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Codigestion at the Derry Township Municipal Authority Clearwater ...

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<strong>Codigestion</strong> <strong>at</strong> <strong>the</strong><strong>Derry</strong> <strong>Township</strong> <strong>Municipal</strong> <strong>Authority</strong>Clearw<strong>at</strong>er Road WWTPWayne A. Schutz<strong>Derry</strong> <strong>Township</strong> <strong>Municipal</strong> <strong>Authority</strong>Hershey, PAAugust 11, 20101


DTMA Organiz<strong>at</strong>ional Overview• Oper<strong>at</strong>ing <strong>Authority</strong> – Staff of 32• Two Wastew<strong>at</strong>er Tre<strong>at</strong>ment Facilities– Clearw<strong>at</strong>er Road WWT• 5.02 MGD– Southwest WWTP• 0.6 MGD• Unmanned S<strong>at</strong>ellite WWTP• Thirteen Pumping St<strong>at</strong>ions• 150+ Miles of Sanitary Sewer– 6” to 48”


DTMA Clearw<strong>at</strong>er Road WWTP


Clearw<strong>at</strong>er Road WWTPProcess Flow Diagram


Major ComponentsWastew<strong>at</strong>er Tre<strong>at</strong>ment• 5.02 MGD Activ<strong>at</strong>ed Sludge– Wastew<strong>at</strong>er Pumping– Preliminary Tre<strong>at</strong>ment– Screening & Grit Removal– Septage Receiving St<strong>at</strong>ion– Primary Clarific<strong>at</strong>ion– Activ<strong>at</strong>ed Sludge Mechanical Aer<strong>at</strong>ion– Biological Nitrogen Removal (Chesapeake Bay compliant)– (anoxic ~ oxic ~ anoxic ~ re-aer<strong>at</strong>ion)– Ferric Chloride (FeCl 3 ) Addition for “P” Removal– Enhanced Final Clarific<strong>at</strong>ion– UV Disinfection


Major ComponentsSolids Processing• Sludge / Biosolids Processing Facilities– Gravity Thickening - Primary Sludge– DAF – WAS– Hershey IPF Sludge– Anaerobic Sludge Digestion (two stage)– Centrifuge– Indirect Paddle Dryer– Biosolids Storage Pad– SteadiGro, Class A – “EQ” Product Beneficial Reuse


Solids Handling2009 Sludge Production• 9.1 DT/D Raw– 5.7 DT/D (63 %) Primary Sludge– 1 DT/D (12%) Septage/Grease Pretre<strong>at</strong>ment MLSS– 2.2 DT/D (24%) WAS– 1 DT/D (11%) IPF Sludge (anaerobic raw)– 0.2 DT/D (2.2%) DTMA SW WAS• 4.1 DT/D Digested• 55% Reduction


Septage Receiving• Septage Receiving– Started in August 1991• Current Receiving St<strong>at</strong>ion– Two Lane– Hauler Kiosk & DTMA Oper<strong>at</strong>or St<strong>at</strong>ion– Lime addition to settle load in primaries– Screening & Grit Removal via WWTP Headworks• 2009 Totals – 20.6 MG• Septage - 13.85 MG [~48,400 GPD]• Grease Trap Wastes - 5.89 MG [~20,600 GPD]• Misc. Sludges - 0.81 MG [~2,800 GPD]


Septage ReceivingFacility Layout


Greasetrap Pretre<strong>at</strong>mentGenesis• Originally Refused Grease Trap Wastes– Grease was loosely define as 750 mg/l FOG• Grease Trap Acceptance “Morphing”– Accepted GTW from <strong>Derry</strong> Restaurants– Requested GTW be diluted• Problems 2– Build up of Grease on Primary Clarifier baffles, weirs,beaches & in <strong>the</strong> PC center wells.• 30 – 40 CY removed from each PC every 3 months– Plugging Primary Sludge Line• Tear down & flush line every month– Visible grease “specks” in digested BFP cake


• Accumul<strong>at</strong>ion in Scum Pit– Genesis of pretre<strong>at</strong>ment idea– Pilot “Digestion” in Scum Pits– Bugs, soda ash, & mixing/aer<strong>at</strong>ionGreasetrap Pretre<strong>at</strong>mentGenesis• Design Concept for Aerobic Grease Pretre<strong>at</strong>ment– KISS– Incorpor<strong>at</strong>e into existing septage receiving st<strong>at</strong>ion– Provide 48-72 Hours of detention (40,000 gal tank)– Computer controlled fill & draw• Decant MLSS to WWTP Headworks


Greasetrap Pretre<strong>at</strong>mentGenesis• Design Concept (continued)– Chopper Pump• Venturi Aer<strong>at</strong>ion• Rotomix Mixing Nozzles– pH Adjustment (original)• Manual control• Lime Addition– pH Adjusment (current)• Autom<strong>at</strong>ic control via pH probe• Magnesium Hydroxide– Addition of Bacteria• ECOBIONICS Biogener<strong>at</strong>or bacteria delivery system


Greasetrap Pretre<strong>at</strong>mentProcess Flow Diagram


Greasetrap Pretre<strong>at</strong>mentProcess Schem<strong>at</strong>ic


Greasetrap Pretre<strong>at</strong>mentPerformance• Immedi<strong>at</strong>e & Dram<strong>at</strong>ic Results throughout WWTP– Within a few weeks grease buildup through out <strong>the</strong> WWTPwas gone.– Within a few months grease “specks” in BFP cakedisappeared.• Change in delivery philosophy– Requested concentr<strong>at</strong>ed and if possible dedic<strong>at</strong>ed greasetrap loads.– “Adjusted” r<strong>at</strong>es to enhance cooper<strong>at</strong>ion


• Improvements– Grinder/macer<strong>at</strong>or on truck discharge to AGP– Addition of rock trap in front of macer<strong>at</strong>orGreasetrap Pretre<strong>at</strong>mentWork in Progress– Addition of pH control for magnesium hydroxide feed– Scum / Foam Control• Cannot oper<strong>at</strong>e system <strong>at</strong> optimal conditions of pH 7 and D.O. 1 or<strong>the</strong> foam/scum problem becomes uncontrollable• Mission impossible


Greasetrap Pretre<strong>at</strong>mentImpact of <strong>Codigestion</strong>• Greasetrap MLSS is discharged into headworks with PlantInfluent– Screening & Grit Removal• Settles out as Primary Sludge• Anaerobic digester feed stock– High Vol<strong>at</strong>iles– Very good alkalinity• Impact of Biogas Production– Because of all <strong>the</strong> variables involved in <strong>the</strong> digestion of sludge and <strong>the</strong>subsequent gener<strong>at</strong>ion of methane, it is very difficult, to establish aquantit<strong>at</strong>ive rel<strong>at</strong>ionship between <strong>the</strong> amount of grease wastesreceived and <strong>the</strong> volume of methane produce, but clearly arel<strong>at</strong>ionship exists.


Impact of <strong>Codigestion</strong>Before Greasetrap Pretre<strong>at</strong>mentBIOGAS PRODUCTION vs. GREASETRAP WASTE VOLUME ACCEPTED700BIOGAS PRODUCEDGREASE ACCEPTED600SCALE AS NOTED5004001,000 GALLONS / MONTH30010,000 CF / MONTH20020032004 2005J F M A M J J A S O N D J F M A M J J A S O N D J F MMONTH


Impact of <strong>Codigestion</strong>After Greasetrap Pretre<strong>at</strong>mentSCALE AS NOTED650600550500450400350300250UNITSTART-UPBIOGAS PRODUCTION vs. GREASETRAP WASTE VOLUME ACCEPTEDMETHANE PRODUCED1,000 GALLONS / MONTH10,000 CF / MONTH2001502005 20062007 20082009M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N D J F M A M J J A S O N DMONTH


Biogas Utiliz<strong>at</strong>ionHistory• 2000 - ES Anaerobic Digester On-line• 2001 - Biogas utiliz<strong>at</strong>ion study– No favorable PPL r<strong>at</strong>e structure– Green Energy not yet in vogue– Phase aligned induction gener<strong>at</strong>or not yet common• 2003 – Plan B– Use biogas to produce steam and dry biosolids intoSTEADIGRO Class A, EQ Product for sale– Some biogas wasted• 2007 – Install Centrifuge– 50% reduction in biogas use due to increased cake solids– Increased biogas production from grease acceptance


• 2008 - Biogas utiliz<strong>at</strong>ion for CHP– PPL r<strong>at</strong>e caps off – 20-30% r<strong>at</strong>e increase– Green Energy / REC’s– Recovered waste he<strong>at</strong> for building he<strong>at</strong>– Payback ~ 8½ yearsBiogas Utiliz<strong>at</strong>ionHistory• 2009 – Cogen & Gas Conditioning Design & Bid– Award Contract ($2,200,000) & Notice to Proceed - July– $500,000 PA Green Energy Works (ARRA/DOE) Grant –December• 2010– Unit start-up June 8 th


• Annual CHP Forecast– Electric Power• 1.5 MW Power Production• Approxim<strong>at</strong>ely 20% of WWTP consumption• $150,0000 savings @ $0.10– Recovered He<strong>at</strong>• 20,000 gallons of #2 fuel oil saved• $47,000 savings (@ $2.365/G)– System O & MBiogas Utiliz<strong>at</strong>ionProjected Performance• Two year bumper to bumper including PMs for Gas Skid & Engine– Payback with Grant• ~6.5 years


Biogas Conditioning


Cogener<strong>at</strong>ion Engine


Cogener<strong>at</strong>ion EngineInside <strong>the</strong> “Box”


Cogener<strong>at</strong>ion EngineConnectionsHe<strong>at</strong> Recovery ConnectionsWaste He<strong>at</strong> Radi<strong>at</strong>or


CONVERTINGWASTEBIOGAS INTOPOWER &HEAT

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