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Cause analysis of corrosion leakage in convection section of ethylene cracking furnace

机译:乙烯裂解炉对流截面腐蚀泄漏的原因分析

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Convection tubes of an ethylene cracking furnace at a petrochemical plant had multiple leaking points along longitudinal directions after a fraction of the anticipated tube life span. To study the cause of the failure, the failed tubes were investigated with macro inspections, chemical composition analysis, metallographic microscopy, scanning electron microscopy (SEM) and energy dispersive spectroscopy (EDS). Through analysis of the failed tube samples, we found no evidence of scaling corrosion caused by S and Cl and no significant corrosion contributed by carburisation of the inner wall. By combining cavitation characteristics observed from the leaking tube inner wall and the feed composition changed by the plant recently, we highly suspected that cavitation was the main reason causing the tube to leak. A simulation model was built to illustrate the possibility of liquid cavitation at the leaking region of the tube. After the plant controlled the heavy component in the light hydrocarbon suspected of causing the liquid cavitation, the investigated tube section did not show any similar leaking problem.
机译:在预期的管寿命跨度的一部分之后,石化厂的乙烯裂化炉的对流管在纵向方向上具有多个泄漏点。为了研究失败的原因,用宏观检查,化学成分分析,金相显微镜,扫描电子显微镜(SEM)和能量分散光谱(EDS)进行失败的管。通过分析失败的管样品,我们发现没有发现由S和Cl引起的缩放腐蚀的证据,并且没有通过内壁的碳化碳造成的显着腐蚀。通过组合从泄漏管内壁观察到的空化特性和最近由工厂改变的进料组合物,我们非常怀疑空化是导致管泄漏的主要原因。建立了模拟模型,以说明管的泄漏区域处的液体空化的可能性。在植物控制疑似液体空化的光烃中的重组分后,所研究的管部分没有显示出任何类似的泄漏问题。

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