AAV Capsid Separation via Primary Amino Solid Phase

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Solution Overview

Problem

Current methods for separating empty AAV capsids from full AAV capsids, such as strong anion exchangers with salt gradients at alkaline pH, face limitations including limited separation efficiency, reproducibility issues, and chemical stress that compromises full capsid stability.

Innovation Solution

A method employing a solid phase modified with primary amino groups, where full AAV capsids bind at a first alkaline pH and empty AAV capsids are selectively removed by increasing the pH further, without the need for excess salt, allowing for superior separation under milder conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If strong anion exchangers with salt gradients at alkaline pH are used, then empty AAV capsids can be separated from full AAV capsids, but the separation efficiency is limited and full capsid recovery is compromised

Engineering Contradiction:
Improveseparation efficiencyVSAvoidfull capsid recovery
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent changes the pH parameter from conventional alkaline pH (9.0-10.0) to a narrower alkaline range (8.0-9.0), and modifies the chromatography media from strong anion exchangers to primary amino group-bearing media. This parameter change enables better separation resolution while maintaining full capsid integrity and recovery, as the milder conditions reduce chemical stress on the capsids.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If strong anion exchangers are used, then empty AAV capsids can be removed, but chemical stress decreases stability of full AAV capsids

Engineering Contradiction:
Improveempty capsid removalVSAvoidfull capsid stability
Core Design Contradiction:
ReliabilityVSStability of the object's composition

Solution Approach 1:

The patent reduces the operating pH range from 9.0-10.0 to 8.0-9.0 and uses primary amino group-bearing media instead of strong anion exchangers. This creates milder chemical conditions that maintain full capsid stability while still achieving effective empty capsid removal, as evidenced by reduced peak tailing and fewer signs of capsid dissociation in chromatograms.

Inventive Principle:
Principle #35Parameter changes

3Ease of manufacture

If step gradient elution is used, then equipment and buffer preparation are simpler, but reproducibility is compromised due to variable process parameters

Engineering Contradiction:
Improveprocess simplicityVSAvoidreproducibility
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent uses a linear pH gradient (0.05-0.1 pH units per column volume) instead of step gradients. This continuous gradient approach provides better reproducibility because the relative relationship between eluting full and empty capsid peaks is insulated from variations in materials or conditions, while still being implementable on standard chromatography equipment.

Inventive Principle:
Principle #35Parameter changes

4Reliability

If linear gradient elution is used, then reproducibility is improved, but equipment cost and process complexity increase

Engineering Contradiction:
ImprovereproducibilityVSAvoidequipment and process complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent implements a linear pH gradient elution method that can be performed on standard chromatography equipment without requiring specialized gradient systems. The gradient is defined by simple buffer preparation (0.05-0.1 pH units per column volume), making it accessible to facilities with conventional chromatography infrastructure while achieving superior reproducibility.

Inventive Principle:
Principle #35Parameter changes

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 achieves enhanced separation of empty from full AAV capsids, improving recovery and stability of full capsids, making it suitable for industrial-scale applications with reduced chemical stress.

Implementation Method 1

a first alkaline milieu at a first pH value, at which the full AAV capsids bind to the solid phase surface

Methodology Applied
Scientific EffectElectrostatic interaction: Ion Repulsion/Attraction

Implementation Method 2

empty AAV capsids are at least partially eluted by means of a second alkaline milieu of a pH value higher than the pH value of the first alkaline milieu

Methodology Applied
Scientific EffectpH-dependent binding: Ion Exchange

Data Source

PatentUS20230167416A1A method for separation or depletion of empty AAV capsids from full AAV capsids
Publication Date: 2023.06.01 SARTORIUS BIA SEPARATIONS D O O
  • US20230167416A1 patent drawing
  • US20230167416A1 patent drawing
  • US20230167416A1 patent drawing

AI summary

A method for the separation or depletion of empty AAV capsids from full AAV capsids in an aqueous mixture comprising empty and full AAV capsids, wherein the mixture is contacted with a primary amino groups bearing solid phase surface in a first alkaline milieu whereby(i) full AAV capsids bind to the solid phase surface whereas empty AAV capsids at least partially do not bind to the solid phase surface,or(ii) both full and empty AAV capsids bind to the solid phase surface, and subsequently the empty AAV capsids are at least partially eluted by means of a second alkaline milieu of a pH value higher than the pH value of the first alkaline milieu, with the proviso that the second alkaline milieu does not elute full AAV capsids from the solid phase surface.