加氢裂化装置失效原因分析

Analysis of Failure Causes of Hydrocracking Units

  • 摘要: 某加氢裂化工艺中氢气压缩机缓冲器下部连接管道断裂,通过对断裂管道进行宏观检查、化学成分分析、硬度检验、金相分析、断口微观形貌以及垢物成分分析等方法综合研究失效断裂的原因。断口呈现典型的解理形态,表明此次失效开裂是由硫化物应力腐蚀开裂。发生失效断裂是由于焊缝在焊接过程中冷却速度过快,导致在焊缝组织及热影响区组织中存在马氏体及贝氏体,由于马氏体及贝氏体组织在承受动载荷的过程中会产生裂纹源,裂纹最易产生在未焊透等应力集中的位置,因此裂纹起始于管子未焊透的位置,向外壁扩展,同时介质中的H2和H2S等腐蚀性介质形成腐蚀性环境,加速管子的开裂断裂。

     

    Abstract: In a hydrocracking process, the connecting pipeline at the bottom of the buffer of the hydrogen compressor fractured. A comprehensive study on the causes of the failure fracture was carried out through methods such as macroscopic inspection, chemical composition analysis, hardness testing, metallographic analysis, microscopic morphology of the fracture surface, and composition analysis of the scale on the fractured pipeline. The fracture surface showed a typical cleavage morphology, indicating that the failure cracking was caused by sulfide stress corrosion cracking. The failure fracture occurred because the cooling rate during the welding of the weld was too fast, resulting in the presence of martensite and bainite in the weld and heat - affected zone tissues. Since martensite and bainite tissues can generate crack sources during the process of bearing dynamic loads, cracks are most likely to occur at stress - concentrated positions such as lack of penetration. Therefore, the crack originated from the lack - of - penetration position of the pipe and propagated towards the outer wall. At the same time, corrosive media such as H₂ and H₂S in the medium formed a corrosive environment, accelerating the cracking and fracture of the pipe.

     

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