WO2007054485A1 - The use of a reduction agent generating system, in particular as auxiliary heating - Google Patents
The use of a reduction agent generating system, in particular as auxiliary heating Download PDFInfo
- Publication number
- WO2007054485A1 WO2007054485A1 PCT/EP2006/068158 EP2006068158W WO2007054485A1 WO 2007054485 A1 WO2007054485 A1 WO 2007054485A1 EP 2006068158 W EP2006068158 W EP 2006068158W WO 2007054485 A1 WO2007054485 A1 WO 2007054485A1
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- WO
- WIPO (PCT)
- Prior art keywords
- heat
- motor vehicle
- heating
- hot gas
- reducing agent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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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
- 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
- F01N3/206—Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
- 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
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features having two or more separate purifying devices arranged in series
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/02—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a heat exchanger
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/14—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a fuel burner
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/25—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an ammonia generator
-
- 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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/28—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a plasma reactor
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/30—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a fuel reformer
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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
- F01N2610/00—Adding substances to exhaust gases
- F01N2610/02—Adding substances to exhaust gases the substance being ammonia or urea
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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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Definitions
- the invention relates to a reducing agent-generating system of an exhaust system of a motor vehicle according to the preamble of claim 1.
- the heat element of the reducing agent generating system (hereinafter called system) is also used to conduct heat to at least one non-system device.
- a heat coupling element is provided, which selectively supplies the heat generated by means of the heat element either to the components which generate the reducing agent, or at least to a system-foreign device. It is also conceivable that the heat is delivered to both assemblies at the same time. Accordingly, the heating element is used for a further purpose, namely heating of system-external devices of the vehicle.
- the heat element is designed as a hot gas delivering heat element.
- the hot gas which preferably originates from a burner, is therefore supplied via the heat coupling element of the system-foreign device, if this mode is desired.
- the word "selectable" mentioned in claim 1 means that a switchover possibility exists to supply the heat only when necessary by means of the heat coupling element of the system-foreign device.
- the heat coupling element has a gas flow path for the hot gas. Accordingly, when the supply of heat to the non-system device is desired, the hot gas is introduced into the gas flow path and thereby reaches the point of use.
- an interior heating of a passenger compartment of the motor vehicle is considered as a system-external device.
- the system-foreign device is an internal combustion engine of the motor vehicle. Consequently, the passenger compartment of the motor vehicle and / or the internal combustion engine of the motor vehicle can be heated with the heat of the heating element. This is particularly advantageous before the starting phase of the internal combustion engine, since a warm start of the engine, especially in winter, this considerably protects and can reduce the environmental impact and fuel consumption.
- a development of the invention provides that the gas flow path of the heat coupling element with a heat exchanger, in particular a stationary heating heat exchanger, a cooling water circuit of the motor vehicle is connectable.
- the heat of the heating element is selectively supplied to the auxiliary heating heat exchanger, whereby the cooling water of the motor vehicle is heated.
- a heating heat exchanger can be operated, which is located in the cooling water circuit and therefore heat is provided for heating the passenger compartment. This increases the comfort of the occupants and the safety of the traffic, as the panes of the passenger compartment do not fog up, the driver does not have a prolonged reaction time at low temperatures and the driver does not have to wear thick clothing when driving.
- the invention relates to a method for operating a reducing agent-generating system of an exhaust system of a motor vehicle, with a heat element that generates heat necessary for the operation of the system, wherein the heat generated by the heat element or a portion thereof also for heating at least one non-system device of the motor vehicle is used.
- the invention relates to a motor vehicle with a reducing agent-generating system according to the preceding embodiments.
- the invention relates to the use of a heat element of a reducing agent-generating system of a Abgas- anläge a motor vehicle for the purpose of heating at least one non-system device of the motor vehicle.
- Figure 1 is a schematic representation of the reducing agent-generating system
- FIGS. 1 to Figure 5 are schematic representations of the reduction-generating system according to further embodiments of the invention.
- FIG. 1 shows a reducing agent-generating system (RGS) 1 assigned to a vehicle, not shown, which has two inputs 3 and 5.
- RGS reducing agent-generating system
- These belong to a nitric oxide generator unit, which can be realized by a thermal plasma, in particular with a so-called Plasmatron 7 with an integrated heating element 9, which is designed as a starting burner.
- a plasmatron is a plasma-generating system whose plasma zone is superimposed by a gas flow and is used scientifically or technically outside of a plasma generation unit.
- the Plasmatron 7 has an output. This is connected to a branch 11, which splits the path into two parts, namely in a standard way 13 and a parking heater 15th In Standardweg 13 is a shut-off 17, which is designed as a 2-2 valve.
- auxiliary heating path 15 again meets the standard route 13 after passing through a heat exchanger 37.
- a catalytic component 21 which is linked to an ammonia generator unit 23, hereinafter referred to as AGC for Ammonia Generating Catalyst or simply as NH 3 generator.
- an exhaust system 25 is present, which is connected to an internal combustion engine 27 of the motor vehicle, which is connected to a diesel oxidation catalyst (DOC) 29.
- DOC diesel oxidation catalyst
- DPF diesel particulate filter
- SCR device 33 which is used to remove nitrogen oxides in oxygen-containing exhaust gases and to reduce them to nitrogen and water.
- AGC ammonia generated by the ammonia generator unit
- the heat exchanger 37 is connected to the branch 11. This can be formed for example as a parking heater heat exchanger. Coming from this heat exchanger 37, a return 39 is provided, which is linked to the branch 19. There, the parking heater 15 again connects to the standard way 13.
- the heat exchanger 37 is connectable / connected to a cooling water circuit 41 of the motor vehicle.
- the heat required for this supplies the heated by the heating element 9 hot gas.
- the ammonia is passed via the junction 35 in the exhaust system 25 and used in the SCR device 33 for the exhaust gas treatment.
- the still put into operation heat element 9 can be used, ie the heat element 9 provides hot gas.
- the heat of the hot gas can be used in particular for non-use of the RGS 1 for heating system-external devices 59 of the motor vehicle, namely the internal combustion engine 27 and / or a passenger compartment of the motor vehicle, which is not shown in FIG.
- a heat coupling element 55 which diverts the heat into a usable form for this purpose, is used. This includes according to Figure 1, the branch 11, an inlet 57 of the parking heater 15, the heat exchanger 37, the return 39, the junction 19 and the shut-off 17.
- the hot gas via the guide 57 in the heat exchanger 37 headed.
- a heat exchange with the cooling water of a cooling water circuit 41 of the internal combustion engine 27 takes place.
- the heat exchanger 37 forms in particular a stationary heating heat exchanger, ie he serves the heating of non-system devices 59 of the particular non-moving motor vehicle.
- the heated cooling water is used for heating (preheating) of the internal combustion engine 27.
- a heating heat exchanger may be provided which uses the heat of the cooling water for heating the passenger compartment.
- the hot gas is then returned to the RGS 1, namely via the return 39 into the branch 19, and finally enters the exhaust system of the internal combustion engine 27.
- the heat coupling element 55 has a gas flow path 61 for the hot gas.
- the core of the invention is accordingly to use the starting burner of the RGS 1 as a heater.
- the internal combustion engine 27 preheated and / or the passenger compartment of the motor vehicle can be preheated.
- the start burner of the RGS 1 (ammonia generator) is not needed, ie in particular before a start of the internal combustion engine, then this is available for the new, inventive purpose.
- the auxiliary heater is used, among other things, the temperature comfort of the occupants. However, it also serves road safety, as it does not fogged windows and does not lead to a prolonged reaction time of the driver due to low temperatures. This also does not need unnecessarily thick clothing.
- the possible by the invention warm start of the engine, especially in winter protects the components and can (with a correspondingly low-emission auxiliary heater) reduce the environmental impact and fuel consumption. Furthermore, the resale value of the vehicle is increased by the auxiliary heater.
- NH 3 is prepared from the starting materials NO and H 2 .
- NO is generated in a lean phase (in air or exhaust mode with ⁇ > 1) in a Plasmatron 7 in air. These nitrogen oxides then flow through the catalytic partial oxidation state (cPOx) and are in the downstream of the catalytic unit (NH 3 - Producer).
- cPOx catalytic partial oxidation state
- the fat phase (0.33 ⁇ ⁇ 1)
- liquid fuel is metered into an evaporation and mixture-forming zone in the area of the plasmatron 7 and in the cPOx stage (catalytic partial oxidation).
- the SCR catalyst has an NH 3 storage capacity, it is possible to continuously achieve the reduction of the nitrogen oxides by means of an SCR process in the exhaust gas full flow, even via a discontinuous process for producing ammonia.
- the catalysts of titanium dioxide (TiO 2) and vanadium pentoxide (V2O5) to set the nitrogen oxides with the produced ammonia at a high rate.
- the invention is accordingly based on the fact that hot combustion gases of the starting burner are used in the auxiliary heating mode.
- the parking heater 15 is no longer used, but the standard way 13, so that the system can be operated again as NH3 generator. It is also a mixed operation conceivable, so both NH 3 production and the heating system-independent devices 59th
- the embodiment of Figure 2 corresponds substantially to that of Figure 1.
- the reference numerals of Figure 2 correspond to those of Figure 1, so that a detailed description is omitted.
- the object of Figure 2 differs only in that instead of a 2-2 valve, a linear valve is used as a shut-off 17, which allows to direct only a partial flow of the hot gas through the heat exchanger 37 and thus the temperature of the catalytic lytica component 21 (cPOx stage) by the other partial flow of the hot gas to raise. This can after reaching a Light-off temperature greatly reduce the HC and CO emissions of the entire burner exhaust gas.
- FIG. 3 also largely corresponds to the arrangement in FIG. 1, so that a detailed description is dispensed with. It is again true that the reference numerals correspond to those of the description of Figure 1.
- the branch 11 is provided after the catalytic component 21. This is followed, as in Figure 1 in Standardweg 13 a shut-off 17 and then the branch 19, where the auxiliary heating path 15 again meets the standard path 13.
- the catalytic component 21 is flowed through in any case (ie also in the auxiliary heating mode) by the hot gas and is operable. This also results in a strong reduction of HC and CO emissions.
- FIG. 4 likewise largely resembles FIG. 1.
- the reference numbers of the description of FIG. 1 correspond to those of FIG. 4.
- a difference from FIG. 1 is that in the auxiliary heating path 15 the hot gas no longer enters the standard path 13 after passing through the heat exchanger 37 is returned before the ammonia generator unit 23, but is introduced directly into the exhaust system 25 in front of the SCR device 33.
- two valves 45 and 47 are provided in the auxiliary heating path 15 .
- the valve 45 is located between the AGC 23 and the confluence 35 in the standard path 13.
- the valve 47 is provided in the stationary heating path 15 between the heat exchanger 37 and a junction 43 which is located in the exhaust system 25 in front of the SCR device 33.
- the hot gas can be conducted either through the standard path 13 and / or through the auxiliary heating path 15.
- FIG. 5 shows a further possible arrangement of the invention.
- the reference numerals used here correspond to those of the description of FIG. 1, so that a detailed description is given. is omitted.
- a valve 49 not shown in detail, which is arranged between the catalytic component 21 and the AGC 23. From the valve 49, a connection 51 additionally goes to the exhaust system 25 (between the internal combustion engine 27 and the catalytic converter 29) and the return 39 of the auxiliary heating system 15 is likewise coupled to the valve 49.
- the valve 49 may be formed as a 4-4 valve, wherein intermediate positions may be possible, as is possible for example in a linear valve.
- the default path 13 is run through with setting a.
- the catalytic component 21 is coupled to the exhaust system 25 via the connection 51.
- the hot gas is in this case passed directly via the catalytic component 21 and the connection 51 into the exhaust system 25.
- the exhaust system 25 is connected to the AGC 23 via the connection 51.
- the exhaust gas is conducted from the engine 27 via the connection 51 into the AGC 23.
- the auxiliary heating path 15 is traversed, wherein the hot gas is conducted around the catalytic component 21 in this arrangement and impinges on the standard path 13 at the valve 49.
- ß Generating Sets is operated in a position the system as NH.
- position b the use of the RGS 1 in a prolonged fat phase with H 2 / CO generation for the regeneration of the diesel particulate filter 31 (DPF regeneration) is used.
- setting c it is possible to use the engine exhaust to heat the AGC 23.
- the burner exhaust gas is passed over the auxiliary heating heat exchanger.
- the burner exhaust gas can be taken via the AGC 23 and an optional small diesel particulate filter or can be routed directly via the gas path to the main exhaust tract in front of the diesel particulate filter.
- a particulate filter within the RGS 1, can be installed, which it allows to filter the particles from the burner exhaust gas.
- the cleaning or regeneration of the particulate filter, which is then provided in the RGS 1, can be achieved by the hot gas which is conducted via the standard route 13.
- the particle filter also filters the particles that are formed in the fat phase in standard operation of the RGS 1.
- the heating element 9 can be operated in such a way that the nitrogen oxides (NO x ) are reduced at the AGC 23.
- the burner most of the burner can be run lean and the AGC stores the nitrogen oxides. To regenerate the memory, the burner (heat element 9) must then be briefly operated in fat ( ⁇ ⁇ 1).
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Abstract
Description
Nutzung eines reduktionsmittelgenerierenden Systems insbesondere als StandheizungUse of a reducing agent-generating system, in particular as auxiliary heating
Die Erfindung betrifft ein reduktionsmittelgenerierendes System einer Abgasanlage eines Kraftfahrzeuges gemäß Oberbegriff des Anspruchs 1.The invention relates to a reducing agent-generating system of an exhaust system of a motor vehicle according to the preamble of claim 1.
Stand der TechnikState of the art
In der Kraftfahrzeugtechnik sind Vorrichtungen zur selektiven kataly- tischen Reduktion (SCR) bekannt, um in sauerstoffhaltigen Abgasen Stickoxide (NOx) zu entfernen und zu Stickstoff und Wasser zu redu- zieren. Als Reduktionsmittel wird hierzu vorzugsweise Ammoniak (NH3) verwendet. Bei mobilen Anwendungen ist es aus Sicherheitsgründen nicht ratsam, große Mengen Ammoniak im Fahrzeug mit zu führen. Deshalb wird es aus unkritischen Substanzen mittels eines reduktionsmittelgenerierenden Systems (RGS) on board, also im Fahrzeug, hergestellt und für die Abgasbehandlung verwendet. Um aus den erwähnten unkritischen Substanzen das Reduktionsmittel zu generieren, ist der Einsatz von Wärme erforderlich. Demzufolge weist ein derartiges reduktionsmittelgenerierendes System ein Wärmeelement auf, das für den Betrieb des Systems die notwendige Wärme liefert. Vorteile der ErfindungIn automotive technology, devices for selective catalytic reduction (SCR) are known in order to remove nitrogen oxides (NO x ) in oxygen-containing exhaust gases and to reduce them to nitrogen and water. As a reducing agent, ammonia (NH 3 ) is preferably used for this purpose. For mobile applications, it is not advisable for safety reasons to carry large amounts of ammonia in the vehicle. Therefore, it is produced from uncritical substances by means of a reducing agent-generating system (RGS) on board, ie in the vehicle, and used for exhaust gas treatment. In order to generate the reducing agent from the mentioned uncritical substances, the use of heat is required. As a result, such a reducing agent-generating system has a heating element which provides the necessary heat for the operation of the system. Advantages of the invention
Aufgrund des erfindungsgemäßen reduktionsmittelgenerierenden Systems lassen sich vorhandene Bauteile kostensparend und/oder zur Vergrößerung einer Einsatzvielfalt im Zuge einer Doppelfunktion nutzen, in dem das Wärmeelement des reduktionsmittelgenerierenden Systems (nachfolgend System genannt) auch dazu verwendet wird, Wärme an mindestens eine systemfremde Einrichtung zu leiten. Hierzu ist ein Wärmekopplungselement vorgesehen, das die mittels des Wärmeelements erzeugte Wärme wählbar entweder den Komponenten zuleitet, die das Reduktionsmittel generieren, oder mindestens einer systemfremden Einrichtung. Es ist auch denkbar, dass die Wärme an beide Baugruppen gleichzeitig geliefert wird. Das Wärmeelement wird demzufolge für einen weiteren Zweck, nämlich ein Hei- zen systemfremder Einrichtungen des Fahrzeuges genutzt.Because of the reducing agent generating system of the present invention, existing components can be used cost-effectively and / or to increase a variety of uses in a dual function in which the heat element of the reducing agent generating system (hereinafter called system) is also used to conduct heat to at least one non-system device. For this purpose, a heat coupling element is provided, which selectively supplies the heat generated by means of the heat element either to the components which generate the reducing agent, or at least to a system-foreign device. It is also conceivable that the heat is delivered to both assemblies at the same time. Accordingly, the heating element is used for a further purpose, namely heating of system-external devices of the vehicle.
Nach einer Weiterbildung der Erfindung ist vorgesehen, dass das Wärmeelement als ein heißgaslieferndes Wärmeelement ausgebildet ist. Das Heißgas, das vorzugsweise von einem Brenner stammt, wird daher über das Wärmekopplungselement der systemfremden Einrichtung zugeführt, sofern diese Betriebsart gewünscht wird. Das in Anspruch 1 erwähnte Wort „wählbar" bedeutet demgemäss, dass eine Umschaltmöglichkeit besteht, die Wärme nur bei Bedarf mittels des Wärmekopplungselements der systemfremden Einrichtung zuzu- führen.According to a development of the invention it is provided that the heat element is designed as a hot gas delivering heat element. The hot gas, which preferably originates from a burner, is therefore supplied via the heat coupling element of the system-foreign device, if this mode is desired. Accordingly, the word "selectable" mentioned in claim 1 means that a switchover possibility exists to supply the heat only when necessary by means of the heat coupling element of the system-foreign device.
Ferner ist es vorteilhaft, wenn das Wärmekopplungselement einen Gasströmungsweg für das Heißgas aufweist. Wenn die Zuführung von Wärme zur systemfremden Einrichtung gewünscht wird, wird demgemäss das Heißgas in den Gasströmungsweg eingeleitet und gelangt hierdurch zur Einsatzstelle.Furthermore, it is advantageous if the heat coupling element has a gas flow path for the hot gas. Accordingly, when the supply of heat to the non-system device is desired, the hot gas is introduced into the gas flow path and thereby reaches the point of use.
Als systemfremde Einrichtung kommt insbesondere eine Innenraum- heizung einer Fahrgastzelle des Kraftfahrzeugs in Betracht. Zusatz- lich oder alternativ kann vorgesehen sein, dass die systemfremde Einrichtung eine Brennkraftmaschine des Kraftfahrzeuges ist. Demzufolge lässt sich mit der Wärme des Wärmeelementes die Fahrgastzelle des Kraftfahrzeuges und/oder die Brennkraftmaschine des Kraftfahrzeuges heizen. Dies ist besonders vor der Startphase der Brennkraftmaschine von Vorteil, da ein Warmstart des Motors, insbesondere im Winter, diesen ganz erheblich schont und die Umweltbelastung und den Kraftstoffverbrauch vermindern kann.In particular, an interior heating of a passenger compartment of the motor vehicle is considered as a system-external device. Additive- Lich or alternatively, it may be provided that the system-foreign device is an internal combustion engine of the motor vehicle. Consequently, the passenger compartment of the motor vehicle and / or the internal combustion engine of the motor vehicle can be heated with the heat of the heating element. This is particularly advantageous before the starting phase of the internal combustion engine, since a warm start of the engine, especially in winter, this considerably protects and can reduce the environmental impact and fuel consumption.
Eine Weiterbildung der Erfindung sieht vor, dass der Gasströmungsweg des Wärmekopplungselements mit einem Wärmetauscher, insbesondere einem Standheizungswärmetauscher, eines Kühlwasserkreislaufes des Kraftfahrzeuges verbindbar ist. Die Wärme des Wärmeelementes wird wählbar dem Standheizungswärmetauscher zuge- führt, wodurch das Kühlwasser des Kraftfahrzeuges aufgeheizt wird. Dies hat zur Folge, dass zum Einen die Brennkraftmaschine erwärmt wird und zum Anderen auch ein Heizungswärmetauscher betrieben werden kann, der sich im Kühlwasserkreislauf befindet und daher Wärme zum Aufheizen der Fahrgastzelle bereit gestellt wird. Da- durch erhöht sich der Temperaturkomfort der Insassen und die Verkehrssicherheit, da die Scheiben der Fahrgastzelle nicht beschlagen, der Fahrer keine verlängerte Reaktionszeit bei tiefen Temperaturen aufweist und dieser beim Fahren keine dicke Kleidung tragen muss.A development of the invention provides that the gas flow path of the heat coupling element with a heat exchanger, in particular a stationary heating heat exchanger, a cooling water circuit of the motor vehicle is connectable. The heat of the heating element is selectively supplied to the auxiliary heating heat exchanger, whereby the cooling water of the motor vehicle is heated. This has the consequence that on the one hand, the internal combustion engine is heated and on the other hand, a heating heat exchanger can be operated, which is located in the cooling water circuit and therefore heat is provided for heating the passenger compartment. This increases the comfort of the occupants and the safety of the traffic, as the panes of the passenger compartment do not fog up, the driver does not have a prolonged reaction time at low temperatures and the driver does not have to wear thick clothing when driving.
Weitere vorteilhafte Ausgestaltungen des Systems ergeben sich aus den Ansprüchen.Further advantageous embodiments of the system will become apparent from the claims.
Ferner betrifft die Erfindung ein Verfahren zum Berieb eines reduktionsmittelgenerierenden Systems einer Abgasanlage eines Kraftfahr- zeuges, mit einem Wärmeelement, das für den Berieb des Systems notwendige Wärme erzeugt, wobei die von dem Wärmeelement erzeugte Wärme oder ein Anteil davon auch zum Heizen mindestens einer systemfremden Einrichtung des Kraftfahrzeuges genutzt wird. - A -Furthermore, the invention relates to a method for operating a reducing agent-generating system of an exhaust system of a motor vehicle, with a heat element that generates heat necessary for the operation of the system, wherein the heat generated by the heat element or a portion thereof also for heating at least one non-system device of the motor vehicle is used. - A -
Vorteilhafte Weiterbildungen des Verfahrens ergeben sich aus den Ansprüchen.Advantageous developments of the method emerge from the claims.
Ferner betrifft die Erfindung ein Kraftfahrzeug mit einem reduktions- mittelgenerierenden System gemäß der vorhergehenden Ausführungen.Furthermore, the invention relates to a motor vehicle with a reducing agent-generating system according to the preceding embodiments.
Schließlich betrifft die Erfindung die Verwendung eines Wärmeelementes eines reduktionsmittelgenerierenden Systems einer Abgas- anläge eines Kraftfahrzeuges auch zum Zwecke der Erwärmung mindestens einer systemfremden Einrichtung des Kraftfahrzeuges.Finally, the invention relates to the use of a heat element of a reducing agent-generating system of a Abgas- anläge a motor vehicle for the purpose of heating at least one non-system device of the motor vehicle.
Die Erfindung wird im Folgenden anhand der Zeichnungen näher erläutert. Es zeigenThe invention will be explained in more detail below with reference to the drawings. Show it
Figur 1 eine schematische Darstellung des reduktionsmittelgenerierenden SystemsFigure 1 is a schematic representation of the reducing agent-generating system
Figur 2 bis Figur 5 schematische Darstellungen des reduktionsmit- telgenerierenden Systems gemäß weiteren Ausgestaltungen der Erfindung.Figure 2 to Figure 5 are schematic representations of the reduction-generating system according to further embodiments of the invention.
Figur 1 zeigt ein einem nicht dargestellten Fahrzeug zugeordnetes reduktionsmittelgenerierendes System (RGS) 1 , das zwei Eingänge 3 und 5 aufweist. Diese gehören zu einer Stickstoffoxid- Erzeugereinheit, die durch ein thermisches Plasma realisiert werden kann, insbesondere mit einem sogenannten Plasmatron 7 mit einem integrierten Wärmeelement 9, das als Startbrenner ausgebildet ist. Ein Plasmatron ist ein plasmaerzeugendes System, dessen Plasma- zone durch eine Gasströmung überlagert wird und außerhalb einer Plasmaerzeugungseinheit wissenschaftlich oder technisch genutzt wird. Das Plasmatron 7 weist einen Ausgang auf. Dieser ist mit einer Abzweigung 11 verbunden, die den Weg in zwei Teile aufspaltet, nämlich in einen Standardweg 13 und einen Standheizungsweg 15. Im Standardweg 13 liegt ein Absperrelement 17, das als 2-2-Ventil ausgebildet ist. Darauf folgt eine weitere Abzweigung 19, an der der Standheizungsweg 15 nach Passieren eines Wärmetauschers 37 wieder auf den Standardweg 13 trifft. Es folgt eine katalytische Kom- ponente 21 , die mit einer Ammoniak-Erzeugereinheit 23, im Weiteren als AGC für Ammonia Generating Catalyst oder vereinfacht als NH3- Erzeuger bezeichnet, verknüpft ist.FIG. 1 shows a reducing agent-generating system (RGS) 1 assigned to a vehicle, not shown, which has two inputs 3 and 5. These belong to a nitric oxide generator unit, which can be realized by a thermal plasma, in particular with a so-called Plasmatron 7 with an integrated heating element 9, which is designed as a starting burner. A plasmatron is a plasma-generating system whose plasma zone is superimposed by a gas flow and is used scientifically or technically outside of a plasma generation unit. The Plasmatron 7 has an output. This is connected to a branch 11, which splits the path into two parts, namely in a standard way 13 and a parking heater 15th In Standardweg 13 is a shut-off 17, which is designed as a 2-2 valve. This is followed by another branch 19, at which the auxiliary heating path 15 again meets the standard route 13 after passing through a heat exchanger 37. This is followed by a catalytic component 21, which is linked to an ammonia generator unit 23, hereinafter referred to as AGC for Ammonia Generating Catalyst or simply as NH 3 generator.
Des Weiteren ist eine Abgasanlage 25 vorhanden, die an eine Brennkraftmaschine 27 des Kraftfahrzeugs angeschlossen ist, der mit einem Diesel-Oxidations-Katalysator (DOC) 29 verbunden ist. Darauf folgt ein Diesel-Partikelfilter (DPF) 31 und eine SCR- Einrichtung 33, die dazu verwendet wird, in sauerstoffhaltigen Abgasen Stickoxide zu entfernen und zu Stickstoff und Wasser zu redu- zieren. Als Reduktionsmittel wird Ammoniak verwendet, das von der Ammoniak-Erzeugereinheit (AGC) 23 erzeugt wird. Zwischen dem DPF 31 und der SCR-Einrichtung 33 ist eine Einmündung 35 vorgesehen, die den AGC 23 mit der Abgasanlage 25 im Bereich zwischen dem Diesel-Partikelfilter 31 und der SCR-Einrichtung 33 verknüpft.Furthermore, an exhaust system 25 is present, which is connected to an internal combustion engine 27 of the motor vehicle, which is connected to a diesel oxidation catalyst (DOC) 29. This is followed by a diesel particulate filter (DPF) 31 and an SCR device 33, which is used to remove nitrogen oxides in oxygen-containing exhaust gases and to reduce them to nitrogen and water. As the reducing agent, ammonia generated by the ammonia generator unit (AGC) 23 is used. Between the DPF 31 and the SCR device 33, a junction 35 is provided which links the AGC 23 to the exhaust system 25 in the region between the diesel particulate filter 31 and the SCR device 33.
Folgt man dem Standheizungsweg 15, so ist mit der Abzweigung 11 der Wärmetauscher 37 verbunden. Dieses kann beispielsweise als Standheizungswärmetauscher ausgebildet sein. Von diesem Wärmetauscher 37 kommend ist eine Rückführung 39 vorgesehen, die mit der Abzweigung 19 verknüpft ist. Dort schließt sich der Standheizungsweg 15 wieder an den Standardweg 13 an. Der Wärmetauscher 37 ist mit einem Kühlwasserkreislauf 41 des Kraftfahrzeuges verbindbar/verbunden.Following the parking heater path 15, the heat exchanger 37 is connected to the branch 11. This can be formed for example as a parking heater heat exchanger. Coming from this heat exchanger 37, a return 39 is provided, which is linked to the branch 19. There, the parking heater 15 again connects to the standard way 13. The heat exchanger 37 is connectable / connected to a cooling water circuit 41 of the motor vehicle.
Bei laufender Brennkraftmaschine 27 wird im Betrieb des reduktionsmittelgenerierenden Systems (RGS) 1 Dieselkraftstoff und Luft/Abgas den Eingängen 3, 5 zugeführt. Im Plasmatron 7 mit integriertem Wärmeelement 9 werden in einer Magerphase Stickoxide erzeugt. Dabei wird das Gasgemisch erhitzt. Nach dem Ausgang trifft das erhitzte Gasgemisch, das sogenannte Heißgas, auf die Abzweigung 11 und danach im Standardweg 13 auf das Absperrelement 17. Im Standard betrieb ist das Absperrelement 17 offen. Das Heißgas wird durch die katalytische Komponente 21 geleitet. Diese setzt wäh- rend einer Fettphase in den Bereich des Plasmatrons 7 eindosierten Kraftstoff zu einem Wasserstoff- und CO-haltigen Gasgemisch um. Danach wird das Heißgas durch den AGC 23 geleitet, wo das zum Betrieb der SCR-Einrichtung 33 notwendige Ammoniak erzeugt wird. Die katalytische Komponente 21 benötigt zum Betrieb eine Tempera- tur von 2500C - 8000C, bevorzugt 650°C, während zum Betrieb des AGC 23 eine Temperatur von 1500C - 350°C, bevorzugt 250°C notwendig ist. Die dafür benötigte Wärme liefert das vom Wärmeelement 9 erhitzte Heißgas. Das Ammoniak wird über die Einmündung 35 in die Abgasanlage 25 geleitet und in der SCR-Einrichtung 33 für die Abgasbehandlung genutzt.When the internal combustion engine 27 is running, diesel fuel and air / exhaust gas are fed to the inputs 3, 5 during operation of the reducing agent-generating system (RGS). In Plasmatron 7 with integrated heat element 9 nitrogen oxides are generated in a lean phase. The gas mixture is heated. After the exit meets the heated gas mixture, the so-called hot gas, on the branch 11 and then in the standard way 13 on the shut-off 17. The standard operation, the shut-off element 17 is open. The hot gas is passed through the catalytic component 21. This converts fuel metered into the area of the plasmatron 7 during a fatty phase into a hydrogen and CO-containing gas mixture. Thereafter, the hot gas is passed through the AGC 23 where the ammonia necessary to operate the SCR device 33 is generated. The catalytic component 21 required for operating a temperature of 250 0 C - 800 0 C, preferably 650 ° C, while the operation of the AGC 23 at a temperature of 150 0 C - 350 ° C, preferably 250 ° C is necessary. The heat required for this supplies the heated by the heating element 9 hot gas. The ammonia is passed via the junction 35 in the exhaust system 25 and used in the SCR device 33 for the exhaust gas treatment.
Vor dem Start der Brennkraftmaschine 27 wird das RGS 1 in der vorstehenden Weise nicht benötigt. Erfindungsgemäß lässt sich jedoch das dennoch in Betrieb genommene Wärmeelement 9 nutzen, d.h. das Wärmeelement 9 liefert Heißgas. Die Wärme des Heißgases kann insbesondere bei Nichtanspruchnahme des RGS 1 für die Beheizung systemfremder Einrichtungen 59 des Kraftfahrzeugs, nämlich der Brennkraftmaschine 27 und/oder einer Fahrgastzelle des Kraftfahrzeugs, die in der Figur 1 nicht dargestellt ist, benutzt wer- den. Dazu wird ein Wärmekopplungselement 55, das die Wärme in eine für diese Zwecke nutzbare Form umleitet, verwendet. Dieses umfasst gemäß Figur 1 die Abzweigung 11 , eine Hinführung 57 des Standheizungswegs 15, den Wärmetauscher 37, die Rückführung 39, die Abzweigung 19 und das Absperrelement 17. Wird das Ab- sperrelement 17 geschlossen, wird das Heißgas über die Hinführung 57 in den Wärmetauscher 37 geleitet. Im Wärmetauscher 37 findet eine Wärmetauschung mit dem Kühlwasser eines Kühlwasserkreislaufes 41 der Brennkraftmaschine 27 statt. Der Wärmetauscher 37 bildet insbesondere einen Standheizungswärmetauscher, d.h. er dient der Heizung von systemfremden Einrichtungen 59 des insbesondere nicht fahrenden Kraftfahrzeugs. Das erwärmte Kühlwasser wird zur Erwärmung (Vorwärmung) der Brennkraftmaschine 27 genutzt. Des weiteren kann im Kühlwasserkreislauf 41 ein Heizungs- Wärmetauscher vorgesehen sein, der die Wärme des Kühlwassers für ein Beheizen der Fahrgastzelle nutzt. Das Heißgas wird anschließend in das RGS 1 zurückgeleitet, nämlich über die Rückführung 39 in die Abzweigung 19, und gelangt schließlich in die Auspuffanlage der Brennkraftmaschine 27. Demgemäss weist das Wärmekopp- lungselement 55 einen Gasströmungsweg 61 für das Heißgas auf.Before starting the engine 27, the RGS 1 is not needed in the above manner. According to the invention, however, the still put into operation heat element 9 can be used, ie the heat element 9 provides hot gas. The heat of the hot gas can be used in particular for non-use of the RGS 1 for heating system-external devices 59 of the motor vehicle, namely the internal combustion engine 27 and / or a passenger compartment of the motor vehicle, which is not shown in FIG. For this purpose, a heat coupling element 55, which diverts the heat into a usable form for this purpose, is used. This includes according to Figure 1, the branch 11, an inlet 57 of the parking heater 15, the heat exchanger 37, the return 39, the junction 19 and the shut-off 17. When the shut-off element 17 is closed, the hot gas via the guide 57 in the heat exchanger 37 headed. In the heat exchanger 37, a heat exchange with the cooling water of a cooling water circuit 41 of the internal combustion engine 27 takes place. The heat exchanger 37 forms in particular a stationary heating heat exchanger, ie he serves the heating of non-system devices 59 of the particular non-moving motor vehicle. The heated cooling water is used for heating (preheating) of the internal combustion engine 27. Furthermore, in the cooling water circuit 41, a heating heat exchanger may be provided which uses the heat of the cooling water for heating the passenger compartment. The hot gas is then returned to the RGS 1, namely via the return 39 into the branch 19, and finally enters the exhaust system of the internal combustion engine 27. Accordingly, the heat coupling element 55 has a gas flow path 61 for the hot gas.
Kern der Erfindung ist es demgemäss, den Startbrenner des RGS 1 als Standheizung zu benutzen. Hierdurch kann beispielsweise die Brennkraftmaschine 27 vorgeheizt und/oder die Fahrgastzelle des Kraftfahrzeugs vorgeheizt werden. Wenn demgemäss der Startbrenner des RGS 1 (Ammoniakerzeuger) nicht benötigt wird, also insbesondere vor einem Start der Brennkraftmaschine, so steht dieser für den neuen, erfindungsgemäßen Zweck zur Verfügung. Die Standheizung dient unter anderem dem Temperaturkomfort der Insassen. Sie dient jedoch auch der Verkehrssicherheit, da es nicht zu beschlagenen Scheiben und nicht zu einer verlängerten Reaktionszeit des Fahrers aufgrund tiefer Temperaturen kommt. Dieser benötigt ferner keine unnötig dicke Kleidung. Der durch die Erfindung mögliche Warmstart des Motors schont insbesondere im Winter die Bauteile und kann (bei entsprechend emissionsarmer Standheizung) die Umweltbelastung und den Kraftstoffverbrauch vermindern. Ferner wird der Wiederverkaufswert des Fahrzeugs durch die Standheizung erhöht.The core of the invention is accordingly to use the starting burner of the RGS 1 as a heater. As a result, for example, the internal combustion engine 27 preheated and / or the passenger compartment of the motor vehicle can be preheated. Accordingly, if the start burner of the RGS 1 (ammonia generator) is not needed, ie in particular before a start of the internal combustion engine, then this is available for the new, inventive purpose. The auxiliary heater is used, among other things, the temperature comfort of the occupants. However, it also serves road safety, as it does not fogged windows and does not lead to a prolonged reaction time of the driver due to low temperatures. This also does not need unnecessarily thick clothing. The possible by the invention warm start of the engine, especially in winter protects the components and can (with a correspondingly low-emission auxiliary heater) reduce the environmental impact and fuel consumption. Furthermore, the resale value of the vehicle is increased by the auxiliary heater.
Im Normalbetrieb des RGS (Benutzung des Standardwegs 13) wird NH3 aus den Edukten NO und H2 hergestellt. NO wird in einer Magerphase (im Luft- oder Abgasbetrieb mit λ> 1 ) in einem Plasmatron 7 in Luft erzeugt. Diese Stickoxide durchströmen anschließend die katalytische partielle Oxidationsstufe (cPOx) und werden in der sich stromabwärts daran anschließenden katalytischen Einheit (NH3- Erzeuger) gespeichert. In einer sich an die Magerphase anschließenden zweiten Betriebsphase, der Fettphase (0,33<λ<1 ), wird im Bereich des Plasmatrons 7 in eine Verdampfungs- und Gemischbildungszone flüssiger Kraftstoff eindosiert und in der cPOx-Stufe (Ca- talytical Partial Oxidation) zu einem Hb- und - CO-haltigen Gasgemisch umgesetzt, das anschließend am NH3-Erzeuger die gespeicherten Stickoxide zu Ammoniak umsetzt. Dieses in einem Nebenstrang erzeugte gasförmige Ammoniak wird dann in den Vollstrom des Abgasstranges vor dem SCR-Katalysator eindosiert. Da der SCR-Katalysator eine NH3-Speicherfähigkeit besitzt, ist es möglich, auch über ein diskontinuierliches Verfahren zur Ammoniakerzeugung kontinuierlich die Reduktion der Stickoxide mittels SCR-Prozess im Abgasvollstrom zu erreichen. Dabei setzen im Temperaturbereich zwischen 1500C und 4500C die Katalysatoren aus Titandioxid (Tiθ2) und Vanadium-Pentoxid (V2O5) die Stickoxide mit dem erzeugten Ammoniak mit hoher Rate um.In normal operation of the RGS (using standard route 13), NH 3 is prepared from the starting materials NO and H 2 . NO is generated in a lean phase (in air or exhaust mode with λ> 1) in a Plasmatron 7 in air. These nitrogen oxides then flow through the catalytic partial oxidation state (cPOx) and are in the downstream of the catalytic unit (NH 3 - Producer). In a second phase of operation subsequent to the lean phase, the fat phase (0.33 <λ <1), liquid fuel is metered into an evaporation and mixture-forming zone in the area of the plasmatron 7 and in the cPOx stage (catalytic partial oxidation). converted to a Hb and - CO-containing gas mixture, which then converts the stored nitrogen oxides to ammonia at the NH 3 generator. This gaseous ammonia produced in a secondary line is then metered into the full flow of the exhaust line before the SCR catalyst. Since the SCR catalyst has an NH 3 storage capacity, it is possible to continuously achieve the reduction of the nitrogen oxides by means of an SCR process in the exhaust gas full flow, even via a discontinuous process for producing ammonia. In this case, in the temperature range between 150 0 C and 450 0 C, the catalysts of titanium dioxide (TiO 2) and vanadium pentoxide (V2O5) to set the nitrogen oxides with the produced ammonia at a high rate.
Die Erfindung beruht demgemäss darauf, dass im Standheizungsbetrieb heiße Brennergase des Startbrenners genutzt werden. Im NH3- Bedarfsfall wird der Standheizungsweg 15 nicht mehr benutzt, sondern der Standardweg 13, so dass das System wieder als NH3- Erzeuger betrieben werden kann. Es ist auch ein Misch betrieb denkbar, also sowohl NH3-Erzeugung als auch die Heizung systemfremder Einrichtungen 59.The invention is accordingly based on the fact that hot combustion gases of the starting burner are used in the auxiliary heating mode. In NH3 requirement, the parking heater 15 is no longer used, but the standard way 13, so that the system can be operated again as NH3 generator. It is also a mixed operation conceivable, so both NH 3 production and the heating system-independent devices 59th
Das Ausführungsbeispiel der Figur 2 entspricht im Wesentlichen dem der Figur 1. Die Bezugsziffern der Figur 2 entsprechen denen der Figur 1 , sodass auf eine detaillierte Beschreibung verzichtet wird. Der Gegenstand der Figur 2 unterscheidet sich nur dadurch, dass anstelle eines 2-2-Ventils ein Linearventil als Absperrelement 17 benutzt wird, das es erlaubt, nur einen Teilstrom des Heißgases durch den Wärmetauscher 37 zu leiten und somit die Temperatur der kata- lytischen Komponente 21 (cPOx-Stufe) durch den anderen Teilstrom des Heißgases anzuheben. Dieser kann nach dem Erreichen einer Anspringtemperatur die HC- und CO-Emission des gesamten Brennerabgases stark vermindern.The embodiment of Figure 2 corresponds substantially to that of Figure 1. The reference numerals of Figure 2 correspond to those of Figure 1, so that a detailed description is omitted. The object of Figure 2 differs only in that instead of a 2-2 valve, a linear valve is used as a shut-off 17, which allows to direct only a partial flow of the hot gas through the heat exchanger 37 and thus the temperature of the catalytic lytischen component 21 (cPOx stage) by the other partial flow of the hot gas to raise. This can after reaching a Light-off temperature greatly reduce the HC and CO emissions of the entire burner exhaust gas.
Auch Figur 3 entspricht in weiten Teilen der Anordnung in Figur 1 , so dass auf eine detaillierte Beschreibung verzichtet wird. Es gilt wieder, dass die Bezugsziffern denen der Beschreibung aus Figur 1 entsprechen. Ein Unterschied besteht darin, dass die Abzweigung 11 nach der katalytischen Komponente 21 vorgesehen ist. Darauf folgt wie in Figur 1 im Standardweg 13 ein Absperrelement 17 und darauf die Abzweigung 19, an der der Standheizungsweg 15 wieder auf den Standardweg 13 trifft. In diesem Fall wird die katalytische Komponente 21 auf jeden Fall (also auch im Standheizungsbetrieb) vom Heißgas durchströmt und ist betriebsfähig. Dieses hat ebenfalls eine starke Minderung der HC- und CO-Emission zur Folge.FIG. 3 also largely corresponds to the arrangement in FIG. 1, so that a detailed description is dispensed with. It is again true that the reference numerals correspond to those of the description of Figure 1. One difference is that the branch 11 is provided after the catalytic component 21. This is followed, as in Figure 1 in Standardweg 13 a shut-off 17 and then the branch 19, where the auxiliary heating path 15 again meets the standard path 13. In this case, the catalytic component 21 is flowed through in any case (ie also in the auxiliary heating mode) by the hot gas and is operable. This also results in a strong reduction of HC and CO emissions.
Figur 4 ähnelt ebenfalls in weiten Teilen Figur 1. Auch hier entsprechen die Bezugsziffern der Beschreibung der Figur 1 denen der Figur 4. Ein Unterschied zu Figur 1 besteht darin, dass im Standheizungsweg 15 das Heißgas nach Passieren des Wärmetauschers 37 nicht mehr in den Standardweg 13 vor der Ammoniakerzeugereinheit 23 zurückgeführt wird, sondern direkt in die Abgasanlage 25 vor die SCR-Einrichtung 33 eingebracht wird. Dabei sind zwei Ventile 45 und 47 (insbesondere zwei 2-2-Ventile) vorgesehen. Das Ventil 45 befindet sich zwischen dem AGC 23 und der Einmündung 35 im Stan- dardweg 13. Das Ventil 47 ist im Standheizungsweg 15 zwischen dem Wärmetauscher 37 und einer Einmündung 43 vorgesehen, welche sich in der Abgasanlage 25 vor der SCR-Einrichtung 33 befindet. Je nach Einstellung der Ventile 45 und 47 kann das Heißgas entweder durch den Standardweg 13 und/oder durch den Standheizungs- weg 15 geleitet werden.FIG. 4 likewise largely resembles FIG. 1. Here too, the reference numbers of the description of FIG. 1 correspond to those of FIG. 4. A difference from FIG. 1 is that in the auxiliary heating path 15 the hot gas no longer enters the standard path 13 after passing through the heat exchanger 37 is returned before the ammonia generator unit 23, but is introduced directly into the exhaust system 25 in front of the SCR device 33. In this case, two valves 45 and 47 (in particular two 2-2 valves) are provided. The valve 45 is located between the AGC 23 and the confluence 35 in the standard path 13. The valve 47 is provided in the stationary heating path 15 between the heat exchanger 37 and a junction 43 which is located in the exhaust system 25 in front of the SCR device 33. Depending on the setting of the valves 45 and 47, the hot gas can be conducted either through the standard path 13 and / or through the auxiliary heating path 15.
In Figur 5 ist eine weitere mögliche Anordnung der Erfindung zu sehen. Auch hier entsprechen wieder die verwendeten Bezugsziffern denen der Beschreibung der Figur 1 , sodass auf eine detaillierte Be- schreibung verzichtet wird. Abweichend ist hier ein nicht näher dargestelltes Ventil 49, das zwischen der katalytischen Komponente 21 und dem AGC 23 angeordnet ist. Von dem Ventil 49 geht zusätzlich eine Verbindung 51 zur Abgasanlage 25 (zwischen Brennkraftma- schine 27 und Katalysator 29) und die Rückführung 39 des Standheizungswegs 15 ist ebenfalls mit dem Ventil 49 gekoppelt. Das Ventil 49 kann als 4-4-Ventil ausgebildet sein, wobei auch Zwischenstellungen möglich sein können, wie es zum Beispiel bei einem Linearventil möglich ist. Je nach Einstellung, die im Folgenden mit Einstel- lungen a, b, c, d bezeichnet werden, wird mit Einstellung a der Standardweg 13 durchlaufen. Mit Einstellung b ist die katalytische Komponente 21 über die Verbindung 51 mit der Abgasanlage 25 gekoppelt. Das Heißgas wird in diesem Fall direkt über die katalytische Komponente 21 und die Verbindung 51 in die Abgasanlage 25 gelei- tet. Mit Einstellung c ist über die Verbindung 51 die Abgasanlage 25 mit dem AGC 23 verbunden. Das Abgas wird aus dem Motor 27 über die Verbindung 51 in das AGC 23 geleitet. Mit Einstellung d wird der Standheizungsweg 15 durchlaufen, wobei das Heißgas in dieser Anordnung um die katalytische Komponente 21 herumgeleitet wird und am Ventil 49 auf den Standardweg 13 trifft. Gemäss der vorstehend Ausführungen wird in Stellung a das System als NHß-Erzeuger betrieben. In der Stellung b wird die Nutzung des RGS 1 in einer verlängerten Fettphase mit H2/CO-Erzeugung zur Regeneration des Dieselpartikelfilters 31 (DPF-Regeneration) eingesetzt. In der Einstel- lung c wird die Nutzung des Motorabgases zur Aufheizung des AGC 23 ermöglicht. Schließlich wird an der Einstellung d das Brennerabgas über den Standheizungswärmetauscher geleitet. Je nach Ausführung des genannten Ventils kann das Brennerabgas über den AGC 23 und einen optional kleinen Dieselpartikelfilter nehmen oder direkt über den Gasweg in den Hauptabgastrakt vor dem Dieselpartikelfilter geleitet werden.FIG. 5 shows a further possible arrangement of the invention. Again, the reference numerals used here correspond to those of the description of FIG. 1, so that a detailed description is given. is omitted. Notwithstanding here is a valve 49, not shown in detail, which is arranged between the catalytic component 21 and the AGC 23. From the valve 49, a connection 51 additionally goes to the exhaust system 25 (between the internal combustion engine 27 and the catalytic converter 29) and the return 39 of the auxiliary heating system 15 is likewise coupled to the valve 49. The valve 49 may be formed as a 4-4 valve, wherein intermediate positions may be possible, as is possible for example in a linear valve. Depending on the setting, which are referred to below as settings a, b, c, d, the default path 13 is run through with setting a. With setting b, the catalytic component 21 is coupled to the exhaust system 25 via the connection 51. The hot gas is in this case passed directly via the catalytic component 21 and the connection 51 into the exhaust system 25. With setting c, the exhaust system 25 is connected to the AGC 23 via the connection 51. The exhaust gas is conducted from the engine 27 via the connection 51 into the AGC 23. With setting d, the auxiliary heating path 15 is traversed, wherein the hot gas is conducted around the catalytic component 21 in this arrangement and impinges on the standard path 13 at the valve 49. According to the above embodiments ß Generating Sets is operated in a position the system as NH. In position b, the use of the RGS 1 in a prolonged fat phase with H 2 / CO generation for the regeneration of the diesel particulate filter 31 (DPF regeneration) is used. In setting c, it is possible to use the engine exhaust to heat the AGC 23. Finally, at setting d, the burner exhaust gas is passed over the auxiliary heating heat exchanger. Depending on the design of the valve mentioned above, the burner exhaust gas can be taken via the AGC 23 and an optional small diesel particulate filter or can be routed directly via the gas path to the main exhaust tract in front of the diesel particulate filter.
Ergänzend zu den beschriebenen Ausgestaltungen der Erfindung kann innerhalb des RGS 1 ein Partikelfilter eingebaut werden, der es ermöglicht, die Partikel aus dem Brennerabgas zu filtern. Die Reinigung bzw. Regeneration des Partikelfilters, der dann im RGS 1 vorgesehen ist, kann durch das Heißgas, das über den Standardweg 13 geleitet wird, erreicht werden. Der Partikelfilter filtert dabei ebenso die Partikel, die in der Fettphase im Standardbetrieb des RGS 1 gebildet werden.In addition to the described embodiments of the invention, within the RGS 1, a particulate filter can be installed, which it allows to filter the particles from the burner exhaust gas. The cleaning or regeneration of the particulate filter, which is then provided in the RGS 1, can be achieved by the hot gas which is conducted via the standard route 13. The particle filter also filters the particles that are formed in the fat phase in standard operation of the RGS 1.
Des Weiteren kann das Wärmeelement 9 so betrieben werden, dass es am AGC 23 zu einer Minderung der Stickstoffoxide (NOx) kommt. Dies kann durch zwei Arten erreicht werden. Zum einen kann das Wärmeelement 9 (Brenner) mit einem optimalen Kraftstoff-Luft- Gemisch (λ=1 ) betrieben werden und dabei kann der AGC über eine 3-Wege-Funktionalität die NOx-, CO- und HC-Emission stark mindern. Zum andern kann der Brenner zum größten Anteil mager be- trieben werden und der AGC speichert die Stickoxide ein. Zur Regeneration des Speichers muss dann der Brenner (Wärmeelement 9) kurzzeitig fett (λ<1) betrieben werden. Furthermore, the heating element 9 can be operated in such a way that the nitrogen oxides (NO x ) are reduced at the AGC 23. This can be achieved by two ways. On the one hand, the heat element 9 (burner) can be operated with an optimum fuel-air mixture (λ = 1), and the AGC can greatly reduce the NO x , CO and HC emissions via a 3-way functionality. On the other hand, most of the burner can be run lean and the AGC stores the nitrogen oxides. To regenerate the memory, the burner (heat element 9) must then be briefly operated in fat (λ <1).
Claims
Applications Claiming Priority (20)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102005054129 | 2005-11-14 | ||
| DE102005054129.1 | 2005-11-14 | ||
| DE102005062556.8 | 2005-12-27 | ||
| DE102005062556 | 2005-12-27 | ||
| DE102006018955.8 | 2006-04-24 | ||
| DE102006018955 | 2006-04-24 | ||
| DE102006020693.2 | 2006-05-04 | ||
| DE102006020693 | 2006-05-04 | ||
| DE102006021490 | 2006-05-09 | ||
| DE102006021490.0 | 2006-05-09 | ||
| DE102006021987 | 2006-05-11 | ||
| DE102006021987.2 | 2006-05-11 | ||
| DE102006022385.3 | 2006-05-12 | ||
| DE102006022385 | 2006-05-12 | ||
| DE102006022992.4 | 2006-05-17 | ||
| DE102006022992 | 2006-05-17 | ||
| DE102006023338.7 | 2006-05-18 | ||
| DE102006023338 | 2006-05-18 | ||
| DE102006043086.7 | 2006-09-14 | ||
| DE102006043086A DE102006043086A1 (en) | 2005-11-14 | 2006-09-14 | Use of a reducing agent-generating system, in particular as auxiliary heating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2007054485A1 true WO2007054485A1 (en) | 2007-05-18 |
Family
ID=37807942
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2006/068158 Ceased WO2007054485A1 (en) | 2005-11-14 | 2006-11-07 | The use of a reduction agent generating system, in particular as auxiliary heating |
Country Status (2)
| Country | Link |
|---|---|
| DE (1) | DE102006043086A1 (en) |
| WO (1) | WO2007054485A1 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008006630A1 (en) * | 2008-01-29 | 2009-07-30 | Volkswagen Ag | Exhaust gas aftertreatment device for exhaust gas flow of diesel engine of motor vehicle, has temperature maintaining device assigned to auxiliary heater of combustion engine by valve arrangement |
| DE102013201947B4 (en) | 2012-02-29 | 2023-01-12 | Ford Global Technologies, Llc | Method and device for heating the interior of a motor vehicle |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010002244A1 (en) * | 1999-01-29 | 2001-05-31 | Jurgen Gieshoff | Process for the selective catalytic reduction of the nitrogen oxides contained in a lean exhaust gas |
| DE10237777A1 (en) * | 2002-08-17 | 2004-02-26 | Daimlerchrysler Ag | Combustion engine with catalytic exhaust gas treatment unit has module for generation of reducing gas containing hydrogen and ammonia which is dosed into exhaust system up-stream of catalyst unit |
| WO2004071646A2 (en) * | 2003-02-12 | 2004-08-26 | Delphi Technologies, Inc. | SYSTEM AND METHOD OF NOx ABATEMENT |
| DE10337901A1 (en) * | 2003-08-18 | 2005-03-24 | Audi Ag | Ammonia synthesis from hydrocarbons and air, especially for use in purifying combustion engine exhaust gases, by conversion to reformate gas followed by plasma-catalyzed reaction |
-
2006
- 2006-09-14 DE DE102006043086A patent/DE102006043086A1/en not_active Withdrawn
- 2006-11-07 WO PCT/EP2006/068158 patent/WO2007054485A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20010002244A1 (en) * | 1999-01-29 | 2001-05-31 | Jurgen Gieshoff | Process for the selective catalytic reduction of the nitrogen oxides contained in a lean exhaust gas |
| DE10237777A1 (en) * | 2002-08-17 | 2004-02-26 | Daimlerchrysler Ag | Combustion engine with catalytic exhaust gas treatment unit has module for generation of reducing gas containing hydrogen and ammonia which is dosed into exhaust system up-stream of catalyst unit |
| WO2004071646A2 (en) * | 2003-02-12 | 2004-08-26 | Delphi Technologies, Inc. | SYSTEM AND METHOD OF NOx ABATEMENT |
| DE10337901A1 (en) * | 2003-08-18 | 2005-03-24 | Audi Ag | Ammonia synthesis from hydrocarbons and air, especially for use in purifying combustion engine exhaust gases, by conversion to reformate gas followed by plasma-catalyzed reaction |
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| Publication number | Publication date |
|---|---|
| DE102006043086A1 (en) | 2007-06-28 |
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