US20160108784A1 - White smoke reduction system for diesel vehicle - Google Patents
White smoke reduction system for diesel vehicle Download PDFInfo
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- US20160108784A1 US20160108784A1 US14/687,850 US201514687850A US2016108784A1 US 20160108784 A1 US20160108784 A1 US 20160108784A1 US 201514687850 A US201514687850 A US 201514687850A US 2016108784 A1 US2016108784 A1 US 2016108784A1
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- smoke reduction
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- 239000000779 smoke Substances 0.000 title claims abstract description 49
- 230000009467 reduction Effects 0.000 title claims abstract description 27
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 claims abstract description 28
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 claims abstract description 27
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000004615 ingredient Substances 0.000 claims abstract description 26
- 239000013618 particulate matter Substances 0.000 claims abstract description 15
- 239000003054 catalyst Substances 0.000 claims abstract description 14
- 230000003647 oxidation Effects 0.000 claims abstract description 5
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 5
- 239000011248 coating agent Substances 0.000 claims description 26
- 238000000576 coating method Methods 0.000 claims description 26
- 239000000463 material Substances 0.000 claims description 21
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 13
- 229910021536 Zeolite Inorganic materials 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 5
- 239000010457 zeolite Substances 0.000 claims description 5
- 238000005192 partition Methods 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- 229910052593 corundum Inorganic materials 0.000 claims 1
- 229910001845 yogo sapphire Inorganic materials 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 26
- 238000002347 injection Methods 0.000 description 14
- 239000007924 injection Substances 0.000 description 14
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000000149 argon plasma sintering Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000004509 smoke generator Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
Images
Classifications
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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, e.g. catalysed diesel particulate filters
-
- 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
-
- 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
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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
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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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/10—Noble metals or compounds thereof
- B01D2255/102—Platinum group metals
- B01D2255/1021—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/206—Rare earth metals
- B01D2255/2065—Cerium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/915—Catalyst supported on particulate filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/30—Sulfur compounds
- B01D2257/302—Sulfur oxides
-
- 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
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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
- F01N2510/00—Surface coverings
- F01N2510/06—Surface coverings for exhaust purification, e.g. catalytic reaction
-
- 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
- F01N2510/00—Surface coverings
- F01N2510/06—Surface coverings for exhaust purification, e.g. catalytic reaction
- F01N2510/063—Surface coverings for exhaust purification, e.g. catalytic reaction zeolites
-
- 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
- F01N2570/00—Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
- F01N2570/04—Sulfur or sulfur oxides
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Definitions
- the present disclosure relate to a white smoke reduction system, and particularly, to a white smoke reduction system capable of discharging sulfur oxide and water, which generate white smoke, at different temperature sections to suppress the sulfur oxide from reacting with the water.
- FIG. 1 is a diagram illustrating a configuration of an exhaust line in a typical diesel vehicle.
- An engine 10 , a diesel oxidation catalyst (DOC) 20 , and a diesel particulate filter (DPF) 30 are sequentially provided at a set interval in the exhaust line of the typical diesel vehicle.
- DOC diesel oxidation catalyst
- DPF diesel particulate filter
- sulfuric acid (H 2 SO 4 ) in the form of steam is generated by the combination of sulfur oxide (SO 2 ) and H 2 O in the process of removing particulate matter (PM) from the DPF 30 .
- the sulfuric acid (H 2 SO 4 ) in the form of steam is cooled, and a particle size thereof is increased when the exhaust gas is discharged to the air, thus causing light scattering and white smoke.
- An aspect of the present inventive concept is directed to a white smoke reduction system for a diesel vehicle, capable of discharging sulfur oxide (SO 2 ) and water (H 2 O), which cause generation of white smoke by their reaction, at different temperature sections to suppress the sulfur oxide from reacting with the water.
- SO 2 sulfur oxide
- H 2 O water
- a white smoke reduction system for a diesel vehicle which reduces white smoke generated from a diesel vehicle, includes a diesel oxidation catalyst (DOC) mounted on an exhaust line which is connected to an engine to oxidize exhaust gas through a catalyst.
- a filter module is connected to a rear end of the DOC to collect particulate matter contained in the exhaust gas and is coated with a ceria (CeO 2 ) ingredient such that sulfur oxide is separated at a temperature equal to or more than 600° C.
- the filer module may be a diesel particulate filter (DPF) connected to the rear end of the DOC.
- DPF diesel particulate filter
- the DPF may be coated with the ceria ingredient.
- the filer module may include a DPF connected to the rear end of the DOC and a white smoke reduction catalyst connected to a rear end of the DPF.
- the white smoke reduction catalyst may have a carrier through which the exhaust gas passes, and which is coated with the ceria ingredient.
- Platinum (Pt) may be contained in the coating material coated on the DOC.
- the coating material coated on the DOC may include alumina (Al 2 O 3 ) and zeolite.
- the coating amount of the ceria ingredient may be 50% or more of the amount of the coating material coated on the DOC.
- FIG. 1 is a diagram illustrating a configuration of an exhaust line in a typical diesel vehicle.
- FIG. 2 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according an embodiment of the present inventive concept.
- FIG. 4 is a graph indicating an increased temperature of a DPF, an SO 2 concentration, and white smoke generation according to post-injection in a comparative example.
- FIG. 2 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according an embodiment of the present inventive concept.
- FIG. 3 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according another embodiment of the present inventive concept.
- the engine 10 generates a driving force according to starting of a diesel vehicle, and serves to forcibly increase an exhaust temperature by performing post-injection according to control signals applied from an engine control unit (ECU) during regeneration of soot.
- ECU engine control unit
- the DOC 20 reduces CO, HC, and the particulate matter in the exhaust gas discharged by driving of the engine 10 , and converts NO into NO 2 . Particularly, the DOC 20 also functions to adsorb a sulfur ingredient onto a coating layer in the form of SO 2 .
- the DOC 20 comprises a carrier made of a ceramic or metal material, and a surface of the carrier is coated with one or more of alumina (Al 2 O 3 ), zeolite, and platinum (Pt) made of a catalytic material.
- a diesel particulate filter (hereinafter, referred to as “DPF”) includes a plurality of porous partition walls and collects the particulate matter passing through the DOC 20 .
- the filter module 100 includes a DPF 110 which is arranged at the rear end of the DOC 20 and coated with the ceria ingredient.
- an amount of the ceria ingredient coated on the DPF 110 may be 10% or more of an amount of a coating material coated on the DOC 20 when Pt is contained in the coating material coated on the DOC 20 .
- a separation temperature of the SO 2 may not be maintained at 600° or more due to a poor influence of the ceria ingredient.
- an amount of the ceria ingredient coated on the DPF 110 may be 50% or more of the amount of the coating material coated on the DOC 20 .
- the filter module 200 includes a conventional DPF 210 arranged at the rear end of the DOC 20 and a carrier 220 which is arranged at a rear end of the DPF 210 and coated with the ceria ingredient.
- the carrier 220 may be realized in a filter form having various shapes such that the exhaust gas may pass through the carrier 220 .
- An amount of the ceria ingredient coated on the carrier 220 may be 10% or more of the amount of the coating material coated on the DOC 20 when Pt is contained in the coating material coated on the DOC 20 , similar to the amount of the ceria ingredient coated on the DPF 110 .
- an amount of the ceria ingredient coated on the carrier 220 may be 50% or more of the amount of the coating material coated on the DOC 20 .
- the fuel used in the diesel engine 10 contains a predetermined sulfur ingredient, and sulfur oxide (SO 2 ) is generated in the combustion process.
- SO 2 sulfur oxide
- the sulfur oxide is present in exhaust gas in a state of absorbing water.
- the sulfur oxide is adsorbed onto the DOC 20 and the DPF 30 at a low temperature equal to or less than 400° C. during discharge of the exhaust gas, and is collected. Subsequently, when the temperatures of the DOC 20 and the DPF 30 are increased by the post-injection, the adsorbed sulfur oxide is separated and sulfuric acid (H 2 SO 4 ) in the form of gas is generated by reaction of the separated SO 2 and pyrolyzed H 2 O due to high temperature. A temperature of the generated sulfuric acid is decreased while the sulfuric acid is discharged to the air together with the exhaust gas, and thus, the sulfuric acid is discharged in the form of white smoke.
- sulfuric acid H 2 SO 4
- the post-injection is performed on the exhaust line configured of the conventional DOC 20 and DPF 30 .
- the post-injection is performed on the exhaust line having the DOC 20 and the ceria-coated DPF 110 according to the embodiment of the present inventive concept.
- the results according to these examples are shown in FIGS. 4 and 5 .
- FIG. 4 is a graph indicating an increased temperature of the DPF, the SO 2 concentration, and the white smoke generation according to the post-injection in the comparative example.
- FIG. 5 is a graph indicating an increased temperature of the DPF, the SO 2 concentration, and the white smoke generation according to the post-injection in the embodiment example.
- opacity is increased to 50% while a large quantity of sulfur oxide (SO 2 ) is discharged in a case in which a temperature T 5 measured at a front end of the DPF 30 when the temperature of the DPF 30 increases by the post-injection is between 400° C. and 600° C., and thus, a large quantity of white smoke is discharged.
- SO 2 sulfur oxide
- the sulfur oxide collected at a low temperature (a temperature equal to or less than 400° C.) when the DPF 30 is forcibly regenerated is separated in quantity between a temperature of 400° C. and 600° C., and sulfuric acid (H 2 SO 4 ) is excessively generated by reaction of the sulfur oxide (SO 2 ) with H 2 O, which is present as a compound in the exhaust line, as the temperature of the H 2 O increases. Consequently, a large quantity of white smoke is discharged.
- the sulfur oxide is separated at a temperature equal to or more than 600° C. instead of the conventional temperature of 400° C. to 600° C., and the H 2 O is discharged.
- the sulfur oxide is separated in a state in which the H 2 O is beforehand exhausted at a temperature less than the separation temperature of the sulfur oxide, the sulfur oxide is suppressed from reacting with the H 2 O. Therefore, it may be possible to suppress the generation of the white smoke while the sulfuric acid (H 2 SO 4 ) generated by the reaction of the sulfur oxide (SO 2 ) and the H 2 O is discharged to the air.
- An experimental result in which the post-injection is performed on the exhaust line having the DOC 20 , the DPF 210 , and the ceria-coated carrier 220 according to another embodiment also shows a pattern which is nearly similar to the above-mentioned experimental result in FIG. 5 .
- sulfur oxide and water may be discharged at different points of time by coating a ceria ingredient on a diesel particulate filter (DPF) or on a carrier which is separately installed at a rear end of the DPF such that sulfur oxide is separated at a higher temperature than a temperature section at which the water is discharged.
- DPF diesel particulate filter
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- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
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Abstract
A white smoke reduction system for a diesel vehicle reduces white smoke generated from a diesel vehicle. The white smoke reduction system includes a diesel oxidation catalyst (DOC) mounted on an exhaust line connected to an engine to oxidize exhaust gas through a catalyst. A filter module is connected to a rear end of the DOC to collect particulate matter contained in the exhaust gas and is coated with a ceria (CeO2) ingredient such that sulfur oxide is separated at a temperature equal to or more than 600° C.
Description
- The present application claims the benefit of priority to Korean Patent Application Number 10-2014-0139782 filed in the Korean Intellectual Property Office on Oct. 16, 2014, the entire contents of which application are incorporated herein for all purposes by this reference.
- The present disclosure relate to a white smoke reduction system, and particularly, to a white smoke reduction system capable of discharging sulfur oxide and water, which generate white smoke, at different temperature sections to suppress the sulfur oxide from reacting with the water.
- Exhaust gas discharged from diesel engine vehicles significantly contains a variety of oxide and particulate matter, compared to gasoline engine vehicles. In recent years, efforts to reduce such noxious exhaust gas are ongoing.
-
FIG. 1 is a diagram illustrating a configuration of an exhaust line in a typical diesel vehicle. Anengine 10, a diesel oxidation catalyst (DOC) 20, and a diesel particulate filter (DPF) 30 are sequentially provided at a set interval in the exhaust line of the typical diesel vehicle. - Particularly, in the diesel engine using fuel which contains 50 ppm or more of sulfur, sulfuric acid (H2SO4) in the form of steam is generated by the combination of sulfur oxide (SO2) and H2O in the process of removing particulate matter (PM) from the
DPF 30. For this reason, the sulfuric acid (H2SO4) in the form of steam is cooled, and a particle size thereof is increased when the exhaust gas is discharged to the air, thus causing light scattering and white smoke. - A large quantity of white smoke is generated by evaporation of water contained in sulfuric acid (H2SO4) into steam when the sulfuric acid containing water is exposed at high temperature (for instance, approximately 400° C. to 600° C. during regeneration of the DPF) while being collected in a catalyst, an exhaust pipe, a muffler, etc. during traveling of the vehicle. Thus, reduction of the white smoke is performed through engine control.
- A variety of white smoke reduction methods are currently proposed during regeneration of the DPF. However, such methods are not relatively effective since reducing white smoke through control of an engine or exhaust gas after-treatment device under a certain temperature.
- Accordingly, a technique for controlling a temperature variation rate when the temperature of the exhaust gas after-treatment device increases according to a vehicle speed has been recently proposed.
- However, since the conventional white smoke technique and the white smoke technique disclosed are performed through control of the engine or exhaust gas after-treatment device, the techniques require significant accuracy in controlling the engine or exhaust gas after-treatment device.
- The matters described as the related art have been provided only for assisting the understanding for the background of the present disclosure and should not be considered as corresponding to the related art already known to those skilled in the art.
- An aspect of the present inventive concept is directed to a white smoke reduction system for a diesel vehicle, capable of discharging sulfur oxide (SO2) and water (H2O), which cause generation of white smoke by their reaction, at different temperature sections to suppress the sulfur oxide from reacting with the water.
- Other objects and advantages of the present disclosure can be understood by the following description, and become apparent with reference to the embodiments of the present inventive concept. Also, it is obvious to those skilled in the art to which the present invention pertains that the objects and advantages of the present disclosure can be realized by the means as claimed and combinations thereof.
- In accordance with an embodiment of the present inventive concept, a white smoke reduction system for a diesel vehicle, which reduces white smoke generated from a diesel vehicle, includes a diesel oxidation catalyst (DOC) mounted on an exhaust line which is connected to an engine to oxidize exhaust gas through a catalyst. A filter module is connected to a rear end of the DOC to collect particulate matter contained in the exhaust gas and is coated with a ceria (CeO2) ingredient such that sulfur oxide is separated at a temperature equal to or more than 600° C.
- The filer module may be a diesel particulate filter (DPF) connected to the rear end of the DOC. The DPF may be coated with the ceria ingredient.
- The filer module may include a DPF connected to the rear end of the DOC and a white smoke reduction catalyst connected to a rear end of the DPF. The white smoke reduction catalyst may have a carrier through which the exhaust gas passes, and which is coated with the ceria ingredient.
- A coating amount of the ceria ingredient may be 10% or more of an amount of a coating material coated on the DOC. The DPF includes a plurality of porous partition walls and collects the particulate matter passing through the DOC.
- Platinum (Pt) may be contained in the coating material coated on the DOC.
- The coating material coated on the DOC may include alumina (Al2O3) and zeolite. The coating amount of the ceria ingredient may be 50% or more of the amount of the coating material coated on the DOC.
-
FIG. 1 is a diagram illustrating a configuration of an exhaust line in a typical diesel vehicle. -
FIG. 2 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according an embodiment of the present inventive concept. -
FIG. 3 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according another embodiment of the present inventive concept. -
FIG. 4 is a graph indicating an increased temperature of a DPF, an SO2 concentration, and white smoke generation according to post-injection in a comparative example. -
FIG. 5 is a graph indicating an increased temperature of a DPF, an SO2 concentration, and white smoke generation according to post-injection in an embodiment example. - Exemplary embodiments of the present inventive concept will be described below in more detail with reference to the accompanying drawings. The present inventive concept may, however, be embodied in different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the present disclosure to those skilled in the art. Throughout the disclosure, like reference numerals refer to like parts throughout the various figures and embodiments of the present inventive concept.
-
FIG. 2 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according an embodiment of the present inventive concept.FIG. 3 is a diagram illustrating a configuration of a white smoke reduction system for a diesel vehicle according another embodiment of the present inventive concept. - As shown in the drawings, the white smoke reduction system for a diesel vehicle according the embodiments of the present inventive concept includes a diesel oxidation catalyst (DOC) 20 which is mounted on an exhaust line connected to an
engine 10 to oxidize exhaust gas through a catalyst. Afilter module DOC 20 to collect particulate matter contained in the exhaust gas and is coated with a ceria (CeO2) ingredient such that sulfur oxide (SO2) is separated at a temperature equal to or more than 600° C. - The
engine 10 generates a driving force according to starting of a diesel vehicle, and serves to forcibly increase an exhaust temperature by performing post-injection according to control signals applied from an engine control unit (ECU) during regeneration of soot. - Here, the post-injection is to additionally inject fuel into high-temperature exhaust gas immediately after explosion in the intake, compression, and explosion/exhaust strokes of the
engine 10 to increase the temperature of the exhaust gas according to additional combustion. The post-injection is performed under regeneration condition determination according to an accumulated amount of particulate matter (PM). - The
DOC 20 reduces CO, HC, and the particulate matter in the exhaust gas discharged by driving of theengine 10, and converts NO into NO2. Particularly, theDOC 20 also functions to adsorb a sulfur ingredient onto a coating layer in the form of SO2. - In this case, the
DOC 20 comprises a carrier made of a ceramic or metal material, and a surface of the carrier is coated with one or more of alumina (Al2O3), zeolite, and platinum (Pt) made of a catalytic material. - The
filter module filter module filter module - A diesel particulate filter (hereinafter, referred to as “DPF”) includes a plurality of porous partition walls and collects the particulate matter passing through the
DOC 20. - As shown in
FIG. 2 , thefilter module 100 according to an exemplary embodiment includes aDPF 110 which is arranged at the rear end of theDOC 20 and coated with the ceria ingredient. - In this case, an amount of the ceria ingredient coated on the
DPF 110 may be 10% or more of an amount of a coating material coated on theDOC 20 when Pt is contained in the coating material coated on theDOC 20. - If the amount of the ceria ingredient is less than 10% of an amount of the coating material coated on the
DOC 20, a separation temperature of the SO2 may not be maintained at 600° or more due to a poor influence of the ceria ingredient. - However, when Pt is not contained in the coating material coated on the
DOC 20 and the coating material mainly contains alumina (Al2O3) and zeolite, an amount of the ceria ingredient coated on theDPF 110 may be 50% or more of the amount of the coating material coated on theDOC 20. - As shown in
FIG. 3 , thefilter module 200 according to another embodiment includes aconventional DPF 210 arranged at the rear end of theDOC 20 and acarrier 220 which is arranged at a rear end of theDPF 210 and coated with the ceria ingredient. - In this case, the
carrier 220 may be realized in a filter form having various shapes such that the exhaust gas may pass through thecarrier 220. - An amount of the ceria ingredient coated on the
carrier 220 may be 10% or more of the amount of the coating material coated on theDOC 20 when Pt is contained in the coating material coated on theDOC 20, similar to the amount of the ceria ingredient coated on theDPF 110. In addition, when Pt is not contained in the coating material coated on theDOC 20, and the coating material mainly contains Al2O3 and zeolite, an amount of the ceria ingredient coated on thecarrier 220 may be 50% or more of the amount of the coating material coated on theDOC 20. - Performance of the white smoke reduction system for a diesel vehicle as described above according to the present disclosure will be described according to comparison of a comparative example and an embodiment example.
- First, a white smoke generator in the diesel vehicle is simply described.
- The fuel used in the
diesel engine 10 contains a predetermined sulfur ingredient, and sulfur oxide (SO2) is generated in the combustion process. The sulfur oxide is present in exhaust gas in a state of absorbing water. - The sulfur oxide is adsorbed onto the
DOC 20 and theDPF 30 at a low temperature equal to or less than 400° C. during discharge of the exhaust gas, and is collected. Subsequently, when the temperatures of theDOC 20 and theDPF 30 are increased by the post-injection, the adsorbed sulfur oxide is separated and sulfuric acid (H2SO4) in the form of gas is generated by reaction of the separated SO2 and pyrolyzed H2O due to high temperature. A temperature of the generated sulfuric acid is decreased while the sulfuric acid is discharged to the air together with the exhaust gas, and thus, the sulfuric acid is discharged in the form of white smoke. - Next, an SO2 concentration and white smoke generation in exhaust gas are compared according to the comparative example and the embodiment example.
- In the comparative example, the post-injection is performed on the exhaust line configured of the
conventional DOC 20 andDPF 30. In the embodiment example, the post-injection is performed on the exhaust line having theDOC 20 and the ceria-coatedDPF 110 according to the embodiment of the present inventive concept. The results according to these examples are shown inFIGS. 4 and 5 . -
FIG. 4 is a graph indicating an increased temperature of the DPF, the SO2 concentration, and the white smoke generation according to the post-injection in the comparative example.FIG. 5 is a graph indicating an increased temperature of the DPF, the SO2 concentration, and the white smoke generation according to the post-injection in the embodiment example. - As seen in the comparative example of
FIG. 4 , it is identified that opacity is increased to 50% while a large quantity of sulfur oxide (SO2) is discharged in a case in which a temperature T5 measured at a front end of theDPF 30 when the temperature of theDPF 30 increases by the post-injection is between 400° C. and 600° C., and thus, a large quantity of white smoke is discharged. - In other words, the sulfur oxide collected at a low temperature (a temperature equal to or less than 400° C.) when the
DPF 30 is forcibly regenerated is separated in quantity between a temperature of 400° C. and 600° C., and sulfuric acid (H2SO4) is excessively generated by reaction of the sulfur oxide (SO2) with H2O, which is present as a compound in the exhaust line, as the temperature of the H2O increases. Consequently, a large quantity of white smoke is discharged. - On the other hand, as seen in the embodiment example of
FIG. 5 , it is identified that a large quantity of sulfur oxide (SO2) is discharged in a case in which the temperature T5 measured at a front end of theDPF 110 when the temperature of theDPF 110 increases by the post-injection is equal to or more than 600° C. (620° C. to 650° C.), but opacity is maintained to the level of 10% or less, and thus, discharge of white smoke is suppressed. - This is because the sulfur oxide collected at a low temperature (a temperature equal to or less than 400° C.) when the
DPF 110 is forcibly regenerated is separated in quantity at a temperature equal to or more than 600° C., but H2O, which is collected as a compound in the exhaust line, is discharged and exhausted, and thus, H2O gas amount decreases rapidly at a temperature section equal to or more than 600° C. Thus, since an amount of H2O to be reacted remarkable decreases even though the sulfur oxide (SO2) separated at the temperature section equal to or more than 600° C. is discharged, the reaction of the sulfur oxide (SO2) and the H2O is suppressed so that the white smoke is nearly invisible with the naked eye. - Accordingly, according to the comparison of the above-mentioned comparative example and embodiment example, when the ceria-coated
DPF 100 is applied, the sulfur oxide is separated at a temperature equal to or more than 600° C. instead of the conventional temperature of 400° C. to 600° C., and the H2O is discharged. Thus, since the sulfur oxide is separated in a state in which the H2O is beforehand exhausted at a temperature less than the separation temperature of the sulfur oxide, the sulfur oxide is suppressed from reacting with the H2O. Therefore, it may be possible to suppress the generation of the white smoke while the sulfuric acid (H2SO4) generated by the reaction of the sulfur oxide (SO2) and the H2O is discharged to the air. - An experimental result in which the post-injection is performed on the exhaust line having the
DOC 20, theDPF 210, and the ceria-coatedcarrier 220 according to another embodiment also shows a pattern which is nearly similar to the above-mentioned experimental result inFIG. 5 . - In accordance with the exemplary embodiments of the present inventive concept, sulfur oxide and water may be discharged at different points of time by coating a ceria ingredient on a diesel particulate filter (DPF) or on a carrier which is separately installed at a rear end of the DPF such that sulfur oxide is separated at a higher temperature than a temperature section at which the water is discharged.
- Thus, it may be possible to prevent generation of white smoke by suppressing the sulfur oxide from reacting with the water.
- While the present disclosure has been described with respect to the specific embodiments, it will be apparent to those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the invention as defined in the following claims.
Claims (8)
1. A white smoke reduction system for a diesel vehicle, which reduces white smoke generated from a diesel vehicle, the system comprising:
a diesel oxidation catalyst (DOC) mounted on an exhaust line connected to an engine to oxidize exhaust gas through a catalyst; and
a filter module connected to a rear end of the DOC to collect particulate matter contained in the exhaust gas, the filter module being coated with a ceria (CeO2) ingredient such that sulfur oxide is separated at a temperature equal to or more than 600° C.
2. The white smoke reduction system of claim 1 , wherein:
the filer module is a diesel particulate filter (DPF) connected to the rear end of the DOC; and
the DPF is coated with the ceria ingredient.
3. The white smoke reduction system of claim 1 , wherein:
the filer module comprises a DPF connected to the rear end of the DOC and a white smoke reduction catalyst connected to a rear end of the DPF; and
the white smoke reduction catalyst includes a carrier through which the exhaust gas passes, the carrier being coated with the ceria ingredient.
4. The white smoke reduction system of claim 2 , wherein a coating amount of the ceria ingredient is 10% or more of an amount of a coating material coated on the DOC.
5. The white smoke reduction system of claim 4 , wherein platinum (Pt) is contained in the coating material coated on the DOC.
6. The white smoke reduction system of claim 4 , wherein the coating material coated on the DOC comprises alumina (Al2O3) and zeolite, and a coating amount of the ceria ingredient is 50% or more of the amount of the coating material coated on the DOC.
7. The white smoke reduction system of claim 3 , wherein a coating amount of the ceria ingredient is 10% or more of an amount of a coating material coated on the DOC.
8. The white smoke reduction system of claim 2 , wherein the DPF includes a plurality of porous partition walls and collects the particulate matter passing through the DOC.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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KR10-2014-0139782 | 2014-10-16 | ||
KR1020140139782A KR101646355B1 (en) | 2014-10-16 | 2014-10-16 | System for decreasing white smoke |
Publications (1)
Publication Number | Publication Date |
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US20160108784A1 true US20160108784A1 (en) | 2016-04-21 |
Family
ID=55638180
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US14/687,850 Abandoned US20160108784A1 (en) | 2014-10-16 | 2015-04-15 | White smoke reduction system for diesel vehicle |
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US (1) | US20160108784A1 (en) |
KR (1) | KR101646355B1 (en) |
DE (1) | DE102015208383A1 (en) |
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KR101091633B1 (en) * | 2009-12-03 | 2011-12-08 | 현대자동차주식회사 | Denitrification catalyst and exhaust system using the same |
US9346018B2 (en) * | 2010-11-02 | 2016-05-24 | Haldor Topsoe A/S | Method for the preparation of a catalysed particulate filter and catalysed particulate filter |
JP5769732B2 (en) * | 2010-12-27 | 2015-08-26 | エヌ・イーケムキャット株式会社 | Selective reduction catalyst, exhaust gas purification apparatus and exhaust gas purification method using the same |
KR20130017392A (en) * | 2011-08-10 | 2013-02-20 | 현대자동차주식회사 | Exhaust gas processing device |
KR101371723B1 (en) | 2012-04-18 | 2014-03-07 | 현대자동차(주) | Method and system for reducing white smoke for diesel vehicle |
-
2014
- 2014-10-16 KR KR1020140139782A patent/KR101646355B1/en not_active Expired - Fee Related
-
2015
- 2015-04-15 US US14/687,850 patent/US20160108784A1/en not_active Abandoned
- 2015-05-06 DE DE102015208383.7A patent/DE102015208383A1/en not_active Withdrawn
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KR101646355B1 (en) | 2016-08-08 |
KR20160045178A (en) | 2016-04-27 |
DE102015208383A1 (en) | 2016-04-21 |
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