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An investigation of the role of N-methyl-diethanolamine in non-aqueous solution for CO2 capture process using C-13 NMR spectroscopy
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Indexed by:Journal Papers

Date of Publication:2015-08-01

Journal:INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL

Included Journals:EI、SCIE、Scopus

Volume:39

Page Number:166-173

ISSN No.:1750-5836

Key Words:N-Methyl-diethanolamine; N-Ethylmonoethanolamine; Non-aqueous solution; VLE; Absorption-desorption

Abstract:CO2 absorption (at 313 K) and desorption (at 363 K) in 15 wt%N-methyl-diethanolamine (MDEA) + 25 wt% N-ethylmonoethanolamine (EMEA) + 60 wt% ethanol and 25 wt% EMEA + 75 wt% ethanol were investigated in order to determine the role of MDEA in non-aqueous solution for CO2 absorption and EMEA regeneration. The equilibrium solubility of CO2 in 15 wt% MDEA+EMEA+ ethanol with different EMEA concentrations (0-25 wt%) was studied in a vapor-liquid equilibrium (VLE) apparatus at 313 K to investigate the effect of the concentration of MDEA and EMEA on the CO2 capture ability in different pressure ranges. The experimental results indicated that the presence of MDEA in EMEA+ethanol can slightly improve the capacity of CO2 due to the deprotonation of EMEA(+)COO(-) by MDEA; however, it did not contribute to the improvement of the EMEA regeneration efficiency. The equilibrium solubility of CO2 increased with increasing EMEA concentration below 150 kPa, however, at higher pressure the solution with low EMEA concentration seems to be more beneficial for CO2 scrubbing. Results of C-13 NMR and H-1-C-13 HMBC spectroscopy confirmed that the carbon containing species after CO2 absorption in MDEA+ EMEA+ ethanol and EMEA+ ethanol solutions originated from the carboxylation reaction of EMEA and ethanol. (C) 2015 Elsevier Ltd. All rights reserved.

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Senior Engineer

Gender:Male

Alma Mater:大连理工大学

Degree:Doctoral Degree

School/Department:化工学院

Discipline:Industrial Catalysis. Chemical Technology

Business Address:大连理工大学西部校区化工实验楼B219

Contact Information:高新区凌工路2号大连理工西校区化工实验楼B219 Tel:0411-84986322

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