Tangguh Lng Terminal
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Summary Information

  • Ownership: BP
    • BP Indonesia, 37.16 %
    • MI Berau B.V. (16.3 per cent),
    • CNOOC Ltd. (13.9 per cent),
    • Nippon Oil Exploration (Berau) Ltd. (12.23 per cent),
    • KG Berau/KG Wiriagar (10 per cent),
    • LNG Japan Corporation (7.35 per cent) and
    • Talisman (3.06 per cent).
  • Website: http://www.bp.com/
  • Location: Teluk Bintuni, Papua Province, Republic of Indonesia
  • Capacity: 7.6 million tons/annum
  • Status: In Operation

Technical Details

  • Storage capacity: Two insulated tanks capable of storing 170,000 m3 each
  • Jetty: LNG export jetty designed for 140,000 ton LNG carriers
  • Licensor: Air Products
  • Constructor: EPC Contractor, Consortium KJP (Kellogg Brown &Root, JGC and PT Pertafenikki)

Ongoing Projects/Project Status

Suppliers / Customers

  • Suppliers: Gas fields in the Berau and Bintuni bay area including the Massive Tangguh Gas Field
  • Customers:
    • A commitment to supply 2.6 mtpa of LNG to CNOOC's Fujian Lng Terminal , People’s Republic of China, was signed in 2002.
    • This was followed by the agreement of POSCO and K-Power of the Republic of Korea in 2004 to purchase up to 0.55 and 0.80 mtpa of Tangguh LNG, respectively, for 20 years starting in 2006. See Gwangyang Lng Terminal
    • On 11 October 2004, a sales purchase agreement was signed with Sempra Energy LNG Corp. for a 20-year LNG supply of up to 3.7 mtpa from Indonesia to markets in the United States and Mexico via the Cameron Lng Terminal and the Costa Azul Lng Terminal

History

  • 2004 - BG Group completes sale of Tangguh LNG interest
  • 2005 - Contracts signed for construction
  • 2006 Japan Bank for International Cooperation (JBIC) signed a loan agreement totaling US$1.2 billion with the Japanese sponsors of the project
  • 2009 - First cargoes shipped

Other Information

  • The main process elements are the following:
    • (i) onshore receiving facility, where the natural gas stream will be separated into gas, hydrocarbon condensate, and water, and which will serve both LNG trains;
    • (ii) gas purification facilities, comprising an acid gas removal unit, which removes CO2, a dehydration unit, and a mercury removal unit, which are required to avoid freezing problems and aluminium attack on the main cryogenic heat exchanger;
    • (iii) gas liquefaction facilities, which remove heavier components of the produced gas and liquefy the remaining gas. Each train includes a liquefaction unit and a fractionation unit. A condensate stabilization unit will serve both LNG trains.
  • LNG from the liquefaction unit is stored at near-atmospheric pressure in large storage tanks. For the initial two train development, two tanks will be installed, each with 5 approximately 170,000 m3 capacity.
  • Condensate, including product from the onshore receiving facility and the fractionation plant, after passing through the stabilization unit, is stored in a 20,000 m3 condensate tank.

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