Comparison of three vibrational modes (twist, vertical and horizontal) for fluidization of fine particles

被引:28
作者
Mawatari, Y [1 ]
Koide, T
Tatemoto, Y
Takeshita, T
Noda, K
机构
[1] Shizuoka Univ, Dept Mat Sci, Hamamatsu, Shizuoka 4328561, Japan
[2] Shizuoka Univ, Dept Chem Engn, Hamamatsu, Shizuoka 4328561, Japan
关键词
fluidization; fine particle; vibrational mode;
D O I
10.1163/15685520052384998
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effects of three vibrational modes (twist, vertical and horizontal) on flow patterns are discussed. The particles used are four powders (glass beads, 6-100 mum), which are Geldart group A or group C. The fluidity of particles is evaluated with vibration strength (Lambda), minimum fluidization velocity (u(mf)), void fraction and flow patterns in the bed. The effect of vibrational mode on the flow patterns appears in whole bed motion, which is horizontal rotation or vertical rotation caused by twist or horizontal vibrational mode, respectively. For 60 and 100 mum particles, bubble behavior is dominant higher than u(mf). Thus, the effects of vibrational mode on the flow patterns in the bed and u(mf) are not significant. For 30 mum particles, the horizontal rotation or vertical rotation are caused by twist or horizontal vibrational mode, respectively. For 6 mum particles, vertical rotation was not observed. When horizontal vibration is added to the bed, the lower limit of gas velocity for channel breakage for 6 Irm is the lowest among the three vibrational modes. It is considered that the horizontal vibration affects channel breakage as the shear force.
引用
收藏
页码:157 / 168
页数:12
相关论文
共 22 条
[1]  
BRATU E, 1971, BRIT CHEM ENG PR TEC, V16, P691
[2]   EFFECT OF INTERPARTICLE FORCES ON THE HYDRODYNAMIC BEHAVIOR OF FLUIDIZED AEROGELS [J].
CHAOUKI, J ;
CHAVARIE, C ;
KLVANA, D .
POWDER TECHNOLOGY, 1985, 43 (02) :117-125
[3]   SOUND-ASSISTED AERATION OF BEDS OF COHESIVE SOLIDS [J].
CHIRONE, R ;
MASSIMILLA, L .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (08) :1185-1194
[4]   HYDRODYNAMIC ASPECTS OF CONVENTIONAL AND VIBROFLUIDIZED BEDS - A COMPARATIVE-EVALUATION [J].
ERDESZ, K ;
MUJUMDAR, AS .
POWDER TECHNOLOGY, 1986, 46 (2-3) :167-172
[5]   TYPES OF GAS FLUIDIZATION [J].
GELDART, D .
POWDER TECHNOLOGY, 1973, 7 (05) :285-292
[6]   AERODYNAMICS OF A VIBRATED FLUID BED [J].
GUPTA, R ;
MUJUMDAR, AS .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1980, 58 (03) :332-338
[7]   Prediction of agglomerate sizes in bubbling fluidized beds of group C powders [J].
Iwadate, Y ;
Horio, M .
POWDER TECHNOLOGY, 1998, 100 (2-3) :223-236
[8]  
KATO K, 1999, J SOC POWDER TECHNOL, V36, P616
[9]   Fluidization of potato starch in a stirred vibrating fluidized bed [J].
Kuipers, NJM ;
Stamhuis, EJ ;
Beenackers, AACM .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (11) :2727-2732
[10]   THE EFFECT OF VIBRATION ON THE FLUIDIZATION BEHAVIOR OF SOME COHESIVE POWDERS [J].
MARRING, E ;
HOFFMANN, AC ;
JANSSEN, LPBM .
POWDER TECHNOLOGY, 1994, 79 (01) :1-10