UB USER INSTRUCTIONS ENGLISH 71569247 07-04

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Prevent excessive external pipe load

Never draw piping into place by applying force to pump flange connections

Do not mount expansion joints so that their force, due to internal pressure, acts on the pump flange

The table in 4.5.3 summarizes the maximum forces and moments allowed on horizontal shaft pump casings.

Ensure piping and fittings are flushed before use.

Typical design – flooded suction

 

 

Concentric

Eccentric

Suction

Discharge

 

conical

conical

isolating

isolating

Non

reducer

reducer

valve

valve

return

 

 

 

 

valve

 

 

 

>5D

Slope up from pump suction

Note:

Ensure piping for hazardous liquids is arranged to allow pump flushing before removal of the pump.

4.5.2 Suction piping

a)The inlet pipe should be one or two sizes larger than the pump inlet bore and pipe bends should be as large a radius as possible.

b)Pipework reducers should be conical and have a maximum total angle of divergence of 15 degrees.

c)On suction lift the piping should be inclined up towards the pump inlet with eccentric reducers incorporated to prevent air locks.

d)On positive suction, the inlet piping must have a constant fall towards the pump.

e)Flow should enter the pump suction with uniform flow, to minimize noise and wear. This is particularly important on large or high-speed pumps, which should have a minimum of five diameters of straight pipe on the pump suction between the elbow and inlet flange. See section 10.3, Reference 1, for more detail.

f)Inlet strainers, when used, should have a net `free area' of at least three times the inlet pipe area.

g)Do not install elbows at an angle other than perpendicular to the shaft axis. Elbows parallel to the shaft axis will cause uneven flow.

h)Except in unusual circumstances strainers are not recommended in inlet piping. If considerable foreign matter is expected a screen installed at the entrance to the wet well is preferable.

i)Fitting an isolation valve will allow easier maintenance.

j)Never throttle pump on suction side and never place a valve directly on the pump inlet nozzle.

Ideally reducers should be limited to one pipe diameter change, ie 150 mm (6 in.) to 200 mm (8 in.). Must have a maximum total angle of divergence of 15 degrees.

Typical design – suction lift

Discharge

 

Concentric

Eccentric

isolating

Non

conical

conical

valve

return

reducer

reducer

valve

Slope down

>5D

from pump

suction

 

Long

 

radius

 

bend

Notes:

1.S = Minimum submergence >3E.

2.Ideally reducers to be limited to one pipe diameter change, ie 150 mm (6 in.) to 200 mm (8 in.). Must have a maximum total angle of divergence of 15 degrees.

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