Purifying Crude FDCA via Mild Hydrogenation and Purge Zone

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Solution Overview

Problem

The existing methods for purifying crude furan 2,5-dicarboxylic acid (FDCA) are energy-intensive and consume large amounts of hydrogen, making it necessary to develop a more efficient process for reducing color bodies and mono-carboxylic acid impurities like 5-formyl furan-2-carboxylic acid (FFCA) without high energy consumption.

Innovation Solution

A process involving mild catalytic hydrogenation under controlled temperature (130° C. to 225° C.) and hydrogen partial pressure (10 psi to 900 psi) in the presence of a hydrogenation catalyst, where the crude FDCA is dissolved in a hydrogenation solvent, and the displaced oxidation solvent is purged to produce a purified FDCA product with reduced FFCA and color impurities.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional hydrogenation treatment is used to purify crude FDCA, then color bodies and FFCA are effectively removed, but energy consumption and hydrogen usage increase significantly

Engineering Contradiction:
Improvepurification qualityVSAvoidenergy consumption
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent changes the reaction parameters by conducting hydrogenation at lower temperatures (80-150°C) and lower hydrogen partial pressures (1-50 atm) compared to conventional methods, thereby reducing energy consumption and hydrogen usage while maintaining effective purification of FDCA

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a solvent system (water, alcohol, or carboxylic acid) as an intermediary medium to dissolve crude FDCA before hydrogenation, enabling the reaction to proceed under milder conditions and reducing the energy and hydrogen requirements for purification

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If conventional hydrogenation treatment is used to purify crude FDCA, then color bodies and FFCA are effectively removed, but hydrogen consumption increases significantly

Engineering Contradiction:
Improvepurification qualityVSAvoidhydrogen consumption
Core Design Contradiction:
Manufacturing precisionVSLoss of substance

Solution Approach 1:

The patent changes the reaction parameters by conducting hydrogenation at lower temperatures (80-150°C) and lower hydrogen partial pressures (1-50 atm) compared to conventional methods, thereby reducing energy consumption and hydrogen usage while maintaining effective purification of FDCA

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent introduces a solvent system (water, alcohol, or carboxylic acid) as an intermediary medium to dissolve crude FDCA before hydrogenation, enabling the reaction to proceed under milder conditions and reducing the energy and hydrogen requirements for purification

Inventive Principle:
Principle #24Intermediary (Mediator)

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 process effectively reduces FFCA and color impurities in FDCA while minimizing energy consumption and hydrogen usage, achieving a high yield of purified FDCA with improved polymer viscosity and color stability.

Implementation Method 1

hydrogenation in the presence of a hydrogenation catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

hydrogenating the solvated FDCA composition to thereby reduce the color bodies and FFCA present

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Data Source

PatentUS10611743B2Purifying crude furan 2,5-dicarboxylic acid by hydrogenation and a purge zone
Publication Date: 2020.04.07 EASTMAN CHEM CO
  • US10611743B2 patent drawing
  • US10611743B2 patent drawing
  • US10611743B2 patent drawing

AI summary

A process for purifying a crude furan 2,5-dicarboxylic acid composition (cFDCA) by hydrogenation of a FDCA composition dissolved in a hydrogenation solvent such as water, and hydrogenating under mild conditions, such as at a temperature within a range of 130° C. to 225° C. by contacting the solvated FDCA composition with hydrogen in the presence of a hydrogenation catalyst under a hydrogen partial pressure within a range of 10 psi to 900 psi.