厌氧浮动生物膜反应器处理高浓度有机废水

本文探讨了厌氧浮动生物膜反应器、处理高浓度有机废水的研究。试验结果表明，在温度２０℃￣２８℃，容积负荷为５．３８￣２０．６２ｋｇＣＯＤ／ｍ＾３·ｄ，水力停留时间２３．４ｈ，ＣＯＤ去除率在９０％以上，反应器内污泥持留量高，抗冲击负荷能力强。微生物既有附着生长系统，也有大量悬浮颗粒污泥，生物膜中与颗粒污泥中的生物相有明显差异。     

流化催化裂化中DeSOx催化剂的研究

用共沉淀法合成了三个系列的ＤｅＳＯｘ催化剂：铜类催化剂、铈类催化剂、铜铈类催化剂。模拟流化催化裂化（ＦＣＣ）条件，分别考察了催化剂的组成、水热处理、反应温度、体系中氧气浓度为ＳＯｘ吸附容量的影响，研究了催化剂吸附ＳＯｘ后的再生性能，同时将合成催化剂与工业催化剂（ＩＮＴＥＲＣＡＴ公司的ＤｅＳＯｘ催化剂）的ＤｅＳＯｘ性能进行了比较。结果表明，随 反应温度５的升高，催化剂的ＳＯｘ吸附容量出现一极大值；水     

缺氧━好氧固定床生物膜系统处理焦化废水的试验研究

采用内填弹性立体填料的缺氧━好氧固定床生物膜系统处理焦化废水，试验效果良好。当总水力停留时间≥３５．２ｈ，ＣＯＤ和ＮＨ＿３─Ｎ的去除率分别这８２％和９６％以上，出水浓度均达到国家排放标准。     

不同形态铝对小麦抗氧化系统的影响

研究了铝在不同ｐＨ条件下的形态分布,测定了单核铝和多核铝对小麦根中超氧化物歧化酶(ＳＯＤ)和过氧化物酶(ＰＯＤ)活性的影响．结果表明,低浓度Ａｌａ和Ａｌｂ激发了小麦根ＳＯＤ活性;ＰＯＤ活性在ｐＨ≤５．０时被显著激活,而当 ｐＨ≥５,５,Ａｌａ与Ａｌｂ浓度较低时ＰＤＤ被显著地抑制;ＳＯＤ与ＰＯＤ活性均在ｐＨ４．５,７５μｍｏｌ·ｌ－１[Ａｌ]时达到本实验最高值,与Ａｌｂ浓度的增加相关．本实验结果显示两种形态的铝对植物的致毒机理可能存在一定差异．     

磁粉活性污泥法工艺技术研究

磁粉活性污泥法（ＦＰＡＳ）是在活性污泥中投加适量磁性粉末的生物处理工艺。通过与普通活性污泥法平行试验比较，去除ＣＯＤｃｒ和氨氮的效率及承受毒物的浓度都不同程度优于普通活性污泥法；明显改善活性污泥絮体结构和沉降性能，克服污泥膨胀；大幅度提高曝气池中活性污泥浓度，从而增大单位容积的处理能力；使设备小型化，节省投资。     

用总有机碳浓度表达活性污泥反应动力学的研究

本研究对废水活性污泥法处理中常用指标ＣＯＤ、ＢＯＤ５、ＭＬＶＳＳ与总有机磷指标的相关性进行了探讨。     

美达棉纤维挂载生物膜法处理石化废水中油

本文介绍了利用美达棉纤维持载生物摸法处理石化废水中油的试验结果。当废水在柱内停留时间为６．３ｈ，废水中油的处理效果是令人满意的。在同一含停留时间下入流水的ＣＯＤｃｒ从４２０ｍｇ／Ｌ变到１８３２ｍｇ／Ｌ时，出流水的ＣＯＤｃｒ在１６８．５ｍｇ／Ｌ以下。     

大红色基G生产中的废酸资源回收

大红色基Ｇ生产中产生的废硫酸内含硫酸达５０％，ＣＯＤ７０ｇ／Ｌ，难用常规的方法来处理。本文给出了用该废酸生产硫酸锌进而生产立德粉的方法，并用ＣＯＤ浓度作为硫酸锌质量的控制指标，氧化锌和了废硫酸后，有机会物从溶液中析了，ＣＯＤ的去除率达９９％。残存的有机物用活性炭吸附法除去。控制ＺｎＳＯ４溶液中ＣＯＤ≤６０ｍｇ／Ｌ，可制得合格的Ｂ３０１立德粉。有杉本法使硫酸资源全部回收并且无废水排放。     

高浓度洗毛废水生物降解的研究

根据高浓度洗毛废水的水质特性,选择、驯化出高效污泥和菌株,并对生物降解该废水时的工艺、污泥量、时间三要素进行了深入的研究．结果表明,对于物化处理彻底的废水, Ｈ／ Ｏ 工艺（ 水解／ 好氧工艺） 与好氧工艺处理差异不大;７０ ％ 左右物化效果时, Ｈ／ Ｏ 工艺处理时, Ｃ Ｏ Ｄｃｒ 去除率增加;废水在处理过程中成分变化大,后段水可用筛选优势菌的方法处理．实验室流动模型运行结果为：在原水ρ（ Ｃ Ｏ Ｄｃｒ） １８５４４ ｍｇ／ Ｌ 和设定ｔ Ｈ Ｒ（ 延滞期） 下,混凝后出水ρ（ Ｃ Ｏ Ｄｃｒ） ５３２２ ｍｇ／ Ｌ,水解池出水ρ（ Ｃ Ｏ Ｄｃｒ） ４７６３ ｍｇ／ Ｌ,好氧池出水 Ｃ Ｏ Ｄｃｒ１９９ ．９ ｍｇ／ Ｌ,总 Ｃ Ｏ Ｄｃｒ去除率为９８ ．９ ％     

活性污泥动力学模型的建立及在完全混合式污泥系统中的应用

首先建立了微生物衰减系数和污泥浓度、底物浓度的函数关系式,带入Lawrence-McCarty第一方程式得到了Logistic方程形式的微生物生长方程式.在分析污泥泥龄和污泥停留时间关系基础上,引入Monod方程建立了活性污泥动力学模型,推导证明了Lawrence-McCarty方程式是模型静态条件下的表达形式.用建立的活性污泥动力学模型对完全混合式污泥系统进行了模拟,并分析了水力停留时间Hydraulic retention time(HRT)和污泥停留时间Sludge retention time(SRT)对完全混合式污泥系统的影响,表明模型能很好地对活性污泥系统的动态过程进行模拟.根据模型编程画出了污泥系统相关变量关于HRT和SRT变化的三维曲面图,通过编程将复杂模型看作一定输入输出的函数,使得模型更易于应用和推广.     

A hybrid membrane process for simultaneous thickening and digestion of waste activated sludge

A hybrid membrane process for simultaneous sludge thickening and digestion (MSTD) was studied. During one cycle (15 d) of operation under a hydraulic retention time of 1 d, the concentration of mixed liquor suspended solids (MLSS) continuously increased from about 4 g·L⁻¹ to 34 g·L⁻¹, and the mixed liquor volatile suspended solids (MLVSS) increased from about 3 g·L⁻¹ to over 22 g·L⁻¹. About 42% of the MLVSS and 39% of the MLSS reduction were achieved. The thickening and digestion effects in the MSTD were further analyzed based on a mass balance analysis. Test results showed that biopolymers and cations of biomass were gradually released to the bulk solution during the process. It was also found that the capillary suction time, colloidal chemical oxygen demand, soluble microbial products, viscosity, and MLSS had significant positive correlations with the membrane fouling rate, whereas extracellular polymeric substances, polysaccharides, and proteins extracted from biomass had negative impacts on membrane fouling.     

污水处理中的污泥减量新技术

污水好氧处理会产生大量污泥，剩余污泥的处理成本高昂，减少污泥产量势在必行。文章介绍了代谢解偶联、增加维持能量消耗、隐性生长、微型动物捕食、高溶解氧工艺和膜生物反应器等污泥减量技术，比较了各种技术的优缺点，指出了不同技术结合将成为污泥减量技术的发展方向。     

臭氧对活性污泥性状的影响

分别在臭氧浓度为31.50,31.96,32.23,33.89,36.65,39.33和40.25mg·l-1下,考察污泥混合液MLSS,MLVSS和pH值及上清液SCOD,TN,NH3-N和,TP等随臭氧作用时间的变化.结果表明:臭氧对污泥混合液中的溶解性同体(DS)具有氧化作用,能有效破解微生物絮体、细胞壁和细胞膜等,使微生物体内有机质溶出,溶出物能被微生物作为底物重新利用,本实验中,MLSS和MLVSS降低最大量分别为1250 mg·l-1和465 Mg·l-1,SCOD增加最大量为250.3 mg·l-1.另外,根据混合液各性状的变化规律分析了臭氧氧化污泥的机理.     

臭氧污泥减量过程中混合液各参数的变化

实验用污泥的初始浓度(MLSS)分别限定为4g/L、7g/L和11g/L,用以探讨不同浓度下臭氧氧化过程中COD、N和P浓度的变化。结果表明:臭氧氧化过程中,MLSS和MLVSS基本呈线性下降;臭氧对污泥细胞的溶解可以引起混合液中COD、N和P浓度的升高,升高速率受污泥浓度和臭氧浓度影响较大;TKN和硝态氮是N的主要存在形式,TKN和TN随时间均呈先增加后趋缓的变化规律;臭氧对氨氮和亚硝酸盐氮有较强的氧化能力,二者浓度均呈先增大后减小的规律;而硝酸盐氮呈一直增加趋势;臭氧对COD的氧化也很明显,表现为COD的增加速率随氧化时间的增加而不断降低;总磷的浓度基本呈线性增加,单位质量污泥的总磷释放量差异不大;臭氧对MLSS的彻底减量会引起臭氧溶胞利用率的降低,因此应该合理控制臭氧化反应的时间。     

寒冷地区城市污水处理厂污泥膨胀及其控制

结合大庆乘风庄污水厂运行 5年来两次污泥膨胀的实例 ,对活性污泥系统发生污泥膨胀的主要原因进行了分析 ,提出在寒冷地区活性污泥系统中 ,除低氧、低负荷外 ,低温也是造成膨胀的原因之一。对此提出采用减小曝气池污泥浓度或单池连续运行以提高负荷和鼓风机进风口空气加热提高曝气池水温的方法 ,可使膨胀得到有效控制。     

可循环利用污泥专用处置场建设的探讨

着重论述了国内外城市污水处理厂污泥的各种处置方法及处置现状，提出污泥土地利用是目前国内外污泥处理中的主体和重点发展的方式。根据上海市具体市情和污泥处置状况，提出在上海市建没污泥专用处置场，以解决污泥大量处置和最终用于土地利用的思路。比较详细地探讨了国外污泥专用处置场运行的现状，指出污泥专用处置场比污泥有效利用场能更大量地处置污泥且可循环反复处置，它占地面积小，在土地紧缺的上海更具利用优势。在此基础上，提出了适合上海市情的污泥专用处置场工艺流程设计、综合运行框架和具体的技术要求，以保证污泥能安全有效地处置利用，经过分析，指出在上海兴建污泥专用处置场处置污泥能获得较好的经济效益和环境效益。     

膜生物反应器无剩余污泥排放的研究

本文介绍了以膜生物反应器为基础的剩余污泥产量最少或无剩余污泥产生的最新的污水处理理论和技术。从技术微生物基本生命活动的物质转化概念和细胞产生和平衡的理论,提出了确定维持微生物基本生命活动的物质转化系数的方法,从理论与实验上计实了膜生物反应器无剩余污泥排放的可能性。     

Transport of Sewage Sludge From the 106-Mile Site - Results From an October Survey

Approximately 8 million tons of sewage sludge were disposed of annually at the 106-Mile Deepwater Municipal Sludge Dump Site (106-Mile Site) between 1987 and 1990. Beginning in 1988 and continuing to the present, the focus of monitoring at the 106-Mile Site moved towards improved understanding of the fate of the sludge. A survey conducted in October 1989 was designed to (1) detect the presence of any sludge particles that settle rapidly following disposal, (2) determine if sludge could be detected in the surface waters at locations away from the immediate disposal site, and (3) determine if water quality was degraded, by assessing whether the Environmental Protection Agency's marine water quality criteria were being exceeded.

The survey showed that the sludge does have a rapidly settling component composed of organic floc. mineral grains, and other heavy, gritlike particles, all of which are relatively large. These particles may settle at rates of between 8 and 180 m h^-1 and may reach the sea floor within 1 to 13 days following disposal. Even though a rapidly settling component is present in the sludge, a significant fraction of the sludge was detectable in the form of intact sludge plumes in the upper 35 m of the water column at least 15 km from the Site. in addition, unique tracers of sludge such as xylem tracheids and Clostridium perfringens plus elevated total suspended solids and trace metals concentrations, were found at locations up to 40 km from the Site. the presence of these tracers correspond with in situ transmissometry data suggesting that a fraction of the sludge was remaining in the near-surface waters above the seasonal pycnocline. Concentrations of metals were below EPA chronic marine water quality criteria, which indicates that the water quality downstream of the Site was not impaired. the detection of sludge downstream of the 106-Mile Site is consistent with the southwestward movement of the surface water mass during the survey, as recorded by satellite-tracked surface drifters and current vectors derived from a current meter moored at 100-m depth immediately west of the Site. Near-surface transport was generally towards the southwest at a speed of approximately 22 cm s^-1*.     

Transport of Sewage Sludge From the 106-Mile Site - Results From an October Survey

Abstract

Approximately 8 million tons of sewage sludge were disposed of annually at the 106-Mile Deepwater Municipal Sludge Dump Site (106-Mile Site) between 1987 and 1990. Beginning in 1988 and continuing to the present, the focus of monitoring at the 106-Mile Site moved towards improved understanding of the fate of the sludge. A survey conducted in October 1989 was designed to (1) detect the presence of any sludge particles that settle rapidly following disposal, (2) determine if sludge could be detected in the surface waters at locations away from the immediate disposal site, and (3) determine if water quality was degraded, by assessing whether the Environmental Protection Agency's marine water quality criteria were being exceeded.

The survey showed that the sludge does have a rapidly settling component composed of organic floc. mineral grains, and other heavy, gritlike particles, all of which are relatively large. These particles may settle at rates of between 8 and 180 m h^?1 and may reach the sea floor within 1 to 13 days following disposal. Even though a rapidly settling component is present in the sludge, a significant fraction of the sludge was detectable in the form of intact sludge plumes in the upper 35 m of the water column at least 15 km from the Site. in addition, unique tracers of sludge such as xylem tracheids and Clostridium perfringens plus elevated total suspended solids and trace metals concentrations, were found at locations up to 40 km from the Site. the presence of these tracers correspond with in situ transmissometry data suggesting that a fraction of the sludge was remaining in the near-surface waters above the seasonal pycnocline. Concentrations of metals were below EPA chronic marine water quality criteria, which indicates that the water quality downstream of the Site was not impaired. the detection of sludge downstream of the 106-Mile Site is consistent with the southwestward movement of the surface water mass during the survey, as recorded by satellite-tracked surface drifters and current vectors derived from a current meter moored at 100-m depth immediately west of the Site. Near-surface transport was generally towards the southwest at a speed of approximately 22 cm s^?1?.