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    • 38. 发明授权
    • Method for producing phthalic anhydride
    • 邻苯二甲酸酐的制造方法
    • US06700000B1
    • 2004-03-02
    • US09700452
    • 2000-11-15
    • Thomas HeidemannHerbert Wanjek
    • Thomas HeidemannHerbert Wanjek
    • C07D30789
    • B01J35/0006B01J23/002B01J27/198B01J37/0223B01J2523/00C07D307/89B01J2523/15B01J2523/47B01J2523/51B01J2523/53B01J2523/55
    • Phthalic anhydride is prepared by catalytic gas-phase oxidation of xylene and/or naphthalene by a gas comprising molecular oxygen in a fixed bed at elevated temperature and using at least three coated catalysts arranged in superposed zones, which catalysts have a layer of catalytically active metal oxides applied to a core of support material. In the process described, the catalyst activity rises from zone to zone from the gas inlet end to the gas outlet end and the activity of the catalysts of the individual zones is set such that the least active catalyst comprises a lower amount of active composition and, if desired, additionally more alkali metal selected from the group consisting of potassium, rubidium and cesium as dopant than the catalyst of the next zone and the subsequent even more active catalyst comprises the same amount of active composition and even less alkali metal as dopant or a greater amount of active composition and, if desired, less alkali metal as dopant than the catalyst of the second zone, with further conditions.
    • 邻苯二甲酸酐通过在固定床中在升高的温度下通过包含分子氧的气体二甲苯和/或萘的催化气相氧化制备,并且使用布置在重叠区中的至少三个涂覆的催化剂,该催化剂具有催化活性金属层 施加到支撑材料的芯的氧化物。 在所描述的方法中,催化剂活性从气体入口端到气体出口端从区域上升,并且各个区域的催化剂的活性被设定为使得最低活性催化剂包含较少量的活性组合物, 如果需要,另外还有更多的选自钾,铷和铯作为掺杂剂的碱金属比下一个区域的催化剂和随后的甚至更活泼的催化剂包含相同量的活性组合物,甚至更少的碱金属作为掺杂剂或 更多量的活性组合物和如果需要,具有比第二区域的催化剂更少的碱金属作为掺杂剂,具有进一步的条件。
    • 39. 发明授权
    • Method for producing phthalic anhydride by means of catalytic vapor-phase oxidation of o-xylol/naphthalene mixtures
    • 通过邻甲酚/萘混合物的催化气相氧化生产邻苯二甲酸酐的方法
    • US06362345B1
    • 2002-03-26
    • US09700427
    • 2000-11-15
    • Thomas HeidemannHeiko ArnoldGerhard HefeleHerbert Wanjek
    • Thomas HeidemannHeiko ArnoldGerhard HefeleHerbert Wanjek
    • C07D30789
    • C07C51/265C07C51/313C07C63/16
    • In a process for preparing phthalic anhydride by catalytic gas-phase oxidation of o-xylene/naphthalene mixtures by molecular oxygen, use is made of a catalyst I in a first zone on the gas inlet side which makes up from 25 to 75 percent by volume of the total catalyst volume, comprising, in each case based on the catalytically active composition, from 1 to 10% by weight of vanadium oxide (calculated as V205), from 1 to 10% by weight of antimony oxide (calculated as Sb203) and from 80 to 98% by weight of titanium dioxide of the anatase type having a BET surface area of from 13 to 28 m2/g and also from 0.05 to 1% by weight of cesium (calculated as Cs) applied to a steatite support and a catalyst II in a second zone which makes up the remaining 75 to 25 percent by volume of the total catalyst volume, comprising, in each case based on the catalytically active composition, from 1 to 10% by weight of vanadium oxide (calculated as V205), from 1 to 10% by weight of antimony oxide (calculated as Sb203) and from 80 to 98% by weight of titanium dioxide of the anatase type having a BET surface area of from 13 to 28 m2/g and from 0.01 to 1% by weight of phosphorus oxide (calculated as P) and also from 0.01 to 0.2% by weight of cesium (calculated as Cs) applied to a steatite support, wherein the cesium content of the catalyst II is less than 15% by weight of the cesium content of the catalyst I and the catalyst I and the catalyst II have been prepared without addition of compounds of niobium.
    • 在通过分子氧的邻二甲苯/萘混合物的催化气相氧化制备邻苯二甲酸酐的方法中,使用在气体入口侧的第一区中的催化剂I,其占25-75体积% 的总催化剂体积,包括在每种情况下基于催化活性组合物,1-10重量%的氧化钒(按V205计算),1-10重量%的氧化锑(以Sb 2 O 3计)和 80至98重量%的具有13至28平方米/克的BET表面积为13至28平方米/克的锐钛矿型二氧化钛和0.05至1重量%的应用于滑石支撑的铯(以Cs计算) 催化剂II在构成总催化剂体积的剩余75至25体积%的第二区域中,在每种情况下基于催化活性组合物,包含1-10重量%的氧化钒(以V205计算) ,1至10重量%的氧化锑(计算为 Sb 2 O 3)和80〜98重量%的BET表面积为13〜28m 2 / g,0.01〜1重量%的氧化磷(P计算)的锐钛矿型二氧化钛,0.01 至0.2重量%的铯(以Cs计算),其中催化剂II的铯含量小于催化剂I的铯含量的15重量%,催化剂I和催化剂II具有 在不添加铌化合物的情况下制备。