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FY 2012_Water Pollution Control Plant Budget PresentationDubuque Water Pollution Dubuque Water Pollution Control DepartmentControl Department Water Pollution Control Department Water Pollution Control Department Department Manager Administrative Assistant Assistant Manager3 Laboratory TechniciansMaintenance Foreman Operators0.16 Intern2 Mechanics & 1 Electrician Eight Fourteen Pumping Stations Provide Fourteen Pumping Stations Provide Service Throughout the CommunityService Throughout the Community Laboratory Services Laboratory Services ––WPCP, Water, WPCP, Water, Landfill, Health Department & CommunityLandfill, Health Department & Community Fy2010 LoadingsFy2010 Loadings TotalRes./Com.Ind.% Ind. Flow8.132 mgd7.048 mgd0.612 mgd 7.5% B.O.D. 17040 lbs.11244 lbs5794 lbs34% 11951 lbs.10600 lbs1315 lbs 11% T.S.S. WPCP PerformanceWPCP Performance FY 2010 Processed 8.132 mgd. Processed 8.132 mgd.  Removed 96.8% of B.O.D. (Biological Removed 96.8% of B.O.D. (Biological  Oxygen Demand)Oxygen Demand) Removed 92.7% of T.S.S. (Total Removed 92.7% of T.S.S. (Total  Suspended Solids)Suspended Solids) Generated 11.65 Dry Tons of BioGenerated 11.65 Dry Tons of Bio--Solids Solids  Daily (4254 tons per year) for Disposal Daily (4254 tons per year) for Disposal through Incinerationthrough Incineration 100% Compliance with NPDES Permit100% Compliance with NPDES Permit  Energy Energy ––The Costs of OperatingThe Costs of Operating Electrical Electrical --$490,710$490,710  Fuel Oil for Incineration Fuel Oil for Incineration --$262,500$262,500  Based on fy10/11 actual unit costsBased on fy10/11 actual unit costs  Use of North Incinerator OnlyUse of North Incinerator Only  Total Projected Costs for Energy Total Projected Costs for Energy --$835,770 $835,770  Percent of Operating Costs to Energy Percent of Operating Costs to Energy ––  Approximately 22% of Operating BudgetApproximately 22% of Operating Budget WPCP WPCP --RenewalRenewal $50.6 million in construction$50.6 million in construction  $ 5.1 million for engineering & $ 5.1 million for engineering &  Construciton servicesConstruciton services $ 5 million for contingency($2.42 million $ 5 million for contingency($2.42 million  for Cogeneration Project)for Cogeneration Project) $ 3.3 million for design$ 3.3 million for design  Total project of $64 millionTotal project of $64 million  WPCP SRF Repayment Impact on RatesWPCP SRF Repayment Impact on Rates SRF 0% design loan 3.25% for constructionSRF 0% design loan 3.25% for construction  Fy12 Fy12 12%12%  Fy13Fy1313%13%  Fy14Fy1414%14%  Fy15Fy157%7%  Fy16Fy160%0%  Proposed Rate Increase Proposed Rate Increase ––15%15% Twelve percent rate increase for Twelve percent rate increase for  constructionconstruction Three percent for OperationThree percent for Operation  Rate ComparisonRate Comparison (based on usage of 800 cubic feet or 6000 gallons per month)(based on usage of 800 cubic feet or 6000 gallons per month) CityRates fy11 fy12 (proposed) Iowa City$36.08 Des Moines$29.60 Sioux City$29.34 West Des Moines$27.10 Davenport$25.61 Dubuque$20.70 $23.77 (proposed fy12) Waterloo$22.36 Ames$21.99 Cedar Rapids$20.77 Council Bluffs$17.24 Average (without Dubuque)$25.57 Current Versus Future CapacityCurrent Versus Future Capacity CurrentCurrentExistingExistingDesignDesignPercent Percent ConditionsConditionsCapacityCapacityConditionsConditionsIncreaseIncrease Wastewater Wastewater FlowFlow 8.1328.13213.413.410.6410.64 AverageAverage 33.633.634.334.340.940.93.5%3.5% PeakPeak BOD Load BOD Load 170401704024,40024,40036,90036,90051%51% ** (lbs/day)(lbs/day) Solids Load Solids Load 119511195124,60024,60029,40029,40019.5%19.5% ** (lbs/day)(lbs/day) *Significant industrial capacity included O&M Budget Current vs ProposedO&M Budget Current vs Proposed Current PlantCurrent Plant$3.73 Million$3.73 Million Proposed PlantProposed Plant$3.49 Million$3.49 Million6.4% less6.4% less New Plant/Two New Plant/Two $3.28 Million$3.28 Million12% less12% less MicroturbinesMicroturbines New Plant/Meet New Plant/Meet $3.14 Million$3.14 Million15.8% less15.8% less Full Electrical Full Electrical Needs?Needs? PotentialPotential???????????????? Lift Station CIP’s for fy2012Lift Station CIP’s for fy2012 Rebuild of Perry and Bradley Pumping Rebuild of Perry and Bradley Pumping  StationsStations Two year reconstruction projectTwo year reconstruction project  Update Electrical and Mechanical SystemsUpdate Electrical and Mechanical Systems  Upgrade Physical Structures and AppearanceUpgrade Physical Structures and Appearance  Terminal Street Pumping StationTerminal Street Pumping Station Mechanical Improvements Mechanical Improvements Engineering fy11Engineering fy11  Construction fy12Construction fy12  Flow MetersFlow Meters  Check ValvesCheck Valves  Control GatesControl Gates  PaintingPainting  WPCP Upcoming ProjectsWPCP Upcoming Projects Digester Gas for Combined Heat & Power (CHP)Digester Gas for Combined Heat & Power (CHP)  Two or Three 200 kw microturbines orTwo or Three 200 kw microturbines or One Heavy Duty 390 kw genset orOne Heavy Duty 390 kw genset or One Normal Speed 450 kw gensetOne Normal Speed 450 kw genset Review of Project Elements Anaerobic Digesters and Control Building Renovation and Lab Addition Replace Equipment In-Plant Waste Pump Remove Ash Ponds Peak Flow Station RAS Pump MLSS Splitter and Dewatering Pad Equalization Station Structure Maintenance Activated Tanks Primary Primary Ash Pad Sludge Building ClarifierClarifier Train C Ash Pond Solids Final Clarifier Activated Final Clarifier Handling Sludge Train B Bldg Primary Clarifier Grit WAS Ash Pond Activated Basins WAS Pumps Sludge Storage Liquid O Train A UV Tank Tank 2 Storage New Primary Clarifier and Final Clarifier Final Clarifier Weir Covers Screening New Cascade Bldg (Remove Domes ) Aerator New Energy Dissipating Reuse Dechlorination New Screens, Grit Inlets Convert Chlorine New Equipment; Upgrade Classifiersand WAS Storage , Contact Tank to UV AerationLOX Controls Aeration BlowersRemove ; Tank Diffusers Chlorine Equipment New Influent Flow Meters and Samplers Chlorine Disinfection to Ultraviolet Chlorine Disinfection to Ultraviolet –– Spring, 2011Spring, 2011 Headworks RebuildHeadworks Rebuild--Bar Screens and Grit Bar Screens and Grit System System ––Fall 2011Fall 2011 Laboratory Addition (Late Winter 2012)Laboratory Addition (Late Winter 2012) Standby Power/Secondary Treatment Standby Power/Secondary Treatment Control Building (Late Winter 2012)Control Building (Late Winter 2012) Anaerobic Digestion in Place of Anaerobic Digestion in Place of Incineration (Spring 2012)Incineration (Spring 2012) Ex South Inc Ex South Inc --Future Heat Exchangers Future Heat Exchangers (Spring 2012)(Spring 2012) Rebuild Primary Clarifiers Rebuild Primary Clarifiers add Fourth Clarifier (Spring 2012)add Fourth Clarifier (Spring 2012) Flow Equalization Flow Equalization ––Summer 2012Summer 2012 BioSolids Processing Building (Summer BioSolids Processing Building (Summer 2012)2012) Administration/Laboratory BuildingAdministration/Laboratory Building–– (Late Summer 2012)(Late Summer 2012) From Julien Dubuque Drive Final Clarifier Modifications (Spring 2013)Final Clarifier Modifications (Spring 2013) *Final Completion *Final Completion ––Fall 2013*Fall 2013* From a Spent Facility to a World of Potential From a Spent Facility to a World of Potential From Disposing Waste to Extracting Resources From Disposing Waste to Extracting Resources Heat Recovery from EffluentHeat Recovery from Effluent Waste Carbon to Usable EnergyWaste Carbon to Usable Energy Nutrient Extraction Nutrient Extraction ––From a Pollutant to a From a Pollutant to a Resource. Resource. Thank you!Thank you!