29
To adjust the pressure regulator, remove the regulator cap and turn the adjustment screw
clockwise to increase pressure or counterclockwise to decrease pressure.
Then replace
the regulator cap securely.
Any necessary major changes in the gas flow rate should be made by changing the size of
the burner orifices. To change orifice spuds, shut off the manual main gas valve and
remove the gas manifold.
For elevations up to 2,000 feet, rating plate input ratings apply. For high altitudes (elevations
over 2,000 ft.), see conversion kit index 92-21519-XX for derating and orifice spud sizes.
Check of input is important to prevent over-firing of the furnace beyond its design-
rated input. Never set input above that shown on the rating plate. Use the following
table or formula to determine input rate.
Heating Value of Gas
(BTU/Cu. Ft.) x 3600
Cu. Ft. Per Hr. Required =
Time in Seconds
(for 1 Cu. Ft.) of Gas
Start the furnace and measure the time required to burn one cubic foot of gas. Prior to
checking the furnace input, make certain that all other gas appliances are shut off, with
the exception of pilot burners. Time the meter with only the furnace in operation.
important note for altitudes above 2,000 feet (610 meters):
The main burner orifices
in your furnace and in these kits are sized for the nameplate input and intended for
installations at elevations up to 2,000 feet in the USA or Canada, or for elevations of
2,000 - 4,500 feet (610 -1,373 meters) in Canada if the unit has been derated at the fac-
tory. For elevations above 2,000 feet (610 meters)
IN THE USA ONLY
(see ANSI-
Z223.1), the burner orifices must be sized to reduce the input 4% for each 1,000 feet
(305 meters) above sea level.
NOTICE: DERATING OF THE HEATING INPUT FOR HIGH ALTITUDE IN THE FIELD
IS UNLAWFUL IN CANADA (REFER TO CAN/CGA 2.17). UNITS INSTALLED IN
ALTITUDES GREATER THAN 2,000 FEET (610 METERS) MUST BE SHIPPED FROM
THE FACTORY OR FROM A FACTORY AUTHORIZED CONVERSION STATION
WITH THE HEATING INPUT DERATED BY 10% SO AS TO OPERATE PROPERLY IN
ALTITUDES FROM 2,000 - 4,500 FEET (610 - 1,373 METERS).
D.CONDENSATE DRAIN
IMPORTANT:
Install a condensate trap to ensure proper condensate drainage. See
Figure 15.
The condensate drain pan has a threaded female 1 inch NPT (11.5 TPI) connection.
Consult local codes or ordinances for specific requirements of condensate drain piping
and disposal.
• To use the removable drain pan feature of this unit, some of the condensate line joints
should be assembled for easy removal and cleaning.
• Use a thin layer of Teflon tape or paste on drain pan connections and install only hand
tight.
• Do not over tighten drain pan connectioins as damage to the drain pan may occur.
• Drain line MUST NOT block service access panels.
• Drain line must be no smaller than drain pan outlet and adequately sized to accommo-
date the condensate discharge from the unit.
• Drain line should slope away from unit a minimum of 1/8” per foot to ensure proper
drainage.
ONE
1
21
1
30
1
34
1
39
3
45
40,000
TEN
13
30
15
0
15
36
16
30
37
30
ONE
0
54
1
0
1
3
1
6
2
30
60,000
TEN
9
0
10
0
10
24
11
0
25
0
ONE
0
41
0
45
0
47
0
50
1
53
80,000
TEN
6
45
7
30
7
48
8
15
18
45
ONE
0
33
0
36
0
38
0
40
1
30
100,000
TEN
5
24
6
0
6
15
6
36
15
0
METER TIME IN MINUTES AND SECONDS FOR NORMAL
INPUT RATING OF FURNACES EQUIPPED FOR NATURAL
OR LP GAS
INPUT
BTU/HR
METER
SIZE
CU. FT.
HEATING VALUE OF GAS BTU PER CU. FT.
900
1000
1040
1100
2500
MIN. SEC. MIN. SEC. MIN. SEC. MIN. SEC. MIN. SEC.
TABLE 3
Содержание RKKL Series
Страница 9: ...9 Illustration ST A0801 17 I FIGURE 6 ROOFCURB INSTALLATION FIGURE 5 ST A1154 02 00...
Страница 41: ...41 TABLE 9 AIR FLOW PERFORMANCE 12 5 TON 43 9 kW RKKL B120 MODELS...
Страница 45: ...45 FIGURE 21...
Страница 46: ...46 FIGURE 22...
Страница 47: ...47 FIGURE 23...
Страница 48: ...48 FIGURE 24...
Страница 49: ...49 FIGURE 25...
Страница 50: ...50 FIGURE 26...
Страница 51: ...51 FIGURE 27 RKKL SYSTEM CHARGE CHART...
Страница 54: ...54...
Страница 55: ...55...
Страница 56: ...56 CM 1110...