<link href="https://fonts.googleapis.com/css2?family=Caveat:wght@500;700&family=JetBrains+Mono:wght@400;500;600&family=Plus+Jakarta+Sans:wght@600;700;800&display=swap" rel="stylesheet" /> Skip to main contentEngineering Courses, Mentoring & Jobs | EveryEng
Health, Safety & Environment (HSE) Fundamentals banner

Health, Safety & Environment (HSE) Fundamentals

Health, Safety & Environment (HSE) Fundamentals banner
Live online Beginner

Health, Safety & Environment (HSE) Fundamentals

4(8)
1 enrolled
1237 views
COMPLETED

Tell us and we’ll notify you when the next batch is scheduled.

6 hrs
-
English
1237 views
kashif jameel
kashif jameelHSE / Process Safety Expert
  • 7-day money-back guarantee
  • Session recordings included
  • Certificate of completion
Volume pricing for groups of 5+

Why enroll

Why Join This Course?

Career Advancement – Enhance your qualifications for HSE roles such as HSE Officer, HSE Manager, and Safety Engineer.
Practical Learning – Learn through real-world case studies, risk assessment techniques, and incident analysis.
Expert-Led Training – Get insights from an experienced CSP®-certified safety professional.
Industry-Relevant Knowledge – Gain essential HSE skills aligned with global standards and best practices.
Networking Opportunities – Connect with like-minded professionals and expand your HSE network.

Is this course for you?

You should take this if

  • You work in Oil & Gas Upstream or Energy & Utilities
  • You're a Chemical & Process / Health, Safety & Environmental professional
  • You prefer live, instructor-led training with Q&A

You should skip if

  • You need a different specialisation outside Chemical & Process
  • You need fully self-paced, on-demand content

Course details

Course suitable for

Key topics covered

Module 1: Introduction to HSE

  • Importance of HSE in the Workplace

  • Roles & Responsibilities of HSE Professionals

  • HSE Regulations & Compliance

Module 2: Hazard Identification & Risk Assessment

  • Risk Assessment Methodologies (Qualitative & Quantitative)

  • Process Hazard Analysis (PHA)

Module 3: Workplace Safety & Incident Prevention

  • Safe Work Practices & Procedures

  • Permit-to-Work (PTW) System

  • Lockout/Tagout (LOTO) & Energy Isolation

  • Personal Protective Equipment (PPE) & Safety Culture

Module 4: Incident Investigation & Root Cause Analysis

  • Steps in Incident Investigation

  • Root Cause Analysis Techniques (5 Whys, Fishbone Diagram)

  • Reporting & Learning from Incidents

Module 5: Emergency Preparedness & Response

  • Fire Safety & Fire Prevention

  • Emergency Response Plans & Drills

  • First Aid & Medical Emergency Management

Module 6: Environmental Management & Sustainability

  • Environmental Aspects & Impacts in Industries

  • Waste Management & Pollution Control

    Module 7: HSE Leadership & Behavioral Safety

  • Building a Positive Safety Culture

  • Human Factors & Safety Behavior

  • Leadership Role in HSE Performance Improvement

Opportunities that await you!

Career opportunities

Training details

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

Live session

Starts

Mon, Apr 21, 2025

3:00 PM UTC· your timezone

Duration

2 hours per day

3 days total

COMPLETED

-

Questions and Answers

A: 19.5% O2 is the boundary that makes this uncomfortable. Personal H2S monitors only sense H2S concentration; they don't measure oxygen. Even with alarms working, nitrogen displacement can drop oxygen below safe limits without triggering anything on the H2S device.

A: 85% HH level is the hard edge here. Continuing circulation keeps generating condensate and risks liquid carryover to flare if HH is crossed. Stopping the heat input removes the source term; draining to atmosphere introduces ignition and exposure risk.

A: 0 LEL with a live signal narrows it. During start-up, ventilation often lags, starving catalytic sensors of oxygen and flow. They read low until airflow stabilizes; poisoning or scaling wouldn't self-correct that cleanly in minutes.

A: 1.1x MAWP sets the relief boundary, not liquid compressibility. A blocked-in liquid can see pressure rise from thermal expansion without vapor generation, and the PSV sized for fire vapor won't relieve that mode fast enough.