首页> 外国专利> High active composite catalyst for simultaneous oxidation of halogenated volatile organic compoundsHVOCs and volatile organic compoundsVOCs and prepararation method of it and controlling method of its reaction

High active composite catalyst for simultaneous oxidation of halogenated volatile organic compoundsHVOCs and volatile organic compoundsVOCs and prepararation method of it and controlling method of its reaction

机译:用于同时氧化卤代挥发性有机化合物HVOC和挥发性有机化合物VOC的高活性复合催化剂及其制备方法和反应控制方法

摘要

The present invention relates to a method of controlling a catalytic reaction activity and which at the same time decomposed effectively the volatile organic compounds and the general VOCs that combines the halogen component can be detoxified (無毒 化) composite oxide catalyst and a method of manufacturing and using the same. .; And active compound oxide catalysts of the invention are two-component or three is more components as a component system catalyst and a main catalyst and co-catalyst and a support, the main catalyst to the active metal is Ru, the co-catalyst to the noble metal Pt and Sn, Zn , Cr, Ce, Co, Mn, Zr, W, a metal oxide of one or more components selected from the group consisting of transition metals such as V in the form of oxide, the support include Al 2 O 3, TiO 2, ZrO 2, SiO as second choice, and a support consisting of one or more substances of which there is a technical feature.; The catalyst of the present invention, main catalyst and co-catalyst 0.05~8wt% by manufactures dispersing 0.5~10wt% to the support, a two-component catalyst is one method for each of the active metal constituting the catalyst from excess solution impregnation and co-precipitation production, and to prepare a solution containing a predetermined amount of the metal precursor such that the amount of the metal oxide which require manufacturing and then dispersed in the support, and the multi-component catalyst coprecipitation a Ru-Sn / Al 2 O 3 and excess solution after the first produced in one way from impregnation complete firing, and technically characterized in that the manufactured through a process in which the final impregnated with a different co-catalyst, and then drying and firing.; And halogenated volatile organic compounds and volatile general control of the catalytic reaction that uses the high activity catalyst composite oxide of the present invention to eliminate oxidation of the organic compound is 150~450 ℃ reaction temperature, and the reaction gas space velocity (GHSV) 2,000~80,000hr - 1, characterized by the reaction in terms of the concentration of moisture 0.05~25vol% also to proceed.; High activity composite oxidation catalyst of the present invention are durable and VOCs oxidation activity as compared to noble metal catalysts, such as the high Pt and Pd oxidation activity for VOCs inferior this is rather characteristic that shows a better activity when HVOCs are mixed exhaust a bar, the solvent and washing step, HVOCs and VOCs generated in the various industrial fields such as petrochemical manufacturing processes in the same time can be removed by oxidation.; Then, the highly active compound oxide catalysts of the present invention group developed HVOCs catalyst losses and waste disposal problems, such as a two-component using solved by a transition metal not only environmentally friendly, or the active oxidation of the respective metal as a component system catalyst to be generated in the catalyst the wide compatibility width economically by reducing the precious metal content, with a synergistic effect can be expected.
机译:控制催化反应活性的方法技术领域本发明涉及一种控制催化反应活性的方法,该方法可有效地分解挥发性有机化合物和结合了卤素成分的一般VOC,该复合VOCs可被无毒化复合氧化物催化剂解毒。使用相同的。 。;并且本发明的活性化合物氧化物催化剂为二组分或三组分以上作为组分体系催化剂和主催化剂,助催化剂和载体,活性金属的主要催化剂为Ru,助催化剂的助催化剂。贵金属Pt和Sn,Zn,Cr,Ce,Co,Mn,Zr,W,一种或多种选自氧化物等过渡金属(例如V形式)的金属氧化物,载体包括Al < Sub> 2 O 3, TiO 2, ZrO 2, SiO作为 second 选择,以及由一种或多种具有技术特征的物质组成的支撑物;通过将0.5〜10wt%分散到载体上来制造本发明的催化剂,主催化剂和助催化剂0.05〜8wt%,两组分催化剂是一种通过过量溶液浸渍和浸渍来构成催化剂的每种活性金属的方法。共沉淀生产,并且制备包含预定量的金属前体的溶液,使得一定量的金属氧化物需要制造然后分散在载体中,并且多组分催化剂共沉淀Ru-Sn / Al < Sub> 2 O 3 和过量溶液在第一次浸渍后以一种方式完全烧制而成,并且技术上的特征在于,其制造过程是通过最终浸渍不同的钴-催化剂,然后干燥和燃烧。而卤代挥发性有机化合物与挥发性催化反应的一般控制,即使用本发明的高活性催化剂复合氧化物消除有机化合物的氧化反应温度为150〜450℃,反应气体空速(GHSV)为2,000 〜80,000hr -1,,其特征在于以水分浓​​度0.05〜25vol%进行反应。与贵金属催化剂相比,本发明的高活性复合氧化催化剂耐用且VOCs氧化活性高,例如对VOC的高Pt和Pd氧化活性较差。当HVOC混合排气时,其显示出更好的活性可以通过氧化除去溶剂和洗涤步骤,同时除去在诸如石油化学制造过程的各种工业领域中产生的HVOC和VOC。然后,本发明的高活性复合氧化物催化剂出现了HVOCs催化剂的损失和废物处理问题,例如两组分使用过渡金属不仅解决了环境友好的问题,或者相应金属作为组分的活性氧化通过降低贵金属含量,可以经济地在催化剂中以宽的相容性宽度生成催化剂体系催化剂,并具有协同作用。

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