WO2006028070A1 - 排気浄化装置 - Google Patents
排気浄化装置 Download PDFInfo
- Publication number
- WO2006028070A1 WO2006028070A1 PCT/JP2005/016296 JP2005016296W WO2006028070A1 WO 2006028070 A1 WO2006028070 A1 WO 2006028070A1 JP 2005016296 W JP2005016296 W JP 2005016296W WO 2006028070 A1 WO2006028070 A1 WO 2006028070A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- particulate filter
- catalyst
- oxidation catalyst
- exhaust gas
- fuel
- Prior art date
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Classifications
-
- 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
- F01N3/033—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 in combination with other devices
- F01N3/035—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 in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/80—Chemical processes for the removal of the retained particles, e.g. by burning
- B01D46/84—Chemical processes for the removal of the retained particles, e.g. by burning by heating only
-
- 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
- B01D53/944—Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
-
- 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
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
- B01D53/9454—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific device
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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 ; 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
-
- 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
- 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
- F01N3/022—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 characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous
-
- 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
- F01N3/022—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 characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous
- F01N3/0222—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 characterised by specially adapted filtering structure, e.g. honeycomb, mesh or fibrous the structure being monolithic, e.g. honeycombs
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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
- F01N3/02—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
- F01N3/025—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 fuel burner or by adding fuel to exhaust
- F01N3/0253—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 fuel burner or by adding fuel to exhaust adding fuel to exhaust gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/01—Engine exhaust gases
- B01D2258/012—Diesel engines and lean burn gasoline engines
-
- 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
- B01D53/9459—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts
- B01D53/9477—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts with catalysts positioned on separate bricks, e.g. exhaust 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
- F01N2250/00—Combinations of different methods of purification
- F01N2250/02—Combinations of different methods of purification filtering and catalytic conversion
-
- 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
- F01N2330/06—Ceramic, e.g. monoliths
-
- 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
- F01N2610/03—Adding substances to exhaust gases the substance being hydrocarbons, e.g. engine fuel
-
- 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
- F01N3/2825—Ceramics
- F01N3/2828—Ceramic multi-channel monoliths, e.g. honeycombs
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Definitions
- the present invention relates to an exhaust purification device.
- Particulate matter (particulate matter) discharged from diesel engines is mainly composed of soot made of carbonaceous matter and SOF content (Soluble Organic Fraction: soluble organic component) that has high boiling point hydrocarbon component power.
- SOF content Soluble Organic Fraction: soluble organic component
- a force that has a composition containing a trace amount of sulfate (mist-like sulfuric acid component) As a measure to reduce this kind of particulates, exhaust gas 2 from diesel engine 1 as shown in Fig. 1 circulates Conventionally, a particulate filter 4 is provided in the middle of the exhaust pipe 3.
- this particulate filter 4 mainly comprises a filter body 7 having a porous hard cam structure made of a ceramic such as cordierite.
- the inlet side of each flow path 5 partitioned in a shape is alternately sealed by the plug body 8, and the flow path 5 whose inlet side is not sealed is sealed by the plug body 9.
- only the exhaust gas 2 that has permeated through the porous thin wall 6 partitioning each flow path 5 is discharged downstream, and particulates are collected on the inner surface of the porous thin wall 6. .
- an acid catalyst 10 carried on a ceramic carrier such as cordierite having a flow-through type Hercam structure is separately arranged in the preceding stage of the particulate filter 4, It is considered that the particulate filter 4 is forcibly regenerated by adding fuel to the exhaust gas 2 upstream of the acid catalyst 10 when the amount of accumulated particulate has increased.
- the fuel (HC) added upstream from the particulate filter 4 undergoes an oxidation reaction while passing through each cell 11 (see FIG. 3) of the oxidation catalyst 10 in the preceding stage, and is increased by the reaction heat.
- the inflow of the warm exhaust gas 2 raises the catalyst bed temperature of the particulate filter 4 immediately after that, the particulates are burned out, and the particulate filter 4 is regenerated.
- post-injection is performed at a non-ignition timing that is later than the compression top dead center following the main injection of fuel performed near the compression top dead center. It is common to add fuel to the exhaust gas by doing this, but it is also possible to add fuel to the exhaust gas 2 by delaying the timing of main injection into the cylinder from normal. In this way, by controlling the fuel injection into the cylinder and leaving a large amount of unburned fuel in the exhaust gas 2, the fuel pipe 3 is simply placed at an appropriate position of the exhaust pipe 3 (even in the exhaust mold). It is also possible to insert an injector as a fuel addition means, and add fuel directly into the exhaust gas 2 by this injector.
- Patent Document 1 As prior art document information related to the forced regeneration of such a particulate filter, there is the following Patent Document 1 by the same applicant as the present invention.
- Patent Document 1 Japanese Patent Application Laid-Open No. 2003-193824
- the vehicle When the particulate filter 4 is forcibly regenerated with this type of fuel filler, the vehicle is operated in such a way that it travels in a congested road, such as a city bus. In this case, it is assumed that the light load operation with a low exhaust temperature will continue continuously, but the fuel addition is performed under the conditions just below the catalyst activation lower limit temperature (about 190 ° C) of the oxidation catalyst 10 in the previous stage. As a result, the mist of the added fuel that cannot be treated is collected on the front end surface of the oxidation catalyst, which is not very high in catalyst activity, and the front end surface of the acid catalyst becomes sticky and wet. There was a risk that the mixture of the particulates deposited here and the mist of the added fuel would become agglomerated after incomplete combustion and clog the front end face of the oxidation catalyst 10.
- the present invention has been made in view of the above circumstances, and an exhaust gas purification system capable of preventing clogging of an acid catalyst provided in the front stage of a catalyst regeneration type particulate filter.
- an exhaust gas purification system capable of preventing clogging of an acid catalyst provided in the front stage of a catalyst regeneration type particulate filter.
- the present invention adds a fuel to the exhaust gas upstream of a catalyst regeneration type particulate filter provided with a flow-through type oxidation catalyst in the preceding stage and provided in the middle of the exhaust pipe.
- Exhaust gas purification device for forcibly regenerating the particulate filter by burning the collected particulate matter in the downstream particulate filter by the heat of reaction when the added fuel undergoes the acidic reaction on the upstream acidic catalyst.
- this is characterized in that the preceding oxidation catalyst is supported on a metal carrier.
- the preceding stage oxidation catalyst is supported on the metal carrier in this way, it is supported on the ceramic carrier as in the prior art, and compared with the case where each of the cells constituting the exhaust gas flow path is used. Since the wall thickness is reduced and the wall surface becomes smooth, the area of the front end of each cell occupying the front end surface of the oxidation catalyst is reduced, and the area where particulates easily adhere is greatly reduced. Particulates are also difficult to adhere to the walls of each cell.
- the present invention adds a fuel into the exhaust gas upstream of a catalyst regeneration type particulate filter provided with a flow-through type oxidation catalyst in the previous stage and provided in the middle of the exhaust pipe.
- a catalyst regeneration type particulate filter provided with a flow-through type oxidation catalyst in the previous stage and provided in the middle of the exhaust pipe.
- an exhaust purification system that forcibly regenerates the particulate filter by burning the collected particulate matter in the downstream particulate filter by the heat of reaction when the added fuel undergoes an acidic reaction on the upstream acidic catalyst.
- the front stage oxidation catalyst is divided into front and rear parts, the divided front oxidation catalyst is supported on a metal carrier, and the divided rear oxidation catalyst is supported on a ceramic carrier. It is also a thing.
- the oxidation catalyst is divided into front and rear parts in this way, and the divided front oxidation catalyst is supported on the metal carrier, and the divided rear oxidation catalyst is supported on the ceramic support.
- the wall thickness of each cell constituting the exhaust gas flow path becomes thinner and the wall surface becomes smoother than in the case where it is supported on a ceramic carrier as in the prior art.
- the area of the front wall of each cell occupying the front surface of the acid catalyst decreases, and the area where particulates tend to adhere is greatly reduced. Curate becomes difficult to adhere.
- the mist component of the added fuel is received by the front acid catalyst and gasified and does not reach the force.
- the catalyst bed temperature is raised by the exhaust gas that has passed through the front of the acid catalyst and the temperature is increased, so that the oxidation reaction of the added fuel (HC) is effectively performed.
- the temperature of the exhaust gas is raised efficiently.
- the front-stage oxidation catalyst is divided into front and rear parts, and the divided front acid catalyst is supported on the metal carrier, and the divided rear acid catalyst is supported on the ceramic carrier.
- FIG. 1 is a schematic diagram showing a conventional example.
- FIG. 2 is a cross-sectional view showing details of the particulate filter in FIG.
- FIG. 3 is a perspective view showing the details of the acid catalyst shown in FIG. 1 with a part cut away.
- FIG. 4 is a cross-sectional view showing an embodiment of the present invention.
- FIG. 5 is a cross-sectional view showing another embodiment of the present invention.
- FIG. 4 shows an embodiment of the present invention.
- the exhaust gas purification apparatus of this embodiment is supported on a ceramic carrier having a conventional hard cam structure.
- the flow-through type acid catalyst 12 supported on a metal carrier with a hard cam structure is placed in front of the catalyst regeneration type particulate filter 4 instead of the flow-through type acid catalyst 10
- a metal with high heat resistance and corrosion resistance such as stainless steel, is used.
- the wall thickness when supported on a ceramic carrier such as cordierite, the wall thickness is about 150 to 200 ⁇ m, and the wall surface is also a rough surface with fine irregularities.
- the wall thickness can be reduced to about 30-: LOO ⁇ m, and the wall surface becomes a smooth surface with very few irregularities.
- the clogging of the acid catalyst 12 provided in the preceding stage of the particulate filter 4 is clogged. It is possible to reliably prevent clogging, and it is possible to realize the forced regeneration of the particulate filter 4 without any trouble, as long as the minimum catalyst activity temperature of the acid catalyst 12 (about 190 ° C.).
- FIG. 5 shows another embodiment of the present invention.
- the oxidation catalyst arranged in the front stage of the particulate filter 4 is divided into front and rear portions.
- the divided acid length catalyst 12 with the short trunk length is supported on the metal carrier, and the divided long length and rear acid catalyst 14 is supported on the ceramic carrier.
- Ru In FIG. 5, reference numeral 15 denotes each cell constituting the flow path of the exhaust gas 2 in the rear catalyst 14.
- the oxidation catalyst is divided into front and rear parts in this way, and the divided front oxidation catalyst 12 is supported on the metal support, and the divided rear oxidation catalyst 14 is used as the ceramic support.
- the wall thickness of each cell 13 forming the flow path of the exhaust gas 2 is reduced in comparison with the case where the catalyst is first supported on the front catalyst 12 at the front portion, and Since the wall surface becomes smooth, the area where the cell front end of each cell 13 occupies in the front end surface of the acid catalyst 12 is reduced, and the area where the particulates easily adhere is greatly reduced. Particulates are also difficult to adhere to the wall surface in the cell 13.
- the mist component of the added fuel is received by the front acid catalyst 12 and gasified and does not reach the force. No clogging due to the accumulation of curate occurs, and the force of the catalyst increases the catalyst bed temperature by the exhaust gas 2 that has passed through the front of the acid catalyst 12 and effectively oxidizes the added fuel (HC). As the reaction proceeds, the temperature of the exhaust gas 2 is efficiently raised by the reaction heat.
- the rear acid catalyst 14 supported on the ceramic carrier having low thermal conductivity has high thermal conductivity and less heat escape than the metal carrier. Since it has the advantage of raising the temperature of exhaust gas 2 in a short time, it is supported on a metal carrier. It is possible to raise the temperature of the exhaust gas 2 at an earlier time than when only the oxidized catalyst 12 is placed in front of the particulate filter 4 alone.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Exhaust Gas After Treatment (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US11/661,428 US20080184698A1 (en) | 2004-09-07 | 2005-09-06 | Exhaust Emission Control Device |
EP05778256A EP1795720A4 (en) | 2004-09-07 | 2005-09-06 | DEVICE FOR CLEANING EXHAUST GAS |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2004259713A JP2006077591A (ja) | 2004-09-07 | 2004-09-07 | 排気浄化装置 |
JP2004-259713 | 2004-09-07 |
Publications (1)
Publication Number | Publication Date |
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WO2006028070A1 true WO2006028070A1 (ja) | 2006-03-16 |
Family
ID=36036351
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2005/016296 WO2006028070A1 (ja) | 2004-09-07 | 2005-09-06 | 排気浄化装置 |
Country Status (4)
Country | Link |
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US (1) | US20080184698A1 (ja) |
EP (1) | EP1795720A4 (ja) |
JP (1) | JP2006077591A (ja) |
WO (1) | WO2006028070A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2002879A2 (en) * | 2006-03-29 | 2008-12-17 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control catalyst and exhaust emission control system |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4671048B2 (ja) * | 2006-11-17 | 2011-04-13 | 三菱自動車工業株式会社 | 排気浄化装置 |
DE102007008954B4 (de) * | 2007-02-21 | 2009-12-17 | Umicore Ag & Co. Kg | Katalysatorsystem und seine Verwendung |
JP2009057922A (ja) * | 2007-08-31 | 2009-03-19 | Honda Motor Co Ltd | 排ガス浄化装置 |
JP5277891B2 (ja) * | 2008-11-17 | 2013-08-28 | 三菱自動車工業株式会社 | 排気浄化装置 |
JP5381661B2 (ja) * | 2009-12-01 | 2014-01-08 | トヨタ自動車株式会社 | 排気浄化装置 |
US9528413B2 (en) * | 2010-07-30 | 2016-12-27 | Ford Global Technologies, Llc | Synergistic SCR/DOC configurations for lowering diesel emissions |
JP6237539B2 (ja) * | 2014-08-27 | 2017-11-29 | トヨタ自動車株式会社 | 内燃機関の排気浄化装置 |
US10598455B2 (en) | 2015-09-29 | 2020-03-24 | Plate Llc | Magazine ammunition loader |
US9689633B1 (en) | 2015-12-22 | 2017-06-27 | Christopher Andrew Plate | Magazine loader |
JP7024392B2 (ja) * | 2017-12-25 | 2022-02-24 | いすゞ自動車株式会社 | 排気後処理装置 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH01299645A (ja) * | 1988-05-27 | 1989-12-04 | Nippon Steel Corp | 自動車排気ガス浄化触媒用金属担体の製造方法 |
JPH1193639A (ja) * | 1997-09-25 | 1999-04-06 | Nippon Soken Inc | ディーゼル排気微粒子浄化装置 |
JP2004162611A (ja) * | 2002-11-13 | 2004-06-10 | Mitsubishi Fuso Truck & Bus Corp | 内燃機関の排気浄化装置 |
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US4902487A (en) * | 1988-05-13 | 1990-02-20 | Johnson Matthey, Inc. | Treatment of diesel exhaust gases |
JP3899534B2 (ja) * | 1995-08-14 | 2007-03-28 | トヨタ自動車株式会社 | ディーゼル機関の排気浄化方法 |
JPH09155203A (ja) * | 1995-12-12 | 1997-06-17 | Nippon Steel Corp | 排ガス浄化用複合担体 |
JPH09222009A (ja) * | 1996-02-15 | 1997-08-26 | Nippon Soken Inc | 内燃機関の排気微粒子浄化装置 |
GB9621215D0 (en) * | 1996-10-11 | 1996-11-27 | Johnson Matthey Plc | Emission control |
JP3954760B2 (ja) * | 1999-07-26 | 2007-08-08 | 日野自動車株式会社 | 排気浄化装置 |
JP3900421B2 (ja) * | 2001-11-09 | 2007-04-04 | トヨタ自動車株式会社 | ウォールフロー型ディーゼル排ガス浄化用フィルタ型触媒およびディーゼル排ガス浄化用装置 |
US6912847B2 (en) * | 2001-12-21 | 2005-07-05 | Engelhard Corporation | Diesel engine system comprising a soot filter and low temperature NOx trap |
US6832473B2 (en) * | 2002-11-21 | 2004-12-21 | Delphi Technologies, Inc. | Method and system for regenerating NOx adsorbers and/or particulate filters |
JP2005083346A (ja) * | 2003-09-11 | 2005-03-31 | Hino Motors Ltd | 排気浄化装置 |
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2004
- 2004-09-07 JP JP2004259713A patent/JP2006077591A/ja active Pending
-
2005
- 2005-09-06 WO PCT/JP2005/016296 patent/WO2006028070A1/ja active Application Filing
- 2005-09-06 US US11/661,428 patent/US20080184698A1/en not_active Abandoned
- 2005-09-06 EP EP05778256A patent/EP1795720A4/en not_active Withdrawn
Patent Citations (3)
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JPH01299645A (ja) * | 1988-05-27 | 1989-12-04 | Nippon Steel Corp | 自動車排気ガス浄化触媒用金属担体の製造方法 |
JPH1193639A (ja) * | 1997-09-25 | 1999-04-06 | Nippon Soken Inc | ディーゼル排気微粒子浄化装置 |
JP2004162611A (ja) * | 2002-11-13 | 2004-06-10 | Mitsubishi Fuso Truck & Bus Corp | 内燃機関の排気浄化装置 |
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Cited By (2)
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EP2002879A2 (en) * | 2006-03-29 | 2008-12-17 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control catalyst and exhaust emission control system |
EP2002879A4 (en) * | 2006-03-29 | 2010-07-14 | Toyota Motor Co Ltd | EXHAUST EMISSION CONTROL CATALYST AND EXHAUST EMISSION CONTROL SYSTEM |
Also Published As
Publication number | Publication date |
---|---|
US20080184698A1 (en) | 2008-08-07 |
EP1795720A1 (en) | 2007-06-13 |
JP2006077591A (ja) | 2006-03-23 |
EP1795720A4 (en) | 2010-01-20 |
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