Flowserve M-series PolyChem User Manual
Page 19

USER INSTRUCTIONS PolyChem M-SERIES ENGLISH 71569218 07-11
flowserve.com
Page 19 of 60
®
short length of flexible piping. The pump should not 
have to support the weight of the pipe or compensate 
for misalignment. It should be possible to install suction 
and discharge bolts through mating flanges without 
pulling or prying either of the flanges. All piping must be 
tight. Pumps may air-bind if air is allowed to leak into 
the piping. If the pump flange(s) have tapped holes, 
select flange fasteners with thread engagement at least 
equal to the fastener diameter but that do not bottom 
out in the tapped holes before the joint is tight. 
 
The following is the recommended procedure for 
attaching piping to the PolyChem M-series pump (see 
section 6.5 for torque values) 
 
Check the surface of both flanges (pump/pipe) to
ensure they are clean, flat, and without defects
Lubricate the fasteners
Hand tighten all of the fasteners in a crisscross
pattern
The fasteners should be torqued in increments
–
based a crisscross pattern
o The first increment should be at 75%
of the full torque
o The second increment should be at the
full torque
o Verify that the torque value of the 1
st
fastener is still at the full torque value
Retorque all fasteners after 24 hours or after the first
thermal cycle
Retorque all fasteners at least annually
 
4.6.2 
Suction piping
To avoid NPSH and suction problems, suction piping 
must be at least as large as the pump suction 
connection. Never use pipe or fittings on the suction 
that are smaller in diameter than the pump suction size. 
 
Figure 4-7 illustrates the ideal piping configuration with a 
minimum of 10 pipe diameters between the source and 
the pump suction. In most cases, horizontal reducers 
should be eccentric and mounted with the flat side up as 
shown in Figure 4-8 with a maximum of one pipe size 
reduction. Never mount eccentric reducers with the flat 
side down. Horizontally mounted concentric reducers 
should not be used if there is any possibility of entrained 
air in the process fluid. Vertically mounted concentric 
reducers are acceptable. In applications where the fluid 
is completely de-aerated and free of any vapor or 
suspended solids, concentric reducers are preferable to 
eccentric reducers. 
Figure 4-7 Figure 4-8
Avoid the use of throttling valves and strainers in the 
suction line. Start up strainers must be removed shortly 
before start up. When the pump is installed below the 
source of supply, a valve should be installed in the 
suction line to isolate the pump and permit pump 
inspection and maintenance. However, never place a 
valve directly on the suction nozzle of the pump. 
 
Refer to the Durco Pump Engineering Manual and 
the Centrifugal Pump IOM Section of the Hydraulic 
Institute Standards for additional recommendations 
on suction piping. (See section 10.) 
 
Refer to section 3.4 for performance and operating 
limits. 
 
4.6.3 
Discharge piping
Install a valve in the discharge line. This valve is 
required for regulating flow and/or to isolate the pump 
for inspection and maintenance. 
When fluid velocity in the pipe is high,
for example, 3 m/s (10 ft/sec) or higher, a rapidly 
closing discharge valve can cause a damaging 
pressure surge. A dampening arrangement should 
be provided in the piping. 
 
4.6.4 
ALLOWABLE NOZZLE LOADS
 
Introduction 
Never use the pump as a support for piping. 
 
Maximum Forces and moments allowed on pump 
flanges vary based on the pump size. When these 
forces and moments are minimized, there is a 
corresponding reduction in misalignment, hot 
bearings, worn couplings, vibration and possible 
failure of the pump casing. The following points 
should be strictly followed: 
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 pipe flange
