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Hybrid membrane-cryogenic CO2 capture technologies: A mini-review

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FRONTIERS IN ENERGY RESEARCH
卷 11, 期 -, 页码 -

出版社

FRONTIERS MEDIA SA
DOI: 10.3389/fenrg.2023.1167024

关键词

carbon capture; hybrid membrane cryogenic process; low temperature membrane cryogenic process; energy consumption; CO2 capture ratio; CO2/N-2 selectivity

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The use of membranes for CO2 capture is an effective and low-cost technique due to its compact size, energy efficiency, and ease of handling. Hybrid membrane cryogenic (HMC) and low-temperature membrane cryogenic (LTMC) systems combine the advantages of membrane and cryogenic techniques. The performance of the membrane is influenced by permeability, selectivity, and operating temperatures. This review analyzes the costs, energy requirements, and membrane parameters of various HMC and LTMC configurations for CO2 capture.
The use of membranes to capture CO2 is a proven carbon capture technique. Gas separation membranes enhance the mole fraction of CO2 in the feed gas. The membrane separation technique is low-cost because of its compact size, excellent energy efficiency, minimum environmental effect, simplicity of scale-up, fewer moving parts, moderate energy consumption, and ease of handling. Hybrid membrane cryogenic (HMC) and low-temperature membrane cryogenic (LTMC) are hybrid capture systems that combine the advantages of membrane and cryogenic techniques. In the HMC process, the flue gas is first pre-treated by the membrane process for CO2 enrichment and the cryogenic process to capture the CO2. In the LTMC process, low-temperature membrane units increase flue gas CO2 concentration to 50%-75%, and a cryogenic process liquefies the rich CO2 stream. Permeability and selectivity are the crucial parameters of the membrane which determine the CO2 purity and recovery of capture. Most polymeric membranes have a trade-off of CO2/N-2 selectivity (a(CO2/N2)) and CO2 permeability (P-CO2). The operating temperatures also impact membrane performance. An anti-trade-off effect was observed upon cooling down by increasing P-CO2 and a(CO2/N2). With increased P-CO2 and a(CO2/N2), sub-ambient temperature-based membrane cryogenic CO2 capture techniques will lower power consumption and energy cost for CO2 capture (CC). This review analyses the costs and energy requirements of various HMC and LTMC configurations for CO2 capture. The study also examines the features of the different membranes used and the effect of operating and membrane parameters on the process performance.

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