Radial porosity peak at the centerline of packed beds with small tube to particle diameter ratios

被引:22
|
作者
Guo, Zehua
Sun, Zhongning
Zhang, Nan [1 ]
Ding, Ming
Cao, Xiaxin
机构
[1] Harbin Engn Univ, Fundamental Sci Nucl Safety & Simulat Technol Lab, Harbin 150001, Heilongjiang, Peoples R China
关键词
Packed bed; Radial porosity; Small tube to particle diameter ratio; Channel at the centerline; Pressure drop; PRESSURE-DROP; FIXED-BEDS; FLOW; WALL; SPHERES;
D O I
10.1016/j.powtec.2017.06.061
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Various mathematical models in literature conclude that the porosity profile varies in an oscillatory fashion and the amplitude decreases with increasing distance from the wall. However, scrutiny of the literature indicates a distinct deviation in the models that a strong porosity peak at the centerline is not amenable to the predictions for packed beds with small tube to particle diameter ratios. In this study, the radial porosity peak at the centerline of packed bed is investigated by experiments. According to the structure of packed beds at D/d < 337, the bed is divided into two parts-the near wall part and the central part. The mean porosity value of different parts is obtained by counting method. In the experimental result, high porosity value at the central part is observed. Then, the reasons that lead to the porosity peak-the highly ordered ring structure and the internal channel similar to the bed at D/d < 2-are identified. Moreover, the channel at the centerline promises that significant bypass flow would occur in the packing arrangement, which should be taken into account for the analysis of transport phenomena in packed beds. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:445 / 451
页数:7
相关论文
共 50 条
  • [1] Mean porosity variations in packed bed of monosized spheres with small tube-to-particle diameter ratios
    Guo, Zehua
    Sun, Zhongning
    Zhang, Nan
    Cao, Xiaxin
    Ding, Ming
    POWDER TECHNOLOGY, 2019, 354 : 842 - 853
  • [2] Estimating radial velocity of fixed beds with low tube-to-particle diameter ratios
    Cheng, ZM
    Yuan, WK
    AICHE JOURNAL, 1997, 43 (05) : 1319 - 1324
  • [3] Experimental study of flow transitions in random packed beds with low tube to particle diameter ratios
    Yang, Jian
    Bu, Shanshan
    Dong, Qingtai
    Wu, Jiangquan
    Wang, Qiuwang
    EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2015, 66 : 117 - 126
  • [4] Influence of the packing structure on the flow through packed beds with small cylinder diameter to particle diameter ratios
    van der Merwe, W. J. S.
    du Toit, C. G.
    Kruger, J-H
    NUCLEAR ENGINEERING AND DESIGN, 2020, 365 (365)
  • [5] Radial porosity in packed beds of spheres
    Mueller, Gary E.
    POWDER TECHNOLOGY, 2010, 203 (03) : 626 - 633
  • [6] RADIAL POROSITY VARIATIONS IN PACKED BEDS
    ROBLEE, LHS
    BAIRD, RM
    TIERNEY, JW
    AICHE JOURNAL, 1958, 4 (04) : 460 - 464
  • [7] Pressure drop and heat transfer in packed beds with small tube-to-particle diameter ratio
    Raichura, R.C.
    Experimental Heat Transfer, 12 (04): : 309 - 327
  • [8] Pressure drop and heat transfer in packed beds with small tube-to-particle diameter ratio
    Raichura, RC
    EXPERIMENTAL HEAT TRANSFER, 1999, 12 (04) : 309 - 327
  • [9] FLUID-PHASE RADIAL TRANSPORT IN PACKED-BEDS OF LOW TUBE-TO-PARTICLE DIAMETER RATIO
    DIXON, AG
    DICOSTANZO, MA
    SOUCY, BA
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1984, 27 (10) : 1701 - 1713
  • [10] Radial variation in porosity in annular packed beds
    du Toit, C. G.
    NUCLEAR ENGINEERING AND DESIGN, 2008, 238 (11) : 3073 - 3079