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S-H₂S-RSH corrosion is a typical type of high-temperature active sulfur corrosion that occurs in oil refining operations. Its impact on equipment manifests in the following ways: uniform thinning of the equipment’s structure. As this is a chemical form of corrosion, it causes the metal walls of the equipment to thin out uniformly. The bottom sections of coking distillation columns are most severely affected, followed by those of distillation and vacuum distillation columns and catalytic distillation columns. Prolonged exposure to this corrosion directly reduces the equipment’s capacity to withstand pressure. Local erosion corrosion intensifies. In areas where the flow velocity changes abruptly, such as elbows, tees, and pump casings, the protective FeS passivation film is easily washed away by the medium, leading to localized thinning in the form of sharp edges, and even local corrosion-induced perforations, which significantly reduces the service life of the equipment. It induces the risk of secondary failures. Under wet operating conditions, this corrosion mechanism is accompanied by hydrogen penetration, which leads to sulfide stress cracking (SSC). This results in sudden failures of the equipment without any obvious warning signs. It can also damage the original sealing structure of the equipment, thereby causing safety hazards such as fluid leakage. Disruption of production operations: The sulfur compound impurities resulting from corrosion can mix into the medium, potentially causing instability or tripping in subsequent process equipment such as electro-dehydration units, and even leading to the breakdown of the plates, thereby affecting the smooth operation of the entire installation.
The original poster has analyzed this very well; S-H₂S-RSH corrosion is indeed a major and persistent problem in the high-temperature areas of oil refining plants. I would like to add three practical insights for reference: Material upgrade: In areas heavily affected by corrosion, such as the bottom of coking distillation towers, it is recommended to replace carbon steel with 1Cr5Mo or aluminum-treated steel, which can significantly delay uniform thinning ; Flow rate monitoring: It is recommended to keep the flow rate at bends and pump casings below 15 m/s. Additionally, local erosion areas should be monitored regularly using ultrasonic thickness measurement and coupon testing; if an abnormal thinning rate is detected, the relevant components must be replaced in advance ; Special care must be taken in wet environments: during shutdowns for maintenance, nitrogen drying protection must be ensured to prevent the combination of condensation water and sulfides from causing SSC, as this can easily lead to cracks without any warning. The above are sharing of practical engineering experience; specific plans require risk assessment based on operational conditions and design specifications. It is recommended that the original poster consult corrosion engineers and standards such as NACE SP0472.