Crossflow Membrane Emulsification for Uniform Solid Particles

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Solution Overview

Problem

Current methods for producing solid particulate materials, particularly for pharmaceutical compounds, face challenges in achieving a narrow size distribution and efficient scaling up, especially for compounds with poor solubility and permeability, often requiring high energy inputs and leading to thermal degradation or heterogeneous particle shapes.

Innovation Solution

A crossflow membrane emulsification method is employed, where a liquid phase containing a compound is directed through a membrane with pores, and supersaturation is controlled via cooling or antisolvent precipitation to produce solid particles with a narrow size distribution, suitable for both crystalline and amorphous forms, allowing for continuous and scalable production.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by stationary object

If conventional crystallisation or re-crystallisation methods are used for purification and control of solid material form and size, then the desired compound can be obtained, but energy consumption is high due to evaporation processes

Engineering Contradiction:
Improveenergy consumptionVSAvoidcontrol of form and size
Core Design Contradiction:
Use of energy by stationary objectVSManufacturing precision

Solution Approach 1:

The invention changes the fundamental parameter of crystallisation from evaporative removal of solvent to antisolvent addition. By adding a second solvent (antisolvent) in which the compound is insoluble or poorly soluble, the solution becomes supersaturated and crystallisation occurs without energy-intensive evaporation, thus reducing energy consumption while maintaining control over crystal form and size through selection of appropriate antisolvent and process conditions

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention introduces an intermediary substance (antisolvent) that mediates the crystallisation process. The antisolvent acts as a bridge between the dissolved compound and the solid crystal form, enabling precipitation by reducing solubility without requiring thermal energy input for evaporation, thereby resolving the contradiction between low energy consumption and controlled crystallisation

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If mechanical milling or high pressure homogenization is used to increase surface area, then bioavailability can be improved, but thermal degradation and heterogeneous particle shapes occur

Engineering Contradiction:
Improvesurface area uniformityVSAvoidthermal degradation
Core Design Contradiction:
Manufacturing precisionVSObject-affected harmful factors

Solution Approach 1:

The invention replaces mechanical post-treatment methods (milling, homogenization) with a controlled crystallisation process that directly produces particles of desired size and shape. By controlling supersaturation level, antisolvent addition rate, and mixing conditions, the process generates uniform particles with high surface area without subjecting the compound to mechanical stress or thermal degradation, thus eliminating harmful effects while achieving the desired manufacturing precision

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

Solution Approach 2:

The invention performs the surface area enhancement action during the crystallisation step itself rather than as a subsequent mechanical treatment. By controlling nucleation and crystal growth conditions to produce fine, uniform particles directly, the desired surface area is achieved preliminarily, avoiding the need for later mechanical processing that would cause thermal degradation and shape heterogeneity

Inventive Principle:
Principle #10Preliminary action

3Productivity

If reverse antisolvent precipitation is used, then small solid particles are formed quickly, but narrow size distribution and scalability are difficult to achieve

Engineering Contradiction:
Improveproduction speedVSAvoidsize distribution uniformity
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The invention introduces dynamic control elements to the antisolvent precipitation process, including controlled addition rate of antisolvent, adjustable mixing intensity, and temperature control. These dynamic parameters allow optimization of both production speed and particle size distribution uniformity, enabling the process to achieve narrow size distribution while maintaining high productivity and scalability that static conventional methods cannot achieve

Inventive Principle:
Principle #15Dynamics

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 method enables the production of uniform solid particles with controlled size distribution, improving bioavailability and scalability, while reducing energy consumption and avoiding thermal degradation, making it suitable for poorly soluble pharmaceutical compounds.

Implementation Method 1

a membrane defining a plurality of pores

Methodology Applied
Scientific EffectPhysical filtration: Filter (physical)

Implementation Method 2

controlling the supersaturation of the liquid phase after it has passed through the membrane via the plurality of pores

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 3

precipitation is induced by the addition of second solvent in which the compound is insoluble or poorly soluble, an antisolvent

Methodology Applied
Scientific EffectAntisolvent precipitation: Precipitation

Implementation Method 4

The solvents are selected such that the compound of interest is partially soluble in one solvent, referred to as 'the solvent' and substantially insoluble in the other solvent, referred to as 'the anti-solvent'

Methodology Applied
Scientific EffectSupersaturation: Supersaturation

Data Source

PatentUS20230271142A1Methods of preparing solid particulate materials
Publication Date: 2023.08.31 MICROPORE TECH LTD
  • US20230271142A1 patent drawing
  • US20230271142A1 patent drawing
  • US20230271142A1 patent drawing

AI summary

There is described a method of preparing solid particles of a compound, said method comprising controlling provision of a liquid phase, wherein said liquid phase comprises a solution of the compound, in a first flow direction to a membrane, said membrane defining a plurality of pores; and controlling the supersaturation of the liquid phase after it has passed through the membrane via the plurality of pores, to form solid particles of the compound. The method may comprise a continuous method.