Nitrogen transformation during coal decoulping combustion Ⅲ: NO and N2O reduction with multi-component of pyrolysis gas
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Graphical Abstract
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Abstract
Reduction of NO and N2O with the simulated pyrolysis gas of NH3-CO-H2-CH4-O2 mixture was experimentally studied in an ideal plug flow reactor. The effects of temperature, excess air number λ, concentration of CH4, CO, H2, NH3 in the simulated pyrolysis gas, concentration of NO and N2O in the simulated flue gas on reduction of NO, N2O and total nitrogen conversion efficiency were experimentally investigated. The results show that adding combustible or reducing species of CO, H2, CH4 into NH3 can decease about 150~200 K of temperature range or window for reducing NO, the obtained optimal temperature range of reducing NO is in a range of 1 073~1 223 K. The excess air number λ or oxygen content in NH3-CO-H2-CH4-O2 mixture shows an important influence on reduction of NO and N2O. When the excess air number λ is controlled as 0.6, i.e., similar to the case of fuel-rich, the maximum decomposition ratio of NO and N2O in the simulated flue gas reaches 60.6% and 100%, respectively. When the excess air number λ is kept at 0.6 in a temperature range of 1 073~1 223 K, higher concentration of CH4, CO, H2 in the simulated pyrolysis gas can result in an effectively decomposition of N2O, but lead to an increase of NO; however, higher conversion efficiency of NO can be achieved under the condition of increasing the concentration of NH3 in the simulated pyrolysis gas.
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