城市污水二级硝化出水的离子交换脱氮除磷

以城市污水二级硝化出水为原水,对比研究了3种强碱性阴离子交换树脂(201×4、D296、D301T)动态脱氮除磷情况,并以201×4树脂为模式树脂考察了树脂活化方式(常规酸碱交替活化与NaCl再生液活化)、腐殖酸(HA)浓度(1.1,2.8和9.4 mg·l~(-1))对树脂动态脱氮除磷的影响.结果表明,3种树脂都具有较好的脱氮除磷效果,达到TP穿透点(0.1 mg·l~(-1),去除率92%)时,201×4树脂具有最大的穿透体积(418 BV),但其对NO_3~--N的去除率(69%)明显低于其它树脂(97%-98%);3种树脂对SO_4~(2-)和HA的去除率分别为97%-99%,71%-80%;常规酸碱活化使树脂穿透体积较再生液活化仅提高了12%;超滤膜法和臭氧氧化法预处理对原水HA的去除率分别为27%和68%;原水HA浓度增加使树脂穿透体积从28lBV降至239BV,同时NO_3~-去除率从80%上升至92%.     

Air pollution transport in the Balkan region and country-to-country pollution exchange between Romania, Bulgaria and Greece

US EPA Models-3 system is used for calculating the exchange of ozone pollution between three countries in southeast Europe. For the purpose, three domains with resolution 90, 30 and 10 km are chosen in such a way that the most inner domain with dimensions 90 × 147 points covers entirely Romania, Bulgaria and Greece.The ozone pollution levels are studied on the base of three indexes given in the EU Ozone Directive, mainly accumulated over threshold of 40 ppb for crops (AOT40C, period May–July), number of days with 8-h running average over 60 ppb (NOD60) and averaged daily maximum (ADM). These parameters are calculated for every scenario and the influence of each country emissions on the pollution of the region is estimated and commented.Oxidized and reduced sulphur and nitrogen loads over the territories of the three countries are also determined. The application of all scenarios gave the possibility to estimate the contribution of every country to the S and N pollution of the others and detailed blame matrixes to be build.Comparison of the ozone levels model estimates with data from the EMEP monitoring stations is made.     

应用高效离子交换色谱分析青枯菌的致病力分

应用高效离子交换色谱和激光光散射仪检测器对不同致病力的青枯菌进行分析,建立了一种快速检测青枯菌致病力分化的新方法青枯菌纯培养物经过高效离子交换色谱分离得到3个致病力不同的特征峰,大小依次为峰3组分>峰2组分>峰1组分.对10株青枯菌进行色谱分析,并结合番茄组培苗感染试验检测其致病力,结果发现,强致病力菌株经过色谱分离只在峰3的保留时间位置出现单一特征峰,在9 d内即可引起100%的番茄组培苗发病;若菌株经过色谱分离形成3个特征峰,则峰3所占的面积比越大,该菌株的致病性相对就越强.25株不同致病力青枯菌的验证试验表明了该方法的可行性,番茄组培苗发病率x与峰3面积比y之间呈现出良好的线性关系,回归方程y=0.9581x+5.4984,相关系数r=0.986.通过对青枯菌色谱行为、致病力、细胞表而黏附的EPS Ⅰ含量三者之间相互关系的进一步研究,发现青枯菌的致病力越强,则细胞表面黏附的EPSⅠ越多,峰3所占的面积比就越大.图3表6参15     

Optimization of phosphorus removal in uniFed SBR system for domestic wastewater treatment

The characteristic of phosphorus removal and appropriate change of the traditional operation modes were investigated in UniFed sequencing batch reactor (SBR) laboratory-scale apparatus (40 L), treating actual domestic wastewater with low ratios of C/N (2.57) and C/P (30.18), providing theoretical basis for actual application of wastewater treatment plant. UniFed SBR system with its unique operation mode had the distinct superiority of phosphorus removal. On this occasion, the effect of volumetric exchange ratio (VER) and the method of influent introduction for phosphorus removal were studied. When the carbon source became the limiting factor to phosphorus release, the higher the VER, the lower the phosphorus concentration in the effluent. Three different influent patterns, including one-time filling, four-time filling, and continuous filling with the same quantity of wastewater could increase the release rate of anaerobic phosphorus from 0.082 to 0.143 mg·P·(L·min)^-1. Appropriate change of the traditional operation modes could optimize the efficiency of phosphorus removal. When the feed/ decant time was extended from 2 h to 4 h, the phosphorous removal efficiency increased from 59.93% to 88.45% without any external carbon source. In the mode of alternation of anoxic-aerobic (A/O) condition, phosphorous removal efficiency increased from 55.07% to 72.27% clearly. The carbon source in the influent can be used adequately, and denitrifying phosphorus removal was carried out in anoxic stage 2 (A2). This mode was optimal for the treatment of actual domestic wastewater with low C/N and C/P ratios.     

富氧-缺氧过程对氧气分布及交换过程影响

为考察底层水体不同的氧动态对水土界面氧气交换过程影响,采用Unisence的微电极测试系统考察底层水体不同的复氧-缺氧环境(物理微曝空气供氧、添加过氧化剂的化学供氧及物理微曝氮气)中,沉积物-水界面氧气的分布及其传输机制,并评估不同富氧与厌氧过程对表层沉积物有机碳的矿化过程的影响.结果表明水体处极度厌氧状况,控制溶解氧分布和交换的水底扩散边界层(DBL)厚度明显变薄(一般在0.2~0.4mm)且溶解氧衰变相对较缓.但底层水体溶解氧丰富甚至处于过饱和状态, DBL层的厚度(一般在0.4~0.7mm)相对较厚且氧气变化迅速 (P<0.05).增加水体氧气供给的条件下,水体与沉积物间溶解氧交换过程加快,溶解氧交换通量由(4.87±0.92)增加至(5.31±0.66 )及(17.14±3.15 ) mmol O2/(m2·d)交换速率,最高提升252%,温度升高氧气交换速率可增加15%,温度效应明显.     

大鹏湾环境容量研究Ⅰ:自净能力模拟分析

在估算大鹏湾污染源强及统计海水污染物浓度的基础上,采用三维水动力模型及污染物扩散模型,模拟了大鹏湾的海水交换及污染物扩散过程,分析了大鹏湾海水交换与生化降解对自净能力的贡献.结果表明,大鹏湾潮差小,约为1m,潮流弱,污染物难于向湾外扩散,其物理自净能力差,湾内海水自净主要取决于生化降解.在吐露港海区与沙头角海区,污染排放较大,水深较小,海水难于交换,容易受到污染.     

纳米银负载型阳离子交换树脂的制备及其对水中碘离子的吸附去除

以大孔型磺酸基聚苯乙烯阳离子树脂为载体,采用硝酸银溶液浸渍、硼氢化钠溶液还原制备了纳米银负载型阳离子交换树脂,并对其吸附去除水中碘离子的性能进行了研究。结果表明：最佳硝酸银浸渍浓度为10 mmol/L,对应载银量19.3 mg/g;25 ℃中性水溶液中,该材料对碘离子的饱和吸附量为74.7 mg/g;吸附量受溶液离子强度的影响较小,但当溶液pH从11降至3时吸附量降低了23%。根据吸附前后材料的XPS谱图变化推测碘离子的去除机理可能为：树脂载体上负载的纳米银活性组分首先与水中溶解氧发生氧化反应产生银离子,随后与溶液中的碘离子结合形成AgI沉淀,从而将碘离子从溶液中去除。     

高效反渗透工艺处理电厂废水

采用“机械加速澄清—重力式过滤—离子交换—除碳—高效反渗透” 工艺处理某电厂废水,将反渗透产水作为冷却塔补水。运行结果表明：弱酸阳离子交换器出水碱度≤0.10 mmol/L、硬度≤0.02 mmol/L、浊度≤0.2 NTU,满足高效反渗透对进水水质的要求;高效反渗透产水浊度<0.1 NTU,COD_Mn≤0.08 mg/L,硬度≤1.12 mg/L,碱度≤8.40 mg/L,ρ（总铁）<10 μg/L,ρ（总硅）<0.5 mg/L,电导率<45 μS/cm,出水水质满足回用要求。针对该系统存在的自用水率高、过滤器污堵以及水量不平衡等问题提出了相应的建议。     

Model of stomatal ammonia compensation point (STAMP) in relation to the plant nitrogen and carbon metabolisms and environmental conditions

Agricultural crops can be either a source or a sink of ammonia (NH₃). Most NH₃ exchange models developed so far do not account for the plants nitrogen (N) metabolism and use prescribed compensation points. We present here a leaf-scale simplified NH₃ stomatal compensation point model related to the plants N and carbon (C) metabolisms, for C₃ plants. Five compartments are considered: xylem, cytoplasm, apoplasm, vacuole and sub-stomatal cavity. The main processes accounted for are the transport of ammonium (NH₄⁺), NH₃ and nitrate (NO₃⁻) between the different compartments, NH₄⁺ production through photorespiration and NO₃⁻ reduction, NH₄⁺ assimilation, chemical and thermodynamic equilibriums in all the compartments, and stomatal transfer of NH₃.The simulated compensation point is sensitive to paramaters related to the apoplastic compartment: pH, volume and active transport rate. Determining factors are leaf temperature, stomatal conductance and NH₄⁺ flux to the leaf. Atmospheric NH₃ concentration seem to have very little effect on the compensation point in conditions of high N fertilization. Comparison of model outputs to experimental results show that the model underestimates the NH₃ compensation point for high N fertilization and that a better parametrisation of sensitive parameters especially active trasport rate of NH₄⁺ may be required.     

微生物在污染环境中的分子生态效应[综述]

生物与环境之间构成了一个开放的自我控制的生态系统,即是一个耗散结构系统．通过物质、能量以及信息的流动构成了系统在功能上的统一性和时间的多样性．生态系统最大的特点是自我调节,自维持其稳态．生物发展进化的过程中,外界环境因子成为生物进化的主要因素和特定的目的物,生物必要朝着这目的物,通过负反馈,不断进行自我调节,以缩小与环境压力之间的差距,当这个差距为零时生物就适应了新的环境．生物就是通过一次又一次的负反馈从环境中获得适应性．众所周知,微生物对于异常环境的适应和抗性能力是任何其它生物所莫及的．探索自…