EP1882090B1 - Exhaust system with two exhaust treatment units - Google Patents
Exhaust system with two exhaust treatment units Download PDFInfo
- Publication number
- EP1882090B1 EP1882090B1 EP06723523A EP06723523A EP1882090B1 EP 1882090 B1 EP1882090 B1 EP 1882090B1 EP 06723523 A EP06723523 A EP 06723523A EP 06723523 A EP06723523 A EP 06723523A EP 1882090 B1 EP1882090 B1 EP 1882090B1
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- EP
- European Patent Office
- Prior art keywords
- treatment unit
- exhaust gas
- exhaust
- gas treatment
- back pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000002485 combustion reaction Methods 0.000 claims abstract description 9
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- 241000264877 Hippospongia communis Species 0.000 description 28
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 15
- 239000003054 catalyst Substances 0.000 description 12
- 238000009826 distribution Methods 0.000 description 9
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- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
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- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000004071 soot Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
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- 239000003344 environmental pollutant Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
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- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 229920000914 Metallic fiber Polymers 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
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- 150000003672 ureas Chemical class 0.000 description 1
Images
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
- F01N3/24—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 constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2803—Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
- F01N3/2807—Metal other than sintered metal
- F01N3/281—Metallic honeycomb monoliths made of stacked or rolled sheets, foils or plates
-
- 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
- F01N13/0097—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 arranged in a single housing
-
- 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
- F01N2260/00—Exhaust treating devices having provisions not otherwise provided for
- F01N2260/06—Exhaust treating devices having provisions not otherwise provided for for improving exhaust evacuation or circulation, or reducing back-pressure
-
- 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
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/30—Honeycomb supports characterised by their structural details
- F01N2330/44—Honeycomb supports characterised by their structural details made of stacks of sheets, plates or foils that are folded in S-form
-
- 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
- F01N2330/00—Structure of catalyst support or particle filter
- F01N2330/30—Honeycomb supports characterised by their structural details
- F01N2330/48—Honeycomb supports characterised by their structural details characterised by the number of flow passages, e.g. cell density
-
- 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
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/0231—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using special exhaust apparatus upstream of the filter for producing nitrogen dioxide, e.g. for continuous filter regeneration systems [CRT]
-
- 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
- F01N3/206—Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
Definitions
- the subject matter of the present invention is an exhaust system for internal combustion engines with two exhaust gas treatment units.
- exhaust emission limits are specified, which must be observed by motor vehicles or stationary internal combustion engines. Often these are relatively complex threshold systems, where, for example, not only one limit for one size but rather several limits must be met simultaneously. In order to comply with these limits, relatively complex exhaust gas reclamation operations are often required which require multiple combined exhaust gas purification components.
- particulate filters require regeneration in which the soot particles collected by the filter are burned. This takes place for example in the form of a continuous regeneration (CRT, continuous regeneration trap) with nitrogen dioxide (NO 2 ). Since there is often insufficient nitrogen dioxide in the exhaust gas flowing into the filter, it is known to provide an oxidation catalyst upstream of the particulate filter, with which nitrogen monoxide (NO) is oxidized to nitrogen dioxide (NO 2 ).
- CRT continuous regeneration trap
- SCR Selective Catalytic Reduction
- NO X Nitric Oxide
- reductant such as urea
- the highest possible reaction rate in the second exhaust gas treatment component as a rule requires most efficient conversion in the first, first exhaust gas treatment component lying in the flow direction before the second exhaust gas treatment component.
- the DE 40 24 942 A1 discloses a monolithic honeycomb body which has consecutively different cell densities in the flow direction, so that the light-off behavior and the thermal aging can be influenced.
- the object of the invention is to propose an exhaust system with a first and a second exhaust treatment unit, in which the highest possible reaction rate in the second exhaust treatment component is achieved and at the same time the smallest possible volume of the exhaust gas treatment components is made possible.
- the exhaust system according to the invention of an internal combustion engine comprising a first exhaust treatment unit with a first dynamic pressure and a second exhaust treatment unit with a second dynamic pressure, wherein the first back pressure is smaller than the second back pressure, characterized in that the first exhaust treatment unit in such a first distance in the flow direction is formed before the second exhaust treatment unit, that during operation of a entering into the first exhaust gas treatment unit gas flow is made uniform.
- the back pressure in the flow direction before the exhaust gas treatment unit is influenced by the first dynamic pressure of the heat exchanger.
- the first distance between the first exhaust treatment unit and the second exhaust treatment unit is less than 15 mm, preferably less than 10 mm, more preferably less than 5 mm, so that the effect of the first stall pressure of the first exhaust treatment unit and the second back pressure of accumulate second exhaust treatment unit, so that the exhaust gas flowing into the first exhaust treatment unit, must overcome a back pressure, which is coarser than the first back pressure of the first exhaust treatment unit alone.
- the internal combustion engine is in particular a diesel or gasoline engine, for example a diesel or gasoline engine of a motor vehicle (eg a passenger car, a truck, a motorized two-wheeler, boat or aircraft) or a stationary or diesel diesel engine.
- a diesel or gasoline engine for example a diesel or gasoline engine of a motor vehicle (eg a passenger car, a truck, a motorized two-wheeler, boat or aircraft) or a stationary or diesel diesel engine.
- honeycomb bodies for example ceramic or metallic honeycomb bodies, or else wire knit bodies, bodies made of metal foam or the like are suitable as exhaust gas treatment units.
- Metallic honeycomb bodies may in particular be constructed from at least one at least partially structured metallic layer and optionally at least one substantially smooth layer, which are wound or stacked together and wound.
- the twisted or wound layers form permeable cavities, which are bounded by the layers.
- the layers are in particular made of a high temperature corrosion resistant material, such as Al or Cr steel.
- the layers may be interconnected, in particular cohesively, such as by a Hochtemperaturlötmaschinene.
- Both the essentially smooth layers and the at least partially structured layers can have microstructures, guide surfaces, perforations and / or perforations, at least in some areas, which serve for even better mixing of the gas flow.
- Under an exhaust gas treatment unit is understood in particular no heat exchanger.
- the exhaust treatment units may also be formed in an exhaust gas recirculation line.
- the equalization of the gas flow before entering the first exhaust gas treatment unit is advantageously carried out by forming the first exhaust gas treatment unit relatively close to the second exhaust gas treatment unit. This leads to an equalization of the gas flow already in the first exhaust gas treatment unit, so that here the conversion rate is improved because the cross section of the first exhaust gas treatment unit is more uniformly exposed to exhaust gas.
- the volume of the first exhaust treatment unit can be reduced in comparison to a conventional structure at the same rate of conversion of the pollutants in the exhaust gas. Due to the much more efficient implementation rate of Pollutants also improves the conversion rate of the second exhaust gas purification unit, so that it may be smaller in size compared to conventional second exhaust gas purification units.
- an exhaust treatment unit having a relatively high back pressure may be a high cell honeycomb body having, for example, a cell density of about 800 cpsi, 1000 cpsi or more.
- the length of the cavities in a honeycomb body has an influence on the dynamic pressure, so that an exhaust gas treatment unit having a relatively small back pressure can be formed by a short honeycomb body and an exhaust gas treatment unit having a relatively large back pressure by a long honeycomb body.
- the first distance is selected such that the effect of the first dynamic pressure and the second dynamic pressure accumulate.
- Cumulating means here in particular that the dynamic pressure present in front of the first exhaust gas treatment unit is greater than the first back pressure that the first exhaust gas treatment unit has as such, which therefore exists when only the first exhaust gas treatment unit is flown, without a second exhaust gas treatment unit being formed ,
- the cumulation of the dynamic pressures advantageously leads to the exhaust gas, before it flows into the first exhaust gas treatment unit, having to overcome a dynamic pressure which is greater than the first back pressure of the first exhaust gas treatment unit.
- the dynamic pressure is even significantly greater than the first dynamic pressure.
- the increase of the dynamic pressure causes ademandze-ß Trent the flow of the first exhaust gas treatment unit and thus the gas flow through the first exhaust gas treatment unit and the second exhaust gas treatment unit.
- a second distance of a gas inlet-side end face of the first exhaust gas treatment unit from a gas inlet-side end face of the second exhaust gas treatment unit is less than 60 mm, preferably less than 45 mm, particularly preferably less than 30 mm.
- the expansion of the first exhaust treatment unit in the flow direction is less than 45 mm, preferably less than 35 mm, particularly preferably 25 mm or less.
- first exhaust gas treatment units Due to the very uniform and effective implementation of the corresponding substances in the exhaust gas relatively small first exhaust gas treatment units can be used.
- the second exhaust treatment unit can also be chosen a smaller volume, for example, in the case that as the second exhaust treatment unit is a particulate filter and the first exhaust treatment unit formed an oxidation catalyst, the more uniform flow of the first exhaust treatment unit causes an improved supply of nitrogen dioxide and thus a more uniform regeneration so that a smaller particulate filter volume is sufficient.
- the first and / or the second exhaust gas treatment unit comprise at least one honeycomb body.
- a first and / or second exhaust treatment unit can be created, whose properties such as surface, pressure, etc., can be very accurately predetermined.
- honeycomb body are particularly suitable metallic or ceramic honeycomb.
- particulate filter can be formed as a honeycomb body with at least partially porous channel walls and optionally channel terminations or corresponding baffles and openings.
- both exhaust gas treatment units in a common housing.
- the exhaust gas treatment units may be held in corresponding beads of the housing by means of a flanging or the like. It is also possible to fit the second exhaust gas treatment unit flush on a front side of the heat exchanger. It may be advantageous, in particular in the last region of the first exhaust gas treatment unit, to allow the exhaust gas to flow crosswise. In the case of honeycomb bodies, this can be achieved by providing perforations in the walls of the cavities in the last region, for example in the last 20% or 10% of the length of the first exhaust gas treatment unit. This is particularly advantageous if the second exhaust gas treatment unit comprises a particle filter with alternately closed channels.
- the duct walls it is also possible to allow the duct walls to end at different points in the area of the gas outlet-side end face of the first exhaust treatment unit or the gas inlet-side end face of the second exhaust treatment unit, so that no smooth end face, but a rugged face of the first and / or the second exhaust treatment unit arises, which can also lead to cross flows in particular between adjacent channels.
- At least the first exhaust gas treatment unit comprises a catalytically active coating.
- the catalytically active coating comprises, for example, a ceramic washcoat which contains materials which catalyze the desired reactions, ie in particular reduce the reaction temperature of these reactions to such an extent that they run to a considerable extent at the temperatures in the exhaust gas recirculation line.
- Suitable catalysts are in particular noble metals such as platinum, rhodium or the like.
- An oxidation catalyst coating catalyzes in particular the oxidation of hydrocarbons (HC) or nitrogen oxides (NO X ).
- the second exhaust gas treatment unit has a catalytically active coating.
- the first exhaust treatment unit may comprise a hydrolysis catalyst, while the second exhaust treatment unit comprises an SCR catalyst.
- the ratio of the first dynamic pressure to the second dynamic pressure is greater than 2, preferably greater than 10.
- All of these three possible second exhaust treatment units (a), (b) and (c) are components with a relatively high dynamic pressure.
- An open particle filter should be characterized in that a particle, in particular a soot particle, can pass through it without being caught by a channel wall.
- a closed particulate filter this is not possible, as this regularly alternately closed channels, so that in a subset channels the exhaust gas can only flow in, but not through a regular channel opening can leave the channel, but rather that the exhaust gas through the porous Walls of the filter must flow, whereby it enters another subset of channels, which in turn have no input-side free flow cross-section, but only an output-side free flow cross-section.
- closed particulate filters in principle, it is not possible to break through a relatively large particle through the filter if it is intact, since the particle gets caught in the porous channel wall. In an open filter system this is possible in principle.
- An open particle filter has porous regions at least in part of its walls.
- an open or closed particulate filter as a second exhaust treatment unit, which is preceded by an oxidation catalyst as the first exhaust treatment unit, so that the particulate filter is continuously regenerated, is oxidized in the oxidation catalyst Nitrogen in oxide to nitrogen dioxide, which can be used for combustion of the soot particles is.
- the oxidation catalyst can be made smaller than when the distance between the two exhaust gas treatment units is not selected according to the invention.
- a closed particulate filter for example a diesel particulate filter of a known type
- a honeycomb body as the first exhaust gas treatment unit and the distance as small as possible, possibly even close to zero by applying the end face of the honeycomb body to the corresponding end face of the particulate filter, is selected
- Another example is a high cell SCR coating honeycomb body second exhaust treatment unit, preceded by a low cell honeycomb body with a urea hydrolysis promoting coating.
- Fig. 1 1 schematically shows an exemplary embodiment of an exhaust system 1 according to the invention of an internal combustion engine 2, which comprises a first exhaust gas treatment unit 3 and a second exhaust gas treatment unit 4.
- the first exhaust treatment unit 3 is designed as a closed particle filter with mutually closed channels, while the second exhaust treatment unit 4 is formed as a honeycomb body with a catalytically active coating, which catalyzes the conversion of nitrogen monoxide to nitrogen dioxide, without the invention being limited thereto.
- the particle filter may be formed as a ceramic solid extrudate or according to metallic layers.
- the first exhaust gas treatment unit 3 has a first hydrodynamic dynamic pressure
- the second exhaust gas treatment unit 4 has a second dynamic pressure, which is greater than the first dynamic pressure.
- the first exhaust gas treatment unit 3 is formed in such a first distance 5 upstream of the second exhaust gas treatment unit 4, so that during operation, a gas flow 6 symbolized by an arrow is homogenized in the first exhaust gas treatment unit 3.
- the first distance 5 is here in particular less than 15 mm, preferably less than 10 mm, particularly preferably less than 5 mm.
- the first 3 and second exhaust treatment unit 4 are designed so that at this first distance 5 to accumulate the effects of the first back pressure and the second back pressure, so that the flowing into the first exhaust treatment unit 3 exhaust gas must overcome a dynamic pressure which is greater than that first back pressure of the first exhaust treatment unit 3 as such. As explained above, this leads to an equalization of the gas flow 6, which flows into the first exhaust gas treatment unit 3.
- Fig. 2 schematically shows the section of the exhaust system 1, which comprises the first 3 and the second exhaust treatment unit 4.
- a second distance 7 between a gas inlet-side end face 8 of the first exhaust gas treatment unit 3 and a gas inlet-side end face 9 of the second exhaust treatment unit 4 is selected according to the invention so that it comes to a homogenization of the flow in the first exhaust gas treatment unit 3.
- the second distance 7 is less than 60 mm, preferably less than 45 mm, particularly preferably less than 30 mm.
- short honeycomb bodies can be used as the first exhaust gas treatment unit 4, in particular an extension 10 in the flow direction of approximately 20 to approximately 40 mm.
- the first distance 5 is for example less than 15 mm, or even 5 mm or less.
- the first distance 5 is selected so that the effect of the first dynamic pressure of the first exhaust treatment unit 3 and the second dynamic pressure of the second exhaust treatment unit 4 accumulate, so that the exhaust gas flowing into the first exhaust treatment unit 3 has to overcome a dynamic pressure that is larger , Preferably significantly greater than the first back pressure of the first exhaust treatment unit 3 alone
- Fig. 3 schematically shows an example of a honeycomb body 11 in cross-section, which may be formed as a first 3 and / or second exhaust treatment unit 4.
- This honeycomb body 11 comprises a honeycomb structure 12 in a jacket tube 13.
- the honeycomb structure 12 has cavities 14 which can be wetted or even flowed through, which are formed by substantially smooth layers 15 and at least partially structured layers 16.
- At least one at least partially structured layer 16 and optionally at least one substantially smooth layer 15 are wound up or stacked and wound one or more stacks in the same direction or in opposite directions.
- Substantially smooth layers 15 may have microstructures whose amplitude is smaller than the patterning amplitude of the at least partially structured layer 16.
- Layers 15, 16 are preferably metallic layers, in particular sheet metal layers and / or metallic fiber layers, in particular of high-temperature resistant and corrosion-resistant material such as Al or Cr steels can be made.
- the layers 15, 16 may have microstructures, perforations, apertures and / or baffles.
- Fig. 4 schematically shows a first probability distribution 17 of the velocity v and a second probability distribution 18 of the velocity v.
- the first probability distribution 17 results if only the first exhaust gas treatment unit 3 is flowed with gas, ie without a second exhaust gas treatment unit 4 being formed behind it in the flow direction. Plotted for both distributions, the probability that a certain speed is present in the gas. Both the probability and the speed are given in relative units.
- the second probability distribution 18 is the probability distribution in a system according to the invention. It therefore relates to an exhaust system 1 of a first exhaust treatment unit 3 and a second exhaust treatment unit 4.
- the second probability distribution 18 is wider, in particular has a greater width at half maximum height (full width half maximum) than the first probability distribution 17. This is based on the invention Equalization of the flow.
- the exhaust system 1 advantageously allows the formation of systems with two exhaust treatment units 3, 4, which are arranged one behind the other in the flow direction. Due to the flow equalization, the first 3 and / or the second exhaust treatment unit 4 can be made smaller. This applies, for example, if the first exhaust gas treatment unit 3 is an oxidation catalytic converter and a second exhaust gas treatment unit 4 is a particle filter. By equalizing the flow in the first exhaust gas treatment unit 3, the conversion rate is increased, so that first 3 and / or second exhaust treatment unit 4 can be made smaller. This saves considerable costs in the design of such systems.
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- 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)
- Processes For Solid Components From Exhaust (AREA)
Abstract
Description
Gegenstand der vorliegenden Erfindung ist eine Abgasanlage für Verbrennungskraftmaschinen mit zwei Abgasbehandlungseinheiten.The subject matter of the present invention is an exhaust system for internal combustion engines with two exhaust gas treatment units.
In vielen Ländern sind Abgasgrenzwerte vorgegeben, die von Kraftfahrzeugen oder auch stationären Verbrennungskraftmaschinen einzuhalten sind. Oft sind dies relativ komplexe Grenzwertsysteme, bei denen beispielsweise nicht nur ein Grenzwert für eine Größe, sondern vielmehr mehrere Grenzwerte gleichzeitig eingehalten werden müssen. Um diese Grenzwerte einzuhalten, sind oft relativ komplexe Aufarbeitungsvorgänge des Abgases nötig, die mehrere kombinierte Abgasreinigungskomponenten erfordern.In many countries exhaust emission limits are specified, which must be observed by motor vehicles or stationary internal combustion engines. Often these are relatively complex threshold systems, where, for example, not only one limit for one size but rather several limits must be met simultaneously. In order to comply with these limits, relatively complex exhaust gas reclamation operations are often required which require multiple combined exhaust gas purification components.
Beispielsweise erfordern Partikelfilter eine Regeneration, in der die durch den Filter gesammelten Rußpartikel verbrannt werden. Dies erfolgt beispielsweise in Form einer kontinuierlichen Regeneration (CRT, continuous regeneration trap) mit Stickstoffdioxid (NO2). Da oft nicht genügend Stickstoffdioxid im Abgas, welches in den Filter einströmt, vorhanden ist, ist es bekannt, vor dem Partikelfilter einen Oxidationskatalysator vorzusehen, mit welchem Stickstoffmonoxid (NO) zu Stickstoffdioxid (NO2) oxidiert wird.For example, particulate filters require regeneration in which the soot particles collected by the filter are burned. This takes place for example in the form of a continuous regeneration (CRT, continuous regeneration trap) with nitrogen dioxide (NO 2 ). Since there is often insufficient nitrogen dioxide in the exhaust gas flowing into the filter, it is known to provide an oxidation catalyst upstream of the particulate filter, with which nitrogen monoxide (NO) is oxidized to nitrogen dioxide (NO 2 ).
Ein anderes Beispiel ist die selektive katalytische Reduktion (SCR, selective catalytic reduction) von Stickoxiden (NOX), bei der die Zufuhr von Reduktionsmittel wie beispielsweise Harnstoff erforderlich ist. Dieser Harnstoff muss hydrolysiert werden, so dass oftmals in Strömungsrichtung vor einem SCR-Katalysator ein Hydrolysekatalysator ausgebildet ist.Another example is Selective Catalytic Reduction (SCR) of Nitric Oxide (NO X ), which requires the introduction of reductant such as urea. This urea must be hydrolyzed, so that often in the flow direction upstream of an SCR catalyst, a hydrolysis catalyst is formed.
So gibt es eine Vielzahl von Beispielen von Systemen, die zwei oder mehr verschiedene Abgasbehandlungseinheiten, die zusammenwirken, benötigt werden. Alle diese Systeme weisen also in Strömungsrichtung hintereinander liegende erste und zweite Abgasbehandlungseinheiten auf.Thus, there are a variety of examples of systems that require two or more different exhaust treatment units that work together. All of these systems therefore have first and second exhaust gas treatment units lying one behind the other in the flow direction.
Bei all diesen Fällen erfordert im Regelfall eine möglichst hohe Reaktionsrate in der zweiten Abgasbehandlungskomponente eine möglichst effiziente Umsetzung in der ersten, in Strömungsrichtung vor der zweiten Abgasbehandlungskomponente, liegenden ersten Abgasbehandlungskomponente.In all these cases, the highest possible reaction rate in the second exhaust gas treatment component as a rule requires most efficient conversion in the first, first exhaust gas treatment component lying in the flow direction before the second exhaust gas treatment component.
Die
Davon ausgehend liegt der Erfindung die Aufgabe zugrunde, eine Abgasanlage mit einer ersten und einer zweiten Abgasbehandlungseinheit vorzuschlagen, bei der eine möglichst hohe Reaktionsrate in der zweiten Abgasbehandlungskomponente erreicht und gleichzeitig ein möglichst kleines Bauvolumen der Abgasbehandlungkomponenten ermöglicht wird.Based on this, the object of the invention is to propose an exhaust system with a first and a second exhaust treatment unit, in which the highest possible reaction rate in the second exhaust treatment component is achieved and at the same time the smallest possible volume of the exhaust gas treatment components is made possible.
Diese Aufgabe wird gelöst durch eine Abgasanlage mit den Merkmalen des Anspruchs 1. Vorteilhafte Weiterbildungen sind Gegenstand der abhängigen Ansprüche.This object is achieved by an exhaust system with the features of
Die erfindungsgemäße Abgasanlage einer Verbrennungskraftmaschine, umfassend eine erste Abgasbehandlungseinheit mit einem ersten Staudruck und eine zweite Abgasbehandlungseinheit mit einem zweiten Staudruck, wobei der erste Staudruck kleiner als der zweite Staudruck ist, zeichnet sich dadurch aus, dass die erste Abgasbehandlungseinheit in einem solchen ersten Abstand in Strömungsrichtung vor der zweiten Abgasbehandlungseinheit ausgebildet ist, dass im Betrieb eine in die erste Abgasbehandlungseinheit eintretende Gasströmung vergleichmäßigt wird. Das bedeutet insbesondere, dass der Staudruck in Strömungsrichtung vor der Abgasbehandlungseinheit durch den ersten Staudruck des Wärmetauschers beeinflusst wird.The exhaust system according to the invention of an internal combustion engine, comprising a first exhaust treatment unit with a first dynamic pressure and a second exhaust treatment unit with a second dynamic pressure, wherein the first back pressure is smaller than the second back pressure, characterized in that the first exhaust treatment unit in such a first distance in the flow direction is formed before the second exhaust treatment unit, that during operation of a entering into the first exhaust gas treatment unit gas flow is made uniform. This means, in particular, that the back pressure in the flow direction before the exhaust gas treatment unit is influenced by the first dynamic pressure of the heat exchanger.
Bei der erfindungsgemäßen Abgasanlage beträgt der erste Abstand zwischen der ersten Abgasbehandlungseinheit und der zweiten Abgasbehandlungseinheit weniger als 15 mm, bevorzugt weniger als 10 mm, besonders bevorzugt weniger als 5 mm, so dass sich der Effekt des ersten Standrucks der ersten Abgasbehandlungseinheit und des zweiten Staudrucks der zweiten Abgasbehandlungseinheit kumulieren, so dass das Abgas, welches in die erste Abgasbehandlungseinheit strömt, einen Staudruck überwinden muss, der gröber als der erste Staudruck der ersten Abgasbehandlungseinheit alleine ist.In the exhaust system according to the invention, the first distance between the first exhaust treatment unit and the second exhaust treatment unit is less than 15 mm, preferably less than 10 mm, more preferably less than 5 mm, so that the effect of the first stall pressure of the first exhaust treatment unit and the second back pressure of accumulate second exhaust treatment unit, so that the exhaust gas flowing into the first exhaust treatment unit, must overcome a back pressure, which is coarser than the first back pressure of the first exhaust treatment unit alone.
Die Verbrennungskraftmaschine ist insbesondere ein Diesel- oder Ottomotor, beispielsweise ein Diesel- oder Ottomotor eines Kraftfahrzeugs (z. B. eines Personenkraftwagens, eines Lastkraftwagens, eines motorbetriebenen Zweirades, Bootes oder Luftfahrzeugs) oder ein Diesel- oder Ottomotor in stationärer Anwendung.The internal combustion engine is in particular a diesel or gasoline engine, for example a diesel or gasoline engine of a motor vehicle (eg a passenger car, a truck, a motorized two-wheeler, boat or aircraft) or a stationary or diesel diesel engine.
Als Abgasbehandlungseinheiten eignen sich insbesondere Wabenkörper, beispielsweise keramische oder metallische Wabenkörper, oder auch Drahtgestrickkörper, Körper aus Metallschaum oder ähnliches. Metallische Wabenkörper können insbesondere aus mindestens einer zumindest teilweise strukturierten metallischen Lage und gegebenenfalls mindestens einer im wesentlichen glatten Lage, die miteinander aufgewickelt oder gestapelt und verwunden werden, aufgebaut sein. Die miteinander verwundenen oder aufgewickelten Lagen bilden durchströmbare Hohlräume, die durch die Lagen begrenzt werden. Die Lagen sind insbesondere aus einem hochtemperaturkorrosionsfesten Material, wie Al- oder Cr-Stahl ausgebildet. Die Lagen können miteinander verbunden sein, insbesondere stoffschlüssig, wie beispielsweise durch ein Hochtemperaturlötverfahren. Sowohl die im wesentlichen glatten Lagen als auch die zumindest teilweise strukturierten Lagen können zumindest in Teilbereichen Mikrostrukturen, Leitflächen, Durchbrechungen und/oder Perforationen aufweisen, die einer noch besseren Durchmischung der Gasströmung dienen. Unter einer Abgasbehandlungseinheit wird hier insbesondere kein Wärmetauscher verstanden. Die Abgasbehandlungseinheiten können auch in einer Abgasrückführleitung ausgebildet sein.In particular, honeycomb bodies, for example ceramic or metallic honeycomb bodies, or else wire knit bodies, bodies made of metal foam or the like are suitable as exhaust gas treatment units. Metallic honeycomb bodies may in particular be constructed from at least one at least partially structured metallic layer and optionally at least one substantially smooth layer, which are wound or stacked together and wound. The twisted or wound layers form permeable cavities, which are bounded by the layers. The layers are in particular made of a high temperature corrosion resistant material, such as Al or Cr steel. The layers may be interconnected, in particular cohesively, such as by a Hochtemperaturlötverfahren. Both the essentially smooth layers and the at least partially structured layers can have microstructures, guide surfaces, perforations and / or perforations, at least in some areas, which serve for even better mixing of the gas flow. Under an exhaust gas treatment unit is understood in particular no heat exchanger. The exhaust treatment units may also be formed in an exhaust gas recirculation line.
Die Vergleichmäßigung der Gasströmung vor Eintreten in die erste Abgasbehandlungseinheit erfolgt in vorteilhafter Weise dadurch, dass die erste Abgasbehandlungseinheit relativ nahe vor der zweiten Abgasbehandlungseinheit ausgebildet wird. Dies führt zu einer Vergleichmäßigung der Gasströmung bereits in der ersten Abgasbehandlungseinheit, so dass hier die Umsetzungsrate verbessert wird, da der Querschnitt der ersten Abgasbehandlungseinheit gleichmäßiger mit Abgas beaufschlagt wird. So kann das Volumen der ersten Abgasbehandlungseinheit im Vergleich zu einem üblichen Aufbau bei gleicher Umsetzungsrate der Schadstoffe im Abgas reduziert werden. Durch die deutlich effizientere Umsetzungsrate der Schadstoffe verbessert sich auch die Umsetzungsrate der zweiten Abgasreinigungseinheit, so dass diese im Vergleich zu konventionellen zweiten Abgasreinigungseinheiten unter Umständen kleiner dimensioniert werden kann.The equalization of the gas flow before entering the first exhaust gas treatment unit is advantageously carried out by forming the first exhaust gas treatment unit relatively close to the second exhaust gas treatment unit. This leads to an equalization of the gas flow already in the first exhaust gas treatment unit, so that here the conversion rate is improved because the cross section of the first exhaust gas treatment unit is more uniformly exposed to exhaust gas. Thus, the volume of the first exhaust treatment unit can be reduced in comparison to a conventional structure at the same rate of conversion of the pollutants in the exhaust gas. Due to the much more efficient implementation rate of Pollutants also improves the conversion rate of the second exhaust gas purification unit, so that it may be smaller in size compared to conventional second exhaust gas purification units.
Um eine Abgasbehandlungseinheit auszubilden, die einen nur geringen Staudruck aufweist, ist es möglich, einen Wabenkörper einzusetzen, der eine relativ geringe Zelldichte, beispielsweise weniger als 200 cpsi (cells per square inch, Zellen pro Quadratzoll), bevorzugt weniger als 150 cpsi, besonders bevorzugt 100 cpsi und weniger, aufweist. Eine Abgasbehandlungseinheit mit einem relativ hohen Staudruck kann beispielsweise in einem hochzelligen Wabenkörper bestehen, der beispielsweise eine Zelldichte von etwa 800 cpsi, 1000 cpsi oder mehr aufweist. Weiterhin hat die Länge der Hohlräume in einem Wabenkörper Einfluss auf den Staudruck, so dass eine Abgasbehandlungseinheit mit einem relativ kleinen Staudruck durch einen kurzen Wabenkörper und eine Abgasbehandlungseinheit mit einem relativ großen Staudruck durch einen langen Wabenkörper ausgebildet werden kann.In order to form an exhaust gas treatment unit which has only a low dynamic pressure, it is possible to use a honeycomb body which has a relatively low cell density, for example less than 200 cpsi (cells per square inch), preferably less than 150 cpsi 100 cpsi and less. For example, an exhaust treatment unit having a relatively high back pressure may be a high cell honeycomb body having, for example, a cell density of about 800 cpsi, 1000 cpsi or more. Furthermore, the length of the cavities in a honeycomb body has an influence on the dynamic pressure, so that an exhaust gas treatment unit having a relatively small back pressure can be formed by a short honeycomb body and an exhaust gas treatment unit having a relatively large back pressure by a long honeycomb body.
Gemäß einer vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage ist der erste Abstand so gewählt, dass sich der Effekt des ersten Staudrucks und des zweiten Staudrucks kumulieren.According to an advantageous embodiment of the exhaust system according to the invention, the first distance is selected such that the effect of the first dynamic pressure and the second dynamic pressure accumulate.
Unter Kumulieren wird hier insbesondere verstanden, dass der vor der ersten Abgasbehandlungseinheit anliegende Staudruck größer ist als der erste Staudruck, den die erste Abgasbehandlungseinheit als solche aufweist, der also dann vorliegt, wenn nur die erste Abgasbehandlungseinheit beströmt wird, ohne dass eine zweite Abgasbehandlungseinheit ausgebildet ist. Die Kumulation der Staudrücke führt in vorteilhafter Weise dazu, dass das Abgas vor Einströmen in die erste Abgasbehandlurigseinheit einen Staudruck überwinden muss, der größer ist als der erste Staudruck der ersten Abgasbehandlungseinheit. Je nach Auslegung der ersten und der zweiten Abgasbehandlungseinheit ist der Staudruck sogar deutlich größer als der erste Staudruck. Die Vergrößerung des Staudrucks bewirkt eine Vergleichmä-βigung der Beströmung der ersten Abgasbehandlungseinheit und damit der Gasströmung durch die erste Abgasbehandlungseinheit und die zweite Abgasbehandlungseinheit.Cumulating means here in particular that the dynamic pressure present in front of the first exhaust gas treatment unit is greater than the first back pressure that the first exhaust gas treatment unit has as such, which therefore exists when only the first exhaust gas treatment unit is flown, without a second exhaust gas treatment unit being formed , The cumulation of the dynamic pressures advantageously leads to the exhaust gas, before it flows into the first exhaust gas treatment unit, having to overcome a dynamic pressure which is greater than the first back pressure of the first exhaust gas treatment unit. Depending on the design of the first and the second exhaust gas treatment unit, the dynamic pressure is even significantly greater than the first dynamic pressure. The increase of the dynamic pressure causes a Vergleichmä-ßigung the flow of the first exhaust gas treatment unit and thus the gas flow through the first exhaust gas treatment unit and the second exhaust gas treatment unit.
Gemäß einer weiteren vorteilhaften Ausgestaltung beträgt ein zweiter Abstand einer gaseintrittsseitigen Stirnseite der ersten Abgasbehandlungseinheit von einer gaseintrittsseitigen Stirnseite der zweiten Abgasbehandlungseinheit weniger als 60 mm, bevorzugt weniger als 45 mm, besonders bevorzugt weniger als 30 mm.According to a further advantageous embodiment, a second distance of a gas inlet-side end face of the first exhaust gas treatment unit from a gas inlet-side end face of the second exhaust gas treatment unit is less than 60 mm, preferably less than 45 mm, particularly preferably less than 30 mm.
Diese Werte haben sich als besonders vorteilhaft herausgestellt. Insbesondere kommt es bei üblichen Betriebsbedingungen zu einer Kumulierung der Effekte des ersten und des zweiten Staudrucks kommen.These values have proven to be particularly advantageous. In particular, it comes under normal operating conditions to cumulate the effects of the first and the second dynamic pressure come.
Gemäß einer weiteren vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage beträgt die Ausdehnung der ersten Abgäsbehandlungseinheit in Strömungsrichtung weniger als 45 mm, bevorzugt weniger als 35 mm, besonders bevorzugt 25 mm oder weniger.According to a further advantageous embodiment of the exhaust system according to the invention, the expansion of the first exhaust treatment unit in the flow direction is less than 45 mm, preferably less than 35 mm, particularly preferably 25 mm or less.
Aufgrund der sehr gleichmäßigen und effektiven Umsetzung der entsprechenden Stoffe im Abgas können relativ kleine erste Abgasbehandlungseinheiten verwendet werden. Bei der zweiten Abgasbehandlungseinheit kann gleichfalls ein kleineres Volumen gewählt werden, da beispielsweise in dem Falle, dass als zweite Abgasbehandlungseinheit ein Partikelfilter und als erste Abgasbehandlungseinheit ein Oxidationskatalysator ausgebildet ist, die gleichmäßigere Durchströmung der ersten Abgasbehandlungseinheit eine verbesserte Versorgung mit Stickstoffdioxid und folglich eine gleichmäßigere Regeneration bewirkt, so dass ein kleineres Partikelfiltervolumen ausreichend ist.Due to the very uniform and effective implementation of the corresponding substances in the exhaust gas relatively small first exhaust gas treatment units can be used. In the second exhaust treatment unit can also be chosen a smaller volume, for example, in the case that as the second exhaust treatment unit is a particulate filter and the first exhaust treatment unit formed an oxidation catalyst, the more uniform flow of the first exhaust treatment unit causes an improved supply of nitrogen dioxide and thus a more uniform regeneration so that a smaller particulate filter volume is sufficient.
Gemäß einer weiteren vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage umfassen die erste und/oder die zweite Abgasbehandlungseinheit mindestens einen Wabenkörper.According to a further advantageous embodiment of the exhaust system according to the invention, the first and / or the second exhaust gas treatment unit comprise at least one honeycomb body.
Mit einem Wabenkörper kann eine erste und/oder zweite Abgasbehandlungseinheit geschaffen werden, deren Eigenschaften wie Oberfläche, Standruck, etc. sehr genau vorherbestimmt werden können. Als Wabenkörper eignen sich insbesondere metallische oder keramische Wabenkürper. Auch Partikelfilter können als Wabenkörper mit zumindest teilweise porösen Kanalwänden und gegebenenfalls Kanalabschlüssen oder entsprechenden Leitblechen und Durchbrechungen ausgebildet sein.With a honeycomb body, a first and / or second exhaust treatment unit can be created, whose properties such as surface, pressure, etc., can be very accurately predetermined. As honeycomb body are particularly suitable metallic or ceramic honeycomb. Also particulate filter can be formed as a honeycomb body with at least partially porous channel walls and optionally channel terminations or corresponding baffles and openings.
Insbesondere ist es auch vorteilhaft, beide Abgasbehandlungseinheiten in einem gemeinsamen Gehäuse vorzusehen. Hierbei können die Abgasbehandlungseinheiten in entsprechenden Sicken des Gehäuses mittels einer Ausbördelung oder ähnlichern gehalten sein. Auch ist es möglich, die zweite Abgasbehandlungseinheit bündig auf eine Stirnseite des Wärmetauschers aufzusetzen. Hierbei kann es vorteilhaft sein, insbesondere im letzten Bereich der ersten Abgasbehandlungseinheit dem Abgas die Möglichkeit zu geben, querzuströmen. Dies kann bei Wabenkörpern dadurch erreicht werden, dass im letzten Bereich, beispielsweise in den letzten 20% oder 10% der Länge der ersten Abgasbehandlungseinheit, Perforationen in den Wänden der Hohlräume vorzusehen. Dies ist insbesondere vorteilhaft, wenn die zweite Abgasbehandlungseinheit einen Partikelfilter mit wechselweise geschlossenen Kanälen umfasst. Insbesondere ist es auch möglich, im Bereich der gasaustrittseitigen Stirnseite der ersten Abgasbehandlungseinheit oder die gaseintrittsseitigen Stirnseite der zweiten Abgasbehandlungseinheit die Kanalwandungen an unterschiedlichen Punkten enden zu lassen, so dass keine glatte Stirnfläche, sondern eine zerklüftete Stirnfläche der ersten und/oder der zweiten Abgasbehandlungseinheit entsteht, die auch zu Querströmungen insbesondere zwischen benachbarten Kanälen führen kann.In particular, it is also advantageous to provide both exhaust gas treatment units in a common housing. Here, the exhaust gas treatment units may be held in corresponding beads of the housing by means of a flanging or the like. It is also possible to fit the second exhaust gas treatment unit flush on a front side of the heat exchanger. It may be advantageous, in particular in the last region of the first exhaust gas treatment unit, to allow the exhaust gas to flow crosswise. In the case of honeycomb bodies, this can be achieved by providing perforations in the walls of the cavities in the last region, for example in the last 20% or 10% of the length of the first exhaust gas treatment unit. This is particularly advantageous if the second exhaust gas treatment unit comprises a particle filter with alternately closed channels. In particular, it is also possible to allow the duct walls to end at different points in the area of the gas outlet-side end face of the first exhaust treatment unit or the gas inlet-side end face of the second exhaust treatment unit, so that no smooth end face, but a rugged face of the first and / or the second exhaust treatment unit arises, which can also lead to cross flows in particular between adjacent channels.
Gemäß einer weiteren vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage umfasst zumindest die erste Abgasbehandlungseinheit eine katalytisch aktive Beschichtung.According to a further advantageous embodiment of the exhaust system according to the invention, at least the first exhaust gas treatment unit comprises a catalytically active coating.
Die katalytisch aktive Beschichtung umfasst beispielsweise einen keramischen Washcoat, der Materialien enthält, die die gewünschten Reaktionen katalysieren, also insbesondere die Reaktionstemperatur dieser Reaktionen so weit herabsetzen, dass diese in nennenswertem Umfang bei den Temperaturen in der Abgasrückführleitung ablaufen. Als Katalysatoren eignen sich insbesondere Edelmetalle wie Platin, Rhodium oder ähnliches. Eine Oxidationskatalysatorbeschichtung katalysiert insbesondere die Oxidation von Kohlenwasserstoffen (HC) oder Stickoxiden (NOX). Weiterhin ist es gleichfalls erfindungsgemäß möglich, dass alternativ oder kumulativ die zweite Abgasbehandlungseinheit eine katalytisch aktive Beschichtung aufweist. Beispielsweise kann die erste Abgasbehandlungseinheit einen Hydrolysekatalysator umfassen, während die zweite Abgasbehandlungseinheit einen SCR-Katalysator umfasst.The catalytically active coating comprises, for example, a ceramic washcoat which contains materials which catalyze the desired reactions, ie in particular reduce the reaction temperature of these reactions to such an extent that they run to a considerable extent at the temperatures in the exhaust gas recirculation line. Suitable catalysts are in particular noble metals such as platinum, rhodium or the like. An oxidation catalyst coating catalyzes in particular the oxidation of hydrocarbons (HC) or nitrogen oxides (NO X ). Furthermore, it is likewise possible according to the invention that, alternatively or cumulatively, the second exhaust gas treatment unit has a catalytically active coating. For example, the first exhaust treatment unit may comprise a hydrolysis catalyst, while the second exhaust treatment unit comprises an SCR catalyst.
Gemäß einer weiteren vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage ist das Verhältnis von erstem Staudruck zu zweitem Staudruck größer als 2, bevorzugt größer als 10.According to a further advantageous embodiment of the exhaust system according to the invention, the ratio of the first dynamic pressure to the second dynamic pressure is greater than 2, preferably greater than 10.
Insbesondere bei diesen Staudruckverhältnissen, wenn also der Staudruck der zweiten Abgasbehandlungseinheit um mehr als einen Faktor 2 oder sogar 10 größer ist als der Staudruck der ersten Abgasbehandlungseinheit, kumulieren in besonders vorteilhafter Weise die Effekte des ersten Staudrucks des Wärmetauschers und des zweiten Staudrucks der Abgasbehandlungseinheit bereits bei ersten Abständen von 15 mm oder weniger.Particularly in the case of these dynamic pressure conditions, ie if the dynamic pressure of the second exhaust gas treatment unit is greater than the dynamic pressure of the first exhaust gas treatment unit by more than a factor of 2 or even 10, the effects of the first dynamic pressure of the heat exchanger and the second dynamic pressure of the exhaust gas treatment unit accumulate in a particularly advantageous manner first distances of 15 mm or less.
Gemäß einer weiteren vorteilhaften Ausgestaltung der erfindungsgemäßen Abgasanlage umfasst die zweite Abgasbehandlungseinheit mindestens eines der folgenden Bauteile:
- (a) offener Partikelfilter;
- (b) geschlossener Partikelfilter; und
- (c) SCR-Katalysator.
- (a) open particulate filter;
- (b) closed particulate filter; and
- (c) SCR catalyst.
Alle diese drei möglichen zweiten Abgasbehandlungseinheiten (a), (b) und (c) stellen Bauteile mit einem relativ hohen Staudruck dar.All of these three possible second exhaust treatment units (a), (b) and (c) are components with a relatively high dynamic pressure.
Ein offener Partikelfilter ist dadurch zu charakterisieren, dass durch ihn ein Partikel, insbesondere ein Rußpartikel, grundsätzlich durchtreten kann, ohne von einer Kanalwand aufgefangen worden zu sein. Bei einem geschlossenen Partikelfilter ist dies nicht möglich, da dieser regelmäßig wechselweise verschlossene Kanäle aufweist, so dass also in eine Teilmenge Kanäle das Abgas nur hineinströmen kann, aber nicht durch eine reguläre Kanalöffnung wieder den Kanal verlassen kann, sondern dass vielmehr das Abgas durch die porösen Wände des Filters strömen muss, wodurch es in eine andere Teilmenge von Kanälen gelangt, die wiederum keinen eingangsseitigen freien Strömungsquerschnitt, sondern nur einen ausgangsseitigen freien Strömungsquerschnitt aufweisen. Bei geschlossenen Partikelfiltern ist grundsätzlich das Durchbrechen eines relativ großen Partikels durch den Filter nicht möglich, wenn dieser intakt ist, da das Partikel in der porösen Kanalwand hängen bleibt. Bei einem offenen Filtersystem ist dies grundsätzlich möglich. Ein offener Partikelfilter weist zumindest in einem Teil seiner Wände poröse Bereiche auf.An open particle filter should be characterized in that a particle, in particular a soot particle, can pass through it without being caught by a channel wall. In a closed particulate filter, this is not possible, as this regularly alternately closed channels, so that in a subset channels the exhaust gas can only flow in, but not through a regular channel opening can leave the channel, but rather that the exhaust gas through the porous Walls of the filter must flow, whereby it enters another subset of channels, which in turn have no input-side free flow cross-section, but only an output-side free flow cross-section. In the case of closed particulate filters, in principle, it is not possible to break through a relatively large particle through the filter if it is intact, since the particle gets caught in the porous channel wall. In an open filter system this is possible in principle. An open particle filter has porous regions at least in part of its walls.
Beispielsweise ist es möglich, einen offenen oder geschlossenen Partikelfilter als zweite Abgasbehandlungseinheit vorzusehen, welchem ein Oxidationskatalysator als erste Abgasbehandlungseinheit vorgeschaltet ist, so dass der Partikelfilter kontinuierlich regeneriert wird, in dem im Oxidationskatalysator Stickstoffinonoxid zu Stickstoffdioxid oxidiert wird, welches zur Verbrennung der Rußpartikel einsetzbar ist. Erfindungsgemäß kann der Oxidationskatalysator kleiner ausgebildet sein, als wenn der Abstand zwischen den beiden Abgasbehandlungseinheiten nicht erfindungsgemäß gewählt wird. Insbesondere dann, wenn ein geschlossener Partikelfilter, beispielsweise ein Dieselpartikelfilter an sich bekannter Bauart, als zweite Abgasbehandlungseinheit und ein Wabenkörper als erste Abgasbehandlungseinheit ausgebildet ist und der Abstand möglichst klein, gegebenenfalls sogar nahe null durch Anlegen der Stirnseite des Wabenkörpers an die entsprechende Stirnseite des Partikelfilter, gewählt wird, ist es vorteilhaft, im Endbereich der Kanalwandungen der ersten Abgasbehandlungseinheit Perforationen und/oder gegebenenfalls Leitbleche vorzusehen, die eine weitere Vermischung des Abgases begünstigen.For example, it is possible to provide an open or closed particulate filter as a second exhaust treatment unit, which is preceded by an oxidation catalyst as the first exhaust treatment unit, so that the particulate filter is continuously regenerated, is oxidized in the oxidation catalyst Nitrogen in oxide to nitrogen dioxide, which can be used for combustion of the soot particles is. According to the invention, the oxidation catalyst can be made smaller than when the distance between the two exhaust gas treatment units is not selected according to the invention. In particular, if a closed particulate filter, for example a diesel particulate filter of a known type, is designed as the second exhaust gas treatment unit and a honeycomb body as the first exhaust gas treatment unit and the distance as small as possible, possibly even close to zero by applying the end face of the honeycomb body to the corresponding end face of the particulate filter, is selected, it is advantageous to provide in the end region of the channel walls of the first exhaust treatment unit perforations and / or optionally baffles, which favor further mixing of the exhaust gas.
Ein weiteres Beispiel ist ein hochzelliger Wabenkörper mit SCR-Beschichtung als zweite Abgasbehandlungseinheit, der ein niederzelliger Wabenkörper mit einer die Hydrolyse von Harnstoff fördernder Beschichtung vorgeschaltet ist.Another example is a high cell SCR coating honeycomb body second exhaust treatment unit, preceded by a low cell honeycomb body with a urea hydrolysis promoting coating.
Es wird ausdrücklich darauf hingewiesen, dass es sich hier lediglich um Beispiele für Systeme mit hohem Staudruck handelt, wobei die Erfindung nicht auf diese Beispiele beschränkt ist. Die vorliegende Erfindung wird weiterhin anhand der beigefügten Figuren näher erläutert, ohne dass sie auf die dort gezeigten und beschriebenen Ausführungsbeispiele und Vorteile beschränkt wäre. Es zeigen:
- Fig. 1
- schematisch ein Ausführungsbeispiel einer erfindungsgemäßen Abgasanlage;
- Fig. 2
- schematisch einen Ausschnitt des Ausführungsbeispiels einer erfindungsgemäßen Abgasanlage;
- Fig. 3
- schematisch im Querschnitt einen Wabenkörper; und
- Fig.4
- schematisch Wahrscheinlichkeitsverteilungen von Strömungsgeschwindigkeiten.
- Fig. 1
- schematically an embodiment of an exhaust system according to the invention;
- Fig. 2
- schematically a section of the embodiment of an exhaust system according to the invention;
- Fig. 3
- schematically in cross section a honeycomb body; and
- Figure 4
- schematically probability distributions of flow velocities.
Erfindungsgemäß ist die erste Abgasbehandlungseinheit 3 in einem solchen ersten Abstand 5 in Strömungsrichtung vor der zweiten Abgasbehandlungseinheit 4 ausgebildet, so dass im Betrieb eine in die erste Abgasbehandlungseinheit 3 eintretende durch einen Pfeil symbolisierte Gasströmung 6 vergleichmäßigt wird. Der erste Abstand 5 liegt hier insbesondere bei weniger als 15 mm, bevorzugt bei weniger als 10 mm, besonders bevorzugt bei weniger als 5 mm. Die erste 3 und zweite Abgasbehandlungseinheit 4 sind so ausgeführt, dass es bei diesem ersten Abstand 5 zur Kumulation der Effekte des ersten Staudrucks und des zweiten Staudrucks kommt, so dass das in die erste Abgasbehandlungseinheit 3 einströmende Abgas einen Staudruck überwinden muss, der größer als der erste Staudruck der ersten Abgasbehandlungseinheit 3 als solche ist. Dies führt wie oben dargelegt zu einer Vergleichmäßigung der Gasströmung 6, die in die erste Abgasbehandlungseinheit 3 einströmt.According to the invention, the first exhaust
Die erfindungsgemäße Abgasanlage 1 erlaubt in vorteilhafter Weise die Ausbildung von Systemen mit zwei Abgasbehandlungseinheiten 3, 4, die in Strömungsrichtung hintereinander angeordnet sind. Durch die Strömungsvergleichmäßigung können die erste 3 und/oder die zweite Abgasbehandlungseinheit 4 kleiner ausgeführt werden. Dies gilt beispielsweise dann, wenn als erste Abgasbehandlungseinheit 3 ein Oxidationskatalysator und als zweite Abgasbehandlungseinheit 4 ein Partikelfilter ausgebildet ist. Durch die Vergleichmäßigung der Strömung in die erste Abgasbehandlungseinheit 3 wird die Umsetzungsrate erhöht, so dass erste 3 und/oder zweite Abgasbehandlungseinheit 4 kleiner ausgeführt werden können. Dies spart erhebliche Kosten bei der Auslegung solcher Systeme.The
- 11
- Abgasanlageexhaust system
- 22
- Verbrennungsmotorinternal combustion engine
- 33
- erste Abgasbehandlungseinheitfirst exhaust treatment unit
- 44
- zweite Abgasbehandlungseinheitsecond exhaust treatment unit
- 55
- erster Abstandfirst distance
- 66
- Gasströmunggas flow
- 77
- zweiter Abstandsecond distance
- 88th
- gaseintrittsseitige Stirnseite der ersten AbgasbehandlungseinheitGas inlet side end face of the first exhaust gas treatment unit
- 99
- gaseintritsseitige Stirnseite der zweiten AbgasbehandlungseinheitGas inlet side end side of the second exhaust treatment unit
- 1010
- Ausdehnungexpansion
- 1111
- Wabenkörperhoneycombs
- 1212
- Wabenstrukturhoneycomb structure
- 1313
- Mantelrohrcasing pipe
- 1414
- Hohlraumcavity
- 1515
- im wesentlichen glatte Lageessentially smooth position
- 1616
- zumindest teilweise strukturierte Lageat least partially structured situation
Claims (7)
- An exhaust system (1) for an internal combustion engine (2), comprising a first exhaust gas treatment unit (3) with a first back pressure and a second exhaust gas treatment unit (4) with a second back pressure, wherein the first back pressure is less than the second back pressure, characterized in that the first exhaust gas treatment unit (3) is constructed at a first distance (5) upstream of the second exhaust gas treatment unit (4) in the direction of flow such that during operation a gas flow (6) which enters the first exhaust gas treatment unit (3) is homogenized, in which the first distance (5) between the first exhaust gas treatment unit (3) and the second exhaust gas treatment unit (4) is less than 15 mm, so that the effect of the first back pressure and of the second back pressure accumulate and so that the exhaust gas, before flowing into the first exhaust gas treatment unit (3), has to overcome a back pressure which is higher than the first back pressure of the first exhaust gas treatment unit (3) alone.
- The exhaust system (1) as claimed in claim 1, in which a second distance (7) of a gas inlet end (8) of the first exhaust gas treatment unit (3) from a gas inlet end (9) of the second exhaust gas treatment unit (4) is less than 60 mm, preferably less than 45 mm, particularly preferably less than 30 mm.
- The exhaust system (1) as claimed in one of the preceding claims, in which the extent (10) of the first exhaust gas treatment unit (3) in the direction of flow is less than 45 mm, preferably less than 35 mm, particularly preferably 25 mm or less.
- The exhaust system (1) as claimed in one of the preceding claims, in which the first exhaust gas treatment unit (3) and/or the second exhaust gas treatment unit (4) comprise at least one honeycomb body (11).
- The exhaust system (1) as claimed in one of the preceding claims, in which at least the first exhaust gas treatment unit (3) comprises a catalytically active coating.
- The exhaust system (1) as claimed in one of the preceding claims, in which the ratio of the first back pressure to the second back pressure is greater than 2, preferably greater than 10.
- The exhaust system (1) as claimed in one of the preceding claims, in which the second exhaust gas treatment unit (4) comprises at least one of the following components:(a) an open particle filter;(b) a closed particle filter; and(c) an SCR catalytic converter.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102005014265A DE102005014265A1 (en) | 2005-03-24 | 2005-03-24 | Exhaust system with two exhaust treatment units |
PCT/EP2006/002488 WO2006100003A1 (en) | 2005-03-24 | 2006-03-17 | Exhaust system with two exhaust treatment units |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1882090A1 EP1882090A1 (en) | 2008-01-30 |
EP1882090B1 true EP1882090B1 (en) | 2011-10-05 |
Family
ID=36370833
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP06723523A Active EP1882090B1 (en) | 2005-03-24 | 2006-03-17 | Exhaust system with two exhaust treatment units |
Country Status (5)
Country | Link |
---|---|
US (1) | US7597859B2 (en) |
EP (1) | EP1882090B1 (en) |
JP (1) | JP2009530521A (en) |
DE (1) | DE102005014265A1 (en) |
WO (1) | WO2006100003A1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
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US20090100809A1 (en) * | 2007-10-23 | 2009-04-23 | Baldwin Jr Donald W | Filter assembly for removing particulates in an exhaust gas in a fuel engine |
US20110030325A1 (en) * | 2009-08-06 | 2011-02-10 | Glanfield Ian S | Air filter |
US10387506B2 (en) * | 2013-03-14 | 2019-08-20 | Eharmony, Inc. | Systems and methods for online matchmaking |
US9810125B2 (en) | 2015-12-08 | 2017-11-07 | Jumbomaw Technology Co., Ltd. | Catalytic converter |
EP3179065B1 (en) * | 2015-12-08 | 2017-12-06 | Jumbomaw Technology Co., Ltd. | Catalytic converter |
EP3511541B1 (en) * | 2018-01-15 | 2021-11-03 | AM Group Redback AB | Catalytic converter for classic cars |
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DE581190C (en) * | 1930-10-21 | 1933-07-22 | Wilhelm Widmann | Roll film camera with cutting device |
US3978567A (en) * | 1973-03-19 | 1976-09-07 | Chrysler Corporation | Method of making a catalytic reactor for automobile |
DE3407172C2 (en) * | 1984-02-28 | 1986-09-04 | Degussa Ag, 6000 Frankfurt | Device for cleaning exhaust gases from diesel engines |
JPS62273049A (en) * | 1986-05-21 | 1987-11-27 | Toyota Motor Corp | Metal carrier of metal carrier catalyst |
JPS6318123A (en) * | 1986-07-10 | 1988-01-26 | Fuji Heavy Ind Ltd | Catalytic converter |
JPH086582B2 (en) * | 1986-10-31 | 1996-01-24 | マツダ株式会社 | Engine exhaust gas purification catalytic device |
JPH0394836A (en) * | 1989-09-05 | 1991-04-19 | Cataler Kogyo Kk | Carrier for exhaust gas purifier |
DE4024942A1 (en) | 1990-08-06 | 1992-02-13 | Emitec Emissionstechnologie | MONOLITHIC METAL HONEYCOMB WITH VARIOUS CHANNEL NUMBER |
JP2819864B2 (en) * | 1991-06-26 | 1998-11-05 | トヨタ自動車株式会社 | Metal carrier for exhaust gas purification catalyst |
DE9210010U1 (en) | 1992-07-25 | 1992-10-22 | Heinrich Gillet GmbH & Co KG, 6732 Edenkoben | Device for catalytic cleaning of exhaust gases from internal combustion engines |
JPH07328452A (en) * | 1994-06-13 | 1995-12-19 | Showa Aircraft Ind Co Ltd | Metal carrier for catalyst device |
JPH10205325A (en) * | 1997-01-21 | 1998-08-04 | Isuzu Motors Ltd | Nox reducing and removing honeycomb catalyst device |
DE19858974B4 (en) * | 1998-12-19 | 2006-02-23 | Daimlerchrysler Ag | Process for the catalytic conversion of a starting material, in particular a gas mixture |
DE10003090A1 (en) * | 2000-01-25 | 2001-07-05 | Siemens Ag | SCR catalyst apparatus for reducing nitrogen oxides, comprises two sections made from catalyst-coated grooved plates in stacked assemblies |
US6919052B2 (en) * | 2000-12-04 | 2005-07-19 | Delphi Technologies, Inc. | Catalytic converter |
JP2003062472A (en) * | 2001-08-24 | 2003-03-04 | Toyota Central Res & Dev Lab Inc | Honeycomb reforming catalyst body |
SE524225C2 (en) * | 2002-02-15 | 2004-07-13 | Volvo Technology Corp | An apparatus for treating a gas flow |
DE10254764A1 (en) * | 2002-11-22 | 2004-06-03 | Emitec Gesellschaft Für Emissionstechnologie Mbh | exhaust system |
DE10315593B4 (en) * | 2003-04-05 | 2005-12-22 | Daimlerchrysler Ag | Exhaust gas aftertreatment device and method |
DE10321105A1 (en) * | 2003-05-09 | 2004-12-02 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Regeneration of a particle trap |
JP3896998B2 (en) | 2003-07-08 | 2007-03-22 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
US7740809B2 (en) * | 2006-02-15 | 2010-06-22 | Hitachi Metals, Ltd. | Exhaust gas-cleaning apparatus |
-
2005
- 2005-03-24 DE DE102005014265A patent/DE102005014265A1/en not_active Withdrawn
-
2006
- 2006-03-17 JP JP2008502296A patent/JP2009530521A/en active Pending
- 2006-03-17 WO PCT/EP2006/002488 patent/WO2006100003A1/en not_active Application Discontinuation
- 2006-03-17 EP EP06723523A patent/EP1882090B1/en active Active
-
2007
- 2007-09-24 US US11/859,873 patent/US7597859B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
JP2009530521A (en) | 2009-08-27 |
EP1882090A1 (en) | 2008-01-30 |
US20080008631A1 (en) | 2008-01-10 |
US7597859B2 (en) | 2009-10-06 |
DE102005014265A1 (en) | 2006-10-12 |
WO2006100003A1 (en) | 2006-09-28 |
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