2002
DOI: 10.1016/s0016-2361(02)00016-9
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Kinetic relationship between NO/N2O reduction and O2 consumption during flue-gas recycling coal combustion in a bubbling fluidized-bed

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Cited by 28 publications
(35 citation statements)
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“…Using a constant value of 176 kJ mol À1 for the global surface reaction activation energy, E 0 , for lignite char steam gasification from the literature [7], k 0 o is estimated by best-fitting the gasification data (with minimal transport effects), using Eqs. (4) and (5). k 0 o , for raw coal char prepared at 900 and 1000°C and demineralised coal char prepared at 1000°C, is found to be 34.3, 21.0, 4.39 g m À2 s À1 (g m À3 ) À0.5 , respectively.…”
Section: Experimental Results As Input Data To the Modelmentioning
confidence: 89%
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“…Using a constant value of 176 kJ mol À1 for the global surface reaction activation energy, E 0 , for lignite char steam gasification from the literature [7], k 0 o is estimated by best-fitting the gasification data (with minimal transport effects), using Eqs. (4) and (5). k 0 o , for raw coal char prepared at 900 and 1000°C and demineralised coal char prepared at 1000°C, is found to be 34.3, 21.0, 4.39 g m À2 s À1 (g m À3 ) À0.5 , respectively.…”
Section: Experimental Results As Input Data To the Modelmentioning
confidence: 89%
“…1); k 0 o in this case is found to be 22.1 g m À2 s À1 (g m À3 ) À0. 5 . The global mth-order approach, tested with other gasification data under different steam partial pressures which could possibly result from moisture in coal of various moisture contents (at 900 and 1000°C), was found to be adequate for modelling the char gasification.…”
Section: Experimental Results As Input Data To the Modelmentioning
confidence: 99%
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“…As one of the most efficient NO x emission reduction methods, FGR has been applied in reducing NO x emissions by numerous researchers [1][2][3][4][5][6][7][8][9][10]. However, a fuel-rich zone usually must be created in the application of this technique.…”
Section: Introductionmentioning
confidence: 99%