2018
DOI: 10.1016/j.catcom.2017.11.009
|View full text |Cite
|
Sign up to set email alerts
|

Supported and unsupported manganese oxides for catalytic ammonia combustion

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
5
0

Year Published

2019
2019
2024
2024

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 14 publications
(5 citation statements)
references
References 19 publications
0
5
0
Order By: Relevance
“…The intensity of the diffraction peaks of the activated carbon became weaker, indicating that the diffraction peaks of the activated carbon decreased after loading of manganese onto the activated carbon. It has also been demonstrated that MnO 2 [54] has the best catalytic treatment performance among the various valence states of manganese oxides.…”
Section: Fig 2 Cod Removal Rates Of Different Catalystsmentioning
confidence: 99%
“…The intensity of the diffraction peaks of the activated carbon became weaker, indicating that the diffraction peaks of the activated carbon decreased after loading of manganese onto the activated carbon. It has also been demonstrated that MnO 2 [54] has the best catalytic treatment performance among the various valence states of manganese oxides.…”
Section: Fig 2 Cod Removal Rates Of Different Catalystsmentioning
confidence: 99%
“…The ideal catalyst should be selective and active in a broad temperature range and should possess high water-tolerance and very low sensitivity to sulphur poisoning. 14,15 In the last decades, several catalytic systems have been proposed for this process, such as supported or unsupported noble metals, [16][17][18] transition metal oxides, 16,[19][20][21] and mixed oxides. [22][23][24][25] In particular, iron [26][27][28] and copper [28][29][30][31] oxides have demonstrated to be active and selective catalysts.…”
Section: Nh3 + 3o2 → 2n2 + 6h2omentioning
confidence: 99%
“…The ideal catalyst should be selective and active in a broad temperature range and should possess high water tolerance and very low sensitivity to sulfur poisoning. , In the past decades, several catalytic systems have been proposed for this process, such as supported or unsupported noble metals, transition-metal oxides, , and mixed oxides. In particular, iron and copper oxides have demonstrated to be active and selective catalysts. On the other hand, Fe and Cu demonstrated to be active and selective species also when encapsulated as ions inside zeolitic frameworks probably due to the possibility to work in two different oxidation states (Fe 2+ /Fe 3+ and Cu 2+ /Cu + ) …”
Section: Introductionmentioning
confidence: 99%
“…The apparent reason for this was that Mn-Bi-O system performed optimally under an excess of O 2 , requiring its removal downstream and significantly increasing the costs. In contrast, the use of stoichiometric reactant amounts would likely have had a negative effect on the catalyst stability, as transition metal-based catalysts are known to suffer from deactivation due to over-reduction of the active phase [15,[24][25][26][27] -a key limitation of this class of materials.…”
Section: Introductionmentioning
confidence: 99%