9 stopping and shutdown – Flowserve S-series PolyChem User Manual
Page 29

USER INSTRUCTIONS POLYCHEM S-SERIES ENGLISH 71569207 11-08
Page 29 of 52
flowserve.com
Avoid running a centrifugal pump at drastically reduced 
capacities or with discharge valve closed for extended 
periods of time. This can cause severe temperature 
rise and the liquid in the pump may reach its boiling 
point. If this occurs, the mechanical seal will be 
exposed to vapor, with no lubrication, and may score or 
seize to the stationary parts. Continued running under 
these conditions when the suction valve is also closed 
can create an explosive condition due to the confined 
vapor at high pressure and temperature. 
Thermostats may be used to safeguard against over 
heating by shutting down the pump at a predetermined 
temperature. 
Safeguards should also be taken against possible 
operation with a closed discharge valve, such as 
installing a bypass back to the suction source. The size 
of the bypass line and the required bypass flow rate is a 
function of the input horsepower and the allowable 
temperature rise. 
 
5.8.3 Reduced head 
Note that when discharge head drops, the pump’s 
flow rate usually increases rapidly. Check motor for 
temperature rise as this may cause overload. If 
overloading occurs, throttle the discharge. 
 
5.8.4 Surging condition 
A rapidly closing discharge valve can cause a 
damaging pressure surge. A dampening 
arrangement should be provided in the piping. 
 
5.8.5 Operation in sub-freezing conditions 
When using the pump in sub-freezing conditions 
where the pump is periodically idle, the pump should 
be properly drained or protected with thermal devices 
which will keep the liquid in the pump from freezing. 
 
5.8.6 Bearing monitoring 
If the pumps are operating in a potentially
explosive atmosphere temperature or vibration 
monitoring of the bearings is recommended. 
 
If bearing temperatures are to be monitored it is 
essential that a benchmark temperature is recorded 
at the commissioning stage and after the bearing 
temperature has stabilized. 
• Record the bearing temperature (t) and the 
ambient temperature (ta)
• Estimate the likely maximum ambient
temperature (tb)
• Set the alarm at (t+tb-ta+5) ºC ((t+tb-ta+10) ºF)
and the trip at 100 ºC (212 ºF) for oil lubrication 
and 105 ºC (220 ºF) for grease lubrication. 
It is important, particularly with grease lubrication, 
to keep a check on bearing temperatures. After 
start up the temperature rise should be gradual, 
reaching a maximum after approximately 1.5 to 2 
hours. This temperature rise should then remain 
constant or marginally reduce with time. 
 
5.8.6.1 Normal vibration levels, alarm and trip 
For guidance, pumps generally fall under a 
classification for rigid support machines within the 
International rotating machinery standards and the 
recommended maximum levels below are based on 
those standards. 
 
Alarm and trip values for installed pumps should be 
based on the actual measurements (N) taken on site 
on the bearing housings of the pump in the fully 
commissioned as new condition. 
 
The example (N) value is given for the preferred 
operating flow region (typically this may extend to 70 
to 120 % of the pump best efficiency point); outside 
the preferred flow region the actual vibration 
experienced may be multiplied by up to 2. 
 
These standard values can vary with the rotational 
speed and the power absorbed by the pump. For any 
special case, do not hesitate to consult us. 
 
Measuring vibration at regular intervals will then show 
any deterioration in pump or system operating 
conditions. 
Vibration velocity – 
unfiltered 
Horizontal pumps 
≤ 15 kW (20 hp) 
mm/s (in./sec) 
r.m.s. 
> 15 kW (20 hp)
mm/s (in./sec) 
r.m.s. 
Normal
N
≤ 3.0 (0.12)
≤ 4.5 (0.18)
Alarm
N x 1.25
≤ 3.8 (0.15)
≤ 5.6 (0.22)
Shutdown trip
N x 2.0
≤ 6.0 (0.24)
≤ 9.0 (0.35)
5.9 Stopping and shutdown
 
5.9.1 Shutdown considerations 
Pump sets are normally suitable for the number of 
equally spaced stop/starts per hour shown in the 
table below. Check the capability of the driver and 
control/starting system before commissioning. 
Motor rating kW (hp)
Maximum start ups
per hour
Up to 15 (20)
15
Between 15 and 90 (20 and 120)
10
Above 90 (120)
6
Where duty and standby pumps are installed it is 
recommended that they are run alternately every 
week. 
