Flow Aids Keep Material Flowing Out of Storage Vessels
Guest article by Richard Wahl, Vice Chairman of Vibrascrew, Inc.
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If you've ever had a fully loaded bin that suddenly
stopped discharging, leaving several tons of materials packed in an immovable mass inside,
you know material flow problems can be costly. Lost production isn't the only cost:
Breaking up the ratholes or bridges problems can take much labor and
cleanup, sending workers inside your large storage vessel to unclog the stoppage can be
dangerous and using a sledgehammer or the other device on your vessel's exterior can leave
the vessel stressed and permanently deformed.
Is there any good news? Getting even flow-resistant materials to
flow from a storage vessel doesn't have to be difficult or costly. And in cases where you
don't have enough headroom for a mass-flow storage vessel (whose steep hopper angles
promote flow but require a lot of height, as shown in Figure 1), you can use various flow
aid devices to get materials flowing smoothly.

With free-flowing materials that occasionally hang up, you may need
to apply a localized flow aid to the vessel's wall. Examples of these are a vibrator,
which transfers vibration through the vessel wall to the material or an air injector,
which injects pulses of air into material near the vessel wall.
Since vibrators are attached directly to the vessel wall, they must
be carefully applied to avoid damaging the structure. This limits the force that can be
imparted to the material and they are therefore generally used only for smaller bins with
flow problems.
Air injection can be used in one area of the bin or over a variety
of locations. Localized use targets a particular hang-up while multiple injection points
seek to fluidize a large portion of the stored material to achieve flow. When operated as
a feeder for downstream equipment, air induced fluidization must be carefully used to
avoid upsetting flow through the feeder and loss of accuracy and rate control.
More flow resistant materials often require a bin activator (Figure
2) which replaces a storage vessel's cone section and outlet. The bin activator consists
of a cone or dish-shaped housing with angles from 40 to 60 degrees, less steep than
required by a mass-flow bin. An adapter ring at the unit's top mounts the activator to the
bin bottom. A hanger assembly on the adapter ring suspends the activator from the bin and
isolates the bin structure from vibration. A flexible sleeve is used to seal the gap
between the bin and the bin activator. An internal baffle (called a pressure cone) is
located at the bin activator's center above the outlet, and a vibratory drive is located
on the bin activator's exterior.

In operation the baffle relieves the material head pressure on the
outlet while the vibratory drive vibrates the entire bin activator, the baffle, and the
material in the bin, but not the bin itself. The drive's vibratory thrusts, throw the
material horizontally toward the outlet. At the same time, the baffle resolves the
horizontal thrusts into strong vertical motion that extend far up into the bin, preventing
bridging.
In general, the more flow-resistant the material, the bigger the bin
activator must be in relation to the storage vessel's diameter. As shown in Table 1, for a
Class I granular, free-flowing material, the bin activator should be one-fourth to
one-third the bin diameter, and for a Class IV fibrous or flaky material, the unit should
be the same diameter as the bin. In cases where materials of different classes will
be stored in the same vessel, the bin activator should be sized to handle the most
flow-resistant material. Also, the faster the desired discharge rate, the larger the bin
activator's outlet should be. In general, the bin activator should have the largest
possible outlet the downstream equipment will allow.
Table 1: Material Classifications and Bin Activator
Diameter
| Material
Classification |
Material
Description |
Approximate Bin
Activator Diameter |
| I |
Free flowing granules. Normally
flows unassisted but temperature and humidity can cause occasional bridging.
Examples: granular salt, sugar, plastic pellets. Slide angle is 30 degrees. |
1/4 to 1/3 of the storage vessels diameter |
| II |
Sluggish 100 to 300 mesh powder.
Normally won't flow by gravity alone. Examples: flour, starch. Slide angle diameter
is 35 to 55 degrees. |
1/3 to 1/2 the storage vessels diameter |
| III |
Readily adhesive or easily
fluidizable -325 mesh powder. Examples: adhesive-titanium dioxide, pigments
fluidizable-hydrated lime, cement, talcum powder, confectioner's sugar. Slide angle is 35
to 55 degrees. |
1/2 to 2/3 of the storage vessels diameter |
| IV |
Fibers or flakes with particle
sizes from 1/8-inch strands to 1-inch or longer, chips, relatively low bulk density of 3
to 20 lb./cu ft. Tends to interlock and absorb vibration. Examples: wood chips, slivers,
shavings, asbestos fibers, flakes, grain. Typically has no slide angle. |
Same as the storage vessels diameter |
Notes:
1) Materials Classification is accepted bulk materials handling classifications.
2) Bin activator diameter at the point where the activator is mounted on the storage
vessel's base. |
The choice of which flow aid to use
comes down to the difficulty of the flow problem, cost of the solution and logistics of
the installation. It makes perfect sense to try a relatively inexpensive bin wall vibrator
or air injector first. Bin activators have been successfully employed with the more
difficult flow problems, particularly on existing bins. Mass flow bins can be useful in
the initial design stages of a new process where their unique space requirements can be
accommodated.
Help others by posting your comments, suggestions and
experiences with bulk solids feeding or any other materials handling concerns you may have
on our On-Line Help Forum. For
past Ask Joe ! Articles, visit the Ask Joe! Archived Articles.
Guest articles for the Ask Joe! Column are always welcome,
for more information please contact Joe Marinelli directly at his email address:
joe@solidshandlingtech.com.
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