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DE19753572A1 - Catalytic purification of exhaust gases from diesel engine over wide temperature range - Google Patents

Catalytic purification of exhaust gases from diesel engine over wide temperature range

Info

Publication number
DE19753572A1
DE19753572A1 DE1997153572 DE19753572A DE19753572A1 DE 19753572 A1 DE19753572 A1 DE 19753572A1 DE 1997153572 DE1997153572 DE 1997153572 DE 19753572 A DE19753572 A DE 19753572A DE 19753572 A1 DE19753572 A1 DE 19753572A1
Authority
DE
Germany
Prior art keywords
catalyst
low
temperature
cat
temperature catalyst
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.)
Withdrawn
Application number
DE1997153572
Other languages
German (de)
Inventor
Werner Koehl
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayerische Motoren Werke AG
Original Assignee
Bayerische Motoren Werke AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Bayerische Motoren Werke AG filed Critical Bayerische Motoren Werke AG
Priority to DE1997153572 priority Critical patent/DE19753572A1/en
Publication of DE19753572A1 publication Critical patent/DE19753572A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404Removing only nitrogen compounds
    • B01D53/9409Nitrogen oxides
    • B01D53/9431Processes characterised by a specific device
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N13/00Exhaust 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
    • F01N13/009Exhaust 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Toxicology (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Exhaust Gas After Treatment (AREA)

Abstract

The engine exhaust gases enter a precatalyst unit where they encounter a high-temperature catalyst and a relatively smaller low-temperature catalyst. The gases continue into the main catalyst unit, via a low temperature catalyst. In the low temperature section of the precatalyst unit, when the high temperature catalyst is operational, predetermined hydrocarbon slippage is effected. Preferred features: At high exhaust temperatures, hydrocarbon slip sets in, the precatalyst low temperature section being inadequate to eliminate it.

Description

Die Erfindung bezieht sich nach dem Oberbegriff des Patentanspruches 1 auf ein Verfahren zur katalytischen Abgasreinigung bei Dieselmotoren, wobei das Abgas über mehrere in einem Abgasstrang verteilt angeordnete Katalysatoren mit unter­ schiedlichen Temperaturfenstern für Stickoxid-Reduktionen geleitet wird.According to the preamble of claim 1, the invention relates to Process for catalytic exhaust gas purification in diesel engines, the exhaust gas over a plurality of catalytic converters arranged in an exhaust line with under different temperature windows for nitrogen oxide reductions.

Bekanntlich weisen Katalysatoren für Dieselabgas den gravierenden Nachteil auf, daß ihre DeNOx-Aktivität auf ein enges Temperaturfenster begrenzt ist. Zweck­ mäßigerweise wird hierfür eine serielle Anordnung von Katalysatoren zur Steigerung der Gesamtreduktion von Stickoxiden vorgesehen, wobei nach jeweiliger Ab­ gastemperatur der vordere oder hintere Katalysator im passenden Bereich liegt. Bekannt sind außerdem serielle Anordnungen von Katalysatoren mit unterschied­ lichen Temperaturfenstern, um den Gesamttemperaturbereich, in welchem eine Re­ duktion von Stickoxiden möglich ist, noch weiter aufzuspreizen.As is known, catalysts for diesel exhaust have the serious disadvantage that that their DeNOx activity is limited to a narrow temperature window. Purpose For this purpose, a serial arrangement of catalysts for increasing is moderate the overall reduction of nitrogen oxides is provided, whereby according to the respective Ab gas temperature the front or rear catalytic converter is in the appropriate range. Serial arrangements of catalysts with a difference are also known Lichen temperature windows to the total temperature range in which a Re production of nitrogen oxides is possible to spread even further.

Weiter ist es bekannt, bei Kombinationen von Hoch- und Tieftemperatur-Katalysato­ ren Dieselkraftstoff als Reduktionsmittel entweder im Abgasstrang stromauf eines Vorkatalysators oder direkt im Brennraum bereitzustellen. So ergibt sich bei einer Kombination eines Tieftemperatur-Katalysators in der Vorkatposition mit einem Hochtemperatur-Katalysator in der Hauptkatposition der Nachteil, daß bei hohen Temperaturen, bei welchen der Hauptkat seine maximale NOx-Reduktionswirkung entfalten könnte, dieser nicht mehr mit Reduktionsmittel versorgt wird, da der davor liegende hochaktive Tieftemperaturkat Kohlenwasserstoffe in jenem Temperatur­ bereich nahezu vollständig oxidiert.It is also known for combinations of high and low temperature catalysts Ren diesel fuel as a reducing agent either in the exhaust line upstream of one To provide pre-catalyst or directly in the combustion chamber. This results in one Combination of a low-temperature catalytic converter in the pre-cat position with one High temperature catalyst in the main catalytic converter has the disadvantage that at high  Temperatures at which the main catalyst has its maximum NOx reduction effect could unfold, this is no longer supplied with reducing agent, because of the before lying highly active low-temperature cat hydrocarbons in that temperature area almost completely oxidized.

Bei einer umgekehrten Kombination mit einem Hochtemperatur-Katalysator in der Vorkatposition und einem Tieftemperatur-Katalysator in der Hauptkatposition ergibt sich der Nachteil, daß bei motornaher Anordnung des Hochtemperaturkat bei niedri­ geren Abgastemperaturen kein Reduktionsmittel eingespritzt werden kann, da un­ terhalb des Light-Offs Kohlenwasserstoffe durch beide Katalysatoren durchbrechen. Der Tieftemperatur-Katalysator liegt dann so weit vom Motor entfernt, daß in ihm ebenfalls keine Konversion erfolgt. Damit ist keine NOx-Reduktion bei niedriger Motorlast möglich, außerdem steigen die HC-Emissionen.With a reverse combination with a high temperature catalyst in the Pre-cat position and a low-temperature catalyst in the main cat position results there is the disadvantage that when the high-temperature cat is arranged close to the engine at low At lower exhaust gas temperatures, no reducing agent can be injected, since un break through hydrocarbons through both catalysts below the light-off. The low-temperature catalytic converter is then so far away from the engine that it is in it likewise no conversion took place. This means there is no reduction in NOx Engine load possible, HC emissions also increase.

Der bei der ersten Kat-Kombination sich ergebende Mangel an reduzierenden Koh­ lenwasserstoffen am Hochtemperatur-Katalysator der Hauptkat-Position führt, um das in der Regel größere Volumen des Hochtemperatur-Katalysators in der Haupt­ katposition zur NOx-Reduktion voll zur Verfügung zu haben, dazu, daß vor diesem Hochtemperatur-Katalysator eine geeignete Kraftstoffeindüsung in den Abgasstrang vorgesehen werden muß, um eine Versorgung des Hochtemperatur-Katalysators mit Kohlenwasserstoffen sicherzustellen. Derartige Systeme sind bezüglicher ihrer Ko­ sten und den technischen Risiken nachteilig.The lack of reducing Koh resulting from the first catalyst combination hydrogen at the high-temperature catalytic converter in the main cat position the usually larger volume of the high temperature catalyst in the main To have fully available cat position for NOx reduction, in front of this High-temperature catalyst suitable fuel injection into the exhaust system must be provided to supply the high-temperature catalyst with Ensure hydrocarbons. Such systems are in terms of their Ko most and the technical risks disadvantageous.

Bei der zweiten Kat-Kombination ist eine signifikante NOx-Reduktion in diesel­ typischen Temperaturbereichen ausgeschlossen, außerdem ergeben sich HC-Pro­ bleme.With the second catalyst combination there is a significant NOx reduction in diesel typical temperature ranges excluded, in addition there are HC-Pro bleme.

Der Erfindung liegt die Aufgabe zugrunde, das gattungsgemäße Verfahren zur ka­ talytischen Abgasreinigung bei Dieselmotoren derart zu verbessern, daß mit ge­ ringstem Bauaufwand und ohne Einführung zusätzlicher Reduktionsmittel die kataly­ tische Abgasreinigung qualitativ verbessert ist. The invention has for its object the generic method for ka To improve talytical exhaust gas cleaning in diesel engines so that with ge the least construction effort and without the introduction of additional reducing agents the kataly table exhaust gas cleaning is qualitatively improved.  

Diese Aufgabe ist mit dem Patentanspruch dadurch gelöst, daß das Abgas stromab des Dieselmotors in einer Vorkat-Einrichtung in Strömungsrichtung über einen Hochtemperatur-Katalysator und einen relativ kleineren Tieftemperatur-Katalysator und anschließend in einer Hauptkat-Einrichtung über einen Tieftemperatur-Kataly­ sator geführt wird, wobei über den Vorkat-Tieftemperatur-Katalysator bei wirkendem Hochtemperatur-Katalysator ein vorbestimmter Kohlenwasserstoff (HC)-Schlupf bewirkt wird.This object is achieved with the patent claim in that the exhaust gas downstream of the diesel engine in a pre-cat device in the flow direction via a High temperature catalyst and a relatively smaller low temperature catalyst and then in a main cat facility via a low-temperature catalyzer sator is performed, with the pre-cat low-temperature catalyst at the active High temperature catalyst a predetermined hydrocarbon (HC) slip is effected.

Vorzugsweise wird dieser Kohlenwasserstoff-Schlupf des Vorkat-Tieftemperatur- Katalysators in Ausgestaltung der Erfindung über seine aktive Größe bei hohen Ab­ gastemperaturen erzeugt.This hydrocarbon slip of the pre-cat low-temperature Catalyst in an embodiment of the invention about its active size at high Ab generated gas temperatures.

Mit der in der Vorkat-Einrichtung erfindungsgemäß getroffenen Kombination ist ein verbessertes Verfahren zur katalytischen Abgasreinigung bei Dieselmotoren er­ reicht, wobei dieser Tieftemperatur-Katalysator so beschaffen ist bezüglich Größe und Oxidationsaktivität, daß er bei niedrigen Abgastemperaturen HC-reduziert und seine DeNOx-Wirkung entfaltet, jedoch bei hohen Temperaturen einen Kohlen­ wasserstoff-Schlupf bewirkt. Dieser Kohlenwasserstoff-Schlupf dient bei höheren Abgastemperaturen als Reduktionsmittel für den in der Hauptkat-Einrichtung vorge­ sehenen Tieftemperatur-Katalysator zur Erzielung einer vollen DeNOx-Wirkung.With the combination made according to the invention in the pre-cat device is a improved process for catalytic exhaust gas cleaning in diesel engines enough, this low-temperature catalyst is designed in terms of size and oxidation activity that it reduces HC and at low exhaust temperatures its DeNOx effect develops, but a carbon at high temperatures causes hydrogen slip. This hydrocarbon slip serves at higher ones Exhaust gas temperatures as a reducing agent for the pre-in the main cat facility see low-temperature catalyst to achieve a full DeNOx effect.

Zusammenfassend ergibt sich in vorteilhafter Weise bei niedrigen Abgastemperatu­ ren eine volle NOx-Reduktion sowie eine HC-Reduktion im Tieftemperatur-Kataly­ sator der Vorkat-Einrichtung und bei hohen Abgastemperaturen eine volle NOx-Re­ duktion sowohl im Hochtemperatur-Katalysator der Vorkat-Einrichtung als auch im Tieftemperatur-Katalysator der Hauptkat-Einrichtung, wobei der Kohlenwasserstoff- Schlupf aus der Vorkat-Einrichtung eine zusätzliche Kraftstoffeindüsung zwischen Vorkat-Einrichtung und Hauptkat-Einrichtung in vorteilhafter Weise erübrigt. Bei geschickter Auswahl und Bemessung des Tieftemperatur-Katalysators der Vorkat- Einrichtung ist eine sichere Versorgung mit Kohlenwasserstoffen aus dem Kohlen­ wasserstoff-Schlupf als Reduktionsmittel für den Tieftemperatur-Katalysator der Hauptkat-Einrichtung erreicht. In summary, this advantageously results at low exhaust gas temperatures full NOx reduction and HC reduction in the low-temperature catalyst of the pre-cat device and at high exhaust gas temperatures a full NOx re duction both in the high-temperature catalyst of the pre-cat device and in Low temperature catalytic converter of the main catalytic converter, the hydrocarbon Slip an additional fuel injection from the pre-cat device Pre-cat device and main cat device are advantageously dispensed with. At Skilful selection and dimensioning of the low-temperature catalytic converter of the pre-cat Establishment is a secure supply of hydrocarbons from coal hydrogen slip as a reducing agent for the low-temperature catalyst Main cat facility reached.  

Die Erfindung ist im folgenden beschrieben. Bei einem Verfahren zur katalytischen Abgasreinigung bei Dieselmotoren wird das Abgas über mehrere in einem Ab­ gasstrang verteilt angeordnete Katalysatoren mit unterschiedlichen Temperatur­ fenstern für Stickoxid-Reduktionen geleitet.The invention is described below. In a catalytic process Exhaust gas cleaning in diesel engines, the exhaust gas over several in one Ab Catalysts with different temperatures arranged in a gas line windows for nitrogen oxide reductions.

Zur qualitativen Verbesserung der katalytischen Abgasreinigung bei einfachem Auf­ bau der Vorrichtung und unter Vermeidung der Einführung zusätzlicher Reduk­ tionsmittel wird erfindungsgemäß vorgeschlagen, daß das Abgas stromab des Die­ selmotors in einer Vorkat-Einrichtung in Strömungsrichtung über einen Hochtempe­ ratur-Katalysator und einen relativ kleineren Tieftemperatur-Katalysator sowie an­ schließend in einer Hauptkat-Einrichtung über einen Tieftemperatur-Katalysator ge­ führt wird, wobei über den Vorkat-Tieftemperatur-Katalysator bei wirkendem Hochtemperatur-Katalysator ein vorbestimmter Kohlenwasserstoff (HC)-Schlupf bewirkt wird. Dieser Kohlenwasserstoff-Schlupf des Vorkat-Tieftemperatur-Katalysators wird über seine aktive Größe bei hohen Abgastemperaturen erzeugt.For the qualitative improvement of catalytic exhaust gas cleaning with a simple opening construction of the device and avoiding the introduction of additional Reduk tion medium is proposed according to the invention that the exhaust gas downstream of the selmotors in a pre-cat device in the direction of flow over a high temperature rature catalyst and a relatively smaller low-temperature catalyst as well closing in a main catalyst facility via a low-temperature catalyst leads, being over the pre-catalyst low-temperature catalyst High temperature catalyst a predetermined hydrocarbon (HC) slip is effected. This hydrocarbon slip of the pre-cat low-temperature catalyst is generated via its active size at high exhaust gas temperatures.

Claims (2)

1. Verfahren zur katalytischen Abgas-Reinigung bei Dieselmotoren,
  • - wobei das Abgas über mehrere in einem Abgasstrang verteilt ange­ ordnete Katalysatoren mit unterschiedlichen Temperaturfenstern für Stickoxid-Reduktionen geleitet wird, dadurch gekennzeichnet,
  • - daß das Abgas stromab des Dieselmotors in einer Vorkat-Einrichtung in Strömungsrichtung über einen Hochtemperatur-Katalysator und einen relativ kleineren Tieftemperatur-Katalysator sowie
  • - anschließend in einer Hauptkat-Einrichtung über einen Tieftempera­ tur-Katalysator geführt wird, wobei
  • - über den Vorkat-Tieftemperatur-Katalysator bei wirkendem Vorkat- Hochtemperatur-Katalysator ein vorbestimmter Kohlenwasserstoff (HC)-Schlupf bewirkt wird.
1. Process for catalytic exhaust gas purification in diesel engines,
  • the exhaust gas being passed over a plurality of catalytic converters distributed in an exhaust line with different temperature windows for nitrogen oxide reductions, characterized in that
  • - That the exhaust gas downstream of the diesel engine in a pre-cat device in the direction of flow via a high-temperature catalyst and a relatively smaller low-temperature catalyst and
  • - Is then performed in a main catalyst device over a low-temperature catalyst, wherein
  • - A predetermined hydrocarbon (HC) slip is effected via the pre-cat low-temperature catalyst with the pre-cat high-temperature catalyst acting.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß der Kohlen­ wasserstoff (HC)-Schlupf des Vorkat-Tieftemperatur-Katalysators über seine aktive Größe bei hohen Abgastemperaturen erzeugt wird.2. The method according to claim 1, characterized in that the coals hydrogen (HC) slip of the pre-cat low-temperature catalyst over its active size is generated at high exhaust gas temperatures.
DE1997153572 1997-12-03 1997-12-03 Catalytic purification of exhaust gases from diesel engine over wide temperature range Withdrawn DE19753572A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE1997153572 DE19753572A1 (en) 1997-12-03 1997-12-03 Catalytic purification of exhaust gases from diesel engine over wide temperature range

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1997153572 DE19753572A1 (en) 1997-12-03 1997-12-03 Catalytic purification of exhaust gases from diesel engine over wide temperature range

Publications (1)

Publication Number Publication Date
DE19753572A1 true DE19753572A1 (en) 1999-07-15

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10341869A1 (en) * 2003-09-09 2005-03-31 Volkswagen Ag Regeneration of a diesel particulate filter of a diesel internal combustion engine
CN112031898A (en) * 2019-05-17 2020-12-04 丰田自动车株式会社 Control device and control method for hybrid vehicle

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19617563C1 (en) * 1996-05-02 1997-06-19 Daimler Benz Ag Exhaust gas catalyst for a diesel motor

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19617563C1 (en) * 1996-05-02 1997-06-19 Daimler Benz Ag Exhaust gas catalyst for a diesel motor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10341869A1 (en) * 2003-09-09 2005-03-31 Volkswagen Ag Regeneration of a diesel particulate filter of a diesel internal combustion engine
DE10341869B4 (en) * 2003-09-09 2014-09-11 Volkswagen Ag Regeneration of a diesel particulate filter of a diesel internal combustion engine
CN112031898A (en) * 2019-05-17 2020-12-04 丰田自动车株式会社 Control device and control method for hybrid vehicle
CN112031898B (en) * 2019-05-17 2022-05-13 丰田自动车株式会社 Control device and control method for hybrid vehicle

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