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METHOD hydrotreating the raffinate oil fractions in the presence of catalyst systems

机译:方法在催化剂体系存在下对提余油馏分进行加氢处理

摘要

Method hydrotreating raffinate oil fractions in the presence of a catalyst system containing nickel oxides, cobalt, molybdenum, tungsten, aluminum, followed by solvent dewaxing hydrotreatment product, wherein the hydrotreated oil raffinates is carried out by contacting the feedstock in the first stage with the catalyst under Content, wt .%: nickel oxide - 3,2-5,1; Tungsten oxide - 20,0-31,5; Phosphorus oxide - 0.5-0.8; aluminum oxide - to 100; the second stage - of products of the first stage with the catalyst under Content, wt% cobalt oxide - 5.0;. molybdenum oxide - 19.0; Phosphorus oxide - 0.8; aluminum oxide - to 100 at a volume ratio of catalysts of the first and second steps of 1: 1-1: 11 and the operating conditions for the steps of: a temperature of 300-390 ° C, pressure 4.0-5.0 MPa, volumetric feed rate (ISPS) 0.5-2.0 hours, circulation of the multiplicity of hydrogen-containing gas (K) 500-1000 nm / msyrya.
机译:方法在含有氧化镍,钴,钼,钨,铝的催化剂体系的存在下加氢精制提余油馏分,然后进行溶剂脱蜡加氢处理产物,其中加氢处理的提余油是通过使第一步中的原料与催化剂接触而进行的在含量,wt。%下:氧化镍-3,2-5,1;氧化钨-20,0-31,5;氧化磷-0.5-0.8;氧化铝-至100;第二阶段是第一阶段的产物,催化剂含量为5.0重量%。氧化钼-19.0;氧化磷-0.8;氧化铝-在第一步和第二步催化剂的体积比为1:1-1:11的情况下为100:100,温度为300-390°C,压力为4.0-5.0 MPa,体积进料速度(ISPS)0.5-2.0小时,循环的多种含氢气体(K)500-1000 nm / msyrya。

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