Supercritical CO2 Esterification of FDCA

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Solution Overview

Problem

Current methods for converting furan dicarboxylic acid (FDCA) to esters are inefficient, requiring long reaction times, generating harmful byproducts, and involving unsafe reagents, making large-scale production of furan dicarboxylates not cost-effective or sustainable.

Innovation Solution

The process involves reacting 2,5-furan dicarboxylic acid with alcohols in a CO2 atmosphere without additional catalysts, utilizing supercritical or critical conditions to self-generate CO2 as an acid catalyst, which regenerates during ester synthesis, allowing for efficient production of mono- and di-alkyl furan dicarboxylates.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional acid catalyzed esterification is used to convert FDCA to esters, then the reaction can proceed, but the reaction time is too long (20 hours or more) and requires harmful acid catalysts

Engineering Contradiction:
Improvereaction timeVSAvoidacid catalyst
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the physical state and concentration parameters of CO2 to create supercritical conditions (temperature above critical temperature and pressure above critical pressure). This parameter change transforms CO2 from a simple gas into a supercritical fluid with unique properties that enable catalysis without requiring traditional harmful acid catalysts, thereby reducing reaction time from 20+ hours to a much shorter duration while eliminating harmful substances

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

CO2 acts as an intermediary substance that facilitates the esterification reaction under supercritical conditions. The supercritical CO2 provides a unique reaction environment that enables the reaction to proceed efficiently without direct contact with harmful acid catalysts, serving as a green mediator that can be easily removed after the reaction

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If FDCA is heated to temperatures greater than 180°C for melt polymerization, then the reaction can proceed, but FDCA decomposes to furoic acid leading to poor product quality

Engineering Contradiction:
Improvereaction temperatureVSAvoidproduct quality
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent utilizes parameter changes of CO2 (temperature and pressure) to create supercritical conditions that fundamentally alter the reaction environment. This allows the esterification to proceed at temperatures that would normally cause FDCA decomposition, but the supercritical CO2 environment stabilizes the reaction and prevents decomposition to furoic acid, thereby maintaining high product quality while enabling efficient reaction progression

Inventive Principle:
Principle #35Parameter changes

3Productivity

If activation of FDCA as diacyl chloride is used for esterification, then the reaction efficiency improves, but the process becomes unsafe and not sustainable due to harmful byproducts

Engineering Contradiction:
Improvereaction efficiencyVSAvoidharmful byproducts
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent converts the potentially harmful activation step into a beneficial process by using supercritical CO2 to directly facilitate the esterification without requiring diacyl chloride intermediate formation. This approach eliminates the generation of harmful byproducts (SO2, HCl) that would result from traditional activation methods, while still achieving high reaction efficiency through the unique properties of supercritical CO2

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

4Productivity

If conventional esterification methods are used, then esters can be produced, but purification requires washing with base to remove residual acid catalyst affecting downstream processing

Engineering Contradiction:
Improveester productionVSAvoidpurification process
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The patent employs supercritical CO2 as a temporary, easily removable reaction medium that serves its catalytic function during the reaction and then can be completely removed by simple pressure release. This eliminates the need for complex purification steps like base washing, as the CO2 simply evaporates upon depressurization, leaving clean ester products ready for downstream processing without residual catalyst contamination

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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 significantly reduces reaction time, minimizes side products, and eliminates the need for hazardous reagents, resulting in a more sustainable and cost-effective production of furan dicarboxylates with high purity and selectivity.

Implementation Method 1

The CO2 functions as a self-generating acid catalyst in situ and regenerates back to a reagent during ester synthesis

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

The esterification reaction of FDCA with an alcohol in CO2 is performed under operational conditions that correspond to either supercritical, critical or near-critical reaction temperatures or pressures

Methodology Applied
Scientific EffectSupercritical fluid: Supercritical Fluid

Data Source

PatentUS10155736B2Esterification of 2,5-furan-dicarboxylic acid
Publication Date: 2018.12.18 ARCHER DANIELS MIDLAND CO
  • US10155736B2 patent drawing
  • US10155736B2 patent drawing
  • US10155736B2 patent drawing

AI summary

A method of making a furan dicarboxylate by means of reacting 2,5-furan dicarboxylic acid (FDCA) with an alcohol or mixture of alcohols in a CO2-predominant atmosphere without the presence of any other acid catalyst is described. The reaction is conducted under conditions that correspond to either supercritical, critical or near-critical temperatures and pressures for the alcohol species and/or CO2 gas.