2012
DOI: 10.1016/j.jhazmat.2012.08.026
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Oxidation of ammonia to nitrogen over Pt/Fe/ZSM5 catalyst: Influence of catalyst support on the low temperature activity

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Cited by 51 publications
(28 citation statements)
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“…The main problem is related to development of the effective catalysts operating in the temperature of flue gases with high selectivity to dinitrogen. The catalytic systems studied in the process of selective ammonia oxidation [8] are divided into three main groups: (1) noble metals, which are active in relatively low temperatures but are low-selective to dinitrogen [9][10][11];…”
Section: Introductionmentioning
confidence: 99%
“…The main problem is related to development of the effective catalysts operating in the temperature of flue gases with high selectivity to dinitrogen. The catalytic systems studied in the process of selective ammonia oxidation [8] are divided into three main groups: (1) noble metals, which are active in relatively low temperatures but are low-selective to dinitrogen [9][10][11];…”
Section: Introductionmentioning
confidence: 99%
“…The effective SCO catalyst should operate in a relatively low temperature range (180-400°C) in order to reduce the operational costs connected with additional heating of waste streams [1,[7][8][9][10][11]. Moreover, it should selectively direct the reaction to the formation of the main products and should also be stable in the presence of water vapour or other typical components of flue gases such as COx and SOx [1,12].…”
Section: Introductionmentioning
confidence: 99%
“…However, despite several studies devoted to catalysts for a selective ammonia oxidation, a catalyst possessing high activity and selectivity over the required temperature range has not been presented yet. Major challenges are associated with the design of a suitable downstream catalyst: (i) the catalyst should exhibit high activity at relatively low temperatures (<400C) in order to avoid the need for additional heating of exhaust gases, (ii) the material has to possess sufficient stability in the presence of high concentrations of water vapour or other components of waste gases (COx, SOx) and (iii) should selectively convert NH3 into N2 [28,36,54]. Additionally, the NH3-SCR process was originally developed for stationary emission sources, mainly power plants, where the temperature of exhaust gases is relatively low and varies only in a narrow range of 250-400°C [55,56].…”
Section: Ammonia Slipstream Treatmentmentioning
confidence: 99%
“…28,79,85,116,186,187]. 37,54,105,142]. Investigations considering the influence of changes of the ammonia to oxygen molar ratio on the catalytic performance were only discussed in a limited number of publications [e.g.…”
Section: Effect Of Oxygen Contentmentioning
confidence: 99%