首页> 外文会议>The 7th China-Korea Workshop on Clean Energy Technology(第七届中韩清洁能源技术研讨会) >EFFECTS OF PREPARATION METHODS FOR V2O5-TiO2 AEROGEL CATALYSTS ON SELECTIVE REDUCTION OF NO WITH NH3
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EFFECTS OF PREPARATION METHODS FOR V2O5-TiO2 AEROGEL CATALYSTS ON SELECTIVE REDUCTION OF NO WITH NH3

机译:V2O5-TiO2气凝胶催化剂的制备方法对NH3选择性还原NO的影响

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IntroductionThe emission of nitrogen oxides (NO, NO2 and N2O) produced during high temperature combustion processes, from both mobile and stationary sources, is one of the most important current environmental issues that concerns the scientific community. The selective catalytic reduction with ammonia (NH3-SCR) is one of the most effective post-treatment for the abatement of Nox emission to the atmosphere [1]. Among NH3-SCR catalysts, V2O5 supported on TiO2 is generally recognized as the most active and selective catalyst. It is well-known that TiO2 can be obtained only with a relatively low specific surface area and less thermal and mechanical resistance than other oxides, such as for example silica. To overcome this, the sol gel method has been proposed as an alternative to synthesize catalysts with a high surface area and stable active phase [2]. In this view point aerogels which can be prepared via the sol-gel method and the subsequent removal of solvent by supercritical drying have attracted much attention as catalyst supports. Until now, some works have been reported to apply titania-based aerogels to NH3-SCR [3-6].
机译:简介高温燃烧过程中从移动源和固定源排放的氮氧化物(NO,NO2和N2O)的排放是当前引起科学界关注的最重要的环境问题之一。氨选择性催化还原(NH3-SCR)是减少向大气排放NOx的最有效的后处理方法之一[1]。在NH3-SCR催化剂中,负载在TiO2上的V2O5通常被认为是最具活性和选择性的催化剂。众所周知,与其它氧化物,例如二氧化硅相比,只能以较低的比表面积和较低的热阻和机械阻力来获得TiO 2。为了克服这个问题,提出了溶胶凝胶法作为合成具有高表面积和稳定活性相的催化剂的替代方法[2]。从这一观点出发,可以通过溶胶-凝胶法制备的气凝胶以及随后通过超临界干燥除去溶剂的气凝胶作为催化剂载体已经引起了广泛的关注。到现在为止,已经报道了一些将二氧化钛气凝胶应用于NH3-SCR的工作[3-6]。

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  • 会议地点 太原
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    Department of Applied Chemistry, Division of Biotechnology and Nanotechnology, Ajou University, Wonchun-Dong, Yeongtong-Gu,Suwon, 443-749, Republic of Korea;

    Division of Chemical Engineering and Materials Engineering and Division of Energy Systems Research, Ajou University, Wonchun-Dong, Yeongtong-Gu, Suwon, 443-749, Republic of Korea Clean Technology Research Center, Hawolgok-dong, Seongbuk-Gu,Seoul, 136-791,;

    Division of Chemical Engineering and Materials Engineering and Division of Energy Systems Research, Ajou University, Wonchun-Dong, Yeongtong-Gu, Suwon, 443-749, Republic of Korea;

    Division of Chemical Engineering and Materials Engineering and Division of Energy Systems Research, Ajou University, Wonchun-Dong, Yeongtong-Gu, Suwon, 443-749, Republic of Korea;

    Division of Chemical Engineering and Materials Engineering and Division of Energy Systems Research,Ajou University, Wonchun-Dong, Yeongtong-Gu, Suwon, 443-749, Republic of Korea;

    Clean Technology Research Center, Hawolgok-dong, Seongbuk-Gu,Seoul, 136-791, Republic of Korea;

    Department of Applied Chemistry, Division of Biotechnology and Nanotechnology, Ajou University, Wonchun-Dong, Yeongtong-Gu,Suwon, 443-749, Republic of Korea;

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