Cu／Fe内电解预处理焦化废水的研究

采用混凝沉淀一厌氧水解酸化一催化铁内电解（即Cu／Fe体系）一好氧组合工艺处理焦化废水，研究了催化铁内电解法用于焦化废水的预处理时，对焦化废水的COD、色度、总磷的去除率。结果表明，催化铁用于焦化废水的预处理，可以提高废水的可生化性，使好氧处理的COD去除率提高，达到80％-90％；催化铁对焦化废水有较好的脱色效果，色度去除率为77．7％-89．3％；催化铁能够去除部分总磷，但是由于微生物生长需要，需在厌氧段补充磷。试验证明，催化铁内电解法是一种有效的焦化废水预处理工艺。     

含有机氟工业废水处理工艺的研究

采用预处理-水解酸化-生物接触氧化相结合的处理工艺处理含氟代有机化合物废水。研究结果表明，水解酸化可将含氟废水的B／C比由0．258提高到0．396％；在一定浓度范围内通过物化预处理及生化处理可以脱除氟代有机化合物中的氟原子，使该有机物成为可供微生物利用的基质。含氟废水经该工艺处理后，出水中BOD5为7．5mg/L,CODcr为75mg/L，氨氮未检出，总磷小于1mg/L，氟离子浓度为8．6mg/L。     

无动力厌氧＋人工湿地组合模式处理农村生活污水效果分析

通过对已建污水处理工程无动力厌氧＋人工湿地组合模式的处理效果进行监测，结果表明：正常运行情况下，该处理模式化学需氧量的去除率在28％～90％之间，平均为66％；氨氮的去除率在7％-66％之间，平均34％；总磷的去除率在5％～84％之间，平均42％；90％以上出水水质达到三级排放标准；厌氧池对污染物去除的贡献率基本与后段的人工湿地持平；入水污染物负荷量与去除率呈显著正相关关系。     

凉山州邛海宾馆污水深度处理工艺与效果

利用原有的化粪池作厌氧池,并以射流曝气生物接触氧化处理工艺为主体,串联消毒杀菌装置,即采用厌氧—好氧—化学杀菌三级串联深度处理邛海宾馆污水取得良好效果。处理后的水质清澈透明,无异采,COD31mg/l,BOD_52.1mg/l,去除率均在95％以上。     

加碱混凝沉淀工艺在处理含磷废水中的应用

介绍了加碱混凝沉淀法处理含磷废水的工艺。采用工艺处理效果好，出水稳定，经监测废水中总磷的去除效率可达96％，实际运行证明，该工艺是切实可行的。     

生物接触氧化工艺处理制药废水

采用混凝沉淀-生物接触氧化-过滤工艺处理制药废水，可将CODCr去除约96％、BOD5去除约97％，并脱色澄清，出水水质符合相关排放标准。     

二次催化-固定床生物氧化降解焦化废水的试验研究

制备了一种铁碳基／过渡金属复合催化剂，其物质摩尔配比为Fe：C：TiO2：MnO2：ZnO=2：1：1：1：0．3，使用该催化剂拟定了二次催化—固定床生物氧化降解流程。在pH＝6、温度=90℃的条件下，用该流程处理煤化工工业所产生的洗煤气净化脱酚、蒸氨剩余废水，在无需对原废水进行稀释的前提下可很好地对此废水进行处理，使处理后的出水指标达到《污水综合排放标准》（GB89r78—1966）中规定的二级排放标准。     

复合生物法处理难降解制药废水的研究

针对难降解的制药废水,前端采用厌氧与微氧相结合的复合水解酸化工艺;后端采用交替流生物反应器与双流向曝气生物滤池组成的好氧生物处理工艺,建成了国内医药行业最大的废水处理工程。工程运行结果表明,该处理系统运行稳定可靠,出水达到国家排放标准,并为进一步深度净化、实现中水回用奠定了基础。     

催化氧化复合生物技术处理油气田压裂返排液

针对油气田压裂返排液处理难度大的问题,以四川某气田井组压裂返排液为研究对象,通过对其水质特征和治理技术现状的分析,提出催化氧化复合生物处理工艺并进行了现场实验。实验结果表明:该技术对于压裂返排液COD去除效果明显,最终出水COD浓度均降至100mg/L以下,COD去除率达到98%以上;G-BAF生化系统进水盐度在0.5%~5%时,系统适应性非常好,有机物去除率达93%以上;当盐度提高到8%时,有机物去除率仍能保持在84%左右,G-BAF生化系统适合高盐度压裂返排液的处理;压裂返排液出水主要污染指标COD浓度、氨氮浓度、SS浓度、pH值均达到GB 8978—1996《污水综合排放标准》一级标准,出水可用于油田及污水处理站设备清洁、钻井岩屑清洗等,实现废水综合利用。     

生化技术在采油废水治理中的应用

利用生化技术处理冀东油田的采油废水,在处理工艺流程中采用了悬浮、附着厌氧-好氧氧化池。与其他污水生化处理工艺相比,其不同之处是在池中同时存在悬浮污泥和固着生物膜,保持了很高的生物量,增强了设施耐冲击负荷的性能和处理能力。同时,池中还设置了可自由摆动的中密度弹性立体填料,池底设置了可变微孔曝气管。在曝气过程中,弹性立体填料对气泡有多层次的切割能力,可以提高充氧效率,污染物去除效果明显,对难降解的有机废水也有很好的处理效果。石油类去除率达到83%,COD去除率达到80%,出水水质达到了国家污水综合排放一级标准。     

石化企业污水深度处理与回用研究

以典型石化企业大庆石化公司为例,讨论了污水深度处理回用工程的合理性、必要性及可行性,并以化肥、热电两厂排水和兴化生活污水为回用原水进行了污水深度处理和回用的中型试验。试验工艺选用生物接触氧化、絮凝沉淀、过滤、消毒杀菌工艺。通过试验,确定了混凝剂、助凝剂及杀菌剂的类型、浓度及过滤压力等参数。结果表明:深度处理工艺对源污水中COD、BOD、总磷、氨氮、悬浮物、浊度、OIL、总铁等均有很好的去除效果。用作循环冷却水补水时,经过静态阻垢和旋转挂片试验及动态模拟试验,腐蚀速度达到中石化好级水平,粘附速度和污垢热阻达到中石化允许级水平。     

污水处理厂化学除磷精确控制系统研究——以山东某污水处理厂为例

我国总磷排放标准日趋严格,污水处理厂为保证出水总磷达标,过量投加化学除磷剂,造成资源浪费。为在出水水质达标的基础上节省化学除磷剂添加量,以山东某污水处理厂为例设计了化学除磷精确控制系统。在充分考虑仪器故障潜在风险的前提下,根据进水磷酸盐负荷实时调整药剂投加量,采用“前馈+反馈”控制的模式,实现加药过程的自动化及智能化。此外,该系统还可以显著节省化学药剂用量,如在山东某污水处理厂试验表明,该系统可节省除磷药剂约12.9%。不仅解决了污水厂除磷剂粗投放的问题,而且还可以增加出水稳定性,减轻运营工作的压力,使污水厂管理向精细化方向迈进。     

The short-term effects of prescribed burning on biomass removal and the release of nitrogen and phosphorus in a treatment wetland

Nutrient removal by constructed wetlands can decline over time due to the accumulation of organic matter. A prescribed burn is one of many management strategies used to remove detritus in macrophyte-dominated systems. We quantified the short-term effects on effluent water quality and the amount of aboveground detritus removed from a prescribed burn event. Surface water outflow concentrations were approximately three times higher for P and 1.5 times higher for total Kjeldhal nitrogen (TKN) following the burn event when compared to the control. The length of time over which the fire effect was significant (P < 0.05), 3 d for TKN and up to 23 d for P fractions. Over time, the concentration of soluble reactive phosphorus (SRP) in the effluent decreased, but was compensated with increases in dissolved organic phosphorus (DOP) and particulate phosphorus (PP), such that net total P remained the same. Total aboveground biomass decreased by 68.5% as a result of the burn, however, much of the live vegetation was converted to standing dead material. These results demonstrate that a prescribed burn can significantly decrease the amount of senescent organic matter in a constructed wetland. However, short-term nutrient releases following the burn could increase effluent nutrient concentrations. Therefore, management strategies should include hydraulically isolating the burned area immediately following the burn event to prevent nutrient export.     

Membrane filtration coupled with chemical precipitation to treat recirculating aquaculture system effluents

Effluents from recirculating aquaculture systems (RAS) contain high concentrations of nitrogen and phosphorous wastes and thus often require proper treatment to prevent potential detrimental impacts on receiving water bodies. The purpose of this study was to evaluate the feasibility of membrane filtration coupled with chemical precipitation as a pretreatment step with emphasis on phosphorus removal from RAS effluents. Chemical precipitation tests were conducted by adding magnesium chloride and alum at different chemical concentrations and pH values, respectively. Crossflow, flat-sheet membrane filtration modules were used to examine the effects of transmembrane pressure and crossflow velocity in terms of solid/liquid separation efficiency and permeate flux decline. The results showed that membrane filtration can effectively separate the phosphorus precipitates after chemical precipitation. The total phosphorus in the treated effluent was reduced to less than 0.05 mg L(-1) with a removal efficiency of more than 90%. However, much lower removal efficiencies were obtained for total organic carbon (TOC), total nitrogen, and turbidity. It was concluded that membrane filtration coupled with chemical precipitation can become an effective, compact treatment technology to meet the stringent regulatory requirements for RAS effluent discharge.     

城市污水Al盐化学除磷的试验研究

针对新疆地区污水厂总磷去除效率有限,出水总磷存在超标排放风险的问题。试验中采用自配不同总磷含量的生活污水,通过小试试验,投加AlCl3进行试验室模拟化学除磷试验。研究结果表明:进水总磷浓度为2～4mg/L时,投加AlCl3/TP质量比为8.6;进水总磷浓度为6mg/L时,投加AlCl3/TP质量比上升到13.1,出水总磷浓度均<0.5mg/L,AlCl3投加不会改变污水的pH值,化学沉淀最佳时间为30min。建议设计除磷沉淀池的停留时间为25min～30min。     

印染工业园区污水处理工程的运行及完善探讨

本文对某印染工业园区的混合废水处理装置开展了连续两年的运行调查,并对其进行了完善和提标改造的技术探讨。研究表明,污水处理装置的出水氨氮、总磷达标,BOD5、色度接近排放标准,而CODCr、SS难以达到一级排放要求。在现有工艺流程条件下对出水进行砂滤和二氧化氯强氧化能够保证出水达到一级A排放标准。     

ADDRESSING TOTAL PHOSPHORUS IMPAIRMENTS WITH WATER QUALITY TRADING1

ABSTRACT: Water quality trading is a voluntary economic process that provides an opportunity for dischargers to reduce the costs associated with meeting a discharge limitation. Trading can provide a cost effective solution for point sources (i.e., wastewater treatment plants) to meet strict effluent limitations set in response to total maximum daily loads (TMDLs). A successful trading program often depends on first determining the trading suitability of a pollutant for a particular watershed. A simple technical approach has been developed to identify sub‐watersheds within the Raritan River Basin, New Jersey, where water quality trading could provide a cost effective and scientifically feasible method for addressing total phosphorus impairments. The methodology presented will serve as a model to conduct similar analyses in other watersheds. The Raritan River Basin was divided into 12 subwatershed‐based study areas. Point‐nonpoint source trading opportunities were examined for each study area by examining the point and nonpoint source total phosphorus loading to impaired water bodies. Of the 12 subwatersheds examined, four had a high potential for implementing a successful trading program. Since instream phosphorus concentrations are closely related to soil erosion, an additional analysis was performed to examine soil erodibility. Recommendations are presented for conducting an economic analysis following the feasibility study.     

炼油废水回用于循环冷却水系统深度处理技术

为解决水资源紧缺问题,提高工业水资源的利用率,减少污水排放,采用臭氧催化氧化—活性炭吸附—石灰软化的工艺组合,深度处理炼油厂中二级处理达标排放的污水,探讨最佳工艺参数的选择,进行二级出水回用于循环冷却水的试验研究。试验表明:在臭氧氧化接触时间为40min,活性炭柱吸附通水流量为2L/h,石灰乳投加量0.32g/L、碳酸钠溶液0.06～0.10g/L、石灰软化搅拌15～20min,能使整套工艺达到最佳处理效果。小试阶段COD、氨氮、总硬度及总碱度的去除率分别达到96.00%、44.49%、64.61%、67.85%,硫酸根和氯离子均有所下降,通过整套工艺深度处理后,所得中水可作为循环冷却系统补充水。     

Biological filtration for removal of arsenic from drinking water

The main objective of the study was to find a suitable iron to arsenic ratio in water to reduce arsenic to 5 μg/L or lower through sand filtration. Experiments were conducted by varying the quantity of iron(II) while keeping the arsenic concentration at 100 μg/L. A mixture of iron (II) and arsenic at different ratios (10:1, 20:1, 30:1 and 40:1) was pumped to the sand filters in a down flow mode and effluent arsenic and iron were analyzed. It was found that a ratio of iron to arsenic of 40:1 was necessary to ensure an effluent arsenic concentration of 5 μg/L or lower. Iron in the filtrate was found to be below 0.1 mg/L at all times.