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Download a Printable Version Here (Adobe Acrobat Format) Centrifugal Pumps: Basic Concepts of Operation, Maintenance, and
Troubleshooting
General Symptoms of Cavitation and its Affects on Pump Performance and Pump Parts Perceptible
indications of the cavitation during pump operation are more or less loud noises,
vibrations and an unsteadily working pump. Fluctuations in flow and discharge pressure
take place with a sudden and drastic reduction in head rise and pump capacity. Depending
upon the size and quantum of the bubbles formed and the severity of their collapse, the
pump faces problems ranging from a partial loss in capacity and head to total failure in
pumping along with irreparable damages to the internal parts. It requires a lot of
experience and thorough investigation of effects of cavitation on pump parts to clearly
identify the type and root causes of cavitation. A
detailed description of the general symptoms is given as under. ·
Reduction in capacity of the pump: The
formation
of bubbles causes a volume increase decreasing the space available for the liquid and
thus diminish pumping capacity. For example, when
water changes state from liquid to gas its volume increases by approximately 1,700 times. If the bubbles get big enough at the
eye of the impeller, the pump chokes i.e. loses all suction resulting in a
total reduction in flow. The unequal and uneven formation and collapse of bubbles causes
fluctuations in the flow and the pumping of liquid occurs in spurts. This symptom is
common to all types of cavitations. ·
Decrease in the head developed: Bubbles
unlike liquid are compressible. The head developed diminishes drastically because energy
has to be expended to increase the velocity of the liquid used to fill up the cavities, as
the bubbles collapse. As mentioned earlier, The Hydraulic Standards Institute defines
cavitation as condition of 3 % drop in head developed across the pump. Like reduction in
capacity, this symptom is also common to all types of cavitations. Thus, the hydraulic effect of a cavitating pump is that the pump performance drops off of its expected performance curve, referred to as break away, producing a lower than expected head and flow. The Figure 12 depicts the typical performance curves. The solid line curves represent a condition of adequate NPSHa whereas the dotted lines depict the condition of inadequate NPSHa i.e. the condition of cavitation.
It
is movement of bubbles with very high velocities from low-pressure area to a high-pressure
area and subsequent collapse that creates
shockwaves producing abnormal sounds and vibrations. It has been estimated that during
collapse of bubbles the pressures of the order of 104 atm develops. The sound of cavitation can be
described as similar to small hard particles or gravel rapidly striking or bouncing off
the interior parts of a pump or valve. Various
terms like rattling, knocking, crackling are used to describe the abnormal sounds. The sound of pumps operating while
cavitating can range from a low-pitched steady knocking sound (like on a door) to a
high-pitched and random crackling (similar to a metallic impact). People can easily
mistake cavitation for a bad bearing in a pump motor. To distinguish between the noise due
to a bad bearing or cavitation, operate the pump with no flow. The disappearance of noise
will be an indication of cavitation. Similarly,
vibration is due to the uneven loading of the impeller as the mixture of vapor and liquid
passes through it, and to the local shock wave that occurs as each bubble collapses. Very
few vibration reference manuals agree on the primary vibration characteristic associated
with pump cavitation. Formation and collapsing of bubbles will alternate periodically with
the frequency resulting out of the product of speed and number of blades. Some suggest
that the vibrations associated with cavitation produce a broadband peak at high
frequencies above 2,000 Hertz. Some suggest that cavitation follows the vane pass
frequency (number of vanes times the running speed frequency) and yet another indicate
that it affects peak vibration amplitude at one times running speed. All of these
indications are correct in that pump cavitation can produce various vibration frequencies
depending on the cavitation type, pump design, installation and use. The excessive
vibration caused by cavitation often subsequently causes a failure of the pumps seal
and/or bearings. This is the most likely failure mode of a cavitating pump, ·
Damage to pump parts: o
Cavitation erosion or pitting During cavitation, the collapse of the bubbles occurs at sonic
speed ejecting destructive micro jets of extremely high velocity (up to 1000 m/s) liquid
strong enough to cause extreme erosion of the pump parts, particularly impellers. The
bubble is trying to collapse from all sides, but if the bubble is lying 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 and bangs against the metal creating the
impression that the metal was hit with a "ball pin hammer". The resulting
long-term material damage begins to become visible by so called Pits (see Figure 11), which are plastic deformations of very small dimensions (order of magnitude of micrometers). The damage caused due to action of bubble collapse is commonly referred as Cavitation erosion or pitting. The Figure 13 depicts the cavitation pitting effect on impeller and diffuser surface.
Cavitation erosion from bubble collapse occurs primarily by
fatigue fracture due to repeated bubble implosions on the cavitating surface, if the
implosions have sufficient impact force. The erosion or pitting effect is quite similar to
sand blasting. High head pumps are more likely to suffer from cavitation erosion, making
cavitation a high-energy pump phenomenon.
The most sensitive areas where cavitation erosion has been observed are the low-pressure sides of the impeller vanes near the inlet edge. The cavitation erosion damages at the impeller are more or less spread out. The pitting has also been observed on impeller vanes, diffuser vanes, and impeller tips etc. In some instances, cavitation has been severe enough to wear holes in the impeller and damage the vanes to such a degree that the impeller becomes completely ineffective. A damaged impeller is shown in Figure 14.
The damaged impeller shows that the
shock waves occurred near the outside edge of the impeller, where damage is evident.
This part of the impeller is where the pressure builds to its highest point.
This pressure implodes the gas bubbles, changing the waters state from gas into
liquid. When cavitation is less severe, the damage can occur further down towards
the eye of the impeller. A
careful investigation and diagnosis of point of the impeller erosion on impeller, volute,
diffuser etc. can help predict the type and cause of cavitation. The extent of cavitation erosion or pitting depends on a number
of factors like presence of foreign materials in the liquid, liquid temperature, age of
equipment and velocity of the collapsing bubble. o
Mechanical deformations ·
bending and deflection of shafts, ·
bearing damage and rubs from radial vibration, ·
thrust bearing damage from axial movement, ·
breaking of impeller check-nuts, ·
seal faces damage etc. These mechanical deformations can completely wreck the pump and
require replacement of parts. The cost of such replacements can be huge.
Cavitation
heart attack of the pump
By: Mukesh Sahdev, Associate Content Writer (read
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