Overview
Reference for identifying, understanding, and managing damage mechanisms that affect piping and fixed equipment.
Scope & Applicability
Applies To Industries
Covers — descriptions of damage mechanisms affecting fixed equipment and piping in refining/petrochemical service: general and localized corrosion, high-temperature damage (sulfidation, HTHA, creep), environmental cracking (chloride/caustic/amine SCC, HIC/SOHIC), and mechanical/metallurgical mechanisms, each with critical factors, morphology, and mitigation/monitoring.
Does NOT cover (exclusions) — the following are governed elsewhere:
- The in-service inspection program and intervals → API 570 / API 510.
- Detailed inspection practices/techniques → API RP 574.
- Risk-based inspection methodology → API RP 580 / 581; fitness-for-service → API 579-1.
RP 571 tells you what can go wrong and why; the inspection and RBI codes decide what to inspect and how often.
Key Requirements
RP 571 provides reference knowledge for each damage mechanism:
- Affected Materials — which alloys/grades are susceptible.
- Critical Factors — temperature, environment, stress, and concentration thresholds that drive the mechanism.
- Appearance/Morphology — how the damage looks and where it initiates.
- Prevention & Monitoring — mitigation measures and the inspection/monitoring methods that detect it.
Technical Details
API RP 571 is the reference encyclopedia of damage mechanisms affecting fixed equipment and piping in refining and petrochemical service. For each mechanism — sulfidation, high-temperature hydrogen attack, corrosion under insulation, chloride and amine stress-corrosion cracking, and dozens more — it describes the susceptible materials, critical factors, appearance, and mitigation/monitoring.
It is the knowledge base that makes risk-based inspection possible: you cannot inspect for a threat you have not identified. RP 571 informs where and how to look, feeding the inspection code (API 570) and RBI methodology (API 580/581), but it is not itself an inspection or acceptance code.
Engineering Note: Use RP 571 to build the equipment's credible-damage list before setting inspection plans — an unrecognized mechanism (e.g., HTHA in a hot hydrogen line) is a classic cause of in-service failures that a generic thickness-monitoring plan will miss.
Engineering Notes
The encyclopedia of refinery damage mechanisms — each entry (e.g., sulfidation, high-temperature hydrogen attack, amine cracking, CUI, chloride SCC) describes the affected materials, critical factors, appearance, and prevention/monitoring. It is the knowledge base behind risk-based inspection: you cannot plan inspection for a threat you have not identified. It informs where and how to look, but it is not itself an inspection or acceptance code.
Source, Edition & Status
- Publisher
- API
- Edition Year
- 2020
- Industries
- Refinery, Petrochemical, Chemical Plant
- Last Reviewed
- 2026-07-01
- Last Updated
- 2026-07-01
- Verified By
- Engineering content reviewer
- Content Status
- reviewed
- Official Link
- www.api.org