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Supported catalyst - for acrylic acid prodn contg oxides of nickel, cobalt, iron, phosphorus, potassium and molybdenum

机译:负载型催化剂-用于丙烯酸,镍,钴,铁,磷,钾和钼的丙烯酸类氧化物

摘要

Supported catalyst contg. the active elements in the atomic ratio Ni3-12Co0-12Fe0.5-10Bi0.5-10, PO, 1-6K0.001-2Mo12O37-118 the indices for Ni and Co being not simultaneously zero, on a solid support with a particle size of 0.01-5mm is prepd. by (a) applying to the support an aqs. soln. of ammonium heptamolybdate and phosphoric acid in =1 impregnation stages, the volume of soln. applied being 1-2 times the predetermined pore volume of the support, (b) drying for 3-10 hrs. at 100-300 degrees C after each impregnation, (c) applying to the support an aqs. nitric acid soln, iron, bismuth, potassium and nickel and/or cobalt niraes in =1 impregnation stages, the volume of soln. applied being 1-2 times the predetermined pore volume of the support, (d) maintaning for 2-12 hrs. at 70-95 degrees C after each impregnation, (e) drying for 3-10 hs. at 100-300 degrees C and (f) sintering for 0.5-10 hrs. at 400-700 degrees C so that the catalyst has a BET surface of 5-100 m2/g. Used for prepn. of acrylic acid by the one stage oxidn. of propylene and/or acrolein with oxygen in the gas phase. High yields and conversions are obtained without the need for recycling unconverted reactants, by products and inert gases.
机译:负载型催化剂续在具有颗粒的固体载体上,原子比为Ni3-12Co0-12Fe0.5-10Bi0.5-10,PO,1-6K0.001-2Mo12O37-118的活性元素Ni和Co的指数不同时为零准备的尺寸为0.01-5mm。通过(a)向支持人提出申请soln。 ≥1的浸渍阶段的七钼酸铵和磷酸的溶解量。施加的量是载体预定孔体积的1-2倍,(b)干燥3-10小时。每次浸渍后,在100-300摄氏度下(c)将aq。硝酸盐溶液,铁,铋,钾和镍和/或钴浸渍物在> = 1的浸渍阶段,溶液的体积。施加的量是载体预定孔体积的1-2倍,(d)保持2-12小时。每次浸渍后,在70-95摄氏度下(e)干燥3-10小时。在100-300摄氏度下进行(f)烧结0.5-10小时。在400-700摄氏度下,催化剂的BET表面积为5-100平方米/克。用于准备。一步氧化生成丙烯酸。在气相中加入丙烯和/或丙烯醛。无需回收未转化的反应物,副产物和惰性气体即可获得高收率和转化率。

著录项

  • 公开/公告号FR2148578A1

    专利类型

  • 公开/公告日1973-03-23

    原文格式PDF

  • 申请/专利权人 KNAPSACK AG;

    申请/专利号FR19720028798

  • 发明设计人

    申请日1972-08-09

  • 分类号B01J11/00;

  • 国家 FR

  • 入库时间 2022-08-23 06:43:14

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