
The Full Process Explained — From Planning to Close-Out
Hazard Identification, universally referred to as HAZID, is the structured study that sits at the very start of a facility’s process safety lifecycle. Long before a HAZOP examines individual control loops or a QRA quantifies risk in numbers, HAZID asks the simplest and most important question a project can ask: what could go wrong here, and how badly? For oil and gas fabricators, EPC contractors, and operators pursuing ASME certification or Saudi Aramco AVL registration, a well-executed HAZID is not a formality — it is the foundation that every downstream safety study, engineering decision, and audit trail is built on.
This guide walks through the complete HAZID process as it is actually practiced on oil and gas projects: who should be in the room, how the study is structured, what guidewords and checklists are used, how risk is ranked, and what a defensible HAZID report needs to contain.
What Is HAZID?
HAZID (Hazard Identification) is a qualitative, team-based risk assessment technique used to identify hazards associated with a system, facility, or activity at the earliest practical stage — typically during conceptual or front-end engineering design (FEED). Unlike HAZOP, which drills into process deviations node by node using a piping and instrumentation diagram (P&ID), HAZID takes a broader view: it looks at the whole facility, its surroundings, and the activities around it, using structured guidewords and checklists rather than deviation analysis.
The output of a HAZID is a register of identified hazards, an initial qualitative risk ranking for each one, and a set of recommendations to eliminate or reduce the risk — feeding directly into detailed design, layout decisions, and later safety studies.
HAZID vs. HAZOP vs. QRA — Key Differences
These three studies are often confused because they sit in the same process safety family, but they answer different questions at different project stages.
- HAZID — “What hazards exist?” Broad-brush, conducted early (concept/FEED), covers the whole facility including siting, access, and external hazards.
- HAZOP — “What happens if this parameter deviates?” Detailed, node-by-node review of P&IDs using guidewords like MORE, LESS, NO, REVERSE; conducted once design is mature.
- QRA — “How likely, and how severe, in numbers?” Quantitative risk assessment that calculates individual and societal risk levels, often used to demonstrate ALARP (As Low As Reasonably Practicable).
In practice, HAZID findings feed into HAZOP scope and QRA scenario selection — skipping HAZID often means HAZOP misses hazards that were never process-related to begin with, such as vessel siting, dropped-object risk, or vehicle access during an emergency.
When HAZID Is Conducted in a Project Lifecycle
Timing is what makes HAZID valuable. Conducted too late, its recommendations become expensive rework instead of free design input.
- Conceptual design / pre-FEED — first HAZID, focused on siting, layout philosophy, and major hazard scenarios.
- FEED (Front-End Engineering Design) — the primary HAZID, using preliminary P&IDs, plot plans, and process descriptions.
- Detailed design — HAZID revalidation if scope, layout, or process conditions changed materially.
- Pre-commissioning / modification — a focused HAZID for management-of-change (MOC) items or brownfield tie-ins.
The HAZID Team — Who Should Be in the Room
HAZID is a workshop-based technique, not a desk exercise. Its value depends entirely on the breadth and seniority of the team assembled around the table.
- HAZID Chairman/Facilitator — independent, trained in hazard identification techniques, controls the session and guideword sequence.
- Scribe — records hazards, discussion, and actions in real time into the HAZID register.
- Process Engineer — explains process intent, chemistry, and operating conditions.
- Process Safety / HSE Engineer — brings major accident hazard experience and regulatory context.
- Operations Representative — grounds the discussion in how the facility will actually be run and accessed.
- Mechanical / Piping / Layout Engineer — addresses siting, spacing, and equipment arrangement hazards.
- Instrumentation & Control Engineer — covers safeguarding, shutdown systems, and alarm philosophy.
- Client/Owner Representative — confirms design basis and accepts or challenges recommendations.
Step-by-Step HAZID Process
Step 1: Planning and Scope Definition
The facilitator defines the study boundary (battery limits), gathers reference documents — process description, plot plan, PFDs, preliminary P&IDs, site data — and agrees the guideword set and hazard categories to be used. A kickoff agenda and attendee list are issued in advance so the right disciplines attend.
Step 2: System / Node Breakdown
The facility is divided into manageable nodes or areas — not by P&ID line number as in HAZOP, but by physical or functional zones: process area, storage/tankage, utilities, flare system, loading facilities, control room, site access roads, and so on. Each node is examined in turn.
Step 3: Guideword-Based Hazard Identification
For each node, the team works through a structured checklist of hazard categories and guidewords, capturing every credible hazard, its potential cause, and its potential consequence. Typical guideword/hazard categories include:
- Process hazards — fire, explosion, toxic release, loss of containment
- Mechanical hazards — rotating equipment, dropped objects, lifting operations
- Utility hazards — loss of power, instrument air, cooling, or nitrogen
- External hazards — extreme weather, seismic activity, nearby facilities, third-party interference
- Human factors — access/egress, manual handling, operator error, ergonomics
- Environmental hazards — spill to ground/sea, emissions, waste handling
- Security — unauthorized access, sabotage, vehicle-borne threats
Each hazard is logged with its causes, existing safeguards, and potential consequences before any risk ranking is applied — ranking too early biases the discussion toward “likely” hazards and causes teams to under-record low-probability, high-consequence events.
Step 4: Risk Ranking (Likelihood × Severity)
Once a hazard, its causes, and existing safeguards are documented, the team assigns a qualitative likelihood and severity rating using an agreed risk matrix, producing an initial risk ranking of Low, Medium, High, or Extreme. This ranking is not the final word on risk — it screens which hazards need further quantitative study (QRA) or dedicated engineering attention.
| Likelihood \ Severity | 1 – Negligible | 2 – Minor | 3 – Moderate | 4 – Major | 5 – Catastrophic |
| 5 – Almost Certain | M | H | H | E | E |
| 4 – Likely | M | M | H | H | E |
| 3 – Possible | L | M | M | H | H |
| 2 – Unlikely | L | L | M | M | H |
| 1 – Rare | L | L | L | M | M |
Step 5: Recommendations and Action Tracking
For every Medium-and-above ranked hazard, the team proposes a recommendation following the hierarchy of controls: eliminate, substitute, engineer, administer, or protect (PPE) — in that order of preference. Each recommendation is assigned an owner and a target close-out stage (FEED, detailed design, or pre-startup).
Step 6: Reporting and Close-Out
The facilitator issues a HAZID report containing the register, methodology, attendee list, risk matrix definition, and the full action list. Recommendations are tracked to close-out through an action tracking register, and unresolved items are formally carried forward into HAZOP or the project’s hazard and effects register — nothing is allowed to simply disappear between studies.
| Documentation Tip Auditors and Aramco AVL reviewers consistently flag HAZID reports where recommendations were “closed” without traceable evidence. Every closed action needs a linked reference — a drawing revision, a procedure number, or a design calculation — not just a status of “Done.” |
Regulatory and Standards Context
HAZID methodology is not defined by a single mandatory code, but its practice is shaped by a consistent set of international references that most oil and gas clients and certifying bodies expect to see cited in the study basis:
- ISO 17776 — Guidelines on tools and techniques for hazard identification and risk assessment (offshore/petroleum industry origin, widely applied onshore).
- API RP 14C / 14J — Analysis, design, and hazard evaluation of production facility safety systems.
- OSHA Process Safety Management (29 CFR 1910.119) — requires a documented process hazard analysis, of which HAZID is an accepted early-stage technique.
- Saudi Aramco Engineering Standards — Aramco projects and AVL-registered vendors are typically required to demonstrate a documented HAZID as part of the project safety file, aligned with Aramco’s own process safety management requirements.
- ASME B31.3 / Section VIII context — while ASME codes govern mechanical design and fabrication, HAZID findings often drive design-condition inputs (relief scenarios, MAWP considerations) that feed pressure equipment design.
Common Pitfalls That Weaken a HAZID Study
- Conducting HAZID too late, after layout and major equipment selection are frozen — recommendations become costly change orders instead of free design input.
- Assembling a team without operations or HSE representation, producing a study that reads well but misses real-world hazards.
- Ranking risk before hazards, causes, and safeguards are fully documented, which skews the register toward familiar hazards.
- Vague recommendations with no owner or close-out evidence, leaving auditors unable to verify anything was actually done.
- Treating HAZID as a one-time exercise instead of revalidating it after scope changes, layout revisions, or modifications.
HAZID Documentation Package — What a Complete Report Includes
A defensible HAZID package that will stand up to client review, third-party audit, or Aramco AVL assessment typically includes:
- Study basis and methodology statement, including guideword set and risk matrix definition
- Attendee list with roles and qualifications
- Reference document register (P&IDs, PFDs, plot plans, process descriptions used)
- Full hazard register (node, hazard, cause, consequence, safeguards, initial risk ranking)
- Recommendations and action tracking register with owners and target dates
- Close-out evidence log linking each action to a drawing, procedure, or calculation
- Executive summary highlighting High/Extreme ranked hazards carried forward to HAZOP or QRA
How FreeDocumentsHub Supports Your HAZID Documentation
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