Solid circulation characteristics in an internally circulating fluidized bed with orifice-type draft tube

2002 ◽  
Vol 19 (5) ◽  
pp. 911-916 ◽  
Author(s):  
Sang Done Kim ◽  
Yo Han Kim ◽  
Seon Ah Roh ◽  
Dong Hyun Lee
2012 ◽  
Vol 600 ◽  
pp. 261-264
Author(s):  
Teng Ge Mi ◽  
Ying Zhao ◽  
Chang Qing Dong ◽  
Wei Liang Cheng

In this paper, a dual fluidized bed has been established. The effect of bed material build-up height and gas velocity on the solid circulation rate of CFB (circulating fluidized bed) and BFB (bubble fluidized bed) has been studied. The results show that the solid circulation rate is increased with the increasing of gas velocity Uc and the bed material build-up height. Bed material build-up height of BFB and CFB is changed with the changing of gas velocity Uc. The bed material heights of CFB and BFB have been also investigated in this experiment.


2014 ◽  
Vol 52 (4) ◽  
pp. 522-529 ◽  
Author(s):  
Dong-Ho Lee ◽  
Sung-Ho Jo ◽  
Gyoung-Tae Jin ◽  
Chang-Keun Yi ◽  
Ho-Jung Ryu ◽  
...  

1999 ◽  
Vol 16 (5) ◽  
pp. 618-623 ◽  
Author(s):  
Hong-Sik Ahn ◽  
Woon-Jae Lee ◽  
Sang-Done KimDg ◽  
Byung-Ho Song

2015 ◽  
Vol 12 (04) ◽  
pp. 1540005 ◽  
Author(s):  
Ravi Gujjula ◽  
Narasimha Mangadoddy

This paper presents a numerical study of gas and solid flow in an internally circulating fluidized bed (ICFB). Two-fluid Eulerian model with kinetic theory of granular flow option for solid phase stress closure and various drag laws were used to predict the hydrodynamic behavior of ICFB. 2D and 3D geometries were used to run the simulations. The 2D simulation results by various drag laws show that the Arastoopour and Gibilaro drag models able to predict the fluidization dynamics in terms of flow patterns, void fractions and axial velocity fields close to the experimental data. The effect of superficial gas velocity, presence of draft tube on solid hold-up distribution, solid circulation pattern, and variations in gas bypassing fraction for the 3D ICFB are investigated. The mechanism governing the solid circulation and solids concentration in an ICFB has been explained based on gas and solid dynamics obtained from the simulations. Predicted total granular temperature distributions in the draft tube and annular zones qualitatively agree with experimental data. The total granular temperature tends to increase with increasing solids concentration in the dilute region (ε < 0.1) and decreases with an increase of solids concentration in the dense region (ε > 0.1). In the dense zone, the decreasing trend in the granular temperature is mainly due to the reduction of the mean free path of the solid particles.


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