HAZOP (Hazard and Operability Study)

HAZOP is a structured, facilitator-led study that tests process deviations against design intent to uncover hazards, operability gaps, and required safeguards before startup.

How HAZOP works in practice

A practical sequence teams can use to run studies consistently and close actions on time.

1

Define scope and study nodes

Set boundaries, operating modes, and node breakdown (for example feed, reaction, separation, and discharge) so the workshop is complete and focused.

2

Prepare the design pack

Gather P&IDs, control logic, procedures, alarm philosophy, and maintenance context so the team works from one source of truth.

3

Assemble the right team

Include process engineering, operations, maintenance, HSSE, and an independent facilitator with a dedicated scribe.

4

Run guideword-based sessions

For each node, test deviations with guidewords, identify causes and consequences, and evaluate safeguard adequacy.

5

Assign actions and owners

Convert findings into specific actions with owners, target dates, and risk rationale that can be tracked to closure.

6

Verify closure before startup

Confirm priority actions are implemented and effective through pre-startup review and management sign-off.

Where HAZOP has the most impact

These are the areas where mature teams typically see measurable gains.

01

For HSSE Teams

HAZOP creates traceable evidence that major process hazards were identified and addressed before operation. Outputs feed procedures, training, and assurance planning.

02

For IT & CIOs

HAZOP produces high-volume risk data and actions that must stay linked to change control, ownership, and compliance reporting across the asset lifecycle.

Deep Dive

HAZOP explained for operations, HSSE, and leadership teams

A practical reference for scope, governance, deliverables, and execution quality.

What HAZOP covers

A Hazard and Operability Study (HAZOP) is a systematic, multidisciplinary review of how a process can deviate from design intent and what those deviations could cause.

Teams typically examine five deviation domains:

  1. Flow and inventory deviations (no flow, low flow, reverse flow, overfill).
  2. Pressure and temperature deviations beyond design envelope.
  3. Composition and contamination deviations (wrong material, dilution, impurity).
  4. Phase and physical state deviations (unexpected vaporization, condensation, solids).
  5. Timing and sequencing deviations during startup, shutdown, and abnormal operations.

Timing and governance

Most projects run HAZOP during detailed design (roughly 60-80% complete) or before commissioning. At this point, documentation is mature enough for meaningful analysis and there is still time to implement changes.

The method is commonly aligned to IEC 61882 and mapped into local process safety requirements and management-of-change workflows.

Expected outputs

A high-quality HAZOP should produce structured deliverables, not just meeting notes:

  • Node-by-node deviation records with causes, consequences, and existing safeguards.
  • Residual risk judgement and recommendation rationale.
  • Action register with owners, due dates, and closure evidence.
  • Pre-startup verification trail confirming critical safeguards are in place.

Manual versus digital execution

Spreadsheet-led studies often lose context and closure discipline. Digital HAZOP workflows improve consistency by standardizing data capture, linking findings to change management, and surfacing overdue actions automatically.

Common pitfalls to avoid

  • Starting before design data is mature enough to support credible decisions.
  • Running sessions without operations or maintenance representation.
  • Treating action tracking as optional after workshop closeout.
  • Allowing facilitator bias to narrow the scope of challenge.

Guidewords

IEC 61882 guidewords at a glance

Use guidewords consistently so deviations are tested the same way across every node.

CriteriaMeaningExample deviation
NONo part of design intent is achieved.No flow to feed tank.
MOREQuantitative increase from design condition.Cooling failure causes higher reactor temperature.
LESSQuantitative decrease from design condition.Lower suction pressure causes pump cavitation.
AS WELL ASAdditional material or condition is present.Contaminant enters product stream.
PART OFOnly a portion of design intent is achieved.Partial blockage reduces expected flow.
REVERSECondition occurs in opposite direction.Backflow from discharge to upstream tank.
OTHER THANA different condition or substance occurs.Wrong chemical loaded into line.
EARLYAction occurs earlier than intended.Discharge valve opens before stabilization.
LATEAction occurs later than intended.Shutdown response triggers too late.

Frequently asked questions

IEC 61882 is the international standard for FMEA (Failure Modes and Effects Analysis) and HAZOP methodology. It defines the formal process, guidewords, documentation requirements, and team composition for conducting systematic hazard analysis studies. Conducting HAZOP in accordance with IEC 61882 ensures consistency, rigour, and regulatory acceptance. Most major projects, insurers, and regulators reference IEC 61882 as the standard methodology.

Operationalize HAZOP at workforce scale

Dockt helps teams move from manual credential tracking to proactive, audit-ready competence management.