腈纶纱染色的废水预处理工程实例

为使腈纶纱染色废水达到接管标准的要求,采用水解-塔式生物滤池和混凝沉淀工艺,对腈纶纱染色的废水预处理工程进行设计。经工程运行表明,原水COD≤1600mg／L时,适当增大回流量,水解-塔式生物滤池对COD的去除率可达57％;再经混凝沉淀,COD的去除率可达45％,出水COD〈380mg／L,满足了接管要求,而色度、SS远低于接管要求。     

微波-Fenton氧化-PAFSi絮凝法处理含油废水

采用微波-Fenton氧化-PAFSi絮凝法处理含油废水,结果表明,200mL水样先经微波辐射6rnin,在pH=2,H2O2（30％）3．5g／L,Fe2＋ 1．3g／L的条件下氧化4h后,采用聚硅酸铝铁（Al：Fe：Si=10：2：1）和聚丙烯酰胺在pH：8时进行絮凝实验,处理后废水浊度、SS、COD、含油量和色度分别降低了99．46％、96．66％、91．94％、97．97％和95．00％,且经处理后废水的BOD5／COD由原水的0．04提高到0．53。实验还分析了含油废水的降解机理。     

道路径流SS和COD污染特征及出流规律

选择芜湖市火车站点进行长期监测,采集降雨7次;同时选择5个不同功能区,采集典型降雨1次。探讨了道路径流中总固体悬浮物(SS)和化学需氧量(COD)的污染特征、影响因素及出流规律,结果表明,7次降雨事件SS和COD平均值范围分别为198～1 529 mg/L和66～367 mg/L。SS和COD污染较为严重。SS在不同功能区中大小顺序为:工业区>居民区>商业区>交通区>文教区,总COD大小顺序为:工业区>交通区>居民区>商业区>文教区,溶解态COD大小顺序为:工业区>交通区>商业区>文教区>居民区,颗粒态COD大小顺序为:工业区>居民区>交通区>文教区>商业区。工业活动对地表径流SS和COD含量影响最大。SS受降雨历时影响较大,溶解态COD受平均雨强影响较大,颗粒态COD受最大雨强影响较大。不同降雨强度下,SS、溶解态COD及颗粒态COD的出流规律不同,降雨强度对径流初期效应的影响显著。     

用于高校优质中水原位处理的设备研究

为了提高高校优质中水的处理与回用率,提出了适用于高校优质中水的处理与回用系统,设计了中水原位处理设备,并进行了试验验证.结果表明,沉淀-SOBMR-过滤设备能够实现无动力、自动化运行,尤其适合于盥洗和洗浴废水的处理.沉淀单元对盥洗废水COD和SS去除率分别为23.8%和55.7%;SOBMR单元对盥洗废水COD和SS去除率分别为35.8%和27.9%;过滤单元能有效去除废水中绝大部分SS,且能耐受SS冲击负荷,对废水COD去除率先增后降,受水力负荷的影响,负荷越小,处理效果越好.整个系统出水水质满足杂用水对COD、SS和色度等要求,可用于冲厕和杂用.每套处理装置可节约水资源151.2 m3/a,设备投资回收期为2.01年,具有巨大的经济效益.     

电絮凝处理煤层气产出水

采用电絮凝法处理煤层气产出水,通过铁和铝2种电极材料的处理效果的比较,选择铝电极进行实验,研究了电极间距、原水pH值以及电流密度等因素对电絮凝处理效果的影响。实验结果表明,电絮凝法对煤层气产出水的化学需氧量(COD)和固体悬浮物(SS)具有良好的去除效果,原水pH接近中性时处理效果较好,电絮凝处理过程中不需添加可溶性盐和改变pH值。实验中确定的电絮凝处理条件为:电极间距1 cm,电流密度30 A/m2,反应10 min后,出水的COD、SS分别为9.6 mg/L和8.5 mg/L,去除率分别达到75.1%和88.8%,出水pH为7.8,电能消耗为1.75 kWh/m3。     

铁炭微电解法预处理超高盐榨菜腌制废水

超高盐榨菜腌制废水是高盐、高氮磷及高有机物废水,目前常采用生物方法进行处理,但因高污染物浓度及高盐度影响,处理效果不够理想;因此,选用铁炭微电解法对超高盐榨菜腌制废水进行预处理。通过静态烧杯实验,研究了反应时间、初始pH、铁炭体积比和铁水体积比对COD和氨氮去除率的影响。单因素实验的最佳处理条件：原水pH4～4．5,反应时间为30min,铁炭体积比为1：1,铁水体积比为2：1,出水COD和氨氮的去除率分别为57．29％和53．11％,盐度由原水的6．62％下降为3．63％,去除率达45．17％,pH由原水4．01升高为6．38。正交实验结果表明,影响COD和氨氮去除率的因素从大到小的顺序为：铁水体积比、初始pH、反应时间、铁炭体积比。实验表明,采用铁炭微电解法能够对超高盐榨菜腌制废水中的COD和氨氮进行有效去除,出水的pH升高和盐度下降,能满足后续生物处理的预处理要求。     

Fe/C内电解法处理二硝基重氮酚废水实验研究

采用Fe/C内电解法处理DDNP废水,研究了该方法在酸性和碱性条件下对DDNP废水的处理效果,并考察了pH值、反应时间及铁碳比对处理效果的影响。结果表明:Fe/C内电解法可有效去除DDNP废水中由硝基苯类物质引起的COD、S2-、SS和色度,在最佳酸性实验条件下,COD、S2-、SS和色度的去除率分别为85.65%、91.6%、100%和99.63%。在最佳碱性实验条件下,COD、S2-、SS和色度的去除率分别为90.13%、99.73%、100%和99.63%。     

厌氧-好氧工艺处理制药废水的中试研究

将由厌氧折流板反应器(ABR)、移动床生物膜反应器(MBBR)和膜生物反应器(MBR)组合而成的厌氧-好氧工艺用于处理制药废水的中试研究.试验结果表明,当原水SS平均值为1000 mg/L,COD为10 000 mg/L,NH3-N为500 mg/L时,出水浊度、COD和NH3-N分别为3 NTU、500 mg/L以及10 mg/L以下,去除率分别为98%、95%和98%以上.     

活性炭三维电极法处理超高盐榨菜腌制废水

将粒状活性炭作为三维电极的粒子电极处理超高盐榨菜腌制废水。采用静态实验,对比了二维电极与三维电极对该废水COD和磷酸盐的去除效果,考察了三维电极条件下极板间距、活性炭填充量、电解时间、电解电流及初始pH等对该废水COD和磷酸盐去除率的影响。结果表明：三维电极对超高盐榨菜腌制废水COD和磷酸盐的去除率明显高于二维电极;在原水pH（4．3—5．0）,废水体积600mL,电流8A,活性炭填充量250g,极板间距6．5cm,电解时间150min时,处理效果良好,COD和磷酸盐去除率分别为76．47％和97．81％。由波长扫描图可初步认为部分有机物直接被氧化为二氧化碳。     

Fenton-混凝法处理苯胺废水

农药生产过程中产生的苯胺废水,COD浓度高、生物毒性强、可生化性差,一般生化方法很难处理。研究了Fenton与PAC联用处理苯胺废水。结果表明,Fenton氧化处理苯胺废水在最佳条件为pH=6、m（H2O2）/m（COD）=1.8、n（H2O2）/n（Fe2＋）=8时,COD和色度去除率分别为78.4%和92.3%。Fenton氧化后废水B/C值由0.037提高到0.324。最佳条件下联用PAC,在投加量为320 mg/L时COD与色度去除率分别为83.6%和94.8%,并且处理时间显著缩短,实际应用中可减少水力停留时间和构筑物体积。     

城市污水厂水质相关性及分布状态的研究和应用

采用统计学及质量控制的一些基本理论及方法对污水处理厂的运行数据进行分析,得出城市污水处理厂BOD5、COD、SS、TN、TP等主要出水指标呈正态分布的规律;城市污水BOD5、COD、TN、TP等指标间存在显著线性相关性的结论.研究结论可用于污水处理厂制定经济合理的出水监测方案以及对污水处理厂运行可靠性等进行评估.     

城市污水厂水质相关性及分布状态的研究和应用

采用统计学及质量控制的一些基本理论及方法对污水处理厂的运行数据进行分析,得出城市污水处理厂BOD5、COD、SS、TN、TP等主要出水指标呈正态分布的规律;城市污水BOD5、COD、TN、TP等指标间存在显著线性相关性的结论.研究结论可用于污水处理厂制定经济合理的出水监测方案以及对污水处理厂运行可靠性等进行评估.     

An approach to wastewater treatment in organised industrial districts: a pilot-scale example from Turkey

In this study, a detailed wastewater profile and treatability studies of Demirtas Organized Industrial District (OID) were undertaken on a pilot-scale. The industrial categorisation of Demirtas OID was determined, and the wastewater characterisations of each industrial sector were analysed and the flow-rates were measured. The results were used to design a wastewater treatment plant for Demirtas OID. Pilot-scale chemical and biological treatability studies were carried out. The steady-state performance of the pilot-scale treatment system in removing chemical oxygen demand (COD) and suspended solids (SS) was studied for a period of three months. The removal efficiencies obtained in this study were 42% of COD and 67% of SS in the chemical treatment, and 84% of COD and 25% of SS in the biological treatment. The overall removal efficiency of the pilot-scale system was 91% COD and 75% SS. The pilot-scale study showed that the wastewater from Demirtas OID could be treated with biological and chemical methods, and the treated wastewater met the Regulation of Discharge Standards of Turkey. The significance of this study is that it is the first such system in Turkey to be tested on a pilot scale.     

Application of a constructed wetland for industrial wastewater treatment: a pilot-scale study

The main objective of this study was to examine the efficacy and capacity of using constructed wetlands on industrial pollutant removal. Four parallel pilot-scale modified free water surface (FWS) constructed wetland systems [dimension for each system: 4-m (L)x1-m (W)x1-m (D)] were installed inside an industrial park for conducting the proposed treatability study. The averaged influent contains approximately 170 mg l(-1) chemical oxygen demand (COD), 80 mg l(-1) biochemical oxygen demand (BOD), 90 mg l(-1) suspend solid (SS), and 32 mg l(-1) NH(3)-N. In the plant-selection study, four different wetland plant species including floating plants [Pistia stratiotes L. (P. stratiotes) and Ipomoea aquatica (I. aquatica)] and emergent plants [Phragmites communis L. (P. communis) and Typha orientalis Presl. (T. orientalis)] were evaluated. Results show that only the emergent plant (P. communis) could survive and reproduce with a continuous feed of 0.4m(3)d(-1) of the raw wastewater. Thus, P. communis was used in the subsequent treatment study. Two different control parameters including hydraulic retention time (HRT) (3, 5, and 7d) and media [vesicles ceramic bioballs and small gravels, 1cm in diameter] were examined in the treatment study. Results indicate that the system with a 5-d HRT (feed rate of 0.4m(3)d(-1)) and vesicles ceramic bioballs as the media had the acceptable and optimal pollutant removal efficiency. If operated under conditions of the above parameters, the pilot-plant wetland system can achieve removal of 61% COD, 89% BOD, 81% SS, 35% TP, and 56% NH(3)-N. The treated wastewater meets the current industrial wastewater discharge standards in Taiwan.     

Analysis of chemical compositions contributable to chemical oxygen demand (COD) of oilfield produced water

This work was to give a comprehensive estimation for the chemical compositions contributable to COD of the produced water treatment system. For this purpose, the wastewater samples were collected from an onshore wastewater treatment plant. The chemical compositions of the wastewater were investigated, and the COD contributed by each component was estimated. The results showed that the COD levels of O&G and SS presented decreasing trends during the whole process and achieved total removal percentages of 95.1% and 62.3%, respectively. The final COD of organic acids and low-molecular-weight carbonyl compounds were respectively lowered to nearly 64% and 35% of their initial levels, and no regular trends were found for the COD of these chemicals during the whole treatment process. The COD of inorganic components presented minor variations at all sampling spots. The majority of COD was originated from O&G in raw wastewater. The COD contributed by O&G decreased greatly with continuous treatment and finally was lower than 17% of measured COD. At each sampling spot, the ratios of COD contributed by SS did not exceed 7.6% of measured COD. Other measured chemicals, including organic acids, carbonyl compounds, volatile phenols, reductive anions, metals and TDP were not the main sources of COD during the whole treatment process, and the ratio of COD was below 9% at each sampling spot. Most of the soluble components contributable to residual COD were still unknown after biological treatment, and the COD contributed by these components was greater than 57% of measured COD.     

高盐工业废水人工湿地处理中植物的筛选

通过人工湿地中试实验,考察了芦苇、睡莲、水葱、狭叶香蒲和宽叶香蒲水生植物单元对经生化处理的石油和精细化工工业区的工业废水中盐含量较高、氮磷营养盐含量较低和化学需氧量(COD)含量较高的废水中污染物的去除情况,研究了在植物不同生长阶段系统中COD的去除同盐度之间的关系,探讨了盐度差异对植物生长状况的影响,为确定人工湿地适合的进水盐度,达到有效去除高含盐量工业废水中有机污染物提供依据。结果表明,芦苇、睡莲和狭叶香蒲3种植物单元内高含盐量工业废水中污染物的净化效果较水葱和宽叶香蒲单元的净化效果好:前3种植物单元内COD、生化需氧量(BOD)和总磷(TP)的去除率大约在38%、55%和62%左右,而水葱和宽叶香蒲2种植物单元内COD、BOD和TP的去除率大约在30%、36%和52%左右;系统中各个单元内总氮(TN)去除率都在85%以上。在植物的不同生长阶段,人工湿地系统中氯离子浓度与COD浓度之间的相关性存在差异:植物生长初期,系统中氯离子浓度与系统中COD浓度之间无显著相关性,而在植物生长旺期和末期,两者则成正相关关系。因此,需根据植物的生长阶段调整人工湿地的进水盐度。     

废水COD 4种物化表征方法的比较与评估

为了确定废水COD组分表征的物化分析方法,对0.1μm滤膜过滤、0.45μm滤膜过滤、絮凝和絮凝+0.45μm滤膜过滤4种方法进行了实验比较和评估。结果表明:某些材料的滤膜会因"COD溶出"而影响表征结果;4种方法分离废水的重现性都很好,相互没有明显区别;物化分离对废水快速可生物降解COD(SS)没有影响,但4种方法得到的处理液中可生物降解COD仍含降解速率明显不同的组分,其中SS仅占35%～45%。因此,物化方法不能合理表征SS;絮凝+0.45μm滤膜过滤速度快、干扰少、分离机理与活性污泥系统类似,更适用于废水溶解性惰性COD组分(SI)表征。     

废纸造纸废水处理工程应用

报道了自制混凝剂产品处理废纸造纸废水的工程应用情况。经过 1年多的运行结果表明 ,当进水CODCr、悬浮物浓度分别为 972mg/L、82 5mg/L以及色度为 3 0 0倍时 ,采用该工艺处理后 ,CODCr去除率平均为 95 .7% ,SS去除率平均为 98.9% ,色度去除率平均为 99.3 % ,出水水质远低于国家一级排放标准 (GB3 5 44 - 92 ) ,并且工厂实践表明 ,对生产有显著的效益 ,从而证明该方法对于废纸造纸废水的处理是可行的。该处理工艺设备简单 ,系统运行稳定 ,操作方便 ,成本低