Factors affecting density transients in a fluidized bed

AIChE Journal ◽  
1959 ◽  
Vol 5 (2) ◽  
pp. 169-174 ◽  
Author(s):  
James M. Dotson
1993 ◽  
Vol 93 (1-3) ◽  
pp. 101-109 ◽  
Author(s):  
R. Wesdyk ◽  
Y.M. Joshi ◽  
J. De Vincentis ◽  
A.W. Newman ◽  
N.B. Jain

2015 ◽  
Vol 152 ◽  
pp. 107-112 ◽  
Author(s):  
Jaeshik Chung ◽  
Eunhoo Jeong ◽  
Jae Woo Choi ◽  
Seong Taek Yun ◽  
Sung Kyu Maeng ◽  
...  

2019 ◽  
Vol 9 (8) ◽  
pp. 1576 ◽  
Author(s):  
Chiou-Liang Lin ◽  
Jing-Dong Chou ◽  
Wang-Chang Weng

In this study, a two-stage fluidized-bed gasification system was used to determine the distribution of heavy metal contaminants in simulative waste and evaluate the effect of the bed operating temperature, Equivalence ratio (ER), and Steam/Biomass ratio (S/B) in stage 1. The heavy metal concentrations in bed materials and fly ash were measured in two stages. The results show that as the operating temperature of stage 1 increased, the quantity of heavy metals entrapped by stage 1 bed material decreased, while that captured by stage 2 bed material increased. The less volatile Cu was mostly entrapped in stage 1 bed material. The ER and S/B results show that increasing the ER and S/B caused a slight increase in the concentrations of heavy metals entrapped in stage 1 and stage 2 bed materials. However, the influences of ER and S/B were less than that of temperature. The major factors affecting the heavy metal distribution were the operating temperature and the heavy metal volatility. Stage 2 bed material was able to entrap gaseous heavy metals or particles containing heavy metals by particle filtration and chemical adsorption. Thus, the heavy metals (Cu and Pb) had a downward trend after passing through stage 2.


2016 ◽  
Vol 6 (3) ◽  
pp. 1029-1034 ◽  
Author(s):  
A. Shukrie ◽  
S. Anuar ◽  
A. N. Oumer

Fluidized bed combustion (FBC) has been recognized as one of the suitable technologies for converting a wide variety of biomass fuels into energy. One of the key factors affecting the successful operation of fluidized bed combustion is its distributor plate design. Therefore, the main purpose of this article is to provide a critical overview of the published studies that are relevant to the characteristics of different fluidized bed air distributor designs. The review of available works display that the type of distributor design significantly affects the operation of the fluidized bed i.e., performance characteristics, fluidization quality, air flow dynamics, solid pattern and mixing caused by the direction of air flow through the distributors. Overall it is observed that high pressure drop across the distributor is one of the major draw backs of the current distributor designs. However, fluidization was stable in a fluidized bed operated at a low perforation ratio distributor due to the pressure drop across the distributor, adequate to provide uniform gas distribution. The swirling motion produced by the inclined injection of gas promotes lateral dispersion and significantly improves fluidization quality. Lastly, the research gaps are highlighted for future improvement consideration on the development of efficient distributor designs.


2014 ◽  
Vol 140 (1) ◽  
pp. 77-83 ◽  
Author(s):  
Rowena M. Briones ◽  
Mark Daniel G. de Luna ◽  
Chia-Chi Su ◽  
Ming-Chun Lu

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