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抚顺石油化工研究院近期开发的３９３６馏分油加氢精制催化剂，以Ｍｏ－Ｎｉ为加氢组分，用低硅稳定的氧化铝作载体，加氢活性高、稳定性好，主要用于加氢裂化原料油的加氢脱硫、加氢脱氮和芳烃加氢饱和。试验结果表明，在模拟工业加氢裂化装置的精制条件下，以氮含量１４２５～１９００μｇ／ｇ、干点５１８～５６４℃的ＶＧＯ与ＣＧＯ等多种混合油为原料，精制油氮含量为４～８μｇ／ｇ，加氢脱氮率为９９．４％～９９．８１％。该催化剂１９９５年１月开始在茂名石油化工公司８０万ｔ／ａ加氢裂化装置上应用，加工干点５３４℃的进口原油混合ＶＧＯ，在精制油碱性氮含量＜２μｇ／ｇ的情况下，精制反应器的加权平均温度为３８２．５℃，加氢脱氮效果良好。
Fushun Petrochemical Research Institute recently developed 3936 distillate hydrotreating catalyst to Mo-Ni as a hydrogenation component, with low silica stabilized alumina as a carrier, high hydrogenation activity, good stability, mainly for hydrogenation Hydrodesulfurization of cracked feedstock, hydrodenitrogenation and saturation of aromatics hydrogenation. The experimental results show that under the condition of simulating the industrial hydrocracking unit, the mixed oil of VGO and CGO with nitrogen content of 1425-1900μg / g and dry point of 518-564 ℃ is used as raw material, the refined oil nitrogen content is 4 ~ 8μg / g, the hydrodenitrogenation rate of 99.4% ~ 99.81%. The catalyst started to be used on the 800,000 t / a hydrocracking unit of Maoming Petrochemical Company in January 1995. The imported crude oil mixed VGO with the dry point of 534 ℃ was processed. When the basic nitrogen content of refined oil was <2μg / g, The weighted average temperature of the refined reactor was 382.5 ° C, and the hydrodenitrogenation effect was good.