摘要
随着SF_6在电力行业中的应用越来越广泛,年排放量也达到了相当大的规模,由于其具有高GWP值,对SF_6降解后无害化处理就显得尤为重要。通过自行设计的DBD等离子体反应器对体积分数为2%的SF_6进行流动降解处理,分别分析了加H_2O和O_2对SF_6降解效率和降解产物的影响。研究表明,在单独加H_2O或O_2或两者都加时均能极大提高SF_6的降解率,使2%的高浓度SF_6降解率从60%提高到96%以上;在添加0.5%的H_2O和2%的O_2协同作用下,在50 mL/min的体积流量下SF_6降解率达到了98.2%。通过GC-MS和FTIR检测结果显示H_2O的参与使SF_6降解过程中倾向于生成SO_2,O_2的参与使SF_6降解过程中倾向于生成SO_2F2,为调节降解产物提供了研究方向。
With the increasingly application of SF_6 in the power industry, the annual emissions have reached a considerable scale. Because of its high global warming potential(GWP) value, the harmless treatment of SF_6 after degradation is important. In this paper, the SF_6 with a concentration of 2% was degraded by a self-designed DBD plasma reactor under flowing conditions. The effects of adding H_2O and O_2 on the degradation efficiency and products of SF_6 were analyzed. Studies show that when H_2O or O_2 is added alone or when both are added, the degradation rate of SF_6 can be greatly increased, and the degradation rate of high concentration SF_6(2%) is increased from 60% to more than 96%; Under the addition of 0.5% H_2O and 2% O_2, the degradation rate of SF_6 reaches 98.2% at a flow rate of 50 ml/min. The results of GC-MS and FTIR show that the participation of H_2O tends to generate SO_2 during the degradation of SF_6, and the involvement of O_2 tends to generate SO_2F2, which provide a research direction for the regulation of degradation products.
引文
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