US20060213189A1 - Treatment of nox sorber regeneration gas - Google Patents
Treatment of nox sorber regeneration gas Download PDFInfo
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- US20060213189A1 US20060213189A1 US10/561,093 US56109304A US2006213189A1 US 20060213189 A1 US20060213189 A1 US 20060213189A1 US 56109304 A US56109304 A US 56109304A US 2006213189 A1 US2006213189 A1 US 2006213189A1
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- sorber
- engine
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- exhaust gas
- engine according
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features having two or more separate purifying devices arranged in series
- F01N13/0097—Exhaust or silencing apparatus characterised by constructional features having two or more separate purifying devices arranged in series the purifying devices are arranged in a single housing
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9481—Catalyst preceded by an adsorption device without catalytic function for temporary storage of contaminants, e.g. during cold start
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
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- F01N3/0871—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents using means for controlling, e.g. purging, the absorbents or adsorbents
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- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
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- 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
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- 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
- F01N3/2093—Periodically blowing a gas through the converter, e.g. in a direction opposite to exhaust gas flow or by reversing exhaust gas flow direction
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- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
- F02M26/13—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
- F02M26/14—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories in relation to the exhaust system
- F02M26/15—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories in relation to the exhaust system in relation to engine exhaust purifying apparatus
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- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
- F02M26/13—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
- F02M26/14—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories in relation to the exhaust system
- F02M26/16—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories in relation to the exhaust system with EGR valves located at or near the connection to the exhaust system
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- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
- F02M26/65—Constructional details of EGR valves
- F02M26/71—Multi-way valves
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- F02M63/00—Other fuel-injection apparatus having pertinent characteristics not provided for in groups F02M39/00 - F02M57/00 or F02M67/00; Details, component parts, or accessories of fuel-injection apparatus, not provided for in, or of interest apart from, the apparatus of groups F02M39/00 - F02M61/00 or F02M67/00; Combination of fuel pump with other devices, e.g. lubricating oil pump
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- F01N2610/02—Adding substances to exhaust gases the substance being ammonia or urea
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- F02M63/00—Other fuel-injection apparatus having pertinent characteristics not provided for in groups F02M39/00 - F02M57/00 or F02M67/00; Details, component parts, or accessories of fuel-injection apparatus, not provided for in, or of interest apart from, the apparatus of groups F02M39/00 - F02M61/00 or F02M67/00; Combination of fuel pump with other devices, e.g. lubricating oil pump
- F02M63/02—Fuel-injection apparatus having several injectors fed by a common pumping element, or having several pumping elements feeding a common injector; Fuel-injection apparatus having provisions for cutting-out pumps, pumping elements, or injectors; Fuel-injection apparatus having provisions for variably interconnecting pumping elements and injectors alternatively
- F02M63/0225—Fuel-injection apparatus having a common rail feeding several injectors ; Means for varying pressure in common rails; Pumps feeding common rails
Definitions
- This invention relates to treatment of NO x in engine exhaust gas, more particularly to the treatment of NO x sorber regeneration gas in the exhaust of a lean-burn reciprocating engine.
- sorb terms based on the word ‘sorb’ will be used to denote ‘absorb’ or ‘adsorb’ or any occurrence of both such processes; and metal compounds effective to sorb NO x will be referred as ‘oxides’, with the understanding that this term includes other oxidic compounds such as hydroxides and carbonates effective as NO x sorbents and present in the conditions of exhaust gas treatment.
- EP-B-0341832 (incorporated herein by reference) describes a process for combusting particulate matter in diesel exhaust gas, which method comprising oxidising nitrogen monoxide in the exhaust gas to nitrogen dioxide on a catalyst, filtering the particulate matter from the exhaust gas and combusting the filtered particulate matter in the nitrogen dioxide at up to 400° C.
- a catalyst for oxidising nitrogen monoxide in the exhaust gas to nitrogen dioxide on a catalyst
- filtering the particulate matter from the exhaust gas and combusting the filtered particulate matter in the nitrogen dioxide at up to 400° C.
- Such a system is available from Johnson Matthey and is marketed as the CRT®.
- a problem associated with NO x sorber regeneration is that it generates a pulse of enriched exhaust gas containing unburned hydrocarbon (HC) fuel as reductant and NO x . Unreacted HC and NO x are emitted from the tailpipe and can often be seen as a puff of smoke. Since typical NO x sorber regeneration strategies comprise regenerating for a second or so every few minutes, such emissions can contribute to failure of future emission standards for particulates, HC and NO x .
- HC unburned hydrocarbon
- a lean-burn reciprocating engine emitting exhaust gas containing NO x and having a treatment system comprising at least one NO x sorber for sorbing NO x when the exhaust gas is lean means for intermittently contacting the at least one NO x sorber with an agent effective to convert NO x to N 2 thereby to regenerate the at least one NO x sorber and means for feeding effluent of said contacting to the engine inlet.
- the engine is preferably one equipped for exhaust gas recirculation (EGR) in normal or occasional modes of operation.
- EGR exhaust gas recirculation
- an EGR system can be added to an engine not normally using EGR.
- the system preferably includes at least two NO x sorbers arranged in parallel and means for selectively contacting fewer than all of them with the agent.
- the flow rate of the gas in the NO x sorber(s) under regeneration is preferably limited further, to be less than in the remaining NOx sorber(s) and especially to be below the rate of recirculation in an existing EGR system.
- Such system preferably includes an EGR pump, which determines the flow rate of the recycled effluent.
- the agent may be a non-selective reductant such as hydrocarbon, CO or hydrogen, injected as such or as compound(s), for example engine fuel, convertible thereto in regeneration conditions over the NO x sorber or in a pre-injection step.
- a non-selective reductant such as hydrocarbon, CO or hydrogen
- injected as such or as compound(s) for example engine fuel, convertible thereto in regeneration conditions over the NO x sorber or in a pre-injection step.
- Non-selective reductant is evidently used if provided by rich/neutral operation of a cylinder.
- the agent may be a NO x -specific reactant, for example a nitrogen hydride such as ammonia or hydrazine, conveniently provided as a precursor such as an amide for example urea or ammonium carbamate, and possibly fed via a catalyst effective to generate the free hydride.
- a nitrogen hydride such as ammonia or hydrazine
- a precursor such as an amide for example urea or ammonium carbamate
- the engine exhaust system may include: upstream of the NO x sorber(s), catalytic oxidation of HC and CO to steam and CO 2 and/or of NO to NO 2 ; and PM collection preferably downstream of that catalytic oxidation; and/or downstream of the NO x sorber(s): catalytic oxidation of residual HC and CO; collection of PM passing the NO x sorbers or passing an upstream filter as a result of too small particle size or release by filter flow reversal.
- the engine may be designed and calibrated to emit raw exhaust gas containing enough NO x for the combustion, after oxidation of NO to NO 2 , of the whole carbonaceous fraction of said PM. Alternatively it may be designed and calibrated to emit, at least temporarily, raw exhaust gas containing too little NO x to complete said combustion, after oxidation of NO to NO 2 .
- the PM collection means preferably comprises a catalyst effective to promote said combustion and possibly also an oxygen storage material. In each combustion procedure the temperature is at or above the ‘balance temperature’ for NO 2 or, additionally, for oxygen, continuously or at intervals when PM has accumulated to a design level. If PM collection uses a filter, provision may be made for intermittent reversal of flow direction therethrough.
- the NO x sorbent is typically selected from:
- catalytic materials such as precious metals, especially Pt+Rh, effective to promote reaction of NO x with reductant or NO x -specific reactant.
- the sorbent(s) and catalyst(s) are suitably disposed on a flowthrough monolithic substrates composed of ceramic, wound corrugated metal, or metal foam or sinter or ordered or random-packed wire or flat wire.
- Filters if used, may use substrates similar to those of sorbents and catalysts, but in ‘filter-grade’ permeable to gas and having limited permeability to PM.
- the system suitably includes a 4-way valve.
- a 4-way valve typically comprises: an outer cylindrical or frusto-conical casing formed with angularly spaced apertures each leading to external flow connections; and deflector means effective to: direct either of two incoming streams to a single outlet; or to direct a single incoming stream to either of two outlets; or to combine two incoming streams into a single stream.
- the valve means comprises also actuator means operating through a seal.
- the deflector is preferably operable over an arcuate path between two extreme positions at which selected gas flow is required.
- the deflector may be a ‘butterfly’.
- the valve casing may be formed with a wall-region of greater diameter corresponding to an intended traverse of the butterfly, and the change to the lesser diameter at the extremities of the traverse is formed as a step conformed to the profile of the butterfly and effective as a seal against gas leakage.
- the traverse of the butterfly is typically 10 to 20% of the circumference of the casing. If the intermediate non-selective gas flow is required, this is provided by the actuator means.
- the deflector means may be provided by a barrel fitting fluid-tightly within the casing and rotatable on an axis transverse to the main direction of fluid flow; formed along each of two or more radial planes of the barrel at least one fluid tight dividing member; and formed in each division at least one passage open at mutually angled positions about the circumference of the barrel, said positions corresponding to the apertures.
- the barrel (if used) can be provided by uniting sheet material to define its outer shape and internal passages or by shaping solid material and forming the passages by boring thereinto, so that the residues between bores constitute the dividing members.
- Each passage normally has an outlet angled to its inlet, for example perpendicularly in a 4-way valve with one inlet connection and two or three outlet connections. In a 4-way valve having two inlet connections and two outlet connections, each passage may have one inlet and two outlets.
- FIG. 1 is a flow sheet showing an exhaust gas treatment system in which the valve is used to provide switching flow between two NO x sorbers;
- FIG. 2 is a flow sheet showing an exhaust gas treatment system in which also the valve in a variant is used to provide flow-reversal through a PM filter;
- FIGS. 3A, 3B and 3 C show enlarged plan views of a valve as used in FIGS. 1 and 2 ;
- the inlet system comprises fuel feed 12 , air feed 14 and exhaust gas recirculation (EGR) feed 16 , and exhaust gas passes out through manifold 18 to exhaust gas aftertreatment system 19 comprising reactor 20 containing oxidation catalyst 22 consisting of a ceramic honeycomb carrying a washcoat and Pt, followed by PM filter 24 .
- Filter 24 consists of a filter-grade ceramic honeycomb the passages of which are alternatingly open and closed at the inlet end and, corresponding to the inlet open passages, alternatingly closed at the outlet end. It may carry a catalyst for soot oxidation, for example Pt or La/Cs/V 2 O 5.
- the downstream end of reactor 20 is provided with outlets 26 leading respectively to NO x sorbers 30 A and 30 B, each of which holds a ceramic honeycomb unit carrying an alumina washcoat containing metallic Pt+Rh and barium oxide.
- Sorbers 30 A,B may be provided in separate cans as shown or, to save space, may be in fluid-tight subdivisions of a single can.
- Each sorber 30 A,B is equipped with an injector 32 A,B for hydrocarbon from the common-rail system of the engine (connection not shown), or of ammonia or precursor thereof.
- Each outlet end of sorbers 30 A,B is connected to one of the two inlets of 4 -way valve 28 , whose outlets 34 to the EGR inlet 16 (via a pump, not shown) and 36 to atmosphere align with one or other of the outlets indicated by arrows.
- Valve 28 is operable between three positions 28 X, 28 Y and 28 Z (Y and Z insets).
- the exhaust gas comprising steam(H 2 O (g) ), dinitrogen (N 2 ), oxygen (O 2 ), carbon dioxide (CO 2 ), unburned hydrocarbon fuel (HC), carbon monoxide (CO), nitrogen oxides (NO x ) and particulate matter (PM), at e.g. 300° C. contacts catalyst 22 over which NO is oxidised to NO 2 and some of the HC and CO are oxidised to steam and CO 2 . It then enters filter 24 on which most of the PM is collected and combusted by reaction with the NO 2 formed in catalyst 24 and possibly also with O 2 .
- steam(H 2 O (g) ), dinitrogen (N 2 ), oxygen (O 2 ), carbon dioxide (CO 2 ), unburned hydrocarbon fuel (HC), carbon monoxide (CO), nitrogen oxides (NO x ) and particulate matter (PM) at e.g. 300° C. contacts catalyst 22 over which NO is oxidised to NO 2 and some of the HC and CO are oxidised to
- the PM-freed gas then undergoes treatment in one of the three modes: 28 X: sorbers 30 A and 30 B each sorb NO x from approximately half the total gas flowing; sorber outlet gas passes mainly to atmosphere or further treatment at 36 , partly to EGR at 34 at the flow rating of the EGR pump (not shown); 28 Y: sorber 30 A receives a fraction, corresponding to the EGR pump rating, of the total gas flowing and also HC or ammonia injected at 32 A.
- valve 28 Operation of valve 28 is the same as in FIG. 1 , except that outlet 36 to atmosphere is replaced by connection 37 to vessel 38 holding filter 40 , the duty of which is to collect PM released from filter 25 .
- PM is typically ash, in which event filter 40 may be disposable, such as a fibre or paper filter.
- Another duty of filter 40 can be to collect any ultra-fine combustible PM not collected by filter 25 .
- a characteristic of modern diesel engines is that engine out NO x and/or exhaust gas temperature can be too low for passive filter regeneration using NO 2 generated catalytically by oxidation of NO as described in EP-B-0341832.
- One solution to this problem is to regenerate the filter actively by increasing the temperature in the exhaust system thereby to combust PM on the filter and maintain the back pressure across the filter within acceptable design tolerances.
- Such active regeneration techniques are described in EP 0758713 (incorporated herein by reference), for example.
- An advantage of the system disclosed in FIG. 2 to the practical application of the CRTO process is that flow reversal in the filter can be used to clear PM that is not readily combusted in NO 2 over a drive cycle.
- the uncombusted PM can be collected on a second, disposable filter for removal at suitable intervals.
- the arrangement has particular use to the retrofit market, providing a practical and economic alternative to installing expensive and fuel-costly active regeneration apparatus.
- each external connection is numbered as in FIGS. 1 and 2 .
- the plan views shown in these figures relate to an essentially cylindrical valve casing 50 formed internally with circumferential regions 52 of greater diameter, defining the range of traverse of rectangular butterfly deflector 54 having pivoted operating shaft 56 extending out of the valve casing via a seal to an actuator (not shown).
- the extremities of the range of traverse are defined by steps 58 between regions differing in diameter, such steps limiting gas leakage out of its intended path.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Biomedical Technology (AREA)
- Toxicology (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Exhaust Gas After Treatment (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Exhaust-Gas Circulating Devices (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0314245.2A GB0314245D0 (en) | 2003-06-18 | 2003-06-18 | Engine exhaust gas treatment |
| GB0314245.2 | 2003-06-18 | ||
| PCT/GB2004/002612 WO2004113693A1 (en) | 2003-06-18 | 2004-06-18 | TREATMENT OF NOx SORBER REGENERATION GAS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20060213189A1 true US20060213189A1 (en) | 2006-09-28 |
Family
ID=27636877
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US10/561,093 Abandoned US20060213189A1 (en) | 2003-06-18 | 2004-06-18 | Treatment of nox sorber regeneration gas |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20060213189A1 (https=) |
| EP (1) | EP1633961A1 (https=) |
| JP (1) | JP2006527814A (https=) |
| KR (1) | KR20060038947A (https=) |
| CN (1) | CN1806099A (https=) |
| GB (1) | GB0314245D0 (https=) |
| MX (1) | MXPA05013254A (https=) |
| WO (1) | WO2004113693A1 (https=) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140353064A1 (en) * | 2013-06-03 | 2014-12-04 | Caterpillar Inc. | Modular exhaust system |
| CN112221301A (zh) * | 2020-09-30 | 2021-01-15 | 武汉钢铁有限公司 | 活性炭烟气净化系统及其方法 |
| EP4080036A1 (en) * | 2021-04-21 | 2022-10-26 | Volvo Truck Corporation | Internal combustion engine system |
| US12590554B2 (en) | 2020-09-01 | 2026-03-31 | Mercedes-Benz Group AG | Catalytic converter for a motor vehicle, as well as a motor vehicle |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3699683A (en) * | 1971-04-05 | 1972-10-24 | Chemical Construction Corp | Engine exhaust emission control system |
| US5409784A (en) * | 1993-07-09 | 1995-04-25 | Massachusetts Institute Of Technology | Plasmatron-fuel cell system for generating electricity |
| US5910097A (en) * | 1996-07-17 | 1999-06-08 | Daimler-Benz Aktiengesellschaft | Internal combustion engine exhaust emission control system with adsorbers for nitrogen oxides |
| US6082100A (en) * | 1997-10-29 | 2000-07-04 | Daimlerchrysler Ag | Method for operating a multicylinder internal combustion engine |
| US6170259B1 (en) * | 1997-10-29 | 2001-01-09 | Daimlerchrysler Ag | Emission control system for an internal-combustion engine |
| US6560958B1 (en) * | 1998-10-29 | 2003-05-13 | Massachusetts Institute Of Technology | Emission abatement system |
| US20040237506A1 (en) * | 2001-08-27 | 2004-12-02 | Osamu Yamada | Method of controlling operation of internal combustion engine |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4902487A (en) | 1988-05-13 | 1990-02-20 | Johnson Matthey, Inc. | Treatment of diesel exhaust gases |
| WO2000021647A1 (en) * | 1998-10-12 | 2000-04-20 | Johnson Matthey Public Limited Company | Process and apparatus for treating combustion exhaust gas |
-
2003
- 2003-06-18 GB GBGB0314245.2A patent/GB0314245D0/en not_active Ceased
-
2004
- 2004-06-18 CN CNA2004800164985A patent/CN1806099A/zh active Pending
- 2004-06-18 US US10/561,093 patent/US20060213189A1/en not_active Abandoned
- 2004-06-18 MX MXPA05013254A patent/MXPA05013254A/es not_active Application Discontinuation
- 2004-06-18 KR KR1020057024346A patent/KR20060038947A/ko not_active Withdrawn
- 2004-06-18 WO PCT/GB2004/002612 patent/WO2004113693A1/en not_active Ceased
- 2004-06-18 EP EP04742967A patent/EP1633961A1/en not_active Withdrawn
- 2004-06-18 JP JP2006516438A patent/JP2006527814A/ja not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3699683A (en) * | 1971-04-05 | 1972-10-24 | Chemical Construction Corp | Engine exhaust emission control system |
| US5409784A (en) * | 1993-07-09 | 1995-04-25 | Massachusetts Institute Of Technology | Plasmatron-fuel cell system for generating electricity |
| US5910097A (en) * | 1996-07-17 | 1999-06-08 | Daimler-Benz Aktiengesellschaft | Internal combustion engine exhaust emission control system with adsorbers for nitrogen oxides |
| US6082100A (en) * | 1997-10-29 | 2000-07-04 | Daimlerchrysler Ag | Method for operating a multicylinder internal combustion engine |
| US6170259B1 (en) * | 1997-10-29 | 2001-01-09 | Daimlerchrysler Ag | Emission control system for an internal-combustion engine |
| US6560958B1 (en) * | 1998-10-29 | 2003-05-13 | Massachusetts Institute Of Technology | Emission abatement system |
| US20040237506A1 (en) * | 2001-08-27 | 2004-12-02 | Osamu Yamada | Method of controlling operation of internal combustion engine |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140353064A1 (en) * | 2013-06-03 | 2014-12-04 | Caterpillar Inc. | Modular exhaust system |
| US9140155B2 (en) * | 2013-06-03 | 2015-09-22 | Caterpillar Inc. | Modular exhaust system |
| US12590554B2 (en) | 2020-09-01 | 2026-03-31 | Mercedes-Benz Group AG | Catalytic converter for a motor vehicle, as well as a motor vehicle |
| CN112221301A (zh) * | 2020-09-30 | 2021-01-15 | 武汉钢铁有限公司 | 活性炭烟气净化系统及其方法 |
| EP4080036A1 (en) * | 2021-04-21 | 2022-10-26 | Volvo Truck Corporation | Internal combustion engine system |
| EP4080035A1 (en) * | 2021-04-21 | 2022-10-26 | Volvo Truck Corporation | Internal combustion engine system |
| US11536227B2 (en) | 2021-04-21 | 2022-12-27 | Volvo Truck Corporation | Internal combustion engine system |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2004113693A1 (en) | 2004-12-29 |
| JP2006527814A (ja) | 2006-12-07 |
| MXPA05013254A (es) | 2006-03-09 |
| KR20060038947A (ko) | 2006-05-04 |
| GB0314245D0 (en) | 2003-07-23 |
| EP1633961A1 (en) | 2006-03-15 |
| CN1806099A (zh) | 2006-07-19 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: JOHNSON MATTHEY PUBLIC LIMITED CO., UNITED KINGDOM Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:ALLANSSON, EIVE TORD RONNY;ANDREASSON, ANDERS KLAS;LAVENIUS, MATS;REEL/FRAME:017908/0658;SIGNING DATES FROM 20051213 TO 20060119 |
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| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |