Reactor System and Process for the Manufacture of Ethylene Oxide
    24.
    发明申请
    Reactor System and Process for the Manufacture of Ethylene Oxide 审中-公开
    用于制造环氧乙烷的反应器系统和工艺

    公开(公告)号:US20090234144A1

    公开(公告)日:2009-09-17

    申请号:US11886800

    申请日:2006-03-20

    IPC分类号: C07D301/10 B01J8/06

    摘要: A reactor system for the epoxidation of ethylene, which reactor system comprises an elongated tube having an internal tube diameter of more than 40 mm, wherein contained is a catalyst bed of catalyst particles comprising silver and a promoter component deposited on a carrier, which promoter component comprises an element selected from rhenium, tungsten, molybdenum and chromium; a process for the epoxidation of ethylene comprising reacting ethylene with oxygen in the presence of the catalyst bed contained in the reactor system; and a method of preparing ethylene glycol, an ethylene glycol ether or an ethanol amine comprising obtaining ethylene oxide by the process for the epoxidation of ethylene, and converting the ethylene oxide into ethylene glycol, the ethylene glycol ether, or the ethanol amine. Preferably, the internal tube diameter is at least 45 mm.

    摘要翻译: 一种用于乙烯环氧化的反应器系统,该反应器系统包括内管直径大于40mm的细长管,其中包含催化剂床的催化剂床,所述催化剂颗粒包含银和沉积在载体上的助催化剂组分,该促进剂组分 包括选自铼,钨,钼和铬的元素; 一种乙烯环氧化方法,包括在反应器系统中包含的催化剂床存在下使乙烯与氧反应; 以及制备乙二醇,乙二醇醚或乙醇胺的方法,包括通过乙烯环氧化方法获得环氧乙烷,并将环氧乙烷转化为乙二醇,乙二醇醚或乙醇胺。 优选地,内管直径至少为45mm。

    Catalyst for removing aromatic halogenated compounds comprising dioxin, carbon monoxide, and nitrogen oxide and use thereof
    26.
    发明申请
    Catalyst for removing aromatic halogenated compounds comprising dioxin, carbon monoxide, and nitrogen oxide and use thereof 审中-公开
    用于除去包含二恶英,一氧化碳和氮氧化物的芳族卤代化合物的催化剂及其用途

    公开(公告)号:US20060258528A1

    公开(公告)日:2006-11-16

    申请号:US11491139

    申请日:2006-07-24

    IPC分类号: B01J23/00

    摘要: The present invention relates to a catalyst for removing aromatic halogenated compounds comprising dioxin, carbon monoxide and nitrogen oxide simultaneously and a method for preparing the catalyst, more particularly, a catalyst comprising 0.1 to 5% by weight of vanadium, 1 to 12% by weight of metals in 6A family and 0.1 to 10% by weight of Ag in titania carrier or, alternatively, a catalyst produced by impregnating said catalyst in 0.05 to 1M sulfuric acid solution to carry out acid treatment. The catalyst according to the present invention has improved efficiency for removing 1,2-dichlorobenzene as a reactant model of dioxin and carbon monoxide rather than existing catalysts and also, alternative efficiency for removing nitrogen oxide substantially equal to commonly known catalysts, so that the catalyst can effectively control various air pollutants contained in exhaust gas.

    摘要翻译: 本发明涉及一种用于同时除去包含二恶英,一氧化碳和氮氧化物的芳族卤代化合物的催化剂,以及一种制备该催化剂的方法,更具体地说,涉及一种催化剂,其包含0.1-5重量%的钒,1至12重量% 的6A族金属和0.1〜10重量%的Ag在二氧化钛载体中,或者是通过将所述催化剂浸渍在0.05〜1M硫酸溶液中进行酸处理而制备的催化剂。 根据本发明的催化剂具有提高的作为二恶英和一氧化碳的反应物模型的1,2-二氯苯的效率,而不是现有的催化剂,以及用于除去基本上等于通常已知的催化剂的氮氧化物的替代效率,使得催化剂 可有效控制废气中含有的各种空气污染物。

    Calcination in an inert gas in the presence of a small concentration of an oxidizing component
    27.
    发明申请
    Calcination in an inert gas in the presence of a small concentration of an oxidizing component 有权
    在惰性气体中在少量氧化组分存在下煅烧

    公开(公告)号:US20060252639A1

    公开(公告)日:2006-11-09

    申请号:US11124646

    申请日:2005-05-09

    IPC分类号: B01J23/04

    摘要: This invention relates to an improved process for preparing silver catalysts useful for the vapor phase production of ethylene oxide from ethylene and oxygen. An inert support is impregnated with a solution of a catalytically effective amount of a silver containing compound, a promoting amount of an alkali metal containing compound, and a promoting amount of a transition metal containing compound. The impregnated support is calcined by heating at a temperature of from about 200° C. to about 600° C. to convert the silver in the silver containing compound to metallic silver and to decompose and remove substantially all organic materials. The heating is conducted under an atmosphere comprising a combination of an inert gas and from about 10 ppm to about 5% by volume of a gas of an oxygen containing oxidizing component.

    摘要翻译: 本发明涉及一种制备用于从乙烯和氧气气相生产环氧乙烷的银催化剂的改进方法。 用催化有效量的含银化合物,促进量的含碱金属的化合物和促进量的含过渡金属的化合物的溶液浸渍惰性载体。 浸渍的载体通过在约200℃至约600℃的温度下加热煅烧,以将含银化合物中的银转化成金属银,并分解和除去基本上所有的有机材料。 加热在包括惰性气体和约10ppm至约5体积%的含氧氧化组分的气体的组合的气氛下进行。