Multi-layer catalyst for producing phthalic anhydride
    6.
    发明授权
    Multi-layer catalyst for producing phthalic anhydride 失效
    用于生产邻苯二甲酸酐的多层催化剂

    公开(公告)号:US07968491B2

    公开(公告)日:2011-06-28

    申请号:US11914147

    申请日:2005-11-28

    摘要: The present invention relates to a catalyst for preparing phthalic anhydride by gas phase oxidation of o-xylene and/or naphthalene, comprising at least three catalyst zones which have different compositions and, from the gas inlet side toward the gas outlet side, are referred to as first, second and third catalyst zone, the catalyst zones having in each case an active composition comprising TiO2 with a content of Na of less than 0.3% by weight, and the active composition content decreasing from the first catalyst zone disposed toward the gas inlet side to the third catalyst zone disposed toward the gas outlet side, with the proviso that (a) the first catalyst zone has an active composition content between about 7 and 12% by weight, (b) the second catalyst zone has an active composition content in the range between 6 and 11% by weight, the active composition content of the second catalyst zone being less than or equal to the active composition content of the first catalyst zone, and (c) the third catalyst zone has an active composition content in the range between 5 and 10% by weight, the active composition content of the third catalyst zone being less than or equal to the active composition content of the second catalyst zone. Also described is a preferred process for preparing such a catalyst and the preferred use of the titanium dioxide used in accordance with the invention.

    摘要翻译: 本发明涉及通过邻二甲苯和/或萘的气相氧化制备邻苯二甲酸酐的催化剂,其包括至少三个具有不同组成的催化剂区域和从气体入口侧朝向气体出口侧的催化剂区域 作为第一,第二和第三催化剂区域,催化剂区域在每种情况下都具有包含Na含量小于0.3重量%的TiO 2的活性组合物,并且活性组合物含量从朝向气体入口设置的第一催化剂区域减少 (a)第一催化剂区的活性组成物含量在约7至12重量%之间,(b)第二催化剂区具有活性组成含量 在6至11重量%的范围内,第二催化剂区的活性组分含量小于或等于第一催化剂区的活性组成含量,和(c) 第三催化剂区的活性组成含量在5至10重量%的范围内,第三催化剂区的活性组成含量小于或等于第二催化剂区的活性组成含量。 还描述了制备这种催化剂的优选方法和根据本发明使用的二氧化钛的优选用途。

    Multi-Layer Catalyst for Producing Phthalic Anhydride
    7.
    发明申请
    Multi-Layer Catalyst for Producing Phthalic Anhydride 失效
    用于生产邻苯二甲酸酐的多层催化剂

    公开(公告)号:US20080064593A1

    公开(公告)日:2008-03-13

    申请号:US11597307

    申请日:2005-05-22

    IPC分类号: B01J21/06

    摘要: The present invention relates to a catalyst for preparing phthalic anhydride by gas phase oxidation of o-xylene and/or naphthalene, comprising at least three catalyst zones which have different compositions and, from the gas inlet side toward the gas outlet side, are referred to as first, second and third catalyst zone, the catalyst zones having in each case an active composition comprising TiO2, and the active composition content decreasing from the first catalyst zone disposed toward the gas inlet side to the third catalyst zone disposed toward the gas outlet side, with the proviso that (a) the first catalyst zone has an active composition content between about 7 and 12% by weight, (b) the second catalyst zone has an active composition content in the range between 6 and 11% by weight, the active composition content of the second catalyst zone being less than or equal to the active composition content of the first catalyst zone, and (c) the third catalyst zone has an active composition content in the range between 5 and 10% by weight, the active composition content of the third catalyst zone being less than or equal to the active composition content of the second catalyst zone. Also described is a preferred process for preparing such a catalyst and the preferred use of the titanium dioxide used in accordance with the invention.

    摘要翻译: 本发明涉及通过邻二甲苯和/或萘的气相氧化制备邻苯二甲酸酐的催化剂,其包括至少三个具有不同组成的催化剂区域和从气体入口侧朝向气体出口侧的催化剂区域 作为第一,第二和第三催化剂区域,催化剂区域在每种情况下都包含包含TiO 2的活性组合物,并且活性组合物含量从朝向气体入口侧设置到第三催化剂区域的第三催化剂区域减少 催化剂区域设置在气体出口侧,条件是(a)第一催化剂区的活性组成含量为约7至12重量%,(b)第二催化剂区的活性组成含量在 6和11重量%,第二催化剂区的活性组分含量小于或等于第一催化剂区的活性组成含量,和(c)第三催化剂区具有活性 组合物含量在5至10重量%的范围内,第三催化剂区的活性组成含量小于或等于第二催化剂区的活性组合物含量。 还描述了制备这种催化剂的优选方法和根据本发明使用的二氧化钛的优选用途。

    SHELL CATALYST, IN PARTICULAR FOR OXIDATION OF METHANOL TO FORMALDEHYDE, AND ALSO METHOD FOR PRODUCTION THEREOF
    8.
    发明申请
    SHELL CATALYST, IN PARTICULAR FOR OXIDATION OF METHANOL TO FORMALDEHYDE, AND ALSO METHOD FOR PRODUCTION THEREOF 有权
    壳催化剂,特别是将甲醇氧化成甲醛,还有其生产方法

    公开(公告)号:US20100016640A1

    公开(公告)日:2010-01-21

    申请号:US12094288

    申请日:2006-11-23

    IPC分类号: B01J23/28 C07C45/29

    摘要: The invention relates to a coated catalyst, especially for oxidation of methanol to formaldehyde, which, on an inert, preferably essentially nonporous, support body, has at least one coating which comprises, before the removal of the organic fractions of components b) and c): (a) oxides, or precursor compounds convertible to the corresponding oxides, of molybdenum and iron, where the molar ratio of Mo:Fe is between 1:1 and 5:1, and optionally further metallic components or metal oxide components or precursor compounds convertible to the corresponding oxides, (b) at least one organic binder, preferably an aqueous dispersion of copolymers, especially selected from vinyl acetate/vinyl laurate, vinyl acetate/ethylene, vinyl acetate/acrylate, vinyl acetate/maleate, styrene/acrylate or mixtures thereof, and (c) at least one further component selected from the group consisting of SiO2 sol or precursors thereof, Al2O3 sol or precursors thereof, ZrO2 sol or precursors thereof, TiO2 sol or precursors thereof, waterglass, MgO, cement, monomeric, oligomeric or polymeric silanes, alkoxysilanes, aryloxysilanes, acryloyloxysilanes, aminosilanes, siloxanes or silanols. Additionally described is a process for preparing the catalyst and its preferred use.

    摘要翻译: 本发明涉及一种涂覆的催化剂,特别是用于将甲醇氧化成甲醛,其在惰性,优选基本上无孔的载体上具有至少一个涂层,其包含在除去组分b)和c的有机部分之前 ):(a)钼和铁的氧化物或可转化成相应氧化物的前体化合物,其中Mo:Fe的摩尔比为1:1至5:1,以及任选的其它金属组分或金属氧化物组分或前体 化合物可转化为相应的氧化物,(b)至少一种有机粘合剂,优选共聚物的水分散体,特别是选自乙酸乙烯酯/月桂酸乙烯酯,乙酸乙烯酯/乙烯,乙酸乙烯酯/丙烯酸酯,乙酸乙烯酯/马来酸酯,苯乙烯/丙烯酸酯 或其混合物,和(c)至少一种选自SiO 2溶胶或其前体,Al 2 O 3溶胶或其前体,ZrO 2溶胶或其前体,TiO 2溶胶或预制物 游离体,水玻璃,MgO,水泥,单体,低聚或聚合硅烷,烷氧基硅烷,芳氧基硅烷,丙烯酰氧基硅烷,氨基硅烷,硅氧烷或硅烷醇。 另外描述了制备催化剂及其优选用途的方法。