Porous hollow fiber membrane-based continuous cross-flow anti-solvent crystallizer for production of API nanocrystals

• Crossflow around hollow fiber membrane (HFM) was used for antisolvent crystallization. • Nanocrystals of drugs, griseofulvin and L-glutamic acid, were continuously produced. • Continuous crossflow of drug solution in HFM module had low residence time, t res. • For a solvent/nonsolvent flow rate ratio, nanocrystal size grew linearly with t res. • Distributed supersaturation generation allows growth to overshadow nucleation rate. In porous hollow fiber membrane (HFM) based anti-solvent crystallization (AsCr) technique, the anti-solvent is injected from HFM bore into the active pharmaceutical ingredient (API) containing solution flowing in the shell side. Conventionally, shell-side feed solution flows along the HFM. In our compact module design, the shell-side liquid flows perpendicular to the HFMs; the mean flow length is ∼ 3 cm reducing considerably the residence time ( t res ) which strongly influences crystal growth. We investigated AsCr of griseofulvin (GF) from its acetone solution using anti-solvent water injected through HFM pores. The range of t res was 5–30 s; the volume flow rate ratio (FRR) of acetone/water ranged between 0.35 and 1.66; griseofulvin concentration was varied between saturation (3.73 g/100 g acetone) to 0.4 g GF in 100 g of solution having 50 wt% acetone in the total solution. Low t res yielded nanocrystals < 100 nm. The average API crystal size ( D avg ) remained around 230 nm in a three-hour-long experiment. At a fixed mass FRR of 1.34 ± 0.1 , D avg increased linearly from 48 to 280 nm as t res increased from 5 to 28 s. For two HFM modules in series with the nanocrystal suspension from one module fed to the next module independently fed with anti-solvent water, GF crystallization yields as high as 98 % were achieved. AsCr of L-glutamic acid in water with anti-solvent acetone in the same device illustrated continuous nanocrystal production and similar behaviors vis-à-vis variation s of t res and FRR. The cross-flow HFM based continuous AsCr technique can continuously produce nanocrystals of APIs.

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Publication Details

Journal
Separation and Purification Technology
Published
2025-07-16
DOI
https://doi.org/10.1016/j.seppur.2025.134331
Citations
1
Primary Topic
Crystallization and Solubility Studies
Type
article
Field-Weighted Citation Impact
0.52

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article

Porous hollow fiber membrane-based continuous cross-flow anti-solvent crystallizer for production of API nanocrystals

Kamalesh K. Sirkar, Zhong Wei, Piero M. Armenante, Padmini K. Ananthoji et al.
1 citations
Separation and Purification Technology
Crystallization and Solubility Studies
0.52
article

Porous hollow fiber membrane-based continuous cross-flow anti-solvent crystallizer for production of API nanocrystals

Kamalesh K. Sirkar, Zhong Wei, Piero M. Armenante, Padmini K. Ananthoji, Yufeng Song, Lixin Feng, S.K. Tripathi
article en
1 citations

Abstract

• Crossflow around hollow fiber membrane (HFM) was used for antisolvent crystallization. • Nanocrystals of drugs, griseofulvin and L-glutamic acid, were continuously produced. • Continuous crossflow of drug solution in HFM module had low residence time, t res. • For a solvent/nonsolvent flow rate ratio, nanocrystal size grew linearly with t res. • Distributed supersaturation generation allows growth to overshadow nucleation rate. In porous hollow fiber membrane (HFM) based anti-solvent crystallization (AsCr) technique, the anti-solvent is injected from HFM bore into the active pharmaceutical ingredient (API) containing solution flowing in the shell side. Conventionally, shell-side feed solution flows along the HFM. In our compact module design, the shell-side liquid flows perpendicular to the HFMs; the mean flow length is ∼ 3 cm reducing considerably the residence time ( t res ) which strongly influences crystal growth. We investigated AsCr of griseofulvin (GF) from its acetone solution using anti-solvent water injected through HFM pores. The range of t res was 5–30 s; the volume flow rate ratio (FRR) of acetone/water ranged between 0.35 and 1.66; griseofulvin concentration was varied between saturation (3.73 g/100 g acetone) to 0.4 g GF in 100 g of solution having 50 wt% acetone in the total solution. Low t res yielded nanocrystals < 100 nm. The average API crystal size ( D avg ) remained around 230 nm in a three-hour-long experiment. At a fixed mass FRR of 1.34 ± 0.1 , D avg increased linearly from 48 to 280 nm as t res increased from 5 to 28 s. For two HFM modules in series with the nanocrystal suspension from one module fed to the next module independently fed with anti-solvent water, GF crystallization yields as high as 98 % were achieved. AsCr of L-glutamic acid in water with anti-solvent acetone in the same device illustrated continuous nanocrystal production and similar behaviors vis-à-vis variation s of t res and FRR. The cross-flow HFM based continuous AsCr technique can continuously produce nanocrystals of APIs.

Separation and Purification TechnologyVol. 377
New Jersey Institute of Technology (US), Biogen (United States) (US), Amgen (United States) (US), Amgen (United Kingdom) (GB)
National Science Foundation
Openalex Percentile: Top 36%
Crystallization and Solubility Studies
0.52
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