{"id":209,"title":"API 653 Practice Questions 2026: 30 Tank Inspector MCQs with Answers","slug":"api-653-practice-questions","date":"May 16, 2026","snippet":"API 653 practice questions 2026: 30 MCQs, API 653/650/575 references, settlement analysis, MFL floor scan, hydrotest. Atlantis NDT tank inspector guide.","content":"<!-- atlantis-inline-anchors-v1 -->\n<p>This 2026 question bank prepares candidates for the <strong><a href=\"/api-653-certification\">API 653</a> Aboveground Storage Tank (AST) Inspector</strong> certification. Questions reference <strong>API 653 Tank Inspection, Repair, Alteration, and Reconstruction</strong>, <strong>API 650 Welded Tanks for Oil Storage</strong>, <strong>API RP 575 Inspection Practices for AST</strong>, <strong>API RP 577 Welding</strong>, <strong>API 571 Damage Mechanisms</strong>, <strong>API RP 651 Cathodic Protection</strong>, <strong>API RP 652 Linings for Tank Bottoms</strong>, and <strong>ASME BPVC V and IX</strong>.</p>\n<h2>API 653 Exam Format Overview</h2>\n<p>From the API 653 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 653, API Std 650, API RP 571, RP 575, RP 576 (selected sections), RP 577, RP 651, RP 652, ASME Section V and Section IX (editions per the current Publications Effectivity Sheet).</li>\n</ul>\n<h2>API 653 Practice Questions</h2>\n<div class=\"question\"><h3>Question 1: Per API 653, the maximum interval between external inspections of an AST 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 required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 (6.3.2.1) requires a visual external inspection by an authorized inspector at least every 5 years or RCA/4N years, whichever is less (RCA = remaining corrosion allowance of the shell, N = shell corrosion rate). Owner personnel also perform routine in-service inspections at intervals not exceeding one month.</p></div>\n<div class=\"question\"><h3>Question 2: The maximum interval for internal inspection of an AST (out-of-service) is:</h3><ul class=\"options\"><li><strong>A.</strong> 10 years if no corrosion rate is known; otherwise based on bottom remaining life</li><li><strong>B.</strong> 5 years always</li><li><strong>C.</strong> 30 years</li><li><strong>D.</strong> Never required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 (6.4) sets the first internal inspection at no more than 10 years after service begins, unless the safeguards in Table 6.1 (linings, cathodic protection, release prevention barrier, etc.) add credits, capped at 20 years without an RPB or 30 years with one. Subsequent intervals are calculated from bottom corrosion rates against the Table 4.4 minimum thickness, or set by an RBI assessment meeting the code&apos;s requirements; check the current edition (5th ed. with Addendum 4, 2025) for the limits that apply.</p></div>\n<div class=\"question\"><h3>Question 3: A typical tank bottom is most susceptible to corrosion:</h3><ul class=\"options\"><li><strong>A.</strong> Underside from the soil due to moisture and pH</li><li><strong>B.</strong> Top only</li><li><strong>C.</strong> Never</li><li><strong>D.</strong> Only at welds</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> The product side and the underside both corrode, but underside (soil-side) corrosion is often the limiting factor for tank life. API RP 651 (cathodic protection) and API RP 652 (internal linings) are commonly applied to extend bottom life.</p></div>\n<div class=\"question\"><h3>Question 4: Per API 653, the minimum thickness for the bottom plate is calculated based on:</h3><ul class=\"options\"><li><strong>A.</strong> Remaining life, corrosion rate, and protection method</li><li><strong>B.</strong> Tank height only</li><li><strong>C.</strong> Diameter only</li><li><strong>D.</strong> Owner preference</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 Section 4.4 sets minimum bottom plate thickness based on calculated corrosion rate, projected service interval, and whether the underside has release prevention barrier (RPB), cathodic protection, or lining. Table 4.4 minimums at the next inspection are 2.5 mm (0.10 in.) with no means to detect and contain a bottom leak, and 1.27 mm (0.05 in.) with such a means or with a reinforced lining over 0.05 in. per API RP 652.</p></div>\n<div class=\"question\"><h3>Question 5: Tank settlement evaluation per API 653 Annex B compares:</h3><ul class=\"options\"><li><strong>A.</strong> Measured settlement to allowable uniform, planar tilt, and out-of-plane settlement</li><li><strong>B.</strong> Tank diameter to height</li><li><strong>C.</strong> Wind load to tank weight</li><li><strong>D.</strong> Not evaluated</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 Annex B provides methods to evaluate settlement: uniform (no shell distress), planar tilt (allowable based on H/D), edge settlement (between shell and bottom), out-of-plane (Fourier analysis to evaluate bending stresses).</p></div>\n<div class=\"question\"><h3>Question 6: Per API 653 Section 4.3, the minimum thickness of the shell course is calculated by:</h3><ul class=\"options\"><li><strong>A.</strong> 1-foot method or variable design point method using current measured thickness less FCA</li><li><strong>B.</strong> ASME VIII formula</li><li><strong>C.</strong> Material specification only</li><li><strong>D.</strong> Owner choice</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 uses the same 1-foot method (Eq. 4-1) and variable-design-point method (Section 4.3.3.2) as API 650 for required shell thickness, applied with measured thickness less FCA to determine fitness for continued service.</p></div>\n<div class=\"question\"><h3>Question 7: A floating roof has potential damage from:</h3><ul class=\"options\"><li><strong>A.</strong> Seal wear, pontoon leaks, corrosion under sediment, drain hose failure, ice loading</li><li><strong>B.</strong> Only the seal</li><li><strong>C.</strong> No damage possible</li><li><strong>D.</strong> Only welds</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Floating roof external inspection per API 653 includes seals (primary, secondary), pontoon compartments (must be inspected internally), deck plates, drain hoses, anti-rotation devices, and emergency overflow drains. Pontoon flooding causes catastrophic sinking events.</p></div>\n<div class=\"question\"><h3>Question 8: Per API 653 Section 9, a major alteration to a tank requires:</h3><ul class=\"options\"><li><strong>A.</strong> Engineering review, qualified WPS, NDT, and possibly hydrostatic test</li><li><strong>B.</strong> Only welder qualification</li><li><strong>C.</strong> No documentation</li><li><strong>D.</strong> Owner decision only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> A major alteration (e.g., shell height change, new nozzles in stressed areas, foundation rework) requires engineering review per API 653 Section 9, qualified procedures and welders per ASME IX, NDT per API 650 acceptance criteria, and hydrotest per Section 12.</p></div>\n<div class=\"question\"><h3>Question 9: A magnetic flux leakage (MFL) floor scanner is used to:</h3><ul class=\"options\"><li><strong>A.</strong> Detect bottom plate corrosion and pitting on internal inspection</li><li><strong>B.</strong> Measure shell thickness</li><li><strong>C.</strong> Detect cracks</li><li><strong>D.</strong> Verify alloy</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> MFL scanners cover large areas of tank floor rapidly during internal inspection, detecting product-side and underside metal loss. Suspect areas are then confirmed with UT prove-up. API 653 (4.4.4) notes that MFL is commonly used with UT confirmation, and Annex G can be used to qualify the examiners and procedures; reporting thresholds are set in the qualified procedure, not by a fixed percentage in the code.</p></div>\n<div class=\"question\"><h3>Question 10: Per API 653, hydrostatic test pressure for a tank after reconstruction is:</h3><ul class=\"options\"><li><strong>A.</strong> Full liquid head to maximum design liquid level</li><li><strong>B.</strong> 1.5 &#xD7; design</li><li><strong>C.</strong> No test</li><li><strong>D.</strong> Pneumatic only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> ASTs are tested by filling with water to the maximum operating liquid level (or the design liquid level for new tanks). API 650 paragraph 7.3.6 provides hydrotest procedures. There is no pressure multiplier; full-head water test demonstrates the static-only loading.</p></div>\n<div class=\"question\"><h3>Question 11: An authorized API 653 inspector must:</h3><ul class=\"options\"><li><strong>A.</strong> Hold current API 653 certification with required experience</li><li><strong>B.</strong> Be the owner</li><li><strong>C.</strong> Hold a PE license</li><li><strong>D.</strong> Be a welder</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Authorized inspectors are certified under the API ICP program, which requires education plus tank-related experience (e.g., BS + 1 year, 2-year degree + 2 years, high school + 3 years, no formal education + 5 years, each including 1 year in supervision or performance of inspection).</p></div>\n<div class=\"question\"><h3>Question 12: An overlay weld repair on a tank bottom is permitted when:</h3><ul class=\"options\"><li><strong>A.</strong> Per API 653 Section 9 with qualified WPS, NDT, and within thickness/area limits</li><li><strong>B.</strong> Never</li><li><strong>C.</strong> Always</li><li><strong>D.</strong> Only by replacement</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Bottom plate repairs include patch plates (lap-welded or butt-welded), overlay (build-up), or full plate replacement. API 653 Section 9 specifies size limits, weld details, and NDT (typically vacuum box testing on bottom welds).</p></div>\n<div class=\"question\"><h3>Question 13: A vacuum box test on a tank bottom weld is performed at:</h3><ul class=\"options\"><li><strong>A.</strong> A partial vacuum of roughly 3 to 5 psi (21 to 35 kPa) gauge, with bubble solution applied to the weld</li><li><strong>B.</strong> 1.5 bar above atmospheric</li><li><strong>C.</strong> No vacuum</li><li><strong>D.</strong> 10 bar</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 650 Section 7.3.4 specifies the vacuum box method: apply soap solution, place box over weld, draw a partial vacuum (API 650 specifies about 3 to 5 psi / 21 to 35 kPa gauge; check the edition on the effectivity sheet). Bubble formation indicates a through-weld leak. Standard for tank bottom welds.</p></div>\n<div class=\"question\"><h3>Question 14: Per API 653, a temporary repair is:</h3><ul class=\"options\"><li><strong>A.</strong> Limited in scope and time, to be replaced with a permanent repair within a defined period</li><li><strong>B.</strong> Permanent</li><li><strong>C.</strong> Not allowed</li><li><strong>D.</strong> Always required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Temporary repairs (e.g., clamps, doublers) are allowed under API 653 with engineering review and a documented timeline for permanent repair, typically by the next turnaround.</p></div>\n<div class=\"question\"><h3>Question 15: Per API RP 651, cathodic protection of tank bottoms uses:</h3><ul class=\"options\"><li><strong>A.</strong> Galvanic (sacrificial) anodes or impressed current</li><li><strong>B.</strong> Paint only</li><li><strong>C.</strong> Concrete</li><li><strong>D.</strong> No protection</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Underside CP uses either sacrificial anodes (typically Mg or Zn) for small tanks or impressed current systems for larger tanks. Effectiveness measured at &#x2212;850 mV (Cu/CuSO4 reference) per NACE SP0169 and API RP 651.</p></div>\n<div class=\"question\"><h3>Question 16: Per API 653, the maximum interval for ultrasonic thickness measurement of the shell is:</h3><ul class=\"options\"><li><strong>A.</strong> Calculated from corrosion rate; not to exceed 15 years for tanks without RBI</li><li><strong>B.</strong> Annually</li><li><strong>C.</strong> Once at construction</li><li><strong>D.</strong> 30 years</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 (6.3.3) sets the shell UT interval at a maximum of 5 years when the corrosion rate is not known; when it is known, the maximum is the lesser of RCA/2N years or 15 years. External UT can be done while the tank is in service.</p></div>\n<div class=\"question\"><h3>Question 17: An edge settlement (between bottom and shell) is critical because:</h3><ul class=\"options\"><li><strong>A.</strong> Bending stresses can cause shell-to-bottom weld cracks</li><li><strong>B.</strong> Only cosmetic</li><li><strong>C.</strong> Improves drainage</li><li><strong>D.</strong> No concern</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Edge settlement (sometimes called dish-out) creates bending of the bottom plates near the shell, generating high secondary stresses at the chime weld. API 653 Annex B provides evaluation criteria based on length and depth.</p></div>\n<div class=\"question\"><h3>Question 18: A roof rafter inspection during internal entry must check:</h3><ul class=\"options\"><li><strong>A.</strong> Section thickness loss, rafter clip attachment, top angle, deck plate corrosion</li><li><strong>B.</strong> Only the column</li><li><strong>C.</strong> Only welds</li><li><strong>D.</strong> Not required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Fixed cone/dome roof internals: rafters, columns (lateral movement and base plates), top angle, deck plates (corrosion from acidic vapor space), and overflow/vent screens. RP 575 details fixed roof inspection.</p></div>\n<div class=\"question\"><h3>Question 19: Per API 653, an API 650 nameplate must be attached to:</h3><ul class=\"options\"><li><strong>A.</strong> The tank, in a permanent and accessible location</li><li><strong>B.</strong> The piping</li><li><strong>C.</strong> The roof</li><li><strong>D.</strong> Never required</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Per API 650 Section 10, the nameplate identifies manufacturer, year built, design code edition, capacity, maximum operating liquid level, design metal temperature, specific gravity, and the API monogram. Original nameplates must be preserved on reconstruction.</p></div>\n<div class=\"question\"><h3>Question 20: A tank that has been out of service for an extended period requires:</h3><ul class=\"options\"><li><strong>A.</strong> Verification of inspection records, condition assessment, and potential re-inspection before returning to service</li><li><strong>B.</strong> No action</li><li><strong>C.</strong> Always full reconstruction</li><li><strong>D.</strong> Pneumatic test only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Idle tanks may suffer from internal humidity corrosion, settlement, foundation issues, biological growth. API 653 requires a re-commissioning condition assessment per Section 6 prior to return to service.</p></div>\n<div class=\"question\"><h3>Question 21: Per API 653, a release prevention barrier (RPB) is:</h3><ul class=\"options\"><li><strong>A.</strong> A secondary containment beneath the tank bottom to detect leaks</li><li><strong>B.</strong> A dike</li><li><strong>C.</strong> A vent</li><li><strong>D.</strong> A roof</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> RPB systems (e.g., HDPE liner, concrete pad with leak detection grooves) detect underside leaks and prevent soil/groundwater contamination. API 650 Annex I describes RPB designs; some jurisdictions and owner specifications require them, and API 653 gives internal-inspection interval credit for them.</p></div>\n<div class=\"question\"><h3>Question 22: A linear out-of-roundness on a tank shell can indicate:</h3><ul class=\"options\"><li><strong>A.</strong> Foundation settlement or wind damage</li><li><strong>B.</strong> Improved capacity</li><li><strong>C.</strong> No concern</li><li><strong>D.</strong> Painted surface</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Tank shell roundness is measured externally with optical or laser methods. Out-of-roundness beyond API 653 limits indicates uneven foundation settlement, wind buckling, vacuum collapse, or installation defects requiring engineering review.</p></div>\n<div class=\"question\"><h3>Question 23: Per API 571, atmospheric corrosion of an AST shell is accelerated by:</h3><ul class=\"options\"><li><strong>A.</strong> Industrial atmosphere, coastal salt, wet/dry cycles, broken paint</li><li><strong>B.</strong> Dry desert</li><li><strong>C.</strong> Vacuum</li><li><strong>D.</strong> Inert gas</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> External atmospheric corrosion accelerates in industrial atmospheres (SO2, NOx), coastal (chlorides), wet/dry cycles, and where paint has failed. Recoating intervals depend on environment severity. API RP 652 covers lining; API 575 covers coating inspection.</p></div>\n<div class=\"question\"><h3>Question 24: A tank nozzle stiffening per API 650 is required when:</h3><ul class=\"options\"><li><strong>A.</strong> The nozzle opening reduces shell pressure-bearing capacity below limits</li><li><strong>B.</strong> Always</li><li><strong>C.</strong> Never</li><li><strong>D.</strong> Owner choice</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Nozzle reinforcement is calculated per API 650 Section 5.7.5 using area replacement rules. Reinforcement plates compensate for removed shell material. Low-type and regular-type nozzle details have prescribed reinforcement.</p></div>\n<div class=\"question\"><h3>Question 25: Per API 653 Section 12, hydrostatic testing after major repair is required when:</h3><ul class=\"options\"><li><strong>A.</strong> The repair affects pressure-containing welds beyond limits specified in Section 12</li><li><strong>B.</strong> Always</li><li><strong>C.</strong> Never</li><li><strong>D.</strong> Owner choice</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 Section 12 specifies when hydrotest is mandatory after repair/alteration. Generally, replacement of significant shell plate areas, raising tank height, or modifying nozzles in critical zones requires hydrotest. Vacuum box testing is acceptable for bottom-only repairs.</p></div>\n<div class=\"question\"><h3>Question 26: A tank double bottom installation is:</h3><ul class=\"options\"><li><strong>A.</strong> A repair where a new bottom is placed above the existing leaking bottom with annulus monitoring</li><li><strong>B.</strong> New tank</li><li><strong>C.</strong> Not allowed</li><li><strong>D.</strong> Same as RPB</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Double bottom retrofit places a new bottom above the existing bottom with a small annular space (often filled with sand or instrumented for leak detection). This reduces downtime vs full bottom replacement. Engineering review for height/structural impact required.</p></div>\n<div class=\"question\"><h3>Question 27: Per API 653, NDT methods commonly used on tanks include:</h3><ul class=\"options\"><li><strong>A.</strong> VT, UT thickness, MFL floor scan, PT/MT on welds, vacuum box, RT on shell welds</li><li><strong>B.</strong> Only VT</li><li><strong>C.</strong> Only hardness</li><li><strong>D.</strong> Eddy current only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Tank inspection NDT: VT (mandatory), UT thickness on shell/roof, MFL on floor, PT/MT on critical welds, vacuum box on bottom and annular welds, RT on shell butt welds. PEC for through-coating screening. Settlement survey by total station/laser.</p></div>\n<div class=\"question\"><h3>Question 28: Per API 653, a tank weld defect repair requires:</h3><ul class=\"options\"><li><strong>A.</strong> Excavation to sound metal, NDT to confirm, qualified WPS, post-repair NDT per acceptance criteria</li><li><strong>B.</strong> Cover with paint</li><li><strong>C.</strong> Replacement of full plate</li><li><strong>D.</strong> No repair</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Standard weld repair sequence per ASME IX and API 650/653: excavate defect (grinding or arc gouging), NDT to confirm full removal (typically MT or PT), weld per qualified WPS, post-repair NDT (VT plus MT/PT/RT/UT as specified).</p></div>\n<div class=\"question\"><h3>Question 29: Per API 653, the minimum thickness for tank annular ring plate is:</h3><ul class=\"options\"><li><strong>A.</strong> Calculated based on shell stress, with minimum values per Section 4.5</li><li><strong>B.</strong> 1 mm always</li><li><strong>C.</strong> 50 mm</li><li><strong>D.</strong> No minimum</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> Annular plates (the ring of thicker bottom plates beneath the shell) carry high stress from shell. API 653 sets annular plate minimum thickness at the next inspection from a table based on the first shell course thickness and its hydrotest/product stress, with an absolute floor of 0.10 in. (2.5 mm); check the current edition for the table values.</p></div>\n<div class=\"question\"><h3>Question 30: A tank inspection report per API 653 must include:</h3><ul class=\"options\"><li><strong>A.</strong> Findings, calculations, NDT records, photos, repair recommendations, signed by authorized inspector</li><li><strong>B.</strong> Verbal summary only</li><li><strong>C.</strong> Photos only</li><li><strong>D.</strong> Welder names only</li></ul><p><strong>Correct Answer: A</strong></p><p><em>Explanation:</em> API 653 reporting and recordkeeping requirements (inspection reports in section 6 and records in section 13) cover: tank ID and history, measured thicknesses, settlement data, NDT records, deficiencies and recommendations, calculations, photos, and the certified inspector&#x2019;s signature.</p></div>\n<h2>Study Tips for API 653</h2>\n<ul>\n<li><strong>Master settlement analysis:</strong> API 653 Annex B is heavily tested. Practice uniform, planar tilt, edge, and out-of-plane settlement evaluation by hand.</li>\n<li><strong>Tank components vocabulary:</strong> Annular ring, sketch plate, chime, knuckle, top angle, wind girder, rafter clip. Misidentifying components is a common exam pitfall.</li>\n<li><strong>Calculations:</strong> Shell thickness by 1-foot method, bottom remaining life, MAOL (maximum allowable operating liquid level), nozzle reinforcement.</li>\n<li><strong>Damage mechanisms:</strong> Underside soil corrosion, MIC, atmospheric, settlement-induced cracking. API 571 sections relevant to tanks.</li>\n<li><strong>Index your references (provided on screen in the open-book part):</strong> API 653 Sections 4 to 13, API 650 Sections 5 (design) and 7 (fabrication), RP 575, RP 651, RP 652, RP 577.</li>\n</ul>\n<h2>Recommended Study Materials</h2>\n<ul>\n<li>API 653 Tank Inspection, Repair, Alteration, and Reconstruction</li>\n<li>API 650 Welded Tanks for Oil Storage</li>\n<li>API RP 575 Inspection Practices for AST</li>\n<li>API RP 651 Cathodic Protection of AST</li>\n<li>API RP 652 Linings for AST Bottoms</li>\n<li>API RP 577 Welding Inspection and Metallurgy</li>\n<li>API 571 Damage Mechanisms</li>\n<li>ASME BPVC V and IX</li>\n<li>Atlantis NDT <a href=\"/api-653-certification\">API 653 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 experience is required for API 653?</h3>\n<p>A: BS + 1 year, 2-year degree + 2 years, high school + 3 years, or no formal education + 5 years of tank-related experience, each including 1 year in supervision or performance of inspection. No NDT certification is required. Verify current API ICP requirements.</p>\n<h3>Q: What is the difference between API 510, 570, and 653?</h3>\n<p>A: 510 = pressure vessels, 570 = piping, 653 = aboveground storage tanks. Stacking all three is common for refinery and terminal inspectors.</p>\n<h3>Q: Is API 653 valid for all tank types?</h3>\n<p>A: API 653 applies to API 650 / API 12 series welded storage tanks. Riveted tanks and bolted tanks have specific provisions; underground tanks are not in scope (governed by other codes).</p>\n<h3>Q: How often must a tank be inspected internally?</h3>\n<p>A: First internal inspection within 10 years of service unless Table 6.1 safeguards add credit (capped at 20 years without an RPB, 30 years with one); thereafter based on bottom corrosion rates against the Table 4.4 minimum, or by an RBI assessment meeting API 653&apos;s requirements.</p>\n<h3>Q: What is a tank API monogram?</h3>\n<p>A: An API licensee monogram (API 650, 12F, 12D, etc.) certifies the tank was built to the applicable API standard by a licensed shop. Reconstruction work may also be monogrammed.</p>\n<h3>Q: Does Atlantis NDT offer API 653 review courses?</h3>\n<p>A: No. Atlantis NDT does not run API 653 exam-preparation courses. Our <a href=\"/consulting/api-653-tank-inspector-services\">API 653 tank inspection support</a> is ASNT Level III technical work on tank programmes, not exam coaching.</p>\n<h3>Q: How does floating roof inspection differ from cone roof?</h3>\n<p>A: Floating roofs add seals, pontoons, drain hoses, anti-rotation, ladder/stairway, and roof drainage. Cone/dome roofs add rafters, columns, and vent design. Both inspected under API 653 Section 6 and RP 575.</p>\n<h3>Q: What is the API 653 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: Is settlement always rejectable?</h3>\n<p>A: No &#x2014; uniform settlement is usually benign. Differential settlement (tilt, edge, out-of-plane) must be evaluated per API 653 Annex B against allowable limits. Engineering review for borderline cases.</p>\n<h3>Q: How does API 653 relate to ASME B31.3 or <a href=\"/blog/api-510-vs-570-comparison\">API 510/570</a>?</h3>\n<p>A: API 653 is for storage tanks. ASME B31.3 covers process piping. API 510 covers pressure vessels (over 15 psig). <a href=\"/api-570-certification\">API 570</a> covers in-service piping. Many terminal and refinery inspectors hold more than one of the three API inspector certifications.</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":30,"createdAt":"2026-05-16","updatedAt":"2026-10-18","metaDescription":"API 653 practice questions 2026: 30 MCQs, API 653/650/575 references, settlement analysis, MFL floor scan, hydrotest. Atlantis NDT tank inspector guide."}