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

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:
Here is an example:
Never allow anonymous technical conclusions.
2. Required Minimum Data
Set a minimum data requirement. Event records shall have the following fields populated:
Event
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:
|
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 |
|
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 |
|
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:
Materials of construction must have a material specification per the appropriate code or the common manufacturer's name. See the examples below:
Never accept unspecified generic names. Here are some examples:
5. Fluid Standardization
Select fluids from a controlled, validated list. Ideally, it should be a composite of the lists from:
Examples include:
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:
Never allow just a damage mechanism like "corrosion" without qualifiers like:
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
Level 2 - Physical Cause
Level 3 - Underlying Cause
Level 4 - Organizational Cause
8. Failure Conditions
We need to capture general conditions at the time of, or shortly before, failure. Here are some recommendations:
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:
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:
Unsupported conclusions should not be allowed.
12. Image Requirements
If some of the evidence is photographs or images, the recommended minimum metadata should be:
13. AI Readability Rules
Every field for each event record should be machine-readable. That means specific values like:
They should never be vague descriptions, such as:
15. Standard Units
Units of data fields need to be standardized and automatically converted, such as:
Store the original units alongside the conversions.
16. Security and Privacy
Separate technical data from sensitive information.
Store separately:
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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