Enhanced carbon dioxide absorption using alcohol solvents in a microreactor: Comparison with MEA plus water mixture

被引:11
作者
Heidaryan, Ehsan [1 ]
Aghel, Babak [2 ,3 ]
Sahraie, Sasan [3 ]
Maleki, Mahmoud [3 ]
机构
[1] Univ Wyoming, Dept Chem & Biomed Engn, Laramie, WY 82071 USA
[2] Tech Univ Darmstadt, Inst Energy Syst & Technol, Darmstadt, Germany
[3] Kermanshah Univ Technol, Fac Energy, Dept Chem Engn, Kermanshah, Iran
关键词
Carbon dioxide absorption; Microreactor; Physical solvent; Monoethanolamine; MASS-TRANSFER CHARACTERISTICS; LIQUID 2-PHASE FLOW; CO2; ABSORPTION; N-METHYLDIETHANOLAMINE; AQUEOUS-SOLUTIONS; MICROCHANNELS; DESORPTION; CAPTURE; DIETHANOLAMINE; SOLUBILITIES;
D O I
10.1016/j.jtice.2023.105105
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Background: Carbon dioxide absorption using solvents is a critical process in mitigating greenhouse gas emis-sions. The monoethanolamine (MEA) + water (30 wt.%) mixture is the most commonly used solvent, but alternative solvents with better performance are desired.Methods: This study investigated the effects of temperature, solvent flow rate, and gas flow rate on carbon dioxide absorption and liquid-side volumetric mass transfer coefficient in a microreactor using various solvents. The performance of the tested solvents was compared to the MEA + water (30 wt.%) mixture.Significant findings: Ethylene glycol achieved the highest absorption (91.57%) at 15 degrees C, with a solvent flow rate of 0.05 l.min � 1 and a gas flow rate of 1 l.min � 1. The maximum klav value of 18.2 s-1 was reached at 15 degrees C, with a solvent flow rate of 0.01 l.min � 1 and a gas flow rate of 1 l.min � 1. This value was 1.3 times higher than that of the MEA + water (30 wt.%) mixture under similar conditions, indicating the potential to replace glycolytic solvents with amine-based solvents in carbon dioxide absorption applications.
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页数:13
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