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Showing papers on "High Shear Granulation published in 2006"


Journal ArticleDOI
TL;DR: In this paper, discrete element method (DEM) is used in parallel with a model for coalescence of deformable surface wet granules for use in derivation of an overall coalescence kernel.

90 citations


Journal ArticleDOI
TL;DR: In this paper, the authors used a high speed camera and particle image velocimetry (PIV) software to measure particle velocities in a high shear mixer with a three-blade impeller.

46 citations


Journal ArticleDOI
TL;DR: In this article, a volume-based multi-dimensional population balance model based on the approach used by Verkoeijen et al. is further developed and applied to a wet granulation process of pharmaceutically relevant material, performed in a high shear mixer.

44 citations


Journal ArticleDOI
TL;DR: Differences in the diffuse reflectance spectra of pellet samples related to particle size offer a fast instrumental method for the in-process control in order to evaluate the effects of independent process variables during high-shear pelletisation.

37 citations


Journal ArticleDOI
TL;DR: Investigating the different mechanisms of material exchange during the equilibrium phase of the granulation process and whether these mechanisms are consistent with the mechanisms described in the growth regime map, to study how material properties and process conditions affect these exchange mechanisms, and to correlate Stokes deformation number to the exchange mechanisms.

30 citations


Journal ArticleDOI
TL;DR: The results of this study show that the properties of the granules and the tablets fall into two groups according to whether the molecular weight of the polymer is high or low, with smaller and more compact granules with better flow properties but with less tensile strength of the compacts.

28 citations


Journal ArticleDOI
TL;DR: In this paper, the effects of binder particle size on high shear and extrusion granulation using the wet granulation method by evaluating the properties of granules and tablets were investigated.

3 citations


01 Jan 2006
TL;DR: Scale-up of high shear granulation in the pharmaceutical industry has been approached in a number of ways, Typically, impeller tip speeds were kept constant as a scale-up parameter (kinematically similar criterion) and Froude number was also suggested a Scale-Up parameter even for geometrically dissimilar granulators.
Abstract: Mandated changes in the way pharmaceutical manufacturers are developing products are being ushered by the Food and Drug Administration (FDA) for new drug applications and generic ANDAs. Prior to the phasing in of pharmaceutical quality assessment systems for submission review (chemistry, manufacturing and controls (CMC)) targeting implementation in 1Q2007 [1], development of solid products by granulation was and is still by and large an empirical, ‘look, touch and feel’ exercise. Barriers to progress in this area lay in the reluctance by industry to embrace new methods that may not be readily accepted by the FDA (the perception being that old proven methods were more likely to be accepted by the regulators); but barriers also existed and still exist because of the limited fundamental understanding of the complex materials behaviours and the many mechanisms at work in granulators. Pharmaceutical development requires an understanding of scale up behaviours in manufacturing processes based on predictive characterization of the way granules form via wetting and nucleation, the way granules grow viz a viz consolidation and coalescence and the way they break by attrition. This understanding, however, is in its naissance as the different mechanisms in play need to be separated and studied individually. Scale-up of high shear granulation, therefore in the pharmaceutical industry, has been approached in a number of ways [1-7]. Typically, impeller tip speeds were kept constant as a scale-up parameter (kinematically similar criterion). Froude number was also suggested a scale-up parameter (as a for dynamic similarity criterion) even for geometrically dissimilar granulators [4].

1 citations


Dissertation
01 Jan 2006
TL;DR: In this article, the authors investigated the influence of granulation conditions and operating conditions on granule properties on the abrasion of Perspex and found that the granulation was undertaken in an unstable regime dictated by the need to produce small granules and that it was difficult to achieve reproducibility in making the granules.
Abstract: This work investigates the granulation of fine calcium carbonate powder to form microgranules (less than lOOf.lll1). The influence offormulation and operating conditions on granule properties was investigated. This work analyses experimental data using a database approach to relate granulation conditions to granule properties, to fmd propertyto-property relationships and to investigate the influence on the abrasion of Perspex. It was found that the granulation was undertaken in an unstable regime dictated by the need to produce small granules. As a result, it was not possible to achieve reproducibility in making the granules. For the range of granules produced it was difficult to determine variation in abrasiveness within the experimental errors, a detailed error analysis was carried out. A theoretical relationship between strength and porosity is developed and the factors influencing abrasive wear are investigated. Two theoretical models are presented: 1) Impact Failure model and 2) Granule Consolidation model. The impact failure model relates dynamic impact strength to static strength, which enables the prediction of a failure distribution curve (how many particles will fail per hundred impacts as a function of velocity). This is done using a "critical normal impact velocity" determined from the properties of the granule, properties of the impact surface and experimentally measured granule static strength. The granule consolidation model allows the qualitative prediction of the rate and extent of consolidation from granulation conditions. It models the compaction of a granule by descnbing the packing of its primary particles within an imaginary internal granule. Sphere packing is discussed with implications for determining the maximum packing of a primary particle size distribution.