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AND EYALUAT}ON OF: ALTERNA'~tYE$ <br /> <br /> Proceed with Alternative 3 - develop the BF for effluent reuse through the construction <br /> of a dedicated effluent irrigation pipeline and installation of irrigation pumps. <br /> <br /> If all reuse projects identified irt Alternatives 1 through 4 are successful (publicly and <br /> operationally), go forward with measures to implement Alternative 5 - full scale Level <br /> IV reuse of 2.5- to 5.0-mgd of additional Level IV reuse. <br /> <br />6.5 Biosolids Management <br />Solids management Ls accomphshed through processes located at the WPCF, BMF, and <br />Biocycle Farm. Processes located at the WPCF include two gravity belt thickeners (GBTs) <br />and three mesophilic anaerobic digesters. Processes located at the BMF include four FSLs, <br />three belt filter presses, and thirteen air-drying beds. The Biocycle Farm is a 595-acre <br />dedicated biosolids land apphcation site planted in poplars and grass. Approxh~ately 7,500 <br />acres of local cooperative farms are also available for lemd-applying dewatered biosolids. <br /> <br />Primary clarifiers thicken settleable solids and skim fats, oils and greases. These solids are <br />pumped to anaerobic digesters. Waste activated sludge produced in the secondary <br />treatment process at the WPCF is thickened through the GBTs and ~s then pumped to the <br />anaerobic digesters. Anaerobically digested sludge overflows to sludge holding tanks. <br />Sludge holding tank solids are then pumped from the sludge holding tanks at the WPCF <br />through a 5.5-rrdle pipehne (biosolids force main) to the FSLs at the BMF. Biosolids are <br />discharged into the FSLs where it remains for approximately 3 years. Each year from March <br />through September the biosohds in the FSLs are removed. A dredge ~s used to pump <br />biosolids (stabilized sludge), out of the FSLs, where it is then dewate~ed through three belt <br />filter presses. Dewatered biosolids are then stored in static piles in the air-drying beds <br />where they are periodically turned and windrowed. A small portion of the annual biosolids <br />production (less than 5 percent) is composted through aerated static piles. Beginning in July <br />the dewatered biosolids are trucked to local cooperative farms where they are land-applied <br />as a Class B biosolids product. Beginning in the summer of 2004 the first of three phases of <br />development at the Biocycle Farm will become operational and will be able to receive liquid <br />biosolids from the FSLs, as well as dewatered biosolids from the belt filter presses. <br /> <br />MWMC also owns the 290-acre Seasonal Industrial Waste Facility (SIWF), which is located <br />approximately I mile northeast of the BMF. The site includes a 14-acre lagoon and <br />approximately 215 acres of farmable land. The site was originally constructed to treat <br />industrial liquid waste. The farmable land is currently being leased to a farmer. Currently, <br />the SIWF provides MWMC with a buffer against future regulatory, environmental, and <br />process changes. <br /> <br /> 6.5.1 Biosolids Stabilization Processes <br /> MWMC achieves biosolids stabilization through anaerobic digestion FSLs, and dewatering <br /> (primarily mechanical). Anaerobic digestion and the FSLs are interrelated in functioning to <br /> stabilize solids through the reduction of pathogens and volatile su~pended solids (VSS). <br /> Further pathogen destruction occurs following the dewatering process when the dewatered <br /> cake is windrowed to a dry solids content of 40 to 50 percent, l~e capacities of these <br /> processes are sufficient to treat the current flows and loads seen at the WPCF. However, <br /> <br /> MWMC_60_REVI 1 DOC 6-31 <br /> <br /> <br />