共查询到15条相似文献,搜索用时 46 毫秒
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脉冲放电等离子体处理硝基苯废水的实验研究 总被引:9,自引:0,他引:9
脉冲放电等离子体水处理技术主在利用高压毫微脉冲发生装置,在气液混合体中发生高压脉冲放电产业高能电子,紫外线以及气体放电产生臭氧多因素综合作用,增强处理效果,达到降解有机物的目的,实验结果表明,酸性和碱性条件有利于硝基苯的降解。 相似文献
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TiO2催化高压脉冲放电等离子体降解2,4-二硝基苯酚 总被引:3,自引:3,他引:0
采用TiO2催化高压脉冲放电等离子体降解废水中的2,4-二硝基苯酚,对反应进行了动力学研究.研究结果表明,在高压脉冲放电等离子体及TiO2催化高压脉冲放电等离子体反应中,2,4-二硝基苯酚的降解过程均符合表观一级反应动力学方程.加入TiO2催化剂、提高放电电压均可提高2,4-二硝基苯酚的降解反应速率常数.在TiO2加入量为0.15%、放电电压为16 kV时,2,4-二硝基苯酚的降解率为87.4%,TiO2的催化效应增强因子为1.55. 相似文献
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采用多针-板鼓泡气液混合纳秒脉冲放电等离子体系统对吸附苯酚饱和的活性炭进行再生。考察了外加电压、初始溶液电导率、初始溶液pH以及活性炭与高压电极之间的距离对活性炭再生效果的影响,表征了放电处理后活性炭表面官能团的变化。实验结果表明:在高低压电极间距25 mm、初始溶液电导率5 μS/cm、初始溶液pH=6、活性炭与高压电极之间距离0 mm的条件下,活性炭再生效果最好,再生率为126%,能量效率为15.1 kg/(kW·h)。表征结果显示,再生炭表面的O—H、C=C、C=O、C—O等官能团的含量均增加。 相似文献
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采用共沉淀—喷涂法制备了(Cu5Mn7Zr1O22)0.08/(γ-Al2O3)0.1/堇青石蜂窝陶瓷催化剂。表征结果显示:催化剂孔隙率较高,表面均匀分散着粒径介于20~100 nm的晶体颗粒。以硫化氢和乙硫醇为典型含硫恶臭污染物进行了低温等离子体协同催化降解实验,结果表明:污染物的降解率随着输入功率的增加而提高;与单纯低温等离子体相比,低温等离子体协同催化能获得更好的降解效果。降解机理可能为:在高能电子和活性粒子作用下,H2S或C2H5SH分子中键能较弱的H—S、C—S和C—C键断裂形成·SH、·C2H5、·CH2SH、·CH3等小碎片基团,这些小碎片基团进一步发生聚合、氧化或自由基链式反应,最终降解为CO2、SO2、SO3、H2O等无毒小分子。 相似文献
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系统分析了煤化工行业的产排污情况,梳理了国内外相关排放标准。结果表明:国内仅焦化等部分工序有行业排放标准,其余工序目前执行水或大气的综合排放标准,其污染物项目不能全面反映煤化工行业的污染特征,急需制定煤化工行业污染物排放标准;国外相关标准情况与国内类似,无直接借鉴意义。建议:合理界定煤化工排放标准的适用范围,与其他排放标准协调配套,控制整个行业的污染物排放;针对大气污染物,明确各排放口的特征污染物,结合综合指标和高毒性物质指标进行挥发性有机物的排放控制;针对水污染物,引入综合毒性指标以有效控制废水中有毒有害污染物排放的环境风险。 相似文献
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Takafumi Fujita Takayuki Kawano Liwei Huang Yoshihiro Kojima Hitoki Matsuda Koichi Ushiroebisu 《Journal of Material Cycles and Waste Management》2007,9(1):15-20
To control the emission of halides into the environment, an experiment on the nonthermal plasma decomposition of the halides
CF4, CHF3, C2HCl3, and CHClF2 was conducted in a wire-in-tube corona reactor. It was found that the decomposition of C2HCl3 and CHClF2 was easy compared with the decomposition of CF4 and CHF3. With the addition of H2 in N2 gas, the decomposition ratio of CF4, C2HCl3, and CHClF2 increased. In contrast, the decomposition ratio of CHF3 in a hydrogen-rich atmosphere was lower than that in an N2 atmosphere. It was demonstrated that the yields of HF and/or HCl formed during halide decomposition clearly increased in
the presence of H2 in N2 gas. Furthermore, in order to prevent the production of unwanted products from halide decomposition, a combination of plasma
decomposition and in situ alkaline absorption was devised by coating a layer of Ca(OH)2 onto the surface of the grounding electrode. It was demonstrated that the Ca(OH)2 sorbent played an effective role as a scavenger, participating in halide decomposition by capturing reaction products such
as HCl and HF, therefore resulting in increased halide decomposition. 相似文献
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In this study, mono-digestion of rendering wastes and co-digestion of rendering wastes with potato pulp were studied for the first time in continuous stirred tank reactor (CSTR) experiments at 55 °C. Rendering wastes have high protein and lipid contents and are considered good substrates for methane production. However, accumulation of digestion intermediate products viz., volatile fatty acids (VFAs), long chain fatty acids (LCFAs) and ammonia nitrogen (NH4-N and/or free NH3) can cause process imbalance during the digestion. Mono-digestion of rendering wastes at an organic loading rate (OLR) of 1.5 kg volatile solids (VS)/m3 d and hydraulic retention time (HRT) of 50 d was unstable and resulted in methane yields of 450 dm3/kg VSfed. On the other hand, co-digestion of rendering wastes with potato pulp (60% wet weight, WW) at the same OLR and HRT improved the process stability and increased methane yields (500–680 dm3/kg VSfed). Thus, it can be concluded that co-digestion of rendering wastes with potato pulp could improve the process stability and methane yields from these difficult to treat industrial waste materials. 相似文献