COMBUSTION OF VOLATILE MATTER IN FLUIDIZED BEDS.

被引:0
|
作者
Atimtay, Aysel T. [1 ]
机构
[1] Middle East Technical Univ, Ankara, Turk, Middle East Technical Univ, Ankara, Turk
来源
关键词
CARBON - Combustion - CHEMICAL OPERATIONS - Fluidization;
D O I
暂无
中图分类号
学科分类号
摘要
The times required for burnout of volatile materials from coal particles in fluidized beds have been investigated for different particle sizes, superficial gas velocities, volatile matter contents, and masses charged. The results show that the volatile material takes about 3-12 s to burn for particle sizes from 1. 53 to 3. 06 mm and fluidizing velocities from 0. 38 to 0. 58 m/s. The radial velocity of the volatiles coming out of each particle was found to be close to U//m//f and to increase with particle size. The presence of volatiles in the coal particles increases the combustion rate of the particles of char remaining after volatiles have left.
引用
收藏
页码:452 / 456
相关论文
共 50 条
  • [31] RATE OF GAS EXCHANGE BETWEEN ADJACENT FLUIDIZED BEDS.
    Maskaev, V.K.
    Petrov, V.I.
    Baskakov, A.P.
    Shishko, I.I.
    Theoretical Foundations of Chemical Engineering, 1981, 15 (01) : 58 - 62
  • [32] AXIAL DISPERSION CHARACTERISTICS OF THREE PHASE FLUIDIZED BEDS.
    Kim, S.D.
    Kim, C.H.
    Journal of Chemical Engineering of Japan, 1983, 16 (03): : 172 - 178
  • [33] COMBUSTION OF COAL IN FLUIDIZED BEDS
    ROBERTS, AM
    ENERGIA ES ATOMTECHNIKA, 1971, 24 (04): : 159 - &
  • [34] COMBUSTION IN FLUIDIZED-BEDS
    DRY, RJ
    LANAUZE, RD
    CHEMICAL ENGINEERING PROGRESS, 1990, 86 (07) : 31 - 47
  • [35] STUDY OF THE HYDRODYNAMICAL CHARACTERISTICS OF THREE-PHASE FLUIDIZED BEDS.
    Hu Tsung-ting
    Zhang Ying
    Huang Lu
    Chi Tsun-chien
    Tianjin Daxue Xuebao (Ziran Kexue yu Gongcheng Jishu Ban)/Journal of Tianjin University Science and Technology, 1983, (01): : 15 - 24
  • [36] COAL COMBUSTION IN FLUIDIZED BEDS
    WRIGHT, SJ
    CHEMIE INGENIEUR TECHNIK, 1968, 40 (21-2) : 1106 - &
  • [37] TIME-DEPENDENT BEHAVIOR OF BUBBLE VOLUME IN FLUIDIZED BEDS.
    Clough, David E.
    Weimer, Alan W.
    Industrial & Engineering Chemistry, Fundamentals, 1985, 24 (02): : 235 - 241
  • [38] Simulation study of instantaneous heat trace in bubbling fluidized beds.
    Sharma, KR
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2002, 223 : U481 - U481
  • [39] The mobility of fine particles in uniform gas-fluidized beds.
    Valverde, JM
    Castellanos, A
    Quintanilla, MAS
    POWDERS AND GRAINS 2001, 2001, : 573 - 576
  • [40] The effect of particle aggregation on the collapse of gas-fluidized beds.
    Castellanos, A
    Valverde, JM
    Quintanilla, MAS
    Mills, P
    POWDERS AND GRAINS 2001, 2001, : 569 - 572