If you are designing a new system or replacing an existing air-cooled condenser, Trane can satisfy
virtually any application need. Whether coupled with an industrial compressor, a single zone
commercial self-contained unit, compressor chiller or a Cold Generator® chiller, Trane has the right
air-cooled condenser for the job. When teamed with any one of a wide range of compressorevaporator combinations, Trane air-cooled condensers, available in 20 to 120 tons, are ideal for
multistory office buildings, hotels, schools, municipal and industrial facilities.
Trane 20 to 120 ton air-cooled condensers have an operating range of 40°F to 115°F, with a low
ambient option down to 0°F.
The control panel is factory-installed and wired to prevent potential damage and to provide
weathertight protection.
The control panel contains:
•fan motor contactors.
•fan cycling controls.
•terminal point connection for compressor interlock.
•115-volt control power transformer.
These standard features reduce installation costs and provide easy interface with control logic.
All Trane air-cooled condenser coils are an all aluminum Microchannel design. The 20 to 30 ton
condensers are single circuit; 40 to 120 ton units are dual circuited; all feature integral subcooling.
Units can have optional corrosion protected condenser coil.
Durable Construction
Trane 20 to 120 ton condensers are built for long life. The unit frame is constructed of 14 gauge
galvanized steel. Louvered panels provide excellent coil protection while enhancing unit
appearance and strength. The unit surface is phosphatized and finished with Trane Slate Grey airdry paint. This air dry-paint finish exceeds 500 consecutive hour salt spray resistance in accordance
with ASTM B117.
Microchannel Condenser Coils
Microchannel coils are an all aluminum coil that has
been successfully used in the automotive industry for
many years, and is now being applied in the HVAC
industry. The coils have a fully-brazed construction
which increases coil rigidity making them more
rugged to withstand the rigors of jobsite handling.
Additionally, the light weight simplifies coil handling.
The all aluminum construction creates an exceptional
heat transfer capability, allowing the refrigerant
charge to be reduced to levels that exceed LEED EACredit 4 requirements. Bottom line, less refrigerant is
being used, which creates a healthier and greener
environment.
4 ACDS-PRC003-EN
Application Considerations
Certain application constraints should be considered when sizing, selecting, and installing aircooled condensers. Unit and system reliability depends on properly and completely
acknowledging these considerations. Consult your local Trane sales engineer if your application
varies from these guidelines.
Setting the Unit
A base or foundation is not required if the selected unit location is level and strong enough to
support the operating weight. Refer to the Weights section for the weight of individual units.
Isolation and Sound Emission
The most effective method of noise isolation is proper unit location. Units should be placed away
from noise sensitive areas. Structurally transmitted noise can be reduced with the use of spring
isolators and they are recommended for acoustically sensitive applications. Flexible electrical
conduit, for maximum isolation effectiveness, will reduce sound transmitted through electrical
conduit.
State and local codes on sound emissions should always be considered. Since the environment in
which a sound source is located affects sound pressure, unit placement must be carefully
evaluated.
Servicing
Recommended minimum space envelopes for servicing are located in the Dimensional Data
section and serve as guidelines for providing adequate clearance. The minimum space envelopes
also allow for control panel door swing and routine maintenance requirements.
Unit Location
Unobstructed flow of condenser air is essential to maintaining capacity and operating efficiency.
When determining unit placement, careful consideration must be given to assure a sufficient flow
of air across the condenser heat transfer surface. Two detrimental conditions are possible and must
be avoided: Warm air recirculation and coil starvation.
Warm air recirculation occurs when discharge air from the condenser fans is recycled back at the
condenser coil inlet. Coil starvation occurs when free airflow to the condenser is restricted.
Both warm air recirculation and coil starvation cause reductions in unit efficiency and capacity
because of the higher head pressures associated with them. In more severe cases, nuisance unit
shutdowns will result from excessive head pressures.
Cross winds, those perpendicular to the condenser, tend to aid efficient operation in warmer
ambient conditions. However, they tend to be detrimental to operation in lower ambients or when
hot gas bypass is used due to the accompanying loss of adequate head pressure. As a result, it is
advisable to protect air-cooled condensers from continuous direct winds exceeding 10 miles per
hour.
Debris, trash, supplies, etc., should not be allowed to accumulate in the vicinity of the air-cooled
condenser. Supply air movement may draw debris into the condenser coil, blocking spaces
between coil fins and causing coil starvation. Special consideration should be given to low ambient
units. Condenser coils and fan discharge must be kept free of snow or other obstructions to permit
adequate airflow for satisfactory unit operation.
Clearance
Vertical condenser air discharge must be unobstructed. While it is difficult to predict the degree of
warm air recirculation, a unit installed with a ceiling or other obstruction above it will lose capacity
and the maximum ambient operation will be reduced. Nuisance high head pressure tripouts may
also occur.
The inlet to the coil must also be unobstructed. A unit installed closer than the minimum
recommended distance to a wall or other vertical riser may experience a combination of coil
ACDS-PRC003-EN5
Application Considerations
starvation and warm air recirculation, resulting in unit capacity and efficiency reductions, as well
as possible excessive head pressures. The recommended lateral distances are listed in the
Dimensional Data section.
Voltage
Nominal voltage is the nameplate rating voltage. The actual range of line voltages at which the
equipment can satisfactorily operate is given below:
Table 1.Voltage range
Nominal VoltageVoltage Utilization Range
200/230180-220 or 208-254
460416-508
575520-635
200/230-volt units ship from the factory set for operation in the 180 through 220-volt range. By
changing leads on unit transformers, the unit will operate in the 208 through 254-volt range.
Effects of Altitude
The tables in the Performance Data section are for use at sea level. At elevations substantially
above sea level, the decreased air density will decrease condenser capacity. Refer to the
Performance Adjustment Factors section to correct performance at other altitudes.
Ambient Limitations
Trane condensers are designed for year-around applications in ambients from 0°F through 115°F.
For operation below 0 F or above 115 F, contact the local Trane sales office.
Start-up and operation of Trane condensers at lower ambient temperatures require that sufficient
head pressure be maintained for proper operation. Minimum operating ambient temperatures for
standard unit selections and units with hot gas bypass are shown in the General Data section.
These temperatures are based on still conditions (winds not exceeding five mph.) Greater wind
velocities will result in a drop in head pressure, therefore, increasing the minimum starting and
operating ambient temperatures.
Units with the low ambient option are capable of starting and operating in ambients down to 0°F,
10°F with hot gas bypass. Optional low ambient units use a condenser fan damper arrangement
that controls condenser capacity by modulating in response to head pressure.
Maximum cataloged ambient temperature operation of a standard condenser is 115°F. Operation
at design ambients above 115°F can result in excessive head pressures. For operation above 115°F,
contact the local Trane sales office.
Minimum Outdoor Air Temperature for Mechanical Cooling
Standard Ambient
Operating Range (F)
Low Ambient Option (F)000000000
(a) Gross Heat Rejection is at a 30 F ITD (Initial Temperature Difference) between condensing temperature and ambient air entering condenser (includes
the effect of subcooling).
(b) At conditions of 95° ambient, condenser is 95 percent full
(c) Condensing units are shipping with nitrogen holding charge only.
(d) Operating charge is for condensing unit only, and does not include charge for low side or interconnecting lines.
When manually matching condensers with compressors, performance cross plotting becomes
necessary. The following procedure should be used to determine the correct condenser.
1. Determine the total cooling load. Make a prelimary compressor selection based on the
expected evaporator SST and condensing temperature.
Example:
Given-Total cooling load = 101 tons (1212 Mbh)
Design outdoor temperature = 95°F
Assume-Evaporator SST = 45°F (used in this example - application dependent)
Condenser SCT between 115°F and 125°F (20-30°F ITD SCT-ambient)
2. Select compressors from manufacturer's data to meet the load at the evaporator SST (for chiller
low suction applications contact Trane applications) -
Table 3.Compressor capacity with subcooling
(Qty 2) CSHN611 Trane R-410A Trio Scrolls Performance data includes 15°F subcooling
SSTSCTTonsMbh
451151101320
451251031236
Notes:
1. SST = Saturated Suction Temperature
2. SCT = Saturated Condensing Temperature
a. Remove the subcooling effect from the compressor performance at two or more compressor
capacity points. R-410A capacity increases 0.75% for every degree of subcooling (0.75% x
15°F = 11.25%). So if compressor performance is at 15°F subcooling, divide capacity by 1.1125
to get capacity at 0°F subcooling. Plot these two points (SCT vs. compressor tons a 0°F
subcooling) as shown in the selection example (Figure 1, p. 11).
Table 4.Compressor capacity with subcooling removed
(Qty 2) CSHN611 Trane R-410A Trio Scrolls
Capacity
15°F subcooling0°F subcooling
(a)
SST
45115110132098.91187
45125103123692.61111
(a) SST = Saturated Suction Temperature
(b) SCT = Saturated Condensing Temperature
SCT
(b)
TonsMbhTonsMbh
b. Select a condenser from Figure 3, p. 13 (CAUJ-D10 assumed for this example) and read two
condenser only heat rejection points. Divide the condenser heat rejection by the compressor
N factor (Table 6, p. 11) to convert from heat rejection to net capacity (Net Tons Less
Subcooling). The N factor equals the ratio of compressor heat rejection divided by
compressor capacity at 0°F subcooling. Plot these two points (SCT vs. Net Tons at 0°F
subcooling) as shown in Figure 1, p. 11 selection example.
ACDS-PRC003-EN9
Selection Procedures
Table 5.Condenser net capacity Mbh (less subcooling)
Assumed ∆T°F ITD
Notes:
1. ITD = Initial Temperature Difference
2. SCT = Saturated Condensing Temperature
3. N Factor = Compressor Efficiency Ratio
Note: Note that evaporator selection must also meet performance requirements. For this
(SCT - ambient)
20951159381.2773961.5
309512514181.33106688.8
Ambient,
°FSCT, °F
Cond only heat
rejection, Mbh N factor
Net capacity less subcooling
MbhTons
c. As shown on Figure 1, p. 11, draw a line though the points representing the compressor
capacity at 0°F subcooling. Next, draw a line through the points representing condenser net
capacity less subcooling.
d. At the point of intersection of the compressor and condenser lines draw dashed lines to the
left and bottom margins as shown in Figure 1, p. 11. The end points of these lines will show
a resultant gross capacity of 92 tons at 126.1°F condensing temperature.
e. From Figure 2, p. 12 calculate the percent increase in total heat rejection due to subcooling,
and multiply by the N factor (see Tab le 6 , p . 11 ) to get the percent increase in net capacity
due to subcooling.
Example:
At 95°F ambient and 126.1°F condensing temperature Figure 2, p. 12 shows there is a 7. 8 %
increase in total heat rejection due to subcooling. Tab l e 6 shows a 1.34 N factor by linear
interpolation. This yields a system capacity of 92 tons x (1 + 7. 8 % x 1. 34 ) = 102 tons.
f. If necessary use the values in Table 7, p. 12 to adjust the system capacity for altitude.
g. Compare this result with the design capacity and condensing temperature.
The required cooling load is 101 tons, therefore, the CAUJ-D10 is the proper selection.
Repeat the process steps B through G as necessary to achieve the most economic condenser
selection.
example, the evaporator needs to provide at least 105 tons at 45°SST. A conservative
estimate for liquid temperature entering the evaporator is the SCT minus the design
subcooling (125.1 - 15°F = 110.1°F for the example above). Contact Trane Applications if
excessive refrigerant line lengths or pressure drops are required.
10 ACDS-PRC003-EN
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