Kinetics of the Catalytic Decomposition of N2O over Bed Materials from Industrial Circulating Fluidized-Bed Boilers Burning Biomass Fuels and Wastes

2005 ◽  
Vol 19 (6) ◽  
pp. 2340-2349 ◽  
Author(s):  
Vesna Barišić ◽  
Fredrik Klingstedt ◽  
Pia Kilpinen ◽  
Mikko Hupa
Keyword(s):  
Fluidized Bed ◽  
Circulating Fluidized Bed ◽  
Catalytic Decomposition ◽  
Biomass Fuels ◽  
Bed Materials ◽  
Fluidized Bed Boilers ◽  
Kinetics Of

Catalytic Decomposition of N2O over the Bed Material from Circulating Fluidized-Bed (CFB) Boilers Burning Biomass Fuels and Wastes

2004 ◽  
Vol 18 (6) ◽  
pp. 1909-1920 ◽  
Author(s):  
Vesna Barišić ◽  
Ahmad Kalantar Neyestanaki ◽  
Fredrik Klingstedt ◽  
Pia Kilpinen ◽  
Kari Eränen ◽  
...  
Keyword(s):  
Fluidized Bed ◽  
Circulating Fluidized Bed ◽  
Catalytic Decomposition ◽  
Biomass Fuels ◽  
Bed Material

scholarly journals Modelling of dynamics of combustion of biomass in fluidized beds

2004 ◽  
Vol 8 (2) ◽  
pp. 107-126 ◽  
Author(s):  
Jaakko Saastamoinen
Keyword(s):  
Particle Size ◽  
Fluidized Bed ◽  
Circulating Fluidized Bed ◽  
Fuel Mixture ◽  
Linear Increase ◽  
Fuel Feed ◽  
New Process ◽  
Fuel Particles ◽  
The Stability ◽  
Fluidized Bed Boilers

New process concepts in energy production and biofuel, which are much more reactive than coal, call for better controllability of the combustion in circulating fluidized bed boilers. Simplified analysis describing the dynamics of combustion in fluidized bed and circulating fluidized bed boilers is presented. Simple formulas for the estimation of the responses of the burning rate and fuel inventory to changes in fuel feeding are presented. Different changes in the fuel feed, such as an impulse, step change, linear increase and cyclic variation are considered. The dynamics of the burning with a change in the feed rate depends on the fuel reactivity and particle size. The response of a fuel mixture with a wide particle size distribution can be found by summing up the effect of different fuel components and size fractions. Methods to extract reaction parameters form dynamic tests in laboratory scale reactors are discussed. The residence time of fuel particles in the bed and the resulting char inventory in the bed decrease with increasing fuel reactivity and differences between coal and biomass is studied. The char inventory affects the stability of combustion. The effect of char inventory and oscillations in the fuel feed on the oscillation of the flue gas oxygen concentration is studied by model calculation. A trend found by earlier measurements is explained by the model.

Ten residual biomass fuels for circulating fluidized-bed gasification

2001 ◽  
Vol 20 (1) ◽  
pp. 45-56 ◽  
Author(s):  
A van der Drift ◽  
J van Doorn ◽  
J.W Vermeulen
Keyword(s):  
Fluidized Bed ◽  
Circulating Fluidized Bed ◽  
Biomass Fuels ◽  
Residual Biomass
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