© Gastech 2005 Gastech 2005 MEDGAZ Pipeline: Ensuring Energy
Transcription
© Gastech 2005 Gastech 2005 MEDGAZ Pipeline: Ensuring Energy
Gastech 2005 MEDGAZ Pipeline: Ensuring Energy Security for the Iberian Peninsula by Jay Chaudhuri, MEDGAZ S.A. www.medgaz.com 16th March 2005 © Gastech 2005 SUMMARY 90,00 The paper details the design, operation and environmental considerations which have governed the project development strategy to-date. The proposed pipeline is expected to be commissioned during 2008. 80,00 70,00 60,00 b c m /y e a r It is accepted by the energy economists that for short to medium distance gas transportation; high pressure trunk lines are the safest and cheapest way of transporting gas to market. The proposed ultra-deep water natural gas pipeline linking Algeria and Spain is designed to transport up to 16 BCM/year gas into the Iberian and European energy markets. When commissioned, the proposed pipeline will be well placed to meet the demand for gas in the Iberian market which has shown compound annual growth rates of 17%. Extensive technical studies conducted by Medgaz have already validated the proposed deepwater pipeline design and the associated offshore route, which will traverse the Mediterranean Sea at water depth in excess of 2000 metres. Internal and external studies indicate that the proposed Medgaz pipeline will be the most economic solution for enhancing and ensuring energy security for the Iberian Peninsula. 50,00 40,00 30,00 20,00 10,00 0,00 2002 2003 2004 2005 2006 Year 2007 2008 2009 2010 2011 GME Larrau Medgaz Barcelona Cartagena Huelva Bilbao Mugardos Sagunto Annual demand Peak demand Fig. 1 – Spanish Gas System Capacity (Source : CNE, 2004) 240 mcm/day 200 1.- GAS CONSUMPTION & SUPPLY COSTS : IBERIAN PENINSULA • • • • • Iberia’s fast growing energy market poses challenges to the existing infrastructure. Spanish gas consumption has grown from 21.4 BCM in year 2002 to 28.3 BCM in year 2004. It is anticipated that in the year 2011 annual demand will exceed 44 BCM (Fig. 1). Manufacturing growth and need to switch to ‘Kyoto Protocol’ friendly fuels is increasing gas demand at 17% compound rate; while system capacity has barely managed to keep in pace with the demand growth. There are a number of gas and power infrastructure projects underway but peak capacity shortages currently being experienced will stretch to year 2010 (Fig. 2). Delays in increasing infrastructure capacity will harm the development of the Iberian energy market in the short to medium term and growth potential of the economy. ‘Average to peak’ capacity margin lower than OECD average. © Gastech 2005 160 120 80 40 0 2003 Demand 2003 Supply 2005 Demand 2005 Supply 2010 Demand 2010 Supply FirmDemand Interruptible Demand Indigenous Production Contracted Supply Storage (*) Additional Capacity Fig. 2 – Spanish Peak Day Gas Supply & Demand (Source : Wood Mackenzie, 2003) The Long Run Marginal Cost (excluding producing country royalty) for potential gas supply to Spain has been studied extensively by independent energy consultants OME and Wood Mackenzie. The studies indicate clearly the economic benefits of the proposed MEDGAZ gas pipeline, since this is the lowest cost supply option for Spain (Fig. 3). Chaudhuri 2 of 2155 m and an approximate length of 200 km (Fig. 6). The proposed route is characterized by: - non-steep continental slopes on either side of the Alboran Sea; - quaternary clay soil for the major part of the route; - stable sea-bed conditions. Two onshore terminals will assure the safe and efficient transportation of gas: - BSCS: Beni Saf Compressor Station, near Sidi Djelloul in Algeria - OPRT: Offshore Pipeline Receiving Terminal, near Almería in Spain Phase 1: Construction of the east offshore pipeline and the short onshore sections for the second west pipeline, the compressor station at Beni Saf and the receiving terminal at Almería – Capacity 8 billion m³/year. Phase 2 : Construction of the west pipeline – Total capacity of the two pipelines 16 billion m³/year Onshore connecting pipelines (to be constructed by others): - Algerian section: 550 km. - Spanish section: 285 km. Supply costs* for potential gas supply for SPAIN (2010-2020) ALGERIA via Medgaz • ALGERIA via GME NETHERLANDS ALGERIA-LNG NORWAY-North Sea Troll EGYPT LNG LIBYA LNG NORWAY-North Sea Medium fields VENEZUELA-LNG TRINIDAD &TOBAGO-LNG QATAR LNG • NIGERIA LNG IRAN LNG UAE LNG OMAN LNG YEMEN LNG NORWAY- LNG Snohvit NORWAY-Norwegian Sea 0,8 1 1,2 1,4 1,6 1,8 2 2,2 2,4 2,6 * Long Marginal Cost excluding producer country's royalty 2,8 3 $/MBTU 3,2 • Fig. 3 – LRMC supply cost (source: OME) 2.- OVERVIEW OF THE MEDGAZ PROJECT • MEDGAZ project was initiated by Cepsa and Sonatrach in 2001. Current partnership structure of the project is shown in Fig. 4. • TOTAL 12% ENDESA 12% GdF 12% SONATRACH 20% MEDGAZ - Transportation System OFFSHORE SECTION ALGERIA CEPSA 20% IBERDROLA 12% SPAIN 0 -100 -200 -300 BP 12% -400 -500 -600 -700 Water Depth (m) -800 Fig. 4 MEDGAZ Partnership Structure -900 -1000 -1100 -1200 -1300 -1400 -1500 -1600 -1700 -1800 -1900 -2000 Schematic of the pipeline routing is illustrated in Fig. 5. -2100 -2200 0 10 20 30 40 50 60 70 80 90 100 110 120 130 140 150 160 170 180 190 200 KP (km) Fig. 6 – Pipeline Route Profile 3. TECHNO – COMMERCIAL DATA Gas transportation build-up profile: Year Flow [BCM/y] Number of pipelines Fig. 5 - Medgaz Offshore Pipeline Route The principal features of the Medgaz system are outlined below: • • Capacity to supply 16 billion m³/year of gas to the Iberian Peninsular and Europe via two 24 inch diameter submarine pipelines planned for construction in two phases. Two offshore pipelines will directly connect the Algerian gas fields and Spanish gas network across the Mediterranean (Alboran Sea) at a maximum depth © Gastech 2005 1 2 3 4 5 15 6 7 8 8 8 16 1 1 1 1 1 2 Design Pressure = 220 barg Maximum temperature = 60º C Minimum temperature = 0º C Design Code Steel Grade X70 Pipe Thickness Chaudhuri 3 = DnV OS F101 = SAWL 485 I DUF = 22.9 / 28.5 / 29.9 mm 4. MARINE SURVEY CAMPAIGNS 7. GEOTECHNICAL INVESTIGATIONS Several marine surveys were performed during 2002 – 2004 period; • • • • • • Geological inspections of the proposed route Environmental survey of marine flora/fauna on the offshore and onshore sections on the Algerian and Spanish sides. Geophysical investigations close to coast at 25m depth isobathe Onshore inspection of the shore approach in Algeria and Spain High resolution seismic survey of the route for better evaluation of the geological risks. Bathymetry, environmental, visual and magnetic surveys 5. ROUTE SELECTION The information provided by the survey campaigns has permitted selection of the definitive pipeline route to meet the following objectives: • • • • • • • During 2002, CSIC performed a comprehensive study of the geo-morphology and seismic risks of the proposed offshore route which helped to focus the critical zones of the route for subsequent detailed study and geotechnical investigations (Figs. 8 and 9). During 2003, an in-depth geotechnical investigation was performed involving soil sampling and in-situ tests at more than 130 locations along pipeline route. Work programme included; • Sampling by piston corer • Cone penetration test (CPT) • Seismic CPTs • T-bar test • Water temperature and chemical assay in laboratory • Geotechnical laboratory tests including shear cyclic loading and carbon dating Minimisation of environmental impact Protection of marine flora/fauna on the offshore and onshore sections on the Algerian and Spanish sides. Avoidance of natural obstacles that exist along the route Low geological and geotechnical risks Minimal number of cable crossings Ensuring the feasibility to employ S-and/or, J-lay construction method Minimisation of ‘free-span’ risks 6. ROUTE CHARACTERISTICS • • • • • • • • Length of offshore route 198.3 km Maximum water depth 2155m (49% > 1000m) 19 curvature points 5 crossings of telecommunications cables (all at water depth greater than 1000m ) 1 geological fault crossing : Yusuf Fault Critical zone KP71 – KP77: Slopes <14 degrees More than 95% of the route: slopes less than 4 degrees (Fig. 7) Critical zone KP71 – KP77: Habibas escarpment Source: CSIC Fig. 8 Bathy-Morphological Characteristics of Pipeline Route Fig. 7 Slopes of the Spanish Continental Shelf © Gastech 2005 Chaudhuri 4 • Phase 1 conditions for operation of a single offshore pipeline: 40.0 LEGEND MAGNITUDE SCALE Ms 10 39.0 9 IBERIAN FO RELAND 4.0 4.5 5.0 5.5 6.0 6.5 7.0 to to to to to to to 4.5 5.0 5.5 6.0 6.5 7.0 7.5 Pipeline Route 8 38.0 11 SY BE TIC Granada Basin ST EM 6 37.0 36.0 4 W estern A lbor an Basin Faults Eastern Alb or an Basin e id g nR ra bo Al Sou thern Albo ran Basin 3 15 20 M otr il B asin 2 2 TE 1 ORAN YUSUF LA 16 S 14 DL E A TL : 8 BCM/year - 3 compressors in service : 2 LP+1 HP • Phase 2 conditions for operation of two pipelines: 13 M ID 2 AT RIF 34.0 18 AS SA 33.0 1 LL 1 35.0 - Capacity 17 South Bal ear ic Ba sin 5 12 14 Province number 7 HA R A 19 A TL AS AFRICAN F ORELAND - Capacity : 16 BCM/year - 5 compressors in service : 3 LP+2 HP offshore HIGH ATLAS 32.0 -6.0 -5.0 -4.0 -3.0 -2.0 -1.0 0.0 1.0 2.0 3.0 4.0 LONGITUDE Fig 9 Seismic Risk Source Distribution 8. GEOHAZARD EVALUATIONS Based on the results of various surveys conducted by MEDGAZ and subsequent technical studies, it can be concluded that the proposed`pipeline route will benefit from; • • • Absence of significant geological and seismic risks; Ideal seabed conditions for pipelay and long-term operation of the pipeline; The steepest slopes encountered at the Habibas escarpment (KP71 - KP77) will not affect pipeline stability and long-term operation. • The critical slopes of the route are stable for seismotectonic events with return periods of 475 years. • The design of the pipeline is demonstrated to be extremely robust for safe operation in conceivable earthquake conditions. Fig. 10 BSCS – 3D Visualisation 11. DESIGN BASIS FOR RECEIVING TERMINAL • OPRT Arrival Pressure : 82 barg • OPRT arrival temperature : 0º C (min) • Energy requirement for gas heating : - 0 MW for steady state operation - 12, 6 MW during re-start from marine pipeline packed condition • Spanish pipeline entry pressure : 80 barg 9. MEETING THE ENVIRONNEMENTAL CHALLENGES The pipeline design incorporates the following features; • To minimize the problems of environment during construction, shore approach sections of the second 24 inch pipeline will be built during Phase 1 of construction of the first pipeline. Thus, when the second offshore pipeline is constructed, there will be no significant onshore construction activity in Algeria and Spain. • The width of the offshore corridor is minimized; while allowing sufficient space for the installation of the future second line. • The program of work is planned to avoid significant construction installation activities close to the coastal zones during the peak tourism periods of the summer months. • Dredging and rock-dumping is minimized to reduce the disturbance of sea-bed flora and fauna. Fig. 11 OPRT – 3D Visualisation 12. ENVIRONMENTAL ASPECTS FOR DESIGN OF ONSHORE TERMINALS The MEDGAZ project has applied proven environmental principles for the design of the terminals. Some of the design features considered to minimise environmental impact include: Specification of dry low emission turbines compressor drives; • Selection of BSCS compressor configuration 10. DESIGN BASIS FOR COMPRESSOR STATION optimum fuel consumption at projected transportation rates; • BSCS inlet pressure : 45 barg • Use of air for actuation of BSCS valves; • Use of flaring (instead of venting) during planned • BSCS outlet pressure : 200 barg (max.) pressurisation of either terminal; © Gastech 2005 Chaudhuri 5 • for for gas de- • Specification of low NOx burners for OPRT gas reheaters. 15. ACKNOWLEDGEMENTS 13. PROJECT SCHEDULE The author wishes to thank the companies which have participated in the Medgaz project to-date, for their technical contribution to the project e.g.: The current execution schedule is shown below in Fig. 12. 2001 2002 2003 2004 2005 2006 2007 2008 2009 1S 2S 1S 2S 1S 2S 1S 2S 1S 2S 1S 2S 1S 2S 1S 2S 1S 2S - Project Launch Feasibility Study Route Confirmation & FEED1 Transition to Construction Company Commercial Agreements Permitting Investment Decission (FID)2 Project Execution Start-up (First Gas) 1 Front End Engineering & Desing Decision C&C Technologies Inc. Snamprogetti s.p.a. CSIC Fugro b.v. Fugro (UK) Ltd. INTEC Engineering (UK) Ltd. Rambøll A/S Initec S.A. D’Appolonia s.p.a. Geoconsult A/S JP Kenny Ltd. 2 Firm Investment Fig. 12 MEDGAZ Project Schedule Abbreviations: 14. SUMMARY AND CONCLUSIONS Technical summary: • • • Route selection is based on results of exhaustive geophysical and geotechnical investigation, which has minimised project technical risks. MEDGAZ project has implemented latest and proven deepwater pipeline construction technologies to overcome the technical challenges; ensuring minimum transport costs for the proposed new route of gas supply to the Iberian peninsula. In-depth ‘baseline’ studies and proven environmental principles have been adopted to ensure environmentfriendly project implementation. In addition, the Medgaz project will contribute significantly towards the implementation of sustainable development strategies of an integrated energy plan for the Iberian peninsula. BSCS OPRT BCM DnV OS FEED EIA FID ROW SAWL LP HP LRMC KP MCM Economic and commercial summary: • • • • • Enhancement of security of energy supply for Spain and Europe. The most economic method of gas supply to the Iberian peninsula. Promotes competition in the Spanish and Southern European energy markets. Approved as ‘Quick Start’ Priority Project under the EU TEN-E programme (Decision 1229/2003/CE). On 12th January, 2005 the Spanish Government advised that priority rating “A” will be accorded to the MEDGAZ project, ensuring project implementation to progress for ‘First Gas’ delivery in 2009. © Gastech 2005 Chaudhuri 6 : : : : : : : : : : : : : : Beni Saf Compressor Station Offshore Pipeline Receiving Terminal Billion Cubic Metres Det Norske Veritas Offshore Front End Engineering Design Environmental Impact Assessment Firm Investment Decision Rights of Way Submerged Arc Weld Longitudinal Low Pressure High Pressure Long Run Marginal Cost Kilometre Point Million Cubic Metres