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PROCESS FOR PRODUCING CATALYTIC CRACKING GASOLINE WITH A HIGH OCTANE NUMBER

机译:辛烷值高的催化裂化汽油的生产方法

摘要

The present disclosure relates to a process for producing catalytic cracking gasoline comprising the following steps: i) subjecting a heavy feedstock oil to a catalytic cracking reaction in the presence of a first catalytic cracking catalyst to obtain a first reaction product; ii) subjecting a hydrogenated cycle oil to a catalytic cracking reaction in the presence of a second catalytic cracking catalyst to obtain a second reaction product; iii) separating a mixture of the first reaction product and the second reaction product to obtain a catalytic cracking gasoline and a catalytic cracking light cycle oil; iv) subjecting the catalytic cracking light cycle oil or a fraction thereof to hydrogenation to obtain a hydrogenated product; and v) recycling the hydrogenated product to the step ii) as the hydrogenated cycle oil. The present disclosure also relates to a catalytic cracking system for carrying out the process. The process and system according to the present application are capable of providing optimized reaction conditions for the hydrogenated cycle oil and the heavy feedstock oil, thereby providing a high yield of high-octane gasoline.
机译:本公开涉及一种生产催化裂化汽油的方法,其包括以下步骤:i)在第一催化裂化催化剂的存在下使重质原料油进行催化裂化反应以获得第一反应产物; ii)在第二催化裂化催化剂的存在下使氢化循环油进行催化裂化反应,得到第二反应产物; iii)分离第一反应产物和第二反应产物的混合物以获得催化裂化汽油和催化裂化轻循环油; iv)对催化裂化轻循环油或其馏分进行氢化以获得氢化产物; v)将氢化产物作为氢化循环油再循环至步骤ii)。本公开还涉及用于进行该方法的催化裂化系统。根据本申请的方法和系统能够为氢化循环油和重质原料油提供优化的反应条件,从而提供高收率的高辛烷值汽油。

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