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HAZOP Guide Words Reference Card

Quick Reference for Facilitators & Team Members | SANS 1461 Compliant

Free Resource Version 2026
📊 Quick Reference Table
Guide Word Meaning Common Parameters Example Deviation
NO / NONE Complete absence Flow, Power, Signal, Level No flow through cooling pump
MORE Quantitative increase Flow, Pressure, Temp, Level High pressure in reactor vessel
LESS Quantitative decrease Flow, Pressure, Temp, Level Low temperature in distillation
AS WELL AS Something extra present Composition, Phase, Contaminants Water contamination in acid
PART OF Something missing Composition, Components, Steps Reactant B missing from batch
REVERSE Opposite direction Flow, Rotation, Sequence Reverse flow in return line
OTHER THAN Complete substitution Material, Operation, Mode Wrong chemical loaded
EARLY Action before intended Sequence, Timing, Operations Valve opens before safe state
LATE Action after intended Sequence, Response, Alarms Interlock activates too late
SOONER/LATER Duration deviation Batch time, Residence, Process Reaction completes early
📋 Detailed Guide Word Application

NO / NONE / NOT

Complete negation of design intent — nothing happens

Flow No flow → Pump failure, closed valve, blockage
Pressure No pressure → Leak, open vent, supply failure
Level No level → Drain open, massive leak
Power No power → Outage, breaker trip

Facilitator Prompt

"What could cause this process parameter to be completely absent? What happens if there's zero flow, zero pressure, zero signal?"

↑+

MORE / MORE OF

Quantitative increase beyond normal operating range

Flow High flow → Control valve fails open, pump over-speed
Pressure High pressure → Blockage, runaway, overcharging
Temperature High temp → Cooling failure, exothermic reaction
Level High level → Outlet blocked, overfilling

Facilitator Prompt

"What if this parameter increases significantly above normal? Consider control system failures, operator errors, and upstream upsets."

↓−

LESS / LESS OF

Quantitative decrease below normal operating range

Flow Low flow → Pump wear, partial blockage
Pressure Low pressure → Small leak, relief valve open
Temperature Low temp → Heater failure, excess cooling
Mixing Low mixing → Agitator fault, baffles missing

Key Difference: LESS vs NO

LESS = reduced but still present (pump running slowly). NO = completely absent (pump stopped).

REVERSE / OPPOSITE

Logical opposite of design intent — direction reversal

Flow Reverse flow → Check valve failure, pressure reversal
Rotation Reverse rotation → Phase error, wiring mistake
Reaction Reverse reaction → Equilibrium shift
Sequence Reverse sequence → Operator error, PLC fault

⚠️ Most Overlooked Guide Word

REVERSE is frequently skipped. Always ask: "What if flow direction reverses? What if the sequence runs backward?"

±

AS WELL AS / PART OF

Qualitative change — extra present or component missing

AS WELL AS Water, air, impurities, additional phase present
PART OF Missing reactant, skipped step, absent phase

Facilitator Prompt

"What contaminants could enter this stream? What component of the mixture could be missing?"

OTHER THAN / INSTEAD

Complete substitution — something entirely different

Material Wrong chemical loaded, mislabeled container
Operation Wrong procedure followed, different mode
Destination Material routed to wrong location
Mode Operating in wrong state (startup vs normal)

Human Error Focus

OTHER THAN scenarios often involve human error. Ask: "What if an operator makes a mistake? What if the wrong material is delivered?"

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✅ HAZOP Facilitator Checklist

Before the Workshop

  • Distribute reference cards to all participants
  • Explain each guide word with facility examples
  • Clarify LESS vs PART OF difference
  • Emphasize REVERSE is mandatory
  • Review node definitions and P&IDs

During the Workshop

  • Apply all guide words systematically
  • Consider startup, shutdown, abnormal ops
  • Don't combine multiple deviations
  • Trace consequences to worst credible outcome
  • Document all safeguards, even obvious ones

Before Moving to Next Node

  • All 7 primary guide words applied
  • Timing deviations considered (if relevant)
  • At least one cause per deviation
  • Risk rankings assigned
  • Recommendations specific and actionable

Pro Tips for Effective HAZOP Sessions

⚠️ Common Mistakes to Avoid
Mistake Solution
Skipping "obvious" deviations Apply all guide words systematically, even if outcome seems unlikely
Combining multiple deviations Consider each deviation separately; combined scenarios come later
Only considering equipment failure Include human error, external events, and process upsets as causes
Stopping at immediate consequence Follow the consequence chain to the worst credible outcome
Ignoring existing safeguards Document all protective measures before ranking risk