swro design and optimization
TRANSCRIPT
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Advanced Membrane TechnologiesStanford University, May 07, 2008Advanced Membrane TechnologiesStanford University, May 07, 2008
Seawater Reverse Osmosis Design and Optimization
Nikolay Voutchkov, PE, BCEE
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Typical Desalination Cost-of-Water Breakdown
Typical Desalination Cost-of-Water Breakdown
ItemItem Percent of Total Cost Percent of Total Cost of Water (of Water (*)*)
SWRO System SWRO System 40 %40 %
EnergyEnergy 30 %30 %Intake, Discharge & Intake, Discharge & PretreatmentPretreatment 15 %15 %
Other CostsOther Costs 15 %15 %
Total Cost of WaterTotal Cost of Water 100 % 100 % (*) Note: Percentage Could Vary Depending on Project-Specific Factors
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Performance Optimization Focus
Performance Optimization Focus
►SWRO System Design & Operations;
►Energy Reduction;
► Intake & Discharge Configuration/Collocation;
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Optimizing RO System Performance – Size Matters!Optimizing RO System Performance – Size Matters!
• Large SWRO Trains;• Large RO Membrane Elements;• Alternative RO Train Configurations;• Internally Staged Design.
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Trinidad SWRO Plant– the Largest SWRO Trains
In Use – 5.5 MGD
Trinidad SWRO Plant– the Largest SWRO Trains
In Use – 5.5 MGD
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Large SWRO Membrane ElementsLarge SWRO Membrane Elements
Standard 8” RO Membrane Element
16” RO Membrane Element
Large Size RO Membranes – Advantages• Potential Space Savings – 10 to 15 %.
• Capital Cost Savings – 5 to 10 %.
• Total Cost of Water Savings – 4 to 6 %
Potential Disadvantages• Loading Requires Special Equipment
and Extra Space.
• Uneven Flow Distribution –Accelerated Fouling.
• Special Vessels Needed.
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Large Element Space Savings Could Be Elusive!
Large Element Space Savings Could Be Elusive!
Brackish DesalinationPlant
Yuma, Arizona12-inch RO Elements
Large Space NeededFor the Machine
For Element Loading!
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Feed Pro F
Brine Pro R
Feed Pro F
Brine Pro R
Feed Pro F Feed Pro F
Brine Pro R Brine Pro R
Feed Pro F
Brine Pro R 15
16
17
12
11
13
14
10
Pro FFeed
Brine Pro R
31 33
3131
Large-Diameter SWRO Vessels in Vertical Position
I
Large & Smart MembranesVertically Positioned PV
Easy Load
Source: IDE
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Optimizing Performance by Redistributing Flux/EnergyOptimizing Performance by Redistributing Flux/Energy
Flux is Proportional to the Difference of the Feed and Permeate Pressure
Flux of First Element Can Be Reduced by:1.Increase in Permeate Pressure:•Permeate Pressure Control Valve;•Permeate Interconnector Disk (Acciona).
3. Decrease in Feed Pressure:• Two Pass RO System
w/ Interstage Booster Pump;• “Nano-Nano” Configuration.
2. “Inter-stage” Design:Low Permeability/HighPermeability MembraneCombo.
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Internally Staged Design (1-1-5)
Internally Staged Design (1-1-5)
Element Flow at Standard Test Conditions
~7500 ~9000 ~12500gpd gpd gpd
Compared to standard SWRO design, ISD SWRO offers:Compared to standard SWRO design, ISD SWRO offers:
-- Higher average permeate flux with same lead element flux;Higher average permeate flux with same lead element flux;-- Good permeate quality; Good permeate quality; -- Energy Savings Energy Savings -- 5% 5% -- 10%;10%;
Courtesy: Dow ChemicalCourtesy: Dow Chemical
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Two-Pass RO SystemsTwo-Pass RO Systems
Two-Pass RO Systems (Perth, Tuas, Trinidad)
TDS < 50 mg/L
Interstage BoosterPumps
Interstage BoosterPumps
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34 MGD Point Lisas SWRO Plant, TrinidadTwo Pass /Two-stage
SWRO System
34 MGD Point Lisas SWRO Plant, TrinidadTwo Pass /Two-stage
SWRO SystemTDS = 35 ppt
TDS =85 mg/L
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Reducing Power Use –A Hair Rising Challenge?Reducing Power Use –A Hair Rising Challenge?
• Putting Power Use in Prospective;
• Improving Energy Recovery;
• Maximizing Pump Efficiency;
• Desalination Plant Collocation;
• Source Water Salinity & Energy.
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Putting Desalination PowerUse In Prospective
Putting Desalination PowerUse In ProspectivePower Needed to Produce
Drinking Water from Seawater for One Family for One Year is Over Two
Times Lower than the Power Used by Family’s
Water Heater!
TreatmentTreatment Power UsePower Use(kWh/kgal)(kWh/kgal)
ConventionalConventionalSurface Water Surface Water 0.8 to 1.60.8 to 1.6
Water Imports Water Imports -- PumpingPumping 6.0 to 10.66.0 to 10.6
ReclamationReclamationOf Municipal Of Municipal WastewaterWastewater
3.0 to 5.03.0 to 5.0
Seawater Seawater DesalinationDesalination 7.5 to 10.07.5 to 10.0
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Reducing Energy for SWRO – Practical SolutionsReducing Energy for SWRO – Practical Solutions
►Pressure Exchanger Energy Recovery (35 to 40 % Energy Reduction);
►Use of Alternative RO Membrane Vessel Configurations (10 to 15 % Energy Reduction);
►Application of Large RO Trains/Pumps (3 to 5 % Energy Reduction);
►Use of Warm Power Plant Cooling Seawater(5 to 10% Energy Reduction).
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Improving Energy Recovery –Pressure ExchangersImproving Energy Recovery –Pressure Exchangers
Dhekelia, Cyprus SWRO PlantDhekelia, Cyprus SWRO Plant Barbados SWRO PlantBarbados SWRO Plant5 to 15 % Better Recovery than Traditional Pelton Wheel Systems5 to 15 % Better Recovery than Traditional Pelton Wheel Systems
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Maximizing Pump EfficiencyMaximizing Pump Efficiency
►Pump Efficiency ~n x (Q/H)0.5x (1/H)0.25
Where:
n = pump speed (min -¹);
Q = nominal pump capacity (m³/s);
H = pump head (m).
Pump Efficiency:
One Pump Per Train – 83 %
Carboneras, Spain & Perth –One Pump per 2 RO Trains
Ashkelon, Israel –Two Pumps per 16 RO Trains
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Flattening the Pump Curve For Wide Range of Flows - The Three-Center DesignFlattening the Pump Curve For Wide Range of Flows - The ThreeThree--Center DesignCenter Design
Lowest Energy Use
SWRO PlantWorldwide – 14.4
kWh/kgal @ 40 ppt
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Change in SWRO Plant Operations Paradigm!Change in SWRO Plant Operations Paradigm!
Tri-Center DesignDelivers VaryingFlow by Change inRecoveryRather than By TurningRO Trains On & Off!
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Energy Use and TemperatureEnergy Use and Temperature
2
2.5
3
3.5
4
4.5Energy Use (kWh/m3)
4 8 12 16 20 24 28 32 36 40Temperature, degrees C
Disproportional Increase Above 12 °C
Proportional to TemperatureBetween 12 and 38 °C• Use of WarmUse of Warm
Water May Be Water May Be Beneficial!Beneficial!
•• Use of Use of Intake Wells Intake Wells or Deep Intakesor Deep IntakesMay Result in May Result in Energy Penalty!Energy Penalty!
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Collocation with Power PlantCollocation with Power PlantCollocation with Power PlantDesalination Plant Intake &
Discharge Connection toPower Plant Discharge
Avoids Construction of:•New Intake;
•New Discharge;•New Screening Facilities.
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Potential Energy Benefits of CollocationPotential Energy Benefits of Collocation
►Reduced Intake and Discharge Pumping Costs (1-2% Power Savings).
►Power Cost Savings due to Warmer Source Water (5-15 % Power Use Reduction).
►Use of Power Plant “Spinning Reserve” Energy Where Available.
►Potential Avoidance of Power Grid Connection Charges/Power Tariff Fees.
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Collocation –Capital Cost Savings
Collocation –Capital Cost Savings
►Avoidance of Construction of New Intake & Discharge Facilities – 10 to 50 % of Construction Costs;
►Avoidance of Construction & Operation of New Screening Facilities;
►Electrical System Cost Savings:■ Lower or No Power Grid Use Tariff Charge;■ Use of the “Spinning Reserve” of “Must Run”
Power Plants.
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Collocation in Tampa, FloridaCollocation in Tampa, Florida
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Collocation Concepts in AshkelonCollocation Concepts in Ashkelon
Desalination Plant
Power Plant
Ashkelon Power Generation Plant -Waste Heat Used to Warm Intake Seawater
Co-discharge ofCooling Water and Concentrate
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Main Areas Expected to Yield Cost Savings in the Next 5 Years Main Areas Expected to Yield Cost Savings in the Next 5 Years ► Improvements in Membrane Element Productivity:
- Nano-composite SWRO Membranes;- Larger Membrane RO Elements (16” Diameter or Higher).
► Increased Membrane Useful Life and Reduced Fouling:- Increased Membrane Material Longevity;- Use of Systems for Continuous RO Membrane Cleaning;- UF/MF Membrane Pretreatment.
► Wider Use of Pressure Exchanger Type Energy Recovery Systems;
► Co-Location With Power Plants;
► Larger RO Trains and Equipment;
► Full Automation of All Treatment Processes.
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SWRO Performance Optimization -Future Improvements Will Come From Better
Membranes and Lower Cost Materials!
Questions ?