Selecting a sifter for scalping, removing fines, or
grading
Robert D. Ricklefs,
Great Western Manufacturing Co.
A sifter (also called a screener) is a unique
and often misunderstood machine compared with other equipment
in the powder and bulk solids handling industries: Only
one material goes into a sifter, but two or more materials
come out. This article takes the mystery out of the machine
by discussing sifter uses, where to install a sifter, sifter
types, and selection factors.
Any dry free-flowing material can be handled in a sifter,
including pharmaceutical and cosmetic powders; wood chips
and wood flour; minerals such as limestone, pumice, and
silica; food products such as wheat flour, sugar, and
baking soda; plastics and rubber; and pigments such as
carbon black. The sifter mechanically separates the material
according to individual particle size by moving the material
in relation to a screen.
You can use a sifter in a quality assurance program to
scalp material, remove fines, or grade material. You can
also use a sifter to grade material in a manufacturing
process.
- For scalping, the sifter's most common quality
assurance application, the sifter removes oversize or
foreign materials. These can be agglomerates and lumps
in materials such as flour mixes, as well as foreign
materials such as insects, bin wall scale and flakes,
moldy material, or tramp metal.
- For removing fines, the sifter removes undersize
and dedusts the material to meet final product specs.
This is useful for friable materials that give off fines
or other materials that release fines in response to
excessive or rough handling. Typical applications include
removing fines from dried herbs, spices, sugar, and
granular pharmaceuticals.
- For grading, the sifter controls both oversize
and undersize in your material. A common example for
quality assurance is grading sugar to simultaneously
remove the lumps and fines. In manufacturing, in addition
to removing coarse oversize and fines, grading can produce
multiple intermediate particle sizes in materials such
as wood particles or polystyrene beads.
In each of these uses, sifting provides another benefit:
Passing through the screen aerates the material, which
gives it a more uniform bulk density for subsequent processing
and handling steps.
Where to install a sifter
For quality assurance applications, especially for sanitary
applications such as food manufacturing, the traditional
sifter location is immediately prior to your material's
final point of use. This will provide quality control
of the material as close as possible to its use in your
final product and your customer's use of the product.
Any problems that come to light after you analyze the
sifter tailings can help you pinpoint a problem with the
material supplier, the transport company, or your own
plant. If you produce a material mixture that has a tendency
to agglomerate, you can also sift it after dry blending.
The next most common sifter location for quality assurance
is immediately after raw materials are received. When
materials are received in bulk, the sifter can be inserted
into a pneumatic unloading system to sift the materials
before they reach bulk storage. Sifting at this point
allows you to monitor the supplier's and transport company's
quality control and sanitation practices while allowing
you to remove contaminants before they can enter your
bulk storage vessels. When raw materials are received
in small bags, the bags are emptied directly into the
sifter before the materials are moved to storage or processing.
The sifter not only breaks up and removes lumps but separates
any torn bag pieces, strings, or other contaminants from
the raw materials.
For a manufacturing application such as grading, a common
sifter location is just prior to packaging and shipping.
This allows you to package different grades of material
for shipment to specific customers.
During sifting, each material behaves in a unique
way.
Less commonly, a portable truck-mounted sifter1
can also be stationed outside a plant or shipping container
for either quality assurance or manufacturing applications.
For instance, the truck-mounted sifter can supply emergency
sifting for scalping oversize or contaminants from a shipment
of material to your plant. The material can be conveyed
from your receiving silo to the truck-mounted sifter,
which removes the oversize before the material enters
your process. The truck-mounted sifter can also be used
to transload material from a train to trucks. For
instance, a flour mill in the Midwest can ship flour in
a unit train to a central location nearer its bakery customers.
Here, the truck-mounted sifter can remove contaminants
while transferring the flour to bulk trucks. Each bulk
truck can then deliver a contaminant-free load to an individual
local bakery.
Sifter types
When classified by their application, sifters are either
gravity-flow or in-line units.
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Figure 1
Gravity-flow and
in-line sifters
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In a gravity-flow sifter, shown in Figure 1a,
material flows at atmospheric pressure through the sifter
by gravity. The material can be fed to and carried away
from the sifter by a pneumatic conveying system (shown
in the figure) or mechanical conveyors. With a pneumatic
conveying system, two blowers are typically required,
one for conveying material to the sifter and one for conveying
material away from it. However, the machine is designed
to sift material without the influence of positive or
negative airflow on the sifting motion.
Using the gravity-flow sifter can require auxiliary equipment
such as a cyclone or filter receiver, airlocks, a blower
package, and associated dust control equipment. However,
the gravity-flow sifter itself costs less and is less
likely to leak than an in-line sifter. If the flexible
connections linking the sifter's inlet and outlet to the
conveying equipment fail, less spillage will result because
of the sifter's operation at atmospheric pressure. The
gravity-flow sifter also allows you to separate your material
into multiple fractions and more easily use metal detectors.
In an in-line sifter, shown in Figure 1b, which
is installed directly in a pressure or vacuum pneumatic
conveying system, the material flows with the conveying
air at the conveying line pressure into and then away
from the sifter. But because the pressure is equalized
above and below each screen in the sifter, no force other
than gravity causes the material to pass through the screen.
Only one blower (that for the conveying system) is required,
thus simplifying the operation and reducing the system's
cost by eliminating the need for auxiliary equipment.
This limited amount of equipment also reduces the system's
installation costs, including those for electrical controls,
and reduces maintenance and power costs over the system's
life.
Whether used for a gravity-flow or in-line application,
the sifter typically provides one of several types of
screening motion. Each type of motion results from the
differential movement between the screen and particles
at a given amplitude and speed. Usually the particles
are moved in relation to the screen, but in one case (the
centrifugal sifter, described in the next subsection),
the particles move while the screen remains static. For
best sifting results, the material must be metered uniformly
to the sifter and be well distributed over the full screen
surface with minimal agitation. The particles naturally
stratify, with fine particles migrating to the material
bed's bottom and thus having maximum exposure to the screen
surface.
The most common types of screening motion are centrifugal,
vibratory, gyratory-reciprocal, and gyratory. Each motion
typically is suitable for sifting any dry free-flowing
material, but has advantages and disadvantages you need
to consider before selecting a sifter for your application.
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Figure 2
Centrifugal sifter
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Centrifugal. A typical centrifugal sifter
is shown in Figure 2a. In operation, an integral screw
feeder meters material into the sifter's stationary screening
chamber, which is formed by a cylindrical screen. Rotating
beaters or paddles in the chamber impact the material
and accelerate its movement through the screen, shown
in Figure 2b. This high velocity presents the particles
to the screen surface many times, providing many chances
for the particles to pass through the screen.
Moving material so quickly requires high energy. Containing
this energy causes the screen to deflect and flex, which
helps prevent screen blinding without requiring screen
cleaners (which are discussed in the next section). Although
all screens eventually fail, the centrifugal sifting motion's
flexing severity reduces the screen life more than other
sifting motions.
The centrifugal sifter is compact and typically easy
to disassemble and maintain. It doesn't have flexible
connections at the inlet and outlet, eliminating this
common source of leaks. According to most centrifugal
sifter manufacturers, the sifter can break up soft agglomerates
in sticky materials or materials that contain fat, which
can be an advantage in some applications.
However, the centrifugal sifter has relatively high power
requirements, applies high stresses to the screen, and
isn't typically suited for precise separations of near-sized
particles. Current Baking Industry Sanitation Standards
Committee guidelines suggest using sifters that "employ
no rubbing or physical pressure to facilitate" flow through
the screen; the centrifugal sifter's rotating beaters
do apply rubbing or pressure, which can be a concern for
food products because the beaters can fracture particles
and force them through the screen.
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Figure 3
Vibratory sifter
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Vibratory. A vibratory sifter, shown in
Figure 3a, has horizontal screens. Each screen is typically
mounted in a round frame; each screen and frame together
form a screen deck. (Each screen deck also includes
a large-opening wire mesh, called a backwire, that's
mounted below the screen to hold a set of screen cleaners,
such as rubber or plastic balls or cubes. The cleaners
bounce against the screen's bottom surface during sifter
operation to prevent screen blinding.) Material is fed
into the sifter as a drive mechanism applies both short,
back-and-forth linear motion and vertical motion to each
screen, shown in Figure 3b.
The vibratory sifter's benefits include its simple drive
mechanism, which makes the sifter inexpensive, and its
simple design. However, the vertical motion tends to disturb
the particles' natural stratification on the screen surface,
so that material tends to be airborne much of the time
rather than in contact with the screen; this, coupled
with the sifter's short linear stroke, reduces the sifter's
efficiency. Because the sifting motion is relatively small,
relatively little energy is imparted to the sifter's screen
cleaners, which can lead to screen blinding. The machine
also won't break up lumps or agglomerates, but this may
not matter for some applications.
The sifter has an additional disadvantage for grading
applications: its inefficient use of screen area. This
is because most vibratory sifters have only one screen
per size grade, providing the same screen surface area
for each grade, regardless of the quantity of material
in each grade. So, for instance, if the sifter separates
a material into four grades (greater than 10 mesh, between
10 and 20 mesh, between 20 and 40 mesh, and less than
40 mesh), the sifter's capacity would, for most applications,
be limited by the 40-mesh screen area. As a result, excess
screen area would be provided for the 10- and 20-mesh
screens.
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Figure 4
Gyratory-reciprocal sifter
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Gyratory-reciprocal. A gyratory-reciprocal
sifter, shown in Figure 4a, has a rectangular, relatively
steeply inclined screen and a drive mechanism that imparts
a gyratory motion at the sifter inlet end and a reciprocating,
linear motion at the outlet. Together, these movements
produce a gentle elliptical motion, shown in Figure 4b,
that both conveys the material and promotes particle flow
through the screen.
The sifter's benefits include its simple design and gentle
sifting motion. The sifter also requires little headroom
because, for each mesh size required, only one screen
deck is used to provide the application's required screen
area. The screen's incline and linear motion at the discharge
also help it convey bulky material or high volumes of
material from the inlet to the outlet.
However, the sifter's conveying action can limit the
particles' maximum exposure to the screen openings, reducing
the sifting efficiency. The screen's large area results
in other disadvantages, including increasing the sifter's
required floor space and making the screen unwieldy and
awkward to handle for service or replacement. Like a vibratory
sifter, the gyratory-reciprocal machine isn't usually
configured to accurately allocate the screen area required
for the application.
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Figure 5
Gyratory sifter
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Gyratory. A gyratory sifter, shown in Figure
5a, consists of a stack of multiple square, rectangular
(Figure 5a), or round (Figure 5b) screen decks. Multiple
screens in the stack can have the same mesh size to provide
the required screen area for the application. A drive
mechanism imparts a circular motion in a horizontal plane
to the screens, shown in Figure 5b. The horizontal screens
and lack of vertical motion produce the sifter's gentle
sifting motion and maintain the material's natural stratification
-- with fine particles adjacent to the screen and coarse
particles at the material bed's top.
In an application producing only two fractions, multiple
screens arranged in a series provide the required screen
area. The oversize pass from one screen to the next, and
each screen removes a portion of the particles that pass
through it while the oversize continue to pass from one
screen to the next.
In an application producing more than two separations,
the gyratory sifter provides a major benefit: Because
it uses smaller stacked screen frames, the screens can
be accurately allocated to each separation's requirements.
For instance, to handle the grading application previously
discussed for the 10-, 20-, and 40-mesh screens, the gyratory
sifter's screen area would be allocated appropriately.
Typically, the 10-mesh separation would require a smaller
screen area and thus fewer screens than the 20-mesh, and
the 20-mesh would require less than the 40-mesh. The result
is that no excess screen material, cleaners, or maintenance
would be required for underused screens and screen frames.
You should also be aware that a common misconception
when the gyratory sifter uses multiple screens with the
same mesh size is that the material is sifted repeatedly
on each screen. This isn't the case. Instead, as the material
enters the sifter, the gentle motion immediately stratifies
the material. Fines are in contact with the screen and
begin to pass through. The fines that didn't pass through
the first screen along with the oversize flow onto the
next screen. Separated materials of the same size discharge
together from the sifter in individual channels. As long
as the sifter is correctly designed for the material and
flowrate, only oversize will remain and travel over the
last screen to exit the sifter.
Other benefits of the gyratory sifter include both its
gentle motion and its lack of vertical motion or incline,
which makes the sifting efficient and provides accurate
material separation. The screens are typically smaller
and easier to handle than those on a vibratory or gyratory-reciprocal
sifter with equal screen area. The screen cleaners also
work more efficiently than in a vibratory sifter because
the gyratory motion imparts more energy to the cleaners.
However, the gyratory sifter has a more complex flow
pattern and more complex drive mechanism than other sifters,
which can make the unit harder to operate and maintain.
The gyratory sifter's gentle motion won't break up lumps
or agglomerates. The sifter's stacked-screen design also
requires more headroom than other sifters.
Selection factors
To choose a sifter for your application, you need to
consider several factors. Begin by analyzing your material
characteristics. Then consider factors about the sifter,
including the sifting motion, screen, screen tension,
screen attachment method, and screen cleaners.
Material characteristics. During sifting,
each material behaves in a unique way. For instance, a
granular, free-flowing material is easier to sift than
a fine, sticky material. The key material characteristics
that affect sifting performance by promoting or slowing
the material's flow through the sifter are:
- Particle size distribution (including the distribution
for each ingredient in a material mixture).
- Particle shape (spherical, flat, irregular, interlocking,
or other).
- Oil and moisture content.
- Temperature (which can be high after processing or
pneumatic conveying).
- Bulk density.
- Electrostatic charge (which can increase after grinding
or pneumatic conveying).
Work closely with your sifter manufacturer to determine
how these factors will affect your sifter choice.
Sifting motion. The amount of energy imparted
to your material during sifting greatly affects the process.
Choosing the right sifting motion (centrifugal, vibratory,
gyratory-reciprocal, or gyratory), the right sifter speed,
and the right stroke or amplitude of motion will provide
the right amount of energy for distributing your material
over the full screen surface with minimal agitation. Applying
too little energy can cause a sticky material such as
starch to sit in a mass on the screen. But applying too
much energy can cause a free-flowing material such as
whole grains or pellets to bounce around rather than fall
through the screen.
Work with the sifter manufacturer to test your material
on various sifters at various speeds. This will help determine
which sifting motion and speed are best for meeting your
requirements.
Screen.Consider screen type, mesh size,
and open area to select the screen for your sifter.
Screen type: Screen can be synthetic (either nylon
or polyester) or wire (stainless steel, magnetic stainless
steel, carbon steel, or plated or coated carbon steel).
Nylon screen often lasts longer than polyester, but can
absorb moisture and lose screen tension. Either type of
synthetic screen resists fatigue better than wire. In
sifting, especially in a centrifugal sifter, the screen
is constantly flexing. Resistance to fatigue is an important
consideration for obtaining long screen life.
Wire can be thinner than synthetic filament, thus producing
screen with a greater open area and higher sifting capacity
than synthetic screen. Eventually any screen will fail,
and fragments that break off the wire screen and fall
into the material can be detected by a metal detector,
which is important in many applications. However, the
wire diameter in some screen can be so small that a detector
must be carefully selected and calibrated to detect the
tramp metal, particularly since its largest dimension
won't always be oriented toward the detector.
Maintaining proper tension on the screen will keep
your material well-stratified.
One option for solving this problem is to use magnetic
stainless steel (400 series) wire screen because fragments
of this wire can be removed from the sifted material by
magnets. However, the wire is more brittle than carbon
steel or 300-series stainless steel wire and thus is more
likely to fail due to fatigue. The magnets also must be
regularly inspected and cleaned to ensure that they effectively
remove the tramp metal.
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Figure 6
Mesh size
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Mesh size: Choosing mesh size is critical in selecting
a screen for your sifter because the right mesh size allows
an efficient sifting rate while ensuring that oversize
particles and contaminants are effectively removed from
the on-size particles. Mesh size, as shown in Figure 6,
is the number of openings in the screen, in each direction,
from center to center of parallel filaments or wires per
linear inch. For instance, a 30-mesh screen has 30 openings
per linear inch. If both mesh measurements M shown
in Figure 6a are 1 inch, then the mesh size for the top
section is 1 mesh and for the bottom section is 2 mesh.
Open area: In addition to specifying the mesh
size, also specify the opening size, or open area (measurement
O in Figure 6a). In Figure 6b, all the mesh sections
have the same mesh size but different mesh opening sizes,
with resulting differences in the percentage of open area.
The greater the open area, the greater the sifting capacity.
Table I
Differences in open area for screens with
comparable mesh opening sizes
| Screen |
Filament
or
wire diameter
(inches) |
Mesh
opening size
(inches) |
Open
area
(percent) |
| US Standard
- (30 mesh) |
0.0154 |
0.0234 |
36.8 |
| 30 SSMW |
0.0095 |
0.0238 |
51.0 |
| 34 SSBC |
0.0065 |
0.0229 |
60.7 |
| 3-590/42 |
0.0126 |
0.0232 |
42.0 |
| 3-600/51 |
0.0094 |
0.0236 |
51.1 |
The data in Table I shows how open area can vary among
different screen types with matching or very similar mesh
sizes. In the table, the filament or wire diameter, mesh
opening size, and open area for US Standard 30-mesh screen
are compared with those of some commercially available
screens.
The 30-mesh US Standard mesh screen is listed only for
comparison. This screen is used for particle sizing tests
and isn't suitable for production applications because,
besides not being widely commercially available for sifter
screens, its filament diameter is so large and the resulting
open area is so small that its sifting capacity is extremely
limited. The open area in the next four screens (the first
two are wire and the last two are nylon) matches the US
Standard 30-mesh screen's open area as closely as possible.
For instance, the 3-590/42 screen (3 indicates
nylon, 590 indicates the opening size in microns,
and 42 indicates percent open area) is equivalent
to 28 mesh, and the 3-600/51 screen is equivalent to 30.2
mesh.
In the table, you can see that the open area varies widely
for these similar screens. Monitoring this value is a
good way to ensure that the screen you choose can provide
the capacity you need, because the greater the open area,
the greater the opportunity for particles to pass through
the screen. But consider more than open area, because
in some screens, obtaining a greater open area comes at
the cost of reducing the filament or wire diameter. This
reduces the screen's durability. If screen life is important
to your application -- for instance, if you sift an abrasive
material -- you may choose to select a smaller open area
and, thus, lower capacity in return for larger-diameter
filaments or wires that will extend the screen life.
Screen tension. Maintaining proper tension
on the screen will keep your material well-stratified,
ensuring that the fines are in contact with the screen
but preventing the material from pooling on the screen.
A well-tensioned screen also flexes less, extending its
life. The screen will be easier to keep clean, because
the screen cleaners can bounce harder against the taut
screen. Consult your sifter manufacturer for help determining
the right screen tension for your sifter.
Screen attachment method. One factor in
achieving the right screen tension is to select an effective
method for attaching the screen to the screen deck frame.
The attachment method also affects the sifter's performance
and the screen's sanitation level and maintenance ease.
There are two main screen attachment types: mechanical
and bonded.
Mechanical attachment: Mechanical attachment requires
no special tools, equipment, or adhesives, allowing the
screen to be removed and replaced on the frames by workers
in your plant. The screen can have grommets that are attached
to hooks on the frame. Another option is a screen with
looped edges into which stainless steel rods are inserted;
the edges with the rods are then clamped and tensioned
around the screen frame by set screws. Mechanical attachment
methods require very accurately fabricated screen edges
to maintain good screen tension. Even when properly fabricated,
the screen's resulting tension can be lower than that
achieved with a bonded attachment method. Material can
also collect between the screen edges and the frame, posing
a contamination risk.
Applying too little energy can cause a sticky material
such as starch to sit in a mass on the screen.
Bonded attachment: Bonded attachment requires
stretching the screen over the frame with mechanical or
pneumatic equipment, which develops better tension than
mechanical attachment, and then bonding the screen edges
to the frame by gluing them in place. The improved tension
improves sifter and screen cleaner performance and increases
the screen life. The glued edges also eliminate spots
for potential material buildup. Stretching equipment and
adhesives for replacing bonded screens in your plant are
available for some sifters. If you prefer not to invest
in the equipment and adhesives, you can send the screen
frames back to the manufacturer for rescreening or, when
removing the adhesive isn't possible or practical, discard
the frames and buy new ones.
Screen cleaners. Screen cleaners for vibratory,
gyratory-reciprocal, and gyratory sifters are available
in many materials (typically rubber or plastic) and types,
including balls, cubes, belts, and other molded shapes
with studs or brushes.
Ball cleaners are effective for dislodging near-size
particles, but they can pack or tamp sticky materials
against the screen's underside. Cube cleaners scrape or
scour the screen's underside and are particularly effective
for cleaning oily or sticky materials, but can be hard
on the screen. Belt cleaners or molded cleaners with brushes
are effective because they wipe the screen's underside.
However, they tend to disintegrate faster, and the resulting
loose threads or bristles can contaminate your material.
Work with your sifter manufacturer to determine which
cleaner type and quantity is best for your material and
capacity requirements. If your sifter's capacity or performance
eventually drops because of screen blinding, try switching
to a different type or quantity of cleaner or use a combination
of different cleaners. PBE
Reference
- More information on portable truck-mounted sifters
is available from the author.
Robert D. Ricklefs
is sales manager at Great Western Manufacturing
Co., PO Box 149, Leavenworth, KS 66048; 913-682-2291,
fax 913-682-1431. He has more than 20 years experience
in cereal and grain processing.
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