Insights into high CO-SCR performance of CuCoAlO catalysts derived from LDH/MOFs composites and study of H2O/SO2 and alkali metal resistance

2021 ◽  
Vol 426 ◽  
pp. 131873
Author(s):  
Yu Zhang ◽  
Ling Zhao ◽  
Mengdi Kang ◽  
Ziang Chen ◽  
Shengjun Gao ◽  
...  
Author(s):  
Peng Wu ◽  
Kai Shen ◽  
Yiliang Liu ◽  
Yaping Zhang ◽  
Guobo Li ◽  
...  

Series of V0.04W0.03MoxSby/TiO2 catalysts were prepared by impregnating various content of Mo and Sb. The preferred V0.04W0.03Mo0.015Sb0.018/TiO2 catalyst exhibited better SCR activity at a wide temperature range of 160-320 °C,...


Catalysts ◽  
2021 ◽  
Vol 11 (8) ◽  
pp. 979
Author(s):  
Zexiang Chen ◽  
Meiqing Shen ◽  
Chen Wang ◽  
Jianqiang Wang ◽  
Jun Wang ◽  
...  

To improve the alkali metal resistance of commercial catalyst Cu/SSZ-13 for ammonia selective catalytic reduction (NH3-SCR) reaction, a simple method to synthesize Cu/SSZ-13 with a core–shell like structure was developed. Compared with smaller-sized counterparts, Cu/SSZ-13 with a crystal size of 2.3 μm exhibited excellent resistance to Na poisoning. To reveal the influence of the crystal size on Cu/SSZ-13, physical structure characterization (XRD, BET, SEM, NMR) and chemical acidic distribution (H2-TPR, UV-Vis, Diethylamine-TPD, pyridine-DRIFTs, EDS) were investigated. It was found that the larger the crystal size of the molecular sieve, the more Cu is distributed in the crystal core, and the less likely it was to be replaced by Na to generate CuO. Therefore, a 2.3 μm sized Cu/SSZ-13 well-controlled the reactivity of the side reaction NH3 oxidation and the generation of N2O. The result was helpful to guide the extension of the service life of Cu/SSZ-13.


2019 ◽  
Vol 54 (24) ◽  
pp. 14707-14719 ◽  
Author(s):  
Huirong Li ◽  
Jifa Miao ◽  
Qingfa Su ◽  
Yanke Yu ◽  
Yanting Chen ◽  
...  

TAPPI Journal ◽  
2012 ◽  
Vol 11 (7) ◽  
pp. 9-14 ◽  
Author(s):  
AINO LEPPÄNEN ◽  
ERKKI VÄLIMÄKI ◽  
ANTTI OKSANEN

Under certain conditions, ash in black liquor forms a locally corrosive environment in a kraft recovery boiler. The ash also might cause efficiency losses and even boiler shutdown because of plugging of the flue gas passages. The most troublesome compounds in a fuel such as black liquor are potassium and chlorine because they change the melting behavior of the ash. Fouling and corrosion of the kraft recovery boiler have been researched extensively, but few computational models have been developed to deal with the subject. This report describes a computational fluid dynamics-based method for modeling the reactions between alkali metal compounds and for the formation of fine fume particles in a kraft recovery boiler furnace. The modeling method is developed from ANSYS/FLUENT software and its Fine Particle Model extension. We used the method to examine gaseous alkali metal compound and fine fume particle distributions in a kraft recovery boiler furnace. The effect of temperature and the boiler design on these variables, for example, can be predicted with the model. We also present some preliminary results obtained with the model. When the model is developed further, it can be extended to the superheater area of the kraft recovery boiler. This will give new insight into the variables that increase or decrease fouling and corrosion


Author(s):  
Д. И. Блецкан ◽  
В. В. Вакульчак ◽  
А. В. Лукач

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