Bubbling Fluidized Bed Co-Combustion of Different Sustainable Fuels: Trace Element Behaviour

Author(s):  
N. Wolski ◽  
R. Berger ◽  
J. Maier ◽  
K. R. G. Hein

With this paper the author will show interesting results of the co-combustion of coal in combination with bark and paper sludge in fluidized bed combustion. The results presented were collected during two measurement campaigns at a 30 kW electrically stabilized bubbling fluidized bed. The fluidized bed combustor was compared to large scale combustors in different campaigns before and thus gives an idea of the output of industrial plants. The main focus of the measurements was the behavior of trace elements of Ni Pb, Zn, Cr and Cu with a changing bed material. One bed material was pre-used under the exposure of combustion of a ternary fuel mixture of coal, bark and paper sludge over a long period of time resulting in a bed composition of 2/3 SiO2 and 1/3 Al2O3. The second bed material utilized, which was a sand (primarily SiO2) not used before thus not enriched in any compounds. When comparing the results of all trials three different trace metal partitioning effects were monitored. First an increase in the elemental concentration in the bed material which was primarily due to the higher input concentration with the pre-used bed material which was found for all three alternatives plus a decrease in filter and cyclone concentrations (Ni, Pb). Secondly an increase in all three ash fractions was detected for Cu. The third was a mixture of both with increasing filter concentrations but decreasing cyclone concentrations (Zn, Cr). An attempt was made to link the before primarily to the enrichment in Al-compounds and to a bed capacity of retention. The results presented indicate the need for longer periods of testing even at small scaled facilities if the comparison to large scale facilities is attempted.

Fuel ◽  
2008 ◽  
Vol 87 (10-11) ◽  
pp. 1974-1981 ◽  
Author(s):  
I Nyoman Suprapta Winaya ◽  
Tadaaki Shimizu ◽  
Yousuke Nonaka ◽  
Kazuaki Yamagiwa

Author(s):  
H. J. M. Visser ◽  
S. C. van Lith ◽  
J. H. A. Kiel

In (bubbling) fluidized-bed combustion and gasification of biomass, several potential problems are associated with the inorganic components of the fuel. A major problem area is de-fluidization due to bed agglomeration. The most common found process leading to de-fluidization in commercial-scale installations is “coating-induced” agglomeration. During reactor operation, a coating is formed on the surface of bed material grains and at certain critical conditions (e.g., coating thickness or temperature) sintering of the coatings initiates the agglomeration. In an experimental approach, this work describes a fundamental study on the mechanisms of de-fluidization. For the studied process of bed de-fluidization due to sintering of grain-coating layers, it was found that the onset of the process depends on: a) a critical coating thickness, b) on the fluidization velocity when it is below approx. four times the minimum fluidization velocity and c) on the viscosity (stickiness) of the outside of the grains (coating).


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

2015 ◽  
Vol 140 ◽  
pp. 57-66 ◽  
Author(s):  
Chinnathan Areeprasert ◽  
Antonio Coppola ◽  
Massimo Urciuolo ◽  
Riccardo Chirone ◽  
Kunio Yoshikawa ◽  
...  

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

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.


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