首页> 外国专利> PROCESS FOR PRODUCTION OF LIGHT OLEFINS AND BTX USING FCC UNIT PROCESSING HEAVY FEEDSTOCK OIL OF HIGHLY HYDROTREATED VGO TYPE AND COUPLED WITH AROMATIC COMPLEX

PROCESS FOR PRODUCTION OF LIGHT OLEFINS AND BTX USING FCC UNIT PROCESSING HEAVY FEEDSTOCK OIL OF HIGHLY HYDROTREATED VGO TYPE AND COUPLED WITH AROMATIC COMPLEX

机译:利用FCC装置加工轻质VGO型重芳烃加芳族配合物的轻质烯烃和BTX的工艺

摘要

PROBLEM TO BE SOLVED: To solve specific thermal balancing problems posed by the cracking of highly hydrogenated cuts in FCC processes and linked to the fact that these feedstock oils are not good coke precursors.SOLUTION: A process for the production of light olefins and BTX from a first feedstock oil of a hydrotreated VGO or unconverted oil (UCO) type resulting from hydrocracking, or from any mixture of these two feedstock oils, and from a second naphtha-type feedstock oil with an initial distillation point greater than 30°C and a final distillation point less than 220°C. The process comprises a catalytic cracking (FCC) unit processing the hydrotreated VGO feedstock oil or the unconverted oil, a catalytic reforming unit (REF) processing a feedstock oil referred to as naphtha (30°C-220°C), and an aromatic complex (AC) fed by the catalytic reforming (REF) effluents and a fraction referred to as LCN (IP-160°C) of the FCC effluents.
机译:解决的问题:解决由FCC工艺中高度氢化的馏分裂解所引起的特定热平衡问题,并与这些原料油不是优质的焦炭前体这一事实联系起来。加氢裂化或这两种原料油的任何混合物产生的加氢VGO或未转化油(UCO)型的第一原料油,以及初始蒸馏点大于30°C的第二种石脑油型原料油和最终蒸馏点低于220℃。该方法包括处理加氢处理的VGO原料油或未转化油的催化裂化(FCC)单元,处理被称为石脑油(30°C-220°C)的原料油的催化重整单元(REF)和(AC)由催化重整(REF)废水进料,以及一部分被称为LCC(IP-160°C)的FCC废水。

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