ENGLISH
7.2 PIPE WORK
Pump connection flanges are plugged to avoid any contamination during
transport and storage. Protective covers should be removed only before
installing the pump in the piping. Remove dust before removing the
covers from pump flanges. Especially for new pipe work : clean
thoroughly piping before connecting it to the pump.
Remove protective covers
Add flange gaskets
Fasten suction pipe
Fasten discharge pipe
No stress must be applied to the pump casing by the pipe work. If
excessive, those forces and moments cause misalignment,
overheating of bearings, coupling wear, vibrations and possible failure or
explosion of pump casing.
After replacement of a pump or during connection of pipes to
pump flanges, never use pump flanges as a support to pull or push
the pipe works.
The axial displacement of expansion coupling (if installed) should be
limited. Use tie rods as recommended by the manufacturer.
Two designs are possible for the suction line : positive suction head and
suction lift operation.
Positive suction head operation :
Nominal diameter of the pipeline is often larger diameter than pump
suction flange. Unequal nominal diameter should be compensated by an
eccentric transition part. It is recommended to install a straight pipe
before the pump inlet (size L should be 2 to 3 times the pipe nominal
dimension). The suction line should be laid with a downward slope
toward the pump.
Suction lift operation :
Nominal diameter of the suction pipe must be equal or a size larger than
the pump suction flange diameter. Pipe inlet should be set below lower
liquid level. Install a strainer with foot valve to prevent priming loss. The
strainer will be installed far enough from the pit bottom to avoid
excessive suction head losses and particles intake. Ensure there is no air
intake along the suction pipe and that the suction pipe is inclined
upwards towards the pump inlet. Avoid air pocket creation.
Suction line should be airtight and as short as possible. Use of large
radius bends should be preferred. If possible the nominal diameter of
suction pipe will be the same as pump nominal diameter. The size of
pipe will be selected to limit flow speed to 2m/s. A straight pipe (length
= 2 times the pipe diameter) will be installed on pump suction side.
During pump priming period air contained in the suction pipe is
eliminated and liquid is lifted up to suction flange level.
When suction pipe is full of liquid the pump is acting like a standard
centrifugal pump.
Priming time will increase if a larger pipe diameter is used or if pipe
length is increased. Any air intake along this pipe will delay or avoid
pump priming.
Check that pump required NPSH (NPSH
available NPSH (NPSH
Discharge pipe :
During priming time, air contained in suction pipe is pumped through
the pump to the discharge pipe. Free exhaust of this gas to the
atmosphere should be possible.
If this requirement cannot be met, a vent pipe connected before the
NRV and going back to the pit/sump or an automatic air‐vent valve
should be installed.
If an explosion hazard exists, check that the area around the outlet
of this venting pipe is identified as an ATEX zone.
A vent pipe or an automatic air vent valve must be installed ahead of
the non‐return valve. A motorized valve can be used to close vent pipe
and avoid recirculation of fluid during normal operation.
Nominal diameter of discharge pipe should be chosen to ensure a max
flow speed of 3m/s.
Filter/strainer :
If required a filter can be installed before the pump intake. To ensure
proper working of pump the equivalent exchange surface of the strainer
should be 3 time the pipe sectional area.
Clogging state of filter/strainer should be checked regularly.
Valves :
It is advised to install isolating valves on suction and discharge side for
maintenance purpose. Those valves should be of large passage type and
could be locked in position.
Isolating valve on suction side will not be connected directly to pump
suction flange.
Auxiliary piping :
For most of applications a single mechanical seal is used. If the sealing
must be equipped with auxiliary equipments, check that there are no
leakages and that direction of flow is respected.
Single mechanical seal with quench :
External piping system or raised tank should be installed in the state of
the art. Pressure in the quench should not exceed 0,35 bar.
Single mechanical seal with external flushing :
Flushing fluid should be pressurized at 0,5 / 1 bar above pump discharge
pressure.
After pipe work is done turn the pump shaft by hand and check that it
turns freely. If it appears that it is difficult to turn the pump shaft, then
check forces applied by piping to pump casing. Installation of piping
should be done again.
7.3 ELECTRICAL CONNECTION / EARTHING
Check that motor winding corresponds to site electric power
supply characteristics before electrical connections are performed.
Connecting a 230/400V motor on a 400V power supply or
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