Electroneutral Porous Separator for Oxocarbon Electrolyzers

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Solution Overview

Problem

Current oxocarbon electrolyzers face challenges in achieving mechanical stability while maintaining ion exchange capacity, leading to high costs and reliability issues due to the need for charged ion exchange membranes, which restricts the use of high differential pressures and complicates the production of stable stacks.

Innovation Solution

The use of an electroneutral separator, which is ionically conductive and mechanically sturdy, allows for ionic migration between the anode and cathode areas without incorporating charged chemicals, reducing costs and improving reliability by separating the areas while supporting electrodes and withstanding pressure differentials.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If charged ion exchange membranes are used to enable ion migration, then ion exchange capacity is improved, but mechanical stability deteriorates and cost increases

Engineering Contradiction:
Improveion exchange capacityVSAvoidmechanical stability
Core Design Contradiction:
ReliabilityVSStrength

Solution Approach 1:

The separator is divided into two functional components: a mechanically stable support structure (microporous substrate) and an ion-exchange functional layer (ionomer coating). This segmentation allows each component to optimize its specific function - the support provides mechanical strength while the thin ionomer layer provides ion exchange capacity, resolving the contradiction between mechanical stability and ion exchange capacity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention uses a composite structure combining a microporous support material (such as PTFE, polyolefin, or ceramic) with an ionomer layer (such as Nafion or other perfluorosulfonic acid polymers). This composite material approach allows the separator to simultaneously achieve mechanical stability from the support and ion exchange capacity from the ionomer layer, while reducing the amount of expensive charged material needed.

Inventive Principle:
Principle #40Composite materials

2Reliability

If charged chemicals are implanted into membranes to facilitate ion migration, then ion exchange capacity is improved, but manufacturing cost increases significantly

Engineering Contradiction:
Improveion exchange capacityVSAvoidmanufacturing cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The invention uses a microporous support structure that provides a high surface area framework. This porous structure allows a thin layer of ionomer to coat the internal surfaces, maximizing ion exchange capacity per unit mass of charged material. The porosity enables efficient ion transport pathways while minimizing the quantity of expensive charged chemicals required, thereby reducing manufacturing cost.

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The invention extracts the ion-exchange function from the bulk membrane structure and concentrates it into a thin functional coating layer on the porous support. This extraction allows the majority of the membrane structure to be made from inexpensive, mechanically stable, uncharged materials, while only a thin layer contains the charged chemicals needed for ion exchange, significantly reducing material costs.

Inventive Principle:
Principle #2Taking out (Extraction)

3Reliability

If traditional charged membranes are used, then ion migration is enabled, but the use of high differential pressures is restricted

Engineering Contradiction:
Improveion migration capabilityVSAvoidpressure differential tolerance
Core Design Contradiction:
ReliabilityVSStress or pressure

Solution Approach 1:

The invention uses a thin ionomer coating layer on a rigid porous support, creating a structure that is mechanically robust yet ionically conductive. The thin functional layer allows efficient ion migration while the rigid porous support structure withstands high differential pressures, enabling the separator to function reliably under pressure conditions that would damage traditional charged membranes.

Inventive Principle:
Principle #30Flexible shells and thin films

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 reduces the overall cost and increases the reliability of oxocarbon electrolyzers, enabling the use of higher pressure differentials and facilitating the production of stable stacks, thereby enhancing the efficiency and stability of the electrolysis process.

Implementation Method 1

The electroneutral separator can be formed by electrically insulative material while being ionically conductive. As such, the separator can allow for ionic migration between the anode area and cathode area

Methodology Applied
Scientific EffectIonic migration: Electrolysis

Implementation Method 2

A conductive electrolyte of the electrolysis reactor can fill the pores of the separator to provide a path for ions to migrate through the separator

Methodology Applied
Scientific EffectCapillary action: Capillary Action

Data Source

PatentUS12139801B2Electroneutral porous separator for oxocarbon electrolyzer
Publication Date: 2024.11.12 DIOXYCLE
  • US12139801B2 patent drawing
  • US12139801B2 patent drawing
  • US12139801B2 patent drawing

AI summary

Methods and systems related to oxocarbon electrolyzers are disclosed herein. A disclosed system includes an oxocarbon electrolysis reactor with an anode area with an oxidation substrate, cathode area with an oxocarbon species as a reduction substrate, and an electroneutral separator separating the anode area and the cathode area while allowing ionic migration between the anode area and cathode area. The electroneutral separator may be a porous electroneutral separator. The oxocarbon electrolyzer may also include a conductive electrolyte applied to the separator. Ionic migration between the anode area and the cathode area may be accomplished via the conductive electrolyte in the porous electroneutral separator.