Liangsheng He , Shengnan Yan , Zhenggui Li , Fang Chen , Qin Zhao , Hongteng Wu , Yawei Bai , Xiaolin Yang
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引用次数: 0
Abstract
The CaO/CaCO3 cycle system holds broad application prospects in high-temperature processes such as thermal chemical energy storage for concentrated solar power generation and CO2 capture and utilization. However, most numerical studies typically employ calcium-based particles of a single particle size, making it difficult to reflect the influence of particle size distribution on fluidization and reaction behaviour within actual systems. To elucidate the fluidization and reaction characteristics of CaO/CaCO3 in bubbling fluidized beds, this study employs polydisperse calcium-based particles as the research subject. Numerical simulations incorporating chemical reactions are conducted to investigate particle fluidization behaviour under varying gas velocities, inlet CO2 volume fractions, and dynamic operating conditions from a parameterisation perspective. By comparing different particle size combinations, characteristic parameters such as bed solid content distribution, time-averaged CO2 concentration, time-averaged axial solid content, and time-averaged velocity were analysed. Results indicate that at constant gas velocity, the bed’s CO2 adsorption efficiency gradually decreases as particle size increases from 75 μm to 136 μm. In the mixed-particle-size system, at the same gas velocity, the CaCO3 solid content in the single-particle-size bed was slightly lower than that in the mixed-particle-size bed, while the CaO solid content was higher than that in the mixed-particle-size bed. Under different inlet CO2 concentration conditions, higher CO2 concentrations led to decreases in the bed's time-averaged velocity and time-averaged axial solid content. Considering particle temperature distribution, CO2 adsorption efficiency, CaO conversion rate, and energy storage density comprehensively, the calcium-based particle system demonstrated superior overall performance when the inlet CO2 volume fraction was 0.85.
期刊介绍:
The Journal of CO2 Utilization offers a single, multi-disciplinary, scholarly platform for the exchange of novel research in the field of CO2 re-use for scientists and engineers in chemicals, fuels and materials.
The emphasis is on the dissemination of leading-edge research from basic science to the development of new processes, technologies and applications.
The Journal of CO2 Utilization publishes original peer-reviewed research papers, reviews, and short communications, including experimental and theoretical work, and analytical models and simulations.