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Freeze-Drying From Organic Co-Solvent Systems, Part 2: Process Modifications to Reduce Residual Solvent Levels and
Claudia Kunz1, Sonja Schuldt-Lieb2, Henning Gieseler3
1Friedrich-Alexander University (FAU) Erlangen-Nürnberg, Division of Pharmaceutics, Freeze Drying Focus Group, Erlangen 91058, Germany.
Abstract:
The use of co-solvent systems can benefit the freeze-drying process and product performance. In this study, cycle designs were applied based on existing recommendations for water-based formulations. Modifications thereof and the influence on the process (e.g., drying times) and product quality attributes (e.g., product appearance, residual solvent) were tested for various cosolvent systems. It was found that fast freezing was associated with the formation of large crystals for 50 mg/g polyvinylpyrrolidone in 40% 1,4-dioxane (w/w), resulting in a 7% reduction of primary drying. The application of high shelf temperatures during primary drying for 50 mg/g polyvinylpyrrolidone in 70% tert-butanol was feasible, resulting in shorter primary drying times but high residual solvent levels (7.7%). Most notable was that the inclusion of an evaporation step after freezing improved the product appearance for low-melting co-solvents (10% ethanol and 10% acetone). No ice or solvent nucleation occurred in the case of 50 mg/g mannitol in 50% N,N-dimethylacetamide during the normal freezing stage. Instead, the solution viscosity significantly increased after cooling to low shelf temperatures, followed by product evaporation (rather than sublimation) during the drying phase and failure to form a product cake after drying. The application of annealing enabled nucleation and sublimation.
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