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污水深度处理工艺化学强化除磷单元药剂选择及优化 总被引:1,自引:0,他引:1
试验采用化学除磷工艺补充处理河南某污水处理厂的改良氧化沟脱氮工艺二级处理出水,以达到深度除磷目的,使出水满足《城镇污水处理厂污染物排放标准》(GB 18918—2002)一级A的要求。分析聚氯化铝、聚硫酸铁和三氯化铁三种混凝剂对二级出水中总磷的去除效果,并确定其最合适的投加量。试验结果显示当二级处理水总磷为2~3 mg/L,出水总磷达到0.5 mg/L要求时,投加量:氯化铁聚氯化铝聚硫酸铁,即氯化铁的投加量最少;年投加混凝剂的费用:聚氯化铝氯化铁聚硫酸铁。综合考虑,最合适的混凝剂为聚氯化铝,其最合适的投加量为59 mg/L。 相似文献
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为解决污水处理厂生化池出水总磷浓度不稳定的现象,从投加量、pH、沉降时间和原水总磷浓度4个方面考察了PAFC和PAC两种混凝剂的除磷效果,结果表明,混凝剂PAFC具有较好的除磷性能。在此基础上进行响应面优化试验,以混凝剂PAFC投加量、pH、沉降时间为自变量,总磷去除率为响应值,采用Box-Behnken试验设计方法,建立二次多项式响应曲面模型。模型优化结果显示,影响因子对总磷去除率影响顺序为:PAFC投加量pH沉降时间,最佳工艺条件为:PAFC的投加量为13.22mg/L,pH为8.0,沉降时间为11min。该条件下,总磷去除率达到最大为93.35%。验证性试验表明,此模型具有较高的可行性和有效性,研究结果为污水处理厂处理工艺改造提供了技术支持。 相似文献
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景观水体补充水源中磷的处理,与污水磷的处理在原水水质和处理目标上均有较大差异。关于污水除磷和景观水体除磷的研究较多,而有关景观水体补充水源除磷的研究却鲜见报道。对景观水体补充水源中磷处理方法的选择、处理原理、药剂、加药量的确定、降低投药量的辅助措施等方面进行了研究,并对实际工程中出现的两类水质差别较大的水源分别进行研究,确定采用25mg/L和60mg/L的硫酸铝进行混凝,对于水质较差的河网水,通过加硫酸调pH、加次氯酸钠预氧化和加聚丙烯酰胺以及过滤的方法可有效促进磷的去除,降低投药量。最后对工程实际运行中磷超标的情况,提出了相应可采取的措施。 相似文献
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结合苏州娄江污水处理厂生产运行实践,研究了改良型一体化交替反应池在实现良好反硝化除磷条件下的运行工况.实践表明,提高反硝化除磷的关键是要有充足的硝酸盐氮为反硝化聚磷菌(DPB)提供电子受体,当NO-2N浓度在5 mg/L以上时,可以实现较好的反硝化除磷;当SRT为12~14 d时,反硝化除磷和系统脱氮除磷效果最好,生物除磷运行成本较低.此外,进水COD/TP、好氧池DO、厌氧池MLSS以及SRT也是影响一体化反应池生物除磷的主要因素.针对雨季低负荷运行除磷效果不理想的现象,提出了相应的工况运行措施. 相似文献
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有机膨润土在污水处理中的应用研究 总被引:4,自引:0,他引:4
通过正交试验研究了改性的有机膨润土对乌鲁木齐东郊污水厂污水中COD的吸附条件 及主要的影响因素,并确定了污水处理的最佳条件。结果表明:在试验条件下,有机膨润土对COD 有很好的吸附效果。有机膨润土对污水处理的最佳条件是新疆乌兰陵格产有机膨润土A,投加量为 8 g/L,pH为6,振荡时间为20 min,转速为150 r/min。同时探讨了有机膨润土A在污水处理中的 相关影响因素:pH是影响COD吸附效果的关键因素,其最佳取值范围为6-8;有机膨润土A投加 量的最佳取值范围是4-8 g/L;振荡时间的最佳取值范围是10-20 min。 相似文献
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城市污水处理厂化学除磷效果及运行成本研究 总被引:3,自引:1,他引:2
通过对硫酸亚铁、氯化铁、硫酸铝、聚氯化铝和聚氯化铝铁的小试研究,以及时北京城市排水集团下属三座污水处理厂在沉砂池、曝气池的生产性试验研究,详细论述了化学除磷的除磷效果与化学药剂投加量、运行成本和磷削减成本的关系,用于指导和控制城市污水处理厂除磷的直接成本,并保证城市污水处理厂高效、稳定的处理效果。试验表明,当出水总磷要求小于1 mg/L和0.5 mg/L时,药剂中金属元素与去除磷元素的物质的量之比(Me/P)、运行成本、磷削减成本分别为:2~2.5、0.1~0.13元/m~3、4.5万~5.5万元/t和3~6、0.13~0.2元/m~3、5万~15万元/t。 相似文献
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Effect of microbially available phosphorus (MAP) on biofilm development in drinking water systems was investigated at the pilot-scale experiments over 3 years. Completely mixed biofilm reactors Propella (water detention time 24 h, flow rate 0.25 m s(-1), PVC pipe coupons) were used as water distribution network models. Four experimental runs were carried out with water containing different levels of phosphorus which was limiting nutrient for bacterial growth. Positive correlation between MAP in the inlet water and heterotrophic plate count (correlation coefficient 0.95) in biofilm, as well as for the total bacteria number (correlation coefficient 0.71), was observed. However, our experiments showed that removal of phosphorus down to very low levels (below detection limits of chemical method and MAP < 1 microg L(-1) was not an efficient strategy to eliminate bacterial regrowth and biofilm formation (< 51,00,000 cells/cm2) in drinking water supply systems. 相似文献
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以南京水利科学研究院铁心桥试验基地内象目湖微污染水体为对象,研究总氮大于1.0 m3/(m2·d)的高水力负荷条件下,鹅卵石、陶粒、砾石、钢渣、蛭石、碎石和砂子等多种基质和再力花、芦苇、美人蕉及菖蒲等水生植物组合条件下的垂直流湿地和水平潜流湿地对氮磷的去除效果。试验结果表明:进水总氮浓度在0.793~2.662 mg/L时,种植菖蒲,填料从上到下分别为鹅卵石、碎石、粗砂和细砂的垂直潜流湿地单元(20单元)出水总氮平均浓度最低,为0.905 mg/L;总氮、氨氮和硝态氮平均去除率最高,达80.89%,43.06%和46.32%;总氮浓度从Ⅳ类水体提升至Ⅲ类。进水TP浓度在0.035~1.003 mg/L时,20单元总磷平均去除率最高,为30.59%,价格相对便宜的碎石对磷素的去除效果较好。种植菖蒲及填料组合为鹅卵石、碎石、粗砂和细砂的人工湿地处理单元可以应用于饮用水源地原水等微污染水强化处理。 相似文献
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Seven major water treatment plants in Seoul Metropolitan Area, which are under Korea Water Resources Corporation (KOWACO)'s management, take water from the Paldang Reservoir in the Han River System for drinking water supply. There are taste and odour (T&O) problems in the finished water because the conventional treatment processes do not efficiently remove the T&O compounds. This study evaluated T&O removal by ozonation, granular activated carbon (GAC) treatment, powder activated carbon (PAC) and an advanced oxidation process in a pilot-scale treatment plant and bench-scale laboratory experiments. During T&O episodes, PAC alone was not adequate, but as a pretreatment together with GAC it could be a useful option. The optimal range of ozone dose was 1 to 2 mg/L at a contact time of 10 min. However, with ozone alone it was difficult to meet the T&O target of 3 TON and 15 ng/L of MIB or geosmin. The GAC adsorption capacity for DOC in the three GAC systems (F/A, GAC and O3 + GAC) at an EBCT of 14 min is mostly exhausted after 9 months. However, substantial TON removal continued for more than 2 years (>90,000 bed volumes). GAC was found to be effective for T&O control and the main removal mechanisms were adsorption capacity and biodegradation. 相似文献
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Y Suzuki T Kondo K Nakagawa S Tsuneda A Hirata Y Shimizu Y Inamori 《Water science and technology》2006,53(6):107-113
A new biological nutrient removal process, anaerobic-oxic-anoxic (A/O/A) system using denitrifying polyphosphate-accumulating organisms (DNPAOs), was proposed. To attain excess sludge reduction and phosphorus recovery, the A/O/A system equipped with ozonation tank and phosphorus adsorption column was operated for 92 days, and water quality of the effluent, sludge reduction efficiency, and phosphorus recovery efficiency were evaluated. As a result, TOC, T-N and T-P removal efficiency were 85%, 70% and 85%, respectively, throughout the operating period. These slightly lower removal efficiencies than conventional anaerobic-anoxic-oxic (A/A/O) processes were due to the unexpected microbial population in this system where DNPAOs were not the dominant group but normal polyphosphate-accumulating organisms (PAOs) that could not utilize nitrate and nitrite as electron acceptor became dominant. However, it was successfully demonstrated that 34-127% of sludge reduction and around 80% of phosphorus recovery were attained. In conclusion, the A/O/A system equipped with ozonation and phosphorus adsorption systems is useful as a new advanced wastewater treatment plant (WWTP) to resolve the problems of increasing excess sludge and depleted phosphorus. 相似文献
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电絮凝作为一种具有广泛应用前景的低廉高效污水处理技术,已经被证明在工业废水、生活污水等污染严重的水体处理上具有显著效果,但是目前对于电絮凝净化微污染水的相关研究较少。通过对电絮凝分批处理河水的实验研究,分析电絮凝方法处理微污染水的可行性,讨论极板间距的改变对电絮凝处理效果的影响。结果表明,电絮凝处理技术可以用于微污染水净化中,在电流密度为17.75 A/m2、极板间距为1.5 cm的条件下,反应30 min时,色度去除率为73.76%,浊度去除率为76.00%,悬浮固体去除率为85.71%,化学需氧量去除率为42.86%,总磷去除率为61.36%。在电絮凝反应中,极板间距对于微污染水的色度、浊度、悬浮固体和总磷去除效果具有明显的影响。 相似文献
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根据青岛市大沽河下游咸水分布区水文地质条件,采集该地区代表性中砂进行砂槽模拟试验,分析了抽水量、抽水井的位置以及抽水持续时间对咸水体修复效果的影响。试验结果表明:进行抽水修复时,各观测点盐度依次降低,并且形成突降;抽水量越大,咸水的去除速率越高,修复时间越短,抽水量从80.2 mL/min分别增至160.2 mL/min、240.2 mL/min时,修复时间缩短为之前的52.4%和34.9%;将抽水井安置在隔水边界附近,能够有效地抽取高浓度咸水,显著提高地下咸水体的整体修复效果;该试验条件下,抽水持续时间为115 min时,虽然结束抽水时的出水盐度为0.274%,但是依靠自然修复仍然能够满足饮用水标准,相较于出水盐度为0.10%的抽水持续时间缩短了30.3%,大幅降低修复成本,对咸水体的工程研究具有明显的经济意义。 相似文献
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常规混凝沉淀工艺对阴离子表面活性剂的去除研究 总被引:8,自引:0,他引:8
随着阴离子表面活性剂(LAS)在民用和工业上的广泛应用,由此带来的水污染问题也日益加剧,对供水安全造成了很大威胁。针对目前大部分水厂仍采用混凝沉淀常规水处理工艺,考察了常规混凝沉淀工艺对LAS的去除效果。以Al2(SO4)3,PAC,FeCl3,PFS为混凝剂,非离子PAM为助凝剂进行了试验,结果表明混凝沉淀对LAS有一定的去除效果,而且有机物和LAS的去除有一定相关关系。但浊度与LAS的去除相关性较差。试验条件下对于LAS去除最佳混凝方案是投加量为40 mg/L的FeCl3。相同水质条件下铁盐混凝剂在除浊、除有机物和除LAS方面优于铝盐混凝剂。pH和水温对LAS的去除有一定影响,较低的pH和较高的水温均有利于LAS的去除。 相似文献