A primary drying model-based comparison of conventional batch freeze-drying to continuous spin-freeze-drying for unit doses.

An innovative continuous spin-freeze-drying technology for unit doses was recently developed. For this technology, a mechanistic primary drying model was developed allowing the calculation of the optimal dynamic drying trajectory for spin-frozen formulations. In this work, a model-based and experimentally verified comparison was made between conventional batch freeze-drying and spin-freeze-drying by analyzing the outputs (i.e., primary drying endpoint, optimal shelf temperature/power heater and product temperature profile) of both primary drying models. Input parameters such as dried product layer resistance (Rp) and heat input parameters (Kv,Ptot) were experimentally determined for both freeze-drying methods and compared. In addition, optimal dynamic process parameters were calculated for 3 model formulations by using both mechanistic models. Finally, model predictions were validated by measuring the product temperature and primary drying endpoint. It was observed that, when considering the same layer thickness, Rp was generally lower for continuous spin-frozen formulations compared to vials frozen in a conventional batch freeze-dryer. This observation contributes to the short primary drying times of spin-frozen formulations. In addition, as spin-freezing drastically increases the surface area of the product and lowers the dried layer thickness, drying times can be reduced even further while an excellent cake structure and appearance can still be obtained. The primary drying model for spin-frozen formulations proved to be equally accurate for the prediction of the primary drying endpoint and product temperature compared to the batch freeze-drying model.

Continuous manufacturing of a pharmaceutical cream: Investigating continuous powder dispersing and residence time distribution (RTD).

Recently, an innovative continuous manufacturing technology for a pharmaceutical oral suspension was proposed, based on two consecutive mixing units. A limitation of this technology is the need to dissolve or disperse powder-based raw materials in a liquid via a batch step before continuous manufacturing. Therefore, the aim of the current study was to develop and investigate a method to introduce powders continuously into the existing equipment via the implementation of two upstream continuous unit operations: a powder feeder and powder dispersing unit. A pharmaceutical cream was selected as model formulation to demonstrate the flexibility of the continuous manufacturing technology towards different types of semi-solid and liquid formulations. The ability to continuously feed and disperse active pharmaceutical ingredient (API) using the proposed method was assessed via an experimental design, in which the impact of several process parameters of the powder dispersing unit on the API concentration (relative error (RE) and relative standard deviation (RSD)) was examined. A Raman spectroscopic method was developed to quantify the API concentration in-line after the powder dispersing step. The API concentration was independent of the process parameters and fell within the acceptance limits, except for two experimental runs where a deviating API concentration was observed. These results demonstrate that the continuous powder feeding and dispersing method was suitable, and that a completely continuous manufacturing system was obtained. To achieve raw material traceability and understanding the mixing behavior, the residence time distribution (RTD) of a tracer inside the continuous manufacturing equipment was determined using a colorimetric technique. The time required to remove all tracer from the powder dispersing unit operation was very long (1481 s) and therefore the volume inside this unit operation should be reduced by designing new equipment with smaller dimensions. At the two consecutive mixing units, the peak and mean residence time were influenced by throughput, whereas mixing speed in both mixing units had a significant impact on the degree of axial mixing. Finally, the continuously manufactured cream had a similar rheological behavior as the original batch-wise manufactured cream.

Development of a controlled release formulation by continuous twin screw granulation: Influence of process and formulation parameters.

The aim of this study was to evaluate the potential of twin screw granulation for the continuous production of controlled release formulations with hydroxypropylmethylcellulose as hydrophilic matrix former. Metoprolol tartrate was included in the formulation as very water soluble model drug. A premix of metoprolol tartrate, hydroxypropylmethylcellulose and filler (ratio 20/20/60, w/w) was granulated with demineralized water via twin screw granulation. After oven drying and milling, tablets were produced on a rotary Modul™ P tablet press. A D-optimal design (29 experiments) was used to assess the influence of process (screw speed, throughput, barrel temperature and screw design) and formulation parameters (starch content of the filler) on the process (torque), granule (size distribution, shape, friability, density) and tablet (hardness, friability and dissolution) critical quality attributes. The torque was dominated by the number of kneading elements and throughput, whereas screw speed and filling degree only showed a minor influence on torque. Addition of screw mixing elements after a block of kneading elements improved the yield of the process before milling as it resulted in less oversized granules and also after milling as less fines were present. Temperature was also an important parameter to optimize as a higher temperature yielded less fines and positively influenced the aspect ratio. The shape of hydroxypropylmethylcellulose granules was comparable to that of immediate release formulations. Tensile strength and friability of tablets were not dependent on the process parameters. The use of starch as filler was not beneficial with regard to granule and tablet properties. Complete drug release was obtained after 16-20h and was independent of the design's parameters.