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141 W ti 1 I.HL <br />kNU , <br />PINI. <br />"KIMNF.V <br />HEAT METHOD: <br />TLICO <br />HACI,UF <br />HEAT ME'lwil): <br />NA► bAt), <br />USTOMER NAME:ULRICH <br />RESIDENCE <br />T LASS <br />187,:►,_► <br />TETC:O <br />EL <br />DUAL FUEL <br />EL TA T <br />p2 <br />KIA! <br />_ , E <br />COST t <br />WH CST <br />OSS/Hk <br />)2 <br />DACh UP <br />1490 OF, <br />TE TCO <br />ON I T <br />BAC: LIP <br />UN F T <br />U'TPUT <br />'61 C►.► <br />OUTPUT <br />Ii!i►,:►00 <br />EFF= (% ► <br />7,► <br />LUST <br />9UTDR ETU/HR <br />OUTDR <br />ETU/HR <br />TEETCO <br />SEASON <br />SEASON <br />EIACP UP <br />E+ACM LIP <br />SEASON <br />TEMP <br />LOSS <br />TEMP <br />LOSS <br />RUN <br />HEAT <br />TE_TL'U <br />INPUT <br />INPUT <br />6AC1 UP <br />6L: LOW <br />TIME <br />HOURS <br />INPUT <br />(bTU) <br />(UNIT <br />INPUT <br />65 DEG <br />(F WH) <br />(UNITS) <br />62 <br />228 <br />_ <br />684 <br />.01894 <br />735 <br />45.931 <br />0 <br />i► <br />�► <br />57 <br />8 <br />e <br />1824 <br />. 05056 ► <br />6,;►9 <br />101 . 49 <br />i ► <br />,:► <br />i <br />52 <br />229 <br />11 <br />2964 <br />.08206 <br />522 <br />141.76 <br />0 <br />0 <br />47 <br />'.'='a <br />18 <br />4104 <br />.11362 <br />468 <br />175.48 <br />�► <br />,:► <br />i► <br />42 <br />22E1 <br />2' <br />5244 <br />.14518 <br />504 <br />241.47 <br />u <br />0 <br />0 <br />37 <br />228 <br />28 <br />6384 <br />.17674 <br />623 <br />363.:.7 <br />U <br />i► <br />0 <br />3. <br />228 <br />331 <br />7524 <br />.20831 <br />666 <br />457.8 <br />a <br />0 <br />(► <br />27 <br />228 <br />38 <br />8664 <br />.23987 <br />598 <br />473.15 <br />22 <br />228 <br />4' <br />9804 <br />.27143 <br />526 <br />471.15 <br />0 <br />U <br />0 <br />7 <br />228 <br />48 <br />10944 <br />.30299 <br />357 <br />356.95 <br />12 <br />22H <br />53 <br />12084 <br />. 3-3•455 <br />288 <br />'_.17. 96 <br />0 <br />i <br />i► <br />7 <br />5a <br />13224 <br />.36611 <br />219 <br />264.59 <br />0 <br />►:► <br />,i <br />2 <br />228 <br />b'• <br />14364 <br />.39767 <br />177 <br />232. '.28 <br />i ► <br />. r <br />,i <br />-3 <br />22H <br />68 <br />15504 <br />.42974 <br />124 <br />17';.it) 4 <br />0 <br />i► <br />,_► <br />-8 <br />.'.b <br />77 <br />16644 <br />. 460UL) <br />72 <br />1 09. 49 <br />i► <br />,_, <br />- 1 3 <br />78 <br />17784 <br />. a92 IT6 <br />46 <br />74. 741.1 <br />- I H <br />2:El <br />8'> <br />18924 <br />. �2 <br />50 <br />86.447 <br />i <br />,.► <br />,., <br />88 <br />20064 <br />.55548 <br />8 <br />14.665 <br />0 <br />U <br />i <br />93 <br />21 204 <br />. 58704 <br />7 <br />5. 81 1 / <br />0 <br />0 <br />U <br />TOTALS <br />41 1 �.►. O <br />i, <br />DUAL FUEL <br />NON <br />DUAL FUEL <br />rETCO OP COST <br />121.71 <br />TETCO <br />OF COST <br />�45,5i► <br />NTR PUMF <br />COST <br />16.82 <br />WTR PUMP COST <br />19.55 <br />MCkUP OP COST <br />i► <br />HALKUP UP COST <br />u <br />TOT bTU <br />FEO <br />4.49E7 <br />TOTAL HEAT CST <br />225.05 <br />7FF F1 6 T U REO 6. 28E6 <br />3FF PM. HT COST 52. 96 7 <br />rOTAL HEAT CST 193.49 <br />407E: THESE FIGURES ARE ESTIMATES ONLY. ACTUAL GEkFOkMANCE MAY VAkY DUE_ <br />TO UNPREDICTABLE CIRCUMSTANCES. <br />-v <br />P <br />