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METHOD OF PREPARING CATALYTIC SYSTEM FOR HYDROFINING OF HYDROCARBON FEEDSTOCK
METHOD OF PREPARING CATALYTIC SYSTEM FOR HYDROFINING OF HYDROCARBON FEEDSTOCK
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机译:制备烃原料的加氢催化体系的方法
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FIELD: petroleum processing. SUBSTANCE: system is prepared by layerwise charging oxide and pre-sulfidized catalysts obtained by mixing of (i) catalyst granules comprising carrier and one or more catalytically active metals on oxide form and (ii) elementary sulfur in the form of particles lesser in size than particles of catalyst and taken in proportion no more than 50% on the weight of catalyst at temperature below boiling point of sulfur. Mixture is heated at temperature above boiling point of sulfur in air or inert gas flow at continuous stirring. Layerwise charged pre-sulfidized and oxide catalysts are treated by circulating hydrogen-containing or inert gas at flow rate 2.0-4.5 m3/m3 at 100-250o and excessive pressure 10-20 atm. Circulation of gas through catalytic system is preferably started when temperature of catalyst in the inlet of reactor achieves 100-140o and temperature is then raised with a rate of 10-20o/h. Stirring of components is preferably effected in rotary-drum apparatus at rotation speed 0.7-2.5 rpm and with residence time at least 60 min. EFFECT: simplified preparation procedure and simplified use of catalytic system in hydrocarbon hydrofining process. 3 cl, 3 tbl, 9 ex
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机译:领域:石油加工。物质:通过将氧化物和预硫化的催化剂分层装料来制备系统,该催化剂是通过将(i)包含载体和一种或多种催化活性金属的催化剂颗粒以氧化物形式和(ii)尺寸小于在低于硫的沸点的温度下,不超过催化剂重量的50%的催化剂颗粒。在连续搅拌下,将混合物加热到高于空气中硫的沸点或惰性气流的温度。通过使含氢或惰性气体在100-250 下以2.0-4.5 m 3 Sup> / m 3 Sup>的流量循环处理分层装料的预硫化和氧化物催化剂o Sup>和过高的压力10-20 atm。当反应器入口的催化剂温度达到100-140 o Sup>,然后以10-20 o Sup>的速度升高温度时,优选开始通过催化系统的气体循环。 /H。组分的搅拌优选在转鼓设备中以0.7-2.5rpm的转速和至少60分钟的停留时间进行。效果:简化了制备程序,简化了烃加氢精制过程中催化体系的使用。 3 cl,3 tbl,9前
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