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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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