{"title":"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","authors":"Jianchao Han, Zihan Qiu, Yuyan Chen, Xia Gui, 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":"{\"title\":\"A Novel Phase Change Absorbent for CO2 Capture with Low Viscosity and Effective Absorption–Desorption Properties\",\"authors\":\"Jianchao Han, Zihan Qiu, Yuyan Chen, Xia Gui, 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}","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}
A Novel Phase Change Absorbent for CO2 Capture with Low Viscosity and Effective Absorption–Desorption Properties
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.
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.