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作 者:HU XiaoYing DONG ChangQing YANG YongPing ZHANG JunJiao
出 处:《Chinese Science Bulletin》2011年第14期1429-1433,共5页
基 金:supported by the National Natural Science Foundation of China (50976032);the National High Technology Research and Development of China (2008AA05Z302);the National Basic Research Program of China (2009CB219801);the Key Project of Ministry of Education of China (108033,107119);Nature Science Foundation of Beijing (3101001);Fundamental Research Funds for the Central Universities (09ZG03);Doctoral Program of North China Electric Power University (200822015)
摘 要:The fossil fuel consumption and pollutant emissions in a coal fired fluidized bed boiler could be reduced by biomass pyrolysis gas reburning.The influence of three kinds of biomass pyrolysis gases on the emission of N_2O in a laboratory scale fluidized bed was investigated using the mechanism of GRI3.0 in this paper.The results showed that:the effect of sawdust pyrolysis gas reburning on N_2O was more significant than that of rice husk and orange peel under the same conditions;the increase of initial oxygen content from 1% to 8% in flue gas would restrain the decomposition of N_2O;the N_2O decomposition was enhanced by increasing reaction temperature from 1073.15 K to 1323.15 K,and the decomposition rate may reach 99% at 1223.15 K.The fossil fuel consumption and pollutant emissions in a coal fired fluidized bed boiler could be reduced by biomass pyrolysis gas reburning. The influence of three kinds of biomass pyrolysis gases on the emission of N2O in a laboratory scale fluidized bed was investigated using the mechanism of GRI3.0 in this paper. The results showed that: the effect of sawdust pyrolysis gas reburning on N2O was more significant than that of rice husk and orange peel under the same conditions; the increase of initial oxygen content from 1% to 8% in flue gas would restrain the decomposition of N2O; the N2O decomposition was enhanced by increasing reaction temperature from 1073.15 K to 1323.15 K, and the decomposition rate may reach 99% at 1223.15 K.
关 键 词:N2O排放 生物质热解 流化床锅炉 气体再燃 燃煤 N2O分解 实验室规模 燃料消耗
分 类 号:TK229.6[动力工程及工程热物理—动力机械及工程]
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