Numerical simulation study on gas-solid flow characteristics and SO2 removal characteristics in circulating fluidized bed desulfurization tower

被引:15
|
作者
Liu, Peng [1 ]
Wu, Xuan [1 ]
Wang, Zhengyang [1 ]
Bo, Yuxuan [1 ]
Bao, Haoran [1 ]
机构
[1] Inner Mongolia Univ Sci & Technol, Sch Energy & Environm, Baotou 014010, Peoples R China
基金
中国国家自然科学基金;
关键词
Computational particle fluid dynamics; Circulating fluidized bed flue gas; desulfurization; Desulfurization efficiency; Gas -solid two-phase flow; Structural optimization; FLUE-GAS; CPFD SIMULATION; MODEL; HCL;
D O I
10.1016/j.cep.2022.108974
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Circulating fluidized bed flue gas desulfurization technology is widely used in the world. The computational particle fluid dynamics (CPFD) numerical simulation method was used to study the gas-solid two-phase flow and desulfurization characteristics in the circulating fluidized bed desulfurization tower. The CPFD method is based on the MP-PIC method, which uses the stochastic particle method for the particle phase and the Euler method for the fluid phase to solve the dense particle flow. The established model was firstly verified by the experimental results of gas-solid flow field and desulfurization efficiency. Then, the effects of flue gas parameters on the flow field in the desulfurization tower and the effects of flue gas parameters, SO2 inlet concentration, and Ca/S on desulfurization efficiency were numerically simulated. An effective optimization scheme was also proposed to improve the desulfurization efficiency. The research results showed that the CPFD simulation results were in good agreement with the experimental results, which proved the reliability of the method. The particle motion state in the bed of the desulfurization tower presents a core-annular flow. As the flue gas inlet flow increased, the distribution of flue gas and particles has a serious deviation, and the desulfurization efficiency also decreased. The desulfurization efficiency will decrease with the increased of SO2 inlet concentration and increased with the increased of Ca/S. According to the distribution of SO2 concentration in the bed, three characteristic desulfurization zones can be proposed, namely, the initial mixing process zone, the high-efficiency desulfurization process zone, and the low-efficiency desulfurization process zone. Installing a baffle at the bottom of the desulfurization tower can optimize the distribution of gas-solid two-phase flow in the bed and the desulfurization efficiency.
引用
收藏
页数:15
相关论文
共 50 条
  • [1] CPFD Simulation of Gas-solid Flow Characteristics of Circulating Fluidized Bed Desulfurization Tower
    Wu, Xuan
    Liu, Peng
    Wei, Nan
    Pan, Hui
    Li, Xiaorui
    [J]. Zhongguo Dianji Gongcheng Xuebao/Proceedings of the Chinese Society of Electrical Engineering, 2020, 40 (10): : 3229 - 3240
  • [2] Chaotic characteristics of gas-solid flow in a circulating fluidized bed
    Ji, H
    Ohara, H
    Tsutsumi, A
    Yoshida, K
    [J]. FLUIDIZATION IX, 1998, : 605 - 612
  • [3] Numerical simulation of the flow field in a circulating fluidized bed desulfurizer and its gas-solid separation characteristics
    Energy Source Science and Engineering College, Harbin Institute of Technology, Harbin 150001, China
    [J]. Reneng Dongli Gongcheng, 2006, 5 (487-490):
  • [4] Numerical simulation of hydrodynamic characteristics in a gas-solid fluidized bed
    Wang, Lijun
    Xie, Xin
    Wei, Guangchao
    Li, Rundong
    [J]. PARTICULATE SCIENCE AND TECHNOLOGY, 2017, 35 (02) : 177 - 182
  • [5] Numerical simulation on gas-solid flow characteristics and NOxformation of a full-scale dual circulating fluidized bed boiler
    Nie, Hua
    Li, Jianbo
    Zhang, Yi
    Liu, Qingcai
    Wang, Quanhai
    Lu, Xiaofeng
    [J]. ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2020, 46 (01) : 15592 - 15607
  • [6] Effect of elevated pressure on gas-solid flow characteristics in a circulating fluidized bed
    Liu, Daoyin
    Hu, Jinding
    Song, Jialong
    Liang, Cai
    Xu, Chuanlong
    Chen, Xiaoping
    [J]. POWDER TECHNOLOGY, 2020, 366 (470-476) : 470 - 476
  • [7] Numerical simulation of the gas-solid flow characteristics in fluidized bed with wide particle size distribution
    Wang, Wei-Wen
    Dong, Hai-Hong
    Chen, Guang-Hui
    Li, Jian-Long
    [J]. Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2011, 25 (02): : 276 - 282
  • [8] Numerical Simulation of Gas-Solid Flow in a Wurster Fluidized Bed
    Zhou, Hang
    Wang, Haigang
    Tu, Qiuya
    [J]. PROCEEDINGS OF THE 7TH INTERNATIONAL CONFERENCE ON DISCRETE ELEMENT METHODS, 2017, 188 : 1005 - 1012
  • [9] NUMERICAL SIMULATION OF GAS-SOLID FLOW IN AN INTERCONNECTED FLUIDIZED BED
    Canneto, Giuseppe
    Freda, Cesare
    Braccio, Giacobbe
    [J]. THERMAL SCIENCE, 2015, 19 (01): : 317 - 328
  • [10] Numerical simulation of gas-solid flow characteristics in radial moving bed
    Lu, Chun-Xi
    Long, Wen-Yu
    Lin, Quan-Zhi
    [J]. Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2015, 29 (01): : 49 - 57