Choosing the NDE Method by Damage Mechanism (API 510/570/653)

Short answer: pick the NDE method from the damage you expect, not from habit. API 510, API 570 and API 653 all tie examinations to credible damage mechanisms, using API RP 571 as the reference for how each one appears. General thinning calls for UT thickness or scanning. Localized corrosion and pitting call for area coverage: corrosion mapping, profile radiography, or MFL on tank floors. Surface cracking calls for WFMT, ACFM or ET. Embedded or sub-surface cracking calls for angle-beam UT, PAUT or TOFD.

The details are where inspection plans go wrong. A method that is excellent for one mechanism can be blind to another on the same component. Thickness readings at fixed points will not find chloride stress corrosion cracking. Wet fluorescent magnetic particle testing will not size internal HIC. Tank-floor MFL screens thickness loss but does not tell you which side the loss is on unless you check. This guide gives a mechanism-to-method matrix for vessels, piping and tanks. It explains what each method finds and misses, and how the codes expect the choice to be justified and recorded. It is a technique-selection guide. Setting inspection intervals by risk is a separate engineering exercise, covered only briefly here.

Scoping a turnaround or tank outage? Send us your damage mechanism list for an NDE scope and quote, answered within 24 hours.

What the codes require: method must match mechanism

The three in-service codes say the same thing in different words. NDE has to be chosen to find the damage that is credible for the equipment.

The common reference is API RP 571, Damage Mechanisms Affecting Fixed Equipment in the Refining Industry. The current edition was published in 2020. For each mechanism it describes the affected materials, critical factors, affected units, appearance, prevention, and inspection and monitoring. API 571 tells you what to look for. Choosing, qualifying and applying the examination technique is NDE engineering, and that is where an ASNT Level III adds value.

Mechanism-to-method matrix

The table groups common mechanisms into families. It lists the methods usually first in line and the main limitation to plan around. It is a starting point for a written plan, not a substitute for the mechanism-specific guidance in API RP 571, the owner's procedures, or a qualified Level III's review of the specific geometry and material.

Damage family (examples)What it looks likePrimary NDE methodsMain limitation to plan around
General thinning (uniform corrosion, many sulfidation cases)Broad, gradual wall lossUT thickness at CMLs; UT scanning; corrosion mapping on hot spotsSpot readings miss local minima; temperature and coatings affect readings
Localized corrosion and pitting (under-deposit, dead legs, injection points, MIC)Isolated pits or patchesAutomated UT or PAUT corrosion mapping; profile RT on small bore; visual and pit gauging where accessiblePoint UT misses pits between grid points; pit bottoms scatter sound
Erosion and erosion-corrosionGrooves, wavy or horseshoe patterns at bends, tees, downstream of valvesUT scanning or mapping of the extrados and downstream zones; profile RTDamage is directional; fixed CMLs often sit in the wrong place
Corrosion under insulation (CUI)External wall loss under insulation, often at penetrations and low pointsVisual of insulation condition; screening by pulsed eddy current, profile or real-time RT, guided wave on piping; follow-up UT after insulation removalScreening methods average over an area and need prove-up; insulation removal decides the final answer
Wet H2S cracking (HIC, SOHIC, SSC, blistering)Stepwise internal cracking, surface-breaking SSC at hard welds, blistersWFMT for surface cracks; angle-beam UT, PAUT or TOFD for embedded HIC/SOHIC; UT mapping for blisters and laminationsSurface methods miss mid-wall HIC; MT needs clean, ground surfaces
Environmental cracking (chloride SCC, caustic and amine cracking, polythionic acid SCC)Fine branched surface cracks, often at welds and heat-affected zonesPT on austenitic stainless; WFMT or ACFM on carbon steel; ET or ACFM through coatings; angle-beam UT or PAUT for depthTight cracks need careful surface prep; depth sizing needs UT
Mechanical and thermal fatigueCracks at weld toes, attachments, mixing pointsMT or PT at stress concentrations; ACFM; angle-beam UT or PAUT for depthLocation must come from stress and process review
High-temperature hydrogen attack (HTHA)Internal fissuring and decarburization in susceptible steelsCombination advanced UT techniques (for example PAUT, TOFD and backscatter-type methods) applied by specially qualified teamsEarly-stage HTHA is very hard to detect; API RP 941 addresses susceptibility and inspection
Creep (heaters, high-temperature lines)Bulging, swelling, micro-voids, cracking at weldsDimensional checks and strapping; replication by qualified metallographers; UT for weld crackingDamage is microstructural before it is visible
Tank floor soil-side corrosionUnderside pitting invisible from insideMFL floor scanning with UT prove-up; robotic UT for in-service bottomsMFL screens to a threshold; edge, sump and lap-weld zones need other coverage
Tank floor product-side pitting and shell corrosionVisible pits; thinning at the liquid line and lower coursesVisual and pit gauging; UT on shells; MFL or UT mapping on bottomsPit gauging is manual; coatings hide early loss

For more on individual mechanisms, see our field guide to API 571 damage mechanisms.

What each method finds and what it misses

Ultrasonic thickness (spot UT)

Spot UT measures remaining wall at a point and is the backbone of CML programmes. It is quick and repeatable when probe, couplant and locations are controlled. Its weakness is coverage. It finds what is under the probe and nothing between grid points. That is fine for general thinning and poor for pitting, erosion and CUI.

Corrosion mapping (automated UT and PAUT)

Mapping records thickness over an area, so it finds the minimum rather than sampling it. It suits localized corrosion, hot spots identified by spot UT, nozzle regions and baseline surveys that later surveys can be compared with. Coverage, index step and data review set its value, so specify them. See corrosion mapping.

Angle-beam UT, phased array and TOFD

These volumetric weld and plate techniques detect and size embedded flaws: HIC and SOHIC, weld cracking, lack of fusion, and fatigue cracks growing from the surface. PAUT gives imaging and coverage from fewer positions. TOFD is strong at through-wall height sizing. Both depend on procedure qualification, calibration and the operator's skill. See phased array inspection and TOFD testing.

Wet fluorescent magnetic particle (WFMT) and MT

WFMT is the standard surface crack method on carbon steel for wet H2S and other cracking surveys. It is very sensitive on clean, ground surfaces. It does not work on austenitic stainless steel, and it gives no depth information.

Penetrant testing (PT)

PT finds surface-breaking flaws on non-magnetic materials, including chloride SCC on stainless steel. It needs clean, dry, open cracks and gives no depth. Rough or contaminated surfaces reduce its sensitivity.

Eddy current and ACFM

Surface eddy current and ACFM can detect surface cracks through thin coatings, which reduces surface preparation. ACFM can also estimate crack length and depth. Tube eddy current techniques serve heat exchanger bundles. All depend on the right probe, frequency and reference standard for the material.

Radiography (profile, real-time and weld RT)

Profile radiography shows wall loss, deposits and erosion on small-bore and insulated piping without stripping insulation. Weld RT detects volumetric weld flaws. It brings radiation safety controls and licensing, and it is poor at finding tight planar cracks that are not aligned with the beam.

Guided wave, pulsed eddy current and MFL screening

These are screening tools. Guided wave covers long lengths of pipe from one location and flags areas of change for follow-up. Pulsed eddy current estimates average wall thickness through insulation. Tank-floor MFL screens plate area for metal loss above a threshold. None of them gives the final thickness. Each needs UT prove-up of the indications it raises. See MFL tank floor scanning.

NDT tank inspection: matching methods to tank damage

For aboveground storage tanks under API 653, the credible damage set is short and well known: soil-side floor corrosion, product-side floor pitting, shell thinning (often at the liquid line and lower courses), roof and structural corrosion, weld cracking in some services, and settlement. The usual method set follows from it:

API 653 requires the owner's authorized inspector to assure the quality and completeness of NDE results at internal inspections, and to evaluate them. When you buy "NDT tank inspection", you are buying the examination data that inspector needs. See aboveground storage tank inspection.

Worked example, described qualitatively

Consider a carbon steel overhead drum and its outlet piping in a sour water service, plus a nearby crude tank. The plant's corrosion specialist lists the credible mechanisms. On the drum and piping: wet H2S cracking, ammonium bisulfide corrosion with erosion-corrosion at high-velocity locations, and CUI on insulated sections. On the tank: soil-side floor corrosion and product-side pitting at the water draw-off.

Each line of the plan names the mechanism, the method, the extent, the procedure and the qualified examiner. The inspector of record then has a plan that answers the code question: can these techniques adequately identify this damage and its severity?

Inspection effectiveness and RBI: context only

Readers who use risk-based inspection will know the idea of inspection effectiveness. In the API RP 580 and 581 framework, an inspection is graded by how likely it is to detect and quantify a given damage mechanism, given the method and extent. The RBI assessment then uses that grade. It is a useful discipline even outside RBI, because it forces the question this page is about: will this method, at this coverage, find this damage?

Setting intervals with RBI is an engineering assessment the owner commissions under API RP 580/581 and the in-service code's RBI provisions. Atlantis does not perform RBI assessments. What we do is supply the technique detail the owner's RBI or inspection team needs: what each method detects, its coverage and its limitations. For background, see time-based vs risk-based intervals.

Personnel, procedures and documentation the inspector expects

Common mistakes in method selection

Regulatory overlay: PSM, SPCC and Canada

Under OSHA PSM (29 CFR 1910.119(j)), inspection and testing of covered equipment must follow recognized and generally accepted good engineering practices, at frequencies consistent with them and with operating experience. Using API 510, 570 and 653 together with API RP 571 is the usual way plants show that. For tanks, EPA SPCC (40 CFR 112) requires integrity testing on a regular schedule according to industry standards. In Canada, provincial pressure equipment regulators (for example ABSA in Alberta and TSSA in Ontario) oversee owner inspection programmes, and many accept or reference the API codes. Confirm what your jurisdiction expects before finalizing the plan.

How Atlantis supports this

Atlantis NDT performs the examinations your inspection plan calls for: UT thickness and corrosion mapping, PAUT and TOFD, WFMT, MT, PT, eddy current, guided wave screening and MFL tank floor scanning. The work is done by ASNT-certified technicians under ASNT Level III oversight, and radiography is done by crews licensed where the work is. Our Level III reviews the damage mechanisms the owner's corrosion specialist has identified and recommends matching techniques, procedures and coverage. We then perform the NDE and report results with coverage maps for the owner's API inspector, who remains inspector of record and owns the plan. Atlantis does not perform RBI or fitness-for-service assessments. See inspection services and Level III consulting. Over 1,500 inspection activities completed.

Request an NDE scope review and quote.

Frequently asked questions

What is NDT tank inspection?

The nondestructive examinations used to assess an aboveground storage tank: MFL and UT on floors, UT thickness on shells, visual examination, and MT, PT and vacuum box testing on welds and repairs. Under API 653, the results feed the authorized inspector's evaluation and interval calculation.

What does "API NDT" mean?

Usually NDT performed to support API in-service inspection codes (API 510, 570, 653). The examinations are done by qualified NDE personnel, and the results are evaluated by the owner's API-certified inspector.

What should I look for in an API NDT company?

Written procedures for each technique, ASNT-certified examiners under a written practice, Level III oversight, the ability to cover the methods your damage mechanisms need, and reports that record coverage and locations. Also confirm the company does not claim to be your authorized inspector unless it actually holds that role.

Which NDT method is best for corrosion?

For general thinning, UT thickness. For localized corrosion and pitting, area methods such as UT or PAUT corrosion mapping. For screening large areas, MFL on tank floors and guided wave or pulsed eddy current on piping, followed by UT prove-up.

Which NDT method finds stress corrosion cracking?

PT on stainless steel, WFMT or ACFM on carbon steel, and eddy current through coatings for detection. Angle-beam UT or PAUT is then used to estimate depth.

Does API 571 tell you which NDE method to use?

It gives inspection and monitoring guidance for each mechanism. The final choice of technique, procedure and extent belongs in the owner's inspection plan, reviewed for the specific equipment.

Can one method cover all damage mechanisms?

No. Thickness methods do not find cracks, and surface crack methods do not measure wall loss or embedded flaws. Most equipment needs a combination.

What is inspection effectiveness?

A grading, used in API RP 580/581 risk-based inspection, of how well an inspection method and coverage detect a given damage mechanism. It is part of the owner's RBI work. Atlantis supplies the technique detail but does not perform RBI.

Who decides the NDE methods in an API inspection plan?

The inspector and/or engineer who develops the plan, with a corrosion specialist identifying mechanisms. An NDE Level III can advise on technique capability and procedures.

Do you perform NDT tank inspections outside Texas?

Yes. Atlantis performs onsite NDE at the client's facility. Contact us with the tank location and scope for a quote.

Planning NDE by damage mechanism? Get a quote from our Level III team.

Related reading: damage mechanism screening per API 571 and tank floor pitting and MRT.

Speak to an ASNT NDT Level III

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