TOTAL STATIC PRESSURE (Includes Coil, Ductwork etc.)
- 2 -
SELECTION DATA
The selection of an air cooled condenser is based on the
heat rejection capacity at the condenser rather than net
refrigeration effect at the evaporator because the refrigerant gas absorbs additional energy in the
compressor. This additional energy, the heat of
compression, varies appreciably with the operating
conditions of the system and with compressor design,
whether open or suction cooled hermetic type.
Some compressor manufacturers publish heat rejection
figures as part of their compressor ratings. Since heat
rejection varies with compressor design, it is
recommended that the compressor manufacturer’s data
be used whenever available in selecting an air cooled
condenser.
HEAT REJECTION FACTORS
CONDENSER LOAD = COMPRESSOR CAPACITY X FACTOR
OPEN COMPRESSORS
TABLE NO. 4
EVAPORATOR
TEMP
°F.°C.
-30
-20
-10
10
20
30
40
50
-34
-29
-23
0
-18
-12
-7
-1
4
10
* Outside of normal limits for single stage compressor application.
For two stage application use formulas above.
CONDENSING TEMPERATURE °F. (°C.)
90
(32)
1.37
1.33
1.28
1.24
1.21
1.17
1.14
1.12
1.09
100
(38)
1.42
1.37
1.32
1.28
1.24
1.20
1.17
1.15
1.12
110
(43)
1.47
1.42
1.37
1.32
1.28
1.24
1.20
1.17
1.14
120
(49)
*
1.47
1.42
1.37
1.32
1.28
1.24
1.20
1.17
130
(54)
*
*
1.47
1.41
1.36
1.32
1.27
1.23
1.20
140
(60)
1.47
1.42
1.37
1.32
1.28
1.24
*
*
*
If thecompressor manufacturer does not publish heat
rejection ratings, factors from Table Nos. 4 and 5 may be
used to estimate total heat rejection-THR.
For systems outside the normal limits of single stage
compressor application, (such as compound or cascade
refrigeration systems) the following formulas may be
used to arrive at the heat rejection requirements for
selection of the condenser:
Open Compressors
THR = Compressor Capacity (Btuh) + 2545 x Bhp
Suction Cooled Hermetic Compressors
THR = Compressor Capacity (Btuh) + 3413 x KW
SUCTION COOLED HERMETIC COMPRESSORS
TABLE NO. 5
EVAPORATOR
TEMP
°F.°C.90 (32)
-30
-20
-10
10
20
30
40
50
-34
-29
-23
0
-18
-12
-7
-1
4
10
* Outside of normal limits for single stage compressor application.
For two stage application use formulas above.
rerejection data is not available, determine the
heat rejection factors for the specified conditions
from Table No. 5 above (1.27).
(2)Multiply the compressor capacity by the heat
rejection factor to estimate the required
condenser capacity.
(3)Since R-22 is specified, select the proper
condenser from Table No. 1 based on the
specified difference between condensing
refrigerant and the ambient air (T.D.).
SELECTION:
Using the heat rejection factor from Table No. 5 above,
the required condenser capacity is:
1.27x 350.000 = 444,000 Btuh
From Table No. 1 for the specified T.D. of 25°F the proper
selection is the Model KCC 237 with a capacity of
536,600 Btuh. In this instance the condenser is slightly
oversized and the condenser will balance the
compressor heat rejection at less than the maximum
condensing temperature of 120°F.
- 3 -
MULTIPLE COMPRESSOR APPLICATIONS
Multi-section units are available for applications where
more than one compressor is used either on the same
system or separate systems. Usually, this
arrangement will result in lower installation costs as
opposed to using separate units.
Coils for multi-section condensers are factory circuited
and divided into the proper number of sections, each sized
to meet the specified capacity. Each circuit is supplied
with a hot gas inlet and liquid outlet connection and
tagged for identification. The fan on a multi-section unit
should remain operative as long as a condensing requirement exists in any section of the coil.
TABLE 6 HEAT REJECTION CAPACITY PER FACE TUBE (BTU / HR) - R12
°F. (°C) TEMPERATURE DIFFERENCE = CONDENSING TEMPERATURE MINUS AMBIENT TEMPERATURE
1 (.6)10 (6)15 (8)20 (11)25 (14)30 (17)
GIVEN:
Six hermetic compressors with capacities and
evaporator temperatures (tabulated below).
RefrigerantR-22
Ambient Air Temperature100°F.
Maximum Condensing Temperature120°F.
PROCEDURE:
1.Tabulate the compressor capacities, evaporator
temperatures and heat rejection factors for each
compressor. (See Sample Tabulation, below.)
2.Determine the required heat rejection capacity for
each compressor.
3.Total the sectional heat rejection capacities for the
six compressors.
SELECTION:
Based on the total heat rejection capacity for the six
compressors of 186,160 Btuh, it can be seen from
Table No. 1 that the smallest unit which will meet this
requirement is the Model KCC217 with 210,000 Btuh
SAMPLE TABULATION
COMPRESSOR
NO.
1
2
3
4
5
6
COMPRESSOR
CAPACITY (BTUH)
13500
10000
36000
11000
31000
25000
EVAPORATOR
TEMPERATURE
°F.°C.
+20
-15
+15
+20
-10
+20
at 20 °F. T.D. Table No. 6 lists the heat rejection
capacity per “face tube” at various T.D.’s.
At 20 °F. T.D., the KCC 217 has a capacity of 9534 Btuh
per “face tube”. To determine the required number of face
tubes for each section, divide the required sectional
capacity by the capacity per “face tube”. For example,
compressor No. 1 requires 18,000 : 9534 = 2 “face tubes”.
Section No. 1 should be eircuited with 2 “face tubes” for
Compressor No. 1. Following this same procedure will
determine the size of each section for the remaining
compressors.
The sample tabulation shows the results of this selection
and indicates that 22 “face tubes” are required when
using the Model KCC 217. Since the Model KCC 217
has 22 “face tubes” available, the selection has been
satisfied. If the total required number of “face tubes”
exceeds the number of “face tubes” available as listed in
Table No. 6 it will be necessary to permit a slightly higher
condensing temperature than planned for one or two of
the sections. A second alternative would be to select the
next larger size condenser.
REQUIRED
CONDENSER
CAPACITY (BTUH)
18000
17440
51400
15070
50000
_34250_
186160
NUMBER OF
FACE TUBES
-7
-23
-9
-7
-23
-7
HEAT REJECTION
FACTOR
1.37
1.57
1.40
1.37
1.57
1.37
REQUIRED
2
2
6
2
6
_4_
22
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