Alkaline Electrolysis Circulation Valves for Selective Mixing

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Solution Overview

Problem

Alkaline electrolysis systems face efficiency losses and safety risks due to imbalanced lye concentrations and hydrogen-oxygen crossover, particularly at fluctuating current densities or low production capacities, leading to potential explosion hazards.

Innovation Solution

An electrolysis arrangement with controlled mixing modes (mixed, partly mixed, and separate) for anolyte and catholyte circulation, using valves and pipes to manage electrolyte flow based on current density, preventing hydrogen-oxygen crossover and maintaining safe operation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Stability of the object's composition

If full mixing of lye cycles from anode and cathode sections is implemented, then lye concentration balance is improved, but hydrogen-oxygen crossover increases causing safety risks

Engineering Contradiction:
Improvelye concentration balanceVSAvoidhydrogen-oxygen crossover
Core Design Contradiction:
Stability of the object's compositionVSObject-affected harmful factors

Solution Approach 1:

The patent segments the lye circulation system into separate anode and cathode loops with independent flow control. Instead of fully mixing lye from both sections, the system maintains separate circulation paths that can be independently managed, thereby preventing hydrogen-oxygen crossover while still allowing selective mixing when needed for concentration balancing.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent implements dynamic control of lye mixing based on operating conditions. Control valves and sensors adjust the degree of mixing between anode and cathode lye streams in real-time according to current density and concentration requirements. This dynamic approach allows the system to optimize concentration balance while minimizing hydrogen-oxygen crossover during low current density operation.

Inventive Principle:
Principle #15Dynamics

2Loss of energy

If lye concentration is increased to improve electrical conductivity, then ohmic losses decrease, but crystallisation risk increases

Engineering Contradiction:
Improveohmic lossesVSAvoidcrystallisation risk
Core Design Contradiction:
Loss of energyVSReliability

Solution Approach 1:

The patent employs feedback control through sensors that continuously monitor lye concentration and temperature. When concentration approaches levels that could cause crystallisation, the system automatically adjusts flow rates and mixing ratios to maintain safe operating parameters while still achieving low ohmic losses through optimized concentration management.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The patent dynamically adjusts lye concentration parameters based on operating conditions. By controlling temperature, flow rates, and mixing ratios, the system optimizes electrical conductivity to minimize ohmic losses while maintaining concentration within safe limits that prevent crystallisation, particularly during variable current density operation.

Inventive Principle:
Principle #35Parameter changes

3Use of energy by moving object

If electrolysis operates at low current density, then energy consumption decreases, but hydrogen-to-oxygen crossover increases causing explosion risks

Engineering Contradiction:
Improveenergy consumptionVSAvoidhydrogen-to-oxygen crossover
Core Design Contradiction:
Use of energy by moving objectVSObject-affected harmful factors

Solution Approach 1:

The patent applies preliminary anti-action by implementing control measures that prevent hydrogen-to-oxygen crossover before it becomes a safety hazard. During low current density operation, the system proactively adjusts lye flow rates and mixing ratios to maintain concentration gradients that inhibit hydrogen diffusion through the membrane, thereby preventing explosive conditions before they can develop.

Inventive Principle:
Principle #9Preliminary anti-action

Solution Approach 2:

The patent uses lye concentration gradients as an intermediary mechanism to control hydrogen diffusion. By carefully managing the concentration and flow of lye in the anode and cathode sections, the system creates a chemical environment that acts as a barrier to hydrogen crossover, particularly during low current density operation when this risk is highest.

Inventive Principle:
Principle #24Intermediary (Mediator)

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

Ensures safe operation across varying capacities and current densities by controlling lye concentration balance and minimizing crossover, thereby preventing explosion risks and optimizing efficiency.

Implementation Method 1

the electrolysis stack is supplied with a direct current for the electrochemical production of hydrogen and oxygen

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

hydrogen and oxygen are susceptible to diffusion through the membrane (diaphragm) which separates the anode and cathode chamber

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 3

This imbalance is further triggered by the electro-osmotic drag of hydroxyl ions, as each hydroxyl ion is able to take up to 2 water molecules

Methodology Applied
Scientific EffectElectro-osmotic drag: Electro-Osmosis

Data Source

PatentUS12421611B2Electrolysis arrangement for alkaline electrolysis
Publication Date: 2025.09.23 LAIR LIQUIDE SA POUR LETUDE & LEXPLOITATION DES PROCEDES GEORGES CLAUDE
  • US12421611B2 patent drawing
  • US12421611B2 patent drawing
  • US12421611B2 patent drawing

AI summary

The invention relates to an electrolysis arrangement for the electrochemical production of hydrogen and oxygen from an alkaline electrolyte having anode and cathode separators for the separation of oxygen and hydrogen from the electrolyte, and an anode and cathode pipe system to circulate electrolyte between anode and cathode sections of an electrolysis stack of the electrolysis arrangement. Control valves and interconnections are configured so that dependent on an electrolyte flow rate passing first, second and third control valve, oxygen and hydrogen depleted electrolyte withdrawn from the separators can be supplied unmixed, partly mixed or fully mixed to the anode and cathode sections of the electrolysis stack to control hydrogen to oxygen and oxygen to hydrogen crossover in the electrolysis arrangement.