These come up in every API 510 and 570 examination and in every re-rating discussion, and they are genuinely distinct. The difference is which thickness and which allowances go into the calculation.
All three are pressures. They are calculated from different thicknesses, for different purposes, and they answer different questions.
What it is: the pressure the purchaser specified when the equipment was ordered. An input, not a result.
The designer takes it, adds temperature, material and geometry, and calculates a required thickness — then adds corrosion allowance and rounds up to a plate size that can actually be bought. So the vessel as built is usually somewhat thicker than the design pressure strictly required.
It never changes. It is a specification, and it is what appears on the nameplate alongside the rated conditions.
What it is: the maximum pressure the equipment is permitted to operate at, calculated from the actual current thickness less any future corrosion allowance, in the corroded condition, at the design temperature.
This is the number that matters in service, and it is the one that falls as the equipment corrodes.
A new vessel typically has a MAWP above its design pressure, because of that rounding up to a standard plate thickness. As corrosion consumes the extra, MAWP falls. When it reaches design pressure, the margin from rounding is gone. When it would fall below, the equipment must be repaired, replaced, or re-rated to the lower pressure.
Two details that catch people out:
What it is: the maximum pressure the equipment could hold in the new and cold condition — full nominal thickness, no corrosion allowance deducted, at ambient temperature.
It is the theoretical ceiling for that geometry and material. Always the highest of the three.
What it is used for: establishing hydrotest pressure, and understanding how much margin existed at the start. It is not an operating limit and nobody operates to it.
| Design pressure | MAWP | MAP | |
|---|---|---|---|
| Thickness used | Specified, not measured | Actual, less future corrosion | Nominal, new |
| Corrosion allowance | Added on top | Deducted | Not deducted |
| Temperature | Design | Design | Ambient |
| Changes over time | No | Yes — it falls | No |
| Relative size | Lowest of the three, usually | Middle | Highest |
| Used for | Specification | The operating limit | Hydrotest, reference |
A vessel designed for 20 bar. Calculation says 9.4 mm is required; add 3 mm corrosion allowance and buy 12.7 mm plate.
At that point the options are the usual four: reduce the future corrosion allowance if the inspection interval justifies it, repair, replace, or re-rate to the pressure the remaining wall supports.
If the process never needs 20 bar — and many vessels operate far below their rating — re-rating to 16 bar may be entirely acceptable and costs nothing but the paperwork and a nameplate change. It is frequently the cheapest legitimate outcome of an assessment, and it is one of the remediation options API 579 explicitly lists.
When a flaw is found, one of the standard outputs of an API 579 assessment is a reduced MAWP — the pressure at which the damaged component still has acceptable margin.
For local metal loss the link is direct: the remaining strength factor scales the acceptable pressure. If the calculated RSF is below the acceptance value of 0.90, the component can be operated at a pressure reduced in proportion, rather than being condemned. That is the same re-rating decision, arrived at through the assessment.
Which is why MAWP, not design pressure, is the number an integrity engineer tracks. Design pressure tells you what somebody wanted in 1987. MAWP tells you what the metal in front of you can actually do.
The quick check takes thickness, diameter and material and returns the minimum required thickness and the MAWP the remaining wall supports.
Open the quick checkWho 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