2013
DOI: 10.1016/j.apcatb.2013.01.026
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Selective catalytic reduction of NO with NH3 over Cr-ZSM-5 catalysts: General characterization and catalysts screening

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Cited by 41 publications
(28 citation statements)
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“…(2) 1.210 g TEPA was added to solution and stirred for 1.0 h. (3) 0.7000 g NaOH and 0.5140 g NaAlO 2 (equals to about 0.2107 g Al 2 O 3 ) were added and stirred for 60 min. (4) 3.600 mL silica sol (equals to about 1.228 g SiO 2 ) was stirred with the solution for 3 h. (5) The mixed solution was transferred to Teflon-lined autoclaves and the crystallization reaction was carried out at 140 8C for 96 h. Then the product was washed and dried at 1008C for 12 h. (6) The product was treated in the nitric acid solution (pH = 1) at 80 8C for 12 h. Then it was separated by vacuum filtration, washed, and dried at 100 8C for 12 h. (7) The product was calcined at 550 8C for 4 h. By changing the mole ratios of Cu-TEPA/Al 2 To study the hydrothermal stability, the zeolite was treated in air flow containing 10 vol.% H 2 O of 25.0 mL·min À1 for 24 h at 750 8C. In order to study the anti-sulfur performance, the selected sample was treated in the gas atmosphere of 100 ppm SO 2 /Ar at 350 8C for 16 h. 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 NH 3 -SCR activity measurement: The NH 3 -SCR activity of the Cu-SSZ-13 was measured in the micro reactor.…”
Section: Methodsmentioning
confidence: 99%
“…(2) 1.210 g TEPA was added to solution and stirred for 1.0 h. (3) 0.7000 g NaOH and 0.5140 g NaAlO 2 (equals to about 0.2107 g Al 2 O 3 ) were added and stirred for 60 min. (4) 3.600 mL silica sol (equals to about 1.228 g SiO 2 ) was stirred with the solution for 3 h. (5) The mixed solution was transferred to Teflon-lined autoclaves and the crystallization reaction was carried out at 140 8C for 96 h. Then the product was washed and dried at 1008C for 12 h. (6) The product was treated in the nitric acid solution (pH = 1) at 80 8C for 12 h. Then it was separated by vacuum filtration, washed, and dried at 100 8C for 12 h. (7) The product was calcined at 550 8C for 4 h. By changing the mole ratios of Cu-TEPA/Al 2 To study the hydrothermal stability, the zeolite was treated in air flow containing 10 vol.% H 2 O of 25.0 mL·min À1 for 24 h at 750 8C. In order to study the anti-sulfur performance, the selected sample was treated in the gas atmosphere of 100 ppm SO 2 /Ar at 350 8C for 16 h. 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 NH 3 -SCR activity measurement: The NH 3 -SCR activity of the Cu-SSZ-13 was measured in the micro reactor.…”
Section: Methodsmentioning
confidence: 99%
“…Chromium based catalysts, e.g. amorphous and crystalline Cr 2 O 3, chrome supported on TiO 2, Al 2 O 3, Cr–MnOx mixed‐oxide, and Cr exchanged ZSM‐5 catalysts have been extensively studied over the last decade for the SCR of NO with NH 3 . They are quite promising catalysts for low‐temperature SCR operations.…”
Section: Introductionmentioning
confidence: 94%
“…The texture of PILC depends greatly on the pillars. Chromium oxide is not only a frequently used pillar, but also a SCR catalyst because of its large range of oxidation numbers and relative acidity . Chromium based catalysts, e.g.…”
Section: Introductionmentioning
confidence: 99%
“…Metal‐based ZSM‐5 zeolites were investigated as SCR catalysts in the beginning of 1990s, and quickly gained attention because of the comparable, or even superior performance on comparison with the commercialized V 2 O 5 ‐WO 3 /TiO 2 catalysts . In the past few decades, many transition metals (Cu, Fe, Cr, Mn, etc.) promoted ZSM‐5 catalysts have been utilized for NH 3 ‐SCR after the precursory work by Iwamoto and Hamada on Cu‐ZSM‐5.…”
Section: Current Zeolite‐based Nh3‐scr Materialsmentioning
confidence: 99%