Sterling 25001301 Benutzerhandbuch

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System Installation 
NOTE:  All installation and maintenance are to be performed 
only by qualified personnel who are familiar with local codes 
and regulations, and experienced with this type of 
equipment. CAUTION: Sharp edges and coil surfaces are 
a potential injury hazard. Avoid contact with them. 
General 
1.  Structure supporting unit must be designed to support both 
the unit and the fluid. Table 2 provides weight of fluid per 
gallon. Tables 3 and 4 provide unit weight and volume 
data. Provide suitable flashing of the roof, if this is a roof 
installation. For ground level mounting, a concrete pad is 
recommended. Mounting holes permit the unit to be bolted 
down to withstand wind pressures. Provide adequate clear-
ance for unobstructed air flow to coils. See page 2 for 
Space and Location requirements. 
2.  Level mounting is necessary to assure proper fluid distr-
Table 2. Fluid Weight Per Gallon 
Percent Glycol 
Pounds Per Gallon 
0 (Water) 8.345 
10 8.395 
20 8.495 
30 8.604 
40 8.712 
50 8.804 
 
bution through the coil as well as flooded suction for the 
pump. 
3.  Water piping must comply with local codes. Correct pipe 
sizing will help reduce pumping power and operating costs. 
4. 
In case of doubt, consult the manufacturer for the dry 
cooler fluid pressure drop at the specific conditions on 
your job. 
5. 
Provide sufficient valves and unions to permit easy ac-
cess to parts subject to wear and possible repair or re-
placement. 
6.  After fluid piping is completed, all joints should be leak 
tested. 
7.  Where city water makeup is required, follow local codes, 
making certain that disconnecting provisions are provided. 
8.  Select wire in accordance with nameplate data and local 
codes. 
Piping Installation 
The piping system should provide maximum leak pre-
vention. Weld or sweat joints should be used where possible 
or tightly drawn Teflon tape threaded pipe joints should be made 
if needed. The fact that glycol solutions or other heat transfer 
fluids will leak where water will not, must be taken into ac-
count. 
The glycol system should not employ a pressure reduc-
ing valve. This is because a slight leak would lead to dilution 
of the mixture. Any refill should be controlled so as to main-
tain the proper glycol-to-water ratio. 
Table 3 shows pressure drops for various pipe sizes at 
flow rates commonly used with a typical dry cooler. These 
pipe sizes are not necessarily always correct for the run from 
the condenser to the dry cooler. Proper pipe size will depend 
on available pump head. This can be determined by subtract-
ing from the total available pump head at design flow, the con-
denser pressure drop and the dry cooler pressure drop. Allow 
some safety factor for last minute pipe fittings added to the 
system and for eventual fouling of the system. 
a.  Glycol piping requires no insulation except when fluid tem-
perature will be below ambient dewpoint temperatures. 
Dry coolers normally produce about 70° or higher fluid 
temperatures. 
b.  Vents are required at all high points in the piping to bleed 
air when filling the system. If fluid coolers are at high 
points, vent valves should be installed at each fluid cooler. 
c. It is recommended that gate valves be installed on 
both sides of the pump to prevent loss of fluid in the event 
the pump should require repair or replacement. Shut-off 
valves are also recommended at water cooled condensers 
in case the condensing unit is to be moved or requires 
maintenance involving the coolant system. 
Table 3. Pressure Loss in Feet of Water 
Flow 
GPM
Pipe 
Size 
Steel 
Type "L"
O.D. 
Copper
Schedule 40 Steel 
Head Ft./100 Ft. 
Equiv. Length 
Copper Tube Head 
Head Ft./100 Ft. 
Equiv. Length 
15
1
1
1
/
8
17.6 15.0
20
1
1
1
/
8
30.2 23.1
25
1
1
1
/
8
— 34.6
25
1
/
4
3
/
8
11.5 12.6
30
1
/
4
3
/
8
16.3 17.4
35
1
/
4
3
/
8
21.8 23.0
40
3
/
8
— 26.3
40 1 
1
/
2
 1 
5
/
8
 13.0 
12.9 
45
1
1
/
2
5
/
8
16.5 15.7
60
5
/
8
— 26.3
60
2
1
/
8
7.9 7.0
80
2
1
/
8
13.7 12.0
100
1
/
2
5
/
8
8.5 
6.1
150
1
/
2
5
/
8
18.6 12.9
200
3
1
/
8
10.7 
9.1
250
3
1
/
8
16.5 13.7
300
1
/
2
5
/
8
11.1 
9.2
300
4
1
/
8
5.9 4.9
350
4
1
/
8
7.9 6.5
400 4  4 
1
/
8
 10.2 
8.2 
 
Glycol Charge 
The amount of ethylene glycol required depends upon 
the following: 
a.  The holding volume of the system which includes the hold-
ing capacity of the condenser, the holding capacity of the 
interconnecting piping (Table 3) and the holding capacity 
of the dry cooler (see Table 3). 
b.  Percentage of glycol required by volume to provide pro-
tection at the design minimum outside temperature (see 
Table 2).