Enhancing drug solubility through advanced polymer extruded shellac-based matrix drug delivery systems
Abstract
The main objective of this study is to enhance the solubility of the model drug
fenofibrate, by forming amorphous solid dispersions using a hot melt extrusion process.
Hot melt extrusion offers an efficient way of increasing the solubility of a poorly soluble
drug by forming amorphous solid dispersion. Shellac has potential as a pharmaceutical
matrix polymer that can be used in extrusion processes, with further advantages for use
in enteric drug delivery systems because of its unique pH-sensitive properties. The
rheological property of a material affects the extrusion process conditions by their flow
and deformation behaviour inside the barrel. However, there was a distinct lack of data
on the processability of various shellac materials in the literature. Hence the initial step
in this study was to explore various types of shellac and characterize their
physicochemical and thermal properties along with their processability in the hot melt
extrusion application. The analysis indicated that there was no chemical difference
between the various shellac types compared in this study. It was found that the extrudable
temperature ranges and rheological properties of different shellac types varied. SSB 55
Pharma FL had the lowest processing temperature and glass transition temperatures.
Moreover, due to the shear-thinning behaviours, shellac can be extruded at lower
temperatures.
Subsequently, a prototype delivery construct was produced using hot melt extrusion
which was based on fenofibrate as an amorphous solid dispersion, with shellac as the
polymeric component. From the analysis of the data, enhanced solubility was achieved
as evidenced by an increase in the dissolution rate of the drug in dissolution media. The
amorphous solid dispersion formulation improved the solubility by over 8-times relative
to untreated fenofibrate. The fenofibrate-shellac binary system provides a different
approach from the traditional strategies and can be considered a convenient choice for
optimising the oral delivery of fenofibrate. Moreover, a shellac base drug delivery system
has an innate advantage due to its pH-sensitive nature and can be potentially used as a
colon target delivery system. However, this section highlighted the disadvantages of a
universal screw configuration due to insufficient mixing of the kneading section. The drug
content in the drug formulation is varied, resulting in the error bar in the dissolution
experiment being too large. In the dissolution experiment, the dissolution profile was
similar when the maximum solubility of the drug in the aqueous solution was reached.
Numerical simulation was used to understand the impact of two classical geometrical parameters on the mixing: the influence of different screw speeds and the
stagger angles of a twin-screw extruder. The mixing performance was studied based on
mixing characteristic parameters such as the maximum shear rate, stretching rate, mixing
index, time-averaged efficiency, and residence time distribution. Based on these studies,
it was found that the best mixing performance was achieved at a screw speed of 60 rpm.
In the aspect of kneading block stagger angle parameters, the increase of stagger angle
can promote the mixing performance of the extruder. On the contrary, the residence time
increase with the increase of the stagger angle.
Based on the simulation result, a new screw design was created and used to produce
a new batch of drug formulations. The final section report, on amorphous solid
dispersions of fenofibrate prepared with different types of shellac polymers and
employing a hot melt extrusion process with optimized screw configuration. The
predominant characteristics of the compositions were amorphous nature, reduced particle
size, and improved uniformity, which resulted in an enhancement of drug dissolution and
solubility. The rapid in vitro dissolution and the high degree of supersaturation
demonstrated the success of these amorphous solid dispersion systems prepared by the
hot melt extrusion process. The standard error of drug content, error bar in the dissolution
and the SEM image confirmed the success of the newly designed screw configuration
having a better mixing performance than the universal screw design.
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