Electrochemical Cell With Solution Infused Porous Layer

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Solution Overview

Problem

Current water electrolysis systems for hydrogen production are costly and inefficient, with high energy requirements due to inefficiencies such as solution resistance losses and electrode over-potentials, and maintaining a pH differential across the electrolyzer cell is energy-intensive and time-consuming.

Innovation Solution

Incorporating porous layers infused with specified solutions into the electrolyzer cell to maintain a pH differential between the anode and cathode, allowing for easier maintenance of a pH gradient with reduced energy input, using an anion exchange membrane to facilitate the passage of OH- ions and reduce the need for rebalancing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Power

If a pH differential is maintained across the electrolyzer cell to reduce cell voltage and improve safety, then the electrochemical performance is improved, but additional energy is required to maintain the pH differential over time

Engineering Contradiction:
Improvecell voltageVSAvoidenergy to maintain pH differential
Core Design Contradiction:
PowerVSUse of energy by moving object

Solution Approach 1:

The porous layers are pre-infused with specific pH solutions (acidic solution at the anode, alkaline solution at the cathode) before operation begins. This preliminary action establishes the desired pH differential immediately, eliminating the need for continuous energy input to maintain the gradient, as the pH buffering capacity is built into the structure itself

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The porous layers act as intermediary elements between the electrolyte solutions and the electrodes. These layers buffer and maintain the pH differential locally at each electrode interface, preventing direct equilibration between the anode and cathode compartments while still allowing ionic conduction necessary for the electrochemical reactions

Inventive Principle:
Principle #24Intermediary (Mediator)

2Device complexity

If conventional electrolysis systems operate without pH differential to simplify operation, then the system complexity is reduced, but solution resistance losses and electrode over-potentials increase energy consumption

Engineering Contradiction:
Improvesystem complexityVSAvoidsolution resistance losses
Core Design Contradiction:
Device complexityVSLoss of energy

Solution Approach 1:

The system implements local quality by creating different pH environments specifically at the electrode interfaces through the infused porous layers, while the bulk electrolyte solutions can remain relatively simple. This localized pH control reduces solution resistance losses and electrode over-potentials at the critical reaction sites without requiring complex system-wide pH control mechanisms

Inventive Principle:
Principle #3Local quality

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 energy required to maintain the pH differential, improves cell efficiency, and allows for operation at lower voltages, enhancing the overall performance of the electrolyzer cell by delivering reactants directly to the electrodes, thus reducing the need for electrolyte solutions in the chambers.

Implementation Method 1

a first porous layer in contact with the first electrode, wherein the first porous layer is infused with a first specified solution

Methodology Applied
Scientific EffectCapillary action: Capillary Action

Implementation Method 2

using an anion exchange membrane to facilitate the passage of OH- ions

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 3

Water electrolysis uses electricity to split water molecules into H2 gas and oxygen gas (O2)

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentUS20240158924A1Electrochemical cell including solution infused layer
Publication Date: 2024.05.16 VERDAGY INC
  • US20240158924A1 patent drawing
  • US20240158924A1 patent drawing
  • US20240158924A1 patent drawing

AI summary

An electrochemical cell comprises a first electrode configured for a first electrochemical half reaction, a first electrolyte solution in contact with the first electrode, a second electrode configured for a second electrochemical half reaction, a second electrolyte solution in contact with the second electrode, a separator positioned between the first electrode and the second electrode, and a first porous layer in contact with the first electrode, wherein the first porous layer is infused with a first specified solution comprising a first reactant for the first electrochemical half reaction.