|
|
|
| the
Biturbine : concept and use? |
|
|
|
How does it work? |
|
Imagine
for one moment that you have thousands of small turbines or
mini-cylinders which can individually coat 20, 50, 100... grams of
fragile or sticky products without the damaging effect of weight.
Let
us assume that these turbines are working in such a pattern as to
create a continuous flow.
This
is achieved by associating two parallel helicoïdal screws made of
soft fibers. The two screws counter-rotate in a special
8-shaped trough. |
 |
The
base product is fed in. Liquid or powder ingredients are metered from
top of the oepen trough, at some positions . Due to the rotation
of the screws, the product and the ingredients undergo a transfer and
mixing effect which result in a homogeneous coating.
This is the
Mini-Turbine-Effect A
complete continuous process can be designed by associating ancillary
equipment : feeding hopper, liquid tank and spraying manifold, powder
doser... |
|

|

|
| How to use
it? |
Product
|
The minimal particle
size can be as small as 0.5 mm. The maximal particle size is
limited by the space left between the screw shafts and the trough wall.
A thumb rule is that the product size should be no more than a third
of the distance left. By example, the TB 300 (the trough diameter is
300 mm) can accomodate tortilla chips without causing damage to
them.
The presence of fines
should be elminated from the base product. It is the main source of
agglomeration on the screw shafts and trough, and ultimately
jamming of the Biturbine.
The temperature of the product
should match the temperature of the ingredient applied and vice versa.
It is better if the temperature gap is minimal to prevent early
setting and crystallization thus hindering an optimal ingredient
dispersion and homogeeous coating. A dried RTE cereal should be coated
rigth after drying to benefit from the drying temperature.
|
| Liquid
ingredients |
The characteristics
of a liquid indredient should be known (melting temperature,
concentration, viscosity). The factors are connected. The lower the
viscosity, the better the coating. Hence the necessity to work at a
temperature above the setting point. The jacketed walls of the
Biturbine provide an ideal environment for the application of high
temperatrure setting point liquids such as hydrogenated fats or waxes.
A suspension containing
particles can be applied ; it is only a matter of transferring and
dispersing it properly : cheese slurry, peanut paste...
Application systems range from
the simple infeed tube to airless or air-powered spraying nozzles. For
fat or high concentratred sugar syrup, a jacketed transfer pipe and
manifold is a must.
|
| Powder
ingredients |
Powder
ingredients dispersion is easy thanks to the
mini-turbine-effect. If applied rigth after the liquid addition, the
powder is intimately mixed to the liquid : this is an
alternative to the use of a prepared suspension/slurry.
The powder can be used as a dusting.
In this case, the base product need only to be ligthly humidified (wated,
hydrocolloïd or fat) to stick the powder onto it. There are two
solutions. Either the product runs on a "bed" of powder in
excess (the excess is recovered through a perforated section att the
end of the same Biturbine section). Or the powder is applied with a
powder dispenser which distributes it over a given length.
It is recommended to keep the
liquid and powder addition separate in tho individual sections
(one Biturbine after the other). This avoids agglomeration at
the liquid/powder phase fronts, generally just under the powder feeder
chute.
|
| The Biturbine |
The Biturbine is made of modular
sections : generally one infeed section of 1500 mm where product
and liquid ingredients are metered from the top and mixed inside, one
or two extra sections of 1000 mm for further mixing or for powder
addition.
The Biturbine works generally in a horizontal
position.
It is sometimes tilted
backwards to improve the mixing effect with square toffee) or
smooth surface products (jelly, gum, hard-boiled candies) as they tend
to glide instead of rollling onto themselves.
The self-cleaning effect of
the brushes and the open top make it easy to inspect and clean. Either
by flushing it with hot water (60°C°) or removing the screw
brushes (in less than 30 seconds) for thorough cleaning. It is
sufficient to sanitize the machine and prevent microbiological growth.
The brush bristles are made of polyamide
(Nylon 66). Max. temperature 110°C. They are sealed inside a bore in
the shaft to prevent accidental tear and loss. |
| Process |
The throughput is given in
liters/hour as is depends of the density of the base product.
The TB 100 delivers 1000 l/hr at 60 rpm : 100 kg/h of cereal with 0.1
density. The throughput depends the infeed device (vibrating feeder,
elevator, drier outlet...). The screw speed is only used to
control the residence time i.e. the volume inside the Biturbine. A
mean residence time value is 30 seconds. It is short compared to
a drum or coating pan : it is a quick process aimed at thin film
coating and not dragee-paning or chocolate enrobing.
Jacketed walls are
indispensable when fat or syrup are to be applied : just to prevent
them to set on the trougth instead of the product surface. The
heat source is water or thermal oil circulation or electrical
resistances. It maintains the temperature at its correct value. But
the Biturbine is not an heat exchanger. Nor is it a drier as it
is closed, to the exception of the infeed and outlet ports.
Note that many coating applications
require a finishing step : polishing (resin), setting (fat),
drying (syrup).
|
| Production |
The small volume
present in the Biturbine has many advantages : quick adjustement
to parameters modification, quick start-up or shut-down.
It can be stopped or restarted at
will under the supervision of a product presence sensor.
It is a continuous process
which works best when inserted in a continuously working line (between
extruder and drier in RTE cereal coating line). Or it can serve
several batch process equipment working alternatively (pre-gumming of
dragee centers prior to panning).
|
|
Trouble shooting for developpers.!
|
| Agglomeration |
Adjust the
temperature of the jacketed walls above the setting point Lower
the concentration of the liquid solution
Eliminate fines from the infeed
product. Separate the liquid
and powder addition in two individual Biturbines. Then feed
first the powder in the infeed port then the liquid coated product.
|
| Uneven coating |
Adjust (increase
or lower) the screw speed to fill the troughs up to the shafts level.
Tilt sligthly by 5° the Biturbine
body.
Increase the ingredient rate or lower
the product infeed rate.
Increase the number of liquid
(manifold with more nozzles) or powder addition (use a longitudinal
screw dispenser).
Add the ingredient the sooner/closer
after the base product infeed point. Or increase the length of the
mixing zone after the ingredient addition.
Lower the concentration of the liquid
solution
|
|
A few critics at least!
|
| Difficult to
clean? |
Not as it is
self-cleaning with the brushes. Use hot (60°C) water. The brushes can
be extracted for cleaning separately in less than 30 seconds. A spare
set allows for immediate start up. |
| Microbiologically
safe? |
Made of stainless
steel and nylon essentially, it is constantly swept by the processed
product. By design, there is no dead spot. Hot water proves to
sanitize it satisfactorily. It is used in the diry industry to coat
cheese with antisticking oil or talcum. |
| Bristle losses? |
Yes, it happened
twice in the very early days of development. This critical problem has
been solved by literally clipping the bristles inside the holes
drilled in the shaft. |
| Damage to the
product? |
In the contrary,
no. The bristles tend to ply off when in contact with the product
avoiding hard contact. The action of the counter-rotating
helicoidal brushes is similar to hands shuffling inside the product
mass. If not potatoe chips, tortilla chips are flavoured in a
Biturbine. |
|
|
|
Back to page top |
|
|
|
|