Bifunctional Acid Synergy in a Solid NiCo@C Catalyst for Promoted Amine Regeneration in CO <sub>2</sub> Capture

The industrial application of MEA-based carbon capture processes is significantly constrained by a low desorption rate and high energy consumption. To address these limitations, a NiCo@C catalyst was synthesized by using a hydrothermal-assisted impregnation method. The incorporation of Ni–Co dual doping into the carbon-based framework not only enhanced its stability and catalytic activity but also optimized its pore structure. A series of systematic characterizations were performed to evaluate the physicochemical properties of the material. The results indicate that the NiCo@C catalyst exhibits a substantially larger specific surface area and pore size compared to the Ni@C and Co@C catalysts. Additionally, the bimetallic catalysts introduce both weakly acidic and strongly acidic sites while maintaining a well-defined three-dimensional spherical structure. Compared to the noncatalytic MEA system, the introduction of NiCo@C increases the maximum desorption rate by 158% and the maximum desorption amount by 41.24%. These improvements contribute to a 53.48% reduction in energy consumption along with excellent cycle stability. The catalytic mechanism of NiCo@C was further investigated using 13C NMR, FT-IR, and Raman spectroscopy. The results reveal that bifunctional acid synergy in the solid NiCo@C catalyst promotes proton transfer and facilitates the breaking of C–N bonds, thereby enabling more efficient desorption with a lower energy consumption.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2026-02-27
DOI
https://doi.org/10.1021/acs.iecr.5c05222
Primary Topic
Catalysts for Methane Reforming
Type
article
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article

Bifunctional Acid Synergy in a Solid NiCo@C Catalyst for Promoted Amine Regeneration in CO 2 Capture

ChenLu Mi, Hongtai Liu, Yuchen Liu, Jichao Hu et al.
Industrial & Engineering Chemistry Research
Catalysts for Methane Reforming
article

Bifunctional Acid Synergy in a Solid NiCo@C Catalyst for Promoted Amine Regeneration in CO 2 Capture

ChenLu Mi, Hongtai Liu, Yuchen Liu, Jichao Hu, Yuetong Zhao, K. K. Zhao, Pengfei Qu, Pan Zhang, Ruigeng Xie, Zedong Niu, Lemeng Wang, Dong Fu, Luanxiang Chao, Jian Ma
article en

Abstract

The industrial application of MEA-based carbon capture processes is significantly constrained by a low desorption rate and high energy consumption. To address these limitations, a NiCo@C catalyst was synthesized by using a hydrothermal-assisted impregnation method. The incorporation of Ni–Co dual doping into the carbon-based framework not only enhanced its stability and catalytic activity but also optimized its pore structure. A series of systematic characterizations were performed to evaluate the physicochemical properties of the material. The results indicate that the NiCo@C catalyst exhibits a substantially larger specific surface area and pore size compared to the Ni@C and Co@C catalysts. Additionally, the bimetallic catalysts introduce both weakly acidic and strongly acidic sites while maintaining a well-defined three-dimensional spherical structure. Compared to the noncatalytic MEA system, the introduction of NiCo@C increases the maximum desorption rate by 158% and the maximum desorption amount by 41.24%. These improvements contribute to a 53.48% reduction in energy consumption along with excellent cycle stability. The catalytic mechanism of NiCo@C was further investigated using 13C NMR, FT-IR, and Raman spectroscopy. The results reveal that bifunctional acid synergy in the solid NiCo@C catalyst promotes proton transfer and facilitates the breaking of C–N bonds, thereby enabling more efficient desorption with a lower energy consumption.

Industrial & Engineering Chemistry ResearchVol. 65(9)
Electric Power University (VN), North China Electric Power University (CN), Lucas Research (US), CAS Key Laboratory of Urban Pollutant Conversion (CN)
Affordable and clean energy
Openalex Percentile: Top 41%
Catalysts for Methane Reforming
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