DE102007022858A1 - Catalytic nitrogen oxide-reduction selecting device for use in internal combustion engine, has larger ammonia storage medium connected with smaller ammonia storage medium by reloading valve - Google Patents
Catalytic nitrogen oxide-reduction selecting device for use in internal combustion engine, has larger ammonia storage medium connected with smaller ammonia storage medium by reloading valve Download PDFInfo
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- DE102007022858A1 DE102007022858A1 DE102007022858A DE102007022858A DE102007022858A1 DE 102007022858 A1 DE102007022858 A1 DE 102007022858A1 DE 102007022858 A DE102007022858 A DE 102007022858A DE 102007022858 A DE102007022858 A DE 102007022858A DE 102007022858 A1 DE102007022858 A1 DE 102007022858A1
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- ammonia gas
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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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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2062—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4525—Gas separation or purification devices adapted for specific applications for storage and dispensing systems
-
- 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
-
- 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
- F01N2610/10—Adding substances to exhaust gases the substance being heated, e.g. by heating tank or supply line of the added substance
-
- 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
- F01N2610/14—Arrangements for the supply of substances, e.g. conduits
-
- 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
- F01N2610/14—Arrangements for the supply of substances, e.g. conduits
- F01N2610/1406—Storage means for substances, e.g. tanks or reservoirs
-
- 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
- F01N2610/14—Arrangements for the supply of substances, e.g. conduits
- F01N2610/1486—Means to prevent the substance from freezing
-
- 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
- F01N5/00—Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy
- F01N5/02—Exhaust or silencing apparatus combined or associated with devices profiting by exhaust energy the devices using heat
-
- 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
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
Die Erfindung betrifft eine Vorrichtung zur selektiven katalytischen NOX-Reduktion nach Oberbegriff des Anspruchs 1. Die Erfindung betrifft ferner ein hierauf gerichtetes Verfahren.The invention relates to a device for selective catalytic NO x reduction according to the preamble of claim 1. The invention further relates to a method directed thereto.
Stand der TechnikState of the art
Ammoniak
ist bekannt als selektives und effizientes Reduktionsmittel für
die katalytische Reduktion von Stickoxyden in sauerstoffhaltigen
Abgasen beispielsweise von Verbrennungsmotoren. Aus Gründen
seiner Toxizität sowie der Sicherheitsprobleme, die durch
die Lagerung gasförmigen Ammoniaks entstehen, wurden Verfahren
entwickelt, wonach Ammoniak erst am Ort seiner Verwendung als Reduktionsmittel
durch Hydrolyse von Harnstoff erzeugt wird. Die hierauf gerichteten
Apparaturen waren aber sehr umfangreich und kompliziert zu steuern.
Zur Vermeidung von deren Nachteilen schlägt die
Offenbarung der ErfindungDisclosure of the invention
Aufgabe der Erfindung ist es, einen Ammoniakspeicher und ein Verfahren zur Freisetzung von Ammoniak bereitzustellen, das die genannten Nachteile vermeidet.task The invention is an ammonia storage and a method for To provide release of ammonia, the disadvantages mentioned avoids.
Hierzu wird eine Vorrichtung zur selektiven katalytischen NOX-Reduktion in sauerstoffhaltigen Abgasen eines Verbrennungsmotors vorgeschlagen, mit einem Reduktionskatalysator und unter Verwendung von Ammoniakgas, das durch Speichermediumaufheizen zur Verfügung gestellt wird. Es ist vorgesehen, dass mindestens zwei unterschiedlich große Ammoniakgasquellen vorgesehen sind, die jeweils ein festes Ammoniakspeichermedium und jeweils eine Heizung aufweisen. Als Speichermedium kommen feste Ammoniakspeichersubstanzen zum Einsatz, aus denen Ammoniak mittels Temperaturanhebung freigesetzt wird. Geeignete Speichersubstanzen sind hierbei etwa Salze, insbesondere Chloride und/oder Sulfate eines oder mehrerer Erdalkalielemente wie beispielsweise MgCl2, CaCl2 und/oder eines oder mehrerer 3d-Nebengruppenelemente wie Mangan, Eisen, Kobalt, Nickel, Kupfer und/oder Zink. Die Speichermedien sind hierbei in unterschiedlich großen Speichern ausgebildet, die jeweils eine selbstständige Ammoniakgasquelle bilden. Hierbei ist die eine Ammoniakgasquelle deutlich größer als die andere ausgebildet. Im Kaltstartbetrieb, also dann, wenn das Speichermedium kalt ist und kein oder nur sehr wenig gasförmiges Ammoniak vorliegt, wird die kleinere Ammoniakgasquelle verwendet, die sich unter Einsatz einer geringeren Energiemenge auf das gewünschte und/oder erforderliche Temperaturniveau erhitzen lässt. Auf diese Weise wird die benötigte Ammoniakgasmenge in relativ kurzer Zeit und mit relativ geringem Energieaufwand erzielt, so dass die katalytische NOX-Reduktion schnell wirksam werden kann.For this purpose, a device for selective catalytic NO x reduction in oxygen-containing exhaust gases of an internal combustion engine is proposed, with a reduction catalyst and using ammonia gas, which is provided by storage medium heating. It is provided that at least two different sized ammonia gas sources are provided, each having a solid ammonia storage medium and each having a heater. As a storage medium solid ammonia storage substances are used, from which ammonia is released by means of temperature increase. Suitable storage substances here are, for example, salts, in particular chlorides and / or sulfates, of one or more alkaline earth elements, for example MgCl 2 , CaCl 2 and / or one or more 3d sub-group elements, such as manganese, iron, cobalt, nickel, copper and / or zinc. The storage media are in this case formed in different sized memories, each forming an independent ammonia gas source. Here, the one ammonia gas source is significantly larger than the other formed. In cold start mode, that is, when the storage medium is cold and no or very little gaseous ammonia is present, the smaller source of ammonia gas is used, which can be heated using a smaller amount of energy to the desired and / or required temperature level. In this way, the required amount of ammonia gas is achieved in a relatively short time and with relatively little expenditure of energy, so that the catalytic NO x reduction can be effective quickly.
In einer weiteren Ausführungsform ist die Heizung der kleineren Ammoniakgasquelle eine elektrische Heizung. Elektrische Heizungen, wie aus dem Stand der Technik bekannt, sind über das KFZ-Bordnetz, gegebenenfalls unter Verwendung verstärkter Batterien, leicht realisierbar. Dadurch, dass die elektrische Heizung (zunächst) nur für die kleinere Ammoniakgasquelle in Betrieb ist, ist die Belastung des elektrischen Bordnetzes im Vergleich zu Ausführungsformen, wie sie aus dem Stand der Technik bekannt sind, gering. Auf diese Weise kann schnell und mit geringem Energieaufwand die benötigte Ammoniakgasmenge freigesetzt werden.In In another embodiment, the heater is the smaller one Ammonia gas source an electric heater. Electric heaters, As known from the prior art, are via the vehicle electrical system, optionally using reinforced batteries, easily realizable. Because the electric heater (initially) is only in operation for the smaller ammonia gas source, is the load of the electrical system compared to embodiments, as known from the prior art, low. To this Way can quickly and with little energy required Amount of ammonia gas are released.
In einer weiteren Ausführungsform ist vorgesehen, dass die Heizung der größeren Ammoniakgasquelle eine elektrische und/oder eine Abwärmeheizung ist. Selbstverständlich kann auch die Heizung der größeren Ammoniakgasquelle, die insbesondere erst zeitversetzt nach der kleineren Ammoniakgasquelle zugeschaltet wird, eine elektrische Heizung sein, insbesondere dann, wenn ihre Versorgung bereits über den Drehstromgenerator des Fahrzeugs und nicht mehr allein aus Akkumulatoren erfolgt. Bevorzugt ist aber eine Kombination oder auch eine ausschließliche Verwendung einer Abwärmeheizung vorgesehen, also einer solchen, die die in Verbrennungsmotoren in großem Maße produzierte Abwärme nutzt, beispielsweise über Wärmetauscher, die in das Kühlsystem eingebunden sind, oder die in anderer Weise die Abwärme des Verbrennungsmotors nutzen.In A further embodiment provides that the Heating the larger ammonia gas source an electric and / or a waste heat heating. Of course can also be the heating of the larger ammonia gas source, in particular only delayed in time after the smaller source of ammonia gas is switched on, be an electric heater, in particular, if their supply already has the three-phase generator of the vehicle and not solely from accumulators. Prefers but is a combination or an exclusive Use of a waste heat heating provided, so one such as those in internal combustion engines to a large extent produced waste heat uses, for example, over Heat exchangers, which are integrated into the cooling system are, or in other ways the waste heat of the internal combustion engine use.
In einer bevorzugten Ausführungsform ist die Abwärmeheizung eine Verbrennungsabgasheizung. Zur Beheizung der größeren Ammoniakgasquelle wird in dieser Ausführungsform das heiße Abgas des Verbrennungsmotors verwendet, das über einen geeigneten, entsprechend dimensionierten Abgaswärmetauscher und/oder einen Wärmetauscherkreislauf unter Verwendung eines Mediums wie beispielsweise Wasser oder Öl, der Heizung der größeren Ammoniakgasquelle zugeführt wird. Hierbei wird das elektrische Bordsystem nicht belastet.In a preferred embodiment, the waste heat heater is a combustion exhaust gas heater. For heating the larger source of ammonia gas, the hot exhaust gas of the internal combustion engine is used in this embodiment, which has a suitable, appropriately sized exhaust gas heat exchanger and / or a heat exchanger circuit using a medium such as water or oil, the heating of the larger ammonia gas source is supplied. In this case, the electrical system is not charged.
In einer weiteren bevorzugten Ausführungsform ist das größere Ammoniakspeichermedium mit dem kleineren Ammoniakspeichermedium über mindestens ein Wiederbeladungsventil verbunden. Der Prozess der thermisch bedingten Ammoniakgasfreisetzung aus einem festen Ammoniakspeichermedium ist bei den meisten festen Ammoniakspeichermedien, insbesondere Salzen, umkehrbar. Das System zur Wiederbeladung muss hierbei den erforderlichen Betriebsbedingungen entsprechend für die Wiederbeladung ausgeführt werden, wobei diese von dem verwendeten Speichermedium abhängen. Für den Fall, dass NH3 im MgCl2 in der Form Mg(NH3)6Cl2 gespeichert wird, kann die Wiederbeladung, also die Absorption von NH3 durch MgCl2 beispielsweise, bei einer Temperatur von 25°C und einem Druck von 4 bar erfolgen. Dieser Druckaufbau auf die erforderliche Druckstärke erfolgt über das mindestens eine Wiederbeladungsventil aus dem größeren Ammoniakspeichermedium hin zum kleineren Ammoniakspeichermedium und eine Beaufschlagung des kleineren Ammoniakspeichermediums mit Ammoniak aus dem größeren Ammoniakspeichermedium, der bei dessen Betrieb zur Verfügung steht. Diese Zuleitung erfolgt insbesondere in Zeiten, in denen der Ammoniakbedarf im Abgasstrang zur NOX-Reduktion gering ist. Für Mg(NH3)6Cl2 kann die Desorption bei 5 bar und 200°C erfolgen. Alternativ kann die Wiederbeladung des kleineren Ammoniakspeichermediums auch nach Abstellen des Verbrennungsmotors erfolgen, solange die Temperatur in dem größeren Ammoniakspeichermedium hoch genug ist. Selbstverständlich sind hier alle Ausführungsformen denkbar, die in einer technisch sinnvollen Art und Weise und bezogen auf die verwendeten Ammoniakspeichermedien realisierbar sind.In a further preferred embodiment, the larger ammonia storage medium is connected to the smaller ammonia storage medium via at least one reload valve. The process of thermally induced ammonia gas evolution from a solid ammonia storage medium is reversible in most solid ammonia storage media, especially salts. The system for reloading must be carried out according to the required operating conditions for reloading, depending on the storage medium used. In the event that NH 3 is stored in MgCl 2 in the form of Mg (NH 3 ) 6 Cl 2 , the reloading, ie the absorption of NH 3 by MgCl 2, for example, at a temperature of 25 ° C and a pressure of 4 bar. This pressure build-up to the required pressure level via the at least one reload from the larger ammonia storage medium towards the smaller ammonia storage medium and an admission of smaller ammonia storage medium with ammonia from the larger ammonia storage medium, which is available during its operation. This supply takes place in particular in times when the ammonia requirement in the exhaust gas system for NO x reduction is low. For Mg (NH 3 ) 6 Cl 2 desorption can be carried out at 5 bar and 200 ° C. Alternatively, the reloading of the smaller ammonia storage medium may be done even after the engine is turned off as long as the temperature in the larger ammonia storage medium is high enough. Of course, all embodiments are conceivable here, which can be realized in a technically meaningful manner and based on the ammonia storage media used.
Weiter wird ein Verfahren zur selektiven katalytischen NOX-Reduktion in sauerstoffhaltigen Abgasen eines Verbrennungsmotors vorgeschlagen, mit einem Reduktionskatalysator und unter Verwendung von Ammoniakgas, das durch Speichermediumaufheizen zur Verfügung gestellt wird. Es ist vorgesehen, dass zwei unterschiedlich große Ammoniakgasquellen verwendet werden, wobei die kleinere Ammoniakgasquelle während eines Startvorgangs des Verbrennungsmotors Ammoniakgas durch Aufheizung zur Verfügung stellt. Während des Startvorgangs des Verbrennungsmotors wird das Ammoniakgas durch Aufheizung des Ammoniakspeichermediums der kleineren Ammoniakgasquelle gewonnen, wobei der Energiebedarf wesentlich geringer ist als bei Aufheizung der größeren Ammoniakgasquelle. Insbesondere ist hierbei vorgesehen, dass die kleinere Ammoniakgasquelle wesentlich kleiner als die größere Ammoniakgasquelle gewählt wird, beispielsweise in einer solchen Art und Weise, dass sie gerade die im Startvorgang (oder etwas darüber hinaus) benötigte Ammoniakgasmenge zur Verfügung stellt, wobei nach Erreichen einer erforderlichen Betriebstemperatur des Verbrennungsmotors und der größeren Ammoniakgasquelle auf jene umgeschaltet wird.Further, a method for selective catalytic NO x reduction in oxygen-containing exhaust gases of an internal combustion engine is proposed, with a reduction catalyst and using ammonia gas provided by storage medium heating. It is envisaged that two different sized ammonia gas sources will be used, with the smaller ammonia gas source providing ammonia gas by heating during a start-up of the engine. During the starting process of the internal combustion engine, the ammonia gas is recovered by heating the ammonia storage medium of the smaller ammonia gas source, wherein the energy requirement is much lower than when heating the larger ammonia gas source. In particular, it is provided in this case that the smaller source of ammonia gas is chosen to be substantially smaller than the larger source of ammonia gas, for example in such a way that it provides just the amount of ammonia gas required in the starting process (or slightly more), after reaching a required operating temperature the internal combustion engine and the larger ammonia gas source is switched to those.
Weitere vorteilhafte Ausführungsformen ergeben sich aus den Unteransprüchen und aus Kombinationen derselben.Further advantageous embodiments will become apparent from the dependent claims and combinations thereof.
Kurze Beschreibung der ZeichnungenBrief description of the drawings
Die Erfindung wird nachfolgend anhand eines Ausführungsbeispiels und von Figuren näher erläutert.The Invention will be described below with reference to an embodiment and explained in more detail by figures.
Es zeigenIt demonstrate
Ausführungsform(en) der ErfindungEmbodiment (s) of the invention
Die
Heizung
ZITATE ENTHALTEN IN DER BESCHREIBUNGQUOTES INCLUDE IN THE DESCRIPTION
Diese Liste der vom Anmelder aufgeführten Dokumente wurde automatisiert erzeugt und ist ausschließlich zur besseren Information des Lesers aufgenommen. Die Liste ist nicht Bestandteil der deutschen Patent- bzw. Gebrauchsmusteranmeldung. Das DPMA übernimmt keinerlei Haftung für etwaige Fehler oder Auslassungen.This list The documents listed by the applicant have been automated generated and is solely for better information recorded by the reader. The list is not part of the German Patent or utility model application. The DPMA takes over no liability for any errors or omissions.
Zitierte PatentliteraturCited patent literature
- - EP 0932440 B1 [0002] EP 0932440 B1 [0002]
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102007022858A DE102007022858A1 (en) | 2007-05-15 | 2007-05-15 | Catalytic nitrogen oxide-reduction selecting device for use in internal combustion engine, has larger ammonia storage medium connected with smaller ammonia storage medium by reloading valve |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102007022858A DE102007022858A1 (en) | 2007-05-15 | 2007-05-15 | Catalytic nitrogen oxide-reduction selecting device for use in internal combustion engine, has larger ammonia storage medium connected with smaller ammonia storage medium by reloading valve |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE102007022858A1 true DE102007022858A1 (en) | 2008-11-20 |
Family
ID=39868734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE102007022858A Ceased DE102007022858A1 (en) | 2007-05-15 | 2007-05-15 | Catalytic nitrogen oxide-reduction selecting device for use in internal combustion engine, has larger ammonia storage medium connected with smaller ammonia storage medium by reloading valve |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE102007022858A1 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010105833A1 (en) | 2009-03-18 | 2010-09-23 | Amminex A/S | Improved method for storing and delivering ammonia from solid storage materials using a vacuum pump |
| WO2011113454A1 (en) * | 2010-03-16 | 2011-09-22 | Amminex A/S | Method and device for controlled dosing of a gas with fluctuating supply pressure |
| CN102733915A (en) * | 2012-07-02 | 2012-10-17 | 中国第一汽车股份有限公司 | Post-processing control unit of ammonia storage and supply in electric heating and afterheat manners |
| FR2991712A1 (en) * | 2012-06-06 | 2013-12-13 | Faurecia Sys Echappement | AMMONIA GENERATION DEVICE |
| FR2994454A1 (en) * | 2012-08-09 | 2014-02-14 | Peugeot Citroen Automobiles Sa | Post-processing system for post-processing exhaust fumes produced by internal combustion engine of car, has main cartridges connected to main line through secondary line, and shedding line extending between main cartridges and main line |
| US20160008761A1 (en) * | 2013-02-25 | 2016-01-14 | Umicore Ag & Co. Kg | SCR CATALYTIC CONVERTER HAVING IMPROVED NOx CONVERSION |
| DE102009000411B4 (en) * | 2009-01-26 | 2017-06-08 | Robert Bosch Gmbh | Device for storing and dispensing ammonia and drive device with such a device |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0932440B1 (en) | 1997-07-03 | 2003-04-09 | Robert Bosch Gmbh | METHOD AND DEVICE FOR SELECTIVE CATALYTIC NOx REDUCTION |
-
2007
- 2007-05-15 DE DE102007022858A patent/DE102007022858A1/en not_active Ceased
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0932440B1 (en) | 1997-07-03 | 2003-04-09 | Robert Bosch Gmbh | METHOD AND DEVICE FOR SELECTIVE CATALYTIC NOx REDUCTION |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102009000411B4 (en) * | 2009-01-26 | 2017-06-08 | Robert Bosch Gmbh | Device for storing and dispensing ammonia and drive device with such a device |
| US8551219B2 (en) | 2009-03-18 | 2013-10-08 | Amminex Emissions Technology A/S | Method for storing and delivering ammonia from solid storage materials using a vacuum pump |
| EP2236784A1 (en) | 2009-03-18 | 2010-10-06 | Amminex A/S | Improved method for storing and delivering ammonia from solid storage materials using a vacuum pump |
| WO2010105833A1 (en) | 2009-03-18 | 2010-09-23 | Amminex A/S | Improved method for storing and delivering ammonia from solid storage materials using a vacuum pump |
| US8869514B2 (en) | 2010-03-16 | 2014-10-28 | Amminex Emissions Technology A/S | Method and device for controlled dosing of a gas with fluctuating supply pressure |
| WO2011113454A1 (en) * | 2010-03-16 | 2011-09-22 | Amminex A/S | Method and device for controlled dosing of a gas with fluctuating supply pressure |
| FR2991712A1 (en) * | 2012-06-06 | 2013-12-13 | Faurecia Sys Echappement | AMMONIA GENERATION DEVICE |
| CN103470347A (en) * | 2012-06-06 | 2013-12-25 | 佛吉亚排气系统有限公司 | Device for generating ammonia |
| CN103470347B (en) * | 2012-06-06 | 2016-01-20 | 佛吉亚排气系统有限公司 | For generation of the equipment of ammonia |
| US9567884B2 (en) | 2012-06-06 | 2017-02-14 | Faurecia Systemes D'echappement | Device for generating ammonia |
| DE102013105775B4 (en) * | 2012-06-06 | 2017-12-14 | Faurecia Systemes D'echappement | Device for generating ammonia |
| CN102733915A (en) * | 2012-07-02 | 2012-10-17 | 中国第一汽车股份有限公司 | Post-processing control unit of ammonia storage and supply in electric heating and afterheat manners |
| CN102733915B (en) * | 2012-07-02 | 2016-11-23 | 中国第一汽车股份有限公司 | There are electrical heating and the aftertreatment control unit of afterheat manner storing and supplying ammonia |
| FR2994454A1 (en) * | 2012-08-09 | 2014-02-14 | Peugeot Citroen Automobiles Sa | Post-processing system for post-processing exhaust fumes produced by internal combustion engine of car, has main cartridges connected to main line through secondary line, and shedding line extending between main cartridges and main line |
| US20160008761A1 (en) * | 2013-02-25 | 2016-01-14 | Umicore Ag & Co. Kg | SCR CATALYTIC CONVERTER HAVING IMPROVED NOx CONVERSION |
| US9694320B2 (en) * | 2013-02-25 | 2017-07-04 | Umicore Ag & Co. Kg | SCR catalytic converter having improved NOx conversion |
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