e. Multiply gas rate (cu ft/hr) X heating value (Btu/cu ft)
using
natural
gas
heating
value
from
local
gas
utility/supplier.
EXAMPLE: (0—2000 ft altitude)
Furnace rating plate input is 110,000 Btuh.
Btu heating input = Btu/cu ft X cu ft/hr
Heating value of gas = 1050 Btu/cu ft
Time for 1 revolution of 2-cu ft dial = 70 sec
Gas rate = 103 cu ft/hr (from Table 8)
Btu heating input = 1050 X 103 = 108,150 Btuh
In this example, the orifice size and manifold pressure
adjustment is within
±
2 percent of the furnace input rate.
2. Set temperature rise.
Furnace must operate within range of temperature rise speci-
fied on the furnace rating plate. Determine the air temperature
rise as follows.
a. Place duct thermometers in return and supply ducts as near
furnace as possible. Be sure supply-air thermometers do not
"see" heat exchangers so that radiant heat will not affect
thermometer readings. This is particularly important with
straight-run ducts.
b. When thermometer readings stabilize, subtract return-air
temperature from supply-air temperature to determine tem-
perature rise.
c. Adjust air temperature rise by adjusting blower speed.
Increase blower speed to reduce temperature rise. Decrease
blower speed to increase temperature rise.
Disconnect the electrical power before changing the blower
motor speed tap. A failure to follow this warning can cause
personal injury.
d. To change blower motor speed selections for heating mode,
remove blower motor lead from control HEAT terminal.
Table 6—Model 58YAV Orifice Size* and Manifold Pressure for Correct Input
(Continued)
(Tabulated Data Based on 22,000 Btuh per Burner, Derated 4 Percent per 1000 Ft Above Sea Level)
ALTITUDE
RANGE
(FT)
AVG GAS
HEAT VALUE
AT ALTITUDE
(BTU/CU FT)
SPECIFIC GRAVITY OF NATURAL GAS
0.58
0.60
0.62
0.64
0.66
Orifice
No.
Manifold
Pressure
Orifice
No.
Manifold
Pressure
Orifice
No.
Manifold
Pressure
Orifice
No.
Manifold
Pressure
Orifice
No.
Manifold
Pressure
U.S.A.
Only
575
43
2.7
43
2.8
43
2.9
43
3.0
43
3.1
600
43
2.5
43
2.6
43
2.7
43
2.7
43
2.8
9001
625
43
2.3
43
2.4
43
2.4
43
2.5
43
2.6
650
43
2.1
43
2.2
43
2.3
43
2.3
43
2.4
to
675
48
3.7
43
2.0
43
2.1
43
2.2
43
2.2
700
48
3.4
48
3.6
48
3.7
43
2.0
43
2.1
10,000
725
49
3.8
48
3.3
48
3.4
48
3.5
48
3.6
750
49
3.5
49
3.6
49
3.8
48
3.3
48
3.4
775
49
3.3
49
3.4
49
3.5
49
3.6
49
3.7
* Orifices sizes shown in BOLD are factory installed.
Table 7—Altitude Derate Multiplier for U.S.A.
ALTITUDE
(FT)
% OF
DERATE
DERATE MULTIPLIER
FACTOR FOR U.S.A.*
0—2000
0
1.00
2001—3000
8—12
0.90
3001—4000
12—16
0.86
4001—5000
16—20
0.82
5001—6000
20—24
0.78
6001—7000
24—28
0.74
7001—8000
28—32
0.70
8001—9000
32—36
0.66
9001—10,000
36—40
0.62
* Derate multiplier factor is based on midpoint altitude for altitude range.
Table 8—Gas Rate (Cu Ft/Hr)
SECONDS
FOR 1
REVOLUTION
SIZE OF
TEST DIAL
SECONDS
FOR 1
REVOLUTION
SIZE OF
TEST DIAL
1
cu ft
2
cu ft
5
cu ft
1
cu ft
2
cu ft
5
cu ft
10
11
12
13
14
360
327
300
277
257
720
655
600
555
514
1800
1636
1500
1385
1286
50
51
52
53
54
72
71
69
68
67
144
141
138
136
133
360
355
346
340
333
15
16
17
18
19
240
225
212
200
189
480
450
424
400
379
1200
1125
1059
100
947
55
56
57
58
59
65
64
63
62
61
131
129
126
124
122
327
321
316
310
305
20
21
22
23
24
180
171
164
157
150
360
343
327
313
300
900
857
818
783
750
60
62
64
66
68
60
58
56
54
53
120
116
112
109
106
300
290
281
273
265
25
26
27
28
29
144
138
133
129
124
288
277
267
257
248
720
692
667
643
621
70
72
74
76
78
51
50
48
47
46
103
100
97
95
92
257
250
243
237
231
30
31
32
33
34
120
116
113
109
106
240
232
225
218
212
600
581
563
545
529
80
82
84
86
88
45
44
43
42
41
90
88
86
84
82
225
220
214
209
205
35
36
37
38
39
103
100
97
95
92
206
200
195
189
185
514
500
486
474
462
90
92
94
96
98
40
39
38
38
37
80
78
76
75
74
200
196
192
188
184
40
41
42
43
44
90
88
86
84
82
180
176
172
167
164
450
439
429
419
409
100
102
104
106
108
36
35
35
34
33
72
71
69
68
67
180
178
173
170
167
45
46
47
48
49
80
78
76
75
73
160
157
153
150
147
400
391
383
375
367
110
112
116
120
33
32
31
30
65
64
62
60
164
161
155
150
16
