Sulfidation (w/o H2)
General Information
High temperature sulfidation, or simply sulfidation, results from reactions between various sulfur species and metallic materials, typically occurring at temperatures above 230°C (446°F). Sulfidation has been a presence in the refining industry since its inception; however, over the last 30 years, intensified processing of sour crudes has amplified the scale of the problem. Often exacerbated by naphthenic acid corrosion, sulfidation is considered a key and active damage mechanism that critically impacts refinery operations.
Primarily associated with distillation units (CDU/VDUs) and sulfur recovery units (SRUs), sulfidation is also present in other units such as fluid catalytic cracking (FCC) or delayed coking units (DCU). Refinery operators typically do not observe critical sulfidation impacts on units downstream of CDU/VDU when processing sweet crudes ((Stotal <0.6wt%)). However, as the sulfur level in the processed crude oil increases, the risk of sulfidation rises, especially in units like FCC where e.g., furnace tubes, typically made of low alloy steels (typically 5% or less chromium). Therefore, if the total sulfur content in the feed (crude slate) increases, it is crucial to revisit the corrosion risk assessment, considering sulfidic corrosion not only in CDU/VDU but also in all units potentially affected by sulfidation. Table 1 provides a list of units and process areas likely impacted by sulfidation. 1
Sulfidation is governed by a combination of several factors, including the type and concentration of sulfur compounds, temperature, and flow regime.
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References
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