This map is reasonably accurate for the most parts of the
United States but 1s necessarily highly generalized and
consequently not too accurate In mountainous regions,
particularly In the Rockies.
TABLE OF CONTENTS
X
General Description
How To use ....
Heat Pump
Outdoor Model
WQS30A
WQS36AA36AQ-AElectric100%
Heat Pump
Indoor Model
A36AQ-A
Furnace Fuel
Electric100%
Natural Gas
Oil
Propane78%
Natural Gas78%
on
Propane
WQS42A
A42AQ-AElectric
Natural Gas
oil
Propane
24UHPQA
A30AQ-AElectric
Natural Gas
Oil
Propane
Furnace AFUE
Efficiency Rating
78%
78%
78%7
78%
100%9
78%10
78%
78%
100%
78%14
78%15
78%
1
i 1
Pag
1
2
3
4
5
6
8
11
12
13
16
24UHPQB
30UHPQA
30UHPQA
30UHPQA
36UHPQA
A36AQ-A
Electric
Natural Gas
on
Propane
A36AQ-AElectric
Natural Gas
on
Propane
A37AQ-A
Electric
Natural Gas
on
Propane
A42AS-A
A36AQ-A
Electric
Natural Gas
Oil
Propane
Electric
Natural Gas
Oil
Propane
100%
78%18
78%
78%
100%
78%
78%
78%
100%
78%
78%
78%
100%
78%
78%
78%
100%
78%
78%
78%
17
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
11
TABLE OF CONTENTS
Heat Pump
Outdoor Model
36UHPQA
36UHPQA
42UHPQA
48UHPQA
60UHPQA
Heat Pump
Indoor Model
A37AQ-A
A42AS-A
A61AQ-A
A61AQ-A
A61AQ-A
Furnace AFUE
Furnace Fuel
Electric
Natural Gas
Oil
Propane
Electric
Natural Gas78%
Oil
Propane
Electric
Natural Gas
Oil
Propane
Electric
Natural Gas
Oil
Propane
Electric
Natural Gas
Oil
Propane
Efficiency Ratinq
100%
78%
78%
78%
100%
78%
78%
100%
78%
78%
78%
100%
78%
78%
78%
100%
78%
78%
78%
Pa^
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
m
GENERAL DESCRIPTION
WHAT DOES THIS GUIDE SHOW?
This operational cost savings guide has been prepared to show theoretical
cost savings for Bard dual fuel “add-on” heat pumps when used with either
existing or new furnaces. It covers add-on applications for electric, oil,
propane gas and natural gas type forced air furnaces. It Includes both air
source heat pumps and ground water source heat pumps at many combinations of
gas, oil and electrical rates. It enables the user not only to make a
theoretical operating cost comparison at today's fuel costs but also at
future estimated higher energy costs.
It Is Important to understand that this Is a theoretical comparison between
fuels. Actual operation costs can vary depending on many difficult to
predict variables such as the actual design heating or cooling load, air
Infiltration, and wind effects, solar effect, efficiency of existing furnace,
severity of weather for a given heating or cooling season and also individual
usage pattern.
X
SPECIAL FEATURE—FUEL SAVER MODULE
These estimates utilize the Bard Fuel Saver Module which permit the heat pump
to operate below the balance point to maximize the energy savings. For each
application an analysis should be made to determine the economic balance
point which Is the outdoor temperature at which It becomes more cost
effective to shut the heat pump down with an outdoor thermostat. This
temperature varies with each combination of fuel cost and furnace and heat
pump efficiency level. Refer to tables included in the instructions with the
Fuel Saver Module.
FURNACE EFFICIENCY
For purposes of these cost estimates, furnace efficiency levels of 100% AFUE
for electric, 78% AFUE for natural and propane gas and 78% AFUE for oil was
chosen. We recognize that any variation in efficiency from these values will
change the operating cost somewhat. These values were chosen to best
represent typical efficiency levels of most equipment in the field today.
IV
нон то USE DUAL FUEL ADD-ON
HEAT PUMP GUIDE TO ENERGY COST SAVINGS
Determine the heating Btuh loss and cooling Btuh gain for structure
1.
using a Bard "Whole-House Heat Loss and Gain Work Sheet," Form BOOS,
ACCA "Load Calculation," Manual 0.
a. Heating house Btuh loss is ________________________ .
b. Cooling house Btuh gain is ________________________ .
Determine the type of fuel available at structure (what type of [fuel}
2.
heating system is already there).
a. Electricity
b. Natural Gas
c. Propane Gas
Call local utilities and determine area energy costs.
3.
a. Electricity
b. Natural Gas
c. Propane Gas
d. Fuel Oil
Tentatively select an add-on heat pump system using Bard Manual
4.
2100-057, "Heat Pump Sizing" as a guide, and a Bard equipment catalog.
Determine heating region where the structure is located. To do this,
5.
find the geographic location of house on regional heating load hours
map, A map is located inside the front cover of this guide.
A. Region structure is located
_____________________
Indoor Coil
Heat Btuh
•
YOU ARE NOW READY TO USE THE "DUAL FUEL ADD-ON HEAT PUMP GUIDE"
6. Select the "Dual Fuel Add-On Heat Pump Guide" for the region the
structure is located. (See step 5 above.)
Cool
Locate the add-on heat pump model or models you tentatively selected
(Step 4) in the "Guide." Refer to Table of Contents.
EXAMPLE: 36UHPQA w/A36AQ-A Indoor Coil
BARD HANUFACTURIMG COHPANY
DUAL FUEL ADD-OH HEAT PUMP GUIDE TO BKERGY COST SAVINGS
X
RBCIOK 5
Utl .
ARI RATED HEATING CAP.; STUB (47 )
8.
Now locate the furnace type by fuel used (Step 2).
BTUH (17 )_J
36UHPQA/A36AO-A .
INDOOR A36AO-A
C()P(I^_L90, BSPF
) 2.2(T
90 HIN.DHR REG IV
EXAMPLE: A fuel oil furnace with AFUE of 78%.
9.
FURNACE nPB FUEL OIL
You now have located the page or pages that will help you determine annual
FURiWCF EFFICIENCY 78.00 X AFUE
operating cost. See example—Figure 1.
A. Locate the closest structure loss in Btuh column on left side of
page (step 1).
EXAMPLE: 70,000 Btuh Heat Loss
B. Locate the heating cost per unit at top of page (step 3).
EXAMPLE: $1.40 per gallon fuel oil
C. Now read down the fuel cost column until directly across from the
structure heat loss in Btuh. This will be the theoretical annual
heating cost using only the furnace.
EXAMPLE: 70,000 Btuh heat loss 0 $1.40 per gallon fuel oil,
the annual cost will be $1,912.
D. Next locate the electric cost $/KW under Heat Loss Btuh for
structure (step 3).
EXAMPLE; $.06 KW rate
E. Now once again read down the fuel cost column until directly across
from electric cost $/KW. You now have located the annual heating
cost for the house using an add-on heat pump with the furnace.
EXAMPLE: 70,000 Btuh structure heat loss, with $.06 KW cost and
$1.40 per gallon fuel oil. The annual cost using a
36UHPQA Bard heat pump with the oil furnace would be
$1,613 for an annual savings of $299 ($1,912 minus $1,613),
Now repeat steps 8 through 9 for each type fuel and/or heat pump
selected. This will enable you to select the best combination of
furnace and heat pump to use for a structure.
VT
10. The balance point (the outdoor temperature at which the heat pump Is
running 100% of the time and just meeting structure heat loss
requirements) is located on right side of page.
EXAMPLE: For a structure with a 70,000 Btuh with a 36UHPQA heat pump has
a balance point of 31®F. Below this theoretical balance
point, the heating load is automatically transferred between the
heat pump and the furnace by the wall thermostat to maintain the
desired temperature. This is accomplished with the Fuel Saver
Module.
70,000
S 952 1092 1231 1363 1502 1641 1780 1912 2052 2191 2323 2462 <“THKIRmCAL HEATING COST • FURNACE ONLY
11. To find annual cooling cost of heat pump, look at the bottom of page under
annual air conditioning cost. Directly under the electric rate $/KW (step
3) line, is located the annual cooling cost.
EXAMPLE: At .06 $/KW rate for electricity, the cooling cost would be
$91.00 annually.
ANNUAL AIR CONDITIONING COST WHEN COOLING LOAD IS SIZED TO HATCH COaiNG CAPACIH OF HEAT PUMP
.05 /00 . 07 . 08 , 09 .10 .12 ,14 .16
S 75(Jyi06 121 136 151 182 212 243
ACTUAL HEATHER CONDITIONS AND INDIVIDUAL USAGE PAHERN,
IHATES ONLY AND ARE PROVIDL, .
ACTUAL VALUES HAY VARY DEPENDl
<--ELBCTRlC RATE S/XHH
<--THE0RETICAL AIR CONDITIONING COST
A COKHON
ON
¡0
___
NOTE: The accuracy of the "Dual Fuel-Add-On Heat Pump Guide to
Energy Cost Savings," is directly affected by how accurately you
estimate the structure's heat loss and heat gain in step 1.
Because of uncontrollable variables, Bard Manufacturing Company is
not responsible for any variation In actual operating costs from
these theoretical estimates.
VI 1
FIGURE 1
ч
35,000
40,000
50,000
ш
5/Ш
.05
.06
.01
.09
: 1 S
;Ì6^
.05
.06
.07
.08
.09
.10
.12
:ìt
.05
.06
.07
.10
.12
.14
.16
.70 .80 .90 1.00 1.10 1.20 1.30
1300 1321
S 542 626 702 779 855 939 1015 1^92 1168 1252 1328 1405 <--THEORETICAL HEATING СОЕГ * FURNACE ONLY
563
591
646
674
723
751
799
827
§59 9в}
1119 1147
1279 1307
1439 1467
S 681 779 876 973 1071 1168 1266 1^ 1467 1565 1662 1759 <--THEORETICAL HEATING COST * FURNACE ONLY
DUAL FUEL ADD-ON HEAT PUMP GUIDE TO ENERGY COST SAVINGS
REGION 5
ffiAT PURPHOOBLiCOHPRBSSOR SECTION .NOS^A
COOLING CAPACITY AT 45 DEG.F.BKTERINUli^KK M.;J09g0 BTUH
HEATING CAPACITY AT 15 DEG.P.ENTERING HATER TE№. ;~7^_ :
FURNACE TYPE BLECTRICT“ FURNACE EFFTCIKNCY 1
ELEC.
COST
S/THH
_
___
_____
25,000
30,000
35,000
HEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
5306
.05
.06
S
s
•01
$
M
s5561391
.09
s
.10
s
.12
s
.14
.16
s
HEAT
«
•95
s
.06
s
.07
s
.08
s
.09
,10
s730
s
-12
s
.14
s
.16
HEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
S
.05
S
.06
S
.07
s
.08
s758
.09
s
.10
s
.12
s
.14
s
.16
— THEORETICAL ANNUAL HEATING COST —
368925
4381085
4331238
619
744
8622170
994
PUKP'ii]m?'
361
4381112
507
5841488
653
8762232
1022
11682977
— THEORETICAL ANNUAL HEATING COST —
4171085
500
591
6671732
841
10082601
1182
13493471
772
2476
925
1300
1669
1857
2601
1300
1516
1947
2170
3039
lAT ONLY
BALANCE POINT 15- DEG.F.
BALANCE POINT 3- DEG.F.
40,000
HEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
.05
.06
.07
.09
:iS
:]t
50,000
.05
.06
.07
.08
.09
.16
ANNUAL AIR COMDITIOHIHG COST HHEN COOLING LOAD IS SIZED TO MATCH COOLING CAPACin OF HEAT PUMP
HEAT PUMP HI
i
; 869
t 994
i 1119
i 1245
s m
! 1996
s •§! -55 'S f 1^ lit
THE ABOVE AIHUAL HEATING AND COOLING OPERATING COSTS ARB THEORETICAL ESTIMATES ONLY AND ARB PROVIDED FOR A COMMON
BASIS OP COMPARISON BBTMBBH VARIOUS HPES OF HEATNG AND COOLING SYSTEMS. ACTUAL VALUES MAY VARY DEPENDING ON
ACTUAL HEATHER CONDITIONS AND INDIVIDUAL USAGE PAHERN.
— THEORETICAL ANNUAL HEATING COST —
479
577
862
959
1147
1342
1530
1238
1488
1732
1982
2232
2476
2977
3471
3965
fP» Mr
1544
IBS!
2170
3095
3721
4340
4959
AT ONLY
BALANCE POINT 5 DEG.F.
BALANCE POINT 17 DEG.F.
<—
<—
C RATE S/KHH
"ICAL AIR “
CONDITIONING COST
BARD KANUFACTURING COMPANY
DUAL FURL ADO-OH HEAT PUMP GUIDE TO ENERGY COST SAVINGS
REGIO» S
X
ffiAIlHG CAPACITY AT iS DEG.F.ENTERING HATER TEMP.:
FURNACE TYPE NATURAL~GAS FURNACE EFFTUTENCY
BEAT
ELEC.
25,000S
.05
.06
.07
.08
,09
.10
.12
.14
.16
30,000$
.05
.06
•22
.08
.09
.10
.12
.14
.16
35,000s
.05
,06
.07
.08
.09
.10
.12
.14
.16
.35
236
S
271
$
319
S
375
473
5
521
S
626
S
723
$
827
278
s
313
$
375
s
431 438
$
493
$
549
$ 612
s
730
s
848
s
959
326
s
361
s
431
5
493
$
556
s
626
s
688
$
820
s
,946
s
1078
.40
271
271
319
375
473
521
626
723
827
319
319
382
500
556
619
737
855
966
375
361
431
493
556
626
688
820
946
1078
1085
NATURAL
.50 .55
333
278
326
382
479
528
633
730
834
403
326
389
№ 7
563
626
744
862
973
473
375
445
507
570
639
702
834
959
1099
GAS COST -
368 403
278 278
326
382
479
528
633
730 730
834 834
445 486
326
389 396
445
507
563
626
744 751
862
973 980
521 563
382 389
452
514 521
577
646
709 716
841 848
966 973
,45
299
271
319
375
424431
473
521
626
723
827
361
319
382
438
500
556
619
737
855
966
424
368
438
500
563
633
695
827
952
1092
326
382
479
528
633
333
452
514
570
633
869
459
584
653
1106
.60 .65
438
285
333
389
438
486
535
639
737
841
528
333
396
452
514
570
633
751
869
980
612
396
466
528
591
660
723
855
980
1112
______
S/THERH
.70 .75
473
507
285
285
333
333
389
389
438
433
486
486
535
535
639
639
737
737
841
841
605
563
333
340
396
403
459
452
514
521
570
577
633
639
751
758
869
876
987
980
709
660
396
403
473
466
535
528
598
591
660
667
723
730
862
855
980
987
1119
1112
wm BTu6.^^ COP
Y TCTtME
.80 .90
542 605
292
340
396 403
445
493 500
542 549
646
744 751
848 855
646
340
403 410
459
521 528
577 584
639 646
758
876
987
758
410
479
542
605
674 688
737 751
869 883
9941008
1126
1.00
674
674 <”THEORETICAL HEATING COST * FURNACE ONLY
299
299
347
347
403
452
452
500
549
653
653
751
855
730
813
354
347
417
466
473
535
591
653
765
772
890
883
1001
994
946
848
431
424
500
493
563
556
626
619
695
758
890
1015
1140
1147
THEORETICAL HEATING COST • FURN.+ HEAT PUMP
THEORETICAL HEATING COST * FURN.+ HEAT PUMP
THEORETICAL HEATING COST * FURN.+ HEAT PUMP
S PER YEAR
S PER YEAR
BALANCE POINT 15- DEG.F.
S PER YEAR
BALANCE POINT 3- DEG.F.
40,000
50,000
ANNUAL AIR CONDITIONING COST WHEN COOLING LOAD IS SIZED TO MATCH COOLING CAPACITY OF HEAT PUMP
TBB ABOVE
s
.05
s
$
.06
$
.07
s
s
:§l
.10
s 758
$
.12
s
.14
5
.16
$
$
.05
$
.06
s
s
$
.09
1
:1S
$
.14
s
.16
HEATING AND COOLING OPERATING COSTS ARB THEORETICAL ESTIMATES ONLY AND ARE PROVIDED FOR A COMMON
"" BETHBEN VARIOUS HPES OF HEATNG AMD COOLING SYSTEMS. ACTUAL VALUES HAY VARY DEPENDING ON
ITI^ AND INDIVIDUAL USAGE PAHEi
375
403
473
549
6sl
,897
1036
1175
473
493
556
619
681
744
806
M2
1057
1175
.05
35
1043
1182
1085
1203
431
486
410431
486
479
563
556
626
695
772
765
911
904
1050
1189
542
605
549
521
612
584
W
799
772
862
98?
M9
1112
1231
.06
.07
50
42
542
500
577
786
925
1064
1203
674
577
639
827
890
1015
1140
1259
.08
57
591
646
438 445
507 514
584 591
653
660
723
730
793 799
932
939
10711078
1210
1217
744
813
605 626
667 688
730
793
III
855
Bib
918
939
1043
1064
11681189
1286
1307
.09
.10
64
71
702
452
521
598
667
737
806
946
1085
1224
876
653
716
UÌ
904
966
1092
1217
1335
.12
85
758
459
528
605
674
744
813
952
1092
1231
946
681
744
806
869
932
1245
1363
.14
100
813
466
535
612
681
751
820
959
1099
1238
1015
709
772
834
897
959
1022
114?
1272
1391
,16
114
862
973
479 493
549 563
626 639
695
709
765
779
834 848
973 987
1112
1126
12521266
1217
1085
737 793
799
855
862
918
925
980
9871043
1050
1106
1175
1231
1300
1356
14191474
<-THEORETICAL HEATING COST * FURNACE ONLY
1085
507
THEORETICAL HEATING COST
577
653
723
793
862
1001
1140
1279
1356
841
904
966
1029
1092
1154
1279
1405
1523
BALANCE POINT 5 DEG.F.
<-THEORETICAL HEATING COST * FURNACE ONLY
THEORETICAL BEATING COST
BALANCE POINT 17 DEG.F.
<-ELECTRIC RATE S/KHH
<-THEORETlCAL AIR CONDITIONING COST
S PER YEAR
FURH.+ HEAT PUMP
FURN.+ HEAT PUMP
S PER YEAR
BARD MAHUFACTURING COKPAHY
DUAL FUEL ADD-ON HEAT PUMP GUIDE TO ENERGY COST SAVINGS
RB6I0N 5
HBAT PWniOOBL:COMPRESSOR SECTION
^ifííÍG CAPACITY AT TS OEÓ.F.ENfÉRiNG HATER TE№. : ^47Ь0"ВТЦ&!COP
FURNACE TYPE FUEL OIC" FURNACE EFFTCTETCY ТкЩПШ
ANNUAL AIR CONDITIONING COST HHEN COOLING LOAD IS SIZED TO HATCH COOLING CAPACITY OF HEAT PUMP
THE ABOVE ANNUAL BEAT]№ AND COOLING OPERATING COSTS ARB THEORETICS ESTIMATES ONLY AND ARE PROVIDED FOR A COKHON
B^S Qg CQgARlSOM BBTipN VARipUS TYPES OF PATNG AND COOLING SYSTEMS. ACTUAL VALUES HAY VARY DEPENDING ON
ACTUS NEAITO CONDITIO^ USAGrpAnERN.
626
542
438
431
500
loi
584
653
723
716
793
925
932
1071
1064
1210
779
619
681
702
806
869
8%
932
1015
1057
1140
1182 1217 1259
1300
1259
.06
.05
35
42
779 855 939
702
452
535
521
612
598
667
737
806 820
959 966 980
946
1099
1085
1238
1224
973 1071 1168
876
695
653
758 793 834
716
820
lb
883
¿41
946
904
966
1008
1092
1133
1377 1412 1453
1335
.08
.07
57
50
473 486
542
619 633
827 841
1106 1119
1245 1259
730 772
855
918 959
980 1022
1043 1085
1168
1293
.09
64
556
702
m
897
1210
1335
.10
71
1015
500
570
646
855
994
1133
1272
1266
813
876
939
1001
1064
1126
1252
1377
1495
.12
85
1092
514
584
660
730
799
869
1008
1147
1286
1363
848
911
973
1036
1099
1161
1286
1412
1530
.14
100
1168
521
591
667
737
806
876
1015
1154
1293
1467
890
952
1015
1078
1140
1203
1328
1453
1572
.16
114
1252 1328
535
549
605 619
681 695
765
151
820
834
890
904
1029 :1043
1168 1182
1307 1321
1565 1662
925 966
987
1029
1050
1092
1112 1154
1175 :
1217
1238
1279
1363
1405
1488 1530
1606
1648
1405
<-THEORETICAL HEATING COST * FURNACE ONLY
556
THEORETICAL HEATING COST
626
702
772
841
911
1050
1189
1328
1759
1001
THEORETICAL HEATING COST
1064
1126
1189
1252
1314
1439
1565
1683
<-ELECTRIC RATE S/KMH
i-THBORETICAL AIR CONDITIONING COST
S PER YEAR
BALANCE POINT 5 DEG.F.
S PER YEAR
BALANCE POINT 17 DEG.F.
FURN.+ HEAT PUMP
FURNACE ONLY
FURN.+ HEAT PUMP
BARD HAKUFACTURING COMPANY
DUAL FUEL ADD-ON HEAT PUMP GUIDE TO ENERGY COST SAVINGS
RBGICN
HEAT pi
штш саршт!_ат_15^6ёс:р:шк1'»)с щ1ш:1“тш"ии&;ЧЗ^сор
FURNACE ПРВ PROPANOAS
HEAT
т
_____
tins CAPAC
Е1ЛС.
COGI
5/ККН
:CO№RBSSOR SECTION H0S30A TUnoOR .
1 AT ^ РЕд.Р.ВШ1Ми%Ш 1Ж.: 30900 ВТ1ШЛ7ЛГ
FURNACE'ЁГГТШИСУ тбЛЮГАРЦЕ
.60 .65 .70 .75 .80 .85 .90
s/GALLON
.95
1.00 1.10 .20 1.20
...
АЗур-А
)ББГ
V
Ч.
25,000
30,000
35,000
702
744
.05
.06
.01
.10
.16
.05
.06
.01
.09
,10
.12
.14
.16
S 626 674 730 779 834 883 939 987 1043 1147 1252 1252 <-THEORETICAL HEATING COST * FURNACE ONLY
COOLING SYSTEMS. ACTUAL VALUES HAY VARY DEPENDING ON
542
612
688
897
1036
1175
563
563
633
633
709
709
779
779
848
848
918
918
1057
1057
1196 1196
1335 1335
1203 1203
THEORETICAL HEATING COST
THEORETICAL HEATING COST
<-ELECTRIC RATE S/KHH
<-THBORETICAL AIR CONDITIONING COST
S PER YEAR
BALANCE POINT 5 DEG.F.
S PER YEAR
BALANCE POINT 17 DEG.F.
FURN.+ HEAT PUMP
FURN.+ HEAT PUMP
BARD MANUFACTURING COMPANY
DUAi, FUEL ADD-ON HEAT PUMP GUIDE TO ENERGY COST SAVINGS
REGION 5
..^JBGÍAPACm AT 45 DEG. P. ENTER INU HATER TKHF7I
HEATING CAPACITY AT 15 DEG.P.ENTERING WATER TEMP.:
FURNACE nPB ELECTRIC"
BEAT
35,000
40,000
ELEC.
COST
S/KHH
.05
,06
.01
.09
.10
.12
.14
.16
•S
.06
.07
.09
.10
,12
.14
.16
;COKPRBSSai SECTIOj
“ AT 45 DEG.P.EKT
HEAT PUKP KITH ELECTRIC HEAT ELECTRIC HEAT ONLY
HEAT PUKP KITH ELECTRIC HEAT
S
$
s
s
s
s
s
s
s
— THBORFTICAL ANNUAL HEATING COST —
417
500
577
667
751
1168
1328
— THEORETICAL ANNUAL
466
563
660
751
841
939
1126
1307
1502
INDOOR
36950 BTUH.15«IT
_
____
FURNACE EFFICIENCY
32300 BTUé. ■‘1750 COP
1085
1300
m
1947
M
3039
3471
ING COST —
LECTRIC HEAT ONLY
1238
1488
1732
1982
2232
2476
2977
3471
3965
106
m~AFUE
BALANCE POINT 13- DEG.F.
50,000
,05
.06
.07
.08
,09
.10
.12
.16
60,000
.05
.06
•52
.00
-09
.10
.12
.14
.16
70,000
ANNUAL AIR COHDITIOHIHG COST KHKN COOUHG LOAD IS SIZED TO MATCH COOLING CAPACITY OF HEAT PUKP
HEAT PUKP KITH ELECTRIC HEAT ELECTRIC HEAT ONLY
s
s
s
s925
s
s
$
s1620
s
HEAT PUKP KITH ELECTRIC HEAT ELECTRIC HEAT ONLY
$709
s
s
s
s
$
s
s
$2260
HEAT PUKP KITH ELECTRIC HEA'
S
07
s
10
1
ii
s2782
16
™ THEORETICAL ANNUAL HEATING COST —
577
695
806
1043
1154
1384
1850
— THEORETICAL ANNUAL HEATING COST —
848
987
11262977
1272
1412
1697
1982
AL
869
1036
1217
1739
.05
44
.06
53
• a
.0870.09
79
.10
88
1544
1857
2170
2476
278?
3095
3721
4340
4959
1857
2232
2601
3345
3721
4465
5210
5954
ING COST —
TRIG HEAT ONLY
3039
3471
3902
4340
U
6942
l06 Í23
.16
141
BALANCE POINT 2 DEG.F.
BALANCE POINT 12 DEG.F.
BALANCE POINT 20 DEG.F.
;TR1C RATE S/KNH
<-BLl
IRETICAL AIR CONDITIONING COST
<-t:
__
THE ABOVE ANNUAL HEATING AND COOLING OPERATING COSTS ARB THEORETICAL ESTIMATES ONLY AND ARE PROVIDED FOR^A COMMON
BASIS OP COMPARISON BBTKEBN VARIOUS TYPES OF HBATNG AND COOLING SYSTEMS. ACTUAL VALUES HAY VARY DEPENDING ON
ACTUAL KBATHKR CONDITIONS AND INDIVIDUAL USAGE PATTERN.
BARD KANUFACTURINC COHPANY
DUAL FUEL AOO-OK HEAT PUHP GUIDE TO ENERGY COST SAVINGS
COOLING OPERATING COSTS ARE THEORETICAL ESTIMATES ONLY AND ARB PROVIDED FOR A COMMON
.16
141
2302 2302
THEORETICAL HEATING COST
THEORETICAL^
8
S PER YEAR
BALANCE POINT 12 DEG.F.
COST * FUFN.+ HEAT PUMP
BALANCE POINT 20 DEG.F.
RATE S/RNB
ICAL AIR CONDITIONING COST
FÜRN.+ HEAT PUMP
HEAT
BARD MAHUFACTURING COKFANY
DUAL FUEL ADD-ON BEAT PUMP GUIDE TO ENERGY COST SAVINGS
8BGIM1 5
---
PUPOOOBL:COMPRESSOR
,IMG CAPACITY AT “
iTIHG CAPACin AT
■ ':bhpeelectri
ELEC.
COST
S/KNE
------DEG.P.ENTERING HATER TEMP.;“
I’EHtTT 43
FURNACE El
40.000
50,000
60,000
HEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
.05$486
.06S
:S1
.09S876
1
.14S1363
.16S
HEAT PUMP'iilf'
.05
S 598
.06
I 716
.07
; 834
.08
i 952
.09
i 1071
! 1196
.10
.12
; 1432
S 1669
.14
.16
! 1905
BEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
.05$709
.06S
.07s994
.08S
.09
s
.10
s
.12517044465
519895210
.16S2274
— THEORETICAL ANNUAL HEATING COST —
584
1238
1488
7?9
2232
I?S
1565
iRETICAL ANNUAL
'.ECTRIC HEAT;LECTRlC*^ArONLY
l\]l
3471
3965
2170
2476
2789
3095
3721
4340
4959
— THEORETICAL ANNUAL HEATING COST —
855
1140
1279
14l9
1857
2232
2601
2977
3345
3721
5954
BALANCE POINT 8- DEG.F.
BALANCE POINT 4 DEG.F.
70.000— THEORETICAL ANNUAL HEATING COST —
HEAT PUMP HITH ELECTRIC HEAT ELECTRIC HEAT ONLY
.05
.06S1008
.09
.12$20245210
.14s
.16
80,000
07
ANNUAL AIR CONDITIONING COST WHEN COOLING LOAD IS SIZED TO HATCH COOLING CAPACITY OF HEAT PUMP
THE ABOVE ANNUAL HEATING AND COOLING OPERATING COSTS ARE THEORETICAL ESTIMATES ONLY AMD ARE PROVl^ FOR A COMMON
BASIS OF COMPARISON BETHESN VARIOUS nPES OF HEATN6 AND COOLING SYSTEMS. ACTUAL VALUES HAY VARY DEPENDING ON
ACTUAL HEATHER CONDITIONS AND INDIVIDUAL USAGE PATTERN.
841
S
s
11823039
5
1349
1516
S
1690
s
2358
2698
s
HEAT PUMP Hll
ilC
1405
2010
ANNUAL HEATING COST —
HEAT ELECTRIC HEAT ONLY
$ 3220
f, il •?! i? lil lii ii§
2170
2601
3471
3902
4340
6079
6942
2476
2977
3471
3965
4465
i
7936
BALANCE POINT 13 DEG.F.
BALANCE POINT 19 DEG.F,
<—
RATE S/KHH
ICAL AIR CONDITIONING COST
BEAT
BARD HAKUFACTURING COHPANY
DUAL FURL ADO-OH HEAT PUMP GUIDE TO SHERGY COST SAVINGS
■iW." 43600^SuH^l
nfliiuv IDrU . ; Tik/WA/ Di Vll^J i arilSIl
DBG.P.ENTERING
EL8C.
.35 ,40 .45
HATER TEMP.: 375TO BTU6.“3T0 COP
FURNACE EFFTCMT
‘ÎJ-.T5 ,80 .50 1.C«
X
X
35.000
40.000
50.000
60.000
S 326 375 424 473 521 563 612 660 709 758 848 946 <“TBEORBTICAL HEATING COST * FURNACE ONLY
THEORETICAL HEATING COST
890 890 897 897 904 911
102;
1029 1029 10^ 1036 10» 1050
1161
1168 1168 1175 1175 1182 1189
S 375 431 486 542 591 646 702 758 813 862 973 1085 <-THEORETlCAL HEATING COST * FURNACE ONLY
.05
.06
.07
.09
.10
.12
.14
.16
,05
.06
.07
.08
;5?
.12
;i^
.07
:io
■,iî
.16
424
431
500
507 514 514 521
431 438 438 445
507
IS Ilf Ilf 111 I|1 ^
9?3 Mo kj 98? Hi 994
1133 1140 1140 1147 1147 1154 1161
1293 1300 1300 1307 1307 1314 1321
S 473 542 605 674 744 813 876 946 1015 1085 1217 1356 <-THEORETICAL HEATING COST * FURNACE ONLY