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►Lht% 4 iHt hrl. Ir•11• <br />NOF; f HWF ti TE <br />I:rJ ! NUUa t R (�;L. <br />f'�;kl <br />NEW R I CHLAND. <br />PIN. `_,6� ► <br />�; <br />PRIMARY HEAT MEIHUD: <br />1EFCO <br />6ACPUP <br />HEAP METHOD: <br />NAT GAS <br />cos TOMER <br />NAME s ULR I CH <br />RE 5 I DENCE <br />HT LOSS <br />:: 21;►1;► <br />TETCO <br />ELEG <br />DELTA T <br />82 <br />1,W <br />_ <br />6 <br />DUAL FUEL <br />LOSS/HR <br />4i-'4 <br />EIACP UP <br />. <br />COST Y <br />,►�� <br />hWH CST <br />TE T CC) <br />UN T T <br />MACI, UP <br />OU I PUT <br />49475 <br />OU I F'U T <br />1 1►1►0! it ► <br />BACM UP <br />EFF <br />UN I T <br />(% ) <br />711 <br />CUS I <br />OUTUR E4TU/HR <br />IEMF' LOSS <br />OUTDR <br />TEMP <br />FITU/HR <br />TETCO SEASON <br />SEASON <br />HACP UP <br />PACT UP <br />SEASON <br />bELOW <br />LOSS <br />RUN <br />TIME <br />HEAT <br />HOURS <br />TE7C0 <br />INPUT <br />IrJPUf <br />INPUT <br />E%Al.1 U►-' <br />65 DEG <br />(bTU) <br />(UNIT <br />INPUT <br />6:: <br />404 <br />1 <br />1212 <br />.i►24S!i <br />7-5 <br />0WH) <br />64.82i► <br />! ► <br />(UNITS) <br />1 <br />41►4 <br />8 <br />� " - -► <br />J2 <br />- <br />.u6�_._ <br />609 <br />14�.2", <br />1;► <br />�-► <br />�► <br />!► <br />`2 <br />47 <br />404 <br />13 <br />5: 52 <br />. 1061 <br />522 <br />199.49 <br />!► <br />!► <br />U <br />41j4 <br />18 <br />7272 <br />.14698 <br />468 <br />247.64 <br />U <br />U <br />42 <br />404 <br />23 <br />9292 <br />.18781 <br />�,� iq <br />40. 77 <br />0 <br />!'► <br />0 <br />0 <br />37 <br />32 <br />4! iq <br />20 <br />'_.3 <br />1 1-312 <br />. 22864 <br />62? <br />S 12. 80 <br />Ij <br />Ij <br />0 <br />i <br />, <br />27 <br />404 <br />► 332 <br />.26947 <br />666 <br />646.08 <br />0 <br />0 <br />'j <br />404 <br />38 <br />1 J3Ja <br />. 31 l►� t:► <br />598 <br />668, 01 <br />1;1 <br />0 <br />22 <br />41:►4 <br />4'. <br />17372 <br />.33113 <br />526 <br />664.89 <br />I j <br />17 <br />404 <br />48 <br />19 392 <br />.39196 <br />357 <br />503. 74 <br />Ij <br />u <br />U <br />0 <br />11 <br />q� i4 <br />e � <br />�_ <br />.� <br />�1412 <br />.43278 <br />288 <br />448.71 <br />U <br />0 <br />Ij <br />7 <br />404 <br />58 <br />23432 <br />.47361 <br />21y <br />373.41;► <br />i► <br />0 <br />2 <br />404 <br />63 <br />25432 <br />.�1444 <br />177 <br />327.80 <br />i► <br />(•) <br />1> <br />-3 <br />404 <br />68 <br />27-�72 <br />. JJJ27 <br />124 <br />247.8i <br />1► <br />1,► <br />-8 <br />40,0 <br />73 <br />29492 <br />.59610 <br />72 <br />154.51 <br />0 <br />U <br />0 <br />1.1 <br />-13 <br />404 <br />78 <br />3151 c <br />. 63693 <br />46 <br />105.48 <br />�, <br />1_► <br />-•18 <br />404 <br />83 <br />33332 <br />.67776 <br />050 <br />122.0!i <br />0 <br />�► <br />i► <br />,, <br />-23 <br />404 <br />88 <br />35552 <br />.7185`1 <br />8 <br />2i►.69!, <br />0 <br />l'► <br />-:8 <br />404 <br />93 <br />` <br />35 2 . 7.. <br />.73941 <br />'• <br />a.2101 7 <br />0 <br />,a <br />0 <br />u <br />c► <br />OTALs <br />'8U!►. 1 <br />0 <br />DUAL <br />ETCO OF <br />FUEL <br />COST <br />174.58 <br />NON <br />DUAL FUEL <br />TR PUMP <br />COST <br />21.75 <br />TETCO <br />OP COST <br />290.01 <br />ACKUP OP <br />COST <br />i► <br />WTR PUMP COST <br />215. 29 <br />OT BTU RED <br />6. 3 ►E7 <br />BACKUP OP COST <br />i� <br />F PK SITU <br />RED <br />E!. 17E6 <br />TOTAL. <br />HEAT <br />CST <br />_ 1 J' ~�► <br />F P1, H F <br />cos T <br />82. j5/-1 <br />OTAL HEAT <br />CST <br />271.69 <br />r lEs THESE F I(3URES ARE ESTIMATES ONLY. ACTUAL. PERFORMANCE MAY VARY DIJE <br />TO UNPREDICTABLE L:INCUMSTANCE'S. <br />. b `, <br />