首页|期刊导航|煤炭转化|10 MWth生物质化学链燃烧双循环流化床装置的降阶模拟

10 MWth生物质化学链燃烧双循环流化床装置的降阶模拟OA

Order-reduced simulation of a 10 MWth dual circulating fluidized bed biomass chemical looping combustion system

中文摘要英文摘要

化学链燃烧技术通过氧载体在燃料反应器与空气反应器之间的循环实现氧的传递,具有CO2捕集和低NOx排放等优势,是极具潜力的低碳燃烧技术.然而,化学链燃烧系统涉及多尺度、多物理场耦合的复杂过程,其工程化应用仍面临反应器设计与氧载体优化等挑战.利用一维降阶模型对双循环流化床构型的10 MWth生物质化学链燃烧装置进行了快速模拟,并考察了反应器内部化学链燃烧状态、反应情况及能量分布特征.模拟结果表明:系统可实现96 kg/s的固体循环流量,燃料反应器燃烧效率达到95.56%,碳捕集效率为85.8%.从整个系统热量分布的角度来看,空气反应器和燃料反应器均达到了热平衡且能实现自热运行,自热状态下空气反应器上部布置的水冷壁吸热量为1.24 MWth,实现了系统的热量输出.在此基础上,重点探讨了燃料反应器温度、系统输入热功率、氧载体性能衰减及其类型差异对燃烧效率与碳捕集效率的影响规律.敏感性分析表明:提高燃料反应器温度可使碳捕集效率从85.8%上升至92.25%,燃烧效率从95.56%上升至96.4%,但温度过高会破坏自热平衡;当系统热功率从8MWth增加到13 MWth时,燃烧效率受到的影响较小,而碳捕集效率则从89.21%下降至81.84%;氧载体性能从100%衰减至40%的过程中,燃烧效率和碳捕集效率分别从95.56%、85.8%下降至71.09%、81.21%;钙钛矿型氧载体凭借其高载氧量与优异反应活性,表现出优于铁基氧载体的性能,燃烧效率可达97.75%.

Chemical looping combustion(CLC)circulates oxygen carriers(OCs)between a fuel reactor(FR)and an air reactor(AR),thereby enabling inherent CO2 capture and low NOx emissions,making it a promising low-carbon combustion technology.However,CLC involves complex multi-scale and multi-physics coupled processes,and its scale-up faces challenges such as reactor design and OC optimization.In this study,a reduced-order model was developed to simulate a 10 MWth biomass-fueled CLC system with a dual-circulating-fluidized-bed configuration.The model was used to investigate the system's combustion behavior,reaction characteristics,and energy distribution.Simulation results indicate that the system achieves a solids circulation rate of 96 kg/s,a combustion efficiency of 95.56%in the FR,and a carbon capture efficiency of 85.8%.From a system-level energy perspective,both reactors attain thermal equilibrium,thus enabling autothermal operation.Under autothermal operation,the water wall installed in the upper section of the AR absorbs 1.24 MWth,which constitutes the useful heat output of the system.The effects of FR operating temperature,system thermal input,OC performance degradation,and OC type on combustion and carbon capture efficiencies were further examined.Sensitivity analysis shows that increasing the FR temperature increases the carbon capture efficiency from 85.8%to 92.25%and the combustion efficiency from 95.56%to 96.4%,although excessively high temperatures can disrupt the autothermal balance.As the system thermal input increases from 8 MWth to 13 MWth,the combustion efficiency is only marginally affected,whereas the carbon capture efficiency decreases from 89.21%to 81.84%.When the OC performance degrades from 100%to 40%,the combustion efficiency decreases from 95.56%to 71.09%,and the carbon capture efficiency decreases from 85.8%to 81.21%.In contrast,owing to their higher oxygen transport capacity and superior reactivity,perovskite type OCs significantly outperform their ironbased counterparts,with combustion efficiency reaching up to 97.75%.

周培昀;陶冶;陆杰;童永祺;赵海波

华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉华中科技大学煤燃烧与低碳利用全国重点实验室,430074武汉

化学化工

生物质化学链燃烧降阶模拟氧载体敏感性分析

biomasschemical looping combustionreduced-order simulationoxygen carriersensitivity analysis

《煤炭转化》 2026 (4)

44-56,13

国家自然科学基金项目(52536008)和湖北省重点研发项目(2025BCB042)

10.19726/j.cnki.ebcc.202604005

评论