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UV Disinfection for Unfiltered Surface Water Regulatory Compliance. Kevin Castro, PE | GHD. Image placeholder. Image placeholder. Image placeholder. UV Disinfection for Unfiltered Surface Water Regulatory Compliance. Kevin Castro, PE | GHD. Presentation outline. Background
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UV Disinfection for Unfiltered Surface Water Regulatory Compliance Kevin Castro, PE | GHD Image placeholder Image placeholder Image placeholder
UV Disinfection for Unfiltered Surface Water Regulatory Compliance Kevin Castro, PE | GHD
Presentation outline • Background • Regulatory Requirements • Water Quality • Basis of Design • Procurement/Construction • Benefits/Results • Lessons Learned • Questions Image place holder Image place holder Image place holder
Village of Skaneateles, New York • Village demands • 0.6 mgd average daily demand • 1.2 mgd maximum daily demand • 2.0 mgd pump capacity • Served off City of Syracuse Skaneateles Lake supply • FAD since 1991 • 3 log giardia inactivation through chlorination (using City of Syracuse chlorination) • Population served ± 3,000
Regulatory requirements • SWTR • 1991 FAD • 3 log giardia inactivation through chlorination • 4 log virus inactivation through chlorination • Contact tank and contact transmission main constructed 1995 • LT2ESWTR • 2 or 3 log cryptosporidium inactivation • Two barriers: UV/Cl2
Water quality • Turbidity • Average = 0.8 NTU • Range = 0.5 to 10 NTU • Syracuse intake shutdowns control turbidity • UVT • Average = 97% • Minimum value = 92% • ICR = 96 to 98% • Limited historical data • Design Range = 90 to 98% • Cryptosporidium • 1 oocyst detected since 1986 • 2 log cryptospordium inactivation required • Fouling Potential - Low Image place holder Image place holder Image place holder
Basis of design • 2 log cryptospuridium inactivation = 5.8 mJ/cm2 • 3 log giardia inactivation = 11 mJ/cm2 • Designed for 3 log giardia inactivation • UVT – 90% minimum • 95% average • Turbidity < 10 NTU • Lamp Technology – Medium Pressure or LPHO • Two 100% redundant UV reactors
Basis of design (cont’d) • Max flow = 2 mgd • Ave flow = 1 mgd • Min flow = 0.5 mgd • Reduce giardia chlorine contact time requirements • Max headloss – 7 inches • Improved monitoring (UVT, Turbidity, Cl2)
Procurement • Preselection vs. pre-purchase • Preselection approach chosen to give contractor ultimate responsibility for system performance. • Life cycle cost bid • Equipment costs • Lamp/ballast costs • Power costs
Procurement • Procurement results • Trojan awarded selection
Construction • Space available with BPS • Pump replacement * • VFDs provided * • Reduce pump flow to 1 mgd (90% speed) • Reduce pump energy cost by $4,000/year • Reduce pump starts to < 4/day • Eliminate cavitation of pumps on low lake level • SCADA for monitoring/control/reporting • *Provided through ARRA grant Image place holder Image place holder Image place holder
Construction UV Controls UV Disinfection
Construction Image place holder SCADA Pumps
Construction Image place holder Turbidity/Chlorine/UVT Monitoring Chlorine Booster System& Monitoring
Results/benefits • 2 log cryptosporidium inactivation – compliance • 3 log giardia inactivation through UV/Cl2 • 4 log virus inactivation through Cl2 • Use transmission main and contact tank for improved fire protection (currently under development) • Reduced pump starts to < 4/day • Reduced energy/cost for pumping • Improved monitoring/reporting of CT, turbidity, Cl2 residual • < 0.1% off-spec water since March 2012
Lessons learned • Validation layout ≠ Approved layout • Alarm management during maintenance • Nuisance alarms during lamp and UVT transmitter maintenance • Preselection was effective procurement approach • Avoid pre-preselection design layouts ($$) • Define distances for power/instrumentation cabling • LT2ESWTR allows off-spec water
Questions? • Please contact Kevin Castro at kevin.castro@ghd.com