scholarly journals Layer formation mechanism of K-feldspar in bubbling fluidized bed combustion of phosphorus-lean and phosphorus-rich residual biomass

2019 ◽  
Vol 248 ◽  
pp. 545-554 ◽  
Author(s):  
Katharina Wagner ◽  
Gustav Häggström ◽  
Nils Skoglund ◽  
Juraj Priscak ◽  
Matthias Kuba ◽  
...  
1987 ◽  
Author(s):  
E J Anthony ◽  
H A Becker ◽  
R K Code ◽  
R W McCleave ◽  
J R Stephenson

Fuel ◽  
2014 ◽  
Vol 128 ◽  
pp. 390-395 ◽  
Author(s):  
Hao Wu ◽  
Tor Laurén ◽  
Patrik Yrjas ◽  
Pasi Vainikka ◽  
Mikko Hupa

2016 ◽  
Vol 4 (2) ◽  
pp. 2278-2290 ◽  
Author(s):  
Gabriel M. Faé Gomes ◽  
Caterina Philipssen ◽  
Eduardo K. Bard ◽  
Leandro Dalla Zen ◽  
Guilherme de Souza

2016 ◽  
Vol 30 (3) ◽  
pp. 2227-2232 ◽  
Author(s):  
Hanbing He ◽  
Xiaoyan Ji ◽  
Dan Boström ◽  
Rainer Backman ◽  
Marcus Öhman

Author(s):  
A. J. Minchener

Fluidized bed combustion (FBC) in various forms has been used to burn all types of coal, coal waste and a wide variety of other fuels, either singly or cofired with coal. FBC boilers are currently available commercially in the capacity range from 1 MWth to over 250 MWe and continue to be adopted for a variety of commercial, industrial and power generation applications. There are two main derivatives of FBC, namely bubbling fluidized bed combustion (BFBC) and circulating fluidized bed combustion (CFBC). There are also several hybrid systems and pressurized versions of both BFBC and CFBC. The status of these different systems, with some now fully commercial and some still under development, is described, with projections made for future development requirements and market opportunities.


2014 ◽  
Vol 699 ◽  
pp. 660-665
Author(s):  
M. Fadhil ◽  
M.S. Aris ◽  
A.H. Abbas ◽  
A.B.A. Ibrahim ◽  
N. Aniza

Research on the thermodynamic behavior of sand beds was carried out using a commercial computational dynamic package. The work involved simulating, with the use of the Ergun equation, the air flow through a two-dimensional bubbling bed reactor to predict the bed character whilst considering the major effective function (particle size, particle density, bed height and reactor width). The Minimum Fluidization Velocity (Umf) values were then calculated before the optimum value of Umfneeded to ensure a workable Bubbling Fluidize Bed Combustor (BFBC) system. The effects of using different Umfvalues on the flow behavior were also investigated using the numerical approach at different times. The results from these investigations indicate that the bubbling region in the fluidized bed combustion can be correlated to the sand bed expansion with minimum errors and assist in enhancing the combustion efficiency by supplying the required volume of oxygen into the system.


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