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Biomedical subjects

Thomas Vilhelmsen

Publications and source records attributed to Thomas Vilhelmsen.

3 recordsLinked to original sources

Effect of a melt agglomeration process on agglomerates containing solid dispersions.

The purpose was to produce solid dispersions of a poorly water-soluble drug, Lu-X, by melt agglomeration in a laboratory scale rotary processor. The effect of binder type and method of manufacturing on the dissolution profile of Lu-X was investigated. Lactose monohydrate and Lu-X were melt agglomerated with Rylo MG12, Gelucire 50/13, PEG 3000, or poloxamer 188. Either a mixture of binder, drug, and excipient was heated to a temperature above the melting point of the binder (melt-in procedure) or a dispersion of drug in molten binder was sprayed on the heated excipient (spray-on procedure). The agglomerates were characterized by DSC, XRPD, SEM, and EDX-SEM. The study showed that the agglomerates containing solid dispersions had improved dissolution rates compared to physical mixtures and pure drug. The melt-in procedure gave a higher dissolution rate than the spray-on procedure with PEG 3000, poloxamer 188, and Gelucire 50/13, whereas the opposite was found with Rylo MG12. This was explained by differences in mechanisms of agglomerate formation and growth, which were dominated by immersion with PEG 3000, poloxamer 188, and Gelucire 50/13, and by distribution and coalescence with Rylo MG12. The spray-on procedure resulted in a higher content of Lu-X in the core of the agglomerates when immersion was the dominating mechanism, and in a higher content in the agglomerate surface when distribution was dominating. The melt-in procedure resulted generally in a homogeneous distribution of Lu-X in the agglomerates. The compounds in the agglomerates were found primarily to be crystalline, and the dissolution profiles were unchanged after 12 weeks storage at 25 degrees C at 50% RH.

Calorimetry, Differential Scanning↗

Agglomerate formation and growth mechanisms during melt agglomeration in a rotary processor.

The purpose of this study was to investigate the effect of the binder particle size and the binder addition method on the mechanisms of agglomerate formation and growth during melt agglomeration in a laboratory scale rotary processor. Lactose monohydrate was agglomerated with molten polyethylene glycol (PEG) 3000 by adding the PEG either as solid particles from the size fraction 0-250, 250-500, or 500-750 microm or as droplets with a median size of 25, 48, or 69 microm. It was found that the PEG particle size, the PEG droplet size, and the massing time significantly influenced the agglomerate size and size distribution. Agglomerate formation and growth were found to occur primarily by distribution and coalescence for the PEG size fraction 0-250 microm and mainly by the immersion mechanism for the PEG size fractions 250-500 and 500-750 microm. When the PEG was sprayed upon the lactose, the mechanism of agglomerate formation was supposed to be a mixture of immersion and distribution, and the agglomerate growth was found to occur by coalescence regardless of the PEG mean droplet size. Compared to high shear mixers and conventional fluid bed granulators, the mechanisms of agglomerate formation and growth in the rotary processor resembled mostly those seen in the fluid bed granulator.

Drug Compounding↗

Melt pelletization with polyethylene glycol in a rotary processor.

The purpose of this study was to investigate the effect of the airflow, the binder concentration, the massing time, the friction plate rotation speed, and the surface structure of the friction plate on melt pelletization in a laboratory scale rotary processor. Lactose monohydrate was melt agglomerated with polyethylene glycol (PEG) 3000 as meltable binder. The study was performed as a full factorial design. An increase in agglomerate size was found when the binder concentration, the massing time, or the friction plate rotation speed was increased. The agglomerate size was also increased when increasing the shearing forces by using a friction plate with a different surface structure. The size distribution of the agglomerates was significantly narrowed when the binder concentration or the shearing forces caused by the friction plate were increased. An increase in the adhesion of material to the friction plate was found when the shearing forces of the friction plate were increased either by the rotation speed or by the surface structure. Generally, the rotary processor was found to be a suitable alternative to melt pelletization in a high shear mixer.

Adhesiveness↗