Gas Diffusion Electrode Shutdown Protocol for Alkali Chloride Electrolysis

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Solution Overview

Problem

Existing methods for commissioning and decommissioning electrolysis cells with gas diffusion electrodes are inadequate, leading to damage and reduced service life due to oxidative damage, corrosion, and osmotic pressure issues during startup and shutdown processes.

Innovation Solution

A specific sequence of voltage reduction and electrolyte exchange is implemented, including maintaining a voltage between 0.1 and 1.4 V, adjusting pH, cooling the anolyte, and carefully emptying and refilling compartments with diluted alkali metal chloride or hydroxide solutions, while maintaining oxygen flow and controlling temperature differences to prevent damage.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Adaptability or versatility

If standard commissioning and decommissioning procedures are used, then operational flexibility is improved, but oxidative damage and corrosion occur leading to reduced service life

Engineering Contradiction:
Improveoperational flexibilityVSAvoidservice life
Core Design Contradiction:
Adaptability or versatilityVSReliability

Solution Approach 1:

The patent applies preliminary action by implementing specific preparatory steps before shutdown: reducing voltage to 0.1-1.4V range, adjusting pH to 2-12, and maintaining these conditions until catholyte is depleted. This preliminary preparation prevents oxidative damage before it can occur, allowing flexible operation while protecting the gas diffusion electrode and ion exchange membrane from corrosion and damage during commissioning and decommissioning cycles

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent applies preliminary anti-action by introducing counter-measures against oxidative damage in advance: maintaining voltage at 0.1-1.4V and pH at 2-12 creates a protective environment that counteracts the harmful oxidative effects that would otherwise occur during shutdown. This anti-action is implemented before the damaging process can begin, preventing catalyst oxidation and membrane damage while maintaining operational flexibility

Inventive Principle:
Principle #9Preliminary anti-action

2Reliability

If voltage is reduced to 0.1-1.4V and pH adjusted to 2-12 during shutdown, then oxidative damage is prevented, but process complexity increases

Engineering Contradiction:
Improveprotection from oxidative damageVSAvoidshutdown procedure complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent applies parameter changes by modifying voltage and pH parameters during shutdown: voltage is reduced to the 0.1-1.4V range and pH is adjusted to 2-12. These parameter changes create a protective environment that prevents oxidative damage to the catalyst and membrane. The method transforms the shutdown process from a simple power-off procedure into a controlled parameter-adjustment process that protects the electrochemical components while maintaining manageable complexity through systematic parameter control

Inventive Principle:
Principle #35Parameter changes

3Temperature

If cooling is performed while maintaining voltage, then temperature control is improved, but chlorine release may occur

Engineering Contradiction:
Improvetemperature controlVSAvoidchlorine release
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

Solution Approach 1:

The patent applies preliminary action by removing chlorine through electrolysis at controlled voltage before cooling the anolyte. This preliminary removal of chlorine prevents the harmful combination of cooling and voltage maintenance that would otherwise cause chlorine release. By establishing chlorine-free conditions in advance, the method enables safe temperature control during shutdown without generating harmful chlorine gas

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent applies the skipping principle by rapidly removing chlorine through electrolysis before the cooling process begins. This rushed-through approach eliminates the harmful chlorine from the system in advance, allowing subsequent cooling operations to proceed safely without the risk of chlorine release. The method skips over the dangerous condition where both cooling and voltage are simultaneously applied in the presence of chlorine

Inventive Principle:
Principle #21Skipping (Rushing through)

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 method allows for repeated operation and shutdown of electrolyzers without damage, extending the service life of gas diffusion electrodes and ion exchange membranes, and maintaining electrolysis performance over multiple start-up and shutdown cycles.

Implementation Method 1

The gas diffusion electrode (GDE) typically comprises an electrically conductive support and a gas diffusion layer containing a catalytically active component... only platinum and silver have achieved practical significance as catalysts for the reduction of oxygen in alkaline solutions

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

The membranes are provided with a hydrophilic layer on the cathode side or on both sides... Ion transport occurs via acidic sulfonate groups and/or carboxylate groups polymerized into these polymers

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 3

The invention relates to a process for the electrolysis of aqueous solutions of alkali chlorides by means of gas diffusion electrodes

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Data Source

PatentEP3670706B1Method for the membrane electrolysis of alkali chloride solutions with gas diffusion electrode
Publication Date: 2024.02.21 COVESTRO DEUTSCHLAND AG

AI summary

Methods for the electrolysis of alkali chlorides using oxygen-consuming electrodes with special operating parameters for decommissioning and recommissioning are described.