{"id":208,"title":"API 570 Practice Questions 2026: 30 Piping Inspector MCQs & Answers","slug":"api-570-practice-questions","date":"May 16, 2026","snippet":"API 570 practice questions 2026: 30 MCQs, ASME B31.3 & API 570/571/577 references, TML, CUI, NAC, hot tap. Free Atlantis NDT piping inspector guide.","content":"<!-- atlantis-inline-anchors-v1 -->\n<p>This 2026 practice exam bank prepares candidates for the <strong><a href=\"/api-570-certification\">API 570</a> Piping Inspector</strong> certification. The questions reflect the API 570 Body of Knowledge (BOK) and reference <strong>API 570 Piping Inspection Code (In-service Inspection, Rating, Repair, and Alteration)</strong>, <strong>API RP 574 (Inspection Practices for Piping System Components)</strong>, <strong>API RP 577 (Welding Inspection and Metallurgy)</strong>, <strong>API RP 578 (Material Verification Program)</strong>, <strong>API RP 576 (Pressure-Relieving Devices)</strong>, <strong>ASME PCC-2</strong>, <strong>API 571 (Damage Mechanisms)</strong>, <strong>ASME B31.3 (Process Piping)</strong>, and <strong>ASME B16.5, BPVC V and IX</strong>.</p>\n<h2>API 570 Exam Format Overview</h2>\n<p>From the API 570 program page on api.org (check it before you book; details change by exam window):</p>\n<ul>\n<li><strong>Questions:</strong> 170 multiple-choice (140 scored, 30 unscored pretest).</li>\n<li><strong>Structure:</strong> a closed-book part (110 questions) and an open-book part (60 questions) with the reference publications provided electronically on screen.</li>\n<li><strong>Time:</strong> about 7.5 hours including the tutorial and a break.</li>\n<li><strong>Delivery:</strong> in person at Prometric test centers only (remote proctoring for API 510, 570 and 653 ended with the September 2024 window).</li>\n<li><strong>Pass mark:</strong> a scaled score (API reports scaled scores; 400 is the pass point on API&apos;s scale), not a fixed percentage.</li>\n<li><strong>Recertification:</strong> every 3 years: at least 20% of working time on inspection activities, 24 continuing professional development (CPD) hours, and an online web quiz every 6 years.</li>\n<li><strong>Referenced documents:</strong> API 570, API RP 571, RP 574, RP 576, RP 577, RP 578, ASME Section V, Section IX, ASME B16.5, B31.3 and ASME PCC-2 (editions per the current Publications Effectivity Sheet).</li>\n</ul>\n<h2>API 570 Practice Questions</h2>\n<div class=\"question\"><h3>Question 1: Per API 570, the maximum interval for visual external inspection of Class 1 piping is:</h3><ul class=\"options\"><li><strong>A.</strong> 5 years</li><li><strong>B.</strong> 10 years</li><li><strong>C.</strong> 1 year</li><li><strong>D.</strong> Never</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 570&apos;s recommended maximum inspection interval table gives visual external intervals of 5 years for Class 1, 5 years for Class 2, 10 years for Class 3, and optional for Class 4. (The half-remaining-life limit applies to thickness measurements, not external visual.) Class definitions depend on consequence (toxic/flammable/etc.).</p></div>\n<div class=\"question\"><h3>Question 2: Class 1 piping per API 570 is:</h3><ul class=\"options\"><li><strong>A.</strong> Highest consequence (e.g., flammable services that vaporize, anhydrous HF, H2S above 3%)</li><li><strong>B.</strong> Lowest consequence</li><li><strong>C.</strong> Tanks</li><li><strong>D.</strong> Vessels only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 570 classifies piping by consequence: Class 1 highest (flashing flammables, HF, H2S above 3%, anhydrous HCl), Class 2 (most flammables, on-site steam, acids/caustics), Class 3 (flammables that do not vaporize, non-toxic), Class 4 (water, plant air).</p></div>\n<div class=\"question\"><h3>Question 3: Per ASME B31.3, the minimum required thickness of straight pipe under internal pressure is:</h3><ul class=\"options\"><li><strong>A.</strong> t = PD / (2(SE + PY))</li><li><strong>B.</strong> t = PR / 2S</li><li><strong>C.</strong> t = D / 10</li><li><strong>D.</strong> Determined experimentally</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME B31.3 Eq. 3a: t = PD / (2(SE + PY)) where P = pressure, D = OD, S = allowable stress, E = quality factor, Y = coefficient from Table 304.1.1. Add mill tolerance (typically 12.5%) and corrosion allowance for required nominal thickness.</p></div>\n<div class=\"question\"><h3>Question 4: A thickness measurement location (TML) for piping is typically:</h3><ul class=\"options\"><li><strong>A.</strong> At elbows, tees, reducers, and high-velocity/turbulent zones where erosion/corrosion is expected</li><li><strong>B.</strong> Anywhere convenient</li><li><strong>C.</strong> Only on straight runs</li><li><strong>D.</strong> Never on fittings</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Per API 570 and RP 574, TMLs concentrate at locations of expected damage: elbows (extrados &amp; intrados), tees, reducers, dead legs, injection points, mixing points, vents/drains, and at known damage mechanism locations.</p></div>\n<div class=\"question\"><h3>Question 5: Injection points per API 570 require:</h3><ul class=\"options\"><li><strong>A.</strong> Special inspection circuits with dedicated TMLs upstream, downstream, and at the injection point</li><li><strong>B.</strong> No special inspection</li><li><strong>C.</strong> Removal at every turnaround</li><li><strong>D.</strong> Visual only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Injection points (e.g., corrosion inhibitor, water, antifoulant injection) experience accelerated localized corrosion downstream. API 570 treats injection points as separate circuits; the recommended upstream limit is the greater of 12 in. (300 mm) or three pipe diameters upstream, and the downstream limit is the lesser of the second change in flow direction past the injection point or 25 ft (7.6 m) beyond the first change in flow direction. Injection-point thickness measurements have a 3-year recommended maximum interval.</p></div>\n<div class=\"question\"><h3>Question 6: Corrosion under insulation (CUI) is most likely on piping in service between:</h3><ul class=\"options\"><li><strong>A.</strong> &#x2212;12 to 175&#xB0;C (10 to 350&#xB0;F), with peak risk near dew point</li><li><strong>B.</strong> Above 500&#xB0;C only</li><li><strong>C.</strong> Cryogenic only</li><li><strong>D.</strong> Not real</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> CUI is most aggressive in the temperature range where moisture can be present beneath the insulation: &#x2212;12 to 175&#xB0;C (carbon steel). API 570 and API RP 583 give CUI risk-based inspection guidance. Stainless can suffer chloride SCC in this same range.</p></div>\n<div class=\"question\"><h3>Question 7: Dead legs in piping are concerning because:</h3><ul class=\"options\"><li><strong>A.</strong> Stagnant fluid concentrates corrosion attack</li><li><strong>B.</strong> They reduce pressure drop</li><li><strong>C.</strong> They are required by code</li><li><strong>D.</strong> They prevent corrosion</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Dead legs (block valves, vent lines, dead-end caps) accumulate stagnant fluid, water, sediment, or vapor that drive localized corrosion, MIC, and freeze damage. API 570 requires identification and special inspection of dead legs.</p></div>\n<div class=\"question\"><h3>Question 8: Per API 570, online (on-stream) inspection may be used in lieu of internal inspection when:</h3><ul class=\"options\"><li><strong>A.</strong> External NDT can determine the integrity of the piping with equivalent confidence</li><li><strong>B.</strong> The owner waives the inspection</li><li><strong>C.</strong> Pressure is below 50 psi</li><li><strong>D.</strong> Never</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Most piping cannot be entered for internal inspection. API 570 requires external NDT (UT, RT, guided wave UT, PEC, PAUT corrosion mapping) at intervals that establish integrity. Internal inspection at openings is performed where access allows.</p></div>\n<div class=\"question\"><h3>Question 9: A piping system suffering high temperature hydrogen attack (HTHA) per API 941 (Nelson curves) typically has:</h3><ul class=\"options\"><li><strong>A.</strong> Service above hydrogen partial pressure / temperature limits for the alloy</li><li><strong>B.</strong> Service in air only</li><li><strong>C.</strong> Cold service</li><li><strong>D.</strong> Vacuum service</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> HTHA per API 941 occurs in carbon and low-alloy steels exposed to hydrogen partial pressure and elevated temperature combinations that exceed Nelson curve limits. AUBT (Advanced Ultrasonic Backscatter Technique), TOFD, and metallographic replication are used to detect HTHA.</p></div>\n<div class=\"question\"><h3>Question 10: Per API RP 578, a material verification program (PMI) is required to:</h3><ul class=\"options\"><li><strong>A.</strong> Verify alloy components are the specified material grade</li><li><strong>B.</strong> Measure thickness</li><li><strong>C.</strong> Detect cracks</li><li><strong>D.</strong> Test welds only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Positive Material Identification (PMI) uses portable XRF or OES to verify alloy composition during construction, repair, and in-service. API RP 578 prevents catastrophic failures from material mix-ups (e.g., carbon steel instead of 5Cr-1/2Mo in a hot piping system).</p></div>\n<div class=\"question\"><h3>Question 11: Per API 570, the maximum thickness measurement interval for Class 1 piping is:</h3><ul class=\"options\"><li><strong>A.</strong> 5 years or 1/2 remaining life, whichever is less</li><li><strong>B.</strong> 10 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 570 limits thickness measurement intervals to the lesser of one-half remaining life or the table maximum: 5 years for Class 1, 10 years for Class 2, 10 years for Class 3, optional for Class 4 (3 years for injection points). RBI may modify these intervals.</p></div>\n<div class=\"question\"><h3>Question 12: An authorized piping inspector per API 570 must:</h3><ul class=\"options\"><li><strong>A.</strong> Hold current API 570 certification and meet experience requirements</li><li><strong>B.</strong> Hold <a href=\"/consulting/ndt-consulting-level-iii\">ASNT Level III</a></li><li><strong>C.</strong> Be a PE</li><li><strong>D.</strong> Be the owner</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 570 Section 4 requires the inspector to hold current API 570 certification, experience per the API ICP requirements, and operate under the owner/user&#x2019;s inspection management system.</p></div>\n<div class=\"question\"><h3>Question 13: A repair to in-service piping per API 570 requires:</h3><ul class=\"options\"><li><strong>A.</strong> Written repair plan approved by inspector and engineer, qualified WPS, qualified welders, NDT, and post-weld treatment as required</li><li><strong>B.</strong> Just the welder&#x2019;s name</li><li><strong>C.</strong> Only the engineer</li><li><strong>D.</strong> No documentation</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 570 Section 8 requires documented repair plans, qualified WPS/PQR per ASME IX or B31.3 Chapter V, qualified welders, applicable NDT, and PWHT as required by base metal and service.</p></div>\n<div class=\"question\"><h3>Question 14: A bolted clamp on a leaking pipe is:</h3><ul class=\"options\"><li><strong>A.</strong> A temporary repair allowed under specific API 570 limits</li><li><strong>B.</strong> Always prohibited</li><li><strong>C.</strong> A permanent solution</li><li><strong>D.</strong> Required at every flange</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Bolted clamps and enclosures (e.g., engineered leak repair) are temporary repairs that must be designed, documented, and replaced with a permanent repair by the next planned turnaround per API 570 Section 8.</p></div>\n<div class=\"question\"><h3>Question 15: ASME B31.3 sets the allowable stress S based on:</h3><ul class=\"options\"><li><strong>A.</strong> The lower of UTS/3, YS/1.5, creep, or rupture data at temperature</li><li><strong>B.</strong> Only UTS</li><li><strong>C.</strong> Only YS</li><li><strong>D.</strong> Manufacturer choice</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME B31.3 Table A-1 allowable stress S is the lowest of (UTS at T)/3, (UTS at 38&#xB0;C)/3, (YS at T)/1.5, (YS at 38&#xB0;C)/1.5, and creep/rupture rules. Different ratios apply for high-pressure piping (Chapter IX).</p></div>\n<div class=\"question\"><h3>Question 16: A flange rating per ASME B16.5 (e.g., Class 150, 300, 600) refers to:</h3><ul class=\"options\"><li><strong>A.</strong> Pressure-temperature rating tables for various materials</li><li><strong>B.</strong> Outside diameter</li><li><strong>C.</strong> Bolt count</li><li><strong>D.</strong> Manufacturer code</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> B16.5 Class is a pressure rating that varies with material group and temperature. For example, Class 300 carbon steel (Group 1.1) rates 740 psig at 100&#xB0;F and drops to 290 psig at 850&#xB0;F. Each class has a full temperature-pressure curve.</p></div>\n<div class=\"question\"><h3>Question 17: A test pressure for piping per ASME B31.3 is typically:</h3><ul class=\"options\"><li><strong>A.</strong> 1.5 &#xD7; design pressure (hydrostatic) or 1.1 &#xD7; (pneumatic)</li><li><strong>B.</strong> 1.0 &#xD7; design</li><li><strong>C.</strong> 5 &#xD7; design</li><li><strong>D.</strong> No test required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> B31.3 paragraph 345 specifies hydrostatic test at 1.5 &#xD7; design pressure adjusted for temperature ratio, or pneumatic at 1.1 &#xD7; design with hazard considerations. Sensitive leak testing is allowed under specific conditions.</p></div>\n<div class=\"question\"><h3>Question 18: Per API 571, naphthenic acid corrosion (NAC) typically affects:</h3><ul class=\"options\"><li><strong>A.</strong> Crude unit vacuum tower and side draws at 220 to 400&#xB0;C, high TAN crudes</li><li><strong>B.</strong> Sour water piping</li><li><strong>C.</strong> Refrigerated services</li><li><strong>D.</strong> Steam lines</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> NAC affects crude distillation and vacuum unit piping when TAN exceeds 0.5 mg KOH/g, in the 220 to 400&#xB0;C window, with high velocity/turbulence. 316/317 stainless or 5Cr-1/2Mo with selective upgrade are typical remedies.</p></div>\n<div class=\"question\"><h3>Question 19: A pipe support that is missing or damaged may cause:</h3><ul class=\"options\"><li><strong>A.</strong> Excessive thermal stress, sag, fatigue, and accelerated wear at adjacent supports</li><li><strong>B.</strong> No issue</li><li><strong>C.</strong> Improved flow</li><li><strong>D.</strong> Heat loss only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Inspectors should record damaged or missing pipe supports during external inspection. Loss of support shifts loads to remaining supports, creates fatigue, and may cause excessive stress in nozzles and flanges.</p></div>\n<div class=\"question\"><h3>Question 20: Per API 570, soil-to-air interface inspection on buried piping is critical because:</h3><ul class=\"options\"><li><strong>A.</strong> Accelerated corrosion occurs at the transition due to moisture, coatings damage, and aeration</li><li><strong>B.</strong> Decoration</li><li><strong>C.</strong> Maintenance access only</li><li><strong>D.</strong> Not required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> The soil-to-air interface (generally considered to run from 12 in. below to 6 in. above the soil surface) experiences accelerated external corrosion. API 570 requires these zones to be inspected, including excavation or coating removal where indicated.</p></div>\n<div class=\"question\"><h3>Question 21: A piping system with intermittent service that allows water accumulation may suffer:</h3><ul class=\"options\"><li><strong>A.</strong> Microbiologically influenced corrosion (MIC)</li><li><strong>B.</strong> No damage</li><li><strong>C.</strong> Only creep</li><li><strong>D.</strong> Only fatigue</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> MIC by sulfate-reducing bacteria (SRB) and other microbes accelerates pitting and weld metal corrosion. Common in firewater piping, intermittent service lines, and hydrotest water left in pipe. API 571 documents MIC mechanisms and inspection.</p></div>\n<div class=\"question\"><h3>Question 22: A guided wave UT (GWUT) survey on piping is best for:</h3><ul class=\"options\"><li><strong>A.</strong> Screening long lengths of pipe for significant cross-section reductions</li><li><strong>B.</strong> Crack sizing</li><li><strong>C.</strong> Surface flaw detection</li><li><strong>D.</strong> Hardness</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> GWUT sends low-frequency (20 to 100 kHz) torsional/longitudinal waves along the pipe wall. It detects cross-sectional area changes (typically &gt;5%) up to 30 to 50 m on insulated, buried, or elevated pipe. It is a screening tool, not a sizing tool.</p></div>\n<div class=\"question\"><h3>Question 23: Pulsed eddy current (PEC) inspection of insulated piping detects:</h3><ul class=\"options\"><li><strong>A.</strong> Average wall thickness loss through insulation without removal</li><li><strong>B.</strong> Surface cracks</li><li><strong>C.</strong> Painted welds</li><li><strong>D.</strong> Internal liquid</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> PEC pulses a magnetic field through insulation/weather jacket and measures the decay to estimate average wall thickness. It is a screening tool for CUI &#x2014; not absolute thickness. Spot UT after PEC indications is standard practice.</p></div>\n<div class=\"question\"><h3>Question 24: A piping circuit per API 570 is:</h3><ul class=\"options\"><li><strong>A.</strong> A grouping of piping with similar service, material, and damage potential for inspection planning</li><li><strong>B.</strong> Only one pipe</li><li><strong>C.</strong> Tank only</li><li><strong>D.</strong> Vessels</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Piping is grouped into inspection circuits by service, material, expected damage mechanism, and operating conditions. Each circuit has a defined set of TMLs and inspection records. API RP 574 provides circuit definition guidance.</p></div>\n<div class=\"question\"><h3>Question 25: Per ASME B31.3, branch reinforcement is required when:</h3><ul class=\"options\"><li><strong>A.</strong> The header is weakened by the branch opening beyond the limits in para 304.3</li><li><strong>B.</strong> Always</li><li><strong>C.</strong> Only for vacuum</li><li><strong>D.</strong> Never</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASME B31.3 paragraph 304.3 requires branch reinforcement calculation. If header thickness in excess of pressure-design accounts for the removed material, no extra reinforcement is needed; otherwise, pads, weldolets, or wall thickness must compensate.</p></div>\n<div class=\"question\"><h3>Question 26: A flange leak path most commonly occurs at:</h3><ul class=\"options\"><li><strong>A.</strong> The gasket seating surface due to inadequate bolt torque, gasket damage, or thermal cycling</li><li><strong>B.</strong> The pipe wall</li><li><strong>C.</strong> The nut threads</li><li><strong>D.</strong> Never</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Most flange leaks are gasket seating issues. Proper bolt torque (per ASME PCC-1), gasket selection (compatible with service), and avoiding flange face damage are key. Hot-bolting (re-tightening at operating temperature) is sometimes needed.</p></div>\n<div class=\"question\"><h3>Question 27: A pipe wall thickness reading of 9.5 mm on a 10.0 mm nominal pipe with 12.5% mill tolerance is:</h3><ul class=\"options\"><li><strong>A.</strong> Acceptable within mill tolerance (minimum 8.75 mm)</li><li><strong>B.</strong> Unacceptable</li><li><strong>C.</strong> Indicates massive corrosion</li><li><strong>D.</strong> Always rejected</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Mill tolerance on seamless pipe is 12.5% under nominal. A 10 mm nominal pipe could be as thin as 8.75 mm new. 9.5 mm is normal new-pipe variation; corrosion is not implied unless previous baseline was higher.</p></div>\n<div class=\"question\"><h3>Question 28: Per API 570 owner/user responsibilities include:</h3><ul class=\"options\"><li><strong>A.</strong> Establishing the inspection program, classifying piping, supervising the inspector</li><li><strong>B.</strong> Performing the inspection personally</li><li><strong>C.</strong> Designing the piping</li><li><strong>D.</strong> Only welding</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 570 places the program responsibility with the owner/user, who classifies piping, sets inspection intervals, employs authorized inspectors and engineers, and maintains records. The inspector verifies code compliance.</p></div>\n<div class=\"question\"><h3>Question 29: A piping system below MDMT during a startup may be at risk of:</h3><ul class=\"options\"><li><strong>A.</strong> Brittle fracture</li><li><strong>B.</strong> Creep</li><li><strong>C.</strong> Sulfidation</li><li><strong>D.</strong> Erosion</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Carbon steel below MDMT (often around &#x2212;29&#xB0;C for non-impact-tested A106) loses toughness and may fail brittlely when pressurized. Cold blowdowns and autorefrigeration upsets must be analyzed and limited.</p></div>\n<div class=\"question\"><h3>Question 30: NDT methods commonly used by an API 570 inspector include:</h3><ul class=\"options\"><li><strong>A.</strong> VT, UT thickness, UT shear wave, RT (profile), PT, MT, PAUT, GWUT, PEC, MFL</li><li><strong>B.</strong> Only VT</li><li><strong>C.</strong> Only RT</li><li><strong>D.</strong> Hardness</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> An API 570 inspector commands a broad NDT toolbox: visual, thickness UT, shear wave UT (for cracks), profile RT, PT, MT, PAUT, TOFD, GWUT, PEC, MFL, eddy current array. The inspector selects techniques based on the damage mechanism &#x2014; not the other way around.</p></div>\n<h2>Study Tips for API 570</h2>\n<ul>\n<li><strong>Master ASME B31.3:</strong> Especially para 304 (design), Chapter V (fabrication and inspection), and the allowable stress tables in Appendix A. B31.3 is heavily referenced on open-book questions.</li>\n<li><strong>Know the damage mechanisms:</strong> API 571 is essential. Memorize CUI, MIC, NAC, sulfidation, HTHA, chloride SCC, caustic embrittlement, and their typical NDT.</li>\n<li><strong>Practice TML and remaining life calculations:</strong> Long-term and short-term corrosion rates, remaining life with and without FCA, MAWP for a piping circuit.</li>\n<li><strong>Index your references (provided on screen in the open-book part):</strong> API 570 sections 5 to 9, ASME B31.3 para 304/Chapter V/Appendix A, ASME IX QW-200 essential variables, API RP 574 inspection methods.</li>\n<li><strong>Practice 300+ MCQs:</strong> Work through several hundred practice questions across all the referenced documents before exam day.</li>\n</ul>\n<h2>Recommended Study Materials</h2>\n<ul>\n<li>API 570 Piping Inspection Code (current edition)</li>\n<li>API RP 574 Inspection Practices for Piping System Components</li>\n<li>API RP 577 Welding Inspection and Metallurgy</li>\n<li>API RP 578 Material Verification Program</li>\n<li>API RP 576 Inspection of Pressure-Relieving Devices</li>\n<li>ASME B16.5 Pipe Flanges and Flanged Fittings</li>\n<li>ASME PCC-2 Repair of Pressure Equipment and Piping</li>\n<li>API 571 Damage Mechanisms</li>\n<li>ASME B31.3 Process Piping</li>\n<li>ASME BPVC Sections V and IX</li>\n<li>Atlantis NDT <a href=\"/api-570-certification\">API 570 certification overview</a> (free guide; Atlantis does not run exam-prep courses)</li>\n</ul>\n<h2>Frequently Asked Questions</h2>\n<h3>Q: What is the difference between API 570 and API 510?</h3>\n<p>A: API 570 covers in-service piping inspection; API 510 covers in-service pressure vessels. See our <a href=\"/blog/api-510-vs-570-comparison\">API 510 vs 570 comparison</a>.</p>\n<h3>Q: Can I take API 570 before API 510?</h3>\n<p>A: Yes &#x2014; the API ICP certifications are independent. Many inspectors take API 510 first (more vessel work) but API 570 first is fine.</p>\n<h3>Q: How long does API 570 certification last?</h3>\n<p>A: 3 years. Recertification needs at least 20% of working time on inspection activities and 24 CPD hours each cycle, plus an online web quiz every 6 years.</p>\n<h3>Q: What is API 570 Class 1 piping?</h3>\n<p>A: The highest consequence category &#x2014; toxic, flammable that vaporizes on release, HF acid, H2S above 3%. Class 1 has the shortest inspection intervals.</p>\n<h3>Q: Is hot tapping covered in API 570?</h3>\n<p>A: API 570 references API RP 2201 for hot tapping procedures. Pre-tap NDT, qualified hot tap WPS, and burn-through prevention are required.</p>\n<h3>Q: Does Atlantis NDT offer corporate group API 570 training?</h3>\n<p>A: No. Atlantis NDT does not run API 570 exam-preparation courses. Our <a href=\"/consulting/api-570-piping-inspector-services\">API 570 piping inspection support</a> is ASNT Level III technical work on piping programmes, not exam coaching.</p>\n<h3>Q: Is API 570 recognized in the Middle East and India?</h3>\n<p>A: Yes &#x2014; widely recognized by Aramco, ADNOC, KOC, QatarEnergy, Reliance, Indian Oil, BPCL, and most major refineries.</p>\n<h3>Q: What is the API 570 exam pass rate?</h3>\n<p>A: API publishes exam statistics in its ICP status updates. The April 2024 update reported per-window pass rates for API 510, 570 and 653 ranging from roughly 45% to 72% between 2018 and early 2024, with a scaled pass point of 400. Check the latest API ICP statistics report rather than relying on third-party estimates.</p>\n<h3>Q: How much does an API 570 inspector earn?</h3>\n<p>A: Pay varies widely by region, employer, rotation and overtime. For US figures use attributed sources such as the Bureau of Labor Statistics or the ASNT salary survey; see our <a href=\"/ndt-inspector-salary\">NDT inspector salary guide</a>.</p>\n<h3>Q: How does API 570 relate to <a href=\"/blog/cswip-31-exam-prep\">CSWIP 3.1</a>?</h3>\n<p>A: CSWIP 3.1 is a welding inspection certification commonly used in welding fabrication QC. API 570 is in-service piping inspection. Many inspectors hold both for complete fabrication-to-service coverage.</p>\n\n<h2>About Atlantis NDT</h2>\n<p>Atlantis NDT is an NDT technology and services company based in Houston, Texas, led by founder Anoop Rayavarapu (ASNT NDT Level III). We provide <a href=\"/training\">NDT training under ASNT SNT-TC-1A</a> (Level I, II and III), <a href=\"/consulting\">ASNT Level III consulting</a> on NDT procedures and written practices, and inspection software: the <a href=\"/erp\">Atlantis ERP</a> and the Digital Twin platform.</p>\n<p>Atlantis NDT does not run API 510, 570 or 653, CWI, CSWIP or PCN exam-preparation courses; the guides on this site are free, independent study resources. Our ASNT-based training is delivered self-paced online or onsite at your facility.</p>\n<p><strong>Call us at +1 (281) 840-8969</strong> or email <a href=\"mailto:sales@atlantisndt.com\">sales@atlantisndt.com</a> for a quote on corporate group NDT training, delivered self-paced online or on-site at your facility.</p>\n","author":"Atlantis NDT","order":29,"createdAt":"2026-05-16","updatedAt":"2026-10-18","metaDescription":"API 570 practice questions 2026: 30 MCQs, ASME B31.3 & API 570/571/577 references, TML, CUI, NAC, hot tap. Free Atlantis NDT piping inspector guide."}