Laserfiche WebLink
DEVELOPMENT AND EVALUATION OF ALTERNATIVES <br /> <br />Alternative 1 - Conventional, ~lesophilic Digester <br />Alternative 1 consists of constructing a traditional mesophilic digester. It is likely that the <br />anaerobic digestion process would be the typical h~gh-rate, single-stage process. <br />Advantages and disadvantages o£ this alternaQve are listed below. <br /> <br />Advantages: <br /> A conventional process recognLzed and £amffiar to WPCF staff <br /> Non-proprietary process <br /> Proven performance record in municipal wastewater treatment plants <br /> Operating schemes more in line with current digestion process <br />o Most widely implemented digestion process at publicly owned treatment works <br /> (POTWs) across the U.S <br /> <br />Disadvantages: <br /> Potential foaming problems <br /> Low volatile solids reduction compared with other alternatives <br /> May require larger retention times to achieve required volatile solids reduction <br />· Good mixing system required to maintain active digester volume <br /> <br />The major equipment that would be necessary under this alternative includes sludge <br />recirculation pump(s), heat exchanger(s), a digester mixing pump(s), a digested sludge <br />transfer pump, and hot water recircttlahon pump(s). <br /> <br />Alternative 2 - Pasteurization <br />Pre-pasteurization of predigested sludge involves heating raw sludge to 70°C (160°F) before <br />transferring it to a separate holding tank, in this case one of the existing digesters. The <br />temperature of the solids in the holding tank is maintained at a minimum of 70°C for 30 <br />minutes. Upon completion of the pasteurization process, the temperature of the solids is <br />decreased to 40°C (100°F) in a spiral heat exchanger and transferred to the digester. By using <br />a sludge/sludge spiral heat exchanger, it is possible to recover greater than 50 percent of the <br />required thermal energy prior to entering the digester. <br /> <br />Advantages: <br /> Requires minimal solids retention time and also provides Class A biosolids that satisfy <br /> regulatory requirements <br /> <br /> Although more heat is required and higher heating costs are incurred, this process has <br /> been reported to recover over 50 percent of the thermal energy <br /> <br /> May improve dewatering characteristics <br /> <br />· Greater flexibLlity in reverting to mesophilic operations because thermophilic organisms <br /> do not need to be developed <br /> <br /> Abil/ty to meet vector attraction reduction (VAR) requirements, when combined with <br /> anaerobic digestion <br /> <br />· Small reactor is required ahead of the existing digestion process <br /> <br />· Public recognizes the "pasteurization" term and, therefore, public education and <br /> acceptance may be easier <br /> <br />IVIWMC_60_REVI 1 DOC 6-35 <br /> <br /> <br />