污水地下渗滤系统强化脱氮试验研究

构建了3套以5%炉渣+95%草甸棕壤为基质的地下渗滤系统室内模拟试验装置,在水力负荷为0.1m3/(m2·d)条件下进行了生活污水处理试验.结果表明,当分流位置位于系统内110cm处,分流比为1:1时,可提高地下渗滤对总氮的去除效率,总氮的去除率由59.37%提高至68.41%,且对COD和总磷的去除效果没有影响.     

含油污泥无害化处置优化研究及生命周期评价

提出含油污泥的优化处置方案,并通过生命周期评价方法(LCA)对优化方案进行环境影响评价。结果表明,与原处置工艺相比优化后环境负荷降低了99.62%。     

基于部分湿式氧化法的污泥资源化研究

介绍了部分湿式氧化法的基本原理,指出COD去除率是判断是否部分湿式氧化的重要指标。用高压反应釜进行污泥处理,在一定的温度、压力和适合氧气量的条件下,考察了COD去除率、有机物降解率、pH值、过滤性能等随反应时间的变化。试验结果表明,通过控制反应时间,可以实现污泥的部分湿式氧化。考察了污泥经过部分湿式氧化后产物的性质,包括颗粒分布、有机物含量、养分含量和重金属等项目,分析结果表明,产物具有良好的资源化前景。     

曝气调节-水解酸化-生物接触氧化工艺处理城镇生活污水

介绍了采用曝气调节-水解酸化-两级生物接触氧化为主的工艺处理城镇生活污水的工程实例。经过调试运行,污水处理系统运行稳定,工艺运行成本低,污染物处理效果好。其中COD、BOD5、SS与氨氮去除率均在85%以上,出水水质优于GB 8978-1996《污水综合排放标准》一级排放标准。     

一体化接触氧化反应器处理景区生活污水

常州某旅游景区采用一体化生活污水处理装置处理该区生活污水,通过试验确定反应器的最佳工艺参数,研究表明采用接触氧化反应器处理农村污水,在反应器内溶解氧维持在2.0~4.0 mg/L,水力负荷为3.53 m3/(m3.d)的运行条件下,对COD、NH3-N及TN去除率分别达80.82%、69.12%、63.16%,出水可稳定达GB18918-2002《城镇污水处理厂污染物排放标准》一级标准。     

电石渣和石灰对污泥的改性效果比较

在含水率为86.1%的脱水污泥中分别添加10%的电石渣和工业生石灰,其搅拌30min后及自然晾晒24,48,72,96,120 h后的含水率持续线性下降,自然晾晒120 h后可达到填埋标准;添加电石渣及石灰的污泥,其单位质量水分蒸发速率与原污泥有本质差异;两种改性剂均可使污泥比阻降低50%左右;经板框压滤机压滤出的泥饼...     

四川某中小城镇污水处理厂进水水质统计分析

生活污水水质对处理工艺的选择、设计参数的选取以及稳定运行十分重要。运用SPSS软件,对四川某中小城镇污水处理厂为期一年的进水指标(水量、COD、氨氮、总磷、pH、SS)进行方差和相关性分析。方差分析结果显示进水量、氨氮和SS在月份和季节之间存在显著性差异,而总磷和pH仅在月份之间存在显著差异,COD在季度和月份之间无显著性差异;指标相关性分析表明,进水量和氨氮之间呈负相关,氨氮和总磷、COD和总磷之间呈正相关,且相关性显著。在此分析的基础上对污水处理厂设计、工艺选择及运行管理提出了一些建议。     

Mobilities and leachabilities of heavy metals in sludge with humus soil

Chemical forms of Zn, Ni, Cu, and Pb in municipal sewage sludge were investigated by adding humus soil to sludge and by performing sequential extraction procedures. In the final sludge mixtures, Zn and Ni were mainly found in Fe/Mn oxide-bound (F3) and organic matter/sulfide-bound (F4) forms. For Zn, exchangeable (F1), carbonate-bound (F2), and F3 forms were transformed to F4 and residual forms (F5). For Ni, F1 and F2 forms were transformed to F1, F2, and F3 forms. Both Cu and Pb were strongly associated with the stable forms F4 and F5. For Cu, F2 and F3 forms were major contributors, while for Pb, F3 and F4 forms were major contributors to F5. Humus soil dosage and pH conditions in the sludge were strongly correlated with the forms of heavy metals. Five forms were used to evaluate metal mobilities in the initial and final sludge mixtures. The mobilities of the four heavy metals studied decreased after 28 days. The metal mobilities in the final sludge mixtures were ranked in the following order: Ni > Zn > Cu = Pb. Leaching tests showed that the mobilities of Zn and Ni in lower pH conditions (pH 4) were higher than those in higher pH conditions (pH 8).     

Impacts of wastewater sludge amendments in restoring nitrogen cycle in p-nitrophenol contaminated soil

The possible impacts on nitrogen-cycle in a p-nitrophenol (PNP) polluted soil and the e ectiveness of wastewater sludge amendments in restoring nitrification potential and urease activity were evaluated by an incubation study. The results indicated that PNP at 250 mg/kg soil inhibited urease activity, nitrification potential, arginine ammonification rate and heterotrophic bacteria counts to some extents. After exposure to PNP, the nitrification potential of the tested soil was dramatically reduced to zero over a period of 30 days. Based on the findings, nitrification potential was postulated as a simple biochemical indicator for PNP pollution in soils. Nitrogen-cycling processes in soils responded positively to the applications of wastewater sludges. A sludge application rate of 200 tons/ha was su cient for successful biostimulation of these nitrogen processes. The microbial activities in sludge-amended, heavy PNP-polluted soils seemed to recover after 30–45 days, indicating the e ectiveness of sludge as a useful soil amendment.     

Evaluation of reusing alum sludge for the coagulation of industrial wastewater containing mixed anionic surfactants

A coagulation-flocculation process is typically employed to treat the industrial wastewater generated by the consumer products industry manufacturing detergents, soaps, and others. The expenditure of chemicals including coagulants and chemicals for pH adjustment is costly for treating this wastewater. The objective of this study was to evaluate the feasibility of reusing the aluminum sulfate (alum) sludge as a coagulant or as a coagulation aid so that the fresh alum dosage can be minimized or the removal e ciency can be enhanced. The experiments were conducted in a jar-test apparatus simulating the coagulation-flocculation process for simultaneous removals of organic matters, anionic surfactants, suspended solids, and turbidity. At the optimum initial pH value of 10 and the fresh alum concentration of 400 mg/L, the total suspended solids (TSS), total chemical oxygen demand (TCOD), total anionic surfactants, and turbidity removal e ciencies were 71.5%, 76.4%, 95.4%, and 98.2%, respectively. The addition of alum sludge as a coagulant alone without any fresh alum addition could significantly remove the turbidity, TCOD, and anionic surfactants. The TSS was left in the supernatants after the settling period, but would subsequently be removed by adding the fresh alum. The TSS, TCOD, and turbidity removal e ciencies were also enhanced when both the alum sludge and the fresh alum were employed. The TCOD removal e ciency over 80% has been accomplished, which has never fulfilled by using the fresh alum alone. It is concluded that the alum sludge could be reused for the treatment of industrial wastewater generated by the consumer products industry.