乙烯工业 ›› 2018, Vol. 30 ›› Issue (4): 60-64.

• 裂解炉 • 上一篇    

Pyracrack1-1裂解炉化学清洗实践

薛魁,李怀强,马国民,杨志楠,周尖   

  1. 中国石油天然气股份有限公司独山子石化分公司,新疆 独山子 833699
  • 收稿日期:2017-12-07 接受日期:2018-07-06 出版日期:2018-12-25 发布日期:2018-12-30
  • 作者简介:薛魁,男, 2017年取得中国石油大学(北京)硕士研究生学位,主要从事乙烯工艺技术管理工作,高级技师,中国石油天然气集团公司技能专家。

Chemical Cleaning Practice of Linde Pyracrack1-1 Cracking Furnace

Xue Kui,Li Huaiqiang,Ma Guomin,Yang Zhinan,Zhou Jian   

  1. PetroChina Dushanzi Petrochemical Company,Dushanzi,Xinjiang,P.C.833699
  • Received:2017-12-07 Accepted:2018-07-06 Online:2018-12-25 Published:2018-12-30

摘要: 中国石油独山子石化百万吨乙烯装置设计有8台Linde Pyracrack1-1型裂解炉,单炉设计乙烯生产能力为150 kt/a。装置自2009年9月开工以来,已运行8年,对流段积灰较严重,轻烃裂解炉超高压蒸汽(SS)过热温度不足,在提高过剩空气系数后,SS温度仅能保持在465~485 ℃,裂解炉能耗增加,热效率低,虽经人工清洗,并增设了高频声波吹灰器,仍无法满足工艺需要,影响装置的长周期运行。通过化学清洗对流段,有效解决了此项生产难题,提高了裂解炉热效率,减少了废气排放。

关键词: 裂解炉, 对流段, 化学清洗, 热效率

Abstract: 8 Linde Pyracrack1-1 cracking furnaces are designed for the Megaton ethylene plant at PetroChina Dushanzi Petrochemical Company, each with an ethylene production capacity of 150 thousand tons per year. The ethylene plant has been operated for 8 years since its startup in September 2009. The fouling in convection section was serious, and the superheating temperature of super-high-pressure steam (SS) in light hydrocarbon cracking furnace was low. By increasing the excess air coefficient, the temperature of SS was only maintained at 465~485 ℃. The energy consumption of cracking furnace was increased, and the thermal efficiency was low. Although manual cleaning was performed and high frequency acoustic wave soot blower was installed, the process requirements could not be met, thus influencing the long term operation of the ethylene plant. The chemical cleaning of convection section effectively solved this problem, improved the thermal efficiency of cracking furnace and reduced the emission of exhaust gas.

Key words: cracking furnace;convection section, chemical cleaning, thermal efficiency