Kinetics of SO2 Removal from Flue Gas on CuO/Al2O3 Sorbent Catalyst

2007 ◽  
Vol 30 (9) ◽  
pp. 1221-1227 ◽  
Author(s):  
Z. H. Jia ◽  
Z. Y. Liu ◽  
Y. H. Zhao
Keyword(s):  
Flue Gas ◽  
1993 ◽  
Vol 42 (4-6) ◽  
pp. 673-677 ◽  
Author(s):  
H. Mätzing ◽  
H. Namba ◽  
O. Tokunaga

ACS Omega ◽  
2020 ◽  
Vol 5 (30) ◽  
pp. 19194-19201
Author(s):  
Jinxiao Dou ◽  
Yongqi Zhao ◽  
Xiaoxu Duan ◽  
Hongning Chai ◽  
Lichun Li ◽  
...  

2015 ◽  
Vol 48 (3) ◽  
pp. 827-835 ◽  
Author(s):  
Mingliang Tang ◽  
Xuerun Li ◽  
Yusheng Shen ◽  
Xiaodong Shen

Modeling of the kinetics of the synthesis process for calcium sulfate α-hemihydrate from gypsum formed by flue gas desulfurization (FGD) is important to produce high-performance products with minimal costs and production cycles under hydrothermal conditions. In this study, a model was established by horizontally translating the obtained crystal size distribution (CSD) to the CSD of the stable phase during the transformation process. A simple method was used to obtain the nucleation and growth rates. A nonlinear optimization algorithm method was employed to determine the kinetic parameters. The model can be successfully used to analyze the transformation kinetics of FGD gypsum to α-hemihydrate in an isothermal batch crystallizer. The results showed that the transformation temperature and stirring speed exhibit a significant influence on the crystal growth and nucleation rates of α-hemihydrate, thus altering the transformation time and CSD of the final products. The characteristics obtained by the proposed model can potentially be used in the production of α-hemihydrate.


Author(s):  
Anton Petukhov ◽  
Artem Atlaskin ◽  
Maria Sergeeva ◽  
Sergey Kryuchkov ◽  
Dmitry Shablykin ◽  
...  

2012 ◽  
Vol 197 ◽  
pp. 468-474 ◽  
Author(s):  
Yangxian Liu ◽  
Jun Zhang ◽  
Zhuliang Wang

1998 ◽  
Vol 9 (5) ◽  
pp. 535-547 ◽  
Author(s):  
Ryunosuke Kikuchi

A bench-scale test (800 Nm3/h) for electron beam treatment of flue gas was conducted. It was concluded that the method is favourable for treatment of flue gas with a high SO2 concentration (5,500 ppm) at low electron beam irradiation (5 kGy). Results are consistent with the claim that SOx is removed from flue gas by the reaction of SOx with ammonia, and the intermediate salts formed are oxidised by radicals to sulphate salts consisting mainly of ammonium sulphate (a N-fertiliser). A typical flue gas desulphurization (FGD) method such as the wet limestone process cannot remove NOx and SO3 effectively (Ando, 1990), but the electron beam process removes SO2, SO3 and NOx simultaneously without generating waste water and CO2.


Processes ◽  
2020 ◽  
Vol 8 (1) ◽  
pp. 124 ◽  
Author(s):  
Pandey ◽  
Daas ◽  
Solms

In this study, the kinetics of flue gas hydrate formation in bulk water in the presence of selected amino acids and surfactants are investigated. Four amino acids (3000 ppm) are selected based on different hydropathy index. Constant-ramping and isothermal experiments at 120 bar pressure and 1 °C temperature are carried out to compare their hydrate promotion capabilities with surfactant sodium dodecyl sulfate (SDS) (500–3000 ppm) and water. Based on experimental results, we report the correlation between hydrate promotion capability of amino acids and their hydrophobicity. Hydrophobic amino acids show stronger flue gas hydrate promotion capability than water and hydrophilic amino acids. We discuss the controlling mechanisms to differentiate between promoters and inhibitors’ roles among the amino acids. Between 2000–3000 ppm concentrations, hydrophobic amino acids have near similar promotion capabilities as SDS. This research highlights the potential use of amino acids as promoters or inhibitors for various applications.


2013 ◽  
Vol 27 (6) ◽  
pp. 3080-3089 ◽  
Author(s):  
Zheng Yan ◽  
Lili Liu ◽  
Yueling Zhang ◽  
Jinping Liang ◽  
Jinping Wang ◽  
...  

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