7
2.2.7
fig. 2.7 illustrates stanchion plates at the pump inlet and outlet
ports that may be supplied for installation convenience. Isolation
pads must be used under the legs and monitored as pipe hang-
ers are adjusted to ensure the pump flanges are not support-
ing the piping. Bolting to the floor or housekeeping pad is not
recommended. If the stanchions are bolted down the bolts must
be isolated from the stanchion or an inertia base and flexible
pipe connectors used.
2.2.8
fig. 2.8 illustrates installations with stanchion plates for seismi-
cally active regions. Seismically rated isolation pads or snubbers
with bolts isolated from the stanchion plates are installed to
restrain the pump during a seismic event. Pipe hangers carry the
weight of the equipment as seismic components are designed
only to restrain the equipment during a seismic event.
2.2.9
Many Vertical In-Line pumps are piped successfully into
grooved piping systems. In-line pumps are supported well by
grooved piping however flange adapter locking devices or a
welded flange at the pump should be used to prevent the pos-
sibility of pipe mounted pumps rotating in the piping. Armstrong
oers grooved suction guides with cast-in outlet flanges and
Flo-Trex valves with Armgrip™ fittings to prevent this
possibility. (fig. 2.9)
2.2.10
Do not support the unit by the motor eye bolts (fig. 2.10)or by
any other part of the motor.
2.2.11
Connecting the pump to a permanent rigid base (fig.2.11)is not
recommended unless isolated from the piping by flexible con-
nectors and the base isolated from the building structure on an
inertia base. (fig. 2.11 is generally acceptable when using
plastic piping).
2.2.12
The motor and integrated control assembly can be rotated in
90° increments to meet installation spacing requirements.
Where applicable, remove the coupling guard to access the
motor bolts.Remove the motor bolts to rotate the motor and
integrated control assembly by hand.Larger motors may need
strapping and slight lifting to break the contact with the ped-
estal.Care should be taken that the controls are not damaged
during lifting and that the flushline, flushline accessories and the
coupling guard removal/seal service window are not compro-
mised following the turn (fig. 2.12).vil pumping units without
integrated controls can also be rotated in a similar manner to
facilitate access to the the motor terminal box.
2.2.13
For d1 and d2chassis Design Envelope units (110 kW–315 kW),
ensure adequate space is available for the access door to swing
open. (fig. 2.13)
important:
All Design Envelope 4300 pumps contain a tapped hole in the
motor bracket above the discharge flange (see fig. 2.14) for
draining the well. Pipe this drain hole to a floor drain to avoid
overflow of the cavity caused by collecting chilled water conden-
sate or from seal failure.
2.3 pump piping – general
Never connect a pump to piping, unless extra care is taken to
measure and align the piping flanges well. Always start piping
from pump.
Use as few bends as possible and preferably long radius elbows.
Do not use flexible connectors on the suction or discharge of a
vertical in-line pump, unless the pump is rigidly mounted to a
foundation.
Ensure piping exerts no strain on pump as this could distort
the casing causing breakage or early failure due to pump
misalignment.
All conecting pipe flanges must be square to the pipework and
parallel to the pump flanges.
Suction and discharge pipes may be increased or decreased at
pump nozzle to suit pump capacity and particular conditions of
installation. Use eccentric reducers on suction connection with
flat side uppermost.
Layout the suction line with a continual rise towards the pump
without high points, thus eliminating possibility of air pockets
that may prevent the pump from operating eectively.
A strainer of three or four times the area of the suction pipe,
installed in the suction line, will prevent the entrance of foreign
materials into the pump. V" (3mm) diameter perforations in the
strainer is typical.
In open systems, test suction line for air leaks before starting;
this becomes essential with long suction line or static lift.
Install, at the pump suction, a straight pipe of a length equiva-
lent to four or six times its diameter; this becomes essential
when handling liquids above 120°f (49°c). Armstrong suction
guides may be used in place of the straight pipe run and
in-line strainer.
Install an isolation valve in both suction and discharge lines on
flooded suction application; these valves are used primarily to
isolate the pump for inspection or repair.
Install a non-slam non-return check valve in discharge line
between pump and isolation valve to protect pump
from excessive back pressure and to prevent water running back
through the pump in case of driver failure on open systems.