Electric Power ›› 2013, Vol. 46 ›› Issue (11): 66-71.DOI: 10.11930/j.issn.1004-9649.2013.11.66.5

• Energy Consercation and Environmental Protection • Previous Articles     Next Articles

Feasibility Analysis of Three-Phase Circulating Fluidized Bed for Ammonia Decarbonization

HU Kang-tao1, LIU Jing-hao1, YANG Hai-rui1, LEI Xiu-jian2   

  1. 1. Key Laboratory for Thermal Science and Power Engineering of Ministry of Education, Beijing Key Laboratory for CO2 Utilization and Reduction Technology, Department of Thermal Engineering, Tsinghua University, Beijing 100084, China; 2. Sichuan Baima Circulating Fluidized Bed Demonstration Power Plant Limited Liability Company, Neijiang 641000, China
  • Received:2013-05-19 Online:2013-11-23 Published:2015-12-10

Abstract: The gas-liquid-solid three-phase fluidized bed is widely used in petrochemical, electrochemical and biochemical processes. Compared with the traditional three-phase fluidized bed, the features of gas-liquid-solid circulating fluidized bed include operation simplicity, large inter-phase contact area, uniform gas-liquid mixture, good heat and mass transfer effect and easy temperature control. Therefore, it can be one of the potential reactors for ammonia decarbonization in coal-fired power plants. Based on the tests of three-phase circulating fluidized bed, the ammonia decarbonization technology with three-phase circulating fluidized bed acting as reactor is simulated and analyzed in Aspen Plus environment. The feasibility of the technology is also discussed.

Key words: CO2 separation, three-phase circulating fluidized bed, ammonia absorption

CLC Number: