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Method of converting heavy fractions oil to produce a load of catalytic cracking of distillates of low sulfur content

机译:转化重馏分油以产生低硫含量馏出物催化裂化负荷的方法

摘要

Treatment of a charge of which at least 80% has a boiling point above 340 degrees C and contains at least 0.05% sulfur, to produce a gasoil of sulfur content less than 50 ppm by a 4 stage process involving mild hydrocracking, separation of gases form the effluent formed, hydrotreatment and separation of hydrogen with production of a gasoil of less than 50 ppm of sulfur. ??The process comprises: ??(a) mild hydrocracking in a catalytic fixed bed at 330-500 degrees C, 2-12 MPa, VVH of 0.1-10 h-1 and in the presence of 100-5000 Nm3 of H2/m3 of charge, the net conversion to products boiling below 360 degrees C being 10-50 wt.%; ??(b) the separation from the effluent of a gas containing H2, H2S and a fraction heavier than the gasoil; ??(c) hydrotreatment by contact with a catalyst of a distillate cut obtained in (b) which includes a gasoil fraction at 300-500 degrees C, 2-12 MPa, a VVH of 0.1-10 h-1 and in the presence of 200-5000 Nm3 of H2/m3 of charge; and ??(d) the separation of H2, gases and a gasoil of S content less than 50 ppm weight. ??An Independent claim is also included for the apparatus used for the above process.
机译:通过涉及温和加氢裂化的4阶段工艺处理至少80%的沸点高于340摄氏度且含有至少0.05%的硫的装料,以生产硫含量小于50 ppm的粗柴油生成的废水,加氢处理和分离氢气,并产生少于50 ppm硫的粗柴油。所述方法包括:(a)在催化固定床中于330-500℃,2-12MPa,VVH为0.1-10h -1且在100℃存在下进行轻度加氢裂化。 -5000Nm 3的H 2 / m 3电荷,至沸点低于360℃的产物的净转化率为10-50重量%; (b)从废气中分离出含有H 2,H 2 S和比粗柴油重的馏分的气体; (c)通过与(b)中获得的馏分馏分的催化剂接触进行加氢处理,所述馏分包括在300-500℃,2-12MPa,VVH为0.1-10h -1的粗柴油馏分。在H 2 / m 3电荷为200-5000 Nm 3的情况下; (d)H 2,气体和S含量小于50ppm重量的粗柴油的分离。用于上述过程的设备也包括独立权利要求。

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