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Startseite » News » Particle engineering of a needle-like active pharmaceutical ingredient into size controlled agglomerates: Part I. Process scalability and development

Particle engineering of a needle-like active pharmaceutical ingredient into size controlled agglomerates: Part I. Process scalability and development

23. November 2025
Particle engineering of a needle-like active pharmaceutical ingredient into size controlled agglomerates

Particle engineering of a needle-like active pharmaceutical ingredient into size controlled agglomerates

Abstract

Pharmaceutical solid oral dosage forms often require optimized crystal size, shape, and bulk powder properties for effective drug formulation. Spherical agglomeration has emerged as a transformative technique to convert undesired crystal shapes into larger, denser agglomerates with improved flow properties. However, achieving scalable, small agglomerate sizes efficiently, remains a challenge. This study investigates spherical agglomeration integrated with a high shear wet mill to consistently achieve smaller agglomerate sizes (<300 µm) for an active pharmaceutical ingredient with challenging particle properties.

Highlights

  • Spherical agglomerates produced with median sizes between 30 and 300 µm.
  • Multivariate DoE showed particle size tuneability via three key process variables.
  • A second-order growth mechanism was observed under immersion regime.
  • Scale-up to 5 L improved flow vs. original API and left minimal bridging liquid content.
  • Drying test needed 225 impeller revolutions and 5 hrs to yield acceptable solids.

A multivariate Design-of-Experiment approach was employed to evaluate the effects of key process variables; bridging liquid addition time, bridging liquid to solids ratio and wet milling speed on agglomerate attributes and bulk powder properties. Optimal process conditions were shown to generate robust agglomerates with a median size range of 30–300 µm. The agglomerates showed good scalability across 250 mL–5 L agitated stirred-tanks when targeting three median sizes (35 µm, 80 µm and 145 µm) with minimal residual solvent content as well as good flow performance.

A parallel agitated-filter isolation study demonstrated that over 225 impeller revolutions (five hours of drying) was sufficient to deliver acceptable product quality. Proper agitation during drying was crucial to avoid breakage and attrition in order to preserve agglomerate properties. Overall, the intensified process significantly improved the particle size, shape, density and flowability of the API. This technique shows great potential in pharmaceutical manufacturing as an important particle engineering tool for enabling downstream processing applications.

Read more here

Bilal Ahmed, Vishal Raval, Mark McGowan, Yihui Yang, Marianne Langston, Charles D. Papageorgiou, Kenneth Smith, Particle engineering of a needle-like active pharmaceutical ingredient into size controlled agglomerates: Part I. Process scalability and development, International Journal of Pharmaceutics, Volume 686, 2025, 126363, ISSN 0378-5173, https://doi.org/10.1016/j.ijpharm.2025.126363.


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