石油炼制与化工 ›› 2025, Vol. 56 ›› Issue (3): 121-126.

• 设备及防腐 • 上一篇    下一篇

轻烃裂解炉对流段炉管泄漏分析与防护

马红杰1,张文泽1,伍世昌2,王明明3,杨伟东1   

  1. 1. 中国石油独山子石化分公司研究院
    2. 中国石油独山子石化分公司机动设备部
    3. 中国石油独山子石化分公司乙烯一部
  • 收稿日期:2024-09-25 修回日期:2024-11-02 出版日期:2025-03-12 发布日期:2025-02-25
  • 通讯作者: 马红杰 E-mail:yjy_mhj@163.com

LEAKAGEANALYSIS AND PROTECTION OF THE CONVECTION SECTION TUBE IN LIGHT HYDROCARBON CRACKING FURNACE

  • Received:2024-09-25 Revised:2024-11-02 Online:2025-03-12 Published:2025-02-25

摘要: 某石化公司轻烃裂解炉对流段原料预热第一段炉管频繁发生泄漏,采用宏观检查、光谱分析、金相分析、扫描电子显微镜及能谱分析等方法进行检测分析,结果表明泄漏炉管底部密布马蹄形、海绵状的腐蚀凹坑,形成与炉管轴向平行排列的多条腐蚀沟槽,炉管最大腐蚀速率为0.58mm/a。考虑腐蚀介质、对流段工艺流程、烧焦工艺流程及汽蚀等影响因素,分析了原料预热第一段炉管的腐蚀原因,发现轻烃裂解炉对流段执行轻烃流程时产生的汽蚀与烧焦时产生的溶解氧腐蚀是导致原料预热第一段炉管腐蚀泄漏的主要原因,在二者的共同作用下,炉管内壁不断腐蚀、减薄,并最终出现穿孔泄漏。采用在原料预热第一段入口设置稀释蒸汽吹扫线的工艺防护措施可从根本上避免炉管的腐蚀泄漏。

关键词: 轻烃, 裂解炉, 对流段, 炉管, 腐蚀, 防护

Abstract: Frequent leakage of the convection section of the raw material preheating section seriously affects the long-term and safe operation of the cracking furnace. Macroscopic inspection, spectral analysis, metallographic analysis, scanning electron microscopy, and energy spectrum analysis were used to detect and analyze the leaking furnace tube. The results showed that the bottom of the leaking furnace tube was densely covered with horseshoe shaped and sponge shaped corrosion pits, which overlapped and connected with each other. Multiple corrosion grooves arranged parallel to the axial direction of the furnace tube were formed, and the maximum corrosion rate at the leakage point of the furnace tube was 0.58mm/a. From the perspective of corrosive media, convection section process flow, coking process flow, and cavitation factors, the corrosion reasons of the preheating section of the raw material furnace tube were analyzed. It was found that the cavitation generated during the execution of the light hydrocarbon process in the convection section of the light hydrocarbon cracking furnace and the dissolved oxygen corrosion generated during coking were the main reasons for the corrosion and leakage of the preheating section of the raw material furnace tube. Under the combined action of both, the inner wall of the furnace tube continuously corroded and thinned. And ultimately, perforation leakage occurred. Finally, the process protection measures of setting a dilution steam blowing line at the inlet of the raw material preheating section were proposed and applied, fundamentally avoiding corrosion and leakage of the furnace tubes.

Key words: light hydrocarbons, cracking furnace, convection section, furnace tube, corrosion, protect