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。     

染料废水脱色的物理化学处理技术

染料废水目前主要的脱色方法有吸附、混凝、氧化还原和生化法.活性炭吸附适用于低浓度的染料废水处理.聚硅硫酸铁混凝效果与Fe/SiO4摩尔比和pH值相关.氢氧化镁可有效去除印染废水中的直接红染料.有机絮凝剂往往需要和其它药剂复配.氧化法脱色率大,但成本高昂,且受染料废水的组成、氧化性及pH值影响.还原法药剂价格低廉,但还原降解产物具有毒性,必须经过二次处理.生物法成本较低,又受制于染料的生物降解性.因此发展多种手段联合应用已是当前染料废水处理的研究方向.     

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。     

混凝法处理混合化工废水的试验研究

丁苯胶乳废水、SMA废水、苯丙基料废水和苯丙乳胶漆废水的浓度较高，毒性较大，可生化性低。采用混凝法进行预处理可去除其中大量有机物，从而极大降低废水的有机物浓度，并可提高废水的可生化性。本文重点讨论了不同参数条件对废水处理效果的影响，得出了最佳工艺路线。     

物化——生化工艺处理印染废水的研究

本文介绍了采用常用混凝剂对毛巾印染废水的脱色及有机物去除进行的试验探讨和混凝气浮工艺参数,并应用混凝气浮——生物转盘——气浮工艺处理毛巾印染废水取得了良好的处理效果。     

复合氧化混凝工艺处理印染废水的研究

本文介绍了复合氧化混凝法处理印染废水及其污泥资源化、减量化的研究。     

混凝处理皮革废水研究

利用混凝剂对皮革废水进行处理，包括综合废水、铬鞣液及加碱处理后铬鞣液。对三种无机混凝剂和十种有机混凝剂进行了初步筛选。结果表明，混凝处理对三种废水均有一定作用，最适用于综合废水，而铬鞣液直接混凝效果不佳。最佳混凝剂为PAM(分子量900x10^4—1200x10^4)40mg／L Al2(S04)3 1000mg／L，色度能完全去除，对SS、COD、Cr的去除率也较高。     

钻井固废渗滤液的处理研究

针对油气田钻井产生大量固体废物渗滤液的问题,利用化学混凝沉降+氧化还原法对固废渗滤液的处理进行了实验研究。实验结果表明:经过调整渗滤液pH值,加入聚合氯化铝铁及助凝剂PAM,进行絮凝沉降,再用芬顿试剂和氯酸钠氧化,可以处理高浓度废水,特别是对CODCr、色度等指标获得有效去除,达到GB8978-1996《污水综合排放标准》一级指标。     

染料废水物理化学处理技术的现状与进展

本文按吸附、膜滤、混凝、氧化刑、离子交换、Fenton试剂、光催化氧化、湿式氧化、电化学等方法分别论述了染料废水物理化学处理技术的现状和发展趋势。     

Fenton试剂-混凝法快速降解熄焦循环水中COD

以Fenton试剂氧化结合混凝法对焦化厂熄焦循环水COD进行快速去除实验,结果证明:当[Fe2+]/[H2O2]为1∶15,初始p H为3,30%H2O24.5 ml/100 ml废水时,反应90 min,COD去除率可达到90%,满足回用标准。但是,此时水的颜色较深,继续调节p H至7,加入Fe C13140 mg/L,PAM(聚丙烯酰胺)5 mg/L,搅拌5 min,静置30 min,COD去除率可达95.4%。Fenton-混凝对低浓度NH3-N几乎没有去除作用,CN-的去除率接近30%。整个处理过程中,有机物的种类和数量发生较大变化,Fenton氧化120 min后,混凝,污水基本接近无色,但仍含有单环芳香族化合物。     

高铁酸盐氧化絮凝去除含油污水中的油

油田产出的油、水经分离后会产生大量的含油污水,选用高铁酸钾对污水进行处理已成为人们关注的一个问题。用荧光比色法测定非均相固-液悬浮体系中油含量的实验证明:(1)高铁酸盐在含油污水中的初始反应速度快,可将大部分有机物氧化;(2)氧化法处理含油污水受多种因素的影响;(3)高铁直接氧化和芬顿氧化法均可比较彻底地处理油田含油污水。用高铁氧化法处理含油污水技术上很有发展前景,各种浓度的污水经处理后都可达到国家排放标准。     

On-line production of ferrate with an electrochemical method and its potential application for wastewater treatment – A review

A number of studies on the oxidation of various organic/inorganic contaminants by ferrate(VI) were reported in the 1980s and 1990s. The exploration of the use of ferrate(VI) for water and wastewater treatment has been well addressed recently. However, challenges have existed for the implementation of ferrate(VI) technology in practice due to the instability of a ferrate solution or high production cost of solid ferrate products. The research has been carried out aiming at the generation and application of ferrate(VI) in situ. This paper thus reviews ferrate chemistry and its overall performance as a water treatment chemical, discusses the factors affecting the ferrate yield efficiency using the electrochemical method, and finally, summarises the work on the production and use of ferrate in situ which is currently under study.     

高铁酸钾氧化去除弱碱性地下水中低浓度石油类污染物实验研究

研究一般地下水弱碱性水溶液中,高铁酸钾对低浓度石油烃类污染物的氧化去除率。采用0#柴油模拟石油类污染物试验水样,氧化反应在200mL烧杯中模拟完全混合状态完成。实验分析浓度分别为5.02mg/L、2.05mg/L、1.01mg/L和0.52mg/L 4个水样石油类污染物氧化去除率。实验研究显示,石油类污染浓度与高铁酸钾浓度分别按1∶1、1∶2和1∶3投加进行配比,最大氧化去除率97.51%,平均氧化去除率89.46%,氧化反应结束时间为25T。采用乙酸等效计算的导致溶液p H降低小分子有机酸累积量较小;在高铁酸钾过量条件下,石油类污染物氧化反应近似为一级反应。     

The application of potassium ferrate for sewage treatment

The comparative performance of potassium ferrate(VI), ferric sulphate and aluminium sulphate for the removal of turbidity, chemical oxygen demand (COD), colour (as Vis400-abs) and bacteria in sewage treatment was evaluated. For coagulation and disinfection of sewage, potassium ferrate(VI) can remove more organic contaminants, COD and bacteria in comparison with the other two coagulants for the same doses used. Also, potassium ferrate(VI) produces less sludge volume and removes more contaminants, which should make subsequent sludge treatment easier.     

秦皇岛港污水回用工程出水水质标准的制定

污水深度处理后回用不仅节约水资源,也减少了大量污染物的排放,是一项一举多得的益事。秦皇岛港污水深度处理回用工程利用城市二级处理的污水,经深度生物处理后用于煤炭除尘,解决了除尘水源紧张的局面。本文就如何确定回用工程的出水水质指标及其标准进行了讨论,阐述了制定出水水质标准的基本原则。     

CT4-35钻井废水处理剂的研制及应用

CT-35是一种高效的钻井废水处理剂，与其它常用药剂相比，该混凝剂对处理高浓度钻井废水特别是处理难度很大的磺化类废水有明显的优势。介绍了CT4-35研制、生产工艺，用它处理现场钻井废水的情况。现场使用表明：利用CT4-35处理钻井废水，COD的去除率可达85％以上，浊度去除率为100％，处理后出水呈中性（PH6～8），色度小于原水样的1／10，出水清澈透明，并且产生的污泥量少。通过对处理前、后出水的水质分析，证明其中无药剂残留。     

Application of low-cost adsorbents for dye removal – A review

Dyes are an important class of pollutants, and can even be identified by the human eye. Disposal of dyes in precious water resources must be avoided, however, and for that various treatment technologies are in use. Among various methods adsorption occupies a prominent place in dye removal. The growing demand for efficient and low-cost treatment methods and the importance of adsorption has given rise to low-cost alternative adsorbents (LCAs). This review highlights and provides an overview of these LCAs comprising natural, industrial as well as synthetic materials/wastes and their application for dyes removal. In addition, various other methods used for dye removal from water and wastewater are also complied in brief. From a comprehensive literature review, it was found that some LCAs, in addition to having wide availability, have fast kinetics and appreciable adsorption capacities too. Advantages and disadvantages of adsorbents, favourable conditions for particular adsorbate–adsorbent systems, and adsorption capacities of various low-cost adsorbents and commercial activated carbons as available in the literature are presented. Conclusions have been drawn from the literature reviewed, and suggestions for future research are proposed.     

篦齿眼子菜对废水中氮和磷的去除行为研究

一些常见的沉水草本植物对水质具有较强的净化作用,能够有效控制氮和磷的浓度。本试验通过模拟氮、磷污染的水质条件,采用篦齿眼子菜对氮、磷营养盐的吸附和去除效果进行研究。结果表明:设定模拟废水中的初始总氮(TN)浓度在1~50 mg/L范围内,培养30天后的植株对总氮的去除率最高可达85.4%,随着初始培养环境中总氮浓度的增加,去除效率呈下降的趋势;模拟废水水体中的总磷浓度范围为0.2~10.0 mg/L时,对总磷(TP)去除效率最高为78.3%。使用蓖齿眼子菜对实际的废水进行氮、磷营养盐的去除处理,效果较好。由此可见,水生植物富集废水中高浓度营养盐的能力具有较大的应用前景,本研究可为蓖齿眼子菜应用于废水预处理工艺提供可靠的理论支持。     

高压电化学絮凝技术去除酿酒废水中总磷的研究

为了使酿酒废水中总磷有效去除并达标排放,通过对酿酒废水总磷的排放情况调查,有针对性的选用高压电化学絮凝技术,对酿酒废水中总磷的去除效果进行实验研究。从实验结果看,调节进水pH值为2.3、停留时间45分钟时总磷去除率可达到99%以上,在该条件下COD的去除率也能达到50%左右,废水总磷排放浓度能够达到1.0mg/L的排放要求。     

Nitrous oxide emissions from wastewater treatment and water reclamation plants in southern California

Nitrous oxide (N?O) is a long-lived and potent greenhouse gas produced during microbial nitrification and denitrification. In developed countries, centralized water reclamation plants often use these processes for N removal before effluent is used for irrigation or discharged to surface water, thus making this treatment a potentially large source of N?O in urban areas. In the arid but densely populated southwestern United States, water reclamation for irrigation is an important alternative to long-distance water importation. We measured N?O concentrations and fluxes from several wastewater treatment processes in urban southern California. We found that N removal during water reclamation may lead to in situ N?O emission rates that are three or more times greater than traditional treatment processes (C oxidation only). In the water reclamation plants tested, N?O production was a greater percentage of total N removed (1.2%) than traditional treatment processes (C oxidation only) (0.4%). We also measured stable isotope ratios (δN and δO) of emitted N?O and found distinct δN signatures of N?O from denitrification (0.0 ± 4.0 ‰) and nitrification reactors (-24.5 ± 2.2 ‰), respectively. These isotope data confirm that both nitrification and denitrification contribute to N?O emissions within the same treatment plant. Our estimates indicate that N?O emissions from biological N removal for water reclamation may be several orders of magnitude greater than N?O emissions from agricultural activities in highly urbanized southern California. Our results suggest that wastewater treatment that includes biological nitrogen removal can significantly increase urban N?O emissions.