2019
DOI: 10.1016/j.apcatb.2019.01.039
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Investigation of the robust hydrothermal stability of Cu/LTA for NH3-SCR reaction

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Cited by 73 publications
(44 citation statements)
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“…The data in Table 1 show that the hydrothermal aging at 900 • C resulted in about 7% decrease in BET surface area of PdLTA, whereas the corresponding value was about 27% for PdAl. The BET results are in line with earlier measurements on similar samples, for example we observed 542 m 2 /g for Cu/LTA treated at 750 • C and 495 m 2 /g when it was aged at 900 • C [17]. Moreover, the aging only caused minor changes in pore volume for PdLTA and PdAl (Table 1).…”
Section: Characterizationsupporting
confidence: 92%
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“…The data in Table 1 show that the hydrothermal aging at 900 • C resulted in about 7% decrease in BET surface area of PdLTA, whereas the corresponding value was about 27% for PdAl. The BET results are in line with earlier measurements on similar samples, for example we observed 542 m 2 /g for Cu/LTA treated at 750 • C and 495 m 2 /g when it was aged at 900 • C [17]. Moreover, the aging only caused minor changes in pore volume for PdLTA and PdAl (Table 1).…”
Section: Characterizationsupporting
confidence: 92%
“…For PdAl, small changes in diffraction peaks corresponding to the support material can be noted, however it can be concluded that support material mainly consisted of γ-Al 2 O 3 also after the hydrothermal aging [23]. The N 2 physisorption and XRD results indicate that the LTA zeolite is extraordinarily resistant towards structural changes upon hydrothermal aging, which agrees well with our previous report [17]. However, Al 2 O 3 expressed also high thermal stability.…”
Section: Characterizationsupporting
confidence: 90%
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“…Limited by the narrow temperature window (320-450 • C), insufficient hydrothermal stability and biotoxicity, conventional vanadia catalysts have gradually been replaced by nontoxic metal-based zeolite catalysts, especially Cu-based zeolites with a wide temperature window (200-500 • C) and high hydrothermal stability in NH 3 -SCR [4,5], owing to their unique properties such as high surface areas, considerable acidity and well-defined pore systems with stable structure which can sustain up to 800 • C [6,7]. In addition, due to the high redox activity of Cu species, Cu-based zeolites such as Cu/SSZ-13 [7,8], Cu/SAPO-34 [9,10], Cu/LTA [8,11] and Cu/SSZ-39 [12,13] have become the most used catalysts in NH 3 -SCR, especially in the low temperature range (200-350 • C) [13,14]. Currently, Cu/SSZ-13-based catalysts have been commercially applied in the treatment of diesel engine exhausts in the USA and Europe [5,14,15].…”
Section: Introductionmentioning
confidence: 99%