Process Safety · HAZOP Study

Green Hydrogen Electrolysis Project

HAZOP in Action – From Kick-off to Recommendation Closure

Sector: Renewable Energy / Green Hydrogen Study: HAZOP Capacity: 500 TPA Status: ✓ Completed

One HAZOP deviation. One missed safeguard. One potentially serious consequence.

This case study presents how a structured HAZOP study was prepared, facilitated and followed through for a 500 TPA green hydrogen production and operation project — covering every stage from kick-off to recommendation closure.

500 TPA
Project Capacity
6
Process Sections
8
Eng. Doc Types Reviewed
100%
Recommendations Closed

Overview

Project Overview

Aura Safety & Risk Consultants supported a green hydrogen electrolysis project through a structured Hazard and Operability Study (HAZOP), covering the study process from initial kick-off and engineering-document review through node definition, multidisciplinary workshop discussions, recommendation development and action closure.

The production process included six key sections. The HAZOP was used to systematically identify process deviations, understand credible causes and consequences, review safeguards and define practical recommendations where further action was required.

💧Water Treatment
PEM Electrolyser
⚗️Gas / Liquid Separation
🔬H₂ Purification
🔧Compression
🏭Storage & Export

Learn more about Aura Safety's HAZOP Study Services →

Introduction

Why Green Hydrogen Projects Demand Rigorous HAZOP

Green hydrogen projects combine electrochemical processes, gas generation, separation, purification, compression, controls and storage. This makes clear process understanding and multidisciplinary review important when examining how deviations could develop across the plant.

In this project, the HAZOP was treated as more than a worksheet exercise. The focus was on establishing design intent, asking the right technical questions, testing safeguards and ensuring that recommendations could be converted into accountable engineering actions.

Why It Matters

  • Hydrogen is flammable across a wide concentration range
  • O₂ co-generation creates additional hazard interactions
  • High-pressure systems require systematic safeguard review
  • Early-stage HAZOP prevents expensive late-design changes
  • Multidisciplinary review finds gaps no single engineer sees

Study Objectives

Objectives of the HAZOP Study

Deviation Identification

Identify process deviations across the entire green hydrogen production system.

Cause Analysis

Understand credible causes associated with each identified deviation.

Consequence Challenge

Challenge potential consequences and escalation scenarios systematically.

Safeguard Review

Review the adequacy of existing safeguards and controls at every node.

Recommendations

Develop clear, practical and traceable recommendations for engineering action.

Safer Design

Support safer design decisions and more reliable future plant operation.

Preparation Phase

Before the HAZOP Workshop

The case study shows that effective HAZOP preparation begins well before guide words are applied. Study quality depends heavily on how clearly the scope, technical information, process boundaries and nodes have been prepared.

  1. Kick-off: align the team on purpose, scope, team composition, ground rules and schedule.
  2. Document Review: review relevant engineering documents for accuracy, completeness and current revision status.
  3. Process Understanding: understand process intent, equipment function, utilities and operating methods.
  4. Node Marking: divide the process into logical sections that enable focused, structured discussion.
  5. Node Finalisation: confirm and approve the node list with the full HAZOP team before commencing the workshop.

Document Review

Engineering Documents Reviewed

The project review used the available engineering information to establish what the plant was intended to do before assessing how it could deviate from that intent.

PFDs / P&IDs

Process flow, connections and equipment layout for the full plant.

Process Design Basis

Design assumptions, criteria and operating parameters.

Equipment Datasheets

Ratings, design limits, materials of construction.

Cause & Effect Diagrams

Possible causes, expected process responses and alarm settings.

Control Philosophy

Control strategies, interlock logic and key safeguards.

Line / Equipment Lists

Supporting process information for all streams and equipment items.

Relief Philosophy

Overpressure-protection strategy, relief valve set points.

Utility Information

Utility requirements, design limits and supply interdependencies.

Every document helps the team understand the intended design — and therefore what a deviation actually means.

Node Definition

HAZOP Node Marking

Node selection was approached as more than a drawing exercise. The team considered six key factors when defining each node to ensure meaningful, focused workshop discussions.

Process Intent

Define what each section of the process is intended to achieve operationally.

Equipment Function

Understand the role of each equipment item within its process section.

Control Boundaries

Recognise where control strategies and operating conditions change across the plant.

Interfaces

Pay particular attention to transitions and handoff points between process sections.

Operating Conditions

Consider all relevant parameters: pressure, temperature, flow and composition.

Clear Design Intent

Keep one clear, unambiguous design intent per node wherever practical.

Clear node marking + clear design intent = a more effective HAZOP discussion.

Workshop Phase

The HAZOP Workshop: Guide Words Applied

Once preparation was complete, the multidisciplinary team used guide words to challenge how the process could differ from its intended operation. Examples illustrated in the case study:

Noe.g. No flow — complete loss of intended flow parameter.
Moree.g. High pressure — parameter above design intent.
Lesse.g. Low flow — parameter below design intent.
Reversee.g. Reverse flow — flow in unintended direction.
Other Thane.g. Wrong composition — unexpected process fluid or phase.
As Well Ase.g. Additional condition — unexpected co-occurring parameter.

The team did not stop at "What can fail?" The discussion examined what could happen when the process did not behave as intended.

Example Scenario

A Realistic Hydrogen HAZOP Discussion

Example Deviation: H₂ / O₂ Cross-Contamination

One of the scenarios presented in the case study involved hydrogen and oxygen cross-contamination inside the electrolyser separator. The discussion followed the potential development of the scenario step by step.

Abnormal Differential PressureInitial signal
Membrane / Separator DeteriorationRoot cause
Gas CrossoverPhysical event
Unsafe CompositionHazard state
Ignition PotentialConsequence

The team challenged the scenario by asking:

  • How would the condition be detected?
  • What happens if the analyser fails?
  • Does the shutdown happen automatically?
  • What happens to the gas during the abnormal condition?

Good questions uncover weak points. Better understanding supports safer design decisions.

Workshop Discipline

Key HAZOP Discussion Points

For each credible deviation identified, the workshop focused on eight structured questions:

  • Is the cause credible?
  • What is the immediate consequence?
  • What is the worst credible consequence?
  • How is the deviation detected?
  • Is the safeguard available in time?
  • Is the safeguard independent?
  • What happens if the safeguard fails?
  • Does the recommendation improve the design?

HAZOP is not a spreadsheet exercise. It is a structured conversation about uncertainty.

From Finding to Action

From Finding to Recommendation

The case study shows that a recommendation should solve an identified problem rather than simply fill a worksheet row. Each potential finding was discussed technically before an action was finalised.

  1. Finding: identify a potential HAZOP issue from the guide word + deviation discussion.
  2. Discussion: evaluate causes, detection, protection and safeguard independence.
  3. Challenge: assess whether existing safeguards are adequate for the worst credible consequence.
  4. Action: define clearly how protection should be improved or verified.

Following multidisciplinary discussion, a recommendation could be refined, merged, rewritten or rejected. The objective was to arrive at technically meaningful actions with a clear engineering basis.

Recommendation Quality

Recommendation Finalisation

A strong recommendation needs enough detail to be assigned, implemented and verified. The case study highlights six practical questions every recommendation must answer:

01
What?
What specifically needs to be done?
02
Who?
Who owns and is accountable for the action?
03
Priority?
What urgency level or risk-based priority applies?
04
Why?
Why is the action required — what hazard does it address?
05
Where?
Where does the design, drawing or document change?
06
How?
How will closure be verified and recorded?

Post-Workshop Phase

After the Workshop

The HAZOP did not end when the workshop ended. The follow-up process presented in the project moved through a formal five-stage closure path:

Report
Action Owner
Technical Response
Evidence
Closure

This follow-up is essential because a recommendation that is never implemented is not a completed risk reduction. Strong action tracking turns workshop discussions into practical, verifiable risk-reduction measures.

Outcome & Value

Outcome & Project Value

The case study presents the value of the HAZOP primarily in qualitative engineering and project terms. Four outcomes were consistently achieved across the study:

Better Design

Potential problems were challenged while design changes were still possible — avoiding expensive rework during construction or commissioning.

Shared Understanding

Process, instrumentation, mechanical, electrical, operations and HSE disciplines reviewed the same scenarios together, closing knowledge gaps across teams.

Traceable Actions

Recommendations became owned and trackable engineering actions — with a named responsible party and closure evidence required for each one.

Preventive Thinking

Potential failure chains — including the H₂/O₂ cross-contamination scenario — were examined and addressed before they could become operational incidents.

Sector Context

Why HAZOP Is Important for Green Hydrogen Projects

In a green hydrogen facility, interactions between hydrogen, oxygen, electrical energy, pressure, controls and process equipment require systematic examination. A structured HAZOP helps the project team identify deviations, test assumptions, examine safeguards and document actions before issues become operational problems.

The central lesson from this project is simple: challenge the design before the design challenges you.

For broader context, read Aura Safety's Green Hydrogen Safety: Understanding Hazards and Managing Risks →

Our Services

Partner with Aura Safety & Risk Consultants

Aura Safety supports process industries with structured hazard identification and risk-assessment studies designed to improve process understanding, challenge safeguards and convert findings into practical engineering actions.

FAQs

Frequently Asked Questions

What was the scope of this green hydrogen HAZOP case study?

The case study covers a 500 TPA green hydrogen production and operation project and follows the HAZOP process from kick-off and preparation through workshop discussions, recommendations and formal closure of every action.

Which process sections were part of the project?

The source material identifies water treatment, a PEM electrolyser, gas/liquid separation, hydrogen purification, compression and storage/export within the green hydrogen production process — six distinct process sections.

Why was node marking important?

Node marking helped create logical study sections with clear design intent. The project considered equipment function, control boundaries, operating conditions, interfaces and changes in pressure or temperature — ensuring each workshop session had a focused and productive scope.

What hydrogen-related scenario was examined?

The case study illustrates an H₂/O₂ cross-contamination scenario and challenges how the condition could develop — from abnormal differential pressure through membrane deterioration and gas crossover to unsafe composition and ignition potential — and what safeguards would respond at each stage.

Does HAZOP follow-up continue after the workshop?

Yes. The case study shows a formal five-stage follow-up path: Report → Action Owner → Technical Response → Evidence → Closure. A recommendation that is never implemented is not a completed risk reduction.

Can Aura Safety conduct a HAZOP for our green hydrogen or hydrogen project?

Yes. Aura Safety & Risk Consultants delivers HAZOP studies for green hydrogen, renewable energy, chemical, oil & gas, and manufacturing projects across India. Contact us to discuss your project stage, scope and timeline.

India-Wide HAZOP Consulting

Looking to Conduct a HAZOP Study for Your Facility or Project?

Discuss your process, project stage, available documentation and HAZOP requirements with Aura Safety & Risk Consultants. We respond within 24 hours.

Phone: +91 99994 02106   Email: info@aurasafety.com

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