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December 10, 2009 TOWN OF PALM BEACH WATER COMMITTEE Discussion of Water Plant Options
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PRESENTATION AGENDA Update of City’s Water Program Desalination Plant Cost Estimate Floridan Reverse Osmosis Cost Estimate Summary of Town’s Options
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WEST PALM BEACH WATER PROGRAM UPDATE
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Water Program Update Water Plant Performance Pilot Testing Water Supply Improvements Water Treatment Improvements Water Distribution Improvements Next Steps with Water Program
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Water Plant Performance Excellent water quality being produced Finished water turbidity remains low 2009 DOH Sanitary Survey required 20 actions items vs. 571 in 2008 (everything has been fully repaired/replaced) Delivery pressure to the island consistently ranges from 50 – 60 psi Drought protection measures underway Improvements made for water supply, treatment and distribution infrastructure
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Pilot Testing Pathogens Membranes Natural Organic Matter Magnetic Ion Exchange (MIEX) Enhanced Coagulation (EC) Enhanced Softening (ES) Taste & Odor PAC Enhanced Ozone Chlorine Dioxide UV GAC
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Pathogens Removal Submerged Membrane (UF) Pressurized Membrane (MF)
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Organics Removal MIEX pretreatment substantially reduced the influent TOC MIEX led to 73% reduction in coagulant demand (from 75 mg/L to 20 mg/L) compared to raw water and eliminated the need for pH adjustment
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Taste & Odor Compounds Removal Various blends of Powdered Activated Carbon were tested for their ability to remove MIB & Geosmin from Clear Lake PAC Type E was the most effective
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Water Supply Improvements Active Projects Source Water Protection Program Control Structure Replacements Raw Water Pump Stations Optimize Stormwater Capture ASR Well Activation Groundwater Assessments AWT Plant – reuse water Control Structure #4 Exploratory Groundwater Well Source Water Protection ASR Well $2.5M Control Structures $4.5M Raw Water Pumping $0.8M Source Water $4.6M AWT Wetlands $0.6M Total Supply $13M ASR Well $2.5M Control Structures $4.5M Raw Water Pumping $0.8M Source Water $4.6M AWT Wetlands $0.6M Total Supply $13M
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Water Treatment Improvements Automation$ 4.0M Chemical Systems$ 4.1M Electrical$ 5.6M Filters$ 1.8M Valves $ 0.6M Pumps & Piping$ 1.2M Security$ 1.2M Structures$ 2.3M Total $20.8M Automation$ 4.0M Chemical Systems$ 4.1M Electrical$ 5.6M Filters$ 1.8M Valves $ 0.6M Pumps & Piping$ 1.2M Security$ 1.2M Structures$ 2.3M Total $20.8M Plant Automation Chemical System Upgrades Redundant Critical Components Modernized Filters New Valves & Pumps Training & SOPs Carbon Dioxide System Automation Component High Service Pump Active Projects
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Water Distribution Improvements Remote Pump Stations New Chlorination Systems Corrosion Control Program Hydraulic Model – pipes, tanks & quality Telemetry Remote Stations $ 1.5M Hydraulic Model $ 0.7M Corrosion Control $ 0.2M Westward PS $ 4.0M Water Storage Tank $ 1.2M Total $7.6M Remote Stations $ 1.5M Hydraulic Model $ 0.7M Corrosion Control $ 0.2M Westward PS $ 4.0M Water Storage Tank $ 1.2M Total $7.6M Corrosion Testing Equipment Remote Pump Station Telemetry Screen Active Projects
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Next Steps with Water Program Meetings with Regulatory Agencies Alternatives Evaluation Cost Estimates Refined Commission Workshops Decision to Health Department March 10 th
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DEDICATED TOWN DESALINATION PLANT
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PROCESS FLOW DIAGRAM Pre-TreatmentPost-Treatment Chlorine Coagulant Chlorine Caustic Soda Fluoride Cleaning System Deep Injection Well Membranes Source Residuals Fine Screens Coagulation & Flocculation ClarificationClarification MicrofiltrationMicrofiltration Ultraviolet Light Cartridge Filters Flocculant Aid Bisulfite 1 st and 2 nd RO Passes Calcite Contactor Storage Tank High Service Pump Station Carbon Dioxide Calcium Carbonate Corrosion Inhibitor Backwash Equalization Gravity Sludge Thickening DewateringDewatering LandfillLandfill Intracoastal Raw Water Intake Structure & Pump Station Intracoastal Raw Water Intake Structure & Pump Station
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15 MGD RAW WATER INTAKE $17 million
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PROCESS FLOW DIAGRAM Pre-TreatmentPost-Treatment Chlorine Coagulant Chlorine Caustic Soda Fluoride Cleaning System Deep Injection Well Membranes Source Residuals Fine Screens Coagulation & Flocculation ClarificationClarification MicrofiltrationMicrofiltration Ultraviolet Light Cartridge Filters Flocculant Aid Bisulfite 1 st and 2 nd RO Passes Calcite Contactor Storage Tank High Service Pump Station Carbon Dioxide Calcium Carbonate Corrosion Inhibitor Backwash Equalization Gravity Sludge Thickening DewateringDewatering LandfillLandfill Intracoastal Raw Water Intake Structure & Pump Station Intracoastal Raw Water Intake Structure & Pump Station
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10 MGD MEMBRANE TREATMENT $154 million
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COMPLETE COST ESTIMATE $222 million The Town has other options: Floridan Aquifer 10 mgd Water Plant Reclaimed Water – City’s AWT Facility Membrane Biological Reactor (MBR) Plant Remain “as-is” customer
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FLORIDAN AQUIFER PLANT OPTION
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FLORIDAN AQUIFER PLANT COSTS $99 million
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OPTIONS SUMMARY OptionCost Desalination WTP$ 222 million Floridan Reverse Osmosis WTP$99 million Reclaimed Water from CityTBD MBR for Irrigation WaterTBD Remain “as-is” Customer$0 The City requests the Town provide its decision quickly.
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QUESTIONS?
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