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Improvements relating to the preparation of catalysts for the refining of lubricating oils and to the use of such catalysts in such refining

机译:与用于精制润滑油的催化剂的制备有关的改进以及在此类精制中使用此类催化剂的改进

摘要

A catalyst useful for refining lubricating oils consists of Al2O3 and 4-12% of MoO3, 6-20% of Fe2O3, the content of Fe2O3 being at least equal to the content of MoO3. The catalyst may be activated by contact in the presence of hydrogen with a sulphur-containing mineral oil at a temperature of at least 300 DEG C. for a period of at least 24 hours. The Al2O3 used in making the catalyst is preferably g -Al2O3 obtained by calcination of hydrargillite at above 500 DEG C. Suitably the Al2O3 used has pores of approximately 30 and surface area of 250 sq. m./gm. Preferably the Al2O3 is impregnated with a solution of ferric nitrate which has been acidified with nitric acid and thereafter dried at 110 DEG C., calcined at 550 DEG C., impregnated with ammonium molybdate solution and further dried and calcined. Lubricating oils are contacted in the presence of hydrogen at 150 DEG -340 DEG C. with catalysts as described above. Preferably the hydrogen pressure is 5-70 atmospheres and the hydrogen feed rate is 5-150 volumes per volume of oil treated. An example is given.
机译:用于精制润滑油的催化剂由Al 2 O 3和4-12%的MoO 3,6-20%的Fe 2 O 3组成,Fe 2 O 3的含量至少等于MoO 3的含量。催化剂可以通过在氢气存在下与含硫的矿物油在至少300℃的温度下接触至少24小时来活化。用于制备催化剂的Al 2 O 3优选是通过在超过500℃下煅烧水辉石获得的g -Al 2 O 3。合适地,所使用的Al 2 O 3具有约30个孔和250平方米/克的表面积。优选将Al 2 O 3浸入已用硝酸酸化的硝酸铁溶液中,然后在110℃下干燥,在550℃下煅烧,再用钼酸铵溶液浸渍,然后进一步干燥和煅烧。使润滑油在氢存在下于150℃-340℃下与如上所述的催化剂接触。氢气压力优选为5-70个大气压,并且氢气进料速率为每体积处理过的油5-150体积。举一个例子。

著录项

  • 公开/公告号GB917345A

    专利类型

  • 公开/公告日1963-02-06

    原文格式PDF

  • 申请/专利权人 THE BRITISH PETROLEUM COMPANY LIMITED;

    申请/专利号GB19620031863

  • 发明设计人

    申请日1959-04-23

  • 分类号B01J23/88;B01J23/881;B01J23/882;C10G45/08;

  • 国家 GB

  • 入库时间 2022-08-23 17:00:51

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