Inhalable Particles via Supercritical Anti-Solvent Precipitation

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Solution Overview

Problem

Current methods for preparing inhalable or insufflable powder formulations of antimuscarinic agents like tolterodine face challenges due to unhelpful crystalline habits and issues with particle size distribution and cohesion, leading to poor aerosolization and handling problems.

Innovation Solution

The use of supercritical anti-solvent (SAS) precipitation to produce particles with a D50 of 4 μm or less and a D90 of 10 μm or less, resulting in more readily inhalable or insufflable particles with improved shape and size distribution, avoiding the issues associated with milling.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If conventional crystallisation is used to prepare inhalable powder formulations, then the process is simple, but it produces needle-shaped crystals with unhelpful crystalline habits that cannot be directly prepared in required particle sizes

Engineering Contradiction:
Improvesimplicity of crystallisation processVSAvoidparticle size distribution control
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent changes the physical parameters of the system by using supercritical fluids (supercritical anti-solvent) instead of conventional liquid solvents. This parameter change enables control over particle size distribution while maintaining crystalline structure, resolving the contradiction between process simplicity and particle size control.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent utilizes phase transition of the anti-solvent from supercritical state to gaseous state during the precipitation process. This phase transition enables precise control over particle formation and size distribution, allowing production of particles with D50 ≤ 4 μm and D90 ≤ 10 μm while avoiding needle-shaped crystal formation.

Inventive Principle:
Principle #36Phase transitions

2Manufacturing precision

If milling/micronisation is used to reduce particle size, then respirable particle ranges are achieved, but the material becomes highly charged and cohesive causing severe downstream handling and processing issues

Engineering Contradiction:
Improveparticle size reductionVSAvoiddownstream handling and processing
Core Design Contradiction:
Manufacturing precisionVSEase of operation

Solution Approach 1:

The patent replaces mechanical milling/micronisation with a chemical-physical process (supercritical anti-solvent precipitation). This substitution eliminates mechanical stress that causes particle charging and cohesion, producing respirable particles (D50 ≤ 4 μm, D90 ≤ 10 μm) that are free-flowing and easy to handle.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The supercritical anti-solvent acts as an intermediary medium that enables controlled particle formation. It allows precipitation of particles in the required size range without the mechanical violence of milling, thus avoiding particle charging and cohesion issues while maintaining respirable particle dimensions.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If milling is used to produce fine particles, then particle size is reduced, but irregular shaped and sized particles are produced with bimodal distribution and poor aerosolization

Engineering Contradiction:
Improveparticle size reductionVSAvoidparticle shape regularity
Core Design Contradiction:
Manufacturing precisionVSShape

Solution Approach 1:

The patent changes the formation mechanism from mechanical fracture (milling) to controlled precipitation (supercritical anti-solvent). This parameter change results in uniform, regular-shaped particles with monomodal size distribution (D50 ≤ 4 μm, D90 ≤ 10 μm) rather than irregular particles with bimodal distribution, significantly improving aerosolization performance.

Inventive Principle:
Principle #35Parameter changes

4Manufacturing precision

If amorphous hygroscopic domains are formed during milling, then particle size is reduced, but particle recrystallisation and growth occur upon uptake of water

Engineering Contradiction:
Improveparticle size reductionVSAvoidparticle stability upon water uptake
Core Design Contradiction:
Manufacturing precisionVSStability of the object's composition

Solution Approach 1:

The patent uses supercritical anti-solvent precipitation to form stable crystalline particles directly in the required size range, avoiding formation of amorphous hygroscopic domains. The crystalline structure produced is stable and does not undergo recrystallisation or growth upon water uptake, resolving the stability issue associated with milled particles.

Inventive Principle:
Principle #36Phase transitions

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach enables the production of fine, free-flowing powders with a narrow particle size distribution, facilitating rapid aerosolization and improved clinical outcomes by reducing the required dose and enabling rapid onset of action.

Implementation Method 1

contacting a stream of anti-solvent with a stream of solution of antimuscarinic agent to form particles of antimuscarinic agent

Methodology Applied
Scientific EffectSupercritical fluid extraction: Supercritical Fluid Extraction

Implementation Method 2

to precipitate particles of antimuscarinic agent

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Data Source

PatentUS11759420B2Inhalable particles
Publication Date: 2023.09.19 CRYSTEC
  • US11759420B2 patent drawing
  • US11759420B2 patent drawing
  • US11759420B2 patent drawing

AI summary

A powder formulation, or pharmaceutical composition comprising or consisting of particles of an antimuscarinic agent, said particles being obtainable by supercritical anti-solvent (SAS) precipitation and having a D50 of 4 μm or less and a D90 of 10 μm or less. Methods of forming the formulation and composition are also disclosed, as are uses of the composition.