CN107542563A - Fault Identification is carried out in SCR system by means of ammonia fill level - Google Patents
Fault Identification is carried out in SCR system by means of ammonia fill level Download PDFInfo
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- CN107542563A CN107542563A CN201710500625.8A CN201710500625A CN107542563A CN 107542563 A CN107542563 A CN 107542563A CN 201710500625 A CN201710500625 A CN 201710500625A CN 107542563 A CN107542563 A CN 107542563A
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- Prior art keywords
- ammonia
- scr
- scr catalyst
- fill level
- actual
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 211
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 106
- 239000003054 catalyst Substances 0.000 claims abstract description 145
- 238000000034 method Methods 0.000 claims abstract description 39
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical class [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 11
- 238000002485 combustion reaction Methods 0.000 claims abstract description 9
- 230000008859 change Effects 0.000 claims description 11
- 238000004590 computer program Methods 0.000 claims description 9
- 238000005259 measurement Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- 230000004888 barrier function Effects 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 238000004364 calculation method Methods 0.000 claims 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 39
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 20
- 229910052757 nitrogen Inorganic materials 0.000 description 10
- 239000002912 waste gas Substances 0.000 description 9
- 238000011282 treatment Methods 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N11/00—Monitoring or diagnostic devices for exhaust-gas treatment apparatus, e.g. for catalytic activity
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
- F01N13/0093—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series the purifying devices are of the same type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2006—Periodically heating or cooling catalytic reactors, e.g. at cold starting or overheating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2066—Selective catalytic reduction [SCR]
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2550/00—Monitoring or diagnosing the deterioration of exhaust systems
- F01N2550/02—Catalytic activity of catalytic converters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2560/00—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
- F01N2560/02—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
- F01N2560/026—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting NOx
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2560/00—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
- F01N2560/14—Exhaust systems with means for detecting or measuring exhaust gas components or characteristics having more than one sensor of one kind
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2900/00—Details of electrical control or of the monitoring of the exhaust gas treating apparatus
- F01N2900/06—Parameters used for exhaust control or diagnosing
- F01N2900/16—Parameters used for exhaust control or diagnosing said parameters being related to the exhaust apparatus, e.g. particulate filter or catalyst
- F01N2900/1602—Temperature of exhaust gas apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2900/00—Details of electrical control or of the monitoring of the exhaust gas treating apparatus
- F01N2900/06—Parameters used for exhaust control or diagnosing
- F01N2900/16—Parameters used for exhaust control or diagnosing said parameters being related to the exhaust apparatus, e.g. particulate filter or catalyst
- F01N2900/1616—NH3-slip from catalyst
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2900/00—Details of electrical control or of the monitoring of the exhaust gas treating apparatus
- F01N2900/06—Parameters used for exhaust control or diagnosing
- F01N2900/16—Parameters used for exhaust control or diagnosing said parameters being related to the exhaust apparatus, e.g. particulate filter or catalyst
- F01N2900/1622—Catalyst reducing agent absorption capacity or consumption amount
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2900/00—Details of electrical control or of the monitoring of the exhaust gas treating apparatus
- F01N2900/06—Parameters used for exhaust control or diagnosing
- F01N2900/18—Parameters used for exhaust control or diagnosing said parameters being related to the system for adding a substance into the exhaust
- F01N2900/1806—Properties of reducing agent or dosing system
- F01N2900/1818—Concentration of the reducing agent
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
The present invention relates to the method that Fault Identification is carried out in the SCR system for internal combustion engine in a motor vehicle, SCR system has two SCR catalysts and two NOx sensors.Methods described includes:First SCR catalyst is heated to following temperature, can be about zero by the maximum ammonia fill level that the first SCR catalyst stores for the temperature;Adjust the ammonia fill level for setting defined in the first SCR catalyst;Measure the nitrous oxides concentration of the upstream of SCR catalyst and the nitrous oxides concentration and the summation that forms of ammonia density in the downstream by SCR catalyst;Draw the comparison of the actual ammonia fill level of the second SCR catalyst and the desired ammonia fill level of the second SCR catalyst when there is ammonia sliding;Failure at least one SCR catalyst in two SCR catalysts is identified according to the comparison of the actual ammonia fill level of the second SCR catalyst when there is ammonia sliding and desired ammonia fill level.
Description
Technical field
It is used for the present invention relates to a kind of when there is ammonia sliding by means of ammonia fill level with two SCR catalysts
The method that Fault Identification is carried out in SCR system.In addition, the present invention relates to a kind of computer program, the computer program its
Each step of methods described is performed when being run on calculator, and the present invention relates to a kind of machine readable storage medium, should
Storage medium stores the computer program.Finally the present invention relates to a kind of electronic controller, the electronic controller to be set up
For performing methods described.
Background technology
SCR(SCR)It is in current wide-scale distribution, the waste gas for making the combustion motors in motor vehicle
Nitrogen oxides(NOx)The technology of reduction.In SCR system, AdBlue will be commercially also served as®And known urine
Element-water-solution by jet module at least one SCR catalyst injected upstream into exhaust system.From the urea-water-
The ammonia separated in solution is at the SCR catalyst with SCR and reaction of nitrogen oxides generation element
Nitrogen.
Multiple SCR catalysts are used due to the introducing of stricter emission regulation, the SCR catalyst is to same
Waste gas works.In the situation of the efficiency deficiency for making SCR catalyst that the discharged nitrous oxides in the exhaust system reduce
Descend the detection method, it is specified that with vehicle itself(Generally realized in electronic controller)Carry out Fault Identification.For this reason,
Continuously monitored in the implementation during normal operation of the vehicle.For common detection method, at least one cloth is used
Put the nitrogen sensor in the upstream of the SCR catalyst and the nitrogen sensing at least one downstream for being arranged in the SCR catalyst
Device.For single SCR catalyst, two NOx sensors are enough to be used in calculating the efficiency of the SCR system simultaneously
And discharged nitrous oxides are monitored simultaneously.
The SCR system expanded in same exhaust system multiple(n)The way of SCR catalyst is according to tradition with n+
Premised on 1 NOx sensor, for by means of pin-point(Pin mark type)Strategy come obtain it is at least one without or
Less preferably play the SCR catalyst of function.Correspondingly, it can targetedly repair either to change and or less preferably not play work(
Can SCR catalyst, and preferably play the SCR catalyst of function or the SCR system then remains unaffected.But,
The use of the pin mark type strategy is not necessarily to during normal operation the vehicle, because herein only to the efficiency
It is monitored just enough.For in the case of the SCR catalyst of function or is not less preferably played, than if passing through
Signal lamp on instrument board alarms to driver, and the vehicle is such as reached maintenace point by subsequent driver.Tieed up in maintenace point
During repairing, using the pin mark type strategy being previously mentioned in detection method, work(or is not less preferably played for acquisition is described
The SCR catalyst of energy.
The content of the invention
Methods described is related to the SCR system of the combustion motors in motor vehicle.Here, the SCR system is common at one
There are two SCR catalysts successively arranged in exhaust system.Waste gas first passes around the first SCR catalyst and then continues to lead
Give the second SCR catalyst so that two SCR catalysts work to the waste gas.In addition, the SCR system has two
NOx sensor, the NOx sensor are equally arranged in this exhaust system.First NOx sensor cloth
Put in the upstream of described two SCR catalysts, and can there measure and exhaust-gas treatment is being carried out by the SCR catalyst
Nitrous oxides concentration before.Second nitridation nitrogen sensor arrangement is in the downstream of described two SCR catalysts and can be at that
In measurement summation for being made up of nitrous oxides concentration and ammonia density after exhaust after-treatment is carried out by the SCR catalyst,
Wherein described ammonia density and the ammonia occurred when ammonia fill level exceedes maximum ammonia fill level slide(Ammoniak-
Schlupf)It is consistent.
It the described method comprises the following steps.First SCR catalyst is heated to following temperature first, for the temperature
Almost can be zero by the maximum ammonia fill level that first SCR catalyst stores for degree.This is than if under
It is accomplished to state mode:The temperature dependency of the maximum ammonia fill level shows and therefrom obtained down as characteristic curve
Temperature is stated, the characteristic curve is less than the limiting value of defined for the temperature.Especially this temperature arrives in 400 DEG C
In the range of 600 DEG C.It is noted that the temperature of second SCR catalyst is preferably kept into alap degree so that
Second SCR catalyst can store ammonia loading almost corresponding with normal operation.It is preferred that pass through the SCR catalyst
Upstream hot-fluid, such as first SCR catalyst is added by the heating for the waste gas in the internal combustion engine
Heat.Compared with also only meeting with the second SCR catalyst of less hot-fluid, due to thus causing for first SCR catalyst
Higher heat exchange and easily reach desired temperature difference.
Then, the ammonia fill level for setting defined in first SCR catalyst is adjusted.The ammonia fill level of defined
(Ammoniak-Füllstand)In the maximum ammonia fill level by that can be stored in second SCR catalyst and also
On the summation formed when former with the ammonia fill level of the reaction of nitrogen oxides.Can correspondingly it contemplate, not described
The ammonia amount for being used to reduce nitrogen oxides in one SCR catalyst is stored in second SCR catalyst completely.
Then measure the nitrous oxides concentration of the upstream of the SCR catalyst and the downstream by the SCR catalyst
The summation that nitrous oxides concentration and ammonia density are formed.Traditional NOx sensor has laterally sensitive relative to ammonia density
Property, thus the NOx sensor in the downstream by being arranged in the SCR catalyst is enabled in particular to measure by the nitrogen oxygen
The summation that compound concentration and the ammonia density are formed.Especially by the summation signals that the sensor measures relative to desired nitrogen
The change of oxide concentration may originate from the ammonia density consistent with the sliding of the ammonia of second SCR catalyst.The ammonia sliding
Show following ammonia amount, this ammonia amount passes through the SCR catalyst, without participating in the reduction.It is preferred that urged from described two SCR
Change the actual ammonia loading that the second SCR catalyst described in when the ammonia sliding occur is obtained in the ammonia density in the downstream of device.
It can provide in another aspect, be obtained from the characteristic curve for second SCR catalyst and the ammonia cunning occurring
The desired ammonia loading of second SCR catalyst described in during shifting(Ammoniak-Füllmenge).
In further process, during the analysis phase, implement the 2nd SCR catalysis described in when the ammonia sliding occur
The comparison of the actual ammonia loading of device and desired ammonia loading.Finally, identify on basis of the comparison described
The failure at least one SCR catalyst in two SCR catalysts.If here it is preferred, in particular, that there is the ammonia
The actual ammonia loading of second SCR catalyst described in during sliding is different from desired ammonia loading, then identifies described
Failure in two SCR catalysts,.
Alternatively, can methods described the nitrogen oxides implemented at the beginning for the upstream of the SCR catalyst it is dense
The measurement of degree and for described two SCR catalysts downstream nitrous oxides concentration measurement.Here, described two SCR
Catalyst converter works in normal operation.If the nitrous oxides concentration in the downstream of described two SCR catalysts and desired nitrogen
Oxide concentration is not consistent, then identifies the failure in the SCR system.If here it is preferred, in particular, that as described
Identify the failure in the SCR system like that and extraly when there is ammonia sliding described in the second SCR catalyst
Actual ammonia loading and desired ammonia loading is consistent, then identifies the failure in first SCR catalyst.
It can provide in another aspect, faulty catalyst converter is repaired or changed on the basis of methods described
Afterwards, the distance of the motor-driven vehicle going defined and/or time and then methods described is implemented again.Thus also to described
Two SCR catalysts have a case that failure is this in the identical time and rare taken in.Alternatively, can implement again
Also the analysis phase is changed during methods described, so as to cover bigger fault spectrum(Fehlerspektrum).
The computer program is configured for:Especially implement the side when it is being implemented on calculator or controller
Each step of method.The computer program can implement methods described in traditional electronic controller, without entering to it
Change in row structure.Therefore, the computer program is stored in the machine readable storage medium.
The electronic controller is obtained by the way that the computer program is loaded on traditional electronic controller, the electricity
Sub-controller is configured for implementing Fault Identification in the SCR system.Here, the electronic controller can not only be car
Itself controller and also can be outside controller, such as diagnostor, the controller of the outside is carrying out failure knowledge
It is connected during not with the SCR system and controls methods described.
Brief description of the drawings
Embodiments of the invention are shown in the drawings and are explained in detail in the following description.Wherein:
Fig. 1 schematically shows SCR system, and the SCR system includes two SCR catalysts and three NOx sensors simultaneously
And Fault Identification can be implemented by means of traditional method;
Fig. 2 schematically shows SCR system, and the SCR system includes two SCR catalysts and two NOx sensors simultaneously
And by means of Fault Identification can be implemented in the present inventive method;
Fig. 3 shows a kind of flow chart of embodiment in the present inventive method;And
Fig. 4 shows the chart of the temperature dependency of the ammonia fill level of SCR catalyst, it is described in the present inventive method one
The temperature dependency can be used in kind embodiment.
Embodiment
Figure 1 illustrates a kind of common SCR system 100 of the unshowned combustion motors in motor vehicle, the SCR systems
System has the first SCR catalyst 101 and the second SCR catalyst 102, and tradition can be used for above-mentioned two SCR catalyst
Method identify failure.Described two priorities of SCR catalyst 101 and 102 are arranged in exhaust system 120, wherein described first
SCR catalyst 101 is arranged to closer to jet module 130, and the jet module is by urea-water-solution in described two SCR
The injected upstream of catalyst converter 101 and 102 is into the exhaust system 120.In addition, the SCR system 100 includes the first nitrogen oxides
Sensor 110, first NOx sensor are arranged between the jet module 130 and first SCR catalyst 101
And the nitrogen oxidation of the waste gas before exhaust after-treatment is carried out by the SCR catalyst 101 and 102 can be measured there
Thing concentration NOx_Before processing.In addition, the SCR system 100 includes the second NOx sensor 111, second nitrogen oxides sensing
Device is arranged in the downstream of second SCR catalyst 102 and can measured there by described two SCR catalysts
The nitrogen concentration NOx_ of waste gas after 101 and 102 progress exhaust after-treatmentsAfter processing.The SCR system also extraly includes the 3rd nitrogen
Oxide sensor 112, the 3rd NOx sensor are arranged in first SCR catalyst 101 and urged with the 2nd SCR
It can measure between change device 102 and there useless after exhaust after-treatment is carried out by first SCR catalyst 101
The nitrous oxides concentration of gas.Three NOx sensors 110,111 and 112 and the jet module 130 that are previously mentioned with
Electronic controller 140 is connected and controlled by the electronic controller.
In the method for being traditionally used for carrying out Fault Identification, the sum at first NOx sensor 110 is obtained
The actual difference of nitrous oxides concentration at 3rd NOx sensor 112, or obtain the 3rd nitrogen oxidation
The actual difference of nitrous oxides concentration at thing sensor 112 and described second NOx sensor 111, and will
It is compared with desired difference.If at least one difference and corresponding desired difference in the actual difference
It is worth inconsistent, then to be inferred in the SCR catalyst 101 or 102 that is formed therebetween failure.
Fig. 2 shows the SCR system 200 of the unshowned combustion motors in motor vehicle, and the SCR system equally includes first
The SCR catalyst 202 of SCR catalyst 201 and second, can be by means of described by the present invention's for above-mentioned two catalyst converter
A kind of embodiment of method identifies failure.Described two SCR catalysts 201 and 202 are correspondingly successively arranged in exhaust system
In 220, wherein first SCR catalyst 201 is arranged to closer to jet module 230 as previously described.
But, SCR system 200 herein shown only include being arranged in jet module 230 and first SCR catalyst 201 it
Between the first NOx sensor 210 and be arranged in second SCR catalyst 202 downstream the second nitrogen oxides sensing
Device 211.Described two SCR catalysts 210 and 211 and the jet module 230 are connected and at least with electronic controller
Controlled during Fault Identification is carried out by the electronic controller.In another embodiment, the electronic controller energy
Enough it is outside equipment, the equipment of the outside is connected during Fault Identification is carried out with the SCR system 200.
First NOx sensor 210 measures to be located after waste gas is carried out by the SCR catalyst 101 and 102
The nitrous oxides concentration NOx_ of waste gas before reasonBefore processing, and second NOx sensor 211 according to it relative to ammonia
The horizontal sensitivity of concentration measures by useless after exhaust after-treatment is carried out by described two SCR catalysts 101 and 102
The nitrogen concentration NOx_ of gasAfter processingWith ammonia density NHAfter 3_ processingThe summation signals of composition.Fig. 2 SCR system 200 therefore the SCR systems with Fig. 1
Differing only in for system has lacked the 3rd NOx sensor 112.
Implement by a kind of the of method for being used to carry out Fault Identification in SCR system 200 described above of the present invention
Example as flow chart figure 3 illustrates.It is dense to the nitrogen oxides at first NOx sensor 210 in the first step
Spend NOx_Before processingWith the nitrous oxides concentration NOx_ at second NOx sensor 211After processingImplement measurement 300.If
The nitrous oxides concentration NOx_ after exhaust after-treatment is carried out by described two SCR catalysts 201 and 202After processingWith from described
Nitrous oxides concentration NOx_Before processingDifferent with the desired numerical value obtained in the conversion ratio of described two SCR catalysts, that is just known
The failure not haveing in 301 SCR systems 200.That is, at least one SCR catalyst in described two SCR catalysts
201 or 202, there are the two SCR catalysts that there is functional fault and/or at least one reduce in the case of rare
Conversion ratio.If not identifying the failure in 301 SCR systems 200, terminate 302 methods describeds.
Otherwise, the combustion motors conversion 303 of the motor vehicle of stopping is existed into idle running and then in another step
304 combustion motors are run in the operating point of defined.Then wait always, until first NOx sensor
Nitrous oxides concentration NOx_ at 210Before processingWith the nitrous oxides concentration NOx_ at second NOx sensor 211After processing
It is identical.First SCR catalyst 201 is then heated 306 and arrives following temperature T, for the temperature, described first
The maximum ammonia fill level NH of SCR catalyst 2013_ maximum fill levelsAlmost it is zero.The temperature of first SCR catalyst is used for this
The characteristic curve 400 of correlation is spent, as illustrated in Figure 4.In such an embodiment, the temperature(T)About 500
℃.Then by the urea-water-solution injection 306 into the exhaust system 220.
Therefore, the ammonia fill level NH in first SCR catalyst 2013_ fill levelsIncrease to the numerical value of defined always.
This defined numerical value is in the maximum ammonia fill level NH of second SCR catalyst 2023_ maximum fill levelsWith described first
On the ammonia amount reacted in SCR catalyst 201 when the nitrogen oxides reduces.As a result, by all in the nitrogen oxidation
The ammonia reacted when thing reduces not at first SCR catalyst 201 hands to second SCR catalyst 202.Due to height
In the maximum ammonia fill level NH of second SCR catalyst3_ maximum fill levelsAmmonia fill level NH3_ fill levels, described second
Occurs ammonia sliding at SCR catalyst 202, not stored ammonia amount passes through this SCR catalyst for ammonia sliding
202, the reduction without participating in the nitrogen oxides.
If reach the ammonia fill level NH of defined3_ fill levels, then on the one hand first nitrogen oxides is sensed again
Nitrous oxides concentration NOx_ at device 210Before processingAnd the nitrous oxides concentration by second NOx sensor 211
NOx_After processingWith ammonia density NHAfter 3_ processingThe summation signals of composition implement measurement 308.The ammonia density NHAfter 3_ processingInstitute can be attributed to
State the ammonia sliding occurred at the second SCR catalyst.Therefore, once the summation signals are obtained by the ammonia sliding occurred
Improve, then obtain the ammonia fill level NH actual when there is the ammonia sliding3_ is actual.On the other hand, urged from the 2nd SCR
Change and the ammonia fill level NH desired when there is the ammonia sliding is obtained in the characteristic curve 500 of device3_ is expected, wherein described first
The maximum ammonia fill level NH of second SCR catalyst3_ maximum fill levelsAs reference.
In comparing 311, during the analysis phase, when will occur the ammonia sliding at second SCR catalyst 202
Actual ammonia fill level NH3_ is actualWith desired ammonia fill level NH3_ is expectedCompareed.If the actual ammonia filling
Horizontal NH3_ is actualWith desired ammonia fill level NH3_ is expectedDifference, then identify the event in 320 second SCR catalysts 202
Barrier.As further step 321, faulty second SCR catalyst 202 is repaired or changed.If the reality
The ammonia fill level NH on border3_ is actualWith desired ammonia fill level NH3_ is expectedIt is consistent, then the 2nd SCR catalysis is not can determine that
Failure at device 202.But because in the failure measured in identifying the SCR system 200 in 300, it can set
Think, first SCR catalyst 201 is faulty.Correspondingly, 330 first SCR catalysts are identified in this case
Failure in 201.Herein, as further step 331, faulty first SCR catalyst 201 is repaired or
Change.
In order to exclude all faulty this rare situation of described two SCR catalysts 201 and 202, identifying first
During failure in 320 second SCR catalysts 202, time and/or distance as defined in the motor-driven vehicle going 340.Then from
Methods described is repeated at the beginning.Provide in another embodiment, change the analysis phase when repeating methods described.
Fig. 4 shows the maximum ammonia fill level NH3_ maximum fill levelsThe characteristic curve 400 depending on temperature T.This
In embodiment, the maximum ammonia fill level of second SCR catalyst 202 on 401 is being put when temperature is 500 DEG C
NH3_ maximum fill levelsIt is not different with zero.It is noted that the temperature where the point 401 depends on used SCR catalyst simultaneously
And such as it may be about in another embodiment as 450 DEG C.
Claims (11)
1. the SCR system for internal combustion engine in a motor vehicle(200)The middle method for carrying out Fault Identification, the SCR system tool
There are two SCR catalysts(201;202)With two NOx sensors(210;211), one of NOx sensor
(210)It is arranged in described two SCR catalysts(201;202)Upstream, an and NOx sensor(211)It is arranged in
The downstream of described two SCR catalysts, the described method comprises the following steps:
- by the first SCR catalyst(201)Heating(306)To following temperature(T), can be by described for the temperature
One SCR catalyst(201)The maximum ammonia fill level of storage(NH3_ maximum fill levels)About zero;
- tune is set(307)First SCR catalyst(201)The ammonia fill level of middle defined(NH3_ fill levels), the ammonia of defined
Fill level, which is in, is used for the second SCR catalyst(202)Maximum ammonia fill level(NH3_ maximum fill levels)On;
- measurement(308)The SCR catalyst(201;202)Upstream nitrous oxides concentration(NOx_Before processing)And by described
SCR catalyst(201;202)Downstream nitrous oxides concentration(NOx_After processing)And ammonia density(NHAfter 3_ processing)The summation of composition;
- during the analysis phase, will the second SCR catalyst described in when ammonia sliding occur(202)Actual ammonia fill level
(NH3_ is actual)With when there is ammonia sliding described in the second SCR catalyst(202)Desired ammonia fill level(NH3_ is expected)Carry out
Compare(311);
- according to the second SCR catalyst described in when ammonia sliding occur(202)Actual ammonia fill level(NH3_ is actual)With it is pre-
The ammonia fill level of phase(NH3_ is expected)Comparison(311)To identify(320;330)Described two SCR catalysts(201;202)In
At least one SCR catalyst in failure.
2. the method as described in claim 1, it is characterised in that if the second SCR catalyst described in when ammonia sliding occur
(202)Actual ammonia fill level(NH3_ is actual)With desired ammonia fill level(NH3_ is expected)It is different(311), then identify
(320)Second SCR catalyst(202)In failure.
3. the method as described in claim 1, it is characterised in that at the beginning to the SCR catalyst(202;203)Upstream
Nitrous oxides concentration(NOx_Before processing)And by described two SCR catalysts(201;202)Downstream nitrous oxides concentration
(NOx_After processing)And ammonia density(NHAfter 3_ processing)The summation of composition implements measurement(300), two of which SCR catalyst(201;202)
Worked in normal operation, and if by described two SCR catalysts(201;202)Downstream nitrous oxides concentration
(NOx_After processing)And ammonia density(NHAfter 3_ processing)The summation of composition is not consistent with desired nitrous oxides concentration, then identifies(301)
The SCR system(200)In failure.
4. the method as described in claim 3, it is characterised in that if identified(301)The SCR system(200)In event
Barrier and the second SCR catalyst described in when ammonia sliding occur(202)Actual ammonia fill level(NH3_ is actual)With it is desired
Ammonia fill level(NH3_ is expected)It is consistent(311), then identify(330)First SCR catalyst(201)In failure.
5. the method as any one of preceding claims, it is characterised in that repairing or changing(321;331)There is event
The catalyst converter of barrier(201;202)Afterwards, the motor-driven vehicle going(340)The distance of defined and/or time and then repeat
Methods described.
6. the method as described in claim 5, it is characterised in that change the analysis phase when repeating methods described.
7. the method as any one of preceding claims, it is characterised in that the 2nd SCR described in when ammonia sliding occur is urged
Change device(202)Actual ammonia fill level(NH3_ is actual)From described two SCR catalysts(201;202)Downstream ammonia density
(NHAfter 3_ processing)Middle acquisition(309).
8. the method as any one of preceding claims, it is characterised in that the 2nd SCR described in when ammonia sliding occur is urged
Change device(202)Desired ammonia fill level(NH3_ is expected)From for second SCR catalyst(202)Characteristic curve
(500)Middle acquisition(310).
9. computer program, the computer program is configured for:Implement the side as any one of claim 1 to 8
Each step of method.
10. machine readable storage medium, stored in the machine readable storage medium based on described in claim 9
Calculation machine program.
11. electronic controller, the electronic controller is configured for:By means of as any one of claim 1 to 8
Method implements Fault Identification in the SCR system.
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109339918A (en) * | 2018-12-03 | 2019-02-15 | 潍柴动力股份有限公司 | Mixer crystallizes detection method, mixer crystallizing treatment process and device |
CN110173333A (en) * | 2018-02-19 | 2019-08-27 | 罗伯特·博世有限公司 | Method for being monitored to nitrogen oxides-storage type catalyst converter |
CN111601957A (en) * | 2018-01-19 | 2020-08-28 | 戴姆勒股份公司 | Method for operating an exhaust gas system of a motor vehicle internal combustion engine and exhaust gas system for a motor vehicle internal combustion engine |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT521117B1 (en) * | 2018-04-06 | 2022-04-15 | Avl List Gmbh | Procedure for checking the function of SCR catalytic converters in an SCR system |
US10808590B2 (en) * | 2018-07-03 | 2020-10-20 | Fca Us Llc | Selective catalytic reduction adaptation for accuracy and minimized tailpipe impact |
DE102018217047B4 (en) * | 2018-10-05 | 2022-01-27 | Vitesco Technologies GmbH | Method and device for determining a state of an exhaust gas treatment element for a motor vehicle |
CN113339113B (en) * | 2021-07-15 | 2022-08-19 | 中国能源建设集团江苏省电力设计院有限公司 | Method and system for predicting NOx generation and ammonia demand of SCR system and storage medium |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101278110A (en) * | 2005-09-29 | 2008-10-01 | 沃尔沃拉斯特瓦格纳公司 | Diagnosis method for exhaustion reprocessing system |
DE102008041603A1 (en) * | 2008-08-27 | 2010-03-04 | Robert Bosch Gmbh | Method for operating an internal combustion engine with SCR catalytic converter |
JP2010077812A (en) * | 2008-09-24 | 2010-04-08 | Mazda Motor Corp | Exhaust emission control device for engine |
WO2014072607A1 (en) * | 2012-11-12 | 2014-05-15 | Peugeot Citroen Automobiles Sa | Device for purifying exhaust gas with a controlled injection of reducing agent |
JP2014101778A (en) * | 2012-11-19 | 2014-06-05 | Toyota Industries Corp | Exhaust emission control system |
CN104343512A (en) * | 2013-07-30 | 2015-02-11 | 曼卡车和巴士股份公司 | Method and apparatus for determining efficiency of exhaust gas purification device |
CN105308282A (en) * | 2013-06-28 | 2016-02-03 | 雷诺股份公司 | System and method for diagnosing the selective catalytic reduction system of a motor vehicle |
-
2016
- 2016-06-28 DE DE102016211575.8A patent/DE102016211575A1/en active Pending
-
2017
- 2017-06-27 CN CN201710500625.8A patent/CN107542563B/en active Active
- 2017-06-27 KR KR1020170081286A patent/KR20180002057A/en active Search and Examination
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101278110A (en) * | 2005-09-29 | 2008-10-01 | 沃尔沃拉斯特瓦格纳公司 | Diagnosis method for exhaustion reprocessing system |
DE102008041603A1 (en) * | 2008-08-27 | 2010-03-04 | Robert Bosch Gmbh | Method for operating an internal combustion engine with SCR catalytic converter |
JP2010077812A (en) * | 2008-09-24 | 2010-04-08 | Mazda Motor Corp | Exhaust emission control device for engine |
WO2014072607A1 (en) * | 2012-11-12 | 2014-05-15 | Peugeot Citroen Automobiles Sa | Device for purifying exhaust gas with a controlled injection of reducing agent |
JP2014101778A (en) * | 2012-11-19 | 2014-06-05 | Toyota Industries Corp | Exhaust emission control system |
CN105308282A (en) * | 2013-06-28 | 2016-02-03 | 雷诺股份公司 | System and method for diagnosing the selective catalytic reduction system of a motor vehicle |
CN104343512A (en) * | 2013-07-30 | 2015-02-11 | 曼卡车和巴士股份公司 | Method and apparatus for determining efficiency of exhaust gas purification device |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111601957A (en) * | 2018-01-19 | 2020-08-28 | 戴姆勒股份公司 | Method for operating an exhaust gas system of a motor vehicle internal combustion engine and exhaust gas system for a motor vehicle internal combustion engine |
CN111601957B (en) * | 2018-01-19 | 2022-03-22 | 戴姆勒股份公司 | Method for operating an exhaust gas system of a motor vehicle internal combustion engine and exhaust gas system for a motor vehicle internal combustion engine |
CN110173333A (en) * | 2018-02-19 | 2019-08-27 | 罗伯特·博世有限公司 | Method for being monitored to nitrogen oxides-storage type catalyst converter |
CN109339918A (en) * | 2018-12-03 | 2019-02-15 | 潍柴动力股份有限公司 | Mixer crystallizes detection method, mixer crystallizing treatment process and device |
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