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Startseite » News » Formulation Components’ Role in Shaping Continuous Nanocarrier Production through Impingement Jet Mixing

Formulation Components’ Role in Shaping Continuous Nanocarrier Production through Impingement Jet Mixing

28. May 2024
Formulation Components' Role in Shaping Continuous Nanocarrier Production through Impingement Jet Mixing

Formulation Components' Role in Shaping Continuous Nanocarrier Production through Impingement Jet Mixing

Presented at the 14th World Meeting on Pharmaceutics, Biopharmaceutics and Pharmaceutical  (PBP) Technology, 18 – 21 March 2024, Vienna, Austria:

INTRODUCTION

The predominant approach for manufacturing nanocarriers on an industrial scale is batch production [1]. Here, a specific quantity of raw materials undergoes a stepwise transformation from a raw state into a refined dispersion. Once the processing line is complete, the dispersion is filled into dosing units, subjected to quality control, released for use, and the production unit is prepared for the next batch. However, this involves the risk that a batch may not meet the release specifications and has to be discarded, or scalability problems may occur [2,3]. One way to overcome these challenges is to produce nanocarriers in a continuous production line that includes real-time monitoring and in-line quality control. Flash nanoemulsification using impingement jet mixing (IJM) represents a promising bottom-up approach to enable the production of nanocarriers that meet the final product specifications [4]. In addition, spatially resolved dynamic light scattering (SR-DLS) has the unique capability to measure droplet sizes in-line under flow conditions, including very turbid samples [3]. This study focused on optimizing the amount and ratio of various formulation components to tailor lipid-based nanocarriers via IJM considering size measurements.

 

MATERIALS & METHODS

  • Organic phase: Labrafac™ lipophile WL 1349 (lipid) in ethanol in various concentrations (2 -30 mg/ml)
  • Aqueous phase: Tween® 80 (stabilizer) in water in various concentrations (0.1 – 7.5 mg/ml)

Material

  • Investigation of the following parameters:
    • Variation of the flow rates at 1:1 phase ratio using IJM1 and different lipid and stabilizer concentrations
    • Variation of the flow rates at various aqueous to organic phase ratios (1:1 – 4:1)
  • Characterization: DLS and SR-DLS

 

RESULTS

Stabilizer proportion

Most pronounced effect of stabilizer
proportion on size

Total flow rate

Size dependent on total flow rate
and ratio of the two phases

Slight size deviations

Slight size deviations of DLS and SR-DLS due to different light source

 

CONCLUSION

This study revealed that the droplet sizes were directly related to the applied stabilizer concentrations, the aqueous to organic phase ratios and the total flow rates. Thereby, comparable results were obtained using DLS and SR-DLS highlighting that undiluted samples can be measured via SR-DLS even in the presence of an organic solvent. This study is therefore a first step toward formulation optimization and targeting of a continuous bottom-up nanomanufacturing line equipped with process analytical technology (PAT) including SR-DLS to facilitate the manufacturing of adequate end products.

 

See the full poster on “Shaping Continuous Nanocarrier” here

(click the picture to download the poster)

Formulation Components' Role in Shaping Continuous Nanocarrier Production through Impingement Jet Mixing

Source: Carolin Tetyczka, Manuel Zettl, Christina Glader, Ramona Jeitler, Svea Stephan, Marius Seg, Yan Wang, Philippe Caisse, Vanessa Bourgeaux, Martin Spoerk,Johannes Khinast, Eva Roblegg, Gattefossé, www.rcpe.at, poster “Shaping Continuous Nanocarrier“, PBP 14th World Meeting, 18 – 21 March 2024, Vienna


Do you want to see more posters of the PBP World Meeting 2024 in Vienna?

Have a look at our overview page

Tags: excipientsformulation

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