Modular CO2 Electrolyzer Stack for High-Pressure Gas Conversion

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Solution Overview

Problem

Existing CO2 electrolyzers face limitations in conversion rate due to low CO2 solubility in water, mass-transport issues, and product crossover, necessitating a continuous-flow, direct CO2 gas-fed setup with high current density, selectivity, and efficiency for industrial applications.

Innovation Solution

A modular, multi-cell electrolyzer stack with bipolar plate assemblies and Ti-frit anode structures, allowing flexible operation under elevated pressures, and optimized flow-channel designs for series/parallel configurations, coupled with catalysts on high surface area carbon supports and ion exchange membranes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If a typical PEM based CO2 electrolyzer configuration with liquid catholyte and gas diffusion layer is used, then some known problems are overcome, but CO2 conversion rate is limited due to low CO2 solubility in water and mass-transport issues

Engineering Contradiction:
ImproveCO2 conversion rateVSAvoidCO2 solubility in water
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The patent changes the physical state of CO2 from dissolved (liquid phase) to gaseous phase by using a gas-phase electrolyte instead of liquid catholyte. This allows direct contact of CO2 gas with the catalyst, dramatically increasing the effective concentration of CO2 at the electrode surface and overcoming the solubility limitation while maintaining high conversion rates

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a gas-phase electrolyte system where CO2 gas flows directly through the electrolyzer cell, utilizing gas-phase transport mechanisms instead of liquid-phase diffusion. This pneumatic approach enables higher CO2 concentrations at the catalyst interface and improves mass transport rates

Inventive Principle:
Principle #29Pneumatics and hydraulics

2Productivity

If high current density is used to increase productivity, then CO2 conversion rate improves, but product crossover and H+ crossover from anode through membrane increase

Engineering Contradiction:
ImproveCO2 conversion rateVSAvoidproduct crossover
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent applies different catalyst compositions and properties to different regions of the electrolyzer. The cathode uses catalysts optimized for CO2 reduction to specific products, while the anode uses catalysts optimized for water oxidation. This local optimization of catalyst quality enables high current densities with reduced unwanted side reactions and product crossover

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The patent modifies operational parameters including cell voltage, temperature, and gas flow rates to optimize the balance between conversion rate and product selectivity. By carefully controlling these parameters, the system achieves high productivity while minimizing H+ crossover and product migration through the membrane

Inventive Principle:
Principle #35Parameter changes

3Productivity

If elevated pressure is used to improve CO2 solubility and conversion, then CO2 conversion rate increases, but device complexity and manufacturing difficulty increase

Engineering Contradiction:
ImproveCO2 conversion rateVSAvoidpressure control system complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent uses gas-phase CO2 flow directly into the electrolyzer cell, utilizing the natural pressure differential and gas flow dynamics to achieve high conversion rates. This approach eliminates the need for complex high-pressure liquid handling systems while maintaining elevated CO2 concentrations at the catalyst interface

Inventive Principle:
Principle #29Pneumatics and hydraulics

Solution Approach 2:

The patent divides the electrolyzer into modular segments with separate gas inlet and outlet channels, allowing independent pressure control of the gas stream. This segmentation simplifies the overall pressure management system by enabling localized pressure optimization without requiring system-wide high-pressure containment

Inventive Principle:
Principle #1Segmentation

4Productivity

If continuous-flow direct CO2 gas-fed setup is used to overcome mass-transport issues, then CO2 conversion rate improves, but device complexity increases

Engineering Contradiction:
ImproveCO2 conversion rateVSAvoidflow-channel design complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent designs flow channels that serve multiple functions simultaneously: they distribute CO2 gas uniformly across the catalyst surface, remove reaction products, manage heat transfer, and maintain optimal pressure gradients. This multi-functionality reduces the need for separate dedicated components, thereby limiting the increase in device complexity despite the continuous-flow configuration

Inventive Principle:
Principle #6Universality (Multi-functionality)

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

The stack achieves high CO2 conversion rates, scalability, and flexibility in producing gas-phase products, suitable for industrial use and adaptable to varying production needs.

Implementation Method 1

convert carbon dioxide gas into various gas-phase products via electrolysis

Methodology Applied
Scientific EffectElectrochemical reduction: Electrolysis

Implementation Method 2

catalysts on high surface area carbon supports

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 3

ion-exchange membrane which is in direct contact with the catalysts

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Implementation Method 4

cathode electrocatalyst is immobilized on a porous gas diffusion layer (GDL), which is typically in contact with a flowing liquid catholyte, while CO2 gas is also fed through the GDL

Methodology Applied
Scientific EffectDiffusion: Diffusion

Data Source

PatentUS12385146B2Modular electrolyzer stack and process to convert carbon dioxide to gaseous products at elevated pressure and with high conversion rate
Publication Date: 2025.08.12 ECHEMICLES ZRT
  • US12385146B2 patent drawing
  • US12385146B2 patent drawing
  • US12385146B2 patent drawing

AI summary

An electrolyzer cell, electrolyzer setup, and related methods are provided for converting gaseous carbon dioxide to gas-phase products at elevated pressures with high conversion rates via electrolysis performed by the electrolyzer cell (100″). The electrolyzer cell (100″) is a multi-stack CO2 electrolyzer cell having individual stacks (40) that each include bipolar plate assemblies that have unique gas and fluid flow architecture formed therein.