铬回收和生物接触氧化—混凝气浮工艺在制革废水处理中的应用

本文着重介绍制革废水处理中,经分隔治理,再采用生物接触氧化和气浮工艺的实际应用,运行效果良好。其中生化级采用生物接触氧化单元是新的尝试,为同类废水的处理积累了一定的经验。     

碳五加氢石油树脂化工废水的处理

本文介绍了应用新型曝气沉淀池-曝气生物滤池工艺处理碳五加氢石油树脂化工废水的工程实例。运行表明，通过调节水的pH值，改善铝的去除率。新型曝气沉淀池能有效地去除SS、CODCr、石油类和部分有机物，为后续好氧生物处理创造了一个良好的环境；新型挂膜方式的曝气生物滤池(BAF)工艺能稳定高效地去除SS、CODCr、硫化物、苯等，出水水质达到了国家一级排放标准.     

混凝沉降-生物膜法处理制革废水

采用混凝沉降-生物膜法处理蓝湿牛皮制革废水。工程实践证明:该法对废水COD和BOD的去除率可达94%以上,且对废水的脱色效果良好,是一种合理有效的处理皮革废水工艺路线。     

改性粉煤灰处理制革废水试验研究

本试验利用硫酸溶液对粉煤灰进行踟陛，研究了改性粉煤灰对制革废水的处理效果及其影响因素。试验结果表明，经酸处理后的改性粉煤灰对制革废水具有较好的处理效果。     

油田化学表面活性剂生物毒性评价研究

以常用的油田化学表面活性剂为研究目标,采用发光细菌法对其生物毒性进行了评价,考察了pH值和矿化度等对生物毒性的影响。结合表面活性剂对细菌中蛋白质含量变化情况,对表面活性剂的生物毒性效应进行进一步分析。实验结果表明：发光细菌法可以快速、简便地对油田化学剂的生物毒性进行评价,但对体系条件要求严格,pH值与矿化度对评价结果具有明显影响;发光细菌法得出的生物毒性评价结论不能简单的推演到其他毒性评价方法,单一的发光细菌法生物毒性评价标准无法全面判断油田化学剂的生物毒性效应,应结合多种评价方法对油田化学剂的毒性效应进行综合分析。     

高效生物处理技术在炼油厂碱渣废水处理中的应用

结合大港石化实际情况,在详细介绍柴油碱渣应用QBR高效生物处理技术取得成功的基础上,提出酸化回收粗酚或环烷酸并配套QBR、QBF等高效生物处理技术处理各种碱渣的新型工艺路线。经QBR处理后,出水COD去除率可达97%以上,石油类和挥发酚的去除率可达98%以上,硫化物去除率在99%以上。该技术的成功应用解决了困扰石化公司多年的碱渣废水处理的老大难问题,为炼厂碱渣废水乃至高浓度有机废水的处理开辟了一条新的途径。     

制革废水中Cr的一种快速简便测定方法

目前,测定水中铬的方法,基本上都适用于清洁水和一般的工业废水。而制革废水由于成分比较复杂,内含大量的有机质、硫化物、BOD_5、COD等,用现有的方法分析时,都不能得到满意的结果。本文在大量条件试验的基础上,对已有的方法进行了改进,提出了一个简便、快速、可行的测定方法。     

硫化物生物氧化脱硫技术研究现状

介绍了近年来国内外硫化物生物氧化为单质硫的各种脱硫技术.分析总结了硫化物生物氧化为单质硫工艺的各种影响因素,包括氧硫比、溶解氧浓度、硫化物浓度、化学氧化、微生物菌种、pH值、温度等因素.提出了生物氧化脱硫技术的发展前景.该技术将脱硫和单质硫的回收和为一体,是一种安全、低成本将含硫废液变废为宝的工艺技术.     

川东地区气田水处理技术及工程应用

针对川东地区气田水的性质和目前气田水处理工艺存在的问题,通过对不同水样进行室内蒸发及生物氧化实验,开发了蒸发-生物-臭氧以及氧化-生物-臭氧联合工艺技术。实验结果表明:经蒸发-生物-臭氧复合工艺以及氧化-生物-臭氧复合工艺处理后,川东地区气田水中主要指标CODCr、Cl-、硫化物以及石油类的去除率超过95%,出水指标达到GB 8978-1996《污水综合排放标准》一级排放要求;这两种处理工艺整体适应能力强,抗来水冲击负荷高,能高效处理气田水中污染物且出水稳定,有效实现了气田水的达标处置,实现资源化配置,符合国家环保政策,可实现较好的经济、社会和环境效益,对当前川东地区气田水处理有一定的参考价值。     

序批式活性污泥法在炼油化工废水处理中的应用

炼油化工废水处理的传统处理工艺中存在一定的弊端。为此,玉门炼油化工总厂对其废水处理设施进行了改建和扩建,其生物处理系统采用了序批式活性污泥法处理工艺。经过 3年运行的结果表明:该系统运行效果良好,处理后的水质可达到《GB8978-1996》(石化)一级排放标准的要求;化学需氧量(COD)和生化需氧量(BOD)分别降低78.6%和91.2%,硫化物去除率为98.2%,挥发酚去除率为99.6%。而且该反应器具有较强的耐冲击负荷能力,进水中COD在600 mg/L以下且有大幅度波动时,该系统仍可稳定地运行,处理后的水可达标排放。     

Use of constructed wetland systems with Arundo and Sarcocornia for polishing high salinity tannery wastewater

Treatment of tannery wastewater is problematic due to high and variable concentrations of complex pollutants often combined with high salinity levels. Two series of horizontal subsurface flow constructed wetlands (CWs) planted with Arundo donax and Sarcocornia fruticosa were set up after a conventional biological treatment system operating at a tannery site. The aim of the CWs was polishing organics and nitrogen from the high salinity effluent (2.2-6.6?g Cl(-)?L(-1)). Both plant species established and grew well in the CW. Arundo, however, had more vigorous growth and a higher capacity to take up nutrients. The CWs were efficient in removing COD and BOD(5) with removal efficiencies varying between 51 and 80% for COD (inlet: 68-425?mg?L(-1)) and between 53 and 90% for BOD(5) (inlet: 16-220?mg?L(-1)). Mass removal rates were up to 615?kg COD ha(-1)?d(-1) and 363 BOD(5) kg?ha(-1)?d(-1). Removal efficiencies were 40-93% for total P, 31-89% for NH(4)(+) and 41-90% for Total Kjeldahl Nitrogen. CW systems planted with salt tolerant plant species are a promising solution for polishing saline secondary effluent from the tannery industry to levels fulfilling the discharge standards.     

Assessing the application of an additive model to estimate toxicity of a complex effluent

A number of industries monitor levels of chemicals in their effluent, but few have undertaken prolonged biological monitoring of this wastewater. The focus of the present study was to determine whether past chemical data for effluent from a lead smelter could be used to estimate its past toxicity. Since the interactive effects of metals in effluents are often assumed to be additive, it was hypothesized that an additive model, 100/[sigma(metal concentration in effluent/EC50 for individual metal)], could be used to generate an EC50 from chemical data (where EC50 is the concentration of test material that affects 50% of the test organisms). To test the approach, a larval development toxicity test with the marine polychaete, Galeolaria caespitosa, was used to test 26 separate samples of effluent from a lead smelter, generating empirical EC50 values. EC50 values for each individual metal in the effluent were also generated using the larval development toxicity test. The concentrations of trace metals in each effluent sample were determined and, using the additive model, EC50 values were calculated. For the majority of effluent samples tested, the additive model underestimated toxicity, suggesting the presence of additional unidentified contaminants in the effluent samples. Additionally, a nonlinear rather than linear regression curve was found to best describe the relationship between the model and empirically derived EC50 values. This relationship was then used to estimate past trends in toxicity of the smelter effluent. Forty-eight percent of the variability in measured toxicity was explained by the model, with the model underestimating toxicity in the majority of samples.     

Biological treatment of synthetic wastewater containing 2,4 dichlorophenol (DCP) in an activated sludge unit

Chlorophenol compounds present in many chemical industry wastewaters are resistant to biological degradation because of the toxic effects of such compounds on microorganisms. Synthetic wastewater containing different concentrations of 2,4 dichlorophenol (DCP) was subjected to biological treatment in an activated sludge unit. Effects of feed DCP concentration on COD, DCP, and toxicity removals and on sludge volume index were investigated at a constant sludge age of 10 days and hydraulic residence time (HRT) of 25 h. The Resazurin method based on dehydrogenase activity was used for assessment of toxicity for the feed and effluent wastewater. Percent COD, DCP, and toxicity removals decreased and the effluent COD, DCP, and toxicity levels increased with increasing feed DCP concentrations above 150 mgl(-1) because of inhibitory effects of DCP. Biomass concentration in the aeration tank decreased and the sludge volume index (SVI) increased with feed DCP concentrations above 150 mgl(-1) resulting in lower COD and DCP removal rates. The system should be operated at feed DCP concentrations of less than 150 mgl(-1) in order to obtain high COD, DCP, and toxicity removals.     

硫化物恶臭脱除技术的发展

介绍了硫化物脱臭技术的现状,论述了生物脱臭技术及活性炭吸附技术的研究和进展。针对炼厂恶臭污染日益突出的特点,应用泥炭生物填料塔及活性炭吸附技术,对５０μＬ／Ｌ以下的Ｈ２Ｓ脱除工艺进行了研究。生物脱臭法采用经过驯化后的泥炭生物填料塔,Ｈ２Ｓ脱除率可接近１００％,负荷达到８５ｇＨ２Ｓ－Ｓ／（ｍ３干填料·ｈ）以上;活性炭吸附法采用日本的两种活性炭（ＩＶＰ和Ｃｅｎｔａｕｒ）,吸附容量分别达到１７０ｇ／Ｌ和８０ｇ／Ｌ以上。上述工艺均可应用于炼厂中低浓度硫化物恶臭污染的治理     

Merits of ozonation and catalytic ozonation pre-treatment in the algal treatment of pulp and paper mill effluents

Since the performance of algal treatment for pulp mill effluent decreases with increasing color intensity and AOX content, which mainly originate from the chlorine bleaching of Kraft pulp, the separated CEH bleaching effluent was pre-treated by both the conventional and the heterogeneous catalytic ozonation processes. An increase in the BOD(5)/COD ratio from 0.11 to 0.28 and 87% color abatement in terms of Pt-Co were achieved by catalytic ozonation, which had the best treatment performance. Biodegradability enhancement of the CEH effluent correlated well with a decrease in toxicity, high-molecular-weight-compound content, and AOX abatement. By the pre-treatment of the CEH bleaching effluent, the overall efficiencies of algal treatment of the combined pulp mill effluent in terms of the fractional removal of COD and color were increased from 76% and 53% to 86-90% and 96-99%, respectively. Effects of both the conventional and the catalytic ozonation pre-treatments on subsequent biological treatment were close to each other and they reduced the filling period of the Sequential Batch Reactor (SBR) cycle from 8 to 5 days.     

双滤料曝气生物滤池污水深度处理的研究

采用陶粒、沸石为滤料的曝气生物滤池对生物处理系统二级出水进行深度处理回用,研究了水力停留时间、气水体积比对污染物COD和NH3-N处理效果的影响。结果表明：水力停留时间为8 h,气水体积比为3∶1的工况下,处理效果较好。稳定运行后,出水COD、BOD5、SS、NH3-N、TP和色度平均值分别为15.6 mg/L、3.2 mg/L、8.5 mg/L、1.24 mg/L、0.40mg/L和8度,达到《城市污水再生利用—城市杂用水水质》（GB/T 18920-2002）标准,出水可用于道路清扫、绿化等。     

采油系统硫化氢治理技术探索

文章提出一种针对油田采油系统由于井筒原生和地面集输系统次生造成硫化氢污染的综合治理技术,研究形成了集输系统次生硫化氢外源微生物抑制硫酸盐还原菌技术,实现对次生硫化氢的生物抑制。该技术能使油井硫化氢降至5mg/m3,集输系统次生硫化氢降至25mg/m3以下,改善了原油集输系统作业场所工作环境,消除了硫化氢气体对人体危害的安全隐患。     

ACUTE RESIDUAL TOXICITY OF SEVERAL DISINFECTANTS IN DOMESTIC AND INDUSTRIAL WASTE WATER1

ABSTRACT: This study determined the acute toxicity of waste water disinfected with chlorine, bromine chloride, or ozone. The residual toxicity of effluent dechlorinated with sulfur dioxide was also tested. Toxicity tests were conducted with cyprinid, salmonid, and centrarchid fishes, as well as several species of fresh water macroinvertebrates. Residual chlorine exhibited the greatest toxicity of the disinfectants tested; dechlorination with sulfur dioxide effectively eliminated the toxicity of chlorinated effluent. Residual ozone produced mortality in test animals only under special conditions where subjects were exposed to effluent immediately after it was contacted with ozone, and chlorobrominated effluent was more toxic to salmonids than chlorinated effluent.