KR960002520B1 - Particle material removing method of exhaust gas - Google Patents
Particle material removing method of exhaust gas Download PDFInfo
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- KR960002520B1 KR960002520B1 KR1019930005166A KR930005166A KR960002520B1 KR 960002520 B1 KR960002520 B1 KR 960002520B1 KR 1019930005166 A KR1019930005166 A KR 1019930005166A KR 930005166 A KR930005166 A KR 930005166A KR 960002520 B1 KR960002520 B1 KR 960002520B1
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- Prior art keywords
- exhaust gas
- trap
- particulate matter
- filter
- diesel vehicle
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- 238000000034 method Methods 0.000 title claims description 13
- 239000000463 material Substances 0.000 title claims description 6
- 239000002245 particle Substances 0.000 title description 5
- 239000002816 fuel additive Substances 0.000 claims abstract description 13
- 239000011810 insulating material Substances 0.000 claims abstract description 10
- -1 lanthanide metal compounds Chemical class 0.000 claims abstract description 5
- 229910052742 iron Inorganic materials 0.000 claims abstract description 4
- 150000001341 alkaline earth metal compounds Chemical class 0.000 claims abstract description 3
- 229910052788 barium Inorganic materials 0.000 claims abstract description 3
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 3
- 229910052747 lanthanoid Inorganic materials 0.000 claims abstract description 3
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 3
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 3
- 150000003623 transition metal compounds Chemical class 0.000 claims abstract description 3
- 239000013618 particulate matter Substances 0.000 claims description 24
- 239000003054 catalyst Substances 0.000 claims description 20
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 9
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
- 239000000919 ceramic Substances 0.000 claims description 7
- 239000000446 fuel Substances 0.000 claims description 6
- 229910052697 platinum Inorganic materials 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000010425 asbestos Substances 0.000 claims description 4
- 239000000378 calcium silicate Substances 0.000 claims description 4
- 229910052918 calcium silicate Inorganic materials 0.000 claims description 4
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 229910052763 palladium Inorganic materials 0.000 claims description 4
- 229910052895 riebeckite Inorganic materials 0.000 claims description 4
- 229910052703 rhodium Inorganic materials 0.000 claims description 3
- 239000010948 rhodium Substances 0.000 claims description 3
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 3
- 239000011575 calcium Substances 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims description 2
- 239000011521 glass Substances 0.000 claims description 2
- 239000006262 metallic foam Substances 0.000 claims description 2
- 239000002557 mineral fiber Substances 0.000 claims description 2
- 239000011152 fibreglass Substances 0.000 claims 1
- 239000006260 foam Substances 0.000 claims 1
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 1
- 239000011707 mineral Substances 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 8
- 229910052684 Cerium Inorganic materials 0.000 abstract description 2
- 229910000510 noble metal Inorganic materials 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 230000008929 regeneration Effects 0.000 description 13
- 238000011069 regeneration method Methods 0.000 description 13
- 239000000654 additive Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000010969 white metal Substances 0.000 description 1
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
- F01N3/08—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
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/10—Filter screens essentially made of metal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1615—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of natural origin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2003—Glass or glassy material
- B01D39/2017—Glass or glassy material the material being filamentary or fibrous
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2027—Metallic material
- B01D39/2051—Metallic foam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2082—Other inorganic materials, e.g. ceramics the material being filamentary or fibrous
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/20—Other self-supporting filtering material ; Other filtering material of inorganic material, e.g. asbestos paper, metallic filtering material of non-woven wires
- B01D39/2068—Other inorganic materials, e.g. ceramics
- B01D39/2093—Ceramic foam
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Organic Chemistry (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Toxicology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
본 발명은 디젤차량 배기가스중의 입자상물질을 제거하는 방법에 관한 것이다.The present invention relates to a method for removing particulate matter in diesel vehicle exhaust gas.
현재 디젤차량의 보유비율이 전체 차량의 42%에 달하는 한국에서는 디젤차량의 배기가스로 배출되는 입자상물질이 주요한 대기오염요인으로 대두되고 있다. 디젤차량의 배기가스로 배출되는 입자상물질은 평균직경이 0.3㎛ 정도의 미연소 탄소입자로서 배기가스중의 농도가 환경기준치(1993년 해비듀티 차량의 경우 스모크 규제치 : 40%)를 초과할 경우 시각적으로 심한 불쾌감을 초래할 뿐아니라 암등 인체에 유해한 병을 유발하는 원인이 되고 있다. 따라서, 이러한 입자상물질의 강화된 배출규제가 요구되어 해비듀티 디젤차량의 경우 한국은 1996년에 0.67g/Hp. Hour, 미국은 1994년부터 0.1g/Hp. Hour로 규제를 강화할 예정이지만 아직까지 이를 만족시키는 기술이 상용화되지 못하여 다양한 연구가 활발히 수행되고 있다.In Korea, where the proportion of diesel vehicles is 42% of total vehicles, particulate matter emitted by the exhaust gas of diesel vehicles is a major air pollution factor. Particulate matter discharged from the exhaust gas of diesel vehicles is unburned carbon particles with an average diameter of about 0.3 μm. When the concentration in the exhaust gas exceeds the environmental standard value (the smoke limit of 40% for a heavy duty vehicle in 1993: As well as causing severe discomfort, it is the cause of harmful diseases such as cancer. Therefore, in the case of heavy duty diesel vehicles, in 1996, 0.67 g / Hp. Hour, United States since 1994, 0.1g / Hp. The company plans to strengthen regulations with Hour, but various studies are being actively conducted since the technology that satisfies this has not been commercialized.
입자상물질의 제거기술 개발방향은 엔진의 고효율화를 통한 미연소 물질의 생성억제, 연료첨가제를 이용한 연소성능의 개선, 입자상물질의 후처리기술등이 있으며 엔진의 고효율화 및 연료첨가제를 이용하는 방법은 엔진내에서의 연소효과를 증가시켜 입자상물질이나 매연등의 유해물질을 근본적으로 감소시킬 수 있으나 비용이 과다하게 소요되고, 현재의 기술수준으로는 완벽한 억제가 용이하지 않아 결국은 배기가스를 통해서 배출되고 있는 실정이다. 상기 후처리 기술은 배기가스중의 입자상불질을 여과하는 여과기술과 여과된 입자상물질을 연소하여 여과재를 재생하는 기술로 구성되며 여과기술은 배기가스중의 입자상물질을 효과적으로 포집할 수 있는 성능이 우수한 여과재의 선택과 실제의 차량에 적합하게 응용될 수 있도록 하는 연구에 주력하고 있다.The development direction of the removal of particulate matter includes the suppression of the production of unburned materials through the high efficiency of the engine, the improvement of the combustion performance using the fuel additive, and the post-treatment technology of the particulate matter. It is possible to fundamentally reduce harmful substances such as particulate matter and soot by increasing the combustion effect in Esau, but it is excessively expensive, and it is not easy to be completely suppressed by the current technology level, and is finally discharged through exhaust gas. It is true. The post-treatment technology is composed of a filtration technology for filtering particulate impurities in exhaust gas and a technology for regenerating the filter material by burning the filtered particulate matter. The filtration technology has an excellent ability to effectively collect particulate matter in exhaust gas. The research focuses on the selection of filter media and its application to actual vehicles.
그러나, 입자상물질의 여과에 따른 엔진배기통로의 배압상승으로 여과재를 손상시키고 엔진의 성능저하를 유발하며, 입자상물질의 침착된 여과재를 높은온도 조건에서 연소시킬때 효과적으로 연소시키기 위한 재생기술의 개발이 필요하게 되었다.However, the development of regeneration technology for damaging the filter medium and degrading the engine performance by increasing the back pressure of the engine exhaust passage due to the filtration of particulate matter and effectively burning the deposited filter medium of particulate matter at high temperature conditions. It became necessary.
현재까지 가장 널리 알려진 재생기술은 버너, 히터등을 이용하여 2차 에너지를 공급하거나 쒼背틀링으로 배기가스 온도를 높여 재생하는 방법과 연료에 촉매를 첨가하거나 촉매를 여과재에 침착시켜 재생시키는 방법이 있다.The most widely known regeneration technology to date is a method of supplying secondary energy by using a burner, a heater, or the like by regenerating the exhaust gas by raising the exhaust gas temperature, and adding a catalyst to the fuel or depositing the catalyst on the filter medium. have.
미합중국 특허 제3951613호, 제3761729호, 일본특허 공개 제86225282호에 의하면 연료에 구리, 셀륨, 망간, 규소, 철 등의 유기금속 첨가제를 연료에 주입하여 여과재를 재생하는데, 이 경우 첨가제주입량에 따라 재생성능이 변하며 우수한 재생성능을 나타내도록 첨가제주입량을 높일 경우 일부의 작은 양이 배가가스와 함께 여과재를 거쳐 대기로 배출되어 2차 공해를 유발하는 것으로 알려져 있다.According to US Patent Nos. 3951613, 3761729, and Japanese Patent Publication No. 86225282, fuel, organic metal additives such as copper, selium, manganese, silicon, and iron are injected into the fuel to regenerate the filter material. It is known that when the additive injection amount is increased and the regeneration performance is changed, and the additive injection amount is increased, a small amount of some is discharged to the atmosphere through the filter medium together with the doubling gas, causing secondary pollution.
한국특허 공고 제89-3594호, 미합중국 특허 제5083427호에는 여과재에 백금, 팔라듐, 로듐등의 귀금속촉매를 여과재에 침착시키고 이를 엔진배기관에 장착하여 여과재를 재생하는 방법이 보고되어 있다. 그러나, 이러한 벙법은 여러가지 단점이 있다. 즉, 예를들면 300℃ 정도인 보통의 디젤엔진 배기가스 온도에서는 입자상물질이 효과적으로 연소되지 못한다. 디젤엔진 배기가스 온도는 500℃ 이상으로 올라갈 경우도 있으나 대부분 300℃ 또는 그 이하인 경우가 일반적이다. 예를들면, 시내주행과 같이 간헐적인 고속운전을 제외하고는 서행운전속도이므로 그 온도는 통상적으로 300℃ 또는 그 이하가 된다. 따라서 촉매화된 여과재를 사용하는 경우 낮은 배기가스온도에서 입자상물질이 충분히 연소되지 못하고 과도하게 축적되어 배기가스 배출압력을 상승시키고 과량의 탄소물질이 급격히 연소하므로써 과도한 온도상승에 의해서 여과재가 파손되는 문제가 실제적용상의 큰 문제인 것으로 알려져 있다.Korean Patent Publication No. 89-3594 and US Pat. No. 5083427 report a method of depositing a noble metal catalyst such as platinum, palladium, rhodium, and the like on a filter medium and mounting it on an engine exhaust pipe to regenerate the filter medium. However, this approach has several disadvantages. That is, particulate matter is not effectively combusted at an ordinary diesel engine exhaust gas temperature of, for example, about 300 ° C. Diesel engine exhaust gas temperature may be raised to 500 ℃ or more, but most of the temperature is 300 ℃ or less in general. For example, except for intermittent high speed operation such as city running, the temperature is typically 300 ° C. or lower since it is a slow running speed. Therefore, in the case of using the catalyzed filter medium, particulate matter is not sufficiently burned at low exhaust gas temperature and excessively accumulated, thereby increasing the exhaust gas discharge pressure, and excessive carbon material is rapidly burned, causing the filter medium to be damaged by excessive temperature rise. Is known to be a big problem in practical application.
본 발명자들은 상기의 문제점들을 해결하기 위하여 광범위한 연구를 수행한 결과, 엔진 배기관을 흐르는 배기가스의 온도가 열손실로 인해 여과트랩에서는 엔진배기구보다 낮게 유지된다는 점을 발견하고, 본 발명은 이러한 발견에 기초하여 배기관을 단열시스템으로 개선하므로써 완성되었다.The present inventors have conducted extensive research to solve the above problems and found that the temperature of the exhaust gas flowing through the engine exhaust pipe is kept lower than the engine exhaust pipe in the filter trap due to heat loss. On the basis of this, the exhaust pipe was completed by improving the insulation system.
따라서, 본 발명은 쒼背틀링이나 2차 에너지의 공급없이 배기관내의 온도를 촉매가 작동하는 적절한 온도로 유지시킴으로써 상기 기술의 문제점인 재생효율을 상당히 향상시키는 방법을 제공하는데 그 목적이 있다.It is therefore an object of the present invention to provide a method of significantly improving the regeneration efficiency, which is a problem of the above technique, by maintaining the temperature in the exhaust pipe at an appropriate temperature at which the catalyst operates without quenching or supplying secondary energy.
상기 목적을 달성하고자 본 발명의 방법은 연료첨가제를 함유한 디젤과 여과트랩을 동시에 사용하거나 촉매를 코팅한 여과트랩(이하, 즉 매트랩)을 단독으로 사용하여 입자상 물질을 제거하는데 있어서, 엔진 배기관으로부터 상기 여과트랩에 이르는 배기관 또는 상기 촉매트랩까지를 단열재나 단열재를 함유한 하우징을 장착함으로서 여과트랩의 온도를 높여 입자상물질을 제거하는 방법으로 구성된다.In order to achieve the above object, the method of the present invention removes particulate matter by simultaneously using diesel and filter traps containing a fuel additive or by using a catalyst-coated filter trap (hereinafter, referred to as a mat trap) alone. By mounting a housing containing a heat insulating material or a heat insulating material to the exhaust pipe leading to the filter trap or up to the catalyst trap is configured to increase the temperature of the filter trap to remove particulate matter.
본 발명에서 사용하는 여과트랩은 연료첨가제를 사용할 경우에는 세라믹퐁, 세라믹 화이버 필터, 오픈 플로우 세라믹하니컴, 웰 플로우 하니컴 모노리스, 오픈 플로우 메탈하니컴, 메탈폼, 메탈메쉬등 디젤 입자상 물질 여과에 유용한 것으로 이미 공지된 모든 삼차원 구조물이 사용될 수 있으며 이에 특별한 제한은 없다.The filter trap used in the present invention is useful for filtration of diesel particulate matter such as ceramic pong, ceramic fiber filter, open flow ceramic honeycomb, well flow honeycomb monolith, open flow metal honeycomb, metal foam, metal mesh, etc. All known three-dimensional structures can be used and there is no particular limitation.
본 발명에 사용하는 연료첨가제는 유용성 전이금속화합물(Mn, Fe, Ni, Ce, Cu, Co등), 알칼리토금속화합물(Ba, Ca), 란타나이드계금속화합물(Ce등)중 1종 또는 2종 이상을 디젤에 첨가시켰을때 매연억제에 유용한 것으로 이미 공지된 모든 조연첨가제가 사용될 수 있으며 이에 특별한 제한은 없다.One or two of the fuel additives used in the present invention are oil-soluble transition metal compounds (Mn, Fe, Ni, Ce, Cu, Co, etc.), alkaline earth metal compounds (Ba, Ca), and lanthanide metal compounds (Ce, etc.). When added more than one species to the diesel can be used for all fuel additives known to be useful for suppressing soot, there is no particular limitation.
본 발명에서 사용하는 촉매트랩은 상기 여과트랩에 백금, 로듐, 팔라듐등 1종 또는 2종이상의 백금속금속을 코팅하여 제작한 것으로 디젤 입자상물질의 여과 및 재생에 유용한 것으로 이미 공지된 삼차원 구조물이 사용될 수 있으며 이에 특별한 제한은 없다.The catalyst trap used in the present invention is produced by coating one or two or more kinds of white metals such as platinum, rhodium, and palladium on the filter traps, and a three-dimensional structure already known to be useful for filtration and regeneration of diesel particulates may be used. There is no special limitation to this.
본 발명에서 사용하는 단열재는 석면, 미네랄 화이버, 셀룰라 글래스, 칼슘 실리케이트, 실리카 에어로젤, 다이아로마이트등 일반적으로 300℃ 이상의 고온에서도 단열성능이 우수한 것으로 이미 공지된 물질에 특별한 제한은 없다. 엔진 배기관부터 여과트랩이나 촉매트랩까지를 단열재나 단열재를 함유한 하우징을 장착하고 연료첨가제를 함유한 디젤을 주입하였다.Insulation materials used in the present invention is asbestos, mineral fibers, cell glass, calcium silicate, silica airgel, diatomite, etc. In general, there is no particular limitation to materials that are known to have excellent heat insulation performance even at high temperatures of 300 ° C or higher. From the engine exhaust pipe to the filter trap or the catalyst trap, a housing containing a heat insulating material or a heat insulating material was mounted, and diesel containing a fuel additive was injected.
이상과 같은 방법으로 연료첨가제와 여과트랩을 동시에 사용한 경우 트랩내의 온도가 50℃~150℃정도 상승하여 저속, 저부하에서도 재생이 쉽게 일어났음은 물론이고, 촉매트랩만 사용했을 때에도 입자상물질의 과다한 축적없이 재생이 용이하게 일어나서 과다한 배압의 변화로 인한 여과재의 손상을 최소화할 수 있었다.When the fuel additive and the filter trap are used at the same time as described above, the temperature inside the trap is increased by 50 ° C to 150 ° C, so that regeneration is easily performed even at low speed and low load, and even when only the catalyst trap is used, Regeneration could easily occur without accumulation, minimizing damage to the filter media due to excessive back pressure changes.
이하, 실시예 및 비교예를 통해 본 발명의 구성 및 그 효과를 구체적으로 설명하기로 하나, 이 예가 발명의 범주를 제한하지는 않는다.Hereinafter, the configuration and effects of the present invention will be described in detail with reference to Examples and Comparative Examples, but the examples do not limit the scope of the present invention.
[실시예1]Example 1
디젤연료 혼합물의 입자방출을 측정하기 위해 입자트랩 다이나모메타 실험을 실시하였다. 페터 AV-B 수퍼차지드 단일실린더 디젤 실험용 엔진이 사용되었다. 이 엔진은 코팅 EX-54세라믹 단일체 여과기와 연결되었다. 엔지배기관에서 여과트랩까지의 석면테이프(제일화학사의 Pack Non Drop Worp)로 두께가 5㎜가 되도록 감았다. 세륨나프테네이트를 500ppm 함유한 디젤조성물 15ℓ를 제조한다. 상기 디젤연료 조성물을 엔진에 주입하고 착화시 운전파워를 기록한다. 기존연료를 주입하여 운전속도 2250±20rpm, 냉각수온도 100±2℃, 오일온도 90±2℃, 오일압력 2.5±0.2bar, 공기투입구 압력 2280±15mbar의 정상운전조건에서 엔진의 바이패스 밸브를 잠그고 여과트랩 밸브를 연다. 엔진에서 방출된 입자가 여과기에 쌓임에 따라 엔진과 여과트랩 사이의 압력이 증가한다. 쒼背틀 밸브를 조작하여 5분마다 파워를 0.6KW씩 올려 압력이 급격히 감소하는 순간까지 트랩후단의 온도, 압력을 측정한다. 이때 재생이 일어나는 시간과 온도, 압력의 변화관계는 하기 표1과 같다.Particle trap dynamometer experiments were conducted to measure particle emissions of diesel fuel mixtures. A Peter AV-B supercharged single cylinder diesel engine was used. The engine was connected to a coated EX-54 ceramic monolithic filter. Asbestos tape (Pack Non Drop Worp from Cheil Chemical Co., Ltd.) from the engine exhaust pipe to the filter trap was wound to a thickness of 5 mm. 15 L of a diesel composition containing 500 ppm of cerium naphthenate is prepared. Inject the diesel fuel composition into the engine and record the operating power at ignition. By inserting the existing fuel, the engine bypass valve is shut off under normal operating conditions of 2250 ± 20rpm, coolant temperature 100 ± 2 ℃, oil temperature 90 ± 2 ℃, oil pressure 2.5 ± 0.2bar, air inlet pressure 2280 ± 15mbar. Open the filter trap valve. As the particles released from the engine accumulate in the filter, the pressure between the engine and the filter trap increases. Operate the chute valve and increase the power by 0.6KW every 5 minutes to measure the temperature and pressure at the end of the trap until the moment the pressure decreases rapidly. At this time, the relationship between the regeneration time and the temperature, pressure is shown in Table 1.
[비교예][Comparative Example]
실시예 1의 장치에서 석면테이프를 제거한 후 실시예 1과 동일한 조건에서 실험하였으며, 이때 재생이 일어나는 시간과 온도, 압력의 변화관계는 하기 표2와 같다.After removing the asbestos tape in the apparatus of Example 1, the experiment was carried out under the same conditions as in Example 1, wherein the time of regeneration occurs, and the change in temperature and pressure is shown in Table 2 below.
[표 1]TABLE 1
[표 2]TABLE 2
상기 표1과 2에서 알 수 있듯이 본 발명의 연료첨가제와 여과재를 동시에 사용하여 디젤 입자상물질에 제거하는 장치에 단열재를 부착하는 방법은 저파워, 저배압에서도 단시간에 쉽게 재생이 일어남을 알 수 있다.As can be seen from Tables 1 and 2, the method of attaching the insulation to the diesel particulate matter removal apparatus using the fuel additive and the filter medium of the present invention can be seen that the regeneration occurs easily in a short time even at low power and low back pressure. .
[실시예2]Example 2
월 플로우 하니컴 모노리스에 알루미나와 알루미나를 기준으로 백금과 팔라듐이 각각 0.5wt% 장착된 촉매여과재를 트랩에 조립한 후 페터 AV-B 슈퍼차지도 단일 실린더 디젤 실험용 엔진의 배기관에 장착하였다. 엔진배기관으로부터 촉매트랩까지를 감싸는 하우징을 충진두께가 8㎜가 되도록 제작하여 부착한 후, 배기관에서 촉매트랩에 이르는 배기장치와 하우징 사이의 공간에 칼슘실리케이트 분말을 충진하였다. 첨가제가 들어가지 않는 디젤을 시험용 연료로 사용하여 실시예 1과 동일한 운전조건에서 실험하였으며, 이때 재생이 일어나는 시간과 온도, 압력의 변화관계는 하기 표3과 같다.The wall flow honeycomb monolith was equipped with alumina and alumina-based platinum filter and palladium-based catalyst filter, respectively, in a trap, and then the Peter AV-B supercharger was mounted on the exhaust pipe of a single-cylinder diesel engine. The housing surrounding the catalyst trap from the engine exhaust pipe to the catalyst trap was fabricated and attached so that the filling thickness was 8 mm, and then calcium silicate powder was filled in the space between the exhaust device and the housing from the exhaust pipe to the catalyst trap. Using the additive-free diesel as a test fuel was tested under the same operating conditions as in Example 1, wherein the regeneration time, temperature, pressure change relationship is shown in Table 3.
[비교예2]Comparative Example 2
실시예 2의 장치에서 칼슘실리케이트 하우징을 제거한 후 실시예 2와 같은 조건에서 실험하였으며, 이때 재생이 일어나는 시간과 온도, 압력의 변화관계는 하기 표4와 같다.After the calcium silicate housing was removed from the apparatus of Example 2, the experiment was carried out under the same conditions as in Example 2, and the relationship between the time at which regeneration occurred, the temperature, and the pressure change was shown in Table 4 below.
[표 3]TABLE 3
[표 4]TABLE 4
상기 표3과 4에서 알 수 있듯이 본 발명의 촉매트랩만을 단독으로 사용하여 디젤 입자상물질을 제거하는 장치에 단열재를 부착하는 방법은 저파워, 저배압에서도 단시간에 쉽게 재생이 일어나므로 배압의 급격한 변화로 인한 여과재의 손상을 최소화할 수 있음을 알 수 있다. 따라서, 실제차량에 적용시 단열재를 부착하는 것만으로 저속, 저부하의 운전조건에서 촉매트랩이 재생되는 온도를 유지할 수 있어서, 2차 에너지를 공급하는 경우에 필요한 많은 장치를 제거할 수 있으므로 양산시 저렵하게 제작할 수 있는 장점이 있다.As can be seen from Tables 3 and 4, the method of attaching the insulating material to the apparatus for removing diesel particulate matter using only the catalyst trap of the present invention alone is low power, so that regeneration occurs easily in a short time even at low back pressure, so the rapid change in back pressure It can be seen that the damage caused by the filter medium can be minimized. Therefore, it is possible to maintain the temperature at which the catalyst trap is regenerated under low-speed and low-load operating conditions by simply attaching heat insulator when applied to the actual vehicle, thus eliminating many devices necessary for supplying secondary energy. There is an advantage that can be made.
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