Performance of ventilation air methane combustion over transition metal oxide oxygen carriers
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摘要: 采用反應管對基于過渡金屬氧化物載氧體的煤礦通風瓦斯(VAM)處理性能展開了研究.結果表明,經活化后的三種載氧體均能將CH4完全轉化為CO2,其活性順序為CuO60/γ-Al2O3 > NiO60/γ-Al2O3 > Fe2O360/γ-Al2O3;基于CuO60/γ-Al2O3的CH4轉化率隨空速的增加而減小,隨CuO負載量和床層溫度的升高而增大;煤礦通風瓦斯中的CH4濃度越低,CH4轉化率達到90%所需的床層溫度就越低;對活性物質低分散高負載的CuO60/γ-Al2O3和活性物質高分散低負載的CuO5.5/γ-Al2O3兩種CuO/γ-Al2O3系載氧體進行了比較,發現兩種載氧體的CH4轉化機理均包含有化學鏈燃燒和催化燃燒兩種機理,基于催化燃燒機理的CH4轉化率在一定溫度下存在極大值,當床層溫度高于該極大值溫度時,化學鏈燃燒對CH4轉化率的貢獻明顯大于催化燃燒對CH4轉化率的貢獻;相同條件下,CuO5.5/γ-Al2O3的初期活性優于Cu60/γ-Al2O3,但CuO60/γ-Al2O3的活性穩定性優于CuO5.5/γ-Al2O3.Abstract: The performance of combustion of ventilation air methane (VAM) over transition metal oxide oxygen carriers was studied through experiments with using tube reactors. The results show that the activity of activated oxygen carriers in converting CH4 to CO2 is as follows:CuO60/γ-Al2O3 > NiO60/γ-Al2O3 > Fe2O360/γ-Al2O3. CH4 conversion based on CuO60/γ-Al2O3 decreases with increasing gas hourly space velocity, but increases with increasing bed temperature and CuO loading. The lower the initial CH4 concentration of ventilation air methane, the lower is the temperature for the CH4 conversion of 90%. There are catalytic combustion mechanisms and chemical-looping combustion mechanisms for CH4 combustion over both CuO60/γ-Al2O3, for which dispersion of the active component is low but loading is high, and CuO5.5/γ-Al2O3, for which dispersion of the active component is high but loading is low. There exists a maximum for CH 4 conversion based on the catalytic combustion mechanism at some temperatures, and when the bed temperature is higher than this temperature, the contribution of chemical-looping combustion is greater than that of catalytic combustion. The initial activity of CuO5.5/γ-Al2O3 is higher than that of CuO60/γ-Al2O3, while the stability of CuO60/γ-Al2O3 activity is better than that of CuO5.5/γ-Al2O3 activity under the same conditions.
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參考文獻
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