The continuous increase in fuel prices at refueling stations and the costs of extraction, refining and supply chain management leads the Companies to purchase low-cost crude oils, characterized by high acidity and high sulphur content. The processing of such crude oils results in a drastic increase in corrosion rates, relative to sulfidation and naphthenic acid corrosion mechanisms, thus, it is necessary to take mitigation actions, conducting a cost-benefit assessment and reviewing inspection and maintenance plans. A petroleum refinery has implemented a monitoring system, through ultrasonic corrosion probes, and an inhibitor injection system at specific points in its atmospheric distillation units; the goal is to manage crude oil with TAN (Total Acid Number) value that not exceed 1.5 mg(KOH)/g.In this report, the layout and operation of the system are described, with a brief mention of the used inhibitor’s family; the choice of injection and monitoring points and the measured corrosion rate are presented for the first months in service

Monitoring and Management of Naphthenic Acid Corrosion in Distillation Units of a Petroleum Refinery

Giacobbe A.
;
2024-01-01

Abstract

The continuous increase in fuel prices at refueling stations and the costs of extraction, refining and supply chain management leads the Companies to purchase low-cost crude oils, characterized by high acidity and high sulphur content. The processing of such crude oils results in a drastic increase in corrosion rates, relative to sulfidation and naphthenic acid corrosion mechanisms, thus, it is necessary to take mitigation actions, conducting a cost-benefit assessment and reviewing inspection and maintenance plans. A petroleum refinery has implemented a monitoring system, through ultrasonic corrosion probes, and an inhibitor injection system at specific points in its atmospheric distillation units; the goal is to manage crude oil with TAN (Total Acid Number) value that not exceed 1.5 mg(KOH)/g.In this report, the layout and operation of the system are described, with a brief mention of the used inhibitor’s family; the choice of injection and monitoring points and the measured corrosion rate are presented for the first months in service
2024
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11570/3320069
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