HAZID • HAZOP • ALARP • Human factors

HAZID & HAZOP Studies

Independent, structured hazard studies for projects and operating facilities—from early-stage HAZID workshops through to detailed, guideword-based HAZOP studies for mature process designs.

ExConform facilitates multidisciplinary teams to identify credible hazards, challenge process deviations, evaluate safeguards, prioritise actions and demonstrate that risks have been reduced to a level that is As Low As Reasonably Practicable.

The right study at the right project stage

From Early Hazard Identification to Detailed Operability Review

HAZID and HAZOP are complementary Process Hazard Analysis methods. A HAZID is normally used during concept selection, feasibility, front-end engineering or other early project phases, when the objective is to identify major hazard themes and influence the design before key decisions become difficult or expensive to change.

A HAZOP is most effective once the process design is sufficiently mature and the intended operating conditions, process flow diagrams, piping and instrumentation diagrams, control philosophy and safeguarding arrangements are available for detailed review.

Early phase

HAZID Study

A structured, multidisciplinary review used to identify credible hazard sources, major accident scenarios, affected people and assets, environmental impacts and the principal prevention or mitigation measures required by the developing design.

Concept selection and feasibility studies Site selection, layouts and interfaces Technology selection and project risk registers Early identification of safety-critical studies
Mature phase

HAZOP Study

A detailed, guideword-based examination of how process conditions can deviate from design intent, what can cause each deviation, the consequences that may follow, whether safeguards are effective and what further actions are justified.

Detailed design, commissioning and modification projects Process nodes and operating modes Start-up, shutdown, maintenance and abnormal operation Periodic revalidation of existing installations

How the study is delivered

A Clear and Traceable Study Process

Effective HAZID and HAZOP workshops depend on good preparation, the right multidisciplinary team and disciplined facilitation. The study process is structured so that assumptions, discussions, decisions, risk rankings and recommendations can be followed from workshop preparation through to final close-out.

1 Define scope and basis Confirm objectives, boundaries, design maturity, operating modes, risk criteria and required outputs.
2 Prepare the study Review drawings and process information, define HAZOP nodes or HAZID categories and plan the workshop.
3 Facilitate the workshop Apply guidewords or hazard prompts, challenge assumptions and record the team’s findings live.
4 Assess risk and ALARP Evaluate consequences, likelihood, safeguards, residual risk and the need for LOPA or further study.
5 Report and prioritise Issue complete worksheets, findings, recommendations and a prioritised action summary.
Example piping and instrumentation diagram marked with nine colour-coded HAZOP nodes that divide the process into manageable study sections.
Example P&ID marked with colour-coded HAZOP nodes. Each node defines a manageable study section with a clear design intent and boundary.

HAZOP study preparation

Noding Turns a Complex P&ID into a Structured Review

A detailed HAZOP is normally performed node by node, rather than reviewing an entire facility as one system. Before the workshop, the process is divided into manageable sections that share a coherent design intent, operating conditions and set of process parameters.

Node boundaries are marked on the current P&IDs so the team can see exactly which equipment, lines, instruments and interfaces are being reviewed. The colour-coded example illustrates how a complex process can be separated into distinct study areas, helping the team maintain coverage, avoid unintended gaps or duplication and follow a logical workshop sequence.

For every node, the facilitator confirms the design intent and relevant operating modes before applying suitable parameters and guidewords. The proposed node list is agreed during preparation and may be refined during the workshop where the team identifies a more effective study boundary.

Unique node number and title
Clearly marked P&ID boundaries
Defined design intent
Relevant process parameters
Applicable guidewords
Normal and abnormal operating modes
Interfaces with adjacent nodes
Drawing revision and traceability

Detailed HAZOP worksheet

Every Scenario Is Recorded with a Clear Audit Trail

The example worksheet shows a HAZOP node for a hydrogen generation system. The study begins with a process deviation such as No Flow, then records credible causes and consequences before assessing the risk both before and after safeguards.

The worksheet structure supports traceability from the initiating cause through to the final recommendation. It also identifies whether a scenario requires escalation to a more detailed Layer of Protection Analysis.

Node, parameter and deviation
Cause and consequence
Severity and likelihood
Risk before safeguards
Existing safeguards
Residual risk after safeguards
LOPA screening decision
Recommendation and study comment
Example HAZOP worksheet for a hydrogen generation system showing no-flow deviations, causes, consequences, severity and likelihood, risk before and after safeguards, LOPA screening, safeguards, recommendations and comments.
Example HAZOP worksheet for a hydrogen generation system. Click the image to open the full-size version. Study formats are adapted to the client’s risk matrix, document control system and reporting requirements.
Safety risk classification matrix combining consequence levels from none to catastrophic with likelihood categories from improbable to regular, producing negligible, ALARP and intolerable risk regions.
Example safety risk classification matrix. Consequence and likelihood are combined to classify risk as Negligible, ALARP or Intolerable. The matrix used for a study should be agreed with the client and aligned with the organisation’s risk criteria.

Risk ranking and decision support

Consistent Risk Classification and Demonstration of ALARP

The risk matrix provides a transparent basis for comparing scenarios and deciding where additional safeguards, further analysis or management attention are required. The example matrix combines consequence categories—from none through to catastrophic—with likelihood categories ranging from improbable to regular.

Scenarios within the ALARP region require a reasoned demonstration that further risk reduction measures have been considered and that additional measures would be grossly disproportionate to the benefit achieved. Intolerable scenarios require further risk reduction before the activity can be accepted.

Documented risk criteria
Pre- and post-safeguard ranking
Challenge of safeguard effectiveness
Further risk reduction options
Proportionate ALARP justification
Escalation to LOPA where required

ALARP Is More Than a Colour on the Risk Matrix

A defensible ALARP demonstration records the options considered, the effectiveness and practicability of additional controls, the reason for accepting or rejecting each option, and the responsibilities and timescales for agreed improvements.

Our facilitators encourage the team to consider the hierarchy of controls and the complete lifecycle of safeguards, including design, operation, inspection, testing, maintenance, proof testing, competence and management of change.

Prevent the initiating event Inherently safer design, inventory reduction, simplification, materials selection, reliable utilities and robust operating envelopes.
Detect and control deviations Instrumentation, alarms, trips, interlocks, operator response, diagnostics and safety instrumented functions.
Mitigate the consequence Containment, relief, ventilation, fire and gas detection, drainage, separation, emergency response and personal protection.
Important: A HAZOP risk ranking is not a substitute for detailed quantitative analysis. Scenarios involving high consequence, uncertainty, dependence on administrative controls or a need to verify independent protection layers can be referred to LOPA, SIL identification, consequence modelling or another focused study.

Facilitated by Experienced Process Safety Personnel

HAZID and HAZOP studies are facilitated by experienced personnel with strong practical experience in the energy sector, aerospace industry, hazardous chemical processing, waste treatment and effluent treatment systems.

This experience helps the workshop move beyond generic prompts and focus on credible equipment failures, process interactions, operating modes, human-system interfaces and safeguards that can be implemented and maintained in real facilities.

Energy and hydrogen systems Hydrogen production plants, electrolysers, hydrogen refuelling stations, compression, storage, distribution, vent systems and associated utilities.
Aerospace and advanced manufacturing Tank farms, chemical processing lines, process tanks, transfer systems, cleaning processes, hazardous materials and effluent treatment facilities.
Waste and environmental treatment Hazardous waste incineration plants, reagent dosing, combustion systems, off-gas treatment, wastewater and industrial effluent treatment plants.

Human performance in process safety

Human Factors Are Integrated into the Study

Process deviations are not caused only by equipment failure. Procedures, workload, interfaces, alarm design, access, communication, competence, staffing and maintainability can all influence whether a hazardous scenario is initiated, detected or successfully controlled.

HF

Human Factors Trained Facilitation

Our facilitators have completed Human Factors training through an IChemE course and use that knowledge to challenge assumptions about operator action, task reliability and human-system interaction.

01

Operator Response

Where a safeguard depends on human action, the study considers detection, diagnosis, available response time, workload, access to information, competing tasks and the clarity of the required response.

02

Procedures and Operating Modes

The review includes normal operation as well as start-up, shutdown, maintenance, isolation, sampling, cleaning, testing and foreseeable abnormal or temporary operating conditions.

03

Control Room and Alarm Interfaces

The team can examine alarm presentation, prioritisation, suppression, set-point rationale, control system indications and the potential for ambiguous or misleading information.

04

Maintenance and Testing

Safeguards are challenged for accessibility, testability, proof-test coverage, bypass management, restoration after maintenance and the possibility of common-cause or latent failures.

05

Organisational Controls

Competence, supervision, shift handover, contractor interfaces, permit-to-work, simultaneous operations and management of change are considered where they influence scenario likelihood or safeguard performance.

Sector experience

Typical Facilities and Process Systems

The facilitation approach is adapted to the process technology, hazard profile, project phase and operational context. Typical applications include new projects, modifications, packaged units, brownfield interfaces and revalidation of existing facilities.

Hydrogen and Electrolyser Plants

Electrolyser stacks, water treatment, gas-liquid separation, purification, drying, compression, storage, pressure control, venting, detection and emergency shutdown.

Hydrogen Refuelling Stations

Delivery, generation, compression, cascade storage, pre-cooling, dispensing, vehicle interfaces, pressure protection, vent systems and hazardous-area controls.

Hazardous Waste Incineration

Waste receipt, transfer and storage, burners, combustion chambers, auxiliary fuel, reagent systems, flue-gas treatment, residues, emissions and utility failures.

Aerospace Tank Farms

Bulk chemical storage, unloading, transfer, overfill protection, bunding, incompatible materials, vapour release, drainage, emergency isolation and distribution systems.

Chemical Processing Lines

Process baths and tanks, corrosive and highly toxic chemicals, heating, dosing, agitation, extraction, rinsing, cleaning, transfer and abnormal reaction scenarios.

Effluent Treatment Plants

Collection, segregation, neutralisation, precipitation, pH control, chemical dosing, gas generation, sludge handling, storage and discharge-quality protection.

Study preparation

Information Required for an Effective Workshop

The exact input package depends on the project stage. Missing or uncertain information does not always prevent a study, but assumptions and data gaps should be identified before the workshop so they can be managed transparently.

Typical HAZID Inputs

Project description, design basis, process overview, site and plot plans, inventories, preliminary flow diagrams, technology information, surrounding receptors, interfaces, environmental constraints and applicable risk criteria.

Best timing: when the project can still influence layout, technology, inventories and major design choices.

Typical HAZOP Inputs

Current P&IDs, preferably marked with proposed node boundaries, together with the process description, design and operating data, equipment information, control narrative, cause-and-effect charts, alarm and trip philosophy, relief information, utility details and operating procedures where available.

Best timing: when the design intent is sufficiently defined but recommendations can still be implemented efficiently.

Workshop Arrangements

Agreed scope, node list or HAZID categories, risk matrix, attendee roles, workshop schedule, document revision status, action ownership protocol and a suitable method for remote, hybrid or in-person participation.

Quality factor: continuity of the core team and access to the right technical specialists materially improve the study.

Multidisciplinary participation

The Workshop Team Matters

The facilitator provides the method and keeps the study systematic, but the quality of the output depends on combining design knowledge with practical operating experience. The core team should be proportionate to the system and should include the people able to explain the design intent, challenge failure scenarios and judge whether safeguards are realistic.

ExConform can support workshop planning, attendee selection, node preparation, pre-reading and alignment of the study with the client’s approval and action-management processes.

Independent facilitator / chair Leads the method, maintains pace and depth, challenges assumptions and protects consistency.
Study scribe / recorder Records discussions, safeguards, recommendations and decisions directly into the worksheet.
Process / technology engineer Explains chemistry, process conditions, design intent, operating envelope and process interactions.
Operations representative Provides practical knowledge of start-up, shutdown, abnormal operation, access and operator response.
Control and instrumentation engineer Explains alarms, trips, interlocks, logic, independence, failure modes and control-system behaviour.
Mechanical / package specialist Supports equipment, piping, pressure protection, materials, package interfaces and mechanical integrity.
Maintenance and inspection Challenges testability, proof testing, bypasses, restoration, accessibility and degradation mechanisms.
Process safety / HSE specialist Supports hazard interpretation, risk criteria, consequence assessment and follow-on study requirements.

HAZID / HAZOP Deliverables

Deliverables are structured to provide a usable study record, clear action ownership and a complete technical basis for project assurance, design development, operational risk management and future revalidation.

HAZID or HAZOP workshop preparation and facilitation
Study scope, boundaries, assumptions and methodology
Node list, marked-up P&IDs, design intent and guideword structure
Live recording of workshop findings in structured worksheets
Causes, consequences and affected receptors
Existing safeguards and safeguard challenge
Pre- and post-safeguard risk ranking
ALARP considerations and further risk reduction options
Identification of scenarios requiring LOPA or another specialist study
Prioritised action summary with recommended owners and timescales
Complete HAZID / HAZOP Study Report
All findings, recommendations, decisions and study comments
Workshop recording: this refers to structured, live recording of the team’s discussions and findings in the study worksheet. Audio or video recording is not assumed and would only be used where specifically agreed by all parties and permitted by the client’s information-security requirements.

When to commission a study

Typical Project and Operational Triggers

HAZID and HAZOP are not limited to greenfield projects. They can support design assurance, modification control, commissioning readiness and the periodic review of existing facilities.

Concept and FEED

HAZID to identify major hazards, compare concepts, influence layout and determine the studies required as the design develops.

Detailed Design

HAZOP when P&IDs and control arrangements are mature enough for a systematic node-by-node review.

Design Change

Focused HAZID or HAZOP for new equipment, capacity increases, process changes, new chemicals, control changes or altered operating envelopes.

Pre-Start-Up Assurance

Review of open recommendations, design changes made after the study and the readiness of safety-critical safeguards before operation.

Operational Revalidation

Periodic confirmation that the previous study remains valid and that plant changes, incidents, degradation and operating experience have been considered.

Incident and Learning Review

Targeted re-examination of scenarios where incidents, near misses, audit findings or industry learning challenge previous assumptions or safeguards.

Common questions

HAZID and HAZOP FAQs

What is the difference between a HAZID and a HAZOP?

A HAZID is a broad hazard-identification study suited to early project phases and high-level systems or site interfaces. A HAZOP is a detailed, guideword-based study normally performed when the process design and operating intent are sufficiently mature for node-by-node examination.

Can a HAZOP be completed before the P&IDs are final?

Yes, provided the design is sufficiently developed and the document status is understood. The benefit of early review must be balanced against the risk of repeated work. Design gaps and assumptions should be recorded, and significant changes after the workshop should be screened for re-HAZOP.

Does a HAZOP demonstrate that a design is safe?

A HAZOP provides structured evidence that deviations, causes, consequences and safeguards have been examined by a competent team. It does not replace good engineering, verification, quantitative analysis, commissioning controls or lifecycle management of safeguards.

When is LOPA required after a HAZOP?

LOPA may be appropriate where a scenario remains significant, where the adequacy or independence of protection layers must be demonstrated, where a safety instrumented function may be required, or where the organisation’s risk criteria specify escalation to semi-quantitative analysis.

Can the study be facilitated remotely?

Yes. Remote or hybrid studies can be effective when documents are well controlled, the platform supports clear drawing review, participants have reliable access and the sessions are planned to manage attention and fatigue. In-person workshops may be preferred for complex systems, site walkdowns or teams unfamiliar with the process.

Planning a HAZID or HAZOP Study?

We can support study planning, document readiness, node definition, multidisciplinary workshop facilitation, risk ranking, ALARP review, action prioritisation and complete reporting for new projects, modifications and operating facilities.

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