Deciphering the transfer mechanisms for CO2 absorption into binary blended solutions

IF 9.7 1区 环境科学与生态学 Q1 ENGINEERING, ENVIRONMENTAL Journal of Cleaner Production Pub Date : 2024-09-02 DOI:10.1016/j.jclepro.2024.143535
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Abstract

A thorough understanding of the mechanisms involved in CO2 chemical absorption is crucial for the development of efficient CO2 capture technologies. Due to the insufficient insight into the interaction mechanism of different components in blended solutions, CO2 absorption reactions were often categorized as unidirectional transfer between absorption products. In this study, the CO2 absorption performance of binary blended solutions, including piperazine (PZ)/n-methyldiethanolamine (MDEA), ethanolamine (MEA)/MDEA, ammonia (NH3)/MDEA, PZ/potassium carbonate (K2CO3), and NH3/K2CO3, was investigated using a combination of experimental and computational methods. The CO2 absorption mechanisms of “competitive reaction”, “transfer reaction” and “parallel reaction” in the binary blended solution system were proposed. Kinetic experiments revealed that different blended solutions had varying impacts on the process of CO2 absorption. Among them, PZ/MDEA and MEA/MDEA solutions reduced the absorption rates by an average of 8% and 25%, respectively, compared to PZ or MEA component solutions. NH3/MDEA and PZ/K2CO3 solutions had absorption rates similar to those of single NH3/PZ component solutions. NH3/K2CO3 solutions, on the other hand, exhibited an average increase of 17% in absorption rates compared to NH3 solutions. Quantum mechanical (QM) methods were employed to evaluate of the absorption products and key processes in terms of kinetics and thermodynamics. Quantitative 13C NMR analyses were conducted to further investigate the interactions between components and the pathways of mass transport in blended solutions, which demonstrated proton transfer and CO2/-COO transfer between adsorption products. This study highlights an accurate description of the transfer mechanisms of various blended systems for the enhanced CO2 capture.

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破解二元混合溶液吸收二氧化碳的转移机制
透彻了解一氧化碳化学吸收的机理对于开发高效的一氧化碳捕获技术至关重要。由于对混合溶液中不同成分的相互作用机理了解不够,CO 吸收反应通常被归类为吸收产物之间的单向转移。本研究采用实验和计算相结合的方法,研究了哌嗪(PZ)/正甲基二乙醇胺(MDEA)、乙醇胺(MEA)/MDEA、氨(NH)/MDEA、PZ/碳酸钾(KCO)和 NH/KCO 等二元混合溶液的 CO 吸收性能。提出了二元混合溶液体系中 "竞争反应"、"转移反应 "和 "平行反应 "的 CO 吸收机理。动力学实验表明,不同的混合溶液对 CO 吸收过程有不同的影响。其中,PZ/MDEA 和 MEA/MDEA 溶液与 PZ 或 MEA 组分溶液相比,吸收率平均分别降低了 8%和 25%。NH/MDEA 和 PZ/KCO 溶液的吸收率与单一 NH/PZ 组分溶液相似。另一方面,与 NH 溶液相比,NH/KCO 溶液的吸收率平均提高了 17%。我们采用量子力学(QM)方法从动力学和热力学角度对吸收产物和关键过程进行了评估。定量 C NMR 分析进一步研究了混合溶液中各组分之间的相互作用和质量传输途径,结果表明吸附产物之间存在质子传输和 CO/COO 传输。这项研究突出强调了对各种混合系统的传输机制的准确描述,以增强对 CO 的捕获。
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来源期刊
Journal of Cleaner Production
Journal of Cleaner Production 环境科学-工程:环境
CiteScore
20.40
自引率
9.00%
发文量
4720
审稿时长
111 days
期刊介绍: The Journal of Cleaner Production is an international, transdisciplinary journal that addresses and discusses theoretical and practical Cleaner Production, Environmental, and Sustainability issues. It aims to help societies become more sustainable by focusing on the concept of 'Cleaner Production', which aims at preventing waste production and increasing efficiencies in energy, water, resources, and human capital use. The journal serves as a platform for corporations, governments, education institutions, regions, and societies to engage in discussions and research related to Cleaner Production, environmental, and sustainability practices.
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