采用离子液体吸收促进剂和沸石分子筛解吸催化剂,推进有机胺溶液的高效CO2捕集

IF 9 1区 工程技术 Q1 ENGINEERING, CHEMICAL Separation and Purification Technology Pub Date : 2025-08-14 Epub Date: 2025-02-21 DOI:10.1016/j.seppur.2025.132094
Hang Liu , Yupeng Xing , Dongya Zhao , Shijian Lu , Yurong Chen , Shizhang Cui , Xinwang Song
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引用次数: 0

摘要

烷醇胺溶液因其低成本和稳定的性能而被广泛用于二氧化碳捕集。然而,其固有的结构限制导致了重大挑战,例如低二氧化碳吸收-解吸能力和高能量再生需求。为了解决这些问题,本研究提出了一种高效的CO2捕获系统,该系统采用2-(2-氨基乙胺)乙醇(AEEA)作为其性能稳定的主要吸附剂,通过一步法合成的氨基功能化离子液体(AIL)作为吸收促进剂,并采用适量的固体酸催化剂(SAC)作为脱附催化剂。实验结果表明,由20 wt% AEEA(一次吸附剂)、10 wt% [DETAH][Pz](吸收促进剂)和0.1 wt% HZSM-5(脱附催化剂)组成的复合体系为最佳构型。系统对新鲜溶液的CO2吸收量为0.50172 g CO2/g amine,经过5次再生循环后,CO2吸收量降至0.42619 g CO2/g amine,保持了原始吸收量的84.95 %。与MEA/水系统相比,脱附率超过85 %,再生能耗降低30.22 %。值得注意的是,HZSM-5(21)催化剂的加入在最初的20 min内显著增强了CO2的解吸过程。与非催化体系相比,脱附量提高了62.78 %,平均脱附率提高了40.85 %,峰值脱附率提高了31.94 %,实现了更高效、完整的CO2脱附过程。13C NMR分析表明,AEEA与[DETAH][Pz]之间的协同吸收效应显著提高了体系对CO2的吸收能力。同时,HZSM-5(21)分子筛上的Brønsted和Lewis酸位点与[Pz]-H一起有效地促进了氨基甲酸酯的分解,从而催化了CO2的脱附过程。
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Advancing energy-efficient CO2 capture with organic amine solutions using ionic liquid absorption promoters and zeolite molecular sieve desorption catalysts
Alkanolamine solutions have been widely used for CO2 capture due to their low cost and stable performance. However, their inherent structural limitations led to significant challenges, such as low CO2 absorption–desorption capacity and high energy demands for regeneration. To address these issues, this work proposes an efficient CO2 capture system that employs 2-(2-aminoethylamino)ethanol (AEEA) as the primary absorbent due to its stable performance, amino-functionalized ionic liquid (AIL) synthesized via a one-step method as absorption promoters, and an appropriate amount of solid acid catalyst (SAC) as desorption catalysts. The experimental results demonstrated that the composite system comprising 20 wt% AEEA (primary absorbent), 10 wt% [DETAH][Pz] (absorption promoter), and 0.1 wt% HZSM-5 (desorption catalyst) represents the optimal configuration. The system achieved a CO2 absorption capacity of 0.50172 g CO2/g amine for the fresh solution, which decreased to 0.42619 g CO2/g amine after five regeneration cycles, maintaining 84.95 % of the original capacity. The desorption ratio exceeded 85 %, while regeneration energy consumption was reduced by 30.22 % compared to the MEA/water system. Notably, the inclusion of the HZSM-5(21) catalyst significantly enhanced the CO2 desorption process during the initial 20 min. The desorption amount increased by 62.78 % relative to the non-catalytic system, the average desorption rate improved by 40.85 %, and the peak desorption rate rose by 31.94 %, resulting in a more efficient and complete CO2 desorption process. Analysis using 13C NMR demonstrated that the synergistic absorption effect between AEEA and [DETAH][Pz] significantly improved the CO2 absorption capacity of the system. Meanwhile, the Brønsted and Lewis acid sites on the HZSM-5(21) molecular sieve, along with [Pz]-H, effectively facilitated the decomposition of carbamates, thereby catalyzing the CO2 desorption process.
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来源期刊
Separation and Purification Technology
Separation and Purification Technology 工程技术-工程:化工
CiteScore
14.00
自引率
12.80%
发文量
2347
审稿时长
43 days
期刊介绍: Separation and Purification Technology is a premier journal committed to sharing innovative methods for separation and purification in chemical and environmental engineering, encompassing both homogeneous solutions and heterogeneous mixtures. Our scope includes the separation and/or purification of liquids, vapors, and gases, as well as carbon capture and separation techniques. However, it's important to note that methods solely intended for analytical purposes are not within the scope of the journal. Additionally, disciplines such as soil science, polymer science, and metallurgy fall outside the purview of Separation and Purification Technology. Join us in advancing the field of separation and purification methods for sustainable solutions in chemical and environmental engineering.
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