Sialyllactose Purification via Dual Membrane Filtration

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Solution Overview

Problem

Current methods for purifying sialyllactose from microbial fermentation broths are complex, costly, and inefficient, particularly in removing contaminating carbohydrates and recombinant DNA/polypeptides, making it challenging to produce sialyllactose suitable for human consumption, especially in infant formulas and medical nutrition.

Innovation Solution

A two-step membrane filtration process using membranes with molecular weight cut-offs of 300-500 Dalton and 600-800 Dalton to separate sialyllactose from contaminating carbohydrates, eliminating the need for organic solvents and discontinuous chromatographic steps, while ensuring the removal of nucleic acids and polypeptides.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If traditional purification methods (chromatography, organic solvent crystallization) are used, then sialyllactose can be purified from fermentation broth, but the process becomes complex, costly, and inefficient

Engineering Contradiction:
Improvepurity of sialyllactoseVSAvoidcomplexity of purification process
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The purification process is divided into multiple sequential filtration steps, each targeting specific contaminants. First, nanofiltration removes monosaccharides and disaccharides, then ultrafiltration removes larger oligosaccharides and biomacromolecules, and finally diafiltration removes recombinant DNA and polypeptides. This segmentation allows each step to focus on a specific purification task, achieving high overall purity without requiring complex single-step methods.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Membranes serve as intermediary elements that enable separation based on molecular weight cut-off properties. The nanofiltration membrane (300-500 Dalton MWCO) and ultrafiltration membrane (600-800 Dalton MWCO) act as selective barriers, allowing smaller molecules to pass while retaining larger ones. This intermediary approach simplifies the purification process compared to direct chromatographic methods.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If complex purification schemes are implemented to remove recombinant DNA and polypeptides, then product safety for human consumption is ensured, but production costs increase significantly

Engineering Contradiction:
Improvesafety for human consumptionVSAvoidproduction cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The diafiltration process continuously replaces the fermentation broth with water or buffer while maintaining constant volume, allowing persistent removal of recombinant DNA and polypeptides until detection limits are reached. This continuous action ensures thorough removal of contaminants without requiring multiple batch processing cycles, reducing both time and cost while ensuring product safety.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The patent replaces complex chemical or enzymatic degradation methods with a purely mechanical/physical separation approach using membrane filtration. The nanofiltration and ultrafiltration membranes physically separate contaminants based on size, and diafiltration uses continuous dilution and filtration, eliminating the need for costly chemical treatments or specialized enzymatic processes.

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

3Manufacturing precision

If multiple filtration steps with different molecular weight cut-offs are used, then contaminating carbohydrates are effectively removed, but the process time increases

Engineering Contradiction:
Improveremoval of contaminating carbohydratesVSAvoidpurification process time
Core Design Contradiction:
Manufacturing precisionVSLoss of time

Solution Approach 1:

Nanofiltration is performed first to remove monosaccharides and disaccharides before ultrafiltration removes larger oligosaccharides. This preliminary removal of smaller contaminants prevents them from interfering with subsequent ultrafiltration steps, making the overall process more efficient. The sequential arrangement based on molecular size optimizes the timing and effectiveness of each filtration step.

Inventive Principle:
Principle #10Preliminary action

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 provides a simple, cost-effective, and scalable process for purifying sialyllactose, achieving high purity and suitability for human consumption, reducing production costs and eliminating contaminants, thus making sialyllactose more accessible for infant formulas and medical nutrition.

Implementation Method 1

subjecting an aqueous solution containing a sialyllactose and said other carbohydrates to two membrane filtration steps using different membranes, wherein one membrane has a molecular weight cut-off of between about 300 to about 500 Dalton

Methodology Applied
Scientific EffectNanofiltration: Semipermeable Membrane

Implementation Method 2

wherein the other membrane has a molecular weight cut-off of between about 600 to about 800 Dalton

Methodology Applied
Scientific EffectUltrafiltration: Semipermeable Membrane

Data Source

PatentEP3801037B1A simple method for the purification of a sialyllactose
Publication Date: 2022.10.19 CHR HANSEN HMO GMBH

AI summary

Provided is a method for the purification of a sialyllactose from other carbohydrates, characterized in that the method comprises the steps of subjecting an aqueous solution containing the sialyllactose to two membrane filtration steps using different membranes, a membrane having a molecular weight cut-off of between about 300 Dalton to about 500 Dalton and a membrane having a molecular weight cut-off of between about 600 Dalton to about 800 Dalton.