A Novel Phase Change Absorbent for CO2 Capture with Low Viscosity and Effective Absorption–Desorption Properties

IF 3.6 4区 工程技术 Q3 ENERGY & FUELS
Jianchao Han, Zihan Qiu, Yuyan Chen, Xia Gui, Xiao Chen
{"title":"A Novel Phase Change Absorbent for CO2 Capture with Low Viscosity and Effective Absorption–Desorption Properties","authors":"Jianchao Han,&nbsp;Zihan Qiu,&nbsp;Yuyan Chen,&nbsp;Xia Gui,&nbsp;Xiao Chen","doi":"10.1002/ente.202400114","DOIUrl":null,"url":null,"abstract":"<p>Excessive carbon dioxide (CO<sub>2</sub>) emissions can lead to environmental problems, and the use of phase change absorbents for CO<sub>2</sub> capture has received much attention due to their excellent absorption and desorption properties. Herein, a novel liquid–liquid phase change absorbent consisting of N-aminoethylpiperazine (AEP), diethylene glycol dimethyl ether (DEGDME), and H<sub>2</sub>O is utilized. Under the optimal absorption conditions, the absorption capacity is 1.23 mol CO<sub>2</sub>·mol<sup>−1</sup> amine. The rich-phase viscosity of the AEP/DEGDME/H<sub>2</sub>O solution is only 6.2 mPa s<sup>−1</sup>, and the rich phase-to-volume ratio is 52.7%, which is suitable for industrial applications. After five cycles of absorption–desorption experiments, the cyclic capacity reaches 0.62 mol CO<sub>2</sub>·mol<sup>−1</sup> amine. However, it should be noted that this leads to an increase in the viscosity of the solution with time. The <sup>13</sup>C Nuclear Magnetic Resonance characterization is used to analyze the material distribution and phase separation mechanism, and it is found that during the absorption process, the carbamate and carbonate products generated by the reaction of the amino group in the AEP with CO<sub>2</sub> are mainly located in the rich phase, while the DEGDME and H<sub>2</sub>O mainly remain in the lean phase. In the desorption process, most of the absorbed products are decomposed, and the regeneration efficiency is 66.8%. Through the regeneration energy consumption experiment, when the regeneration efficiency is 56%–67%, the total regeneration energy consumption is 2.71–2.89 GJ t<sup>−1</sup> CO<sub>2</sub>, which is 0.91–1.09 GJ t<sup>−1</sup> CO<sub>2</sub> lower than that of the regeneration efficiency of 30 wt% MEA solution at 63%, which indicates that this absorbent has certain energy-saving advantages.</p>","PeriodicalId":11573,"journal":{"name":"Energy technology","volume":null,"pages":null},"PeriodicalIF":3.6000,"publicationDate":"2024-06-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Energy technology","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/ente.202400114","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0

Abstract

Excessive carbon dioxide (CO2) emissions can lead to environmental problems, and the use of phase change absorbents for CO2 capture has received much attention due to their excellent absorption and desorption properties. Herein, a novel liquid–liquid phase change absorbent consisting of N-aminoethylpiperazine (AEP), diethylene glycol dimethyl ether (DEGDME), and H2O is utilized. Under the optimal absorption conditions, the absorption capacity is 1.23 mol CO2·mol−1 amine. The rich-phase viscosity of the AEP/DEGDME/H2O solution is only 6.2 mPa s−1, and the rich phase-to-volume ratio is 52.7%, which is suitable for industrial applications. After five cycles of absorption–desorption experiments, the cyclic capacity reaches 0.62 mol CO2·mol−1 amine. However, it should be noted that this leads to an increase in the viscosity of the solution with time. The 13C Nuclear Magnetic Resonance characterization is used to analyze the material distribution and phase separation mechanism, and it is found that during the absorption process, the carbamate and carbonate products generated by the reaction of the amino group in the AEP with CO2 are mainly located in the rich phase, while the DEGDME and H2O mainly remain in the lean phase. In the desorption process, most of the absorbed products are decomposed, and the regeneration efficiency is 66.8%. Through the regeneration energy consumption experiment, when the regeneration efficiency is 56%–67%, the total regeneration energy consumption is 2.71–2.89 GJ t−1 CO2, which is 0.91–1.09 GJ t−1 CO2 lower than that of the regeneration efficiency of 30 wt% MEA solution at 63%, which indicates that this absorbent has certain energy-saving advantages.

一种具有低粘度和有效吸解特性的新型二氧化碳捕集相变吸收剂
过量的二氧化碳(CO2)排放会导致环境问题,而相变吸收剂因其优异的吸收和解吸特性,在二氧化碳捕获中的应用备受关注。本文利用一种由 N-氨基乙基哌嗪(AEP)、二乙二醇二甲醚(DEGDME)和 H2O 组成的新型液-液相变吸收剂。在最佳吸收条件下,吸收能力为 1.23 摩尔 CO2-摩尔-1胺。AEP/DEGDME/H2O 溶液的富相粘度仅为 6.2 mPa s-1,富相体积比为 52.7%,适合工业应用。经过五个循环的吸收-解吸实验后,循环容量达到 0.62 mol CO2-mol-1胺。但需要注意的是,这会导致溶液的粘度随着时间的推移而增加。利用 13C 核磁共振表征分析了物质分布和相分离机理,发现在吸收过程中,AEP 中氨基与 CO2 反应生成的氨基甲酸酯和碳酸盐产物主要位于富相,而 DEGDME 和 H2O 主要留在贫相。在解吸过程中,大部分吸收产物被分解,再生效率为 66.8%。通过再生能耗实验,当再生效率为 56%-67% 时,再生总能耗为 2.71-2.89 GJ t-1 CO2,比再生效率为 63% 的 30 wt% MEA 溶液低 0.91-1.09 GJ t-1 CO2,说明该吸收剂具有一定的节能优势。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
Energy technology
Energy technology ENERGY & FUELS-
CiteScore
7.00
自引率
5.30%
发文量
0
审稿时长
1.3 months
期刊介绍: Energy Technology provides a forum for researchers and engineers from all relevant disciplines concerned with the generation, conversion, storage, and distribution of energy. This new journal shall publish articles covering all technical aspects of energy process engineering from different perspectives, e.g., new concepts of energy generation and conversion; design, operation, control, and optimization of processes for energy generation (e.g., carbon capture) and conversion of energy carriers; improvement of existing processes; combination of single components to systems for energy generation; design of systems for energy storage; production processes of fuels, e.g., hydrogen, electricity, petroleum, biobased fuels; concepts and design of devices for energy distribution.
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信