连续流态下好氧颗粒污泥的培养及处理制药废水的性能

在上流式好氧颗粒污泥床反应器中, 以厌氧颗粒污泥和好氧絮状活性污泥为接种泥, 采用人工配制的模拟废水, 成功培养出性能优异的好氧颗粒污泥.反应器内污泥浓度稳定在5g/L左右, 颗粒污泥粒径为0.5~2.0mm, 当进水COD为2000mg/L, 容积负荷为4.8kg/(m3·d)时, 系统对COD的去除率稳定在96%以上.通过扫描电镜观察, 好氧颗粒污泥是层状结构, 表面有大量丝状菌缠绕, 内部有短杆菌和空穴存在.逐步提高制药废水在进水中的比例, 经过47d的培养, 生物制药废水完全取代模拟废水, 系统对COD、NH₃-N、TP的去除率分别稳定在90%、90%和70%以上.      

胜利油田采油污水综合特征及利用评价

胜利油田作为我国石油的重要赋存区,其地热资源也相当丰富。在节能减排的背景下,采油产生的污水由于其相对较高的温度,除了用于回注开采层提高石油采收率,还能用于供暖、洗浴等。通过采集胜利油田济阳坳陷探区19个典型采油联合站分离出的采油污水,分析其水化学组分和微量元素,总结了采油污水的基本水化学特征以及腐蚀性和结垢性趋势。研究结果表明,本次采集的采油污水属于咸水-卤水,矿化度最高可达59.7gL-1,其中锂和锶的含量达到了作为矿水的要求。综合腐蚀性系数和拉申指数评价方法得出采油污水属于强腐蚀性水。结垢性评价结果表明,这些采油污水不会形成碳酸钙垢,也不具备二氧化硅的结垢条件,仅滨南和河口采油厂采油污水有硫酸钙结垢的可能性,综合利用前需要及时预防和处理。采油污水可以用于开采层回注、供暖、洗浴、温室大棚和水产养殖等,一方面可以减少环境污染,另一方面还能改善能源结构,具有良好的社会和经济效益。在综合利用采油污水时,需要考虑其腐蚀性和结垢性,选择合适的预处理方式及管道。     

Intra-annual variability of urban effects on streamflow

While considerable research has established the impacts of urbanization on streamflow, there has been little emphasis on how intra-annual variations in streamflow can deepen the understanding of hydrological processes in urban watersheds. This study fills this critical research gap by examining, at the monthly scale, correlations between land-cover and streamflow, differences in streamflow metrics between urban and rural watersheds, and the potential for the inflow and infiltration (I&I) of extraneous water into sewers to reduce streamflow. We use data from 90 watersheds in the Atlanta, GA region over the 2013–2019 period to accomplish our objectives. Similar to other urban areas in temperate climates, Atlanta has a soil-water surplus in winter and a soil-water deficit in summer. Our results show urban watersheds have less streamflow seasonality than do rural watersheds. Compared to rural watersheds, urban watersheds have a much larger frequency of high-flow days during July–October. This is caused by increased impervious cover decreasing the importance of antecedent soil moisture in producing runoff. Urban watersheds have lower baseflows than rural watersheds during December–April but have baseflows equal to or larger than baseflows in rural watersheds during July–October. Intra-annual variations in effluent data from wastewater treatment plants provide evidence that I&I is a major cause of the relatively low baseflows during December–April. The relatively high baseflows in urban watersheds during July–October are likely caused by reduced evapotranspiration and the inflow of municipal water. The above seasonal aspects of urban effects on streamflow should be applicable to most urban watersheds with temperate climates.     

中山市河涌水体及污水处理厂中 合成麝香的分布规律

对中山市5个区域的48条主要河涌水体与2间污水处理厂各工艺流程水体进行样品采集,运用固相微萃取进行前处理并结合气相色谱—质谱联用技术,检测各样品中佳乐麝香、吐纳麝香和酮麝香这3种合成麝香的含量,并分析其分布特征以及探讨污水处理厂处理工艺中合成麝香的浓度变化规律。结果表明：1）合成麝香已经普遍存在于中山市的河涌水体中。中山市西部地区和南部地区的河涌水体中合成麝香总含量相对其他区域最低,中部地区河涌水体中合成麝香含量亦较低。2）中山市雁企涌和魁魁涌等28条河涌水体中的主要合成麝香为佳乐麝香,一埒涌和乌沙涌等13条河涌水体的主要合成麝香为酮麝香,仅有苏埒涌和石军涌等7条河涌水体的主要合成麝香为佳乐麝香和酮麝香这2种合成麝香。3）氧化沟和A2/O工艺均能对合成麝香产生一定的去除效果。污水处理厂A对佳乐麝香、吐纳麝香和酮麝香的去除率分别为86.94%、72.15%和89.36%;而污水处理厂B对以上3种合成麝香的去除率分别为82.09%、85.73%和87.90%。4）2间污水处理厂的二沉池以及污水处理厂A的紫外消毒亦可对合成麝香产生进一步的去除效果;2间污水处理厂均能对酮麝香产生比佳乐麝香和吐纳麝香更高的去除率。     

天然磁铁矿处理含Hg（Ⅱ）废水实验研究

利用重金属离子可在水合金属氧化物和氢氧化物矿物表面产生吸陵作用的原理，进行了天然磁铁矿处理含Hg(Ⅱ）废水的实验研究，结果表明：当温度为25℃，吸附平衡时间为60分钟、试样用量为20g/L，试样粒径为200目以下、pH值为6.40，离子强度为零时，Hg(Ⅱ）初始浓度为1.12mg/L的溶液的吸附率可达98%，使废水中Hg(Ⅱ）的浓度达到国家排放标准。pH值、离子强度、粒径、试样用量、废水浓度、温度、时间均对Hg(Ⅱ）的吸附率有一定的影响，其中pH值的影响最大，Hg(Ⅱ）在天然磁铁矿上的吸附等温曲线不同于Langmuir和Freundlich等温曲线，而是表现为台阶段，符合分级离子/配位子交换等温曲线。     

胶印含铬废水化学处理工艺条件应用研究

实验研究了胶印含铬废水化学处理的方法及工艺条件。经化学法处理 ,Cr( )和总 Cr的浓度均能达到国家工业污水排放标准 ;研究结果表明 ,废水中 Cr( )还原成 Cr( )的反应 ,还原剂 Na HSO3 投加量应是 Cr( )重量的 7倍以上 ;Cr(OH) 3 的沉淀反应的适宜 p H范围在 7.5～ 8.5 ,以 p H 8.0时为最佳 ;Cr(OH) 3 的沉淀反应的搅拌时间应在 2 0 min以上为宜 ;沉淀反应的烘干沉渣量为废水总 Cr量的 11倍。该实验研究结果可为含铬废水化学处理法的工艺设计提供理论依据     

水生植物凤眼莲(Eichhornia crassipes Somls)对含银废水的净化与资源化生态工程的实施方案及其发展前景

本文通过凤眼莲等水生植物对含银废水的净化与资源化的生产性应用试验,提出了工程实施的基本工艺,阐述了该工艺方案的特点和运行控制要求,分析了这一废水净化与资源化生态工程的环境效益和经济效益。这对我国感光材料工业和其它有关行业净化低浓度含银废水,并从中回收白银具有重要的意义。     

A Numerical Model for Mixing Areas of Pollutant Discharging into Tidal Flows

- A combined numerical model for computing mixing areas of pollution vertical jet discharging into tidal flows has been developed. This numerical model is composed of a 2-D depth-averaged dynamic far-field numerical model and a 2-D vertical dynamic near-field numerical model. The former uses finite node method to compute velocity, and improved finite node method to compute pollutant concentration distribution; the latter is a k-e turbulence model, and uses SIMPLE (Semi-Implicit Method for Pressure Linked Equations) method to compute velocity. At the same time, the former provides boundary conditions for the latter. This model can simulate both far- field pollutant concentration distribution and near-field vertical recirculation quickly and precisely. This model has been verified by measured data of pollutant F of the Dachang reach of the Changjing River and test data presented by Chen el al. (1992). On the basis of verification, the authors use a designed hydrograph to compute this mixing area for a cer     

Urban stream temperature patterns: Spatial and temporal heterogeneity in the Philadelphia region,Pennsylvania, USA

Stream temperature is a critical water quality parameter that is not fully understood, particularly in urban areas. This study explores drivers contributing to stream temperature variability within an urban system, at 21 sites within the Philadelphia region, Pennsylvania, USA. A comprehensive set of temperature metrics were evaluated, including temperature sensitivity, daily maximum temperatures, time >20°C, and temperature surges during storms. Wastewater treatment plants (WWTPs) were the strongest driver of downstream temperature variability along 32 km in Wissahickon Creek. WWTP effluent temperature controlled local (1–3 km downstream) temperatures year-round, but the impacts varied seasonally: during winter, local warming of 2–7°C was consistently observed, while local cooling up to 1°C occurred during summer. Summer cooling and winter warming were detected up to 12 km downstream of a WWTP. Comparing effects from different WWTPs provided guidelines for mitigating their thermal impact; WWTPs that discharged into larger streams, had cooler effluent, or had lower discharge had less effect on stream temperatures. Comparing thermal regimes in four urban headwater streams, sites with more local riparian canopy had cooler maximum temperatures by up to 1.5°C, had lower temperature sensitivity, and spent less time at high temperatures, although mean temperatures were unaffected. Watershed-scale impervious area was associated with increased surge frequency and magnitude at headwater sites, but most storms did not result in a surge and most surges had a low magnitude. These results suggest that maintaining or restoring riparian canopy in urban settings will have a larger impact on stream temperatures than stormwater management that treats impervious area. Mitigation efforts may be most impactful at urban headwater sites, which are particularly vulnerable to stream temperature disruptions. It is vital that stream temperature impacts are considered when planning stormwater management or stream restoration projects, and the appropriate metrics need to be considered when assessing impacts.     

Electrocoagulation/Electroflotation Process for Removal of Organics and Microplastics in Laundry Wastewater

In the present research, laundry wastewater treatment is studied using the electrocoagulation/electroflotation process. For the optimization of treatment conditions such as electrode type (Al–Al, Al–Fe, Fe–Fe, and Fe–Al), initial pH (5–9), current (0.54–2.16 A), and application time (15–60 min), response surface methodology is used. Removal efficiencies of chemical oxygen demand (COD), color, anionic surfactant, microplastic, and phosphate are studied. It is determined that the most effective removal is obtained with 2.16 A current, pH 9, and 60 min reaction time using Fe–Al electrode. Here, 91%, 94%, 100%, and 98% removal efficiencies are achieved for COD, surfactant, color, and microplastic, respectively. The operating cost of the combined process is calculated as $1.32 m^?3 for the optimum removal parameters. The adsorption kinetics study shows that the removal follows second‐order kinetics. The laboratory‐scale test results indicate that the electrocoagulation/electroflotation process is feasible for the treatment of laundry wastewater.