API 571 - API 571 Corrosion and Materials Practice Test

API 571 Corrosion Study Guide 2026

API 571 defines the damage mechanisms affecting fixed equipment in the refining industry and serves as the technical backbone for API 510, 570, and 653 inspector certifications. This study guide covers every major corrosion type, metallurgical principle, and inspection concept tested on the API 571 examination — helping process industry professionals earn their certification and advance into higher-paying inspection and process safety roles.

About API 571 and Its Role in Inspector Certifications

API 571, formally titled Damage Mechanisms Affecting Fixed Equipment in the Refining Industry, is a recommended practice published by the American Petroleum Institute. It catalogs over 60 damage mechanisms that degrade pressure vessels, piping, heat exchangers, storage tanks, and other fixed equipment in petroleum refining and petrochemical facilities.

Understanding API 571 is not optional for serious inspection professionals. The API 510 (Pressure Vessel Inspector), API 570 (Piping Inspector), and API 653 (Aboveground Storage Tank Inspector) certification exams all draw heavily from API 571 content. Candidates who master damage mechanisms earn higher scores across all three credentials and are better equipped to make critical fitness-for-service decisions in the field.

API 571 organizes damage mechanisms into broad categories — mechanical, metallurgical, corrosion, and environment-assisted cracking — and for each mechanism describes the affected materials, critical process variables, morphology, inspection methods, and prevention strategies. This structure mirrors how working inspectors must think: identify the mechanism, understand its drivers, and select the right NDE technique.

API 571 Exam Format and Structure

The API 571 examination is administered by the American Petroleum Institute as part of its Inspector Certification Program. The exam consists of multiple-choice questions completed over a 2.5-hour testing window. Questions test both conceptual understanding of damage mechanisms and applied knowledge of how those mechanisms manifest in real refinery equipment.

Candidates are permitted to bring reference materials into the exam, including their copy of API 571 itself. However, open-book access does not reduce the need for thorough preparation — the time constraint means candidates must know where to locate information quickly and must already understand the underlying concepts well enough to interpret questions correctly.

The exam is typically taken in conjunction with one of the primary inspector certification exams (API 510, 570, or 653). Strong performance on the API 571 portion significantly improves overall pass rates for all three credentials.

Key API 571 Damage Mechanisms at a Glance

🔴 HIC and SOHIC – High Priority
Wet H2SCarbon SteelCracking
  • Full Name: Hydrogen-Induced Cracking / Stress-Oriented HIC
  • Affected Materials: Carbon steel, low-alloy steel
  • Environment: Wet H2S service, sour water systems
  • Key Driver: Atomic hydrogen absorption at sulfide inclusions
  • Detection Method: UT shear wave, TOFD, phased array UT
🟠 Amine Corrosion – Common Exam Topic
Amine UnitsCarbon SteelCorrosion
  • Mechanism Type: Aqueous corrosion / flow-accelerated
  • Affected Equipment: Amine absorbers, regenerators, exchangers, piping
  • Key Driver: Degraded amine, heat stable salts, high velocity
  • Temperature Range: Elevated temperatures in lean amine service
  • Mitigation: Amine quality control, velocity limits, inhibitors
🟡 High-Temperature H2 Attack (HTHA) – Nelson Curves
HydrogenHigh TemperatureSteel
  • Also Known As: Nelson curves damage, hydrogen decarburization
  • Affected Materials: Carbon steel, low-alloy steels at elevated temps
  • Key Driver: H2 partial pressure and temperature exceeding Nelson curve limits
  • Effect: Decarburization, methane bubble formation, fissuring
  • Reference: API 941 Nelson curves — mandatory exam knowledge
🟢 Corrosion Under Insulation (CUI) – Field Relevance
External CorrosionInsulated PipingVessels
  • Risk Zone Temperature: -4°F to 350°F (-20°C to 175°C) for carbon steel
  • Aggravating Factors: Damaged insulation, cyclic service, coastal environments
  • Affected Materials: Carbon steel, 300-series stainless (chloride SCC risk)
  • Inspection Method: Strip and inspect, pulsed eddy current, NRT, RT
  • Prevention: Proper insulation design, coatings, jacketing maintenance
🔵 Sulfidation – Refinery Specific
High TemperatureSulfurH2S
  • Mechanism Type: High-temperature sulfur corrosion
  • Threshold Temperature: Above approximately 500°F (260°C)
  • Affected Materials: Carbon steel; alloy steel more resistant
  • Key Standard: McConomy curves for sulfidation rate estimation
  • Mitigation: Upgrade to Cr-Mo alloys; 9Cr-1Mo for severe service
🟣 Chloride Stress Corrosion Cracking (Cl-SCC) – Stainless Steel Risk
Austenitic SSChloridesCracking
  • Affected Material: 300-series austenitic stainless steel primarily
  • Temperature Threshold: Generally above 140°F (60°C)
  • Morphology: Transgranular branching cracks
  • Common Locations: Heat exchangers, condenser tubing, CUI zones
  • Mitigation: Use duplex SS or high-nickel alloys; eliminate chloride exposure
API 571 Materials and Metallurgy Essentials

A solid understanding of materials science separates candidates who pass from those who struggle. API 571 requires knowledge of how different metals respond to corrosive environments, elevated temperatures, and mechanical stresses common in refinery service.

  • Carbon steel is the most widely used material in refineries and the most frequently damaged — candidates must know its vulnerabilities to wet H2S, CUI, sulfidation, and HTHA.
  • Low-alloy steels (1.25Cr-0.5Mo, 2.25Cr-1Mo, 5Cr-0.5Mo, 9Cr-1Mo) offer improved resistance to high-temperature hydrogen attack and sulfidation — their Nelson curve positions are a common exam topic.
  • 300-series austenitic stainless steels (304, 316, 321, 347) resist general corrosion but are susceptible to chloride SCC, polythionic acid SCC, and sensitization-related intergranular corrosion.
  • Duplex stainless steels provide higher chloride SCC resistance than austenitic grades and are increasingly used in sour water and amine service.
  • Copper alloys and nickel alloys appear in specialized service — candidates should know their specific susceptibilities (e.g., copper alloy dezincification, nickel alloy stress corrosion in caustic service).
  • Weld heat-affected zones (HAZ) are preferential sites for many damage mechanisms — sensitization in stainless welds, PWHT requirements for preventing SOHIC in carbon steel welds, and hardness limits in sour service are all examinable.

Inspection Principles and NDE Methods in API 571

API 571 does not exist in isolation — it connects directly to inspection practice through its guidance on detection methods for each damage mechanism. For every mechanism covered, the standard identifies which nondestructive examination (NDE) techniques are appropriate and what the inspector should look for.

Candidates preparing for API 510, 570, or 653 need to correlate damage mechanisms with their corresponding NDE methods. For example, wet H2S cracking mechanisms including HIC, SOHIC, and sulfide stress cracking are best detected by shear-wave ultrasonic testing, time-of-flight diffraction (TOFD), or phased array UT — not conventional straight-beam UT alone. CUI requires techniques capable of penetrating insulation, such as pulsed eddy current (PEC) or neutron radiography (NRT).

Understanding the link between mechanism and method is essential because exam questions frequently describe a scenario and ask candidates to select the appropriate inspection technique or explain why a given method would or would not detect a specific form of damage.

API Inspector Certification Levels

The API Inspector Certification Program offers several credentials that rely on API 571 knowledge. Understanding the structure of these credentials helps candidates plan their study path and career progression.

API 510 — Pressure Vessel Inspector: Covers inspection, repair, alteration, and re-rating of pressure vessels. API 571 damage mechanisms for pressure vessel service (reactors, heat exchangers, drums) are directly tested. Requires documented inspection experience in refinery or related industry.

API 570 — Piping Inspector: Covers inspection, repair, and alteration of in-service piping systems. Damage mechanisms specific to piping — including erosion-corrosion, flow-accelerated corrosion, and CUI on piping — feature prominently. Requires qualifying experience in piping inspection.

API 653 — Aboveground Storage Tank Inspector: Covers inspection and repair of aboveground storage tanks. Tank-specific damage mechanisms such as MIC, underside corrosion, and shell corrosion are covered by API 571. Requires qualifying tank inspection experience.

All three certifications are renewed every three years through continuing education and examination, making ongoing study of API 571 updates a career-long requirement for certified inspectors.

Career Outlook and Salary for API-Certified Inspectors

API 571 certification adds measurable market value to inspection and process safety professionals. Certified inspectors working in petroleum refining, petrochemical plants, and related process industries report salaries ranging from approximately $80,000 to $130,000 annually in the United States, with variation based on specialty, geographic region, employer type, and additional certifications held.

Entry-level inspectors with a single API certification and limited field experience typically start in the $80,000–$95,000 range. Experienced inspectors holding multiple API credentials (510 + 570 + 653), with additional qualifications in advanced NDE or fitness-for-service assessment per API 579, can command $110,000–$130,000 or more at major refining companies or as independent consultants.

Process safety engineers who leverage API 571 knowledge for risk-based inspection (RBI) program development — a growing specialty in the industry — often reach the upper end of this salary range, as RBI expertise directly reduces equipment failure risk and maintenance costs for plant operators.

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API 571 Questions and Answers

What is the difference between HIC and SOHIC in API 571?

Hydrogen-Induced Cracking (HIC) occurs when atomic hydrogen absorbed from wet H2S environments collects at internal defects such as sulfide inclusions, forming blisters or stepwise cracks that propagate parallel to the plate surface. Stress-Oriented HIC (SOHIC) involves similar hydrogen absorption but the cracking is driven by applied or residual stress, causing the cracks to stack and link in a through-thickness orientation that can lead to rapid through-wall failure. SOHIC is considered more dangerous than HIC because the stress orientation significantly accelerates crack linking. Both mechanisms affect carbon and low-alloy steels in wet H2S service, and both are detected using shear-wave UT, phased array UT, or TOFD rather than conventional straight-beam techniques.

What are Nelson curves and why are they important for API 571 exam candidates?

Nelson curves, defined in API 941, plot the safe operating limits for various steel alloys in hydrogen service based on temperature and hydrogen partial pressure. Above these limits, atomic hydrogen reacts with carbon in the steel to form methane gas at grain boundaries, causing decarburization, bubble formation, and fissuring — a phenomenon known as high-temperature hydrogen attack (HTHA). API 571 exam questions frequently require candidates to identify whether operating conditions for a given alloy fall within safe or unsafe regions of the Nelson curves, and to recommend appropriate material upgrades (such as specifying 2.25Cr-1Mo or 9Cr-1Mo steel) when conditions exceed the limits for carbon steel.

How does corrosion under insulation (CUI) develop and what inspection methods detect it?

CUI develops when water penetrates damaged, poorly designed, or aged insulation systems and contacts the underlying metal surface. Carbon steel equipment operating between approximately -4°F and 350°F (-20°C to 175°C) is most susceptible because condensation occurs during thermal cycling. Austenitic stainless steel in insulated service faces additional risk of chloride stress corrosion cracking from chloride-containing water. Aggravating factors include steam tracing leaks, process upsets, coastal environments with airborne chlorides, and insulation systems that trap moisture. Detection methods include strip-and-inspect (most reliable but costly), pulsed eddy current (PEC) for screening through insulation, neutron radiography (NRT), and profile radiography. Risk-based inspection programs prioritize CUI inspection based on insulation condition, service temperature, and exposure history.

Which damage mechanisms are most commonly tested on the API 571 exam?

Based on the scope of API 510, 570, and 653 examinations, the most heavily weighted API 571 topics include wet H2S damage mechanisms (HIC, SOHIC, sulfide stress cracking, hydrogen blistering), high-temperature hydrogen attack and Nelson curves, sulfidation and McConomy curves, amine corrosion, corrosion under insulation, chloride stress corrosion cracking of austenitic stainless steels, erosion-corrosion and flow-accelerated corrosion, and polythionic acid SCC. Candidates should be able to identify the affected materials, key process variables, morphology, and appropriate NDE method for each of these mechanisms without needing to search the reference extensively.
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