KR20100016947A - Novel scr catalysts and after-treatment devices for diesel engine exhaust gas - Google Patents

Novel scr catalysts and after-treatment devices for diesel engine exhaust gas Download PDF

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KR20100016947A
KR20100016947A KR1020080076607A KR20080076607A KR20100016947A KR 20100016947 A KR20100016947 A KR 20100016947A KR 1020080076607 A KR1020080076607 A KR 1020080076607A KR 20080076607 A KR20080076607 A KR 20080076607A KR 20100016947 A KR20100016947 A KR 20100016947A
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module
scr catalyst
exhaust gas
diesel engine
scr
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KR1020080076607A
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KR101011760B1 (en
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한현식
김은석
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희성촉매 주식회사
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Priority to KR1020080076607A priority Critical patent/KR101011760B1/en
Priority to US13/056,284 priority patent/US20110126525A1/en
Priority to EP08793086A priority patent/EP2318674A1/en
Priority to PCT/KR2008/004572 priority patent/WO2010016631A1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust 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
    • F01N3/18Exhaust 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
    • F01N3/20Exhaust 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
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    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust 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
    • F01N3/18Exhaust 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
    • F01N3/20Exhaust 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
    • F01N3/2066Selective catalytic reduction [SCR]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/9404Removing only nitrogen compounds
    • B01D53/9409Nitrogen oxides
    • B01D53/9413Processes characterised by a specific catalyst
    • B01D53/9418Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
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    • B01D53/9459Removing 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
    • B01D53/9477Removing 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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    • F01N13/00Exhaust 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
    • F01N13/009Exhaust 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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    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust 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
    • F01N3/105General auxiliary catalysts, e.g. upstream or downstream of the main catalyst
    • F01N3/106Auxiliary oxidation catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/01Engine exhaust gases
    • B01D2258/012Diesel engines and lean burn gasoline engines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/92Chemical or biological purification of waste gases of engine exhaust gases
    • B01D53/94Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
    • B01D53/944Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts
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    • F01N2250/00Combinations of different methods of purification
    • F01N2250/02Combinations of different methods of purification filtering and catalytic conversion
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    • F01N2330/00Structure of catalyst support or particle filter
    • F01N2330/02Metallic plates or honeycombs, e.g. superposed or rolled-up corrugated or otherwise deformed sheet metal
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F01N2330/00Structure of catalyst support or particle filter
    • F01N2330/06Ceramic, e.g. monoliths
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    • F01N2370/00Selection of materials for exhaust purification
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    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust 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
    • F01N3/033Exhaust 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
    • F01N3/035Exhaust 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
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Abstract

PURPOSE: An SCR catalyst composition and an exhaust gas ejecting device using the same is provided to reach desired NOx conversion rate without oxidation catalyst and improve low-temperature activity. CONSTITUTION: An exhaust gas ejecting device using SCR catalyst composition comprises an SCR(Selective Catalytic Reduction) catalytic module, an oxidation catalyst module, and a CSF(Catalyzed Soot Filter) module. The SCR catalytic module comprises an injection unit positioned on the lower part of the diesel engine. The oxidation catalyst module is positioned on the lower part of the catalytic module. The CSF module is successively and serially positioned.

Description

NOx 전환율이 개선된 SCR 촉매조성물 및 이를 이용한 디젤엔진 배기가스 배출장치{Novel SCR catalysts and after-treatment devices for diesel engine exhaust gas}Noc SCR catalysts and after-treatment devices for diesel engine exhaust gas with improved NOC conversion

본 발명은 NOx 전환율이 개선된 SCR 촉매조성물 및 이를 이용한 디젤엔진 배기가스 후처리장치에 관한 것이며, 더욱 상세하게는 엔진으로부터 발생되는 NOx를 무해한 성분으로 유효하게 전환시킬 수 있는 성능을 가지는 SCR 촉매조성물 및 이를 이용하여 디젤엔진 배기가스 정화능력, 특히 질소산화물 정화능력이 개선된 배기가스 배출장치에 관한 것이다.The present invention relates to an SCR catalyst composition having improved NOx conversion rate and a diesel engine exhaust gas after-treatment apparatus using the same, and more particularly, to an SCR catalyst composition having an ability to effectively convert NOx generated from an engine into a harmless component. And it relates to an exhaust gas discharge device with improved diesel engine exhaust gas purification capacity, in particular nitrogen oxide purification capacity using the same.

디젤엔진은 고유의 높은 열효율 (즉, 우수한 연료 경제성) 및 저속에서의 높은 토크 (torque)로 인하여 운송수단 (vehicle)의 동력장치로서 우수한 유용성을 가지며, 디젤엔진은 매우 연료가 희박한 조건하에서 높은 A/F (공기 대 연료) 비에서 구동한다. 이러한 이유로 디젤엔진은 탄화수소 및 일산화탄소 전환율은 우수하나, 디젤 배기가스에는 질소 산화물 (NOx) 및 미립자의 방출이 높다. 질소산화물 (NOx) 및 미립자 양자는 무해성분으로 전환시키기 어려운 디젤 배기가스 성분이나, 최근에 환경문제와 관련되어 이들 방출 기준이 매우 높아지고 있다. 특히, 질소산 화물 제거를 위한 다양한 방안이 모색되고 있다. 선택적 촉매환원방식 (SCR, Selective Catalytic Reduction) 또는 질소산화물 흡착 (Lean NOx Trap, LNT) 촉매시스템이 언급될 수 있으나, 본 발명은 SCR 기술과 관련된 것이다. Diesel engines have excellent utility as vehicle powertrains due to their inherent high thermal efficiency (i.e. good fuel economy) and high torque at low speeds, and diesel engines have high A under very fuel-lean conditions. / F (air to fuel) drive in rain For this reason, diesel engines have good hydrocarbon and carbon monoxide conversion rates, but diesel emissions have high emissions of nitrogen oxides (NOx) and particulates. Both nitrogen oxides (NOx) and particulates are diesel exhaust components that are difficult to convert to harmless components, but these emission standards have recently been very high in relation to environmental issues. In particular, various methods for removing nitrogen oxides have been sought. Selective Catalytic Reduction (SCR) or Lean NOx Trap (LNT) catalyst systems may be mentioned, but the present invention relates to SCR technology.

도 1은 SCR 시스템을 개략적으로 도시한 것이다. SCR은 환원제인 암모니아 또는 요소를 사용하여 NOx를 아래와 같이 N2와 H2O로 환원한다.1 schematically illustrates an SCR system. SCR reduces NOx to N2 and H2O using ammonia or urea as reducing agents.

4NO + 4NH3 + O2 ⇒ 4N2 + 6H2O     4NO + 4NH3 + O2 ⇒ 4N2 + 6H2O

2NO2 + 4NH3 + O2 ⇒ 3N2 + 6H2O     2NO2 + 4NH3 + O2 ⇒ 3N2 + 6H2O

NO + NO2 + 2NH3 ⇒ 2N2 + 3H2O     NO + NO2 + 2NH3 ⇒ 2N2 + 3H2O

통상 SCR 시스템에서의 SCR 촉매로는 V2O5/TiO2 촉매가 적용되며, V2O5/TiO2 촉매의 작동온도 구간은 250-450℃ 이나, 특히 NO만이 존재할 경우 저온에서 성능이 확보되지 않는다. 그러나 배출가스 중에 NO2 성분이 많으면 성능이 향상되고 저온작동 구간도 확장되므로 SCR 시스템 상류(upstream)에 산화촉매를 설치하여 NO를 NO2 로 산화하여 NO2 농도를 높이는 방법이 사용된다. 반면 NO2/NO 비가 너무 높으면 도리어 성능이 떨어져 NO2/NO = 1 수준으로 유지하는 것이 가장 좋은 것으로 알려져 있다. 이러한 원리를 구현한 대표적인 특허 (이하, JMI 특허라 함)는 배기가스에서의 NOx환원 시스템 (PCT/GB/00292, WO 99/29809) 특허를 참조할 수 있으며, 도 2는 상기 참조특허의 시스템을 개략적으로 도시한 것이며, 이는 엔진으로부터 발생되는 NOx 중 NO 성분을 NO2로 전환시키는 산화촉매, 미립자필터, 환원제 주입 부 및 SCR 촉매가 순차적으로 구성된다. 이러한 배열의 SCR 시스템은 NOx 전환율을 80% 이상으로 달성하는 등의 효과가 있는 것으로 기재된다. 상기 JMI 특허에서 V2O5/WO3/TiO2 SCR 촉매가 적용되었다.In general, as the SCR catalyst in the SCR system, the V2O5 / TiO2 catalyst is applied, and the operating temperature range of the V2O5 / TiO2 catalyst is 250-450 ° C, but especially when only NO is present, performance is not secured at low temperatures. However, if there are many NO2 components in the exhaust gas, the performance is improved and the low-temperature operation section is extended. Therefore, an oxidation catalyst is installed upstream of the SCR system to oxidize NO to NO2 to increase the NO2 concentration. On the other hand, if the NO2 / NO ratio is too high, it is known that it is best to keep the NO2 / NO = 1 at the level. Representative patents embodying this principle (hereinafter referred to as JMI patents) may refer to patents for NOx reduction systems (PCT / GB / 00292, WO 99/29809) in exhaust gas, and FIG. It is shown schematically, which consists of an oxidation catalyst, a particulate filter, a reducing agent injection unit and an SCR catalyst sequentially converting NO components of the NOx generated from the engine to NO2. SCR systems of this arrangement are described as having an effect such as achieving an NOx conversion rate of 80% or more. In the JMI patent, a V2O5 / WO3 / TiO2 SCR catalyst was applied.

한편, 상기 JMI 특허에서 언급된 미립자를 감소시키기 위한 미립자필터는 촉매화 슈트 필터(Catalyzed Soot Filter, CSF)라고도 칭하는, 촉매화 디젤미립자 필터 (Catalyzed Diesel Particulate Filter, CDPF)이다. 개략적으로 설명하면, 이들 필터는 배기가스 미립자를 포집 및 재생하기 위한 구성으로, 일차적으로 미립자 포집을 위하여 허니컴 월-풀로우 (honeycomb wall-flow) 필터를 포함하여, 디젤 배기물로부터 미립자를 포집하는데 사용될 수 있는 다수의 공지된 필터 구조물이 있고, 필터에 포집되어 축적된 미립자는 연속적으로 또는 주기적으로 필터로부터 연소(재생)되어야 하므로, 이에 필요한 연소 온도를 저하시키는 수단으로 촉매가 제공되어 촉매화 디젤미립자 필터를 구성하여, CDPF 또는 CSF는 축적되는 미립자의 수동적 (passive) 연소 및 이에 따른 필터 재생과 함께 90% 이상의 미립자 감소를 효과를 얻을 수 있다.On the other hand, a particulate filter for reducing particulates mentioned in the JMI patent is a Catalyzed Diesel Particulate Filter (CDPF), also called a Catalyzed Soot Filter (CSF). Schematically, these filters are configured for capturing and regenerating exhaust particulates, including honeycomb wall-flow filters primarily for particulate capture, to collect particulates from diesel exhaust. There are a number of known filter structures that can be used, and particulates collected and accumulated in the filter must be burned (regenerated) from the filter continuously or periodically, so that a catalyst is provided as a means to lower the combustion temperature required for this catalyzed diesel. By constructing a particulate filter, the CDPF or CSF can benefit from at least 90% particulate reduction with passive combustion of the accumulating particulates and thus filter regeneration.

본 발명자들은 JMI 특허에서 언급된 SCR 촉매는 1) NO2/NO 비율에 따라서 NOx 전환율이 좌우되므로 SCR 촉매 상류에 배치되는 산화촉매능이 동시에 고려되어야 한다는 문제점, 2) SCR 저온활성이 낮아 저온에서는 NOx 전환율이 원활하지 않다는 문제점에 주목하여, 이를 해결하기 위하여 SCR 촉매를 새로이 디자인하기에 이르렀다. 본 발명자들은 다양한 촉매설계방법에 근거하여 새로운 SCR 촉매를 개발하였으며, 본 발명에 의한 SCR 촉매는 저온활성이 우수하여 엔진에서 배출되는 배기가스의 온도에서도 효과적으로 반응될 수 있을 뿐 아니라 산화촉매의 조력없이도 소망하는 NOx 전환율을 달성할 수 있음을 확인하였다. 따라서, 본 발명에 의한 SCR 촉매를 적용하면 종래 JMI 특허에서 구현되었던 배치와는 현저하게 차별되는 구성을 달성할 수 있고, 이에 따라 종래 SCR 촉매 및 상류에 배치되었던 산화촉매와의 연관성을 고려하지 아니하고도 NOx 전환율이 높은 디젤엔진 배기가스 배출장치를 구현할 수 있다. 도 3은 본 발명에 의해 달성될 수 있는 디젤엔진 배기가스 배출장치를 개략적으로 도시한 것이다.The inventors of the present invention have found that the SCR catalyst mentioned in the JMI patent has the following considerations: 1) NOx conversion rate depends on the NO2 / NO ratio, so that the oxidation catalyst capacity disposed upstream of the SCR catalyst should be considered at the same time. Paying attention to this inconvenient problem, the SCR catalyst has been newly designed to solve this problem. The present inventors have developed a new SCR catalyst based on various catalyst design methods, and the SCR catalyst according to the present invention has excellent low temperature activity and can be effectively reacted even at the temperature of the exhaust gas discharged from an engine, without the aid of an oxidation catalyst. It was found that the desired NOx conversion could be achieved. Therefore, applying the SCR catalyst according to the present invention can achieve a configuration that is remarkably different from the batch implemented in the conventional JMI patent, and thus without considering the association with the conventional SCR catalyst and the oxidation catalyst disposed upstream Also, a diesel engine exhaust gas discharge device having a high NOx conversion rate can be realized. Figure 3 schematically shows a diesel engine exhaust gas discharge apparatus that can be achieved by the present invention.

본 발명의 목적은 저온활성 및 NOx 전환율이 우수한 SCR 촉매조성물을 제공하는 것이다. 본 발명에 의한 SCR 촉매의 개선된 NOx 전환율로 인하여 종래 SCR 촉매 상류에 필연적으로 배치되어야 하는 산화촉매의 배치를 배제할 수 있다.An object of the present invention is to provide an SCR catalyst composition having excellent low temperature activity and NOx conversion rate. The improved NOx conversion of the SCR catalysts according to the present invention can preclude the placement of oxidation catalysts which must be inevitably disposed upstream of the conventional SCR catalyst.

본 발명의 다른 목적은 저온활성 및 NOx 전환율이 우수한 SCR 촉매를 적용한 디젤엔진 배기가스 배출장치를 제안하는 것이다.Another object of the present invention is to propose a diesel engine exhaust gas exhauster using an SCR catalyst having excellent low temperature activity and excellent NOx conversion rate.

상기 목적을 달성하기 위하여 본 발명은, 디젤엔진 하류에 배치된 인젝션 수단을 포함한 SCR 촉매모듈, 상기 촉매모듈 하류에 배치된 산화촉매모듈 및 연속하여 CSF 모듈이 직렬로 구성된 디젤엔진 배기가스 배출장치를 제안하는 것이다. In order to achieve the above object, the present invention provides a diesel engine exhaust gas exhaust system comprising an SCR catalyst module including an injection means disposed downstream of a diesel engine, an oxidation catalyst module disposed downstream of the catalyst module, and a CSF module serially arranged. I would suggest.

본 발명의 SCR 촉매조성물은 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu 또는 Fe 내포 - 제올라이트 ; 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu, Fe 또는 Si 내포 알루미나로 구성된 것을 특징으로 한다.The SCR catalyst composition of the present invention comprises Cu or Fe inclusion-zeolite, in which platinum, palladium and rhodium are impregnated alone or in combination of two components; It is characterized by consisting of Cu, Fe or Si inclusion alumina impregnated with platinum, palladium, rhodium alone or in combination of two components.

본 발명에 의한 SCR 촉매는 종래 디젤산화촉매에 의해 임의적으로 조절되어야 하였던 NO2/NOx 비율에 구속되지 않고도 높은 NOx 전환율을 저온에서 달성할 수 있으며, 이러한 SCR 촉매를 적용함으로써 디젤엔진 배기시스템 디자인에 유동성을 부여할 수 있는 효과가 있다.The SCR catalyst according to the present invention can achieve high NOx conversion at low temperature without being bound to the NO2 / NOx ratio, which had to be arbitrarily controlled by the conventional diesel oxidation catalyst, and by applying such SCR catalyst, fluidity in diesel engine exhaust system design There is an effect that can be given.

본 발명에 의한 배기 배출장치는 도 3에 도시된 바와 같다. 즉 SCR 촉매모듈-DOC(디젤산화촉매)모듈-CSF(촉매화 디젤미립자 필터)모듈 배열을 특징으로 한다. Exhaust exhaust apparatus according to the present invention is as shown in FIG. That is, the SCR catalyst module-DOC (diesel oxidation catalyst) module-CSF (catalyzed diesel particulate filter) module array is characterized by the arrangement.

본 명세서에서 배기가스 '하류'라 함은, 엔진을 기준으로 배기가스 흐름 방향을 언급하는 것이다. '모듈'이라 함은 하나의 기능을 수행하기 위한 최소 단위의 장치를 의미하는 것으로, 예를 들면 '촉매화 디젤미립자 필터 모듈'이라 함은 디젤 엔진에서 배출되는 입자를 포집하는 기능을 수행하기 위한 필터 장치를 의미하는 것이고, 'DOC모듈'이라 함은 디젤엔진에서 배출되는 탄화수소(HC) 또는 CO를 무해한 성분으로 산화시키기 위한 소위 디젤산화촉매가 코팅된 캐리어를 의미하는 것이다. Exhaust gas 'downstream' herein refers to the exhaust gas flow direction relative to the engine. 'Module' refers to a unit of the minimum unit for performing a function, for example, 'catalyzed diesel particulate filter module' means to collect the particles discharged from the diesel engine It means a filter device, 'DOC module' refers to a carrier coated with a so-called diesel oxidation catalyst for oxidizing hydrocarbon (HC) or CO emitted from the diesel engine into a harmless component.

본 발명에 의한 실시예에 의하면, 본 발명에 의한 배출장치는, 디젤엔진에서 배출되는 배기가스가 유입되어, 측면에서 유입되는 환원제에 의해 NOx 전환을 유도하는 SCR 촉매모듈, 상기 SCR 촉매모듈 하류에 배치되어 탄화수소 및 CO 산화를 유도하는 디젤산화촉매모듈, 및 연속하여 미립자를 포집하기 위한 촉매화 디젤미립자 모듈이 직렬 배치되는 디젤엔진 배기 배출장치로 구성된다. According to an embodiment of the present invention, the exhaust device according to the present invention, the SCR catalyst module for inducing NOx conversion by the reducing agent introduced from the exhaust gas discharged from the diesel engine, the side, downstream of the SCR catalyst module A diesel oxidation catalyst module arranged to induce hydrocarbon and CO oxidation, and a diesel engine exhaust exhaust device in which a catalytic diesel particulate module for continuously collecting particulates is arranged in series.

이하 각 요소들을 상세하게 기술한다.Each element is described in detail below.

1) SCR 촉매 모듈1) SCR Catalyst Module

본 발명에 의한 개선된 SCR 촉매는 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu 또는 Fe 내포 - 제올라이트; 또는 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu, Fe 또는 Si 내포 알루미나로 구성되며, 이러한 촉매는 코디어라이트와 같은 세라믹형 또는 스테인레스 강과 같은 내화성 금속형 캐리어에 코팅되어 SCR 촉매 모듈을 구성한다. 전형적인 캐리어(carrier)는, 전면 및 후면을 가지며 캐리어를 연장하여 그 전면 및 후면들을 연결하는 다수의 미세 채널을 가지는 '플로우 쓰로우(flow-through)'형 캐리어가 적용된다. 상기 SCR 촉 매 모듈에는 전단에 장착되는 환원제를 분무하는 공지의 인젝션 수단을 포함한다. 예를 들면, 이러한 인젝션 수단은 환원제로 작용되는 요소 또는 암모니아를 분무하기 위한 펌프 및 인젝션 노즐을 포함할 수 있다.The improved SCR catalysts according to the invention include Cu or Fe inclusion-zeolites in which platinum, palladium, rhodium are impregnated alone or in combination of two components; Or Cu, Fe or Si inclusion alumina impregnated with platinum, palladium, rhodium alone or in combination of two components, such catalysts are coated on a refractory metal carrier such as ceramic or stainless steel such as cordierite Configure the catalyst module. Typical carriers are 'flow-through' type carriers having a front side and a rear side and having a plurality of microchannels extending the carrier to connect the front side and the back side. The SCR catalyst module includes known injection means for spraying a reducing agent mounted at the front end. For example, such injection means may comprise a pump and an injection nozzle for spraying urea or ammonia acting as a reducing agent.

본 발명의 SCR 촉매모듈에 적용되는 SCR 촉매조성물 제조방법은 다음과 같다. 본 발명에서 적용되는 SCR 촉매조성물은, 5~10 중량 % 구리가 내포된 제올라이트에 0.5 중량 % 이하 백금이 함침되도록 슬러리를 제조 후 코디어라이트 및 금속형 캐리어에 코팅하여 건조, 소성과정으로 제조될 수 있다. 동일한 방법으로 5~10 중량 % 철이 내포된 제올라이트에 동일한 중량의 백금을 함침시켜 제조할 수 있다. 상기 제올라이트를 대신하여 알루미나를 담체로 제조할 수도 있으며, 이때 선택되는 알루미나는 Cu, Fe, 또는 Si가 내포된 알루미나가 바람직하다. SCR catalyst composition production method applied to the SCR catalyst module of the present invention is as follows. SCR catalyst composition to be applied in the present invention, after the slurry is prepared so that 5 to 10% by weight of platinum impregnated in copper containing 5 to 10% by weight of copper and coated on a cordierite and a metal carrier to be dried and produced by a sintering process Can be. In the same way it can be prepared by impregnating 5-10 wt% iron-containing zeolite with the same weight of platinum. Alumina may be prepared as a carrier in place of the zeolite, and the alumina selected herein is preferably alumina containing Cu, Fe, or Si.

본 발명에 의한 SCR 촉매의 NOx 전환성능을 실험하기 위하여, 종래 통상적인 SCR 촉매 (V2O5/TiO2) 단독, 종래 SCR 촉매 및 DOC 촉매(Pt/Al2O3)의 조합, 및 본 발명에 의한 신규 SCR 촉매를 대상으로 NH3/NOx 비율을 1로 설정하여 NOx 전환율을 조사하여, 도 4에 도시하였다. 이에 의하면, 본 발명에 의한 SCR 촉매는 실질적으로 디젤엔진에서 나오는 배가가스의 온도에 해당하는 250 내지 280℃ 범위에서 매우 효과적으로 NOx를 전환시킬 수 있음을 확인할 수 있다. In order to test the NOx conversion performance of the SCR catalyst according to the present invention, the conventional conventional SCR catalyst (V2O5 / TiO2) alone, a combination of the conventional SCR catalyst and DOC catalyst (Pt / Al2O3), and the novel SCR catalyst according to the present invention The NH3 / NOx ratio was set to 1, and the NOx conversion rate was examined as shown in FIG. 4. According to this, it can be seen that the SCR catalyst according to the present invention can effectively convert NOx in the range of 250 to 280 ° C. substantially corresponding to the temperature of the doubling gas from the diesel engine.

구체적으로는 디젤엔진 배기가스 온도에 해당되는 250℃~280℃ 범위에서, 본 발명에 의한 SCR 촉매를 적용한 결과, 약 90% 이상의 NOx 전환율을 달성할 수 있었으며, 이러한 개선된 효율은 종래 SCR 촉매 단독으로 적용한 경우 얻을 수 있었던 60~80% NOx 전환율과 대비된다. 또한, JMI 특허에서 NO2/NO 비율을 최적으로 설정 하기 위하여 SCR 전단에 필수적으로 구비되었던 DOC 조합의 경우 얻을 수 있었던 80% 내외의 효율과 대비할 때 본 발명에 의한 신규한 SCR 촉매는 전환율에 있어서 상당한 효과를 보이고 있다.Specifically, in the range of 250 ° C. to 280 ° C. corresponding to the diesel engine exhaust gas temperature, as a result of applying the SCR catalyst according to the present invention, NOx conversion of about 90% or more was achieved. This contrasts with the 60-80% NOx conversion rate that would have been achieved with the application. In addition, the novel SCR catalysts according to the present invention exhibit significant conversion in contrast to the 80% efficiency achieved with DOC combinations, which were essential for SCR shearing in order to optimally set the NO2 / NO ratio in the JMI patent. It is showing effect.

2) 디젤산화촉매모듈(Diesel Oxidation Catalyst, DOC)2) Diesel Oxidation Catalyst (DOC)

DOC는 디젤엔진 배기가스중 HC와 CO를 산화시켜 무해한 성분으로 전환시키며, 입자상 물질(PM)의 용해성유기물질인 SOF(soluble organic fraction) 성분도 50-80%를 제거하며 또한 디젤악취(diesel odor)와 흑연(black smoke)도 감소시키며 촉매로는 백금(platinum;Pt)이나 팔라듐(palladium;Pd)을 사용하며, 예를 들면 Pt/AlsO3 촉매는 대표적인 DOC 촉매로 알려져 있다. 본 발명에서 적용되는 DOC 촉매는 공지의 모듈을 적용할 수 있는 것이다.DOC oxidizes HC and CO in diesel exhaust gas and converts it into harmless components, removes 50-80% of soluble organic fraction (SOF), which is a soluble organic substance of particulate matter (PM), and also diesel odor. Also, black smoke is reduced and platinum (Pt) or palladium (Pd) is used as the catalyst. For example, Pt / AlsO3 catalyst is known as a representative DOC catalyst. DOC catalyst to be applied in the present invention is to apply a known module.

3) 촉매화 디젤미립자모듈 (Catalyzed Diesel Particulate Filter, CDPF, 또는 CSF)3) Catalyzed Diesel Particulate Filter, CDPF, or CSF

통상 디젤미립자모듈은 디젤엔진에서 배출되는 입자상 물질(PM)을 포집하기 위한 필터이며, 세라믹 모노리스필터(Ceramic Monolith Filter), 세라믹 파이버 필터(Ceramic Fiber Filter), 금속필터 (Sintered Metal Filter) 등 다수의 공지된 필터구조물이 있으나, 가장 바람직한 모듈로는 다공질의 코디어라이트 세라믹으로 구성된 세라믹 벽면-유동필터라고도 하는 세라믹 모노리스 필터이며, 모듈 채널입구 및 출구가 교대로 막혀 있으며, 입구에서 유입된 배출가스는 출구가 막혀 있으 므로 다공질벽을 통과하여 이웃 채널 출구로 빠져나가게 되며, 이때 입자상 물질은 유입된 채널에 포집되는 구조이다. 도 4에 세라믹 모노리스 입구 정면도 및 배기가스 흐름 방향 단면도가 도시되어 있다. 벽면의 다공질 크기는 포집 입자 크기 및 엔진 배압에 직접적인 영향을 주기 때문에 모듈 선택에 있어서 중요한 인자이며 대략 10um이며, 이러한 다공질 구조에서 PM 입경 0.01um부터 포집할 수 있으며, PM 저감율은 85% 이상인 것으로 선택된다. 이러한 필터에 포집된 PM은 가능하면 단시간 내에 태워서 필터가 다시 PM을 포집할 수 있도록 하는 재생(regeneration) 과정이 요구되며, 특히 포집된 PM 점화 온도인 550-600℃를 250℃정도까지 낮추기 위하여 필터 채널에 촉매를 적용하는 방식에 따라 CRT (Continuous Regeneration Trap) 및 DPX 모듈이 적용될 수 있다. 제안 가능한 모듈은 엥겔하드사에서 입수가능한 250g/ft3 ZrO2, 500g/ft3 CeO2, Pt 75g/ft3의 CSF 12 촉매화 디젤미립자모듈이 예시될 수 있다. 본 발명에서 적용되는 DOC 촉매는 공지의 모듈을 적용할 수 있는 것이다.In general, the diesel particulate module is a filter for collecting particulate matter (PM) discharged from the diesel engine, a number of ceramic monolith filter (Ceramic Monolith Filter), ceramic fiber filter (Seramic Fiber Filter), metal filter (Sintered Metal Filter) Although there are known filter structures, the most preferred module is a ceramic monolith filter, also called a ceramic wall-flow filter, composed of porous cordierite ceramic, the channel inlet and outlet of the module are alternately blocked, and the exhaust gas flowing from the inlet is Since the outlet is blocked, it passes through the porous wall and exits to the neighboring channel outlet, where particulate matter is collected in the inlet channel. 4 is a front view of the ceramic monolith inlet and a cross sectional view of the exhaust gas flow direction. Since the porous size of the wall directly affects the trapped particle size and the engine back pressure, it is an important factor in the module selection, which is approximately 10 μm. In such a porous structure, the porous size can be collected from the 0.01 μm PM particle size and the PM reduction rate is 85% or more. do. PM collected in such a filter is required to be regenerated in a short time if possible so that the filter can collect PM again. In particular, to lower the collected PM ignition temperature 550-600 ° C to about 250 ° C. Depending on how the catalyst is applied to the channel, the Continuous Regeneration Trap (CRT) and DPX modules may be applied. The proposed module may be illustrated as 250 g / ft3 ZrO2, 500g / ft3 CeO2, Pt 75g / ft3 CSF 12 catalyzed diesel particulate module available from Engelhard. DOC catalyst to be applied in the present invention is to apply a known module.

도 1은 SCR 시스템의 개략도이고, 1 is a schematic diagram of an SCR system,

도 2는 종래 JMI 특허에서의 디젤엔진 배기시스템를 개략적으로 도시한 것이며,Figure 2 schematically shows a diesel engine exhaust system in the conventional JMI patent,

도 3은 본 발명에 의한 디젤엔진 배기시스템을 도시한 것이며,Figure 3 shows a diesel engine exhaust system according to the present invention,

도 4는 비교 촉매들 및 본 발명에 의한 신규 촉매조성물에 대하여 NOx 전환율을 측정한 그래프이다.Figure 4 is a graph measuring the NOx conversion rate for the comparative catalysts and the novel catalyst composition according to the present invention.

Claims (5)

디젤엔진 하류에 배치된 인젝션 수단을 포함한 SCR 촉매모듈, 상기 촉매모듈 하류에 배치된 산화촉매모듈 및 연속하여 CSF 모듈이 직렬로 구성된, NOx 전환율을 개선하는 디젤엔진 배기가스 배출장치.An SCR catalyst module including an injection means disposed downstream of a diesel engine, an oxidation catalyst module disposed downstream of the catalyst module, and a CSF module serially arranged in series, thereby improving a NOx conversion rate. 제1항에 있어서, 상기 SCR 촉매모듈에 적용되는 SCR 촉매는, 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu 또는 Fe 내포 - 제올라이트 ; 또는 백금, 파라듐, 로듐이 단독 또는 이성분 조합으로 함침된, Cu, Fe 또는 Si 내포 알루미나로 구성된 것을 특징으로 하는, NOx 전환율을 개선하는 디젤엔진 배기가스 배출장치.The SCR catalyst according to claim 1, wherein the SCR catalyst applied to the SCR catalyst module comprises: Cu or Fe inclusion-zeolite impregnated with platinum, palladium or rhodium alone or in combination of two components; Or diesel, exhaust gas improving apparatus for NOx conversion, characterized in that it is composed of Cu, Fe or Si-containing alumina impregnated with platinum, palladium, rhodium alone or in combination of two components. 제2항에 있어서, 상기 촉매는 세라믹형 또는 스테인레스 강의 내화성 금속형 캐리어에 코팅되는 것을 특징으로 하는, NOx 전환율을 개선하는 디젤엔진 배기가스 배출장치.3. The diesel engine exhaust gas exhaust system according to claim 2, wherein the catalyst is coated on a refractory metal carrier of ceramic type or stainless steel. 제2항에 있어서, 상기 SCR 촉매는, 5~10 중량 % 구리 또는 철이 내포된 제올라이트에 백금, 파라듐 또는 로듐 단독 또는 복수의 성분이 0.5 중량 % 이하 함침되는 것을 특징으로 하는, NOx 전환율을 개선하는 디젤엔진 배기가스 배출장치.The method of claim 2, wherein the SCR catalyst, 5-10 wt% copper or iron impregnated with a zeolite containing platinum, palladium or rhodium alone or a plurality of components impregnated 0.5x% by weight, improving the NOx conversion rate Diesel engine exhaust gas discharge device. 제2항에 있어서, 상기 SCR 촉매는, 5~10 중량 % 구리 또는 철 또는 규소가 내포된 알루미나에 백금, 파라듐 또는 로듐 단독 또는 복수의 성분이 0.5 중량 % 이하 함침되는 것을 특징으로 하는, NOx 전환율을 개선하는 디젤엔진 배기가스 배출장치.According to claim 2, The SCR catalyst, NOx, characterized in that 5 to 10% by weight of alumina containing copper or iron or silicon impregnated with platinum, palladium or rhodium alone or a plurality of components 0.5% by weight or less, NOx Diesel engine exhaust emissions improve conversion.
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