乙烯工业 ›› 2023, Vol. 35 ›› Issue (2): 29-32.

• 工业技术 • 上一篇    下一篇

裂解气中CO超标原因分析及应对措施

刘  驰1,武传朋2,谭伟洪1,郑文兢1,苟成冬2   

  1. 1 中科(广东)炼化有限公司,广东 湛江 524000;2 中石化安全工程研究院有限公司,山东 青岛 266000
  • 收稿日期:2022-09-09 修回日期:2023-02-14 出版日期:2023-06-25 发布日期:2023-07-11
  • 作者简介:刘驰,男,2017年毕业于中国石油大学(华东)过程装备与控制工程专业,主要从事乙烯装置生产管理工作,助理工程师。

Cause Analysis and Countermeasures for Excessive CO in Cracking Gas

Liu Chi1, Wu Chuanpeng2, Tan Weihong1, Zheng Wenjing1, Gou Chengdong2   

  1. 1. ZhongKe (Guangdong) Refinery & Petrochemical Company Limited, Zhanjiang, Guangdong, P.C.524000; 2. SINOPEC Research Institute of Safety Engineering Co., Ltd., Qingdao, Shandong, P.C.266100
  • Received:2022-09-09 Revised:2023-02-14 Online:2023-06-25 Published:2023-07-11

摘要:

乙烯是石油化工重要的基础原料,在裂解生产过程中伴随有CO的生成。裂解气中CO含量超标会使碳二加氢催化剂中毒,出现漏炔现象,造成乙烯产品不合格,更甚者导致装置联锁停车,影响乙烯的正常生产。文中论述了蒸汽裂解装置CO的生成过程,根据装置实际生产工况系统性分析了裂解气中CO含量超标的原因,其最主要原因为裂解炉炉管出口温度(COT)超温、裂解原料硫含量减少和投料前炉管注硫钝化不完全。同时根据CO超标的原因提出了相应的处置措施。

关键词: 乙烯裂解  CO超标 , 炉管出口温度 , 硫含量

Abstract:

Ethylene is an important basic raw material for petrochemical industry, and CO will be generated during ethylene cracking. Excessive CO in cracking gas will lead to the poisoning of C2 hydrogenation catalyst and the leakage of acetylene, resulting in unqualified ethylene products or even the interlock shutdown of the plant and affecting normal ethylene production. This paper discusses the generation process of CO in steam cracking unit, and systematically analyzes the causes of the excessive CO in cracking gas according to the actual production conditions of the plant. The main reasons for the excessive CO in cracking gas are the over high COT in cracking furnace, the reduced sulfur content of cracking raw material and the incomplete passivation of furnace tube before feeding. Some corresponding countermeasures are proposed according to the reasons for the excessive CO.

Key words: ethylene cracking, excessive CO, coil outlet temperature/COT, sulfur content