TY - JOUR
T1 - Performance study of nickel-potassium/calcium oxide catalyst for carbon dioxide capture and conversion
AU - Quan, Cui
AU - Suo, Haojie
AU - Liu, Xiaobin
AU - Cheng, Xizhi
AU - Gao, Ningbo
N1 - Publisher Copyright:
© 2026 Elsevier B.V. All rights are reserved, including those for text and data mining, AI training, and similar technologies.
PY - 2026/6
Y1 - 2026/6
N2 - In the context of the urgent need to reduce global greenhouse gas emissions, the utilization of CO2 as a resource has emerged as a key strategy for addressing both climate change and the energy crisis. Carbon dioxide capture and conversion technology is considered one of the effective measures to tackle this challenge. This study prepared CaO-based catalysts loaded with active metals Ni and K to enhance CO2 capture and improve reverse water-gas shift (RWGS) performance. By tuning reaction temperature and Ni loading, the effects of different operating conditions on CO production during CO2 hydrogenation were systematically investigated. The results show that at 15% Ni loading, the catalyst achieved a CO2 adsorption capacity of 16.88mmolg−1 at 600 °C, while delivering a CO yield of 8.53mmolg−1 with 97% selectivity. The catalyst may be related to a relatively stable Ni(0)/NiO redox equilibrium, which may be related to the synergistic effects of oxygen vacancies and potassium promotion. In addition, the optimized pore structure further promoted CO production, ultimately enabling the highest observed CO yield. After ten reaction cycles, the target CO yield of the 15Ni1K/CaO catalyst showed only a slight decrease, from 8.53mmolg−1 to 7.32mmolg−1, demonstrating moderate cyclic stability.
AB - In the context of the urgent need to reduce global greenhouse gas emissions, the utilization of CO2 as a resource has emerged as a key strategy for addressing both climate change and the energy crisis. Carbon dioxide capture and conversion technology is considered one of the effective measures to tackle this challenge. This study prepared CaO-based catalysts loaded with active metals Ni and K to enhance CO2 capture and improve reverse water-gas shift (RWGS) performance. By tuning reaction temperature and Ni loading, the effects of different operating conditions on CO production during CO2 hydrogenation were systematically investigated. The results show that at 15% Ni loading, the catalyst achieved a CO2 adsorption capacity of 16.88mmolg−1 at 600 °C, while delivering a CO yield of 8.53mmolg−1 with 97% selectivity. The catalyst may be related to a relatively stable Ni(0)/NiO redox equilibrium, which may be related to the synergistic effects of oxygen vacancies and potassium promotion. In addition, the optimized pore structure further promoted CO production, ultimately enabling the highest observed CO yield. After ten reaction cycles, the target CO yield of the 15Ni1K/CaO catalyst showed only a slight decrease, from 8.53mmolg−1 to 7.32mmolg−1, demonstrating moderate cyclic stability.
KW - COcapture and conversion
KW - Dual-function materials
KW - Ni–CaO catalyst
KW - Potassium promotion
UR - https://www.scopus.com/pages/publications/105035234428
U2 - 10.1016/j.scp.2026.102403
DO - 10.1016/j.scp.2026.102403
M3 - 文章
AN - SCOPUS:105035234428
SN - 2352-5541
VL - 51
JO - Sustainable Chemistry and Pharmacy
JF - Sustainable Chemistry and Pharmacy
M1 - 102403
ER -