{"id":207,"title":"API 510 Practice Questions 2026: 30 MCQs with Answers & Code References","slug":"api-510-practice-questions","date":"May 16, 2026","snippet":"2026 API 510 exam prep: 30 practice MCQs with full explanations, ASME VIII Div 1 and API 510/571/572/580 references, exam tips, study plan and FAQ.","content":"<!-- atlantis-inline-anchors-v1 -->\n<p>This 2026 practice question bank prepares candidates for the <strong><a href=\"/api-510-certification\">API 510</a> Pressure Vessel Inspector</strong> certification exam administered by the American Petroleum Institute (API). The questions below are referenced to the API 510 Body of Knowledge (BOK), with primary code references to <strong>API 510 Pressure Vessel Inspection Code (In-service Inspection, Rating, Repair, and Alteration)</strong>, <strong>API RP 572 (Inspection Practices for Pressure Vessels)</strong>, <strong>API RP 576 (Inspection of Pressure-Relieving Devices)</strong>, <strong>API RP 577 (Welding Inspection and Metallurgy)</strong>, <strong>API RP 580 (Risk-Based Inspection)</strong>, <strong>API 579-1/ASME FFS-1 (Fitness-for-Service)</strong>, and <strong>ASME BPVC Sections V, VIII Div 1, and IX</strong>.</p>\n<h2>API 510 Exam Format Overview</h2>\n<p>The API 510 exam is administered as a computer-based test (CBT) at Prometric centers in two parts:</p>\n<ul>\n<li><strong>Closed-book:</strong> 50 multiple-choice questions in 2 hours and 45 minutes. Covers general knowledge of vessel inspection, basic metallurgy, NDT, welding, corrosion, and code requirements that can be answered without reference materials.</li>\n<li><strong>Open-book:</strong> 60 to 80 multiple-choice questions in 4 hours and 45 minutes. Candidates use the full set of API 510 reference publications (downloaded as searchable PDFs at the test center).</li>\n<li><strong>Pass mark:</strong> 70% (combined or per section depending on cycle).</li>\n<li><strong>Recertification:</strong> Every 3 years (with reduced exam) and 6 years (full exam).</li>\n</ul>\n<h2>API 510 Practice Questions</h2>\n<div class=\"question\"><h3>Question 1: Per API 510, the maximum interval between external inspections of a pressure vessel is:</h3><ul class=\"options\"><li><strong>A.</strong> 1 year</li><li><strong>B.</strong> 3 years</li><li><strong>C.</strong> 5 years</li><li><strong>D.</strong> 10 years</li></ul><p><strong>Correct Answer: C</strong></p><p><em>Explanation:</em> Per API 510 Section 6.4, external inspection intervals shall not exceed 5 years or the required internal/on-stream inspection interval, whichever is less. Insulated vessels follow the same rule with CUI considerations.</p></div>\n<div class=\"question\"><h3>Question 2: The maximum internal inspection interval for a pressure vessel is:</h3><ul class=\"options\"><li><strong>A.</strong> The lesser of half the remaining life or 10 years</li><li><strong>B.</strong> 5 years</li><li><strong>C.</strong> 20 years</li><li><strong>D.</strong> Never required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 510 Section 6.5.1 limits the internal (or on-stream) inspection interval to the lesser of one-half the remaining corrosion life or 10 years. RBI-based intervals can extend this with proper justification under API 580.</p></div>\n<div class=\"question\"><h3>Question 3: Long-term corrosion rate is calculated by:</h3><ul class=\"options\"><li><strong>A.</strong> Initial thickness minus current thickness divided by time since installation</li><li><strong>B.</strong> Current thickness divided by years in service</li><li><strong>C.</strong> Wall loss in the last year</li><li><strong>D.</strong> Not calculated</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Long-term corrosion rate (LTCR) = (t-initial &minus; t-actual) / (years between t-initial and t-actual). Short-term rate (STCR) uses the period between the previous and current inspection. The greater rate is generally used for remaining life calculations.</p></div>\n<div class=\"question\"><h3>Question 4: Per API 510, a pressure vessel weld repair requires:</h3><ul class=\"options\"><li><strong>A.</strong> No special procedure</li><li><strong>B.</strong> Written repair plan approved by the inspector and engineer, qualified WPS, qualified welders, NDT, and post-weld treatment as required</li><li><strong>C.</strong> Only welder qualification</li><li><strong>D.</strong> Only NDT after repair</li></ul><p><strong>Correct Answer: B</strong></p><p><em>Explanation:</em> API 510 Section 8 requires a documented repair plan, qualified WPS/PQR per ASME IX, qualified welder/welding operator, applicable NDT, and post-weld heat treatment (PWHT) where required by original construction code or alteration analysis.</p></div>\n<div class=\"question\"><h3>Question 5: A vessel’s MAWP is governed by:</h3><ul class=\"options\"><li><strong>A.</strong> Hydrostatic test pressure</li><li><strong>B.</strong> The weakest component, calculated using current thickness less FCA</li><li><strong>C.</strong> Operator preference</li><li><strong>D.</strong> Nameplate pressure regardless of corrosion</li></ul><p><strong>Correct Answer: B</strong></p><p><em>Explanation:</em> MAWP is the maximum pressure at which the weakest component will safely operate, calculated using current measured thickness minus the future corrosion allowance (FCA). MAWP is updated when corrosion or alterations change the rating.</p></div>\n<div class=\"question\"><h3>Question 6: Per API 580, RBI (Risk-Based Inspection) uses:</h3><ul class=\"options\"><li><strong>A.</strong> Probability of failure (PoF) &times; Consequence of failure (CoF) = Risk</li><li><strong>B.</strong> Only corrosion rate</li><li><strong>C.</strong> Only vessel age</li><li><strong>D.</strong> Random selection</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Risk = PoF &times; CoF. PoF accounts for damage mechanisms, inspection effectiveness, and remaining life; CoF accounts for safety, environmental, and business impact. The risk matrix drives inspection planning per API 580/581.</p></div>\n<div class=\"question\"><h3>Question 7: Pressure relief valve (PRV) inspection per API 510 and API 576 must occur:</h3><ul class=\"options\"><li><strong>A.</strong> At the same interval as the vessel internal inspection, not to exceed 5 years (clean service) or 10 years for RBI</li><li><strong>B.</strong> Every 20 years</li><li><strong>C.</strong> Never</li><li><strong>D.</strong> Only when leaking</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 510 Section 6.6 and API 576 typically require PRV testing/inspection every 5 years (clean services) or 10 years (RBI-justified). PRVs in severe or fouling service may require more frequent inspection.</p></div>\n<div class=\"question\"><h3>Question 8: Per ASME VIII Div 1 Appendix 3, the minimum thickness for a cylindrical shell under internal pressure is:</h3><ul class=\"options\"><li><strong>A.</strong> t = PR / (SE &minus; 0.6P)</li><li><strong>B.</strong> t = PD / 2S</li><li><strong>C.</strong> t = PR / (SE + 0.4P)</li><li><strong>D.</strong> Determined by test only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME VIII Div 1 UG-27: t = PR / (SE &minus; 0.6P) for circumferential stress (governs thin-walled cylinders). The alternate formula t = PR / (2SE + 0.4P) for longitudinal stress is rarely governing. Joint efficiency E depends on RT.</p></div>\n<div class=\"question\"><h3>Question 9: An on-stream inspection differs from internal inspection in that:</h3><ul class=\"options\"><li><strong>A.</strong> It is performed while the vessel is in service using NDT from outside</li><li><strong>B.</strong> It requires shutdown</li><li><strong>C.</strong> It is illegal</li><li><strong>D.</strong> Only used for tanks</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> On-stream inspection uses external NDT (UT, RT, profile RT, guided wave UT, PEC) to assess vessel condition without entry. Per API 510, on-stream may substitute for internal inspection if the inspector and engineer can determine vessel integrity to the same degree.</p></div>\n<div class=\"question\"><h3>Question 10: Per API 510, an authorized pressure vessel inspector must:</h3><ul class=\"options\"><li><strong>A.</strong> Hold a current API 510 certification and the experience requirements of API 510 Section 4</li><li><strong>B.</strong> Hold <a href=\"/consulting/asnt-level-iii-consulting-services\">ASNT Level III</a> in all methods</li><li><strong>C.</strong> Be a licensed PE</li><li><strong>D.</strong> Be the vessel owner</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Authorized inspectors must hold current API 510 certification with required experience (4-year degree + 1 yr, or 2-year degree + 2 yrs, or HS + 3 yrs, etc.) and operate under a quality system. PE is required only when API 510 specifies engineer involvement.</p></div>\n<div class=\"question\"><h3>Question 11: When a vessel has a corrosion rate of 0.1 mm/yr, FCA of 1.6 mm, current thickness of 12 mm, minimum required thickness of 10 mm, the remaining life is:</h3><ul class=\"options\"><li><strong>A.</strong> 4 years</li><li><strong>B.</strong> 20 years</li><li><strong>C.</strong> 100 years</li><li><strong>D.</strong> 2 years</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Remaining life = (t-actual &minus; t-min) / corrosion rate = (12 &minus; 10) / 0.1 = 20 years (without FCA) or (12 &minus; 10 &minus; 1.6) / 0.1 = 4 years if FCA must be retained. API 510 uses the more conservative number for inspection planning.</p></div>\n<div class=\"question\"><h3>Question 12: Per API 510 alteration vs repair definition, an alteration is:</h3><ul class=\"options\"><li><strong>A.</strong> Any physical change that changes the design conditions, vessel rating, or geometry</li><li><strong>B.</strong> Any weld repair</li><li><strong>C.</strong> Replacement of a gasket</li><li><strong>D.</strong> External painting</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Per API 510, an alteration changes the design conditions (T, P, MAWP), vessel rating, or geometry (e.g., adding a nozzle). A repair restores the vessel to a condition suitable for safe operation without changing the rating. Alterations require engineering review.</p></div>\n<div class=\"question\"><h3>Question 13: Hot tapping refers to:</h3><ul class=\"options\"><li><strong>A.</strong> Welding on equipment in service while contents are flowing</li><li><strong>B.</strong> Cleaning the vessel with steam</li><li><strong>C.</strong> Heat treatment</li><li><strong>D.</strong> Hydrostatic test</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Hot tapping is welding (typically a nozzle) onto a pressurized line or vessel and then drilling through. API RP 2201 governs hot tap procedures including burn-through prevention, hazard analysis, and procedure qualification.</p></div>\n<div class=\"question\"><h3>Question 14: Per API 510, weld overlay used as a repair must:</h3><ul class=\"options\"><li><strong>A.</strong> Be classified as a temporary repair only</li><li><strong>B.</strong> Use a qualified WPS, NDT after welding, and PWHT if required</li><li><strong>C.</strong> Not be permitted</li><li><strong>D.</strong> Use bolted patches</li></ul><p><strong>Correct Answer: B</strong></p><p><em>Explanation:</em> Weld overlay (build-up) repairs are permitted as permanent repairs under API 510 Section 8, requiring qualified WPS, qualified welders, NDT, and PWHT if mandated by base metal P-number or carbon equivalent rules.</p></div>\n<div class=\"question\"><h3>Question 15: A fillet weld patch (lap patch) is:</h3><ul class=\"options\"><li><strong>A.</strong> A permanent repair</li><li><strong>B.</strong> A temporary repair limited by API 510 Section 8.1.5</li><li><strong>C.</strong> Always prohibited</li><li><strong>D.</strong> A nozzle attachment</li></ul><p><strong>Correct Answer: B</strong></p><p><em>Explanation:</em> Fillet welded patches are permitted as temporary repairs per API 510 Section 8.1.5 with limits on size, design analysis, NDT, and a defined service period until a permanent repair can be made.</p></div>\n<div class=\"question\"><h3>Question 16: Per ASME VIII Div 1 UCS-79, post-weld heat treatment is required when:</h3><ul class=\"options\"><li><strong>A.</strong> Always</li><li><strong>B.</strong> Based on P-number, thickness, and service per UCS-56 tables</li><li><strong>C.</strong> Only stainless</li><li><strong>D.</strong> Never required</li></ul><p><strong>Correct Answer: B</strong></p><p><em>Explanation:</em> ASME VIII Div 1 UCS-56 specifies PWHT requirements based on material P-number and nominal thickness. Common rule: P-No. 1 carbon steel typically needs PWHT above 19 mm (3/4 in) thickness; lower-alloy steels at lesser thickness.</p></div>\n<div class=\"question\"><h3>Question 17: API 579-1/ASME FFS-1 Level 1 assessment is for:</h3><ul class=\"options\"><li><strong>A.</strong> Conservative screening calculations using look-up tables and simple formulas</li><li><strong>B.</strong> Finite element analysis only</li><li><strong>C.</strong> Material replacement</li><li><strong>D.</strong> Never used</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 579 organizes Fitness-for-Service assessments in three levels: Level 1 (conservative tables/formulas), Level 2 (more detailed calculations with material properties), Level 3 (advanced FEA / probabilistic). The inspector typically performs Level 1; engineers Level 2 and 3.</p></div>\n<div class=\"question\"><h3>Question 18: Stress corrosion cracking (SCC) in stainless steel is typically caused by:</h3><ul class=\"options\"><li><strong>A.</strong> Chloride ion exposure at elevated temperature</li><li><strong>B.</strong> Carbon dioxide</li><li><strong>C.</strong> Sulfur</li><li><strong>D.</strong> Inert gas</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Chloride stress corrosion cracking (Cl-SCC) of austenitic stainless steel (304/316) occurs typically above 60&deg;C in chloride-bearing solutions. Insulation chlorides leaching with water is a common source. API RP 581 lists SCC mechanisms.</p></div>\n<div class=\"question\"><h3>Question 19: Per API RP 577, hydrogen damage in welds includes:</h3><ul class=\"options\"><li><strong>A.</strong> Hydrogen-induced cracking (HIC), sulfide stress cracking (SSC), HTHA</li><li><strong>B.</strong> Only fatigue</li><li><strong>C.</strong> Only creep</li><li><strong>D.</strong> Only erosion</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API RP 577 and API 571 cover hydrogen damage: HIC (blistering and crack networks in wet H2S), SSC (sulfide stress cracking in hard welds and HAZ), HSC (hydrogen stress cracking), and HTHA (high-temperature hydrogen attack &mdash; Nelson curves).</p></div>\n<div class=\"question\"><h3>Question 20: Per API 510, a vessel that has had a major repair must be:</h3><ul class=\"options\"><li><strong>A.</strong> Hydro-tested at 1.3 &times; MAWP or otherwise verified</li><li><strong>B.</strong> Hydrotested at MAWP only</li><li><strong>C.</strong> Vented</li><li><strong>D.</strong> Replaced</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Hydrostatic test pressure after major repair/alteration is typically 1.3 &times; MAWP &times; (Sa/Sd) per ASME VIII Div 1 UG-99, where Sa/Sd is the stress ratio at test/design temperatures. Alternative NDT and engineering analysis may substitute.</p></div>\n<div class=\"question\"><h3>Question 21: The most common NDT method for verifying vessel wall thickness from outside is:</h3><ul class=\"options\"><li><strong>A.</strong> Ultrasonic thickness gauging (UT)</li><li><strong>B.</strong> Liquid penetrant</li><li><strong>C.</strong> Magnetic particle</li><li><strong>D.</strong> Visual only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> UT thickness is the workhorse NDT for vessel wall measurement. Spot UT at TML (thickness measurement locations) and scanning UT (corrosion mapping) are both used. Profile RT, PAUT corrosion mapping, and PEC for through-insulation are also acceptable.</p></div>\n<div class=\"question\"><h3>Question 22: A vessel’s thickness measurement location (TML) is selected based on:</h3><ul class=\"options\"><li><strong>A.</strong> Damage mechanism, geometry (heads, shells, nozzles), and historical thinning</li><li><strong>B.</strong> Random</li><li><strong>C.</strong> Only the manway</li><li><strong>D.</strong> Anywhere convenient</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> TMLs are placed at expected damage locations based on the dominant damage mechanism, geometry (shells, heads, knuckle radii, nozzles, manways), inlet/outlet, level lines, and historical thinning. API RP 572 provides guidance on TML selection.</p></div>\n<div class=\"question\"><h3>Question 23: Per API 510, the inspector’s authority includes:</h3><ul class=\"options\"><li><strong>A.</strong> Approving repair plans, accepting NDT results, and verifying conformance to code</li><li><strong>B.</strong> Designing new vessels</li><li><strong>C.</strong> Setting operating pressure</li><li><strong>D.</strong> Hiring welders without qualification</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> The authorized inspector is responsible for verifying inspection, repair, and alteration activities meet API 510 and applicable code. Design and reratings involve the engineer (PE or qualified equivalent).</p></div>\n<div class=\"question\"><h3>Question 24: Joint efficiency E in ASME VIII Div 1 depends on:</h3><ul class=\"options\"><li><strong>A.</strong> Type of joint and extent of radiography</li><li><strong>B.</strong> Only the welder</li><li><strong>C.</strong> Pressure</li><li><strong>D.</strong> Material density</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME VIII Div 1 Table UW-12 gives joint efficiencies based on joint type (Type 1 butt weld, Type 2 single-V, etc.) and radiography category (Full, Spot, None). Typical values: E=1.0 for Type 1 with full RT; E=0.85 with spot; E=0.70 with no RT.</p></div>\n<div class=\"question\"><h3>Question 25: A nameplate on a pressure vessel must include:</h3><ul class=\"options\"><li><strong>A.</strong> Manufacturer, MAWP, design temperature, year built, serial number, code stamp</li><li><strong>B.</strong> Only serial number</li><li><strong>C.</strong> Only manufacturer</li><li><strong>D.</strong> No requirement</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME VIII Div 1 UG-119 requires the nameplate to include manufacturer, MAWP, design temperature, MDMT, year of construction, manufacturer’s serial number, and the appropriate ASME code stamp (U, UM, etc.).</p></div>\n<div class=\"question\"><h3>Question 26: Per API 571, sulfidation corrosion typically occurs:</h3><ul class=\"options\"><li><strong>A.</strong> At elevated temperatures in sulfur-containing hydrocarbon streams (e.g., crude unit, FCC)</li><li><strong>B.</strong> At ambient temperature</li><li><strong>C.</strong> Only in stainless</li><li><strong>D.</strong> Only with water</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Sulfidation is high-temperature corrosion of iron-based alloys by sulfur compounds, typically above 260&deg;C. The McConomy curves and modified McConomy provide thinning rate vs. temperature, sulfur content, and material. Common in crude distillation and FCC units.</p></div>\n<div class=\"question\"><h3>Question 27: A pressure vessel under cyclic service may be subject to:</h3><ul class=\"options\"><li><strong>A.</strong> Fatigue damage</li><li><strong>B.</strong> Only creep</li><li><strong>C.</strong> No damage</li><li><strong>D.</strong> Only corrosion</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Pressure cycles, thermal cycles, and vibration can initiate and propagate fatigue cracks, particularly at stress concentrations (nozzles, weld toes). API RP 579-1 Part 14 provides fatigue assessment procedures.</p></div>\n<div class=\"question\"><h3>Question 28: The minimum design metal temperature (MDMT) of a vessel is:</h3><ul class=\"options\"><li><strong>A.</strong> The lowest metal temperature at which the vessel can safely contain pressure</li><li><strong>B.</strong> Ambient temperature</li><li><strong>C.</strong> Operating temperature</li><li><strong>D.</strong> Hydrotest temperature</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> MDMT is the lowest expected metal temperature considering operation, startup, shutdown, and upsets. Material toughness must be sufficient at MDMT per UCS-66 charts. Brittle fracture risk increases as temperature drops below MDMT.</p></div>\n<div class=\"question\"><h3>Question 29: Per API 510, a temporary repair must be replaced with a permanent repair:</h3><ul class=\"options\"><li><strong>A.</strong> By the next scheduled turnaround, or as specified in the repair plan</li><li><strong>B.</strong> Never &mdash; temporary repairs are permanent</li><li><strong>C.</strong> Within 1 hour</li><li><strong>D.</strong> Only if leaking</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Temporary repairs are limited in scope and time. API 510 Section 8.1.5 requires them to be replaced with a permanent repair by the next scheduled turnaround or as documented in the engineering and inspector-approved repair plan.</p></div>\n<div class=\"question\"><h3>Question 30: Welder qualification per ASME IX requires:</h3><ul class=\"options\"><li><strong>A.</strong> Successful welder performance qualification (WPQ) test record</li><li><strong>B.</strong> Only a written test</li><li><strong>C.</strong> Visual inspection only</li><li><strong>D.</strong> No qualification needed</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME IX requires a welder performance qualification (WPQ) including production of a test coupon and acceptable NDT (RT or bend testing). The WPQ has essential variables that, if changed, may require requalification. Welders must maintain continuity (typically welding within the 6 months prior).</p></div>\n<h2>Study Tips for API 510</h2>\n<ul>\n<li><strong>Master the BOK:</strong> Download the API 510 Body of Knowledge from the API Individual Certification Programs (ICP) page. Every question on the exam maps to a BOK item.</li>\n<li><strong>Use the right edition:</strong> The exam references specific editions of API 510, RP 572, RP 576, RP 577, RP 580, ASME V, VIII Div 1, IX, and API 571. Check the API ICP body of knowledge document for the current exam cycle.</li>\n<li><strong>Tab your books:</strong> Open-book is open-book in name only &mdash; if you cannot find the answer in 90 seconds, you will not finish. Tab key sections in every reference: API 510 Sections 5-8, ASME VIII UG-22 to UG-37 and UG-99, ASME IX QW-200 to QW-300.</li>\n<li><strong>Practice calculations:</strong> MAWP from t-min, remaining life, corrosion rates, joint efficiency, hydrotest pressure. Plan on 200+ calculation problems before the exam.</li>\n<li><strong>Read API 571:</strong> Damage mechanisms appear on every exam. Memorize the 30+ mechanisms in API 571 with morphology and typical NDT.</li>\n</ul>\n<h2>Recommended Study Materials</h2>\n<ul>\n<li>API 510 Pressure Vessel Inspection Code (current edition)</li>\n<li>API RP 572 Inspection Practices for Pressure Vessels</li>\n<li>API RP 576 Inspection of Pressure-Relieving Devices</li>\n<li>API RP 577 Welding Inspection and Metallurgy</li>\n<li>API RP 580 Risk-Based Inspection</li>\n<li>API 571 Damage Mechanisms Affecting Fixed Equipment</li>\n<li>ASME BPVC Sections V, VIII Div 1, and IX</li>\n<li>Atlantis NDT <a href=\"/api-510-certification\">API 510 exam preparation course</a></li>\n</ul>\n<h2>Frequently Asked Questions</h2>\n<h3>Q: What experience do I need to sit the API 510 exam?</h3>\n<p>A: API 510 requires combinations like: BS in engineering plus 1 year, or 2-year engineering degree plus 2 years, or high school plus 3 years of NDT/inspection-related experience. Verify the current API ICP requirements.</p>\n<h3>Q: How long does API 510 certification last?</h3>\n<p>A: 3 years to a reduced recertification exam (open-book only), then 6 years for the full recertification exam. Continuous practice as an inspector is also required.</p>\n<h3>Q: Are API 510 and ASNT certifications the same?</h3>\n<p>A: No. API 510 certifies you as a vessel inspector (a code-driven role); ASNT certifies you in NDT methods (UT, RT, MT, PT, etc.). Many inspectors hold both. See our <a href=\"/blog/asnt-vs-pcn-certification-comparison\">ASNT vs PCN comparison</a> for NDT body certifications and our <a href=\"/asnt-certification\">ASNT certification page</a> for ASNT routes.</p>\n<h3>Q: Is API 510 recognized internationally?</h3>\n<p>A: Yes. API 510 is widely recognized globally, especially in oil &amp; gas. In Europe, PED-driven Notified Body assessments may also apply. In Saudi Aramco SAES requirements explicitly reference API 510 inspectors.</p>\n<h3>Q: What is the difference between API 510 and API 570?</h3>\n<p>A: API 510 covers pressure vessels; API 570 covers in-service piping. See our <a href=\"/blog/api-510-vs-570-comparison\">API 510 vs API 570 comparison</a>.</p>\n<h3>Q: Does Atlantis NDT offer API 510 review courses?</h3>\n<p>A: No. Atlantis NDT does not run API 510 exam-preparation courses. Our <a href=\"/consulting/api-510-pressure-vessel-inspector-services\">API 510 pressure vessel inspection support</a> is ASNT Level III technical work on vessel programmes — RBI, FFS and data review — not exam coaching.</p>\n<h3>Q: Can I take the API 510 exam online?</h3>\n<p>A: API exams are administered through Prometric test centers worldwide (computer-based test). Online proctoring options have been piloted; verify the latest with API ICP at the time of registration.</p>\n<h3>Q: What is the API 510 exam pass rate?</h3>\n<p>A: Industry averages range from 50 to 65% first attempt. Candidates from structured prep courses typically report 80%+ first try.</p>\n<h3>Q: How much does an API 510 certified inspector earn?</h3>\n<p>A: In the US, $90,000 to $140,000/year base, plus offshore/turnaround premiums. In the Middle East, $7,000 to a modest cost/month tax-free for experienced inspectors. Salary scales with API 570 + 653 stacking.</p>\n<h3>Q: Does the API 510 exam include ASME IX?</h3>\n<p>A: Yes &mdash; welding procedure and welder performance qualification under ASME IX is a major open-book topic. Tab QW-200 (WPS/PQR), QW-300 (welder performance), and QW-400 (essential variables tables).</p>\n\n<h2>About Atlantis NDT</h2>\n<p>Atlantis NDT is a global NDT technology and services company headquartered in Houston, Texas with operations across India and the Middle East. We deliver <a href=\"/training\">accredited NDT training</a>, <a href=\"/consulting\">technical consulting</a>, certification preparation, and digital inspection software trusted by oil &amp; gas, fabrication, EPC, and power generation clients. Our team of <strong>ASNT Level III</strong> instructors has trained thousands of inspectors worldwide.</p>\n<p>Whether you are preparing for <a href=\"/asnt-certification\">ASNT certification</a>, <a href=\"/api-510-certification\">API 510</a>, <a href=\"/api-570-certification\">API 570</a>, or <a href=\"/api-653-certification\">API 653</a>, our exam preparation programs combine classroom theory, hands-on practical training, and proctored mock exams that mirror the real test environment.</p>\n<p><strong>Call us at +1 (281) 840-8969</strong> or email <a href=\"mailto:sales@atlantisndt.com\">sales@atlantisndt.com</a> to enroll in the next training cohort. Same-day quotes for corporate group training, delivered online, live-virtual, or on-site at your facility.</p>\n","author":"Atlantis NDT","order":28,"createdAt":"2026-05-16","updatedAt":"2028-01-17","metaDescription":"API 510 practice questions 2026: 30 MCQs, code references (ASME VIII, API 510/571), exam tips, FAQ. Free pressure vessel inspector study guide."}