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Content available remote Numerical simulation of NO production in a pulverized coal fired furnace
EN
Behaviour of air-coal mixture has been described using the Navier-Stokes equations for the mixture of air and coal particles, accompanied by the turbulence model. The undergoing chemical reactions are described by the Arrhenius kinetics (reaction rate proportional to exp(-E/RT) ). Heat transfer via conduction and radiation has also been considered. The system of partial difference equations is discretized using the finite volume method and the advection upstream splitting method as the Riemann solver. The resulting ordinary differential equations are solved using the 4th order Runge-Kutta method. Results of simulation for typical power production level are presented together with the air staging impact on NO production.
EN
Thermal plasma based system for fire support and stabilization in pulverized coal fired boiler, developed in Laboratory for Thermal Engineering and Energy, Institute of Nuclear Sciences "Vinca", Belgrade, is planed to be an alternative to existing oil burner's system at boiler A1 in the TPP Nikola Tesla in Obrenovac, Serbia. Assuming steady plasma-coal gasification process in the steady air-coal mixture channel flow, preliminary calculation predicted temperature of channel's inner wall at level higher then 700°C. This could induce thermal dilatations of thin-wall steel channel with rectangular cross­section that can remarkably affect air-coal mixture channel flow. In order to prevent occurrence of significant disturbances in the mean air-coal mixture flow, reconstructive operations on existing lower segments of burner's section are dane including replacement of one rectangular air-coal mixture channel with two channels having circular cross section. The aim of this work is to evaluate influence of thermally loaded channel dilatations on air-coal mixture flow in both cases.
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