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Scraped Surface Crystallizers

Our
scraped surface continuous crystallizer consists of multiple double pipe
elements, generally with 6, 8, 10, or 12 inch nominal diameter inner
pipes and larger diameter outer pipes. The annular space between the
inner pipe and outer pipe is filled with cooling fluid. Each inner pipe
contains a rotating scraper blade element which mixes the process fluid
flowing through the inner pipe, and removes deposits which form on the
inner pipe wall as cooling occurs.
In
effect our scraped surface continuous crystallizer is a heat exchanger,
but quite an unusual one, because it generally performs as a cooling
crystallizer. Heat transfer occurs across the inner pipe wall, with cold
fluid outside, and process fluid inside. As cooling occurs, crystals
tend to form on the inner pipe wall. The scraper blades rotate on the
inner pipe wall and remove these deposits which would inhibit heat
transfer. The majority of the crystallization takes place in the bulk of
the fluid, as opposed to the wall, thus allowing growth of easily
separable crystals.
A
typical commercial sized installation will consist of several double
pipe elements, each with a length of 20 to 40 feet, connected in series.
This provides a long thin flow path which promotes a close approach to
plug flow, which is very important in many crystallizations.
Advantages of Scraped Surface Continuous Crystallizers over
other methods of Crystallization
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Smaller
equipment, which generally means less expensive installations, less
floor space needed, less operator labor, and no duplication of
instrumentation, pipe, etc.
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Better
process control, less upsets of hazardous or expensive materials and
less peak utility demand.
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Modular
design allows for easy expansion with growth in demand.
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Simple,
self contained construction with minimum instrumentation and auxiliaries
such as condensers, vacuum systems, etc.
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May be
run for extended periods between hot washings whereas many shell and
tube exchangers would plug up in minutes.
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May be
run at much higher process fluid-coolant temperature differences than
could shell and tube equipment without serious fouling or plugging.
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May be
used over an extremely wide temperature range (-75 C to +100 C).
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May be
used with high percentages of solids (as high as 65% solids as slurry).
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High
viscosities are not a problem (has been used with mother liquor
viscosities of 10,000 cp or higher).
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Flow
pattern in once-through operation closely approaches plug flow so
conversion from batch operation is easy and virtually any desired
time/temperature pattern is possible.
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In small
capacity cases, a scraped surface crystallizer will be very inexpensive.
This is also true in cases where, for much larger installations, vacuum
crystallization may seem most attractive.
Dewaxing of
Lubricating Oils
Dewaxing lubricating oil
represents the largest use of our scraped surface continuous
crystallizers. Wax has the same boiling point range as lubricating
oil fractions, but has a much higher freezing point. Therefore,
cooling crystallization is a very effective way to separate the two
materials.
Many of the lube oil processing
plants are quite large and require many scraped surface continuous
crystallizers, often with a number of units in a series. Larger plants
usually require several parallel trains of crystallizers.
Armstrong/Chemtec is frequently involved in the process design to optimize heat
transfer, residence time and pressure drops, as well as determining the optimal use of
refrigeration. A primary goal in designing scraped surface crystallizers for
dewaxing is to maximize the time on stream between turnarounds.
Crystallization of
Organic Compounds
Many organic mixtures may be separated by cooling crystallization.
In simple terms, cooling crystallization means that a mixture of organic chemicals is
partially crystallized by reduction in temperature, without removal of any of the
components by evaporation.
Crystallization is a one-way process; the heat is removed,
crystals are formed, and the mixture of solids and liquids are then separated. Many
crystallizations take place at near ambient temperature so there is little heat up or cool
down required to get the right conditions for the separation to start.
In the great majority of crystallizations, the crystals which form are 100% pure
material, as opposed to something only slightly richer than the feed material as in
distillation. With crystallization, it is not necessary to repeatedly melt and
refreeze to obtain high purity. Minor impurities can be present in cooling
crystallization but these can be removed easily.
Viscous Liquid
Cooling
Highly viscous fluids do not present problems to the scraped surface heat
exchanger but may make other heat exchangers totally inoperable. Nearly all liquids
show an increase in viscosity as they cool. With a highly viscous fluid, this effect
may present significant resistance to heat transfer at the cold wall and thereby greatly
increase the required surface area. Scraped surface exchangers greatly reduce the
resistance at the cold wall by constantly disrupting (reducing) the wall boundary layer
and exposing the wall to warmer, lower viscosity fluid.
Pilot Testing Program

Armstrong/Chemtec offers a pilot testing program
to help you determine whether crystallization is the best method of separation for your
specific application. This enables you to evaluate the process before scale up.
A number of pilot units are available on a rental basis. The sizes of these
units range from a 4" diameter by 4' long jacketed section to 12" by 10'.
These units are as small as can be used to gather reliable information on the
process. The rental units are normally either carbon steel throughout or SS316 on
the process side.
Over the many years, Armstrong/Chemtec engineers
have assisted with dozens of piloting programs of organic compounds using our scraped
surface crystallizers. As a result, we know how a given compound will react and can often
save a great deal of time and effort by avoiding tests that will not scale up. Since
many various tests are usually required to complete piloting, it is recommended to conduct
the testing at the client's plant, where separation equipment, feed stock including
variations, etc., are available.
A significant amount of information can be learned from piloting:
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Heat transfer characteristics
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Some idea of crystal size
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Crystal habit and size distribution
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Best cooling cycle and residence time
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Methods of separation to be used
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Crystal purity
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Best solvent or magma ratios
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Color pickup

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