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pp 2 of ~ <br /> <br /> The Shaffer 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 ETU/hr. The average <br />propane consumption is 30 ~ph which results in burner heat <br />release of 2.75 MM BTU/hr. The recovered aluminum requires <br />approximately 840,000 BTU/hr, the scrap iron al'proxima%ely <br />110,000 BTU/hr and the heat loss was estimated et 100,000 <br />BTU/hr resulting in a net difference of approximately 1.S5 <br />MM BTU/hr discharged from th£ 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 from your recovery process. <br /> <br /> A baghouse installation requires an infiuent gas stream <br />that is a~bove 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 ~ases be <br />coo!e~ 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 ~00 SCFM with <br />the furnace burner operatln~ at its rated capacity of 3 F~ <br />BTU/hr. The products of combustion from the propane are 510 <br />SCFM resulting in a total required gas flow of ~9i0 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 ~he furnace. The balance of the air required ~il! <br />De introduced to ~he suction of the blower through a damper <br />inlet valve. <br /> <br /> Th~ flue gas ~_e~ <br /> o.~ ~ exDec~_~ to be low by our <br />field observations. A filter ba~ cas ratio to square area <br />w~!l be approximately 9:1 resulting in a baghouse sizin~ of <br />approximately 1500 Ft <br /> <br /> The process involves aluminum which classifies as a <br />light metal. Therafora, the baghouse must be ~ns~¢~led ~ ~ <br />outdoors and away f~, the bu_=~g in order to be "~*~ <br />the fire codes. <br /> <br /> <br />