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炼油厂混合C4深度脱硫与加工方案探讨
引用本文:刘勇,杨黎峰,刘争飞.炼油厂混合C4深度脱硫与加工方案探讨[J].石油与天然气化工,2013,42(3):222-226.
作者姓名:刘勇  杨黎峰  刘争飞
作者单位:中国石油大学(北京)重质油国家重点实验室
基金项目:国家自然科学基金项目(21073235,21276277);中国石油天然气股份有限公司基金项目(0809-05-02).
摘    要:介绍了国内外典型的选择性加氢脱硫工艺及加氢脱硫-辛烷值恢复工艺的研究进展。对各工艺的流程及特点进行比较,并概述了目前工业上常用的FCC汽油加氢脱硫催化剂。最后,对FCC汽油加氢脱硫技术的发展趋势进行了展望。

关 键 词:加氢脱硫  辛烷值恢复  催化剂  研究发展趋势
收稿时间:4/1/2013 12:00:00 AM
修稿时间:2013/4/12 0:00:00

Deep desulfurization and processing scheme of mixing C4 in refineries
Liu Yong,Yang Lifeng and Liu Zhengfei.Deep desulfurization and processing scheme of mixing C4 in refineries[J].Chemical Engineering of Oil and Gas,2013,42(3):222-226.
Authors:Liu Yong  Yang Lifeng and Liu Zhengfei
Affiliation:(State Key Laboratary of Heavy Oil Processing, China University of Petroleum ,Beijing 102249, China)
Abstract:The research progresses of typical selective hydrodesulfurization process and hydro desulfurization-octane recovery process at home and abroad were reviewed. The processes and characteristics of each process were compared. The current commercial hydrodesulfurization cata- lysts of FCC gasoline were also summarized. Finally, the development tendency of hydrodesulfu- rization technologies was put forward.
Keywords:hydrodesulfurization  octane number recovery  catalyst  research developmenttendency
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