Evaluation of mixing of a secondary solid phase in a circulating fluidized bed riser

被引:2
作者
Nikku, Markku [1 ]
Myohanen, Kari [1 ]
Ritvanen, Jouni [1 ]
Hyppanen, Timo [1 ]
机构
[1] LUT Univ, Sch Energy Syst, PL 20, FI-53851 Lappeenranta, Finland
基金
芬兰科学院;
关键词
Circulating fluidized bed; Mixing; Dispersion; CFD modeling; Eulerian; FUEL FLOW; PARTICLES; SIMULATION; MODEL; CFD; SEGREGATION; BEHAVIOR; FURNACE;
D O I
10.1016/j.ces.2023.118503
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mixing of the secondary solids phase, i.e. fuel or sorbent is crucial in fluidized bed reactors due to its effect on the performance of the reactor. Fluctuations in the gas-particle flow affect mixing, thus model -ing this is essential for the analysis of mixing. However, simplified mixing models are used for large cir-culating fluidized bed (CFB) reactors, which causes uncertainties. A novel averaging method is presented to obtain representative results of transient secondary solid phase mixing in CFBs, acknowledging the effect of fluctuations. A parametric study is performed to investigate the effect of particle size, density, and inlet velocity on mixing and for insight into the mixing process. Additionally, the presented approach is used to compare different steady-state mixing methods to evaluate their applicability for modeling mixing in CFB reactors. Initial momentum and elutriation tendency of fuel were found to affect the mix-ing behavior, with two distinct routes identified.(c) 2023 The Author(s). Published by Elsevier Ltd. This is an open access article under the CC BY license (http://creativecommons.org/licenses/by/4.0/).
引用
收藏
页数:12
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