1993
DOI: 10.1016/0920-5861(93)80023-t
|View full text |Cite
|
Sign up to set email alerts
|

Selective oxidation of ammonia to nitrogen over SiO2-supported MoO3 catalysts

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

3
47
0

Year Published

2001
2001
2022
2022

Publication Types

Select...
8

Relationship

0
8

Authors

Journals

citations
Cited by 71 publications
(50 citation statements)
references
References 29 publications
3
47
0
Order By: Relevance
“…30,36,88,96,120,130,146,181] and (iii) the internal selective catalytic reduction (i-SCR) mechanism [e.g. 32,37,38,89,96,105,109,111,138,144,179,191]. A detailed description of these mechanisms was given by Jabłońska et al [e.g.…”
Section: The Mechanisms Of Nh3-scomentioning
confidence: 99%
See 1 more Smart Citation
“…30,36,88,96,120,130,146,181] and (iii) the internal selective catalytic reduction (i-SCR) mechanism [e.g. 32,37,38,89,96,105,109,111,138,144,179,191]. A detailed description of these mechanisms was given by Jabłońska et al [e.g.…”
Section: The Mechanisms Of Nh3-scomentioning
confidence: 99%
“…[28][29][30][31][32]. The application areas for NH3-SCO include for instance the treatment of waste gases from chemical production processes, ammonia slip from the NH3-SCR process and gasification of biomass [e.g.…”
Section: Introductionmentioning
confidence: 99%
“…The N 2 /NO 2 was added to the stream when the ammonia concentration was just below 0.2 mol-%. The conversion (Conv) of ammonia was calculated in the ordinary way as: Ef= |df(x,y)/dx|*Ex +|df(x,y)/dy|*Ey (12) In our case, E f is the error of margin of the conversion, |df(x,y)/dx| the partial differential of the conversion with respect to x (inlet molar ratio, if y is outlet molar ratio) and E x the margin of error in parameter x.…”
Section: Nox Reduction In the Model Synthesis Gasmentioning
confidence: 99%
“…In some of them [9,10] the concentration of CO and H 2 is very low, compared to a real synthesis gas produced in a gasifier. In others [11][12][13][14][15], it is not clear if the process studied really is SCO or ammonia cracking driven by the temperature increase, caused by CO and H 2 combustion in the catalytic bed due to the oxygen injection.…”
Section: Introductionmentioning
confidence: 99%
“…Various kinds of catalysts that oxidize gaseous NH 3 have been examined. For example, de Boer et al (1993) studied the selective conversion of NH 3 to N 2 over V 2 O 5 , MoO 3 , and WO 3 catalysts on various supports at 525 K in the SCO reaction. Amblard et al (2000) performed excellent selective conversion of NH 3 to gaseous nitrogen using a γ-Al 2 O 3 -supported Ni catalyst in an SCO process.…”
Section: Introductionmentioning
confidence: 99%