Module 5

Floating LNG (FLNG)

Overview

Take the gas plant to the gas. An FLNG vessel is a hull with the entire liquefaction plant, storage and offloading built on top, moored over the field for 20–25 years. No pipeline to shore, no onshore site, no jetty.

FLNG — nameplate
Capacity0.5–3.6 mtpa LNG per vessel. Prelude is 3.6 mtpa LNG plus 1.3 mtpa condensate and 0.4 mtpa LPG
HullNewbuild (Prelude: 488 m long, 74 m wide, ~600,000 t displaced when loaded) or converted LNG carrier (Golar Hilli, Gimi)
StorageIn-hull membrane or SPB tanks, 100,000–220,000 m³ LNG plus condensate and LPG tanks
MooringInternal turret with chains and piles (cyclone-rated), or spread mooring in benign waters
RefrigerationDMR (Prelude), nitrogen expander (PFLNG Satu, Coral Sul), PRICO (Golar conversions)
OffloadingSide-by-side to a conventional LNG carrier via loading arms, or tandem (bow-to-stern) with cryogenic hoses in rough seas
Design life on station20–25 years without dry-docking
Crew100–250 people on board, FIFO by helicopter
Loading the floating LNG process deck…

Why FLNG exists

Plenty of gas sits in fields that are too small, too far offshore, or too far from any coast to justify a pipeline and an onshore plant. Prelude's field is about 475 km north-east of Broome — a pipeline to shore plus a greenfield plant on the Kimberley coast was studied and rejected on cost and environmental grounds. FLNG avoids the pipeline, the onshore land acquisition and approvals, the jetty and the dredging. When the field is depleted the vessel can, in principle, be moved to another one.

It also compresses the schedule. The hull and topsides are built in a shipyard (Prelude at Samsung Heavy Industries in Korea, Coral Sul at Samsung too), which is the most controlled construction environment in the industry. The whole plant is commissioned as far as possible at the yard before the tow.

Anatomy of an FLNG vessel

  1. Subsea and risers. Wells on the seabed produce through flowlines to the turret. Flexible risers carry gas, condensate and MEG up to the vessel. At Prelude the turret is 93 m tall and the vessel weathervanes around it, always facing into the weather.
  2. Inlet and separation. Gas, condensate and water are separated on deck. Condensate is stabilised and stored in the hull. Water is treated and discharged. Everything a baseload plant does in its slug catcher and stabiliser happens here, in a fraction of the space.
  3. Gas treatment. Amine CO₂ removal, mol sieve dehydration, mercury removal — the same chemistry as onshore, but the columns are designed to work with the vessel tilted and rolling. Structured packing replaces trays because trays malfunction when the liquid sloshes.
  4. Liquefaction. Prelude uses Shell's DMR process with two mixed refrigerant loops and a spiral-wound exchanger; there's no propane, so no large pressurised LPG inventory on deck. Nitrogen-expander designs are chosen by others precisely because the refrigerant is inert — on a vessel where you can't walk away from a fire, that matters. Heat exchangers are designed and tested for tilt; spiral-wound units tolerate motion better than plate-fin.
  5. Storage in the hull. LNG goes down into cryogenic tanks inside the hull — membrane tanks (like an LNG carrier) or self-supporting prismatic (SPB) tanks that resist sloshing at any fill level. Sloshing is a real structural load: partly-filled membrane tanks in a seaway can hammer the insulation, so fill levels and sea states are managed together.
  6. Offloading. An LNG carrier moors alongside (side-by-side) every week or so and loads through articulated arms that can follow the relative motion of two vessels. In harsher seas, tandem offloading with the carrier trailing behind uses floating cryogenic hoses. Condensate is offloaded to tankers separately.
  7. Utilities and people. Power generation (Prelude: steam turbines and gas turbines producing well over 100 MW), seawater cooling drawn from depth through risers, flare tower, living quarters, helideck, lifeboats. The vessel is a town and a refinery at once.

What's different from onshore

IssueOnshoreFLNG
SpaceHectares; equipment spaced out for safetyEverything within a hull footprint; multi-level decks; safety gaps are engineered with blast walls and layout studies
MotionNoneRoll, pitch and heave affect distillation columns, exchangers, tank sloshing, crane ops and offloading windows
WeatherShut in for cyclones, shelter on landDesigned to stay on station through a Category 5 cyclone; crew may be evacuated but the vessel rides it out on the turret
MaintenanceTurnarounds with thousands of contractorsEverything by helicopter and supply boat; heavy spares must fit the deck cranes; 25 years without dry dock means marine systems are designed for in-place inspection
CoolingAir fin-fans (Australia) or seawaterCold deep seawater — a big efficiency advantage over Karratha air cooling
Regulation (Australia)State WHS and dangerous goods regimesNOPSEMA under the Offshore Petroleum and Greenhouse Gas Storage Act, plus marine class rules — a different safety case system
RefrigerantPropane and MR inventories are normalMinimised; nitrogen or DMR preferred; no LPG storage on deck if avoidable

The FLNG fleet

VesselOperator / locationCapacityTypeNotes
PFLNG SatuPetronas, Malaysia1.2 mtpaNewbuild, nitrogen expanderFirst FLNG cargo in the world, 2017; has already been moved to a second field
PreludeShell, Browse Basin, WA3.6 mtpa LNGNewbuild, DMRLargest floating structure ever built; first cargo 2019; troubled early years with power system trips and an extended shutdown after a 2021 incident
Hilli EpiseyoGolar / Perenco, Cameroon2.4 mtpaConverted 1975-built LNG carrier, PRICOShowed conversion could be done for a fraction of newbuild cost
PFLNG DuaPetronas, Malaysia1.5 mtpaNewbuild, deepwaterExternal turret, 1,300 m water depth
Coral SulEni, Mozambique3.4 mtpaNewbuild, dual nitrogen expanderFirst cargo 2022; often cited as the smooth start-up FLNG
GimiGolar / BP, Mauritania-Senegal2.5 mtpaConversionGreater Tortue Ahmeyim project, first cargo 2025
Tango FLNGExmar / Eni, Congo0.6 mtpaBarge-basedShows the small end of the concept

Newbuild vs conversion

Newbuild (Prelude, Coral Sul, PFLNG)

  • Hull designed for the topsides load and 25 years on station.
  • Larger capacity and more storage.
  • Five-plus years and many billions to build.
  • Prelude's cost was never officially disclosed; estimates run US$12–17 billion.

Conversion (Hilli, Gimi, Golar fleet)

  • Take an old Moss-sphere LNG carrier, strip it, build a plant on deck.
  • Roughly US$1–2 billion, 2–3 years.
  • Capacity capped by the hull; usually 2–3 mtpa.
  • Simpler PRICO or nitrogen liquefaction in modular blocks.

Operating an FLNG vessel

Life on board is offshore platform life with a refinery attached. Crews rotate FIFO by helicopter on a roster measured in weeks. The operating challenges that don't exist onshore: managing tank fill levels against sea state to control sloshing; scheduling offloading around weather windows; keeping the marine systems (ballast, mooring chain tension, hull inspection) in step with the process plant; and the fact that any significant repair means bringing people and parts across hundreds of kilometres of ocean. Prelude's early years showed that power system reliability is the crux — when the vessel loses power, every system from process to hotel goes dark, and the 2021 event that left the crew without full power for days led to a lengthy regulator-directed shutdown.

Safety specifics for FLNG

There's nowhere to go. Escape, evacuation and rescue design assumes the crew may have to shelter in a temporary refuge and leave by lifeboat in a cyclone-affected sea. Layout uses the hull length to separate the accommodation (at one end) from the process (along the deck) with the flare at the far end and blast walls between. Simultaneous operations — an LNG carrier alongside, helicopters, supply boats, hot work — are controlled through a permit system tighter than any onshore plant. Cryogenic spills onto the deck are a hull integrity issue as well as a personnel one: carbon steel decking exposed to −162 °C can crack, so spill trays, drip trays and stainless or concrete protection cover the LNG zones.

Self-check — Module 5
  1. Give two reasons a developer chooses FLNG over a pipeline and onshore plant.
  2. Why do FLNG designers prefer nitrogen expander or DMR over C3MR?
  3. What is sloshing and why does it constrain operations?
  4. What does "weathervane" mean for a turret-moored vessel?
  5. Which regulator oversees FLNG safety in Australian Commonwealth waters?