石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (10): 28-34.

• 加工工艺 • 上一篇    下一篇

催化裂解装置旋风分离器料腿结焦原因分析及应对措施

李维1,刘佳琪2,刘舜2,梁金强2,彭威2   

  1. 1. 中海石油宁波大榭石化有限公司
    2. 中国石油大学(北京)克拉玛依校区
  • 收稿日期:2025-04-14 修回日期:2025-06-18 出版日期:2025-10-12 发布日期:2025-10-09
  • 通讯作者: 彭威 E-mail:pengwei@cupk.edu.cn
  • 基金资助:
    克拉玛依市创新人才专项

ANALYSIS AND COUNTERMEASURES FOR DIPLEG COKING IN CYCLONE SEPARATORS OF DEEP CATALYTIC CRACKING UNITS

  • Received:2025-04-14 Revised:2025-06-18 Online:2025-10-12 Published:2025-10-09

摘要: 旋风分离器料腿结焦是制约催化裂解装置长周期稳定运行的关键问题之一。对某2.2 Mt/a催化裂解装置沉降器内旋风分离器料腿长期结焦问题进行分析,发现其主要原因是二级旋风分离器料腿内催化剂质量流量偏低,下行颗粒对料腿内壁结焦无冲刷作用。此外,二级旋风分离器料腿翼阀埋入沉降器密相床层,翼阀负压差大、排料困难,油气在料腿内停留时间长导致缩合结焦。针对二级旋风分离器料腿负压差大、料柱低,翼阀容易形成窜气,造成阀板磨损的问题提出了相应的解决方案。一是将二级旋风分离器翼阀安装标高提高3.6 m,减小负压差;二是将每个一级旋风分离器入口面积由0.3444 m2更改为0.3357 m2,二级旋风分离器料腿内径由273 mm缩小到219 mm,增大二级旋风分离器料腿内的催化剂质量流量,强化催化剂对内壁结焦的冲刷效果。经过两次检修改造,结焦堵塞的旋风分离器料腿数目明显减少,油浆固含量和烟气颗粒浓度稳定,旋风分离器料腿结焦问题得到改善,为同类装置旋风分离器结焦问题的解决提供了参考。

关键词: 催化裂解, 旋风分离器, 料腿, 翼阀, 结焦

Abstract: Coking in the cyclone separator dipleg is one of the key challenges restricting the long-term stable operation of deep catalytic cracking units. An in-depth analysis of the persistent coking issue in the diplegs of cyclone separators within the disengager of a 2.2 Mt/a catalytic cracking unit indicated that the primary cause was the insufficient catalyst mass flow rate in the secondary cyclone separator diplegs. This inadequacy hindered the downward-flowing particles from effectively scouring the coke deposits on the inner walls.Additionally, the trickle valves of the secondary cyclone separator diplegs were submerged within the dense fluidized bed in the disengager, leading to a significant negative pressure differential and challenges in catalyst discharge.The prolonged residence time of oil vapor in the diplegs resulted in condensation and coking. To address the challenges associated with high negative pressure differentials, low catalyst column heights, and gas channeling in the secondary cyclone separator diplegs, which contributed to valve plate wear, a series of targeted solutions were developed.First, the installation elevation of the secondary cyclone separator trickle valves was raised by 3.6 m to reduce the negative pressure differential. Second, the inlet area of each primary cyclone separator was reduced from 0.3444 m2 to 0.3357 m2, and the inner diameter of the secondary cyclone separator diplegs was reduced from 273 mm to 219 mm. This increased the catalyst mass flow rate in the secondary cyclone separator diplegs, enhancing the scouring effect of the catalyst on the inner walls to remove coke deposits. After two rounds of maintenance and modifications, the number of coked and clogged cyclone separator diplegs significantly decreased. The solid content in the slurry oil and the particle concentration in the flue gas remained stable, indicating that the coking issue in the cyclone separator diplegs had been effectively mitigated. This approach can provide a valuable reference for addressing similar coking problems in cyclone separators of comparable units.

Key words: deep catalytic cracking, cyclone separator, diplegs, trickle valve, coking