高压脉冲放电等离子体处理活性红X-3B染料废水

采用高压脉冲放电等离子体技术对活性红X-3B染料废水进行处理,考察了废水电导率、脉冲电压、脉冲频率、针板间距以及曝气量对处理效果的影响。实验结果表明,当废水电导率为200μS/cm、脉冲电压为34kV、脉冲频率为60Hz、针板间距为15mm、曝气量为12L/h、处理时间为60m in时,活性红X-3B染料废水脱色率能达到98.6%。     

多孔性Mn3O4的制备及其对水中镉的吸附

采用硫酸锰水解-氧化两步法制备了多孔性四氧化三锰,以X射线衍射、扫描电镜和氮吸附比表面仪对其进行了表征,研究了该多孔性Mn3O4在不同的溶液pH值、吸附时间、投加量和温度下对水中Cd(Ⅱ)的吸附行为,并测定了吸附过程的动力学和热力学参数。实验结果表明,该法合成的四氧化三锰属四方体心结构,一次晶粒尺寸为45.8 nm,颗粒间存在大量的孔洞,BET法比表面积为40.27 m2/g。在293 K,pH 5.5,吸附12 h时达到平衡,饱和吸附量为12.8 mg/g。该吸附过程符合准二级反应动力学模型,其反应的吸附活化能为2.743 kJ/mol,吸附等温线较好地符合Langmuir等温方程,吸附焓变和熵变均为正值,自由能变为负值,说明该吸附过程为自发的吸热过程。     

不同因素对人工湿地基质脱氮除磷效果的影响

在人工配制的污水中投入一定量的基质,不同条件下振荡培养,评价沸石、炉渣和陶瓷滤料3种基质在不同因素影响下对氨氮(NH4+-N)和总磷(TP)的吸附能力。结果表明,不同吸附时间时,沸石对NH4+-N的吸附效果最好,陶瓷滤料对TP的吸附效果最好;进水浓度对沸石吸附NH4+-N的影响较大,其吸附量随进水浓度的增大而增大,进水浓度对炉渣和陶瓷滤料吸附NH4+-N及炉渣吸附TP影响不大;3种基质对NH4+-N和TP的吸附量均是随吸附剂量的增加而降低,要达到较好的去污效果,应根据实验结果考虑基质投入量;pH值对沸石吸附NH4+-N影响显著,pH值6～7范围内吸附效果最好,pH值8～12的碱性条件有利于基质对TP的吸附。     

臭氧联用技术深度处理腈纶废水的效果对比

将臭氧分别与超声波、H2O2、紫外光等联用，深度处理干法腈纶生产厂生化池出水，对各种联用技术的处理效果进行了研究。实验结果表明：在进水流量2 L/min、反应时间30 min、臭氧加入量3.5 g/（L?h）的条件下，当超声功率为300 W时，臭氧-超声联用技术的COD去除率为30.0%；当H2O2加入量为0.4 mL/L时，臭氧-H2O2联用技术的COD去除率为50.7%；当紫外灯功率为40 W时，臭氧-紫外光联用技术的COD去除率为49.9%；在各种联用技术中，臭氧-H2O2联用技术的运行成本最低（为7.5 元/t），且处理后出水COD为143 mg/L，达到《<污水综合排放标准>（GB8978—1996）中石化工业COD标准值修改单》中的一级排放标准。综合考虑，臭氧-H2O2联用技术是深度处理干法腈纶废水的最优工艺。     

低SO_2氧化率脱硝催化剂的开发

介绍了SCR脱硝催化剂中V2O5对SO2的氧化及SO2氧化对脱硝催化剂及其下游设备的危害,分析了脱硝催化剂中V2O5对SO2氧化的原理和影响因素,探讨了低SO2氧化率脱硝催化剂开发方面的研究成果。     

Organochlorine pesticides and PCBs in fish from lakes of the Tibetan Plateau and the implications

High mountains may play significant roles in the global transport of persistent organic pollutants (POPs). This work aims to investigate the levels, patterns and distribution of semi-volatile organoclorine pollutants and to improve the understanding of the long-range atmospheric transport and fate of contaminants on the Tibetan Plateau. A total of 60 fish samples were collected from eight lakes located between 2813 and 4718 m above sea level across the Plateau. Concentrations of polychlorinated biphenyls (PCBs), organochlorine pesticides (OCPs) including dichlorodiphenyltrichloroethane and its metabolites (DDTs), hexachlorocyclohexanes (HCHs) and hexachlorobenzene (HCB) were measured in fish muscle. The results showed that concentrations of DDT, HCH and HCB were comparable to or lower than those found in remote mountains of Europe, Canada and US, while PCB concentrations in fish were, on average, about 4-150 times lower on Tibet than at other mountain areas. The transport and fate of contaminants in the Plateau are significantly influenced by the unique climatological and meteorological conditions, particularly by the summer Indian monsoon and winter westerly jet stream.     

Optimum conditions for microbial carbonate precipitation

The type of bacteria, bacterial cell concentration, initial urea concentration, reaction temperature, the initial Ca(2+) concentration, ionic strength, and the pH of the media are some factors that control the activity of the urease enzyme, and may have a significant impact on microbial carbonate precipitation (MCP). Factorial experiments were designed based on these factors to determine the optimum conditions that take into consideration economic advantage while at the same time giving quality results. Sporosarcina pasteurii strain ATCC 11859 was used at constant temperature (25°C) and ionic strength with varying amounts of urea, Ca(2+), and bacterial cell concentration. The results indicate that the rate of ureolysis (k(urea)) increases with bacterial cell concentration, and the bacterial cell concentration had a greater influence on k(urea) than initial urea concentration. At 25 mM Ca(2+) concentration, increasing bacterial cell concentration from 10(6) to 10(8)cells mL?1 increased the CaCO(3) precipitated and CO(2) sequestrated by over 30%. However, when the Ca(2+) concentration was increased 10-fold to 250 mM Ca(2+), the amount of CaCO(3) precipitated and CO(2) sequestrated increased by over 100% irrespective of initial urea concentration. Consequently, the optimum conditions for MCP under our experimental conditions were 666 mM urea and 250 mM Ca(2+) at 2.3×10? cells mL?1 bacterial cell concentration. However, a greater CaCO(3) deposition is achievable with higher concentrations of urea, Ca(2+), and bacterial cells so long as the respective quantities are within their economic advantage. X-ray Diffraction, Scanning Electron Microscopy and Energy Dispersive X-ray analyzes confirmed that the precipitate formed was CaCO(3) and composed of predominantly calcite crystals with little vaterite crystals.     

用废变压器油吸收废气中的二甲苯

以废变压器油作为吸收剂对二甲苯废气进行吸收处理,考察了影响二甲苯气体去除率的因素。实验结果表明:二甲苯废气流量为350 L/h、废变压器油喷淋量为40 L/h、进口二甲苯废气平日质量浓度为935 mg/m~3、吸收温度为18℃、吸收时间为50 min时,出口二甲苯气体质量浓度为35 mg/m~3,二甲苯去除率高达96.3%,小于GB16297—1996《大气污染物综合排放标准》中二甲苯质量浓度90 mg/m~3的排放标准。     

Immobilization of non-point phosphorus using stabilized magnetite nanoparticles with enhanced transportability and reactivity in soils

Laboratory batch and column experiments were conducted to investigate the immobilization of phosphorus (P) in soils using synthetic magnetite nanoparticles stabilized with sodium carboxymethyl cellulose (CMC-NP). Although CMC-stabilized magnetite particles were at the nanoscale, phosphorus removal by the nanoparticles was less than that of microparticles (MP) without the stabilizer due to the reduced P reactivity caused by the coating. The P reactivity of CMC-NP was effectively recovered when cellulase was added to degrade the coating. For subsurface non-point P pollution control for a water pond, it is possible to inject CMC-NP to form an enclosed protection wall in the surrounding soils. Non-stabilized “nanomagnetite” could not pass through the soil column under gravity because it quickly agglomerated into microparticles. The immobilized P was 30% in the control soil column, 33% when treated by non-stabilized MP, 45% when treated by CMC-NP, and 73% when treated by both CMC-NP and cellulase.     

NH3选择性还原NOx催化剂的制备及性能评价

以堇青石蜂窝陶瓷为载体,采用TiO2浆液涂覆载体,再负载活性组分V和W,制备了NH3选择性还原NOx催化剂,研究了TiO2涂层的制备工艺条件,并对催化剂的活性及稳定性进行了评价.实验结果表明,制备TiO2涂层的最佳工艺条件为:TiO2浆液中铝溶胶质量分数12％,浆液pH 1.91,浆液固含量(TiO2与铝溶胶中Al2O...