NOTICE
Breaker Cracking Pressure!
The 1/2-inch NPT, 15 degree swing check valve vacuum
breaker is recommended because other vacuum
breakers, such as spring-loaded ball-check breakers,
have cracking pressures as high as 1.25 inches Hg (17
inches of water). Vacuum breakers with fitting sizes
smaller than 1/2 inch NPT are too small to relieve
vacuum quick enough to ensure complete condensate
drainage. Other types of swing check valve vacuum
breakers are acceptable if the fittings size is not smaller
than 1/2-inch NPT and the cracking pressure is not
larger than 0.25 inches HG (3.5 inches of water). Failure
to follow these instructions could result in equipment
damage.
Piping and Connections
44 CLCH-SVX013B-EN
To prevent coil damage, complete the following
recommendations:
• Install a 1/2-inch NPT, 15 degree swing check valve
vacuum breaker
with cracking pressure of 0.25 inches
Hg (3.4 inches water) or lower at the top of the coil. This
vacuum breaker should be installed as close to the coil
as possible.
• For coil type NS, install the vacuum breaker in the
un
used condensate return tapping at the top of the
coil.
• Vent the vacuum breaker line to atmosphere or
connect it into the return main at
the discharge side of
the steam trap
Note: Vacuum breaker relief
is mandatory
when the coil
is controlled by a modulating steam supply or
automatic two position (ON-OFF) steam supply
valve. Vacuum breaker relief is also recommended
when face-and-bypass control is used.
NOTICE
Coil Condensate!
Condensate must flow freely from the coil at all times
to prevent coil damage from water hammer, unequal
thermal stresses, freeze-up and/or corrosion. In all
steam coil installations, the condensate return
connections must be at the low point of the coil. Failure
to follow these instructions could result in equipment
damage.
Proper steam trap installation is necess
ary for satisfactory
coil performance and service life. For steam trap
installation:
1. Install the steam trap discharge 12 inches below the
condensate return con
nectio
n. Twelve inches provides
sufficient hydrostatic head pressure to overcome trap
losses and ensures complete condensate removal.
a. Use float and thermostatic
traps with atmospheric
pressure gravity condensate return, with automatic
controls, or where the possi
bility of low-pressure
supply steam exists. (Float and thermostatic traps
are recommended because of gravity drain and
continuous discharge operation.)
b. Use bucket traps only when the supply steam is not
m
odulated and is 25 psig or higher.
Note: Trane steam coils require a minimu
m of 2 psi of
pressure to assure even heat distribution.
2. Trap each coil separately to prevent holding up
condensate in
one or more of the
coils.
3. Install strainers as close as possible to the inlet side of
the trap.
4. If installing coils in series
airflow
, control each coil
bank independently with an automatic steam-control
valve. Size the traps for each coil using the capacity of
the first coil in direction of airflow.
5. Use a modulating valve that
has linear flow
charac
teristics to obtain gradual modulation of the coil
steam supply.
Note: Do not
modulate systems with over
head or
pressurized returns unless the condensate is
drained by gravity into a receiver, vented to
atmosphere, and returned to the condensate
pump.
6. Pitch all supply and return steam piping down 1 inch
for eve
ry 10 feet in the direction of the
steam or
condensate flow.
Note: Do
not drain the steam mains or take-offs
through
the coils. Drain the mains ahead of the coils
through a steam trap to the return line.
7. Ensure overhead returns have 1 psig of pressure at the
stea
m trap discharge for
every 2 feet of elevation for
continuous condensate removal.
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