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首页> 外文期刊>Chemical engineering journal >Catalytic activity of facilely synthesized mesoporous HZSM-5 catalysts for optimizing the CO2 desorption rate from CO2-rich amine solutions
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Catalytic activity of facilely synthesized mesoporous HZSM-5 catalysts for optimizing the CO2 desorption rate from CO2-rich amine solutions

机译:易于合成的介孔HZSM-5催化剂的催化活性,用于优化CO2富含胺溶液的二氧化碳解吸速率

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Post-combustion CO2 capture using aqueous alkanolamine solutions has a great potential to reduce anthropogenic CO2 emissions but the large-scale deployment of this technique is hindered due to a highly energy-intensive solvent regeneration mainly because of poor CO2 desorption kinetics. To overcome this limitation, we synthesized a series of mesoporous HZSM-5 catalysts through facile alkaline desilication and surfactant-induced re-assembly of dissolved species originating from the parent HZSM-5 crystals, and evaluated their performance to optimize the CO2 desorption rate from benchmark 30 wt% monoethanolamine (MEA) solution under mild temperature condition (40-82 degrees C). X-ray diffraction (XRD) patterns showed that the synthesized catalysts retained their crystallinity. Desilication by treatment in the alkaline medium led to a remarkable development of mesoporosity, with an increase in the Brunauer-Emmett-Teller (BET) surface area as well. The experimental results suggested that the synthesized catalysts significantly enhanced the CO2 desorption rate at low temperatures (up to 350-580% at <= 82 degrees C), improved the total amount of desorbed CO2 up to 60%, and minimized the heat duty by 24-37%. Detailed characterization revealed that the synergistic effect of higher mesoporosity and increased number of Lewis acid sites (LAS) and Bronsted acid sites (BAS) was crucial to improve the CO2 desorption rate. Based on the characterization and experimental results, a plausible reaction mechanism for catalyst aided CO2 desorption was also presented. This investigation highlights the role of catalysts in optimizing the CO2 capture process and presents new understanding for the design of high-performance catalysts for this purpose.
机译:使用链烷醇胺水溶液的燃烧后CO2捕获具有巨大的潜力来减少人为二氧化碳排放,但由于高能量 - 密集的溶剂再生,这种技术的大规模部署是由于差的CO2解吸动力学。为了克服这种限制,我们通过容易碱性溶解和表面活性剂诱导的溶解物种的重新组装成了一系列介孔HZSM-5催化剂,该系列的源于亲本HZSM-5晶体,并评估它们的性能,以优化来自基准的CO2解吸速率温度温度条件下30wt%单乙醇胺(MEA)溶液(40-82℃)。 X射线衍射(XRD)图案表明,合成催化剂保留了它们的结晶度。通过在碱性培养基中治疗的溶解导致了中间渗透性的显着发育,并且也增加了Brunauer-Emmett-Teller(BET)表面积。实验结果表明,合成催化剂在低温下显着提高了CO2解吸速率(在<= 82℃下高达350-580%),改善了解吸的CO 2的总量高达60%,并通过最小化了所述热量24-37%。详细表征揭示了较高的介体率和较高数量的路易斯酸性位点(LAS)和支架酸位点(BAS)的协同效应对于提高CO 2解吸速率至关重要。基于表征和实验结果,还提出了一种催化剂助催化CO2解吸的合理反应机理。本研究突出了催化剂在优化CO2捕获过程方面的作用,为此目的提供了高性能催化剂的设计。

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