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INNOVATIVE GLATT FLUID BED PELLETISING
TECHNOLOGIES
by Dr. Norbert Pöllinger, Glatt
Pharmaceutical Services, Technology Center Binzen
In multi-particulate systems the dosage
of the drug substance is – in contrast to classic single-unit
dosage forms like tablets – divided on a plurality
of sub-units, consisting of thousands of spherical pellet
particles with a diameter of typically 100 – 2000 µm.
Although their manufacture and design
is more complex in comparison to classic single-unit dosage
forms, multi-particulate dosage forms offer a magnitude of
different interesting options and advantages to accomplish
unique product characteristics and in particular specific drug
release patterns. In contrast to nondisintegrating monolithic
single-unit forms which retain their structure in the digestive
tract, the multiparticular preparations consist of numerous
sub-units which disperse after administration. Each single
sub-unit acts as an individual modified release entity. As
a consequence of this property, the multiple-unit approach
offers certain advantages for a modified release dosage form
over monolithic preparations like tablets:
- reduced variability
of the gastric emptying
- reduced dependency on the nutrition state
- minimised risk of high local drug concentrations within
the GI tract
- reduced risk of sudden dose dumping
- lower intra- and inter-individual variability
- controlled onset time of drug release
- delivery of the active ingredient to distal sites within
the GI tract
With multiparticular pharmaceutical drugs
an optimised pharmacokinetic behaviour can go together with
good patient compliance.
Many creative options in order to
end up with intelligent, sophisticated and reliably acting
pharmaceutical dosage forms are technically available. The
question is: do we have feasible technologies in order to
establish reproducible product and process quality?
The described
multiparticulate pellet units can be formulated to different
drug application forms (fig. 1): the most conventional form
is the capsule. Pellets may further be compressed to tablets – after
disintegration of the tablet in the stomach the pellets
are set free acting as multiparticulates.
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| Fig. 1: Final drug application
forms with pellets |
Pellets having
a particle size < 500 µm can be applied
as oral suspensions without providing a sandy mouthfeel.
To achieve such small pellet sizes particular technologies
providing micropellets are required – the extrusion
technique is not applicable therefore (fig.
2).
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| Fig. 2: Product Characteristics
with different pelletization technologies |
With classic
fluid bed drug layering and coating technologies like the
Wurster and the Rotor technology such pellet particle sizes
are basically achievable taking into account that the Wurster
process is limited to drug layering approaches; an optimised
Rotor technology could lead to an even better performance
than the existing one.
In addition to said existing and established
pelletising technologies GLATT has developed new pelletising
technologies (fig. 3) allowing new formulation options and
product qualities. In particular, unique benefits and opportunities
such as a small pellet size range of 100 – 500 µm,
uniformity of particle size distribution, smooth particle
surface, high density and high drug loading are achievable.
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| Fig. 3: Innovative GLATT
pelletization technologies |
1.
CPS™ Technology (Controlled Release Pelletising Technology)
CPS™ Technology
is a direct pelletisation process resulting in matrix type
pellets. Release characteristics of API from CPS™ pellets
depend both on the pellet formulation and on the pelletising
process.
The CPS™ technology
is an advanced fluid bed rotor technology allowing the preparation
of matrix pellets with particular properties in a batch process;
extremely low dosed and high potent drug can be formulated to
CPS™ matrix
pellets as well as high dosed APIs (fig.
2); the drug concentration
can vary from < 1% up to 90%.
Due to its modifications compared
to the established GLATT Rotor system the CPS™ Technology
works with a conical shaped rotating disc and additional devices
ensuring a directed particle movement (fig.
4).
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| Fig. 4: Rotor Technology
and CPS™ Technology |
Inert starting
beads are not required for the CPS™ Technology; typically,
microcrystalline cellulose powder is used as a basic excipient;
moreover, other functional excipients like polymers, disintegrants,
solubilizers and the like can be part of the CPS™ formulations
in combination with the API.
The starting powder (blend) is wetted with the pelletising
liquid until a defined stage of moisture will have been achieved;
at this time, spherical pellets begin to form (fig.
5). The
pelletising liquid can be water and / or organic solvents
which may also contain functional compounds. As an option,
dry powder may be fed into the process.
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| Fig. 5: CPS™ Pelletising
process in progress |
With the help of
torque measurement at the CPS™ rotor the endpoint of
the pelletisation can be defined. By means of a characteristic
rolling particle movement and thereby the application of
different forces, in particular of centrifugal forces on
the arising pellet cores, a defined densification of the
particles can be reached. Finally the pellets are dried in
the CPS™ or in a classical
fluid bed dryer configuration.
Fig. 6 shows the characteristics
of CPS™ pellets containing 75% of an API
in comparison with the same pellet formulation manufactured
by extrusion (fig. 7): the CPS™ pellets provide a higher
density due to the particular spheronisation process; their
surface is smoother than the one of the extruded pellets
and therefore provides ideal prerequisites for coating applications.
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| Fig. 6: CPS™ Matrix
Pellets |
Outstanding product characteristics of
CPS™ pellets:
- spherical and smooth pellet surfaces = ideal for coating
applications
- high density / low porosity of pellets
- broad potency range for APIs
- low attrition and friability
- dust free surfaces
- mean particle size range: 100 – 1500 µm
- narrow particle size distribution (fig. 8)
- controlled drug release from the CPS matrix (fig. 9)
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| Fig. 7: Pellets from
an Extrusion / Spheronisation process |
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| Fig. 8: Particle size
distribution of extended release CPS™ pellets |
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| Fig. 9: Effect of particle
size distribution on the in vitro dissolution of extended
release CPS™ pellets (phosphate buffer
pH 6.8, 37°C) |
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