1995
DOI: 10.1016/0016-2361(95)92650-u
|View full text |Cite
|
Sign up to set email alerts
|

Formation and decomposition of N2O in fluidized bed boilers

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
20
0

Year Published

1996
1996
2015
2015

Publication Types

Select...
6
1

Relationship

0
7

Authors

Journals

citations
Cited by 54 publications
(21 citation statements)
references
References 8 publications
1
20
0
Order By: Relevance
“…It can be concluded from the calculated E A -values, that in the case of coke the overall combustion process is mainly chemically controlled at combustion temperatures between 750 and 950°C, whereas in the case of coal and semianthracite the influence of mass transfer processes distinctly dominates. With E A -values of about 94 kJ/mol [23] and 98-104 kJ/mol [24] for several kinds of coke quite comparable values have been published recently. Whereas the first value was kept also in the case of fluidized bed combustion, the latter values are results of similar model considerations in a fixed bed reactor.…”
Section: Fig 12supporting
confidence: 57%
“…It can be concluded from the calculated E A -values, that in the case of coke the overall combustion process is mainly chemically controlled at combustion temperatures between 750 and 950°C, whereas in the case of coal and semianthracite the influence of mass transfer processes distinctly dominates. With E A -values of about 94 kJ/mol [23] and 98-104 kJ/mol [24] for several kinds of coke quite comparable values have been published recently. Whereas the first value was kept also in the case of fluidized bed combustion, the latter values are results of similar model considerations in a fixed bed reactor.…”
Section: Fig 12supporting
confidence: 57%
“…In the power generation sector, circulating fluidized bed (CFB) combustion is often applied for its wide fuel adaptability, high combustion efficiency and intensity, and lower NO x emission, etc. However, the reported N 2 O emission level even reached 360 mg/m 3 at part load condition for a CFB boiler with thermal output above 200 MW [3], which is much higher than conventional pulverized coal-fired power plants. The nitrogen chemistry in CFB combustion and other fuel utilizing industry has long been a research focus [4][5][6][7][8][9] but it is still not fully understood because of the complex coupling of in-furnace combustion, heat and mass transfer, homogeneous and heterogeneous chemical reactions, etc.…”
Section: Introductionmentioning
confidence: 83%
“…The nitrogen chemistry in CFB combustion and other fuel utilizing industry has long been a research focus [4][5][6][7][8][9] but it is still not fully understood because of the complex coupling of in-furnace combustion, heat and mass transfer, homogeneous and heterogeneous chemical reactions, etc. The dependence of N 2 O emission on important process parameters such as furnace temperature, excess air ratio, stoichiometry, with or without the presence of limestone was studied [3,[10][11][12][13], but the detailed mechanism still deserves more research effort.…”
Section: Introductionmentioning
confidence: 99%
“…Both the amount of nitrogen in fuel and the fuel-O/fuel-N ratio have an effect on N 2 O emissions (Hämäläinen and Aho, 1996). N 2 O is formed not only from volatile nitrogen species (e.g., HCN) originating from fuel nitrogen but also from nitrogen of char and by heterogeneous reactions on the char surface (Bonn et al, 1995). Therefore, N 2 O formation can also take place, especially in fluidized-bed combustion, by the reduction of the initially formed NO by the char particles ( Jones and Thomas, 1995).…”
Section: Resultsmentioning
confidence: 99%