Fluidized Bed System
Full fluidization is guaranteed with the unique revolutionary swirl generating method which gives great uniformity of coverage and high returns to the end product. The major difficulty is how optimal and uniform granule covering may be achieved. All grains engaged in the process of coating should have the same coating thickness, irrespective of their size.
In addition to handling aqueous as well as organic film
coating systems, an advanced control panel helps you to monitor and record all
the settings for the Fluid bed processor.
The chamber generally is a vertical cylinder in a fluidized
bed processor. A column of air that flows up from the lower center of the
cylinders fluidizes the pellets. The tablets in the center travel upward and
downwards through the chamber wall, from the base of the column into the air
stream again. In the base and top of the chamber, there are spray nozzles used
to insert the coating solution.
The core of the pellet is fragile, abrasive, and
tearing-prone, which makes it difficult even under optimal conditions to
completely coat the tablet. This is due to the tablet-to-tablet collision
as well as the contact between the tablet chamber and the tablet.
Two main configurations are utilized to implement
fine tablet coating solutions:
1. High-Pressure
Airless System
Airless spray fluid is pushed into
a small orifice between 0.02 and 0.2 mm in diameter at the high pressure of 1.7
to 20 MPa (250 to 3000 Psi) to produce a fine spray. The atomization degree
and the spray rate are all regulated by fluid pressure, viscosity, and size of
the aperture.
2. Low-Pressure
Atomized Air Systems
The liquid is pushed through a
wider opening between 0.05 and 2.5 mm in diameter with a relatively low
pressure of 35 – 350 kPa (5 to 50 psi). At the top of the atomizer, the
low-pressure air reaches the liquid stream and a finely distributed spray
pattern is created. The degree of atomization is determined by the size of
the aperture, fluid viscosity, fluid pressure, air cap design, and air
pressure.
Operation
1.
Bottom-Spray Coating (Wurster coating)
This processing option uses the energy
and controls the fluidized
bed processor to create a pneumatic mass transport inside a special insert,
which is consisted of a perforated bottom screen with defined free areas.
This uniform statistical residence
time of all particles in the coating zone results in a very uniform coating.
Due to the high kinetic energy provided by the pneumatic mass flow moist
particles are separated, as such allowing the individual coating of even very
small particles. Due to the nozzle being positioned directly inside the product
and concurrently spraying a premature viscosity change of the coating droplet
is avoided. All these features result in the highest possible coating quality,
which is imperatively required to produce defined and reproducible drug
delivery profiles.
2.
Top-Spray Coating
Spray coating can be used for all fluid bed systems, be it in batch or continuous operation or if the film is applied from a sprayed solution or suspension. For this processing option from the parameters has to be chosen to avoid agglomeration, i.e. liquid bridges between the air suspended particles.
If spraying a solution or suspension the liquid only serves as a vehicle to deliver the coating material to the surface of the substrate. The quality of the coating extensively depends on the statistical residence time of the particles in the coating zone. In classic fluid bed equipment only top-spray coating is possible. Bottom- spray arrangement can be made by the replacement of container. A perfect film is generally not required for this function, but care must be taken that the droplets should not be too viscous before touching the substrate, in order to maintain a good spreadability. As however neither the particle motion, nor the travel distance of droplet from the nozzle to substrate is uniform, the film structure is generally rather porous, but nevertheless measuring up to the above-described requirements.
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