Poly-α-glutamic Acid Polymerization Molecular Weight Control

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Solution Overview

Problem

Current methods for preparing poly-α-glutamic acid often result in materials with uncontrolled and high molecular weights, requiring chromatographic separation, and can lead to the spontaneous formation of pyroglutamic ester at the amino terminus, limiting the production of poly-α-glutamic acids with desired molecular weight ranges and purity.

Innovation Solution

A process involving the polymerization of tertiary γ-esters of α-glutamic acid N-carboxy anhydride in specific solvents with chosen initiators, followed by acid hydrolysis, to control molecular weight and prevent pyroglutamic ester formation, yielding poly-α-glutamic acid with a molecular weight range of 8,000 to 40,000 Da and a polydispersity index ≤2, using solvents like 1,4-dioxane and initiators such as DBU.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional polymerization methods are used to prepare poly-α-glutamic acid, then polymerization can proceed, but the molecular weight becomes uncontrolled and excessively high, requiring additional chromatographic separation steps

Engineering Contradiction:
Improvemolecular weight controlVSAvoidproduction efficiency
Core Design Contradiction:
Manufacturing precisionVSProductivity

Solution Approach 1:

The patent changes the chemical parameters of the polymerization system by selecting specific initiators (alkoxides, amines, or carboxylic acids) and controlling their equivalents relative to NCA monomer (0.01-10 eq). This parameter control enables precise molecular weight regulation while maintaining high polymerization efficiency, eliminating the need for chromatographic separation

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces specific initiator molecules as intermediaries that mediate the polymerization between NCA monomer and polymer chain. These initiators (such as sodium methoxide, potassium tert-butoxide, DBU, DMAP) act as controlled mediators that regulate chain growth and prevent uncontrolled high molecular weight formation, thereby improving both molecular weight precision and production efficiency

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If conventional polymerization conditions are applied, then polymerization occurs, but pyroglutamic ester spontaneously forms at the amino terminus, reducing product purity

Engineering Contradiction:
ImprovepurityVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent changes the chemical environment parameters by selecting specific initiators and controlling reaction conditions (temperature 10-50°C, solvent type, initiator equivalents). These parameter modifications suppress the spontaneous formation of pyroglutamic ester at the amino terminus, achieving high purity products without requiring additional purification steps

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the potential harmful side reaction (pyroglutamic ester formation) into a beneficial outcome by selecting initiators and conditions that suppress this side reaction. The controlled polymerization conditions transform what would be a harmful impurity formation into a clean reaction pathway, yielding high purity poly-α-glutamic acid directly

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

3Productivity

If high molecular weight poly-α-glutamic acid is produced, then polymerization yield is high, but additional chromatographic separation is required to achieve desired molecular weight ranges

Engineering Contradiction:
Improvepolymerization yieldVSAvoidmolecular weight range control
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent implements feedback control in the polymerization process by using initiator equivalents (0.01-10 eq relative to NCA) as a control parameter. The initiator concentration provides feedback control over chain initiation rate, enabling precise molecular weight regulation while maintaining high polymerization yield. The molecular weight can be predicted and controlled based on the amount of initiator used

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent changes the stoichiometric parameters of the reaction system by controlling the equivalents of initiator relative to NCA monomer. This parameter change enables direct control over the number of polymer chains formed, thereby controlling molecular weight while maintaining high yield. The relationship between initiator equivalents and molecular weight provides a straightforward control mechanism

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

The process effectively controls molecular weight and polydispersity, avoiding pyroglutamic ester formation, and allows for the production of poly-α-glutamic acid with precise molecular weight ranges, enhancing the efficiency and purity of the polymerization process.

Implementation Method 1

the polymerisation of a tertiary γ-ester of α-glutamic acid N-carboxy anhydride

Methodology Applied
Scientific EffectPolymerisation:

Implementation Method 2

acid hydrolysis of the ester groups

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Data Source

PatentEP2027145B1A process for the preparation of poly-alfa-glutamic acid and derivatives thereof
Publication Date: 2012.03.07 CTI BIOPHARMA CORP
  • EP2027145B1 patent drawing
  • EP2027145B1 patent drawing
  • EP2027145B1 patent drawing

AI summary

The invention relates to an improved process for the preparation of poly-a-glutamic acids which comprises the polymerisation of tertiary ?-esters of a-glutamic acid N-carboxy anhydride with appropriate solvents and initiators, followed by acid hydrolysis of the resulting poly-a-glutamic acid-?-ester. The process is particularly advantageous in that it allows to carefully control the molecular weight of the resulting poly-a-glutamic acid. The invention also relates to poly-a-glutamic acids capped at the amino terminus with carboxylic acids or amino acids and to a process for the preparation thereof.