2023
DOI: 10.1016/j.apsusc.2022.156159
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Synergistic effect of V2O5-WO3/TiO2 and H-ZSM-5 catalysts prepared by physical mixing on the selective catalytic reduction of NOx with NH3

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Cited by 12 publications
(4 citation statements)
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“…For the P/Z-S catalyst, the band at 3649 cm –1 was attributed to hydroxyl groups. The bands at 3333, 1607, 1196, and 1180 cm –1 were assigned to coordination NH 3 at the Lewis acid site while the bands at 1475 and 1420 cm –1 were attributed to NH 4 + at the Brønsted acid site. ,,, N 2 O 4 (1725 cm –1 ), bidentate nitrates (1530 cm –1 ), and –NH 2 (1338 cm –1 ) were also observed. , It indicated that the P/Z-S catalyst followed the i-SCR reaction mechanism in NH 3 –SCO reactions. By comparing the infrared profiles of P/Z and P/Z-S catalysts, it was concluded that sulfuric acid treatment of the ZrO 2 support could increase the number of acid sites on the surface of the P/Z-S catalyst, especially Brønsted acid sites.…”
Section: Resultsmentioning
confidence: 87%
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“…For the P/Z-S catalyst, the band at 3649 cm –1 was attributed to hydroxyl groups. The bands at 3333, 1607, 1196, and 1180 cm –1 were assigned to coordination NH 3 at the Lewis acid site while the bands at 1475 and 1420 cm –1 were attributed to NH 4 + at the Brønsted acid site. ,,, N 2 O 4 (1725 cm –1 ), bidentate nitrates (1530 cm –1 ), and –NH 2 (1338 cm –1 ) were also observed. , It indicated that the P/Z-S catalyst followed the i-SCR reaction mechanism in NH 3 –SCO reactions. By comparing the infrared profiles of P/Z and P/Z-S catalysts, it was concluded that sulfuric acid treatment of the ZrO 2 support could increase the number of acid sites on the surface of the P/Z-S catalyst, especially Brønsted acid sites.…”
Section: Resultsmentioning
confidence: 87%
“…The bands at 3333, 1607, 1196, and 1180 cm −1 were assigned to coordination NH 3 at the Lewis acid site while the bands at 1475 and 1420 cm −1 were attributed to NH 4 + at the Brønsted acid site. 13,61,80,81 N 2 O 4 (1725 cm −1 ), bidentate nitrates (1530 cm −1 ), and −NH 2 (1338 cm −1 ) were also observed. 71,77 It indicated that the P/Z-S catalyst followed the i-SCR reaction mechanism in NH 3 −SCO reactions.…”
Section: Interaction Between Nh 3 and Omentioning
confidence: 90%
“…Except for these zeolite catalysts, scholars tried to combine metal-based catalysts (V 2 O 5 -WO 3 /TiO 2 ) with zeolite catalysts (H-ZSM-5) to prepare the composite catalyst PM. The PM catalyst exhibited higher catalytic activity than the V 2 O 5 WO 3 /TiO 2 catalyst because the PM catalyst adsorbed more NO 2 and N 2 O 4 [49]. Given the complexity of the exhaust purification system in SCR, some researchers adopted an H 2 selective catalytic reduction method using Pt/KFI molecular sieve catalysts from 150 • C to 250 • C, and the conversion rate of NO x reached 80% [50].…”
Section: Selective Catalytic Reduction (Scr) Of No Xmentioning
confidence: 99%
“…3,4 Among them, the selective catalytic reduction (SCR) of NO with NH 3 as the reductant is nowadays well-established as the most effective technique to eliminate NOx. 5,6 However, typical commercial SCR technologies suffer from disadvantages such as high operating temperature (300-400 °C) of catalysts (V 2 O 5 -WO 3 /TiO 2 ) 7,8 and secondary pollution caused by ammonia slip. 9 In contrast, the direct catalytic decomposition of NO is deemed the most ideal technology given that no reductant is needed and no harmful products are formed.…”
Section: Introductionmentioning
confidence: 99%