HZSM-5分子筛固定床分离水体中硝基氯苯异构体

以Al₂O₃为粘结剂对粉末状HZSM-5分子筛成型,并通过HZSM-5分子筛固定床分离水体中硝基氯苯异构体.研究流量对分子筛固定床动态吸附与温度、流量对固定床动态脱附的影响,得出其动态吸附-脱附最优化条件:吸附流量25 mL/h;处理量1.35 L/批次;脱附温度40 ℃;脱附流量10 mL/h.设计了双柱串联吸附实验,以直接高效分离水体中的对硝基氯苯与邻硝基氯苯.结果表明,采用双柱串联吸附-脱附工艺,可从硝基氯苯混合液中同时回收纯度高于95%的对硝基氯苯和邻硝基氯苯,且动态吸附-脱附实验具有较好的重现性.      

柴油挥发行为的研究

对柴油进行了在玻璃表面皿上和在土壤中的挥发实验研究。在玻璃表面皿的挥发实验中,进行了30℃条件下柴油与90^#汽油、煤油及沙特原油挥发的对比实验。实验结果表明,柴油和煤油的挥发量与挥发时间呈指数关系,而90^#汽油与沙特原油的挥发量与挥发时间呈对数关系。柴油在土壤中的挥发实验表明,土壤质地、土壤的含水量及柴油浓度都影响柴油的挥发量。土壤中的柴油污染物有一种向上运动的所谓“灯芯”作用,适度的土壤含水量会促进“灯芯”作用,而过高的含水量则抑制其发生。     

SBAR中同步脱氮好氧颗粒污泥的菌种特性

采用气提式内循环间歇反应器进行好氧颗粒污泥培养,用分批培养法对好氧颗粒污泥中具有脱氮作用的菌种进行分离纯化.对各菌种进行了鉴别,通过培养过程中对氧气条件的控制,考察了各菌种反硝化生长特性和需氧性.结果表明,好氧颗粒污泥纯化培养可得到异养硝化-好氧反硝化菌以及兼性亚硝化菌和硝化菌,分离得到的反硝化菌在有氧反硝化条件下能够生长,因此好氧颗粒污泥中微生物具有多样性和较强的适应性,从侧面体现出好氧颗粒污泥微观结构的复杂性.     

人工湿地基质微生物状况与净化效果相关分析

利用混菌法和稀释法,测定了不同植物以及无植物潜流水平湿地基质中微生物的数量.结果表明:不同植物湿地基质中微生物的数量差异不显著,有植物和无植物湿地的差别不明显;湿地基质中不同空间位置的微生物数量各不相同,一般上层多于下层;在湿地运行条件相对稳定的情况下,湿地基质中会逐渐形成数量和活性比较稳定的生物群落.分析了人工湿地基质中微生物数量与污水净化效果的关系.结果表明:微生物数量与BOD₅及TN的去除有显著的相关性,说明微生物的作用是去除它们的重要途径;基质微生物数量与TP的去除率相关性不明显.测定了湿地基质硝化速率,其硝化能力与亚硝化细菌的数量呈显著相关.      

改性半焦脱除烟气中SO2的研究

对内蒙工业副产褐煤半焦（比表面积49.187m^2／g,孔容0.0351cm^2／g）,采用加压水热化学活化法,HNO3活化法和高温煅烧相结合的方法制备出半焦烟气脱硫剂,并对脱硫剂的脱硫性能进行固定床活性评价。分析表明,其脱硫效果比较好,转化率维持在50％以上的累计硫容可达24．30％,脱硫时间长达35h,远远高于原料半焦的脱硫效果（硫容为0．68％,时间为1．5h）;同时采用水洗法对脱硫剂进行再生,其再生液可用来制备浓度为9.01％的稀硫酸。     

Non-biodegradable landfill leachate treatment by combined process of agitation,coagulation, SBR and filtration

This study describes the complete treatment of non-biodegradable landfill leachate by combined treatment processes. The processes consist of agitation as a novel stripping method used to overcome the ammonia toxicity regarding aerobic microorganisms. The NH₃-N removal ratio was 93.9% obtained at pH 11.5 and a gradient velocity (G) 150 s^?1 within a five-hour agitation time. By poly ferric sulphate (PFS) coagulation followed the agitation process; chemical oxygen demand (COD) and biological oxygen demand (BOD₅) were removed at 70.6% and 49.4%, respectively at an optimum dose of 1200 mg L^?1 at pH 5.0. The biodegradable ratio BOD₅/COD was improved from 0.18 to 0.31 during pretreatment step by agitation and PFS coagulation. Thereafter, the effluent was diluted with sewage at a different ratio before it was subjected to sequencing batch reactor (SBR) treatment. Up to 93.3% BOD₅, 95.5% COD and 98.1% NH₃-N removal were achieved by SBR operated under anoxic–aerobic–anoxic conditions. The filtration process was carried out using sand and carbon as a dual filter media as polishing process. The final effluent concentration of COD, BOD₅, suspended solid (SS), NH₃-N and total organic carbon (TOC) were 72.4 mg L^?1, 22.8 mg L^?1, 24.2 mg L^?1, 18.4 mg L^?1 and 50.8 mg L^?1 respectively, which met the discharge standard. The results indicated that a combined process of agitation-coagulation-SBR and filtration effectively eliminated pollutant loading from landfill leachate.     

Experimental study on the stability of the ClHgSO3 − in desulfurization wastewater

Environmental Science and Pollution Research - Wet flue gas desulfurization technologies have received much concern for their superior performance on co-controlling the acid gases and mercury....     

Effects of river-lake interactions in water and sediment on phosphorus in Dongting Lake,China

Environmental Science and Pollution Research - As a large river connected lake, Dongting Lake is influenced by anthropogenic activities and the discharge from its upstream tributaries in the lake...