Numerical simulation of the simultaneous removal of particulate matter in a wet flue gas desulfurization system

2019 ◽  
Vol 27 (2) ◽  
pp. 1598-1607 ◽  
Author(s):  
Yueqi Huang ◽  
Chenghang Zheng ◽  
Qingyi Li ◽  
Jun Zhang ◽  
Yishan Guo ◽  
...  
2014 ◽  
Vol 541-542 ◽  
pp. 1288-1291
Author(s):  
Zhi Feng Dong ◽  
Quan Jin Kuang ◽  
Yong Zheng Gu ◽  
Rong Yao ◽  
Hong Wei Wang

Calculation fluid dynamics software Fluent was used to conduct three-dimensional numerical simulation on gas-liquid two-phase flow field in a wet flue gas desulfurization scrubber. The k-ε model and SIMPLE computing were adopted in the analysis. The numerical simulation results show that the different gas entrance angles lead to internal changes of gas-liquid two-phase flow field, which provides references for reasonable parameter design of entrance angle in the scrubber.


RSC Advances ◽  
2018 ◽  
Vol 8 (66) ◽  
pp. 38013-38021 ◽  
Author(s):  
Dean Fang ◽  
Xuefei Zhang ◽  
Xiangxin Xue

A novel resource utilization method using wet magnesia flue gas desulfurization residue for the simultaneous removal of ammonium nitrogen and heavy metal pollutants from vanadium industrial wastewater was proven to be viable and effective.


2019 ◽  
Vol 116 ◽  
pp. 00101
Author(s):  
Tomasz Wypiór ◽  
Renata Krzyżyńska

The paper presents data concerning the influence of ammonia on wet flue gas desulfurization (WFGD) absorber. Paper presents preliminary results of an industrial scale study on WFGD absorber, that collects flue gases from four boilers with total flue gas flow capacity of the WFGD equal to 1 500 000 Nm3/h. Each boiler is equipped with selective non-catalytic reduction (SNCR) with urea injection. It was shown, that ammonia present in the flue gas upstream the WFGD increases the pH of absorption slurry, impacting the desulphurization process. In addition, analysis of particulate matter upstream and downstream the absorber shows an increase of the concentration of ammonium species in the particulate matter about 14 times, as average. Moreover, a non-optimized denitrification process can cause a high NH4+ concentration in the absorption slurry (up to 768 mg/L) and raw wastewater (up to 891 mg/L).


2015 ◽  
Vol 88 (3) ◽  
pp. 284-291 ◽  
Author(s):  
S.J. Wang ◽  
P. Zhu ◽  
G. Zhang ◽  
Q. Zhang ◽  
Z.Y. Wang ◽  
...  

2020 ◽  
Vol 31 (1) ◽  
pp. 323-331 ◽  
Author(s):  
Feng Wu ◽  
Kai Yue ◽  
Weiwei Gao ◽  
Ming Gong ◽  
Xiaoxun Ma ◽  
...  

2013 ◽  
Vol 91 (5) ◽  
pp. 386-390 ◽  
Author(s):  
Qiang Tang ◽  
Qin Wang ◽  
Pengfei Cui ◽  
Weiwei Cao ◽  
Shifeng Hou

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