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FAILURE ANALYSIS OF BANK TUBE IN PACKAGE BOILER

机译:装箱锅炉内储罐故障分析

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Generally, it is well know that the bank tubes are one of the components of package boilers that fail frequently. In the investigated case the bank tube experienced a leak due to a circumferential through wall crack developed on the top half. This portion of the tube is swaged and connected to the steam drum. The failures occurred in tubes positioned in the first and second rows as a rule. The boiler has a design capacity of 140 tons per hour (140 Megagrams per hour) and is operated at a pressure of 42 barg (43 kg/cm~2) and temperature of 340°C (644°F). It was commissioned in 1993. Bank tubes have OD about 2.5-inches (63.5 mm) and wall thickness of 0.126-inches (3.2 mm). The results of metallographic and SEM/EDS examinations are presented and discussed. Numerous rounded pits about 0.8 mm in depth were found on the inner surface of swaged area. Intergranular cracks propagated from the bottom of these pits. The most probable failure mechanisms are also discussed. Most likely the bank tube failed due to caustic gouging followed by intergranular caustic cracking that developed from the bottom of the pits.
机译:通常,众所周知,排管是经常发生故障的成套锅炉的组件之一。在所研究的情况下,由于在上半部形成了周向贯穿的壁裂,因此堤管发生了泄漏。管的该部分被型锻并连接到蒸汽鼓。通常,故障发生在位于第一排和第二排的管中。该锅炉的设计容量为每小时140吨(每小时140毫克),并在42 barg(43 kg / cm〜2)的压力和340°C(644°F)的温度下运行。它于1993年投入使用。堤坝管的外径约为2.5英寸(63.5毫米),壁厚为0.126英寸(3.2毫米)。介绍并讨论了金相和SEM / EDS检查的结果。在型锻区域的内表面上发现了许多深约0.8毫米的圆形凹坑。晶间裂纹从这些凹坑的底部扩展。还讨论了最可能的故障机制。最有可能是由于苛性气刨而导致管破裂,随后是从凹坑底部形成的晶间苛性裂纹。

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