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Agenda - Council - 11/25/1980
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Agenda - Council - 11/25/1980
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Meetings
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Meeting Type
Council
Document Date
11/25/1980
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- 19 - <br /> <br />ENERGY RECOVERY <br />Energy recovery methods include production and processing of <br />re~use-derived fuel, and use of waterwall furnaces and modular <br />incinerators. The following descriptions o~ energy recovery <br />technologies are from the Minnesota Resource Recovery Plan <br />(MPCA, 1979). <br /> <br />a. Refuse-Derived Fuel (RDF) <br /> The basic RDF system processes municipal solid waste to pro- <br /> duce a transportable alternative solid fuel for use in fossil- <br /> fuel-fired energy systems. <br /> RDF fuel may be classified as coarse, fluff or dust, depending <br /> on the degree o~ processing. Coarse RDF can be used in <br /> boilers equipped with grates, fluff RDF can be used in Suspen- <br /> sion-fired boilers, and dust RDF can be burned alone or emulsi- <br /> fied with oil to form a slurry ~or use in conventional <br /> boilers. Each o~ the fuels can be substituted for others that <br /> have received less processing. <br /> Coarse RDF is prepared by shredding raw refuse. During t~is <br /> stage of processing, the nominal size of the incomxng re~use <br /> is reduced, resulting xn partial homogenxzation of the waste. <br /> Coarse RDF contains large quantities of grit. All the unde- <br /> sxrable components o~ the refuse (91ass, grit, metal, chlor- <br /> inated plastics) that present corrosion, erosion, and material- <br /> handling problems are contained in the fuel. Coarse RDF <br /> bridges easily (hangs up in hoppers and will not flow) in stor- <br /> age. Coarse RDF has the same thermal properties as raw solid <br /> waste; that is, 4,600 Btu/lb., and burns to 26 percent <br /> moisture and 29 percent ash. <br /> Fluff RDF is prepared by air-classifying and screening coarse <br /> RDF to remove most of the grit and large inerts such as cans, <br /> rocks and metal debris. Air-classification vacuums off light <br /> material, separating it ~rom most of the chlorinated plas- <br /> tics. Unfortunately, large wood fragments are also separated, <br /> thus causing the loss of a desirable fuel component. Removal <br /> of screenable dirt, grxt and glass ~ragments to decrease <br /> fuel ash content further increases the heating value of the <br /> 'fuel while reducing'the amount of material to be handled in <br /> the boiler's ash handing system. Fluff RDF has a nominal <br /> shelf life of about five days. Longer storage encourages spon- <br /> taneous combustion. The material has the same bridging and <br /> flow characterxstics as coarse RDF. Unscreened fluff RDF has <br /> a heating value of 5,000 Btu/lb., burns to 26 percent mois- <br /> ture and 22 percent ash. Screened material has a higher heat- <br /> ing value of 5,550 Btu/lb. and and burns to 12 percent ash. <br /> It must be recognized that less total tonnage of screened <br /> fluff RDF is made because of grit removal; hence, while screen- <br /> ing improves the fuel product, some recoverable energy is <br /> sacrificed. <br /> <br /> <br />
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