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Chemical Panel Engineers Australia WA Division &  The Institution of Chemical Engineers (WA) Gary J. Crisp Global Business Leader – Desalination: GHD BSc. Civil Engineering, C Eng., MICE, CP Eng., FIE Aust., PMP Auditorium, Engineers Australia 712 Murray Street, West Perth, WA  Monday, 14 March 2011 Desalination Sustainably Drought Proofing Australia
It’s not about water. It’s about   energy!
“ Energy is eternal delight!” Energy is liberation. William Blake, author, poet, visionary, 1757 – 1827
Energy Use Across the Water Cycle  (1kWh/m 3  = 3.79 kWh/kgal - 4 kWh/m 3  = 15.14 kWh/kgal) California State Water Project = 2.5 kWh/m 3  = 9.50 kWh/kgal Gold Coast Desalination Plant = 3.23 kWh/m 3  = 12.24 kWh/kgal SOURCE TRANSPORT WTP DISTRIBUTION WWTP COLLECTION USE DISPOSAL/ RECYCLE
Presentation Overview ,[object Object],[object Object],[object Object],[object Object],[object Object]
Desalination – Where Are We Today? 14,754 Desalination Plants Worldwide – 16,700 MGD Source : IDA Desalination Yearbook 2009-2010
Source: WDR, July 2010 Projected New Desalination  Capacity in 2010 6.8 GL/day Actual New Capacity in 2009  3.9 GL/day
Water Resource Cost Trends: US $/m 3 ,[object Object],Cost ($/m 3 ) Year THE TRIPLE BOTTOM LINE The  TRUE  Value of Water Obtained with Minimal  Environmental Impact The Environmental “ Forgotten” Perth Seawater Desalination Plant Water Cost 0.90 $/m 3 Global Water Intelligence - October 2006
Membrane Separation - Filtration Spectrum Courtesy of Osmonics
Reverse Osmosis Water   Molecules Protozoa Bacteria Virus Organics Inorganics An RO Membrane is like a Microscopic Strainer that allows Water Molecules to pass through
Seawater Reverse Osmosis (SWRO)
Seawater Reverse Osmosis (SWRO) 0.77 bar per 1000 mg/L
Seawater Reverse Osmosis (SWRO) Specific Energy Consumption (SEC) ,[object Object],[object Object],[object Object],[object Object]
0.2 µm 40 µm 120 µm Polyamide Polysulfone Ultra thin Barrier Layer Microporous Polysulfone Substrate Reinforcing Polyester Fabric Cross-Section TFC
Membrane arrangement Membrane element Feed spacer Permeate spacer Membrane leaf
Reverse Osmosis Spiral Wound Membrane
The Desalination Process
[object Object],The Big 6
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],1143 mm 533 mm 787 mm *Average annual rainfall ,[object Object],[object Object],[object Object],508 mm Australia Rainfall and Seawater Desalination Courtesy – Bob Yamanda - SDCWA
The Big Six – No. 1  Perth Seawater Desalination Plant (Perth I) - 38 mgd (144 MLD) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Perth Seawater Desalination Plant ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Courtesy of Water Corporation 6.5 ha
Perth Seawater Desalination Plant 6.5 ha 3 ha
Integrated  Water Supply Scheme GROUNDWATER SOURCE SURFACE WATER SOURCE AREA SERVED TRUNK MAINS PERTH Goldfields & Agricultural WS Mandurah Stirling Sth Dandalup Serpentine Nth Dandalup Mundaring Victoria Canning Wungong Pinjar Wanneroo Lexia Mirrabooka Neerabup Sth Whitfords Gwelup Jandakot ,[object Object],[object Object],[object Object],Harvey Dam and Wokalup Pipehead Dam 2002 Yarragadee Bores Samson Pipehead Dam 2001 Yarragadee Expansion Harris Pumpback PSDP Nicholson   Rd   Pumpstn
Seawater Intake Pre-treatment SWRO & BWRO Remineralisation/Storage  Potable water pump station Residuals Treatment Brine discharge HV substation Admin/Lab Chemical Storage Aerial View of Desalination Plant Raw Seawater screen and pump station Brine discharge Courtesy of Water Corporation
Perth Seawater Desalination Plant Seawater Intake System – Inlet Structure Courtesy of the Water Corporation
Perth Seawater Desalination Plant Courtesy of the Water Corporation Seawater Intake System – Inlet Structure
Perth Seawater Desalination Plant Courtesy of the Water Corporation Courtesy of the Water Corporation Seawater Intake System – Pipes and Works
Perth Seawater Desalination Plant Onshore Active Screening – Band Screen Courtesy of the Water Corporation
Perth Seawater Desalination Plant Seawater Intake and Outlet Works Courtesy of the Water Corporation
Perth Seawater Desalination Plant Single Stage Dual Media Pressure Filtration and Cartridge Filters
Perth Seawater Desalination Plant Each Pump Equivalent to 15  Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each.* *Red Book (Australia) specifications High Pressure Pumps 2.6 MW Each (6 in total) Courtesy of the Water Corporation
Perth Seawater Desalination Plant PRETREATED WATER PRODUCTION HP Pump Energy Recovery System (12 x 16 in Parallel) REJECT (Common By-pass) 2 nd  Stage 1 st   Stage 1 ST  PASS FEEDING (recycling) First Pass Second Pass MDJV in Alliance with Water Corporation Reverse Osmosis Process Flow  – Operating Principals & Arrangement
Perth Seawater Desalination Plant Circulation Pumps 134 kW each (12 in total) Courtesy of the Water Corporation Each Pump Equivalent to 1  Toyota RAV 4 5st 4dr Man 4x4 2.0i 0.132 MW @ 5200rpm each.* *Red Book (Australia) specifications
Perth Seawater Desalination Project (PSDP)   First Pass  Reverse Osmosis Racks
Perth Seawater Desalination Plant RO Building Looking South – 2 nd  Pass RO Courtesy of the Water Corporation
Perth Seawater Desalination Plant Each Rack Equivalent to 8 Ford Escape Wagon 4dr Auto 4sp 4x4 3.0i  0.152 MW @ 4750rpm each.* *Red Book (Australia) specifications Pressure Exchanger Rack 1.2 MW each (12 in total) Courtesy of Water Corporation
Perth Seawater Desalination Project   PX Process
Perth Seawater Desalination Project   Beyond Tomorrow
Perth Seawater Desalination Plant Potabilization System and Drinking Water Storage Tank Courtesy of Water Corporation
Perth Seawater Desalination Plant Drinking Water Transfer Pump Station Courtesy of Water Corporation
Perth Seawater Desalination Plant Concentrate Discharge Courtesy of Water Corporation
Perth Seawater Desalination Plant Concentrate Discharge Courtesy of Water Corporation
Perth Seawater Desalination Plant
Perth Seawater Desalination Project   Long Term Monitoring Macrobenthic To monitor the response of the sediment fauna over several years Benthic macrofauna pilot survey – complete Benthic macrofauna   comprehensive baseline survey – commenced March 2006 Annual monitoring (for three years initially)
Perth Seawater Desalination Plant 50 m limit for mixing zone 30 m mixing zone – achieve 42 x dilution Outfall pipeline Brine Discharge System 20 diffuser ports at 5 m spacing 3 Ha
Perth Seawater Desalination Plant Initial mixing zone = 100  metres 45x dilution farfield diffuser Courtesy of Water Corporation Seawater Concentrate - Salinity water surface
Perth Seawater Desalination Project  Baseline DO
Perth Seawater Desalination Plant Real Time Monitoring Courtesy of Water Corporation
Perth Seawater Desalination Plant These tests proved the Mathematical / Computer Model analyses.  Note the marine growth on the diffuser ports. Rhodamine Dye Test Courtesy of Water Corporation
Under the Surface Courtesy of the Water Corporation
Sustainable Power - Wind Energy for PSDP Greenhouse Gas Emissions  (tonnes per annum) Stanwell/Griffin Joint Venture -  Emu Downs wind generation facility – 100 Miles North of Perth Water Corporation is purchasing 68 percent of the energy output 0 85,000 231,000 24 MW (21.1 MW average - 185 GW hrs/annum)  Renewable or Sequestration Gas Grid Option Energy
Courtesy of the Water Corporation Zero Greenhouse Gas Emissions Stanwell/Griffin Joint Venture -  Emu Downs wind generation facility – at Badgingarra 200 north of Perth Water Corporation is purchasing 66 percent of the energy output 24 MW (185 GW hrs/annum) Opened on 12 November 2006  Perth Seawater Desalination Plant Sustainable Power - Wind Energy
Perth Seawater Desalination Plant Sustainable Power - Wind Energy ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Perth Seawater Desalination Plant Courtesy of the Water Corporation
The Big Six – No. 1 Perth Seawater Desalination Plant – Demonstration Plant
Perth Seawater Desalination Project  Plant Load Requirements Single Source 132 kV supply from Western Power 417 V Yes     Minor Drives Only Post Treatment Switchboard 416 V Yes 560 4 Drinking Water Pumps Drinking Water Switchboard 415 V Yes 110 12 RO Pass 1 HP Booster Pumps RO Auxiliary Switch Board 690 V Yes 630 6 RO Pass 2 HP pumps RO Pass 2 Switchboard 11 kV No 2,500 6 RO Pass 1 HP pumps Main Switchboard 690 V Yes 560 6 Seawater Intake Pumps Seawater Intake Switchboard     (kW)       Voltage Selected Variable Speed Requirement Drive Size Number Drives Serviced Application
Perth Seawater Desalination Project  Specific Energy Consumption of Components and Total *approx 7 miles of conveyance to Perth Integrated Water Supply System (IWSS) 3.60 3.48 0.21* 0.19 516,487 7,988* 501,271 7,228 144 kWh/kL kWh/kL kWh/kL kWh/kL kWh kWh kWh kWh ML Total Plant Desal Plant Only Potable Water Pumping  Intake Pumping Excluding Pre-Treatment Total Plant Potable Pumping Desal Plant Plus Pre-Treatment Only  Intake Pumping Total Potable Water Production Perth Seawater Desalination Plant - Specific Energy Consumption (SEC) for Components of Plant
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Perth Seawater Desalination Project Costs (2007)
Perth, Australia: Two-year Feed Back on Operation and Environmental Impact (Steve Christie – Water Corporation, Véronique Bonnélye - Degremont) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Gold Coast Desalination Plant - 35 mgd (133 MLD) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],The Big Six – No. 2
Gold Coast Desalination Plant ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
REVERSE OSMOSIS RESIDUALS REMINERALISATION OUTFALL PRETEATMENT INTAKE
Seawater Intake & screen Pre-treatment SWRO & BWRO Remineralisation/Storage  Potable water pump station Residuals Treatment Brine discharge shaft HV substation Admin/Lab Chemical Storage Aerial View of Desalination Plant
Twin 2.5 OD intake/outfall tunnels 2.2 km & 2.0 km sized for 340 MLD  125 MLD Plant ave. 94% availability 133 MLD peak daily production  26 km 1.1 m distribution main  30 ML reservoir & pump station
Marine Tunnels
Marine Tunnels  ,[object Object]
Marine Tunnels  ,[object Object]
Marine Tunnels ,[object Object],[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Seawater   Intake Contra-shear Drum Screen
 
2.11 m 6.32 m Seawater Intake - Coarse Screen
[object Object],[object Object],[object Object],[object Object],[object Object],Pretreatment
Pretreatment
[object Object],[object Object],[object Object],Residuals
[object Object],[object Object],[object Object],[object Object],Desalination Plant Feed
[object Object],[object Object],[object Object],[object Object],First Pass SWRO
4 x High Pressure Pumps 4.8 MW Each (Each equivalent to 28  Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each - Red Book Specifications) Desalination Plant Feed – 1 st  Pass
Seawater Reverse Osmosis - ERD PRETREATED WATER ,[object Object],PRODUCTION 3+1 HP Pumps Energy  Recovery  System  (1 per rack) REJECT (Common By-pass) 2 nd  Stage 1 st   Stage 1 ST  PASS FEEDING (recycling) First Pass Second Pass (Partial Split)
Energy Recovery Device - 1 st  Pass Pressure Exchanger Rack 1.6 MW Each (9 racks in total)  (Equivalent to 11 Mazda Tribute Wagon 4dr Auto 4sp 4x4 3.0i   0.152 MW @ 4750rpm each - Red Book Specifications) Re-circulation Pumps 180 kW Each Equivalent to 11  Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each - Red Book Specifications)
RO Building Pressure Vessel Racks - 1 st  Pass
[object Object],[object Object],[object Object],[object Object],[object Object],Second Pass SWRO
[object Object],[object Object],[object Object],[object Object],[object Object],Remineralisation and Storage
[object Object],[object Object],[object Object],[object Object],Brine   Discharge
Diffuser 6.0 yd 6.5 yd 1200mm PE
Network   Connection ,[object Object],[object Object],[object Object],[object Object]
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2
Courtesy of WaterSecure Gold Coast Desalination Plant - 35 mgd (133 MLD) The Big Six – No. 2
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 My Office for 2 years
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD)
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 Minimal Drum Screen Screenings (note the “Wheelie Bin”) Drum Screen 1/8 inch (3mm) mesh American Translation “Trash Can”
Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 3 duty 1 standby High Pressure Pumps (4.8 MW each)
Gold Coast Desalination Plant  Specific Energy Consumption of Components and Total *approx 26 km of conveyance to system with high static head 3.54 3.05 0.35* 0.15 489,256 47,725* 463,590 20,941 36,137 kWh/kL kWh/kL kWh/kL kWh/kL kWh kWh kWh kWh kgal Total Plant Desal Plant Only Potable Water Pumping  Intake Pumping Including Pre-Treatment Total Plant Potable Pumping Desal Plant Plus Pre-Treatment Only  Intake Pumping Total Potable Water Production Gold Coast Desalination Plant - Specific Energy Consumption (SEC) for Components of Plant
Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 Why So Expensive? Wonthaggi Desalination Plant – Electricians $220,000/year Connecting System (IWSS): $198 million Total Capital Cost: $943 million Total Operating Cost: $32 million/year Unit Cost: $2.38/kL
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Sydney Desalination Plant - 66 mgd (250 MLD) – Expandable to 132 mgd (500 MLD) The Big Six – No. 3
The Big Six – No. 3 Courtesy of Sydney Water Sydney Desalination Plant - 66 mgd (250 MLD) – Expandable to 132 mgd (500 MLD)
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Adelaide Desalination Plants I and II – 40 + 40 mgd (150 MLD each) The Big Six – No. 4
Adelaide Desalination Plants I and II – 40 + 40 mgd (150 MLD each) The Big Six – No. 4 Courtesy of SA Water
Southern Seawater Desalination Plant (Perth II) - 40 mgd (150 MLD) to 80 mgd (300 MLD) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],The Big Six – No. 5
Southern Seawater Desalination Plant (Perth II) 150 MLD (40 mgd) Expandable to 300 MLD (80 mgd) The Big Six – No. 5 Courtesy of Water Corporation
The Big Six – No. 6 The Victorian Desalination Project - 120 mgd (450 MLD) to 160 mgd (600MLD) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
The Victorian Desalination Project - 120 mgd (450 MLD) then 160 mgd (600 MLD) The Big Six – No. 6 Courtesy of Victorian Government
 
Future Desalination Developments ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Future Desalination Developments ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Desalination – Key Trends? ,[object Object],[object Object],[object Object],[object Object],[object Object]
Year 2005-2010  The Five Lowest-Cost SWRO Projects Worldwide SWRO Plant Cost of Water (US$/kL) Power Use of RO System (kWh/kL) & TDS (ppt)  Sorek, Israel – 409 MLD (startup – 2014) 0.53 2.59 (40 ppt) Mactaa, Algeria – 719 MLD (startup – 2013) 0.56 2.56 (39 ppt) Tuas, Singapore – 136 MLD (startup – 2007) 0.57 3.04 (34 ppt) Tenes, Algeria – 200 MLD (startup – 2011) 0.59 2.85 (38 ppt) Hadera, Israel – 329 MLD (startup – 2010) 0.60 2.67 (40 ppt)
Key Factors Affecting Costs ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Reducing Power Use for SWRO Separation   - Still a Hair Rising Challenge? Lowest Theoretical Energy Use = 0.75 kWh/kL (100 % Recovery) Lowest Theoretical Energy Use  @ 50 % Recovery = 1.09kWh/kL ADC - Lowest Energy Use @  42 % Recovery & 10.2 LMH = 1.59 kWh/kL ADC – “Most Affordable Point”  48 % Recovery & 15.3  LMH   = 2.01 kWh/kL Low Bracket of Energy Use for  Large SWRO Projects  (45-50 % Recovery & 14.3 to 16.3 LMH ) = 2.51 to 2.74 kWh/kL Note:  All Energy Use Values for  Seawater  @ TDS = 35 ppt & 25ºC
SWRO Power Consumption  (July 1, 2001)
50 MGD SWRO Plant –  Key Energy Uses Intake – 5 %  (0.19 kWh/kL) Product Water Delivery  6 %  RO System – 71 %  Pretreatment –  11 %  (0.40 kWh/kL) (2.54 kWh/kL) (0.20 kWh/kL) Other Facilities 7 % (0.24 kWh/kL) Total Energy Use  3.57 kWh/kgal
Optimizing RO System Performance ,[object Object],[object Object],[object Object],[object Object],[object Object]
2008-11  Evolving SWRO Membrane Performance ,[object Object],[object Object],[object Object],[object Object],[object Object]
2.6 MGD Power Seraja SWRO Plant, Singapore – 16-inch Elements
Large RO Elements – Key Manufacturers/Models Source: IDA  Journal, Vol. 2, 2010
Optimizing Performance by Redistributing Flux/Energy ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Courtesy  - Nikolay Voutchkov Flux is Proportional to the Difference of the Feed and Permeate Pressures
Second  (Brackish RO) Pass Concentrate – Second Pass Permeate Conventional RO System Configuration (Perth Seawater Desalination Plant – Perth I) HP Pump Booster Pump Concentrate – First Pass to ERD First (SWRO) Pass Courtesy  - Nikolay Voutchkov Feed Seawater
First (SWRO) Pass Smaller   Second  (Brackish RO) Pass Permeate Smaller  Booster Pump Split “Regulated” First Pass RO System Configuration (Gold Coast Desalination Plant) 20% to 40% of Total Permeate  Concentrate – Second Pass HP Pump Concentrate – First Pass to ERD Courtesy  - Nikolay Voutchkov Feed Seawater
First (SWRO) Pass Smaller   Second  (Brackish RO) Pass Permeate Smaller  Booster Pump Split “Regulated” First Pass RO System Configuration (Adelaide Desalination Plant) 20% to 40% of Total Permeate  Concentrate – Second Pass HP Pump Plug Concentrate – First Pass to ERD Courtesy  - Nikolay Voutchkov Feed Seawater
I nternally  S taged  D esign (1-1-5) ,[object Object],Compared to Standard SWRO Design, ISD SWRO Offers: - Higher average permeate flux with same lead element flux; - Good permeate quality;  - Energy Savings - 5% - 10%. Courtesy: Dow Filmtec Courtesy  - Nikolay Voutchkov Low Productivity/ High Salt Rejection  High Productivity/ Low Salt Rejection  7,500 gpd  9,000 gpd  12,500 gpd
Second  (Brackish RO) Pass Concentrate – Second Pass Permeate HP Pump Lower Feed Pressure Booster Pump Concentrate to ERD Low Productivity/ High Rejection  High Productivity/ Low Rejection  Internally-Staged Design (ISD) Courtesy  - Nikolay Voutchkov Feed Seawater
First SWRO Pass Smallest Second  (Brackish RO) Pass Permeate Smallest   Booster Pump ISD + Split “Regulated” RO System Configuration Southern Seawater Desalination Plant (Perth II) 20% to 40% of Total Permeate  Concentrate to ERD Concentrate – Second Pass HP Pump Lowest  Feed Pressure Courtesy  - Nikolay Voutchkov Feed Seawater
3-Center Design –  Pump, Energy Recovery & RO Membrane Centers Courtesy: IDE Highly Efficient  Energy Use 2.5 to 2.6 kWh/kgal Courtesy  - Nikolay Voutchkov
Bigger Pumps Rule! Pump Efficiency Increases with Size ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Perth, Australia –  6 Pumps for 12 RO Trains Ashkelon, Israel – (3+1) 7,100-hp Pumps per 16 RO Trains Courtesy  - Nikolay Voutchkov
Radially Split Case Pumps ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Courtesy  - Nikolay Voutchkov
Energy Recovery Systems  are Getting Bigger & More Efficient!
Pressure Exchangers Allow the Use of Larger Pumps/RO Trains Pelton Wheel Pressure Exchanger Provides 40 - 42 % of the Energy Provides 2 % of the Energy Provides 44-46 % of the Energy
ERI System – Current Status ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
ERI – New Energy Recovery Equipment ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
DWEER System – Current Status ,[object Object],[object Object],[object Object],[object Object],[object Object],Tuas, Singapore Triple DWEER 1100 4 MGD SWRO Trains
Calder AG (Flowserve) – ROVA 300 ,[object Object],[object Object],[object Object],[object Object]
Calder AG (Flowserve) – DWEER GA ,[object Object],[object Object],[object Object],[object Object]
Hydraulic Turbocharger – Large Installations (8.9 to 10.0 kWh/kgal) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Pump Efficiency  ~   n x (Q/H) 0.5 x (1/H) 0.25
CALDER – DWEER PRESSURE EXCHANGER CALDER - PELTON WHEEL IMPULSE TURBINE KSB – SALTEC PRESSURE EXCHANGER ERI - PX  PRESSURE EXCHANGER PEI – TURBO BOOSTER  AXIAL PISTON PRESSURE EXCHANGER PUMP Energy Recovery Devices The Sustainability of SWRO
IDE – IRIS  PRESSURE EXCHANGER ROVEX  PRESSURE EXCHANGER DYPREX PRESSURE EXCHANGER ERI – TITAN PX  PRESSURE EXCHANGER FEDCO HYDRAULIC PRESSURE BOOSTER Energy Recovery Devices The Sustainability of SWRO
AQUALING – ORIGINAL RECUPERATOR  PRESSURE EXCHANGER AQUALING –  NEW RECUPERATOR  PRESSURE EXCHANGER Energy Recovery Devices The Sustainability of SWRO
Biofouling –  Still the Key “Energy Chellenge”  of SWRO Desalination
Membrane Pretreatment is Becoming More Popular for Large Plants! ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
New “Tools” for Combating Biofouling ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
“ The Best” of Seawater Desalination Present Status & Future Forecasts Parameter Today Within 5 Years Within 20 Years Cost of Water  (2010 US$/kgal) US$2.0-3.0 US$1.5-2.5 US$1.0-1.5 Construction Cost (Million US$/kL/day) 1200-2150 1060-1720 530-930 Power Use of SWRO System (kWh/kL) 2.5-2.8 2.1-2.6 1.3-1.7 Membrane Productivity (gallons/day/membrane) 24-47 34-57 95-151 Membrane Useful Life (years) 5-7 7-10 10-15 Plant Recovery Ratio (%) 45-50 50-55 55-65
Selected Tariffs City Combined Tariff Average Domestic use (L/head/day) Adelaide $3.60/m 3  605 Brisbane  $4.85/m 3 605 Chicago $0.99/m 3   616 Copenhagen $8.00/m 3 114 Los Angeles $2.49/m 3 606 Melbourne $4.36/m 3 606 San Diego $4.93/m 3   616 Sydney  $5.03/m 3 606 Costs in US$ per cubic metre of water  =  Water + Wastewater fixed costs + Water Variable costs Wastewater variable costs Total Sales Tax Summary of key data from the 2010 GWI Global Water Tariff Survey
The Sustainability of SWRO
The Sustainability of SWRO In 1896 the worlds largest desalination plant was built in Western Australia at Coolgardie Mammoth Water Condenser,  Coolgardie Water Distillery, 132,000 gpd The ultimate in un-sustainability
It’s not about water. It’s about   energy!
Theoretical minimum SEC for seawater @ 35000 mg/L TDS is 2.83 kWh/kgal (0.748 kWhr /m 3  )   To convey 1 kgal of untreated water horizontally over 260 miles uses 12.38 kWh/kgal (3.3 kWh/m3) The Sustainability of SWRO Affordable Desalination Collaboration (ADC) Gold Coast Desalination Plant produces high quality water locally at 12.38 kWh/kgal (3.3 kWh/m3)
Responding to the Clear Trend of Global Warming! The total Energy Needed to Operate All California Desalination Projects  (1514 MLD) Will Result in 0.03 – 0.04 % Increase in the Current California Water Sector Energy Demand.
The Sustainability of SWRO Process Electrical Thermal  Total (kWh/m 3 )  (kWh/m 3 )  (kWh/m 3 ) MSF 3.2 – 3.7 9.8 – 6.8 13.0 – 10.5 MED 2.5 - 2.9 6.6 - 4.5 9.0 – 7.4 METC 2.0 - 2.5 12.0 - 6.5 14.0 - 9.0 MVC 8.0 - 17.0 N/A N/A SWRO 3.3  - 8.5  N/A 3.3  - 8.5 BWRO 1.0 - 2.5  N/A 1.0 - 2.5 Waste Water Reuse 1.0 - 2.5  N/A 1.0 - 2.5 Conventional 0.2 – 1.0 N/A 0.2 – 1.0 Water piped > 250 Miles 3.3 N/A 3.3 Specific Energy Consumption for Different Water Sources
Unit Costs of Carbon Footprint Reduction Alternatives CF Reduction Alternative Unit Cost of Carbon Footprint Reduction (US$/tons CO2 reduced) 1.  Collocation & Energy Efficient Technology US$20/ton CO2 2.  CO2 Use for Water Production US$70/ton CO2 3.  Purchase of Carbon Credits US$100/ton CO2 4.  Re-forestation US$200/ton CO2 5.  CO2 Sequestration in Coastal Wetlands US$400/ton CO2 6.  Solar Panels US$1,900/ton CO2 7.  Green Building Design US$3,400/ton CO2
$0.62 $1.07 $1.16 $5.10 0.5 1.0 <3.5 and reducing to 3.3 by 2010  12.0 0 2 4 6 8 10 12 14 Current metro bulk water South West Yarragadee Seawater Desalination Kimberley Pipeline Unit cost ($/m 3 ) Power (kWh/m 3 ) To convey 1 kL over 370 miles uses 3.3 kWh/m 3 Water Source Comparison  (including another unsustainable concept) The Sustainability of SWRO
Energy Comparison The Sustainability of SWRO Old Fridge Energy Requirement  = 1300 kWh/Year Efficient Desalination Plant (SEC)  Specific Energy Consumption  = 15.52 kWhr/kgal (4.1 kWh/m 3  )Total Equivalent Annual Water Production  =  84000 gallons   /year  (317 m 3 /year) Garage Fridge  =  A single total domestic water use  per year inside and outside Reverse Cycle Air 8 kW @ 4 h/day in Winter and Summer (6 months) = 5760 kW/h (Water for 4.5 homes)
Energy Comparison – The MacMansion The Sustainability of SWRO Temperature under black roof 61 ° C.  Radiated heat 26  ° C inside house Temperature under reflective roof 31 ° C. Radiated Heat 39  ° C inside house.
Energy Comparison – The MacMansion The Sustainability of SWRO If you look at all the energy requirements of  new homes (City Beach 8858 kW/hr per year average per home) you would not believe there is a greenhouse gas emission issue.  Some Big Mac’s (supersized) have up to 15 kW air conditioning systems. To add insult to injury, the latest fashion is a black roof with no eaves – additional air conditioning required  (high calories – just like the Big Mac supersized).  Reverse Cycle Air 15 kW @ 4 hr/day in Winter and Summer (6 months) = 10800 kW/h (SWRO water for 8.5 homes I did not see one black roof on the Canary Islands (and I do not think it was just because the islanders have aesthetic appreciation).
Energy Comparison – The MacMansion The Sustainability of SWRO The West Australian Tuesday March 8 2007 Record heat ruins fruit, drains power Western Power claimed it coped with the increased demand despite using temporary generators as power consumption hit a peak of 3574MW at 4.55 pm, beating Tuesday’s high of 3533 MW. The Perth Seawater Desalination Plant uses  0.67%  of this energy, whilst Perth was using over  30%  of the energy for air-conditioning. Note the new umbilical cords to ensure that the black roof keeps the Big Mac cool inside
[object Object],So …
= + + + + + The Sustainability of SWRO Energy Comparisons
or, how many PSDP’s? The Sustainability of SWRO Energy Comparisons = + +
and the answer is! Taking Off Power  = 77 MW  Cruising Power = 65 MW Full Power of One Engine = 26 MW Full Power Requirement PSDP = 24 MW The Sustainability of SWRO Energy Comparisons Water for 405,000 homes (Aus) 300,000 homes (USA) or a total 116,000 passengers transported in one year assuming Jumbo is always full, and Jumbo’s cannot use renewable energy. + + = One Jumbo Jet
[object Object],So …
= + + + + + The Sustainability of SWRO Energy Comparisons
or, how many PSDP’s? The Sustainability of SWRO Energy Comparisons = + + +
and the answer is! ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],The Sustainability of SWRO Energy Comparisons = + + +
Surface Water Source – Serpentine Dam Courtesy of the Water Corporation Not So Sustainable
Seawater Desalination vs.  Surface Water Source ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Footprint Comparison – Serpentine Dam
Where Future Cost Savings Will Come From?
Main Areas Expected to Yield Cost Savings in the Next 5 Years (20 % Cost Reduction Target) ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Nano-Structured SWRO Membranes
Potential to Reduce 60 to 80 % of Energy Costs & 15 to 25 % of Cost of Water Source: OASYS
Harnessing Osmotic Power Source: Statkraft
Osmotic Power – A Competitive Energy Source Source: Statkraft
Desalination Energy Use Factors
Why SWRO is Sustainable & the Future Solution ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Why SWRO is Sustainable & the Future Solution ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Why SWRO is Sustainable & the Future Solution ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Concluding Remarks ,[object Object],[object Object],[object Object],[object Object]
“ I have said that I thought if we could ever competitively get fresh water from saltwater…that it would be in the long range interests of humanity which would really dwarf any other scientific accomplishment.” John F. Kennedy, September 22, 1961  “ If we could produce clean unlimited energy at a viable cost, that would  indeed be a great service to humanity and would dwarf any other scientific accomplishment.” Gary J. Crisp, 2006
Perth Seawater Desalination Plant Awarded GWI World Membrane Desalination Plant of the Year 2007 ERI Awarded GWI Environmental Contribution of the Year 2007 Courtesy of ERI Courtesy of Water Corporation
Gold Coast Desalination Plant Awarded GWI World Membrane Desalination Plant of the Year   2009 Courtesy of WaterSecure
International Desalination Association Awarded 2011 World Congress - to Perth  Western Australia See You There!
Questions? Thank you.
Pseudo Greenies and Nimby’s
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Fuelling the Future
Nuclear Fusion (Hans Bethe) 1938 ,[object Object],[object Object],[object Object],[object Object],[object Object]
Nuclear Fusion (Hans Bethe) 1938 ,[object Object],[object Object],[object Object],[object Object]
Nuclear Fission (Otto Hahn, Leis Meitner and Fritz Strassmann) 1938 ,[object Object],[object Object],[object Object],[object Object]

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Chemical Panel Engineers Australia WA Division &amp; The Institution of Chemical Engineers (WA) Gary J. Crisp Global Business Leader – Desalination: GHD

  • 1. Chemical Panel Engineers Australia WA Division & The Institution of Chemical Engineers (WA) Gary J. Crisp Global Business Leader – Desalination: GHD BSc. Civil Engineering, C Eng., MICE, CP Eng., FIE Aust., PMP Auditorium, Engineers Australia 712 Murray Street, West Perth, WA Monday, 14 March 2011 Desalination Sustainably Drought Proofing Australia
  • 2. It’s not about water. It’s about energy!
  • 3. “ Energy is eternal delight!” Energy is liberation. William Blake, author, poet, visionary, 1757 – 1827
  • 4. Energy Use Across the Water Cycle (1kWh/m 3 = 3.79 kWh/kgal - 4 kWh/m 3 = 15.14 kWh/kgal) California State Water Project = 2.5 kWh/m 3 = 9.50 kWh/kgal Gold Coast Desalination Plant = 3.23 kWh/m 3 = 12.24 kWh/kgal SOURCE TRANSPORT WTP DISTRIBUTION WWTP COLLECTION USE DISPOSAL/ RECYCLE
  • 5.
  • 6. Desalination – Where Are We Today? 14,754 Desalination Plants Worldwide – 16,700 MGD Source : IDA Desalination Yearbook 2009-2010
  • 7. Source: WDR, July 2010 Projected New Desalination Capacity in 2010 6.8 GL/day Actual New Capacity in 2009 3.9 GL/day
  • 8.
  • 9. Membrane Separation - Filtration Spectrum Courtesy of Osmonics
  • 10. Reverse Osmosis Water Molecules Protozoa Bacteria Virus Organics Inorganics An RO Membrane is like a Microscopic Strainer that allows Water Molecules to pass through
  • 12. Seawater Reverse Osmosis (SWRO) 0.77 bar per 1000 mg/L
  • 13.
  • 14. 0.2 µm 40 µm 120 µm Polyamide Polysulfone Ultra thin Barrier Layer Microporous Polysulfone Substrate Reinforcing Polyester Fabric Cross-Section TFC
  • 15. Membrane arrangement Membrane element Feed spacer Permeate spacer Membrane leaf
  • 16. Reverse Osmosis Spiral Wound Membrane
  • 18.
  • 19.
  • 20.
  • 21.
  • 22. Perth Seawater Desalination Plant 6.5 ha 3 ha
  • 23.
  • 24. Seawater Intake Pre-treatment SWRO & BWRO Remineralisation/Storage Potable water pump station Residuals Treatment Brine discharge HV substation Admin/Lab Chemical Storage Aerial View of Desalination Plant Raw Seawater screen and pump station Brine discharge Courtesy of Water Corporation
  • 25. Perth Seawater Desalination Plant Seawater Intake System – Inlet Structure Courtesy of the Water Corporation
  • 26. Perth Seawater Desalination Plant Courtesy of the Water Corporation Seawater Intake System – Inlet Structure
  • 27. Perth Seawater Desalination Plant Courtesy of the Water Corporation Courtesy of the Water Corporation Seawater Intake System – Pipes and Works
  • 28. Perth Seawater Desalination Plant Onshore Active Screening – Band Screen Courtesy of the Water Corporation
  • 29. Perth Seawater Desalination Plant Seawater Intake and Outlet Works Courtesy of the Water Corporation
  • 30. Perth Seawater Desalination Plant Single Stage Dual Media Pressure Filtration and Cartridge Filters
  • 31. Perth Seawater Desalination Plant Each Pump Equivalent to 15 Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each.* *Red Book (Australia) specifications High Pressure Pumps 2.6 MW Each (6 in total) Courtesy of the Water Corporation
  • 32. Perth Seawater Desalination Plant PRETREATED WATER PRODUCTION HP Pump Energy Recovery System (12 x 16 in Parallel) REJECT (Common By-pass) 2 nd Stage 1 st Stage 1 ST PASS FEEDING (recycling) First Pass Second Pass MDJV in Alliance with Water Corporation Reverse Osmosis Process Flow – Operating Principals & Arrangement
  • 33. Perth Seawater Desalination Plant Circulation Pumps 134 kW each (12 in total) Courtesy of the Water Corporation Each Pump Equivalent to 1 Toyota RAV 4 5st 4dr Man 4x4 2.0i 0.132 MW @ 5200rpm each.* *Red Book (Australia) specifications
  • 34. Perth Seawater Desalination Project (PSDP) First Pass Reverse Osmosis Racks
  • 35. Perth Seawater Desalination Plant RO Building Looking South – 2 nd Pass RO Courtesy of the Water Corporation
  • 36. Perth Seawater Desalination Plant Each Rack Equivalent to 8 Ford Escape Wagon 4dr Auto 4sp 4x4 3.0i 0.152 MW @ 4750rpm each.* *Red Book (Australia) specifications Pressure Exchanger Rack 1.2 MW each (12 in total) Courtesy of Water Corporation
  • 37. Perth Seawater Desalination Project PX Process
  • 38. Perth Seawater Desalination Project Beyond Tomorrow
  • 39. Perth Seawater Desalination Plant Potabilization System and Drinking Water Storage Tank Courtesy of Water Corporation
  • 40. Perth Seawater Desalination Plant Drinking Water Transfer Pump Station Courtesy of Water Corporation
  • 41. Perth Seawater Desalination Plant Concentrate Discharge Courtesy of Water Corporation
  • 42. Perth Seawater Desalination Plant Concentrate Discharge Courtesy of Water Corporation
  • 44. Perth Seawater Desalination Project Long Term Monitoring Macrobenthic To monitor the response of the sediment fauna over several years Benthic macrofauna pilot survey – complete Benthic macrofauna comprehensive baseline survey – commenced March 2006 Annual monitoring (for three years initially)
  • 45. Perth Seawater Desalination Plant 50 m limit for mixing zone 30 m mixing zone – achieve 42 x dilution Outfall pipeline Brine Discharge System 20 diffuser ports at 5 m spacing 3 Ha
  • 46. Perth Seawater Desalination Plant Initial mixing zone = 100 metres 45x dilution farfield diffuser Courtesy of Water Corporation Seawater Concentrate - Salinity water surface
  • 47. Perth Seawater Desalination Project Baseline DO
  • 48. Perth Seawater Desalination Plant Real Time Monitoring Courtesy of Water Corporation
  • 49. Perth Seawater Desalination Plant These tests proved the Mathematical / Computer Model analyses. Note the marine growth on the diffuser ports. Rhodamine Dye Test Courtesy of Water Corporation
  • 50. Under the Surface Courtesy of the Water Corporation
  • 51. Sustainable Power - Wind Energy for PSDP Greenhouse Gas Emissions (tonnes per annum) Stanwell/Griffin Joint Venture - Emu Downs wind generation facility – 100 Miles North of Perth Water Corporation is purchasing 68 percent of the energy output 0 85,000 231,000 24 MW (21.1 MW average - 185 GW hrs/annum) Renewable or Sequestration Gas Grid Option Energy
  • 52. Courtesy of the Water Corporation Zero Greenhouse Gas Emissions Stanwell/Griffin Joint Venture - Emu Downs wind generation facility – at Badgingarra 200 north of Perth Water Corporation is purchasing 66 percent of the energy output 24 MW (185 GW hrs/annum) Opened on 12 November 2006 Perth Seawater Desalination Plant Sustainable Power - Wind Energy
  • 53.
  • 54. Perth Seawater Desalination Plant Courtesy of the Water Corporation
  • 55. The Big Six – No. 1 Perth Seawater Desalination Plant – Demonstration Plant
  • 56. Perth Seawater Desalination Project Plant Load Requirements Single Source 132 kV supply from Western Power 417 V Yes     Minor Drives Only Post Treatment Switchboard 416 V Yes 560 4 Drinking Water Pumps Drinking Water Switchboard 415 V Yes 110 12 RO Pass 1 HP Booster Pumps RO Auxiliary Switch Board 690 V Yes 630 6 RO Pass 2 HP pumps RO Pass 2 Switchboard 11 kV No 2,500 6 RO Pass 1 HP pumps Main Switchboard 690 V Yes 560 6 Seawater Intake Pumps Seawater Intake Switchboard     (kW)       Voltage Selected Variable Speed Requirement Drive Size Number Drives Serviced Application
  • 57. Perth Seawater Desalination Project Specific Energy Consumption of Components and Total *approx 7 miles of conveyance to Perth Integrated Water Supply System (IWSS) 3.60 3.48 0.21* 0.19 516,487 7,988* 501,271 7,228 144 kWh/kL kWh/kL kWh/kL kWh/kL kWh kWh kWh kWh ML Total Plant Desal Plant Only Potable Water Pumping Intake Pumping Excluding Pre-Treatment Total Plant Potable Pumping Desal Plant Plus Pre-Treatment Only Intake Pumping Total Potable Water Production Perth Seawater Desalination Plant - Specific Energy Consumption (SEC) for Components of Plant
  • 58.
  • 59.
  • 60.
  • 61.
  • 62. REVERSE OSMOSIS RESIDUALS REMINERALISATION OUTFALL PRETEATMENT INTAKE
  • 63. Seawater Intake & screen Pre-treatment SWRO & BWRO Remineralisation/Storage Potable water pump station Residuals Treatment Brine discharge shaft HV substation Admin/Lab Chemical Storage Aerial View of Desalination Plant
  • 64. Twin 2.5 OD intake/outfall tunnels 2.2 km & 2.0 km sized for 340 MLD 125 MLD Plant ave. 94% availability 133 MLD peak daily production 26 km 1.1 m distribution main 30 ML reservoir & pump station
  • 66.
  • 67.
  • 68.
  • 69.
  • 70.  
  • 71. 2.11 m 6.32 m Seawater Intake - Coarse Screen
  • 72.
  • 74.
  • 75.
  • 76.
  • 77. 4 x High Pressure Pumps 4.8 MW Each (Each equivalent to 28 Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each - Red Book Specifications) Desalination Plant Feed – 1 st Pass
  • 78.
  • 79. Energy Recovery Device - 1 st Pass Pressure Exchanger Rack 1.6 MW Each (9 racks in total) (Equivalent to 11 Mazda Tribute Wagon 4dr Auto 4sp 4x4 3.0i 0.152 MW @ 4750rpm each - Red Book Specifications) Re-circulation Pumps 180 kW Each Equivalent to 11 Toyota Lexus GX Wagon 8st 4dr Man 6sp 4x4 4.0i 0.179 MW @ 5200rpm each - Red Book Specifications)
  • 80. RO Building Pressure Vessel Racks - 1 st Pass
  • 81.
  • 82.
  • 83.
  • 84. Diffuser 6.0 yd 6.5 yd 1200mm PE
  • 85.
  • 86. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2
  • 87. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2
  • 88. Courtesy of WaterSecure Gold Coast Desalination Plant - 35 mgd (133 MLD) The Big Six – No. 2
  • 89. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 My Office for 2 years
  • 90. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD)
  • 91. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 Minimal Drum Screen Screenings (note the “Wheelie Bin”) Drum Screen 1/8 inch (3mm) mesh American Translation “Trash Can”
  • 92. Courtesy of WaterSecure Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 3 duty 1 standby High Pressure Pumps (4.8 MW each)
  • 93. Gold Coast Desalination Plant Specific Energy Consumption of Components and Total *approx 26 km of conveyance to system with high static head 3.54 3.05 0.35* 0.15 489,256 47,725* 463,590 20,941 36,137 kWh/kL kWh/kL kWh/kL kWh/kL kWh kWh kWh kWh kgal Total Plant Desal Plant Only Potable Water Pumping Intake Pumping Including Pre-Treatment Total Plant Potable Pumping Desal Plant Plus Pre-Treatment Only Intake Pumping Total Potable Water Production Gold Coast Desalination Plant - Specific Energy Consumption (SEC) for Components of Plant
  • 94. Gold Coast Desalination Plant - 36 mgd (133 MLD) The Big Six – No. 2 Why So Expensive? Wonthaggi Desalination Plant – Electricians $220,000/year Connecting System (IWSS): $198 million Total Capital Cost: $943 million Total Operating Cost: $32 million/year Unit Cost: $2.38/kL
  • 95.
  • 96. The Big Six – No. 3 Courtesy of Sydney Water Sydney Desalination Plant - 66 mgd (250 MLD) – Expandable to 132 mgd (500 MLD)
  • 97.
  • 98. Adelaide Desalination Plants I and II – 40 + 40 mgd (150 MLD each) The Big Six – No. 4 Courtesy of SA Water
  • 99.
  • 100. Southern Seawater Desalination Plant (Perth II) 150 MLD (40 mgd) Expandable to 300 MLD (80 mgd) The Big Six – No. 5 Courtesy of Water Corporation
  • 101.
  • 102. The Victorian Desalination Project - 120 mgd (450 MLD) then 160 mgd (600 MLD) The Big Six – No. 6 Courtesy of Victorian Government
  • 103.  
  • 104.
  • 105.
  • 106.
  • 107. Year 2005-2010 The Five Lowest-Cost SWRO Projects Worldwide SWRO Plant Cost of Water (US$/kL) Power Use of RO System (kWh/kL) & TDS (ppt) Sorek, Israel – 409 MLD (startup – 2014) 0.53 2.59 (40 ppt) Mactaa, Algeria – 719 MLD (startup – 2013) 0.56 2.56 (39 ppt) Tuas, Singapore – 136 MLD (startup – 2007) 0.57 3.04 (34 ppt) Tenes, Algeria – 200 MLD (startup – 2011) 0.59 2.85 (38 ppt) Hadera, Israel – 329 MLD (startup – 2010) 0.60 2.67 (40 ppt)
  • 108.
  • 109. Reducing Power Use for SWRO Separation - Still a Hair Rising Challenge? Lowest Theoretical Energy Use = 0.75 kWh/kL (100 % Recovery) Lowest Theoretical Energy Use @ 50 % Recovery = 1.09kWh/kL ADC - Lowest Energy Use @ 42 % Recovery & 10.2 LMH = 1.59 kWh/kL ADC – “Most Affordable Point” 48 % Recovery & 15.3 LMH = 2.01 kWh/kL Low Bracket of Energy Use for Large SWRO Projects (45-50 % Recovery & 14.3 to 16.3 LMH ) = 2.51 to 2.74 kWh/kL Note: All Energy Use Values for Seawater @ TDS = 35 ppt & 25ºC
  • 110. SWRO Power Consumption (July 1, 2001)
  • 111. 50 MGD SWRO Plant – Key Energy Uses Intake – 5 % (0.19 kWh/kL) Product Water Delivery 6 % RO System – 71 % Pretreatment – 11 % (0.40 kWh/kL) (2.54 kWh/kL) (0.20 kWh/kL) Other Facilities 7 % (0.24 kWh/kL) Total Energy Use 3.57 kWh/kgal
  • 112.
  • 113.
  • 114. 2.6 MGD Power Seraja SWRO Plant, Singapore – 16-inch Elements
  • 115. Large RO Elements – Key Manufacturers/Models Source: IDA Journal, Vol. 2, 2010
  • 116.
  • 117. Second (Brackish RO) Pass Concentrate – Second Pass Permeate Conventional RO System Configuration (Perth Seawater Desalination Plant – Perth I) HP Pump Booster Pump Concentrate – First Pass to ERD First (SWRO) Pass Courtesy - Nikolay Voutchkov Feed Seawater
  • 118. First (SWRO) Pass Smaller Second (Brackish RO) Pass Permeate Smaller Booster Pump Split “Regulated” First Pass RO System Configuration (Gold Coast Desalination Plant) 20% to 40% of Total Permeate Concentrate – Second Pass HP Pump Concentrate – First Pass to ERD Courtesy - Nikolay Voutchkov Feed Seawater
  • 119. First (SWRO) Pass Smaller Second (Brackish RO) Pass Permeate Smaller Booster Pump Split “Regulated” First Pass RO System Configuration (Adelaide Desalination Plant) 20% to 40% of Total Permeate Concentrate – Second Pass HP Pump Plug Concentrate – First Pass to ERD Courtesy - Nikolay Voutchkov Feed Seawater
  • 120.
  • 121. Second (Brackish RO) Pass Concentrate – Second Pass Permeate HP Pump Lower Feed Pressure Booster Pump Concentrate to ERD Low Productivity/ High Rejection High Productivity/ Low Rejection Internally-Staged Design (ISD) Courtesy - Nikolay Voutchkov Feed Seawater
  • 122. First SWRO Pass Smallest Second (Brackish RO) Pass Permeate Smallest Booster Pump ISD + Split “Regulated” RO System Configuration Southern Seawater Desalination Plant (Perth II) 20% to 40% of Total Permeate Concentrate to ERD Concentrate – Second Pass HP Pump Lowest Feed Pressure Courtesy - Nikolay Voutchkov Feed Seawater
  • 123. 3-Center Design – Pump, Energy Recovery & RO Membrane Centers Courtesy: IDE Highly Efficient Energy Use 2.5 to 2.6 kWh/kgal Courtesy - Nikolay Voutchkov
  • 124.
  • 125.
  • 126. Energy Recovery Systems are Getting Bigger & More Efficient!
  • 127. Pressure Exchangers Allow the Use of Larger Pumps/RO Trains Pelton Wheel Pressure Exchanger Provides 40 - 42 % of the Energy Provides 2 % of the Energy Provides 44-46 % of the Energy
  • 128.
  • 129.
  • 130.
  • 131.
  • 132.
  • 133.
  • 134. CALDER – DWEER PRESSURE EXCHANGER CALDER - PELTON WHEEL IMPULSE TURBINE KSB – SALTEC PRESSURE EXCHANGER ERI - PX PRESSURE EXCHANGER PEI – TURBO BOOSTER AXIAL PISTON PRESSURE EXCHANGER PUMP Energy Recovery Devices The Sustainability of SWRO
  • 135. IDE – IRIS PRESSURE EXCHANGER ROVEX PRESSURE EXCHANGER DYPREX PRESSURE EXCHANGER ERI – TITAN PX PRESSURE EXCHANGER FEDCO HYDRAULIC PRESSURE BOOSTER Energy Recovery Devices The Sustainability of SWRO
  • 136. AQUALING – ORIGINAL RECUPERATOR PRESSURE EXCHANGER AQUALING – NEW RECUPERATOR PRESSURE EXCHANGER Energy Recovery Devices The Sustainability of SWRO
  • 137. Biofouling – Still the Key “Energy Chellenge” of SWRO Desalination
  • 138.
  • 139.
  • 140. “ The Best” of Seawater Desalination Present Status & Future Forecasts Parameter Today Within 5 Years Within 20 Years Cost of Water (2010 US$/kgal) US$2.0-3.0 US$1.5-2.5 US$1.0-1.5 Construction Cost (Million US$/kL/day) 1200-2150 1060-1720 530-930 Power Use of SWRO System (kWh/kL) 2.5-2.8 2.1-2.6 1.3-1.7 Membrane Productivity (gallons/day/membrane) 24-47 34-57 95-151 Membrane Useful Life (years) 5-7 7-10 10-15 Plant Recovery Ratio (%) 45-50 50-55 55-65
  • 141. Selected Tariffs City Combined Tariff Average Domestic use (L/head/day) Adelaide $3.60/m 3 605 Brisbane $4.85/m 3 605 Chicago $0.99/m 3 616 Copenhagen $8.00/m 3 114 Los Angeles $2.49/m 3 606 Melbourne $4.36/m 3 606 San Diego $4.93/m 3 616 Sydney $5.03/m 3 606 Costs in US$ per cubic metre of water = Water + Wastewater fixed costs + Water Variable costs Wastewater variable costs Total Sales Tax Summary of key data from the 2010 GWI Global Water Tariff Survey
  • 143. The Sustainability of SWRO In 1896 the worlds largest desalination plant was built in Western Australia at Coolgardie Mammoth Water Condenser, Coolgardie Water Distillery, 132,000 gpd The ultimate in un-sustainability
  • 144. It’s not about water. It’s about energy!
  • 145. Theoretical minimum SEC for seawater @ 35000 mg/L TDS is 2.83 kWh/kgal (0.748 kWhr /m 3 ) To convey 1 kgal of untreated water horizontally over 260 miles uses 12.38 kWh/kgal (3.3 kWh/m3) The Sustainability of SWRO Affordable Desalination Collaboration (ADC) Gold Coast Desalination Plant produces high quality water locally at 12.38 kWh/kgal (3.3 kWh/m3)
  • 146. Responding to the Clear Trend of Global Warming! The total Energy Needed to Operate All California Desalination Projects (1514 MLD) Will Result in 0.03 – 0.04 % Increase in the Current California Water Sector Energy Demand.
  • 147. The Sustainability of SWRO Process Electrical Thermal Total (kWh/m 3 ) (kWh/m 3 ) (kWh/m 3 ) MSF 3.2 – 3.7 9.8 – 6.8 13.0 – 10.5 MED 2.5 - 2.9 6.6 - 4.5 9.0 – 7.4 METC 2.0 - 2.5 12.0 - 6.5 14.0 - 9.0 MVC 8.0 - 17.0 N/A N/A SWRO 3.3 - 8.5 N/A 3.3 - 8.5 BWRO 1.0 - 2.5 N/A 1.0 - 2.5 Waste Water Reuse 1.0 - 2.5 N/A 1.0 - 2.5 Conventional 0.2 – 1.0 N/A 0.2 – 1.0 Water piped > 250 Miles 3.3 N/A 3.3 Specific Energy Consumption for Different Water Sources
  • 148. Unit Costs of Carbon Footprint Reduction Alternatives CF Reduction Alternative Unit Cost of Carbon Footprint Reduction (US$/tons CO2 reduced) 1. Collocation & Energy Efficient Technology US$20/ton CO2 2. CO2 Use for Water Production US$70/ton CO2 3. Purchase of Carbon Credits US$100/ton CO2 4. Re-forestation US$200/ton CO2 5. CO2 Sequestration in Coastal Wetlands US$400/ton CO2 6. Solar Panels US$1,900/ton CO2 7. Green Building Design US$3,400/ton CO2
  • 149. $0.62 $1.07 $1.16 $5.10 0.5 1.0 <3.5 and reducing to 3.3 by 2010 12.0 0 2 4 6 8 10 12 14 Current metro bulk water South West Yarragadee Seawater Desalination Kimberley Pipeline Unit cost ($/m 3 ) Power (kWh/m 3 ) To convey 1 kL over 370 miles uses 3.3 kWh/m 3 Water Source Comparison (including another unsustainable concept) The Sustainability of SWRO
  • 150. Energy Comparison The Sustainability of SWRO Old Fridge Energy Requirement = 1300 kWh/Year Efficient Desalination Plant (SEC) Specific Energy Consumption = 15.52 kWhr/kgal (4.1 kWh/m 3 )Total Equivalent Annual Water Production = 84000 gallons /year (317 m 3 /year) Garage Fridge = A single total domestic water use per year inside and outside Reverse Cycle Air 8 kW @ 4 h/day in Winter and Summer (6 months) = 5760 kW/h (Water for 4.5 homes)
  • 151. Energy Comparison – The MacMansion The Sustainability of SWRO Temperature under black roof 61 ° C. Radiated heat 26 ° C inside house Temperature under reflective roof 31 ° C. Radiated Heat 39 ° C inside house.
  • 152. Energy Comparison – The MacMansion The Sustainability of SWRO If you look at all the energy requirements of new homes (City Beach 8858 kW/hr per year average per home) you would not believe there is a greenhouse gas emission issue. Some Big Mac’s (supersized) have up to 15 kW air conditioning systems. To add insult to injury, the latest fashion is a black roof with no eaves – additional air conditioning required (high calories – just like the Big Mac supersized). Reverse Cycle Air 15 kW @ 4 hr/day in Winter and Summer (6 months) = 10800 kW/h (SWRO water for 8.5 homes I did not see one black roof on the Canary Islands (and I do not think it was just because the islanders have aesthetic appreciation).
  • 153. Energy Comparison – The MacMansion The Sustainability of SWRO The West Australian Tuesday March 8 2007 Record heat ruins fruit, drains power Western Power claimed it coped with the increased demand despite using temporary generators as power consumption hit a peak of 3574MW at 4.55 pm, beating Tuesday’s high of 3533 MW. The Perth Seawater Desalination Plant uses 0.67% of this energy, whilst Perth was using over 30% of the energy for air-conditioning. Note the new umbilical cords to ensure that the black roof keeps the Big Mac cool inside
  • 154.
  • 155. = + + + + + The Sustainability of SWRO Energy Comparisons
  • 156. or, how many PSDP’s? The Sustainability of SWRO Energy Comparisons = + +
  • 157. and the answer is! Taking Off Power = 77 MW Cruising Power = 65 MW Full Power of One Engine = 26 MW Full Power Requirement PSDP = 24 MW The Sustainability of SWRO Energy Comparisons Water for 405,000 homes (Aus) 300,000 homes (USA) or a total 116,000 passengers transported in one year assuming Jumbo is always full, and Jumbo’s cannot use renewable energy. + + = One Jumbo Jet
  • 158.
  • 159. = + + + + + The Sustainability of SWRO Energy Comparisons
  • 160. or, how many PSDP’s? The Sustainability of SWRO Energy Comparisons = + + +
  • 161.
  • 162. Surface Water Source – Serpentine Dam Courtesy of the Water Corporation Not So Sustainable
  • 163.
  • 164. Where Future Cost Savings Will Come From?
  • 165.
  • 167. Potential to Reduce 60 to 80 % of Energy Costs & 15 to 25 % of Cost of Water Source: OASYS
  • 168. Harnessing Osmotic Power Source: Statkraft
  • 169. Osmotic Power – A Competitive Energy Source Source: Statkraft
  • 171.
  • 172.
  • 173.
  • 174.
  • 175. “ I have said that I thought if we could ever competitively get fresh water from saltwater…that it would be in the long range interests of humanity which would really dwarf any other scientific accomplishment.” John F. Kennedy, September 22, 1961  “ If we could produce clean unlimited energy at a viable cost, that would indeed be a great service to humanity and would dwarf any other scientific accomplishment.” Gary J. Crisp, 2006
  • 176. Perth Seawater Desalination Plant Awarded GWI World Membrane Desalination Plant of the Year 2007 ERI Awarded GWI Environmental Contribution of the Year 2007 Courtesy of ERI Courtesy of Water Corporation
  • 177. Gold Coast Desalination Plant Awarded GWI World Membrane Desalination Plant of the Year 2009 Courtesy of WaterSecure
  • 178. International Desalination Association Awarded 2011 World Congress - to Perth Western Australia See You There!
  • 180. Pseudo Greenies and Nimby’s
  • 181.
  • 182.
  • 183.
  • 184.

Editor's Notes

  1. This version edited August 26, 2009.
  2. ACKNOWLEDGE THE CONTRIBUTION OF THE CUST. ADVISORY COUNCIL A key tool to assist in the Water Corporation’s endeavours to anticipate customer needs and deliver innovative customer service. The Corporation is committed to establishing closer links with its customers and establishing avenues for effective two-way communication. A close working relationship with groups such as the Customer Advisory Council helps the Corporation to understand and keep pace with changing customer needs and to shape our business accordingly. Residential/Commercial customer satisfaction levels high (86%) Thank the Customer Advisory Council for their contribution to improving the Corporation’s relationship with its customers
  3. ACKNOWLEDGE THE CONTRIBUTION OF THE CUST. ADVISORY COUNCIL A key tool to assist in the Water Corporation’s endeavours to anticipate customer needs and deliver innovative customer service. The Corporation is committed to establishing closer links with its customers and establishing avenues for effective two-way communication. A close working relationship with groups such as the Customer Advisory Council helps the Corporation to understand and keep pace with changing customer needs and to shape our business accordingly. Residential/Commercial customer satisfaction levels high (86%) Thank the Customer Advisory Council for their contribution to improving the Corporation’s relationship with its customers
  4. Lets look at energy use across the complete water cycle. What we have seen in the last 100 years is that urbanisation and demand for higher water quality is driving up the energy footprint of water. Originally most schemes linear and very low energy footprints Source water close to population and limited treatment Mention Kalgoorlie, State Water project Briefly go over each element – higher water quality –more energy Western Corridor, NewWater at the other end
  5. ACKNOWLEDGE THE CONTRIBUTION OF THE CUST. ADVISORY COUNCIL A key tool to assist in the Water Corporation’s endeavours to anticipate customer needs and deliver innovative customer service. The Corporation is committed to establishing closer links with its customers and establishing avenues for effective two-way communication. A close working relationship with groups such as the Customer Advisory Council helps the Corporation to understand and keep pace with changing customer needs and to shape our business accordingly. Residential/Commercial customer satisfaction levels high (86%) Thank the Customer Advisory Council for their contribution to improving the Corporation’s relationship with its customers
  6. A membrane consists usually of three layers. The active separating layer is cast on a polysulphone microfiltration membrane, and the whole is supported on a non-woven polyester for mechanical stability
  7. Complex integrated scheme Unique in Australia (one dam systems in Melbourne and Sydney) Multiple sources provide robust system + security Groundwater + surface water - spread geographically, complex system Variability of chemical constituents of water Dams - 10 major, 3 pump backs, 2 pipehead Groundwater schemes – 8 and 12 independent artesian bores 202 bores in total, 41 turned off for environmental reasons ***Integrating the desalination supply adds further complexity Investment $678M over past decade Increased source capacity 192GL
  8. The procurement strategy consisted of four broad phases being: 1. Registration of Interest 2. Preselection process [3 months] Presentations, Interviews and evaluation / selection of top two: Australian Desal Company - Ondeo Degremont, Multiplex Constructions, and Australian Water Services Perth Desal Company - Vivendi Water, United KG, Leightons &amp; Sinclair Knight &amp; Merz Development of participation; Award of Project Development Phase 3. Project development phase [~6 months] Delivering a detailed technical and commercial proposal Two teams work in competition and are paid for their work on a cost-reimbursable basis 4. Construction and operations phase [18-20 months] Project Structure Beneficial, as hasn’t committed industry to large sums of money Can accommodate either PPP or DBO Alliance. Provides significant flexibility to cope with changing circumstances and constraints
  9. The procurement strategy consisted of four broad phases being: 1. Registration of Interest 2. Preselection process [3 months] Presentations, Interviews and evaluation / selection of top two: Australian Desal Company - Ondeo Degremont, Multiplex Constructions, and Australian Water Services Perth Desal Company - Vivendi Water, United KG, Leightons &amp; Sinclair Knight &amp; Merz Development of participation; Award of Project Development Phase 3. Project development phase [~6 months] Delivering a detailed technical and commercial proposal Two teams work in competition and are paid for their work on a cost-reimbursable basis 4. Construction and operations phase [18-20 months] Project Structure Beneficial, as hasn’t committed industry to large sums of money Can accommodate either PPP or DBO Alliance. Provides significant flexibility to cope with changing circumstances and constraints
  10. The procurement strategy consisted of four broad phases being: 100% Traveling Band Screens Wet Well (Dry Well Forwarding Pumps, through duel media filters, cartridge filters and on to HP pumps) Media Filters 2 Banks 12 pressure filters (52 m2 each) SDI &lt; 3 Two Pass Bromide &lt; 0.1 mg/L TDS approximately &lt; 45 mg/L Energy Recovery Pressure Exchangers PX by ERI
  11. TechnoBiz Training Program (www.technobiz-asia.com)
  12. TechnoBiz Training Program (www.technobiz-asia.com)
  13. Time Constraints Power Consumption Power Consumption - 14-17 MW daily average required to produce 30 GL/a for plant efficiency of between 4 &amp; 5 kWh/kL. Seawater Conditions Favourable indicating that pre-treatment costs likely to be minimised Deliverables Environmental Approval Obtained Two consortia selected for PDP Site Selection narrowed to two sites Feasibility Study completed
  14. TechnoBiz Training Program (www.technobiz-asia.com)
  15. TechnoBiz Training Program (www.technobiz-asia.com)
  16. TechnoBiz Training Program (www.technobiz-asia.com)
  17. TechnoBiz Training Program (www.technobiz-asia.com)
  18. TechnoBiz Training Program (www.technobiz-asia.com)
  19. ACKNOWLEDGE THE CONTRIBUTION OF THE CUST. ADVISORY COUNCIL A key tool to assist in the Water Corporation’s endeavours to anticipate customer needs and deliver innovative customer service. The Corporation is committed to establishing closer links with its customers and establishing avenues for effective two-way communication. A close working relationship with groups such as the Customer Advisory Council helps the Corporation to understand and keep pace with changing customer needs and to shape our business accordingly. Residential/Commercial customer satisfaction levels high (86%) Thank the Customer Advisory Council for their contribution to improving the Corporation’s relationship with its customers
  20. ACKNOWLEDGE THE CONTRIBUTION OF THE CUST. ADVISORY COUNCIL A key tool to assist in the Water Corporation’s endeavours to anticipate customer needs and deliver innovative customer service. The Corporation is committed to establishing closer links with its customers and establishing avenues for effective two-way communication. A close working relationship with groups such as the Customer Advisory Council helps the Corporation to understand and keep pace with changing customer needs and to shape our business accordingly. Residential/Commercial customer satisfaction levels high (86%) Thank the Customer Advisory Council for their contribution to improving the Corporation’s relationship with its customers
  21. TechnoBiz Training Program (www.technobiz-asia.com)
  22. TechnoBiz Training Program (www.technobiz-asia.com)
  23. TechnoBiz Training Program (www.technobiz-asia.com)
  24. TechnoBiz Training Program (www.technobiz-asia.com)
  25. TechnoBiz Training Program (www.technobiz-asia.com)
  26. TechnoBiz Training Program (www.technobiz-asia.com)
  27. The procurement strategy consisted of four broad phases being: 100% Traveling Band Screens Wet Well (Dry Well Forwarding Pumps, through duel media filters, cartridge filters and on to HP pumps) Media Filters 2 Banks 12 pressure filters (52 m2 each) SDI &lt; 3 Two Pass Bromide &lt; 0.1 mg/L TDS approximately &lt; 45 mg/L Energy Recovery Pressure Exchangers PX by ERI