Impact of screw configuration on the particle size distribution of granules produced by twin screw granulation.

Twin screw granulation (TSG) has been reported by different research groups as an attractive technology for continuous wet granulation. However, in contrast to fluidized bed granulation, granules produced via this technique typically have a wide and multimodal particle size distribution (PSD), resulting in suboptimal flow properties. The aim of the current study was to evaluate the impact of granulator screw configuration on the PSD of granules produced by TSG. Experiments were performed using a 25 mm co-rotating twin screw granulator, being part of the ConsiGma™-25 system (a fully continuous from-powder-to-tablet manufacturing line from GEA Pharma Systems). Besides the screw elements conventionally used for TSG (conveying and kneading elements), alternative designs of screw elements (tooth-mixing-elements (TME), screw mixing elements (SME) and cutters) were investigated using an α-lactose monohydrate formulation granulated with distilled water. Granulation with only conveying elements resulted in wide and multimodal PSD. Using kneading elements, the width of the PSD could be partially narrowed and the liquid distribution was more homogeneous. However, still a significant fraction of oversized agglomerates was obtained. Implementing additional kneading elements or cutters in the final section of the screw configuration was not beneficial. Furthermore, granulation with only TME or SME had limited impact on the width of the PSD. Promising results were obtained by combining kneading elements with SME, as for these configurations the PSD was narrower and shifted to the size fractions suitable for tableting.

[1]  C Vervaet,et al.  Twin screw granulation as a simple and efficient tool for continuous wet granulation. , 2004, International journal of pharmaceutics.

[2]  Michael J. Hounslow,et al.  Twin screw wet granulation: Granule properties , 2010 .

[3]  B. J. Ennis,et al.  Nucleation, growth and breakage phenomena in agitated wet granulation processes: a review , 2001 .

[4]  James J. Cartwright,et al.  Twin screw granulation: steps in granule growth. , 2012, International journal of pharmaceutics.

[5]  Andy Ingram,et al.  Comparison of granule properties produced using Twin Screw Extruder and High Shear Mixer: A step towards understanding the mechanism of twin screw wet granulation , 2013 .

[6]  Peter Kleinebudde,et al.  Continuous granulation with a twin-screw extruder: Impact of material throughput , 2010, Pharmaceutical development and technology.

[7]  C Vervaet,et al.  Comparison of two twin-screw extruders for continuous granulation. , 2009, European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V.

[8]  Thomas Rades,et al.  Distribution of binder in granules produced by means of twin screw granulation. , 2014, International journal of pharmaceutics.

[9]  T De Beer,et al.  Stability and repeatability of a continuous twin screw granulation and drying system. , 2013, European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V.

[10]  P. Anderson,et al.  Simulation of distributive mixing inside mixing elements of co-rotating twin-screw extruders , 2013 .

[11]  P. Kleinebudde,et al.  Influence of the Granulation Step on Pellets Prepared by Extrusion/Spheronization , 1999 .

[12]  Peter Kleinebudde,et al.  Impact of screw elements on continuous granulation with a twin-screw extruder. , 2008, Journal of pharmaceutical sciences.

[13]  J. Sun,et al.  Wet granulation in a twin-screw extruder: implications of screw design. , 2010, Journal of pharmaceutical sciences.

[14]  Jean Paul Remon,et al.  Visualization and understanding of the granulation liquid mixing and distribution during continuous twin screw granulation using NIR chemical imaging. , 2014, European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V.

[15]  T De Beer,et al.  Continuous twin screw granulation: influence of process variables on granule and tablet quality. , 2012, European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V.

[16]  James D. Litster,et al.  Granulation rate processes in the kneading elements of a twin screw granulator , 2013 .

[17]  H. Sämann Screw Elements for Co-rotating, Closely Intermeshing, Twin-Screw Extruders , 2008 .

[18]  Jonathan Seville,et al.  Regime map development for continuous twin screw granulation , 2013 .

[19]  Michael J. Hounslow,et al.  Twin screw wet granulation: Effect of powder feed rate , 2011 .

[20]  Michael J. Hounslow,et al.  Twin screw granulation using conveying screws: Effects of viscosity of granulation liquids and flow of powders , 2013 .

[21]  C Vervaet,et al.  Validation of a continuous granulation process using a twin-screw extruder. , 2008, International journal of pharmaceutics.

[22]  Michael J. Hounslow,et al.  Twin screw wet granulation: Effects of properties of granulation liquid , 2012 .

[23]  Jean Paul Remon,et al.  Continuous granulation in the pharmaceutical industry , 2005 .

[24]  Niklas Sandler,et al.  Influence of raw material properties upon critical quality attributes of continuously produced granules and tablets. , 2014, European journal of pharmaceutics and biopharmaceutics : official journal of Arbeitsgemeinschaft fur Pharmazeutische Verfahrenstechnik e.V.

[25]  J. Carson Overcoming Particle Segregation in the Pharmaceutical and Cosmetics Industries , 1988 .

[26]  James D. Litster,et al.  Twin screw wet granulation: Influence of formulation parameters on granule properties and growth behavior , 2013 .

[27]  Kazumori Funatsu,et al.  Flow patterns and mixing mechanisms in the screw mixing element of a co‐rotating twin‐screw extruder , 2002 .

[28]  Umang Shah,et al.  Use of a modified twin-screw extruder to develop a high-strength tablet dosage form , 2005 .