炼油技术与工程 ›› 2023, Vol. 53 ›› Issue (9): 42-45.

• 催化剂和助剂 • 上一篇    下一篇

应对焦化石脑油加氢装置长周期运行的催化剂策略研究

陈光, 徐大海, 丁贺, 范思强   

  1. 1.中国石化催化剂有限公司; 2.中石化(大连)石油化工研究院有限公司
  • 收稿日期:2023-04-11 出版日期:2023-09-15 发布日期:2023-09-27
  • 作者简介:陈光,高级工程师,本科,主要从事馏分油加氢处理工艺技术研究工作。联系电话:010-87997517,E-mail:cheng602.chji@sinopec.com。;
  • 基金资助:
    中国石油化工股份有限公司课题(121013-3);辽宁省“兴辽人才计划”项目(XLYC2002102);大连市高层次创新创业项目(2020RD10);

Research on catalyst strategy for long cycle operation of coking naphtha hydrotreating unit

Chen Guang, Xu Dahai, Ding He, Fan Siqiang   

  1. 1.SINOPEC Catalyst Co., Ltd.; 2.SINOPEC (Dalian) Research Institute of Petroleum and Petrochemicals Co., Ltd.
  • Received:2023-04-11 Online:2023-09-15 Published:2023-09-27

摘要:

目前焦化石脑油加氢装置要实现长周期稳定运行,需要重点解决两大问题:焦化石脑油的二烯烃含量高,在较高的反应温度下易缩合生焦,导致反应器压力降上升;前序加工阶段使用的含硅添加剂会造成二氧化硅在催化剂表面沉积,导致催化剂失活快、运行周期短。针对上述问题提出了解决方案:对焦化石脑油加氢工艺流程进行了改进,增设了低温脱二烯烃保护反应器;配套开发了容硅能力强的加氢捕硅剂及高活性加氢精制催化剂。应用结果表明:焦化石脑油加氢装置的运行周期大幅延长,为装置的长周期运行提供了技术保障。

关键词: 焦化石脑油, 加氢装置, 加氢捕硅剂, 低温保护反应器, 高活性加氢精制催化剂, 硅杂质沉积量

Abstract:

At present, in order to realize long-term stable operation of coking naphtha hydrogenation unit, two major problems need to be solved: high diolefin content in coking naphtha is easy to condense and coke at relatively high reaction temperatures, which leads to the rise of reactor pressure drop; silicon-containing additives used in the pre-processing stage can cause silicon dioxide deposition on the surface of the catalyst, resulting in fast deactivation and short operation cycle of catalyst. These strategies are proposed include the addition of low-temperature de-diolefin protection reactors to the process, the development of hydro-desilicification guard catalyst with strong silicon capacity and high activity hydrofining catalyst. The industrial application results show that the operation cycle of the coking naphtha hydrogenation unit is greatly extended, which provides technical support for the long cycle operation of the unit.

Key words: coking naphtha, hydrogenation unit, hydro-desilicification guard catalyst, low-temperature protection reactors, high activity hydrofining catalyst, deposition amount of silicon impurities