城镇面貌三年大变样环保行动成效显著

自实施城镇面貌三年大变样环保行动计划以来,我省城市空气质量持续改善,2008年,全省设区城市空气质量二级以上天数平均达到324天,比2007年增加11天。今年128月,设区城市空气二级以上天数平均达到232天,比去年同期增加8天,全省“蓝天”（空气二级及二级以上）数平均每月达29天。     

复合混凝剂用于夏季太湖水混凝脱浊研究

用特征粘度系列化的聚二甲基二烯丙基氯化铵(PDM)与聚合氯化铝(PAC)复合得到稳定的复合混凝剂,用于夏季高藻太湖水强化混凝脱浊处理.通过混凝烧杯实验.考察了无机/有机复合比例、PDM特征粘度对脱浊效果及絮团沉淀性能的影响.结果表明,对浊度为30-33 NTU,温度为28～30℃,藻含量为2.6×107个儿的太湖水,在与某市水厂混凝强度相近的搅拌强度下.当达到该水厂2NTU沉淀池出水的余浊标准时,PAC需7.00 mg/L的投加量.质量复合比例为5:1、10:1、20:1的PAC(以Al2O3计)/PDM复合混凝剂所需PAC投加量随PDM特征粘度0.52、1.53、2.46 dL/g的增加分别为3.00-2.83 ms/L、3.50-3.49ms/L、5.37-4.67 mg/L,相对于PAC减少投加量57.14%-59.57%、50%-50.14%、23.29%-33.29%;作为深度处理的技术准备.当沉淀出水浊度要求提高至1NTU的情况下,复合药剂依然可发挥好的作用,PAC需10 mg/L的投加量,PAC(以Al2O3计)与PDM质量复合配比为20:1、10:1、5:1的复合混凝剂需8.33-3.91 mg/L的投加量,能比PAC减少投加量16.7%～60.9%.可见,PDM明显提高了PAC的混凝脱浊效果与沉淀性能,且PAC/PDM质量复合配比越低,PDM特征粘度越高,脱浊效果与沉淀性能越好.     

两点短时游离氯后转氯胺的顺序氯化消毒工艺研究

基于顺序氯化消毒工艺的原理,采用两点短时游离氯后转氯胺的两点顺序氯化消毒工艺,即在过滤和清水池前的两点分别加氯,并在清水池加氯后立即加氨转化为氯胺消毒的工艺,该工艺在常规处理工艺的给水厂进行了消毒试验.结果表明,加氯点的适当提前,不仅有利于控制消毒副产物的生成量,而且有效抑制了滤池中的生物膜滋生.两点顺序氯化消毒工艺中生成的卤代消毒副产物比相同条件下一次性加入等量的氯消毒剂的消毒方法产生的三卤甲烷(THMs)平均减少了51.6％,卤乙酸(HAAs)平均减少了46.7％.细菌学指标HPC的结果也显示出了该工艺在保障水质的微生物安全方面的优势.     

Development and application of a two-dimensional water quality model for the Daqinghe River Mouth of the Dianchi Lake

Water quality models are important tools to support the optimization of aquatic ecosystem rehabilitation programs and assess their efficiency. Basing on the flow conditions of the Daqinghe River Mouth of the Dianchi Lake, China, two-dimensional water quality model was developed in the research. The hydrodynamics module was numerically solved by the alternating direction iteration (ADI) method. The parameters of the water quality module were obtained through the in situ experiments and the lab analyses that were conducted from 2006 to 2007. The model was calibrated and verified by the observation data in 2007. Among the four modelled key variables that were water level, CODcr, NH3-N and PO4-P, the minimum value of the coefficient of determination (CoD) was 0.69, which mean the model performed reasonably well. The developed model was then applied to simulate the water quality changes at the downstream cross-section assuming that the designed restoration programs were implemented. According to the simulated results, the restoration programs could cut down the loads of CODcr and PO4-P about 15%, however, they would have very little effect on the NH3-N removal. Besides, the water quality at the outlet cross-section would be still in class V (3838-02), indicating more measures should be taken to further reduce the loads. The study demonstrated the capability of water quality models to support aquatic ecosystem restorations.     

二苯碳酰二肼光度法测定水中六价铬方法的改进

对比了6种酸体系对二苯碳酰二肼光度法测量六价铬的影响,得出盐酸体系步骤简化。分析速度快,易操作。线性关系、精密度、准确度能得到保证。     

Selective removal of 2,4-dichlorophenoxyacetic acid from water by molecularly-imprinted amino-functionalized silica gel sorbent

A molecularly-imprinted amino-functionalized sorbent for selective removal of 2,4-dichlorophenoxyacetic acid(2,4-D) was prepared by a surface imprinting technique in combination with a sol-gel process.The 2,4-D-imprinted amino-functionalized silica sorbent was characterized by FT-IR,nitrogen adsorption and static adsorption experiments.The selectivity of the sorbent was investigated by a batch competitive binding experiment using an aqueous 2,4-D and 2,4-dichlorophenol(2,4-DCP) mixture or using an aqueous 2...     

水源水中典型化学品突发污染的应急处理

针对被典型化学品双酚A(BPA)与邻苯二甲酸二乙酯(DEP)污染原水的应急处理工艺进行了研究.结果表明,活性炭吸附可有效去除双酚A和DEP.拟二级动力学模型和Elovich模型较好地描述粉末活性炭对原水中BPA和DEP的吸附过程.中试条件下,50 mg/L的粉末活性炭可分别将原水中浓度约为500 μg/L的双酚A和3.3 mg/L的DEP处理达标.炭砂滤柱对2种化学品的动态吸附表明,BPA和DEP的去除率受它们初始浓度的影响较小,在滤速为5.1～15.3 m/h的范围内BPA和DEP的去除率基本不受滤速的影响.当同时采用粉末活性炭和炭砂滤柱工艺时, PAC的吸附过程是去除污染的主要阶段,炭砂滤柱可以作为粉末活性炭的有效补充保证一定的安全系数.KMnO₄和Cl₂均不能氧化DEP,3 mg/L的KMnO₄和1.5 mg/L的Cl₂可几乎完全氧化水中浓度为850　μg/L的BPA,BPA的氯化产物和KMnO₄的氧化产物及其毒性有待于进一步研究.　1.5 mg/L高锰酸钾和PAC联用对去除DEP无协同作用,对去除BPA有促进作用.     

碳源类型对A~2O系统脱氮除磷的影响

采用52.5 L的A2O反应器,以乙酸和丙酸分别作为进水唯一碳源,系统研究了进水碳源类型对脱氮除磷和代谢过程的影响.结果表明,在进水COD为250 mg/L左右,NH+4-N为52 mg/L左右的条件下,原水碳源类型对TN的去除影响不大,系统TN去除率均在65%左右.进水碳源类型对TP的去除及相应污泥中PHA的类型、含量和代谢及糖原的变化影响较大.乙酸为唯一碳源时,厌氧区放磷浓度较高,污泥中PHA的成分主要为PHB和PHV,两者在厌氧区的合成量差别不大,PHB在随后的反应过程中变化较大,对除磷代谢过程起主要作用,而PHV的变化较小.丙酸作为进水唯一碳源时,厌氧区的放磷浓度偏低,主要合成PHV,几乎不含PHB,PHV在随后吸磷过程中浓度变化较大,对除磷代谢起主要作用,而且出水TP浓度偏低.碳源类型对污泥中糖原的代谢也有影响,乙酸为碳源时糖原的含量高,变化范围也较大,丙酸为碳源时糖原的变化幅度较小.在同步脱氮除磷系统中,与乙酸相比,丙酸是一种更合适的碳源.     

颗粒物对紫外线灭活二级出水中粪大肠菌的影响

用低压紫外线照射具有相同颗粒物粒径分布的一系列水样,把实验结果带入二重动力学模型进行计算,评价自然状态下颗粒物对粪大肠菌的保护作用. 结果表明,二级出水中的大部分粪大肠菌都与颗粒物交连在一起;在颗粒物<10⁵ C·mL^-1时,颗粒物的增加会明显降低紫外线对二级出水中粪大肠菌的灭活率,但当颗粒物>10⁵ C·mL^-1时,这种影响不明显.从二重动力学模型的计算结果来看,对于不同颗粒物浓度的水样,难灭活的微生物所占的比重很小且比较稳定,大多数与颗粒物结合的粪大肠菌都较易被紫外线灭活.     

质粒pJP4水平转移介导生物膜系统强化降解2,4-D效应

以携带质粒pJP4[其上含编码2,4-二氯苯氧基乙酸(2,4-dichlorophenoxyacetic acid,2,4-D)降解功能的基因簇(tfd)]的基因工程菌Pseudomonas putida SM1443::gfp2x(pJP4::dsRed)为供体菌,以生物膜系统为对象,通过半连续流实验研究了质粒pJP4水平转移介导基因强化降解2,4-D效应,考察了目标基因在系统中存在状况及基因强化对系统菌群结构的影响.结果表明,以2,4-D(初始浓度为170 mg/L±10 mg/L)为唯一碳源,向生物膜系统加入携pJP4质粒的基因工程菌对2,4-D的降解具有促进作用,运行初期,促进作用较弱,随着半连续流反应的进行,促进作用显著增强,基因强化系统较对照系统对2,4-D的平均降解速率之差达13.3 mg/(L.h).通过对基因强化系统功能基因片段tfdB基因及报告基因gfp的跟踪检测,证实了在pJP4质粒介导下生物膜系统基因水平转移的发生.PCR-DGGE结果表明基因强化的生物膜系统较对照系统在受到2,4-D冲击条件下保持了相对更加稳定的菌群结构.