CO2 Separation Membrane with Amine-Functionalized Layer
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Solution Overview
Problem
Current CO2 separation membranes face limitations in both CO2 selectivity and permeability, leading to high energy consumption and operational costs, making them unsuitable for commercial use in heavy industries like cement and steelmaking.
Innovation Solution
A CO2 separation membrane design featuring a CO2-philic layer with mobile and immobile amine-based carriers, combined with a CO2-permeable layer, enhances both selectivity and permeability through a hybrid structure that includes nanostructures and crosslinking, allowing for improved gas transport and reduced manufacturing challenges.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If conventional membrane materials (perfluoropolymers, thermally arranged polymers, iptycene-containing polymers) are used to achieve high CO2 permeability, then CO2 permeability is improved, but CO2 selectivity deteriorates
Solution Approach 1:
The patent employs composite materials by combining perfluorinated polymer matrix with amine-functionalized polymer coatings and porous metal oxide nanoparticles. This composite structure allows the base polymer to provide high permeability while the functionalized layers provide selectivity through chemical interaction with CO2, resolving the trade-off between permeability and selectivity.
Solution Approach 2:
The patent applies local quality by creating a gradient structure where the bulk polymer matrix maintains high permeability properties while the surface and near-surface regions contain concentrated amine functional groups and porous metal oxides that provide selective CO2 interaction. This spatial differentiation of functional properties allows simultaneous optimization of permeability and selectivity.
2Manufacturing precision
If amine-functionalized materials (polyvinylamine, polyethyleneimine, polyallylamine) are used to improve CO2 selectivity, then CO2 selectivity is improved, but CO2 permeability deteriorates
Solution Approach 1:
The patent changes the physical and chemical parameters of amine-functionalized materials by controlling the degree of functionalization, polymer chain length, and molecular weight. By optimizing these parameters, the material achieves sufficient CO2 selectivity through chemical interaction while maintaining adequate permeability through controlled functional group density and mobility.
Solution Approach 2:
The patent incorporates porous metal oxide nanoparticles (such as alumina, silica, or titania) into the amine-functionalized polymer matrix. These porous structures provide additional CO2 transport pathways that are not blocked by amine functional groups, thereby maintaining permeability while the amine groups provide selectivity through chemical interaction.
3Productivity
If adsorption or absorption processes are used for CO2 capture, then CO2 capture capacity is improved, but energy consumption and operational costs increase
Solution Approach 1:
The patent replaces the mechanical/thermal processes of adsorption and absorption with a membrane-based separation process that operates at lower energy levels. The membrane process uses intrinsic material properties (permeability and selectivity) to separate CO2 from other gases, eliminating the need for energy-intensive heating, pressurization, or chemical solvent regeneration required by conventional methods.
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 membrane achieves high CO2/N2 selectivity and permeance, reducing energy consumption and operational costs, making it suitable for commercial-scale CO2 capture in industrial settings.
Implementation Method 1
CO2 transportation within polymeric membranes is usually through solution-diffusion, which depends on the polymer material's intrinsic properties
Implementation Method 2
water adsorption nanostructures
Data Source
AI summary
A CO2 separation membrane can include a CO2-philic layer comprising one or more mobile CO2 carriers and one or more immobile CO2 carriers and a blended CO2-permeable and CO2-selective matrix that hosts the immobile or mobile CO2 carriers and porous nanostructures that adsorb water vapors. The CO2-philic layer can be disposed upstream of the CO2-permeance layer such that a flow of source gas to be separate enters the membrane from a feed side at which the CO2-philic layer is present and CO2 exits the membrane at a permeate side after passing through both the CO2-philic layer and the CO2-permeance layer.


