Zirconia-Catalyzed CHDA Isomerization for High Trans Content

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Solution Overview

Problem

Existing methods for producing trans-cyclohexane dicarboxylic acid (t-CHDA) from cis-cyclohexane dicarboxylic acid (c-CHDA) result in low t-CHDA concentrations and are inefficient, costly, or difficult to handle due to high temperatures and purity requirements.

Innovation Solution

A catalytic isomerization method using an isomerization catalyst containing zirconia with a BET specific surface area of 50 m2/g or more, which adsorbs c-CHDA and desorbs t-CHDA, improving reaction efficiency and yield.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If thermal isomerization method is used to increase t-CHDA concentration, then t-CHDA purity can be improved, but the obtained t-CHDA becomes very hard and difficult to handle

Engineering Contradiction:
Improvet-CHDA purityVSAvoidhandling ease
Core Design Contradiction:
Manufacturing precisionVSEase of operation

Solution Approach 1:

The patent changes the isomerization method from thermal to catalytic, using zirconia-based catalysts with specific surface area parameters (50-500 m²/g) to achieve high t-CHDA concentration without the adverse effects of thermal treatment. This parameter change in the reaction mechanism allows obtaining high-purity t-CHDA that remains easy to handle.

Inventive Principle:
Principle #35Parameter changes

2Ease of manufacture

If conventional hydrogenation methods are used to produce CHDA, then the process is simpler, but the t-CHDA concentration remains low (less than 50%)

Engineering Contradiction:
Improveprocess simplicityVSAvoidt-CHDA concentration
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent introduces zirconia-based catalysts as intermediaries in the isomerization process. These catalysts with specific surface areas (50-500 m²/g) mediate the conversion of c-CHDA to t-CHDA, achieving high t-CHDA concentration (60-90%) while maintaining process simplicity through catalytic rather than thermal methods.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Manufacturing precision

If high purity t-CHDA (98%) is obtained through heat treatment and recrystallization, then product quality is improved, but additional processing steps and costs are required

Engineering Contradiction:
Improvet-CHDA purityVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent performs preliminary action by using zirconia catalysts with optimized surface areas (50-500 m²/g) to achieve high t-CHDA concentration directly during the isomerization process itself. This preliminary catalytic action eliminates the need for subsequent heat treatment and recrystallization steps, reducing process complexity while maintaining high purity.

Inventive Principle:
Principle #10Preliminary action

4Productivity

If zirconia catalyst with high BET specific surface area (500 m²/g or more) is used, then reaction efficiency is improved, but catalyst cost and complexity increase

Engineering Contradiction:
Improvereaction efficiencyVSAvoidcatalyst complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent optimizes the BET specific surface area parameter of zirconia catalysts to a specific range (50-500 m²/g). This parameter optimization achieves high reaction efficiency without excessive catalyst complexity or cost, identifying the optimal balance point where sufficient surface area provides adequate activity without the diminishing returns of ultra-high surface area materials.

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 method allows for high-yield production of CHDA with a high t-CHDA content, easily adjustable trans/cis ratio, and reduced process costs, without the handling difficulties of previous methods.

Implementation Method 1

an isomerization catalyst containing zirconia and having a BET specific surface area of 50 m2/g or more

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS12606514B2Isomerization method of cyclohexane dicarboxylic acid
Publication Date: 2026.04.21 HANWHA SOLUTIONS CORP
  • US12606514B2 patent drawing
  • US12606514B2 patent drawing
  • US12606514B2 patent drawing

AI summary

The present disclosure relates to an isomerization method of a cyclohexane dicarboxylic acid (CHDA) and, more specifically, to a method for preparing a trans-cyclohexane dicarboxylic acid (t-CHDA) from a cis-cyclohexane dicarboxylic acid (c-CHDA) by means of catalytic isomerization.Particularly, an embodiment of the present disclosure provides a method for preparing, in high efficiency and high yield and at a low cost, a CHDA having a high t-CHDA content from a CHDA mainly containing c-CHDA, by using an isomerization catalyst containing zirconia and having a BET specific surface area of 50 m2/g or more.