KR100250817B1 - Preparation of catalyst body containing pt,pd or rh for automotive exhaust gas - Google Patents

Preparation of catalyst body containing pt,pd or rh for automotive exhaust gas Download PDF

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KR100250817B1
KR100250817B1 KR1019970081452A KR19970081452A KR100250817B1 KR 100250817 B1 KR100250817 B1 KR 100250817B1 KR 1019970081452 A KR1019970081452 A KR 1019970081452A KR 19970081452 A KR19970081452 A KR 19970081452A KR 100250817 B1 KR100250817 B1 KR 100250817B1
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catalyst
exhaust gas
rhodium
platinum
palladium
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KR19990061196A (en
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여권구
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정몽규
현대자동차주식회사
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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
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/024Multiple impregnation or coating
    • 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
    • B01D53/9445Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
    • B01D53/945Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC] characterised by a specific catalyst
    • 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
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/464Rhodium
    • 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
    • B01J23/63Platinum group metals with rare earths or actinides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/04Mixing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Catalysts (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PURPOSE: Provided is a catalytic converter containing Pt, Pd, and Rd for purifying automobile flue gas, which has improved thermal resistance, durability, and has competitiveness in cost. CONSTITUTION: The catalytic converter is manufactured by impregnating Al2O3 with Pt, Rh, Pd at the ratio of 0.5-3:12-15:0.5-3; blending and milling; adding Ce-Zr oxides to prepare washcoat slurry (solid content: 30-50%) having rare earth metal content of up to 10g/L; washcoating the slurry on the surface of a honeycomb monolith: drying the honeycomb monolith in the temperature range of 100 to 150deg.C; and then sintering it in the temperature range of 400 to 600deg.C.

Description

백금, 팔라듐 또는 로듐이 함유된 자동차 배기가스 정화용 촉매체의 제조방법Method for producing catalyst body for automobile exhaust gas purification containing platinum, palladium or rhodium

본 발명은 백금, 팔라듐 및 로듐 등의 귀금속류를 지지체에 함침한 뒤 담체에 코팅하는 과정을 포함하는 자동차 배기가스 정화용 촉매의 제조방법에 관한 것이다.The present invention relates to a method for preparing a catalyst for automobile exhaust gas purification comprising the step of impregnating a noble metal such as platinum, palladium and rhodium on a support and then coating the carrier.

20세기 초 미국의 포드사 등에서 대량으로 생산되기 시작한 자동차는 폭발적으로 증가하여 현재에는 없어서는 안될 중요한 운송수단이 되었다. 이러한 자동차의 이용도가 증가함에 따라 교통량의 증가로 도로의 혼잡, 각종 교통사고와 진동 등에 따른 피해 및 배기가스로 인한 심각한 대기오염 등이 중요한 사회문제로 대두되고 있다.Cars, which began mass production at Ford Corp. in the early 20th century, exploded and became an indispensable vehicle for now. As the use of such vehicles increases, traffic increases, traffic congestion, damage caused by various traffic accidents and vibrations, and serious air pollution due to exhaust gases are emerging as important social problems.

자동차에서 배출되는 가스는 배기가스, 블로바이가스(blow-by-gas) 및 증발가스로 나누어진다. 이 중에서 배기가스는 연료가 실린더내에서 연소하여 고온ㆍ고압의 가스로 된 후 팽창함으로써 일을 마치고 배기파이프로부터 대기중으로 방출되는 가스로서 이 배기가스의 대부분을 차지하는 것은 수증기와 이산화탄소(CO2)이며, 그밖에 일산화탄소(CO), 미연 탄화수소(HC) 및 질소산화물(NOX) 등의 유해물질이 있다. 배기가스 중의 성분 중 특히 삼원가스로 불리우는 일산화탄소, 미연 탄화수소 및 질소산화물 등은 매우 심각한 환경오염을 야기시켜 이러한 물질을 감소시키려는 연구가 활발히 진행되고 있다. 즉, 전기자동차 등 배기가스가 전혀 발생되지 않는 자동차를 개발하려는 연구가 진행되고 있으나, 효율 면에서 아직도 개선할 점이 많아 상용화 하는데 상당한 어려움이 있다. 한편, 기존의 자동차에서 각 기관의 형상, 작동조건 및 작동상태 등을 개선하여 유해한 배기가스의 발생을 줄이려는 연구가 계속되고 있다. 또한, 배기가스를 촉매로 분해하여 이러한 유해성분이 방출되는 것을 줄이려는 연구가 진행되고 이러한 노력이 상당한 효과가 있어 현재 각종 차량에 적용되고 있다.Gases emitted from automobiles are divided into exhaust gas, blow-by-gas and evaporative gas. Exhaust gas is a gas which is discharged from the exhaust pipe to the atmosphere after the fuel is combusted in a cylinder, becomes a gas of high temperature and high pressure, and expands, and it is water vapor and carbon dioxide (CO 2 ). And other hazardous substances such as carbon monoxide (CO), unburned hydrocarbons (HC), and nitrogen oxides (NO X ). Among the components in the exhaust gas, carbon monoxide, unburned hydrocarbons, and nitrogen oxides, which are called three-way gas, cause very serious environmental pollution, and studies are being actively conducted to reduce such substances. That is, research is being conducted to develop automobiles in which exhaust gas is not generated at all, but there are still many difficulties in commercialization in terms of efficiency. On the other hand, the research to reduce the generation of harmful exhaust gas by improving the shape, operating conditions and operating conditions of each engine in the existing vehicle continues. In addition, research has been conducted to reduce the emission of these harmful components by decomposing the exhaust gas into a catalyst, and these efforts have a considerable effect and are currently applied to various vehicles.

촉매는 자동차 및 다른 가솔린 연료의 엔진과 같은 내연기관의 배기가스 처리를 포함하는 많은 분야에 유용하게 적용된다. 상기한 오염물질에 대한 방출기준이 정부에 의해 정해져 있으며, 신규 자동차는 이러한 기준을 충족시켜야 한다. 이와 같은 기준을 충족시키기 위해서 적당한 촉매를 함유하는 소위 촉매 컨버터(catalytic converter)가 내연기관의 배기가스관에 설치되어 미연 탄화수소의 분해, 일산화탄소의 산화 및 질소산화물의 환원을 촉진시킨다. 촉매 컨버터는 그 기능상 산화촉매 컨버터와 삼원촉매 컨버터로 크게 대별된다. 우선, 산화촉매 컨버터는 촉매 펠렛이라 불리는 입상의 알루미나 표면에 촉매작용을 하는 팔라듐 또는 팔라듐+백금 등의 귀금속을 극히 얇게 부착시킨 것으로 배기가스 중의 일산화탄소와 미연 탄화수소를 이산화탄소와 수증기로 만든다. 한편, 삼원촉매 컨버터는 촉매작용을 하는 귀금속류 즉, 백금+로듐 또는 백금+로듐+팔라듐 등을 사용한 것으로 배기가스 중의 일산화탄소, 미연 탄화수소 및 질소산화물을 동시에 저감시키는 역할을 하며, 현재는 삼원촉매 컨버터가 많이 사용되고 있다.Catalysts are usefully applied in many fields, including exhaust gas treatment of internal combustion engines such as engines of automobiles and other gasoline fuels. Emission standards for these pollutants are set by the government, and new vehicles must meet these standards. In order to meet these standards, a so-called catalytic converter containing a suitable catalyst is installed in the exhaust pipe of the internal combustion engine to promote decomposition of unburned hydrocarbons, oxidation of carbon monoxide and reduction of nitrogen oxides. Catalytic converters are largely classified into functional catalytic converters and three-way catalytic converters. First, the oxidation catalyst converter attaches extremely thin noble metals such as palladium or palladium + platinum, which catalyzes the surface of granular alumina called catalyst pellets, and makes carbon monoxide and unburned hydrocarbons in the exhaust gas into carbon dioxide and water vapor. Meanwhile, the three-way catalytic converter uses precious metals such as platinum + rhodium or platinum + rhodium + palladium to catalyze carbon monoxide, unburned hydrocarbons and nitrogen oxides in the exhaust gas at the same time. It is used a lot.

상기한 미연 탄화수소, 일산화탄소 및 질소산화물을 이산화탄소, 물 및 질소로 전환시키는데 양호한 활성 및 긴 수명을 갖는 촉매를 경제적으로 제조하기 위해 많은 노력을 해왔다. 삼원전환 촉매에서는, 통상적으로 배기가스가 미처리되고 있는 엔진중에 도입되는 공기 대 연료의 비는 실질적으로 동시에 최적의 환원/산화반응(Redox reaction)을 성취하기 위한 화학양론적 양에서 좁은 편차로서 초과해야하다. 삼원전환을 촉진하기 위하여, 당업계에서는 고표면적 지지체 상에 분산된 1종 이상의 귀금속류으로 이루어지는 촉매가 잘 알려져 있다. 지지체는 당업계에서 잘 알려진 바와 같이, 벌집구조의 내화 세라믹으로 모노리틱(monolithic) 담체와 담체 기질상에 충전된 고표면적 알루미나 코팅으로 이루어질 수 있다. 알루미나 지지체는 다수의 미세가스 유통로가 전체에 퍼져 있는, 벌집 형태의 기질과 같은 담체 기질상에 담지되는 것이 좋다. 이러한 미세 통로를 용이하게 코팅하기 위해서는 워시코트(washcoat)라고 하는 극히 미세한 활성 알루미나 입자로 된 슬러리를 만든뒤 기질에 도포하여 제조한다.Many efforts have been made to economically produce catalysts with good activity and long lifetimes for converting the above unburned hydrocarbons, carbon monoxide and nitrogen oxides into carbon dioxide, water and nitrogen. In three-way conversion catalysts, the ratio of air to fuel that is typically introduced in the engine where the exhaust gas is not treated must be substantially exceeded as a narrow deviation in the stoichiometric amount to achieve an optimal redox reaction at substantially the same time. Do. In order to promote ternary conversion, catalysts consisting of one or more noble metals dispersed on a high surface area support are well known in the art. The support may be composed of a monolithic carrier and a high surface area alumina coating filled on a carrier substrate with a honeycomb refractory ceramic, as is well known in the art. The alumina support is preferably supported on a carrier substrate, such as a honeycomb substrate, in which a plurality of microgas flow paths are spread throughout. In order to easily coat such a micropath, a slurry of extremely fine activated alumina particles called washcoat is made and then applied to a substrate.

내열 및 내구성이 요구되는 자동차 배기가스 정화용 촉매에 있어서, 백금, 팔라듐 또는 로듐 등의 귀금속류가 함유된 촉매가 활발히 연구되고 있으며, 또한 생산되는 자동차에 적용되고 있다. 이러한 귀금속류가 함유된 촉매는 백금, 팔라듐 또는 로듐 등의 귀금속류를 각각 지지체에 함침시킨 뒤 슬러리화하여 담체에 다중 코팅함으로써 각각의 귀금속 성분이 골고루 분산되게 하여 고 내열성 및 고 내구성을 지니게 하였다.In automobile exhaust gas purification catalysts requiring heat resistance and durability, catalysts containing precious metals such as platinum, palladium or rhodium have been actively studied and applied to automobiles produced. These catalysts containing noble metals were impregnated with noble metals, such as platinum, palladium or rhodium, respectively, and then slurried and multi-coated to the carrier so that each noble metal component was evenly dispersed to have high heat resistance and high durability.

그러나, 고가의 귀금속류인 백금, 팔라듐 또는 로듐을 지지체에 함침시킨 뒤 슬러리화하여 담체에 다층으로 코팅하기 때문에 촉매의 생산원가가 상승하게 되었다.However, since the expensive precious metals such as platinum, palladium or rhodium are impregnated into the support and then slurried to coat the carrier in multiple layers, the production cost of the catalyst is increased.

이에 본 발명자는 상기와 같은 문제점을 해결하기 위해 연구를 계속하여 오던 중, 자동차 배기가스 정화용 촉매에 요구되는 내열 및 내구성이 유지되고, 촉매의 성능이 향상되며, 제조원가를 절감시킬 수 있는 우수한 촉매의 제조방법을 개발하여 본 발명을 완성하였다.Accordingly, the inventors of the present invention continue to solve the above problems, while maintaining the heat resistance and durability required for the catalyst for automobile exhaust gas purification, the performance of the catalyst is improved, and the production cost of the excellent catalyst can be reduced The manufacturing method was developed to complete the present invention.

본 발명의 목적은 내열성 및 내구성을 지니고, 촉매의 성능이 향상되며, 제조원가를 절감시킬 수 있는 백금, 팔라듐 또는 로듐 등의 귀금속류가 함유된 자동차 배기가스 정화용 촉매의 제조방법을 제공하는 것이다.SUMMARY OF THE INVENTION An object of the present invention is to provide a method for preparing a catalyst for purification of automobile exhaust gas containing precious metals such as platinum, palladium or rhodium, which has heat resistance and durability, improves the performance of the catalyst, and reduces manufacturing costs.

상기와 같은 목적을 달성하기 위하여, 본 발명에서는 백금, 팔라듐 또는 로듐 등의 귀금속류가 함유된 자동차 배기가스 정화용 촉매의 제조방법을 제공한다.In order to achieve the above object, the present invention provides a method for producing a catalyst for automobile exhaust gas purification containing noble metals such as platinum, palladium or rhodium.

이하, 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.

본 발명의 제조방법은 백금, 팔라듐 또는 로듐 등의 귀금속류를 각각 지지체에 함침시킨 뒤 혼합하고, 밀링하여 워시코트를 제조한 뒤 담체에 코팅하여 건조시킨 다음 소성하는 과정으로 구성된다.The production method of the present invention consists of a process of impregnating a noble metal such as platinum, palladium or rhodium into a support, followed by mixing, milling to prepare a washcoat, coating the carrier, drying and firing.

먼저, 백금 용액, 로듐 용액 및 팔라듐 용액을 지지체인 알루미나(Al2O3)에 각각 함침시킨 뒤 혼합한다.First, the platinum solution, the rhodium solution and the palladium solution are impregnated in alumina (Al 2 O 3 ), which is a support, respectively, and then mixed.

다음으로 혼합된 지지체를 습식 밀링하여 워시코트 슬러리를 얻는다. 이때 전체 분말 성분의 90% 이상이 9㎛ 이하의 입도로 분포되고, 고형분의 함량이 45~50%가 되도록 밀링하는 것이 바람직하다. 또한, 습식 밀링시 희토류 산화물, 알칼리 금속 산화물을 첨가하며, 습식 밀링하여 얻은 슬러리에 세륨(Ce)-지르코늄(Zr) 복합산화물을 첨가하는 것이 바람직하다.Next, the mixed support is wet milled to obtain a washcoat slurry. At this time, 90% or more of the entire powder component is distributed to a particle size of 9 μm or less, and it is preferable to mill so that the content of solid content is 45 to 50%. In addition, rare earth oxides and alkali metal oxides are added during wet milling, and cerium (Ce) -zirconium (Zr) composite oxides are preferably added to the slurry obtained by wet milling.

상기 과정을 통하여 제조된 워시코트 슬러리를 벌집구조의 촉매 담지체에 코팅한다. 이때 귀금속 농도가 최고 10g/ℓ까지인 슬러리를 최고 2.0ℓ까지를 사용하여 코팅하는 것이 바람직하며, 백금; 팔라듐; 로듐의 함량비는 0.5~3: 12~15: 0.5~3이 되도록 조절하는 것이 바람직하다. 또한 워시코트 슬러리를 촉매 딤체에 단일 코팅 또는 이중 코팅하는 것이 바람직하며, 단일 코팅하는 것이 더욱 바람직하다.The washcoat slurry prepared through the above process is coated on the catalyst carrier of the honeycomb structure. At this time, it is preferable to coat the slurry having a noble metal concentration of up to 10 g / l using up to 2.0 l, platinum; Palladium; The content ratio of rhodium is preferably adjusted to be 0.5 to 3:12 to 15 to 0.5 to 3. It is also preferred to single coat or double coat the washcoat slurry onto the catalyst pellets, more preferably to single coat.

코팅된 담체는 건조시키고 소결하여 촉매체를 제조한다. 이때, 백금, 팔라듐 및 로듐 등의 귀금속이 함유된 워시코트 슬러리가 코팅된 담지체를 100~150℃에서 건조시킨 다음 400~600℃에서 소결하는 것이 바람직하다.The coated carrier is dried and sintered to produce a catalyst body. At this time, it is preferable to dry the carrier coated with a washcoat slurry containing precious metals such as platinum, palladium and rhodium at 100 to 150 ° C and then sinter at 400 to 600 ° C.

이하, 실시예에 의하여 본 발명의 자동차 배기가스 정화용 촉매체에 관하여 상세히 설명한다. 단 이들 실시예는 본 발명을 예시하는 것일 뿐 본 발명이 실시예에 의하여 한정되는 것은 아니다.Hereinafter, the catalyst body for automobile exhaust gas purification of this invention is demonstrated in detail by an Example. However, these Examples are only for illustrating the present invention and the present invention is not limited by the Examples.

[실시예 1]Example 1

백금용액, 로듐 용액 및 팔라듐 용액을 지지체인 알루미나에 함침시킨 뒤 14시간 동안 볼-밀(ball-mill)을 이용하여 습식 밀링(milling)하여 입도분포가 8㎛이고, 백금: 팔라듐: 로듐의 함량 비가 1:14:1이며, 농도가 3.6g/ℓ인 워시코트 슬러리(고형분의 함량: 45~50%)를 제조하고, 이 슬러리 1ℓ를 촉매 딤지체에 단일 코팅하여 130℃에서 건조시킨 뒤 500℃의 온도에서 소결하여 촉매체를 제조하였다.The platinum solution, rhodium solution and palladium solution were impregnated into alumina as a support, followed by wet milling using a ball-mill for 14 hours. The particle size distribution was 8 µm, and the content of platinum: palladium: rhodium A washcoat slurry (solid content: 45-50%) with a ratio of 1: 14: 1 and a concentration of 3.6 g / L was prepared, 1 L of this slurry was coated on a catalyst dim-die, dried at 130 ° C., and then 500 Sintered at a temperature of ℃ to prepare a catalyst body.

[실시예 2]Example 2

상기 실시예 1과 같은 방법으로 제조된 워시코트 슬러리 1ℓ를 촉매 담지체에 이중으로 코팅하여 130℃에서 건조시킨 뒤 550℃의 온도에서 소결하여 촉매체를 제조하였다.1 L of the washcoat slurry prepared in the same manner as in Example 1 was coated on the catalyst carrier, dried at 130 ° C., and then sintered at a temperature of 550 ° C. to prepare a catalyst body.

한편, 상기한 실시예의 촉매와 비교하기 위하여 하기 비교실시예의 촉매를 제조하였다.On the other hand, the catalyst of the following Comparative Example was prepared in order to compare with the catalyst of the above Example.

[비교실시예]Comparative Example

백금용액 및 로듐 용액을 지지체인 알루미나에 함침시킨 뒤 14시간 동안 볼-밀로 습식 밀링하여 입도분포가 9㎛ 이하이고, 백금: 로듐의 함량 비가 5:1이며, 농도가 2.0g/ℓ인 워시코트 슬러리(고형분의 함량:30~50%)를 제조하고, 이 슬러리 1ℓ를 촉매 담지체에 이중으로 코팅하여 130℃에서 건조시킨 뒤 550℃의 온도에서 소결하여 촉매체를 제조하였다.The platinum solution and the rhodium solution were impregnated with alumina as a support, followed by wet milling with a ball-mill for 14 hours, and the washcoat had a particle size distribution of 9 μm or less, a platinum: rhodium content of 5: 1, and a concentration of 2.0 g / l. A slurry (solid content: 30-50%) was prepared, and 1 liter of this slurry was coated on the catalyst carrier in duplicate, dried at 130 ° C., and sintered at a temperature of 550 ° C. to prepare a catalyst body.

[실험예]Experimental Example

촉매의 내열성 및 내구성 측정Measurement of the heat resistance and durability of the catalyst

상기 실시예 및 비교실시예에서 얻은 촉매체를 각각 950℃에서 140시간 및 1100℃에서 100시간 동안 노화시킨 뒤 삼원가스[탄화수소(HC), 일산화탄소(CO) 및 질소산화물(NOX)]의 산화 및 환원 특성을 측정하여 그 결과를 하기 표 1에 나타내었다.Aging of the catalyst body obtained in the above Examples and Comparative Examples for 140 hours at 950 ℃ and 100 hours at 1100 ℃, respectively, oxidation of three-way gas (hydrocarbon (HC), carbon monoxide (CO) and nitrogen oxides (NO X )) And the reduction properties were measured and the results are shown in Table 1 below.

[표 1a]TABLE 1a

950℃에서 140시간 동안 노화Aging at 950 ° C. for 140 hours

Figure kpo00001
Figure kpo00001

[표 1b]TABLE 1b

1100℃에서 100시간 동안 노화Aging at 1100 ° C. for 100 hours

Figure kpo00002
Figure kpo00002

또한, 상기 실시예 및 비교실시예의 촉매체로 제조된 촉매 컨버터를 실제 차량에 장착한 후 FTP(federal test procedure)시험(100,000마일의 주행에 상당하도록 엔진을 노화시킴)을 수행하여 그때의 삼원가스[탄화수소(HC), 일산화탄소(CO) 및 질소산화물(NOX)]의 산화 및 환원 특성을 측정하였으며, 그 결과를 하기 표 2에 나타내었다.In addition, after the catalytic converter made of the catalyst bodies of the above examples and the comparative examples was mounted on an actual vehicle, a FTP (federal test procedure) test (aging the engine to correspond to 100,000 miles of driving) was performed to perform three-way gas [ Hydrocarbon (HC), carbon monoxide (CO) and nitrogen oxides (NO X )] were measured for oxidation and reduction properties, the results are shown in Table 2 below.

[표 2]TABLE 2

FTP 시험(100,000마일의 주행에 상당한 엔진 노화)FTP test (significant engine aging for 100,000 miles of driving)

Figure kpo00003
Figure kpo00003

이상에서 살펴본 바와 같이, 본 발명의 제조방법을 통하여 제조된 촉매체는 기존의 촉매체에 비해 삼원가스를 산화 및 환원시켜 무해한 질소가스 또는 이산화 탄소 등으로 분해시키는 특성이 크고, 내열성 및 내구성이 우수하며, 제조원가가 기존의 촉매체에 비해 10~15% 절감되는 우수한 촉매체로서, 자동차 배기가스 정화용 촉매를 제조하는데 유용하게 사용될 수 있다.As described above, the catalyst body produced through the production method of the present invention has a greater property of oxidizing and reducing ternary gas into harmless nitrogen gas or carbon dioxide, and has higher heat resistance and durability than conventional catalyst bodies. In addition, the production cost is excellent catalyst body that is reduced by 10 to 15% compared to the existing catalyst body, it can be usefully used to prepare a catalyst for automobile exhaust gas purification.

Claims (2)

백금(Pt), 로듐(Rh) 또는 팔라듐(Pd)이 함유된 자동차 배기가스 정화용 촉매의 제조방법에 있어서, 함량비가 각각 0.5~3: 12~15: 0.5~3인 백금, 로듐 및 팔라듐을 각각 지지체에 함침시킨 뒤 혼합하고 밀링한 후, 세륨(Ce)-지르코늄(Zr) 복합 산화물을 더 첨가하여, 귀금속 농도가 최고 10g/ℓ까지인 워시코트 슬러리(고형분의 함량: 30~50%)를 만든 후, 이 워시코트슬러리를 최고 2ℓ까지 담체에 단일층 또는 이중층으로 코팅하여 건조시킨 다음 소성하는 과정으로 구성되는 자동차 배기가스 정화용 촉매체의 제조방법In the method for preparing a catalyst for automobile exhaust gas purification containing platinum (Pt), rhodium (Rh) or palladium (Pd), platinum, rhodium and palladium having a content ratio of 0.5 to 3:12 to 15 to 0.5 to 3, respectively After impregnating the support, mixing and milling, a cerium (Ce) -zirconium (Zr) composite oxide was further added to prepare a washcoat slurry (solid content: 30 to 50%) having a noble metal concentration of up to 10 g / l. After manufacturing, the washcoat slurry is coated with a single layer or a double layer on a carrier up to 2 L, dried, and then fired. 제1항에 있어서, 백금, 로듐 또는 팔라듐이 함침된 지지체를 혼합하고 밀링하는 과정에 있어서, 희토류 산화물 또는 알칼리 금속 산화물을 첨가하는 것을 특징으로 하는 자동차 배기가스 정화용 촉매체의 제조방법The method of claim 1, wherein in the process of mixing and milling the support impregnated with platinum, rhodium, or palladium, a rare earth oxide or an alkali metal oxide is added.
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