催化裂化(FCC)高温烟气管道的修复

Siva Kumar Chiluvuri, Yeswanth Kumar Adusumilli, J. Penso
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摘要

典型的流动催化裂化装置(FCCU)在催化剂再生过程中产生高温烟气。在使用废热回收装置(WHRU)或CO锅炉去除催化剂细粒和余热后,该烟气被转移到烟囱中。该烟气管道为大直径(1.2 m / 2m)管道,由孔室上游的热壁(带有外保温的裸SS304H管道)和下游的冷壁(带有内部耐火衬里的碳钢管道)组成。在某大型改造工程中,对大部分烟气管道进行了尺寸和设计上的改造。运行约2年后,发现孔室下游热壁到冷壁过渡接头SS304H侧出现裂缝。该生产线在700°C和0.15 Bar(g)的压力下工作。经测量,初始裂纹约为250 ~ 300 mm,并在短时间内扩展为全周裂纹,导致少量含催化剂颗粒的烟气泄漏。本文讨论了如何在现场解决问题的细节,并在机组仍在运行的情况下,在线安全地进行了临时修复(即在高温管道上焊接一个盒子)。此外,本文还介绍了在计划周转期间对热壁到冷壁过渡接头实施的根本原因评估和设计修改。
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Repair of High Temperature Flue Gas Line in Fluid Catalytic Cracking (FCC) Service
A typical Fluid Catalytic Cracking Unit (FCCU) generates high temperature flue gas in the process of regenerating the catalyst. This flue gas is diverted to a stack after removal of catalyst fines and excess heat using a Waste Heat Recovery Unit (WHRU) or CO boiler. This flue gas line is a large diameter (1.2 m /2 m) piping and is a combination of Hot Wall (bare SS304H piping with external insulation) upstream of Orifice Chamber and Cold Wall (Carbon steel piping with internal refractory lining) for the downstream side. In a major revamp project, large portion of flue gas line was replaced with some dimensional and design changes. A crack was noticed at the SS304H side of hot wall to cold wall transition joint downstream of Orifice Chamber after approximately 2 years in operation. The line operates around 700 °C and 0.15 Bar(g) at the location of the crack. The initial crack was measured to be approximately 250 mm to 300 mm and grew to a full circumference crack in a short time resulting in minor flue gas leaking with catalyst fines. This paper discusses the details on how the issue was addressed on site and a temporary repair (i.e. welding of a box on high temperature piping) was carried out online safely, while the unit remained in operation. Further, the paper presents the root cause assessment and design modifications implemented for hot wall to cold wall transition joint during a scheduled turnaround.
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