LOPA • Independent protection layers • SIL identification • ALARP

Layer of Protection Analysis

Structured, semi-quantitative LOPA studies that test whether existing or proposed safeguards provide sufficient risk reduction for clearly defined hazardous scenarios.

ExConform facilitates multidisciplinary teams to evaluate initiating-event frequency, enabling conditions, conditional modifiers and independent protection layers, then compare the resulting mitigated event likelihood with the organisation’s tolerable-risk criteria.

A focused bridge between HAZOP and detailed risk assessment

What a LOPA Study Is Designed to Answer

Layer of Protection Analysis is a semi-quantitative, scenario-based risk assessment method. It examines a single initiating cause and consequence pair, applies agreed order-of-magnitude data and determines whether the credited protection layers reduce risk to the organisation’s target level.

LOPA is commonly used after a HAZOP has identified scenarios that need more consistent evaluation, where safeguard independence must be demonstrated, or where the required performance of a safety instrumented function needs to be established. It is more structured than qualitative risk ranking, while remaining less data-intensive than a full quantitative risk assessment.

Input from PHA Clearly defined scenarios are normally taken from HAZOP, HAZID, What-If or another recognised hazard evaluation.
Order-of-magnitude analysis Initiating-event and protection-layer values are applied consistently using an agreed company or project methodology.
Decision-focused output The study identifies whether existing layers are adequate, what additional protection is needed and whether a SIL target is justified.

How the study is performed

A Clear and Traceable LOPA Workflow

Effective LOPA depends on disciplined scenario definition, transparent assumptions and consistent application of the organisation’s risk criteria. Each step is documented so that reviewers can understand how the final risk-reduction requirement was derived.

1 Select the scenario Confirm the initiating cause, consequence endpoint, affected receptors and study boundary.
2 Assign initiating frequency Use approved data, plant history or justified engineering assumptions without double counting.
3 Apply modifiers Consider enabling conditions and conditional modifiers only where technically justified.
4 Credit valid IPLs Assign PFD values only to layers that meet the required effectiveness and independence criteria.
5 Compare and act Compare mitigated likelihood with the target, define the risk gap and record recommendations or SIL targets.

The risk-reduction concept

Protection Layers Work Together to Close the Risk Gap

The unmitigated process risk associated with a hazardous scenario is reduced by prevention, control, protection and mitigation measures. LOPA makes this layered concept explicit by quantifying the portion of risk reduction that can be credited to each valid protection layer.

The total reduction achieved by all credited layers is compared with the necessary risk reduction required to reach the tolerable-risk target. Existing non-SIS layers should be considered before assigning the remaining gap to a safety instrumented function.

This supports proportionate design decisions and helps avoid both under-protection and unnecessary dependence on instrumented safeguards.

Inherently safer design measures
Basic process control functions
Alarms and operator response
Mechanical and passive safeguards
Safety instrumented functions
Mitigation and emergency measures
Risk reduction diagram showing process risk, tolerable risk and residual risk, with the necessary and actual risk reduction shared between safety instrumented systems and other protection layers.
Risk-reduction concept showing how all credited protection layers contribute to reducing process risk to the tolerable or residual-risk region. Click the image to open the full-size version.

Independent protection layers

Safeguards Are Credited Only When They Meet IPL Criteria

A safeguard identified during HAZOP is not automatically an Independent Protection Layer. The team must demonstrate that the layer can prevent or mitigate the scenario without being defeated by the initiating event or by the failure of another credited layer.

01

Effective and Specific

The layer must act on the defined scenario and be capable of preventing or mitigating the stated consequence endpoint.

Key question: Does this safeguard directly interrupt the scenario being analysed?
02

Independent

The layer must not be compromised by the initiating cause, by the same failure mechanism or by another protection layer credited in the calculation.

Key question: Are sensors, logic, utilities, final elements and human actions genuinely independent?
03

Dependable and Auditable

The claimed performance must be supported by design, inspection, testing, maintenance, procedures, competence and records.

Key question: Can the organisation demonstrate that the layer will continue to achieve its claimed PFD?
Example LOPA worksheet for a hydrogen generation system showing deviations, initiating causes and frequencies, consequences, risk categories, conditional modifiers, target mitigated event likelihood, independent protection layers, PFD values, residual likelihood, risk reduction factor, recommended SIL and actions.
Example hydrogen-generation LOPA worksheet. The record links each scenario to its initiating frequency, consequence, target criteria, credited IPLs, PFD values, mitigated event likelihood, required risk reduction and recommended SIL. Click the image to open the full-size version.

Example study record

A LOPA Worksheet Makes the Decision Basis Visible

The example worksheet covers hydrogen-generation scenarios including toxic exposure during maintenance, electrocution and inadvertent remote start-up. For every scenario, the worksheet records the cause, expected frequency, consequence severity and the target mitigated event likelihood before protection-layer credit is applied.

Credited safeguards are then listed with their assigned probability of failure on demand. The worksheet calculates the resulting mitigated event likelihood, the LOPA ratio or risk gap, the required risk reduction factor and any recommended SIL.

Recommendations and comments provide traceability for design changes, operating controls, assumptions, exclusions and the rationale for “No SIL” outcomes where non-instrumented measures are sufficient.

Deviation and initiating cause
Initiating-event frequency
Consequence and severity
Enabling conditions and modifiers
Target mitigated event likelihood
IPLs and assigned PFDs
Mitigated event likelihood
RRF, SIL target and actions

Transparent Calculation, ALARP Demonstration and Recommendation Logic

LOPA does not seek false numerical precision. It uses controlled, order-of-magnitude assumptions to support consistent decisions. Every frequency, modifier, PFD and risk criterion should have a documented source or justification, and uncertainty should be made visible to the decision-makers.

Where the calculated mitigated event likelihood remains above the target, the study identifies additional prevention or protection measures and records why the selected solution is reasonably practicable. The output can therefore support ALARP demonstration, provided it is integrated with engineering judgement, option evaluation and the wider risk-management process.

Simplified LOPA relationship Mitigated event likelihood = initiating-event frequency × enabling-condition factors × conditional modifiers × PFD of each credited IPL
Consistent risk criteria Use approved tolerability targets that reflect consequence category, affected receptors and company requirements.
Visible assumptions Record data sources, occupancy assumptions, enabling conditions, ignition probabilities and any conservative simplifications.
Proportionate recommendations Prioritise inherently safer design and robust non-SIS layers before assigning residual risk reduction to a SIF.
Important: LOPA determines the required risk reduction for a scenario. It does not, by itself, verify that a proposed SIF architecture, proof-test interval, diagnostics, hardware reliability or lifecycle arrangements will achieve the target SIL. Those activities belong within the functional safety lifecycle.

SIL, PFD and risk reduction factor

Translating a Risk Gap into a SIL Target

Where additional risk reduction is to be provided by a safety instrumented function, the LOPA output can be used to identify the required Safety Integrity Level. In low-demand applications, the SIL bands correspond to target ranges of average probability of failure on demand and their reciprocal risk reduction factors.

A SIL target is a performance requirement for the complete safety instrumented function—not simply for an individual sensor, logic solver or valve. The subsequent functional safety lifecycle must define the Safety Requirements Specification, verify the design, manage systematic capability, validate the function and maintain the required performance throughout operation.

Terminology note: “SIL 0” or “No SIL” is often used in project worksheets to indicate that no SIL-rated SIF is required or that the remaining RRF is 10 or less. SIL 0 is not a formal Safety Integrity Level in IEC 61511; formal SIL levels are SIL 1 to SIL 4, and SIL 4 is rarely used in the process sector.
Table showing SIL levels with target average probability of failure on demand and corresponding target risk reduction factor ranges.
Relationship between SIL, target average PFD and target RRF for low-demand safety instrumented functions. Click the image to open the full-size version.

Human factors in LOPA

Operator Actions Need the Same Discipline as Engineered Layers

Alarm-and-operator-response layers and procedural safeguards can only be credited when the required action is clear, timely, achievable and supported by reliable detection, alarm presentation, procedures, competence and working conditions.

01

Detection and Diagnosis

The operator must receive an unambiguous indication, recognise the scenario and diagnose the required response without relying on the failed initiating function.

02

Available Response Time

The process safety time must allow detection, decision and action with a realistic margin for workload, access and abnormal operating conditions.

03

Competence and Assurance

Procedures, training, drills, alarm management, staffing and audit records must support the claimed human reliability and continued IPL performance.

Facilitated by Experienced Process Safety Personnel

LOPA studies are facilitated by experienced personnel with strong process safety and hazard-study experience across the energy sector, hydrogen plants, electrolysers, hydrogen refuelling stations, hazardous-waste incineration plants, aerospace facilities, tank farms, chemical processing lines, process tanks and effluent treatment plants.

This sector experience supports practical challenge of initiating events, maintenance and operating modes, safeguard independence, operator response, hydrogen hazards, toxic releases, fire and explosion scenarios, utilities and package-system interfaces.

Hydrogen and energy systems Electrolysers, compression and storage, refuelling stations, utilities, package units and hazardous operating modes.
Aerospace and chemical processing Tank farms, chemical lines and tanks, high-reliability operations, hazardous materials and complex control interfaces.
Waste and effluent treatment Incineration, toxic and corrosive streams, treatment plants, emissions controls and environmental consequence pathways.

Preparation and team composition

What Is Needed for an Effective LOPA Workshop

The quality of a LOPA depends on the quality of the underlying HAZOP scenarios and the availability of reliable technical and operational information. The study basis, risk criteria and data sources should be agreed before the workshop.

ExConform can support scenario screening, workshop planning, data preparation, attendee selection, facilitation, live recording and post-workshop reporting.

HAZOP worksheets P&IDs Risk criteria Cause & effect Alarm list Interlock narratives Operating procedures Proof-test data Occupancy data Incident history
LOPA facilitator / chair Controls the methodology, prevents double counting, challenges IPL claims and maintains consistency.
Study scribe / recorder Records scenario assumptions, calculations, decisions, recommendations and comments live.
Process / technology engineer Explains design intent, process conditions, chemistry, consequence endpoints and initiating causes.
Operations representative Provides operating, start-up, shutdown, maintenance, alarm-response and bypass experience.
Control and instrumentation engineer Explains BPCS functions, alarms, interlocks, SIF architecture, independence and failure modes.
Functional safety specialist Supports SIL determination, lifecycle interfaces, SRS development and follow-on verification requirements.
Mechanical / package specialist Supports relief protection, package controls, mechanical safeguards, utilities and equipment interfaces.
Process safety / HSE specialist Supports risk criteria, consequence interpretation, receptors, environmental impact and ALARP review.

LOPA Study Deliverables

Deliverables are structured to provide a complete and reviewable decision basis for risk reduction, SIL identification, project assurance and subsequent functional safety activities.

LOPA study planning, preparation and facilitation
Scenario screening and confirmation of study boundaries
Documented methodology, risk criteria and data sources
Structured LOPA worksheets for each assessed scenario
Initiating-event frequencies and technical justification
Enabling conditions and conditional modifiers
IPL assessment, independence challenge and assigned PFDs
Mitigated event likelihood and comparison with target criteria
Required RRF and recommended SIL where applicable
ALARP considerations and alternative risk-reduction options
Prioritised action summary with recommended owners
Complete LOPA Study Report with findings and recommendations
Recommended reporting practice: the report should distinguish between existing verified IPLs, proposed layers, assumptions requiring confirmation and recommendations that must be closed before the LOPA conclusion can be relied upon. Any resulting SIF should be transferred into the functional safety lifecycle with a clear functional description and target SIL.

Connected services and competence

Support Beyond the LOPA Workshop

LOPA often sits at the interface between Process Hazard Analysis, engineering design and functional safety. These related services help organisations carry the findings through to implementation and lifecycle assurance.

When to commission a LOPA

Typical Project and Operational Triggers

LOPA can support new designs, modifications and operating facilities whenever a hazardous scenario needs a more consistent and auditable assessment of safeguard adequacy.

After HAZOP

Assess scenarios escalated by the HAZOP team because of high consequence, uncertain safeguard adequacy or company risk-screening criteria.

SIL Identification

Determine whether a safety instrumented function is required and define the target risk reduction for the function.

Design Development

Compare alternative safeguards and establish whether proposed prevention or mitigation layers close the identified risk gap.

Management of Change

Reassess scenarios where process conditions, control logic, equipment, chemicals, occupancy or operating modes have changed.

Revalidation

Confirm that initiating-event assumptions, credited IPLs, testing arrangements and target criteria remain valid over time.

Incident Learning

Revisit scenarios where incidents, near misses, audit findings or industry learning challenge previous frequency or IPL assumptions.

Common questions

LOPA Study FAQs

What is the difference between HAZOP and LOPA?

HAZOP is a qualitative, guideword-based method used to identify deviations, causes, consequences and safeguards. LOPA takes selected cause-consequence scenarios and evaluates them semi-quantitatively using initiating frequencies, modifiers and credited IPL PFD values.

Does every HAZOP scenario need a LOPA?

No. Scenarios are normally screened using the organisation’s risk criteria. LOPA is most useful where the consequence is significant, safeguard adequacy is uncertain, a SIL target may be required, or company rules specify escalation.

Can any safeguard be credited as an IPL?

No. The safeguard must be effective for the scenario, sufficiently independent, dependable and auditable. Shared sensors, utilities, logic, final elements, human dependencies and common-cause failures must be challenged before credit is assigned.

Does LOPA prove that a SIF achieves its SIL?

No. LOPA identifies the required risk reduction or target SIL. Demonstrating that the SIF achieves and maintains that target requires specification, design verification, reliability calculation, validation, proof testing, management of change and other functional safety lifecycle activities.

Can LOPA be used for environmental or asset consequences?

Yes, provided the organisation has suitable consequence categories and tolerability criteria. The scenario definition should clearly identify whether the endpoint concerns people, environmental receptors, assets, business interruption or a combination of these.

Can a LOPA study be facilitated remotely?

Yes. Remote or hybrid LOPA can be effective when the HAZOP scenarios and supporting documents are mature, the calculation basis is agreed, the team can review worksheets clearly and sessions are planned to maintain concentration and challenge.

Need a LOPA or SIL Identification Study?

We can support scenario screening, data preparation, multidisciplinary workshop facilitation, IPL assessment, ALARP review, SIL target identification, action prioritisation and complete reporting for new projects, modifications and operating facilities.

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