Effect of the jet direction of gas nozzle on the residence time distribution of solids in circulating fluidized bed risers

被引:17
|
作者
Yoo, Hoanju [1 ]
Moon, Hokyu [2 ]
Choi, Seungyeong [3 ]
Park, Yong-Ki [4 ]
Cho, Hyung Hee [3 ]
机构
[1] Korea Aerosp Ind LTD, Aircraft Res & Dev Div, 78,Gongdan 1 Ro, Sacheon 52529, Gyeongnam, South Korea
[2] Natl Fus Res Inst, Tokamak Engn Dept, 169-168 Gwahak Ro, Daejeon 34133, South Korea
[3] Yonsei Univ, Dept Mech Engn, 50 Yonsei Ro, Seoul 03722, South Korea
[4] Korea Res Inst Chem Technol, Green Chem Proc Res Div, Ganjeongro 141, Daejeon 34114, South Korea
关键词
Circulating fluidized bed; Gas nozzle; Jet direction; Solid residence time distribution; Numerical simulation; CFD SIMULATION; COEFFICIENT CORRELATIONS; MODEL; INLET; FLOW;
D O I
10.1016/j.jtice.2016.12.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The authors investigate the effects of the direction of the gas jet on the solid residence time distribution in a CFB riser. Tracer technique was employed to calculate the RTD of solids. A Eulerian-Eulerian model with kinetic theory of granular flow and species transport was used to simulate the motion of tracer particles in a CFB riser. For a comparative analysis of the direction of the gas jet, simulations of vertical, horizontal and hybrid jets were carried out. The direction of the gas jet significantly influenced the axial and radial structure of bed, and hence affected the RTD for solid particles. The mean residence time of solids was changed, and the results showed that 16.3 s, 14.8 s, and 11.4 s with vertical, horizontal and hybrid jets nozzles, respectively. (C) 2016 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:235 / 243
页数:9
相关论文
共 50 条
  • [21] Radial Distribution of Liquid Velocity in a Liquid-Solids Circulating Fluidized Bed
    Zheng, Ying
    Zhu, Jesse
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2003, 1
  • [22] Numerical study of the effect of the gas and solids distributors on the uniformity of the radial solids concentration distribution in CFB risers
    Peng, B.
    Zhang, C.
    Zhu, J.
    POWDER TECHNOLOGY, 2011, 212 (01) : 89 - 102
  • [23] Comparisons of particle clustering phenomenon between gas-solids high-density and low-density circulating fluidized bed risers via numerical study
    Sun, Zeneng
    Zhang, Chao
    Zhu, Jesse
    POWDER TECHNOLOGY, 2022, 397
  • [24] Modeling Gas-Solid Flows in Circulating Fluidized Bed Risers Using Computational Fluid Dynamics
    Venturi, Diego Nei
    Duarte, Carlos Antonio Ribeiro
    de Souza, Francisco Jose
    COMPUTATIONAL PARTICLE MECHANICS, 2024,
  • [25] A new method for solids residence time distribution measurement in continuous fluidized beds
    Liu, Pengbo
    Jiang, Qiuqiao
    Xu, Chenhuan
    Li, Shuyue
    Zhang, Yongmin
    Song, Haitao
    POWDER TECHNOLOGY, 2024, 443
  • [26] Effect of pressure variation at downcomer bottom on axial bed density distribution in a circulating gas fluidized bed riser
    Kuramoto, K
    Chiba, T
    Hirama, T
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1997, 30 (04) : 631 - 636
  • [27] Modelling a circulating fluidized bed riser reactor with gas-solids downflow at the wall
    Puchyr, DMJ
    Mehrotra, AK
    Behie, LA
    Kalogerakis, NE
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1997, 75 (02): : 317 - 326
  • [28] Fine-grid simulations of gas-solids flow in a circulating fluidized bed
    Benyahia, Sofiane
    AICHE JOURNAL, 2012, 58 (11) : 3589 - 3592
  • [29] Effect of Pressure on Solids Flow Characteristics in Recycle System of a Circulating Fluidized Bed
    Kim, Sung Won
    Kim, Sang Done
    KOREAN CHEMICAL ENGINEERING RESEARCH, 2010, 48 (02): : 198 - 204
  • [30] Axial and radial development of solids holdup in a high flux/density gas-solids circulating fluidized bed
    Wang, Chengxiu
    Zhu, Jesse
    Barghi, Shahzad
    Li, Chunyi
    CHEMICAL ENGINEERING SCIENCE, 2014, 108 : 233 - 243