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    수동적 암모니아/ＳＣＲ용 암모니아 생성 삼원 촉매의 제조 방법 및 이에 의해 제조된 삼원 촉매
    25.
    发明公开
    수동적 암모니아/ＳＣＲ용 암모니아 생성 삼원 촉매의 제조 방법 및 이에 의해 제조된 삼원 촉매 有权
    无源氨氮SCR技术生产氨基甲酸的制造方法及其应用

    公开(公告)号：KR1020130060028A

    公开(公告)日：2013-06-07

    申请号：KR1020110126307

    申请日：2011-11-29

    Applicant: 현대자동차주식회사 ,  포항공과대학교 산학협력단

    Inventor： 정진우 ,  남인식 ,  윤달영 ,  허일정

    IPC: B01J23/46 ,  B01J21/06 ,  B01J37/08

    CPC classification number: B01J23/464 ,  B01J21/00 ,  B01J23/10 ,  B01J37/08

    Abstract: PURPOSE: A manufacturing method of three-way catalyst producing ammonia for passive ammonia/selective catalytic reduction and a tree-way catalyst manufactured by the same are provided to be effectively used for environmentally-friendly automobiles. CONSTITUTION: A catalyst for reducing nitrogen oxide into ammonia is carried in a metal oxide carrier. A manufacturing method of the catalyst includes a step for thermally treating noble metal powder carried in the metal oxide carrier in the process of manufacturing a three-way catalyst based on an impregnation method. The noble metal is rhodium(Rh). The metal oxide support is Al2O3, SiO2, ZrO2, CeO2, C3Z1(Ce0.75Zr0.25O2), or the mixture. The noble metal carried in the carrier is thermally treated at 800-1,200 deg. C. The weight ratio of the noble metal impregnated in the metal oxide carrier is 0.01-1 weight%. [Reference numerals] (AA) NH3 productivity(ppm)

    Abstract translation: 目的：提供用于产生用于被动氨/选择性催化还原的氨的三元催化剂的制造方法和由其制造的树脂催化剂，以有效地用于环境友好的汽车。 构成：用于将氮氧化物还原成氨的催化剂在金属氧化物载体中进行。 催化剂的制造方法包括在基于浸渍法的三元催化剂的制造工序中对金属氧化物载体中载持的贵金属粉末进行热处理的工序。 贵金属是铑（Rh）。 金属氧化物载体为Al2O3，SiO2，ZrO2，CeO2，C3Z1（Ce0.75Zr0.25O2）或混合物。 承载在载体上的贵金属在800-1200度热处理。 浸渍在金属氧化物载体中的贵金属的重量比为0.01-1重量％。 （标号）（AA）NH 3生产率（ppm）

    희토류 금속을 함유하는 배기가스내 질소 산화물의 선택적 환원용 촉매 및 이의 제조방법
    26.
    发明公开
    희토류 금속을 함유하는 배기가스내 질소 산화물의 선택적 환원용 촉매 및 이의 제조방법 有权
    含有稀土金属的催化剂用于选择性催化还原氮氧化物在排气中的应用

    公开(公告)号：KR1020110062145A

    公开(公告)日：2011-06-10

    申请号：KR1020090118737

    申请日：2009-12-02

    Applicant: 현대자동차주식회사 ,  오덱(주)

    Inventor： 정진우 ,  길정기 ,  남인식 ,  차문순 ,  권혁재 ,  김영진 ,  강대환

    IPC: B01J29/69 ,  B01J29/26 ,  B01J37/12 ,  B01D53/94

    CPC classification number: B01J29/69 ,  B01D53/9409 ,  B01J37/08 ,  B01J37/12

    Abstract: PURPOSE: A catalyst for selective reduction of nitric oxide within exhaust gas containing rare earth metal and a manufacturing method thereof are provided to eliminate nitric oxide within exhaust gas of hydro-thermal treatment former and post treatment in the high temperature by using rare earth metal as co-catalyst and by using Mn and Fe as active component and zeolite as carrier. CONSTITUTION: The catalyst for the selective reduction of the nitric oxide within the exhaust gas containing the rare earth metal is immersed in the zeolite carrier. The catalyst contains more than one kind of manganic compound, and the iron compound selected from the rare earth metal. The co-catalyst component contains 4~40 weight% based of the standard of catalyst of total 100 weight of the rare earth metal and manganese and iron. The manganese contains 10~60 weight%. The iron contains 4~40 weight%. The zeolite is included in 20~200 parts by weight. The catalyst has the reduction activity capability of the nitric oxide of 80~100% in the reaction temperature of 200~400 °C after the hydro-thermal treatment. The reduction reaction of catalyst uses the element (Urea) or the ammonia (NH3) as the reducing agent.

    Abstract translation: 目的：提供一种用于选择性还原含稀土金属废气中的一氧化氮的催化剂及其制造方法，其用于通过使用稀土金属作为水热处理剂的排气中的一氧化氮和高温后处理 助催化剂，以Mn和Fe为活性组分，沸石为载体。 构成：将含有稀土金属的废气中的一氧化氮选择性还原的催化剂浸入沸石载体中。 该催化剂含有一种以上的锰化合物和选自稀土金属的铁化合物。 助催化剂组分含有4〜40重量％的标准催化剂，共100重量份的稀土金属和锰和铁。 锰含量为10〜60重量％。 铁含量为4〜40％。 沸石的含量为20〜200重量份。 在热处理后，催化剂的反应温度为200〜400℃，一氧化氮的还原活性为80〜100％。 催化剂的还原反应使用元素（尿素）或氨（NH 3）作为还原剂。

    페로브스카이트 ＮＯ 산화용 촉매 및 그 제조방법
    30.
    发明公开
    페로브스카이트 ＮＯ 산화용 촉매 및 그 제조방법 审中-实审
    用于无氧化的PERVOSKITE催化剂及其制备方法

    公开(公告)号：KR1020130137868A

    公开(公告)日：2013-12-18

    申请号：KR1020120061504

    申请日：2012-06-08

    Applicant: 현대자동차주식회사 ,  포항공과대학교 산학협력단

    Inventor： 남인식 ,  윤달영 ,  김문규 ,  임은호 ,  정진우

    IPC: B01J23/10 ,  C01F17/00 ,  C01G45/00 ,  C01G5/00

    CPC classification number: B01J23/002 ,  B01J23/50 ,  B01J37/08 ,  B01J2523/00 ,  B01J2523/18 ,  B01J2523/3706 ,  B01J2523/72

    Abstract: The present invention relates to a perovskite catalyst for NO oxidation and a manufacturing method thereof and, in particular, to a perovskite catalyst for NO oxidation and a manufacturing method thereof capable of accelerating the usage of the perovskite catalyst for NO oxidation and reducing production costs owing to the excluded use of precious metals because the perovskite catalyst for NO oxidation can be used as a main component of an aftertreatment system for reducing NOx in exhaust gas of a leanburn gasoline engine or a diesel engine by producing the perovskite catalyst including silver (Ag) having the function of NO oxidation and excellent hydrothermal stability. The perovskite catalyst for NO oxidation is the core technology of an aftertreatment system for vehicle exhaust gas which can be used for an eco-friendly low-pollution vehicle to react to environmental restrictions in the WTO system. [Reference numerals] (AA) Pt-based commercial catalyst

    Abstract translation: 本发明涉及一种用于NO氧化的钙钛矿催化剂及其制造方法，特别涉及一种用于NO氧化的钙钛矿催化剂及其制造方法，其能够促进钙钛矿催化剂的NO氧化的使用，并降低生产成本 对于排除使用的贵金属，因为用于NO氧化的钙钛矿催化剂可以用作通过生产包含银（Ag）的钙钛矿催化剂来减少稀薄汽油发动机或柴油发动机的废气中的NOx的后处理系统的主要成分， 具有NO氧化功能和极好的水热稳定性。 NO氧化的钙钛矿催化剂是车用废气后处理系统的核心技术，可用于环保型低污染车辆对世贸组织体系的环境限制作出反应。 （附图标记）（AA）Pt基商业催化剂

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