Short Term Overheating | Materials And Corrosion Control
Damage Mechanism |
Short-term Overheating |
Damage Description |
· Permanent deformation, typically from 3% to 10%, occurring at relatively low stress levels as a result of localized overheating.
· Eventually results in bulging and failure by stress rupture. · Ruptures are characterized by open “fishmouth” failures and normally with thin lip fractures · In ferritic steels especially, bulging is typically associated with local microstructural changes that confirm high temperature exposure · It is a fairly common damage mechanism in utility boiler tubes and is sometimes associated with starvation (loss of steam/water on the tubeside). · Bulging and distortion can be significant at low stresses, as temperatures increase. |
Affected Materials/Equipment |
· All fired heater and boiler tube materials and common materials of construction.
· Flow starvation can cause short term overheating and even failure in any refining furnace but it is particularly critical in hydrogen or steam reformer furnaces · Overheating may also be caused by deposit built-up inside furnace tubes. Furnaces with coking tendencies such as crude, vacuum, heavy oil hydroprocessing are susceptible to this overheating. · Refractory lined equipment in the Fluid Catalytic Cracking, sulfur recovery and other units may suffer localized overheating due to refractory damage and/or excessive firing. |
Control Methodology |
· Verify the material selection conform to the design temperatures and pressure
· Check that metal temperatures do not exceed design limits · Monitor for flame impingement using visual inspection via peep holes, or local overheating with infrared guns or thermography. · Install and maintain bed thermocouples in reactors and minimize the likelihood of hot spots through proper design and operation. · Fired heaters require proper burner management and fouling/deposit control to minimize hot spots and localized overheating. · Utilize burners which produce a more diffuse flame pattern. · Perform remaining life assessment per API STD 530 or |
Monitoring Techniques |
· In fired heaters, visual observation, IR monitoring of tubes and tubeskin thermocouples are used to monitor temperatures.
· Check for distortion and diametric growth during turnaround inspection. · Metallographic replication and hardness testing can be used to micro-structural categorization and detection for evidence of overheating · Refractory lined equipment can be monitored with heat indicating paint and periodic infrared thermography. Inspect for refractory damage during shutdowns. |
Inspection Frequency |
· Monitor temperature trends every shift especially in hotter/outlet sections of fired heaters
· Internal inspection and diametric dimensional checks at T&I · Metallographic replication and hardness testing after every process upset or temperature excursion or as advised by CSD Metallurgical Specialist |
KPIs |
· Number of internal visual inspection
· Number of metallographic replication and hardness testing checks · Number of life assessments · Calculated life fraction consumed · Number of temperature excursions (over design limits) and durations · Number of chemical cleaning operations carried out (boilers) · Number of decoking operations carried out (process heaters, · Steam/hydrocarbon ratio (hydrogen or steam reformers) |
Reference Resources (Standards/GIs/BPs) |
· API RP 571 (DM #30)
· NALCO Guide to Boiler Failure Analysis · API STD 530 · API RP 579, Section 10 |
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