EP1669563B1 - Exhaust gas purifying device - Google Patents
Exhaust gas purifying device Download PDFInfo
- Publication number
- EP1669563B1 EP1669563B1 EP04787865A EP04787865A EP1669563B1 EP 1669563 B1 EP1669563 B1 EP 1669563B1 EP 04787865 A EP04787865 A EP 04787865A EP 04787865 A EP04787865 A EP 04787865A EP 1669563 B1 EP1669563 B1 EP 1669563B1
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- EP
- European Patent Office
- Prior art keywords
- filter
- filter body
- plasma
- exhaust gas
- particulates
- 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.)
- Expired - Lifetime
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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
- F01N3/103—Oxidation catalysts for HC and CO only
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/025—Combinations of electrostatic separators, e.g. in parallel or in series, stacked separators or dry-wet separator combinations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/06—Plant or installations having external electricity supply dry type characterised by presence of stationary tube electrodes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
- B03C3/155—Filtration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/41—Ionising-electrodes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/49—Collecting-electrodes tubular
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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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- 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
- F01N13/011—Exhaust or silencing apparatus characterised by constructional features having two or more purifying devices arranged in parallel
- F01N13/017—Exhaust or silencing apparatus characterised by constructional features having two or more purifying devices arranged in parallel the purifying devices are arranged in a single housing
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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
- F01N3/027—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 electric or magnetic heating means
- F01N3/0275—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 electric or magnetic heating means using electric discharge means
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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
- F01N3/033—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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/12—Cleaning the device by burning the trapped particles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/30—Details of magnetic or electrostatic separation for use in or with vehicles
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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
- F01N2240/00—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
- F01N2240/28—Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a plasma reactor
Definitions
- the present invention relates to an exhaust emission control device for removing particulates in exhaust gas from an internal combustion engine such as diesel engine.
- Particulates or particulate matter discharged from a diesel engine is mainly constituted by carbonic soot and a soluble organic fraction (SOF) of high-boiling hydrocarbon and contains a trace of sulfate (misty sulfuric acid fraction).
- SOF soluble organic fraction
- a particulate filter 4 is incorporated in an exhaust pipe 3 through which exhaust gas 2 from a diesel engine 1 flows.
- the particulate filter 4 comprises a filter body 7 in the form of a porous honeycomb made of ceramics such as cordierite.
- the filter body 7 has passages 5 or grid-like compartments with inlets alternately plugged by plugs 8, the passages 5 with the unplugged inlets being plugged by the plugs 8 at their outlets; only the exhaust gas 2 passing through porous thin walls 6, which compartmentalize the passages 5, is discharged downstream and the walls 6 capture the particulates at their inner surfaces.
- the particulates in the exhaust gas 2 are thus captured by and accumulated on the inner surfaces of the walls 6 and spontaneously ignite to be burned off upon shifting to a region of operation with increased exhaust temperature.
- an operation or driving with temperature at or above a predetermined temperature requisite tends not to continue for a long time, for example, in a vehicle such as a shuttle-bus running mainly on congested city roads, there may be a fear that an accumulated particulate amount exceeds a treated amount, disadvantageously resulting in clogging of the particulate filter 4.
- the invention was made in view of the above and has its object to provide a plasma assisted exhaust emission control device with less electric power consumption and with no harmful gas discharged into atmosphere.
- the invention is directed to an exhaust emission control device comprising a filter body constituted by porous members through which exhaust gas passes for capture of particulates entrained in the exhaust gas and electrodes for generating plasma in said filter body, thereby providing a plasma regenerative particulate filter, said particulate filter being incorporated in a filter casing within an exhaust pipe, oxidation catalysts being arranged upstream and downstream of and adjacent to the particulate filter in the filter casing so as to obtain heat insulation effect to the particulate filter.
- the plasma regenerative particulate filter is sandwiched and heat insulated by the upstream and downstream oxidation catalysts in one and the same filter casing, so that the filter body is rapidly elevated in temperature when the oxidization reaction of the captured particulates begins.
- the particulates have tendency of being more readily burned off and can be burned off with a shorter electric discharge time than they could conventionally and thus required electric power consumption is less than that required conventionally.
- the harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of the plasma is oxidized into harmless CO 2 or H 2 O when it passes through the downstream oxidation catalyst and is discharged.
- the plasma regenerative particulate filter is divided into a plurality of smaller units which are arranged in parallel with each other in the filter casing, voltage for electric discharge being separately applied to the respective smaller units.
- the smaller units of the plasma regenerative particulate filter can be separately regenerated, with an advantageous result that power source with relatively small capacity will suffice. Division into the smaller units improves combustibility of the particulates per unit, so that regeneration of the filter through plasma can be attained during stoppage of an engine for example in a vehicle with an idle stopper.
- the porous members constituting the filter body integrally carry oxidation catalysts, which accelerates the oxidation reaction of the particulates captured by the filter body to lower ignition temperature.
- combustibility of the particulates in a condition of operation with lower exhaust temperature is further enhanced to attain further satisfactory burn-off of the particulates.
- a filter body having a plurality of passages in the form of honeycomb through which exhaust gas passes, inlet and outlet ends of the passages being alternately plugged.
- the filter body may have a rod-like electrode inserted at its axis and a cylindrical electrode fitted over an outer periphery of the filter body.
- the harmful gas such as highly concentrated CO or HC generated due to combustion of the particulate with relatively low temperature by the aid of plasma can be oxidized into harmless CO 2 or H 2 O when it passes through the downstream oxidation catalyst and is discharged. Thus, the harmful gas is prevented from remaining in the exhaust gas finally discharged into the atmosphere.
- (III) NO occupying majority of NO x in the exhaust gas can be converted into highly reactive NO 2 when the exhaust gas passed through the upstream oxidation catalyst, which can substantially accelerate the oxidation reaction of the particulates under a condition of operation with relatively high exhaust temperature. This promotes spontaneous combustion of the particulates by no aid of plasma to obtain sufficient burn-off.
- FIGS. 3 and 4 show an embodiment of the invention in which parts similar to those in Figs. 1 and 2 are represented by the same reference numerals.
- a plasma regenerative particulate filter 11 comprising a filter body 7 similar to that shown in Fig. 2 above and rod-like and cylindrical electrodes 9 and 10 so as to generate plasma in the filter body 7.
- the filter body 7 in each of the smaller units 11A, 11B, 11C and 11D has the rod-like electrode 9 inserted into an axis of the filter body 7 and the cylindrical electrode 10 fitted over the outer periphery of the filter body 7.
- the rod-like electrodes 9 of the smaller units 11A, 11B,11C and 11D are connected to an anode of a power source or buttery 14 through change-over relays 13a, 13b, 13c and 13d, respectively.
- the cylindrical electrodes 10 of the smaller units 11A, 11B,11C and 11 D are connected to a cathode of the power source 14 through an electrically conductive support member 15 and the filter casing 12 so that voltage for electric discharge may be separately applied to the respective smaller units 11A, 11B, 11C and 11D.
- the support member 15 serves for support of the smaller units 11A, 11B, 11C and 11D of the particulate filter 11 in the filter casing 12 and also serves as partition or filler for gap between the smaller units 11A,11B,11C and 11D.
- the above-mentioned particulate filter 11 divided into the plural smaller units 11A, 11B,11C and 11D is accommodated in the filter casing 12 within the exhaust pipe 3.
- oxidation catalysts 16 and 17, respectively are arranged upstream and downstream of and adjacent to the particulate filter 11 in the filter casing 12 so as to obtain heat insulation effect to the particulate filter 11.
- Each of the upstream and downstream oxidation catalysts 16 and 17 is of flow-through type and comprises a carrier with a honeycomb structure made of ceramics such as cordierite, said carrier carrying an appropriate amount of platinum.
- the upstream catalyst 17 may have its capacity and platinum-carrying amount less than those of the downstream catalyst 16.
- porous members constituting the filter body 7 of each of the above-mentioned smaller units 11A,11B,11C and 11D may carry oxidation catalysts so as to promote the oxidation reaction of the particulates captured by the filter body 7.
- the inner gas of the filter body 7 is excited to convert oxygen into ozone and NO into NO 2 .
- These excited exhaust gas components are being activated so that oxidization reaction of the particulates captured by the filter body 7 is accelerated by the excited exhaust gas components, whereby the particulates are satisfactorily burned off even in a condition of operation with lower exhaust temperature.
- the plasma regenerative particulate filter 11 is sandwiched and heat insulated by the upstream and downstream oxidation catalysts 16 and 17 in one and the same filter casing 12, so that when the oxidation reaction of the captured particulates begins, the filter body 7 is rapidly elevated in temperature.
- the particulates have tendency of being more readily burned off and can be burned off with a shorter electric discharge time than they could conventionally and thus required electric power consumption is less than that required conventionally.
- the harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of plasma is oxidized into harmless CO 2 or H 2 O when it passes through the downstream oxidation catalyst 17 and is discharged.
- the particulates captured by the filter body 7 can be efficiently burned off by the aid of plasma; the filter body 7 can be rapidly elevated in temperature due to heat insulation effect by the upstream and downstream oxidation catalysts 16 and 17 into environment for ready burn-off the particulates, so that the particulates can be burned off with a shorter electric discharge time than they could conventionally, whereby electric power consumption can be substantially reduced.
- the harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of plasma is oxidized into harmless CO 2 or H 2 O when it passes through the downstream oxidation catalyst 17 and is discharged. As a result, the harmful gas is prevented from remaining in the exhaust gas 2 finally discharged into the atmosphere.
- NO occupying majority of NO x in the exhaust gas 2 can be converted into highly reactive NO 2 when the exhaust gas passes through the upstream oxidation catalyst 16, which substantially accelerates the oxidation reaction of the particulates under a condition of operation with relatively high exhaust temperature, whereby spontaneous combustion of the particulates is promoted by no aid of plasma, thereby providing satisfactory burn-off of the particulates.
- the particulate filter 11 when the particulate filter 11 is divided into the plural smaller units 11A, 11B, 11C and 11D which are arranged in parallel with each other within the filter casing 12, voltage for electric discharge being separately applicable to the respective smaller units 11A, 11B, 11C and 11D, even the power source 14 with relatively small capacity will suffice; regeneration of the filter through plasma can be attained during stoppage of an engine, for example, in a vehicle with an idle stopper.
- the oxidation reaction of the particulates captured by the filter body 7 can be accelerated by the oxidation catalysts, so that further reliable burn-off of the particulates can be attained in a region of operation with lower exhaust temperature.
- an exhaust emission control device of the invention is not limited to the above-mentioned embodiment and that various changed and modifications may be made.
- the plasma regenerative particulate filter may be constituted by a single unit.
- the filter body may or may not carry oxidation catalysts. Shapes and arrangement of the filter body and electrodes are not limited to those shown.
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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)
- Materials Engineering (AREA)
- Toxicology (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Exhaust Gas After Treatment (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
- The present invention relates to an exhaust emission control device for removing particulates in exhaust gas from an internal combustion engine such as diesel engine.
- Particulates or particulate matter discharged from a diesel engine is mainly constituted by carbonic soot and a soluble organic fraction (SOF) of high-boiling hydrocarbon and contains a trace of sulfate (misty sulfuric acid fraction). In order to suppress such kind of particulates from being discharged into atmosphere, it has been envisaged as shown in
Fig. 1 that aparticulate filter 4 is incorporated in anexhaust pipe 3 through whichexhaust gas 2 from a diesel engine 1 flows. - As detailedly shown in
Fig. 2 , theparticulate filter 4 comprises afilter body 7 in the form of a porous honeycomb made of ceramics such as cordierite. Thefilter body 7 haspassages 5 or grid-like compartments with inlets alternately plugged byplugs 8, thepassages 5 with the unplugged inlets being plugged by theplugs 8 at their outlets; only theexhaust gas 2 passing through porousthin walls 6, which compartmentalize thepassages 5, is discharged downstream and thewalls 6 capture the particulates at their inner surfaces. - The particulates in the
exhaust gas 2 are thus captured by and accumulated on the inner surfaces of thewalls 6 and spontaneously ignite to be burned off upon shifting to a region of operation with increased exhaust temperature. However, when an operation or driving with temperature at or above a predetermined temperature requisite tends not to continue for a long time, for example, in a vehicle such as a shuttle-bus running mainly on congested city roads, there may be a fear that an accumulated particulate amount exceeds a treated amount, disadvantageously resulting in clogging of theparticulate filter 4. - Thus, development of a plasma assisted exhaust emission control device has been promoted so as to satisfactorily burn off the particulates even in a region of operation with lower exhaust temperature. In the kind of plasma assisted exhaust emission control device, electric discharge to the
exhaust gas 2 to thereby generate plasma excites theexhaust gas 2 to convert oxygen into ozone and NO into NO2. Because of these excited exhaust gas components being activated, the particulates can be satisfactorily burned off even in a region of operation with lower exhaust temperature. - Prior publications on plasma assisted exhaust emission control devices are recited in, for example, the following Reference 1. [Reference]
WO 99/38603 A1
describes an exhaust emission control device according to the preamble of claim 1.JP 2002 276333 A - However, in such conventional plasma assisted exhaust emission control devices, much electric power consumption is required for regeneration of the
particulate filter 4 so that power source is needed which has larger capacity to an extent that cannot be afforded by any existing vehicle buttery. Moreover, charging is required which matches the consumed electric power, resulting in deterioration of fuel mileage. - Since the particulates are burned off at relatively low temperature upon regeneration of the
particulate filter 4, there may be also a fear that harmful gas such as highly concentrated CO or HC is generated and discharged into atmosphere. - The invention was made in view of the above and has its object to provide a plasma assisted exhaust emission control device with less electric power consumption and with no harmful gas discharged into atmosphere.
- The invention is directed to an exhaust emission control device comprising a filter body constituted by porous members through which exhaust gas passes for capture of particulates entrained in the exhaust gas and electrodes for generating plasma in said filter body, thereby providing a plasma regenerative particulate filter, said particulate filter being incorporated in a filter casing within an exhaust pipe, oxidation catalysts being arranged upstream and downstream of and adjacent to the particulate filter in the filter casing so as to obtain heat insulation effect to the particulate filter.
- Thus, when the exhaust gas having flown into the filter casing passes through the upstream oxidation catalyst, NO occupying majority of NOx in the exhaust gas is converted into highly reactive NO2, which substantially accelerates an oxidization reaction of the particulates to bring about satisfactory burn-off of the particulates in a condition of operation with exhaust temperature over about 250°C.
- However, when a condition of light-load operation with exhaust temperature greatly falling below 250°C continues for a long time, for example, during running or driving on congested city roads, satisfactory burn-off of the particulates cannot be expected; then, at a right moment when an accumulated particulate amount is estimated to exceed a predetermined amount (estimation may be based on, for example, pressure difference between the entering and discharge sides of the filter body or operational time period), voltage is applied across the electrodes of the filter body to discharge electricity in the filter body.
- When voltage is thus applied across the electrodes of the filter body to discharge electricity in the filter body, inner gas is excited to convert oxygen into ozone and NO into NO2, these excited gas components which are being activated accelerate the oxidation reaction of the particulates captured by the filter body. As a result, the particulates are satisfactorily burned off even in a condition of operation with lower exhaust temperature.
- The plasma regenerative particulate filter is sandwiched and heat insulated by the upstream and downstream oxidation catalysts in one and the same filter casing, so that the filter body is rapidly elevated in temperature when the oxidization reaction of the captured particulates begins. As a result, the particulates have tendency of being more readily burned off and can be burned off with a shorter electric discharge time than they could conventionally and thus required electric power consumption is less than that required conventionally.
- The harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of the plasma is oxidized into harmless CO2 or H2O when it passes through the downstream oxidation catalyst and is discharged.
- It is preferable in the invention that the plasma regenerative particulate filter is divided into a plurality of smaller units which are arranged in parallel with each other in the filter casing, voltage for electric discharge being separately applied to the respective smaller units.
- Thus, the smaller units of the plasma regenerative particulate filter can be separately regenerated, with an advantageous result that power source with relatively small capacity will suffice. Division into the smaller units improves combustibility of the particulates per unit, so that regeneration of the filter through plasma can be attained during stoppage of an engine for example in a vehicle with an idle stopper.
- In the invention, it is preferable that the porous members constituting the filter body integrally carry oxidation catalysts, which accelerates the oxidation reaction of the particulates captured by the filter body to lower ignition temperature. As a result, combustibility of the particulates in a condition of operation with lower exhaust temperature is further enhanced to attain further satisfactory burn-off of the particulates.
- Upon carrying out the invention more concretely, employable is a filter body having a plurality of passages in the form of honeycomb through which exhaust gas passes, inlet and outlet ends of the passages being alternately plugged. When such filter body is employed, the filter body may have a rod-like electrode inserted at its axis and a cylindrical electrode fitted over an outer periphery of the filter body.
- According to an exhaust emission control device of the invention, various meritorious effects can be obtained as follows.
- (I) Even in a condition of operation with lower exhaust temperature such as light-load operation, the particulates captured by the filter body can be effectively burned off by the aid of plasma. Moreover, due to the heat insulation effect by the upstream and downstream oxidation catalysts, the filter body can be rapidly elevated in temperature into environment for ready burn-off of the particulates, so that the particulates can be burned off with a shorter electric discharge time than they could conventionally, whereby electric power consumption can be substantially reduced.
- (II) The harmful gas such as highly concentrated CO or HC generated due to combustion of the particulate with relatively low temperature by the aid of plasma can be oxidized into harmless CO2 or H2O when it passes through the downstream oxidation catalyst and is discharged. Thus, the harmful gas is prevented from remaining in the exhaust gas finally discharged into the atmosphere.
- (III) NO occupying majority of NOx in the exhaust gas can be converted into highly reactive NO2 when the exhaust gas passed through the upstream oxidation catalyst, which can substantially accelerate the oxidation reaction of the particulates under a condition of operation with relatively high exhaust temperature. This promotes spontaneous combustion of the particulates by no aid of plasma to obtain sufficient burn-off.
- (IV) When the plasma regenerative particulate filter is divided into a plurality of smaller units which are arranged in parallel with each other in the filter casing, voltage for electric discharge being separately applied to the respective smaller units, even a power source with relatively small capacity will suffice. Regeneration of the filter through plasma can be also attained during stoppage of an engine for example in a vehicle with an idle stopper.
- (V) When employed are porous members constituting the filter body and integrally carrying oxidation catalysts, the oxidation reaction of the particulates captured by the filter body can be accelerated by the oxidation catalysts, so that the particulates can be further reliably burned off in a region of operation with lower exhaust temperature.
-
- [
Fig. 1 ] A schematic view showing arrangement of a conventional particulate filter. - [
Fig. 2 ] A sectional view showing particulars of the particulate filter shown inFig. 1 . - [
Fig. 3 ] A sectional view showing an embodiment of the invention. - [
Fig. 4 ] A sectional view looking in the direction of arrows II inFig. 3 . -
- 2 exhaust gas
- 3 exhaust pipe
- 4 particulate filter
- 5 passage
- 7 filter body
- 9 rod-like electrode (electrode)
- 10 cylindrical electrode (electrode)
- 11 plasma regenerative particulate filter
- 11A, 11B, 11C and 11D smaller unit
- 12 filter casing
- 16 upstream oxidation catalyst
- 17 downstream oxidation catalyst
- An embodiment of the invention will be described in conjunction with the drawings.
Figs. 3 and 4 show an embodiment of the invention in which parts similar to those inFigs. 1 and 2 are represented by the same reference numerals. - As shown in
Figs. 3 and 4 , used in an exhaust emission control device of the invention is a plasma regenerativeparticulate filter 11 comprising afilter body 7 similar to that shown inFig. 2 above and rod-like and 9 and 10 so as to generate plasma in thecylindrical electrodes filter body 7. Shown is an example of the plasma regenerativeparticulate filter 11 divided into a plurality of (four in the figure shown) 11A, 11B, 11C and 11D which are arranged in parallel with each other within thesmaller units filter casing 12. - The
filter body 7 in each of the 11A, 11B, 11C and 11D has the rod-smaller units like electrode 9 inserted into an axis of thefilter body 7 and thecylindrical electrode 10 fitted over the outer periphery of thefilter body 7. The rod-like electrodes 9 of the 11A, 11B,11C and 11D are connected to an anode of a power source or buttery 14 through change-oversmaller units 13a, 13b, 13c and 13d, respectively. Therelays cylindrical electrodes 10 of the 11A, 11B,11C and 11 D are connected to a cathode of thesmaller units power source 14 through an electricallyconductive support member 15 and thefilter casing 12 so that voltage for electric discharge may be separately applied to the respective 11A, 11B, 11C and 11D.smaller units - The
support member 15 serves for support of the 11A, 11B, 11C and 11D of thesmaller units particulate filter 11 in thefilter casing 12 and also serves as partition or filler for gap between the 11A,11B,11C and 11D.smaller units - The above-mentioned
particulate filter 11 divided into the plural 11A, 11B,11C and 11D is accommodated in thesmaller units filter casing 12 within theexhaust pipe 3. Arranged upstream and downstream of and adjacent to theparticulate filter 11 in thefilter casing 12 are 16 and 17, respectively, so as to obtain heat insulation effect to theoxidation catalysts particulate filter 11. - Each of the upstream and
16 and 17 is of flow-through type and comprises a carrier with a honeycomb structure made of ceramics such as cordierite, said carrier carrying an appropriate amount of platinum. Thedownstream oxidation catalysts upstream catalyst 17 may have its capacity and platinum-carrying amount less than those of thedownstream catalyst 16. - The porous members constituting the
filter body 7 of each of the above-mentioned 11A,11B,11C and 11D may carry oxidation catalysts so as to promote the oxidation reaction of the particulates captured by thesmaller units filter body 7. - In the exhaust emission control device thus constructed, when the
exhaust gas 2 having flown into the filter casing 12 passes through theupstream oxidation catalyst 16, NO occupying majority of NOx in theexhaust gas 2 is converted into highly reactive NO2, so that oxidation reaction of the particulates is substantially accelerated into satisfactory burn-off of the particulates under a condition of operation with exhaust temperature over about 250°C. - However, when a condition of light-load operation with exhaust temperature greatly falling below 250°C continues for a long time, for example, during running or driving on congested city roads, satisfactory burn-off of the particulates cannot be expected; for this reason, at a right moment when an accumulated particulate amount is estimated to exceed a predetermined amount (estimation may be based on, for example, pressure difference between the entering and discharge sides of the filter body or operational time period), voltage for electric discharge is applied separately to the
11A, 11B,11C and 11 D to discharge electricity across the respective rod-smaller units like electrodes 9 andcylindrical electrodes 10, thereby generating plasma in the inner gas of thefilter body 7. - Thus, the inner gas of the
filter body 7 is excited to convert oxygen into ozone and NO into NO2. These excited exhaust gas components are being activated so that oxidization reaction of the particulates captured by thefilter body 7 is accelerated by the excited exhaust gas components, whereby the particulates are satisfactorily burned off even in a condition of operation with lower exhaust temperature. - In this case, the plasma regenerative
particulate filter 11 is sandwiched and heat insulated by the upstream and 16 and 17 in one and thedownstream oxidation catalysts same filter casing 12, so that when the oxidation reaction of the captured particulates begins, thefilter body 7 is rapidly elevated in temperature. As a result, the particulates have tendency of being more readily burned off and can be burned off with a shorter electric discharge time than they could conventionally and thus required electric power consumption is less than that required conventionally. - Since voltage is applied across each of the
11A, 11B, 11C and 11D in thesmaller units particulate filter 11 so as to discharge electricity, thepower source 14 with relatively small capacity will suffice. Division into the 11A, 11B,11C and 11D improves combustibility of the particulates per unit, so that regeneration of the filter through plasma can be attained during stoppage of an engine for example in a vehicle with an idle stopper.smaller units - The harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of plasma is oxidized into harmless CO2 or H2O when it passes through the
downstream oxidation catalyst 17 and is discharged. - Thus, according to the above embodiment, even in a condition of operation with lower exhaust temperature such as light-load operation, the particulates captured by the
filter body 7 can be efficiently burned off by the aid of plasma; thefilter body 7 can be rapidly elevated in temperature due to heat insulation effect by the upstream and 16 and 17 into environment for ready burn-off the particulates, so that the particulates can be burned off with a shorter electric discharge time than they could conventionally, whereby electric power consumption can be substantially reduced.downstream oxidation catalysts - The harmful gas such as highly concentrated CO or HC generated due to combustion of the particulates with relatively low temperature by the aid of plasma is oxidized into harmless CO2 or H2O when it passes through the
downstream oxidation catalyst 17 and is discharged. As a result, the harmful gas is prevented from remaining in theexhaust gas 2 finally discharged into the atmosphere. - NO occupying majority of NOx in the
exhaust gas 2 can be converted into highly reactive NO2 when the exhaust gas passes through theupstream oxidation catalyst 16, which substantially accelerates the oxidation reaction of the particulates under a condition of operation with relatively high exhaust temperature, whereby spontaneous combustion of the particulates is promoted by no aid of plasma, thereby providing satisfactory burn-off of the particulates. - As especially shown in the embodiment, when the
particulate filter 11 is divided into the plural 11A, 11B, 11C and 11D which are arranged in parallel with each other within thesmaller units filter casing 12, voltage for electric discharge being separately applicable to the respective 11A, 11B, 11C and 11D, even thesmaller units power source 14 with relatively small capacity will suffice; regeneration of the filter through plasma can be attained during stoppage of an engine, for example, in a vehicle with an idle stopper. - In a case where employed are the porous members constituting the
filter body 7 and integrally carrying oxidation catalysts, the oxidation reaction of the particulates captured by thefilter body 7 can be accelerated by the oxidation catalysts, so that further reliable burn-off of the particulates can be attained in a region of operation with lower exhaust temperature. - It is to be understood that an exhaust emission control device of the invention is not limited to the above-mentioned embodiment and that various changed and modifications may be made. For example, the plasma regenerative particulate filter may be constituted by a single unit. The filter body may or may not carry oxidation catalysts. Shapes and arrangement of the filter body and electrodes are not limited to those shown.
Claims (6)
- An exhaust emission control device comprising a filter body (7) constituted by porous members through which exhaust gas (2) passes for capture of particulates entrained in the exhaust gas (2) and electrodes (9,10) for generating plasma in said filter body (7), thereby providing a plasma regenerative particulate filter (11), said particulate filter (11) being incorporated in a filter casing (12) within an exhaust pipe (3),
characterized in,
that oxidation catalysts (16,17) being arranged respectively upstream and downstream of and adjacent to the particulate filter (11) in the filter casing (12) so as to obtain heat insulation effect to the particulate filter (11), and
that the plasma regenerative particulate filter (11) is divided into a plurality of smaller units (11A, 11B,11C, 11D) which are arranged in parallel with each other within the filter casing (12), voltage for electric discharge being separately applicable to the respective smaller units (11A, 11B, 11C, 11 D). - The exhaust emission control device according to claim 1,
characterized in,
that the filter body (7) is constituted by porous members integrally carrying oxidation catalyst. - The exhaust emission control device according to claim 1,
characterized in,
that the filter body (7) is employed which comprises a number of passages in the form of honeycomb through which exhaust gas (2) passes, inlet and outlet ends of the respective passages being alternately plugged. - The exhaust emission control device according to claim 2, characterized in, that the filter body (7) is employed which comprises a number of passages in the form of honeycomb through which exhaust gas (2) passes, inlet and outlet ends of the respective passages being alternately plugged.
- The exhaust emission control device according to claim 3, characterized in, that the filter body (7) has a rod-like electrode (9) inserted at an axis of the filter body (7) and a cylindrical electrode (10) fitted over an outer periphery of the filter body (7).
- The exhaust emission control device according to claim 4, characterized in, that the filter body (7) has a rod-like electrode (9) inserted at an axis of the filter body (7) and a cylindrical electrode (10) fitted over an outer periphery of the filter body (7).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003319850A JP2005083346A (en) | 2003-09-11 | 2003-09-11 | Exhaust emission control device |
| PCT/JP2004/013225 WO2005026506A1 (en) | 2003-09-11 | 2004-09-10 | Exhaust gas-purifying device |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP1669563A1 EP1669563A1 (en) | 2006-06-14 |
| EP1669563A4 EP1669563A4 (en) | 2006-12-20 |
| EP1669563B1 true EP1669563B1 (en) | 2008-06-25 |
Family
ID=34308586
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP04787865A Expired - Lifetime EP1669563B1 (en) | 2003-09-11 | 2004-09-10 | Exhaust gas purifying device |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20070028603A1 (en) |
| EP (1) | EP1669563B1 (en) |
| JP (1) | JP2005083346A (en) |
| DE (1) | DE602004014627D1 (en) |
| WO (1) | WO2005026506A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011029730A1 (en) * | 2009-09-14 | 2011-03-17 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Device for treating exhaust gas containing soot particles |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4327506B2 (en) * | 2003-06-03 | 2009-09-09 | 日野自動車株式会社 | Exhaust purification equipment |
| JP2005344581A (en) * | 2004-06-02 | 2005-12-15 | Hino Motors Ltd | Particulate filter |
| JP2006077591A (en) * | 2004-09-07 | 2006-03-23 | Hino Motors Ltd | Exhaust emission control device |
| GB2429417B (en) * | 2005-08-25 | 2010-08-11 | Perkins Engines Co Ltd | Autoselective regenerating particulate filter |
| JP5288342B2 (en) * | 2005-10-05 | 2013-09-11 | ダイハツ工業株式会社 | Electrode for plasma reactor |
| JP4513861B2 (en) * | 2005-10-18 | 2010-07-28 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP4692220B2 (en) * | 2005-10-27 | 2011-06-01 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP2007187136A (en) * | 2006-01-16 | 2007-07-26 | Ooden:Kk | Particulate matter removing device, and particulate matter removing method |
| KR101410229B1 (en) | 2007-08-20 | 2014-06-23 | 삼성전자주식회사 | Method and apparatus for encoding continuation sinusoid signal information of audio signal, and decoding method and apparatus thereof |
| DE102008035562A1 (en) * | 2008-07-30 | 2010-02-04 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Emission control system for diesel engines of commercial vehicles |
| CN103761971B (en) * | 2009-07-27 | 2017-01-11 | 延世大学工业学术合作社 | Method and apparatus for processing audio signal |
| DE102009041092A1 (en) * | 2009-09-14 | 2011-03-24 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Exhaust treatment device with two honeycomb bodies for generating an electrical potential |
| DE102010034250A1 (en) * | 2010-08-13 | 2012-02-16 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Holder for at least one electrode in an exhaust pipe |
| DE102010045506A1 (en) * | 2010-09-15 | 2012-03-15 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Device for generating an electric field in an exhaust system |
| CN103845997A (en) * | 2014-03-24 | 2014-06-11 | 德清天皓环保科技有限公司 | Plasma organic waste gas purifier box body |
| FR3058648A1 (en) * | 2016-11-14 | 2018-05-18 | Universite De Poitiers | PROCESS FOR DECONTAMINATION OF A CARBON CONTAMINATED CATALYST |
| CN108839540A (en) * | 2018-06-25 | 2018-11-20 | 芜湖万向新元环保科技有限公司 | A kind of pretreatment plasma component |
| SG11202109812QA (en) * | 2019-03-11 | 2021-10-28 | Univ Southern California | Systems and methods for plasma-based remediation |
| GB2586611A (en) * | 2019-08-28 | 2021-03-03 | Hieta Tech Limited | Nonthermal plasma generator and method of manufacturing the same |
| KR102530208B1 (en) * | 2022-12-30 | 2023-05-09 | 에너젠(주) | Smoke reduction device for diesel generators |
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| JPH02104830U (en) * | 1988-10-05 | 1990-08-21 | ||
| JP2591260B2 (en) * | 1990-06-13 | 1997-03-19 | 日産自動車株式会社 | Engine exhaust purification device |
| BR9507282A (en) * | 1994-04-06 | 1997-09-23 | Minnesota Mining & Mfg | Filter cartridge and diesel particulate filter |
| US5746984A (en) * | 1996-06-28 | 1998-05-05 | Low Emissions Technologies Research And Development Partnership | Exhaust system with emissions storage device and plasma reactor |
| JP3230799B2 (en) * | 1996-10-11 | 2001-11-19 | 日野自動車株式会社 | Exhaust gas purification equipment for diesel engines |
| GB9801775D0 (en) * | 1998-01-29 | 1998-03-25 | Aea Technology Plc | Gas purification |
| JP3690112B2 (en) * | 1998-05-22 | 2005-08-31 | トヨタ自動車株式会社 | Diesel engine exhaust purification system |
| DE10130163B4 (en) * | 2000-11-21 | 2012-01-12 | Siemens Ag | Arrangement for reducing carbonaceous particulate emissions from diesel engines |
| JP2002276333A (en) * | 2001-03-22 | 2002-09-25 | Mitsubishi Heavy Ind Ltd | Discharge type exhaust gas purification device |
| US6722584B2 (en) * | 2001-05-02 | 2004-04-20 | Asb Industries, Inc. | Cold spray system nozzle |
| JP3855777B2 (en) * | 2002-01-23 | 2006-12-13 | トヨタ自動車株式会社 | Particulate filter for internal combustion engine |
| US20030182930A1 (en) * | 2002-03-28 | 2003-10-02 | Goulette David Alexander | Integrated non-thermal plasma reactor-diesel particulate filter |
| US7258723B2 (en) * | 2004-09-27 | 2007-08-21 | Arvin Technologies, Inc. | Particulate filter assembly and associated method |
-
2003
- 2003-09-11 JP JP2003319850A patent/JP2005083346A/en active Pending
-
2004
- 2004-09-10 DE DE602004014627T patent/DE602004014627D1/en not_active Expired - Fee Related
- 2004-09-10 EP EP04787865A patent/EP1669563B1/en not_active Expired - Lifetime
- 2004-09-10 WO PCT/JP2004/013225 patent/WO2005026506A1/en not_active Ceased
- 2004-09-10 US US10/571,535 patent/US20070028603A1/en not_active Abandoned
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011029730A1 (en) * | 2009-09-14 | 2011-03-17 | Emitec Gesellschaft Für Emissionstechnologie Mbh | Device for treating exhaust gas containing soot particles |
| RU2503829C2 (en) * | 2009-09-14 | 2014-01-10 | Эмитек Гезельшафт Фюр Эмиссионстехнологи Мбх | Cleaning device of waste gas containing soot particles |
Also Published As
| Publication number | Publication date |
|---|---|
| DE602004014627D1 (en) | 2008-08-07 |
| EP1669563A1 (en) | 2006-06-14 |
| WO2005026506A1 (en) | 2005-03-24 |
| US20070028603A1 (en) | 2007-02-08 |
| EP1669563A4 (en) | 2006-12-20 |
| JP2005083346A (en) | 2005-03-31 |
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