城市污水深度处理试验

对城市污水在二级处理的基础上进行深度处理并重复利用,是四个现代化的需要。为此,我们进行了加药混凝、臭氧化、沉淀过滤、活性炭吸附等工艺的单项和综合处理试验。一、二级处理出水的混凝沉淀试验     

加压混凝沉淀对蓝藻水处理中消毒副产物的控制

为了降低蓝藻水处理中消毒副产物的产生,采用物理加压法取代传统化学氧化法进行预处理,从而减少新的化学物质的产生,降低消毒副产物风险,实验对比研究了加压混凝沉淀和预氧化混凝沉淀除藻工艺中消毒副产物及其前驱物的浓度。结果表明,经0.7 MPa加压1 min后混凝沉淀处理,藻类去除率达到95.8%,浊度0.58 NTU,均比原水混凝沉淀和预氧化混凝沉淀后效果大幅度提高。蓝藻水加压后三卤甲烷前驱物降低26.2%,卤乙酸前驱物无变化,混凝沉淀处理后前驱物比原水混凝沉淀后略有减少。加压水过滤消毒后消毒副产物与原水处理后持平。而经1~2 mg/L的Na Cl O预氧化水混凝沉淀过滤消毒后,三卤甲烷和卤乙酸浓度分别比原水处理后增加了3~4倍和1.7~2.5倍。加压混凝沉淀工艺处理蓝藻水,比传统预氧化工艺更有效控制了消毒副产物的产生。     

制革废水试验研究

采用预处理-混凝沉淀-微滤组合工艺对制革废水进行试验研究.结果表明,制革废水经预处理后用硫酸亚铁酸洗废液作混凝剂是行之有效的,经此工艺处理后,COD、BOD5、SS和色度去除率分别为80.4%、87.2%、88.6%和91.7%,处理后废水水质达到排放标准且可回用于生产.在较低温度下,用硫酸亚铁作混凝剂仍能较好地完成混凝沉淀,验证了硫酸亚铁的低温混凝效果.此工艺具有很好的应用前景,尤其适合北方寒冷地区.     

强化活性炭吸附技术深度处理焦化废水的可行性研究

采用混凝沉淀、活性炭吸附以及混凝沉淀 活性炭吸附工艺对焦化厂生化出水进行深度处理.单独混凝沉淀或活性炭吸附均可以将水样中COD降到100 mg/L以下,达到国家污水一级排放标准和冷却用水建议标准.活性炭根据不同的材质和进水而表现出不同的吸附性能,对于焦化厂生化出水,煤质炭Ⅰ和果壳炭均表现出良好的吸附效果,并使出水COD＜100 mg/L,但处理成本较高.混凝沉淀 活性炭吸附工艺充分发挥适合去除大分子污染物的混凝沉淀与适宜去除小分子污染物的活性炭吸附技术两者的协同增效作用,吸附单元采用廉价的煤质炭,使出水水质达到个别生产或生活用水回用标准,并且降低深度处理成本.研究结果表明,混凝沉淀 活性炭吸附作为焦化厂生化出水回用工艺是经济可行的.     

聚合氯化铝铁的形态分布对微污染源水混凝效果的影响

针对微污染源水中浊度、叶绿素a等的强化去除问题,研究了碱化度、铝铁比和加碱方式等对聚合氯化铝铁形态分布的影响,并考察了形态分布与混凝除污效率和混凝沉淀出水中残铝浓度的关系.结果表明:在铁摩尔分数一定时,混凝剂中单体、中等聚合物和无定形凝胶含量与碱化度存在线性相关性,并推导出中等聚合物含量的计算公式;在碱化度一定时,混凝剂中单体、中等聚合物和无定形凝胶含量与铁摩尔分数也存在线性相关性;增加碱化度或降低铁摩尔分数,可以增加中等聚合物含量、降低单体含量,从而影响混凝除污效率和混凝沉淀后出水中残铝浓度.混凝实验结果表明,混凝过程中叶绿素a去除率和浊度去除率均与混凝剂中中等聚合物含量存在线性相关性,但两者相关系数不同.混凝沉淀后出水中残铝浓度与混凝剂中单体含量存在线性相关性.因此,预聚合的无机高分子混凝剂对提高混凝过程中的除浊、除藻效率,降低混凝沉淀后出水中残铝浓度具有重要的意义.     

难降解混合化工废水预处理试验研究

对某化工开发区混合化工废水进行预处理试验研究，分别对铁还原后加中和混凝沉淀以及直接中和混凝沉淀两种预处理方法进行了试验，重点讨论了铁还原工艺的各种影响因素。研究了曝气与不曝气，加炭与不加炭以及不同CODCr、不同pH值对铁还原处理效果的影响，并考察了铁的消耗与废水中铁离子的作用及变化情况。     

重介质混凝沉淀工艺工程应用中的难点及解决方案

为了解决重介质混凝沉淀技术中重介质微粒粒径小、密度高、流动性差、对后续工艺影响大等难点问题,通过调节重介质粉的材质与参数、设计投加与回收方式、改善沉淀池斜板清洗方案等各项技术,申请相关设备专利并提供了解决方案。结果表明,在实际运行过程中,CASS出水的水质经重介质混凝沉降后得到进一步的改善。另一方面,与传统混凝沉淀工艺的土地占地面积相比,能够节省20%以上的占地面积以及20%左右混凝剂的投加量。工艺的改进也提高了工艺运行的稳定性和重介质粉的回收率。研究从整体优化了重介质混凝沉淀工艺,有利于其在实际工程中的应用。     

混凝沉淀前处理对丙烯酸丁酯废水陶瓷膜过滤膜污染的影响

采用混凝沉淀-双层滤料过滤-陶瓷膜过滤组合工艺去除丙烯酸丁酯废水中浊度物质。结果表明,废水pH值、混凝药剂投加量、混凝沉淀水力条件不仅对丙烯酸丁酯废水混凝沉淀出水和双层滤料过滤单元出水浊度具有重要影响,而且对后续陶瓷膜过滤单元膜污染均具有重要影响。双层滤料过滤出水浊度与陶瓷膜污染阻力具有明显的正相关关系,双层滤料过滤出水浊度越高,陶瓷膜污染阻力越大。废水pH在7.0~10.0范围内、混凝药剂PAC或PAM投加过量、废水流量过高都会造成双层滤料过滤出水浊度偏高,导致陶瓷膜污染严重。     

本期推荐

正本期"工程应用实例"栏目刊发了贾伯林、卢建波、肖峰、邹瑜斌、尤亚建、陈勇华、杨志宏撰写的《重介质混凝沉淀工艺工程应用中的难点及解决方案》一文。该文以重介质混凝沉淀技术为基础,根据实际工程中存在的问题和难点,针对现有技术提出了全面的改进方案,解决了其在实际应用中重介质微粒粒径小、密度高、流动性差、对后续工艺影响大等难点问题。重介质混凝沉淀工艺作为一种新型的水处理工艺,在传统的混凝沉淀过程中投加了惰性重介质粉,并将此重介质微颗粒作     

常用城市污水再生处理工艺净化效果比较分析

以城市污水回用为目的,对常规混凝-沉淀-过滤工艺、臭氧生物活性炭和直接超滤等深度处理技术处理城市污水处理厂二级出水的效果进行了试验研究,对各种工艺的去除效果进行了评价。     

高锰酸盐复合药剂强化混凝改善再生水景观湖水质研究

实验通过投加助凝剂以强化混凝沉淀过程,从而达到去除再生水景观水中的藻类。以PAC为混凝剂,高锰酸盐复合药剂(PPC)为预氧化助凝剂,通过烧杯实验确定PPC、PAC同时投加,最佳投量分别为1 mg/L、60 mg/L。生产性实验中,机械加速澄清池强化混凝对TP、叶绿素、藻密度的去除率分别为54%、32.3%和35.4%,湖水中TP、TN逐渐降低分别由4.9 mg/L、23 mg/L降至0.72 mg/L、10.3 mg/L。PPC提高了混凝沉淀对藻类的去除效果,改善了再生水景观湖水质,降低水中氮磷营养盐的含量。     

二相厌氧-混凝法处理制浆造纸综合废水的工艺设计及调试

湖南某造纸厂采用二相厌氧 混凝法处理制浆造纸综合废水取得了显著效果 ,CODCr排放总量削减率达 80 % ,水体水质明显改善。本文介绍了该工程的工艺设计及调试。     

强化混凝处理城市纳污河污水运行过程中搅拌能量的影响

介绍了采用混凝技术大规模处理运河污水时所遇到的问题，并通过混凝试验分析了问题的原因。提出并初步探讨了混凝搅拌能量及其计算方式，利用混凝搅拌能量参数分析混凝反应效果的差异，说明在实际生产中混凝反应过程需要有足够的能量。     

Competition of coagulation sink and source rate: New particle formation in the Pearl River Delta of China

The coagulation sink and its role in new particle formation are investigated based on data obtained during the PRIDE-PRD2004 campaign at Xinken of Pearl River Delta, China. Analysis of size distributions and mode contributions of the coagulation sink show that the observed higher load of accumulation mode particles impose a significant effect on the coagulation sink and result in higher coagulation sinks at Xinken despite of the lower total particle number compared with other areas. Hence it is concluded that the higher coagulation sink may depress the occurrence frequency of new particle formation events. The strategies targeting at controlling accumulation mode particles may have influences on the frequency of new particle formation events at this area. The factors affecting the coagulation sink are evaluated. The relatively lower ambient relative humidities may weaken the coagulation sink and facilitate the occurrence of new particle formation events during noontime, while the surmise of nucleation and growth involving organic matter may imply an actually higher coagulation sink than expected. These factors have a significant influence on the ultimate fate of the newly formed nuclei and new particle formation. A comparison of event and non-event days indicates that the coagulation sink is not the only decisive factor affecting new particle formation, other factors including the precursor vapors and photochemical activity are none the less important either. Competition of coagulation sink and high source rate leads to the occurrence of new particle formation events at Xinken.     

混凝与Fenton联用处理垃圾渗滤液的效能及成本

为对混凝/Fenton工艺与Fenton/混凝工艺处理垃圾渗滤液的效果和成本进行比较,分别对年轻渗滤液和老龄渗滤液原液按照混凝/Fenton工艺与Fenton/混凝工艺2种技术路线进行处理。实验结果表明,Fenton试剂对年轻垃圾渗滤液和老龄垃圾渗滤液COD去除率最高的反应条件为pH=3.5、H2O2和Fe2+的摩尔比为6、H2O2和渗滤液原液的COD质量比为3、反应时间4 h;在PAC与渗滤液原液的COD质量比为0.6时,PAC混凝对渗滤液原液的COD去除率最高。在对渗滤液COD去除率最高的Fenton反应和PAC混凝反应条件下,混凝/Fenton工艺对年轻渗滤液和老龄渗滤液的COD去除率分别为90.56%和86.56%;Fenton/混凝工艺对年轻渗滤液和老龄渗滤液的COD去除率分别为89.99%和85.99%,2种技术路线对渗滤液COD的去除率相差不大,但先PAC混凝后Fenton氧化工艺比先Fenton后混凝工艺每t节省62.6元,是更优化的渗滤液处理工艺。     

滤布滤池强化处理城市二级出水中试研究

采用滤布滤池对南方某城市污水处理厂二级出水进行强化处理中试研究，以达到中水回用的目的。实验选用氯化铁(FeCl₃)、聚合氯化铝铁（PAFC）和聚合氯化铝（PAC）作为强化滤布滤池除磷效果的混凝剂。当不投加混凝剂时，滤布滤池对TP和COD的平均去除率为28.76%和8%，其中TP的去除效果受进水水质影响较大；当投加氯化铁、聚合氯化铝铁与聚合氯化铝强化滤布滤池时，滤布滤池对TP的平均去除率分别为63.58%、60.13%和66.94%，TP去除效果受进水水质影响较小；对SS的平均去除率分别为70.7%、64.3%和49.1%；对COD平均去除率分别为17.7%、26.3%和27.7%。滤布滤池对TN和NH₃-N去除效果不稳定。     

水解——好氧——混凝沉淀工艺处理涤纶厂聚酯废水

报道了用上流式厌氧污泥床和生物接触氧化池对涤纶厂聚酯废水所进行的中试。当上流式厌氧污泥床进水ＣＯＤｃｒ浓度为１２００ｍｇ／Ｌ，经水解－好氧工艺处理后，好氧池出水的ＣＯＤｃｒ浓度为１６９．１ｍｇ／Ｌ，进一步混凝沉淀处理后，出水ＣＯＤｃｒ达８０ｍｇ／Ｌ。     

Identification and characterization of coagulation inhibitor proteins derived from cyanobacterium Microcystis aeruginosa

The excess growth of cyanobacteria in semi enclosed water areas caused by eutrophication brings about coagulation inhibition in drinking water treatment processes. In this study, coagulation inhibitor proteins produced by Microcystis aeruginosa, a major cyanobacterium in algal bloom, were acquired by a phage display technique, an aluminum-immobilized affinity chromatography and a protein expression technique using Escherichia coli cells. Two cyanobacterial peptides with a high ratio of metallophilic amino acids were recovered, which were a part of homologues of a thiol oxidase enzyme Ero1p and a trans-acting repressor ArsR. It was also shown that the homologue of ArsR exhibited a stronger inhibitory effect on the coagulation of kaolin suspension with polyaluminum chloride than the control proteins. This is the first report to identify a cyanobacterial cell component to inhibit coagulation. The compositions of polar amino acids were critical to explain the strength of coagulation inhibition potential. Polar proteins from cyanobacteria could collectively consume coagulants or stabilize clay particles, which would be plausible explanations for causing coagulation inhibition. Meanwhile, results from the kaolin coagulation tests using the control proteins implied that the neutralization of positive charges of coagulant constituents by simple electrostatic interactions might not be the key mechanism on the protein-induced coagulation inhibition.     

Effect of pre-ozonation on optimized coagulation of a typical North-China source water

Although ozone is widely used as a pre-oxidant before coagulation in water treatment, the effect of pre-ozonation on optimized coagulation for removal of particle and natural organic matter (NOM) is still not fully understood. In this paper, pilot-scale investigation was conducted to examine the impact of pre-ozonation on coagulation for particle and NOM removal. Changes in the particle and NOM distributions were characterized by various methods, including laser light granularity system, particle counter, ultrafiltration, and resin absorbent fractionation. A novel composite flocculant–HPAC was compared with the traditional ferric chloride coagulant in terms of coagulation efficiency under the influence of pre-ozonation. Typical micro-polluted North China surface water was used for pilot coagulation tests. The results show that the effect of pre-ozonation on coagulation is associated with the dosage of ozone, coagulant type, and water contamination characteristics. For FeCl₃, pre-ozonation acts as a coagulation aid at low dosage (1.0 mg L⁻¹ O₃) for turbidity and UV₂₅₄ removal; while at higher dosage (2.0 mg L⁻¹ O₃), pre-ozonation is detrimental to UV₂₅₄ removal although it is still beneficial for turbidity removal. In the case of composite flocculant–HPAC, pre-ozonation demonstrates negligible influence on both turbidity and UV₂₅₄ removal. Ozone can simultaneously aggregate fine particles and break down large ones, making them more mineralized and easier to remove. NOM with intermediate molecular weight and hydrophobic neutral property increases at lower ozone dosage, favoring removal by coagulation. At higher ozone dosages, NOM becomes more hydrophilic and its molecular weight becomes smaller, decreasing NOM removal.     

Effect of Pre-ozonation on Optimized Coagulation of a Typical North-China Source Water

Although ozone is widely used as a pre-oxidant before coagulation in water treatment, the effect of pre-ozonation on optimized coagulation for removal of particle and natural organic matter (NOM) is still not fully understood. In this paper, pilot-scale investigation was conducted to examine the impact of pre-ozonation on coagulation for particle and NOM removal. Changes in the particle and NOM distributions were characterized by various methods, including laser light granularity system, particle counter, ultrafiltration, and resin absorbent fractionation. A novel composite flocculant–HPAC was compared with the traditional ferric chloride coagulant in terms of coagulation efficiency under the influence of pre-ozonation. Typical micro-polluted North China surface water was used for pilot coagulation tests. The results show that the effect of pre-ozonation on coagulation is associated with the dosage of ozone, coagulant type, and water contamination characteristics. For FeCl₃, pre-ozonation acts as a coagulation aid at low dosage (1.0 mg L⁻¹ O₃) for turbidity and UV₂₅₄ removal; while at higher dosage (2.0 mg L⁻¹ O₃), pre-ozonation is detrimental to UV₂₅₄ removal although it is still beneficial for turbidity removal. In the case of composite flocculant–HPAC, pre-ozonation demonstrates negligible influence on both turbidity and UV₂₅₄ removal. Ozone can simultaneously aggregate fine particles and break down large ones, making them more mineralized and easier to remove. NOM with intermediate molecular weight and hydrophobic neutral property increases at lower ozone dosage, favoring removal by coagulation. At higher ozone dosages, NOM becomes more hydrophilic and its molecular weight becomes smaller, decreasing NOM removal.