Toshiro Sakai1, Markus Thommes. 1. Pharmaceutical Research and Technology Laboratories, Astellas Pharma Inc., Yaizu, Shizuoka, Japan.
Abstract
OBJECTIVES: The goal of this investigation was to qualify the DSM Xplore Pharma Micro Extruder as a formulation screening tool for early-stage hot-melt extrusion. METHODS: Dispersive and distributive mixing was investigated using soluplus, copovidone or basic butylated methacrylate copolymer with sodium chloride (NaCl) in a batch size of 5 g. Eleven types of solid dispersions were prepared using various drugs and carriers in batches of 5 g in accordance with the literature. KEY FINDINGS: The dispersive mixing was a function of screw speed and recirculation time and the particle size was remarkably reduced after 1 min of processing, regardless of the polymers. An inverse relationship between the particle size and specific mechanical energy (SME) was also found. The SME values were higher than those in large-scale extruders. After 1 min recirculation at 200 rpm, the uniformity of NaCl content met the criteria of the European Pharmacopoeia, indicating that distributive mixing was achieved in this time. For the solid dispersions preparations, the results from different scanning calorimetry, powder X-ray diffractometry and in-vitro dissolution tests confirmed that all solid-dispersion systems were successfully prepared. CONCLUSIONS: These findings demonstrated that the extruder is a useful tool to screen solid-dispersion formulations and their material properties on a small scale.
OBJECTIVES: The goal of this investigation was to qualify the DSM Xplore Pharma Micro Extruder as a formulation screening tool for early-stage hot-melt extrusion. METHODS: Dispersive and distributive mixing was investigated using soluplus, copovidone or basic butylated methacrylate copolymer with sodium chloride (NaCl) in a batch size of 5 g. Eleven types of solid dispersions were prepared using various drugs and carriers in batches of 5 g in accordance with the literature. KEY FINDINGS: The dispersive mixing was a function of screw speed and recirculation time and the particle size was remarkably reduced after 1 min of processing, regardless of the polymers. An inverse relationship between the particle size and specific mechanical energy (SME) was also found. The SME values were higher than those in large-scale extruders. After 1 min recirculation at 200 rpm, the uniformity of NaCl content met the criteria of the European Pharmacopoeia, indicating that distributive mixing was achieved in this time. For the solid dispersions preparations, the results from different scanning calorimetry, powder X-ray diffractometry and in-vitro dissolution tests confirmed that all solid-dispersion systems were successfully prepared. CONCLUSIONS: These findings demonstrated that the extruder is a useful tool to screen solid-dispersion formulations and their material properties on a small scale.
Authors: Lærke Arnfast; Jeroen van Renterghem; Johanna Aho; Johan Bøtker; Dhara Raijada; Stefania Baldursdóttir; Thomas De Beer; Jukka Rantanen Journal: Pharmaceutics Date: 2020-02-01 Impact factor: 6.321