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Corrosion fatigue cracking of tube coils in an actifier column catalytic cracker

机译:精馏塔催化裂化器中管卷的腐蚀疲劳开裂

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Tube coils made of 25Cr-20Ni austenitic stainless steel were horizontally installed in the fluidized bed of an actifier column of a catalytic cracker installation in an oil refinery unit. Catalyst particles and flue gases were moved in the fluidized bed. When the catalyst lost activity, carbon in the catalyst was burned out in the fluidized bed to recover the activity of the catalyst. Meanwhile, a steam-water mixture was formed with a pressure of 4 MPa and saturation temperature of 250 deg C in the tube coils by the heating of the flue gases. Thus, the heat in the fluidized bed was utilized to generate steam. However, after the installation had been in service for about 40 days, leakage occurred in the tube coils. In general the positions of leaks were in the upper part of the tubes within about 6 m of the inlet. Microscopic analyses indicated that cracks initiated at local corrosion pits where chloride ions present in the feedwater enriched and accumulated. The crack propagated in an intergranular or transgranular manner. Obvious striations were found on the crack surfaces at some positions. Based on the failure analysis and heat transfer calculation. failure of the tube coils was mainly caused by the effects of corrosion fatigue. The lifetime of the tube coils can be prolonged by changing the steam-water flow conditions.
机译:将由25Cr-20Ni奥氏体不锈钢制成的管卷水平安装在炼油厂单元中催化裂化装置的活化塔的流化床中。催化剂颗粒和烟道气在流化床中移动。当催化剂失去活性时,催化剂中的碳在流化床中燃烧掉以恢复催化剂的活性。同时,通过加热烟道气在管盘管中形成压力为4MPa,饱和温度为250℃的蒸汽-水混合物。因此,利用流化床中的热量产生蒸汽。但是,安装已使用约40天后,在管卷中发生泄漏。通常,泄漏的位置在进水口约6 m之内的管道上部。微观分析表明,裂纹始于局部腐蚀坑,在该腐蚀坑中给水中存在的氯离子富集并积累。裂纹以晶间或跨晶的方式扩展。在某些位置的裂纹表面发现明显的条纹。基于故障分析和传热计算。管线圈的故障主要是由于腐蚀疲劳的影响。通过改变蒸汽-水的流动条件可以延长管式盘管的寿命。

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