Chapter 3 An Investigation into the Powder and ODT Properties of Commercially available Grades of
3.2 Materials and Methods
3.3.4 ODT Disintegration
Figure 3.10 shows a graph of the mean disintegration times of three ODT’s tested for each grade of
mannitol, compared to milled mannitol (F2). From the results it was observed that the spray dried
grades, Mannogem EZ and Pearlitol 200SD, produced ODTs with fast disintegration time. Upon
statistical analysis it was also seen that the spray dried grades were significantly better disintegrating
than both the crystalline powders and granulated forms of mannitol tested. This was because the
spray dried powders had a fairly small particle size of between 150-200 μm as well as pores on the
surface as seen in SEM images which may have helped increase the water uptake into the ODT, leading
to faster disintegration. At 75 MPa the crystalline powders also had relatively low disintegration times
of around 50 seconds, which wasn’t statistically different from the spray dried grades, however there
was a big increase in disintegration time at 225 MPa compared to the spray dried grades. At 75 MPa
the ODTs composed of the crystalline powder disintegrated quite quickly as it had a relatively small
particle size which allowed wetting of the tablet, and as the hardness was fairly low, water was able
to penetrate the tablet structure more rapidly, allowing a fast disintegration of the ODT. At 225 MPa
there would have been significant fragmentation occurring in the crystalline powder tablet, and as
hardness was high, the subsequent disintegration time of the tablet was also high. However the
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granulated forms had a significantly higher disintegration time than all the other commercial grades,
and at 225 MPa the disintegration time was only significantly higher when compared to the spray
dried forms, with the crystalline form having similar times at this compaction force. The high
disintegration time of the granulated powders may have been due to the large particle size of the
mannitol, the highest disintegration time observed was with the Pearlitol 500DC which had the largest
mean size of particle, which in turn led to a slower disintegration time as the large particles took longer
to break down within the disintegration medium (S Velmurugan and Vinushitha, 2010). This would
have been due to the agglomeration of the mannitol crystals into one large particle, which would have
resulted in large particles with the absence of pores, meaning it would have been more difficult for
water to penetrate the particle and allow subsequent disintegration. Both Mannogem grades also
displayed long disintegration times due to the very large particles present within the powder.
0 50 100 150 200 250 300 350 400 F2 Mannogem Powder Mannogem 2080 Mannogem Granular Mannogem EZ Pearlitol 50C Pearlitol 500DC Pearlitol 200SD Dis in tegratio n time (s ) Powder 75MPa 225MPa
Figure 3.10: A graph showing the disintegration times of the commercial mannitol grades compared to the
milled mannitol. The results clearly show that milled mannitol provides advantages for tablet disintegration with the milled mannitol being significantly better than all grades at both compaction forces (except for the Mannogem Powder and Pearlitol 50C at 75 MPa. Data is presented as mean ± SD (n=3, p<0.05).
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The clear advantage of milled mannitol compared to the commercial grades was its improved
disintegration time. Statistical analysis showed that disintegration times with the milled mannitol was
significantly lower than all the commercial grades at the 225 MPa compaction force, and all
commercial grades at 75 MPa, except the crystalline powders (Mannogem powder and Pearlitol 50C).
The poor disintegrating qualities of the granulated grades was due to the very large sized
agglomerated particles, which led to significantly longer disintegration. Although the spray dried
grades presented advantages in terms of disintegration compared to the granules, possibly due to the
spherical smaller sized particles which contained pores, the milled mannitol was still clearly
advantageous. This was due to the very small particle size of the milled powders (approximately 11
μm) and increased wettability of the mannitol crystal. This increased wettability of the powder
particles was due to a higher exposure of the (011) plane, established as the most hydrophilic plane
on the mannitol crystal, which led to an improved wetting of the ODT and therefore a faster
disintegration of the dosage form (Koner et al., 2015).
Table 3.2 shows the porosities of the ODT’s manufactured from the different grades of mannitol tested
in this study. Statistical analysis showed that at 75 MPa, the milled mannitol was more porous than
the commercial grades, which also gave further evidence for the faster disintegration of the ODTs. The
spray dried form was expected to be more porous than the granulated grades as there were visible
pores within the particles on the SEM monographs obtained, with significant pores visible on the
Mannogem EZ (Figure 3.1 (E)). It can be said that the porosity differences between the graded
mannitol was negligible, with all powders displaying a high porosity. The high porosity of the crystalline
powder was due to the fragmentation of the needle shaped particles which led to a more porous
structure, and it was seen that the Pearlitol 50C did have a slightly higher porosity than Mannogem
powder due to more profound needle shaped crystals present within the powder blend. The
granulated forms also formed highly porous ODT’s as the large particles were unable to fill in the voids
between the individual particles during packing resulting in more open pores within the tablet
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However the F2 milled powder tended to show a lower porosity at 225 MPa compared to all of the
grades of mannitol tested in this study. This was due to the fact that the milled powders contained
very small particles, which when poured into the die before compaction, and during rearrangement
within the dies, could fill any small spaces of air and allow a more solid compact to be formed with a
less porous structure. Compared to the 75 MPa ODTs, where the compaction force wasn’t high enough
to force the small voids to be filled, the 225 MPa tablets presented a less porous structure than the
commercial grades. However, for milled mannitol, disintegration of the ODTs at 225 MPa was
massively improved compared to the commercial grades, largely due to the increased hydrophilicity
and wettability of the dosage forms.
3.4 Conclusion
In conclusion it can be seen that the spray dried mannitol had the best mechanical properties for
utilisation as a binder within ODT tablets. This study indicated that it forms ODT’s that have very high
hardness and low friability, whilst also giving the lowest overall disintegration times of all the
commercial brands tested. This was due to the presence of the alpha polymorph within the powder,
which, as previously shown in literature, had the highest compressibility of all the mannitol
polymorphs. The granulated forms however didn’t display any significant improvements in tablet
properties. This was due to the lack of α-mannitol present within the powder. The granulated forms
did display a significant improvement in flow which is a key component for tabletting. If the excipient
flows well it will promote the uniform flow of the bulk powder blend into the dies before compression,
which is the key advantage of using granulated mannitol as opposed to the crystalline mannitol
powder.
The key advantage of the milled mannitol was its very low disintegration time due to the increased
wettability of the powder, providing ODTs that disintegrated rapidly, much faster than any of the
commercial grades. Although mechanical strength and the friability of the milled mannitol ODT’s was
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difference and upgrade compared to the commercial powders. The main disadvantage of the milled
powders was the flowability which was very, very poor. As mentioned above, good powder flow is key
in tableting to allow homogenous bulk powder movement into the dies, which produces a uniform
and reproducible tablet. The flowability of the milled mannitol, as seen in the previous chapter, was
capable of being enhanced to suitable levels, and therefore the milling of mannitol provided a suitable
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