Laserfiche WebLink
1 '1 - 7 A'd <br />Ntjl (r1(hF. iTL:.M't! INt,i)_)'i, I►.I- I ►.F1 <br />PIF'N 6,;1_HLANI,. M ., •��, <br />►- HUNE ( J1.1 7 ! 4 <br />FRIMARY HEAT METHOD: <br />TET(:O <br />SALT OF <br />HEAI ME THt11): <br />NAI GAS <br />CUSTOMER <br />NAME: <br />ULk I CH <br />RESIDENCE <br />HT LOSS <br />2--0000 <br />TETCO <br />ELEC <br />DUAL_ FUEL_ <br />DELTA T <br />82 <br />h W <br />'.. 7 <br />COST i <br />, 05 <br />h WH CS T <br />LOSS/Hk <br />2dli <br />PACI`UP <br />TE 1 CO <br />LIN I T <br />EACh UP <br />blcf : OF <br />UNIT <br />OUTPUT <br />37400 <br />OUI FIIT <br />11:►1►Ui►►:► <br />EFF (%) <br />71;► <br />COST <br />OUTDR ETU/HR <br />OUTDR <br />ETU/Hk <br />TETC:O <br />SEASON <br />SEASON <br />HACF UP <br />EACI UP <br />SEASON <br />TEMP LOSS <br />TEMP <br />LOSS <br />RUN <br />HEAT <br />TETCO <br />INPUT <br />INPUT <br />EACIUP <br />BELOW <br />TIME <br />HOURS <br />INPUT <br />(ETU) <br />(UNIT <br />INPUT <br />65 DEG <br />(KWH) <br />QINI TS) <br />62 <br />-' <br />840 <br />. 0`46 <br />735 <br />54.476 <br />O <br />0 <br />!► <br />57 <br />28�) <br />8 <br />22411 <br />.05989 <br />609 <br />120. 3% 7 <br />0 <br />1;► <br />i► <br />52 <br />280 <br />13 <br />3%64G <br />. 097,33 <br />522 <br />167.65 <br />0 <br />0 <br />!, <br />47 <br />280 <br />18 <br />5040 <br />.13476 <br />468 <br />12 <br />u <br />u <br />u <br />42 <br />2130 <br />6440 <br />.17219 <br />504 <br />286.739 <br />0 <br />0 <br />37 <br />280 <br />28 <br />7840 <br />.21(1963 <br />62= <br />430.97 <br />0 <br />0 <br />U <br />32 <br />280 <br />33 <br />9240 <br />, 247u6 <br />666 <br />542.99 <br />0 <br />0 <br />0 <br />27 <br />280 <br />38 <br />10640 <br />.28449 <br />598 <br />561.42 <br />c► <br />p <br />U <br />^.2 <br />280 <br />43 <br />12040 <br />.3219; <br />326 <br />358.80 <br />i► <br />0 <br />0 <br />17 <br />280 <br />48 <br />13440 <br />.35936 <br />457 <br />423.36 <br />0 <br />Ij <br />O <br />12 <br />280 <br />57 <br />14840 <br />.79679 <br />288 <br />377.11 <br />0 <br />Ij <br />11 <br />7 <br />21BO <br />58 <br />16240 <br />. 4 3422 <br />219 <br />31-1. 81 <br />(► <br />! i <br />0 <br />28!► <br />6:, <br />17644:1 <br />.47166 <br />177 <br />275. 5I:1 <br />li <br />►, <br />,, <br />_. 3 <br />281.1 <br />68 <br />194.440 <br />. 5091.►9 <br />1 : 4 <br />: (►y . ' :.' <br />I.► <br />! i <br />77 <br />54652 <br />7: <br />129.9n <br />1:► <br />�t <br />! t <br />-1_� <br />�13L:► <br />78 <br />.58"'96 <br />46 <br />88.b45 <br />!i <br />li <br />►;, <br />-Iti <br />:H+) <br />W, <br />2'240 <br />.621_9 <br />4"rI,1 <br />1i1_ ;' <br />�► <br />!i <br />►► <br />-_ ' <br />'190 <br />88 <br />2'464u <br />.65882 <br />a <br />1 7. ;97 <br />/j <br />1; <br />-28 <br />28!► <br />93 <br />26040 <br />.69626 <br />3 <br />6.8929 <br />C► <br />it <br />G <br />OTALS <br />4874.6 <br />DUAL <br />FUEL <br />NOV <br />DUAL F UE L <br />ETCO OP <br />LUST <br />146.73 <br />TETCO OF LUST <br />24'(, 73 <br />TR PUMP <br />COST <br />19.94 <br />WTk FUME' COST <br />�2 . 19 <br />ACI,.UF OF, <br />COST <br />11 <br />NACU OF UP COST <br />- <br />li <br />OT BTU %EO <br />�. '2E7 <br />TOTAL HEAT CST <br />266. 9: <br />V F! BTU RE <br />7.45E6 <br />t F P� HT <br />COST <br />6:'. 821 <br />OrAL- HEAT <br />CST <br />229.49 <br />TEt THEME. FIGURES ARE ESTIMATES ONLY, ACTUAL PER-DRMANCE MA* ,,,iF;v DtJF <br />TU UNFREDICTAKE C104CUMIS1ANCES. <br />. `, 9 <br />