Multiple Membrane Electrolysis Cell for Copper Ion Crossover Reduction

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Solution Overview

Problem

The existing Cu-Cl cycle electrolysis cells face efficiency issues due to copper ion crossover between the anode and cathode compartments, which compromises hydrogen production over time, as copper species can diffuse or be transported across single-layer membranes, affecting long-term performance and economic viability.

Innovation Solution

An electrochemical cell design featuring multiple ion exchange membranes between the anode and cathode compartments, with a center compartment filled with reticulated vitrious carbon and gas diffusion layers, allowing for copper ion removal through flushing or chemical reactions, thereby reducing copper crossover and maintaining electrolysis efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a single membrane is used to separate anode and cathode compartments, then the device complexity is low, but copper ion crossover occurs reducing electrolysis efficiency

Engineering Contradiction:
Improveelectrolysis efficiencyVSAvoidmembrane structure
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The single membrane separator is divided into multiple membrane layers (first membrane and second membrane) with a center compartment in between. This segmentation creates multiple barriers to copper ion crossover while maintaining manageable complexity through modular construction.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A center compartment filled with reticulated vitreous carbon is introduced as an intermediary between the anode and cathode compartments. This intermediate structure actively removes copper ions that cross the first membrane, preventing them from reaching the cathode and interfering with hydrogen production.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Reliability

If multiple ion exchange membranes are used to prevent copper ion crossover, then electrolysis efficiency is maintained, but the device complexity increases

Engineering Contradiction:
Improvelong-term performanceVSAvoidmembrane configuration
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The separator is segmented into multiple functional membrane layers rather than using a single complex membrane. Each membrane layer performs the basic separation function, while the center compartment handles the copper ion removal, distributing complexity across manageable components.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Reticulated vitreous carbon with its porous structure is used to fill the center compartment. The porous material provides large surface area for copper ion adsorption and removal while allowing efficient flow of electrolyte, maintaining low resistance to ion transport.

Inventive Principle:
Principle #31Porous materials

3Productivity

If copper ions are allowed to cross to the cathode compartment, then the device operation is simple, but hydrogen production efficiency decreases over time

Engineering Contradiction:
Improvehydrogen productionVSAvoidoperational duration
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

The system performs preliminary action by removing copper ions in the center compartment before they can reach the cathode and cause harm. The reticulated vitreous carbon is positioned in advance to intercept and remove copper ions that cross the first membrane, preventing cumulative degradation of hydrogen production efficiency.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The multiple membrane structure with center compartment maintains continuous effective separation throughout operation. By creating multiple barriers and an active removal zone, the system sustains high electrolysis efficiency over extended operational periods without the performance degradation seen in single-membrane systems.

Inventive Principle:
Principle #20Continuity of useful action

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 use of multiple ion exchange membranes significantly reduces copper ion transfer to the cathode, enhancing the long-term performance and efficiency of the CuCl/HCl electrolysis cell, as demonstrated by reduced copper presence in the catholyte over extended periods, thereby improving hydrogen production.

Implementation Method 1

a plurality of ion exchange membranes disposed between the anode compartment and the cathode compartment

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 2

the center compartment is filled with reticulated vitrious carbon

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 3

an electrochemical cell for producing hydrogen gas and cupric chloride

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentEP2831311B1Electrolysis cell with multiple membranes for cucl/hcl electrolysis in hydrogen production
Publication Date: 2017.05.31 ATOMIC ENERGY OF CANADA LIMITED
  • EP2831311B1 patent drawingFigure 1
  • EP2831311B1 patent drawingFigure 2
  • EP2831311B1 patent drawingFigure 3

AI summary

An electrochemical cell for producing hydrogen gas and cupric chloride. The cell comprises: an anode compartment comprising an anode for disposition in an anolyte, wherein the anolyte is cuprous chloride in hydrochloric acid; a cathode compartment comprising a cathode, wherein the cathode comprises an electrocatalyst; a plurality of ion exchange membranes disposed between the anode compartment and the cathode compartment; and at least one center compartment defined by a pair of said ion exchange membranes and comprising at least one element for removal or sequestering of copper ions that cross at least one of said membranes from the anode compartment. Also described is a method for CuC1/HC1 electrolysis in the production of hydrogen using the electrochemical cell.