Optimal design of a wet-type desulphurization absorber by the numerical simulation method

被引:13
作者
Xiao, Y. J. [1 ,2 ]
Li, C. T. [1 ,2 ]
Li, S. H. [1 ,2 ]
Zeng, G. M. [1 ,2 ]
Wen, Q. B. [1 ,2 ]
Guo, G. Q. [1 ,2 ]
Song, J. K. [1 ,2 ]
机构
[1] Hunan Univ, Coll Environm Sci & Engn, Changsha 410082, Hunan, Peoples R China
[2] Hunan Univ, Key Lab Environm Biol & Pollut Control, Minist Educ, Changsha 410082, Hunan, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
Structural optimization; Two-phase flow; Temperature distribution; Liquid-phase distribution; Numerical simulation; Eulerian-Lagrangian model; FLUE-GAS DESULFURIZATION; EULERIAN-LAGRANGIAN SIMULATIONS; EXPERIMENTAL VALIDATION; SEPARATION EFFICIENCY; MASS-TRANSFER; LIQUID FLOWS; 2-PHASE FLOW; HYDROCYCLONE; MODEL; CYCLONE;
D O I
10.1016/j.cherd.2013.10.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Numerical study of gas-liquid flow in a wet-type desulphurization absorber is presented and the influences of different inlet and deflector structures on the device performance are identified for optimizing its structure. The dependability of numerical model is validated by the good agreement between the measured and predicted results. Besides, the results of droplet trajectories analyzed by the mechanical formulas are consistent with the simulation results as well. The performance of gas flow field is affected significantly by the inlet structures. The main reason for uneven distribution of liquid-phase is the first layer deflector rather than the gas flow. After removing the first layer deflector, the mass percentage distribution of liquid-phase in the near-wall region is reduced from 68-87% to 25-40%. The temperature distribution and relative humidity depend largely on the distribution of liquid-phase and the gas flow field. Optimized structures improve the pressure drop of device. (C) 2013 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1257 / 1266
页数:10
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