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Both cavitation and air ingestion have an affect on the pump. The bubbles collapse as they pass from the eye of the pump to the higher pressure side of the impeller. Air ingestion seldom causes damage to the impeller or casing. The main effect of air ingestion is loss of capacity.
Cavitation
Cavitation means different things to
different people. It has been described as:
- A reduction in pump capacity.
- A reduction in the head of the
pump.
- The formation of bubbles in a low
pressure area of the pump volute.
- A noise that can be heard when
the pump is running.
- Damaged that can be seen on the
pump impeller and volute.
The capacity of the pump is reduced
- This happens because bubbles take
up space and you cannot have bubbles and liquid in the same place at the
same time.
- If the bubble gets big enough at
the eye of the impeller, the pump will lose its suction and will require
priming.
The head is often reduced
- Bubbles unlike liquid are
compressible. It is this compression that can change the head.
The bubbles form in a lower pressure
area because they cannot form in a high pressure area.
- As the velocity of a fluid
increase, the pressure of the fluid decreases. This means that high
velocity liquid is by definition a lower pressure area. This can be a
problem any time a liquid flows through a restriction in the piping,
volute, or changes direction suddenly. The fluid will accelerate as it
changes direction. The same acceleration takes place as the fluid flows in
the small area between the tip of the impeller and the volute cut water.
A noise is heard
- Any time a fluid moves faster
than the speed of sound, in the medium you are pumping, a sonic boom will
be heard. The speed of sound in water is 4800 feet per second (1480
meters/sec) or 3,273 miles per hour (5,267 kilometers per hour).
Pump parts show damage
- The bubble tries to collapse on
its self. This is called imploding, the opposite of exploding. The bubble
is trying to collapse from all sides, but if the bubble is laying against
a piece of metal such as the impeller or volute it cannot collapse from
that side, so the fluid comes in from the opposite side at this high
velocity proceeded by a shock wave that can cause all kinds of damage.
There is a very characteristic round shape to the liquid as it bangs
against the metal creating the impression that the metal was hit with a
"ball peen hammer".
- This damage would normally occur
at right angles to the metal, but experience shows that the high velocity
liquid seems to come at the metal from a variety of angles. This can be
explained by the fact that dirt particles get stuck on the surface of the
bubble and are held there by the surface tension of the fluid. Since the
dirt particle has weakened the surface tension of the bubble it becomes
the weakest part and the section where the collapse will probably take
place.
- The pressure of the implosion has
been calculated to be in the region of 1000 bar, with velocities around
4000 m/s.
To cure cavitation problems you must
either increase the suction head, lower the fluid temperature or decrease the
N.P.S.H. Required.
Increase the suction head
- Raise the liquid level in the
tank
- Raise the tank
- Put the pump in a well
- Reduce the piping losses. These
losses occur for a variety of reasons that include :
- The system was designed
incorrectly. There are too many fittings and/or the piping is too small
in diameter.
- A pipe liner has collapsed.
- Solids have built up on the
inside of the pipe.
- The suction pipe collapsed when
it was run over by a heavy vehicle.
- A suction strainer is clogged.
- Be sure the tank vent is open
and not obstructed. Vents can freeze in cold weather
- Something is stuck in the pipe,
It either grew there or was left during the last time the system was
opened. Maybe a check valve is broken and the seat is stuck in the pipe.
- The inside of the pipe or a
fitting has corroded.
- A bigger pump has been installed
and the existing system has too much loss for the increased capacity.
- A globe valve was used to
replace a gate valve.
- A gasket is protruding into the
piping.
- The pump speed has increased.
- Install a booster pump
- Pressurise the tank
Lower the fluid temperature
- Injecting a small amount of
cooler fluid at the suction is often practical.
- Insulate the piping from local
heat sources.
- Minimise discharge recirculation
lines, they can heat up the suction fluid.
Reduce the N.P.S.H. Required
- Use a double suction pump. Use a
lower speed pump
- Use a pump with a larger impeller
eye opening.
- If possible install an Inducer.
These inducers can cut N.P.S.H.R. by almost 50%.
- Use several smaller pumps. Three
half capacity pumps can be cheaper than one large pump plus a spare. This
will also conserve energy at lighter loads.
Both cavitation and air ingestion have an affect on the pump. The bubbles collapse as they pass from the eye of the pump to the higher pressure side of the impeller. Air ingestion seldom causes damage to the impeller or casing. The main effect of air ingestion is loss of capacity.
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