The solids flow in the CFB-riser quantified by single radioactive particle tracking

被引:36
|
作者
Mahmoudi, Shiva [1 ]
Baeyens, Jan [1 ]
Seville, Jonathan [1 ]
机构
[1] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
基金
英国工程与自然科学研究理事会;
关键词
CFB; Riser; Solids flow; Operating regimes; Slip factor; CIRCULATING FLUIDIZED-BED; RESIDENCE TIME DISTRIBUTION; REFLECTION PROBES; VOLUME-FRACTION; TOMOGRAPHY; VELOCITY; PROFILES; VISUALIZATION; HYDRODYNAMICS; SYSTEM;
D O I
10.1016/j.powtec.2011.04.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Single radioactive particle tracking was used to measure the overall solids residence time (and its distribution) in the riser of a CFB, operating at superficial air velocities (U) of 1 to 9 ms(-1) and solids circulation fluxes (G) between 20 to 600 kg m(-2)s(-1). The results demonstrate that the particle motion and mixing differ according to the operating mode of the riser, with a fairly constant velocity throughout the riser achieved in the dilute or dense riser flow, but with a significant amount of back-mixing for intermediate values of U and/or G. This back-mixing is due to the core-annulus mode of particle flow. Whereas experimental results and theoretical predictions are in fair agreement for the dilute and dense riser flow, the core-annulus regime needs to account for a U and G dependent slip factor (phi), in excess of the commonly proposed value phi=2, especially at U-U-TR < 2 ms(-1). Moreover, the previously published riser operation diagram is confirmed by the experiments, although a further analysis of the core-annulus regime is needed. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:135 / 143
页数:9
相关论文
共 50 条
  • [1] Quantification of solids flow in a gas-solid riser: single radioactive particle tracking
    Bhusarapu, S
    Al-Dahhan, M
    Dudukovic, MP
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (22-23) : 5381 - 5386
  • [2] Overall solids movement and solids residence time distribution in a CFB-riser
    Smolders, K
    Baeyens, J
    CHEMICAL ENGINEERING SCIENCE, 2000, 55 (19) : 4101 - 4116
  • [3] The solids flow in the riser of a Circulating Fluidised Bed (CFB) viewed by Positron Emission Particle Tracking (PEPT)
    Van de Velden, M.
    Baeyens, J.
    Seville, J. P. K.
    Fan, X.
    POWDER TECHNOLOGY, 2008, 183 (02) : 290 - 296
  • [4] Hydrodynamic predictions of dense gas-solids flow in CFB riser
    Wang, Xueyao
    Wu, Xuezhi
    Wang, Shengdian
    Xu, Xiang
    Xiao, Yunhan
    ELECTRICAL POWER & ENERGY SYSTEMS, PTS 1 AND 2, 2012, 516-517 : 917 - +
  • [5] Gas-solids flow behavior: CFB Riser vs. Downer
    Zhang, H
    Huang, WX
    Zhu, JX
    AICHE JOURNAL, 2001, 47 (09) : 2000 - 2011
  • [6] Experimental and computational study of multiphase gas/particle flow in a CFB riser
    Mathiesen, V
    Solberg, T
    Arastoopour, H
    Hjertager, BH
    AICHE JOURNAL, 1999, 45 (12) : 2503 - 2518
  • [7] Solids flow diagram of a CFB riser using Geldart B-type powders
    Shiva Mahmoudi
    Chian Wen Chan
    Anke Brems
    Jonathan Seville
    Jan Baeyens
    Particuology, 2012, 10 (01) : 51 - 61
  • [8] Solids flow diagram of a CFB riser using Geldart B-type powders
    Mahmoudi, Shiva
    Chan, Chian Wen
    Brems, Anke
    Seville, Jonathan
    Baeyens, Jan
    PARTICUOLOGY, 2012, 10 (01) : 51 - 61
  • [9] Local solid-particle concentration and flow development in a long CFB riser
    Huang, Wei-Xing
    Qi, Xiao-Bo
    Pan, Yong-Liang
    Zhu, Jing-Xu
    Shi, Yan-Fu
    Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2002, 16 (06): : 626 - 631
  • [10] Position and velocity of a large particle in a gas solid riser using the radioactive particle tracking technique
    Godfroy, L
    Larachi, F
    Chaouki, J
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02): : 253 - 261