DFT modelling of the NO reduction process at the Cu-doped SrTiO3(1 0 0) stepped surface

2020 ◽  
Vol 511 ◽  
pp. 119813
Author(s):  
Silvia Carlotto ◽  
Andrea Vittadini ◽  
Maurizio Casarin
2018 ◽  
Vol 5 (10) ◽  
pp. 180969
Author(s):  
Bang Wu ◽  
Ge Pu ◽  
Jiantai Du

An experiment and simulation study of the effect of using liquid additives on the selective non-catalytic reduction (SNCR) process is presented, providing a novel way for plants reducing NO X emissions. An experimental study is conducted in an entrained flow reactor, and CHEMKIN is applied for simulation study. Ethanol additive can effectively shift the temperature window of the NO X OUT process to a lower range and the NO X OUT efficiency ranges from 29 to 56% at 700–800°C. Furthermore, ethanol additive has a significant inhibitory effect on ammonia slip. Na 2 SO 4 and C 2 H 5 OH can be combined into a compound additive, which has a synergistic effect on NO reduction. The addition of methanol can greatly promote denitrification efficiency from 650°C to 725°C, indicating the potential of compound additives in NO reduction. The HNCO + OH = H 2 O + NCO pathway is also proven to be enhanced for ethanol decomposition, thereby providing OH•, which is active in NO reduction. Finally, the reaction routes for ethanol on the urea-based SNCR process at the proper temperature are proposed.


Author(s):  
Vitaly E. Matulis ◽  
Ekaterina G. Ragoyja ◽  
Oleg A. Ivashkevich ◽  
Dmitry A. Lyakhov ◽  
Dominik Michels

2011 ◽  
Vol 383-390 ◽  
pp. 3017-3021 ◽  
Author(s):  
Sheng Li Niu ◽  
Kui Hua Han ◽  
Chun Mei Lu

Nitric oxide (NO) reduction through coal, biomass and their blend reburning is conducted on a drop tube furnace experimental system and it is proved to be feasible of using the coal-biomass blend as the reburning fuel. For a high NO reduction efficiency, the excess air ratio in the reburning zone should be less than 0.9 and the reaction temperature is required to be higher than 1373K. 50-60% of the biomass percentage in the blend is enough for an acceptable efficiency. At the same time, for a thorough NO reduction process, the reburning fuel fraction and the residence time in the reburning zone must be guaranteed about 20% and 0.6-0.8s, respectively. Also, when the initial NO concentration is excess 600ppm, the efficiency is varied little at different NO concentrations.


2015 ◽  
Vol 38 (7) ◽  
pp. 1373-1380 ◽  
Author(s):  
Jun Chen ◽  
Lei Wang ◽  
Ji Zheng ◽  
Jianmeng Chen

RSC Advances ◽  
2016 ◽  
Vol 6 (92) ◽  
pp. 89259-89273 ◽  
Author(s):  
Maria Mihet ◽  
Vasile-Mircea Cristea ◽  
Paul-Serban Agachi ◽  
Ana-Maria Cormos ◽  
Mihaela D. Lazar

CFD simulations and parametric studies of the NO reduction process in a fixed bed catalytic reactor.


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