Continuous FDCA Production via Electrochemical Oxidation

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Solution Overview

Problem

The existing methods for producing 2,5-furandicarboxylic acid (FDCA) consume large amounts of energy and result in reactant loss and impurity formation due to high basicity, which decreases productivity and economic feasibility in batch reaction systems.

Innovation Solution

A continuous production system that includes raw material supply units, a micro-mixing unit, and an electrochemical reaction unit with a membrane and lattice-type or bulk-type flow paths, allowing for a single-pass reaction of an aqueous HMF solution and a basic aqueous solution to produce high-purity FDCA, minimizing material degradation and impurities.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If a batch reaction system is used to produce FDCA, then the reaction can be performed with simple equipment, but material loss and impurity formation occur due to high basicity and prolonged reaction time

Engineering Contradiction:
Improveequipment simplicityVSAvoidreactant loss
Core Design Contradiction:
Ease of manufactureVSLoss of substance

Solution Approach 1:

The patent implements a continuous flow reaction system where HMF solution and basic solution are continuously fed into a reactor, allowing the oxidation reaction to proceed continuously without batch interruptions. This continuous operation maintains optimal pH conditions and reaction temperature, preventing the degradation that occurs in batch systems, thereby reducing reactant loss and impurity formation while improving manufacturing efficiency

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The patent introduces dynamic control of reaction parameters including continuous adjustment of pH through automated base addition, variable flow rates of reactants, and real-time temperature control. These dynamic adjustments allow the system to adapt to changing reaction conditions, maintaining optimal performance and minimizing material degradation throughout the continuous operation

Inventive Principle:
Principle #15Dynamics

2Reliability

If high basicity is maintained in batch reaction to preserve pH above 14, then the oxidation reaction can proceed, but base-induced aldol condensation accelerates causing degradation of HMF and intermediates

Engineering Contradiction:
ImprovepH stabilityVSAvoidimpurity formation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The patent incorporates a feedback control system with pH sensors that continuously monitor the reaction mixture pH and automatically adjust base addition rates to maintain pH above 14. This closed-loop control ensures stable alkaline conditions for oxidation while preventing excessive base accumulation that would accelerate harmful aldol condensation reactions, thus reducing impurity formation

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent changes the temporal profile of pH and temperature parameters from static batch conditions to dynamically optimized continuous flow conditions. By maintaining precise pH control through continuous adjustment and optimizing temperature profiles along the flow path, the system achieves reliable oxidation while minimizing side reactions that generate impurities

Inventive Principle:
Principle #35Parameter changes

3Quantity of substance

If chemical oxidizers and noble metal catalysts are used under high temperature and pressure, then FDCA production can be achieved, but large amounts of energy are consumed

Engineering Contradiction:
ImproveFDCA productionVSAvoidenergy consumption
Core Design Contradiction:
Quantity of substanceVSUse of energy by moving object

Solution Approach 1:

The patent replaces thermal-mechanical oxidation systems (requiring high temperature and pressure equipment) with an electrochemical system using electrode reactors. This substitution eliminates the need for high-energy thermal conditions while achieving the same oxidation conversion, dramatically reducing energy consumption for FDCA production

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

Solution Approach 2:

The patent fundamentally changes the energy input parameter from thermal energy (high temperature and pressure) to electrical energy (applied voltage and current). This parameter change enables the oxidation reaction to proceed under milder, more energy-efficient conditions while maintaining high FDCA production rates through electrochemical activation

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 system effectively reduces material loss and impurities, producing high-purity FDCA with improved stability and efficiency by shortening reaction time and maintaining constant current levels during FDCA production.

Implementation Method 1

an electrochemical reaction unit synthesizing FDCA while passing the raw material mixture introduced from the micro-mixing unit in a single pass

Methodology Applied
Scientific EffectElectrochemical oxidation: Oxidation

Implementation Method 2

a micro-mixing unit mixing the aqueous HMF solution and the basic aqueous solution supplied from the raw material supply units, respectively, to form a raw material mixture

Methodology Applied
Scientific EffectDiffusion: Diffusion

Data Source

PatentUS20240368101A1Continuous production system for 2,5-furandicarboxylic acid and continuous production method for 2,5-furandicarboxylic acid
Publication Date: 2024.11.07 KOREA INST OF SCI & TECH
  • US20240368101A1 patent drawing
  • US20240368101A1 patent drawing
  • US20240368101A1 patent drawing

AI summary

Exemplary embodiments of the present invention may provide a continuous production system for 2,5-furandicarboxylic acid (FDCA), the continuous production system including: raw material supply units supplying an aqueous 5-hydroxymethylfurfural (HMF) solution and a basic aqueous solution, respectively; a micro-mixing unit mixing the aqueous HMF solution and the basic aqueous solution supplied from the raw material supply units, respectively, to form a raw material mixture; an electrochemical reaction unit synthesizing FDCA while passing the raw material mixture introduced from the micro-mixing unit in a single pass; and a product storage unit storing a product discharged from the electrochemical reaction unit.