Packed bed structure:: Evaluation of radial particle distribution

被引:11
|
作者
Mariani, NJ
Salvat, WI
Martínez, OM
Barreto, GF [1 ]
机构
[1] Univ Nacl La Plata, Fac Ingn, Dept Ingn Quim, La Plata, Argentina
[2] Univ Buenos Aires, Fac Ciencias Exactas & Nat, Dept Ind, RA-1428 Buenos Aires, DF, Argentina
[3] Univ Nacl La Plata, CONICET, CINDECA, La Plata, Argentina
来源
关键词
bed structure; particle center distribution; voidage profile; aspect ratio;
D O I
10.1002/cjce.5450800202
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A model describing the radial distribution of monosized spheres in randomly packed beds up to distances of about two particle diameters from the vessel wall is presented here. The model is based on the existence of a highly ordered layer of particles adjacent to the wall followed by a more diffuse, but still identifiable, second layer. Expressions generated from simple geometrical concepts (intersection between a cylindrical surface and a sphere) straightforwardly allow calculating the radial voidage profile given the radial distribution of particle centers and vice versa. These expressions are employed to fit the model to measures of voidage profiles within a wide range of aspect ratios, a = (R-T/R-p). The model can be used to accurately predict radial voidage profiles, but it is stressed that the identification of particle distribution constitutes more valuable information than an empirical expression for describing voidage variations.
引用
收藏
页码:186 / 193
页数:8
相关论文
共 50 条
  • [31] Existence of a critical particle concentration in plugging of a packed bed
    Pandya, VB
    Bhuniya, S
    Khilar, KC
    AICHE JOURNAL, 1998, 44 (04) : 978 - 981
  • [32] Electrophoresis of a soft charged particle in a sparsely packed bed
    Dey, Bibaswan
    Sekhar, G. P. Raja
    Burada, P. S.
    CHEMICAL ENGINEERING COMMUNICATIONS, 2018, 205 (07) : 991 - 1010
  • [33] Numerical simulation of particle motion and combustion in a packed bed
    Peters, B
    Dziugys, A
    HEAT TRANSFER 1998, VOL 4: GENERAL PAPERS, 1998, : 277 - 282
  • [34] Particle segregation in a screen baffle packed fluidized bed
    Chyang, CS
    Wu, KT
    Ma, TT
    POWDER TECHNOLOGY, 2002, 126 (01) : 59 - 64
  • [35] DEM simulation of cubical particle percolation in a packed bed
    Kou, Mingyin
    Zhou, Heng
    Wu, Shengli
    Shen, Yansong
    POWDER TECHNOLOGY, 2020, 361 : 306 - 314
  • [36] Packed bed characteristics for binary irregular particle systems
    Shibata, T
    Tsuji, T
    Uemaki, O
    Itoh, H
    Watanabe, T
    '96 CHINA-JAPAN SYMPOSIUM ON PARTICUOLOGY, PROCEEDINGS, 1996, : 13 - 18
  • [37] Particle capture and plugging in packed-bed reactors
    Narayan, R
    Coury, JR
    Masliyah, JH
    Gray, MR
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (11) : 4620 - 4627
  • [38] Discrete particle simulation of flow structure in gas fluidized bed with particle size distribution
    Zhou, Haosheng
    Lu, Jidong
    Qian, Shizhi
    Ranshao Kexue Yu Jishu/Journal of Combustion Science and Technology, 1999, 5 (03): : 270 - 275
  • [39] Liquid flow rate distribution in trickle bed with non-uniformly packed structure
    Li, MS
    Bando, Y
    Suzuki, K
    Yasuda, K
    Nakamura, M
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2000, 33 (02) : 211 - 216
  • [40] Toward the Quantitative Evaluation of an Activated Carbon Particle Electrode Performance in a Packed-Bed System
    Wang, Lizhang
    Kong, Yan
    Wei, Dongyang
    Yang, Shengxiang
    Chen, Qing
    Kong, Ying
    Li, Peng
    Ting, Yen-Peng
    Ong, Choon Nam
    CHEMELECTROCHEM, 2017, 4 (10): : 2464 - 2468