现役CFB锅炉富氧燃烧改造的可行性分析OA
Feasibility Study of Oxy-fuel Combustion Retrofit for Operational CFB Boilers
循环流化床(circulating fluidized bed,CFB)锅炉富氧燃烧作为有效的大规模碳减排技术,因通过电解水消纳新能源使氧气获取成本降低,而更具应用价值.基于成熟的一维CFB锅炉计算模型,模拟了 135 MW和 350 MW CFB锅炉在富氧燃烧条件下的运行情况,重点分析了炉膛及尾部烟道的温度分布和传热特性.模拟计算的结果表明,以纯氧取代空气燃烧氛围,并通过烟气再循环技术调节氧气浓度(体积分数)至大约30%,可在保持锅炉结构不变的前提下,获得与空气燃烧相似的温度分布,实现高效燃烧与稳定传热.研究为现役CFB锅炉的富氧燃烧改造提供了重要参考,并为其在碳捕集领域的工程化应用奠定基础.
Oxy-fuel combustion in circulating fluidized bed(CFB)boilers,as an effective large-scale carbon abatement technology,is increasingly valuable due to the reduced cost of oxygen acquisition via water electroly-sis,which consumes surplus renewable energy.Based on a well-established one-dimensional CFB boiler calcu-lation model,the operations of 135 MW and 350 MW CFB boilers under oxy-fuel combustion conditions are simulated.The temperature distribution and heat transfer characteristics of the furnace and back pass are ana-lyzed.The results show that replacing the air combustion atmosphere with pure oxygen and adjusting the oxy-gen volume concentration to approximately 30%through flue gas recirculation can achieve a temperature distri-bution similar to that of air combustion,while maintaining the structural integrity of the boiler.Furthermore,this retrofit enables efficient combustion and stable heat transfer.The findings provide valuable insights for ret-rofitting operational CFB boilers with oxy-fuel combustion technology and lay a solid foundation for its engineer-ing application in carbon capture.
李超然;吴皓文;周托;张缦;杨海瑞
清华大学 能源与动力工程系,北京 100084清华大学 能源与动力工程系,北京 100084清华大学 能源与动力工程系,北京 100084清华大学 能源与动力工程系,北京 100084清华大学 能源与动力工程系,北京 100084
动力与电气工程
循环流化床富氧燃烧烟气再循环碳捕集、利用与封存流态重构
circulating fluidized bed(CFB)oxy-fuel combustionflue gas recirculation(FGR)carbon cap-ture,utilization and storage(CCUS)fluidization statereconstruction
《电力学报》 2025 (3)
151-160,10
国家重点研发计划(2023YFB4104301)华能集团总部科技项目(HNKJ23-H71).
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