277832-YIM-E-0610
Table 11: Natural Gas Application Data-Single Stage
Available On Models
2,3 Ton
2 Ton
3 Ton
4, 5 Ton
3 Ton
4, 5 Ton
4, 5 Ton
1. Heating capacity valid for elevations up to 2000 feet above sea level. For elevations above 2,000 feet, rated capacity should be reduced by
4% for each 1,000 feet above sea level.
2. Based on 1075 BTU/Ft.
3. The air flow must be adequate to obtain a temperature rise within the range shown. Continuous return air temperature should not be below 55°F.
Table 12: Natural Gas Application Data-Two Stage
Available On Models
2 Ton
3 Ton
3 Ton
4, 5 Ton
4, 5 Ton
1. Heating capacity valid for elevations up to 2000 feet above sea level. For elevations above 2,000 feet, rated capacity should be reduced by
4% for each 1,000 feet above sea level.
2. Based on 1075 BTU/Ft.
3. The air flow must be adequate to obtain a temperature rise within the range shown. Continuous return air temperature should not be below 55°F.
1
Table 13: Propane
(LP) Gas Application Data-Single Stage
Available On Models
2,3 Ton
2 Ton
3 Ton
4, 5 Ton
3 Ton
4, 5 Ton
4, 5 Ton
1. Propane applications are accomplished by field installation of a Propane Conversion Accessory, Model 1NP0807 for 2 and 3 Ton units
with 33-1/2" tall cabinets and Model 1NP0808 for 4 and 5 Ton units with 41-1/2" tall cabinets.
2. Heating capacity valid for elevations up to 2,000 feet above sea level. For elevations above 2,000 feet, rated capacity should be reduced
by 4% for each 1,000 feet above sea level.
3. Based on 2500 BTU/Ft.
4. The air flow must be adequate to obtain a temperature rise within the range shown. Continuous return air temperature should not be below 55°F.
1
Table 14: Propane
(LP) Gas Application Data-Two Stage
Available On Models
2 Ton
3 Ton
3 Ton
4, 5 Ton
4, 5 Ton
1. Propane applications are accomplished by field installation of a Propane Conversion Accessory, Model 1NP0809 for 2 and 3 Ton units
with 33-1/2" tall cabinets and Model 1NP0810 for 4 and 5 Ton units with 41-1/2" tall cabinets.
2. Heating capacity valid for elevations up to 2,000 feet above sea level. For elevations above 2,000 feet, rated capacity should be reduced
by 4% for each 1,000 feet above sea level.
3. Based on 2500 BTU/Ft.
4. The air flow must be adequate to obtain a temperature rise within the range shown. Continuous return air temperature should not be below 55°F.
18
Input
1
(MBH)
45
70
70
80
90
108
135
3
.
Input
1
(MBH)
High Fire/Low Fire
High Fire/Low Fire
70 / 45.5
70 / 45.5
90 / 58.5
108 / 70.2
135 / 87.75
3
.
Input Capacity
Output Capacity
2
(Mbh)
45
70
70
80
90
108
135
3
.
Input Capacity
Output Capacity
2
(Mbh)
High Fire/Low Fire
High Fire/Low Fire
70 / 45.5
70 / 45.5
90 / 58.5
108 / 70.2
135 / 87.75
3
.
Output
Gas Rate
3
(MBH)
Ft.
/Hr.
36
42
56
65
56
65
64
74
72
84
87
100
108
126
Output
Gas Rate
3
(MBH)
Ft.
/Hr.
High Fire/Low Fire
56 / 36.4
65 / 42
56 / 36.4
65 / 42
72 / 46.8
84 / 54
87 / 56.2
100 / 65
108 / 70.2
126 / 82
Gas Rate
3
(Mbh)
Ft.
/Hr.
36
18
56
28
56
28
64
32
72
36
87
43
108
54
Gas Rate
3
(Mbh)
Ft.
/Hr.
High Fire/Low Fire
56 / 36.4
28 / 18.2
56 / 36.4
28 / 18.2
72 / 46.8
36 / 23.4
87 / 56.2
43 / 27.95
108 / 70.2
54 / 35.1
2
Number of
Burners
2
3
3
3
4
4
5
2
Number of
Burners
3
3
4
4
5
3
Number of Burners
2
3
3
3
4
4
5
3
Number of Burners
3
3
4
4
5
Johnson Controls Unitary Products
Temp. Rise ºF
3
At Full Input
Min.
Max.
25
55
30
60
25
55
25
55
30
60
35
65
45
75
Temp. Rise ºF
3
At Full Input
Min.
Max.
30
60
25
55
30
60
35
65
45
75
Temp. Rise ºF
4
At Full Input
Min.
Max.
25
55
30
60
25
55
25
55
30
60
35
65
45
75
Temp. Rise ºF
4
At Full Input
Min.
Max.
30
60
25
55
30
60
35
65
45
75
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