氧化沟技术的特点及在新疆的应用前景

氧化沟是一种经济有效的污水处理技术，在诸多的污水处理技术中有着很好的竞争能力，在我区目前经济实力较弱，但又急需加强污水处理的情况下，不失为一种适合我区区情的污水处理技术，在我区有着广泛的应用前景。     

污水处理技术的新发展

概述了污水处理的各种技术，总结了国外污水处理技术的最新发展动态。     

全国小城镇污水处理技术（设备）交流与工程咨询研讨会四月召开

为宣传贯彻城市污水处理与污染防治的有关政策、标准，总结近年来城市污水处理技术及装备的经验成果，研讨我国小城镇污水处理厂建设技术与今后高新技术研发方向，促进科技创新与技术进步，国家环保总局定于２００３年４月１０日至１３日在广东省珠海市组织召开全国小城镇污水处理技术（设备）交流与工程咨询研讨会。该研讨会由中国环保产业协会水污染治理委员会和中国工程咨询协会环保专业委员会联合承办。会议内容：１．宣传贯彻小城镇污水处理相关法规、技术、经济政策及标准；２．研讨小城镇污水处理实用工艺、相关技术路线选择及重点发…     

含硫污水处理方法综述

本文参考国内外文献及技术资料，较全面地论述了各种含硫污水处理方法的优缺点，供从事油气田污水处理的同志参考。     

人工湿地污水处理技术在我国的发展研究

人工湿地作为近20年来发展起来的一种传统污水处理技术的一种廉价的替代方案，越来越受到世界各国的普遍重视。与传统的污水处理法相比具有基建、运行费用低，操作与维护简单等优点。这项技术适合我国国情，尤其适合广大农村、中小城市的污水处理。本文总结了人工湿地系统的研究现状，并对其未来的应用前景做出了展望。     

鄯善油田含油污水处理及回注技术

含油污水必须经过处理达到油田注水水质控制指标才能回注，为尽快将油田污水处理合格后回注地层，吐哈油田先后采用重力式污水处理流程，以及现在的诱导浮选——全自动双德料过滤等方法进行了现场含油污水处理技术的实践，处理后水质达到低渗透油田回注标准，并实施了回注。概述了都善油田污水处理系统试运行及技术改造的实践过程及效果。     

村镇污水处理传统工艺及一体化处理技术研究

探讨了传统A/O、A/A/O及改良式AAO工艺在村镇分散污水处理中的应用及一体化污水处理技术的发展进程,分析了传统工艺在城镇分散污水处理中的优缺点,阐述了一体化污水处理技术的发展,提出了一体化污水处理技术在低碳氮比村镇污水处理中的应用研究建议,为研发简便、可靠、高效、节能环保的一体化污水处理工艺提供参考。     

自然生物处理法在城镇废水治理中的应用

城市污水综合治理是消除污染,取得良好环境效益的一条有效途径。发展城市污水处理,要有切实可行的技术政策。污水治理应以城市污水处理为中心,工矿企业污水处理要服从城市污水处理的要求。对城市污水处理的技术政策,应该是根据各自的具体情况采取不同的技术措施。     

人工湿地处理污水技术在吉林省城市生态建设中的展望

人工湿地污水处理技术因其具有工艺简洁、投资少、运行管理方便、具有较好的经济、生态效益等优点，成为现今污水处理研究应用的一项新技术。结合吉林省省情，探讨了该技术在吉林省城市生态建设中应用的可行性，并指出了具体的发展方向。     

三相好氧生物流化床污水处理技术研究应用进展

阐述了三相好氧生物流化床污水处理技术的工艺特点和发展概况，介绍了三相好氧生物流化床在污水处理领域的研究及应用现状，并分析了其存在的问题和未来的发展方向。     

厌氧消化在纺织印染废水处理中的地位

纺织工业废水具有高浓度、高色度、高碱度、低BOD/COD比值的水质特性。近几年来对该污水采用了厌氧消化工艺,获得了良好的处理效果。本文对该污水处理系统工程中的厌氧消化技术进行小结和评价,从而确定了厌氧消化技术在纺织工业行业污水处理的地位。     

Electrocoagulation of blue reactive,red disperse and mixed dyes,and application in treating textile effluent

This study investigated the efficiency of electrocoagulation in removing color from synthetic and real textile wastewater. Two representative dye molecules were selected for the synthetic dye wastewater: a blue reactive dye (Reactive Blue 140) and a disperse dye (Disperse Red 1). The electrochemical technique showed satisfactory color removal efficiency and reliable performance in treating both individual and mixed dye types. The removal efficiency and energy consumption data showed that, for a given current density, iron was superior to aluminum in treating both the reactive dye and the disperse dye. With an initial dye concentration of 100 mg L^?1, the energy cost in achieving >95% color removal was on the order of 1 kWh m^?3 for both dyes. The effect of changing the initial pH of the samples on the removal efficiency and energy consumption was also studied. It was found that the design parameters used for the synthetic wastewater were less effective for treatment of real textile wastewater, with 1 in 5 tests on real wastewater failing.     

Removal of a red dye using noncommercial peroxidase extracted from rice bran

The present study investigates the application of a noncommercial peroxidase enzyme, which was extracted from rice bran, to decolorize wastewater that was simulating effluent from a textile manufacturer using a red dye in its coloration process.     

Regeneration of industrial district wastewater using a combination of Fenton process and ion exchange—A case study

Regeneration studies of wastewater effluent from an organized industrial district (OID) for possible reuse in textile industry as process water was investigated. Advanced treatment methods including Fenton process, polyaluminium chloride (PAC) coagulation and ion exchange were applied on OID effluent. In Fenton process removal efficiencies for suspended solids (SS), chemical oxygen demand (COD), SAC₄₃₆ (spectral absorption coefficient), SAC₅₂₅ and SAC₆₂₀ were determined 61%, 36%, 35%, 49% and 67%, respectively. After Fenton process, wastewater samples were coagulated with PAC. Optimum removal efficiencies for SS, COD, Fe ion, SAC₄₃₆, SAC₅₂₅ and SAC₆₂₀ were determined 83%, 18%, 93%, 32%, 36% and 58%, respectively. Ion exchange experiments were conducted on chemically coagulated wastewater samples to improve the quality of wastewater. Optimum dosage of resins was determined. The experiments revealed that 1:1 resin ratio (20 mL H-type resin:20 mL OH-type resin) gave the best removal rates for the parameters considered in this study. Study results indicated that quality of the wastewater was suitable for the process water characteristics of textile industry and unit wastewater treatment cost was determined as 2.54 €/m³.     

Effect of stocking density and food quality on the growth and fecundity of an epigeic earthworm (<Emphasis Type="Italic">Eisenia fetida</Emphasis>) during vermicomposting

Physico-chemical characteristics of the feed and optimum worm density are important parameters for the efficient working of a vermicomposting system. Overcrowding of worms can affect the efficiency of a vermicomposting system even if all other parameters have been optimized. This article reports the effect of stocking density and feed quality on the growth and fecundity of Eisenia fetida under laboratory conditions. The feed mixtures contained cow dung and textile mill wastewater sludge in different ratios. Three feed mixtures and five stocking rates (1, 2, 4, 8, and 12) were tested for 12 weeks. The results showed that E. fetida growth rate was faster at higher stocking densities; however, biomass gain per worm was faster at lower stocking densities. Sexual maturity was attained earlier at higher stocking densities. Growth rate was highest in 100% cow dung at all the stocking densities when compared to textile mill wastewater sludge containing feed mixtures. A worm population of 27–53 worms per kg of feed was found to be the most favorable stocking density.     

臭氧氧化法处理印染废水

本实验通过印染废水处理装置的建立,研究了臭氧处理印染废水的消耗量与废水ＣＯＤ值变化、废水色度去除率的关系,,以及不同ｐＨ值的印染废水和臭氧处理时间的关系。实验结果表明：经过处理后废水的ＣＯＤ却除率为３３９％,色度去除率为９９９％。     

Surface water and wastewater treatment using a new tannin-based coagulant. Pilot plant trials

A new tannin-based coagulant-flocculant (Tanfloc) was tested for water treatment at a pilot plant level. Four types of water sample were treated: surface water (collected from a river), and municipal, textile industry (simulated by a 100 mg L^?1 aqueous solution of an acid dye), and laundry (simulated by a 50 mg L^?1 aqueous solution of an anionic surfactant) wastewaters. The pilot plant process consisted of coagulation, sedimentation, and filtration. The experiments were carried out with an average coagulant dosage of 92.2 mg L^?1 (except in the case of the surface water for which the dosage was 2 mg L^?1). The efficacy of the water purification was notable in every case: total turbidity removal in the surface water and municipal wastewater, about 95% dye removal in the case of the textile industry wastewater, and about 80% surfactant removal in the laundry wastewater. Filtration improved the removal of suspended solids, both flocs and turbidity, and slightly improved the process as a whole. The efficiency of Tanfloc in these pilot studies was similar to or even better than that obtained in batch trials.     

Performance of an overland flow system for advanced treatment of wastewater plant effluent

Overland flow (OF) systems were evaluated and compared for advanced treatment of municipal and industrial effluents, including nutrients and nondegradable chemical oxygen demand (COD) removal. Three pilot plants were constructed at the Shahin Shahr Wastewater Treatment Plant (WWTP), Isfahan, Iran. Each pilot was assigned a specific wastewater and all were simultaneously operated for 8 months. Treatment of primary effluent, activated sludge secondary effluent, and lagoon effluent of textile wastewater was investigated at application rates (ARs) of 0.15, 0.25, and 0.35m(3)m(-1)h(-1). During 5 months of stable operation after a 3-month acclimation period, mean removals of total 5-day biochemical oxygen demand (TBOD(5)), total COD (TCOD), total suspended solids (TSS), total nitrogen (TN), total phosphorus (TP) and turbidity were 74.5%, 54.8%, 66.2%, 39.4%, 35.8%, and 67.7% for primary effluent; 52.9%, 52.9%, 66.5%, 44.4%, 39.8%, and 50.1% for activated sludge effluent; 65.7%, 58.7%, 70.3%, 41.7%, 41.3%, and 54.9% for textile wastewater lagoon effluent, respectively. The model of Smith and Schroeder, 1985. Field studies of the overland flow process for the treatment of raw and primary treated municipal wastewater. Journal of Water Pollution Control Federation 57, 785-794] was satisfactory for TBOD(5). For all treatment parameters a standard first-order removal model was inadequate to represent the data but a modified first-order model provided a satisfactory fit to the data. Based on the results of this study, it can be concluded that an OF system as advanced treatment had the ability to meet effluent discharge permit limits and was an economical replacement for stabilization ponds and mechanical treatment options.     

Some properties of a granular activated carbon-sequencing batch reactor (GAC-SBR) system for treatment of textile wastewater containing direct dyes

Resting (living) bio-sludge from a domestic wastewater treatment plant was used as an adsorbent of both direct dyes and organic matter in a sequencing batch reactor (SBR) system. The dye adsorption capacity of the bio-sludge was not increased by acclimatization with direct dyes. The adsorption of Direct Red 23 and Direct Blue 201 onto the bio-sludge was almost the same. The resting bio-sludge showed higher adsorption capacity than the autoclaved bio-sludge. The resting bio-sludge that was acclimatized with synthetic textile wastewater (STWW) without direct dyes showed the highest Direct Blue 201, COD, and BOD(5) removal capacities of 16.1+/-0.4, 453+/-7, and 293+/-9 mg/g of bio-sludge, respectively. After reuse, the dye adsorption ability of deteriorated bio-sludge was recovered by washing with 0.1% sodium dodecyl sulfate (SDS) solution. The direct dyes in the STWW were also easily removed by a GAC-SBR system. The dye removal efficiencies were higher than 80%, even when the system was operated under a high organic loading of 0.36kgBOD(5)/m(3)-d. The GAC-SBR system, however, showed a low direct dye removal efficiency of only 57+/-2.1% with raw textile wastewater (TWW) even though the system was operated with an organic loading of only 0.083kgBOD(5)/m(3)-d. The dyes, COD, BOD(5), and total kjeldalh nitrogen removal efficiencies increased up to 76.0+/-2.8%, 86.2+/-0.5%, 84.2+/-0.7%, and 68.2+/-2.1%, respectively, when 0.89 g/L glucose (organic loading of 0.17kgBOD(5)/m(3)-d) was supplemented into the TWW.