Q: Cavitation is
typically classified into two general categories – inertial and noninertial
cavitation. What is the difference between inertial and noninertial cavitations?
A: Cavitation in general terms is used to describe the
behavior of voids or bubbles in liquid. Any time a flowing liquid falls below
its vapor pressure, vapor bubbles can form. If the flowing liquid is then
subjected to pressures above the vapor pressure, these bubbles can implode
causing damage, which is called cavitation. Cavitation is usually divided into
two classes of behavior: inertial (or transient) cavitation, and noninertial
cavitation. Inertial cavitation is the process where a void or bubble in a
liquid rapidly collapses, producing a shock wave. Noninertial cavitation is the
process in which a bubble in a fluid is forced to oscillate in size or shape
due to some form of energy input, such as an acoustic field.
Q: What are the typical
causes of cavitation in and around pumping systems? What are the typical end
results of cavitation in pumping systems?
A: The cause of cavitation in pumps is usually due to
insufficient NPSH (Net Positive Suction Head) energy on the suction side of the
pump. NPSH is the energy required to push the liquid into the pump. This can be
caused by:
Having the pump at too high of a
distance above the fluid source
Having too small of a diameter of
suction pipe
Having too long of a distance of
suction pipe
Having too many fittings on the suction
pipe
Handling a liquid with a low vapor
pressure
Running the pump too fast.
The end result of cavitation is the collapse of the vapor
bubbles inside the pump, which can cause several problems. The first problem is
a reduction in the pumping capacity of the pump. If the pump is unable to keep
up with the incoming flow, then an overflow situation may occur. Cavitation
also causes damage to the pump. The collapsing vapor bubbles can cause
excessive vibration, which can cause rotating parts, such as the impeller, to
contact non-rotating parts, such as the wear plates or wear rings, causing
damage. Excessive vibration may also cause premature failure to mechanical
seals and bearings. Cavitation can also damage the wetted components themselves
from contact with the imploding vapor bubbles. In these instances, the energy
that is released when the vapor bubbles implode causes pieces of the metal to
break off and collide with other moving parts. The damage typically occurs to
the impeller and can severely reduce the operating life of the pump. The
collapse of vapor bubbles inside a pump can cause severe cavitation damage on
the impeller, resulting in negative process conditions such as vibration,
decreased flow, and noise.
Q: What are some common
warning signs that may signal the end-user that their pumping system is
experiencing cavitating conditions?
A: If the pump is cavitating, it will typically vibrate,
deliver less flow and make a noise that sounds like marbles going through the
pump. The sound may start out at a low level and increase in intensity over
time as material is chipped away and the surface of the parts becomes rougher.
This is due to the additional energy required by the drag (friction) on the
fluid from contacting the rough internal surfaces of the pump.
Cavitation is often confused with another phenomenon called
air entrainment. Air entrainment occurs when air is allowed to enter the pump
on the suction side and expands as it enters the impeller eye. This can often
reduce the flow of the pump and cause vibration from disrupting the laminar
flow stream through the pump. Air entrainment can cause similar damage to
bearings and seals. Unlike cavitation, however, this problem can be easily
remedied by simply identifying air leaks and fixing them.
An interesting point about cavitation and air entrainment is
that some experienced pump users have actually injected small amounts of air
into pumps that were cavitating to attempt to stop cavitation. By injecting air
into a pump that is cavitating, the air bubbles cushion the impact of the
imploding vapor bubbles and reduce the NPSHr of the pump, thus lessening the
cavitation. This technique, however should only be used by skilled pump
technicians, as too much air can cause priming problems and further adding air typically reduces the pump’s
capacity, which could cause an overflow condition.
Q: Why is cavitation so
prevalent in and around the pumping system as compared to other segments of the
process line? What other segments of the process line are particularly
susceptible to cavitating conditions?
A: Cavitation frequently occurs in pumps because of the
varying pressures in pumps. Centrifugal pumps operate from the principle of
creating a low pressure at the eye (center) of the impeller, and atmospheric
pressure forces the fluid to the eye to fill the void. As the fluid approaches
the eye of the impeller, the pressure drops, and if the pressure drops below
the vapor pressure of the particular liquid, it will boil and cause vapor
bubbles to form. As the fluid leaves the impeller eye, it is now exposed to
higher pressures (due to the rotation of the impeller inside the casing), which
can rise above the vapor pressure of the liquid, causing the vapor bubbles to
implode.
Cavitation can also occur in valves where the pressure drops
suddenly and there is a chance for the fluid to drop below its vapor pressure.
This can often occur in throttling type valves, such as gate valves or ball
valves. If the pressure differential from one side of the valve to the other
becomes too great, the fluid can vaporize across the valve and implode on the
downstream side of the valve. The way to avoid cavitation in valves is to size
them properly for the proper velocities. Valves are typically sized for
velocities less than 15 feet per second to avoid the possibility of cavitation.
Q: What are some common
best practices end-users can employ to prevent cavitation in and around their
pumping systems?
A: Always calculate the NPSHa (Net Positive Suction Head
available) from the system, and compare it with the NPSHr (Net Positive Suction
Head required) by the pump. The NPSHa should always be one to two feet above
the NPSHr of the pump to prevent cavitation.
The NPSHr is a function of the pump design and cannot be
changed. The NPSHa is a function of the system parameters and can be changed.
Included in the NPSHa is the atmospheric pressure, vapor pressure of the liquid
being pumped, static height from the water level to the pump, and friction
losses. The atmospheric pressure is related to the altitude. At higher
altitudes, the atmospheric pressure is less and subsequently there is not as
much energy available to push the liquid into the pump. The vapor pressure
varies by the type of liquid and the temperature of the liquid. If the liquid
is allowed to cool before the pump, it can often be pumped easier. Regarding
the static height from the fluid level to the pump, it is often possible to
move the pump closer to the fluid to increase the NPSHa. To reduce the friction
losses, larger diameter pipes can often be employed to increase the NPSHa and
thus prevent cavitation.
If it is not possible to increase the NPSHA as described
above, then the pump user should search for a larger pump or pump that runs at
a lower speed with lower NPSHr.
Q: From a technology
perspective, are there any systems end-users can employ to help them more
effectively diagnose and mitigate cavitation in and around their pumping
systems?
A: The most effective solution is to listen to the pump and
to evaluate the flow. Flow can best be determined using flowmeters, and there
are several types commercially available, depending on the type of fluid being
moved. Listening to the pump can be accomplished by the naked ear by trained
personnel or by using suitable noise level meters. More sophisticated vibration
measuring equipment can also be employed to detect cavitation. These portable
devices can connect to the pump bearing housings to detect movement
(displacement).
Q: How were these
cavitation issues resolved?
A: Among the most common applications that are susceptible to
cavitation are applications that have high-suction lifts with little-to-no
discharge heads, as is the case with bypassing sewage from manholes. In these
applications, the duty point does not fall on the typical performance curve because
there is insufficient discharge pressure. In these applications, it is called
operating “too far to the right of the curve.” The way to fix this is to put
artificial pressure on the discharge of the pump. This can be accomplished by
using smaller-diameter discharge hose or placing a throttling valve in the
discharge line.