Increasing the recovery of heavy metal ions using two microbial fuel cells operating in parallel with no power output

The present study aimed to improve the performance of microbial fuel cells (MFCs) by using an intermittent connection period without power output. Connecting two MFCs in parallel improved the voltage output of both MFCs until the voltage stabilized. Electric energy was accumulated in two MFCs containing heavy metal ions copper, zinc, and cadmium as electron acceptors by connection in parallel for several hours. The system was then switched to discharge mode with single MFCs with a 1000-Ω resistor connected between anode and cathode. This method successfully achieved highly efficient removal of heavy metal ions. Even when the anolyte was run in sequencing batch mode, the insufficient voltage and power needed to recover heavy metals from the cathode of MFCs can be complemented by the developed method. The average removal ratio of heavy metal ions in sequencing batch mode was 67 % after 10 h. When the discharge time was 20 h, the removal ratios of zinc, copper, and cadmium were 91.5, 86.7, and 83.57 %, respectively; the average removal ratio of these ions after 20 h was only 52.1 % for the control group. Therefore, the average removal efficiency of heavy metal ions increased by 1.75 times using the electrons stored from the bacteria under the open-circuit conditions in parallel mode. Electrochemical impedance data showed that the anode had lower solution resistance and polarization resistance in the parallel stage than as a single MFC, and capacitance increased with the length of time in parallel.

     

Influence of filtration velocity on DON variation in BAF for micropolluted surface water treatment

Biological aerated filters (BAFs) are widely used for the treatment of micropolluted surface water. However, the biological process produces dissolved organic nitrogen (DON), which, as precursors of nitrogenous disinfection by-products, pose potential threats to drinking water safety. Therefore, to control DON in BAF effluent, it is necessary to study the influence of BAF operation parameters on DON production. In this study, the influence of filtration velocity in a BAF on DON production was investigated. Under different filtration velocity (0.5, 2, and 4 m/h) conditions, profiles of DON concentrations along the media layer were measured. The profile at a filtration velocity of 0.5 m/h showed a decreasing trend, and the ones under filtration velocities of 2 and 4 m/h fluctuated in a small range (from 0.1 to 0.4 mg/L). Moreover, the relatively high filtration velocities of 2 and 4 m/h resulted in a lower level of DON concentration. Additionally, 3D excitation-emission matrix fluorescence spectroscopy was used to characterize DON. It is found that the patterns of DON at a relatively high filtration velocity condition (4 m/h) were obviously different from the ones under low filtration velocity conditions (0.5 and 2 m/h).     

沸石联合微生物固定化去除微污染水体中氨氮的研究

将沸石联合经过驯化的活性污泥微生物固定化,通过静态实验.考察了不同粒径沸石及不同组分固定化方法对沸石联合微生物固定化去除氨氮的影响;通过动态实验,考察了沸石联合微生物固定化去除微污染水体中低浓度氨氮的机制.结果表明,活性污泥经过16 d的驯化,氨氮去除率为90%以上;沸石吸附氨氮为快速吸附,粒径<0.5 mm的沸石的吸附容量明显大于其他粒径的沸石;不同组分固定化小球对氨氮的去除效率不同,各组分均有贡献,吸附容量依次为:沸石固定化小球>沸石联合微生物固定化小球>微生物固定化小球;沸石联合微生物固定化去除微污染水体中低浓度氨氮可分为4个阶段,即沸石吸附阶段、吸附饱和及微生物适应阶段、硝化作用明显加强和沸石部分再生阶段、微生物作用良好和沸石进一步再生阶段,最终沸石吸附与生物再生处于良好的动态平衡中,氨氮去除率达到60%左右.     

膜生物反应器处理微污染水源水的研究与应用现状

膜生物反应器及其组合工艺能实现水源水中微污染物的有效去除,是一种新型高效水处理工艺.总结了膜生物反应器处理微污染水源水的研究与应用现状、污染物去除效果和机制;在分析膜污染机制基础上归纳了膜污染控制和污染膜清洗方式,展望了膜生物反应器在给水领域应用需克服解决的技术难点.     

PM10-PM2.5冲击采样器的研制与开发

在颗粒物研究中,分级采样是一种常用的监测方法,而冲击采样器是颗粒物分级采样的重要仪器.根据斯托克斯数,对PM10-PM2.5冲击采样器设计参数进行了详细分析,并对PM10-PM2.5的捕集效率特征进行了分析.结果表明,PM10-PM2.5冲击采样器具备理想的PM10和PM2.5捕集效率,PM10冲击采样器、PM2.5冲击采样器切割粒径分别为9.94、2.43μm,均在其允许误差范围内.     

Continuous measurement of peroxyacetyl nitrate (PAN) in suburban and remote areas of western China

Knowledge on atmospheric abundance of peroxyacetyl nitrate (PAN) is important in assessing the severity of photochemical pollution, and for understanding chemical transformation of reactive odd nitrogen and its impact on the budget of tropospheric ozone (O₃). In summer 2006, continuous measurements of PAN were made using an automatic GC–ECD analyzer with an on-line calibrator at a suburban site of Lanzhou (LZ) and a remote site of Mt. Waliguan (WLG) in western China, with concurrent measurements of O₃, total reactive nitrogen (NO_y) and carbon monoxide (CO). At LZ, several photochemical episodes were observed during the study, and the average mixing ratio of PAN (plus or minus standard deviation) was 0.76 (±0.89) ppbv with the maximum value of 9.13 ppbv, compared to an average value of 0.44 (±0.16) ppbv at remote WLG. The PAN mixing ratios in LZ exhibited strong diurnal variations with a maximum at noon, while enhanced concentrations of PAN were observed in the evening and a minimum in the afternoon at WLG. The daily O₃ and PAN concentration maxima showed a strong correlation (r² = 0.91) in LZ, with a regression slope (PAN/O₃) of 0.091 ppbv ppbv^?1. At WLG, six well-identified pollution plumes (lasting 2–8 h) were observed with elevated concentrations of PAN (and other trace gases), and analysis of backward particle release simulation shows that the high-PAN events at WLG were mostly associated with the transport of air masses that had passed over LZ.     

Measurement of gas-phase total peroxides at the summit of Mount Tai in China

Measurement of ambient gas-phase total peroxides was performed at the summit of Mount Tai (Mt. Tai, 1534 m above sea level) in central-eastern China during March 22–April 24 and June 16–July 20, 2007. The hourly averaged concentration of peroxides was 0.17 ppbv (± 0.16 ppbv, maximum: 1.28 ppbv) and 0.55 ppbv (± 0.67 ppbv, maximum: 3.55 ppbv) in the spring and summer campaigns, respectively. The average concentration of peroxides at Mt. Tai, which is in a heavily polluted region, was much lower than hydrogen peroxide measurements made at some rural mountain sites, suggesting that significant removal processes took place in this region. An examination of diurnal variation and a correlation analysis suggest that these removal processes could include chemical suppression of peroxide production due to the scavenging of peroxy and hydroxy radicals by high NO_x, wet removal by clouds/fogs rich in dissolved sulfur dioxide which reacts quickly with peroxides, and photolysis. These sinks competed with photochemical sources of peroxides, resulting in different mean concentrations and diurnal pattern of peroxides in the spring and summer. A principal component analysis was conducted to quantify the major processes that influenced the variation of peroxide concentrations. This analysis shows that in the spring photochemical production was an important source of peroxides, and the major sink was scavenging during upslope transport of polluted and humid air from the lower part of the planetary boundary layer (PBL) and wet removal by synoptic scale clouds. During the summer, highly polluted PBL air (with high NO_x) was often associated with very low peroxides due to the chemical suppression of HO₂ by high NO_x and wet-removal by clouds/fogs in this sulfur-rich atmosphere, especially during the daytime. Higher concentrations of peroxides, which often appeared at mid-nighttime, were mainly associated with subsidence of air masses containing relatively lower concentrations of NO_y.     

新型悬浮填料澄清池中填料对澄清作用的影响初探

为考察可取代传统二沉池的新型悬浮填料澄清池技术的原理及关键参数,小试试验研究了填料对新型悬浮填料澄清池固液分离过程中附着污泥形成及其絮凝性能的影响,并对填料在澄清中的作用机理进行了探讨。结果表明,当泥水界面上升至填料区后,可以形成较悬浮污泥更加致密稳定的附着污泥区,并形成孔道流,强化了对混合液中污泥颗粒的絮凝效果;填料区可以捕捉去除从悬浮污泥区中“逃逸”的微小污泥絮体,并降低出水浊度,有效地保证了出水水质的稳定性。填料的存在发挥了强大的整流作用,降低了雷诺数Re,提高了弗汝德数Fr,从而改善了污泥絮凝的水力条件,提高了澄清能力。     

伞罩型湿式脱硫除尘塔入口结构优化模拟

利用商用CFD软件Fluent,采用k-ε湍流模型和SIMPLE算法,对新型伞罩型湿式脱硫除尘塔内的三维两相流场进行数值模拟,发现了塔内烟气入口处流场所存在的不均匀性。为将其流场调节均匀从而提高脱硫除尘效率,在数值模拟的基础上提出在入口处加装直导流板、阶梯导流板和弯曲导流板,并分析塔内y=0截面速度的分布,以及z＝0.21 m截面上的颗粒浓度、速度和压力等参数的分布。结果表明：通过加装阶梯导流板和弯曲导流板均可以将流场调节均匀,达到较理想状态,从而实现高效净化气体的目的。模拟结果对设备的优化设计和实际运行有一定的指导作用。     

利用烧结脱硫灰制备胶凝材料的研究

研究了烧结烟气半干法脱硫灰复掺矿渣、钢渣,辅之外加剂,制备胶凝材料的可行性。结果表明,采用改性脱硫灰（GXTLH）、钢渣、矿渣及水泥熟料再混磨制备的复合胶凝材料,具有良好的安定性等水化性能和力学性能;当GXTLH 掺入量为20%、CFII 1.5%、减水剂0.5%及水泥熟料23%时,矿渣掺量在12%～44%、钢渣掺量11%～44%之间制备的胶凝材料初凝时间、终凝时间、力学性能满足GB13592-92《钢渣矿渣水泥标准》;矿渣与钢渣比、水泥熟料及外加剂等掺量一定,GXTLH掺量超过30%时,GXTLH胶凝材料的抗压抗折强度均有所下降。