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pp 2 of 2 <br /> <br /> The Sheller furnace was not in service during my visit. <br />It was down for refractory repairs and replacement. <br /> <br /> The propane burner is rated at 3 MM BTU/hr. The average <br />propane consumption is 30 gph which results in burner heat <br />release of 2.75 MM ETU/hr. The recovered aluminum requires <br />approximately 840,000 BTU/hr, the scrap iron approximately <br />110,000 BTU/hr and the heat loss was estimated at 100,000 <br />BTU/hr resulting in a net difference of appro~-~imately 1.95 <br />MM BTU/hr discharged from the furnace with the burner at <br />maximum rate. <br /> <br />PARTICULATE REMOVAL <br /> <br /> The existing water spray is an inefficient method of <br />removing particulates from a flue gas stream. The existing <br />stack from your reverberatory furnace was observed to be <br />clear. However, since a charge of dirty scrap could result <br />in stack emissions, our recommendation is to install a <br />baghouse filter to remove the particulates that can be <br />generated ~rom your recovery process. <br /> <br /> A baghouse installation requires an influent gas stream <br />that is above the dew point to prevent wetting of the filter <br />bags. We therefore recommend that the water sprays be <br />removed from the Shaffer Furnace and that the flue gases be <br />cooled by air dilution to attain the proper baghouse inlet <br />temperatures of from 250 to 300 F. <br /> <br /> During the summer,the cooling air required to lower <br />the baghouse inlet temperature to 300 F is 8400 SCFM with <br />the furnace burner' operating at its rated capacity o~ 3 F~q <br />BTU/hr. The products of combustion from the propane ~re 510 <br />SCFM resu!tin9 in a total required gas flow of 8910 SCFM or <br />13,000 CFM at 300 F. <br /> <br /> A portion of the cooling air enters the system via the <br />hood above the furnace. The balance of the air required will <br />De introduced to the suction~^= the blower through a damper <br />inlet valve. <br /> <br /> The =~' <br /> ~ue gas inlet loading is expected to be low by our <br /> ~e~e observations. A filter bag ~as ratio to square area <br />will be approximately 9:1 resulting in a baghouse sizing of <br />approximately 1500 Ft ~ <br /> <br /> The process involves aluminum w~=~h -~ ~=~ <br />light metal. Therefore, the baghouse must be installed <br />outdoors and away from the building in order to be within <br />the fire codes. <br /> <br /> <br />