TABLE 3: NATURAL GAS APPLICATION DATA
  | INPUT CAPACITY  | OUTPUT  | GAS RATE  | 2  | NUMBER OF  | TEMP. RISE °F AT FULL  | ||
  | 
  | INPUT3  | ||||||
AVAILABLE ON MODELS  | CAPACITY  | 
  | ||||||
(MBH)1  | 
  | 
  | ||||||
  | (MBH)  | FT.3/HR.  | 
  | BURNERS | 
  | 
  | 
  | |
  | 
  | MIN.  | 
  | MAX.  | ||||
  | 
  | 
  | 
  | 
  | 
  | |||
  | 
  | 
  | 
  | 
  | 
  | 
  | ||
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 45  | 36  | 42  | 
  | 2  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 70  | 56  | 65  | 
  | 3  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 80  | 64  | 74  | 
  | 3  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 90  | 72  | 84  | 
  | 4  | 30  | 
  | 60  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 108  | 87  | 100  | 
  | 4  | 30  | 
  | 60  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 135 | 108 | 126 | 
  | 5  | 35  | 
  | 65  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
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.
3.The air flow must be adjusted to obtain a temperature rise within the range shown. Continuous return air temperature should not be below 55°F.
TABLE 4: PROPANE1 (LP) GAS APPLICATION DATA
  | INPUT CAPACITY  | OUTPUT  | GAS RATE  | 3  | NUMBER OF  | TEMP. RISE °F AT FULL  | ||
AVAILABLE ON MODELS  | 
  | INPUT4  | ||||||
(MBH)2  | 
  | 
  | ||||||
  | CAPACITY (MBH)  | FT.3/HR.  | 
  | BURNERS  | 
  | 
  | 
  | |
  | 
  | MIN.  | 
  | MAX.  | ||||
  | 
  | 
  | 
  | 
  | 
  | 
  | ||
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 45  | 36  | 18  | 
  | 2  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 70  | 56  | 28  | 
  | 3  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 80  | 64  | 32  | 
  | 3  | 25  | 
  | 55  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
3 &   | 90  | 72  | 36  | 
  | 4  | 30  | 
  | 60  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 108  | 87  | 43  | 
  | 4  | 30  | 
  | 60  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
4 & 5 TON  | 135 | 108 | 54  | 
  | 5  | 35  | 
  | 65  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
  | 
1.Propane applications are accomplished by field installation of a Propane Conversion Accessory, Model 1NP0807 for 3 and 
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.3.
4.The air flow must be adjusted to obtain a temperature rise within the range shown. Continuous return air temperatures should not be below 55°F.
Johnson Controls Unitary Products  | 7  |