Purification of Glucuronide Derivatives via Methanol Precipitation

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Solution Overview

Problem

Existing methods for purifying quinolinyl-2-yl-phenylalamine glucuronide derivatives, such as those described in WO 2016/135052, are not compliant with industrial scale production due to difficulties in handling solid extracts and achieving acceptable purity and residual solvent levels.

Innovation Solution

A method involving a solubilization step with methanol followed by precipitation with water, and a drying step at a temperature of 30° C or lower, is developed to purify quinolinyl-2-yl-phenylalamine glucuronide derivatives, allowing for industrial-scale compliance and improved purity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If extraction with ethyl acetate followed by concentration to dryness is used to purify crude compound (1), then purification is achieved, but the process is not compliant with industrial scale production due to difficulties in handling solid extracts

Engineering Contradiction:
Improvepurification qualityVSAvoidindustrial scale compliance
Core Design Contradiction:
Manufacturing precisionVSEase of manufacture

Solution Approach 1:

The invention replaces the concentration-to-dryness step with a precipitation step where the purified compound is induced to precipitate from solution as a solid. This phase transition from dissolved state to precipitated solid allows for easy filtration and handling at industrial scale, while maintaining purification quality. The precipitated solid can be directly filtered and washed without requiring concentration to dryness.

Inventive Principle:
Principle #36Phase transitions

2Manufacturing precision

If concentration to dryness is performed after extraction, then solid extract is obtained, but residual solvent amounts exceed ICH level requirements

Engineering Contradiction:
Improvepurity levelVSAvoidresidual solvent amounts
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The invention uses precipitation instead of concentration to dryness, allowing the compound to be recovered as a precipitated solid that can be filtered and washed. This approach enables more effective removal of residual solvents through washing, ensuring compliance with ICH level requirements while maintaining high purity levels.

Inventive Principle:
Principle #36Phase transitions

Solution Approach 2:

The invention changes the physical state parameters by precipitating the compound from solution rather than concentrating to dryness. By controlling precipitation conditions and followed by washing, the residual solvent content is reduced to meet ICH requirements while maintaining product purity.

Inventive Principle:
Principle #35Parameter changes

3Manufacturing precision

If solid extracts are handled at industrial scale, then purification is completed, but operational difficulties and feasibility issues arise

Engineering Contradiction:
Improvepurification completionVSAvoidhandling feasibility
Core Design Contradiction:
Manufacturing precisionVSEase of operation

Solution Approach 1:

The invention performs purification while the compound remains in solution phase, then induces precipitation to obtain the purified solid. This eliminates the need to handle concentrated viscous extracts or dry solids during the purification process, making operations much easier and more feasible at industrial scale. The precipitated solid can be directly filtered and processed.

Inventive Principle:
Principle #36Phase transitions

4Manufacturing precision

If existing purification methods are used, then crude compound (1) is purified, but the process is not adapted for industrial implementation with acceptable yield

Engineering Contradiction:
Improvepurification effectivenessVSAvoidindustrial implementation suitability
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The invention uses precipitation to recover the purified compound as a solid that can be easily filtered and washed. This approach improves productivity at industrial scale by eliminating time-consuming concentration steps and enabling efficient solid-liquid separation through filtration. The process maintains purification effectiveness while being fully adapted for industrial implementation.

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

The method achieves high purity levels of the quinolinyl-2-yl-phenylalamine glucuronide derivatives, with residual solvent amounts meeting ICH level requirements, thus addressing the challenges of industrial-scale production.

Implementation Method 1

a solubilization step of said crude compound of formula (I) with methanol

Methodology Applied
Scientific EffectSolubilization: Solvation

Implementation Method 2

followed by a precipitation step with water

Methodology Applied
Scientific EffectPrecipitation: Precipitation

Implementation Method 3

a drying step under a temperature inferior or equal to 30° C.

Methodology Applied
Scientific EffectDrying: Desiccation

Data Source

PatentUS20250145651A1Method of preparation of 1-(n-(quinolin-2-yl)-(phenylamino)-1-deoxy-beta-d-glucopyranuronic acid derivatives
Publication Date: 2025.05.08 ABIVAX
  • US20250145651A1 patent drawing
  • US20250145651A1 patent drawing
  • US20250145651A1 patent drawing

AI summary

A process of purification of a crude compound of formula (I)wherein it includes an isolation step of the crude compound of formula (I) including: (i) a solubilization step of the crude compound of formula (I) with methanol followed by a precipitation step with water, and (ii) a drying step under a temperature inferior or equal to 30° C. Herein is further provided a manufacturing process for preparing a compound of formula (I).