FIRETECH ENGINEERING Engineering & Digital · European Union

Insights · Megaproject of the week · 14.09.2026

Electrify the liquefaction, and the governing fire moves into the electrical building

Papua LNG cleared its last contractual milestones before FID on 7 September, with EPC tendering closed and operatorship passing to ExxonMobil. The plant will drive its refrigerant compressors with electric motors instead of gas turbines — a decision that removes the classic LNG ignition source and puts a substation-sized fire load on the critical path instead.

A coastal liquefaction plant at dusk, with cryogenic tanks, pipe racks and a large windowless electrical building lit from within
Illustration generated for this article. Not a photograph of Papua LNG or of any facility engineered by Firetech Engineering BG.

Project data

ProjectPapua LNG — ExxonMobil operator on completion of the transfer; TotalEnergies 20%, Santos 21.0%, ENEOS Xplora 2.4%, Kumul Petroleum and MRDC 22.5%
LocationCaution Bay, near Port Moresby, Papua New Guinea
Scale5.6 Mtpa of LNG; 6 Mtpa total liquefaction capacity including 2 Mtpa tolled through the existing PNG LNG trains
LiquefactionThree new electrified (eLNG) trains; electric motors rather than gas turbines drive the refrigerant compressors
UpstreamElk and Antelope fields, Gulf Province, about 360 km north-west; 11 wells, one of them for CO2 reinjection
Pipeline320 km network, about 60 km of it onshore
Capital expenditureAround US$14 billion, after close to US$4 billion of savings since 2024
MilestoneEPC tendering completed and operatorship transferred to ExxonMobil, 7 September 2026

What happened

On 7 September TotalEnergies announced that Papua LNG has “achieved major contractual and commercial milestones, marking decisive steps towards a Final Investment Decision”. EPC tendering is closed, and operatorship passes to ExxonMobil, operator of the neighbouring PNG LNG, while TotalEnergies keeps 20% and its offtake share. Redesign and rebidding since 2024 have taken “close to US$ 4 billion” out of the estimate, bringing capital expenditure to “around US$ 14 billion” against “a total production of 5.6 Mtpa”.

The engineering line sits further down. The venture describes three new electrified — “eLNG” — trains at Caution Bay, taking total liquefaction capacity to 6 Mtpa including 2 Mtpa tolled through the existing PNG LNG trains, fed from the Elk and Antelope fields by a 320 km pipeline network, with one of eleven wells reinjecting about 1 Mt of native CO2 a year. The preferred EPC contractor puts it plainly: “electric motors — rather than conventional gas turbines — drive the refrigerant compressors.”

Analysis: the ignition sources leave, the load does not

Electrifying liquefaction is announced as a carbon decision. In fire engineering it is a redistribution: it moves the largest ignition sources out of the process area and concentrates an unfamiliar fire load in buildings that used to be secondary.

Taking out the gas turbines takes out half the classic scenario. A mechanical-drive train puts turbine exhausts, hot casings and large lubricating-oil inventories inside or beside a classified area, and much of the layout exists to keep a release and a hot surface apart. Electric drive breaks that pairing. What remains is the release without an ignition source conveniently next to it, which shifts the weight of the design onto dispersion rather than the jet fire — a different governing case, and a different argument to make to the insurer.

In exchange the plant acquires a substation-sized fire load on the critical path. Compression at this scale means high-voltage motors, converter and variable-speed drive rooms, converter transformers, switchgear halls, and several times the cable volume of a mechanical-drive plant. The scenarios are ordinary — transformer oil, arc flash, dense cable routes — and so are the answers. What is new is their position. Three trains behind one electrical backbone makes this a common-mode question: a fire in one electrical building can idle capacity well beyond the equipment it damages, and delivery times for large motors and HV switchgear are not measured in weeks.

The purge and the penetration are where two disciplines miss each other. Large machines next to a classified area raise protection-concept questions: pressurised enclosures, purge integrity, the action on loss of purge and who is authorised to take it. Penetrations between a safe-area electrical building and the process are at once a gas path and a fire path. Area classification to IEC 60079-10-1 and passive fire protection are usually drawn by different people, at different times.

Why this reaches European projects

Electrification of process drivers is the direction European projects are already being pushed. What differs is the frame it lands in: Seveso III where inventories justify it; ATEX in both of its directions — equipment, and the protection of workers — which is where very large electric machines and their enclosures sit; the Construction Products Regulation for what is built into the works, cable above all; the EN 1473 frame for onshore LNG installations; and an insurer who reads the electrical building as the single point of loss.

The published material says what drives the compressors. It does not say what generates the electricity — and that decides whether a power block with its own combustion, fuel gas and oil inventories stands inside the fence, in which case much of the hazard removed from the train is merely relocated a few hundred metres.

Before an electrified concept is frozen, the questions are narrow. Which single fire takes more than one train off line. Whether drive and converter rooms are separated by distance, by construction, or only by a door. How penetrations between the electrical buildings and the process are sealed against smoke and against gas. And what fire water duty the site must hold once the governing scenario is electrical rather than hydrocarbon.

Vertical diagram of five stages of an electrified liquefaction plant — gas gathering and pipeline, acid gas and CO2 reinjection, electric drive and converter rooms, liquefaction trains, storage and loading — each with its governing fire scenario, above the project figures
The chain of an electrified liquefaction plant, with the governing scenario at each stage. Figures are the project’s own, as published by the venture and by TotalEnergies.

Editorial rule, applied without exception: no figure, designation or claim of fact is published without verification against a primary source. Everything under “Analysis” is our engineering judgement, not reported fact. Illustrations are generated images, not photographs of the facilities described.

LNGElectrificationHazardous area classificationInsurer requirements

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