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Process for converting heavy petroleum fractions for producing a catalytic cracking feedstrock and middle distillates with a low sulfur content

机译:转化重质石油馏分的方法,以生产低硫含量的催化裂化原料油和中间馏分油

摘要

The invention relates to a process and installation for treating heavy petroleum feedstocks for producing a gas oil fraction that has a sulfur content of less than 50 ppm and most often 10 ppm that includes the following stages: a) mild hydrocracking in a fixed catalyst bed, b) separation from hydrogen sulfide of a distillate fraction that includes a gas oil fraction and a heavier fraction than the gas oil, c) hydrotreatment (including desulfurization) of said distillate fraction, and d) separation of a gas oil fraction with less than 50 ppm of sulfur. Advantageously, the heavy fraction is sent into catalytic cracking. The process preferably operates with make-up hydrogen that is brought to stage c), and very advantageously all of the make-up hydrogen of the process in introduced in stage c).
机译:本发明涉及一种处理重质石油原料的方法和装置,以生产硫含量小于50ppm,最通常为10ppm的粗柴油馏分,包括以下步骤:a)在固定催化剂床上的温和加氢裂化, b)从硫化氢中分离出包括粗柴油馏分和比粗柴油重的馏分的馏出馏分,c)所述馏分的加氢处理(包括脱硫),和d)分离小于50的粗柴油馏分。硫的ppm。有利地,将重质馏分送入催化裂化中。该方法优选在进入步骤c)的补充氢下进行,并且非常有利地,在步骤c)中引入的该方法的所有补充氢。

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