Extruded PFSA Membrane Conditioning for Tubular Electrolyzer Conductivity

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Solution Overview

Problem

Current proton exchange membrane (PEM) electrolyzers face high costs due to expensive bipolar plates, porous transport layers, and platinum group metals, with planar designs being particularly costly and inefficient, while tubular geometries offer a potential cost reduction but require effective membrane pretreatment to ensure ionic conductivity.

Innovation Solution

A method for conditioning and hydrolysis of extruded perfluorosulfonyl fluoride membranes using a Sulfure (VI)-Fluoride Exchange (SuFEx) reaction, where fluoride groups are exchanged for hydroxyl groups and subsequently protonated to sulfonic acid, enhancing ionic conductivity, involving triethylsilanol as a catalyst and sodium hydroxide, and optimizing reactant concentrations and reaction times to achieve high proton conductivity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional planar PEM electrolyzers are used, then high conversion efficiency and low gas crossover are achieved, but production costs are high due to expensive bipolar plates, porous transport layers, and platinum group metals

Engineering Contradiction:
Improveconversion efficiencyVSAvoidproduction cost
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

The patent transitions from planar to tubular geometry for the electrolysis cell. The tubular membrane electrode assembly allows for a more compact design that eliminates the need for expensive bipolar plates and porous transport layers, while maintaining high conversion efficiency and low gas crossover through the curved membrane structure.

Inventive Principle:
Principle #14Spheroidality (Curvature)

Solution Approach 2:

The patent extracts and eliminates the expensive components (bipolar plates, porous transport layers, platinum group metals) from the electrolyzer design by using a tubular membrane structure that integrates these functions into a single component, thereby reducing production costs while maintaining performance.

Inventive Principle:
Principle #2Taking out (Extraction)

2Ease of manufacture

If tubular geometry is adopted to reduce production costs, then manufacturing expenses decrease, but membrane ionic conductivity must be enhanced through effective pretreatment

Engineering Contradiction:
Improveproduction costVSAvoidionic conductivity
Core Design Contradiction:
Ease of manufactureVSReliability

Solution Approach 1:

The patent applies preliminary chemical treatment to the extruded membrane before it is installed in the tubular electrolyzer. The membrane undergoes hydrolysis treatment with alkali metal hydroxides and subsequent sulfonation to introduce sulfonic acid groups, which establish the necessary ionic conductivity before the membrane is put into service, ensuring reliable performance from the start.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent changes the chemical parameters of the membrane through controlled hydrolysis and sulfonation reactions. By adjusting treatment time, temperature, and chemical concentration, the membrane's ionic conductivity is optimized to meet the requirements for efficient electrolysis operation in the tubular configuration.

Inventive Principle:
Principle #35Parameter changes

3Device complexity

If extruded membranes are used in tubular cells, then device complexity and assembly costs are reduced, but the membranes require chemical conditioning to achieve sufficient proton conductivity

Engineering Contradiction:
Improveassembly complexityVSAvoidproton conductivity
Core Design Contradiction:
Device complexityVSReliability

Solution Approach 1:

The membrane undergoes preliminary chemical conditioning through hydrolysis and sulfonation treatments during the manufacturing process, before the tubular electrolyzer is assembled and put into operation. This ensures that the membrane achieves the required proton conductivity in advance, eliminating the need for complex on-site conditioning procedures.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The membrane treatment process is designed to be self-contained and integrated into the manufacturing workflow. The extruded membrane automatically undergoes controlled chemical reactions with standardized reagents, requiring minimal external intervention and specialized equipment, thereby maintaining low device complexity while ensuring reliable proton conductivity.

Inventive Principle:
Principle #25Self-service

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 effectively increases the ionic conductivity of the membranes, achieving proton conductivities greater than 90 mS/cm, reducing production costs, and ensuring stable operation in tubular electrolysis cells, thereby addressing the cost and efficiency limitations of traditional PEM electrolyzers.

Implementation Method 1

a) hydrolysis of the membrane with water or with an aqueous solution

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Implementation Method 2

b) activation of S—F bonds to execute nucleophilic exchange of the fluoride group, wherein the reaction may be a Sulfure (VI)-Fluoride Exchange (SuFEx)

Methodology Applied
Scientific EffectNucleophilic substitution: Chemical Bonding

Implementation Method 3

In one embodiment, the perfluorosulfonyl fluoride membranes are commercially pretreated and a fluoride group is exchanged for a hydroxyl group using sodium hydroxide

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentUS20240325986A1Method for conditioning and hydrolysis of an extruded membrane
Publication Date: 2024.10.03 UNIWELL ROHRSYSTEME GMBH & CO KG
  • US20240325986A1 patent drawing
  • US20240325986A1 patent drawing
  • US20240325986A1 patent drawing

AI summary

A method (500) for conditioning or hydrolysis of an extruded membrane is disclosed. The method (500) comprising ion exchange processes in divided electrochemical cells using a cation exchanger membrane. The method (500) includes extruding the perfluorosulfonyl fluoride membranes from perfluorosulfonyl fluoride granulate. The method (500) also includes using a pretreatment technique to increase the ionic conductivity of the extruded perfluorosulfonyl fluoride membranes before using the perfluorosulfonic acid membranes in electrolysis cells. The method (500) also includes applying a milder pretreatment technique by activating S—F bonds to execute nucleophilic exchange of the fluoride group in a reaction. The method (500) also includes hydrolyzing sulfonyl fluoride groups to sulfonic acid using triethylsilanol.