石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (4): 25-28.

• 加工工艺 • 上一篇    下一篇

浆态床渣油加氢装置满负荷长周期运行分析

刘沅林,马强,张小龙,潘学义,景晓   

  1. 浙江石油化工有限公司
  • 收稿日期:2025-08-19 修回日期:2025-12-26 出版日期:2026-05-12 发布日期:2026-04-01
  • 通讯作者: 景晓 E-mail:zsh_jingx@rong-sheng.com

ANALYSIS OF FULL-CAPACITY LONG-TERM OPERATION IN SLURRY RESIDUE HYDROGENATION UNIT

  • Received:2025-08-19 Revised:2025-12-26 Online:2026-05-12 Published:2026-04-01

摘要: 某炼化一体化项目新建的第三套3.0 Mt/a浆态床渣油加氢装置投产后达到了满负荷长周期运行,装置总转化率基本符合设计值,单程转化率略高于设计值,各项指标基本符合预期。单程转化率高而总转化率低说明了反应生成的轻组分没有全部从系统内分离出去,与实际生产中油渣中轻组分含量高于设计值相对应。在吸取第一套和第二套浆态床渣油加氢装置运行经验的基础上,第三套装置设计初期就针对装置的瓶颈点进行了改造,减缓了高负荷长周期运过程中结焦堵塞的情况,为装置改造和后续新建装置提供了优化思路和方向。

关键词: 浆态床渣油加氢, 满负荷, 单程转化率, 浆液分馏单元

Abstract: The newly built third 3.0 Mt/a slurry residue hydrogenation unit in a refining -chemical integration project has achieved full-capacity long-term operation since commissioning. The total conversion rate of the unit generally aligns with the design specifications, while the single-pass conversion rate is slightly exceeds design value. All operational indicators meet expectations. The high single-pass conversion rate coupled with lower total conversion rate indicates that the light components generated during the reaction have not been completely separated from the system, which corresponds to the actual production observation where light components in residual oil exceed design values. Based on the operation experience from the first and second slurry residue hydrogenationunits, the third unit incorporated targeted modifications during initial design to address bottleneck issues. These improvements effectively mitigated coking and blockage problemsunder high-load extended operation conditions, providing valuableoptimization insights and directions for both unit revamping and future new facility construction.

Key words: slurry residue hydrogenation, full-capacity, single-pass conversion rate, slurry fractionation unit