Computational Investigation of Co-Solvent Influence on CO2 Absorption and Diffusion in Water Lean Solvents

被引:2
作者
Sharif, Maimoona [1 ]
Ge, Chunliang [2 ]
Wang, Tao [1 ]
Zhang, Wei [2 ]
Fang, Mengxiang [1 ]
Gao, Xiang [1 ]
机构
[1] Zhejiang Univ, State Key Lab Clean Energy Utilizat, Hangzhou 310027, Peoples R China
[2] Zhejiang Zheneng Technol & Environm Grp Co Ltd, Hangzhou 310003, Peoples R China
基金
国家重点研发计划;
关键词
water-lean solvent; CO2; capture; molecular dynamic simulation; co-solvent; CARBON-DIOXIDE; NONAQUEOUS SOLUTIONS; CAPTURE; ABSORBENTS; ALKANOLAMINES; 2-BUTOXYETHANOL; SOLUBILITY; MIXTURES; KINETICS; AMINES;
D O I
10.3390/pr12081588
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The present research explores water-lean amine-based solvents to enhance carbon capture and provide sustainable solutions for CO2 emissions challenges. A computational approach is employed to evaluate the co-solvent's impact on CO2 capture in MDEA-based systems. The performance of the following systems is examined: MDEA-NMP, MDEA-MAE-NMP, MDEA-MeOH, MDEA-MAE-MeOH, MDEA-EG, MDEA-MAE-EG, and MDEA-MAE with varying water concentrations. The Radial Distribution Function (RDF) analysis revealed significant interactions between amine groups, CO2, and water molecules in each system. The results indicate that the MDEA-NMP (40% H2O) and MDEA-EG (40% H2O) systems had strong interactions, indicating their potential for CO2 capture. However, adding MAE decreased interaction intensities, indicating a less favorable performance. Complementing the RDF findings, the Mean Square Displacement (MSD) analysis quantified CO2 diffusivity across temperatures (313 K, 323 K, and 333 K). MDEA-NMP (40% H2O) demonstrated the highest diffusivity, indicating superior CO2 mobility and capture efficiency. MDEA-MeOH (40% H2O) also showed moderate diffusivity, further supporting its effectiveness. However, solvent systems incorporating MAE consistently displayed lower diffusivity, reinforcing the observation from the RDF analysis. The temperature effect on the diffusivity of selected blends does not follow the regular pattern in a co-solvent-based system, whereas in an aqueous system, it increases with temperature. These molecular dynamic simulations highlight the critical role of solvent composition in optimizing CO2 capture efficiency. Applying these insights can improve solvent formulations, enhance effectiveness, and reduce costs.
引用
收藏
页数:19
相关论文
共 58 条
[1]   PHYSICOCHEMICAL PROPERTIES IMPORTANT FOR CARBON-DIOXIDE ABSORPTION IN AQUEOUS METHYLDIETHANOLAMINE [J].
ALGHAWAS, HA ;
HAGEWIESCHE, DP ;
RUIZIBANEZ, G ;
SANDALL, OC .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1989, 34 (04) :385-391
[2]   Performance of non-aqueous amine hybrid solvents mixtures for CO2 capture: A study using a molecular-based model [J].
Alkhatib, Ismail I. I. ;
Pereira, Luis M. C. ;
AlHajaj, Ahmed ;
Vega, Lourdes F. .
JOURNAL OF CO2 UTILIZATION, 2020, 35 :126-144
[3]  
Allen M P, 2017, Computer Simulation of Liquids, V2, DOI [10.1093/oso/9780198803195.001.0001, DOI 10.1093/OSO/9780198803195.001.0001]
[4]   A Comparative Study of the CO2 Absorption in Some Solvent-Free Alkanolamines and in Aqueous Monoethanolamine (MEA) [J].
Barzagli, Francesco ;
Mani, Fabrizio ;
Peruzzini, Maurizio .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2016, 50 (13) :7239-7246
[5]  
Biovia, 2019, Material Studio
[6]  
Chemspider, 2020, Royal Society of Chemistry Database
[7]   CO2 desorption via microwave heating for post-combustion carbon capture [J].
Chronopoulos, Theo ;
Fernandez-Diez, Yolanda ;
Maroto-Valer, M. Mercedes ;
Ocone, Raffaella ;
Reay, David A. .
MICROPOROUS AND MESOPOROUS MATERIALS, 2014, 197 :288-290
[8]  
Desai B.H., 2020, Yearb. Int. Environ. Law, V31, P319
[9]   Aqueous amine solution characterization for post-combustion CO2 capture process [J].
El Hadri, Nabil ;
Dang Viet Quang ;
Goetheer, Earl L. V. ;
Abu Zahra, Mohammad R. M. .
APPLIED ENERGY, 2017, 185 :1433-1449
[10]   Life cycle cost analysis of power generation from underground coal gasification with carbon capture and storage (CCS) to measure the economic feasibility [J].
Feng, Ye ;
Chen, Jinglong ;
Luo, Ji .
RESOURCES POLICY, 2024, 92