Selective catalytic reduction of NO by methane over Co,H-SSZ-13 catalysts: Types and catalytic functions of active Co sites

被引:27
|
作者
Charrad, Rania [1 ]
Solt, Hanna E. [2 ]
Domjan, Attila [2 ]
Ayari, Faouzi [1 ,3 ]
Mhamdi, Mourad [1 ,4 ]
Valyon, Jozsef [2 ]
Lonyi, Ferenc [2 ]
机构
[1] Univ Tunis El Manar, Fac Sci Tunis, Lab Chim Mat & Catalyse, Tunis, Tunisia
[2] Res Ctr Nat Sci, Inst Mat & Environm Chem, Magyar Tudosok Korutja 2, H-1117 Budapest, Hungary
[3] Univ Monastir, Fac Pharm Monastir, Lab Dev Chim Galen & Pharmacol Medicaments, Rue Avicenne, Monastir 5000, Tunisia
[4] Univ Tunis El Manar, Inst Super Technol Med Tunis, Tunis, Tunisia
关键词
NO-SCR by CH4; Co; H-SSZ-13; Solid state ion exchange; Operando-DRIFTS; STATE ION-EXCHANGE; ZEOLITE-BASED CATALYSTS; NO+O-2 COADSORPTION; NITROGEN-OXIDES; EMISSION CONTROL; RICH ZEOLITES; NITRIC-OXIDE; NA-MOR; FT-IR; COBALT;
D O I
10.1016/j.jcat.2020.02.018
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Co-SSZ-13 zeolite catalysts were prepared by solid-state ion exchange with CoCl2 salt for the selective catalytic reduction of NO with methane (CH4/NO-SCR). Fresh catalysts contained hard-to-reduce lattice Co2+/[Co-OH](+) ions and showed activity proportional to the concentration of these species. The NO conversion was accompanied by steam-generating methane oxidation. Under the arising hydrothermal conditions, a fraction of Co ions transformed into Co-oxo species especially in catalysts of high Co content (Co/Al-F > 0.3), resulting in boosted activity in NO2-forming catalytic NO oxidation. The increased NO2 concentration brought about higher concentration of surface cobalt nitrate species responsible for the rate-determining methane activation, so the overall rate of the NO-SCR reaction was also accelerated. Steam admixed to the feed decreased the conversion of methane more significantly than that of NO. Its observed high hydrothermal stability renders the Co-SSZ-13 catalyst a very promising candidate for the CH4/NO-SCR reaction. (C) 2020 The Author(s). Published by Elsevier Inc.
引用
收藏
页码:87 / 102
页数:16
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