Novel gas fluidized bed stirred media mill: Design and performance of a prototype

被引:0
|
作者
Sadler, LY
Odom, JM
Hood, E
机构
[1] Department of Chemical Engineering, University of Alabama, Tuscaloosa, AL
[2] Chemical Engineering, University of Alabama, Tuscaloosa, AL
[3] Mechanical Engineering, Southern University, Baton Rouge, LA
[4] Department of Chemical Engineering, University of Alabama, Box 870203, Tuscaloosa
关键词
comminution; stirred media; gas; fluidized bed; design; performance; efficiency;
D O I
10.1016/S0032-5910(96)03151-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The performance of a prototype novel gas fluidized bed stirred media mill was compared with that of conventional stirred media mills. The gas fluidized bed stirred media mill concept is thought to offer the advantages of reduced viscous dissipation of energy into the suspending fluid, continuous removal of product fines, and comminution in a dry environment. The test results confirm reduced power consumption relative to the liquid suspension stirred media mill. The energy efficiency (m(2) of new surface generated per kilowatt hour of milling energy supplied) of the prototype was found to be less than that of the liquid suspension mill, but it was greater than when the mill was operated without liquid suspension or air fluidization. Resources did not permit optimization of the mechanical design or operating conditions of the mill. With more work devoted to the concept, higher efficiencies could probably be realized.
引用
收藏
页码:37 / 43
页数:7
相关论文
共 50 条
  • [1] Pressure drop in the gas-solid stirred fluidized bed
    Li, Fan
    Feng, Lian-Fang
    Gu, Xue-Ping
    Wang, Kai
    Liu, Bo
    Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2002, 16 (04): : 384 - 388
  • [2] Hydrodynamic performance of a novel design of pressurized fluidized bed combustor
    Wang, Alan L. T.
    Stubington, John F.
    Xu, Jiangang
    JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2006, 128 (02): : 111 - 117
  • [3] INFLUENCE OF GAS DISTRIBUTOR DESIGN ON THE PERFORMANCE OF FLUIDIZED BED REACTOR.
    Bauer, Werner
    Werther, Joachim
    Emig, Gerhard
    German Chemical Engineering, 1981, 4 (05): : 291 - 298
  • [4] Performance comparison of stirred media mill and ball (BOND) mill in bauxite grinding
    Hacifazlioglu, Hasan
    Korkmaz, Abdul Vahap
    PARTICULATE SCIENCE AND TECHNOLOGY, 2020, 38 (04) : 404 - 408
  • [5] Performance of a fluidized bed jet mill as a function of operating parameters
    Benz, M
    Herold, H
    Ulfik, B
    INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 1996, 44-5 : 507 - 519
  • [6] Bed expansion and fluctuation in cylindrical gas solid fluidized beds with stirred promoters
    Sahoo, Abanti
    ADVANCED POWDER TECHNOLOGY, 2011, 22 (06) : 753 - 760
  • [7] Enhancement of stirred media mill performance by a new mixed media grinding strategy
    Patel, Chetankumar M.
    Chakraborty, Mousumi
    Murthy, Z. V. P.
    JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2014, 20 (04) : 2111 - 2118
  • [8] THE EFFECTS OF FLUIDIZING GAS HUMIDITY ON GAS-SOLID STIRRED FLUIDIZED-BED OPERATION
    TAKAHASHI, T
    KASENO, S
    FUKUI, J
    KAGAKU KOGAKU RONBUNSHU, 1989, 15 (04) : 781 - 787
  • [9] Gas-solid hydroxyethylation of potato starch in a stirred vibrating fluidized bed reactor
    Kuipers, NJM
    Stamhuis, EJ
    Beenackers, AACM
    STARCH-STARKE, 1996, 48 (01): : 22 - 29
  • [10] Numerical simulation of flow behavior of particles in a gas-solid stirred fluidized bed
    Wang, Shuyan
    Chen, Yujia
    Jia, Yubin
    Tian, Ruichao
    Sun, Qiji
    Fan, Jiawei
    Ma, Yimei
    POWDER TECHNOLOGY, 2018, 338 : 119 - 128