CO2 gas-liquid equilibrium study and machine learning analysis in MEA-DMEA blended amine solutions

The combination of primary and tertiary amines represents a promising approach to improve sorbent performance in CO 2 capture by enhancing absorption efficiency and reducing regeneration energy. This study focuses on investigating the absorption performance of binary mixtures of ethanolamine (MEA) and N,N-dimethylethanolamine (DMEA) at temperatures between 298–323 K and CO 2 partial pressures between 5–60 kPa. The species generated during the absorption were analyzed using 13 C NMR spectroscopy, to clarify the intricate role of MEA and DMEA in the capture process. A developed excess property model for DEA-DMEA, based on excess CO 2 loading, predicted equilibrium CO 2 solubility data with an average absolute relative deviation (AARD) of 1.6 %. Additionally, the machine learning models XGBoost, RBFNN, and SVR were applied, providing AARD values between 0.86 % and 1.28 %, demonstrating strong agreement between experimental and predicted outcomes. These comprehensive findings enhance our understanding of mixed amines’ mechanisms and practical applications, contributing to ongoing research development.

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Publication Details

Journal
Separation and Purification Technology
Published
2024-10-06
DOI
https://doi.org/10.1016/j.seppur.2024.130024
Citations
20
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
Field-Weighted Citation Impact
4.25

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article

CO2 gas-liquid equilibrium study and machine learning analysis in MEA-DMEA blended amine solutions

Min Xiao, Xin Zhou, Chao’en Li, Francesco Barzagli et al.
20 citations
Separation and Purification Technology
Carbon Dioxide Capture Technologies
4.25
article

CO2 gas-liquid equilibrium study and machine learning analysis in MEA-DMEA blended amine solutions

Min Xiao, Xin Zhou, Chao’en Li, Francesco Barzagli, Rui Zhang, Haonan Liu, Li Luo, Jiaofei Geng
article en
20 citations

Abstract

The combination of primary and tertiary amines represents a promising approach to improve sorbent performance in CO 2 capture by enhancing absorption efficiency and reducing regeneration energy. This study focuses on investigating the absorption performance of binary mixtures of ethanolamine (MEA) and N,N-dimethylethanolamine (DMEA) at temperatures between 298–323 K and CO 2 partial pressures between 5–60 kPa. The species generated during the absorption were analyzed using 13 C NMR spectroscopy, to clarify the intricate role of MEA and DMEA in the capture process. A developed excess property model for DEA-DMEA, based on excess CO 2 loading, predicted equilibrium CO 2 solubility data with an average absolute relative deviation (AARD) of 1.6 %. Additionally, the machine learning models XGBoost, RBFNN, and SVR were applied, providing AARD values between 0.86 % and 1.28 %, demonstrating strong agreement between experimental and predicted outcomes. These comprehensive findings enhance our understanding of mixed amines’ mechanisms and practical applications, contributing to ongoing research development.

Separation and Purification TechnologyVol. 356
Commonwealth Scientific and Industrial Research Organisation (AU), Hunan University (CN), Institute for the Chemistry of OrganoMetallic Compounds (IT), Xiangtan University (CN)
National Natural Science Foundation of China, Natural Science Foundation of Hunan Province
Openalex Percentile: Top 5%
Carbon Dioxide Capture Technologies
4.25
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