Laserfiche WebLink
i t."hk I Hk.kM . I NL. <br />NORTHWESTERN I NDUS I T< 1 "L 1 Nt,t <br />NEW R I CHLAND , MN. <br />5- l PHUtvE l5t!7) 46to-L21 <br />I <br />Fk I MARY <br />HEAT ME: THUD s 1 E T CO <br />EIALKUF HEAT METHOD: NA 1 GAS <br />CUSTOMER NAME:ULk:CH RESIDENCE: <br />HT LUSS <br />195uu <br />T <br />E 1 C0 <br />E LEL: <br />DUAL F UE L <br />DELTA 1 <br />8: <br />�w <br />.' <br />COST t <br />k.wH CSI <br />LUSS/Hk <br />217 <br />HAcJ UF, <br />14ACI UP <br />TETCO <br />IJN <br />I T <br />EACF UN <br />UNIT <br />OUTPUT <br />37400 <br />OUTPUT <br />IO0,)LK% <br />EFF (i) <br />LOST <br />OUTOR BTU/HR <br />OUTUR BTU/HR <br />TETCO SEASON SEASON <br />BACFOF <br />EACKUP SEASON <br />TEMP <br />LOSS <br />TEMP <br />LOSS <br />RUN <br />HEAT TETCO <br />i NPU T <br />I NF L1 1 E+ACk UP <br />BELOW <br />TIME <br />HOURS INPUT <br />!ETU) <br />(UNIT INPUT <br />65 DEG <br />(h WH) <br />(ON1 TS) <br />62 <br />237 <br />71 <br />711 <br />.01901 <br />735 46.110 <br />i i <br />ij U <br />57 <br />237 <br />8 <br />1896 <br />.05070 <br />609 101.88 <br />Q <br />1) u <br />5-1 <br />237 <br />11 <br />'o81 <br />.08278 <br />522 141.91 <br />U u <br />47 <br />2 7 <br />18 <br />42 66 <br />.11406 <br />468 176.16 <br />it <br />► 0 <br />42 <br />:3 J <br />2'.S <br />5451 <br />.14575 <br />504 242.41 <br />_I <br />1_I L► <br />37 <br />237 <br />:8 <br />6636 <br />.17743 <br />623 364.78 <br />O <br />0 <br />32 <br />23- <br />_.3 <br />7821 <br />.210912 <br />666 459.60 <br />0 <br />27 <br />237 <br />38 <br />9:►06 <br />.24080 <br />598 475.2i, <br />u 0 <br />22 <br />237 <br />4T <br />10191 <br />.27249 <br />526 472.98 <br />a <br />C► U <br />237 <br />48 <br />11376 <br />.304!7 <br />357 358.34 <br />�i7 <br />t2 <br />237 <br />53 <br />1'1561 <br />.33586 <br />288 319.20 <br />C� <br />i► C► <br />7 <br />237 <br />'J8 <br />13746 <br />.36/54 <br />219 265.62 <br />2 <br />237 <br />63 <br />14971 <br />.7•9922 <br />177 233. 19 <br />u <br />! i► <br />- _ <br />, 7 <br />bb <br />16116 <br />. 4"091 <br />124 176.33 <br />i► <br />4 ►> <br />-8 <br />237 <br />73 <br />173U1 <br />.46259 <br />72 149.91 <br />0 <br />i► G <br />-1 <br />37 <br />78 <br />184Q6 <br />.49428 <br />46 75.(►7%1 <br />u <br />1 Q <br />_- 1 H <br />2137 <br />87 <br />1967. <br />. to..-,96 <br />50 136.784 <br />i► <br />-2'• <br />237 <br />88 <br />20856 <br />.55765 <br />8 14. 722 <br />u <br />u t,► <br />-28 <br />237 <br />93 <br />22041 <br />.58933 <br />3 5.8344 <br />a <br />i► u <br />TOTALS <br />41 26. i► <br />u <br />DUAL <br />FUEL <br />NON DUAL FUEL <br />TETCO <br />OP COST <br />124.19 <br />TETCO OF COST <br />24',",.3u <br />WTR PUMF COST <br />16.88 <br />WTR FUME COST <br />ILY.6'• <br />bACO UFO <br />OF COS T <br />(.1 <br />BACKUP OP CAST <br />v <br />TOT BTU <br />REO <br />4.51E7 <br />TOTAL HEAT CST <br />22S.9'• <br />OFF Fh. <br />BTU REO <br />6.31E6 <br />IMF PV <br />HT COST <br />53. 174 <br />TOTAL HEAT CST <br />194.25 <br />NOTE► THESE F 1GUkES ARE ESTIMATES ONLY. ACTUAL. NERFORMANCE iAY VAkY DUE <br />TJ LJWREDIC1ABLk: CIRCUMSTANCES. <br />Ll '-, <br />