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NURfHWL:`;fE_RN INDUSTRIAL <br />F(40 <br />NEW R I CHLAND. <br />MN. 5bt.)7_ <br />- 14 A`A-) <br />PHONE <br />( 5(_17 ) 46.`;-.-_ <br />1 <br />r <br />kIMARY <br />HEAT METHOD: <br />TETCO <br />BACKUP <br />HEAT METHOD: <br />NAT GAS <br />JSTOMER <br />NAME:ULRICH <br />RESIDENCE <br />--LOSS <br />44800 <br />TETCO <br />ELEC <br />DUAL FUEL <br />:LTA T <br />8"2 <br />F,W <br />__-.6 <br />I�OS f t <br />. U� <br />KWH CST <br />)SS/HR <br />546 <br />BACKUP <br />bACF UP <br />--I Co <br />LJN I T <br />ErACF'UP <br />UN I T <br />J TPUT <br />47! i50 <br />UU1 F'U-f <br />1 r j�rQUC' <br />EFF CZ) <br />70 <br />C"UST <br />JUTDR BTU/HR <br />OU,fDF: <br />81'U/HR <br />TETCO <br />SEASON <br />SEASON <br />BACP. UP <br />RACF:::UF' <br />SEASOri <br />'EMF• <br />LOSS <br />TEMP <br />LOSS <br />RUN <br />HEAT <br />TETCO <br />INF'UT <br />1NF'U-f <br />BACKUP <br />BELOW <br />TIME <br />HOURS <br />INPUT <br />(BTU) <br />(UNIT <br />INPUT <br />65 DEG <br />0.WH) <br />(UNITS) <br />62 <br />546 <br />=+ <br />16-8 <br />. 03481 <br />7._+5 <br />92.118 <br />U <br />i r <br />57 <br />546 <br />8 <br />4:.168 <br />.09284 <br />609 <br />203.54 <br />0 <br />0 <br />�> <br />52 <br />546 <br />1- <br />7r.r98 <br />.15086 <br />522 <br />283.5(., <br />0 <br />u <br />�r <br />47 <br />546 <br />18 <br />9828 <br />.20888 <br />468 <br />351.9 <br />0 <br />0 <br />rj <br />42 <br />546 <br />23 <br />12558 <br />.26691 <br />504 <br />4B4.28 <br />0 <br />37 <br />546 <br />28 <br />15288 <br />249_, <br />623 <br />728.76 <br />0 <br />r <br />0 <br />546 <br />18018 <br />. - 829-1 <br />666 <br />910.17 <br />U <br />Cr <br />0 <br />546 <br />-8 <br />j748 <br />.44098 <br />598 <br />949.E4 <br />0 <br />j <br />i27 <br />22 <br />546 <br />43 <br />2.3_147P, <br />. 4990) <br />526 <br />944.91 <br />U <br />0 <br />0 <br />17 <br />546 <br />48 <br />262t 6 <br />.55702 <br />357 <br />715.89 <br />51! 6 <br />5._+ <br />28938 <br />• 61 JUJ <br />288 <br />637.68 <br />U <br />r.t <br />LI <br />7 <br />5 46 <br />58 <br />31668 <br />.67'i r7 <br />219 <br />530. 65 <br />tj <br />rj <br />cj <br />2 <br />546 <br />6- <br />-4?98 <br />. 7 :109 <br />177 <br />465. 85 <br />`.,46 <br />68 <br />;. % 12B <br />. 7891 <br />1 ?4 <br />= 52. 26 <br />0 <br />-8 <br />546 <br />7 <br />�90t#8 <br />.84714 <br />72 <br />219.`8 <br />it <br />-131 <br />546 <br />78 <br />42588 <br />. 90`_,1 6 <br />46 <br />149. 90 <br />tj <br /><r <br />0 <br />-18 <br />546 <br />8.` <br />45318 <br />. 96"; 19 <br />'_jrj <br />17 _,. +7 <br />-23 <br />546 <br />88 <br />48f_148 <br />1 <br />8 <br />28.8 <br />998 <br />. 01426 <br />. 1 14( j6 <br />-28 <br />546 <br />97. <br />Jr -)778 <br />1 <br />7. <br />1 U. d <br />�•7i8 <br />. 6 5 _ 26 <br />.15977 <br />JTAL S <br />8241 . . <br />. <br />DUAL FUEL <br />=TCO OF COST 248.06 <br />fR PUMP COST tj. 91 <br />aCKUP OF' COST . 15 3 i 17 <br />JT BTU REQ 9.lr0E7 <br />=F PK BTU REQ 1.26E7 <br />=F PK HT COST 117.04 <br />JTAL HEAT CST -96.16 <br />NON DUAL FUEL <br />IETCU OF COST 412.07 <br />WTR F='UMF' COS f _S. 94 <br />BACKUP OF COST .17799 <br />TOTAL HEAT CST 440.18 <br />JP'E: THESE FIGURES ARE ESTIMATES ONLY. ACTUAL PERFORMANCE MAY VARY DUE <br />TO UNPREDICTFiBLE CIRCUMSTANCLS. <br />