Getting One Set of Thickness Numbers Out of Several LNG Sites That Each Count Differently
A CML and TML registry standardises how monitoring locations are identified, counted and measured so that thickness data from several LNG sites can be compared. The obstacle is rarely software. It is that each site defines a location differently, applies a different minimum thickness basis, and counts coverage in units that are not the same unit, so the corporate rollup is arithmetic on incompatible quantities.
LNG makes the standardisation problem worse than in refining for a structural reason. A liquefaction site and a regas terminal share a company but not a damage profile, and the cryogenic sections of both are places where wall loss is essentially not the mechanism at all. Corporate integrity leadership nonetheless wants one coverage number. Sites that run mostly warm-side equipment, amine treating, dehydration, mercury removal, hot oil and fuel gas, will carry hundreds of thickness locations. Sites dominated by cryogenic piping in austenitic stainless and 9% nickel steel will carry very few, because the credible threats there are external chloride stress corrosion cracking under cold insulation and mechanical damage, not general thinning. A rollup that divides one by the other and reports a percentage is comparing two different questions. The registry has to make the difference visible instead of averaging it away.
Source: Written against API 570 and API 574 for condition monitoring location practice, API 571 for damage mechanism definitions including amine corrosion and cracking, API 583 for corrosion under insulation and under cold insulation, API 620 Annex Q and API 625 for refrigerated liquefied gas storage, ASME B31.3 for process and cryogenic piping, ASME Section VIII Division 1 and 2 for pressure vessels, and 49 CFR Part 193 with NFPA 59A for United States onshore LNG facilities.
| Plant area | Service and principal metallurgy | Is wall loss the governing threat? | How the registry should treat it |
|---|---|---|---|
| Amine treating, contactor and regenerator circuits | Rich and lean amine, carbon steel with stainless in hot lean service | Yes, strongly | Full thickness location set at flashing points, regenerator overhead and rich amine let-down, with API 571 amine corrosion and amine cracking both recorded as mechanisms |
| Dehydration and molecular sieve regeneration | Wet feed gas then hot regen gas, carbon steel | Yes, cyclic | Locations grouped by thermal cycle exposure, because the regeneration cycle count matters more than elapsed calendar time |
| Mercury removal bed inlet and downstream aluminium | Feed gas with trace mercury, carbon steel to aluminium transition | No, embrittlement risk | Recorded as a monitored location with a non-thickness inspection method, so it appears in coverage without a meaningless thickness trend |
| Main cryogenic heat exchanger and cold box piping | Cryogenic hydrocarbon, austenitic stainless and aluminium | No | Registered as a location under external cracking and cold insulation surveillance, explicitly excluded from thickness corrosion rate rollups |
| Cold insulated lines subject to warm-up cycles | Intermittent cryogenic to ambient, stainless and carbon steel | Sometimes, at the cycling band | Insulation removal plan, API 583 cold service treatment, and chloride cracking flagged on stainless rather than a thickness rate |
| Full containment storage tank, inner and outer | 9% nickel inner, prestressed concrete outer, per API 620 Annex Q | Inner shell not inspectable in service | Held as an asset with settlement, annulus and instrumentation surveillance records, never as an overdue thickness location |
| Seawater or air cooling, fire water and utility systems | Seawater, treated water, carbon steel and coated | Yes | Standard thickness locations, but ring-fenced from process rollups so utility corrosion does not flatter or distort the process coverage number |
The rollup fails before the software is even involved
Corporate integrity leadership at a multi-site LNG operator asks a simple question roughly quarterly. What percentage of our condition monitoring locations are current, and where are we exposed. The question is answerable at each site individually. It becomes unanswerable the moment the three site answers are added together, and the reason is not that the sites use different databases.
It is that they use different definitions. Site A counts a location as an area on a fitting containing four clock-position readings. Site B counts each clock position separately. Site C, which inherited its register from a construction contractor, registered every weld in a circuit as a location and then never read three quarters of them. Adding these produces a number, and the number is meaningless.
Every subsequent fix is downstream of this. Deploying a common system across sites that keep their own definitions simply centralises the incoherence. The work is defining the object, the location, the measurement point, the circuit, the mechanism, the minimum thickness basis, and then migrating each site onto those definitions with its legacy identifiers preserved as aliases so nobody loses their history.
Cryogenic service breaks the assumption the register was built on
Thickness monitoring exists because carbon steel in a corrosive process loses wall at a rate that can be trended and extrapolated. That model holds well across a refinery. It holds badly across an LNG plant, because a large fraction of the plant runs dry, sweet hydrocarbon at temperatures where general corrosion is negligible and the metallurgy is austenitic stainless, aluminium or 9% nickel steel.
The credible threats in those sections are different in kind, not just in rate. External chloride stress corrosion cracking under cold insulation on austenitic stainless, particularly where lines cycle through the moisture condensation range during trips and warm-ups. Mechanical damage and thermal fatigue at cold-warm transitions. Liquid metal embrittlement of aluminium if mercury breaks through the removal bed. None of these announce themselves as a thinning trend, and none are caught by an ultrasonic spot reading.
A registry that only knows how to hold thickness therefore forces a bad choice on the site. Either register cryogenic equipment with thickness locations that will read nominal forever and create false assurance, or leave it out and create a blind spot. The correct design registers the location, records the applicable damage mechanism using API 571 terminology, and attaches the inspection method appropriate to that mechanism, which may be insulation removal and visual, dye penetrant on stainless welds, or a documented surveillance regime under API 583.
Where LNG wall loss really is, and why it clusters on the warm end
The thickness program in an LNG facility earns its keep on the pretreatment train and the utilities. Amine treating for acid gas removal carries the classic set of mechanisms described in API 571: amine corrosion concentrated where rich amine flashes, at the regenerator overhead, and across let-down valves, along with amine stress corrosion cracking in non-post-weld-heat-treated carbon steel. This is the area where a poorly placed grid genuinely misses metal loss.
Dehydration and molecular sieve regeneration add a thermal cycling dimension. Damage accumulates with regeneration cycles rather than with elapsed calendar time, which means a unit that has been swung hard during a demand year has aged faster than the calendar suggests. A registry that only schedules on dates cannot express that, and the site engineer compensates informally, which is precisely the sort of undocumented local practice that breaks a fleet rollup.
Utilities are the quiet one. Seawater cooling, fire water and treated water systems corrode steadily and generate a large share of the total location count. If they sit in the same pool as process locations, a site can raise its headline coverage number simply by reading easy utility points, and the fleet view rewards the wrong behaviour. Ring-fencing them is not cosmetic.
Minimum thickness is where standardisation gets political
Two sites can hold identical readings on identical spools and disagree about remaining life by a decade, because they disagree about what the reading is being compared to. One computes t-min from the pressure design formula in ASME B31.3. Another applies a structural minimum for large-bore, low-pressure piping where the pressure calculation returns an implausibly thin wall. A third carries an owner-specified retirement thickness set above both by a previous integrity manager as a conservatism.
All three are defensible positions. What is not defensible is a fleet remaining life distribution built by pooling them, because the distribution then encodes three different risk appetites and cannot be used to allocate capital. This is the point in a standardisation project where the discussion stops being about software and becomes a corporate engineering decision that someone has to own and sign.
The registry's contribution is to make the divergence impossible to hide. Every location should carry its t-min basis as a governed field, and any rollup that spans more than one basis should either segment by basis or refuse. A system that silently pools them is not neutral. It is generating a number that a senior engineer will later be asked to defend and will not be able to.
Governing the standard without erasing what each site already has
The fastest way to kill a standardisation programme is to renumber everyone's locations. Site engineers know their plant by the identifiers painted on it and printed on twenty years of reports. A migration that replaces them produces a period during which nobody trusts either the old or the new labels, and the field crews quietly keep using the old ones on their sheets.
The workable pattern is a governed corporate identity with unlimited site aliases. The corporate identifier is what the fleet reports on. The site's legacy identifier, the construction contractor's tag and the isometric callout all persist as searchable aliases resolving to the same record. A technician typing the number stencilled on the pipe finds the location. A corporate analyst querying the fleet gets one identity.
Standards also change, so the standard itself must be versioned. When the definition of a condition monitoring location is revised, historical records must remain interpretable under the definition in force when they were created, with an explicit mapping forward. Without that, the first revision destroys the ability to compare this year to last year, and the programme loses its main proof of value.
What a comparable coverage metric actually looks like
A defensible fleet metric names its unit and its scope in the metric itself. Percentage of process condition monitoring locations, counted at location level, with a due date derived from the corporate interval rules, currently within interval. That sentence is longer than the number, and it should be, because every clause in it is a place where two sites can diverge.
Second, the metric should be reported alongside its denominator, not just as a percentage. A site improving from eighty to ninety percent by retiring locations rather than reading them is a familiar pattern, and it is only visible when the count is shown. Retirements should require a reason and an approver, and should appear in the report as a separate line rather than vanishing into the base.
Third, the metric needs an explicit not-applicable category for equipment under a non-thickness surveillance regime. Cryogenic piping under cold insulation surveillance, the inner tank of a full containment storage tank under API 620 Annex Q, and mercury-exposed aluminium are all monitored and none of them belong in a thickness percentage. Reporting them as a named category is the difference between a metric an engineer trusts and one they work around.
The regulatory audience is not the same as the refinery one
United States onshore LNG facilities sit under 49 CFR Part 193, which incorporates NFPA 59A, and the operating and maintenance obligations there are framed differently from the mechanical integrity language a refinery integrity engineer is used to under OSHA 29 CFR 1910.119. Facilities that export or serve marine terminals also carry Coast Guard obligations, and internationally EN 1473 shapes the equivalent expectations.
Practically, this means the evidence an LNG operator has to produce is more about demonstrating a controlled, documented and followed procedure than about defending a specific corrosion rate calculation. That plays to the registry's strengths: an auditable record of who defined a location, on what basis, when it was read, by whom, with what equipment and calibration, and what was done about the result.
It also means the fleet standard has to accommodate sites in different jurisdictions without forking. A regas terminal in one country and a liquefaction train in another will have different statutory inspection triggers layered on top of the same engineering basis. The registry should treat the statutory trigger as an additional constraint on the due date rather than as a separate parallel schedule, so that a location has one due date and a stated reason for it.
How to evaluate a registry for a multi-site LNG estate
Give the vendor two real extracts from two of your sites with their genuine, incompatible conventions, and ask them to produce one comparable coverage number without editing the source data by hand. What you are watching for is whether the system exposes the incompatibility and asks for a governance decision, or silently produces a number. The second behaviour is disqualifying, and it is common.
Ask to see the alias resolution work in the field capture interface. Type the legacy site identifier, the construction tag and the corporate identifier, and confirm all three land on the same location record with the same history. If the field tool only recognises the new corporate number, the crews will not adopt it and the register will drift within one campaign.
Finally, ask the system to represent an asset that legitimately has no thickness programme, such as a full containment inner tank, and show how it appears in the fleet report. A system that can only classify it as overdue, or can only handle it by leaving it out, will force one of your sites to lie in order to look correct. Atlantis will run this exercise against a sample of your own multi-site data during a scoping consultation arranged through info@atlantisndt.com.
Why do two LNG sites report different coverage percentages for identical work?
Because they are counting different things. One site registers a circumferential grid at an elbow as a single condition monitoring location containing four measurement points. Another registers the same grid as four locations. Both read the same steel with the same probe on the same day. The second site reports four times the location count and, if some points are overdue, a materially different overdue percentage. Nothing about the physical program differs.
What is the correct relationship between a CML and a measurement point?
API practice treats the condition monitoring location as the area being monitored and the measurement points as the individual readings within it, typically at defined clock positions. Getting this hierarchy explicit in the data model is the single highest-value standardisation act available to a multi-site LNG operator, because every downstream metric, coverage, overdue count, cost per reading and crew loading, is computed on one of the two levels and the two are not interchangeable.
Should minimum thickness be set by each site or by the corporate standard?
The basis must be corporate, the value is necessarily local. Whether t-min derives from pressure design calculation, from structural minimum for large-bore low-pressure piping, or from an owner-specified retirement thickness above both, is a governance decision that changes remaining life across the fleet. The calculated number for a given spool depends on that spool's diameter, material and design conditions. Mixing bases inside one rollup produces a remaining life distribution that means nothing.
Is API 510, 570 or 653 inspector training part of this offer?
No. Those certifications are administered by API and their examinations sit outside anything Atlantis provides. Atlantis supplies inspection management software, reporting software, digital twin platforms, report validation and ASNT Level III consulting, and delivers NDT method training to ASNT SNT-TC-1A and ISO 9712 across UT, RT, MT, PT, ET, VT, PAUT and TOFD. Standardising a CML registry is a data governance project, not a certification pathway.
How should cryogenic equipment appear in a corporate integrity metric at all?
As monitored, with a stated method that is not thickness. A cold box line under API 583 cold service surveillance, a 9% nickel inner tank tracked through settlement and annulus monitoring, and a mercury removal outlet watched for aluminium embrittlement are all legitimately under control. If the only status a system can assign is a thickness due date, sites will either create fictional thickness locations or leave the equipment out of the register entirely, and both distort the fleet view.
What does it cost a multi-site operator to leave the numbering conventions alone?
The visible cost is the analyst time spent rebuilding a comparable fleet view each quarter. The real cost surfaces during an incident or a regulatory review, when the operator cannot demonstrate that a mechanism identified at one site was checked at the others. Fleet learning is the whole argument for multi-site ownership, and it runs entirely on the ability to ask one question across every site and get one answer.
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