NO x and N2O Formation Mechanisms—A Detailed Chemical Kinetic Modeling Study on a Single Fuel Particle in a Laboratory-Scale Fluidized Bed

2001 ◽  
Vol 123 (3) ◽  
pp. 228-235 ◽  
Author(s):  
Gerhard Lo¨ffler ◽  
Dietmar Andahazy ◽  
Christian Wartha ◽  
Franz Winter ◽  
Hermann Hofbauer

NO x (i.e., NO and NO2) and N2O are known as harmful pollutants. In fluidized bed combustion these are formed from the nitrogen in the fuel. To develop effective primary measures reducing the emissions, more knowledge on the mechanism of formation and destruction ongoing in fluidized beds has to be obtained. In this work, a detailed chemistry model is combined with a two-phase model for a stationary fluidized bed to calculate the emissions of a single fuel particle in a laboratory-scale stationary fluidized bed. The single particle model consists of a simple model for the H2O release during drying, a model for the volatiles composition, and a model for the nitrogen chemistry during char combustion. The detailed reaction mechanism consists of a homogeneous part, heterogeneously catalyzed reactions on the bed material, and radical recombination reactions on the solids’ surface. The results confirm that devolatilization and char combustion are of nearly equal importance for NO and N2O formation. During devolatilization, NO is formed from HCN and NH3, while N2O is formed almost exclusively from HCN. During char combustion, NO is mostly formed by heterogeneous oxidation of char nitrogen, while N2O is formed from homogeneous oxidation of HCN. On the other hand, there is also a back coupling of NO on the homogeneous burnout of the carbon containing species, by sensitizing the oxidation of CH4.

Fuel ◽  
1994 ◽  
Vol 73 (7) ◽  
pp. 1098-1102 ◽  
Author(s):  
I GULYURTLU ◽  
H ESPARTEIRO ◽  
I CABRITA

Author(s):  
Franz Winter ◽  
Xin Liu

The attrition behavior of ash produced from two bituminous and one anthracite coal was studied under laboratory-scale circulating fluidized bed combustor (CFBC) conditions. After the ash was produced in the oven, the ash sample with a size range from 0.1 to 1 mm was fed into the hot CFBC, which was heated by electrical heating shells and fluidized by air. The laboratory-scale CFBC was operated with using fine silica sand (40 to 80 μm) as bed material. After a certain time the operation was stopped, all particles were collected and sieving analysis was performed to obtain the actual particle size distribution (PSD) of the coal ash. The operating conditions were changed in a wide range, i.e. the bed temperature from 600 to 850°C, the fluidizing velocity from 1.2 to 2 m/s, the residence time from 60 to 120 min and the design of the cyclone. The effects of operating conditions and coal type were studied and their relative importance is discussed. Elemental analysis of the coal ashes showed that Si and Ca may play an important role during attrition.


Fuel ◽  
1993 ◽  
Vol 72 (5) ◽  
pp. 701
Author(s):  
I. Gulyurtlu ◽  
H. Esparteiro ◽  
I. Cabrita

1996 ◽  
Vol 26 (2) ◽  
pp. 3325-3334 ◽  
Author(s):  
Franz Winter ◽  
Christian Wartha ◽  
Gerhard Löffler ◽  
Hermann Hofbauer

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