A simplified model for particle internal temperature calculation in fluidized bed

被引:0
|
作者
Rafael F. [1 ]
Jeferson S. [1 ]
Rodrigo D. [1 ]
机构
[1] Federal University of Rio Grande, Rio Grande
关键词
Fluidized-bed; Heat-transfer; Multiphase-flow; Transient-condution;
D O I
10.4028/www.scientific.net/DDF.396.135
中图分类号
学科分类号
摘要
Thermal mechanism analysis of heat exchange between a gas phase flow and the internal region of a particulate is still a subject of interest among researchers, mainly due to its complexity and lack of a simplified (in terms of computational effort) solution. Main goal of present work is to develop a simplified model capable of predict internal particle temperature, as a function of its surface temperature and flow conditions, in a fluidized bed, transporting spherical particles. Proposed model was implemented in C++ programming language and an algorithm was developed to solve two energy equations, for gas and particulate phases, and an algebraic equation to determine internal particle temperature. As a result, predicted particle temperature decreases while gas temperature rises. At approximate 12 m, both temperatures reach the equilibrium at 755 K which remains unaltered up to the riser outlet section. Energy balance verification, between inlet and outlet riser sections, showed that proposed model and balance calculated temperatures agree with a difference of 1.804 x 10-11 kW on the outlet. In terms of internal particle temperature, results showed that it remains higher than surface temperature from riser entrance up to approximated 32.8 m. After this point it reaches surface temperature, which already is in equilibrium with the gas phase temperature. © 2019 Trans Tech Publications Ltd, Switzerland.
引用
收藏
页码:135 / 144
页数:9
相关论文
共 50 条
  • [41] A study on the particle temperature in a conical fluidized bed using infrared thermography
    Hamada Mohamed Abdelmotalib
    Ik-Tae Im
    Journal of Mechanical Science and Technology, 2018, 32 : 4529 - 4534
  • [42] Modeling the temperature in coal char particle during fluidized bed combustion
    Manovic, Vasilije
    Komatina, Mirko
    Oka, Simeon
    FUEL, 2008, 87 (06) : 905 - 914
  • [43] Fluidized bed spray granulation-A new model for the description of particle wetting and of temperature and concentration distribution
    Heinrich, Stefan
    Mörl, Lothar
    Chemical Engineering and Processing, 1999, 38 (4-6): : 635 - 663
  • [44] A MATHEMATICAL CALCULATION MODEL OF THE COOLING INTENSITY OF A PROBE IN THE FLUIDIZED-BED
    GALOVIC, A
    STROJARSTVO, 1987, 29 (05): : 247 - 254
  • [45] A Novel Simplified Distributor Model of Fluidized Bed Based on the Porous Media Theory
    Li, Bin
    Liu, Wei
    Kong, Xiangwei
    Zhang, Shuangtian
    FRONTIERS OF MANUFACTURING AND DESIGN SCIENCE IV, PTS 1-5, 2014, 496-500 : 715 - 718
  • [46] Model for Calculation of Agglomerate Sizes of Nanoparticles in a Vibro-fluidized Bed
    Wang, Hui
    Zhou, Tao
    Yang, Jing-si
    Wang, Jin-jin
    Kage, Hiroyuki
    Mawatari, Yoshihide
    CHEMICAL ENGINEERING & TECHNOLOGY, 2010, 33 (03) : 388 - 394
  • [47] Optimizing calculation of particle size distribution of feeding coal for circulating fluidized bed boiler
    Ma, Suxia
    Chang, Wei-ming
    Zhang, Jian-chun
    Luo, Ding-ling
    APPLIED THERMAL ENGINEERING, 2015, 87 : 463 - 470
  • [48] A particle population balancing model for a circulating fluidized bed combustion system
    Redemann, K.
    Hartge, E. -U.
    Werther, Joachim
    POWDER TECHNOLOGY, 2009, 191 (1-2) : 78 - 90
  • [49] PARTICLE SEGREGATION IN A FLUIDIZED-BED
    CHEN, JLP
    KEAIRNS, DL
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1975, 53 (04): : 395 - 402
  • [50] A revised mono-dimensional particle bed model for fluidized beds
    Mazzei, L
    Lettieri, P
    Elson, T
    Colman, D
    CHEMICAL ENGINEERING SCIENCE, 2006, 61 (06) : 1958 - 1972