Integrated Electrochemical Reactor for CO2 Capture and Hydrogen Delivery

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Solution Overview

Problem

Existing technologies face challenges in producing high-purity methane from organic/biological waste streams due to low carbon dioxide solubility and the high cost and storage of hydrogen, leading to inefficient carbon dioxide utilization and hydrogen generation.

Innovation Solution

An electrochemical reactor system comprising an electrolyzer cell and an alkaline water electrolysis cell, which captures carbon dioxide and generates hydrogen, using a design that avoids bipolar membranes to reduce voltage drop and energy consumption, allowing for the production of high-purity methane and bicarbonate for biomethanation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If bipolar membranes are used in the electrochemical reactor, then carbon dioxide capture and hydrogen generation can be achieved, but voltage drop and energy consumption increase

Engineering Contradiction:
Improvecarbon dioxide capture efficiencyVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The patent removes bipolar membranes from the electrochemical reactor design, extracting the problematic component that caused high voltage drop and energy consumption while retaining the core functionality of carbon dioxide capture and hydrogen generation through alternative cell configurations

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent employs simpler, more durable membrane materials that do not require the complex bipolar membrane structure, reducing both initial investment and operational energy costs while maintaining adequate performance for carbon dioxide utilization

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

2Quantity of substance

If conventional electrolysis systems are used, then hydrogen can be produced, but the cost and storage requirements make the process economically unfavorable

Engineering Contradiction:
Improvehydrogen productionVSAvoidstorage and delivery infrastructure
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The patent combines hydrogen production with carbon dioxide capture and delivery into a single integrated electrochemical reactor system, eliminating the need for separate hydrogen storage and transport infrastructure by delivering hydrogen directly to the biomethanation reactor through the same system that captures carbon dioxide

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The electrochemical reactor performs multiple functions simultaneously: it produces hydrogen, captures carbon dioxide, and delivers both products to the biomethanation reactor through integrated flow paths, making the system economically viable by reducing infrastructure requirements

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

3Ease of operation

If bioreactors operate at atmospheric pressure, then simple operation is maintained, but carbon dioxide utilization is low due to low aqueous solubility

Engineering Contradiction:
Improveoperational simplicityVSAvoidcarbon dioxide utilization
Core Design Contradiction:
Ease of operationVSQuantity of substance

Solution Approach 1:

The patent changes the delivery parameter of carbon dioxide from gas phase at atmospheric pressure to dissolved phase in aqueous solution, dramatically increasing carbon dioxide utilization in the biomethanation reactor while maintaining simple atmospheric pressure operation through the electrolyte flow system

Inventive Principle:
Principle #35Parameter changes

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 system achieves a 67% reduction in energy consumption compared to previous designs, enabling high-purity methane production and efficient carbon dioxide capture, suitable for biomethanation and renewable natural gas generation.

Implementation Method 1

The electrolyzer cell comprises a first anode spaced from a first cathode by an ion exchange membrane between the first anode and the first cathode... adapted and arranged to allow a flow of a first liquid electrolyte to contact the first anode and the first cathode

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 2

The AWE cell comprises a second anode spaced from a second cathode by a porous diaphragm, and the AWE cell is adapted and arranged to allow a flow of a second liquid electrolyte to contact the second anode and the second cathode

Methodology Applied
Scientific EffectElectrolysis: Electrolysis

Implementation Method 3

The ion exchange membrane can be a cation exchange membrane (CEM), or an anion exchange membrane (AEM)

Methodology Applied
Scientific EffectIon exchange: Ion Exchange

Data Source

PatentUS20250283226A1Electrolysis system for hydrogen production and carbon dioxide capture and delivery
Publication Date: 2025.09.11 UCHICAGO ARGONNE LLC
  • US20250283226A1 patent drawing
  • US20250283226A1 patent drawing
  • US20250283226A1 patent drawing

AI summary

An electrochemical reactor for capturing carbon dioxide and producing bicarbonate and hydrogen is described herein. The electrochemical reactor is useful for, among other things, converting biogas to a bicarbonate and hydrogen feedstock for biomethanation. The reactor comprises at least one reactor unit comprising an electrolyzer cell and at least one alkaline water electrolysis (AWE) cell adjacent to the electrolyzer cell. The electrolyzer cell comprises an anode spaced from a cathode by an ion exchange membrane between the anode and the cathode; and the electrolyzer cell is adapted and arranged to allow a flow of a neutral liquid electrolyte to contact the anode and the cathode. The ion exchange membrane can be a cation exchange membrane (CEM), or an anion exchange membrane (AEM). The AWE cell comprises a second anode spaced from a second cathode by a porous diaphragm.