US20030051468A1 - Method and apparatus for determining whether a sensor which is responsive to both a reactant and a substance to be reduced by such reactant is responding to either un-reacted portions of the substance or un-reacted portions of the reactant - Google Patents

Method and apparatus for determining whether a sensor which is responsive to both a reactant and a substance to be reduced by such reactant is responding to either un-reacted portions of the substance or un-reacted portions of the reactant Download PDF

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US20030051468A1
US20030051468A1 US10/101,892 US10189202A US2003051468A1 US 20030051468 A1 US20030051468 A1 US 20030051468A1 US 10189202 A US10189202 A US 10189202A US 2003051468 A1 US2003051468 A1 US 2003051468A1
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reactant
substance
sensor
nox
output signal
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US10/101,892
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Michiel Van Nieuwstadt
Richard Soltis
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Ford Global Technologies LLC
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Ford Global Technologies LLC
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Assigned to FORD MOTOR COMPANY, A DELAWARE CORPORATION reassignment FORD MOTOR COMPANY, A DELAWARE CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: SOLTIS, RICHARD E., VAN NIEUWSTADT, MICHIEL J.
Assigned to FORD GLOBAL TECHNOLOGIES, INC. reassignment FORD GLOBAL TECHNOLOGIES, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: FORD MOTOR COMPANY
Priority to GB0218373A priority patent/GB2382657A/en
Publication of US20030051468A1 publication Critical patent/US20030051468A1/en
Assigned to FORD GLOBAL TECHNOLOGIES, LLC reassignment FORD GLOBAL TECHNOLOGIES, LLC MERGER (SEE DOCUMENT FOR DETAILS). Assignors: FORD GLOBAL TECHNOLOGIES, INC.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9495Controlling the catalytic process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/90Injecting reactants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N11/00Monitoring or diagnostic devices for exhaust-gas treatment apparatus, e.g. for catalytic activity
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust 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
    • F01N3/18Exhaust 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 characterised by methods of operation; Control
    • F01N3/20Exhaust 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 characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/146Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/146Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration
    • F02D41/1461Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration of the exhaust gases emitted by the engine
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D41/146Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration
    • F02D41/1463Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an NOx content or concentration of the exhaust gases downstream of exhaust gas treatment apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/22Safety or indicating devices for abnormal conditions
    • F02D41/221Safety or indicating devices for abnormal conditions relating to the failure of actuators or electrically driven elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2550/00Monitoring or diagnosing the deterioration of exhaust systems
    • F01N2550/02Catalytic activity of catalytic converters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2550/00Monitoring or diagnosing the deterioration of exhaust systems
    • F01N2550/05Systems for adding substances into exhaust
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/02Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
    • F01N2560/021Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting ammonia NH3
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/02Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
    • F01N2560/026Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting NOx
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/02Adding substances to exhaust gases the substance being ammonia or urea
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D41/00Electrical control of supply of combustible mixture or its constituents
    • F02D41/02Circuit arrangements for generating control signals
    • F02D41/14Introducing closed-loop corrections
    • F02D41/1438Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor
    • F02D41/1444Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases
    • F02D2041/1468Introducing closed-loop corrections using means for determining characteristics of the combustion gases; Sensors therefor characterised by the characteristics of the combustion gases the characteristics being an ammonia content or concentration of the exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D2250/00Engine control related to specific problems or objectives
    • F02D2250/36Control for minimising NOx emissions
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/10Capture or disposal of greenhouse gases of nitrous oxide (N2O)
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/40Engine management systems

Definitions

  • This invention relates generally to methods and apparatus for determining whether a sensor which is responsive to both a reactant and a substance to be reduced by such reactant is responding to either un-reacted portions of the substance or un-reacted portions of the reactant. More particularly the invention relates to methods and apparatus for detecting NOx to be reduced with urea using a sensor which is responsive to un-reacted portions of the NOx and un-reacted portions of the urea.
  • the system may improperly reduce injected urea since the system believes excess urea is being produced and thus less urea is necessary. This can result in increased NOx emission.
  • a method wherein a reactant is added into a substance to react with the substance.
  • the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor.
  • the sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant.
  • the method includes changing at least one of the amount of reactant added to the substance and the amount of the substance.
  • a determination is made from said at least one of the change in the amount of reactant and the change in the amount of the substance, and from the change in the output signal, whether the sensor is responding to the substance or to the reactant.
  • a method wherein a reactant is added to a substance to react with such substance.
  • the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor.
  • the sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant.
  • the method includes changing the amount of reactant added to the substance and determining from the response of the sensor to such change in the amount of reactant whether the output signal is responding to the substance or to the reactant.
  • a sensing system wherein a sensor is provided for producing an output signal in response to either a first substance of a reaction or to a second substance of the reaction.
  • the system includes: an injector for changing the level of one of the substances in the reaction; and a processor responsive to the output signal and a signal representative of the change in level of one of the substances, for determining whether the sensor is responding to the first substance or to the second substance.
  • the sensing system is a NOx sensing system.
  • a NOx sensing system includes: a NOx sensor for producing an output signal in response to NOx and urea and a processor responsive to the output signal for determining whether the sensor is responding to NOx or to urea.
  • a method wherein a reactant is added to a substance to react with such substance.
  • the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor.
  • the sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant.
  • the method includes changing the amount of reactant added to the substance, determining whether the change in the amount of reactant and the change in the output signal are in the same direction or in opposite directions, and from such determination determining whether the output signal is responding to the substance or to the reactant.
  • reactant is added to the substance. If the directions are opposite, reactant is reduced from the substance.
  • a change is made in the amount of a reactant added to a substance to be reacted and thereby reduced by, the reactant, the time history of such change in the reactant being represented by:
  • the products of the reaction, along with un-reacted portions of the reactant and the un-reacted portions of the substance are passed by a sensor.
  • the sensor is unable to effectively differentiate between the un-reacted reactant portions and the un-reacted portions of the substance. That is, the sensor produces an output signal V(t) in response to the un-reacted portions of the reactant and the un-reacted portions of the substance.
  • the change in the output signal from the change in the amount of reactant added to the substance may be represented as:
  • the change in the amount of the reactant is recorded over a period of time T.
  • the delay between the change in the amount of the reactant occurring at a time t 0 , to the time the reaction is effected by such change in the amount of reactant is a time delay, D.
  • a signal, I is produced to determine whether the output signal increases or decreases with the changed amount of reactant.
  • I ⁇ t0 t0 + D + T ⁇ ⁇ e ⁇ ⁇ x ⁇ ⁇ c ⁇ V ⁇ ⁇ ( t + D ) ⁇ u ⁇ ⁇ ( t ) ⁇ t
  • the sensor is determined to be responding to the un-reacted reactant.
  • V is much greater than 0 (i.e., V is greater than some calibratable threshold)
  • V is greater than some calibratable threshold
  • a determination may be made as to whether the sensor is responding to the un-reacted reactant, to the un-reacted substance, and whether the injector or the catalyst is faulty.
  • FIG. 1 is a diagrammatical sketch of an engine exhaust system according to the invention having a processor programmed for determining the effectiveness of injected urea in reducing NOx produced by the engine;
  • FIG. 2 is a diagram showing the relationship between an output signal produced by a sensor used in the exhaust system of FIG. 1 as a function of either nitrogen monoxide (NO), nitrogen dioxide (NO 2 ) or urea;
  • FIG. 3 is a diagram showing the output signal produced by the sensor used in the exhaust system of FIG. 1 in response to increases and decreases in the amount of urea injected into the engine exhaust in the system of FIG. 1;
  • FIG. 4 is a flow diagram of the process used by the processor in FIG. 1 to determine the effectiveness of injected urea in reducing NOx produced by the engine exhaust in the system of FIG. 1;
  • FIG. 5 is a functional block diagram of a NOx reduction system according to another embodiment of the invention.
  • FIG. 6 are diagrams showing as a result of computer simulations various parameters produced in the system of FIG. 5 for an assumed Urea to NOx ratio correction factor of +0.32;
  • FIG. 7 are diagrams showing as a result of computer simulations various parameters produced in the system of FIG. 5 for an assumed Urea to NOx ratio correction factor of ⁇ 0.3.
  • FIG. 1 is a diagrammatical sketch of an engine exhaust system 10 is shown having a processor 12 programmed for determining the effectiveness of injected urea in reducing NO x produced by an engine 14 .
  • the system 10 includes a reactant injector 16 , here a urea injector, adapted to inject urea into the exhaust 18 of the engine in response to an excitation signal u(t), where t is time.
  • the injection signal u(t) is made up of two components: a nominal level u 0 and a changeable component û(t).
  • the nominal level u 0 may be produced by providing a sensor 13 in the engine exhaust upstream of the injection of the urea.
  • u 0 k_base*NOx 1
  • NOx 1 is the signal produced by this upstream sensor
  • k_base is a conversion factor stored in a look-up table 15 relating the a priori assumed stoichiometric amount of urea needed to convert the NOx in the upstream engine exhaust.
  • the exhaust 18 together with the injected urea, is directed to a catalyst 20 though the engine's exhaust pipe.
  • the catalyst 20 is used to facilitate the reaction between the NOx and the urea.
  • the injected urea reacts with NOx which may be present in the exhaust 18 in the catalyst 20 to produce a product 22 which includes the reaction products as well as any un-reacted portions of the injected urea or un-reacted portions of the NOx.
  • the processor 12 is also programmed to determine whether the injector 16 is faulty and whether the catalyst 20 is faulty.
  • the output of the catalyst 22 is sensed by a second NOx sensor 26 .
  • the sensor 26 sense only the presence of any NOx at the output of the catalyst
  • current practical automotive NOx sensors as noted above, produce an output signal in response to NOx and urea.
  • these sensors cannot differentiate between NOx and urea. That is, the sensor 26 is a non-selective NOx sensor.
  • Curve 30 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured urea in the presence of only urea. It is noted that the slope of curve 60 is here k_urea.
  • Curve 32 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured NO in the presence of only NO.
  • the slope of curve 60 is here k_no
  • Curve 34 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured NO 2 in the presence of only NO 2 .
  • the slope of curve 60 is here k 13 no 2 .
  • the response of the sensor to NOx is interpolated from the responses to NO and NO 2 . For example a 50-50 mixture of NO and NO 2 would result in the slope (k_no+k_no 2 )/2.
  • the family of interpolated slopes is collectively referred to as k_nox.
  • a urea excitation technique to be described allows one to determine whether the non-selective sensor 26 is responding to NOx or to urea.
  • the amount of urea injected into the engine exhaust 18 is modulated, or changed in a particular, a priori known direction, or sense.
  • the output of the non-selective NOx sensor 26 is processed by processor 12 along with knowledge of the direction in the change in the amount of injected urea.
  • the result of the processing yields an indication of whether the sensor is sensing urea or NOx by determining whether the change in urea injection and the change in sensor 26 output signal are in the same direction or in opposite directions.
  • a small, periodic negative amplitude excitation signal û(t) of duration Texc is superimposed on the excitation signal u 0 in a summer 28 .
  • the summer 28 produces u(t) which provides the excitation signal for the injector urea injector 16 . Since during these negative excursions in the excitation signal u(t) the amount of urea is reduced, less NOx is being reduced, if any.
  • the sensor 26 output signal here a voltage V(t) goes lower in response to the negative excursion in the excitation signal u(t)
  • too much urea is being injected into the exhaust 18 and the sensor 26 output signal change ⁇ circumflex over (V) ⁇ (t) was due to un-reacted urea.
  • the sensor 26 produces a higher voltage V(t) not enough urea was being injected into the exhaust to reduce all of the NO x and the sensor output signal change ⁇ circumflex over (V) ⁇ (t) was due to un-reacted NOx.
  • the processor 12 (FIG. 1) is provided to detect the direction of the change in injected urea u(t) relative to the change in the output signal V(t) of the sensor 26 . That is, the processor determines whether the direction of the change in output signal V(t) of the sensor 26 is the same as, or opposite to, the direction of the change in injected urea u(t). As described above, if they are the same direction, the sensor 26 is detecting urea whereas if the directions are opposite one another the sensor 26 is detecting NOx.
  • Vss ⁇ t0 - T ⁇ ⁇ s ⁇ ⁇ s t ⁇ ⁇ o ⁇ V ⁇ ( t ) ⁇ ⁇ t
  • Vss is the steady state output voltage of the sensor 28 and where the excitation is repeated every Ttot seconds, where Ttot>D+Tss+Texc where Tss is used to take into account the time used to determine Vss.
  • the sensor 26 is determined by the processor 12 to be detecting urea. If, on the other hand, the mathematical product is negative, the sensor 26 is determined by the processor 12 to be detecting NOx.
  • the multiplication is shown by a multiplier 41 which is fed ⁇ circumflex over (V) ⁇ (t) produced by the high pass filter 47 (i.e., a signal proportional to the change in sensor output signal) and by a signal representative of the change in the urea excitation, i.e. û(t).
  • the processor 12 is preferably a digital processor which performs the process shown in FIG. 4.
  • the time history profile of the voltage V(t) produced by the sensor 26 will not be a rapidly changing, pulse, but more a low pass filtered version of a pulse.
  • transport delay i.e., the delay between the time the urea is injected into the exhaust 18 and the time the of reaction in the catalyst 20
  • the voltage V(t) produced by the sensor will be delayed an amount D from the commencement of the change in the injection of the urea.
  • the delay D may be mapped a priori as a function of engine operating conditions, e.g., engine speed using a look-up table.
  • the output of the multiplier 41 is integrated in the processor 12 as represented by integrator 43 .
  • the sensor 26 output signal V(t) can be fed to the transfer function shown by curves 32 or 34 in FIG. 2 and a measurement of the NOx may be obtained. If, one the other hand, I ⁇ 0, the sensor 26 output signal V(t) can fed to the transfer function shown by curve 30 in FIG. 2 and a measurement of the urea may be obtained.
  • V>>0 i.e., greater than some calibrate threshold
  • the procedure works best in the steady state, when, as noted above, it is easy to determine ⁇ circumflex over (V) ⁇ (t), by subtracting the mean over the previous period. If knowledge of engine emissions and catalyst behavior is very accurate, the method may be applied to transients. In this case, it may be able to gain further information about the system catalyst conditions, urea injection system, and NOx sensor by measuring the transient sensor response.
  • the processor is programmed in accordance with the flow diagram shown therein.
  • a determination is made as the open loop quantity of urea u 0 to be added.
  • a negative excitation signal is applied to the urea injector for T 2 seconds.
  • a measurement is made as to the change in the sensor 26 output signal.
  • the signal I is computed as described above. If I ⁇ 0, the NOx transfer function is used and a positive, increase, is made in the amount of urea. If, on the other hand, I ⁇ 0, the urea transfer function is used.
  • FIG. 5 a functional block diagram is shown of a NOx reduction system 10 ′.
  • a NOx sensor 60 is included upstream of the point 19 where urea is added into the engine 14 exhaust 18 via injector 16 .
  • the NOx sensor 26 is disposed downstream of the catalyst 20 , as shown. As noted above in connection with FIG. 1, the NOx sensors 26 and 60 are sensitive to both urea and NOx.
  • the catalyst 20 is positioned between the point 19 where the urea is injected and the position of the NOx sensor 26 .
  • Output signals nox 1 , nox 2 (where nox 2 is referred to as V in connection with FIGS.
  • the processor 12 ′ is shown by a functional block diagram for purposes of understanding the signals processed by such processor 12 ′. It should be understood that preferably the processor 12 ′ is a digital processor programmed to execute an algorithm to be described below. Suffice it to say here that the processor 40 ′ includes a square wave generator 62 which produces an excitation voltage u_exc (where u_exc was referred to as û(t) in connection with FIGS. 1 - 4 ) which may be represented as:
  • u — exc: A — du*k — nox/k — urea if t ⁇ 0.5* T — du
  • A_du is the amplitude of the negative portion of the steady state excitation signal fed to the urea injector 16 (i.e., a negative excitation signal reduces the amount of urea injected into the engine exhaust);
  • k_urea is the sensitivity of the NOx sensor 26 with respect to urea
  • k_NOx is the sensitivity of the NOx sensor 26 with respect to NOx.
  • a correction factor k_nox/k_urea is inserted to account for different sensitivities of the sensor 26 to urea and NOx.
  • the output of the square wave generator 62 is fed, via a switch 64 , to a low pass filter 66 .
  • the function of the low pass filter 66 is to take into account a reaction delay, D, between the time urea is injected into the exhaust and the reaction in the catalyst 20 .
  • the processor 40 ′ provides this low pass filter 66 digitally in accordance with:
  • u_rk is the output of the low pass filter 66 ;
  • kf_rk is time constant of NOx-urea reaction kinetics.
  • the output signal produced by the sensor 26 is here, as noted above, represented as: nox 2 .
  • the signal nox 2 is fed to a high pass filter 42 to produce an output signal nox 2 _hp representing the change in the output signal produced by the sensor 26 .
  • the processor 40 provides this high pass filter output in accordance with:
  • kf_lp_nox 2 is the filter gain for the low pass filter nox 2 .
  • the output of the high pass filter 42 (which represents the change in the output signal produced by the sensor 26 ) and the signal produced by the low pass filter 66 (which represents the change in the excitation signal u_exc to be fed to the urea injector 16 , in a manner to be described, are fed to a multiplier 41 .
  • the mathematical product produced by the multiplier 41 will be positive.
  • the mathematical product produced by the multiplier 41 will be negative.
  • the mathematical product produced by the multiplier 41 is normalized by the signal nox 1 produced by the sensor 60 in a divider 45 to produce:
  • the signal dydu is scaled by ki and integrated by integrator 43 to produce a correction signal k_corr in accordance with:
  • ki>0 is the integral gain used to correct the nominal urea:NOx ratio (which is k_base)
  • the signal k_corr is used to add (if k_corr>0) or subtract from (if k_corr ⁇ 0) the nominal a priori determined amount of urea for correct stoichiometry which is k_base*nox 1 .
  • the actual amount of urea added by the injector is k_base*nox 1 *k_injector, where k_injector is the injector transfer function which is unknown because of aging, etc.
  • the signal k_corr together with u_exc will both modulate the signal k_base*nox 1 to produce the correct stoichiometric urea independent of k_injector. and thus automatically adjust the amount of urea which should be added to the exhaust.
  • the final urea quantity to be applied via the injector 16 is:
  • u — tot — ppm: ( k — base+k — corr )* nox 1+ u — exc;
  • k_base is the nominal urea:NOx ratio.
  • (k_corr+k_base)*k_injector*nox 1 results in the injector 16 delivering stoichiometric urea to the engine exhaust upstream of the catalyst 20 .
  • the signal u_tot_ppm is in parts per million of urea and is converted to mg/sec of urea by using mass air flow (Maf) of the exhaust, the upstream temperature (TMP) of the catalyst and the fuel flow (Wf) in a converter 61 .
  • the integral int_dydu_last is evaluated in a comparator 47 as follows: ⁇ t - T ⁇ ⁇ _ ⁇ ⁇ d ⁇ ⁇ u t ⁇ ⁇ y ⁇ ⁇ u ⁇ ( t ) ⁇ ⁇ t
  • k_corr>k_corr_lmx where k_corr_lmx is the maximum limit for the correction factor k_corr to be declared a failure, (i.e., a blocked injector 16 or a catalyst 20 failure) as determined by comparator 47 , a system failure has occurred (i.e., the catalyst 20 is inactive or the injector 16 is blocked).
  • T 1 temperature upstream of the SCR brick
  • A_du the amplitude of the negative part of the excitation
  • T_du the period of the excitation is T_du
  • k_urea sensitivity of the Nox sensor wrt urea
  • k_nox sensitivity of the Nox sensor wrt urea
  • kf_lp_nox 2 filter gain for low pass filtered nox 2 .
  • kf_rk time constant of nox-urea reaction kinetics.
  • k_dydu_thres:threshold for correction contribution to determine whether further adjustment is needed.
  • k_corr_lmn minimum limit for correction factor to declare a system failure (leaking injector).
  • the processor 12 ′ is a digital processor.
  • the following flow diagram describes the program executed by such digital processor:
  • Step 1 The excitation signal is the repetitive signal with period T_du defined by:
  • u_exc: A_du*k_nox/k_urea if t ⁇ 0.5*T_du
  • u_exc: ⁇ A_du if t>0.5*T_du
  • the correction factor k_nox/k_urea is inserted to account for different sensitivities to Nox and urea. These gains follow from sensor characteristics.
  • Step 2 Compute the switch on_logic (specified later).
  • Step 4 Compute the excitation signal delayed by reaction kinetics:
  • u_rk kf_rk*u_rk+(1 ⁇ kf_rk)*u_exc.
  • Step 5 Obtain the measurement voltage from the second Nox sensor, nox 2 .
  • Step 6 Compute the low pass filtered version nox 2 _lp, with filter constant kf_lp_nox 2 :
  • Step 7 Compute the high pass filtered
  • Step 8 Obtain the measurement voltage from the first Nox sensor:nox 1 .
  • Step 9 Compute the convolution:
  • Step 10 Integrate the convolution into a correction factor:
  • k_corr: k_corr+ki*dydu
  • Step 11 At the end of every period T_du evaluate the integral
  • int_dydu_last ki* ⁇ t t ⁇ T — du dydu(t) dt between the limits t ⁇ T_du and t, where t is the current time.
  • a system failure has occurred: the injection system is leaking.
  • Step 12 The final urea quantity to be applied is:
  • Step 13 Use MAF, Wf, T 1 to convert u_tot_ppm to a quantity in mg/sec: u_tot_mgsec.
  • Step 14 Go to Step 1.

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Abstract

A method wherein a reactant is added to a substance to react with such substance. The product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor. The sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant. The method includes changing the amount of reactant added to the substance. A measurement is made to determine whether the change in the amount of reactant and the change the output signal are in the same direction or in opposite directions. The changes in reactant and output signal are multiplied an integrated to form a correction on the quantity of reactant to be injected.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application is a divisional application of co-pending U.S. patent application Ser. No. 09/682,445 entitled “Method and Apparatus for Controlling the Amount of Reactant to be Added to a Substance Using a Sensor which is Responsive to both the Reactant and the Substance”, filed on Sep. 4, 2001, the entire subject matter thereof being incorporated herein by reference. This application claims the benefit of the Sep. 4, 2001 filing date of said co-pending U.S. patent application Ser. No. 09/682,445 under the provisions of 35 U.S.C. §120.[0001]
  • TECHNICAL FIELD
  • This invention relates generally to methods and apparatus for determining whether a sensor which is responsive to both a reactant and a substance to be reduced by such reactant is responding to either un-reacted portions of the substance or un-reacted portions of the reactant. More particularly the invention relates to methods and apparatus for detecting NOx to be reduced with urea using a sensor which is responsive to un-reacted portions of the NOx and un-reacted portions of the urea. [0002]
  • BACKGROUND
  • As is known in the art, in many applications it is desirable to detect the effectiveness of a reaction used to reduce a substance. One such application is in measuring the effectiveness in urea based selective catalytic reduction (SCR) in reducing nitrogen (NOx) in the exhaust gas of a diesel engine. More particularly, an aqueous solution of urea is injected into the exhaust gas of the engine upstream of a catalyst. In order for the method to reduce NOx in the exhaust effectively, it is important that the amount of urea injected into the exhaust be accurately controlled. Injection of too little urea may result in sub-optimal (i.e., incomplete) NOx conversion. Injection of too much urea may produce nitrates in the exhaust which can reduce the life of the exhaust system downstream of the catalyst, may produce an unpleasant odor, and may also produce increases in regulated emissions. [0003]
  • Thus, it is desirable to have a sensor downstream of the catalyst which can detect the presence of NOx after the reaction. However, the inventors herein have recognized that currently available sensors which are practical, from a size and cost perspective, for automotive use cannot differentiate between NOx and urea. The inventors have further recognized that degraded performance may result when using such a sensor with conventional urea injection methods that adjust the injected urea based on one of measured NOx or measured urea,. In particular, if it is assumed that NOx is measured, yet actually urea is exiting the catalyst, the system may improperly increase injected urea since the system believes excess NOx is being produced and thus more urea is necessary. This can results in increased urea slip. Similarly, if it is assumed that urea is measured, yet actually NOx is exiting the catalyst, the system may improperly reduce injected urea since the system believes excess urea is being produced and thus less urea is necessary. This can result in increased NOx emission. [0004]
  • SUMMARY
  • In accordance with the present invention, a method is provided wherein a reactant is added into a substance to react with the substance. The product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor. The sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant. The method includes changing at least one of the amount of reactant added to the substance and the amount of the substance. A determination is made from said at least one of the change in the amount of reactant and the change in the amount of the substance, and from the change in the output signal, whether the sensor is responding to the substance or to the reactant. [0005]
  • In one embodiment, a method is provided wherein a reactant is added to a substance to react with such substance. The product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor. The sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant. The method includes changing the amount of reactant added to the substance and determining from the response of the sensor to such change in the amount of reactant whether the output signal is responding to the substance or to the reactant. [0006]
  • In accordance with another aspect of the invention, a sensing system is provided wherein a sensor is provided for producing an output signal in response to either a first substance of a reaction or to a second substance of the reaction. The system includes: an injector for changing the level of one of the substances in the reaction; and a processor responsive to the output signal and a signal representative of the change in level of one of the substances, for determining whether the sensor is responding to the first substance or to the second substance. [0007]
  • In one embodiment, the sensing system is a NOx sensing system. Such system includes: a NOx sensor for producing an output signal in response to NOx and urea and a processor responsive to the output signal for determining whether the sensor is responding to NOx or to urea. [0008]
  • In accordance with another aspect of the invention, a method is provided wherein a reactant is added to a substance to react with such substance. The product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant are directed to a sensor. The sensor produces an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant. The method includes changing the amount of reactant added to the substance, determining whether the change in the amount of reactant and the change in the output signal are in the same direction or in opposite directions, and from such determination determining whether the output signal is responding to the substance or to the reactant. [0009]
  • In one embodiment, if the directions are the same, reactant is added to the substance. If the directions are opposite, reactant is reduced from the substance. [0010]
  • In one embodiment of the invention, a change is made in the amount of a reactant added to a substance to be reacted and thereby reduced by, the reactant, the time history of such change in the reactant being represented by: [0011]
  • Û(t) [0012]
  • where t is time. [0013]
  • The products of the reaction, along with un-reacted portions of the reactant and the un-reacted portions of the substance are passed by a sensor. The sensor is unable to effectively differentiate between the un-reacted reactant portions and the un-reacted portions of the substance. That is, the sensor produces an output signal V(t) in response to the un-reacted portions of the reactant and the un-reacted portions of the substance. The change in the output signal from the change in the amount of reactant added to the substance may be represented as: [0014]
  • {circumflex over (V)}(t) [0015]
  • The change in the amount of the reactant is recorded over a period of time T. The delay between the change in the amount of the reactant occurring at a time t[0016] 0, to the time the reaction is effected by such change in the amount of reactant is a time delay, D. A signal, I, is produced to determine whether the output signal increases or decreases with the changed amount of reactant. In one embodiment, I = t0 t0 + D + T e x c V ^ ( t + D ) u ^ ( t ) t
    Figure US20030051468A1-20030320-M00001
  • where Texc is the time duration of the excitation û(t). [0017]
  • If the change in the level of the reactant is in the same sense (i.e., direction) as the resulting change in the output signal, (i.e., if the amount of reactant increases and the output signal increases, or if the amount of reactant decreases and the output signal decreases), I>0. In such case, the sensor is determined to be responding to the un-reacted reactant. [0018]
  • On the other hand, if the change in the level of reactant is in the opposite to resulting change in the output signal, (i.e., if the amount of reactant increases and the output signal decreases, or if the amount of reactant decreases and the output signal increases), I<0. In such case the sensor is determined to be responding to un-reacted substance. [0019]
  • If I=0, there was no change in the reactant and therefore it may be concluded that the injector is faulty. [0020]
  • Further, if V is much greater than 0 (i.e., V is greater than some calibratable threshold), it may be concluded that both the un-reacted substance, and un-reacted reactant are both being measured and therefore a catalyst used to facilitate the reaction is determined to be faulty. [0021]
  • Thus, from the signal I, a determination may be made as to whether the sensor is responding to the un-reacted reactant, to the un-reacted substance, and whether the injector or the catalyst is faulty. [0022]
  • The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description and drawings, and from the claims.[0023]
  • DESCRIPTION OF DRAWINGS
  • FIG. 1 is a diagrammatical sketch of an engine exhaust system according to the invention having a processor programmed for determining the effectiveness of injected urea in reducing NOx produced by the engine; [0024]
  • FIG. 2 is a diagram showing the relationship between an output signal produced by a sensor used in the exhaust system of FIG. 1 as a function of either nitrogen monoxide (NO), nitrogen dioxide (NO[0025] 2) or urea;
  • FIG. 3 is a diagram showing the output signal produced by the sensor used in the exhaust system of FIG. 1 in response to increases and decreases in the amount of urea injected into the engine exhaust in the system of FIG. 1; and [0026]
  • FIG. 4 is a flow diagram of the process used by the processor in FIG. 1 to determine the effectiveness of injected urea in reducing NOx produced by the engine exhaust in the system of FIG. 1; [0027]
  • FIG. 5 is a functional block diagram of a NOx reduction system according to another embodiment of the invention; [0028]
  • FIG. 6 are diagrams showing as a result of computer simulations various parameters produced in the system of FIG. 5 for an assumed Urea to NOx ratio correction factor of +0.32; and [0029]
  • FIG. 7 are diagrams showing as a result of computer simulations various parameters produced in the system of FIG. 5 for an assumed Urea to NOx ratio correction factor of −0.3. [0030]
  • Like reference symbols in the various drawings indicate like elements.[0031]
  • DETAILED DESCRIPTION
  • Referring now to FIG. 1, is a diagrammatical sketch of an [0032] engine exhaust system 10 is shown having a processor 12 programmed for determining the effectiveness of injected urea in reducing NOx produced by an engine 14. The system 10 includes a reactant injector 16, here a urea injector, adapted to inject urea into the exhaust 18 of the engine in response to an excitation signal u(t), where t is time. The injection signal u(t) is made up of two components: a nominal level u0 and a changeable component û(t). The nominal level u0 may be produced by providing a sensor 13 in the engine exhaust upstream of the injection of the urea. Thus, here u0=k_base*NOx1, where NOx1 is the signal produced by this upstream sensor and k_base is a conversion factor stored in a look-up table 15 relating the a priori assumed stoichiometric amount of urea needed to convert the NOx in the upstream engine exhaust.
  • The [0033] exhaust 18, together with the injected urea, is directed to a catalyst 20 though the engine's exhaust pipe. The catalyst 20 is used to facilitate the reaction between the NOx and the urea. The injected urea reacts with NOx which may be present in the exhaust 18 in the catalyst 20 to produce a product 22 which includes the reaction products as well as any un-reacted portions of the injected urea or un-reacted portions of the NOx.
  • As will be described, the [0034] processor 12 is also programmed to determine whether the injector 16 is faulty and whether the catalyst 20 is faulty.
  • More particularly, the output of the [0035] catalyst 22 is sensed by a second NOx sensor 26. While it would be desirable that the sensor 26 sense only the presence of any NOx at the output of the catalyst, current practical automotive NOx sensors, as noted above, produce an output signal in response to NOx and urea. Thus, these sensors cannot differentiate between NOx and urea. That is, the sensor 26 is a non-selective NOx sensor. This is illustrated from FIG. 2. Curve 30 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured urea in the presence of only urea. It is noted that the slope of curve 60 is here k_urea. Curve 32 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured NO in the presence of only NO. It is noted that the slope of curve 60 is here k_no Curve 34 shows the relationship, i.e., transfer function, between sensor 26 output signal (V, volts) and measured NO2 in the presence of only NO2. It is noted that the slope of curve 60 is here k13 no2. (It is noted that the response of the sensor to NOx is interpolated from the responses to NO and NO2. For example a 50-50 mixture of NO and NO2 would result in the slope (k_no+k_no2)/2. The family of interpolated slopes is collectively referred to as k_nox.
  • We have discovered a method which enables differentiation between NOx and urea detection using theses practical NOx non-selective sensors. More particularly, we have discovered that a urea excitation technique to be described allows one to determine whether the [0036] non-selective sensor 26 is responding to NOx or to urea. According to the method, the amount of urea injected into the engine exhaust 18 is modulated, or changed in a particular, a priori known direction, or sense. The output of the non-selective NOx sensor 26 is processed by processor 12 along with knowledge of the direction in the change in the amount of injected urea. The result of the processing yields an indication of whether the sensor is sensing urea or NOx by determining whether the change in urea injection and the change in sensor 26 output signal are in the same direction or in opposite directions.
  • Here, in the system shown in FIG. 1, a small, periodic negative amplitude excitation signal û(t) of duration Texc is superimposed on the excitation signal u[0037] 0 in a summer 28. The summer 28 produces u(t) which provides the excitation signal for the injector urea injector 16. Since during these negative excursions in the excitation signal u(t) the amount of urea is reduced, less NOx is being reduced, if any. If the sensor 26 output signal, here a voltage V(t), goes lower in response to the negative excursion in the excitation signal u(t), too much urea is being injected into the exhaust 18 and the sensor 26 output signal change {circumflex over (V)}(t) was due to un-reacted urea. If, on the other hand, the sensor 26 produces a higher voltage V(t), not enough urea was being injected into the exhaust to reduce all of the NOx and the sensor output signal change {circumflex over (V)}(t) was due to un-reacted NOx. Thus, if we reduce the amount of urea and the voltage V produced by the sensor reduces, (i.e., the direction of the change in urea is in the same direction in the change in the output signal, V(t), of the sensor) the sensor 26 is now known to be responding to urea. On the other hand, if we reduce the amount of urea and the voltage V(t) produced by the sensor increases, (i.e., the direction of the change in urea is in the opposite direction to change in the output signal, V(t), of the sensor) the sensor 26 is now known to be responding to NOx. FIG. 3 illustrates this effect.
  • The processor [0038] 12 (FIG. 1) is provided to detect the direction of the change in injected urea u(t) relative to the change in the output signal V(t) of the sensor 26. That is, the processor determines whether the direction of the change in output signal V(t) of the sensor 26 is the same as, or opposite to, the direction of the change in injected urea u(t). As described above, if they are the same direction, the sensor 26 is detecting urea whereas if the directions are opposite one another the sensor 26 is detecting NOx. Here such determination is made by multiplying a signal representative of {circumflex over (V)}(t) (i.e., the change in the output signal V(t) produced by the sensor 28) with the change in the excitation signal û(t). Thus, the change in the output of the sensor, {circumflex over (V)}(t), is proportional to the change in the output signal of the sensor V(t). Here, the determination in {circumflex over (V)}(t) is made when the system is in a steady-state condition which can be checked by monitoring rate of change of rpm, load, space velocity, etc.
  • Thus, for time [t[0039] 0-Tss, t0], we determine the steady-state output voltage, Vss= t0 - T s s t o V ( t ) t
    Figure US20030051468A1-20030320-M00002
  • Thus, during time from t[0040] 0, to t0+D+Texc:
  • {circumflex over (V)}(t)=V(t)−Vss,
  • Where Vss is the steady state output voltage of the [0041] sensor 28 and where the excitation is repeated every Ttot seconds, where Ttot>D+Tss+Texc where Tss is used to take into account the time used to determine Vss.
  • If the mathematical product of {circumflex over (V)}(t) and û(t) is positive, the [0042] sensor 26 is determined by the processor 12 to be detecting urea. If, on the other hand, the mathematical product is negative, the sensor 26 is determined by the processor 12 to be detecting NOx. In FIG. 1, the multiplication is shown by a multiplier 41 which is fed {circumflex over (V)}(t) produced by the high pass filter 47 (i.e., a signal proportional to the change in sensor output signal) and by a signal representative of the change in the urea excitation, i.e. û(t). It should be understood that the processor 12 is preferably a digital processor which performs the process shown in FIG. 4.
  • It should be noted that due to adsorption and desorption of urea in the [0043] catalyst 20 and reaction kinetics the time history profile of the voltage V(t) produced by the sensor 26 will not be a rapidly changing, pulse, but more a low pass filtered version of a pulse. Further, due to transport delay (i.e., the delay between the time the urea is injected into the exhaust 18 and the time the of reaction in the catalyst 20), the voltage V(t) produced by the sensor will be delayed an amount D from the commencement of the change in the injection of the urea. The delay D may be mapped a priori as a function of engine operating conditions, e.g., engine speed using a look-up table.
  • Here, the output of the [0044] multiplier 41 is integrated in the processor 12 as represented by integrator 43. Thus, if the pulse-width of the change in the urea excitation signal û(t) has a pulse width Texc and starts at a time t0, the output of the integrator 43 may be represented as: I = t0 t0 + D + T e x c V ^ ( t + D ) u ^ ( t ) t
    Figure US20030051468A1-20030320-M00003
  • Thus, if I>0, (i.e., if the integrated mathematical product of {circumflex over (V)}(t) and û(t) is positive), the [0045] sensor 26 is detecting urea. Here, such condition is indicated by a logic 1 produced by comparator 44. Thus, here the amount of urea is V(t)*k_urea
  • If, on the other hand, I<0 (i.e., the integrated mathematical product of {circumflex over (V)}(t) and û(t) is negative), the [0046] sensor 26 is detecting NOx. Here, such condition is indicated by a logic 1 produced by comparator 46. Thus, here the amount of NOx is V(t)*k_nox
  • Having discriminated between sensing urea and sensing NOx, if I<0, the [0047] sensor 26 output signal V(t) can be fed to the transfer function shown by curves 32 or 34 in FIG. 2 and a measurement of the NOx may be obtained. If, one the other hand, I≦0, the sensor 26 output signal V(t) can fed to the transfer function shown by curve 30 in FIG. 2 and a measurement of the urea may be obtained.
  • Here, as noted above, the excitation is repeated every Ttot seconds, where Ttot>D+Texc+Tss. [0048]
  • It should be noted that if I=0, the commanded change in urea was not applied and a diagnosis is that of a faulty injector. Here, such condition is indicated by a [0049] logic 1 produced by comparator 48.
  • If V>>0 (i.e., greater than some calibrate threshold), one may conclude that both the engine exhaust NO[0050] x and the urea are still measured after the catalyst 20 and one can conclude a faulty catalyst 20. Here, such condition is indicated by a logic 1 produced by comparator 50.
  • It should be noted that since here we decrease the amount of urea for a short time, an increase in tail pipe emissions may result. This is the case if I<0. This can be compensated by applying a positive correction+û after T[0051] 0+T1+T2, when I<0. If I>0, too much urea is being injected and a positive correction is not required. This procedure keeps the overall tailpipe emissions neutral.
  • It should also be noted that the procedure works best in the steady state, when, as noted above, it is easy to determine {circumflex over (V)}(t), by subtracting the mean over the previous period. If knowledge of engine emissions and catalyst behavior is very accurate, the method may be applied to transients. In this case, it may be able to gain further information about the system catalyst conditions, urea injection system, and NOx sensor by measuring the transient sensor response. [0052]
  • Referring now to FIG. 4, the processor is programmed in accordance with the flow diagram shown therein. Thus, a determination is made as the open loop quantity of urea u[0053] 0 to be added. Next, a negative excitation signal is applied to the urea injector for T2 seconds. A measurement is made as to the change in the sensor 26 output signal. The signal I is computed as described above. If I<0, the NOx transfer function is used and a positive, increase, is made in the amount of urea. If, on the other hand, I<0, the urea transfer function is used.
  • Having described a method and system for determining whether the [0054] sensor 26 is responding to NOx or Urea, a method and system using these techniques will be described which controls the amount of urea to be injected into the engine exhaust to produce correct stoichiometric urea and diagnostics.
  • Referring now to FIG. 5, a functional block diagram is shown of a [0055] NOx reduction system 10′. Here a NOx sensor 60 is included upstream of the point 19 where urea is added into the engine 14 exhaust 18 via injector 16. The NOx sensor 26 is disposed downstream of the catalyst 20, as shown. As noted above in connection with FIG. 1, the NOx sensors 26 and 60 are sensitive to both urea and NOx. The catalyst 20 is positioned between the point 19 where the urea is injected and the position of the NOx sensor 26. Output signals nox1, nox2 (where nox2 is referred to as V in connection with FIGS. 1-4) produced by sensors 60, 26 respectively are processed by a programmed processor 12′, in a manner to be described, to produce the urea injection signal to urea injector 16. It is noted that part of the output nox2 is due to urea slip.
  • Here, the [0056] processor 12′ is shown by a functional block diagram for purposes of understanding the signals processed by such processor 12′. It should be understood that preferably the processor 12′ is a digital processor programmed to execute an algorithm to be described below. Suffice it to say here that the processor 40′ includes a square wave generator 62 which produces an excitation voltage u_exc (where u_exc was referred to as û(t) in connection with FIGS. 1-4) which may be represented as:
  • u exc:=A du*k nox/k urea if t<0.5*T du
  • u exc:−=A du if t>0.5*T du;
  • where: [0057]
  • A_du is the amplitude of the negative portion of the steady state excitation signal fed to the urea injector [0058] 16 (i.e., a negative excitation signal reduces the amount of urea injected into the engine exhaust);
  • T_du is the period of the excitation signal u_exc; (T_du=Texc×2). [0059]
  • k_urea is the sensitivity of the [0060] NOx sensor 26 with respect to urea;
  • k_NOx is the sensitivity of the [0061] NOx sensor 26 with respect to NOx.
  • Thus, a correction factor k_nox/k_urea is inserted to account for different sensitivities of the [0062] sensor 26 to urea and NOx.
  • The output of the [0063] square wave generator 62 is fed, via a switch 64, to a low pass filter 66. The function of the low pass filter 66 is to take into account a reaction delay, D, between the time urea is injected into the exhaust and the reaction in the catalyst 20. The processor 40′ provides this low pass filter 66 digitally in accordance with:
  • u rk:=kf rk*u rk+(1−kf rk)*u exc,
  • where: [0064]
  • u_rk is the output of the [0065] low pass filter 66;
  • kf_rk is time constant of NOx-urea reaction kinetics. [0066]
  • The output signal produced by the [0067] sensor 26 is here, as noted above, represented as: nox2. The signal nox2 is fed to a high pass filter 42 to produce an output signal nox2_hp representing the change in the output signal produced by the sensor 26. Here, the processor 40 provides this high pass filter output in accordance with:
  • nox[0068] 2_hp:=nox2−nox2_lp; (where nox2_hp was referred to as {circumflex over (V)}(t) in FIGS. 1-4).
  • where nox[0069] 2_lp:=kf_lp_nox2*nox2_lp+(1−kf_lp_nox2)nox2;
  • where: kf_lp_nox[0070] 2 is the filter gain for the low pass filter nox2.
  • The output of the high pass filter [0071] 42 (which represents the change in the output signal produced by the sensor 26) and the signal produced by the low pass filter 66 (which represents the change in the excitation signal u_exc to be fed to the urea injector 16, in a manner to be described, are fed to a multiplier 41. It should be noted that if the direction of change in the excitation signal u_rk is the same as the direction in the change in the sensor 26 signal, the mathematical product produced by the multiplier 41 will be positive. On the other hand, if the direction of change in the excitation signal u_rk is opposite to the direction in the change in the sensor 26 signal, the mathematical product produced by the multiplier 41 will be negative.
  • The mathematical product produced by the [0072] multiplier 41 is normalized by the signal nox1 produced by the sensor 60 in a divider 45 to produce:
  • dydu:nox−hp*u rk/nox1
  • The signal dydu is scaled by ki and integrated by [0073] integrator 43 to produce a correction signal k_corr in accordance with:
  • k_corr:=∫(ki*dydu)dt;
  • where: ki>0 is the integral gain used to correct the nominal urea:NOx ratio (which is k_base) [0074]
  • Thus, if dydu>0 (i.e., the change in the [0075] sensor 26 and the change in the urea excitation are the in the same direction), the amount of urea should be reduced whereas, if dydu<0, (i.e., the change in the sensor 26 and the change in the urea excitation are the in opposite directions),the amount of urea should be increased.
  • The signal k_corr is used to add (if k_corr>0) or subtract from (if k_corr<0) the nominal a priori determined amount of urea for correct stoichiometry which is k_base*nox[0076] 1. The actual amount of urea added by the injector is k_base*nox1*k_injector, where k_injector is the injector transfer function which is unknown because of aging, etc. Thus, with the processor 40, the signal k_corr together with u_exc will both modulate the signal k_base*nox1 to produce the correct stoichiometric urea independent of k_injector. and thus automatically adjust the amount of urea which should be added to the exhaust.
  • More particularly, the final urea quantity to be applied via the [0077] injector 16 is:
  • u tot ppm:=(k base+k corr)*nox1+u exc;
  • where k_base is the nominal urea:NOx ratio. [0078]
  • To put it another way, a priori determined injection signal u[0079] 0=nox1*k_base is modulated by both the correction signal k_corr*nox1 and the square wave signal u_exc. At correct stoichiometry, (k_corr+k_base)*k_injector*nox1 results in the injector 16 delivering stoichiometric urea to the engine exhaust upstream of the catalyst 20.
  • The signal u_tot_ppm is in parts per million of urea and is converted to mg/sec of urea by using mass air flow (Maf) of the exhaust, the upstream temperature (TMP) of the catalyst and the fuel flow (Wf) in a [0080] converter 61.
  • At the end of each period T_du, the integral int_dydu_last is evaluated in a [0081] comparator 47 as follows: t - T _ d u t y u ( t ) t
    Figure US20030051468A1-20030320-M00004
  • between the limits t−T_du and t, where t is the current time. The integral represents the incremental correction to the urea:NOx ratio accumulated over the last excitation period T_du. If int_dydu_last<k_dydu_thres, (where k_dydu_thres is the threshold for correction contribution to determine whether further adjustment is needed), this incremental correction is considered small enough to terminate adjusting the urea and the switch [0082] 64 is open from its initial closed condition. Otherwise, the switch 64 remains closed.
  • If k_corr>k_corr_lmx, where k_corr_lmx is the maximum limit for the correction factor k_corr to be declared a failure, (i.e., a blocked [0083] injector 16 or a catalyst 20 failure) as determined by comparator 47, a system failure has occurred (i.e., the catalyst 20 is inactive or the injector 16 is blocked).
  • If k_corr<k_corr_lmn<0, where k_corr_lmn is the minimum limit for the correction factor k_corr to declare a system failure for a leaking urea injector, as determined by [0084] comparator 49, a system failure has occurred, i.e., the injector is leaking, and excess urea will shorten the life of the exhaust system. For example, for detection of a 50 percent increase, k_corr_lmx is set=0.5.
  • Referring now to FIG. 6, such FIG. 6 shows, as a result of computer simulations various parameters produced in the system of FIG. 5 for a resulting Urea to NOx ratio correction factor of +0.32 (i.e., k_base=0.68) FIG. 7 shows, as a result of computer simulations various parameters produced in the system of FIG. 5 for a resulting Urea to NOx ratio correction factor of −0.3 (i.e., k_base=1.3). [0085]
  • The process described above in connection with FIG. 5 may be summarized as follows: [0086]
  • The following measured inputs are used: [0087]
  • Nox[0088] 1:Nox sensor signal measured before the SCR brick (in ppm)
  • Nox[0089] 2:Nox sensor signal measured after the SCR brick (part of this output is due to urea slip) (in ppm)
  • MAF:mass air flow [0090]
  • T[0091] 1:temperature upstream of the SCR brick
  • Wf:fuel flow [0092]
  • (Maf, T[0093] 1 and Wf are used to convert the urea ppm quantity to a quantity in mg/sec.)
  • The following gains are used and to be calibrated based on experimental data. They may dependent on engine operating conditions (speed and load) and exhaust temperature. [0094]
  • A_du:the amplitude of the negative part of the excitation [0095]
  • T_du:the period of the excitation is T_du [0096]
  • k_urea:sensitivity of the Nox sensor wrt urea [0097]
  • k_nox:sensitivity of the Nox sensor wrt urea [0098]
  • (A_du, k_urea and k_nox determine the amplitude of the positive part of the excitation). [0099]
  • kf_lp_nox[0100] 2:filter gain for low pass filtered nox2.
  • kf_rk:time constant of nox-urea reaction kinetics. [0101]
  • k_base:nominal urea:nox ratio [0102]
  • ki:integral gain to correct the nominal urea:nox ratio [0103]
  • k_dydu_thres:threshold for correction contribution to determine whether further adjustment is needed. [0104]
  • k_corr_lmx:maximum limit for correction factor to declare an OBD failure (blocked injector or catalyst malfunction). [0105]
  • k_corr_lmn:minimum limit for correction factor to declare a system failure (leaking injector). [0106]
  • As noted above, the [0107] processor 12′ is a digital processor. The following flow diagram describes the program executed by such digital processor:
  • THE PROCESS FLOW
  • [0108] Step 1 The excitation signal is the repetitive signal with period T_du defined by:
  • u_exc:=A_du*k_nox/k_urea if t<0.5*T_du [0109]
  • u_exc:=−A_du if t>0.5*T_du [0110]
  • The correction factor k_nox/k_urea is inserted to account for different sensitivities to Nox and urea. These gains follow from sensor characteristics. [0111]
  • [0112] Step 2 Compute the switch on_logic (specified later).
  • Step 3 If on_logic=TRUE, apply u_exc, otherwise don't and return to 1. [0113]
  • [0114] Step 4 Compute the excitation signal delayed by reaction kinetics:
  • u_rk :=kf_rk*u_rk+(1−kf_rk)*u_exc. [0115]
  • [0116] Step 5 Obtain the measurement voltage from the second Nox sensor, nox2.
  • [0117] Step 6 Compute the low pass filtered version nox2_lp, with filter constant kf_lp_nox2:
  • nox[0118] 2_lp:=kf_lp_nox2*nox2_lp+(1−kf_lp_nox2)*nox2.
  • Step 7 Compute the high pass filtered [0119]
  • nox[0120] 2_hp:=nox2−nox2_lp.
  • [0121] Step 8 Obtain the measurement voltage from the first Nox sensor:nox1.
  • Step 9 Compute the convolution: [0122]
  • dydu:=nox[0123] 2_hp*u_rk/nox1
  • [0124] Step 10 Integrate the convolution into a correction factor:
  • k_corr:=k_corr+ki*dydu [0125]
  • Step 11 At the end of every period T_du evaluate the integral [0126]
  • int_dydu_last:=ki*∫[0127] t t−T dudydu(t) dt between the limits t−T_du and t, where t is the current time. This integral represents the incremental correction to the urea:nox ratio accumulated over the last excitation period. If int_dydu_last<k_dydu_thres, this incremental correction is small enough to stop adjusting, and set on_logic=false.
  • Otherwise on_logic is true. [0128]
  • Step 11 If [0129]
  • k_corr>k_corr_lmx [0130]
  • a system failure has occurred:the catalyst is inactive or the injection system is blocked. [0131]
  • If [0132]
  • k_corr<k_corr_lmn [0133]
  • a system failure has occurred: the injection system is leaking. The limit k_corr_lmx corresponds directly to OBD limits. For detection of a 50% increase in a regulated exhaust component, set k_corr_lmx=0.5. [0134]
  • [0135] Step 12 The final urea quantity to be applied is:
  • u_tot_ppm:=(k_base+k_corr)*nox[0136] 1+u_exc.
  • [0137] Step 13 Use MAF, Wf, T1 to convert u_tot_ppm to a quantity in mg/sec: u_tot_mgsec.
  • [0138] Step 14 Go to Step 1.
  • A number of embodiments of the invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. Accordingly, other embodiments are within the scope of the following claims. [0139]

Claims (9)

What is claimed is:
1. A method, comprising:
(a) adding a reactant into a substance to react with the substance, the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant being directed to a sensor, such sensor producing an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant, such method including changing at least one of the amount of reactant added to the substance and the amount of the substance; and
(b) determining from said at least one of the change in the amount of reactant and the change in the amount of the substance, and from the change in the output signal, whether the sensor is responding to the substance or to the reactant.
2. A method, comprising:
(a) adding a reactant into a substance to react with the substance, the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant being directed to a sensor, such sensor producing an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant, such method including changing the amount of reactant added to the substance; and
(b) determining from the change in the amount of reactant and the change the output signal whether the sensor is responding to the substance or to the reactant.
3. A sensing system, comprising:
(a) a sensor for producing an output signal in response to either a first substance of a reaction or to a second substance of the reaction;
(b) an injector for changing the level of one of the substances in the reaction;
(c) a processor responsive to the output signal for determining whether the sensor is responding to the first substance to the second substance.
4. A NOx sensing system, comprising:
(a) a NOx sensor for producing an output signal in response to NOx and urea;
(b) a processor responsive to the output signal for determining whether the sensor is responding to NOx or to urea.
5. A method, comprising:
(a) adding a reactant to the substance to react with a substance, the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant being directed to a sensor, such sensor producing an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant, such method including changing the amount of reactant added to the substance; and
(b) determine whether the change in the amount of reactant and the change the output signal are in the same direction or in opposite directions.
6. A method for use in reducing a substance with a reactant added to the substance to react with such substance, the product of such reaction along with un-reacted portions of the substance and un-reacted portions of the reactant being directed to a sensor, such sensor producing an output signal in response to detection of both the un-reacted portions of the substance and the un-reacted portions of the reactant, such method comprising:
(a) changing the amount of reactant added to the substance;
(b) determining whether the output signal increases or decreases with the changed amount of reactant; and
(c) determining therefrom whether the sensor is responding to the un-reacted reactant or to the un-reacted substance.
7. A method, comprising:
changing an amount of a reactant added to a substance to be reacted , and thereby reduced by, the reactant, the time history of such change in the reactant being represented by:
Û(t)
where t is time;
such reaction taking place in the presence of a catalyst;
wherein un-reacted portions of the reactant and the un-reacted portions of the substance are passed by a sensor, such sensor producing an output signal in response to the un-reacted portions of the reactant or the un-reacted portions of the substance, the change in the output signal from the change in the amount of reactant added to the substance may be represented as:
{circumflex over (V)}(t)
wherein such change takes place over a period of time T, and with a delay between the change in the amount of the reactant, T0, to the time the reaction is effected by such change in the amount of reactant being represented by D;
producing a signal, I, to determine whether the output signal increases or decreases with the changed amount of reactant, such signal being produced in accordance with
I = t0 t0 + D + T e x c V ^ ( t + D ) u ^ ( t ) t
Figure US20030051468A1-20030320-M00005
determining whether, I>0 or I<0;
concluding that the sensor is responding to the un-reacted reactant if I>0 and concluding that the sensor is responding to the un-reacted substance if I<0.
8. The method recited in claim 7 including determining whether I=0, and is so concluding that the injector is faulty.
9. The method recited in claim 7 including determining whether V is greater than a calibratable threshold and if so concluded that the catalyst is faulty.
US10/101,892 2001-09-04 2002-03-19 Method and apparatus for determining whether a sensor which is responsive to both a reactant and a substance to be reduced by such reactant is responding to either un-reacted portions of the substance or un-reacted portions of the reactant Abandoned US20030051468A1 (en)

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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2872544A1 (en) * 2004-06-30 2006-01-06 Bosch Gmbh Robert METHOD FOR MANAGING A CATALYST USED TO CLEAN THE EXHAUST GASES OF AN INTERNAL COMBUSTION ENGINE, AND DEVICE FOR CARRYING OUT THE METHOD
WO2006038473A1 (en) 2004-10-06 2006-04-13 Honda Motor Co., Ltd. Plant control device
EP1688599A1 (en) * 2003-10-22 2006-08-09 Nissan Diesel Motor Co., Ltd. Engine controller and engine operating method
EP1767754A1 (en) * 2004-06-17 2007-03-28 Hino Motors, Ltd. Exhaust gas purification apparatus
WO2007037730A1 (en) * 2005-09-29 2007-04-05 Volvo Lastvagnar Ab A diagnostic method for an exhaust aftertreatment system
EP1801376A1 (en) * 2004-07-23 2007-06-27 Hino Motors, Ltd. METHOD OF MEASURING NOx REDUCTION RATE OF EXHAUST EMISSION CONTROL DEVICE
EP2000641A2 (en) 2007-06-08 2008-12-10 HONDA MOTOR CO., Ltd. Exhaust emission control device for internal combustion engine
US20090007548A1 (en) * 2006-03-06 2009-01-08 Toyota Jidosha Kabushiki Kaisha Exhaust Gas Purification System of Internal Combustion Engine
US20090084086A1 (en) * 2007-04-05 2009-04-02 Robert Bosch Gmbh Procedure for operating an exhaust gas treatment device and the device for implementing the procedure
EP2080873A1 (en) 2008-01-18 2009-07-22 Peugeot Citroen Automobiles SA Method for injecting a reducing agent in an exhaust line
US20090301059A1 (en) * 2007-04-25 2009-12-10 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of internal combustion engine
US20100043405A1 (en) * 2007-03-29 2010-02-25 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of an internal combustion engine
US20100064664A1 (en) * 2008-09-18 2010-03-18 Joris Fokkelman Method for checking the seal of a reagent injector
FR2937089A1 (en) * 2008-10-13 2010-04-16 Bosch Gmbh Robert METHOD AND DEVICE FOR DIAGNOSING A DEVICE FOR DETERMINING A REACTIVE AGENT IN A COMBUSTION ENGINE
EP2224109A3 (en) * 2009-02-26 2011-06-15 Toyota Jidosha Kabushiki Kaisha Controller for internal combustion engine
WO2011075582A1 (en) * 2009-12-16 2011-06-23 Cummins Filtration Ip, Inc. Apparatus and method to diagnose a nox sensor
EP2388450A1 (en) * 2009-01-13 2011-11-23 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification device for internal combustion engines
US20120017568A1 (en) * 2010-05-03 2012-01-26 Mert Geveci Ammonia sensor control, with nox feedback, of an scr aftertreatment system
US20130074590A1 (en) * 2009-11-26 2013-03-28 Continental Automotive Gmbh Method For Determining The State Of A Reducing Agent In A Reducing Agent Tank
US8505371B2 (en) * 2011-11-30 2013-08-13 Ford Global Technologies, Llc Methods for an exhaust fluid sensor
EP2650499A1 (en) * 2012-04-13 2013-10-16 Peugeot Citroën Automobiles Sa Method for monitoring the efficiency of a system for after-treatment of exhaust gas
WO2014166575A1 (en) * 2013-04-10 2014-10-16 Daimler Ag Method for operating an exhaust gas purification system of a motor vehicle combustion engine
US9038373B2 (en) 2010-05-03 2015-05-26 Cummins Inc. Ammonia sensor control of an SCR aftertreatment system
US9388728B2 (en) 2013-06-10 2016-07-12 Cummins Emission Solutions, Inc. Systems and methods for NOx sensor diagnostics
CN106481409A (en) * 2015-09-02 2017-03-08 迪尔公司 For NOXSelf adaptation post processing control system and method
US20180038256A1 (en) * 2016-08-03 2018-02-08 Mazda Motor Corporation Exhaust emission control system of engine
CN111502804A (en) * 2011-04-05 2020-08-07 卡明斯散发控制技术公司 Systems, methods, and apparatus for aftertreatment system monitoring
US20220049636A1 (en) * 2020-08-14 2022-02-17 Ford Global Technologies, Llc System and method for detecting release from an injector

Families Citing this family (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001303934A (en) 1998-06-23 2001-10-31 Toyota Motor Corp Exhaust emission control device for internal combustion engine
DE10100420A1 (en) * 2001-01-08 2002-07-11 Bosch Gmbh Robert Method and device for controlling an exhaust gas aftertreatment system
DE10111586A1 (en) * 2001-03-10 2002-09-12 Volkswagen Ag Process for operating internal combustion engines
DE10117050C1 (en) * 2001-04-05 2002-09-12 Siemens Ag Process for purifying I.C. engine exhaust gas comprises using a measuring signal depending on the lambda value of the exhaust gas downstream of the catalyst
JP3951774B2 (en) * 2002-03-29 2007-08-01 三菱ふそうトラック・バス株式会社 NOx purification device for internal combustion engine
US6882929B2 (en) * 2002-05-15 2005-04-19 Caterpillar Inc NOx emission-control system using a virtual sensor
JP4643263B2 (en) * 2002-08-29 2011-03-02 ジーイー・ヘルスケア・バイオサイエンス・コーポレイション Allele-specific primer extension
DE10241063A1 (en) * 2002-09-05 2004-03-11 Robert Bosch Gmbh Catalytic process and assembly to reduce diesel engine particle and nitrogen emissions by dosed admixture of plasma particles and ozone
US6846464B2 (en) * 2002-11-20 2005-01-25 Ford Global Technologies, Llc Bimodal catalyst-urea SCR system for enhanced NOx conversion and durability
US7093427B2 (en) * 2002-11-21 2006-08-22 Ford Global Technologies, Llc Exhaust gas aftertreatment systems
US6941746B2 (en) * 2002-11-21 2005-09-13 Combustion Components Associates, Inc. Mobile diesel selective catalytic reduction systems and methods
US20040200211A1 (en) * 2003-04-14 2004-10-14 Slaughter Seth E. Sensor configuration for caustic environments
DE10332057B4 (en) * 2003-07-15 2006-02-09 Siemens Ag Method for checking an emission control system
DE102004001331A1 (en) * 2004-01-08 2005-07-28 Robert Bosch Gmbh Introducing ammonia into engine exhaust system containing selective catalytic reduction catalyst reduce nitrogen oxide emissions comprises introducing ammonia after switching off the engine
US7243489B2 (en) * 2004-01-13 2007-07-17 Arvin Technologies, Inc. Method and apparatus for monitoring engine performance as a function of soot accumulation in a filter
US7776265B2 (en) * 2004-03-18 2010-08-17 Cummins Filtration Ip, Inc. System for diagnosing reagent solution quality
DE102004021372B4 (en) * 2004-04-30 2014-05-28 Robert Bosch Gmbh Method for dosing a reagent for cleaning the exhaust gas of internal combustion engines and apparatus for carrying out the method
US7635593B2 (en) * 2004-05-14 2009-12-22 Fossil Energy Research Corp. (Ferco) In-line localized monitoring of catalyst activity in selective catalytic NOx reduction systems
US20050282285A1 (en) * 2004-06-21 2005-12-22 Eaton Corporation Strategy for controlling NOx emissions and ammonia slip in an SCR system using a nonselective NOx/NH3
US7067319B2 (en) * 2004-06-24 2006-06-27 Cummins, Inc. System for diagnosing reagent solution quality and emissions catalyst degradation
US7784272B2 (en) * 2004-08-31 2010-08-31 Cummins Inc. Control system for an engine aftertreatment system
DE102004046639A1 (en) * 2004-09-25 2006-03-30 Robert Bosch Gmbh Method for operating an internal combustion engine and device for carrying out the method
DE102004046640B4 (en) * 2004-09-25 2013-07-11 Robert Bosch Gmbh Method for operating an internal combustion engine and device for carrying out the method
US7178328B2 (en) * 2004-12-20 2007-02-20 General Motors Corporation System for controlling the urea supply to SCR catalysts
US20070042495A1 (en) * 2005-08-22 2007-02-22 Detroit Diesel Corporation Method of controlling injection of a reducing agent in an engine emissions control system
FR2891304B1 (en) * 2005-09-23 2007-12-21 Renault Sas SYSTEM AND METHOD FOR REGENERATING A CATALYTIC PARTICULATE FILTER LOCATED IN THE EXHAUST LINE OF A DIESEL ENGINE
DE102005046316A1 (en) * 2005-09-27 2007-04-12 J. Eberspächer GmbH & Co. KG Mixing element for an exhaust system
DE102005062120B4 (en) * 2005-12-23 2016-06-09 Robert Bosch Gmbh Method and device for monitoring an exhaust aftertreatment system
US7469531B2 (en) * 2006-09-20 2008-12-30 Gm Global Technology Operations, Inc. Method and apparatus to control injection of a reductant into an exhaust gas feedstream
US7810313B2 (en) * 2007-03-19 2010-10-12 Honeywell International Inc. Method and system for the simultaneous measurement of a plurality of properties associated with an exhaust gas mixture
US8713917B2 (en) * 2007-08-30 2014-05-06 GM Global Technology Operations LLC Method for reducing NH3 release from SCR catalysts during thermal transients
DE102007044611A1 (en) * 2007-09-19 2008-10-09 Continental Automotive Gmbh Internal-combustion engine i.e. diesel engine, operating method for motor vehicle, involves determining characteristic of feed ratio and measuring signal, and determining operating condition of selective catalytic reduction system
US8201394B2 (en) * 2008-04-30 2012-06-19 Cummins Ip, Inc. Apparatus, system, and method for NOx signal correction in feedback controls of an SCR system
US8256208B2 (en) * 2008-04-30 2012-09-04 Cummins Ip, Inc. Apparatus, system, and method for reducing NOx emissions on an SCR catalyst
US8161730B2 (en) * 2008-04-30 2012-04-24 Cummins Ip, Inc. Apparatus, system, and method for reducing NOx emissions on an SCR catalyst
US8505278B2 (en) * 2009-04-30 2013-08-13 Cummins Ip, Inc. Engine system properties controller
US8281572B2 (en) * 2008-04-30 2012-10-09 Cummins Ip, Inc. Apparatus, system, and method for reducing NOx emissions from an engine system
US8459012B2 (en) * 2008-11-19 2013-06-11 Caterpillar Inc. Method for purging a dosing system
WO2010065965A2 (en) * 2008-12-05 2010-06-10 Cummins Ip, Inc. Apparatus, system, and method for controlling reductant dosing in an scr catalyst system
US8225595B2 (en) * 2008-12-05 2012-07-24 Cummins Ip, Inc. Apparatus, system, and method for estimating an NOx conversion efficiency of a selective catalytic reduction catalyst
US9657630B2 (en) * 2008-12-18 2017-05-23 GM Global Technology Operations LLC Diagnostic systems and methods for selective catalytic reduction (SCR) systems based on NOx sensor feedback
JP5398372B2 (en) * 2009-06-18 2014-01-29 Udトラックス株式会社 Engine exhaust purification system
US9631538B2 (en) * 2009-07-10 2017-04-25 GM Global Technology Operations LLC Identifying ammonia slip conditions in a selective catalytic reduction application
US8745973B2 (en) * 2009-08-20 2014-06-10 GM Global Technology Operations LLC System and method for controlling reducing agent injection in a selective catalytic reduction system
DE112010003613T5 (en) * 2009-09-10 2012-11-08 Cummins Ip, Inc. Low temperature catalyst for selective catalytic reduction and related systems and processes
US8915062B2 (en) * 2009-10-09 2014-12-23 GM Global Technology Operations LLC Method and apparatus for monitoring a reductant injection system in an exhaust aftertreatment system
JP4875744B2 (en) * 2009-12-09 2012-02-15 本田技研工業株式会社 Catalyst degradation judgment device for exhaust purification system
US8893475B2 (en) * 2010-03-11 2014-11-25 Cummins Inc. Control system for doser compensation in an SCR system
US8733083B2 (en) 2010-04-26 2014-05-27 Cummins Filtration Ip, Inc. SCR catalyst ammonia surface coverage estimation and control
US8793977B2 (en) 2010-07-09 2014-08-05 Paccar Inc Injector control for a selective catalytic reduction system
US9080488B2 (en) * 2011-03-24 2015-07-14 Ford Global Technologies, Llc Method for estimating slippage of a selective catalyst reduction system
US9556779B2 (en) * 2013-10-25 2017-01-31 Cummins Inc. Leak detection and mitigation in reductant delivery systems
GB2512171A (en) * 2013-12-19 2014-09-24 Daimler Ag Method and control assembly for operating an exhaust gas system
US9238984B2 (en) 2014-02-03 2016-01-19 Caterpillar, Inc. Exhaust emission prediction system and method
US9476341B2 (en) * 2014-07-28 2016-10-25 GM Global Technology Operations LLC Exhaust treatment system that generates debounce duration for NOx sensor offset
US9664092B2 (en) * 2014-08-08 2017-05-30 Cummins Emission Solutions, Inc. Diagnosing system for reductant dosing system
JP6338063B2 (en) * 2015-03-03 2018-06-06 トヨタ自動車株式会社 Failure diagnosis device for exhaust purification catalyst of internal combustion engine
KR101684135B1 (en) * 2015-06-26 2016-12-08 현대자동차주식회사 Failure diagnosis method of SCR system
DE102017110234B4 (en) * 2017-05-11 2021-07-29 Denso Corporation Nitrogen oxide reduction for lean-burn engines with SCR storage model
DE102017110235B4 (en) * 2017-05-11 2022-07-28 Denso Corporation Determination of the cause of a deviation in efficiency in nitrogen oxide reduction
US10947910B2 (en) 2019-05-07 2021-03-16 Ford Global Technologies, Llc Method and system for catalyst feedback control
GB2597182B (en) 2019-05-09 2023-11-22 Cummins Emission Solutions Inc Valve arrangement for split-flow close-coupled catalyst
DE102021212868A1 (en) * 2021-11-16 2023-05-17 Robert Bosch Gesellschaft mit beschränkter Haftung Method for determining an exhaust gas composition of an exhaust gas from an internal combustion engine

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992021871A1 (en) 1991-06-03 1992-12-10 Isuzu Motors Limited DEVICE FOR REDUCING NO¿x?
DE4217552C1 (en) 1992-05-27 1993-08-19 Mercedes-Benz Aktiengesellschaft, 7000 Stuttgart, De
DE4315278A1 (en) 1993-05-07 1994-11-10 Siemens Ag Method and device for metering a reducing agent into a nitrogen-containing exhaust gas
DE4334071C1 (en) 1993-10-06 1995-02-09 Siemens Ag Process for reducing the nitrogen oxide concentration in the exhaust gas of an internal combustion engine or a combustion plant
DK0652500T3 (en) 1993-11-04 1999-04-26 Siemens Ag Method and apparatus for dosing a reactant in a flow medium
JPH0925815A (en) 1995-06-07 1997-01-28 Caterpillar Inc Post-injection combustion exhaust-gas purifying system and method thereof
DE59601433D1 (en) 1995-09-29 1999-04-15 Siemens Ag METHOD AND DEVICE FOR IMPLEMENTING A POLLUTANT IN AN EXHAUST GAS ON A CATALYST
JP3852788B2 (en) 1995-10-02 2006-12-06 株式会社小松製作所 Diesel engine NOx catalyst deterioration detection device and its deterioration detection method
JPH1071325A (en) 1996-06-21 1998-03-17 Ngk Insulators Ltd Method for controlling engine exhaust gas system and method for detecting deterioration in catalyst/ adsorption means
DE19629163C1 (en) 1996-07-19 1997-10-09 Daimler Benz Ag Diesel engine operation to suppress nitrogen oxides emission
JP4087914B2 (en) * 1996-07-25 2008-05-21 日本碍子株式会社 Denitration system and denitration method
JPH1047048A (en) 1996-08-02 1998-02-17 Toyota Motor Corp Emission control device for internal combustion engine
JP3426451B2 (en) 1996-10-23 2003-07-14 トヨタ自動車株式会社 Exhaust gas purification device for internal combustion engine
DE19653958A1 (en) 1996-12-21 1998-06-25 Degussa Process for reducing nitrogen oxides in exhaust gas from internal combustion engines
US5831145A (en) 1997-04-30 1998-11-03 Ford Global Technologies, Inc. Method of introducing selectivity to nonselective gas sensors
DE19736384A1 (en) 1997-08-21 1999-02-25 Man Nutzfahrzeuge Ag Method for metering a reducing agent into nitrogen oxide-containing exhaust gas from an internal combustion engine
DE19743337C1 (en) * 1997-09-30 1999-01-07 Siemens Ag Nitrous oxide reduction system for cleaning diesel engine exhaust gas
US6199374B1 (en) * 1997-10-22 2001-03-13 Toyota Jidosha Kabushiki Kaisha Exhaust gas purifying device for engine
DE19801625A1 (en) * 1998-01-17 1999-07-22 Bosch Gmbh Robert Monitoring method for NOx storage catalytic convertors

Cited By (65)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1688599A1 (en) * 2003-10-22 2006-08-09 Nissan Diesel Motor Co., Ltd. Engine controller and engine operating method
EP1688599A4 (en) * 2003-10-22 2012-10-17 Nissan Diesel Motor Co Engine controller and engine operating method
EP1767754A4 (en) * 2004-06-17 2008-09-17 Hino Motors Ltd Exhaust gas purification apparatus
EP1767754A1 (en) * 2004-06-17 2007-03-28 Hino Motors, Ltd. Exhaust gas purification apparatus
US20080034732A1 (en) * 2004-06-17 2008-02-14 Mitsuru Hosoya Exhaust Emission Control Device
FR2872544A1 (en) * 2004-06-30 2006-01-06 Bosch Gmbh Robert METHOD FOR MANAGING A CATALYST USED TO CLEAN THE EXHAUST GASES OF AN INTERNAL COMBUSTION ENGINE, AND DEVICE FOR CARRYING OUT THE METHOD
US7543443B2 (en) 2004-07-23 2009-06-09 Hino Motors, Ltd. Method for determining NOx reduction ratio in exhaust emission control device
EP1801376A1 (en) * 2004-07-23 2007-06-27 Hino Motors, Ltd. METHOD OF MEASURING NOx REDUCTION RATE OF EXHAUST EMISSION CONTROL DEVICE
US20070199307A1 (en) * 2004-07-23 2007-08-30 Hino Motors, Ltd. Method For Determining NOx Reduction Ratio In Exhaust Emission Control Device
EP1801376A4 (en) * 2004-07-23 2008-01-16 Hino Motors Ltd METHOD OF MEASURING NOx REDUCTION RATE OF EXHAUST EMISSION CONTROL DEVICE
EP1811348A1 (en) * 2004-10-06 2007-07-25 HONDA MOTOR CO., Ltd. Plant control device
WO2006038473A1 (en) 2004-10-06 2006-04-13 Honda Motor Co., Ltd. Plant control device
US20080133113A1 (en) * 2004-10-06 2008-06-05 Yuji Yasui Plant Control System
US7698051B2 (en) 2004-10-06 2010-04-13 Honda Motor Co., Ltd. Plant control system
EP1811348A4 (en) * 2004-10-06 2009-08-12 Honda Motor Co Ltd Plant control device
US20090049899A1 (en) * 2005-09-29 2009-02-26 Volvo Lastvagnar Ab Diagnostic method for an exhaust aftertreatment system
EP1931865A1 (en) * 2005-09-29 2008-06-18 Volvo Lastvagnar AB A diagnostic method for an exhaust aftertreatment system
WO2007037730A1 (en) * 2005-09-29 2007-04-05 Volvo Lastvagnar Ab A diagnostic method for an exhaust aftertreatment system
US7854161B2 (en) 2005-09-29 2010-12-21 Volvo Lastvagnar Ab Diagnostic method for an exhaust aftertreatment system
EP1931865A4 (en) * 2005-09-29 2010-10-06 Volvo Lastvagnar Ab A diagnostic method for an exhaust aftertreatment system
US20090007548A1 (en) * 2006-03-06 2009-01-08 Toyota Jidosha Kabushiki Kaisha Exhaust Gas Purification System of Internal Combustion Engine
US8371106B2 (en) * 2006-03-06 2013-02-12 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification system of internal combustion engine
US20100043405A1 (en) * 2007-03-29 2010-02-25 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of an internal combustion engine
US8359830B2 (en) * 2007-03-29 2013-01-29 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of an internal combustion engine
US20090084086A1 (en) * 2007-04-05 2009-04-02 Robert Bosch Gmbh Procedure for operating an exhaust gas treatment device and the device for implementing the procedure
EP2141331A4 (en) * 2007-04-25 2010-12-15 Toyota Motor Co Ltd Exhaust purification device for internal combustion engine
EP2141331A1 (en) * 2007-04-25 2010-01-06 Toyota Jidosha Kabushiki Kaisha Exhaust purification device for internal combustion engine
US20090301059A1 (en) * 2007-04-25 2009-12-10 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of internal combustion engine
US8132402B2 (en) 2007-04-25 2012-03-13 Toyota Jidosha Kabushiki Kaisha Exhaust purification device of internal combustion engine
US7997070B2 (en) * 2007-06-08 2011-08-16 Honda Motor Co. Ltd. Exhaust emission control device for internal combustion engine
EP2000641A2 (en) 2007-06-08 2008-12-10 HONDA MOTOR CO., Ltd. Exhaust emission control device for internal combustion engine
US20080306673A1 (en) * 2007-06-08 2008-12-11 Honda Motor Co., Ltd. Exhaust emission control device for internal combustion engine
EP2000641A3 (en) * 2007-06-08 2009-01-07 HONDA MOTOR CO., Ltd. Exhaust emission control device for internal combustion engine
EP2080873A1 (en) 2008-01-18 2009-07-22 Peugeot Citroen Automobiles SA Method for injecting a reducing agent in an exhaust line
FR2926592A1 (en) * 2008-01-18 2009-07-24 Peugeot Citroen Automobiles Sa METHOD OF INJECTING REDUCING AGENT IN AN EXHAUST LINE
US8561387B2 (en) * 2008-09-18 2013-10-22 Continental Automotive Gmbh Method for checking the seal of a reagent injector
US20100064664A1 (en) * 2008-09-18 2010-03-18 Joris Fokkelman Method for checking the seal of a reagent injector
FR2937089A1 (en) * 2008-10-13 2010-04-16 Bosch Gmbh Robert METHOD AND DEVICE FOR DIAGNOSING A DEVICE FOR DETERMINING A REACTIVE AGENT IN A COMBUSTION ENGINE
EP2388450A1 (en) * 2009-01-13 2011-11-23 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification device for internal combustion engines
EP2388450A4 (en) * 2009-01-13 2013-01-16 Toyota Motor Co Ltd Exhaust gas purification device for internal combustion engines
EP2224109A3 (en) * 2009-02-26 2011-06-15 Toyota Jidosha Kabushiki Kaisha Controller for internal combustion engine
US20130074590A1 (en) * 2009-11-26 2013-03-28 Continental Automotive Gmbh Method For Determining The State Of A Reducing Agent In A Reducing Agent Tank
WO2011075582A1 (en) * 2009-12-16 2011-06-23 Cummins Filtration Ip, Inc. Apparatus and method to diagnose a nox sensor
CN102792140A (en) * 2009-12-16 2012-11-21 康明斯过滤Ip公司 Apparatus and method to diagnose a NOx sensor
US9109493B2 (en) 2009-12-16 2015-08-18 Cummins Emission Solutions Inc. Apparatus and method to diagnose a NOX sensor
US20120017568A1 (en) * 2010-05-03 2012-01-26 Mert Geveci Ammonia sensor control, with nox feedback, of an scr aftertreatment system
US10392991B2 (en) 2010-05-03 2019-08-27 Cummins Inc. Ammonia sensor control, with NOx feedback, of an SCR aftertreatment system
US9476338B2 (en) * 2010-05-03 2016-10-25 Cummins Inc. Ammonia sensor control, with NOx feedback, of an SCR aftertreatment system
US9038373B2 (en) 2010-05-03 2015-05-26 Cummins Inc. Ammonia sensor control of an SCR aftertreatment system
CN111502804A (en) * 2011-04-05 2020-08-07 卡明斯散发控制技术公司 Systems, methods, and apparatus for aftertreatment system monitoring
US9228923B2 (en) 2011-11-30 2016-01-05 Ford Global Technologies, Llc Methods for an exhaust fluid sensor
US8505371B2 (en) * 2011-11-30 2013-08-13 Ford Global Technologies, Llc Methods for an exhaust fluid sensor
EP2650499A1 (en) * 2012-04-13 2013-10-16 Peugeot Citroën Automobiles Sa Method for monitoring the efficiency of a system for after-treatment of exhaust gas
CN103375233A (en) * 2012-04-13 2013-10-30 标致·雪铁龙汽车公司 Method for monitoring the efficiency of a system for after-treatment of exhaust gas
FR2989421A1 (en) * 2012-04-13 2013-10-18 Peugeot Citroen Automobiles Sa METHOD FOR IMPLEMENTING AN EXHAUST GAS POST-PROCESSING SYSTEM
WO2014166575A1 (en) * 2013-04-10 2014-10-16 Daimler Ag Method for operating an exhaust gas purification system of a motor vehicle combustion engine
US9644521B2 (en) 2013-04-10 2017-05-09 Daimler Ag Method for operating an exhaust gas purification system of a motor vehicle combustion engine
US9388728B2 (en) 2013-06-10 2016-07-12 Cummins Emission Solutions, Inc. Systems and methods for NOx sensor diagnostics
US9695727B2 (en) 2015-09-02 2017-07-04 Deere & Company System and method for adaptive aftertreatment control of NOx
EP3139010A1 (en) * 2015-09-02 2017-03-08 Deere & Company System and method for adaptive aftetreatment control of nox
CN106481409A (en) * 2015-09-02 2017-03-08 迪尔公司 For NOXSelf adaptation post processing control system and method
US20180038256A1 (en) * 2016-08-03 2018-02-08 Mazda Motor Corporation Exhaust emission control system of engine
US10329980B2 (en) * 2016-08-03 2019-06-25 Mazda Motor Corporation Exhaust emission control system of engine
US20220049636A1 (en) * 2020-08-14 2022-02-17 Ford Global Technologies, Llc System and method for detecting release from an injector
US11428135B2 (en) * 2020-08-14 2022-08-30 Ford Global Technologies, Llc System and method for detecting release from an injector

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