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Author:

Li, Q. (Li, Q..) | He, F. (He, F..) | Mei, S. (Mei, S..) | Xie, J. (Xie, J..) | Zhang, C. (Zhang, C..) | Deng, Y. (Deng, Y..)

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Scopus

Abstract:

Aiming at a new type of swirl precalciner, numerical simulations were carried out for the pulverized coal combustion, raw meal decomposition coupling, and NOx generation processes. In Euler coor-dinate system gas phase was expressed with the Realizable k-ε two-equation model, in Lagrange coordi-nate system solid phase was expressed with the discrete phase model(DPM),pulverized coal combustion and raw meal decomposition was expressed with the species transport model,radiation was expressed with the P-1 model, NOx generation was expressed with the pollutant model. Thermal NOx and fuel NOx generation are considered. The results show that the tertiary air mainly moves upward along the wall spiral, while the flue gas mainly moves the central axis spiral in the precalciner. When the pulverized coal enters the precalciner, the volatiles are rapidly released and burned, and then the char continues to burn, and its main combustion area is near the shell. When the pulverized coal enters the precalciner, the volatiles are rapidly released and burned, and then the char continues to burn, and its main combustion area is near the shell, and the combustion residence time is approximately 5. 9 s. The raw meal decomposes rapidly after entering the precalciner. When reaching a height of 50 m in the precalciner, the decomposition rate of CaCO3 reaches 90%. At this point, the decomposition times for the lower and upper raw meal are approximately 6. 5 s and 4. 7 s, respectively. 92. 32% decomposition of calcium carbonate at the outlet. Due to the poor coupling between pulverized coal combustion and raw meal decomposition at the shell, local high temperatures are formed at the wall, which makes the NOx generation rate larger, and the NOx at the outlet reaches 1. 251×10-3, which needs to be improved. © 2025, Tianjin University. All rights reserved.

Keyword:

NOx calcium carbonate decomposition precalciner numerical simulation coal combustion computational fluid dynamics

Author Community:

  • [ 1 ] [Li Q.]School of Material Science and Engineering, Wuhan University of Technology, Hubei, Wuhan, 430070, China
  • [ 2 ] [He F.]School of Materials Science and Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 3 ] [Mei S.]School of Material Science and Engineering, Wuhan University of Technology, Hubei, Wuhan, 430070, China
  • [ 4 ] [Xie J.]School of Materials Science and Engineering, Beijing University of Technology, Beijing, 100124, China
  • [ 5 ] [Zhang C.]CBMI Construction Co., Ltd, Beijing, 100176, China
  • [ 6 ] [Deng Y.]CBMI Construction Co., Ltd, Beijing, 100176, China

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Source :

Chemical Industry and Engineering

ISSN: 1004-9533

Year: 2025

Issue: 2

Volume: 42

Page: 177-186

Cited Count:

WoS CC Cited Count:

SCOPUS Cited Count:

ESI Highly Cited Papers on the List: 0 Unfold All

WanFang Cited Count:

Chinese Cited Count:

30 Days PV: 7

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