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

Author:

Lo¨ffler Gerhard1,Andahazy Dietmar1,Wartha Christian1,Winter Franz1,Hofbauer Hermann1

Affiliation:

1. Institute of Chemical Engineering, Fuel Technology, and Environmental Technology, Vienna University of Technology, A-1060 Vienna, Austria

Abstract

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.

Publisher

ASME International

Subject

Geochemistry and Petrology,Mechanical Engineering,Energy Engineering and Power Technology,Fuel Technology,Renewable Energy, Sustainability and the Environment

Reference47 articles.

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2. Wartha, C., 1998, “An Experimental Study on Fuel-Nitrogen Conversion to NO and N2O and on Carbon Conversion under Fluidized Bed Conditions,” Ph.D. thesis, Vienna University of Technology, Vienna, Austria.

3. Hovmand, S., and Davidson, J. F., 1968, “Chemical Conversion in a Slugging Fluidized Bed,” Trans. Inst. Chem. Eng., 46, pp. 190–203.

4. Hovmand, S., and Davidson, J. F., 1971, “Pilot Plant and Laboratory Scale Fluidized Reactors at High Gas Velocities; the Relevance of Slug Flow,” Fluidization, eds., J. F. Davidson and D. Harrison, Academic Press, London and New York.

5. Wartha, C., Winter, F., and Hofbauer, H., 2000, “The Trade-Off Between N2, NO, and N2O Under Fluidized Bed Combustor Conditions,” ASME J. Energy Resour. Technol., 122, pp. 94–100.

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