Flow-Electrode Capacitive Deionization for Continuous Desalination

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Solution Overview

Problem

Current capacitive deionization (CDI) technologies face challenges in achieving continuous water desalination and ion separation due to the need for periodic regeneration of stagnant electrodes, high energy consumption, and large reactor volumes required for high salt concentrations, especially in seawater, which limits their efficiency and economic viability.

Innovation Solution

A single module, flow-electrode apparatus utilizing suspended conductive particles in a fluid within a single cell with ion exchange membranes allows for continuous water desalination and ion separation by recirculating the fluid between compartments with opposite charges, eliminating the need for separate adsorption and regeneration modes and reducing energy consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If periodic regeneration of stagnant electrodes is implemented in CDI, then ion removal capacity is improved, but device complexity and operational discontinuity worsen

Engineering Contradiction:
Improveion removal capacityVSAvoidpiping and valve system complexity
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The patent transforms the static electrode system into a dynamic one by introducing flow electrodes that continuously move between charging and discharging compartments. This dynamic configuration eliminates the need for periodic switching and complex piping systems, achieving continuous operation while maintaining high ion removal capacity

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system is divided into multiple compartments (charging compartments and discharging compartments) that operate simultaneously and independently. This segmentation allows continuous desalination in charging compartments while regeneration occurs in discharging compartments, eliminating operational discontinuity without requiring complex switching mechanisms

Inventive Principle:
Principle #1Segmentation

2Quantity of substance

If high salt concentration treatment is achieved, then desalination effectiveness is improved, but reactor volume increases

Engineering Contradiction:
Improvesalt concentration treatment effectivenessVSAvoidreactor volume
Core Design Contradiction:
Quantity of substanceVSVolume of moving object

Solution Approach 1:

The patent employs porous electrodes with high surface area to volume ratios, which dramatically increase the ion adsorption capacity within a compact reactor volume. The porous structure provides extensive active sites for ion removal without proportionally increasing the reactor size, enabling effective treatment of high salt concentration feeds

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The system utilizes composite electrode structures combining conductive materials with high surface area porous materials, maximizing ion capture efficiency within limited volume. This composite approach allows the reactor to handle high salt concentrations while maintaining a compact footprint suitable for various applications

Inventive Principle:
Principle #40Composite materials

3Productivity

If maximum applied potential is increased beyond equilibrium potential, then ion adsorption rate is improved, but energy consumption and harmful faradaic processes worsen

Engineering Contradiction:
Improveion adsorption rateVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The continuous flow of electrodes between charging and discharging compartments maintains optimal potential differences throughout the process, ensuring high ion adsorption rates without requiring excessive potential that would lead to energy waste and faradaic reactions. The continuous operation prevents the need for high overpotentials

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

The system automatically recovers energy during the discharge phase when electrodes release adsorbed ions, using this energy to offset the input required for the charging phase. This self-service mechanism reduces net energy consumption while maintaining high productivity, eliminating the need for excessive energy input

Inventive Principle:
Principle #25Self-service

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 approach enables efficient desalination of up to 70% of a 1 g/L NaCl solution with 80% water recovery and high current efficiency, while minimizing energy input and reactor volume, and can be scaled for industrial or microfluidic applications.

Implementation Method 1

The Capacitive Deionization process (CDI) utilizes the principle of electro-sorption of ions in the electrical double layer of an electrode-solution interface

Methodology Applied
Scientific EffectElectro-sorption: Adsorption

Implementation Method 2

the principle of electro-sorption of ions in the electrical double layer of an electrode-solution interface

Methodology Applied
Scientific EffectElectrical double layer: Electric Field

Implementation Method 3

A simple Membrane Capacitive Deionization (MCDI) reactor, as shown in FIG. 2, comprises two current collectors 1 and 2, porous electrodes 1a and 2a respectively arranged on the current collectors 1 and 2, and anion and cation exchange membranes AEM and CEM are arranged on the surfaces of the porous electrodes 1a and 2a

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentUS11261109B2Single module, flow-electrode apparatus and method for continous water desalination and ion separation by capacitive deionization
Publication Date: 2022.03.01 DWI LEIBNIZ INST FUR INTERAKTIVE MATERIALIEN EV
  • US11261109B2 patent drawing
  • US11261109B2 patent drawing
  • US11261109B2 patent drawing

AI summary

The present invention relates to a single module, flow-electrode apparatus for continuous water desalination, ion separation and selective ion removal and concentration by capacitive deionization, comprising: a first current collector (1), a first compartment (1′) for a flow electrode, a first ion exchange membrane (AEM, CEM), a first liquid-permeable channel (6a) next to the first ion exchange membrane (AEM, CEM), a second ion exchange membrane (CEM, AEM) with a fixed charge opposite to that of the first ion exchange membrane (AEM, CEM) next to the first liquid-permeable channel (6a), a second liquid-permeable channel (6b) next to the second ion exchange membrane (CEM, AEM), a third ion exchange membrane (AEM, CEM) having the same fixed charge as the first ion exchange membrane (AEM, CEM) next to the second liquid-permeable channel (6b), a second compartment (2′) for a flow electrode, and a second current collector (2), wherein a fluid (4) containing suspended conductive particles or a mixture of conductive and non-conductive particles or particles made of a mixture of conductive and non-conductive materials (5) is provided in the first and second compartments (1′, 2′), acting as the flow electrode, as well as a corresponding method.