Experimental investigation of horizontal tube immersed in gas-solid fluidized bed of large particles using artificial neural network

被引:17
|
作者
Kamble, L. V. [1 ]
Pangavhane, D. R. [2 ]
Singh, T. P. [1 ]
机构
[1] SIT, Pune 412115, Maharashtra, India
[2] Prestige Inst Engn & Sci, Indore 452010, Madhya Pradesh, India
关键词
Fluidized bed; Horizontal tube; Heat transfer coefficient; Large particle; Artificial neural network; HEAT-TRANSFER; PREDICTION;
D O I
10.1016/j.ijheatmasstransfer.2013.11.073
中图分类号
O414.1 [热力学];
学科分类号
摘要
The average heat transfer coefficient is determined between the fluidizing bed and horizontal tube surface immersed in the bed of large particles. The mustard (d(p) = 1.8 mm), raagi (d(p) = 1.4 mm) and bajara (d(p) = 2.0 mm) were used as particles in the bed. The effect of fluidizing gas velocity on the heat transfer coefficient in the immersed horizontal tube is discussed. The results obtained by experiment are compared with correlations and artificial neural network modeling. The parameters particle size, temperature difference between bed and immersed surface were used in the neural network modeling along with fluidizing velocity. The feed-forward network with back propagation structure implemented using Levenberg-Marquardt's learning rule in the neural network approach. The network's performance tested with regression analysis. The predictions of the artificial neural network were found to be in good agreement with the experiment's values, as well as the results achieved by the developed correlations. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:719 / 724
页数:6
相关论文
共 50 条
  • [42] EXPERIMENTAL INVESTIGATION ABOUT SOLID-STATE-FERMENTATION IN A GAS-SOLID FLUIDIZED-BED
    BEHNS, W
    EBENAU, B
    FRIEDRICH, K
    GRAU, W
    HAIDA, H
    KUNNE, HJ
    LAKOWITZ, R
    CHEMISCHE TECHNIK, 1993, 45 (05): : 375 - 382
  • [43] MAXIMUM HEAT-TRANSFER COEFFICIENT BETWEEN A HORIZONTAL TUBE AND A GAS-SOLID FLUIDIZED-BED
    GREWAL, NS
    SAXENA, SC
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1981, 20 (01): : 108 - 116
  • [44] Numerical study of the influence of horizontal tube banks on the hydrodynamics of a dense gas-solid bubbling fluidized bed
    Sharma, Sanjib K. Das
    Mohan, Ratan
    International Journal of Chemical Reactor Engineering, 2002, 1 (01)
  • [45] Numerical Study of the Influence of Horizontal Tube Banks on the Hydrodynamics of a Dense Gas-Solid Bubbling Fluidized Bed
    Das Sharma, Sanjib K.
    Mohan, Ratan
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2003, 1
  • [46] Heat transfer and hydrodynamics in a gas-solid fluidized bed with vertical immersed internals
    Taofeeq, Haidar
    Al-Dahhan, Muthanna
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2018, 122 : 229 - 251
  • [47] Theoretical Investigation on Apparent Viscosity of Gas-Solid Fluidized Bed
    Yamazaki, Ryohei
    KAGAKU KOGAKU RONBUNSHU, 2018, 44 (03) : 142 - 146
  • [48] Investigation of a Gas-solid Fluidized Bed for Lump Coal Separation
    Zhao, Xiaonan
    Wei, Lubin
    Fu, Yu
    Zhang, Mohan
    Wang, Yiyao
    EXPLORATION AND PROCESSING OF MINERAL RESOURCES, 2014, 868 : 433 - 436
  • [49] Experimental and computational study of gas-solid fluidized bed hydrodynamics
    Taghipour, F
    Ellis, N
    Wong, C
    CHEMICAL ENGINEERING SCIENCE, 2005, 60 (24) : 6857 - 6867
  • [50] Experimental Research on Gas-solid Flow in a Dual Fluidized Bed
    Li, Jun
    Dong, Changqing
    Zhang, Junjiao
    Yang, Yongping
    2009 INTERNATIONAL CONFERENCE ON SUSTAINABLE POWER GENERATION AND SUPPLY, VOLS 1-4, 2009, : 1834 - 1839