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Process for deep desulfurization of cracked gasoline with minimum octane loss

机译:以最小的辛烷值损失对裂化汽油进行深度脱硫的方法

摘要

The present invention provides a process for deep desulphurization of cracked gasoline with minimum octane loss of about 1-2 units. In this process full range cracked gasoline from FCC, Coker, Visbreaker etc is sent to Diolefin Saturation Reactor for selective saturation of diolefins. After saturation of diolefins, the stream is sent to Splitter for splitting into three cuts i.e Light Cut (IBP-70° C.), Intermediate Cut (70-90° C.) and Heavy Cut (90-210° C.). The Light Cut which contains majority of the high octane olefins and mercaptan sulfur is desulfurized with caustic treatment using Continuous Film Contactor (CFC). The sulfur in the Intermediate Cut is also predominantly mercaptans and the cut can be desulfurized by caustic treatment using CFC along with Light cut or separately desulfurized before being sent for isomerization. The Heavy Cut containing mainly thiophinic sulfur compounds is treated either by using conventional HDS process or reactive adsorption process.
机译:本发明提供了一种以大约1-2个单位的最小辛烷值损失对裂化汽油进行深度脱硫的方法。在此过程中,将来自FCC,焦化器,Visbreaker等的全系列裂化汽油送入二烯烃饱和反应器,以选择性地使二烯烃饱和。在二烯烃饱和之后,将料流送入分流器以分成三个馏分,即轻馏分(IBP-70℃),中馏分(70-90℃)和重馏分(90-210℃)。使用连续膜接触器(CFC),通过苛性处理将含有大多数高辛烷值烯烃和硫醇硫的轻馏分进行脱硫。中间馏分中的硫也主要是硫醇,该馏分可通过使用CFC和轻馏分的苛性碱处理进行脱硫,或在送入异构化之前进行单独脱硫。通过使用常规HDS工艺或反应吸附工艺处理主要含有硫菲硫化合物的重馏分。

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