Propionic Acid Separation Using Strong Base Anion Exchange Resin

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Solution Overview

Problem

Traditional methods for purifying propionic acid, such as distillation and solvent extraction, are energy-intensive and non-selective, leading to contamination and the formation of undesired byproducts, while existing ion-exchange methods using weak to moderately basic resins are not effective in separating propionic acid from complex liquid mixtures.

Innovation Solution

Chromatographic separation of propionic acid using a strong base anion exchange resin, specifically a gel-type, Type I strong base resin, from a liquid feed mixture containing propionic acid and carbohydrates, organic acids, and other components, which allows for continuous processing and improved selectivity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If distillation is used to purify propionic acid, then separation is achieved, but energy consumption increases and undesired byproducts are formed

Engineering Contradiction:
Improvepurity of propionic acidVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent replaces the thermal distillation process with a chromatographic separation process using ion-exchange resin. Instead of using heat and mechanical vaporization to separate propionic acid, the invention uses chemical interaction between the acid and the ion-exchange resin beads, followed by elution with a base solution, thereby eliminating the need for high-energy heating while achieving comparable or superior separation purity.

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

Solution Approach 2:

The invention changes the separation parameter from temperature-based (distillation) to chemical affinity-based (ion-exchange). By using a strong base anion-exchange resin, the process exploits the ionic interaction between the resin and propionic acid at controlled pH conditions, allowing separation at ambient or mild temperatures rather than requiring the high temperatures of distillation.

Inventive Principle:
Principle #35Parameter changes

2Manufacturing precision

If solvent extraction is used to remove propionic acid, then separation is achieved, but selectivity decreases and product contamination occurs

Engineering Contradiction:
Improvepurity of propionic acidVSAvoidselectivity of separation
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The patent replaces solvent extraction with ion-exchange chromatography. Instead of relying on differential solubility in organic solvents, the invention uses specific ionic interaction between the propionic acid and the functional groups on the ion-exchange resin. This chemical specificity provides superior selectivity, as the resin can be designed to target carboxylic acids while leaving other compounds in the fermentation broth unaffected.

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

Solution Approach 2:

The ion-exchange resin acts as an intermediary substance that selectively binds propionic acid from the complex fermentation mixture. The resin's functional groups temporarily hold the acid through ionic interaction, allowing other components to pass through unchanged. This intermediary mechanism provides the selectivity that direct solvent extraction cannot achieve.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Ease of manufacture

If weak to moderately basic ion-exchange resins are used, then the process is simpler, but separation effectiveness decreases

Engineering Contradiction:
Improvesimplicity of processVSAvoidseparation effectiveness
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The invention changes the key parameter of the ion-exchange resin from weak to strong base functionality. Strong base resins contain quaternary ammonium groups that provide permanent positive charge, enabling them to effectively bind anionic propionic acid across a wider pH range. This parameter change dramatically improves separation effectiveness while maintaining the simplicity of the chromatographic process.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent uses a composite ion-exchange resin material combining a polymer matrix with quaternary ammonium functional groups. This composite structure provides both the mechanical stability needed for column operation and the chemical functionality required for high-selectivity binding of propionic acid, achieving both simplicity and effectiveness.

Inventive Principle:
Principle #40Composite materials

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 effectively separates propionic acid from complex mixtures with high selectivity, reducing energy consumption and byproduct formation, and is suitable for fermentation process liquids, enhancing the purity and efficiency of propionic acid recovery.

Implementation Method 1

chromatographically separating propionic acid from a liquid feed mixture including propionic acid and a carbohydrate by passing the liquid feed mixture through a bed including a strong base anion exchange resin

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentEP3383516B1Chromatographic separation of propionic acid using strong base anion exchange resin
Publication Date: 2019.12.25 DOW GLOBAL TECHNOLOGIES LLC
  • EP3383516B1 patent drawingFigure 1~2
  • EP3383516B1 patent drawing
  • EP3383516B1 patent drawing

AI summary

A method for chromatographically separating propionic acid from a liquid feed mixture including propionic acid and a carbohydrate by passing the liquid feed mixture through a bed including a strong base anion exchange resin.