Loss of Containment (LOC) Event Repository Data Consistency

, 8/19/2026 Be the first to comment

Tags: API 580 Asset Performance Management Damage Mechanisms Data Analysis Data Management Data Validation HSE Inspection Mechanical Integrity Probability Reliability Risk Risk Analysis Risk Management Technology Value


A practical framework for developing a globally standardized Loss of Containment Event Repository. The document defines data validation rules, controlled equipment and damage-mechanism taxonomies, failure-cause hierarchies, confidence scoring, evidence requirements, duplicate detection, standardized units, and AI-readability rules to improve RBI, mechanical integrity, process safety, and failure prediction.
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Loss of Containment (LOC) Event Repository Data Consistency

My last blog post titled "How to improve RBI predictions using a consolidated central repository of failure events" received some great comments. The best one came from Haider Javaid, and here is his LinkedIn profile: (4) Haider Javaid | LinkedIn. Haider said, "The repository idea holds up. The part that usually breaks it is that two operators will describe the same damage mechanism three different ways in their incident reports, so the model ends up learning vocabulary instead of failure. Normalizing that against a common taxonomy is unglamorous work, but it decides whether the whole thing produces signal." Haider, thank you for inspiring me to write this blog.

Haider is absolutely correct. Entering event data into the database without validation makes normalization more difficult. Therefore, for a global loss of containment (LOC) event database/repository, the most important principle is:

If the input data is inconsistent, incomplete, or biased, the analytics built on top of it will produce misleading recommendations.

In my humble opinion, the repository should therefore operate more like an aviation accident database than a simple incident log. Every record should be traceable, standardized, and technically validated.

Below are recommended constraints and business rules.

Category

Constraint / Rule

Reason

Unique Event

One globally unique Event ID

Prevent duplicates

Source

Every event must identify its source

Traceability

Version Control

Original record never overwritten

Audit trail

Time

All dates stored in UTC plus local time zone

Consistency

Units

Automatic conversion to SI and US customary

Global compatibility

Equipment

Equipment classified using controlled taxonomy

Prevent inconsistent names

Materials

Materials selected from approved standards

Enables damage mechanism analysis

Damage Mechanisms

Only approved API RP 571 damage mechanisms

Consistent failure analysis

Cause Codes

Controlled failure taxonomy

AI training consistency

Confidence

Confidence score assigned

Separate facts from assumptions

Validation

Mandatory QA review

Data quality

Confidentiality

Remove proprietary information

Encourage participation

1) Source Validation

Event record source validation is very important. It provides the evidence for confidence scoring. Every record should include:

  • Source
  • Publication date
  • Organization
  • Investigator
  • Report number
  • URL or document reference
  • Copyright status

Here is an example:

  • Source:
    • CSB Investigation Report
    • Report No. 2019-03-I-TX
    • Published:
    • June 2021
    • Confidence Score: 5

Never allow anonymous technical conclusions.

2. Required Minimum Data

Set a minimum data requirement. Event records shall have the following fields populated:

Event

  • Date
  • Country
  • Facility
  • Unit
  • Equipment
  • Material
  • Released fluid
  • Release type
  • Event description

If any of these are missing, reject the record.

3. Standard Equipment Taxonomy

The event record input template should never allow free-text equipment names. Instead, it shall have controlled cascading lists for:

  • Equipment Class – per common API equipment categories

API equipment category

Typical equipment

Primary API standard

Pressure vessels

Reactors, drums, separators, exchangers

API 510

Piping

Process piping, utility piping, injection piping

API 570

Storage tanks

Atmospheric and low-pressure storage tanks

API 653

Relief devices

PSV, PRV, rupture disks

API 576

Pressure-relieving systems

Relief valves and associated systems

API 520 / 521 / 576

Fired heaters

Process heaters, furnaces, boilers in applicable service

API 530 / 535 / 556 / 560

Heat exchangers

Shell-and-tube exchangers, condensers, reboilers

Often API 510, with API 660/661 design standards

Rotating equipment

Pumps, compressors, turbines

API 610, 611, 612, 614, 617, etc.

Tanks

Fixed-roof, floating-roof, internal floating-roof

API 650 / 653

Pipelines

Transmission/process pipelines

API 1160, API 570 and other applicable standards

 

  • Equipment Type – per common API equipment types

Common API equipment type

Typical examples

Primary API reference

Pressure Vessel

Reactors, drums, separators, accumulators

API 510

Heat Exchanger

Shell-and-tube exchanger, condenser, reboiler

API 510 / API 660

Air Cooler

Fin-fan exchanger

API 510 / API 661

Process Piping

Process lines, headers, manifolds

API 570

Pipeline

Hydrocarbon/product pipelines

API 570 / API 1160

Storage Tank

Fixed-roof, floating-roof tanks

API 653 / API 650 / API 620

Pressure Storage Tank

LPG bullets, spheres

API 510 / API 2510

Fired Heater

Process furnace, charge heater

API 530 / API 560

Boiler

Steam boiler, waste-heat boiler

Applicable ASME/API requirements

Relief Valve

PSV, PRV, safety valve

API 576 / API 520

Rupture Disk

Pressure-relief rupture disk

API 520 / API 521

Pump

Centrifugal, reciprocating, positive displacement

API 610 / API 674 / API 676

Compressor

Centrifugal, reciprocating, screw

API 617 / API 618 / API 619

Steam Turbine

Drive turbine

API 611 / API 612

Gas Turbine

Mechanical drive/power generation

API 616

Rotating Equipment

Drivers, gearboxes, couplings, etc.

Various API standards

Column / Tower

Distillation, fractionation, absorption tower

API 510

Reactor

Hydrotreater, reformer, polymerization reactor

API 510

Drum

Reflux drum, knockout drum, surge drum

API 510

Separator

2-phase/3-phase separator

API 510

Accumulator

Hydraulic/process accumulator

API 510

Scrubber

Gas scrubber, suction scrubber

API 510

Filter

Process filter, coalescer, cartridge filter

API 510/570 as applicable

Strainer

Basket/temporary/permanent strainer

API 570 as applicable

Tank

Shell, bottom, and roof

API 650/ API 620

Expansion Joint

Metallic bellows expansion joint

API 570 / applicable standards

Hose / Flexible Connection

Process hose, loading hose

API 17B / other applicable API standards

Furnace Tube

Radiant/convection tubes

API 530 / API 560

 

  • Component Type – per common API component types

Common API component type

Typical examples

Primary API reference

Pressure Vessel

Reactors, drums, separators, accumulators, scrubbers, filters, strainers

API 510

Column - Top

Towers, Distillation Columns

API 510

Column - Middle

Towers, Distillation Columns

API 510

Column - Bottom

Towers, Distillation Columns

API 510

Heat Exchanger - Shell

Shell-and-tube exchanger, condenser, reboiler

API 510 / API 660

Heat Exchanger - Channel

Shell-and-tube exchanger, condenser, reboiler

API 510 / API 660

Heat Exchanger - Bundle

Shell-and-tube exchanger, condenser, reboiler

API 510 / API 660

Air Cooler - Header

Fin-fan exchanger

API 510 / API 661

Air Cooler - Tubes

Fin-fan exchanger

API 510 / API 661

Process Piping – Circuit

Process lines, headers, manifolds

API 570

Pipeline - Segment

Hydrocarbon/product pipelines

API 570 / API 1160

Storage Tank - Shell

Fixed-roof, floating-roof tanks

API 653 / API 650 / API 620

Storage Tank - Bottom

Fixed-roof, floating-roof tanks

API 653 / API 650 / API 620

Storage Tank - Roof

Fixed-roof, floating-roof tanks

API 653 / API 650 / API 620

Pressure Storage Tank

LPG bullets, spheres

API 510 / API 2510

Fired Heater - Radiant Tubes

Process furnace, charge heater

API 530 / API 560

Fired Heater - Convection Tubes

Process furnace, charge heater

API 530 / API 560

Fired Heater - Headers

Process furnace, charge heater

API 530 / API 560

Boiler - Tubes

Steam boiler, waste-heat boiler

Applicable ASME/API requirements

Boiler – Steam Drum

Steam boiler, waste-heat boiler

Applicable ASME/API requirements

Boiler – Mud Drum

Steam boiler, waste-heat boiler

Applicable ASME/API requirements

Boiler – Headers

Steam boiler, waste-heat boiler

Applicable ASME/API requirements

Relief Valve

PSV, PRV, safety valve

API 576 / API 520

Rupture Disk

Pressure-relief rupture disk

API 520 / API 521

Pump - Bowl

Centrifugal

API 610 / API 674 / API 676

Pump – Seal Plate

Centrifugal

API 610 / API 674 / API 676

Pump – Casing

Positive displacement

API 610 / API 674 / API 676

Pump – End Cover

Positive displacement

API 610 / API 674 / API 676

Compressor - Casing

Centrifugal

API 617 / API 618 / API 619

Compressor - Head

Centrifugal

API 617 / API 618 / API 619

Compressor - Cylinder

Positive displacement

API 617 / API 618 / API 619

Compressor – Cylinder Head

Positive displacement

API 617 / API 618 / API 619

Steam Turbine - Casing

Drive turbine

API 611 / API 612

Steam Turbine – Steam Chest

Drive turbine

API 611 / API 612

Steam Turbine – Exhaust Hood

Drive turbine

API 611 / API 612

Gas Turbine - Casing

Mechanical drive/power generation

API 616

Filter

Process filter, coalescer, cartridge filter

API 510/570 as applicable

Strainer

Basket/temporary/permanent strainer

API 570 as applicable

Expansion Joint

Metallic bellows expansion joint

API 570 / applicable standards

Hose / Flexible Connection

Process hose, loading hose

API 17B / other applicable API standards

 

4. Materials

Materials selected from approved standards only. Below are some examples:

  • ASTM
  • ASME
  • EN
  • ISO
  • DIN
  • JIS

Materials of construction must have a material specification per the appropriate code or the common manufacturer's name. See the examples below:

  • SA-106 Grade B
  • SA-516 Grade 70
  • 316L SS
  • Inconel 625
  • Duplex 2205
  • Monel 400

Never accept unspecified generic names. Here are some examples:

  • "Steel"
  • "Carbon Steel"
  • "SS"

5. Fluid Standardization

Select fluids from a controlled, validated list. Ideally, it should be a composite of the lists from:

  • OSHA
  • EPA
  • ECHA
  • HSE
  • Health Canada / Environment and Climate Change Canada
  • Safe Work Australia
  • Japanese Government / NITE
  • Chinese Government / MEE
  • Government of India / PESO

Examples include:

  • Hydrogen
  • Wet H2S
  • Amine
  • Crude Oil
  • Natural Gas
  • Ethylene
  • Steam
  • Cooling Water
  • HF Acid
  • Sulfuric Acid
  • Caustic
  • Ammonia
  • Propane
  • LPG
  • Methanol
  • Ethanol
  • Hydrogen Chloride
  • Oxygen
  • Nitrogen

6. Damage Mechanism Rules

Damage mechanisms should only come from recognized sources. See the list of examples below:

Organization / Country

Standard / Practice

Primary subject

API – USA

API RP 571

Damage mechanisms affecting fixed equipment in refining

ISO

ISO 21457

Materials selection and corrosion control for oil & gas production

NORSOK – Norway

NORSOK M-001

Materials selection, corrosion evaluation and protection

EFC – Europe

EFC Publication 55

Corrosion Under Insulation (CUI)

EFC – Europe

EFC Publication 23

CO₂ corrosion in oil & gas production

EFC – Europe

EFC Publication 39

Corrosion inhibitors

EFC – Europe

EFC Publication 64

Corrosion management of pipelines

AMPP/NACE – International/USA

MR0175 / ISO 15156

H₂S damage, SSC, HIC, SOHIC, SCC

AMPP/NACE – International/USA

MR0103

Sour service materials in petroleum refining

DNV – Norway/International

DNV-RP-F101

Corrosion defects in pipelines

NORSOK – Norway

M-506

CO₂ corrosion rate calculation

EI – UK

Guidelines on Sand Erosion and Erosion-Corrosion Management

Erosion/erosion-corrosion

ISO

ISO 15156 series

H₂S-related cracking mechanisms

 

Some examples include:

  • HTHA
  • CUI
  • External Corrosion
    • Atmospheric
    • CUI
  • Internal Corrosion
    • General
    • Localized
    • Pitting
  • Sulfidation
  • Amine SCC
  • Chloride SCC
  • Fatigue
  • Thermal Fatigue
  • Hydrogen Blistering
  • Hydrogen Embrittlement
  • Erosion
  • FAC
  • MIC
  • Galvanic Corrosion
  • Temper Embrittlement
  • Polythionic Acid SCC
  • Graphitization
  • Creep
  • Stress Rupture

Never allow just a damage mechanism like "corrosion" without qualifiers like:

  • External
  • Atmospheric
  • CUI
  • Internal
  • General
  • Localized
  • Pitting

Qualifiers must be specified. If these are missing, reject the record.

7. Failure Cause Hierarchy

To make the most of the event data, create a failure cause hierarchy and taxonomy that moves from the immediate cause to more researched causes. Here are some recommendations below:

Level 1 - Immediate Cause

  • Examples:
    • Pipe rupture
    • Valve leak
    • Flange leak
    • Instrument failure
    • Tank crack

Level 2 - Physical Cause

  • Examples:
    • General corrosion
    • Localized corrosion
    • Fatigue
    • Overpressure
    • Thermal expansion
    • Hydrogen damage
    • External impact

Level 3 - Underlying Cause

  • Examples:
    • Inspection missed
    • Incorrect RBI interval
    • Poor design
    • Wrong material
    • Improper repair
    • Management of Change failure
    • Training deficiency
    • Procedure not followed

Level 4 - Organizational Cause

  • Examples:
    • Budget reduction
    • Deferred maintenance
    • Contractor issue
    • Management system failure

8. Failure Conditions

We need to capture general conditions at the time of, or shortly before, failure. Here are some recommendations:

  • Operating Pressure
  • Operating Temperature
  • Flow Velocity – especially for acids
  • Stream Composition – in addition to the standard fluid above
  • Corrosion rate – used to predict remaining life
  • Age – time in service
  • Inspection history summarized – including inputs to the condition forecast
  • Previous repair/replacement history summarized

9. Confidence Score

Every event record should have a confidence score, such as:

Verified by Impartial investigation - 5

Verified by metallurgical examination - 4

Company Official investigation - 3

Engineering judgment - 2

Witness statement - 1

Media report - 0

This ensures that any target AI can weigh information accordingly.

10. Duplicate Detection

The database should check for duplicate records. It should periodically and  automatically check the following for each record:

  • Date
  • Location
  • Equipment
  • Source
  • Description similarity

If it finds duplicate records, it should flag them for review. This avoids skewed results from duplicate events.

11. Mandatory References

Every failure event technical conclusion must have evidence. Here are some examples:

  • Laboratory report
  • Metallurgical report
  • CSB investigation
  • Inspection report
  • Failure analysis
  • Photographs
  • API reference

Unsupported conclusions should not be allowed.

12. Image Requirements

If some of the evidence is photographs or images, the recommended minimum metadata should be:

  • Equipment
  • Orientation
  • Damage location
  • Damage mechanism
  • Scale
  • Date

13. AI Readability Rules

Every field for each event record should be machine-readable. That means specific values like:

  • Pressure = 835 psig
  • Temperature = 725°F

They should never be vague descriptions, such as:

  • Pressure = High
  • Temperature = Very Hot

15. Standard Units

Units of data fields need to be standardized  and automatically converted, such as:

  • psi ↔ MPa
  • °F ↔ °C
  • ft ↔ m
  • gal ↔ L
  • lb ↔ kg

Store the original units alongside the conversions.

16. Security and Privacy

Separate technical data from sensitive information.

Store separately:

  • Company identity (optional or anonymized)
  • Personnel names
  • Witness statements
  • Legal findings
  • Insurance information
  • Litigation documents

Provide role-based access controls so contributors can share technical lessons while protecting confidential or legally sensitive information.

A well-governed Global Loss of Containment Event Repository should be more than a collection of incident reports; it should serve as the industry's authoritative technical knowledge base for process safety. By enforcing standardized taxonomies, validated engineering data, traceable evidence, and confidence scoring, it can support consistent failure investigations, improve API 580/581 Risk-Based Inspection (RBI) assessments, identify emerging trends in damage mechanisms, benchmark reliability across industries, and provide high-quality training data for AI systems that predict and help prevent future loss-of-containment events. This transforms historical incidents into actionable engineering intelligence that continuously improves mechanical integrity and process safety worldwide.


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