Why Seals Fail
Seals fail for a number of reasons. Your job is to pinpoint the reason and fix it.
Here
you are in a situation in which the seal has run for a period well
beyond the installation period. Its leaking and now you have to make a
decision. Has the seal failed or simply worn out? What you decide now
will determine whether you fit a replacement seal or seek out an
alternative type. The basics are simple.
A worn out seal will leak when the seal face has worn away completely.
If
we extend this criteria to all leaking seals it becomes sadly obvious
that the majority of seals, perhaps 85% of process seals, fail long
before they are worn out.
This section is
devoted to the three main reasons why seals fail. Only three you say?
Three main reasons and lots of routes to them.
Seals fail because ...
The seal faces open.
Heat causes a problem.
The chemical environment causes a material failure.
OK so there is another category ... the installation failure, but that's covered in the installation section.
Seal Faces Open
The shaft moves for many reasons, those that affect the seal operation are:
Axial
End play
Thrust movement
Temperature growth
Impeller adjustment
Radial
Bearing wear
Bent shaft
Shaft whip
Shaft deflection (discharge closed)
Vibration
System NPSH incorrect causing cavitation
Harmonic
vibration, check the coupling, does it "hum" or "buzz". Rubber
couplings can operate with high degrees of misalignment without total
failure but cause problems for the seal.
Impeller imbalance
Slip-stick.
Not surprisingly not much is known about what happens between seal
faces in service. There are theories. The faces acquire a film of liquid
that lubricates the seal surfaces, the carbon face wears slightly
depositing a layer of carbon on the stationary face so that the carbon
face runs on carbon , but there is a condition that causes the faces to
vibrate open when pumping non-lubricating fluids. Fluids near their
vapour point, very hot water, can cause these conditions. The seal faces
"chatter " against each other in a slip-stick motion slipping when the
drive lug hits the seal head, bouncing round and momentarily stopping
before being hit by the drive lug again. To be a sealman you have to
believe.
Poor pump performance. This statement
covers a host of sins. Consider running two or three pumps into one
discharge line, the odds are that the pump performances will not be
perfectly matched. Does it matter? Not really, unless you are concerned
about your seal life, because what is happening here? One or other of
the pumps, because of poor performance now combined with poor system
design, will be experiencing discharge throttling, tending to over load
the impeller at the throat, causing turbulent flow and shaft bending.
Look into other causes of poor pump performance.
Other causes
The
seal runs against a stationary component. The stationary is usually
fitted into the seal plate which is bolted to the pump and sealed with a
gasket. Now, I do not want to sound too pedantic here but you have to
realize that the seal stationary has to be fitted square to the axis of
the shaft and in proper alignment with the axis of the pump shaft. The
stationary has to be fitted into the seal-plate square. None of this is
easy to achieve and each error compounds the next. The rotating head has
to follow any misalignment from square that the stationary carries.
Every rotation of the shaft causes the rotating seal head to move
back-and-forth twice. Interfere with that movement and the faces are
open.
Difficult
as it is to get the stationary fitted correctly, should you achieve it
then other factors come into play to limit the excellence of your work.
Stress imposed by pipe strain, coupling misalignment, or plain thermal
growth put the pump casing out of shape just enough to cause the seal to
work harder.
All
of the items described mean that the shaft and seal are in constant
relative movement. If anything interferes with the free movement of the
seal, the faces open.
When
the faces open, dirt in the liquid penetrates the lapped surfaces,
embeds in the soft face which gradually changes to a grinding surface to
score and wear away the hard face of the stationary ring. Have you
noticed this effect? Do you look at your failed seals? You should,
because on those faces lie clues to help you find the faults opposing
long seal life. Well when we have gotten through this section and onto
the tell tale signs I bet you will take a bit more notice of your failed
seal bodies.
The main reasons why seal faces open are:
The
elastomer sticks to the shaft. Spring loaded elastomers will stick to
the shaft, O-rings will flex by 0.005" (0.13mm) and then roll. O-rings
will fret a shaft but spring loaded elastomers (teflon wedges, chevrons,
etc.) can cause serious surface damage to your shaft or sleeve leading
to early seal failure. A leak under the seal head looks very much like a
face leak.
The shaft is out on machining
tolerance. Correct tolerance is +0.000" to -0.002" from nominal. A
packing sleeve is not machined to any close tolerance, after all it is
going to wear against the packing so its external dimension is not too
important. An oversize sleeve or shaft will cause the seal to hang-up,
an under size shaft or sleeve will prejudice the ability of the
elastomers to seal the head to the shaft/sleeve.
The
surface finish on the shaft/sleeve is too rough. A lathe finish is not
good enough. The finish should be at least 32 RMS and for that a ground
finish is required.
Have you got a hardened
shaft on your pump unit? The seal set screws will not "bite" into the
shaft and could slip causing the setting dimension of the seal to alter.
The
pumped fluid changes state. Sea water, brine pumps, sugary solutions,
cause crystallizing when the salts come out of solution or the sugars
become caramelized. Other coking substances, heat transfer oil, tar,
cause similar problems. You will see the build up of material around the
leak site.
Solids can cause the seal head to
stick to the shaft or restrict the o-ring flexibility. Take a look at
the double seal arrangement, back to back version. Used on some services
the O-ring could very quickly become clogged preventing the seal head
from moving to accommodate wear of the faces.
Incorrect
setting length at installation. You may never figure this one out. Just
make sure that the fitting dimension is correct when installing the
seal. Otherwise sometime in the future the seal will let go, usually
after the pump is stopped, and the faces will look good but only partly
worn. What has happened is that the spring pressure has reduced to the
point where the seal leaks during idle periods. This can be difficult to
spot, unless you know what to look for ... and when.
Fretting.
Very small movements between components causes a polishing action. The
polishing action removes the surface molecules. On pump shafts made of
stainless materials the surface of the metal consists of chromium oxide.
Elastomers moving very slightly against this surface wipe away the
oxide which immediately reforms. The oxide is carried into the wiping
surface changing its character completely. A rubber ring coated with
chromium oxide becomes more efficient as a polishing, grinding surface
and removes material at a faster rate. A "fret" ring is characterized by
a polish mark on the shaft surface at the point where the seal
elastomer seals against the shaft. If worn badly enough the fret ring
can cause a new seal to fail on installation because the elastomer
cannot seal effectively due to the damage on the surface.
Distortion
of the stationary face. This is not common but the stationary could be
badly fitted leading to over tightening, especially the silicon carbide
grades which are designed with a lip to be clamped in the seal plate.
Failure under these circumstances may be confused with cracking due to
heat checking of the component. S.C grades of 99.9% only heat check if
they are tightened un-evenly, so check out your grade and suspect poor
fitting if its a high grade material failing by cracking. With other
materials such as tungsten carbide, or plated surfaces, such as
stellite, consider the distorting effect of poor clamping if no other
solution presents itself.
Face Mis-centering
or run-off. This is not common and is easy to diagnose. The faces are
not concentric and the rotating head comes off the stationary track and
picks up dirt. Scoring of the stationary and an off center running track
gives you all you need to know.
Incorrect
grade of O-ring material. Lots of things happen to elastomers so check
out the ones on your seal, are they swollen, hard, squashed, shiny,
cracking?
The seal hits something, it is prevented from moving to accommodate runout.
Lots of possibilities here, so I list a few.
The
shaft is bent and hitting the stationary face. You will notice this
pretty quick, but bear in mind that the running clearance of the seal
components and the shaft may be quite tight, so a small shaft
displacement may not be obvious, the seal will show you what is
happening.
Solids in the seal chamber hitting the seal.
Incorrectly fitted gasket extending into the seal chamber. Split casing pumps can suffer this problem.
The shaft is not concentric with the seal chamber.
Insufficient
clearance in the seal chamber. Check this out if you are changing seal
type or intend using different materials to cope with other problems.
A
seal box recirc line is directed at the seal faces. Most seal chambers
have a radial flow insert when most seal manufacturer's will tell you
that a tangential flow insert is safer and causes less disturbance to
the seal faces.
Heat Causes Seal Failures
Heat affects the elastomer. This the part most sensitive to extremes of temperature.
Heat can change the state of the fluid being pumped.
Raising the temperature of corrosive liquids increases their potency. A 16 deg F rise doubles the corrosion rate of most acids.
Differential
expansion rates can destroy plated seal surfaces. Low grade silicon
carbide will crack with sudden changes in temperature.
Differential expansion of shaft and pump casing can change the face loading by altering the fitting dimension.
We now have the over-view of heat related failures so let us look in more detail at what is happening.
Elastomers
A
wide range of elastomers are in use and many of them are rubber
compounds. Teflon materials have a predetermined heat range of up to 226
deg C beyond which Teflon breaks down and burns making small amounts of
phosgene gas. Teflon should not be used in temperatures close to its
ultimate limit because it is a heat insulator and local heat production
may cause it to reach its ultimate temperature.
Rubber
compounds are made by baking the material until it is cured to a
predetermined hardness or durometer. The various materials formed in
this way, nitrile, viton, buna-n, and others, are commonly found in
sealing applications. Less common is Kalrez a specialized compound with a
high resistance to chemical attack. Formed in a heat setting process,
these materials continue to be affected by the heat applied during the
life of the seal. At temperatures beyond the range of the rubber seal
the material continues to harden. As it hardens the shape of the seal
takes on the shape of the groove if an O-ring or splits appear in rubber
bellows as flexibility is lost. O-rings take on a "compression" set and
appear oval and feel hard to the touch. O-rings are manufactured with a
10% tolerance oversize to allow for some thermo-setting in service. At
higher temperatures the elastomer life to full compression set will
depend upon the temperature and time at this temperature. The point for
you is that exceeding the range of the rubber parts of your seal will
shorten the working life of the seal and you need to bear this in mind.
Heat
is generated from the friction running at the seal faces. Depending
upon the type of face material and the seal box environment a rise of
around 25 deg C above the seal fluid temperature can occur. Look at your
seal types, where is the elastomer in relation to the seal faces. The
nearer the elastomer is placed to the running faces the greater the
additional heat it will experience. The use of low friction seal face
combinations will reduce this effect. The carbon / ceramic combination
has the lowest friction rating with hard faces such as tungsten /
tungsten faces the highest.
Unbalanced
seals, because the face weight is varying with the system pressure, can
experience greater rises in face generated heat creating damage to the
elastomer.
Excessive
heat producing a temperature rise of 55 Deg C on a Viton O-ring will
reduce its useful life to less than 1000 hours running time. For a seal
that is expected to run for one year that is an 88% reduction in useful
life. An 82 deg C rise will reduce the life of the seal by 97%.
Loss of water to a cooling water jacket, loss of any cooling arrangements puts your seals at risk.
Changing state of the fluid
Liquid
gases and other volatile fluids can vaporize and freeze water out of
the air on the outside of the seal restricting movement. Shortly before I
took up my post in Saudi Arabia a liquid propane pump blew its seal
open due to a build up of ice around the seal faces. Liquid released
into the atmosphere created a vast cloud of highly flammable gas.
Fortunately no one was hurt and no explosion occurred but it was a close
thing. It was thought appropriate to fit a double seal with a barrier
fluid for future installations.
Liquids
changing state to a gas experience enormous volume increases. Water
increases in volume by 1700 times, so a small drop vaporizing across a
seal face will explosively blow apart the faces. Boiler feed pumps and
other hot water pumps can be heard "popping" or "puffing" if the seals
are not working correctly. As the water droplets expand and open the
seal faces more water rushes in to cool the area, collapsing the steam
bubble and causing the faces to snap shut. Another small droplet
penetrating the faces vaporizes and causes the faces to open again.
Water treatment crystals, entrained oxides, other dirt particles are
trapped between the faces as they close. Your seal is on its way to the
scrap yard.
Some
fluids crystallize with additional heat. Sea-water, brine, and similar
fluids leaking past your seal and drying out around the seal plate can
build up to affect the seal head and prevent it from moving. Crystals
can also score the running surfaces of the seal causing damage leading
to failure.
Hydrocarbons
form coke as they partially burn or vaporize. Coking causes a hard
solid to form around the seal effectively stopping it from moving
freely. A similar effect is seen in food plants handling product
containing sugar. Sugar escaping across a seal face can crystallize, or
simply burn and coke. The signs are un-mistakable on the seal face.
Heat can cause impurities to come out of solution and plate onto seal surfaces, building up hard films or lacquers.
Heat can destroy seal faces
I have mentioned some of these effects but I think a defined list will help you.
Plated
materials can experience differential expansion. Often materials such
as stellite are plated over stainless steel. The expansion rates are
poorly matched so operating outside of the design limits of the
materials will cause strains to appear in the plating interface, causing
cracks to appear. The cracks will cause the carbon face to wear
dramatically fast.
The
less expensive ceramic material (85%) will crack if cold shocked.
Sudden changes in temperature of 38 deg C or more will destroy the seal
face. The higher quality ceramic (99.9%) will cold shock if it is under
distorting stress, properly fitted and evenly clamped it will survive
sudden changes in temperature. Get to know which materials are being
fitted into your seal installations.
Carbon
rings using fillers and fitted into high temperature pumps can have the
filler material melt out of the carbon causing them to become porous
Poor carbons with voids can blister and pit as the trapped air or gases expand and blows pieces off the carbon surface.
Lapped
seal faces can distort, going out of flat. The effect of touching the
lapped surface with a finger is to coat the surface with dirt and skin
oils but also to distort the surface away from flat by the application
of heat from your hand. Distorted seal faces leak.
Heat increases the corrosiveness of most corrosive materials
The carbon part of the seal will show signs of being attacked.
O-ring grooves can be damaged limiting their ability to seal effectively.
O-rings can become hard or start to crack, or become swollen and excessively soft.
Metal surfaces can be attacked and appear pitted which will prejudice the seals ability to work properly.
Springs and other highly stressed parts can fail due to increased corrosion.
Expansion due to heating effects
All
metals expand when heated. A stainless steel shaft 48" long by 4" dia
will grow 0.138" in length when heated through 300 deg F. The working
limit of most carbon seal faces is 0.125" . Seal compression is set at
about 0.064" to produce the spring face weight. A seal mounted on a
shaft moving by 0.138" with other expansion effects happening to the
pump casing is in danger of opening. Apart from ensuring the accurate
placing of the seal on the pump shaft there is little to be done to
compensate for such movement. Tell-tale signs of inaccurate setting of
the seal will be where you need to be looking.
The
shaft diameter will expand too, by about 0.010". The seal material will
expand also but under extreme circumstances this expansion can cause
the seal to hang-up on the shaft. Over-compression of the elastomers
will limit their effectiveness, as well as the other effects mentioned
earlier.
Material Failure
Failure
of materials is usually a sign of a mis-match of material to
environment. The substantial construction of seals excludes major
failure of some main component, so we concentrate on the effects of
environmental attack on sensitive components.
Chemical attack on the elastomer will cause it to swell.
The
carbon will appear pitted. Acid attack on carbon is directed against
the impurities. The reaction of the impurities to the acid solution
cause holes and pits to form, weakening the structure and producing a
porous carbon. A higher grade of carbon is required.
The
springs can break. Stainless steel is known to fail due to chloride
stress corrosion. Many single coil spring driven seals fail because the
spring breaks. They are usually in-expensive and over-engineered, but
they still fail.
Metals corrode. In seals
where metal parts are designed to be thin due to flexibility
requirements, metal bellows seals, welding techniques used in
construction and material compatibility with mating components and
pumped fluids are factors that affect the life of a seal.
Set
screws clamping onto a hardened shaft material will not grip properly,
allowing the seal body to slip, leading to a range of other effects, but
ultimately to a seal failure.
Plated seal faces are not corrosion resistant, so the plating material can be removed from the surface.
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