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METHOD FOR CONVERSION OF LOW-GRADE RAW FEEDSTOCK TO HIGH-QUALITY OIL FUEL

机译:低级生料转化为高品质燃油的方法

摘要

FIELD: oil and gas industry.;SUBSTANCE: invention is related to process of hydrocarbon oil catalytic conversion. Invention is referred to conversion of law-grade raw feedstock which is input to the first reaction zone in catalytic conversion reactor and subjected to catalytic reactions of cracking by means of raw feedstock contacting with catalyst of catalytic conversion. Vapours and used catalyst are mixed at random basis with light raw feedstock and/or cooling medium and are introduced into the second reaction zone in catalytic conversion reactor for the purpose of further cracking, hydrogen transfer and isomerisation reactor. Products of the reaction are separated from used catalyst by separation into gaseous and solid phases and introduced into separation system in order to obtain dry gas, LPG, petrol and diesel fuel and catalytic gas oil with c suspended catalyst (FGO). Used catalyst is desorbed, regenerated and then hot regenerated catalyst is returned to the reactor. FGO is introduced into hydrofining plant and/or plant for aromatic hydrocarbons separation in order to receive hydrofined FGO and/or FGO raffinate. Hydrofined FGO and/or FGO raffinate is transferred to the first reaction zone of catalytic conversion reactor and/or to other FCC plants for further reactions in order to receive the target oil fuel as a high-quality product.;EFFECT: conversion of low-grade feedstock to high-quality oil fuel and propylene and effective use of oil resources by significant reducing output of dry gas and coke.;21 cl, 4 dwg, 10 tbl, 16 ex
机译:技术领域本发明涉及烃油催化转化的方法。本发明涉及法律级原料的转化,其被输入到催化转化反应器中的第一反应区中,并且通过使原料与催化转化的催化剂接触而进行裂化的催化反应。将蒸气和用过的催化剂与轻质原料和/或冷却介质随机混合,并引入催化转化反应器中的第二反应区中,以进一步裂化,氢转移和异构化反应器。通过分离成气相和固相,将反应产物与用过的催化剂分离,并引入到分离系统中,以获得干燥的气体,LPG,汽油和柴油燃料以及具有悬浮催化剂(FGO)的催化粗柴油。将用过的催化剂解吸,再生,然后将热的再生催化剂返回到反应器中。将FGO引入加氢精制厂和/或用于芳烃分离的工厂中,以接收加氢精制的FGO和/或FGO提余液。加氢精制的FGO和/或FGO提余液被转移到催化转化反应器的第一反应区和/或其他FCC工厂进行进一步反应,以接收目标油燃料为高质量的产物。等级原料生产高质量的石油燃料和丙烯,并通过显着减少干气和焦炭的产量有效利用石油资源。; 21 cl,4 dwg,10 tbl,16 ex

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