SBR法处理炼油废水的研究

研究了SBR（程序间歇式活性污泥）法处理炼油废水的最佳工艺条件和除氮效果，以及投菌SBR法处理炼油废水中污染物的效果。确定了SBR法处理炼油废水最佳反应温度为25℃－40℃，pH值为6.0-8.5，反应时间为8－12h，活性污泥浓度为2000－4000mg/L。当反应期内好氧曝气和缺氧搅拌交替进行3－4次，脱氧率可以达到90％以上。将实验室筛选得到的除油菌投加于BR复合生物反应器中处理炼油厂隔油池出水，废水中各种污染物的去除率分别为：COD93．5％，石油类98．6％，总氮89．8％。     

IABR-IBAF工艺处理猪场稳定塘废水的实验研究

难降解有机物含量高且碳氮比失调是造成养猪场稳定塘废水难于处理的主要原因。本文采用基于固定化微生物技术的厌氧折流板（IABR）与曝气生物滤池（IBAF）组合工艺处理稳定塘废水,对比了IABR-IABF组合工艺与单一IBAF工艺的处理效果,研究了碱度和碳源对硝化反硝化过程的影响。组合工艺平均进水COD1532．6mg／L,平均出水为332．7mg／L,去除率为78％,NH3-N平均进水538．6mg／L,平均出水为12．3mg／L,去除率97．7％。以新鲜废水做反硝化阶段的碳源时TN去除率93％,可有效解决脱氮过程中的碳源成本问题。     

一种高效复合絮凝剂对多种废水的处理效果

用聚合氯化铝（PAC）和聚丙烯酰胺（PAM）复配成复合絮凝剂（PAC＋PAM）应用于污染河水、生活污水、工业废水和餐饮废水等6种废水的处理，结果表明。PAC、PAM、PAC＋PAM对污染河水的CODc。SS、浊度有显著降低作用，PAC＋PAM的净水效果明显优于PAC和PAM；PAC＋PAM对6种废水中COD的去除率为81．5％～90．4％，平均84．6％。对SS的去除率为81．9％～96．5％，平均88．9％，对浊度的去除率为91．3％-98．0％，平均95．1％；处理后悬浮物基本被絮凝沉降，水体变得较清澈透明，异味或臭味消除。说明本PAC＋PAM复合絮凝剂对各种废水均有良好的净水效果，具有重要的应用价值。     

梭织布印染废水处理改造工程设计

采用初沉-厌氧-接触氧化-二沉的组合工艺处理梭织布印染废水的运行结果表明，在进水平均cOD5000mg／L、SS500mg／L、色度600倍的条件下，上述各项指标去除率分别为96．7％、95.5％、95％，整个系统对难降解的染料、印染助剂均有很好的去除效果，出水满足广东省地方排放标准。     

汽车制造厂废水处理工程实例分析

采用二级混凝-气浮-水解酸化-SBR-过滤工艺，对某汽车制造厂的混合废水（包括脱脂废水、电泳废水、磷化废水和生活污水等）进行处理。经过对处理工艺进出水主要水质指标连续1个月的监测，发现COD去除率可达92．5％，SS去除率可达95．2％，NH3-N去除率可达58％，TP去除率可达96．7％，出水水质符合国家《污水综合排放标准》（GB8978—1996）一级排放标准，吨水处理成本为1．6元／t，系统运行稳定，具有明显的经济、环保和社会效益。t     

生态浮床及辅助技术治理汇丰河黑臭水体

采用生态浮床为核心,辅以微曝气复氧、纳污减污栅和人工介质等多项技术,对上海市汇丰河黑臭水体进行治理,工程取得了预期效果,水体透明度由原来的平均小于20cm增加到平均50cm以上,主要水质指标NH3-N、TP、CODMn的最大净化率平均分别达到了69．9％、80．7％和63．5％,河道生物多样性显著提高。     

中药废水处理工程设计研究

某工程采用微电解、上流式厌氧污泥床（UASB）、高效接触反应器（HCR）处理中药废水，处理规模2500m^3／d。运行结果表明：采用该工艺COD去除率达97．9％，BOD去除率达97。4％，色度去除率达98．2％，出水完全达到《污水综合排放标准》（GB8978-96）中的一级排放标准，且工程投资和运行费用较低。     

磁种-磁滤技术处理污染河水的试验研究

采用磁种-磁滤技术处理广州市两条河涌的污染水,考察了磁种投加量、混凝剂用量、磁场强度和磁滤速度对出水浊度的影响,并确定了最佳试验条件。结果表明,该工艺对TP、SS和浊度的去除效果较好,去除率分别为96．2％、92．4％和93．9％,对CODCr有一定的去除效果,去除率为68．2％,但对NH4^ -N的去除效果较差,去除率仅为25％。     

沈抚灌渠污水预处理实验研究

以砾石为填料采用生物滤池法和以纤维束为填料采用生物接触氧化法,分别预处理沈抚灌渠污水。试验结果表明,在水力停留时间在3．5h,控制气水比分别为5：1和4：1的反应条件下,砾石填料对COD和NH3-N的平均去除率分别为53．9％和53．6％;纤维束软填料对COD和NH3-N的平均去除率分别为55．7％和47．7％。前者对COD和NH3-N的处理效果都达到了预定要求,而后者对NH3-N的处理效果没有达到要求。     

颗粒活性炭载体新型生物转盘去除生活污水中COD和NH3-N的研究

开发一种改进型生物转盘处理生活污水,将盘片改为转笼状,并向其中加入颗粒活性发作为载体,研究该系统对生活污水的处理效果。结果表明：在转盘转速为15rpm和HRT分别为10h、8h、6h、4．5h情况下,进水COD平均浓度约为223mg／L,出水COD平均浓度分别为15．6、17．9、23．4、28．2mg/L,平均去除率为93．0％、91．9％、89．5％、86．6％;进水NH3-N平均浓度约为22mg／L,出水NH3-N平均浓度分别为0．32、1．13、2．30、5．71mg／L,平均去除率为98．5％、94．8％、89．7％、74．6％。     

催化铁内电解＋CAST工艺耦合处理城市污水脱氮除磷效果研究

开展了催化铁内电解＋CAST工艺耦合系统处理城市污水脱氮除磷的中试试验研究。研究表明：催化铁内电解具有改善活性污泥性状的作用,能够强化生物脱氮,提高脱氮效果;同时通过生物除磷与化学除磷协同作用提高除磷效果。试验期间各项指标去除效果良好,NH3-N平均去除率为96.40%,TN去除率为36.55%,TP去除率为90.00%,各项指标基本上稳定达到一级A标准。     

生物强化技术在污水处理中的应用

生物强化技术是一种利用生物治理废水的高效技术,在废水治理中具有广阔的应用前景。其作用机理是通过在污水中加入优势高效菌种来增加和改善处理系统的能力。文章介绍了生物强化技术的作用机理以及在废水治理中的应用效果,利用实验评价了生物强化作用的效果,并总结了应用中存在的问题。     

MANAGEMENT OF BASEFLOW AUGMENTATION: A REVIEW1

ABSTRACT: Baseflow augmentation refers to the temporary storage of subsurface water in floodplains, streambanks, and/or stream bottoms during the wet season, either by natural or artificial means, for later release during the dry season to increase the magnitude and permanence of low flows. Management strategies for baseflow augmentation fall into the following categories: (1) range management, (2) upland vegetation management, (3) riparian vegetation management, (4) upland runoff detention and retention, and (5) the use of instream structures. The benefits of a management strategy focused on baseflow augmentation are many, including: (1) increased summer flows, (2) healthier riparian areas, (3) increased channel and bank stability, (4) decreased erosion and sediment transport, (5) improved water quality, (6) enhanced fish and wildlife habitat, (7) lower stream temperatures, and (8) improved stream aesthetics. This review has shown that baseflow augmentation has been successfully accomplished in a few documented cases. Given its clear impact on soil and water conservation, particularly in the semiarid western U.S., it appears that baseflow augmentation is a concept whose time has come. Research is needed on how to successfully integrate baseflow augmentation within comprehensive resource management strategies.     

Merits of ozonation and catalytic ozonation pre-treatment in the algal treatment of pulp and paper mill effluents

Since the performance of algal treatment for pulp mill effluent decreases with increasing color intensity and AOX content, which mainly originate from the chlorine bleaching of Kraft pulp, the separated CEH bleaching effluent was pre-treated by both the conventional and the heterogeneous catalytic ozonation processes. An increase in the BOD(5)/COD ratio from 0.11 to 0.28 and 87% color abatement in terms of Pt-Co were achieved by catalytic ozonation, which had the best treatment performance. Biodegradability enhancement of the CEH effluent correlated well with a decrease in toxicity, high-molecular-weight-compound content, and AOX abatement. By the pre-treatment of the CEH bleaching effluent, the overall efficiencies of algal treatment of the combined pulp mill effluent in terms of the fractional removal of COD and color were increased from 76% and 53% to 86-90% and 96-99%, respectively. Effects of both the conventional and the catalytic ozonation pre-treatments on subsequent biological treatment were close to each other and they reduced the filling period of the Sequential Batch Reactor (SBR) cycle from 8 to 5 days.     

盐度、C：N对SBR工艺处理海水产品养殖场废水的影响

海水产品养殖场废水中碳、氮的浓度很高,通过序批式反应器（SBR）处理,能有效的降低碳、氮的浓度。在常温（20℃-25℃）条件下,我们检测了不同盐度、C：N下的处理效果,以期实现SBR工艺运行参数的最优化。实验结果表明：盐度为2．5％～3．5％,C：N为10：1的条件下,除碳和生物脱氮的效果最佳。实验验证了SBR工艺在海水产品养殖场废水处理中可以作为一个非常有效的处理手段而应用。     

含油废水处理工艺优化研究

在已开发的含油废水处理装置的基础上,对其整体结构、旋分分离部分进行改进,并筛选出性能优良的填料。将原处理装置的单向旋分器改进为双向旋分器、采用YS填料之后,对石油类浓度低于400mg/L的含油废水,经该装置处理后,石油类的去除率达到90%以上;石油类浓度低于80mg/L的含油废水,经该装置处理后,石油类的去除率达95%,石油类的浓度小于10mg/L,达到国家《污水综合排放标准》(GB8798-1996)二级标准的要求。改进后的装置对高、中、低不同浓度石油类的含油废水均有较好的处理效果。     

WATER QUALITY ALLOCATED COST FOR MULTIPURPOSE RESERVOIRS1

ABSTRACT: Low flow augmentation from multipurpose reservoirs may yield significant water quality benefits. Cost allocation assigns a portion of reservoir expense to water quality consumers, waste water dischargers who benefit from increased receiving flow. Whereas such allocation currently is not authorized for Federal projects, the procedure is increasingly appropriate for efficient multiobjective management. Waste water treatment costs, multipurpose reservoir costs, and water quality are modeled for Oregon's Willamette River. Water quality is expressed as a function of treatment and augmentation levels. Treatment cost necessary to achieve a given water quality without augmentation less treatment cost with augmentation is an alternative cost of water quality maintenance. With a cost allocation procedure, this alternative cost is used to determine water quality's share of reservoir cost. Under current conditions, water quality beneficiaries could be charged approximately seven percent of annualized reservoir expense. This charge is one-fourth the expense of additional treatment facilities required were augmentation not provided.     

Biological Assessment of Aquaculture Effects on Effluent-Receiving Streams in Ghana Using Structural and Functional Composition of Fish and Macroinvertebrate Assemblages

Biological assessment of aquatic ecosystems is widely employed as an alternative or complement to chemical and toxicity testing due to numerous advantages of using biota to determine ecosystem condition. These advantages, especially to developing countries, include the relatively low cost and technical requirements. This study was conducted to determine the biological impacts of aquaculture operations on effluent-receiving streams in the Ashanti Region of Ghana. We collected water, fish and benthic macroinvertebrate samples from 12 aquaculture effluent-receiving streams upstream and downstream of fish farms and 12 reference streams between May and August of 2009, and then calculated structural and functional metrics for biotic assemblages. Fish species with non-guarding mode of reproduction were more abundant in reference streams than downstream (P?=?0.0214) and upstream (P?=?0.0251), and sand-detritus spawning fish were less predominant in reference stream than upstream (P?=?0.0222) and marginally less in downstream locations (P?=?0.0539). A possible subsidy-stress response of macroinvertebrate family richness and abundance was also observed, with nutrient (nitrogen) augmentation from aquaculture and other farming activities likely. Generally, there were no, or only marginal differences among locations downstream and upstream of fish farms and in reference streams in terms of several other biotic metrics considered. Therefore, the scale of impact in the future will depend not only on the management of nutrient augmentation from pond effluents, but also on the consideration of nutrient discharges from other industries like fruit and vegetable farming within the study area.     

Variation in and constraints upon the decomposition of woolscour sludge

The woolscouring (wool washing) industry has traditionally been viewed as highly polluting and, consequently, effluent treatment systems have been sought. The first stage in the current treatment system for woolscour wastewater, a chemical flocculation process (Sirolan CF), creates a sludge composed of soil and wool grease. We investigated the chemical and biological characteristics of this sludge. The sludge was found to be highly variable on a day to day basis in terms of its chemical composition and biodegradability; 0.8 to 27.8% of sludge total nitrogen was mineralized over 30 d at 37 degrees C. The grease component of sludge (14-40% on a dry weight basis) may retard the decomposition of the sludge but the polyacrylamide flocculant used in its production and its pesticide content had no effect on the rate of decomposition. Our results suggest that variability in substrate quality may translate into variability in treatment performance and have important implications for the biological treatment of industrial wastes, including composting.     

Multiyear nutrient removal performance of three constructed wetlands intercepting tile drain flows from grazed pastures

Subsurface tile drain flows can be a major s ource of nurient loss from agricultural landscapes. This study quantifies flows and nitrogen and phosphorus yields from tile drains at three intensively grazed dairy pasture sites over 3- to 5-yr periods and evaluates the capacity of constructed wetlands occupying 0.66 to 1.6% of the drained catchments too reduce nutrient loads. Continuous flow records are combined with automated flow-proportional sampling of nutrient concentrations to calculate tile drain nutrient yields and wetland mass removal rates. Annual drainage water yields rangedfrom 193 to 564 mm (16-51% of rainfall) at two rain-fed sites and from 827 to 853 mm (43-51% of rainfall + irrigation) at an irrigated site. Annually, the tile drains exported 14 to 109 kg ha(-1) of total N (TN), of which 58 to 90% was nitrate-N. Constructed wetlands intercepting these flows removed 30 to 369 gTN m(-2) (7-63%) of influent loadings annually. Seasonal percentage nitrate-N and TN removal were negatively associated with wetland N mass loadings. Wetland P removal was poor in all wetlands, with 12 to 115% more total P exported annually overall than received. Annually, the tile drains exported 0.12 to 1.38 kg ha of total P, of which 15 to 93% was dissolved reactive P. Additional measures are required to reduce these losses or provide supplementary P removal. Wetland N removal performance could be improved by modifying drainage systems to release flows more gradually and improving irrigation practices to reduce drainage losses.