超水深供气式射流曝气工程设计

以污水处理工程实例，介绍了超水深供气式射流曝气SBR法污水处理工艺的特点、处理效果和可靠性，对其脱氮效果进行了详细的分析。     

污水处理中影响微孔曝气充氧性能因素的研究

对污水处理中微孔曝气充氧性能影响因素的研究是一个复杂而又重要的问题。本文对污水水质、曝气器通气量、曝气池运行负荷和方式等几个主要因素对微孔曝气充氧性能的影响进行了研究探讨。鉴于曝气系统能耗在污水处理厂中所占比重较大，加强对该问题的研究，以降低处理厂能耗，有较好的经济意义。     

旋转曝气机能效限定值及能效等级标准解读

文章介绍了国内外污水处理用旋转曝气机的发展及现状,讲述了制定污水处理用旋转曝气机强制性能效标准的历史背景和依据原则,介绍了旋转式曝气机强制性能效标准的主要内容,旨在通过该标准的实施,普遍提高国产污水处理用旋转曝气机的能效,推动行业技术水平提高并持续发展。     

工业复杂污水综合处理技术研究与应用

普光天然气净化厂在运行中排出的大量污泥、检修中产生的大量成分复杂污水,是困扰下游污水处理的重大难题。文章进行了复杂污水存储技术研究,污水预处理技术研究,污水回收利用技术研究,泥水分离技术研究。文章优化污水存储方案,提升存储空间,解决了净化厂检修污水排放集中、排放量大的难题;组合PAC药剂加注+连续曝气污水预处理工艺技术,最大程度上降低了SBR池处理负担;使外排水满足循环冷却水补水水质要求,实现了外排水的有效回收利用;实现了泥水高效分离,极大降低了污泥处置和运输费用。     

关于新疆地区污水处理的建议

新疆地区气候条件和水资源环境较差,由于土地大面积开垦洗盐灌溉,使得地下水矿化度较高。当地能源也较紧张,经济发展和污水处理运行管理人员的技术水平相对落后。针对以上问题,建议在污水生物处理系统中,采用生物强化手段和地埋式构筑物,引入耐盐菌、耐温菌与其他有机物降解菌混合组成生态系统,实现污水生物处理系统的快速启动;采用曝气精确控制模式,基于进水污染物负荷和溶解氧、温度的相互关系,精确控制曝气,实现污水处理的稳定运行和节能降耗;采用远程感知服务平台,对污水站进行远程监控和服务,保证系统稳定运行,实现智慧水务管理目标。     

低温下SBR法处理生活污水工艺的优选研究

序批式活性污泥法是一种间歇式活性污泥法。该方法将污水处理的曝气及沉淀等单元操作工序在一个反应池中按时间顺序反复进行。在总结SBarg特征和运行控制基础上，为了探讨低温条件（10-15℃）下SBR工艺设计和运行参数的影响因素，实现低温条件下SBR法处理生活污水工艺条件的优选，在一个有效容积为5．5m^3的反应器内进行了试验研究。实验结果表明，当工况时间设置为厌氧3h、曝气8h、缺氧1．5h、闲置1．5h时，达到最佳运行工况。     

污水处理中精确曝气控制的研究进展

针对污水处理环节的曝气能耗问题,概述了污水处理的精确曝气控制现状,并结合我国目前我国实际情况与国内外现有研究结果,介绍了精确控制的重要组成部分之一的控制器的原理,控制器主要包括模糊控制器、神经网络控制器、支持向量机等,总结了各控制器的优缺点及适用情况,旨在加强对精确曝气控制的认识、为现有污水处理中存在的复杂、多变、时滞等特性提供利用精确控制器解决问题的的思路。     

国内外的潜水搅拌机和倒伞曝气机能效比较

本文对国内外污水处理设备中的潜水搅拌器（机）和倒伞曝气机在能耗和效率方面进行了对比，应用实践证明，国产污水处理设备的能效比远远优于引进及仿制的国外同类产品。     

制罐企业废水升级改造工程实例

介绍了国内某大型制罐企业的铝罐生产线废水和生活污水处理站升级改造的工程实例。改造内容主要是升级改造生化处理系统、曝气系统、污泥处理系统等;并对该升级改造工程进行了总结。     

污水处理行业温室气体核算模型开发及减排潜力分析

城镇污水处理行业是我国现代化进程中不可或缺的一部分,它承担着城镇污水处理和减排的重要作用,在运行过程中不可避免会产生大量的温室气体。本研究基于污水处理过程中的温室气体排放机理及排放因子法,构建了污水处理温室气体核算模型,并应用于国内典型的某厌氧—缺氧—好氧工艺的污水处理厂。研究结果表明,开发的模型能够有效识别出厌氧—缺氧—好氧工艺温室气体排放占比较高的环节,该环节为污水处理过程中电耗和污水处理过程中的甲烷排放,其在整个温室气体排放系统内占比高达93.09%。污水处理厂可以采取减小曝气量的措施使溶解氧达到2 ～ 3 mg/L,从而降低污水处理系统曝气电耗;另外,优化泵及鼓风机的运行,选用变频调速水泵等措施,可以降低污水提升环节能耗,达到温室气体间接减排的目的。污水处理厂还可以采取甲烷产能回收利用措施,将CH₄燃烧产生的能量作为污水处理系统内的能源供应,这样不仅可以有效减少污水处理厂的能耗,而且可以实现污水处理过程中温室气体排放减量化。     

曝气生物滤池在石化污水处理工程中的应用

曝气生物滤池可以用于石化污水的二段生化处理,是一种运行可靠、自动化程度高、出水水质好和抗冲击能力强的好氧生物处理新工艺。它与活性污泥法工艺相比,对于低基质污水二段生化工况,其有机物容积负荷高,污水停留时间短,其后不须设置二次沉淀池。与普通生物滤池相比,其占地面积小,不宜堵塞。与生物接触氧化方法相比,生物活性较高,处理效果好。曝气生物滤池集曝气池、二次沉淀池和滤池的功能于一身,其出水水质指标可以完全达到《污水综合排放标准》(GB8978-1996)一级标准。     

Biological treatment of wastewater in aeration tanks: Theoretical bases for process calculations

This article describes the method, based on the kinetics of enzyme reaction, for calculating treatment rates for wastewater effluents of varied concentrations in mixing aeration tanks and continuous flow aeration tanks. Using this method would make it possible to optimize the parameters of the biological treatment of wastewater. In addition, the authors illustrate that partitioning of the aeration space of the mixing aeration tank in a separate KU‐200 compact installation, which is intended for wastewater treatment from small sources, would make it possible to increase its efficiency by a factor of 1.8.     

溶解氧对好氧颗粒污泥影响的研究进展

好氧颗粒污泥技术是一种新颖废水处理技术。溶解氧(DO)是好氧颗粒污泥形成和稳定运行的一个重要参数。好氧颗粒污泥需要的曝气量大,能耗高。高曝气量带来的高DO浓度不利于氨氮通过SND去除。当DO扩散在颗粒内部受到限制时,颗粒中心形成的厌氧层不利于颗粒污泥的长期稳定运行。本文系统分析了DO浓度对好氧颗粒污泥影响的国内外研究现状,对好氧颗粒污泥中DO浓度这一重要参数的研究进行了总结。研究在低DO浓度下保持好氧颗粒污泥的稳定性有利于降低运行成本,采取合适的方法降低颗粒内部的扩散限制有利于增强颗粒的稳定性能。     

Operation strategy of a sequencing batch reactor for simultaneous removal of wastewater organic matter and nutrients

The Sequencing Batch Reactor (SBR) system employing activated sludge process is an alternative wastewater treatment technology. A cycle of the conventional SBR system generally consists of five periods, with complete aeration during the React period to oxidize the organic matter and nitrify the ammonium-nitrogen of wastewater. Laboratory-scale reactors were used to evaluate the feasibility of incorporating alternative aerobic-anoxic-aerobic stages within the React period for simultaneous removal of organic matter, N and P. Two cycles of SBR process per day were maintained.Under the operation strategy of 0.75-h fill, 8-h react (with continuous aeration), 3.25-h settle, draw and idle periods, the treatment performance became consistent after running the system for two to four cycles (1–2 days). The percentages of both BOD₅ and COD removal were around 94% from Cycle 2 onwards, the BOD₅ content dropped from initial 251 mg L⁻¹ to less than 14 mg L⁻¹ in the final effluent. A steady nitrification (about 97%) was obtained from Cycle 4 onwards, with 1 mg NH₄⁺-N L⁻¹ and 25 mg NO₃⁻-N L⁻¹ present in the final effluent. This suggested that the time required for SBR system to acclimate and reach an equilibrium state was relatively short when compared with the time needed for continuous flow activated sludge system. The findings also show that 4-h aeration during the react period was long enough to achieve more than 90% nitrification. With the incorporation of a 3-h anoxic stage after the initial 4-h aeration of the react period, a satisfactory denitrification process was observed, with nitrate level dropped from 27 to around 8 mg L⁻¹ within 3 h. The second aeration stage did not cause significant change in wastewater nitrogen content. The wastewater phosphate content declined rapidly during the initial 4-h aeration and P-release was not observed during the anoxic stage. A slight reduction of P was found in the second aeration stage suggesting that more P-uptake occurred in this stage. A 12-h cyclic SBR system with the incorporation of 4-h aerobic, 3-h anoxic and final 1-h aerobic stages into the 8-h react period was demonstrated to be able to remove C, N and P simultaneously.     

生物滤池—PE管微孔压滤技术治理中药废水

应用ＰＥ管微孔压滤技术，并辅以自然沉降、曝气、生物滤池等技术手段治理中药废水，出水达ＧＢ８９７８－８８中的一级排放标准，并回收了约７０％的水资源，文中的油污给ＰＥ管微孔压液技术带来的影响作了介绍。     

SBR中好氧颗粒污泥的培养

采用竖式SBR作为反应器，利用城市污水处理厂剩余污泥作为接种污泥，通过不间断运行培养出好氧颗粒污泥。实验结果表明，采用非限量曝气模式好氧颗粒污泥降解模拟污水的效果较好，其COD去除率可达98％以上。曝气量对好氧颗粒污泥的形成和稳定具有重要影响，当气速为26．5m／h时，好氧颗粒污泥的性状和处理有机废水效果最佳。同时好氧颗粒污泥对pH值的变化不明显，当pH为5—8范围内，其COD去除率都可达到85％以上。但是未经驯化的好氧颗粒污泥对对硝基苯酚和对氯苯酚两种芳香类有机物较敏感，而对硝基苯酚对其毒性更大。当对硝基苯酚和。对氯苯酚浓度为10mg／L时，其COD去除率仅为42．5％和52％。     

啤酒废水治理技术研究现状

啤酒废水具有水量大、污染物浓度高、易生物降解的特点。介绍了当前厌氧一好氧的组合工艺中UASB—SBR工艺、UASB—CASS工艺、EGSB一接触氧化工艺、USFB—AODT工艺、水解酸化-UASB—A／O工艺等主流工艺的原理和研究现状,以及射流曝气MBR5-艺、双极室联合工艺、光合细菌治理工艺等将来啤酒废水治理热点技术,并对啤酒废水治理技术的未来发展趋势进行了展望。     

EMMC process for combined removal of organics, nitrogen and an odor producing substance

In order to improve the process performance regarding the removal of organics, nitrogen, and an odor-causing compound (sulfide) contained in domestic wastewater, an entrapped-mixed-microbial cell (EMMC) with and without humic substances for both fixed and moving carrier reactors and conventional suspended growth culture (i.e. conventional activated sludge process) were investigated simultaneously. Both synthetic (simulated to the organics concentration of general domestic sewage) and actual domestic wastewater were investigated under operational conditions of 12 h of hydraulic retention time (HRT) with 1 h of aeration and 1 h of non-aeration, and 6 h of HRT with continuous aeration, at a room temperature of 25 +/- 2 degrees C. It was found that entrapping humic substances in the EMMC carriers had no impact on the removal of organics, nitrogen, and the odor-producing compound. Additionally, the performance of the EMMC moving carrier system for the removal of these pollutants is similar to that of the EMMC fixed carrier system. In general, the EMMC associated systems which provide high solids retention time achieve a better removal of chemical oxygen demand (COD), nitrogen, and the odor-producing substance than the suspended growth system for both HRTs of 6 h (continuous aeration) and 12 h (1 h of aeration and 1 h of non-aeration). Both the fixed and moving carrier EMMC processes, therefore, have the potential for improvement or replacement of the existing conventional activated sludge process with regard to improving the effluent qualities (such as COD, nitrogen and odor-producing compound) for reuse/disposal.     

石化企业污水生化处理改造措施分析

随着各炼油厂加工深度和加工能力的日益提高,排放的污水水量不断增加,水质不断恶化,原有的“老三套”中的曝气装置已无法满足生产需要。为此,不少炼油厂都针对各自的具体情况,对生化系统进行了技术改造,主要措施有：淘汰现有表曝池,改造现有表曝池,向表曝池中投加多孔物质或硝化反应与反硝化菌,增建生化预处理设施及将一级生化处理改为二级生化处理等。