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r4Uf•: f t1W- ; I t_t:f4 I NUU::i I F. i F+L. <br />F'F',t•:t <br />NEW R 1 CHLAND . NN. <br />F'HUNE_ ( `,07 ) 46S-:: 1 <br />PRIMARY <br />HEAT ►.E1HUD: <br />"fEfC0 <br />HALFUP HEAT METHOD: <br />N A I C;:;5 <br />CUSTOMER NAME:ULRICH RESIDENCE <br />HT t_OSS <br />:. _'�►)o <br />rETCO <br />ELEC <br />DUAL <br />FUEL <br />DELTA T <br />82 <br />KW <br />=.6 <br />COST S. <br />.ii <br />F;WH <br />CST <br />LOSS HR <br />404 <br />BACKUP <br />BACKUP <br />TETCO <br />UN I T <br />FAG .UP <br />Ur4 I T <br />OUTPUT <br />49475 <br />OUTPUT <br />100 ►Cii ► <br />EFF (%) <br />70 <br />(.:Ut7 f <br />OUTDR BTU/HR <br />OUTDR BTU/HR <br />TETCO SEASON SEA' 0I <br />BACi�`UF' <br />BACKUP SEASON <br />TEMP <br />LOSS <br />TEMP <br />LOSS <br />RUN <br />HEAT TETCO <br />I NPUT <br />I NPUT BACk.UF' <br />BELOW <br />TIME: <br />HOURS INPU1 <br />(BTU) <br />(UNIT INPUT <br />65 DEG <br />(KWH) <br />(UNITS) <br />62 <br />404 <br />.3 <br />1212 <br />. 02450 <br />7_- 5 64. 8'2 ► <br />i i <br />�► <br />C► <br />57 <br />404 <br />8 <br />_�232 <br />.065.33 <br />609 143..212 <br />ii <br />�► <br />C► <br />52 <br />404 <br />131 <br />5252 <br />. 1 i:►615 <br />522 199.49 <br />l► <br />C► <br />C► <br />47 <br />404 <br />18 <br />727A2 <br />.14698 <br />46B 247.64 <br />0 <br />u <br />c_► <br />42 <br />404 <br />23 <br />9292 <br />.18781 <br />504 340.77 <br />C► <br />a <br />0 <br />37 <br />41:14 <br />28 <br />11312 <br />.22864 <br />62-7 512.80 <br />1:► <br />0 <br />0 <br />32 <br />404 <br />3.3 <br />1313+32 <br />.26947 <br />666 646.08 <br />C► <br />0 <br />Q <br />27 <br />404 <br />38 <br />15352 <br />.310 3. 0 <br />598 668.01 <br />ii <br />0 <br />lj <br />22 <br />404 <br />43 <br />17372 <br />.35113 <br />526 664.89 <br />C► <br />0 <br />C► <br />17 <br />404 <br />48 <br />19392 <br />.39196 <br />3.57 503.74 <br />C► <br />0 <br />0 <br />12 <br />404 <br />5 <br />21412 <br />.47278 <br />288 448.71 <br />0 <br />7 <br />404 <br />58 <br />23432 <br />.47361 <br />219 373.40 <br />0 <br />0 <br />0 <br />2 <br />404 <br />63 <br />25452 <br />.51444 <br />177 327.80 <br />i► <br />c:► <br />�� <br />-3 <br />404 <br />68 <br />27472 <br />.555217 <br />124 247.87 <br />0 <br />Q <br />i <br />-8 <br />404 <br />73 <br />29492 <br />. 5961 C► <br />72 154.51 <br />c.) <br />0 <br />0 <br />-13 <br />404 <br />70 <br />31512 <br />.63.693 <br />46 105.48 <br />0 <br />0 <br />__ 18 <br />404 <br />87, <br />3:;532 <br />.67776 <br />5C► 122. 00 <br />C► <br />C► <br />0 <br />-23 <br />404 <br />88 <br />__5552 <br />.71859 <br />8 20.695 <br />C► <br />0 <br />0 <br />-28 <br />404 <br />93 <br />37572 <br />.75941 <br />3+ 8.2017 <br />0 <br />C► <br />0 <br />TOTALS <br />5800.1 <br />0 <br />DUAL FUEL <br />NON DUAL FUEL <br />TETCO <br />OF' COST <br />174.58 <br />TETCO OP COST <br />2290.01 <br />WTR BUMF <br />COST <br />21.75 <br />WTR PUMP COST <br />25.29 <br />BACKUP <br />OF COST <br />0 <br />BACKUP OP COST <br />C► <br />TOT BTU <br />RED <br />6.33E7 <br />TOTAL HEAT CFT <br />-15.:.0 <br />]FF PK <br />BTU FED <br />6.87E6 <br />3FF PK <br />HT COST <br />82.3%50 <br />TOTAL HEAT <br />CST <br />278.69 <br />40TE: THESE FIGURES ARE ESTIMATES ONLY. ACTUAL PERFORMANCE MAY VARY DUE <br />TO UNPREDICTABLE CIRCUMSTANCES. <br />