Technip Supporting Malaysian OTEC Ambitions Jim O SULLIVAN, CTO Technip Kuala Lumpur, Malaysia September 2015 1
Table of contents 1. Technip Today 2. OTEC Design & Economic Issues 3. Malaysian OTEC Opportunities 2
Technip Today 3 Footer can be customized
Technip Today With engineering, technologies and project management, on land and at sea, we safely and successfully deliver the best solutions for our clients in the energy business Worldwide presence with over 38,000 people in 48 countries Industrial assets on all continents, a fleet of 27 vessels (of which 6 under construction) 2014 revenue: 10.7 billion ENERGY IS AT THE CORE OF TECHNIP 4
An Absolute Commitment to HSES The Health and Safety of our people is a core value and an absolute commitment Thierry Pilenko, Chairman and CEO of Technip Technip s global HSES climate change program A Reference Company in HSES ( Chevron, Wheatstone, Shell Prelude, Shell Malikai, Petronas RAPID) DELIVERING EXCELLENT HSES PERFORMANCE AT EVERY LEVEL 5
Malaysia Major Technip Resource Center 4,200 Engineering & Project Management Asiaflex Products, flexible pipe and umbilical manufacturing plant 4,000 Fleet & others 3,400 9,800 2,500 2,500 Asia Pacific 6,000 1,000 4,600 Fabrication Part Owner MMHE Marine Vessels 3,000 in Malaysia Technip Projects: Kikeh Gumusut- Kakap Malikai Petronas FLNG1 6
OTEC Technip Malaysia Technip globally covers the full range of OTEC technologies and delivery capabilities, and envisions OTEC facilities as a future design and delivery service. Technip has a very strong organization in Asia Pacific, centered in Malaysia where we have maintained strong client relationships and made substantial investments. Technip understands Malaysia s desire to be a leader in OTEC and wants to support that ambition. Offshore Malaysia represents an ideal environment for a demonstration plant and educational facility. 7
8 OTEC Design & Economic Issues
OTEC Plant Architecture OTEC System Platform Power Generation Power Delivery Instrument & Control Integration & Installation Hull Structure Ammonia System Platform Substation Platform Management Platform Fabrication Super Structure Heat Exchanger Power Transmission Power Cycle Management Facilities Integration Station Keeping Marine System Cold Water Lift System Warm Water Lift System Onshore Substation Environmental Monitoring Management Transportation and Installation Mixed Water Discharge System Technip has design engineers and supplier networks for all OTEC components 9
Technip Did Designs for 5, 10 & 100 MW Net NH3 Feed Pump NH3 Circ. Pump WW Lift Pump CW Lift Pump Hotel Load Total Parasitic Pow NH3 Turbine Power Generator Power Net Power FI 2001 WARM SEAWATER SUPPLY (20 m depth) 224 kg/s 1003 WARM WATER PIPE (HDPE) FC V-102 AMMONIA DEMISTER LC 2006 1004 OTEC - PROCESS FLOW DIAGRAM CASE X1 TP 5MW Pilot (Delivered Power) Weiland Tube Evaporator/ Weiland Tube Condenser 1005 E-101A-F AMMONIA EVAPORATOR (Weiland Tube) 2006 1007 PC 4003A DISCHARGE (60 m depth) F-101A/B AMMONIA FILTER DISCHARGE PIPE (HDPE) P-101A/B AMMONIA FEED PUMP T-101 AMMONIA TURBINE/ GENERATOR 1008 E-102A/B AMMONIA Condenser CONDENSER (Weiland Tube) 2004 WARM WATER 60.7% 11.29 C V-101 3004 LIFT PUMP 10.29 bar_g AMMONIA 223.6 kg/s BUFFER 0.36 m3/s VESSEL 5739 gpm P-201 690 kw 70.0% 296 kw S-201 WARM WATER SUMP 2003 21 kw 689 kw 1,085 kw 270 kw 2,361 kw 8,001 kw 7,681 kw 5,320 kw Ratio Gen/Net Powe 1.44 Delivered Power Warm Water Flow Cold Water Flow Working Fluid Flow 2001 28.5 C 1.95 bar_g 5,001 kw 20,845 kg/s 13,921 kg/s 1003 11.32 C 8.29 bar_g 223.6 kg/s vfrac= 0 P-201A/B 2003 28.5 C -0.001 bar_g 20845.3 kg/s 20.93 m3/s 331755 gpm 1004 22.59 C 8.29 bar_g 468.3 kg/s 0.77 m3/s 12334 gpm P-102 21 kw 2006 28.5 C 0.22 bar_g 20845.3 kg/s 1006 E-101 287.9 MW UA 78.91E6W/C 2.6 C M in App U= 3383 W/C A= 23325m2 Shells= 5.7 P-102A/B AMMONIA CIRCULATING PUMP 1006 22.59 C 8.29 bar_g 468.3 kg/s vfrac= 0.5 1005 22.6 C 8.45 bar_g 1002 Hydraulics WW#1 inlet Head+Line Loss 0.00 (bar) WW#1 Evaporator loss 0.15 (bar) WW#1 Duct loss+disch Loss 0.08 (bar) WW#1 pump head req 0.23 (bar) CW#1 inlet Head+Line Loss 0.26 (bar) CW#1 Condenser loss 0.21 (bar) CW#1 Duct loss+disch Loss 0.08 (bar) CW#1 pump head req 0.55 (bar) NH3 #1 Evaporator loss 0.16 (bar) NH3 #1 Condenser loss 0.16 (bar) NH3 #1 Pump CV discharge l 2.00 (bar) 1007 22.32 C 8.13 bar_g 223.6 kg/s vfrac= 1 2007 S-401 RETURN WATER SUMP 2007 25.2 C 0.01 bar_g 20845.3 kg/s 20.91 m3/s 331452 gpm 3007 9 C 0 bar_g 13920.9 kg/s 13.92 m3/s 220740 gpm 1002 T-101 8000 kw 81.0% 3007 4001 4001 18.7 C 0.01 bar_g 34766.3 kg/s 34.82 m3/s 551989 gpm 4003A 18.71 C 5.88 bar_g P-101 296 kw 60.7% 1008 11.82 C 5.5 bar_g 223.6 kg/s vfrac= 0.982 E-102 280.3 M W UA 61.5E6W/C 2.1 C M in App U= 2722 W/C A= 22593m2 Shells= 1.8 T-101 8000 kw 81.0% G-101 7681 kw 96.0% Parasit ic 2361 kw N et Power 5320 kw Delivered P 5001 kw 94.0% 3005 1001 Make-Up Ammonia FI 3006 1001 11.1 C 5.33 bar_g 223.6 kg/s 0.36 m3/s 5739 gpm S-301 COLD WATER SUMP COLD WATER PIPE (HDPE) COLD SEAWATER SUPPLY (1000 m depth) Working Fluid WW:CW ratio 1.50 WW Temp CW Temp Working Fluid SW Efficiencies P-301 1086 kw 70.0% 3001 3006 4.2 C 0.27 bar_g 13920.9 kg/s 13.92 m3/s 220705 gpm 3003A 3002A P-301A/B COLD WATER LIFT PUMP 3003 28.5 C 4.2 C NH3 Hysys-Fresh Water Water Pumps 70% Working fluid Pump 61% Pow er Turbine 81% Generator 96% Delivered Pow er Ef 94% HX min. approach temp. Evaporators 3001 4.2 C 98.05 bar_g 2.6 C 2.1 C 3003 4.2 C -0.254 bar_g 13920.9 kg/s 13.92 m3/s 220710 gpm 10
11 5MW Plant Served As The Building Block
Spar Type Considered Motions, Fabrication & Installation Issues For Hull Selection vs Power Capacities Advantages Best in-situ stability for cold pipe design Best operability in cyclonic regions Disadvantages Horizontal fabrication, transport, on site up-righting and topside installation Access for maintenance in hull Multi-Column Type Advantages Vertical fabrication and integration Relatively good stability in cyclonic regions with large deck areas Disadvantages Access for maintenance in hull Low hull inefficiency for higher power capacity 12 Ship Shape Type Advantages Lowest cost for supporting facilities Drydock fabrication and quayside topside integration with large deck areas Disadvantages Vessel motions in cyclonic regions difficult cold pipe designs Caisson Type Advantages Spar like stability excellent operability in cyclonic region Vertical fabrication, transportation and installation Good hull efficiency and access for maintenance Disadvantages Fabrication sites
Installed Capital Cost ($/kw) Resulting Installed CAPEX Curve Similar To Published Curves But Marginally Higher Technical Price Estimates for 5, 10 and 100 MW Net OTEC Power Plants, Installed 45000 40000 35000 30000 25000 20000 15000 10000 5000 Δ < 20MW the installed cost strong function of floater Δ > 20MW the installed cost strong function of numbers of heat exchangers Δ 13 0 0 20 40 60 80 100 Nominal Plant Size, MW-net Differences were in integration, transportation and installation not in hardware and hull
Majority Of Potential Users Have Positive Returns With Today s Energy Prices Market expected return 14 Source: NYU Stern School of Business for Weighted Average Cost of Capital (WACC) of Global Power Generation 2013
Malaysian OTEC 15 Footer can be customized
Potential for OTEC in Malaysia Mild environment, >1000m depth (Sabah Trench), DT>25 C, <120km offshore Several near-by production facilities power users 16
Technip Has Been Involved In Several Sabah Trough Deliveries Know Area Well SHELL Gumusut-Kakap Semi-Sub, Offshore Sabah (Detailed Engineering) MURPHY Kikeh Spar Dry Tree Unit + Subsea facilities, Offshore Sabah (Engineering, Procurement, Construction & Installation) Shell Malikai TLP, Malaysia ( Engineering, Procurement, Construction ) 17
Sabah O&G Deepwater: Technip s OTEC Integration Plan Study O&G fields across entire Sabah Deepwater / Trough Identify power demand for each O&G DW cluster Identify strategies that optimize power costs considering both OTEC and conventional Gas- Fired Turbine Power Generation Support Petronas and PSCs to become pioneer of this hybrid solution and promote it worldwide! 18
Summary OTEC technology is mature Ample supplier base for key components Availability of advanced testing facilities Economics are workable Power generation clear visible market There are other less visible markets Malaysia is an ideal location for OTEC industry Environment ideal National resources available We can do this 19
Thank you 20 www.technip.com