Chemical deactivation of Selective Catalytic Reduction catalyst: Investigating the influence and mechanism of SeO2 poisoning

被引:18
|
作者
Xu, Liwen [1 ]
Wu, Qingru [1 ,2 ]
Chang, Huazhen [3 ]
Li, Guoliang [1 ]
Zou, Jing [1 ]
Wang, Shuxiao [1 ,2 ]
机构
[1] Tsinghua Univ, Sch Environm, State Key Joint Lab Environm Simulat & Pollut Con, Beijing 100084, Peoples R China
[2] State Environm Protect Key Lab Sources & Control, Beijing 100084, Peoples R China
[3] Renmin Univ China, Sch Environm & Nat Resources, Beijing 100872, Peoples R China
关键词
SeO2; Catalyst poisoning; SCR; V2O5-WO3/TiO2; COMMERCIAL SCR CATALYST; DESIGN STRATEGIES; COAL COMBUSTION; FLUE-GAS; CEO2-MOO3; CATALYSTS; TITANIA CATALYSTS; TRACE-ELEMENTS; NITRIC-OXIDE; REGENERATION; PERFORMANCE;
D O I
10.1016/j.fuel.2020.117435
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Selenium (Se) is a major trace element in coal that can easily volatize and become part of flue gas during the combustion process. Currently, the interactions between SeO2 and Selective Catalytic Reduction (SCR) catalysts remain unclear. In this study, a field WA at four coal-fired power plants found that the Se concentration at the SCR inlets were relatively high, with more than 95% present in its gaseous phase. To explore possible interactions between SeO2 and SCR catalyst, a V2O5-WO3/TiO2 (VWTi) catalyst was subjected to various degrees of in situ SeO2 poisoning. A positive correlation between the decreases in catalytic activity and N-2 selectivity and an increasing amount of SeO2 deposition was observed. The decreases in NH3-adsorption capacity and strong acid sites activation ability were responsible for the loss in catalytic activity, while higher ratio of chemisorbed oxygen and stronger reducibility resulted in NH3 being oxidized to N2O and N-2 selectivity loss. Based on these results, it is clear that SeO2 poisoning of SCR catalysts should be taken into consideration to ensure the reliable operation of SCR systems.
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页数:9
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