PSA-Molten Carbonate Fuel Cell Integration for CO2 Capture

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current carbon capture systems face challenges in efficiently capturing CO2 from hydrogen production processes, particularly due to high heat demands and the formation of hazardous compounds in amine-based systems, as well as inefficiencies in integrated systems with molten carbonate fuel cells.

Innovation Solution

A carbon capture system comprising a pressure swing adsorption unit and a multi-stage molten carbonate fuel cell, where the anode of the fuel cell is fed with a portion of the tail gas from the PSA unit, allowing for efficient CO2 transfer and capture, while also producing electric energy that can be used within the system.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If amine absorption stripper systems are used for CO2 capture, then CO2 separation is achieved, but high heat demand and formation of hazardous compounds occur

Engineering Contradiction:
ImproveCO2 separation efficiencyVSAvoidhazardous compounds formation
Core Design Contradiction:
Manufacturing precisionVSObject-generated harmful factors

Solution Approach 1:

The patent changes the chemical parameters of the absorption system by using potassium carbonate solution instead of amine-based solvents. This substitution fundamentally alters the chemical reaction mechanism, avoiding the formation of hazardous compounds like nitrosamines while maintaining effective CO2 separation through a different chemical pathway (carbonate equilibrium reactions)

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a regenerable potassium carbonate solution that can be continuously circulated and regenerated in situ. Rather than using complex amine systems requiring extensive regeneration infrastructure, the system uses a simpler, more stable alkaline solution that can be regenerated through heating and CO2 release, reducing both cost and harmful byproducts

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

2Manufacturing precision

If amine absorption stripper systems are used for CO2 capture, then CO2 separation is achieved, but high heat demand is required

Engineering Contradiction:
ImproveCO2 separation efficiencyVSAvoidheat demand
Core Design Contradiction:
Manufacturing precisionVSUse of energy by moving object

Solution Approach 1:

The patent changes the thermal parameters by using potassium carbonate solution which requires lower regeneration temperatures compared to amine systems. The carbonate system can be regenerated at moderate temperatures through simple heating to release captured CO2, significantly reducing the energy input required for the stripping process

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The system implements continuous CO2 capture and regeneration cycles where the potassium carbonate solution continuously circulates between the absorption and regeneration stages. This continuous operation maintains steady-state efficiency and reduces peak energy demands compared to batch amine stripping systems

Inventive Principle:
Principle #20Continuity of useful action

3Manufacturing precision

If pressure swing adsorption unit is integrated with molten carbonate fuel cell, then CO2 capture efficiency is improved, but system complexity increases

Engineering Contradiction:
ImproveCO2 capture efficiencyVSAvoidsystem integration complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent merges two separate functions (CO2 capture via PSA and electricity generation via MCFC) into a single integrated system. The tail gas from the PSA unit, which contains CO2 and other carbonaceous gases, is directly fed to the MCFC anode, creating a synergistic connection that simplifies the overall process flow while enhancing CO2 capture efficiency and producing additional electrical energy

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The integrated system performs multiple functions simultaneously: the PSA unit captures CO2 from the gas stream, the MCFC generates electricity from the carbonaceous gases in the tail gas, and the system produces purified H2 as a product. This multi-functionality reduces the need for separate equipment and processes, ultimately simplifying the overall system architecture

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 system achieves efficient CO2 capture with improved purity, reduces the need for additional CO2 separation steps, and becomes partially self-supporting by utilizing the produced electric energy, thereby enhancing overall system efficiency and reducing environmental impact.

Implementation Method 1

a pressure swing adsorption unit for producing a product gas and a tail gas comprising at least one carbonaceous gas

Methodology Applied
Scientific EffectPressure swing adsorption: Pressure Swing Adsorption

Implementation Method 2

a molten carbonate fuel cell having a cathode and an anode for transferring CO2 from the cathode to the anode

Methodology Applied
Scientific EffectElectrochemical reaction: Fuel Cell

Data Source

PatentUS20250177902A1Carbon capture system
Publication Date: 2025.06.05 UNIVERSITEIT UTRECHT HOLDING BV
  • US20250177902A1 patent drawing
  • US20250177902A1 patent drawing
  • US20250177902A1 patent drawing

AI summary

A carbon capture system may include a pressure swing adsorption unit for producing a product gas and a tail gas comprising at least one carbonaceous gas. The carbon capture system may include a molten carbonate fuel cell having a cathode and an anode for transferring CO2 from the cathode to the anode. The molten carbonate fuel cell may be a multi-stage fuel cell where the anode is in fluid communication with the pressure swing adsorption unit for receiving at least a portion of the tail gas as an inlet stream.