Comparison tool

Compare LNG vessels and containment systems

Pick up to 4 entries, or start from a preset. Entries are compared on described characteristics only — no scores or rankings are applied.

Educational data

Preset comparisons

Select entries (1/4)

Membrane

The volumetric workhorse behind most modern LNG newbuilds.

Operational role
Conventional Ocean-Going LNG Carrier
Containment system
GTT Mark III Membrane · GTT NO96 Membrane
Capacity class
Conventional (indicative: approximately 125,000–180,000 m³)
Indicative capacity
145K–180K m³
Tank geometry
Hull-conforming prismatic membrane tanks
Typical application
Baseload ocean transport between major liquefaction and import terminals
Hull-space efficiency
High — tanks follow the hull form and maximise cargo volume
Infrastructure requirements
Conventional deep-water LNG terminals
Propulsion options
ME-GI · X-DF · DFDE / TFDE · Steam turbine
BOG management
BOG as fuel · Gas combustion unit · Reliquefaction
Advantages
Best cargo volume per metre of hull, lowering unit freight cost — Very low boil-off with reinforced insulation systems — Broad shipyard availability and a deep spares ecosystem
Limitations
Filling-level restrictions on some systems to avoid sloshing loads — Primary barrier repairs require specialist yard capability
Typical routes
US Gulf – Northwest Europe · Qatar – India · Australia – China

Technical information

Status
Educational overview
Last reviewed
15 September 2026
Source status
Sources pending editorial review.

Technical parameters are indicative and may vary by vessel design, generation, shipyard, operator and intended service.