LNG Liquefaction Plant Operations: Refrigeration Cycles, Cryogenic Equipment and Train Start-Up – Dubai, 23 Aug – 3 Sep 2027
DestinationDubai
Dates23 August – 3 September 2027
Reference707_19019
This session
23 Aug – 3 Sep 2027
This LNG Liquefaction Plant Operations: Refrigeration Cycles, Cryogenic Equipment and Train Start-Up session in Dubai runs from Monday 23 August to Friday 3 September 2027 (week 34, Q3 2027). It is the 2nd of 2 dates in Dubai in 2027, at a fee of 35,100 SAR, the same for each of them. Registration is open for this date. It is held in person at Five-star CBD venue.
DatesMonday 23 Aug – Friday 3 Sep 2027
Week34 of 2027
Duration12 days
Fee35,100 SAR
StatusOpen for registration
FormatIn person
VenueFive-star CBD venue
Programme overview
Introduction:
LNG liquefaction plant operations fail quietly before they fail loudly: a drifting mixed refrigerant composition, a warm-end pinch in the main cryogenic exchanger or a rushed cool-down cuts production, raises specific power and can crack cold equipment. This Core Concept course takes engineers inside the liquefaction train, from feed gas pre-treatment and refrigeration cycles through spiral-wound and plate-fin exchangers, compressors, tanks and boil-off gas, to cool-down, start-up, trips and hazards. Participants produce a Train Start-Up and Performance Review Plan for a case LNG plant.
Course Objectives:
Interpret LNG cooling curves, flash behaviour and feed gas composition to set the operating basis of a liquefaction train
Verify that acid gas, water, mercury and heavy hydrocarbon removal meets the limits that prevent freeze-out and exchanger damage
Compare propane-precooled mixed refrigerant, cascade, single mixed refrigerant and expander cycles on specific power, turndown and equipment count
Diagnose exchanger pinch points, refrigerant composition drift and compressor operating point problems from plant data
Plan cool-down, start-up, shutdown and trip response steps that protect cryogenic materials, tanks and personnel from LNG hazards
Produce a Train Start-Up and Performance Review Plan with efficiency and reliability KPIs for a case LNG plant
Target Audience:
Process engineers accountable for liquefaction train heat and material balance and refrigerant performance
Operations engineers and shift leads who run cool-down, start-up, rundown and shutdown of LNG trains
Mechanical and rotating equipment engineers responsible for refrigerant compressors, drivers and cryogenic exchangers
HSE and process safety engineers who assess cryogenic spill, rollover and vapour cloud scenarios at liquefaction sites
Reliability engineers who track train availability, trips and bad actors on cold section equipment
Course Outline:
Day 1: LNG Properties, Cryogenic Behaviour and Liquefaction Train Basis
Methane-Rich LNG Composition, Minus 162 Degree Boiling Point and Density Behaviour
Temperature-Enthalpy Cooling Curves for Precooling, Liquefaction and Subcooling Zones
Joule-Thomson Expansion, Flash Gas and End Flash Nitrogen Rejection
Feed Gas Composition Envelope: Lean, Rich and Nitrogen-Bearing Cases
Liquefaction Train Block Flow Diagram from Inlet Receiving to Rundown
Day 2: Feed Gas Pre-Treatment for the Cold Section
Amine Acid Gas Removal Unit and CO2 Slip Limits That Prevent Freeze-Out
Molecular Sieve Dehydration Bed Cycle, Regeneration Gas and Breakthrough Signs
Mercury Guard Bed Duty and Protection of Brazed Aluminium Equipment
Scrub Column and NGL Extraction to Remove Heavy Hydrocarbons and Benzene
Cold Section Entry Gas Specification Sheet
Day 3: Liquefaction Refrigeration Cycle Families
Propane-Precooled Mixed Refrigerant Cycle Flow Scheme and Pressure Levels
Pure-Component Cascade Cycle with Propane, Ethylene and Methane Loops
Single Mixed Refrigerant Cycle for Mid-Scale and Modular Trains
Nitrogen and Methane Expander Cycles for Small-Scale and Floating Units
Cycle Selection Matrix: Specific Power, Equipment Count and Turndown
Day 4: Cryogenic Heat Exchangers, Refrigerant Compressors and Train Control
Spiral-Wound Main Cryogenic Exchanger Bundles, Shell-Side Distribution and Warm-End Approach
Membrane Tank Corrugated Stainless Liner and Insulation Panel System
Tank Heat Leak, Boil-Off Rate Estimation and Stratification Monitoring
Boil-Off Gas Compressor, Fuel Gas Header and Reliquefaction Return Routes
Jetty Loading Arm Sequence, Vapour Return Balancing and Ship-Shore ESD Link
Day 7: LNG Hazards, Process Safety and Safeguards
Tank Rollover Mechanism, Density Layering and Mixing Countermeasures
Rapid Phase Transition on LNG Contact with Water and Spill Direction Channels
Vapour Cloud Dispersion, Pool Fire Radiation and Impoundment Basins
Cryogenic Burns, Asphyxiation Risk and Cold-Work Protective Equipment
Emergency Shutdown Hierarchy, Fire and Gas Detection and Cause and Effect Review
Day 8: Cryogenic Materials, Cool-Down, Start-Up and Shutdown Sequences
Cryogenic Materials: Austenitic Stainless, Nickel Steel and Aluminium Alloys
Piping Thermal Contraction, Cold Spring and Support Movement Checks
Controlled Cool-Down Rate Procedures for Exchangers, Piping and Tanks
Train Start-Up Sequence from Refrigerant Charging to First LNG Rundown
Planned Shutdown, Warm-Up, Deriming and Shift Handover Communication
Day 9: Trip Response, Troubleshooting and Liquefaction Performance KPIs
Compressor Trip, Driver Loss and Exchanger Flow Maldistribution Scenarios
Freeze-Out, Hydrate and Fouling Diagnosis from Differential Pressure Trends
Specific Power Consumption and Refrigeration Efficiency Tracking
Train Availability, Production Uptime and Flaring Loss KPIs
Reliability Bad Actor Ranking and Root Cause Analysis Records
Day 10: Capstone: Train Start-Up and Performance Review Plan
Capstone Brief: Case LNG Plant Train Data, Constraints and Outage History
Start-Up Plan Drafting: Cool-Down Steps, Hold Points and Permissives
Performance Review Section: KPI Baselines, Targets and Efficiency Actions
Hazard Safeguard and Trip Response Annex for the Case Train
Plan Presentation to a Peer Panel and Revision Log
Skills You Will Gain:
Cooling Curve Interpretation
Pre-Treatment Specification Checking
Refrigeration Cycle Comparison
Mixed Refrigerant Composition Control
Cryogenic Exchanger Diagnostics
Cool-Down Procedure Planning
Cryogenic Hazard Safeguarding
Liquefaction Performance Benchmarking
Why Attend This Course:
Return with a Train Start-Up and Performance Review Plan built on a case LNG plant and challenged by a peer panel
Read compressor maps, exchanger temperature profiles and refrigerant samples together to find lost production
Run cool-down and restart after a trip without thermal shock to spiral-wound bundles, plate-fin cores or cold piping
Compare liquefaction practice with process, rotating equipment and safety engineers from other trains and operators
Conclusion:
Steady LNG rundown depends on clean feed gas, a well-tuned refrigerant loop, healthy cryogenic exchangers and compressors, and disciplined cool-down and restart. Week one covers LNG properties, pre-treatment, refrigeration cycle families, exchangers, compressors and control, then tests them on a case train. Week two adds tanks and boil-off gas, the loading interface, cryogenic hazards, materials, start-up and shutdown sequences, trip troubleshooting and performance KPIs. The final day produces a Train Start-Up and Performance Review Plan for a case LNG plant.
LNG Liquefaction Plant Operations: Refrigeration Cycles, Cryogenic Equipment and Train Start-Up runs in Dubai over 12 days, with 2 upcoming dates in Dubai. The course fee is 35,100 SAR.
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