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Figure B-5. Typica0RDF Processing <br />Other configurations may include additional separating equipment or exclude <br />tnonnnncdo, but the RDF generated is always shredded so that it is capable of being <br />blown into a furnace. Although results vary with the processing configuration, in <br />general, about 80 percent of the incoming waste stream is converted into RDF for <br />the thermal process. <br />An advantage of this system is in the removal of metals and other materials from the <br />waste stream. While not all these facilities include this step in the processing line, <br />those that do can realize revenue from the sale of recovered metal. For instance, at <br />the North County Resource Recovery Project in West Palm Beach, Florida, the <br />nominal 3,000 TPO facility removed and sold over 30,000 tons of ferrous metals in <br />2003, which represented over 3 percent of the weight of the incoming waste stream. <br />With the removal of non-com buotib|es, the specific heat content of the RDF can be <br />increased by 10 percent over the original MSVV. <br />1.1.4 Refuse-derived Fuel/Fluidized Bed <br />In this incineration process, y4SVV |s shredded to less than four inches mean particle <br />size (the same as with the RDF process described in 1.3,1 above) to produce the fuel <br />(see Figure B-5l before it is blown into a bed of sand in a vertical cylindrical furnace. <br />Hot air isalso injected into the bed from below, and the sand has the appearance of <br />a bubbling fluid as the hot air agitates the sand particles. Moisture in the RDF is <br />evaporated almost instantaneously upon entering the bed, and organics burn out <br />both within the bed and in the freeboard, the volume above the bed. Bbaarn tubes <br />are embedded within the bed, and a transverse section of boiler tubes captures heat <br />from the flue gas exiting the furnace, as shown in Figure B-6. <br />/ Source: generic. <br />GBB/C08027-01 B-8 August 15, 2008 <br />