Under API 653, a composite repair on a storage tank is acceptable only when the inspection finding, the damage mechanism and the engineering support it, and when the owner, the authorized inspector and, where needed, the storage tank engineer accept it on record. It suits localized, characterized damage without cracks; it does not replace steel where the code calls for steel.
This article covers the tank side of that decision: which finding leads to which repair, who signs off, and what the file holds. How a composite repair is designed and qualified is explained in our article on ASME PCC-2 composite repairs and is not repeated here.
What API 653 governs, and where composite fits
API 653 ("Tank Inspection, Repair, Alteration, and Reconstruction") covers aboveground atmospheric steel storage tanks built to API 650 or its predecessor API 12C, from in-service inspection to repair, alteration and reconstruction. In Canada, whether it applies depends on the owner's integrity program, the jurisdiction and the contract; confirm it rather than assume it.
Its repair rules are written around steel: welded plates, bottom or nozzle replacement, weld examination and sometimes hydrostatic testing. A composite repair is therefore an engineered alternative accepted case by case, not a route the code grants by default. Two different things are often confused:
- A lining or coating (internal bottom lining, external shell coating, pit filling under a lining) protects steel and slows a mechanism. API 652 covers bottom linings and API 651 covers cathodic protection; both can be taken into account when the inspection interval is set.
- A composite reinforcement claims to restore lost strength or containment. That is a structural repair: design basis, qualified system data and explicit acceptance.
From inspection finding to repair family
Every repair file starts with the inspection report: routine in-service checks, the formal external inspection, ultrasonic thickness readings and the internal out-of-service inspection that finally shows the bottom. The finding and the mechanism behind it decide the repair family.
Bottom
The bottom is where most files begin, because it is only seen during an internal inspection. Topside pitting from water and sediment under the product is visible once the tank is cleaned. Soil-side (underside) corrosion is not: it is found by scanning methods such as magnetic flux leakage, confirmed by ultrasonic readings, and evaluated against the remaining thickness the owner and API 653 require.
Topside pitting with acceptable remaining thickness is the classic case for pit filling with a metal-filled epoxy followed by an internal lining, which stops the topside mechanism. Soil-side loss below the minimum is a steel problem: welded patch plates, partial or full bottom replacement, or a new bottom, often with a release prevention barrier. A topside lining does nothing for the underside, which depends on the foundation, drainage and cathodic protection designed by a CP specialist. The zone next to the shell, which API 653 calls the critical zone, carries its own restrictions on repairs.
Shell
Shell findings fall into three groups. General thinning is evaluated against the minimum thickness for the fill height and product; the outcomes are continued service, re-rating to a lower fill height, or insert plates. Local metal loss and pitting, often at the chime, under old insulation or along the liquid line, may be acceptable as measured and only need the mechanism stopped, which is a coating or pit-fill job. Cracks, in welds or around penetrations, are examined and repaired by welding; no coating or wrap is a crack repair.
A composite reinforcement on a thinned shell area is possible only as an engineered case, with loads, product, temperature and inspection access all addressed.
Roof
Fixed-roof plates corroded from the vapour space, pinholes and leaking seams are common; floating roofs add deck and pontoon leaks, seal damage and drain problems. The roof does not carry the hydrostatic load, so a composite or epoxy patch is more often considered there, but vapour tightness, emissions, buoyancy and product compatibility still have to be addressed and accepted.
Nozzles and shell penetrations
Thinned nozzle necks, corroded reinforcing pads and leaking flanges are frequent. The steel route is nozzle repair or replacement under API 653's rules for penetrations, with the examination and testing they bring. An external composite wrap on a thinned nozzle neck is an engineered case; a cracked nozzle weld is not a composite candidate. Corroded flange faces are a separate, often simpler repair, covered in our guide to flange face repair without machining.
Decision table: finding, repair family, composite role
| Inspection finding | Usual repair family | Composite or lining role | Who decides |
|---|---|---|---|
| Topside bottom pitting, thickness acceptable | Pit filling and internal lining | Yes, as protection | Owner, authorized inspector |
| Soil-side bottom loss below minimum | Welded patch plates, bottom replacement, new bottom | No: a topside product does not restore underside metal | Inspector, storage tank engineer |
| Through-hole in the bottom | Welded patch plate | Rarely, as a temporary measure accepted on record | Inspector, owner |
| Corrosion in the critical zone or at the shell-to-bottom weld | Welded repair within API 653 restrictions | No | Inspector, storage tank engineer |
| General shell thinning near or below minimum | Re-rating or insert plates | Only as an engineered reinforcement, case by case | Storage tank engineer, inspector, owner |
| Local shell pitting or chime corrosion, thickness acceptable | Pit fill, coating, chime sealing | Yes, as protection | Inspector |
| Crack in a shell weld or at a penetration | Examination, then weld repair | No | Inspector |
| Pinholes or corroded plates, fixed or floating roof | Plate replacement or patch | Candidate, case by case | Owner, inspector |
| Thinned nozzle neck or reinforcing pad, no crack | Nozzle repair or replacement | Engineered external wrap, case by case | Storage tank engineer, inspector |
When a composite repair is acceptable, and when it is not
A composite repair is a reasonable candidate when:
- the damage is localized metal loss, measured and mapped, with no crack;
- the mechanism is identified and either arrested or allowed for in the design life;
- the surface can be prepared to the system's requirements, which on a tank means product residue, salts and moisture under control;
- the service temperature and the stored product are within the system's qualified data;
- the repair can be inspected afterwards, and its design life covers at least the interval to the next inspection;
- the owner accepts it and records it in the tank file.
It is not acceptable, or needs a far stronger case, for a crack, soil-side bottom loss, the critical zone, an active leak without a system qualified for through-wall defects, or thickness below the minimum with no engineering assessment supporting the reinforcement. Where an evaluation goes beyond API 653's own rules, owners commonly turn to a fitness-for-service assessment to API 579-1/ASME FFS-1.
Who decides
- The owner/operator owns the tank, the integrity program and the final acceptance.
- The authorized inspector (API 653 certified, working for the owner or an authorized inspection agency) evaluates the condition, judges whether the repair and its examination meet the code, and sets the next inspection.
- The storage tank engineer, as API 653 defines the role, handles evaluations and repair designs beyond the routine rules.
- The jurisdiction can add requirements (environmental, fire).
- The applicator prepares, applies and documents. It never self-approves the repair.
The file to produce
An inspector will look for a file that stands on its own:
- Inspection report, thickness data and the damage map.
- Damage mechanism and how it is stopped or allowed for.
- Evaluation of the component under API 653 and, where used, API 579-1.
- Repair design and its basis: lining specification, or composite design to the cited standard with qualified system data.
- Qualification of the system and of the applicators.
- Repair procedure with hold points agreed with the inspector.
- Quality records: surface cleanliness and profile, soluble salts, ambient conditions and dew point, film thickness, holiday test, cure.
- Post-repair inspection results and the method for checking the repair next time.
- Acceptance by the owner and the inspector, and the effect on the next inspection interval.
An undocumented repair found at the next inspection is treated as a defect.
Planning the repair inside the shutdown window
The hard part is time: the tank is emptied, cleaned, gas-freed and inspected, and only then is the real scope known, with the restart date already fixed. Three habits help:
- Agree the decision rules before the shutdown. With the inspector and the storage tank engineer, set in advance which findings get a lining, which get pit filling, which go to steel and which trigger an engineering review. Findings then lead to action instead of a meeting.
- Prepare the engineering and materials ahead. A case built after the tank is open eats the window; system data, procedures and crews are lined up before draining.
- Schedule preparation and cure, not just application. Blasting, salt control, dew point and full cure drive the duration; our guide to fitting a tank lining inside the shutdown window breaks down that sequence, and winter work is covered in our cold-weather application guide.
Steel repairs may bring examination and a hydrostatic test that also take window time. Composite does not exempt the tank from any test the inspector requires.
Frequent mistakes
- Treating a lining as a structural repair, or a structural repair as a lining.
- Repairing topside pits while soil-side corrosion keeps going underneath.
- Presenting "designed to ASME PCC-2" as if it were API 653 acceptance.
- Deciding repairs mid-shutdown without the inspector's agreement on hold points.
- Applying over product residue, salts or damp steel, then blaming the product. Our guide to coating failure modes shows how those failures look.
- Leaving out the record, so the next inspector meets an unexplained patch.
FAQ
Does API 653 allow composite repairs? API 653's repair rules are written for steel repairs. A composite repair is an engineered alternative that the owner may accept with the authorized inspector and, where needed, the storage tank engineer. Acceptance is case by case and must be recorded.
Is an internal bottom lining a repair under API 653? It is protection, not restoration of lost metal. A lining applied to API 652 practice stops topside corrosion and can be considered when the inspection interval is set, but plates thinned below the minimum still need a steel repair.
Can a composite repair be used on the tank shell? On local metal loss without cracks, as an engineered reinforcement accepted by the owner and the inspector. General thinning is usually handled by re-rating or insert plates, and cracks always by examination and weld repair.
Who signs off a composite repair on a tank? The owner accepts it, the authorized inspector judges it against the code and sets the next inspection, and the storage tank engineer supports evaluations beyond the routine rules. The applicator documents its work but does not approve it.
When should a tank composite repair be planned? Before the shutdown. The engineering file, decision rules, materials and crew are prepared ahead, and the application happens inside the window, once the internal inspection confirms the finding.
In practice
Induscoat works on storage tank restoration in Quebec and Ontario through its maintenance and rehabilitation service: pit filling with metal-filled epoxy, internal tank linings, localized reinforcement where the engineering supports it, and quality records built for the inspector. We work from the inspection report, with the owner's inspector, and say so when a finding calls for steel. Our article on selecting an internal tank lining covers the lining side. Send the inspection report and thickness data to request a quote. Technical data sheets for the Induscoat range are published on the brand site, induscoat.com.
Hicham M, P Eng, PMP
Engineer and project manager (PMP) at Induscoat. Over 16 years of experience in industrial coatings, composite repairs and wear protection on mining, energy and petrochemical sites in Canada and internationally.
