HANDLING FATS, OILS & GREASES (FOG) AT WASTEWATER ...

More documents

Recommendations

Info

REFERENCE FACILITIESTable 2 describes four facilities which exemplify elements of most FOG handling systems.Table 2 – Reference facilities with specific elements of FOG handlingParameter EJWWTF, VT 1 Pinellas County, FL 2 HRSD, VA 3 JCW, KS 4Facility Size3.3 mgd33 mgd22.5 mgd14.5 mgdFOG QuantitiesReceived2,000 gpd averageday and 9,500 gpdpeak day.2,000 – 6,000 drylb/day of dewateredFOG, 5 days/week4,600 gpd average and6,805 gpd peak12,400 gpd average dayand 30,000 gpd peakdayOff-loadingQuick connect hoseconnectionQuick connect hoseconnectionCombined with SeptageReceivingQuick connect hoseconnectionTransfer tostorageBy gravity to primaryscum pitRotary lobe PumpCollected with primaryscum in primaryclarifiersCombination in linegrinder/rotary lobepumpStorageExisting primaryscum pit (3,000gallons)5,000 gal. dewateredFOG storage tank atSCBWRFWithin ScumConcentrator andHopperThree 15,000 gallonfiberglass reinforcedplastic or polyethylenetanks inside a buildingMixingNoneRecirculation of storedFOG using rotary lobepumpNoneRecirculate FOG wasteusing rotary lobe pumpthrough the heatexchanger and grinder;HeatingNoneTemporary heatingused during winter.Hot water heatexchangers to maintainFOG temperature toabut 130 o FHot water heatexchangers to maintainFOG temperature toabout 80ºFDigester orThermalOxidationFeedingPositivedisplacement pumpfeeds FOG & scummixture to digestersRotary lobe pump usedto pump to digestersrecirculation pipeline.Pumped to mix point ofdewatered solidsconveyor to feed MHFProgressing cavitypumps will feed FOG todigesters.Load TrackingMonitor haulersMonitoring FOGvolume received atFOG dewateringfacilityMonitor haulersPanel containing keypad access; track bycompany, driver andload; security camera atunloading station.Wash downPlant water hose bibbavailable, if needed.Plant water available.Plant water availablePower sprayer available.Concrete access area;wash-down water drainsto plant drain system.Odor ControlNone. Scum pit iscovered.Cartridge filter installedon the vent line of thestorage tankNoneBiotower with carbon1 Personal communication with Jim Jutras, 20102Personal communication with Mike Engelmann, 2010.3 Shea et al, 20094Gabel et al, 2009Descriptions of the features of facilities outlined in Table 2 are provided below.
Johnson County, KSThe expansion of the Douglas L. Smith Middle Basin Wastewater Treatment Plant (MiddleBasin WWTP) in Johnson County, Kansas to 14.5 million gallons per day (mgd) averagecapacity includes an environmentally friendly approach for the treatment of FOG wastes fromlocal restaurants and industrial sources. FOG waste receipts are handled using a separate onsiteliquid receiving facility consisting of the following:• FOG waste unloading station• Rotary lobe receiving pumps with inline grinder and integrated debris/sediment trap• Storage tanks• Pumped mixing and heating• Heat exchangers• Progressing cavity digester feed pumps• Odor controlReceived FOG waste is first pumped through a debris/sediment trap then through a grinder andthe heat exchangers to be pre-heated before entering the storage tanks. The receiving pumps willalso continually mix the contents of the tank as well as maintain a temperature of about 80 o F tominimize issues with pumping the material. Separate pumps transfer the FOG waste to theanaerobic digesters. Insulated force mains with numerous several cleaning taps are provided incase one pipeline becomes clogged. Enhanced gas production from the anaerobic digesters willfuel a 2.12-MW biogas co-generation system that utilizes two duty 1060-kW generators.Industrial FOG waste producers from several food processing facilities located within the countyhave or are planning to install dewatering equipment for their thickened FOG waste stream toreduce truck hauling costs. One food processor is currently dewatering thickened FOG wasteusing polymer and a plate and frame filter press. Another is dewatering using polymer andgravity draining in super-sacks. Other processors are evaluating belt filter presses.To capture these high energy waste streams, a dewatered FOG waste receiving station is underdesign for the Middle Basin WWTP. This facility will include equipment and processes todevelop a slurry that will be pumped to the storage tanks in the liquid FOG waste receivingstation for further processing and blending with the liquid FOG waste prior to being fed to thedigesters. The facility will consist of two below-grade tanks with hoppers to receive thedewatered material from end-dump trucks or roll-offs. A high-pressure water jet will initiate theslurry formation and force the material through an in-line grinder prior to being pumped byrotary lobe pumps to the mixing tank. A pumped mix system in the mixing tank, consisting ofnon-potable water, submersible chopper pump, and heat exchanger will precondition the materialprior to being pumped to the liquid FOG waste receiving facility.Hampton Roads, VAThe Hampton Roads Sanitation District (HRSD), Williamsburg WWTP utilizes a multiple hearthincinerator (MHF) to incinerate biosolids. By blending liquefied FOG and scum into dewateredsolids, the facility can recovery energy in the form of reduced natural gas usage. FOG iscollected concurrently with septage at a receiving pit. The FOG is screened through theheadworks and is transferred between processes before ultimately being captured in the primary
Page 2 and 3: INTRODUCTIONFats, Oils, and Grease
Page 6 and 7: sedimentation basins with the prima
Page 8 and 9: Accepting FOG at a separate facilit

HANDLING FATS, OILS & GREASES (FOG) AT WASTEWATER ...

You also want an ePaper? Increase the reach of your titles

Delete template?

Save as template?