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A new method of amine solvent recovery with acid addition for energy reduction in the CO2 absorption process

Authors
Lee, Hyun SeungLee, Na RiYang, Dae Ryook
Issue Date
12월-2013
Publisher
INST CHEMICAL ENGINEERS
Keywords
CO2 capture; MEA; Absorption and Stripping process; Acid addition; Amine recovery
Citation
CHEMICAL ENGINEERING RESEARCH & DESIGN, v.91, no.12, pp.2630 - 2638
Indexed
SCIE
SCOPUS
Journal Title
CHEMICAL ENGINEERING RESEARCH & DESIGN
Volume
91
Number
12
Start Page
2630
End Page
2638
URI
https://scholar.korea.ac.kr/handle/2021.sw.korea/101374
DOI
10.1016/j.cherd.2013.05.030
ISSN
0263-8762
Abstract
Chemical absorption/stripping technologies using an amine-based solvent have a lot of advantages for capturing carbon dioxide in post-combustion capture system. However, the higher energy demand for the solvent recovery makes the technology difficult to retrofit to existing plants. To overcome this obstacle, an alternative stripping process using an organic acid was studied to decrease the solubility of carbon dioxide and save the energy demand, but further research is necessary to recover the amine solvent and an organic acid effectively. In this study, a new amine recovery method using an organic acid is proposed and the method suggests a two-step of reaction crystallization process to separate the amine and the acid. This study demonstrates that an amine solvent (monoethanolamine, MEA) and an organic acid (oxalic acid) could be recycled effectively by reaction crystallization experiment. MEA and oxalic acid recovery efficiencies were also obtained using the experimental data in this study. The percentages of MEA recovery and the acid losses were estimated through these data. In addition, the energy demands for two recovery processes were estimated. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
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