scholarly journals Particle Velocity and Concentration Profiles in Freeboard of Gas-solid Fluidized Bed and Proposal of a New Elutriation Model with Particle Collision.

2000 ◽  
Vol 37 (3) ◽  
pp. 168-175
Author(s):  
Hiroyuki KAGE ◽  
Hidekazu OGAWA ◽  
Takaya KUWAMOTO ◽  
Takuya SHIGEHIRO ◽  
Hironao OGURA ◽  
...  
2021 ◽  
Vol 381 ◽  
pp. 55-67
Author(s):  
Feng Jiang ◽  
Hongyu Wang ◽  
Yi Liu ◽  
Guopeng Qi ◽  
Ahmed Esmail Al-Rawni ◽  
...  

2017 ◽  
Vol 314 ◽  
pp. 346-354 ◽  
Author(s):  
Chengxiao Song ◽  
Daoyin Liu ◽  
Jiliang Ma ◽  
Xiaoping Chen

1995 ◽  
pp. 661-668 ◽  
Author(s):  
J.C. Bi ◽  
H. Matsuo ◽  
S. Uemiya ◽  
T. Kojima

Author(s):  
Seong W. Lee ◽  
Yun Liu

The transient solid velocity analysis in fluidized bed combustor (FBC) freeboard has been critical in the past two decades (Haidin et al 1998). The FBC cold model (6-in ID) was designed and fabricated. The solid transient velocity in FBC freeboard was measured and analyzed with the assistance of the advanced instrumentation. The laser-based Particle Image Velocimetry (PIV) was applied to the FBC cold model to visualize the transient solid velocity. A series of transient particle velocity profiles were generated for factorial analysis. In each profile, the particle velocity vectors for 100 position points were in the format of Vx and Vy. Analysis of Variance (ANOVA) was used to determine the significant factors that affect the transient particle velocities, time, and position coordinates. Then, the 1010factorial design method was used to develop a specific empirical model of transient particle velocity in FBC freeboard which was in the shape of Vx = f1(t, x, y), and Vy = f2(t, x, y). This unique factorial analysis method was proved to be very effective and practical to evaluate the experimental conditions and analyze the experimental results in FBC systems.


1967 ◽  
Vol 12 (4) ◽  
pp. 274-280
Author(s):  
V. V. Klimenko ◽  
L. A. Akopyan ◽  
A. N. Planovskii

Author(s):  
P. Fede ◽  
G. Moula ◽  
A. Ingram ◽  
T. Dumas ◽  
O. Simonin

The present paper is dedicated to numerical and experimental study of the hydrodynamic of a non-reactive isothermal pressurized fluidized bed. Experimental data have been obtained using PEPT technique allowing to track a particle trajectory inside a dense fluidized bed. A specific post-processing approach has been developed to compute the Eulerian time-averaged particle velocity field. The comparison with 3-dimensional numerical model predictions shows a good agreement in the core of the fluidized bed. In contrast, in the near wall region the numerical model overestimate the downward particle velocity. The modification of particle phase wall boundary condition improves the numerical predictions.


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