新知

1 废水发电机 根据Broadbent的统计,1栋7层高的楼房安装这台废水发电机后可以每年节省1000美元的电费。在不久的将来就会进入消费市场了。     

高氨氮废水短程硝化的影响因素

工业废水中,氨和氮的含量较高,而且全程硝化的工艺很难满足对这些废水的处理要求,因而,高氨氮废水的短程硝化工艺越来越被重视起来.文章将阐述高氨氮废水短程硝化的原理,并着重分析影响高氨氮废水短程硝化的各种因素.     

含油废水处理技术

概述了含油废水的来源、特点、分类及危害,介绍了含油废水的处理方法的原理、优势及存在的问题,同时简述了各种处理方法的最新研究成果,最后提出了含油废水发展趋势。     

采用Anammox颗料污泥工艺对酵母废水进行脱氮处理的研究

本实验采用先进的厌氧氨氧化（Anammox）颗粒污泥工艺对某酵母厂的二沉出水进行了毒性实验与连续流实验。毒性实验结果表明该类废水对Anammox细菌有一定的抑制作用,但没有影响最终的0去除效果;而近一介半月的连续流实验数据则表明：在进水氨氮浓度300-360mg／1的情况下,污泥负荷与容积负荷可以稳定地上升,出水氨氮在50mg／l以下,亚硝酸盐氮维持在5mg／1左右,氨氮去除率可达80％以上。     

冶金高含盐废水处理工艺实践应用

某黄金冶炼厂根据云南当地的实际情况,在废水处理工程中采用太阳能预热-刮板式薄膜蒸法工艺处理黄金深加工过程中产生的高含盐废水,处理效果好,出水稳定,是一种非常有效的处理工艺。氯化物及重金属到达GB5749—2006生活饮用水卫生标准。     

Electro-Fenton法处理印染废水应用研究进展

Electro-Fenton法是利用电解的方法产生Fe2+和H2O2,新生的Fe2+和H2O2作用产生·OH。作为一种新兴的废水处理技术,在处理难降解有机废水方面,国内外已开展了广泛的研究,对于处理高浓度难降解有机废水效果良好。阐述了Electro-Fenton法的发展、分类、反应机理及其在印染废水处理中的应用研究现状,并指出Electro-Fenton法存在的主要问题和今后的发展方向。     

磁絮凝处理染整废水的中试研究

针对染整废水进行磁絮凝的中试研究,将磁粉加载于混凝澄清池,该技术是在接触絮凝加速澄清技术基础上提出的一种应用絮凝形态学理论的新型高效固液分离技术。中试试验经过半年的调试和运行,浊度等水质数据明显优于普通的砂滤出水水质。处理后的出水水质为pH=6~9,COD≤200 mg/L,浊度≤10NTU,色度≤200倍。     

碱改性脱水污泥对水中镉的吸附效能研究

城市市政污水处理厂产生的剩余污泥是一种良好的重金属生物吸附剂制备原料。以北京某市政污水处理厂产生的脱水剩余污泥为原料,采用碱改性处理方法,制备得到碱改性脱水污泥生物吸附剂,通过其对水中镉的等温吸附实验,考察其重金属吸附效能。研究结果表明:碱改性脱水污泥对水中镉的等温吸附曲线符合Langmuir等温吸附模型。碱改性处理后,脱水污泥对水中镉的最大饱和吸附容量提高了2.8倍,达0.966 mmol/g,显著高于同类型脱水污泥生物吸附剂。碱改性脱水污泥对水中镉的最大饱和吸附容量与改性过程中所使用的Na OH浓度之间的线性相关性较差,呈现一定的波动变化趋势。     

Enhanced struvite recovery from wastewater using a novel cone-inserted fluidized bed reactor

The feasibility of struvite recovery at low （12.5 mg/L） and high （120 mg[L） phosphorus concentrations was studied by constructing a novel fluidized bed reactor with cones （FBRwc） and without cones （FBRwoc）. The crystallization process was continuously operated for 133 days under different hydraulic retention times （HRT = 1-10 hr）, pH （7.5-10）, and molar ratios of Mg/P （0.75-1.75）, N/P （1-10） and Ca/Mg （0-2）. The optimum operating conditions of HRT, pH, Mg/P and N/P molar ratios were found to be 2 hr, 9, 1.25, and 7.5, respectively. Under these optimum conditions, the phosphorus precipitation efficiencies of FBRwc were 93% for low and 98% for high phosphorus influent; however, the efficiencies were 78% and 81% for FBRwoc, respectively. Due to crystal losses at each junction （17%-31%）, the crystal recovery efficiency of FBRwoc was relatively low （47%-65%） for both influent concentrations. However, the losses were minimal in FBRwc, which showed 75% and 92% crystal recovery for low and high phosphorus concentrations, respectively. At low calcium concentration, crystal chemical analysis showed the product to be pure struvite （〉 99%）. The scanning electron microscope and X-ray diffraction results further confirmed that the crystal recovered from FBRwc contained pure struvite, which could be considered a high quality fertilizer. Except HRT, all parameters （pH, Mg/P, N/P and Ca/Mg） were found to be influencing factors for FBRwc performance. Overall, inserting cones in each part of the reactor played a significant role in enhancing struvite recovery from a wide range of phosphorus-containing wastewater.     

Removal of phosphate from wastewater using alkaline residue

Alkaline residue(AR) was found to be an efficient adsorbent for phosphate removal from wastewater. The kinetic and equilibrium of phosphate removal were investigated to evaluate the performance of modified alkaline residue. After treatment by NaOH(AR-NaOH), removal performance was significantly improved, while removal performance was almost completely lost after treatment by HCl(AR-HCl). The kinetics of the removal process by all adsorbents was well characterized by the pseudo second-order model. The Langmuir model exhibited the best correlation for AR-HCl, while AR was effectively described by Freundlich model. Both models were well fitted to AR-NaOH. The maximum adsorption capacities calculated from Langmuir equation were in following manner: AR-NaOH AR AR-HCl. Phosphate removal by alkaline residue was pH dependent process. Mechanisms for phosphate removal mainly involved adsorption and precipitation, varied with equilibrium pH of solution. For AR-HCl, the acid equilibrium pH( 6.0) was unfavorable for the formation of Ca-P precipitate, with adsorption as the key mechanism for phosphate removal. In contrast, for AR and ARNaOH, precipitation was the dominant mechanism for phosphate removal, due to the incrase on pH( 8.0) after phosphate removal. The results of both XRD and SEM analysis confirmed CaHPO4·2H2O formation after phosphate removal by AR and AR-NaOH.