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www.thecementgrindingoffice.com
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All rights reserved © 2012-2017 The Cement Grinding Office
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Separators in the cement
industry
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7
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Third generation
separators:
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7.1
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Introduction:
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-
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Also called: Cage
separators or High Efficiency Separators.
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These separators has been
developed in the beginning of the eighties (O'Sepa from Onoda Cement).
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As the second generation,
the air flow required for the separation is produced by an external fan.
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The separator material
feed is carried out mechanically by means of suitable continuous conveyors.
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Fines are conveyed by air
in external cyclones or directly to a bag filter.
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The main separating
device is a cylindrical rotor. The rotor is like a cage composed of blades
closely spaced.
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The rotor is operated by
a variable speed drive.
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The rotor speed
determines swirl in the classifying zone and therefore the cut of the
separator.
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The composition of forces
acting in the separating zone is showed in the figure below:
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Here a non-exhaustive
list of High Efficiency separators:
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O'Sepa (FLSmidth)
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Sepol (Polysius)
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Sepax (FLSmidth)
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SD (Sturtevant)
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Sepmaster (KHD)
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QDK (Pfeiffer)
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TSV (FCB)
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O&K (Orenstein &
Koppel AG)
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PRESEP VTP (PSP
Engineering a.s.)
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CTC SERIES (CEMTEC)
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Cemag (CMP AG)
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Copies from China
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7.2
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Advantages of 3rd
generation dynamic separators:
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Possibility of mechanical
adjustments
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Possibility of very large
flow rates
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Flexibility to produce
products of different qualities
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Better efficiency than
the conventional and cyclones separators
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Reduction of mill
specific consumption
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Increase of the grinding
capacity
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Reduction of the cement
temperature
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Better cement quality
(Straighter RRB curve giving better 28 days and early strengths)
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7.3
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Disadvantages of 3rd
generation dynamic separators:
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Difficulty to get the
optimum seal system
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No constant velocity of
flow and no constant centrifugal acceleration of particles can affect the
efficiency
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7.4
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General principle of
operation:
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The material is generally
fed at the top of the separator.
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There are 2 or more feed
chutes in order to improve the dispersion of the material on the distribution
plate.
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Material falls and is
dispersed in the circulating air by the distribution plate.
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The feed forms a thin
cylindrical curtain of material in the classifying zone.
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The air stream is
generated by an external fan.
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According to the type of
circuit, it is possible to have 100% of fresh air, a part of the air
recirculated or 100% of the air
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recirculated.
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Often, there are a
primary air inlet, a second air inlet and also a tertiary air inlet depending
of the design.
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The airflow leaves the
guide vanes almost tangentially to the outside of the cage.
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Material is arriving in
the separation zone between the guide vanes (or louvres) and the rotating
cage.
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The particles are driven
by three forces: The centrifugal force due to the dispersing plate
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* The centrifugal force
due to the dispersing plate
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* The drag force due to
the air flow
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* The gravity due to the
mass of the particule
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The drag force is trying
to pull the material into the rotating cage.
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The centrifugal force is
trying to push the material toward the guide vanes.
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It is the balance of
these forces which induces a regular cut size of the separator.
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This balance remaining
steady because the material in the classifying zone has always the same
radius of rotation,
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then the centrifugal
force is the same in all areas.
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On
the other hand, the air and material are normally distributed uniformly, the
air velocity (then, drag force) remains equal.
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The
coarse material doesn't enter in the rotating cage and goes out by gravity up
to the bottom device (cone or other).
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The fine material enters
in the cage and exits with the air flow by the upper or lower part of the
separator.
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See the figure below
(from the O'Sepa):
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Warning:
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* Suppliers propose
generally a version for raw and cement mill circuits where the gas and the
material are going
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out together of the mill
and enter from the bottom of the separator.
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* Some suppliers propose
also special versions for circuits with pre-grinding systems (Roller Press).
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* Principles of
operation described in this page only present the classical version for
grinding circuits with
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bucket elevator for the
material feed.
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www.thecementgrindingoffice.com
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7.5
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Principle of operation
for each design:
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O'Sepa (FLSmidth):
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The material enters
through the top of the separator.
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Material falls and is
dispersed by the distribution plate.
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The primary and secondary
air creates a vortex in the separating zone.
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The material falls
between the rotor and the louvres.
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Fines are aspirated.
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Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
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the lower part.
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The fine material exits
with the airflow through the upper part of the housing.
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As a certain number of
fines particles are entrained downwards with coarse particles, the tertiary
air flow
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helps to pick up any
fines in the rejects.
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The fineness of the
product is adjusted by the speed of the rotor.
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Website of the
separator:
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http://www.flsmidth.com
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See the figure above
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Sepol (Polysius):
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The material enters
through the top of the separator.
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Material falls and is
dispersed by the distribution plate.
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There is one tangential
air inlet.
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The material falls
between the rotor and the louvres.
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Fines are aspirated.
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Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
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the lower part.
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The fine material exits
with the airflow through the lower part of the housing.
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The fineness of the
product is adjusted by the speed of the rotor.
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Website of the
separator:
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www.polysius.com
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See the figure below:
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Sepax (FLSmidth):
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The sepax differs by a
body divided into two parts: dispersion and separation parts.
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The material enters
through the middle of the separator on one side.
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Air enters from the
bottom of the separator.
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Material is carried with
the air to the upper part of the separator.
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Material enters in the
classification area between the rotor and the guide vanes.
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Coarse particles are
accelerated by the rotor, held by the guide vanes and slide up to the rejects
cone.
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Fines are aspirated with
air flow through the rotating cage and exit through the upper part of the
separator.
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The fineness of the
product is adjusted by the speed of the rotor.
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Website of the
separator:
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http://www.flsmidth.com
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See the figure below:
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www.thecementgrindingoffice.com
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|
SD (Sturtevant):
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|
-
|
The material enters
through the top of the separator.
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-
|
Material falls and is
dispersed by the distribution plate.
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-
|
The tangential air inlet
is in the upper part of the separator.
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-
|
Various tangential air
inlets can be realized.
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-
|
The material falls
between the rotor and the louvres.
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-
|
Fines are aspirated.
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-
|
Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
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|
the lower part.
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-
|
Some models have
horizontal louvres.
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-
|
The fine material exits
with the airflow through the upper part of the housing.
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|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
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|
-
|
Website of the
separator:
|
sturtevantinc.com
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-
|
See the figure below:
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Sepmaster (KHD):
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-
|
The material enters from
the top of the separator.
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-
|
The air stream is
generated by an external fan.
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-
|
The material falls
between the rotor and the louvres.
|
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-
|
Fines are aspirated.
|
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|
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|
|
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|
-
|
Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
|
|
|
|
|
|
the lower part.
|
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|
-
|
The fine material exits
with the airflow through the upper part of the housing.
|
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|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
|
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-
|
Motor and reducer are on
the bottom of the device.
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|
-
|
Website of the
separator:
|
www.khd.com
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-
|
See the figure below:
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QDK (Pfeiffer):
|
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|
-
|
The material enters
through the top of the separator.
|
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|
-
|
Material falls and is
dispersed by the distribution plate.
|
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|
-
|
There is one tangential
air inlet.
|
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|
-
|
The material falls
between the rotor and the louvres.
|
|
|
|
|
|
|
|
|
-
|
Fines are aspirated.
|
|
|
|
|
|
|
|
|
|
|
|
-
|
Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
|
|
|
|
|
|
the lower part.
|
|
|
|
|
|
|
|
|
|
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|
-
|
The fine material exits
with the airflow through the upper part of the housing.
|
|
|
|
|
|
|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
|
|
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|
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|
-
|
Website of the
separator:
|
www.christianpfeiffer.net
|
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|
-
|
See the figure below:
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|
www.thecementgrindingoffice.com
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TSV (FCB):
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|
-
|
The material enters
through the top of the separator.
|
|
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|
|
|
|
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|
-
|
There is one tangential
air inlet.
|
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|
|
|
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|
-
|
The fine material exits
with the airflow through the top of the housing.
|
|
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|
|
|
|
|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
|
|
|
|
|
|
|
|
-
|
Website of the
separator:
|
www.fivesgroup.com
|
|
|
|
|
|
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|
-
|
See the figure below:
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O&K (Orenstein &
Koppel AG):
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|
-
|
The material enters
through the top of the separator.
|
|
|
|
|
|
|
|
|
-
|
Material falls and is
dispersed by the distribution plate.
|
|
|
|
|
|
|
|
|
-
|
There is one tangential
air inlet.
|
|
|
|
|
|
|
|
|
|
|
-
|
The material falls
between the rotor and the louvres.
|
|
|
|
|
|
|
|
|
-
|
Fines are aspirated.
|
|
|
|
|
|
|
|
|
|
|
|
-
|
Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
|
|
|
|
|
|
the lower part.
|
|
|
|
|
|
|
|
|
|
|
|
-
|
The fine material exits
with the airflow through the lower part of the housing.
|
|
|
|
|
|
|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
|
|
|
|
|
|
|
|
-
|
See the figure below:
|
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|
PRESEP VTP (PSP
Engineering a.s.):
|
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|
-
|
The material enters
through the top of the separator.
|
|
|
|
|
|
|
|
|
-
|
Material falls and is
dispersed by the distribution plate.
|
|
|
|
|
|
|
|
|
-
|
There is one or various
tangential air inlets.
|
|
|
|
|
|
|
|
|
|
-
|
The material falls
between the rotor and the louvres.
|
|
|
|
|
|
|
|
|
-
|
Fines are aspirated.
|
|
|
|
|
|
|
|
|
|
|
|
-
|
Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
|
|
|
|
|
|
the lower part.
|
|
|
|
|
|
|
|
|
|
|
|
-
|
The fine material exits
with the airflow through the lower part of the housing.
|
|
|
|
|
|
|
-
|
Website of the
separator:
|
www.pspeng.cz
|
|
|
|
|
|
|
|
|
-
|
See the figure below:
|
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|
www.thecementgrindingoffice.com
|
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|
CTC SERIES (CEMTEC):
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|
-
|
The material enters
through the top of the separator.
|
|
|
|
|
|
|
|
|
-
|
There is one tangential
air inlet.
|
|
|
|
|
|
|
|
|
|
|
-
|
The fine material exits
with the airflow through the top of the housing.
|
|
|
|
|
|
|
|
-
|
The fineness of the
product is adjusted by the speed of the rotor.
|
|
|
|
|
|
|
|
-
|
Website of the
separator:
|
http://www.cemtec.at
|
|
|
|
|
|
|
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|
-
|
See the figure below:
|
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|
Cemag (Cement and Mining
Processing (CMP) AG)
|
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|
-
|
The material enters
through the top of the separator.
|
|
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|
|
|
|
|
|
-
|
Material falls and is
dispersed by the distribution plate.
|
|
|
|
|
|
|
|
|
-
|
There are two tangential
air inlets.
|
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|
-
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The material falls
between the rotor and the guide vanes.
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Fines are aspirated
inside the rotor.
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Coarse particles are
accelerated by the rotor and held by the guide vanes, which slide out of the
separator through
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the lower part.
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The fine material exits
with the airflow through the lower part of the separator.
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Website of the
separator:
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ww.cmpag.com
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See the figure below:
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www.thecementgrindingoffice.com
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All rights reserved © 2012-2017 The Cement Grinding Office
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