8 running or operation – Flowserve ESP3 User Manual
Page 35

ESP3 USER INSTRUCTIONS ENGLISH 26999943 08-11
Page 35 of 64
It is important that the discharge valve be opened
within a short interval after starting the driver. Failure to 
do this could cause a dangerous buildup of heat, and 
possibly an explosion. 
 
5.8 Running or operation
5.8.1 Minimum continuous flow 
Minimum continuous stable flow is the lowest flow at 
which the pump can operate and still meet the bearing 
life, shaft deflection and bearing housing vibration limits 
documented in the latest version of ASME B73.1M. 
Pumps may be operated at lower flows, but it must be 
recognized that the pump may exceed one or more of 
these limits. For example, vibration may exceed the 
limit set by the ASME standard. The size of the pump, 
the energy absorbed, and the liquid pumped are some 
of the considerations in determining the minimum 
continuous flow (MCF). 
The minimum continuous flow (capacity) is established 
as a percentage of the best efficiency point (BEP). (See 
section 3.4.4.) 
 
5.8.2 Minimum thermal flow 
All ESP3 pumps also have a minimum thermal flow. 
This is defined as the minimum flow that will not 
cause an excessive temperature rise. Minimum 
thermal flow is application dependent. 
Do not operate the pump below
minimum thermal flow, as this could cause an excessive 
temperature rise. Contact a Flowserve sales engineer 
for determination of minimum thermal flow. 
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 bearings and any equipment 
flushed with process fluid will be exposed to vapor, with 
no lubrication, and may score or seize to the stationary 
parts. 
Thermostats may be used to safeguard against 
overheating 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 sump should 
be properly drained or protected with thermal devices 
which will keep the liquid in the sump from freezing. 
External bearing and seal lubrication lines must be 
protected with thermal devices. High chrome iron 
pumps are not recommended for applications below -
18 °C (0 °F). 
 
5.8.6 Operating Checks 
Costly shutdowns will be avoided by making routine 
checks on pump operation. 
a) 
Check to see if liquid is being discharged. A 
discharge pressure gauge is an easy way to 
check whether or not the liquid is being pumped. 
If, at any time, the gauge should drop near or to 
zero, or register an abnormally high pressure, 
shut down the pump immediately. 
b)
Observe pump for any abnormal noise or 
vibration. Especially check for any CHANGE in 
pump noise or vibration. 
c)
Bearing lubricating liquid, and sealing and 
cooling liquid flows, should be checked 
frequently. 
 
5.8.7 Normal vibration levels, alarm and trip 
Alarm and trip values for installed pumps should be 
based on the actual measurements (N) taken on site 
on the motors of vertical pumps in 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 two. 
 
These standard values can vary with the rotational 
speed and the power absorbed by the pump. For 
any special case, contact your nearest Flowserve 
office. 
 
