Effects of pressure on the minimum fluidization velocity and bubble properties in a gas-solid fluidized bed

被引:0
|
作者
Kang, SH
Kang, Y [1 ]
Han, KH
Jin, GT
机构
[1] Chungnam Natl Univ, Sch Chem Engn, Taejon 305764, South Korea
[2] KIER, Clean Energy Res Dept, Taejon 305343, South Korea
关键词
bubble properties; pressurized fluidized bed; pressure fluctuations; cross-correlation function; power spectral analysis;
D O I
暂无
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Effects of pressure on the bubble properties, such as pierced length, rising velocity, and frequency, and on the minimum fluidization velocity were determined in gas-solid fluidized beds by means of a crosscorrelation function and a power spectrum of pressure fluctuations. The pressure fluctuations along the axial distance above the distributor were measured by a differential pressure transducer in the pressurized gas-solid fluidized bed [0.1 m (I.D.) 2.0 m (high)]. Sand and silica sand, having mean diameters of 0.59 and 0.18 mm, respectively, and each having an apparent density of 2590 kg/m(3), were used as bed materials. The pierced length and rising velocity of the bubbles decreased, but the bubble frequency increased, upon an increase in the system pressure. The minimum fluidization velocity of the particles decreased considerably upon increasing the system pressure. The bubble flow behavior in the bed became more periodic and predictable as the bed pressure increased.
引用
收藏
页码:330 / 336
页数:7
相关论文
共 50 条
  • [21] Prediction of minimum fluidization velocity of gas-solid fluidized beds by pressure fluctuation measurements - Analysis of the standard deviation methodology
    Felipe, C. A. S.
    Rocha, S. C. S.
    POWDER TECHNOLOGY, 2007, 174 (03) : 104 - 113
  • [22] DETERMINATION OF MINIMUM FLUIDIZATION VELOCITY BY THE STATISTICAL-ANALYSIS OF PRESSURE-FLUCTUATIONS IN A GAS SOLID FLUIDIZED-BED
    HONG, SC
    JO, BR
    DOH, DS
    CHOI, CS
    POWDER TECHNOLOGY, 1990, 60 (03) : 215 - 221
  • [23] Effect of Gas Distributor Structure on Fluidization Characteristics in a Gas-Solid Fluidized Bed
    Jang Kwangbyol
    Feng Yali
    Li Haoran
    ChinaPetroleumProcessing&PetrochemicalTechnology, 2020, 22 (02) : 102 - 110
  • [24] PREDICTION OF MINIMUM CARRYING VELOCITY OF PARTICLES IN A CONTINUOUS GAS-SOLID FLUIDIZED-BED
    RAGHAVAN, P
    BARARI, HB
    SENGUPTA, P
    INDIAN JOURNAL OF TECHNOLOGY, 1979, 17 (01): : 32 - 34
  • [25] Critical fluidization behavior of gas-solid fluidized bed at elevated temperatures
    Huazhong Univ of Science and, Technology, Wuhan, China
    Ranshao Kexue Yu Jishu, 4 (315-321):
  • [26] Effect of Gas Distributor Structure on Fluidization Characteristics in a Gas-Solid Fluidized Bed
    Kwangbyol, Jang
    Yali, Feng
    Haoran, Li
    CHINA PETROLEUM PROCESSING & PETROCHEMICAL TECHNOLOGY, 2020, 22 (02) : 102 - 110
  • [27] Particle velocity in a dense gas-solid fluidized bed
    Wang, Qicheng
    Zhang, Kai
    Yang, Kuanli
    Jiang, Jianchun
    International Journal of Chemical Reactor Engineering, 2008, 6
  • [28] Particle Velocity in a Dense Gas-Solid Fluidized Bed
    Wang, Qicheng
    Zhang, Kai
    Yang, Kuanli
    Jiang, Jianchun
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2008, 6
  • [29] A study on fluidization of activated carbon particles in gas-solid fluidized bed
    Nikam, S.
    Mandal, D.
    INDIAN CHEMICAL ENGINEER, 2021, 63 (05) : 478 - 490
  • [30] Prediction and evaluation of binary particle fluidization in gas-solid fluidized bed
    Du, Shanlin
    Li, Qian
    Cai, Weihua
    CHEMICAL ENGINEERING JOURNAL, 2024, 488