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Nutt rHWE 'i T tkF4 (r4bUS f t:. 1 cA_ <br />Pf► kt <br />NLW <br />kICHLAND, <br />MN. t-64.172 <br />PHONE (` <br />(0) 46"--2 1 _, <br />=RIMARY <br />HENT METHOD: <br />TETCO <br />BACKUP HEAT METHOD: <br />NOT <br />GAS <br />':USTOMER <br />NAME:ULRICH <br />RESIDENCE <br />IKr LOSS <br />17800 <br />TETCO <br />ELEC <br />DUAL FUEL <br />!DELTA T <br />82 <br />F:W <br />C. 6 <br />COS f t <br />. 0� <br />KWH CST <br />LOSS/HR <br />217 <br />BACKUP <br />BACk:.UF' <br />TETCO <br />UNIT <br />BACKUP <br />UNIT <br />7UTt='UT <br />4925G <br />OUTPUT <br />10�:�G0�� <br />EFF (%) <br />70 <br />COST <br />OUTDR BTU/HR <br />OUTDR BTU/HR <br />TETCO SEASON SEASON <br />BACK.UP <br />BACKUP SEASON <br />TEMP <br />LOSS <br />TEMP LOSS <br />RUN <br />HEAT TETCO <br />INPUT' <br />INPUT BACk:UP <br />BELOW <br />TIME <br />HOURS INPUT <br />(BTU) <br />(UNIT INPUT <br />65 DEG <br />(KWH) <br />(UNITS) <br />62 <br />217 <br />_ <br />651 <br />.01322 <br />7.35 34.976 <br />0 <br />0 <br />0 <br />57 <br />217 <br />a <br />1736 <br />. 03525 <br />609 77.279 <br />0 <br />0 <br />0 <br />52 <br />217 <br />13 <br />2821 <br />.05728 <br />522 i07.64 <br />l► <br />(1 <br />�I <br />47 <br />217 <br />18 <br />3906 <br />.07931 <br />468 133.62 <br />c.► <br />U <br />�i <br />42 <br />217 <br />23 <br />4991 <br />.10134 <br />504 183.87 <br />0 <br />0 <br />0 <br />37 <br />217 <br />28 <br />6076 <br />.12337 <br />623 276.70 <br />0 <br />0 <br />0 <br />32 <br />217 <br />-03 <br />7161 <br />.14540 <br />666 348.61 <br />0 <br />0 <br />C► <br />27 <br />217 <br />--N8 <br />8246 <br />.16743 <br />598 360.45 <br />0 <br />0 <br />0 <br />22 <br />217 <br />43 <br />9331 <br />.18946 <br />526 7' 58.77 <br />0 <br />c) <br />0 <br />17 <br />217 <br />48 <br />10416 <br />.21149 <br />357 271.81 <br />0 <br />0 <br />0 <br />• 17 <br />53 <br />11501 <br />.23Z52 <br />288 -42. 12 <br />0 <br />7 <br />217 <br />58 <br />12586 <br />.25555 <br />219 201.48 <br />0 <br />U <br />11 <br />2 <br />217 <br />6- <br />1 >671 <br />.27758 <br />177 176.88 <br />� ► <br />! � <br />! � <br />-•_ <br />217 <br />69 <br />14756 <br />.29961 <br />124 133.75 <br />0 <br />u <br />-8 <br />217 <br />7 ,�• <br />1 ✓941 <br />.321164 <br />72 63. 370 <br />lj <br />-1: <br />217 <br />78 <br />16926 <br />.34.�68 <br />46 56.91= <br />i_► <br />0 <br />-18 <br />217 <br />8'_': <br />1801 1 <br />'6 ;7 1 <br />th 65. H27 <br />Q <br />0 <br />U <br />-23 <br />217 <br />88 <br />19096 <br />.38774 <br />8 11.167 <br />�:► <br />ii <br />ci <br />-28 <br />217 <br />93 <br />20161 <br />.40977 <br />y 4.4255 <br />0 <br />0 <br />0 <br />'OTALS <br />--l1'29. 6 <br />DUA'- <br />FUEL <br />NON DUAL FUEL <br />'ETCO <br />OP COST <br />94.202 <br />TETCO OP COST <br />156.48 <br />ITR PUMP <br />COST <br />11.74 <br />WTR PUMP COST <br />1�..6`_; <br />1ACKUP <br />OP LOST <br />0 <br />BACK.UP OF' COST <br />Cl <br />`OT BTU <br />RED <br />3.42E7 <br />TOTAL HEAT CST <br />170.1'_, <br />'FF PK BTU RED 4.79E6 <br />OFF PK: HT COST 40 . ' _; <br />OTAL HEAT CST 146.27 <br />OTE: THESE FIGURES ARE ESTIMATES ONLY. ACTUAL PERFORMANCE MAY VARY DUE <br />TO UNPREDICTABLE CIRCUMSTANCES. <br />0 <br />. �y <br />C <br />