Stress corrosion cracking removes almost no metal. That single fact rules out most of the inspection a plant routinely does, and it is why SCC is so often found by a leak rather than by an inspector.
Start with the physics, because it explains everything that follows. A stress corrosion crack is a planar flaw: it has length and depth but almost no width. A crack 100 mm long and 5 mm deep might be a few microns wide. The volume of metal it has removed is negligible.
Now consider what a thickness measurement does. It times an echo from the far wall and reports how much steel is between. A crack removes no measurable thickness, so the reading comes back at full wall. A vessel can be extensively cracked and every UT reading on it will be nominal.
Everything below follows from that. SCC has to be found by a method that responds to a discontinuity, not to a loss of metal.
Magnetise the steel, apply fluorescent magnetic particles, look under UV. Particles gather at the leakage field around a crack and the indication glows. On carbon and low-alloy steel this is the most sensitive practical method for surface-breaking cracking, and it is what the standards call for after any weld repair in wet H₂S service.
Two limits. It works only on ferromagnetic material — useless on austenitic stainless, nickel alloys and copper alloys. And it needs bare, clean metal, which means blasting off coating and scale. On a large vessel the surface preparation is most of the cost and most of the schedule.
Chloride SCC in austenitic stainless is one of the most common cracking mechanisms in the industry, and MT cannot touch it. Penetrant is the standard alternative: dye drawn into the crack by capillary action, then pulled back out onto a developer.
It only sees what is open at the surface and clean. Grinding a surface before inspection smears metal across the crack mouth and can close it completely — a genuinely common way cracking is missed, and the reason the sequence of surface preparation matters.
An array probe covers a swathe rather than a line and works on stainless where MT cannot. It tolerates thin coating, which saves the blasting bill on large areas. Depth sizing is limited, so it is a finding tool rather than a sizing tool.
Alternating current field measurement induces a uniform current in the surface and measures the disturbance around a crack, giving both length and depth. It works through coating, underwater and at elevated temperature. Less sensitive than a properly prepared WFMT inspection, but on a coated structure where blasting is impractical it finds cracks nothing else would.
Surface methods find cracks. They do not tell you how deep they go, and depth is what decides whether a component can stay in service. PAUT images the cross-section and gives through-wall height — which is the number API 579 Part 9 requires.
It is also the method for cracking that starts on the far side. Sulphide stress cracking initiating at the process surface of a vessel is invisible to any external surface method until it breaks through.
AE listens for the stress waves released as a crack actually extends during a controlled pressure change. It answers a question nothing else does: is this damage active?
That question matters because API 579 treats a dormant flaw and a growing flaw completely differently. A dormant crack may be acceptable as it stands; a growing one needs a crack growth analysis and a re-inspection interval. AE only hears what moves during the test, so silence is not proof of a sound vessel.
| Cracking | Material | Primary method | Why not the obvious one |
|---|---|---|---|
| Sulphide stress cracking | Carbon steel | WFMT + hardness survey | Often at the weld HAZ; hardness finds the susceptible zone before cracks appear |
| Chloride SCC | 300-series stainless | PT or eddy current | MT cannot work on austenitic material |
| Caustic embrittlement | Carbon steel | WFMT | Concentrates at non-PWHT welds — inspect those first |
| Amine and carbonate SCC | Carbon steel | WFMT | Weld-associated; PWHT status drives susceptibility |
| Polythionic acid SCC | Sensitised stainless | PT | Happens during shutdown, not operation — inspect after, not before |
| External SCC, buried line | Carbon steel | EMAT ILI | MFL is blind to cracks; the coating hides it from everything external |
| Corrosion fatigue | Any | ACFM or WFMT | Cyclic service — look at nozzles and attachments |
SCC is not random. It needs three things at once: a susceptible material, a specific environment, and tensile stress. The third one is what tells you where to point the inspection.
Residual stress from welding is usually the largest tensile stress in a fabricated component, and it is highest at welds that were not post-weld heat treated. That is why almost every environmental cracking mechanism in the table above concentrates at welds, and why the inspection plan is a list of welds rather than an area.
Identify the mechanism from the service, list the locations where stress is highest — non-PWHT welds, nozzles, attachments, repair welds — inspect those with a surface method matched to the material, then size anything you find with PAUT. Inspecting a whole vessel to find cracking that only occurs at welds spends the budget in the wrong place.
Every crack-like flaw goes to API 579 Part 9, whatever produced it — chloride, fatigue, or a welder. The assessment needs length, through-wall height, position, the material's toughness and the applied stress. Surface methods give you the first; ultrasonics gives you the second.
And Part 9 asks one further question that inspection alone cannot answer: is the mechanism still active? If it is, the flaw will grow, and accepting it as it stands is not valid. That is a process question about whether the environment that caused it is still present — and it is usually the hardest part of the assessment.
Eleven environmental cracking mechanisms in the library, each with the giveaway that identifies it, the material it attacks and the method that finds it.
Open the mechanism libraryWho writes this. A mechanical engineer with twelve years in oil and gas — in-line inspection, fired heater and furnace inspection, and pipeline integrity. What is here comes from the published standards and from what those years in the field actually looked like. It is not written by an API-certified inspector.
This is not an assessment. Nothing on this site may be used to justify a decision about real equipment. Assessing plant requires the current editions of the applicable codes, data from a licensed source, and a competent engineer who signs for the answer. · Integrity Field Guide