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CATALYST FOR HYDROCRACKING OF HEAVY OILS AND METHOD OF HYDROCRACKING HEAVY OILS

机译:重油加氢裂化催化剂和重油加氢裂化方法

摘要

A catalyst for hydrocracking of heavy oils comprises iron and active carbon having an MCH conversion rate of 40-80 %, a specific surface area of 600-1000 m2/g of, a pore volume of 0.5 to 1.4 cm3/g, 2-50 nanometers' mesopore volume of not less than 60% and the average pore diameter of 3-6 nanometers, the iron being carried on the active carbon in an amount of 1 to 20 wt.% to the active carbon. The hydrocracking process by using the catalyst includes the first step of conducting hydrocracking at a temperature within the range of 360-450 °C at a hydrogen partial pressure of 2-14 MPaG and the second step of conducting hydrocracking at a temperature within the range of 400-480 °C at a hydrogen partial pressure of 2-18 MPaG, which can suppress generation of coke and remove in a high efficiency heavy metals such as Ni and V, asphaltene, residual carbon, sulfur and nitrogen from the heavy oils.
机译:用于重油加氢裂化的催化剂包含铁和活性炭,其MCH转化率为40-80%,比表面积为600-1000 m2 / g,孔体积为0.5至1.4 cm3 / g,2-50纳米的中孔体积不少于60%,平均孔径为3-6纳米,其中铁以相对于活性炭1至20wt。%的量负载在活性炭上。使用催化剂进行加氢裂化的步骤包括第一步,在氢气分压为2-14 MPaG的情况下,在360-450°C的温度范围内进行加氢裂化;第二步,在80-450℃的温度范围内进行加氢裂化。在2-18 MPaG的氢气分压下可在400-480°C的温度下抑制焦炭的生成,并以高效率去除重油中的重金属(例如Ni和V,沥青质,残留的碳,硫和氮)。

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