TY - GEN
T1 - Investigation of CO2 desorption performance in tri-solvent blends (MEA-AMP-PZ) with and without catalyst
AU - Zhang, Xiaowen
AU - Liu, Helei
AU - Liang, Zhiwu
N1 - Publisher Copyright:
Copyright © (2017) by AIChE. All rights reserved.
PY - 2017
Y1 - 2017
N2 - In this work, the regeneration characteristics of 6 M MEA-AMP-PZ (monoethanolamine, 2-amino-2-methyl-1-propanol and piperazine) tri-solvent blends with different AMP/PZ molar ratios with four different solid acid catalysts (H-ZSM-5, γ-Al2O3, SAPO-34 and SO4 2-/TiO2) and without catalyst at 369 K were studied in terms of CO2 desorption rate and heat duty and compared with conventional 5 M MEA. For the blank runs, the results showed that the tri-solvent blends of 3 M MEA-2.5 M AMP-0.5 M PZ performs a best CO2 desorption performance among all the tested amines, which reduced the heat duty by 51.9% as compared with 5 M MEA without catalyst (100%). With regard to catalyst, the best blend with H-ZSM-5 provided the combination with the greatest performance in CO2 desorption, which decreased the heat duty by 61.6% in comparison with 5 M MEA without catalyst. Based on the results of this work, the combination of solid acid catalyst with tri-solvent amine blend is proven to be an alternative method for the improvement of the energy efficiency of the CO2 capture process.
AB - In this work, the regeneration characteristics of 6 M MEA-AMP-PZ (monoethanolamine, 2-amino-2-methyl-1-propanol and piperazine) tri-solvent blends with different AMP/PZ molar ratios with four different solid acid catalysts (H-ZSM-5, γ-Al2O3, SAPO-34 and SO4 2-/TiO2) and without catalyst at 369 K were studied in terms of CO2 desorption rate and heat duty and compared with conventional 5 M MEA. For the blank runs, the results showed that the tri-solvent blends of 3 M MEA-2.5 M AMP-0.5 M PZ performs a best CO2 desorption performance among all the tested amines, which reduced the heat duty by 51.9% as compared with 5 M MEA without catalyst (100%). With regard to catalyst, the best blend with H-ZSM-5 provided the combination with the greatest performance in CO2 desorption, which decreased the heat duty by 61.6% in comparison with 5 M MEA without catalyst. Based on the results of this work, the combination of solid acid catalyst with tri-solvent amine blend is proven to be an alternative method for the improvement of the energy efficiency of the CO2 capture process.
KW - CO2 capture
KW - Catalytic CO2 desorption
KW - Heat duty reduction
KW - Novel amines tri-solvent blends
UR - http://www.scopus.com/inward/record.url?scp=85048400171&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:85048400171
T3 - Poster Sessions 2017 - Core Programming Area at the 2017 AIChE Annual Meeting
SP - 1044
BT - Poster Sessions 2017 - Core Programming Area at the 2017 AIChE Annual Meeting
PB - AIChE
T2 - Poster Sessions 2017 - Core Programming Area at the 2017 AIChE Annual Meeting
Y2 - 29 October 2017 through 3 November 2017
ER -