Kiln Cycling Produces that Dam Ring
Anyone
that’s grown up in the Snow Belt is familiar with scraping
ice off the windshield of their car and using the defroster
to defog the inside of the windshield. (Even if you don’t
live in the Snow Belt, you’re still probably familiar
with a fogged up car window.) Both of these phenomena are
actually very analogous to the alkali and sulfate cycles in
a rotary cement kiln.
The ice that forms on the windshield of a car is caused by
the freezing of moisture vapor against the glass surface.
The longer the car sits and the more moisture there is the
more ice that forms. (Of course that’s true only as
long as the outside temperature is below freezing.)
The fog on the inside of the windshield is a slightly different
story. The vehicle occupants exhale carbon dioxide and water
vapor. The water vapor rapidly condenses from body temperature
because of the cold interior onto the cool interior surface
of the windshield. The cars defroster removes the fog by blowing
hot dry air onto the surface. That increases the temperature
gradient and removes the moisture from the air. That’s
also why the quickest way to defrost the inside of a car is
to turn on the air conditioning. The air conditioning removes
the moisture from the air. (In most cars, turning the defroster
on also automatically turns on the air conditioning.)
Hmmm… rapid temperature changes, evaporation, freezing
and melting, air movement. What makes sense for your car also
makes sense for your kiln…
Sulfates
in the kiln system are brought in either through fuel or the
raw materials or both. Alkalis enter through raw meal. As
these materials heat up to about 800ºC they volatilize
(roughly similar to evaporates) in the kiln atmosphere in
the form of alkali chlorides and sulfates. These alkali sulfates
are then pushed to the back of the kiln by the counter current
gas stream and into the lower temperature areas of the kiln
system where they then condense… just like the situation
during freezing weather where the car’s windshield fogs
up on the inside when everyone first gets in and before the
defroster is turned on. After these materials condense towards
the front end of the system, they then travel back towards
the burning zone with the raw meal. Here they’re once
again heated up and re-volatilized into the kiln atmosphere.
If we don’t remove these alkali sulfates or alkali chlorides
they’ll continue to build up more and more material…
just like when a bunch of people are sitting in a car without
the engine running in freezing weather. They keep producing
moisture vapor. Local accumulations of condensate in the form
of melt wetting partially clinkered raw meal causes the meal
to get sticky. This material then accumulates along the kiln
walls. This is how clinker rings form.
Once a ring forms it will impede the progress of raw meal
passing down the kiln. That’s why you’ll also
hear the term “dam ring.” Freezing of the molten
sulfates becomes an even greater problem as the dam rings
grow in size. The growth in size also means growth in material
that is more difficult to heat. (Think of the windshield that
continues to gather ice because the supply of moisture and
freezing temperatures continues. The more ice you have…
the more difficult the removal problem.)
The same principles behind getting ice off your windshield
or defrosting your car’s interior apply to the kiln
as well. You can scrape ice off the windshield… you
can blast the dam rings out. Both alternatives take time,
risk damage, and only treat the symptom. You can also remove
the source of the buildup; either the moisture vapor or the
sulfates. Not very realistic since there’s water vapor
in the atmosphere and sulfates in most materials. You can
make sure that the material condenses where you want. That’s
the whole point of an alkali bypass.
As noted in PCA’s Innovations in Portland Cement
Manufacturing:
The bypass takeoff is usually located in front of the riser
duct because kiln gases coming from below have a tendency
to hit the back wall and create an area with low dust concentration
at the front of the riser pipe. The kiln gases sucked out
of the riser pipe are then quenched to about 350°C (660°F)
to provide the alkali condensation.
We could also control the temperature to make sure that the
material just doesn’t condense. In the car scenario,
we’d just continue to blast hot air from the defroster
onto the inside of the windshield. (In practical terms we’re
keeping the rate of evaporation greater than the rate of condensation.)
A precalciner system has an inherent advantage over other
kilns systems when it comes to dealing with the cycle of alkali
accumulation. In the precalciner we just divert the gas stream
with the alkalis before it can condense.
Going back to PCA’s Innovations in Portland Cement
Manufacturing:
When fuel is burned in two locations, the only process heat
requirements in the kiln are the completion of calcination
and the maintenance of the exothermic clinkering operation.
When the calcination level reaches 85% to 90%, the kiln fuel
rate is nearly independent of the disposition of the kiln
exit gas. If all or part of the kiln gas is wasted, the additional
fuel needed to compensate for the heat losses is provided
through the calciner burners, and the stability of the kiln
operation is not compromised at any bypass level (Warshawsky
and Porter, 1979).
For more information on alkali bypasses and kiln cycles take
a look at PCA’s Innovations
in Cement Manufacturing (CD400).
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