PubMed · 5806410
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1969. [Pharmaceutical technology again?].. https://pubmed.ncbi.nlm.nih.gov/5806410/
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Roller compaction (RC) is an important dry granulation technique. Since pilot and commercial scale roller compactors, which operate continuously on a large scale, usually require kilograms of material per run, formulation and process development directly on such roller compactors is not practical. In contrast, a compaction simulator (CS) can produce ribblets, also known as "slugs", using only a few grams of material with sinusoidal displacement profile replicating the motion of a specific point on the roll surface. Thus, it is possible to develop RC formulation and process in laboratory using a CS-based material-sparing approach. However, because of the inherently different configurations for applying pressure between die compression and roll compression, translating uniaxial pressure from CS experiments to roll pressure during RC is often unreliable, leading to significant uncertainties in the critical quality attributes of ribbons, such as ribbon solid fraction (or porosity) and mechanical strength. The objective of this study was to identify a correction factor (Kp = uniaxial die compression pressure/roll pressure), by correlating the compressibility profiles from CS and a roller compactor of interest, to enable more reliable process translation from CS to roller compactor. In this study, a Kp value of 0.5 was determined for Alexanderwerk WP120 and validated for Gerteis Mini-Pactor and Bepex Pharmapactor. This value may serve as a starting point for translating the optimal compaction pressure identified based on CS investigation to common roller compactors, requiring only minor adjustments to attain optimal RC process parameters (i.e., roll force and roll gap) for a chosen roller compactor.
Unexpected poor flowability during commercial production of a direct compression tablet formulation initiated an investigation of the flow properties of the powder mixture and its components by means of a uniaxial tester. The failure function--a curve describing the strength of the powder bed as a junction of the maximum main stress that has consolidated the bed--of the powder mixture and its components was determined. The drug was more cohesive than the filler, which was somewhat more cohesive than the powder mixture. Three excipients--a hinder, a glidant and a lubricant constituting 3.5 w/w% of the formulation improved the flowability of the mixture of active ingredient and filler. The failure function discriminated powder mixtures with poor flow from mixtures with medium or good flow. However, it was not possible to discriminate medium from good flow by means of the failure function. Attempts to correlate univariately the flow property parameters of the powder mixtures with particle size data or flow property data of included active ingredient and filler batches failed. Therefore a multivariate approach was tested. Principal component analysis (PCA) and projection to latent structures by means of partial least squares (PLS) were employed. An excellent PCA model was obtained with the flow properties of the powder mixture. A good PCA model of tableting performance--based on tablet weight variation and tablet machine speed-was obtained.
The objective of this study was to investigate the properties of granules and tablets prepared by a novel Fluidized Hot-Melt Granulation (FHMG) technique. Macrogol 6000 (polyethylene glycol 6000, PEG 6000), macrogol 20000 (polyethylene glycol 20000, PEG 20000), and glyceryl monostearate (GMS) were used as binders with different levels of viscosity and water solubility. The properties of both granules and tablets were compared with those obtained using the Standard Tablet Formulation (STF, lactose/corn starch/hydroxypropylcellulose/ magnesium stearate: 66/30/3.5/0.5) for fluidized-bed granulation, which is widely used for wet granulation. To obtain suitable flowability as granules for tabletting, the content of the melting material should be approximately 10 w/w%. The rate of increase in the mean diameter of the granules during FHMG was affected by both the melting temperature and the viscosity of the melting material used in the granules. The compression properties of granules prepared by FHMG were also investigated, demonstrating that these granules had a high pressure transmittance. The hardness and the disintegration time of tablets obtained from granules prepared by FHMG were influenced by the properties of the melting material, such as its compaction behavior, solubility, and wettability. No significant differences of hardness were observed when compared to STF tablets. Tablets prepared from FHMG granules disintegrated within 15 min, whereas the STF tablets showed faster disintegration. It was also demonstrated that the hardness and disintegration time of tablets prepared from FHMG granules were not affected by the tablet porosity. Therefore, tablets with a constant quality may be obtainable under a wide range of compression forces. The results of this study suggested that FHMG is a useful method of preparing granules for tableting without using any solvents or water.