Snøhvit Future Development Concepts for increased gas export capacity

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1 Snøhvit Future Development Concepts for increased gas export capacity 2 nd Trondheim Gas Technology Conference 2-3 rd November 2011 Øystein Holt, Technology Manager

2 Snøhvit A dream came true

3 Snøhvit a pioneer project The first large-scale production facility for LNG in Norway and Europe The first offshore project in the Barents Sea The largest-ever industrial development in northern Norway New technology New markets New operation organisation

4 Facts: Discovered: Water depth: m Distance to shore: 140 km Recoverable reserves: 193 GSm 3 Condensate: 34 Mm 3 Snøhvit, Albatross and Askeladd Owners: Statoil ASA (Operator) 33.53% Petoro AS 30.00% Total E&P Norge AS 18.40% GDF Suez Norge AS 12.00% Hess Norge AS 3.26% RWE Dea Norge AS 2.81%

5 Snøhvit Future Development The Snøhvit License is evaluating the basis for increased production Three alternatives are evaluated 1. Lifetime extension of LNG Train I 2. LNG Train II from Increased production from a gas processing facility and pipeline transport from Melkøya in The pipeline case is evaluated by Gassco on behalf of the Snøhvit License

6 Snøhvit Melkøya

7 Snøhvit Melkøya Future Phased subsea development to meet capacity needs for 3 alternative export alternatives Offshore development scheme Train I: LNG train I+II: LNG train I + dewpoint facilities/pipeline:

8 Norwegian Gas Infrastructure Snøhvit Melkøya Åsgard Norne Heidrun Ormen Lange ÅTS Haltenpipe Statfjord Frigg Vesterled Sleipner Troll Nyhamna Kollsnes Kårstø St Fergus Ekofisk Europipe II Europipe I Langeled Zeepipe I Norpipe Teesside Franpipe Easington Emden Zeebrugge Dunkirk

9 Overview of LNG alternative CO2 to Pipeline CO2 Drying and Compression Fractionation LPG Storage (Train I) LPG to Ship via Existing Jetty Train II Trunklines CO2 Removal Dehydration Mercury Removal Liquefaction Train I LNG Storage Train II LNG Storage LNG to Ship Via New & Existing Jetty Feed Gas Train I Trunklines Slugcatcher (Train I) Condensate Inlet Facilities Train II MEG Condensate Treatment Fuel Gas Condensate Storage (Train I) Condensate to Ship via Existing Jetty Train I MEG Recovery Utilities Offsites To Train I & II Pipelines To/from Train I To/from Train I Power from national grid

10 Learnings from Train I Chart shows distribution of downtime since plant start-up One specific heat exchanger type is main source of downtime Failure mode was wear of the tubes against baffle plates caused by flow induced vibration All helix exchangers have now been replaced Plate fin heat exchangers replaced in

11 Snøhvit LNG train II technology selection C3-MR: propane precooled mixed refrigerant process DMR, Dual Mixed Refrigerant process OC, Optimized Cascade process MFC process

12 Overview of dewpoint and pipeline alternative CO2 to Pipeline CO2 Drying and Compression Train II Trunklines CO2 Removal Dehydration Gas Export & Metering System Pig Launcher Rich gas to new pipeline Train I Trunklines Slugcatcher (Train I) Feed Gas Dew Point Control Condensate Train II MEG Condensate Treatment Fuel Gas Condensate Storage (Train I) Condensate to Ship via Existing Jetty Train I MEG Recovery Utilities Offsites To Train I & II Pipelines To/from Train I To/from Train I Power from national grid

13 Summary Increase in Snøhvit reserves expected Offshore development with subsea facilities including compression Onshore capacity increase (LNG or dew point) comprising: Expansion of existing inlet facilities New process and utility facilities Power supply Large investments early (LNG) or later (dew point + pipeline) based on best business case Concept selection in 2012 Many technical challenges ahead interesting tasks for our supply chain

14 Snøhvit Future Development Concepts for increased gas export capacity Øystein Holt Technology Manager Tel

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