KR101068543B1 - Mixtured Catalyst For Emission Reduction Device Of Diesel Vehicles And Preparing Method For The Same - Google Patents

Mixtured Catalyst For Emission Reduction Device Of Diesel Vehicles And Preparing Method For The Same Download PDF

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KR101068543B1
KR101068543B1 KR1020090038462A KR20090038462A KR101068543B1 KR 101068543 B1 KR101068543 B1 KR 101068543B1 KR 1020090038462 A KR1020090038462 A KR 1020090038462A KR 20090038462 A KR20090038462 A KR 20090038462A KR 101068543 B1 KR101068543 B1 KR 101068543B1
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exhaust gas
catalyst
mixed catalyst
diesel vehicle
present
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KR20100119378A (en
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박종수
황경란
이영재
김동국
조성호
이춘부
유경선
최승훈
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한국에너지기술연구원
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Priority to CN200980150069.XA priority patent/CN102245295B/en
Priority to US13/139,500 priority patent/US20110258994A1/en
Priority to PCT/KR2009/007422 priority patent/WO2010068059A2/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56Platinum group metals
    • B01J23/64Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/652Chromium, molybdenum or tungsten
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • 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
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Chemical Kinetics & Catalysis (AREA)
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Abstract

본원발명은 디젤 차량의 배출가스 저감장치용 혼합촉매에 관한 것이다. 상세하게, 상기 혼합촉매는, Ti, Zr, Si, Al 및 Ce중에서 선택된 1종 또는 2종 이상의 금속의 산화물, 백금과 텅스텐의 복합활성금속, 베타-제올라이트, 무기바인더, 분산제를 포함하며, 상기 금속의 산화물의 평균입경은 복합활성금속의 평균입경보다 큰 것을 특징으로 한다.The present invention relates to a mixed catalyst for reducing the exhaust gas of a diesel vehicle. In detail, the mixed catalyst includes an oxide of one or two or more metals selected from Ti, Zr, Si, Al, and Ce, a composite active metal of platinum and tungsten, beta-zeolite, an inorganic binder, and a dispersant. The average particle diameter of the oxide of the metal is characterized by being larger than the average particle diameter of the composite active metal.

또한, 본원발명은 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법을 제공한다. 상세하게, 상기 제조방법은 Ti, Zr, Si, Al 및 Ce으로 구성된 그룹에서 선택된 1종 또는 2종 이상의 금속의 산화물에 백금과 텅스텐의 복합활성금속이 용해된 용액을 담지하여 혼합물 분말을 준비하는 단계, 상기 혼합물 분말을 건조 및 소성하여 촉매 분말을 얻는 단계 및 상기 촉매 분말을 베타-제올라이트, 무기바인더 및 분산제와 혼합하여 디젤 차량의 배출가스 저감장치용 혼합촉매를 얻는 단계를 포함한다.In addition, the present invention provides a method for producing a mixed catalyst for reducing the exhaust gas of a diesel vehicle. In detail, the preparation method is to prepare a mixture powder by supporting a solution in which a composite active metal of platinum and tungsten is dissolved in an oxide of one or two or more metals selected from the group consisting of Ti, Zr, Si, Al, and Ce. Step, drying and calcining the mixture powder to obtain a catalyst powder and mixing the catalyst powder with beta-zeolite, inorganic binder and dispersant to obtain a mixed catalyst for the exhaust gas reduction device of a diesel vehicle.

본원발명의 디젤 차량의 배출가스 저감장치용 혼합촉매로 코팅된 배출가스 저감장치는 배출가스와 같은 반응물질과 접촉할 수 있는 넓은 면적을 확보할 수 있으므로, 미연소 탄화수소, 일산화탄소 및 일산화질소와 같은 오염물질의 산화율을 증진시키고, PM(배기가스 중의 입자상 물질) 제거효율을 높일 수 있다.The exhaust gas reducing device coated with the mixed catalyst for the exhaust gas reducing device of the diesel vehicle of the present invention can secure a large area in contact with a reactant such as the exhaust gas, and thus, such as unburned hydrocarbons, carbon monoxide and nitrogen monoxide. The oxidation rate of contaminants can be improved, and the PM (particulate matter in exhaust gas) removal efficiency can be improved.

촉매 코팅, 디젤산화촉매, 디젤 입자상 필터, 일산화질소 산화, PM 제거효율, 후처리 기술 Catalyst coating, diesel oxidation catalyst, diesel particulate filter, nitrogen monoxide oxidation, PM removal efficiency, post treatment technology

Description

디젤 차량의 배출가스 저감장치용 혼합촉매와 그 제조방법{Mixtured Catalyst For Emission Reduction Device Of Diesel Vehicles And Preparing Method For The Same}Mixed Catalyst For Emission Reduction Device Of Diesel Vehicles And Preparing Method For The Same}

본원발명은 디젤 차량의 배출가스 저감장치용 혼합촉매 및 그 제조방법에 관한 것이다. 상기 혼합촉매로 코팅된 배출가스 저감장치는 배출가스와 같은 반응물질과 접촉할 수 있는 넓은 면적을 확보할 수 있으므로, 미연소 탄화수소, 일산화탄소 및 일산화질소와 같은 오염물질의 산화율이 증진되고, PM 제거효율이 높다.The present invention relates to a mixed catalyst for reducing exhaust gas of a diesel vehicle and a method of manufacturing the same. The exhaust gas reducing device coated with the mixed catalyst can secure a large area in contact with the reactants such as the exhaust gas, thereby improving the oxidation rate of contaminants such as unburned hydrocarbons, carbon monoxide and nitrogen monoxide, and removing PM. High efficiency

일반적으로 자동차 배출가스는 엔진에서 혼합기 연소에 의해 생성되어 배기 파이프를 통해 대기 중으로 방출되는 가스를 말한다. 이러한 배출가스에는 일산화탄소(CO), 질소산화물(NOx), 미연소탄화수소(HC) 등 인체에 유해한 물질이 다량 포함되어 있다. 따라서 자동차 배출가스로 인한 대기오염을 방지하는 것이 환경위생상 중요한 문제로 대두되고 있으며, 자동차에서 배출가스를 배출하기 전에 반드시 정화처리를 하도록 규제하고 있다.Automotive emissions generally refer to gases produced by mixer combustion in an engine and released into the atmosphere through exhaust pipes. These emissions include a large amount of substances harmful to the human body, such as carbon monoxide (CO), nitrogen oxides (NOx), unburned hydrocarbons (HC). Therefore, prevention of air pollution caused by automobile emissions has emerged as an important issue for environmental hygiene, and regulations are required to clean up before emitting emissions from automobiles.

한편, 유해 배출가스의 배출이 상대적으로 많은 디젤 차량의 경우, 연비, 출력면에서 우수함에도 불구하고 가솔린 차량과는 달리 배출가스 내에 질소산화물과 입자상물질(PM, Particulate Matter)이 상당히 많이 함유되어 있다. 이와 같이 디젤 차량에 있어서는 공기가 대부분의 운전조건에서 충분한 상태로 연소되기 때문에 일산화탄소와 탄화수소는 가솔린 차량에 비해 아주 적게 배출되나, 질소산화물과 입자상물질이 많이 배출된다. 또한, 최근 입자상물질은 대기를 오염시키는 가장 주된 원인으로 규명되었고, 인체에도 많은 해를 입히는 것으로 판명되고 있다. 따라서, 디젤 차량의 배출가스 저감기술은 질소산화물과 매연(soot)을 포함하는 입자상물질의 저감에 중점을 두어 연구되고 있다.On the other hand, diesel vehicles, which have relatively high emissions of harmful emissions, have excellent amounts of nitrogen oxides and particulate matter (PM, Particulate Matter) in the exhaust gases, unlike gasoline vehicles, despite excellent fuel economy and output. . As such, in a diesel vehicle, carbon monoxide and hydrocarbons are emitted much less than gasoline vehicles because air is sufficiently burned under most driving conditions, but nitrogen oxides and particulate matter are emitted. In addition, particulate matter has recently been identified as the main cause of air pollution, and has been found to cause many harms to the human body. Therefore, the emission reduction technology of diesel vehicles has been studied with a focus on the reduction of particulate matter including nitrogen oxides and soot (soot).

최근 디젤 차량의 배출기준 강화에 대응하기 위하여 후처리기술로 매연여과필터에 관한 연구가 활발하다. 또한, 상기 매연여과필터가 입자상물질의 제거효율을 높일 수 있는 디젤 차량의 배출가스 저감장치용 혼합촉매에 관한 연구도 활발히 진행되고 있다.Recently, research on soot filtration filters has been actively conducted as a post-treatment technology to cope with strengthening emission standards of diesel vehicles. In addition, studies have been actively conducted on the mixed catalyst for the exhaust gas reducing device of a diesel vehicle in which the particulate filter can increase the removal efficiency of particulate matter.

상기의 문제점을 해결하기 위한 본원발명은, 디젤 차량의 배출가스 저감장치에 코팅되어 인체에 유해한 미연소탄화수소, 일산화탄소, 질소산화물 및 PM(배기가스 중의 입자상 물질)의 산화효율성 및 30nm이하의 나노탄소입자의 포집효율성을 증진시킬수 있는 디젤 차량의 배출가스 저감장치용 혼합촉매를 제공하는 것을 목적으로 한다.The present invention for solving the above problems, coated on the exhaust gas reduction device of diesel vehicles, the oxidation efficiency of unburned hydrocarbons, carbon monoxide, nitrogen oxides and PM (particulate matter in exhaust gas) harmful to the human body and nano carbon below 30nm An object of the present invention is to provide a mixed catalyst for the exhaust gas reducing device of a diesel vehicle that can improve the particle collection efficiency.

상기의 목적을 달성하기 위한 본원발명은, Ti, Zr, Si, Al 및 Ce중에서 선택된 1종 또는 2종 이상의 금속의 산화물, 백금과 텅스텐의 복합활성금속, 베타-제올라이트, 무기바인더, 분산제를 포함하는 디젤 차량의 배출가스 저감장치용 혼합촉매를 제공한다. 바람직하게, 상기 금속의 산화물의 평균입경은 복합활성금속의 평균입경보다 큰 것을 특징으로 한다.The present invention for achieving the above object, an oxide of one or two or more metals selected from Ti, Zr, Si, Al and Ce, a composite active metal of platinum and tungsten, beta-zeolite, inorganic binder, dispersant It provides a mixed catalyst for the exhaust gas reducing device of the diesel vehicle. Preferably, the average particle diameter of the oxide of the metal is larger than the average particle diameter of the composite active metal.

또한, 상기의 목적을 달성하기 위한 본원발명은 Ti, Zr, Si, Al 및 Ce으로 구성된 그룹에서 선택된 1종 또는 2종 이상의 금속의 산화물에 백금과 텅스텐의 복합활성금속이 용해된 용액을 담지하여 혼합물 분말을 준비하는 단계, 상기 혼합물 분말을 건조 및 소성하여 촉매 분말을 얻는 단계 및 상기 촉매 분말을 베타-제올라이트, 무기바인더 및 분산제와 혼합하여 디젤 차량의 배출가스 저감장치용 혼합촉매를 얻는 단계를 포함하는 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법 을 제공한다.In addition, the present invention for achieving the above object is to support a solution in which a composite active metal of platinum and tungsten is dissolved in an oxide of one or two or more metals selected from the group consisting of Ti, Zr, Si, Al and Ce Preparing a mixture powder, drying and firing the mixture powder to obtain a catalyst powder, and mixing the catalyst powder with beta-zeolite, an inorganic binder and a dispersant to obtain a mixed catalyst for an exhaust gas reducing device of a diesel vehicle. It provides a method for producing a mixed catalyst for the exhaust gas reducing device of a diesel vehicle comprising.

본원발명의 디젤 차량의 배출가스 저감장치용 혼합촉매를 배출가스 저감장치에 코팅할 경우, 입경이 큰 베타-제올라이트의 표면에 입경이 작은 본원발명의 혼합촉매가 고르게 분산되어, 넓은 촉매면적을 제공할 수 있다. 그 결과, 본원발명의 혼합촉매가 코팅된 배출가스 저감장치는 인체에 유해한 미연소탄화수소, 일산화탄소, 질소산화물 및 PM(배기가스 중의 입자상 물질)의 산화효율성 및 30nm이하의 나노탄소입자의 포집효율성을 증진시킬 수 있게 된다. When the mixed catalyst for the exhaust gas reducing device of the diesel vehicle of the present invention is coated on the exhaust gas reducing device, the mixed catalyst of the small particle of the present invention is uniformly dispersed on the surface of the beta-zeolite having a large particle size, thereby providing a wide catalyst area. can do. As a result, the exhaust gas reducing device coated with the mixed catalyst of the present invention is capable of reducing the oxidation efficiency of unburned hydrocarbons, carbon monoxide, nitrogen oxides and PMs (particulate matter in exhaust gas) and the collection efficiency of nanocarbon particles of 30 nm or less, which are harmful to the human body. It can be promoted.

본원발명은 디젤 차량의 배출가스 저감장치용 혼합촉매에 관한 것으로서, Ti, Zr, Si, Al 및 Ce중에서 선택된 1종 또는 2종 이상의 금속의 산화물, 백금과 텅스텐의 복합활성금속, 베타-제올라이트, 무기바인더, 분산제를 포함한다. The present invention relates to a mixed catalyst for the exhaust gas reducing device of a diesel vehicle, an oxide of one or two or more metals selected from Ti, Zr, Si, Al and Ce, a composite active metal of platinum and tungsten, beta-zeolite, Inorganic binder and dispersant.

상기 금속산화물의 평균입경은 복합활성금속의 평균입경보다 크며, 평균입경이 서로 다르기 때문에 본원발명의 혼합촉매가 디젤 차량의 배출가스 저감장치에 코팅되면 상기 혼합촉매와 배출가스 간의 접촉면적을 향상시킬 수 있다. 그 결과, 상기 혼합촉매로 코팅된 디젤 차량의 배출가스 저감장치는 인체에 유해한 PM(Particulate Matter, 배기가스 중의 입자상 물질)의 산화효율성 및 30nm이하의 나노탄소입자의 포집효율성을 증진시킬 수 있게 된다. Since the average particle diameter of the metal oxide is larger than the average particle diameter of the composite active metal, and the average particle diameter is different from each other, when the mixed catalyst of the present invention is coated on the exhaust gas reducing device of a diesel vehicle, the contact area between the mixed catalyst and the exhaust gas may be improved. Can be. As a result, the exhaust gas reduction device of the diesel vehicle coated with the mixed catalyst can improve the oxidation efficiency of PM (Particulate Matter) harmful to the human body and the collection efficiency of nano carbon particles of 30 nm or less. .

상기 금속의 산화물의 평균입경은 0.1 ~ 20㎛ 이 될 수 있다. 바람직하게, 상기 금속의 산화물의 평균입경은 0.3 ~ 2㎛ 이 될 수 있다.The average particle diameter of the oxide of the metal may be 0.1 ~ 20㎛. Preferably, the average particle diameter of the oxide of the metal may be 0.3 ~ 2㎛.

상기 복합활성금속의 평균입경은 0.01 ~ 5.0㎛ 이 될 수 있다. 바람직하게, 상기 복합활성금속의 평균입경은 0.02 ~ 1.0㎛ 이 될 수 있다. The average particle diameter of the composite active metal may be 0.01 ~ 5.0㎛. Preferably, the average particle diameter of the composite active metal may be 0.02 ~ 1.0㎛.

상기 무기바인더는 알루미나, 티타니아 또는 실리콘을 포함할 수 있다. The inorganic binder may comprise alumina, titania or silicon.

상기 분산제는 물 또는 알코올이 될 수 있다.The dispersant may be water or alcohol.

상기 금속의 산화물과 복합활성금속은 10 ~ 90 : 90 ~ 10 의 중량비로 혼합될 수 있다. 바람직하게, 상기 금속의 산화물과 복합활성금속은 25 ~ 65 : 35 ~ 75 의 중량비로 혼합될 수 있다.The metal oxide and the composite active metal may be mixed in a weight ratio of 10 to 90:90 to 10. Preferably, the oxide of the metal and the composite active metal may be mixed in a weight ratio of 25 to 65: 35 to 75.

또한, 본원발명은 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법에 관한 것이다. 상세하게, 상기 제조방법은 Ti, Zr, Si, Al 및 Ce으로 구성된 그룹에서 선택된 1종 또는 2종 이상의 금속의 산화물에 백금과 텅스텐의 복합활성금속이 용해된 용액을 담지하여 혼합물 분말을 준비하는 단계, 상기 혼합물 분말을 건조 및 소성하여 촉매 분말을 얻는 단계 및 상기 촉매 분말을 베타-제올라이트, 무기바인더 및 분산제와 혼합하여 디젤 차량의 배출가스 저감장치용 혼합촉매를 얻는 단계를 포함한다.In addition, the present invention relates to a method for producing a mixed catalyst for reducing the exhaust gas of a diesel vehicle. In detail, the preparation method is to prepare a mixture powder by supporting a solution in which a composite active metal of platinum and tungsten is dissolved in an oxide of one or two or more metals selected from the group consisting of Ti, Zr, Si, Al, and Ce. Step, drying and calcining the mixture powder to obtain a catalyst powder and mixing the catalyst powder with beta-zeolite, inorganic binder and dispersant to obtain a mixed catalyst for the exhaust gas reduction device of a diesel vehicle.

상기 건조는 105℃에서 12시간동안 공기분위기에서 실행하며, 상기 소성은 550℃의 공기분위기에서 실행하는 것이 바람직하다.The drying is carried out in an air atmosphere for 12 hours at 105 ℃, the firing is preferably carried out in an air atmosphere of 550 ℃.

이하에서, 본원발명의 바람직한 제조예, 실시예 및 비교예를 참조하여 상세히 설명한다. 아래의 제조예, 실시예 및 비교예는 본원발명의 내용을 이해하기 위해 제시된 것일 뿐이며 당해 분야에서 통상의 지식을 가진 자라면 본원발명의 기술적 사상 내에서 많은 변형이 가능할 것이다. 따라서 본원발명의 권리범위가 이러한 제조예, 실시예 및 비교예에 한정되는 것으로 해석되어서는 안 된다.Hereinafter, with reference to the preferred production examples, examples and comparative examples of the present invention will be described in detail. The following Preparation Examples, Examples and Comparative Examples are only presented to understand the content of the present invention, and those skilled in the art will be capable of many modifications within the technical spirit of the present invention. Therefore, the scope of the present invention should not be construed as being limited to these preparation examples, examples and comparative examples.

<제조예 1> : 디젤 차량의 배출가스 저감장치용 혼합촉매Production Example 1 Mixing Catalyst for Emission Reduction Device for Diesel Vehicle

Ti의 산화물인 이산화티탄(TiO2)을 105℃에서 12시간동안 건조하여, 흡착되어 있는 수분 및 휘발성 유기물질을 제거한 후, 상온으로 냉각하여, 순수한 이산화티탄 500g을 준비하였다.Titanium dioxide (TiO 2 ), which is an oxide of Ti, was dried at 105 ° C. for 12 hours to remove adsorbed moisture and volatile organics, and then cooled to room temperature to prepare 500 g of pure titanium dioxide.

다음으로, 10g의 H2PtCl6·xH2O(Aldrich Co.)과, 25g의 Ammonium Tungstate(Aldrich Co.)를 증류수에 용해하여 복합활성금속이 용해된 용액을 준비하였다.Next, 10 g of H 2 PtCl 6 .xH 2 O (Aldrich Co.) and 25 g of Ammonium Tungstate (Aldrich Co.) were dissolved in distilled water to prepare a solution in which the composite active metal was dissolved.

그 후, 상기 순수한 이산화티탄에 복합활성금속이 용해된 용액을 담지하여 혼합물 분말을 준비하였다. 상기 혼합물 분말을 105℃에서 12시간동안 공기분위기에서 건조한 후, 550℃의 공기분위기에서 소성하여 350g의 촉매 분말(Pt-W/TiO2)을 얻었다.Thereafter, a mixture powder was prepared by supporting a solution in which the composite active metal was dissolved in pure titanium dioxide. The mixture powder was dried in an air atmosphere at 105 ° C. for 12 hours, and then calcined in an air atmosphere at 550 ° C. to obtain 350 g of catalyst powder (Pt-W / TiO 2 ).

상기 Pt-W/TiO2을 attrition mill에서 10분 동안 분쇄하여 평균입경이 0.05 ㎛ 이하가 되도록 하였다. 분쇄된 Pt-W/TiO2을 평균 입경이 0.5㎛ 이하의 베타-제올라이트 150g과 알루미나 졸 166g 및 증류수 780g과 혼합하여 본원발명의 디젤차량의 배출가스 저감장치용 혼합촉매를 얻었다. 상기 알루미나 졸은 무기바인더로서 사용하였고, 상기 증류수는 분산제로서 사용하였다. The Pt-W / TiO 2 was ground in an attrition mill for 10 minutes to have an average particle diameter of 0.05 μm or less. The pulverized Pt-W / TiO 2 was mixed with 150 g of beta-zeolite having an average particle diameter of 0.5 μm or less, 166 g of alumina sol, and 780 g of distilled water to obtain a mixed catalyst for an exhaust gas reducing device of a diesel vehicle of the present invention. The alumina sol was used as an inorganic binder and the distilled water was used as a dispersant.

<실시예 1> : 본원발명의 혼합촉매를 이용한 DOC 지지체/세라믹 필터의 코팅Example 1 Coating of DOC Support / Ceramic Filter Using Mixed Catalyst of the Present Invention

본 실시예에서는, 상기 제조예 1에서 제조한 본원발명의 디젤 차량의 배출가스 저감장치용 혼합촉매를 이용하여 디젤 차량의 배출가스 저감장치의 일종인 코디어라이트 재질의 DOC 지지체/세라믹 필터를 코팅하였다. 상기 DOC는 디젤산화촉매(Disel Oxidation catalyst)를 말한다.In this embodiment, the DOC support / ceramic filter made of cordierite, which is a kind of exhaust gas reducing device of a diesel vehicle, is coated by using a mixed catalyst for the exhaust gas reducing device of the diesel vehicle of the present invention manufactured in Preparation Example 1 above. It was. The DOC refers to a diesel oxidation catalyst.

먼저, DOC 지지체/세라믹 필터 단위부피(1L)당, 제조예 1의 디젤차량의 배출가스 저감장치용 혼합촉매 60g 이 담지되도록 washcoating 하였다.First, per unit volume (1L) of the DOC support / ceramic filter, washcoating was carried so that 60 g of the mixed catalyst for the exhaust gas reducing device of the diesel vehicle of Preparation Example 1 was supported.

다음으로, 상기 DOC 지지체/세라믹 필터를 80℃에서 28시간 동안 건조한 후, 공기분위기에서 550℃ 온도에서 4시간동안 소성하였다. 그 후, 20부피% H2/N2의 혼합기체가 흐르는 조건에서 300℃에서 2시간동안 환원하였다. 그 결과, 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터를 얻었고, 그 모식도를 도 1에 나타냈다. 상기 모식도에 나타난 바와 같이, 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터에는, 입경이 큰 베타-제올라이트의 표면에 입경이 작은 본원발명의 혼합촉매가 고르게 분산되어 있음을 알 수 있다. Next, the DOC support / ceramic filter was dried at 80 ° C. for 28 hours, and then calcined at 550 ° C. for 4 hours in an air atmosphere. Thereafter, the mixture was reduced at 300 ° C. for 2 hours under the condition that 20 vol% H 2 / N 2 mixed gas flowed. As a result, a DOC support / ceramic filter coated with a mixed catalyst of the present invention was obtained, and a schematic diagram thereof is shown in FIG. 1. As shown in the schematic diagram, it can be seen that in the DOC support / ceramic filter coated with the mixed catalyst of the present invention, the mixed catalyst of the small particle size of the present invention is evenly dispersed on the surface of the beta-zeolite having a large particle size.

또한, 도 2a 에서는, 상기 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터의 표면을 SEM 사진으로 나타냈다. 도 2b에서는, 상기 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터의 표면의 단면을 SEM 사진으로 나타냈다. 상기 도 2a 및 도 2b 에서 나타나는 바와 같이, 베타-제올라이트가 다공성 구조를 형성하고, 입경이 큰 베타-제올라이트의 표면에 입경이 작은 본원발명의 혼합촉매가 고르게 분산되어 디젤 차량의 배출가스와 반응할 수 있는 촉매면적이 넓다는 것을 알 수 있다.In addition, in Figure 2a, the surface of the DOC support / ceramic filter coated with the mixed catalyst of the present invention is shown in the SEM photograph. In Figure 2b, a cross-sectional view of the surface of the DOC support / ceramic filter coated with the mixed catalyst of the present invention is shown in SEM photographs. As shown in FIG. 2A and FIG. 2B, the beta-zeolite forms a porous structure, and the mixed catalyst of the present invention having a small particle size is uniformly dispersed on the surface of the beta-zeolite having a large particle diameter to react with the exhaust gas of a diesel vehicle. It can be seen that the catalyst area can be large.

<실시예 2> : Pt-W/TiO2을 이용한 DOC 지지체/세라믹 필터의 코팅Example 2 Coating of DOC Support / Ceramic Filter Using Pt-W / TiO 2

본 실시예에서는, 제조예 1에서 제시한 Pt-W/TiO2을 이용하여 DOC 지지체/세라믹 필터를 코팅하였다.In this example, the DOC support / ceramic filter was coated using Pt-W / TiO 2 shown in Preparation Example 1.

먼저, 코디어라이트 재질의 DOC 지지체/세라믹 필터 단위부피(1L)당, 60g의 Pt-W/TiO2 을 코팅하였다.First, 60 g of Pt-W / TiO 2 was coated per 1 L of DOC support / ceramic filter unit made of cordierite.

다음으로, 상기 DOC 지지체/세라믹 필터를 105℃에서 10시간동안 건조한 후, 공기분위기에서 550℃ 온도에서 4시간동안 소성하였다. 그 후, 20부피% H2/N2의 혼합기체가 흐르는 조건에서 300℃에서 2시간동안 환원하였다. 그 결과, Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터를 얻었고, 그 모식도를 도 3에 나타냈다. 상기 모식도에 나타난 바와 같이, DOC 지지체/세라믹 필터는 입경이 균일한 Pt-W/TiO2 에 의해 코팅되어 디젤 차량의 배출가스와 반응할 수 있는 촉매표면적이 좁다.Next, the DOC support / ceramic filter was dried at 105 ° C. for 10 hours, and then calcined at 550 ° C. for 4 hours in an air atmosphere. Thereafter, the mixture was reduced at 300 ° C. for 2 hours under the condition that 20 vol% H 2 / N 2 mixed gas flowed. As a result, a DOC supporter / ceramic filter coated with Pt-W / TiO 2 was obtained, and a schematic diagram thereof is shown in FIG. 3. As shown in the schematic diagram, the DOC support / ceramic filter is coated with Pt-W / TiO 2 having a uniform particle diameter, and thus has a narrow catalytic surface area capable of reacting with the exhaust gas of a diesel vehicle.

도 4a 에서는, 상기의 DOC 지지체/세라믹 필터의 코팅된 표면을 SEM 사진으로 나타냈다. 도 4b에서는, 상기의 DOC 지지체/세라믹 필터의 코팅된 표면의 단면을 SEM 사진으로 나타냈다. 상기 도 4a 및 도 4b 에서 나타나는 바와 같이, 미세입경을 가지는 Pt-W/TiO2만을 DOC 지지체/세라믹 필터에 코팅할 경우에는 Pt-W/TiO2 층 내의 기공률이 낮아서 디젤 차량의 배출가스와 반응할 수 있는 Pt-W/TiO2 의 면적이 좁다는 것을 알 수 있다.In FIG. 4A, the coated surface of the DOC support / ceramic filter is shown by SEM photograph. In FIG. 4B, the cross section of the coated surface of the DOC support / ceramic filter is shown in SEM image. As shown in FIGS. 4A and 4B, when only Pt-W / TiO 2 having a fine particle diameter is coated on the DOC support / ceramic filter, the porosity in the Pt-W / TiO 2 layer is low to react with the exhaust gas of the diesel vehicle. narrow the area of the Pt-W / TiO 2 that can be seen that the.

<비교예 1> : 60km/hr 의 운행속도에서의 PM 제거효율<Comparative Example 1>: PM removal efficiency at a driving speed of 60 km / hr

실시예 1의 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터와, 실시예 2의 Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터의 PM 제거효율을 비교하는 실험을 하였다. 실시예 1과 실시예 2의 DOC 지지체/세라믹 필터를 각각, 차량에 부착 가능하도록 케닝하여, 3.0L TCl 엔진이 장착된 차량에 부착하여 평균운행속도가 60km/hr 인 조건에서, 운행시간당 PM의 누적량을 측정하였다. Experiments comparing the PM removal efficiency of the DOC support / ceramic filter coated with the mixed catalyst of the present invention of Example 1 and the DOC support / ceramic filter coated with Pt-W / TiO 2 of Example 2 were carried out. The DOC scaffolds / ceramic filters of Examples 1 and 2 were each canned to be attached to a vehicle, attached to a vehicle equipped with a 3.0L TCl engine, and had an average operating speed of 60 km / hr. Cumulative amount was measured.

대조군으로서, 코팅되지 않은 DOC 지지체/세라믹 필터를 3.0L TCl 엔진이 장착된 차량에 부착하여 평균운행속도가 60km/hr 인 조건에서, 운행시간당 PM의 누적량을 측정하였다. 실험결과는 하기의 표 1에 나타냈다.As a control, an uncoated DOC support / ceramic filter was attached to a vehicle equipped with a 3.0L TCl engine to measure the cumulative amount of PM per mileage under conditions of an average running speed of 60 km / hr. The experimental results are shown in Table 1 below.

[표 1]TABLE 1

PM 누적속도(g/hr)PM cumulative speed (g / hr) PM 제거효율(%)PM removal efficiency (%) 실시예 1Example 1 1One 77.877.8 실시예 2Example 2 22 55.555.5 대조군Control group 4.54.5 --

상기의 표 1에서 볼 수 있듯이, 본원발명의 혼합촉매가 코팅된 DOC 지지체/세라믹 필터(실시예 1)를 사용하였을 때의 PM 누적속도는 1g/hr 이며, 코팅되지 않은 DOC 지지체/세라믹 필터(대조군)를 사용하였을 때의 PM 누적속도는 4.5g/hr이었다. 즉, 본원발명의 경우, PM 제거효율이 77.8%에 이른다. 반면, Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터(실시예 2)를 사용하였을 때의 PM 누적속도는 2g/hr이며, PM 제거효율은 55.5%에 불과하다.As can be seen in Table 1, the PM cumulative rate is 1 g / hr when using the mixed catalyst coated DOC support / ceramic filter (Example 1) of the present invention, the uncoated DOC support / ceramic filter ( PM cumulative rate was 4.5g / hr. That is, in the present invention, the PM removal efficiency reaches 77.8%. On the other hand, when using the DOC support / ceramic filter (Example 2) coated with Pt-W / TiO 2 PM accumulation rate is 2g / hr, PM removal efficiency is only 55.5%.

즉, 본원발명의 혼합촉매를 사용하여 DOC 지지체/세라믹 필터를 코팅한 경우에 PM 제거효율이 우수하다는 것을 알 수 있다. That is, it can be seen that the PM removal efficiency is excellent when the DOC support / ceramic filter is coated using the mixed catalyst of the present invention.

<비교예 2> : 100km/hr 의 운행속도에서의 PM 제거효율<Comparative Example 2>: PM removal efficiency at a driving speed of 100 km / hr

실시예 1의 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터와, 실시예 2의 Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터의 PM 제거효율을 비교하는 실험을 하였다. 실시예 1과 실시예 2의 DOC 지지체/세라믹 필터를 각각, 차량에 부착 가능하도록 케닝하여, 3.0L TCl 엔진이 장착된 차량에 부착하여 평균운행속도가 100km/hr 인 조건에서, 운행시간당 PM의 누적량을 측정하였다. Experiments comparing the PM removal efficiency of the DOC support / ceramic filter coated with the mixed catalyst of the present invention of Example 1 and the DOC support / ceramic filter coated with Pt-W / TiO 2 of Example 2 were carried out. The DOC scaffolds / ceramic filters of Examples 1 and 2 were each canned to be attached to a vehicle, attached to a vehicle equipped with a 3.0L TCl engine, and had an average operating speed of 100 km / hr. Cumulative amount was measured.

대조군으로서, 코팅되지 않은 DOC 지지체/세라믹 필터를 3.0L TCl 엔진이 장착된 차량에 부착하여 평균운행속도가 100km/hr 인 조건에서, 운행시간당 PM의 누 적량을 측정하였다. 실험결과는 하기의 표 2에 나타냈다.As a control, an uncoated DOC support / ceramic filter was attached to a vehicle equipped with a 3.0L TCl engine to measure the cumulative amount of PM per mileage under conditions of average driving speed of 100 km / hr. The experimental results are shown in Table 2 below.

[표 2]TABLE 2

PM 누적속도(g/hr)PM cumulative speed (g / hr) PM 제거효율(%)PM removal efficiency (%) 실시예 1Example 1 -6-6 230230 실시예 2Example 2 -2-2 144144 대조군Control group 4.54.5 --

상기의 표 2에서 볼 수 있듯이, 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터(실시예 1)를 사용하였을 때의 PM 누적속도는 -6g/hr 이며, 코팅되지 않은 DOC 지지체/세라믹 필터(대조군)를 사용하였을 때의 PM 누적속도는 4.5g/hr이었다. 즉, 본원발명의 경우, PM 제거효율이 230%에 이르는 반면, Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터(실시예 2)를 사용하였을 때의 PM 누적속도는 -2g/hr이며, PM 제거효율은 144%에 불과하였다.As can be seen in Table 2 above, when the DOC support / ceramic filter (Example 1) coated with the mixed catalyst of the present invention was used, the PM accumulation rate was -6 g / hr, and the uncoated DOC support / ceramic filter was When using (control), the cumulative PM rate was 4.5 g / hr. That is, in the present invention, the PM removal efficiency reaches 230%, while the PM cumulative rate when the DOC support / ceramic filter (Example 2) coated with Pt-W / TiO 2 is used is -2 g / hr. The PM removal efficiency was only 144%.

상기의 결과로부터, 본원발명의 혼합촉매를 사용하여 DOC 지지체/세라믹 필터를 코팅한 경우, PM 제거효율이 우수하다는 것을 알 수 있다.From the above results, it can be seen that the PM removal efficiency is excellent when the DOC support / ceramic filter is coated using the mixed catalyst of the present invention.

이상 본 발명의 구체적 실시형태와 관련하여 본 발명을 설명하였으나 이는 예시에 불과하며 본 발명은 이에 제한되지 않는다. 당업자는 본 발명의 범위를 벗어나지 않고 설명된 실시형태를 변경 또는 변형할 수 있으며, 이러한 변경 또는 변형도 본 발명의 범위에 속한다. 또한 본 명세서에서 설명한 각 구성요소의 물질은 당업자가 공지된 다양한 물질로부터 용이하게 선택하여 대체할 수 있다. 또한 당업자는 본 명세서에서 설명된 구성요소 중 일부를 성능의 열화없이 생략하거나 성능을 개선하기 위해 구성요소를 추가할 수 있다. 뿐만 아니라, 당업자는 공정 환경이 나 장비에 따라 본 명세서에서 설명한 방법 단계의 순서를 변경할 수도 있다. 따라서 본 발명의 범위는 설명된 실시형태가 아니라 특허청구범위 및 그 균등물에 의해 결정되어야 한다.The present invention has been described above in connection with specific embodiments of the present invention, but this is only an example and the present invention is not limited thereto. Those skilled in the art can change or modify the described embodiments without departing from the scope of the present invention, and such changes or modifications are within the scope of the present invention. In addition, the materials of each component described herein can be easily selected and replaced by a variety of materials known to those skilled in the art. Those skilled in the art can also omit some of the components described herein without degrading the performance or add the components to improve performance. In addition, those skilled in the art may change the order of the method steps described herein according to the process environment or equipment. Therefore, the scope of the present invention should be determined by the appended claims and equivalents thereof, not by the embodiments described.

도 1은 본원발명의 디젤 차량의 배출가스 저감장치용 혼합촉매로 코팅된 DOC 지지체/세라믹 필터의 모식도를 나타낸 것이다. Figure 1 shows a schematic diagram of the DOC support / ceramic filter coated with a mixed catalyst for the exhaust gas reducing device of the present invention.

도 2a는, 제조예 1의 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터의 표면을 SEM 사진으로 나타낸 것이다. 도 2b는, 제조예 1의 본원발명의 혼합촉매로 코팅된 DOC 지지체/세라믹 필터의 표면의 단면을 SEM 사진으로 나타낸 것이다. Figure 2a is a SEM photograph of the surface of the DOC support / ceramic filter coated with the mixed catalyst of the present invention of Preparation Example 1. Figure 2b is a SEM photograph showing the cross section of the surface of the DOC support / ceramic filter coated with the mixed catalyst of the present invention of Preparation Example 1.

도 3은 제조예 2의 Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터의 모식도를 나타낸 것이다.Figure 3 shows a schematic diagram of the DOC support / ceramic filter coated with Pt-W / TiO 2 of Preparation Example 2.

도 4a는, 제조예 2의 Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터의 표면을 SEM 사진으로 나타낸 것이다. 도 4b는, 제조예 2의 Pt-W/TiO2로 코팅된 DOC 지지체/세라믹 필터의 표면의 단면을 SEM 사진으로 나타낸 것이다. Figure 4a, shows the surface of the support DOC / ceramic filter coating of Preparation Example 2 with Pt-W / TiO 2 by SEM photograph. Figure 4b, shows the cross section of the surface of the preparation 2 of Pt-W / TiO 2 with DOC substrate / ceramic filter coated with a SEM picture.

Claims (14)

삭제delete 삭제delete 삭제delete 삭제delete 삭제delete 삭제delete (1) Ti, Zr, Si, Al 및 Ce으로 구성된 그룹에서 선택된 1종 또는 2종 이상의 금속의 산화물로서 평균입경은 0.1 ~ 20㎛ 인 것에, 백금과 텅스텐의 복합활성금속으로서 평균입경은 0.01 ~ 5.0㎛인 것이 포함된 용액을 담지하되, 상기 금속의 산화물과 상기 복합활성금속을 10 ~ 90 : 90 ~ 10 의 중량비로 혼합하여 혼합물 분말을 준비하는 제1단계;(1) An oxide of one or two or more metals selected from the group consisting of Ti, Zr, Si, Al, and Ce, with an average particle diameter of 0.1 to 20 μm, and a composite active metal of platinum and tungsten, with an average particle diameter of 0.01 to A first step of preparing a mixture powder by supporting a solution containing 5.0 μm, by mixing an oxide of the metal and the composite active metal in a weight ratio of 10 to 90:90 to 10; (2) 상기 혼합물 분말을 건조 및 소성하여 촉매 분말을 얻는 제2단계; 및(2) a second step of drying and firing the mixture powder to obtain a catalyst powder; And (3) 상기 촉매 분말을 (i) 베타-제올라이트, (ii) 알루미나, 티타니아 및 실리콘으로 구성된 그룹에서 선택된 어느 하나로서, 디젤 차량의 배출가스 저감장치용 혼합촉매 전체 중량대비 0.5 ~ 5 중량%로 포함되는 것을 특징으로 하는 무기바인더 및 (iii) 물 또는 알코올인 것을 특징으로 하는 분산제와 혼합하여 디젤 차량의 배출가스 저감장치용 혼합촉매를 얻는 제3단계; 를 포함하는 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법.(3) the catalyst powder is any one selected from the group consisting of (i) beta-zeolite, (ii) alumina, titania and silicon, and is 0.5 to 5% by weight of the total weight of the mixed catalyst for the exhaust gas reducing device of a diesel vehicle. A third step of obtaining a mixed catalyst for an exhaust gas reducing device of a diesel vehicle by mixing with an inorganic binder and (iii) a dispersant, characterized in that it is water or alcohol; Method for producing a mixed catalyst for exhaust gas reduction device of a diesel vehicle comprising a. 삭제delete 삭제delete 삭제delete 삭제delete 삭제delete 제 7 항에 있어서,The method of claim 7, wherein 상기 건조는 105℃에서 12시간동안 공기분위기에서 실행하며, The drying is carried out in an air atmosphere at 105 ℃ for 12 hours, 상기 소성은 550℃의 공기분위기에서 실행하는 것을 특징으로 하는 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법.The firing is carried out in an air atmosphere of 550 ℃ method for producing a mixed catalyst for the exhaust gas reducing device of a diesel vehicle. 제 7항에 있어서, 상기 금속의 산화물의 평균입경은 복합활성금속의 평균입경보다 큰 것을 특징으로 하는 디젤 차량의 배출가스 저감장치용 혼합촉매의 제조방법.8. The method of claim 7, wherein the average particle diameter of the oxide of the metal is larger than the average particle diameter of the composite active metal.
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US13/139,500 US20110258994A1 (en) 2008-12-12 2009-12-11 Bifunctional Catalyst for Decomposition and Oxidation of Nitrogen Monoxide, Composite Catalyst Including the Same for Apparatus to Decrease Exhaust Gas, and Method for Preparation Thereof
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