ZIF-8 and ZIF-67 as catalysts for promoting carbon dioxide capture based on monoethanolamine solution

IF 8.1 1区 工程技术 Q1 ENGINEERING, CHEMICAL Separation and Purification Technology Pub Date : 2024-11-10 DOI:10.1016/j.seppur.2024.130389
Sihan Ai, Yong Xiang, Xue Chen, Yanlin Zhang, Yufei Zhang, Kangning Lv, Xin Chen, Daoyong Yu, Baosheng Ge, Fang Huang
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Abstract

Carbon dioxide capture, utilization and storage (CCUS) technology is considered an effective solution to achieve carbon neutrality. In CCUS, chemical absorption stands out as an efficient CO2 capture method suitable for environments with low CO2 partial pressures. This study aims to enhance the CO2 capture performance of monoethanolamine (MEA) solution by employing zeolitic imidazolate frameworks ZIF-8 and ZIF-67 as catalysts. The impacts of catalyst concentration and experimental temperature on the quantity, rate of absorption, rate of desorption, and reusability of MEA for CO2 absorption were investigated. Changes in the volume concentration of CO2 in the mixed gas were monitored to assess these parameters. The results demonstrated that at a catalyst concentration of 150 mg/mL for ZIF-8 and 125 mg/mL for ZIF-67, MEA achieved CO2 absorption quantity of 22.22 % and 18.89 %, respectively. This corresponded to substantial increases of 63.39 % and 125.9 % in the CO2 maximum absorption rate of MEA solution. While the maximum desorption rate of MEA was enhanced by 130.1 % and 148.2 %. In conclusion, the introduction of ZIF-8 and ZIF-67 catalysts effectively catalyzed the CO2 capture process, significantly enhancing the CO2 capture quantity of MEA and ensuring energy-efficient regeneration of MEA. This study provides a novel approach for improving the performance of MEA in terms of capturing CO2.

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基于单乙醇胺溶液的促进二氧化碳捕集的催化剂 ZIF-8 和 ZIF-67
二氧化碳捕集、利用和封存(CCUS)技术被认为是实现碳中和的有效解决方案。在 CCUS 技术中,化学吸收是一种高效的二氧化碳捕集方法,适用于二氧化碳分压较低的环境。本研究旨在采用沸石咪唑啉框架 ZIF-8 和 ZIF-67 作为催化剂,提高单乙醇胺(MEA)溶液的二氧化碳捕集性能。研究了催化剂浓度和实验温度对 MEA 吸收二氧化碳的数量、吸收率、解吸率和重复利用率的影响。通过监测混合气体中二氧化碳体积浓度的变化来评估这些参数。结果表明,当 ZIF-8 的催化剂浓度为 150 毫克/毫升、ZIF-67 的催化剂浓度为 125 毫克/毫升时,MEA 的二氧化碳吸收率分别为 22.22% 和 18.89%。这意味着 MEA 溶液的二氧化碳最大吸收率分别大幅提高了 63.39 % 和 125.9 %。而 MEA 的最大解吸率则分别提高了 130.1 % 和 148.2 %。总之,ZIF-8 和 ZIF-67 催化剂的引入有效催化了二氧化碳捕集过程,显著提高了 MEA 的二氧化碳捕集量,确保了 MEA 的节能再生。这项研究为提高 MEA 捕集二氧化碳的性能提供了一种新方法。
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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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