# [1]周颖倩,钟文琪,刘飞,等.烧结烟气鼓泡脱硫的三维数值模拟[J].东南大学学报(自然科学版),2015,45(2):314-319.[doi:10.3969/j.issn.1001-0505.2015.02.021] 　Zhou Yingqian,Zhong Wenqi,Liu Fei,et al.Three-dimensional numerical simulation of sintering flue gas desulfurization in bubbling tower[J].Journal of Southeast University (Natural Science Edition),2015,45(2):314-319.[doi:10.3969/j.issn.1001-0505.2015.02.021] 点击复制 烧结烟气鼓泡脱硫的三维数值模拟() 分享到： var jiathis_config = { data_track_clickback: true };

45

2015年第2期

314-319

2015-03-20

## 文章信息/Info

Title:
Three-dimensional numerical simulation of sintering flue gas desulfurization in bubbling tower

1东南大学能源与环境学院, 南京 210096; 2南京钢铁联合有限公司, 南京 210035
Author(s):
1Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China
2Nanjing Iron and Steel Co., Ltd., Nanjing 210035, China

Keywords:

X75
DOI:
10.3969/j.issn.1001-0505.2015.02.021

Abstract:
Flue gas desulfurization process for sintering process of iron and steel industry was numerically studied. Taking a 220 m2 sintering flue gas desulfurization tower as the object, based on the bubbling bed a 3D numerical model of gas-fluid flow coupling with desulfurization reaction was established for research. The influences of the Ca(OH)2 concentration, the superficial gas velocity, the inlet gas temperature, the SO2 concentration of inlet gas on the removal efficiency of sulfur dioxide were analyzed. Under the reference conditions, which include the superficial gas velocity of 0.11 m/s, the inlet gas temperature of 418 K, the SO2 concentration of inlet gas of 1 600 mg/m3, the Ca(OH)2 concentration of 0.614 mol/L and the slurry temperature of 323 K, the single operation parameter was changed individually. The results demonstrate that with the Ca(OH)2 concentration increasing from 0.1 to 0.614 mol/L, the removal efficiency of sulfur dioxide increases, while it decreases with the gas velocity increasing from 0.07 to 0.21 m/s and the inlet gas temperature changing from 377 to 445 K. With the increase of the SO2 concentration of inlet gas from 2 000 to 2 400 mg/m3, there is a slight fall in the removal efficiency of sulfur dioxide.

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