Parametric study of CO2 capture and thermal energy storage in a CaO/CaCO3 bubbling fluidized bed with polydisperse particles

IF 8.6 2区 工程技术 Q1 CHEMISTRY, MULTIDISCIPLINARY
Journal of CO2 Utilization Pub Date : 2026-03-01 Epub Date: 2026-02-06 DOI:10.1016/j.jcou.2026.103342
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.
多分散颗粒CaO/CaCO3鼓泡流化床CO2捕集与储热参数研究
CaO/CaCO3循环系统在聚光太阳能发电热化学储能、CO2捕集利用等高温工艺中具有广阔的应用前景。然而,大多数数值研究通常采用单一粒径的钙基颗粒,难以反映粒径分布对实际系统内流化和反应行为的影响。为了阐明CaO/CaCO3在鼓泡流化床中的流态化及反应特性,本研究以多分散钙基颗粒为研究对象。结合化学反应的数值模拟从参数化的角度研究了不同气体速度、进口二氧化碳体积分数和动态操作条件下颗粒流化行为。通过对比不同粒径组合,分析了床层固含量分布、时间平均CO2浓度、时间平均轴向固含量、时间平均流速等特征参数。结果表明:当气速恒定时,随着粒径从75 μm增大到136 μm,床层对CO2的吸附效率逐渐降低;在混合粒度系统中,在相同气速下,单粒度床的CaCO3固含量略低于混合粒度床,而CaO固含量高于混合粒度床。在不同的进口CO2浓度条件下,较高的CO2浓度导致床层时间平均速度和时间平均轴向固含量降低。综合考虑颗粒温度分布、CO2吸附效率、CaO转化率和储能密度等因素,当进口CO2体积分数为0.85时,钙基颗粒体系整体性能更优。
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来源期刊
Journal of CO2 Utilization
Journal of CO2 Utilization CHEMISTRY, MULTIDISCIPLINARY-ENGINEERING, CHEMICAL
CiteScore
13.90
自引率
10.40%
发文量
406
审稿时长
2.8 months
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.
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