LNG & Gas Processing
LNG Terminals, Regasification & Bunkering Safety
A three-day programme for terminal, marine and HSE teams covering import terminal and FSRU operation, send-out gas quality, LNG bunkering transfer safety and cryogenic hazard control.
Industry focus: Petrochemical & Manufacturing Plants
Who Should Attend
Designed for these roles
- Import terminal and FSRU operations and technical staff
- Marine, jetty and terminal loading master personnel
- HSE, process safety and emergency response leads at gas facilities
- Bunkering, port and small-scale LNG project teams across Southeast Asia
Delivery formats
- Customised in-house training at your plant or office
- Public classroom delivery, subject to schedule
- Live online delivery where suitable
- Recommended group size: 8–20 participants
Problems Solved
What this course fixes
Cryogenic hazards treated with general hydrocarbon safety thinking
Ship-shore transfer delays and disputes caused by compatibility gaps
Send-out gas quality complaints from downstream users and grid operators
Bunkering operations scaling faster than the competency of the people running them
Learning Outcomes
What participants can do after the programme
Outcomes are written as tasks, not topics — so managers can verify capability back at work.
- Describe terminal and FSRU configurations, vaporiser types and send-out control
- Apply cryogenic hazard controls: brittle fracture, rapid phase transition, vapour dispersion
- Run ship-shore compatibility, ESD and custody interface checks correctly
- Plan an LNG bunkering operation with a defensible safety and simultaneous-operations case
- Respond to LNG spill, leak and vapour cloud scenarios using correct techniques
Course Outline
Detailed programme content
Day 1 — Terminals, FSRUs & Send-Out
- Import terminal and FSRU layouts, storage, pumps and vaporisers
- Open rack, submerged combustion and intermediate fluid vaporiser selection
- Send-out pressure and flow control, metering and grid interface requirements
- Gas quality, nitrogen ballasting, Wobbe index and interchangeability limits
Day 2 — Cryogenic Hazards & Process Safety
- LNG properties, vapour behaviour and dispersion in tropical conditions
- Brittle fracture, cold embrittlement and cryogenic spill protection design
- Rapid phase transition, rollover and confined vapour hazards
- Fire and gas detection, ESD philosophy and emergency response practice
- Exercise: hazard walkdown of a jetty and transfer arrangement
Day 3 — Bunkering & Transfer Operations
- Bunkering modes: truck-to-ship, ship-to-ship and shore-to-ship
- Ship-shore compatibility, transfer procedures and checklists
- Simultaneous operations assessment and safety and security zones
- Custody transfer, cooldown, purging, gassing-up and inerting sequences
- Workshop: build a bunkering operation plan and challenge it as a reviewer
Practical Work
Practical exercises and case studies
Sessions are built around calculations, data interpretation and technical decisions. Case material is generic or anonymised — no client-confidential project data is used.
Vaporiser selection exercise for a given seawater temperature and send-out profile
Hazard walkdown of a jetty, transfer arm and bunkering arrangement
Ship-shore compatibility and pre-transfer checklist exercise
Emergency scenario drill: LNG spill and vapour cloud response decisions
Trainer Profile
Delivered by Ir. Hafiz Rahman
Lead Trainer — Pressure Equipment & ASME Codes
22 years industry experience
Hafiz has spent his career between the design office and the plant floor — sizing shells and heads in the morning, walking down repairs with an inspector in the afternoon. He teaches code work the way it is actually used: calculation sheets, nameplate data, and repair decisions that must survive an audit.
Real project exposure
- Pressure vessel and heat exchanger design review for a Pengerang refinery expansion
- Fitness-for-service assessment on ageing separators at an East Malaysia gas terminal
- Turnaround inspection planning for a Kerteh petrochemical complex
Certifications
- ASME Section VIII Div. 1 Design
- API 510 Pressure Vessel Inspector
- BEM Registered Professional Engineer
Trainer allocation is confirmed in your proposal. Substitute trainers hold equivalent certification and sector experience.
Next Step
Run this programme for your team
We will confirm available dates, trainer, duration and HRD Corp claimable investment — and adjust the outline to your equipment and standards at no extra cost.
No obligation. Proposals include HRD Corp claim guidance.
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