Two different mechanisms share the name amine. One thins the wall and one cracks the welds, and confusing them sends inspectors to look for the wrong thing with the wrong method. The cracking version has a single dominant control, and it was decided when the vessel was built.
Amine units strip acid gas out of hydrocarbon streams using an aqueous alkanolamine solution which is then regenerated and recirculated. They corrode in two quite separate ways, and the first thing to get straight is which one you are dealing with.
The rest of this is about the second one.
Three ingredients, and the third is the one you control:
API RP 945 recommends post-weld heat treatment of carbon steel equipment and piping in amine service, and PWHT relieves the residual stress that the mechanism depends on. The single strongest predictor of whether a component will crack is therefore whether it was PWHT'd. Before planning any inspection of an amine unit, find out — for the vessel, and separately for every repair, every nozzle replacement and every tie-in welded in since. A PWHT'd vessel with a non-PWHT'd repair pad is a PWHT'd vessel with one place where cracking will start.
Cracking is typically intergranular, initiating on the surface wetted by the amine — the inside — and running parallel to the weld in the heat-affected zone, or in the weld metal itself. It can be extensive and fine rather than a single obvious feature, and it may be under a layer of scale or deposit that hides it completely from a casual internal visual.
Because it starts on the process side and grows outward, it spends most of its life invisible from where inspectors usually stand.
Both crack carbon steel welds in units that handle H2S, both are controlled largely by PWHT and weld hardness, and the two get conflated constantly. The distinction that matters practically:
| Amine cracking | Wet H2S cracking | |
|---|---|---|
| Environment | Aqueous alkanolamine, alkaline | Water plus H2S, acidic or near neutral |
| Worst stream | Hot lean amine | Wet sour water, cooler sections |
| Temperature trend | Worse hot | SSC worse cool; HIC across a range |
| Typical form | Intergranular SCC at welds | SSC at welds; HIC and SOHIC as stepwise internal cracking |
| Primary control | PWHT | PWHT, weld hardness limits, clean steel with low sulphur |
They also coexist. An amine unit handles H2S by definition, so a vessel can be susceptible to both, in different places, for different reasons. That is an argument for controlling residual stress and hardness properly rather than for deciding which mechanism to inspect for.
Everything follows from the fact that it is surface-breaking on the inside, at welds.
Rank by residual stress and temperature together. Non-PWHT'd welds in hot lean amine service come first, then repairs and modifications of unknown heat treatment history anywhere in the unit, then nozzle and attachment welds where restraint is highest, then PWHT'd main seams. A unit that was fully heat treated and has stayed that way through every modification is a genuinely low-risk unit for this mechanism — and knowing that with confidence is worth more than any amount of scanning.
Amine cracking, wet H2S cracking, caustic cracking and chloride SCC all attack welds and all need different conditions. The library separates them.
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