4.7 Article

Kinetic and Microhydrodynamic Modeling of Fenofibrate Nanosuspension Production in a Wet Stirred Media Mill

Journal

PHARMACEUTICS
Volume 13, Issue 7, Pages -

Publisher

MDPI
DOI: 10.3390/pharmaceutics13071055

Keywords

poorly water-soluble drugs; wet stirred media milling; breakage kinetics; process modeling; microhydrodynamic model; statistical model; subset selection

Funding

  1. NJIT Department of Chemical and Materials Engineering

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This study analyzed the effects of stirrer speed and bead material loading on fenofibrate particle breakage during wet stirred media milling using various kinetic and microhydrodynamic models. The nth-order model was the most suitable for describing the temporal evolution, showing almost second-order kinetics. Higher stirrer speed and/or loading with zirconia beads led to faster breakage. Additionally, a multiple linear regression model incorporating microhydrodynamic parameters provided the best explanation for the variation in breakage rate constant.
This study examined the impact of stirrer speed and bead material loading on fenofibrate particle breakage during wet stirred media milling (WSMM) via three kinetic models and a microhydrodynamic model. Evolution of median particle size was tracked via laser diffraction during WSMM operating at 3000-4000 rpm with 35-50% (v/v) concentration of polystyrene or zirconia beads. Additional experiments were performed at the center points of the above conditions, as well as outside the range of these conditions, in order to test the predictive capability of the models. First-order, nth-order, and warped-time kinetic models were fitted to the data. Main effects plots helped to visualize the influence of the milling variables on the breakage kinetics and microhydrodynamic parameters. A subset selection algorithm was used along with a multiple linear regression model (MLRM) to delineate how the breakage rate constant k was affected by the microhydrodynamic parameters. As a comparison, a purely empirical correlation for k was also developed in terms of the process/bead parameters. The nth-order model was found to be the best model to describe the temporal evolution; nearly second-order kinetics (n approximately equal to 2) was observed. When the process was operated at a higher stirrer speed and/or higher loading with zirconia beads as opposed to polystyrene beads, the breakage occurred faster. A statistically significant (p-value <= 0.01) MLRM of three microhydrodynamic parameters explained the variation in the breakage rate constant best (R-2 >= 0.99). Not only do the models and the nth-order kinetic-microhydrodynamic correlation enable deeper process understanding toward developing a WSMM process with reduced cycle time, but they also provide good predictive capability, while outperforming the purely empirical correlation.

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