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Modeling of coal combustion in the CFB by the EDC model with the global reaction mechanism

Zhizhong Kang (School of Energy Power and Mechanical Engineering, North China Electric Power University, Beijing, China)
Shixing Ding (School of Energy Power and Mechanical Engineering, North China Electric Power University, Beijing, China)
Zhi-ang Shuai (Sichuan Electric Power Design and Consulting Co. Ltd., Chengdu, China)
Baomin Sun (School of Energy Power and Mechanical Engineering, North China Electric Power University, Beijing, China)

International Journal of Numerical Methods for Heat & Fluid Flow

ISSN: 0961-5539

Article publication date: 3 April 2018

181

Abstract

Purpose

This paper aims to shows the ability of the EDC model with a global reaction mechanism to describe reactions in the Eulerian simulation of a circulating fluidized bed (CFB).

Design/methodology/approach

The eddy dissipation concept (EDC) model is embedded in an Eulerian-Eulerian approach to simulate homogeneous reactions.

Findings

EDC_G is better than ED_FR in describing chemical reactions. The reaction of CH4 with O2 is faster than that of CO with O2, and NH3 is more liable to be converted than HCN. The combustion rate is higher than the Boudouard reaction rate of coal particles.N2O is mainly reduced by carbon, and NO is mainly converted by carbon into N2 and CO2.

Originality/value

The EDC model with a global reaction mechanism is embedded in a multi-fluid Eulerian approach to simulate the homogeneous reactions in the coal combustion in a CFB, including combustion of volatile gases, desulfurizing reactions and NOx reactions.

Keywords

Citation

Kang, Z., Ding, S., Shuai, Z.-a. and Sun, B. (2018), "Modeling of coal combustion in the CFB by the EDC model with the global reaction mechanism", International Journal of Numerical Methods for Heat & Fluid Flow, Vol. 28 No. 4, pp. 963-981. https://doi.org/10.1108/HFF-11-2016-0467

Publisher

:

Emerald Publishing Limited

Copyright © 2018, Emerald Publishing Limited

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