Quick closing valves, positive displacement pumps, and vertical pipe
runs can create damaging pressure spikes, leading to blown diaphragms,
seals and gaskets also destroyed meters and gauges.
Liquid for all practical purposes is not compressible, any energy
that is applied to it is instantly transmitted. This energy becomes
dynamic in nature when a force such as quick closing valve or a pump
applies velocity to the fluid.
Surge (WaterHammer)
Surge or waterhammer, as it is commonly known is the result of a sudden change in liquid velocity. Waterhammer
usually occurs when a transfer system is quickly started, stopped or is
forced to make a rapid change in direction. Any of these events can
lead to catastrophic system component failure.
Without question, the primary cause of waterhammer
in process applications is the quick closing valve, whether manual or
automatic. A valve closing in 1.5 sec. or less depending upon valve
size and system conditions, causes an abrupt stoppage of flow. The
pressure spike(acoustic wave)created at rapid valve closure can be high
as five(5) times the system working pressure.
Unrestricted, this pressure spike or wave will rapidly accelerate to the speed of sound in liquid, which can exceed 4000 ft/sec. It is possible to estimate the pressure increase by the following formula.
Importance of Using this Formula While there are many online waterhammer
calculators, we have found wide variety in the results. We therefore
recommend using old fashioned pencil and paper and this formula:
WaterHammer Formula: P = (0.070) (V) (L) / t + P1
Where P = Increase in pressure
P1 = Inlet Pressure
V = Flow velocity in ft/sec
t = Time in sec.(Valve closing time)
L = Upstream Pipe Length in feet
Here's an example of pressure hammer when closing an EASMT solenoid valve, with a 50 ft long upstream pipe connection:
L = 50 ft
V = 5.0 ft / sec( recommended velocity for PVC piping design)
t = 40 ms(solenoid valve closing time is approx. 40-50 ms)
P1 = 50 psi inlet pressure
therefore, P = 0.07 x 5 x 50 / 0.040 + P1
or P = 437.5 psi + P1
Total Pressure = 437.5 + 50 = 487.5 psi
Pulsation
Pulsation generally occurs when a liquid's motive force is generated
by reciprocating or peristaltic positive displacement pumps. It is most
commonly caused by the acceleration and deceleration of the pumped
fluid. This uncontrolled energy appears as pressure spikes. Vibration
is the visible example of pulsation and is the culprit that usually
leads the way to component failure.
Unlike centrifugal pumps(which produce normally non-damaging
high-frequency but low-amplitude pulses), the amplitude is the problem
because it's the pressure spike. The peak, instantaneous pressure
required to accelerate the liquid in the pipe line can be greater than
ten (10) times the steady state flow pressure produced by a centrifugal
pump. Damage to seals gauges, diaphragms , valves and joints in piping
result from the pressure spikes created by the pulsating flow.
Remedy
Suggest that you install a pulsation dampener. Dampeners provide the
most cost efficient and effective choice to prevent the damaging
effects of pulsation. A surge suppressor is in design essentially the
same as pulsation dampener. The difference primarily lies in sizing and
pressurizing.
The most current pulsation dampener design is the hydro-pneumatic
dampener, consisting of a pressure vessel containing a compressed gas,
generally air or Nitrogen separated from the process liquid by a
bladder or diaphragm. The dampener is installed as close as possible to
the pump or quick closing valve and is charged to 85% of the liquid
line pressure. Proper sizing of the pulsation or surge suppressor
requires several calculations. A close contact with the suppressor's
manufacturer will ensure the correct sizing for a particular
application.
Conclusion
By knowing how to avoid situations that will create waterhammer
or pulsations during the specification process, or while trouble
shooting, you can eliminate a lot of problems, failed valves and
equipment, and costly downtime.
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Trust that answers your Question.
Kind Regards....
__________________
"The number of inventions increases faster than the need for them at the time" - SparkY
Will this phenomenon applies to compressed gas pipe too?
Suppose a air at 15 barg pressure is supplied to a consumer 500 m away, if consumer suddenly closes the shut off valve at their end, what will be the pressure rise before shut off valve and how long it will take to travel to supply point?
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