Insights into gas-solid flow structures in fluidized beds up to 1600 °C via analysis of gas residence time distributions

被引:0
作者
Gao, Han [1 ]
Chen, Zeshi [1 ]
Zhang, Qingjin [1 ,2 ]
Fu, Liangliang [1 ]
Xu, Guangwen [1 ]
Bai, Dingrong [1 ,3 ]
机构
[1] Shenyang Univ Chem Technol, Minist Educ, Key Lab Resources Chem & Mat, Shenyang 110142, Peoples R China
[2] Shenyang Univ Technol, Sch Mat Sci & Engn, Shenyang 110870, Peoples R China
[3] Ordos Lab, Ordos 017010, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas residence time distribution; Gas back-mixing; Temperature; Fluidized bed; Axial dispersion model; Plug flow; HIGH-TEMPERATURES; HYDRODYNAMICS; AGGLOMERATION; DISPERSION; PARTICLES; PRESSURE;
D O I
10.1016/j.powtec.2024.120426
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study investigates gas residence time distributions (RTDs) in a fluidized bed of Al2O3 particles at temperatures ranging from ambient to 1600 degrees C, focusing on the impact of temperature on gas back-mixing and flow patterns. We find that at low temperatures (up to 300 degrees C), gas flows in a near-plug flow pattern, represented by narrow RTD curves with early peaks. As temperature increases to 600 degrees C, the RTD curves broaden, featuring delayed peaks due to bubble breakup and enhanced gas drag. Between 800 degrees C and 1200 degrees C, significant deviations from plug flow emerge, driven by stronger interparticle forces and increased gas transfer to the emulsion phase. Interestingly, beyond 1200 degrees C, the RTD curves shift back toward plug flow, influenced by intensified interparticle forces and physicochemical changes in the bed materials.
引用
收藏
页数:12
相关论文
共 48 条
  • [1] Gas-flow distribution in bubbling fluidized beds: CFD-based analysis and impact of operating conditions
    Bakshi, A.
    Altantzis, C.
    Glicksman, L. R.
    Ghoniem, A. F.
    [J]. POWDER TECHNOLOGY, 2017, 316 : 500 - 511
  • [2] Agglomeration in fluidized beds at high temperatures: Mechanisms, detection and prevention
    Bartels, Malte
    Lin, Weigang
    Nijenhuis, John
    Kapteijn, Freek
    van Ommen, J. Ruud
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2008, 34 (05) : 633 - 666
  • [3] Residence time distribution in fluidized beds: diffusion, dispersion, and adsorption
    Berard, Ariane
    Blais, Bruno
    Patience, Gregory S.
    [J]. ADVANCED POWDER TECHNOLOGY, 2021, 32 (05) : 1677 - 1687
  • [4] Experimental methods in chemical engineering: Residence time distribution-RTD
    Berard, Ariane
    Blais, Bruno
    Patience, Gregory S.
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2020, 98 (04) : 848 - 867
  • [5] Cankurt N.T., 1978, Fluidization:, P307
  • [6] Residence times in fluidized beds with secondary gas injection
    Christensen, D.
    Nijenhuis, J.
    Van Ornmen, J. R.
    Coppens, M. -O.
    [J]. POWDER TECHNOLOGY, 2008, 180 (03) : 321 - 331
  • [7] Gas back-mixing study in a membrane-assisted micro-structured fluidized bed
    Dang, T. Y. N.
    Gallucci, F.
    Annaland, M. van Sint
    [J]. CHEMICAL ENGINEERING SCIENCE, 2014, 108 : 194 - 202
  • [8] Davidson J.F., 1963, FLUIDIZED PARTICLES
  • [9] Development of a membrane-assisted fluidized bed reactor. 1. Gas phase back-mixing and bubble-to-emulsion phase mass transfer using tracer injection and ultrasound experiments
    Deshmukh, SARK
    Laverman, JA
    Cents, AHG
    Annaland, MVS
    Kuipers, JAM
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (16) : 5955 - 5965
  • [10] Gas and solids mixing in a turbulent fluidized bed
    Du, B
    Fan, LS
    Wei, F
    Warsito, W
    [J]. AICHE JOURNAL, 2002, 48 (09) : 1896 - 1909