Creep is the mechanism where the inspection that matters happens long before there is anything to see. By the time a crack appears, most of the component's life has already been spent and none of it comes back.
Above roughly a third to a half of its absolute melting temperature, steel under load does not simply deform elastically and stop. It keeps deforming, slowly, for as long as the load and the temperature persist. That is creep.
Three things make it difficult to inspect for:
| Stage | What is happening | What can detect it |
|---|---|---|
| A — undamaged | Normal microstructure | Nothing to detect |
| B — isolated cavities | Voids forming on grain boundaries | Replication only |
| C — oriented cavities | Voids aligning perpendicular to stress | Replication |
| D — microcracks | Cavities linking along boundaries | Replication; advanced UT sometimes |
| E — macrocracks | Cracking visible at scale | PAUT, TOFD, MT — and it is very late |
Read the right-hand column. For the first four stages the only thing that reliably works is metallography. Conventional NDT arrives at stage E, and at stage E the decision is usually replacement rather than assessment.
The surface is ground, polished and etched in place, and the microstructure is lifted onto a plastic film for examination under a microscope. It can classify creep damage through the stages above.
The limits are real and worth stating: it examines the microstructure at the exact spot polished, on the surface only. Creep damage is often worst mid-wall or on the hotter surface, which on a heater tube is the inside. A clean replica from the outside is weak evidence about the wall behind it.
It is also slow, needs a metallurgist, and needs the right spot chosen. Which makes it a confirmatory method rather than a survey — you replicate where the other evidence says to look.
Creep strains the metal, and on a pressurised component that shows as diametral growth. Retirement criteria for heater tubes are commonly written around a percentage of original outside or inside diameter.
Measured by laser profilometry from inside the tube, or by strapping and callipers from outside. It is a bulk measurement, it covers the whole length, and it needs no metallurgist — which is why it is the practical survey method even though it responds later than replication.
Watch for it in vessels too. Bulging of a reactor shell, or distortion of a hanger or a support in a hot service, is creep deformation and it is assessed under API 579 Part 8 as well as Part 10.
This is the one worth investing in, because creep rate is exponentially sensitive to temperature. A tube 15 °C hotter than its neighbours is not 5% worse off; depending on the material and stress it can have half the life.
So the highest-value creep inspection is often not an inspection at all:
A tube found running hot and corrected has life restored in a way no inspection can achieve after the fact.
Hardness. Long exposure at temperature spheroidises carbides and softens the steel. A hardness survey showing softening is corroboration that a component has run hotter or longer than intended.
Oxide scale thickness. On boiler tubes, the internal oxide grows at a rate governed by temperature, so measuring it ultrasonically gives an estimate of the metal temperature history — a temperature record from a tube that never had a thermocouple.
Creep is assessed under API 579 Part 10, and the method is different from every other part of the standard because there is no flaw to size. Life is consumed:
Consumed life never comes back. Cooling the component stops further accumulation; it does not recover what has gone. A tube at 0.7 life fraction is at 0.7 permanently.
Your answer is only as good as your temperature history. Because the relationship is exponential, a 10 °C error in assumed metal temperature can move the calculated life by a large factor. "We think it runs at about 580" is not an input; it is a guess with a life calculation built on top of it.
Inspection tells you where you are on the curve. It does not slow the mechanism. The things that do are operational:
Move the metal temperature in the creep demonstration and watch remaining life collapse — the relationship is exponential, and seeing it is the point.
Open the demonstrationsWho 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