARY OF THE INVENTION

The present invention relates to an evaluating method for NO.sub.x eliminating catalyst provided in an exhaust gas system of internal combustion engines, an evaluating apparatus therefor, and an efficiency controlling method therefor. The above described NO.sub.x eliminating catalyst is essentially a catalyst for eliminating NO.sub.x components in exhaust gas for cleaning the exhaust gas in the exhaust gas system of the internal combustion engine.

A method for estimating efficiency decrease and deterioration of NO.sub.x eliminating catalyst has been proposed in JP-A-4-265414 (1992) wherein, taking a travelling distance of an automobile as a parameter, efficiency of NO.sub.x eliminating catalyst in the automobile is deemed to be sufficiently deteriorated when the travelling distance exceeds a designated value.

Further, a method for increasing an amount of hydrocarbon (referred to as HC hereinafter) when the HC used for a NO.sub.x eliminating catalyst is deemed to be insufficient has been proposed in JP-A-3-229914 (1991).

However, the conventional methods are unable to evaluate the catalyst correctly because they use a travelling distance as a parameter for evaluating the catalyst indirectly.

Furthermore, as to controlling the amount of HC, conventional techniques can not control the amount of HC correctly because it controls the amount of HC unrelated to the evaluating result of the catalyst deterioration.

SUMMARY OF THE INVENTION

In order to solve the above described problems, an object of the present invention is to provide a preferred evaluating method for an NO.sub.x eliminating catalyst, a preferred evaluating apparatus for an NO.sub.x eliminating catalyst, and a preferred efficiency evaluating method for an NO.sub.x eliminating catalyst.

One of features of the present invention is essentially an evaluating method of an NO.sub.x eliminating catalyst for eliminating NO.sub.x components in exhaust gas, which physical parameters of specified exhaust gas components both at an upstream side and a downstream side of the NO.sub.x eliminating catalyst are compared.

Another of the features of the present invention is essentially an evaluating apparatus for NO.sub.x eliminating catalyst comprising;

(a) a base body composed of ion conductive solid electrolyte, (b) platinum electrodes provided at both sides of the base body with the base therebetween, (c) diffused resistors covering both electrodes respectively, (d) exhaust gas inlet paths for flowing exhaust gas at an upstream side of the NO.sub.x eliminating catalyst to one of the diffused resistors and flowing exhaust gas at a downstream side of the NO.sub.x eliminating catalyst to the another of the diffused resistors respectively, (e) an output portion which supplies an output of electrical signals generated between both platinum electrodes to a postfixed evaluator.

Furthermore, still another of the features of the present invention is essentially an efficiency controlling method for NO.sub.x eliminating catalyst for an eliminating NO.sub.x components in exhaust gas, which includes the steps of evaluating the NO.sub.x eliminating catalyst first and subsequently elevating a temperature of the NO.sub.x eliminating catalyst or increasing an amount of HC.

In the above evaluating apparatus, oxygen concentration in exhaust gas downstream of the NO.sub.x eliminating catalyst increases by reducing the effect of the NO.sub.x eliminating catalyst. Therefore, efficiency and a deterioration degree of the NO.sub.x eliminating catalyst can be estimated by comparing physical parameters of specified gas components an upstream side and at a downstream side of the NO.sub.x eliminating catalyst.

These and other objects, features and advantages of the present invention will become more readily apparent from the following detailed description thereof when taken in conjunction with the accompanying drawings wherein:

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a simplified diagrammatic view showing a total system of the present invention,

FIG. 2(A) and FIG. 2(B) are graphs showing characteristics of catalyst conversion efficiency,

FIG. 3(A) and FIG. 3(B) are graphs showing characteristics of catalyst conversion efficiency,

FIG. 4(A) and FIG. 4(B) are schematic illustrations for explaining a principle of eliminating NO.sub.x by the catalyst relating to the present invention,

FIG. 5(A) and FIG. 5(B) are schematic illustrations for explaining a principle of detecting deterioration of the catalyst relating to the present invention,

FIG. 5(C) is a graph showing that signals from the oxygen sensors before the catalyst and the oxygen sensor after the catalyst have different values,

FIG. 6(A) is a schematic illustration of an apparatus for explaining a detecting method relating to the present invention,

FIGS. 6(B), 6(C), and 6(D) are graphs for explaining the detecting method shown in FIG. 6(A),

FIG. 7(A) is a flow diagram relating to the present invention,

FIG. 7(B) is a schematic graph for explaining the flow diagram shown in FIG. 7(A),

FIG. 8 is a flow diagram relating to the present invention,

FIG. 9 is a flow diagram relating to the present invention,

FIG. 10(A) is a schematic illustration for explaining another detecting method relating to the present invention,

FIGS. 10(B), 10(C), and 10(D) are graphs for explaining the detecting method shown in FIG. 10(A),

FIG. 11 is a schematic illustration of a detecting apparatus relating to the present invention,

FIG. 12 is a flow diagram for controlling the detecting apparatus shown in FIG. 11,

FIG. 13 is a schematic illustration of another detecting apparatus relating to the present invention,

FIG. 14 is a flow diagram for controlling the detecting apparatus shown in FIG. 13,

FIG. 15(A) and FIG. 15(B) are schematic illustrations for explaining another detecting method relating to the present invention,

FIG. 16(A) is a cross section of a detecting sensor used in the detecting method shown in FIG. 15(A),

FIGS. 16(B) and 16(C) are graphs for indicating characteristics of the detecting sensor shown in FIG. 16(A),

FIG. 17 is a flow diagram for control in the detecting method shown in FIG. 15(A),

FIG. 18 is a schematic illustration for explaining another detecting method relating to the present invention,

FIG. 19 is a schematic illustration for explaining another detecting method relating to the present invention,

FIG. 20 is a schematic illustration for explaining another detecting method relating to the present invention,

FIG. 21 is a simplified diagrammatic view showing a total system of another embodiment of the present invention,

FIG. 22 is a simplified diagrammatic view showing a total system of another embodiment of the present invention,

FIG. 23 is a flow diagram for control in the detecting methods shown an FIG. 21 and FIG. 22,

FIG. 24 is a flow diagram for control in the detecting methods shown in FIG. 21 and FIG. 22,

FIG. 25 is a flow diagram for control in the detecting methods shown in FIG. 21 and FIG. 22,

FIG. 26(A) is a schematic illustration for explaining another detecting method relating to the present invention,

FIGS. 26(B) and 26(C) are graphs for explaining the detecting method shown in FIG. 26(A),

FIG. 27 is a flow diagram for control in the detecting method shown in FIG. 26(A),

FIG. 28(A) is a schematic illustration for explaining another detecting method relating to the present invention,

FIGS. 28(B) and 28(C) are graphs for explaining the detecting method shown in FIG. 26(A), and

FIG. 29 is a flow diagram for control in the detecting method shown in FIG. 28(A).

DETAILED DESCRIPTION OF THE DRAWINGS

A simplified diagrammatic view showing a total system of an embodiment of the present invention is illustrated in FIG. 1.

A catalyst 3 is connected to an exhaust gas pipe 2 of an engine 1. In the catalyst 3, lean NO.sub.x catalysts 4 are present for eliminating NO.sub.x under a lean air-fuel ratio condition, and a three way catalyst or an oxide catalyst 5 for eliminating NO.sub.x, CO, and HC under a theoretical air-fuel ratio condition is present. The catalyst 3 is composed in a manner so as to switch between the above two kinds of catalysts by switching valves 6 depending on an operating condition of the engine. As for the lean NO.sub.x catalyst, a copper-zeolite catalyst containing metals, for example, can be used. However, the above exemplified catalyst generally has such a characteristics that the catalyst deteriorates under a high temperature or a rich air-fuel ratio condition. Therefore, bypassing the lean NO.sub.x catalyst is preferable in some cases, for example, when in a power driving condition, in a warming up condition at starting, and so on, by way of the switching valves 6. Under a lean operation condition, the switching valves 6 are closed so as to supply exhaust gas to the lean NO.sub.x catalyst. On the other hand, under a rich air-fuel mixture condition such as a power driving condition and a warming up condition at starting, the switching valves 6 are opened so as to supply the exhaust gas to the three way catalyst or the oxide catalyst provided at a downstream side. In order to determine NO.sub.x conversion efficiency of the lean NO.sub.x catalyst, sensors 7, 8, for detecting the exhaust gas conditions are provided at, for instance, before and after the catalyst 3. As for the sensors 7, 8, for example, an oxygen sensor of which output changes stepwise by an excess air factor .lambda.=1, and an air-fuel ratio sensor of which output changes proportionally to the excess air factor can be employed. Detected values at the above two sensors are taken into a control unit 9, and the conversion efficiency or a deteriorating degree of the catalyst is determined by comparing the values. Air taken through an air cleaner 10 is flowed into a collector 14, after the amount of air is measured by an air sensor 11, via a throttle 13 which is driven by an electric motor 12. Subsequently, the air passes through an independent intake pipe 15 and is taken into the engine 1. At an intake port portion 16, a bypassing path 17 and a dividing valve 18 for generating swirls are provided. In a lean operating region, it is necessary to form swirls in a combustion chamber for improving combustion. Accordingly, in the above case, the dividing valve 18 is closed so that the air flows through the bypassing path 17. Drift is caused in the air, and consequently, swirls are generated in the combustion chamber. Fuel is supplied through a fuel injector 19. The air-fuel mixed gas is ignited by an ignition plug 20. A crank angle detector 21 for determining rotation of the engine shaft per an unit time is provided at a crank shaft 22.

FIG. 2(A) and FIG. 2(B) are graphs indicating characteristics of efficiency of the lean NO.sub.x catalyst to convert NO.sub.x to N.sub.2. FIG. 2(A) is a graph indicating a relationship between catalyst temperature and conversion efficiency and reveals that the catalyst has high efficiency in a certain range of temperature, and that the range of temperature of high efficiency shifts toward a higher temperature range as the catalyst deteriorates. The above described shift of maximum efficiency temperature is indicated graphically in FIG. 2(B) which reveals that the maximum efficiency temperature increases in accordance with increase of travelling distance of the automobile, that is, with increase of the deteriorating degree of the catalyst. A relationship between an amount of HC in the exhaust gas and the conversion efficiency is shown in FIG. 3(A) which indicates that there is an optimum amount of HC for obtaining maximum conversion ratio corresponding to an amount of NO.sub.x, and a higher conversion ratio can be achieved by optimizing the amount of HC. However, the optimum amount of HC for achieving the maximum conversion ratio changes depending on deterioration of the catalyst as shown in FIG. 3(B). Therefore, it is revealed that regularly determining deterioration of the catalyst and changing the amount of HC corresponding to the deterioration of the catalyst are necessary. As shown in FIG. 4(A), exhaust components, which relates to reducing reactions of NO.sub.x, at an engine side 30 of a lean NO.sub.x catalyst 4 which is installed inside of an exhaust pipe 3, are NO.sub.x, HC, and O.sub.2. In FIG. 4(B), molecules of gases are schematically illustrated. Nitrogen, non-combustion hydrocarbon, and oxygen are indicated by N, HC, and O, respectively. On a catalyst, HC reacts with oxygen to form an intermediate product (which is indicated by HCO surrounded by a dash line frame) which causes NO.sub.x to decompose to N.sub.2. Accordingly, the exhaust gas at the downstream side 31 of the catalyst contains N.sub.2, H.sub.2 O, and CO2 because of the NO.sub.x has been reduced. In this case, oxygen concentration changes before and after the catalyst as shown in FIG. 4 (B). Therefore, one detecting methods of a change in the conversion ratio of the NO.sub.x, is to detect oxygen concentration before and after the lean NO.sub.x catalyst.

A principle of detecting oxygen concentration is illustrated in FIGS. 5(A), 5(B), and 5(C). Referring to FIG. 5(A), sensors 7, 8, for detecting oxygen concentration are installed before and after the catalyst, respectively. The sensor 7 for detecting oxygen concentration is composed of platinum electrodes 33a, 33b, which are attached at both sides of a zirconia solid electrolyte 32 respectively. A diffused resistor 34 which regulates gas diffusion is formed on an exhaust gas side of the electrode 33a attached at the exhaust gas side of the electrolyte. The sensor 7 is connected to a casing such as an exhaust pipe 3 and the electrode 33a to a ground. In this case, when a specified voltage is applied to another electrode, generated electric current becomes proportional to oxygen concentration at the exhaust gas side. That is the oxygen concentration can be determined by measuring a value of the electric current. Composition and operation of the sensor 8 is the same as that of the sensor 7.

Components of exhaust gas are schematically illustrated in FIG. 5(B). Before reactions at the catalyst, nitrogen, HC, and oxygen coexist as shown in (a). However, HC is almost completely oxidized by a catalytic reaction of platinum on the electrode 33a of the sensor 7. Therefore, detected oxygen concentration is less by as much as an amount consumed for the oxidation reaction as shown in (b) as the amount surrounded by one dot chain line in a rectangular frame. Further, because the HC is almost completely reacted and oxygen is generated by decomposition of NO.sub.x by a reducing reaction downstream side of the catalyst 4, oxygen concentration detected at the downstream side of the catalyst 4 increases as shown in (c) more than that of the (b) condition as the amount surrounded by one dot chain line in a rectangular frame. Accordingly, as a comparison of the amounts of oxygen indicated by rectangular frames in (b) and (c) reveals, detected oxygen concentration before and after the catalyst 4 differ from each other. Therefore, signals from the oxygen sensors before the catalyst and the oxygen sensor after the catalyst indicate different values from each other as shown in FIG. 5(C).

A principle of detecting deterioration or conversion ratio is illustrated in FIGS. 6(A), 6(B), 6(C), and 6(D). A specified voltage is applied to the electrode 33b of the sensors 7, 8. At that time, voltage drops V1, V2 of electric current flowing through fixed resistors R1, R2 are detected by differential amplifiers 36, 37. These V1, V2 drops are values of electric current flown through the solid electrolyte 32 of respective sensors 7, 8, that is, detected oxygen concentration. Further, a difference of the V1 and V2 values is detected again by a differential amplifier 39. The difference (V1-V2) is a value related to deterioration. The above described sensor changes its output depending on oxygen concentration as indicated in FIG. 6(B), and accordingly, a difference of oxygen concentration before and after the catalyst 4 can be detected. The difference of output voltages are shown in FIGS. 6(C) and 6(D). The V2 value is higher than the V1 value by as much as a difference of oxygen concentration. The output V1 of the sensor 7 before the catalyst can be used concurrently for controlling the air-fuel ratio. Naturally, the output V2 of the sensor 8 after the catalyst also can be used concurrently for controlling air-fuel ratio.

In the present embodiment, the difference of V1 and V2 values is detected by a differential amplifier, but the difference can be obtained by taking V1, V2 into a microcomputer after conversing by an analog-digital convertor and calculating the difference by a calculating process as explained hereinafter.

First, a flow chart for controlling air-fuel ratio is shown in FIG. 7(A). The V1 value measured at step 100, and a target output V.sub.ref of the sensor corresponding to a target air-fuel ratio (A/F) as shown in FIG. 7(B) is retrieved from a map of engine rotation N and load at step 110. The V1 value is compared with the V.sub.ref value at step 120. If V1 is larger than V.sub.ref, the air-fuel ratio at the time is judged as in a leaner side than the target air-fuel ratio, and an amount of injected fuel Ti is increased at step 130 so as to shift the air-fuel ratio to a rich side. If V1 is smaller, the air-fuel ratio at the time is judged as richer than the target air-fuel ratio, and an amount of injected fuel Ti is decreased at step 140 so as to shift the air-fuel ratio to a lean side. As described above, an appropriate amount of injected fuel T is determined and output to a fuel injection valve 19 at step 150. In a manner as described above, controlling of air-fuel ratio can be realized by using sensors for detecting conversion ratio or deterioration.

Next, a flow chart for detecting deterioration of catalyst is shown in FIG. 8. At step 210, V1 and V2 are measured and a difference of V1 and V2 is calculated. If the difference is smaller than a specified value at step 220, an oxygen increase by a reducing reaction of N.sub.2 by the catalyst is judged to be small at step 230 and the catalyst is estimated to be deteriorated. That is, the catalyst is judged to be deteriorated and a deterioration degree is indicated. The larger difference of oxygen concentration before and after the catalyst, that is, a larger difference between V1 and V2 means a stronger reducing reaction of the catalyst and indicates that the catalyst is not deteriorated yet.

A deterioration judging method improved in accuracy is indicated in FIG. 9. The difference between V1 and V2 is calculated at step 300, and a judgment is made as to whether the catalyst temperature Tc or exhaust gas temperature is in a specified range or not at step 310. Because the conversion ratio of the catalyst varies depending on temperature as shown in FIG. 2(A), there may be a possibility to erroneously judge the catalyst to be deteriorated when the catalyst temperature changes. Therefore, the deterioration judgment of the catalyst is performed only at the time when the catalyst temperature exists in a specified range. Furthermore, the above described method is effective in a point that temperature dependency of sensor characteristics can be ignored. The deterioration judgment on the catalyst after the catalyst temperature is confirmed to be in a specified range is performed by the same steps as shown in FIG. 8. That is, when a difference between V2 and V1 obtained at step 320 is lower than a reference value, the catalyst is judged as deteriorated at step 330, and a deteriorating degree corresponding to the difference between V2 and V1 is indicated at step 340.

Next, another detecting method is shown in FIGS. 10(A), 10(B), 10(C), and 10(D). A sensor used in the present method is an oxygen sensor having a non-linear output characteristics corresponding to oxygen concentration (air-fuel ratio) as shown in FIG. 10(B). In using such a sensor as above described, a simple diffused film 42 is sufficient as the diffused film provided at surface of an electrode 40a in an exhaust gas side of the each sensor 7, 8. In other words, a thinner diffused film than the diffused film 34 shown in FIG. 5 can be used in the apparatus shown in FIG. 10(A) which uses oxygen sensors having two values type output. With the above sensor, the electrode 40a at the exhaust gas side is connected to a ground, and voltages (electromotive force) V1, V2 generated at the other electrode 40b are measured. Based on the difference between the voltages of the two sensors, the deteriorating degree is detected. That is, V1 and V2 are measured when the exhaust gas is leaner than a theoretical air-fuel ratio, and the difference between the outputs is determined by a differential amplifier 44. However, the difference can be calculated from the outputs in a microcomputer as previously explained. Based on the difference, a deteriorating degree of the catalyst is estimated. Examples of the outputs, V1, V2, are illustrated in FIGS. 10(C) and 10(D). The output after the catalyst, V2, has less value than the output before the catalyst as shown in FIGS. 10(D) and 10(C), respectively, because the exhaust gas after the catalyst contains relatively more oxygen than the exhaust gas before the catalyst. The difference between V1 and V2 becomes an index indicating the deteriorating degree of the catalyst.

In another embodiment of the present invention is shown in FIG. 11, a prefixed catalyst 53 and a postfixed catalyst 54 in a downstream side are arranged in series, and three sensors, 50, 51, 52 are installed. Efficiency and a deteriorating degree of the prefixed catalyst 53 are determined by the method explained in the previous embodiment using the sensors 50, 51. Efficiency and a deteriorating degree of the postfixed catalyst 54 are determined by the method explained in the previous embodiment using the sensors 51, 52, or sensors, 50, 52. In accordance with the above described arrangement, deterioration diagnosis of a complex catalyst system becomes possible. As for the catalyst, a NO.sub.x reducing catalyst is used for the prefixed catalyst 53 and a three way catalyst or an oxidizing catalyst is used for the postfixed catalyst 54. In this embodiment, a deteriorating degree of the NO.sub.x reducing catalyst 53 is determined by comparing detected outputs of the sensors 50 and 51 as previously explained. A deteriorating degree of the postfixed catalyst 54 can be determined using signals from the sensors 51 and 52, or sensors 50 and 52. The signals from the sensors 50, 51, 52 are fed into a microcomputer 9, and are processed for calculation. A controlling flow chart in this case is shown in FIG. 12.

The NO.sub.x reducing catalyst 53 is effective as a NO.sub.x eliminating catalyst in a lean operating region, and accordingly, judging first whether the catalyst is within the lean operating region occurs at step 400. When the catalyst is judged as within the lean operating region, a diagnosis mode starts. That is, signals V1, V2 from the sensors 50, 51 before and after the catalyst 53 respectively are determined at step 410, and the diagnosis of deterioration is performed at step 420. For this diagnosis, the flow charts shown in FIGS. 8 and 9 are used. Subsequently, a deteriorating degree of the catalyst is indicated at step 430.

In a case of the postfixed catalyst, a deteriorating degree is judged when the catalyst is within an operating region with an excess air factor .lambda.=1 at step 440. Signals V1, V3 from the sensors 50, 52 in the above described operating region are determined at step 450, and the diagnosis of deterioration is performed at step 460 based on the above signals. In this case, the deterioration of the catalyst can also be judged by measuring outputs V2, V3 from the sensors 51, 52 in a same manner.

As explained above, diagnosis of efficiency or deterioration of a complex catalysis system using a plurality of catalysts can be performed preferably when each of the catalysts is within an operation region.

Still another embodiment of the present invention is illustrated in FIG. 13 where a plurality of catalysts are arranged in parallel. Catalysts 55, 56 are arranged in parallel, and a catalyst to which exhaust gas is flows is selectively alterable depending on its operating condition by switching valves 57A, 57B driven by an actuator 58 which is operated by loads or electric power. For instance, when the switching valve 57A is open so as to flow the exhaust gas to the catalyst 56, the switching valve 57B is closed so as not to flow the exhaust gas to the catalyst 55. In this situation, efficiency or deterioration of the catalyst 56 must be judged based on signals from the sensors 58, 59 when the operating condition is such that the catalyst 56 must work. When the switching valves 57A, 57B are rotated so as to flow the exhaust gas to the catalyst 55, the exhaust gas flow to the catalyst 56 is stopped. In this case, efficiency or deterioration of the catalyst 55 must be judged based on signals from the sensors 58, 59 when the operating condition is such that the catalyst 55 must work. Operation of the actuator 58, intake of signals from the sensors 58, 59, and processing are performed by a microcomputer 9.

A flow chart for the above processing steps is shown in FIG. 14. A situation in which one of the catalysts shown in FIG. 13 is a NO.sub.x reducing catalyst, and another catalyst is a three way catalyst or an oxidizing catalyst is explained hereinafter. First, the operating condition is judged as to whether it is or is not within a lean operating region or not at step 500. When the operating condition is within the lean operating region, the switching valve 57A is operated so as to supply exhaust gas to the NO.sub.x reducing catalyst at step 510. Subsequently, after the operating condition is adequately established, signals from the sensors 58, 59 are measured at step 520, diagnosis of deterioration is performed on the NO.sub.x reducing catalyst at step 530, and results of the diagnosis are indicated at step 540. When the operating condition is outside the lean operating region, the switching valve 57A is closed and the switching valve 57B is opened so as to flow the exhaust gas to the three way catalyst at step 550. Subsequently, the operating condition is judged as to whether it is or is not as a theoretical air-fuel ratio .lambda.=1 at step 560. When .lambda.=1, signals from the sensors 58, 59 are measured at step 570, diagnosis of deterioration is performed on the three way catalyst at step 580, and results of the diagnosis are indicated at step 540.

In the present embodiment of FIG. 15(A), a sensor 61 is so composed that the exhaust gas at upstream side of the catalyst 60 is supplied to one plane of the sensor 61 and the exhaust gas at downstream side of the catalyst 60 is supplied to another plane of the sensor 61 in order to determine a difference of oxygen concentration in the exhaust gas at the upstream side and the exhaust gas at the downstream side with only one sensor. In this case, almost all exhaust gas in an exhaust pipe 3 flows to the catalyst 60. However, a small portion of the exhaust gas flows through a path 62 to a chamber 63 which is provided at one side of the sensor 61. The exhaust gas further flows through a path 64 by a sucking effect of a Venturi 65 which is provided at the upstream side of the catalyst. On the other hand, the exhaust gas after the catalyst 60 is led into an exhaust pipe side of the sensor 61. The structure of the sensor 61 is shown in FIG. 15(B) in which the exhaust gas at the upstream side of the catalyst is led to the left side of the sensor, and the exhaust gas at the downstream side of the catalyst is led to the right side of the sensor. The sensor is composed of a zirconia solid electrolyte 66 having platinum electrodes 67a, 67b at both sides, and porous protecting films 68a, 68b are provided outside each of the electrodes. Both sides of the solid electrolyte 66 have catalytic effects and can oxidize HC. In accordance with the structure, the solid electrolyte 66 can determine residual oxygen concentration after the above oxidation. In this case, the solid electrolyte, which is a kind of oxygen concentration cell, is preferable because only a difference of oxygen concentrations between the concentration at one side and at the other side of the solid electrolyte is required. Furthermore, if the electrode 67b at one side is connected to ground, an electric potential measured at the other electrode 67a indicates the difference of oxygen concentration. The measured electric potential is fed into a microcomputer 9 and is processed.

More detailed structure of the sensor 61 is provided in FIG. 16(A). The sensor is arranged in a protecting tube 70. The electrode 67b at the downstream side of the exhaust gas from the catalyst is connected to ground by the protecting tube 70 through a wire printed on an insulator 71. The other electrode 67a at the upstream side of the exhaust gas to the catalyst is led to the outside through a connector portion 69. The sensor body itself is screwed and fixed at the exhaust pipe 72. The exhaust gas before and after the catalyst can be introduced to each of the sides of the sensor. The sensor, a kind of oxygen concentration cell, has a characteristics shown in FIG. 16(B) depending on the difference of oxygen concentrations between each side of the sensor. During a period when the catalyst is not deteriorated, oxygen concentration in the downstream of the exhaust gas from the catalyst is large because oxygen in NO.sub.x is reduced to oxygen molecules as shown in FIG. 5. When the difference of oxygen concentration between those at each side of the sensor is large, an output voltage of the sensor is low as shown by a point (a) in FIG. 16(B). On the contrary, when the difference of oxygen concentration between each side of the sensor is small, the output of the sensor increases because of higher electromotive force in the solid electrolyte 66 as shown by a point (b) in FIG. 16(B). Accordingly, the output from the sensor increases with elapsing time as shown in FIG. 16(C). Therefore, deterioration of the catalyst can be detected by measuring the output of the sensor. As described above, when the deterioration of the catalyst is detected by only one sensor, accuracy of the detection can be improved because temperatures of detecting sides of the sensor are identical and temperature dependency of the sensor can be eliminated.

A flow chart for detecting catalyst deterioration is shown in FIG. 17. First, the operating condition is judged as to whether it is within or not within a lean operating region at step 600. When the operating condition is within the lean operating region, further, the exhaust gas temperature Tg is judged as to whether it is within or not within a specified range at step 610. When the temperature is within the specified range, the sensor is activated, and temperature dependency of the catalyst can be eliminated. As described above, no heater for the sensor is necessary by choosing the temperature range necessary for sensor activation as for the specified temperature range. Subsequently, an output from the sensor is measured at step 620, and a deterioration degree is judged at step 630. This judgment can be performed only by judging whether the output from the sensor is over or below a reference value. A deteriorating degree is judged and indicated at step 640.

In the embodiment shown in FIG. 18 during a lean operating condition, exhaust gas flows into a NO.sub.x reducing catalyst 4 by closing a switching valve 6, and subsequently the exhaust gas flows into a three way catalyst 5 which is located at the downstream side. The switching valve 6 is made in a manner to leak a small amount of gas so that the exhaust gas at the upstream side flows into both a sensor 73 of the type shown in FIG. 16(A) and a catalyst 4. The exhaust gas at the downstream side of the catalyst 4 flows through another side of the sensor 73. Signals from the sensor are fed into a microcomputer 9 and processed. When the switching valve 6 is opened, the exhaust gas does not flow into the NO.sub.x reducing catalyst 4, but flows only into the three way catalyst 5.

In the embodiment shown in FIG. 19, a sensor 73 as shown in FIG. 16(A) is arranged at the upstream side of a switching valve 6. The switching valve 6 is operated by a driving apparatus 74 which is controlled by signals from a microcomputer 9. Exhaust gas before and after a catalyst 4 is introduced into the sensor 73. The switching valve is arranged at the downstream side of the sensor 73 so that the exhaust gas at the downstream side of the catalyst 4 does not flow into a side of the sensor 73 for the exhaust gas at the upstream side of the catalyst 4.

In the embodiment shown in FIG. 20 during a lean operating condition, a switching valve 75 is opened so that exhaust gas flows into a NO.sub.x reducing catalyst 4. Exhaust gas at the downstream side of the catalyst 4 flows to a side of a sensor 78 for the exhaust gas at the downstream side of the catalyst 4. However, because a small amount of gas leaks through the switching valve 75 to an exhaust pipe 76, the exhaust gas at upstream side of the catalyst 4 flows to a side of a sensor 78 for the exhaust gas at the upstream side of the catalyst 4. Under an operating condition other than the lean operating condition, the switching valve 75 is switched in a manner as shown by a dotted line in FIG. 20 so that the exhaust gas flows to an exhaust pipe 76. A three way catalyst 5 is arranged in the exhaust pipe 76. In accordance with the structure described above, deterioration of the catalyst can be detected by only a sensor.

Next, an embodiment of the present invention relating to an engine controlling method for detecting deterioration of catalyst and efficiency of the engine, and subsequently for improving the is described.

FIG. 21 is a simplified diagrammatic view of a total or overall system used for the above engine controlling method. Sensors 7, 8 are provided before and after a catalyst 4. A sensor 80 for detecting gas temperature is provided at an exhaust pipe. It is necessary to control catalyst temperature and HC concentration so as to obtain maximum efficiency of the catalyst as shown in FIG. 2 after judging deterioration of the catalyst based on outputs from the sensors 7, 8.

One of the methods for controlling the catalyst temperature is a method for regulating circulation of cooling water 86 in engine 1. When a circulating amount of the cooling water is decreased by regulating a control valve 87, combustion temperature of the engine 1 is elevated and, accordingly, exhaust gas temperature is also elevated. That is, when the catalyst is judged as deteriorated, the circulating amount of cooling water is regulated to elevate the exhaust gas temperature so as to prevent lowering the efficiency of the catalyst. Another method for controlling temperature is a method for regulating ignition timing of an ignition apparatus 84 and an ignition plug 20. Delayed ignition timing elevates the exhaust gas temperature. That means, when the catalyst is deteriorated, the ignition timing is delayed to elevate the exhaust gas temperature so as to prevent lowering the efficiency of the catalyst. Further, because the required amount of HC changes depending on deterioration of the catalyst, the amount of HC must be increased when the catalyst is deteriorated.

An exhausted amount of HC changes in accordance with change of fuel injection timing of an injection valve 19. Therefore, when the catalyst is deteriorated, a setting of fuel injection timing is changed by a controller 9. Further, when the injection valve 19 is an air assist injection valve which atomizes fuel by a jet stream, an exhausted amount of HC increases by reducing or stopping of the air assist because fuel atomization becomes incomplete. When a flow dividing valve 18 is closed so that intake gas flows through a swirl path 17, swirling currents are generated in a combustion chamber and combustion is improved. Therefore, on the contrary, an amount of air flow through paths other than the swirl path is increased by half opening the flow dividing valve 18, and combustion of fuel becomes incomplete. Accordingly, an exhausted amount of HC is increased. Furthermore, cooling of the engine by increasing the circulating amount of cooling water increases the exhausted amount of HC. Further, advanced ignition timing increases the exhausted amount of HC. Therefore, when the catalyst is deteriorated, the ignition timing may be advanced depending on a deteriorating degree of the catalyst. On the contrary, the catalyst temperature and the exhausted amount of HC can be increased by operation at the exhausted gas side. Vaporized fuel components stored at upper inside portion of a fuel tank 82 are pumped inside the exhaust pipe at the upstream side of the catalyst. As the vaporized fuel components are HC, the efficiency of the catalyst can be improved by supplying the vaporized fuel components to the catalyst. Furthermore, the vaporized fuel components are combustible easily because they are light HC, and the catalyst temperature is elevated by combustion of the vaporized fuel components.

Another method for elevating the catalyst temperature uses an electric heater 88 for heating the catalyst. A driving circuit 81 supplies power to the heater 88 in accordance with signals from the controller 9. The heater elevates the catalyst temperature, and the efficiency of the catalyst is improved. The heater can be one in which carriers of the catalyst are made from conductive materials and power is supplied to the carrier.

Another method for altering the catalyst temperature is indicated in FIG. 22. In this method, a structure wherein a burner is installed inside the exhaust pipe 3 is adopted, and sparks are formed by an ignition plug 91 to which electric voltage is supplied from a driving circuit 81 for ignition apparatus. Fuel is injected into the burner 93 from a fuel injector 92. Air is supplied to the burner 93 by a pump 94. The fuel injected into a chamber 93 is ignited by the ignition plug 91, and flame is formed inside of the exhaust pipe before the catalyst. The flame increases catalyst temperature. A structure having an electric heater 88 is also indicated in FIG. 22. The heater 88 is so composed as to wrap outside of the catalyst 4 in order to heat the catalyst effectively. Further, each of the above described methods can be used in a combined manner or independently. That is, any of the above described methods can operate independently.

A flow chart for control is shown in FIG. 23. When deterioration of catalyst is detected at step 710, a judgment whether any changing in an amount of HC is necessary or not is performed based on the deteriorating degree of the catalyst at step 720. When the change in the amount of HC is judged as necessary, an amount of HC to be changed is determined depending on the deteriorating degree of the catalyst at step 730. Subsequently, an amount of HC supply to the catalyst is changed by any one or any combination of HC increasing or decreasing apparatus shown in FIGS. 21 and 22 at step 740. Generally speaking, a NO.sub.x reducing catalyst is deteriorated, the HC supply to the catalyst must be increased for ensuring its efficiency. Further, when deterioration of the catalyst is detected at step 710, its deteriorating degree is indicated at step 750.

A flow chart for changing catalyst temperature is shown in FIG. 24. When deterioration of the catalyst is detected at step 800, its deteriorating degree is indicated, and a judgment as to whether any change in an operating temperature of the catalyst is necessary or not is performed. When the changing is judged as necessary, a necessary changing degree of the operating temperature is decided at step 820, and the catalyst temperature is changed by any one or any combination of temperature changing apparatus shown in FIGS. 21 and 22 at step 830. Subsequently, the catalyst temperature is judged as to whether it has attained a designated temperature or not, and when it is judged as having attained the designated temperature, the flow of processing is finished.

A flow chart for controlling operating conditions so as to always maintain the maximum conversion efficiency of catalyst is shown in FIG. 25. First, the present operating condition is judged as to whether it is or is not within a lean operating region at step 900, and when it is within the lean operating region, it is judged as to whether it is or is not in a normal operation. When it is in the normal operation within the lean operation region, signals from sensors for measuring efficiency of the catalyst are taken at step 920, and the conversion efficiency of the catalyst is estimated at step 930. When the conversion efficiency of the catalyst is judged as lower than a designated value at step 940, parameters such as catalyst temperature and the supplied amount of HC are changed by controlling an efficiency changing apparatus at step 950. Subsequently, the conversion efficiency of the catalyst is judged as to whether it is or is not improved or not. When it is judged as being improved, the flow of processing is finished in keeping with the changed parameters, and when it is judged as being not improved, the flow of the processing is finished after returning the parameters to the values before changing at the step 970. In accordance with the above described method, an engine can be operated always in a condition with preferable conversion efficiency.

Another method for detecting efficiency and deteriorating degree is shown in FIGS. 26(A), 26(B), and 26(C). In this method, fluctuation width .DELTA.V of output signals from sensors 7, 8 before and after catalyst 4 as shown in FIG. 26(A) are compared with each other. When oxygen concentration upstream of the catalyst 4 is fluctuating, the state of the fluctuation can be determined by the fluctuation width .DELTA.V1 of output signal from sensor 7 as shown in FIGS. 26(B) and 26(C). While the catalyst is new, oxygen concentration downstream from the catalyst 4 fluctuates significantly because of its active reactivity for NO.sub.x reducing reaction. However, as the catalyst deteriorates, its reactivity for NO.sub.x reducing reaction decreases and the fluctuation of the oxygen concentration decreases. Therefore, the fluctuation width .DELTA.V2 of output signal from sensor 8 downstream of the catalyst 4 decreases. Accordingly, a deteriorating degree of the catalyst can be determined by measuring the change of the fluctuation width. A flow chart for detecting the deteriorating degree is shown in FIG. 27. Operating condition is judged at step 1000 as to whether it is or is not within a lean operation region, and when the operating condition is judged as within the lean operating region and the catalyst is in a designated temperature range at step 1010, .DELTA.V1 and .DELTA.V2 are detected and calculated at step 1020. Subsequently, .DELTA.V2/.DELTA.V1 is calculated at step 1030. Next, the .DELTA.V2/.DELTA.V1 is judged as to whether it is or is not smaller than a designated value. When it is smaller, efficiency of the catalyst is judged as decreased at step 1040, the deteriorating degree is indicated at step 1050, and an efficiency improving apparatus starts its operation at step 1060. When only judging the efficiency of the catalyst is required, starting and controlling the efficiency improving apparatus can be omitted.

Furthermore, another method for detecting efficiency and deteriorating degree is indicated in FIGS. 28(A), 28(B), and 28(C). Referring to FIG. 28(A), an air-fuel mixture ratio which is supplied to an engine 1 is altered intentionally by changing the injected amount of fuel and throttle opening of a fuel injecting valve 19, and the deteriorating degree of the catalyst is determined based on the difference in behavior of signals from the sensors 7, 8, which are located at the upstream side and the downstream side of the catalyst 4, respectively. As shown in FIG. 28(B), when the air-fuel ratio is altered stepwise, outputs from the sensors 7, 8 also change stepwise. However, when the catalyst is deteriorated, a difference in responses from the respective sensors 7, 8 located at the upstream side and the downstream side of the catalyst changes from the difference when the catalyst is not deteriorated. For instance, the behavior of sensors which have linear outputs corresponding to the air-fuel ratio are indicated by solid lines in FIG. 28(B), in which the difference in time constant .tau. of the response increases when the catalyst is deteriorated. Behavior of regular oxygen sensor outputs are also indicated by dashed lines, in which the difference in time constant .tau. of the response increases similarly when the catalyst is deteriorated. In FIG. 28(C), a situation when the air-fuel ratio of the mixture at supply side is altered randomly or in accordance with a rule is indicated. The deteriorating degree is determined by correlation between changes in signals from the sensors 7, 8. When the signal from the sensor 8 is remarkable more dull than that from the sensor 7, the catalyst can be regarded as deteriorated. A flow chart for determining the deterioration of the catalyst by the present method is indicated in FIG. 29. After the operating condition is judged at step 1100 as within a lean operating region and in a normal operation, catalyst temperature is judged as to whether it is or is not in a designated temperature range at step 1110. Subsequently, after satisfying the step 1110, air-fuel ratio of mixture supplied to the engine is altered at step 1120. Next, the deteriorating degree of the catalyst is determined by the method indicated in FIGS. 28(A), 28(B), and 28(C) based on the difference of behavior in time constant .tau. of the response signal V1, V2 from the sensors before and after the catalyst at step 1130. When it is judged as deteriorated in step 1140, the deteriorating degree is indicated at step 1150, and, subsequently, operation of the efficiency improving apparatus shown in FIGS. 21 and 22 is started at step 1160.

In accordance with the present invention, it becomes possible accurately to detect decrease in catalyst efficiency on account of long period operation. Furthermore, an engine can be controlled so as to avoid decreasing the catalyst efficiency, and a preferable exhaust gas cleaning characteristics can be maintained.

Although the invention has been described and illustrated in detail, it is to be clearly understood that the same is by way of illustration and example, and is not to be taken by way of limitation. The spirit and scope of the present invention are to be limited only by the terms of the appended claims.

Claims

1. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining oxygen concentration upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition, and

evaluating said catalyst by comparing a difference of the determined oxygen concentration upstream and downstream of said catalyst via the sensor.

2. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining concentration of at least one engine exhaust gas component upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition, and

evaluating said catalyst based on a difference in at least one physical parameter of the at least one exhaust gas component concentration upstream and downstream of said catalyst.

3. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining oxygen concentration upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition,

evaluating said catalyst based on a difference of

oxygen concentration determined by the sensor in exhaust gas upstream of said catalyst and

oxygen concentration determined by the sensor in exhaust gas downstream of said NO.sub.x eliminating catalyst which is changed by effects of said catalyst.

4. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining concentration of at least one exhaust gas component upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition in a steady state, and

evaluating said catalyst based on a difference of at least one physical parameter of the at least one exhaust gas component upstream and downstream of said catalyst.

5. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining oxygen concentration upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition, and

evaluating said catalyst based on differences of the determined oxygen concentration upstream and downstream of said catalyst.

6. An evaluating method for determining deterioration of a lean NO.sub.x catalyst installed in an exhaust gas system of an internal combustion engine for reducing NO.sub.x under a lean air-to-fuel ratio condition, comprising the steps of determining oxygen concentration upstream and downstream of the catalyst with a sensor when the engine is operated under the lean air-to-fuel ratio condition, and

evaluating said catalyst based on differences of the fluctuation width of an output signal of the sensor.