Low temperature selective catalytic reduction of NO by C3H6 over CeOx loaded on AC treated by HNO3

被引:13
作者
Chu Yinghao [1 ,2 ]
Zhang Tengteng [1 ]
Guo Jiaxiu [1 ,2 ,3 ]
Liu Chao [1 ,2 ]
Yin Huaqiang [1 ,2 ,3 ]
Zhu Xiaofan [2 ]
Liu Yongjun [1 ,2 ]
机构
[1] Sichuan Univ, Coll Architecture & Environm, Chengdu 610065, Peoples R China
[2] Sichuan Univ, Natl Engn Technol Res Ctr Flue Gas Desulfurizat, Chengdu 610065, Peoples R China
[3] Sichuan Univ, Sichuan Prov Environm Protect & Environm Catalyt, Chengdu 610065, Peoples R China
基金
中国国家自然科学基金;
关键词
low temperature; activated carbon; cerium oxides; selective catalytic reduction; hydrocarbon; rare earths; ACTIVATED CARBON; NITRIC-OXIDE; SURFACE; OXIDATION; PROPENE; XPS; KINETICS; CERIUM; NH3; SCR;
D O I
10.1016/S1002-0721(14)60429-4
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The activated carbons from coal were treated by HNO3 (named as NAC) and used as carriers to load 7% Ce (named as Ce(0.07)/NAC) by impregnation method. The physical and chemical properties were investigated by thermogravimetric-differential thermal analysis (TG-DTA), Brunauer-Emmett-Teller (BET), X-ray diffraction (XRD), X-ray photoelectron spectra (XPS), scanning electron microscopy (SEM) and NH3-temperature programmed desorption (NH3-TPD) and NO-temperature programmed desorption techniques. The catalytic activities of Ce(0.07)NAC were evaluated for the low temperature selective catalytic reduction (SCR) of NO with C3H6 using temperature-programmed reaction (TP-reaction) in NO, C3H6, O-2 and N-2 as a balance. The results showed that the specific surface area of Ce(0.07)/NAC was 850.8 m(2)/g and less than NAC, but Ce oxides could be dispersed highly on the activated carbons. Ce oxides could change acid sites and NO adsorption as well as oxygen-containing functional groups of activated carbons, and Ce4+ and Ce3+ coexisted in catalysts. The conversion of NO with C3H6 achieved 70% at 280 degrees C over Ce(0.07)/NAC, but with the increase of O-2 concentration, heat accumulation and nonselective combustion were exacerbated, which could cause surface ashing and roughness, resulting in a sharp decrease of catalytic activities. The optimum O-2 concentration used in the reaction system was 3% and achieved the high conversion of NO and the widest temperature window. The conversion of NO was closely related to the NO concentrations and [NO]/[C3H6] ratios, and the stoichiometric number was just close to 2:1, but the presence of H2O could affect the denitration efficiency of catalyst.
引用
收藏
页码:371 / 381
页数:11
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