2017
DOI: 10.1016/j.apcatb.2016.12.007
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Insight of platinum poisoning Cu/SAPO-34 during NH3-SCR and its promotion on catalysts regeneration after hydrothermal treatment

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Cited by 43 publications
(14 citation statements)
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“…As shown in Figure S6, only a peak at 180–280 °C that represents the reduction of isolated Cu 2+ to Cu + ions is observed. This indicates that Cu 2+ ions are the main active sites in the catalyst . The acidity of the Cu/S N ‐In catalysts are also investigated by measuring the DRIFTS spectra of the adsorbed NH 3 .…”
Section: Resultsmentioning
confidence: 99%
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“…As shown in Figure S6, only a peak at 180–280 °C that represents the reduction of isolated Cu 2+ to Cu + ions is observed. This indicates that Cu 2+ ions are the main active sites in the catalyst . The acidity of the Cu/S N ‐In catalysts are also investigated by measuring the DRIFTS spectra of the adsorbed NH 3 .…”
Section: Resultsmentioning
confidence: 99%
“…This indicates that Cu 2 + ions are the main active sites in the catalyst. [4,34] The acidity of the Cu/S N -In catalysts are also investigated by measuring the DRIFTS spectra of the adsorbed NH 3 . As shown in Figure 3a, the negative bands at 3663 and 3606 cm À 1 assigned to the OH vibrations of PÀ OH or SiÀ OH group on external surface and structural hydroxyl groups AlÀ OHÀ Si, respectively, are observed in all catalysts.…”
Section: Resultsmentioning
confidence: 99%
“…Among SAPO materials, SAPO-34w ith aC HA framework structureh as been attracting considerable interesti n methanol to hydrocarbon reactions, [4,5] syngas to hydrocarbon reactions, [6] and selectivec atalytic reduction (SCR) of NO x . [7,8] The structure of SAPO-34 ( Figure 1) consistso ft wo composite buildingu nits, double-six-membered rings (d6r), and cha cages, which are joined together to form at hree-dimensional network of pores with 0.38 nm diameter windows connecting ellipsoidal cages with dimensions of 0.74 nm 1.1 nm. [9] The morphology and crystal size affects the mass transport and the diffusion path of the feedstocks and products.…”
Section: Introductionmentioning
confidence: 99%
“…However, acid sites can be introduced by substitution of silicon into the framework of the AlPOs, which results in so‐called siliconaluminophosphates (SAPOs). Among SAPO materials, SAPO‐34 with a CHA framework structure has been attracting considerable interest in methanol to hydrocarbon reactions, syngas to hydrocarbon reactions, and selective catalytic reduction (SCR) of NO x . The structure of SAPO‐34 (Figure ) consists of two composite building units, double‐six‐membered rings ( d6r ), and cha cages, which are joined together to form a three‐dimensional network of pores with 0.38 nm diameter windows connecting ellipsoidal cages with dimensions of 0.74 nm×1.1 nm…”
Section: Introductionmentioning
confidence: 99%
“…Among various attempts, copper-based catalysts supported on oxides or zeolites have recently emerged as attractive candidates due to their environmentally benign characteristics and high SCR performance in a wide temperature range. [7][8][9][10] Co, Fe, Mn, and Ce have been doped into the phase or co-deposited with Cu on supports, such as zeolites, TiO 2 , and SiO 2 , to fabricate composite Cu-based NH 3 -SCR catalysts. Addition of these elements was found to be benecial for creating charge imbalance, vacancies or unsaturated chemical bonds on the catalysts surface, and practical contribution to the catalytic improvements for NH 3 -SCR-NO x .…”
Section: Introductionmentioning
confidence: 99%