CFD-PBM simulations the effect of aeration rates on hydrodynamics characteristics in a gas-liquid-solid aerobic fluidized bed biofilm reactor

被引:2
|
作者
Ren, Jiehui [1 ,2 ]
Pei, Yao [1 ]
Zhou, Xiaoping [3 ]
Jiao, Meng [3 ]
Cheng, Wen [1 ,2 ]
Wan, Tian [1 ,2 ]
机构
[1] Xian Univ Technol, Dept Municipal & Environm Engn, 5 South Jinhua Rd, Xian 710048, Shaanxi, Peoples R China
[2] Xian Univ Technol, State Key Lab Ecohydraul Northwest Arid Reg China, 5 South Jinhua Rd, Xian 710048, Shaanxi, Peoples R China
[3] Power China Northwest Engn Corp Ltd, Xian 710065, Shaanxi, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas; -liquid; -solid; Simulation; CFD-PBM; Bubble; Aeration rates; FROTH FORMATION; BUBBLE-COLUMNS; FLOW; MODEL; SIZE; COALESCENCE; PARTICLES;
D O I
10.1016/j.powtec.2024.119963
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A CFD-PBM coupling model was developed to simulate and calculate multiphase flow parameters, flow morphology, and bubble diameter in the aerobic fluidized bed biofilm reactor (AFBBR) under different aeration rates. The simulated radial solid volume fraction values were generally in agreement (within +/- 15%) with the experimental values. The gas phase predominantly occupied the central area of the reactor, with three distinct velocity peaks observed in the liquid and solid phases. Higher aeration rates improve the mixing of multiple phases by augmenting fluidization velocity, gas-phase volume fraction, eddies size, and turbulence characteristics, thereby leading to a rise in the average size of bubbles from 1.54 mm to 2.03 mm. However, the proportion of small diameter bubbles (0.27-1.03 mm) decreased from 69.4% to 59.6%. These studies concluded that the multiphase flow parameters under an aeration rate of 5.77 m3/(h & sdot;m3) were more favorable for improving oxygen mass transfer efficiency and reducing energy consumption.
引用
收藏
页数:10
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