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A hydrofining catalyst of a distillate oil and production method

机译:馏分油的加氢精制催化剂及其生产方法

摘要

The present invention discloses a hydrofining catalyst. The catalyst has the following composition based on the total weight of the entire catalyst composition: 1-5 % (wt.) nickel oxide, 12-35 % (wt.) tungsten oxide, 1-9 % (wt.) fluorine, and the balancing amount of composite alumina. Said composite alumina is composed of one or several kinds of micropore alumina and one or several kinds of macropore alumina, wherein the weight ratio of micropore alumina to macropore alumina is 75:25 to 50:50. The term "micropore alumina" in the context means the alumina in which the volume of the pore of diameter less than 80 angstrom occupies more than 95 % of its total pore volume, while the term "macropore alumina" in the context means the alumina in which the volume of the pore of diameter 60-600 angstrom occupies more that 70 % of its total pore volume. The pore distribution mentioned above is determined by BET method of nitrogen adsorption at low temperature. This catalyst is especially suitable for the hydrofining of inferior distillates with high sulfure content and boiling range of 80-550 DEG C.
机译:本发明公开了一种加氢精制催化剂。基于整个催化剂组合物的总重量,催化剂具有以下组成:1-5%(重量)的氧化镍,12-35%(重量)的氧化钨,1-9%(重量)的氟和复合氧化铝的平衡量。所述复合氧化铝由一种或几种微孔氧化铝和一种或几种大孔氧化铝组成,其中微孔氧化铝与大孔氧化铝的重量比为75:25至50:50。在本文中,术语“微孔氧化铝”是指直径小于80埃的孔的体积占其总孔体积的95%以上的氧化铝,而在本文中,术语“大孔氧化铝”是指其中的氧化铝。直径为60-600埃的孔的体积占其总孔体积的70%以上。上述孔分布通过低温下氮吸附的BET法确定。该催化剂特别适用于高硫含量和沸点为80-550℃的劣质馏分的加氢精制。

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