
Introduction
Layer of Protection Analysis (LOPA) is only as strong as the events it considers. At the heart of every scenario lies the initiating event, the trigger that sets the chain of risk in motion. Whether it’s a pump seal failure, a control system crash, or human error, understanding these initiating events and assigning realistic frequencies is critical to making LOPA results credible.
This guide provides a structured approach to identifying valid initiating events, estimating their frequency, and avoiding common pitfalls, with examples drawn from real process safety practice. “An initiating event defined clearly and consistently makes risk decisions defensible even when precision is limited.”
To understand how initiating events fit within the broader LOPA framework, refer to “Layer of Protection Analysis (LOPA): An Engineer’s Overview,” which explains how causes, safeguards, and consequences interact in risk studies.
What is an Initiating Event in LOPA?

- An initiating event is the first failure or action that can lead to an undesired consequence.
- Each LOPA scenario is built on a unique cause consequence pair.
- For consistency, initiating event frequencies are expressed as events per year (e.g., 1 × 10⁻²/yr).
Why it matters: If initiating events are not identified properly, the analysis may underestimate risks or double-count safeguards.
Recognized for excellence.
PROJECTS DELIVERED ACROSS THE GLOBE
Categories of Initiating Events

LOPA classifies initiating events into three main groups:
a) External Events
- Natural disasters: earthquakes, floods, lightning strikes.
- Neighboring facility accidents: fires, explosions.
- Third-party interference: vehicle impact, crane load drop, sabotage.
b) Equipment Failures
- Control system failures:
- Basic Process Control System (BPCS) loop failure
- Software crashes
- Power or utility loss
- Basic Process Control System (BPCS) loop failure
- Mechanical failures:
- Corrosion, fatigue, or brittle fracture
- Overpressure or vacuum collapse
- Seal or gasket failure
- Vibration-induced failures
- Improper maintenance or wrong material substitution
- Corrosion, fatigue, or brittle fracture
c) Human Failures
- Errors of omission: steps skipped (e.g., failing to open a valve).
- Errors of commission: actions taken incorrectly (e.g., wrong valve opened).
- Often linked to training gaps, fatigue, or poor procedures.
Pull Quote: “Most real-world incidents are triggered not by one major failure, but by a chain of small initiating events.”
Once initiating event frequencies are defined, the next step is integrating them into complete scenario development. “Developing LOPA Scenarios: A Complete Guide to Defensible Risk Assessment” provides the methodology to document and validate these scenarios effectively.
Enabling Events and Conditions
Not every initiating event leads to a consequence; some require special conditions to align.
Examples:
- Loss of cooling → Dangerous only during the reaction exotherm phase.
- Double catalyst addition → Risk depends on the number of batches per year.
- Moving cylinders → Only hazardous if a cylinder is uncapped and dropped.
How they are used:
- Expressed as probabilities (e.g., “probability reactor is in exotherm phase = 0.3”).
- May be applied as modifiers to initiating event frequency.
Estimating Frequency of Initiating Events

Data Sources
- Industry databases: CCPS QRA Guidelines, OREDA, IEEE reliability data.
- Company operating history: incident logs, near-miss reports.
- Vendor data: often optimistic; use cautiously.
Best Practices
- Use order-of-magnitude estimates (10⁻¹, 10⁻²) rather than false precision.
- Select frequencies consistently (all upper-bound, mid-point, or conservative).
- Adjust for time at risk: equipment used only during specific operations has a lower annual exposure.
Example: Adjusting for Time at Risk
- Unloading hose: Base failure rate 1 × 10⁻²/yr.
- Used 40 times/year, 2 hrs each → Effective frequency = 1 × 10⁻⁴/yr.
Example Scenarios

Case 1: Hexane Surge Tank Overflow
- Initiating event: Level indicator/controller failure.
- Frequency: ~1 × 10⁻¹ per year.
- Consequence: Overflow spill; severity depends on dike containment.
Case 2: Hexane Storage Tank Overflow
- Initiating event: Inventory control error.
- Frequency: ~1/yr.
- Consequence: Overflow spill into or outside the dike.
Limitations and Cautions
- LOPA is semi-quantitative. For very high-consequence events, use CPQRA, fault trees, or event trees.
- Avoid mixing safeguards into initiating event frequency. (Example: a relief valve is not an initiating event but an IPL).
- Remember failure rates are assumed constant real-world conditions may vary (infant mortality, aging).
While understanding initiating event frequency establishes the starting point of a LOPA study, evaluating how effectively safeguards prevent or mitigate these events is equally vital. To explore this next layer in detail, “Independent Protection Layers (IPLs) in LOPA: Types, Rules, and PFD Values” explains how protective systems are categorized, validated, and assigned probability of failure on demand (PFD) values to quantify risk reduction. Together, these steps ensure each LOPA scenario remains both technically accurate and defensible during safety reviews.
Frequently Asked Questions (FAQs)
What exactly is an “initiating event” in LOPA?
An initiating event is the one specific failure, action, or external occurrence that triggers the risk scenario you’re analyzing. Each LOPA scenario pairs exactly one initiating event with a consequence to maintain clarity and precision.
How do enabling conditions affect the frequency of initiating events?
Enabling conditions are situational factors (like operating phase, batch timing, or occupancy) that must be present for the initiating event to lead to a consequence. Think of them as modifiers not causes.
For example, a double catalyst dosage only matters during certain production cycles. You estimate its frequency as:
Initiating Event Frequency × Probability (Enabling Condition), This ensures you’re estimating only the times the event is genuinely relevant.
What are the main types of initiating events to consider?
LOPA recognizes three categories:
- External events (e.g., earthquakes, vehicle collisions, fires)
- Equipment failures (e.g., BPCS loops, corrosion leading to piping failure)
- Human errors (e.g., missing a procedural step or executing the wrong action)
It’s vital to cover all categories so no cause is overlooked.
Where do I get credible frequency data for initiating events?
Use a mix of sources:
- Industry datasets (e.g., CCPS, OREDA, IEEE)
- Company operational history or incident logs
- Vendor data (but adjust these as they tend to be optimistic)
Good practice is to use order-of-magnitude values (e.g., 10⁻¹, 10⁻³) for defensibility and simplicity.
Why shouldn’t protective layer failures be treated as initiating events?
Protection layer failures (such as an IPL fail-on-demand) occur after the initiating event. Including them in the initiating event frequency misrepresents the scenario and inflates the risk assessment. Always keep initiating events distinct and upstream from safeguards.