石油炼制与化工 ›› 2026, Vol. 57 ›› Issue (4): 15-19.

• 加工工艺 • 上一篇    下一篇

1.2 Mt/a催化裂化装置技术改造与效果分析

宁佐强   

  1. 中石化湖南石油化工有限公司
  • 收稿日期:2025-11-07 修回日期:2025-12-10 出版日期:2026-05-12 发布日期:2026-04-01
  • 通讯作者: 宁佐强 E-mail:ningzq3.hnsh@sinopec.com

TECHNICAL REVAMP AND PERFORMANCE ANALYSIS OF A 1.2 Mt/a CATALYTIC CRACKING UNIT

  • Received:2025-11-07 Revised:2025-12-10 Online:2026-05-12 Published:2026-04-01

摘要: 针对1.2 Mt/a催化裂化装置反应-再生系统存在的再生器稀相尾燃、催化剂跑损严重等核心问题,某石化公司在2021年大修期间实施了以流场系统性优化为核心的技术改造。通过主风分布系统对称性重构、催化剂分配器均匀化改进、PLS型双入口旋风分离器应用及密相格栅增设等关键技术措施,改善了气固分布均匀性与碳-风匹配效率。改造后,稀相尾燃现象消除,催化剂跑损量由3~7 t/d降至1.5 t/d,实现了装置长周期安稳运行。

关键词: 催化裂化, 稀相尾燃, 旋风分离器, 主风分布, 催化剂跑损, 流场优化

Abstract: Addressing technical challenges in the reactor-regenerator section of a 1.2 Mt/a catalytic cracking unit, such as afterburning in the regenerator dilute phase and severe catalyst loss, a systematic revamp focused on flow field optimization was implemented during the 2021 overhaul. Key technical measures included optimizing the main air distribution system, improving the catalyst distributor, applying PLS-type dual-inlet cyclones, and adding dense phase grids. These measures fundamentally improved gas-solid distribution uniformity and carbon-air matching efficiency. Post-revamp, afterburning in the dilute phase was eliminated, catalyst loss reduced from 3―7 t/d to 1.5 t/d, achieving long-term, stable, and safe operation.

Key words: catalytic cracking, dilute phase afterburning, cyclone separator, main air distribution, catalyst loss, flow field optimization