TY - JOUR
T1 - Metal impregnated activated carbon as cost-effective and scalable catalysts for amine-based CO2capture
AU - Bhatti, Ali Hassan
AU - Waris, Mamoona
AU - Kazmi, Wajahat W.
AU - Bhatti, Umair Hassan
AU - Min, Gwan Hong
AU - Park, Byung Cheol
AU - Kweon, Sungjoon
AU - Baek, Il Hyun
AU - Nam, Sung Chan
N1 - KAUST Repository Item: Exported on 2023-02-16
Acknowledgements: This work was supported by the Korea Institute of Energy Technology Evaluation and Planning ( KETEP ) and the Ministry of Trade, Industry & Energy ( MOTIE ) of the Republic of Korea (No. 20212010100050 ).
PY - 2023/1/5
Y1 - 2023/1/5
N2 - One of the main challenges of absorption-based CO2 capture hampering its industrial application is the huge energy penalty during solvent regeneration. The addition of a solid acidic catalyst to the solvent regeneration step can optimize the CO2 desorption at low temperatures and hence reduce the significant regeneration penalty. However, as the majority of the studied catalysts are costly, e.g., metal oxides and zeolites, and their addition can negate the benefit of lowered heat duty, the development of cost-effective and abundant materials is paramount. In this regard, we synthesized metal (Fe, Ni, Mo) supported activated carbon (AC) catalysts and evaluated their performance in the regeneration of the benchmark 5 M monoethanolamine (MEA) solution at 86 °C. The gathered data show that adding metal-impregnated AC catalysts can greatly improve amine solvent regeneration by boosting the rate of CO2 desorption by 113% and lowering the heat duty by 21.2% when compared to the noncatalytic MEA solution. Catalyst characterization data revealed that the CO2 desorption optimization is primarily governed by the number of acid sites available on the catalyst surface. The experimental results indicate that using scalable and inexpensive materials can significantly reduce the utility requirements for CO2 capture, ultimately advancing catalytic CO2 capture towards industrial implementation.
AB - One of the main challenges of absorption-based CO2 capture hampering its industrial application is the huge energy penalty during solvent regeneration. The addition of a solid acidic catalyst to the solvent regeneration step can optimize the CO2 desorption at low temperatures and hence reduce the significant regeneration penalty. However, as the majority of the studied catalysts are costly, e.g., metal oxides and zeolites, and their addition can negate the benefit of lowered heat duty, the development of cost-effective and abundant materials is paramount. In this regard, we synthesized metal (Fe, Ni, Mo) supported activated carbon (AC) catalysts and evaluated their performance in the regeneration of the benchmark 5 M monoethanolamine (MEA) solution at 86 °C. The gathered data show that adding metal-impregnated AC catalysts can greatly improve amine solvent regeneration by boosting the rate of CO2 desorption by 113% and lowering the heat duty by 21.2% when compared to the noncatalytic MEA solution. Catalyst characterization data revealed that the CO2 desorption optimization is primarily governed by the number of acid sites available on the catalyst surface. The experimental results indicate that using scalable and inexpensive materials can significantly reduce the utility requirements for CO2 capture, ultimately advancing catalytic CO2 capture towards industrial implementation.
UR - http://hdl.handle.net/10754/687809
UR - https://linkinghub.elsevier.com/retrieve/pii/S2213343722021042
UR - http://www.scopus.com/inward/record.url?scp=85146415762&partnerID=8YFLogxK
U2 - 10.1016/j.jece.2022.109231
DO - 10.1016/j.jece.2022.109231
M3 - Article
SN - 2213-3437
VL - 11
SP - 109231
JO - Journal of Environmental Chemical Engineering
JF - Journal of Environmental Chemical Engineering
IS - 1
ER -