Swellable Ionic Liquid Particles for Acidic Gas Capture

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Solution Overview

Problem

Existing acidic gas capture technologies, such as liquid and solid-based sorbents, face challenges including low capture efficiency, high energy requirements, corrosion, thermal degradation, and leaching issues, limiting their scalability and performance in industrial applications.

Innovation Solution

The use of amine-functionalized ionic liquids absorbed within swellable support particles, particularly hydrogel particles, which maintain flowability and absorb acidic gases like CO2, H2S, or SO2, with enhanced uptake kinetics and efficiency by forming microdroplets within the swellable support, allowing for improved absorption and desorption capabilities.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If liquid-based amine sorbents are used for CO2 capture, then chemical reaction with acidic gas is improved, but gas-liquid contact area is limited and capture efficiency is low

Engineering Contradiction:
Improvechemical reaction efficiencyVSAvoidcapture efficiency
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The liquid amine sorbent is segmented into discrete solid support particles with high surface area, creating numerous independent reaction sites that increase gas-solid contact area and capture efficiency while maintaining chemical reactivity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Solid support particles with porous structures are used to provide high surface area for gas contact, enabling improved capture efficiency while the amine functional groups maintain chemical reaction capability

Inventive Principle:
Principle #31Porous materials

2Reliability

If liquid amine solutions are used for CO2 absorption, then CO2 capture is achieved, but intensive energy requirements are needed for desorption

Engineering Contradiction:
ImproveCO2 capture capabilityVSAvoidenergy requirements for desorption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The physical state of the amine sorbent is changed from liquid to solid supported form, which modifies the thermodynamics of the system to enable lower temperature desorption and reduce energy requirements while maintaining CO2 capture capability

Inventive Principle:
Principle #35Parameter changes

3Reliability

If liquid amine solutions are used for CO2 absorption, then CO2 capture is achieved, but corrosivity to steel pipes occurs

Engineering Contradiction:
ImproveCO2 capture capabilityVSAvoidcorrosivity
Core Design Contradiction:
ReliabilityVSObject-affected harmful factors

Solution Approach 1:

An inert solid support material serves as an intermediary carrier for the amine functional groups, isolating the corrosive amine solution from contact with steel pipes while maintaining the chemical reaction capability for CO2 capture

Inventive Principle:
Principle #24Intermediary (Mediator)

4Reliability

If liquid amine solutions are used for CO2 absorption, then CO2 capture is achieved, but thermal or chemical degradation of amine groups occurs

Engineering Contradiction:
ImproveCO2 capture capabilityVSAvoidamine group stability
Core Design Contradiction:
ReliabilityVSStability of the object's composition

Solution Approach 1:

The solid support acts as a stable intermediary platform that protects the amine functional groups from thermal and chemical degradation while maintaining their CO2 capture functionality

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

A composite material system combining solid support with amine functional groups is created, where the stable solid support protects the amine groups from degradation while maintaining CO2 capture capability

Inventive Principle:
Principle #40Composite materials

5Reliability

If liquid amine solutions are used for CO2 absorption, then CO2 capture is achieved, but loss of volatile amines into gaseous streams occurs

Engineering Contradiction:
ImproveCO2 capture capabilityVSAvoidamine volatility
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The solid support serves as a non-volatile intermediary that anchors the amine functional groups, preventing their evaporation into the gas stream while allowing CO2 to be captured through the amine groups

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The solid supported amine system eliminates the need to replace volatile amine losses, as the amine groups are fixed on the solid support and can be regenerated through desorption and reabsorption cycles

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

6Productivity

If high surface area solid-based sorbents are used to address uptake rate limitations, then uptake rate is improved, but cost of synthesis becomes high

Engineering Contradiction:
Improveuptake rateVSAvoidsynthesis cost
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

Common porous solid supports with established synthesis methods are used, providing high surface area for improved uptake rate while maintaining cost-effectiveness through the use of readily available materials

Inventive Principle:
Principle #31Porous materials

Solution Approach 2:

The surface area and porosity parameters of the solid support are optimized to achieve high uptake rates without requiring expensive synthesis procedures, balancing performance with manufacturability

Inventive Principle:
Principle #35Parameter changes

7Productivity

If porous support materials are used for CO2 capture, then gas absorption surface area is increased, but stability over time decreases due to degradation

Engineering Contradiction:
Improvegas absorption performanceVSAvoidstability over time
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The chemical composition and structural parameters of the solid support are selected to be chemically stable and resistant to degradation from contaminants and moisture, ensuring long-term stability while maintaining high gas absorption surface area

Inventive Principle:
Principle #35Parameter changes

8Quantity of substance

If liquid ionic liquids are used for CO2 absorption, then absorption capacity is improved, but viscosity increases which limits uptake kinetics

Engineering Contradiction:
Improveabsorption capacityVSAvoiduptake kinetics
Core Design Contradiction:
Quantity of substanceVSProductivity

Solution Approach 1:

The viscous liquid ionic liquid is segmented into discrete solid support particles, which reduces the effective viscosity experienced by CO2 molecules during diffusion and improves uptake kinetics while maintaining high absorption capacity

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Porous solid supports provide pathways for CO2 diffusion through the ionic liquid, reducing the impact of high viscosity on uptake kinetics while maintaining the high absorption capacity of the ionic liquid

Inventive Principle:
Principle #31Porous materials

9Reliability

If rigid non-swellable porous supports are used for CO2 capture, then leaching is reduced, but gas diffusion pathways are limited

Engineering Contradiction:
Improveresistance to leachingVSAvoidgas diffusion rate
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

Swellable porous supports are used instead of rigid non-swellable supports, allowing the pore structure to dynamically adjust and expand to facilitate gas diffusion while maintaining resistance to leaching through the swellable matrix structure

Inventive Principle:
Principle #15Dynamics

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 acidic gas absorbent particulates demonstrate increased absorption capacity, improved recyclability, reduced amine-solvent volatility, and robustness in humid environments, offering a scalable and efficient solution for industrial gas capture.

Implementation Method 1

The acidic gas absorbent particulates can be used for removing one or more acidic gases from a gaseous stream or atmosphere by absorbing the acidic gas

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Implementation Method 2

liquid-based sorbents that are employed typically comprise groups that chemically react with the acidic gas which can capture CO2 from gaseous streams

Methodology Applied
Scientific EffectChemical reaction: Chemical Bonding

Implementation Method 3

an acidic gas absorbent particulate comprising swellable support particles and an amine-functionalised ionic liquid absorbed within the swellable support particles

Methodology Applied
Scientific EffectAbsorption: Absorption (physical)

Implementation Method 4

the acidic gas diffusion distance being significantly reduced allowing for enhanced sorbent uptake kinetics/efficiency

Methodology Applied
Scientific EffectDiffusion: Diffusion

Implementation Method 5

The absorbed acidic gas can then be harvested (e.g. desorbed) from the absorbent, which is regenerated and can be reused

Methodology Applied
Scientific EffectDesorption: Desorption

Data Source

PatentUS20250312730A1Acidic gas absorbents comprising ionic liquids
Publication Date: 2025.10.09 COMMONWEALTH SCI & IND RES ORG
  • US20250312730A1 patent drawing
  • US20250312730A1 patent drawing
  • US20250312730A1 patent drawing

AI summary

The present disclosure is directed to an acidic gas absorbent particulate for capture of an acidic gas from a gaseous stream or atmosphere, the acidic gas absorbent particulate comprising swellable support particles, wherein the swellable support particles contain absorbed amine-functionalised ionic liquid for absorbing the acidic gas, and to apparatuses, processes, methods and uses comprising the same.