2023
DOI: 10.1016/j.apsusc.2023.158124
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Unraveling the synergy between MnOx and CeO2 in MnOx-CeO2 SCR catalysts based on experimental and DFT studies

Fei Wang,
Songda Li,
Ruiyang You
et al.
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Cited by 12 publications
(5 citation statements)
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“…NO x conversion and N 2 selectivity as a function of reaction temperature between 150 and 600 • C in the Cu-SSZ-39, CeO 2 /Cu-SSZ-39, CeMnO x /Cu-SSZ-39, and MnO x /Cu-SSZ-39 catalysts are shown in Figure 3a and Figure S3a. Cu-SSZ-39 showed a so-called "seagull shape" curve resulting from its low Cu loading [18], while MnO x /Cu-SSZ-39 presented an evident decline in NO x conversion over 400 • C. The presence of CeO 2 and CeMnO x significantly benefitted the low-temperature NO x reduction performance of the catalysts, particularly for CeMnO x /Cu-SSZ-39, whose active temperature window is from 180 to 600 • C. The higher catalytic performance of CeMnO x /Cu-SSZ-39 in comparison with those of CeO 2 /Cu-SSZ-39 and MnO x /Cu-SSZ-39 indicated the existence of synergetic effects between Ce and Mn in CeMnO x in improving the low-temperature activity of Cu-SSZ-39 [18,41], which is consolidated by varying Mn/(Ce + Mn) ratios (Figure S4). After hydrothermal aging at 800 • C, NO x conversions of the Cu-SSZ-39-A, CeO 2 /Cu-SSZ-39-A, and MnO x /Cu-SSZ-39-A catalysts declined, and their active temperature window became narrow (Figure 3b).…”
Section: Scr Performancementioning
confidence: 99%
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“…NO x conversion and N 2 selectivity as a function of reaction temperature between 150 and 600 • C in the Cu-SSZ-39, CeO 2 /Cu-SSZ-39, CeMnO x /Cu-SSZ-39, and MnO x /Cu-SSZ-39 catalysts are shown in Figure 3a and Figure S3a. Cu-SSZ-39 showed a so-called "seagull shape" curve resulting from its low Cu loading [18], while MnO x /Cu-SSZ-39 presented an evident decline in NO x conversion over 400 • C. The presence of CeO 2 and CeMnO x significantly benefitted the low-temperature NO x reduction performance of the catalysts, particularly for CeMnO x /Cu-SSZ-39, whose active temperature window is from 180 to 600 • C. The higher catalytic performance of CeMnO x /Cu-SSZ-39 in comparison with those of CeO 2 /Cu-SSZ-39 and MnO x /Cu-SSZ-39 indicated the existence of synergetic effects between Ce and Mn in CeMnO x in improving the low-temperature activity of Cu-SSZ-39 [18,41], which is consolidated by varying Mn/(Ce + Mn) ratios (Figure S4). After hydrothermal aging at 800 • C, NO x conversions of the Cu-SSZ-39-A, CeO 2 /Cu-SSZ-39-A, and MnO x /Cu-SSZ-39-A catalysts declined, and their active temperature window became narrow (Figure 3b).…”
Section: Scr Performancementioning
confidence: 99%
“…Catalysts 2024, 14, x FOR PEER REVIEW 5 of 18 [18,41], which is consolidated by varying Mn/(Ce + Mn) ratios (Figure S4). After hydrothermal aging at 800 °C, NOx conversions of the Cu-SSZ-39-A, CeO2/Cu-SSZ-39-A, and MnOx/Cu-SSZ-39-A catalysts declined, and their active temperature window became narrow (Figure 3b).…”
Section: Scr Performancementioning
confidence: 99%
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“…Ce-based SCR catalysts have attracted the interest of many researchers due to their satisfactory oxygen storage ability and redox performance . However, pristine CeO 2 exhibits fairly low catalytic activity and poor thermal stability at high temperature . A feasible approach is to add Zr in CeO 2 , which is conducive to combining the high refractory property of ZrO 2 and the superior oxygen storage capacity of CeO 2 , thus improving the thermostability and NH 3 -SCR efficiency at medium temperature. However, low-temperature catalytic performance and SO 2 resistance of Ce–Zr mixed oxides are still lacking, which hinders their application in industry.…”
Section: Introductionmentioning
confidence: 99%
“…In recent decades, there has been an exponential increase in exhaust pollution, posing significant dangers to human health and natural systems. Because nitrogen oxides (NO x ) will cause acid rain, photochemical smog, and damage to the ozone layer, removing NO x from the exhaust gas of various combustion sources (e.g., industrial pollution and vehicle exhaust) is one of the key steps toward pollution control. Ammonia-selective catalytic reduction (NH 3 -SCR) is currently the most effective technology for NO x reduction. However, commercialized SCR catalysts (V 2 O 5 /WO 3 /TiO 2 ) typically require an additional heat source to reach the working temperature of around 350–400 °C, which significantly increases the cost and thus is not suitable for most nonelectric factories as indicated in the previous references. Thus, the scientific research area is focusing on low-temperature (LT) SCR (<300 °C) reactions, which have become a current hot spot and a future trend of SCR catalyst studies.…”
mentioning
confidence: 99%