Membrane Absorption CO2 Capture with Low Viscosity Solvent
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Solution Overview
Problem
Current CO2 capture technologies from power plant flue gases, such as amine absorption and membrane processes, face challenges in cost-effectiveness and long-term stability due to high levelized cost of energy and liquid side concentration polarization, which affects the efficiency and durability of the separation process.
Innovation Solution
A membrane absorption process using a CO2 selective solvent with viscosity between 0.2 and 7 cP, where the CO2-containing gas stream contacts one side of a membrane element and the solvent flows on the other side, allowing CO2 to permeate and be chemically absorbed, with a system including a desorber for solvent regeneration and return to the absorber to maintain efficiency and stability.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Quantity of substance
If conventional amine absorption is used for CO2 capture, then CO2 separation can be achieved, but the levelized cost of energy increases by 75-85%
Solution Approach 1:
The patent changes the physical parameter of solvent viscosity by selecting solvents with viscosity between 0.2 and 7 cP, which improves mass transfer characteristics and reduces the energy penalty associated with conventional amine absorption processes
Solution Approach 2:
The patent introduces a membrane contactor as an intermediary device between the gas phase and liquid solvent, facilitating CO2 transfer while reducing the overall energy requirement compared to direct contact absorption methods
2Quantity of substance
If membrane contactor systems are used for CO2 capture, then separation can be achieved, but liquid side concentration polarization affects long-term stability
Solution Approach 1:
The patent addresses concentration polarization by carefully selecting solvents with optimized viscosity parameters (0.2-7 cP) that maintain adequate mass transfer coefficients while preventing excessive concentration buildup at the membrane interface, thereby improving long-term operational stability
Solution Approach 2:
The patent replaces conventional high-viscosity amine solvents with low-viscosity CO2-selective solvents, fundamentally changing the fluid mechanics at the membrane interface to reduce concentration polarization effects and improve reliability
3Quantity of substance
If high viscosity solvent is used for CO2 absorption, then chemical absorption capacity increases, but mass transfer rate decreases due to concentration polarization
Solution Approach 1:
The patent optimizes the viscosity parameter of the absorption solvent to a specific range (0.2-7 cP) that balances CO2 absorption capacity with mass transfer rate, preventing concentration polarization while maintaining adequate chemical absorption capacity
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
This approach reduces concentration polarization, enhances CO2 capture rates, and improves the long-term stability and cost-effectiveness of the separation process by maintaining a stable CO2 removal rate and reducing fouling, while maintaining high selectivity and membrane lifetime.
Implementation Method 1
The CO2 permeates through the hollow fiber membrane pores and is chemically absorbed into the solvent
Implementation Method 2
The CO2 permeates through the hollow fiber membrane pores and is chemically absorbed into the solvent
Implementation Method 3
This approach reduces concentration polarization, enhances CO2 capture rates
Data Source
AI summary
Processes and systems for the capture of CO2 from a CO2-containing gas stream are provided. The CO2-containing gas stream is passed to a membrane contactor absorber wherein the CO2-containing gas contacts or passes a first side of a membrane element while a CO2 selective solvent with a viscosity between 0.2 and 7 cP contacts, passes or flows on second side of the membrane, opposed to the first side. The CO2 permeates through the hollow fiber membrane pores and is chemically absorbed into the solvent.


