水解酸化对感光胶片废水生化反应动力学系数的影响

采用水解酸化工艺可有效地提高工业废水中难生物降解有机物的可生化性,为后续好氧生化处理创造有利条件。本试验在对感光胶片废水采用水解酸化－活性污泥法工艺和常规活性污泥法进行平行对照试验的基础上,从生化反应动力学系数的角度研究水解酸化过程对好氧生化反应的影响。研究结果表明：经水解酸化处理后,在该废水的ＢＯＤ５／ＣＯＤＣｒ比值从０４６－０４８提高至０５４－０５６的同时,后续活性污泥系统的动力学半速度数Ｋｓ从常规活性污泥法的４５９毫克／升下降至１０３毫克／升,最大比降解速度Ｋ从３０／日上升至５０／日,可用于表征该工业废水可生化性和后续好氧化物处理效果改善和提高的程度。     

两段水解—接触氧化工艺处理高浓度玉米淀粉废水的试验

采用两段水解－接触氧化工艺处理高浓度玉米淀粉废水,结果表明：此工艺的水解段具有提高废水可生化性的功能,整个工艺具有较强的抗负荷冲击能力。     

阳离子染料废水处理的工艺研究

首先采用两级物化－电解－吸附工艺对高浓度阳离子染料生产废水进行预处理,再与低浓度生产废水、生活污水混合生化处理,总脱色率和CODcr去除率均可达到99．9％以上,达标排放。     

染色废水处理方案设计

在生化＋物化处理染色废水的常用工艺中，增加兼氧和厌氧预处理，增强其可生化性，运行情况表明，对高浓度染色废水可使其稳定达到GB4287－92二级标准。     

电子厂打磨废水处理新技术的研究

电子厂磨废水含有较多的难降解的高分子打磨剂，废水可生化性极差。本文采用混凝土－缺氧－SBR工艺处理深圳某电子厂的打磨废水，原子CODcr在2000mg/L-4000mg/L之间，出水达到国家和广东省规定的一级排放标准，本研究成果为改造该类废水处理项目提供了科学依据和试验数据。     

生化法烟气脱硫技术综述

简述了SO2的来源及危害,综述了近年来烟气生化法脱硫的主要技术：烟道气脱硫的直接生物方法、间接生化方法、两步微生物脱硫法及生物化学法脱硫工艺,并介绍了其原理及应用现状,指出了主要优势技术各自存在的问题。对我国烟气生物脱硫技术的未来发展提出了建议。     

饼干厂生产废水治理

江门市达能饼厂总废水量为１５０ｍ＾３／ｄ,采取厌氧水解－接触氧化为主体的生化处理工艺,出水达到国家环保排放标准,因受地形限制采用埋地式设计,适应厂方用地要求,流程合理,整体工艺基本自动进行。     

硫化物对厌氧生化作用的影响及解救措施

本文介绍了厌氧生化的两个过程及其特征,分析了S~(2-)对厌氧生化的影响过程,重点研究了影响厌氧微生物活性环境中S~(2-)浓度,强调了环境中S~(2-)浓度与进水中S~(2-)浓度的区别。研究结果表明:厌氧生化过程中,S~(2-)的安全环境浓度为80mg/L,当环境中S~(2-)浓度大于80mg/L时,对厌氧生化有明显的抑制作用。将此研究结果在UASB反应器上进行了试验,取得了良好效果。同时,分析了S~(2-)使UASB反应器中污泥失活的过程,提出厌氧生化S~(2-)中毒的解救方法。     

浅谈废水生物处理的新进展

综述了生物脱氮除磷的反应机理和几种主要工艺,并做出了相应的分析评价,指出在废水生化处理中生物脱氮除磷因工艺简单、处理能力强、运行方式灵活等优点得到国内外的普遍高度重视,并成为当前重点研究的课题。     

共代谢在废水处理中的应用

共代谢是微生物特殊的代谢类型,可对废水中难降解有机物进行高效去除。本文探讨了共代谢的生化机制,详细论述了共代谢在生化机理和工艺方面的研究现状,同时对共代谢降解速率的影响因素作了分析,并针对实验室研究阶段,提出了共代谢在实际废水处理中存在的问题。     

Chemical industry wastewater treatment

Treatment of chemical industrial wastewater from building and construction chemicals factory and plastic shoes manufacturing factory was investigated. The two factories discharge their wastewater into the public sewerage network. The results showed the wastewater discharged from the building and construction chemicals factory was highly contaminated with organic compounds. The average values of chemical oxygen demand (COD) and biochemical oxygen demand (BOD) were 2912 and 150 mgO₂/l. Phenol concentration up to 0.3 mg/l was detected. Chemical treatment using lime aided with ferric chloride proved to be effective and produced an effluent characteristics in compliance with Egyptian permissible limits. With respect to the other factory, industrial wastewater was mixed with domestic wastewater in order to lower the organic load. The COD, BOD values after mixing reached 5239 and 2615 mgO₂/l. The average concentration of phenol was 0.5 mg/l. Biological treatment using activated sludge or rotating biological contactor (RBC) proved to be an effective treatment system in terms of producing an effluent characteristic within the permissible limits set by the law. Therefore, the characteristics of chemical industrial wastewater determine which treatment system to utilize. Based on laboratory results engineering design of each treatment system was developed and cost estimate prepared.     

涂装(前处理)废水处理工艺简介

概括总结了目前涂装(前处理)废水处理工艺,并对这些工艺进行了比较分析,并针对某厂家的涂装废水提出了可行可靠的处理工艺流程。最后提出几点建议来改善和优化涂装废水工艺。     

小叶榕落叶改性条件优化及其处理含Cu~(2+)废水动力学研究

以废弃的小叶榕落叶作为吸附剂,通过正交试验选择制备改性小叶榕落叶的最佳条件,结果表明:当硝酸浓度为10moL/L,干燥温度为120℃和氢氧化钠浓度为1moL/L时,改性后的小叶榕落叶的活性最强,对废水中Cu2+的吸附率最高。利用改性后的小叶榕落叶进行了吸附去除水中Cu2+的研究,得出当pH为5.7,铜的最大吸附容量Qmax=0.59mg(Cu)/g(改性落叶)。并通过非线性回归,构建了影响因素同吸附率之间的数学模型和落叶吸附的动力学模型。     

Treatment of IGCC power station effluents by physico-chemical and advanced oxidation processes

The aim of this work was to improve the quality of aqueous effluents coming from the Gasification Unit in an Integrated Gasification Combined Cycle (IGCC) Thermoelectric Power Station, with the purpose of fulfilling the future more demanding normative. To this end, an integral wastewater treatment including coagulation, flocculation, neutralization, photocatalytic oxidation, and ion-exchange has been studied. A final scheme has been proposed to remove pollutants. All the parameters of the treated wastewater are below pouring specifications. In the first stage, the wastewater was treated with CaCl2 (optimal dose=11 g CaCl2/g F-) as coagulant and a commercial anionic polyelectrolyte (optimal dose=0.02 g/g F-) as flocculant to remove fluoride ions (99%) and suspended solids (92%). The water was then neutralized, improving the degree of transmission of ultraviolet light, allowing the faster photo-degradation of pollutants. The photochemical study included different systems (H2O2, UV/H2O2, Fenton, Fenton-like, UV/Fenton, UV/Fenton-like and UV/H2O2/O2). In the Fenton-like system, the influence of two parameters (initial concentration of H2O2 and amount of Cu(II)) on the degradation of cyanide and formate (taken as the reference of the process) was studied. Experimental results were fit using neural networks (NNs). Results showed that the photocatalytic process was effective for total cyanide destruction after 60 min, while 180 min was needed to remove 80% of formates. However, a more simple system with UV/H2O2/O2 yields similar results and is preferred for industrial application due to fewer complications. Finally, an ion-exchange process with Amberlite IRA-420 was proposed to remove the excess of chlorides added as a consequence of the initial coagulation process.     

Closed wastewater cycle in a meat producing and processing industry

Creta Farm Plc, owns the largest meat producing (pigs rearing), processing and packaging unit in the island of Crete, in Greece, placed outside the city of Rethymnon in the north coast of the island. From the farm, where more than 20 000 pigs of various ages and sizes live, 300–320 m³ of wastewater are collected in a daily basis. From the slaughterhouse and the processing unit another 100–125 m³/d are produced. The wastewater treatment system is a combination of settling and aeration tanks, with decanters operating in different phases of the process, mainly for the removal of the solids from the wastewater. The average biochemical oxygen demand and total suspend solids values of the treated effluent are 40 and 80 mg/l, respectively. From this almost secondary treated effluent about 100 m³ are used for cleaning the sewage pipes of the rearing unit (animals houses). The remaining 300 m³ are disinfected with a weak chlorine solution before used for irrigating trees, grass and various other plants. More than 2000 eucalyptus trees, 1500 tamarix trees and a large number of olive trees are growing in the site creating a pleasant view and at the same time help minimising the odour problem.     

Application of 'waste' wood-shaving bottom ash for adsorption of azo reactive dye

The utilization of wood-shaving bottom ash (WBA) for the removal of Red Reactive 141 (RR141), an azo reactive dye, was investigated. WBA/H(2)O and WBA/H(2)SO(4) were made by treating WBA with water and 0.1M H(2)SO(4), respectively, to increase adsorption capacity. Adsorption of RR141 from reactive dye solution (RDS) and reactive dye wastewater (RDW) by WBA/H(2)O and WBA/H(2)SO(4) involved the BET surface area and pore size diameter. Properties of adsorbents, effect of contact time, initial pH of solution, dissolved metals and elution studies indicated that the decolorisation mechanism involved both chemical adsorption and precipitation with calcium ions. In addition, the WBA/H(2)SO(4) surface might contain sulphate-cation complexes that were specific to enhancing dye adsorption from RDW. The adsorption isotherm had a best fit by the Freundlich model. Freundlich parameters showed that WBA/H(2)O used more heterogeneous surface than WBA/H(2)SO(4) and activated carbon for RDW adsorption. A thermodynamic study indicated that RDW adsorption was an endothermic process. The maximum dye adsorption capacities of WBA/H(2)O, WBA/H(2)SO(4) and activated carbon obtained from a Langmuir model at 30 degrees C were 24.3, 29.9, and 41.5mgl(-1), respectively. In addition, WBA/H(2)O and WBA/H(2)SO(4) could reduce colour and high chemical oxygen demand (COD) of real textile wastewater. According to the difficulty in the elution study, it was an environmentally safe disposal of this waste. Therefore, WBA, a waste from combustion of wood shavings, was suitable to be used as an effective adsorbent for azo reactive dye removal.     

Nitrification in a vertically moving biofilm system

A laboratory continuous feed biofilm reactor, comprising a bulk fluid reactor, a biofilm plastic module, a feed tank, and pneumatic devices and controls, was operated for a total period of 257 days, including seeding time, to treat domestic-strength synthetic wastewater under increasing ammonium nitrogen (NH(4)(+)--N) loading rates, ranging from 0.17+/-0.01 (0.71+/-0.06 gm(-2)d(-1)) to 0.70+/-0.02 kgm(-3)d(-1) (2.9+/-0.1 gm(-2)d(-1)). The biofilm plastic module was moved vertically in and out of the wastewater in continuous cycles. The maximum NH(4)(+)-N removal rate was reached during the maximum loading phase, when a NH(4)(+)--N loading rate of 0.70+/-0.02 kgm(-3)d(-1) (2.9+/-0.1 gm(-2)d(-1)) was applied to the system. During this loading period, the average NH(4)(+)--N removal rate was 0.30+/-0.10 kgm(-3)d(-1) (1.30+/-0.40 gm(-2)d(-1)).     

Application of strategies for sanitation management in wastewater treatment plants in order to control/reduce greenhouse gas emissions

Greenhouse gases (GHG), basically methane (CH(4)), carbon dioxide (CO(2)) and nitrous oxide (N(2)O), occur at atmospheric concentrations of ppbv to ppmv under natural conditions. GHG have long mean lifetimes and are an important factor for the mean temperature of the Earth. However, increasing anthropogenic emissions could produce a scenario of progressive and cumulative effects over time, causing a potential "global climate change". Biological degradation of the organic matter present in wastewater is considered one of the anthropogenic sources of GHG. In this study, GHG emissions for the period 1990-2027 were estimated considering the sanitation process and the official domestic wastewater treatment startup schedule approved for the Metropolitan Region (MR) of Santiago, Chile. The methodology considers selected models proposed by the Intergovernmental Panel on Climate Change (IPCC) and some others published by different authors; these were modified according to national conditions and different sanitation and temporal scenarios. For the end of the modeled period (2027), results show emissions of about 65Tg CO(2) equiv./year (as global warming potential), which represent around 50% of national emissions. These values could be reduced if certain sanitation management strategies were introduced in the environmental management by the sanitation company in charge of wastewater treatment.     

活性污泥工艺中污水毒性研究的现状

活性污泥法是污水处理中应用最为广泛的技术之一,但目前国内外活性污泥工艺中污水毒性研究还很少。本文从目前活性污泥的工艺选择和污水回用的现状出发,对活性污泥工艺中污水毒性测试方法以及毒性研究的现状进行了综述,并对现存问题给出了分析和建议。     

Use of artificial neural network black-box modeling for the prediction of wastewater treatment plants performance

A reliable model for any wastewater treatment plant is essential in order to provide a tool for predicting its performance and to form a basis for controlling the operation of the process. This would minimize the operation costs and assess the stability of environmental balance. This process is complex and attains a high degree of nonlinearity due to the presence of bio-organic constituents that are difficult to model using mechanistic approaches. Predicting the plant operational parameters using conventional experimental techniques is also a time consuming step and is an obstacle in the way of efficient control of such processes. In this work, an artificial neural network (ANN) black-box modeling approach was used to acquire the knowledge base of a real wastewater plant and then used as a process model. The study signifies that the ANNs are capable of capturing the plant operation characteristics with a good degree of accuracy. A computer model is developed that incorporates the trained ANN plant model. The developed program is implemented and validated using plant-scale data obtained from a local wastewater treatment plant, namely the Doha West wastewater treatment plant (WWTP). It is used as a valuable performance assessment tool for plant operators and decision makers. The ANN model provided accurate predictions of the effluent stream, in terms of biological oxygen demand (BOD), chemical oxygen demand (COD) and total suspended solids (TSS) when using COD as an input in the crude supply stream. It can be said that the ANN predictions based on three crude supply inputs together, namely BOD, COD and TSS, resulted in better ANN predictions when using only one crude supply input. Graphical user interface representation of the ANN for the Doha West WWTP data is performed and presented.