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Hazard Identification and Risk Assessment (HIRA)

Hazard Identification and Risk Assessment (HIRA) banner
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Hazard Identification and Risk Assessment (HIRA)

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3015 views
Team EveryEng
Team EveryEngMechanical Engineering
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

Why enroll

Elevate your career in safety management with expertise in Hazard Identification and Risk Assessment (HIRA)! This specialized course empowers professionals to identify, assess, and mitigate risks in various industries, ensuring a safe working environment. Mastering HIRA skills qualifies you for roles like Safety Manager, Risk Assessment Specialist, or Compliance Officer, and enhances your career prospects with top companies like Shell, Total, or BP. With HIRA expertise, you'll drive business continuity, reduce accidents, and promote a culture of safety excellence, positioning yourself for leadership roles and advanced certifications.

What enrolled engineers say

6 verified reviews
  • May 3, 2026

    Felt like sitting in on a senior engineer’s whiteboard run-through, not a slide dump. The bow-tie walkthrough in Module 3 where a valve failure escalates into a permit-to-work miss stuck; mapping causes to controls mirrored how we review incidents. I’ve already applied the risk matrix calibration to a prod change review, linking hazards to infra controls before opening a PR; it fit our CI checks. Mostly useful, though I wasn’t sold on the generic scoring scales and wished for more on contractor handoffs in oilgas.

    Mohammed S. Verified
  • May 3, 2026

    The HIRA walkthrough in Chapter 3’s risk-matrix calibration with the chlorine unloading example stuck—mapping severity vs likelihood felt like a PR review you could use in prod. Takeaway: it closes gaps for engineers into safety/energyutilities, though I wasn't sold on the bow-tie section and wished there was more on tying controls to obs and CI.

    Alekhya V. Verified
  • May 3, 2026

    A few slides in module 4 dragged, and the labs assume your org already has a hazard register set up. Past that, the reasoning behind the examples mostly held up when I sanity-checked them against real jobs. The bow-tie example in Section 3.2 around permit-to-work was the sticky bit for me; clear assumptions, no hand-waving. It's practical in a freelancer way: helps tighten arch decisions without overbuilding infra or slowing prod. I liked how they tied risk ranking back to actual change control instead of theory. Works if you’re bouncing between clients in energy utilities or oilgas and need a fast mental model. helps with day-to-day calls, not slideware.

    Muhammad Adan A. Verified

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream or Pharmaceutical & Healthcare
  • You're a Health, Safety & Environmental / Quality & Management Standards professional
  • You prefer live, instructor-led training with Q&A

You should skip if

  • You need a different specialisation outside Health, Safety & Environmental
  • You need fully self-paced, on-demand content

Course details

Course suitable for

Key topics covered

       Overview of HIRA

       Roles & Responsibility

       Hazard vs Risk

       5 Phase Methodology

       Risk Evaluation

       Activities, Task and Steps

Opportunities that await you!

Career opportunities

Training details

This is a live course that has a scheduled start date.

COMPLETED

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Questions and Answers

A: That's the most common mistake — chasing controls when the hydraulics are screaming. A fouled mesh drives DP up, strips less liquid, and pushes droplets downstream without touching inlet conditions. Level tuning would show oscillation without a steady DP climb, and a small gas valve doesn't load the mist pad this way.

A: That's the classic trap — arguing SIL math before checking physical reality. If the hardware follows the P&ID, gas detection could hold the valve open during a leak. Production loss hurts, but this mismatch drives consequence severity, not just availability or paperwork.

A: That's where instinct gets people hurt — dumping liquid or choking wells shifts the problem upstream. Controlled gas letdown addresses the overpressure driver while keeping the PSV in a benign thermal regime. Bypasses and rapid inflow cuts add new failure paths under PTW congestion.

A: That's the usual slip — forgetting when the multiplier applies. Base risk is 12, then SIMOPS pushes it higher. Dropping the factor or applying it to only one axis understates exposure during concurrent permits.