| Literature DB >> 33768475 |
Héloïse Audat1, Nathalie Heuzé-Vourc'h2,3, Alexie Mayor4,5,1, Béatrice Thibert1, Sylvain Huille1, Renaud Respaud.
Abstract
Respiratory infections are life-threatening and therapeutic antibodies (Ab) have a tremendous opportunity to benefit to patients with pneumonia due to multidrug resistance bacteria or emergent virus, before a vaccine is manufactured. In respiratory infections, inhalation of anti-infectious Ab may be more relevant than intravenous (IV) injection-the standard route-to target the site of infection and improve Ab therapeutic index. One major challenge associated to Ab inhalation is to prevent protein instability during the aerosolization process. Ab drug development for IV injection aims to design a high-quality product, stable to different environment stress. In this study, we evaluated the suitability of Ab formulations developed for IV injection to be extended for inhalation delivery. We studied the aerosol characteristics and the aggregation profile of three Ab formulations developed for IV injection after nebulization, with two mesh nebulizers. Although the formulations for IV injection were compatible with mesh nebulization and deposition into the respiratory tract, the Ab were more unstable during nebulization than exposition to a vigorous shaking. Overall, our findings indicate that Ab formulations developed for IV delivery may not easily be repurposed for inhalation delivery and point to the requirement of a specific formulation development for inhaled Ab.Entities:
Keywords: Formulation development; Inhalation; Mesh nebulization; Monoclonal antibody; Respiratory tract infections
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Substances:
Year: 2021 PMID: 33768475 PMCID: PMC7993445 DOI: 10.1007/s13346-021-00967-w
Source DB: PubMed Journal: Drug Deliv Transl Res ISSN: 2190-393X Impact factor: 4.617
Results of aerosol characterization with NaCl and Ab in formulations expressed as the mean (n=3) ± SD of the flow rate, VMD and % (in V volume) of 1 – 5µm droplets
| NaCl | mAb 1 | mAb 2 | mAb 3 | |||||||||
| Flow rate (mL/min) | VMD (µm) | 1µm <V< 5µm(%) | Flow rate (mL/min) | VMD (µm) | 1µm <V < 5µm(%) | Flow rate (mL/min) | VMD (µm) | 1µm <V< 5µm(%) | Flow rate (mL/min) | VMD (µm) | 1µm <V< 5µm(%) | |
| Device 1 | 0.31 ± 0.02 | 4.1 ± 0.1 | 64.4 ± 0.02 | 0.14 ± 0.02 | 4.4 ± 0.2 | 56.5 ± 0.03 | 0.2 ± 0.02 | 4.1 ± 0.2 | 57.9 ± 0.03 | 0.07 ± 0.01 | 3.3 ± 0.3 | 70.9 ± 0.05 |
| Device 2 | 0.47 ± 0.01 | 3.5 ± 0.2 | 71.0 ± 0.04 | 0.37 ± 0.02 | 3.4 ± 0.2 | 83.8 ± 0.07 | 0.27 ± 0.04 | 3.0 ± 0.1 | 87.6 ± 0.02 | 0.29 ± 0.05 | 3.9 ± 0.2 | 68.1 ± 0.05 |
Fig. 1Subvisible particles measured by flow cell microscopy before and after stress in the mAb formulations. The total number of particles/mL and the number of particles/mL depending on their size are presented in a. All the results correspond to triplicate experiments and are expressed as the mean (n = 3) ± SD. Each value of the particles/mL ≥ 2 µm and their mean are reported in b
Results of Dynamic light Scattering, expressed as the mean (n=3) ± SD of the monomer radius (nm), % pd of the monomer population, % intensity and % mass of monomer and PDI for each Ab formulation before and after stress
| mAb 1 | mAb 2 | mAb 3 | ||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Before stress | Shaking | Device 1 | Device 2 | Before stress | Shaking | Device 1 | Device 2 | Before stress | Shaking | Device 1 | Device 2 | |
| radius (nm) | 7.5 ± 0.3 | 7.0 ± 0.3 | 6.7 ± 0.6 | 6.9 ± 0.4 | 5.5 ± 0.6 | 5.0 ± 0.1 | 5.0 ± 0.1 | 4.9 ± 0.0 | 9.3 ± 0.7 | 8.7 ± 0.4 | 9.2 ± 1.3 | 8.8 ± 0.5 |
| % pd | 9 ± 0.0 | 16 ± 0.1 | 30 ± 0.1 | 16 ± 0.1 | 9 ± 0.0 | 6 ± 0.0 | 7 ± 0.0 | 9 ± 0.1 | 15 ± 0.0 | 18 ± 0.1 | 11 ± 0.0 | 11 ± 0.0 |
| % monomer (intensity) | 100.0 ± 0.0 | 99.7 ± 0.0 | 95.8 ± 0.0 | 96.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 99.8 ± 0.0 | 98.5 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 99.8 ± 0.0 |
| % monomer (mass) | 100.0 ± 0.0 | 99.9 ± 0.0 | 99.9 ± 0.0 | 99.9 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 | 100.0 ± 0.0 |
| PDI | 0.113 ± 0.016 | 0.102 ± 0.004 | 0.214 ± 0.024 | 0.219 ± 0.350 | 0.071 ± 0.010 | 0.070 ± 0.004 | 0.114 ± 0.010 | 0.157 ± 0.029 | 0.119 ± 0.004 | 0.134 ± 0.031 | 0.132 ± 0.012 | 0.162 ± 0.016 |
Results of size exclusion chromatography, expressed as the mean (n=3) ± SD of the % of HMW for each Ab formulation before and after stress
| mAb 1 | mAb 2 | mAb 3 | ||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Before stress | Shaking | Device 1 | Device 2 | Before stress | Shaking | Device 1 | Device 2 | Before stress | Shaking | Device 1 | Device 2 | |
| % HMW | 0.4 ± 0.0 | 0.4 ± 0.0 | 0.5 ± 0.0 | 0.5 ± 0.0 | 0.2 ± 0.0 | 0.2 ± 0.0 | 0.3 ± 0.1 | 0.3 ± 0.0 | 1.0 ± 0.0 | 1.1 ± 0.1 | 1.1 ± 0.0 | 2.1 ± 1.7 |
Fig. 2Correlation curves of Abs in their formulations before and after stress obtained by dynamic light scattering. a mAb 1 correlation curves of one representative sample before stress and one after each stress. b mAb 2 correlation curves of one representative sample before stress and one after each stress. c mAb 3 correlation curves of one representative sample before stress and one after each stress