矿化垃圾床＋三维电极／电Fenton法处理老龄垃圾渗滤液

提出以二级矿化垃圾床为预处理单元，串联三维电极／电Fenton处理老龄垃圾渗滤液的组合工艺。矿化垃圾床处理后渗滤液中COD、氨氮、总磷、色度的去除率分别为80．55％、88．47％、98．32％和87．53％。通过单因素实验和正交实验，确定了三维电极／电Fenton法最佳工艺条件。经该组合工艺后，渗滤液中COD、氨氮、总磷和色度的最高去除率分别可达97．08％、95．24％、99．55％和96．92％，其中COD、总磷、色度这3个指标低于《生活垃圾填埋场污染控制标准》（GB16889．2008）表2规定的排放标准，为该组合工艺在实际中的应用提供重要理论依据。     

老垃圾填埋场渗滤液回灌工艺参数研究

根据理论分析,通过回灌能够实现对老垃圾填埋场所产生渗滤液的场内处理,改善渗滤液水质,同时能加速老填埋场的稳定化进程.以深圳市10座老垃圾填埋场为研究对象,提出渗滤液回灌工艺及其参数.回灌方式以水平渗沟为主,设置聚乙烯罐调节水量.渗滤液回灌加速了填埋气体产生速率,降低了有效应力,可能引起垃圾体边坡失稳.较大的渗滤液回灌量(1.6%)导致较低的垃圾边坡安全系数(1.96).确定满足加速垃圾稳定化和填埋场稳定性的最佳回灌量是填埋场渗滤液回灌大规模应用需要解决的重要问题.     

Biogeochemistry at a wetland sediment–alluvial aquifer interface in a landfill leachate plume

The biogeochemistry at the interface between sediments in a seasonally ponded wetland (slough) and an alluvial aquifer contaminated with landfill leachate was investigated to evaluate factors that can effect natural attenuation of landfill leachate contaminants in areas of groundwater/surface-water interaction. The biogeochemistry at the wetland-alluvial aquifer interface differed greatly between dry and wet conditions. During dry conditions (low water table), vertically upward discharge was focused at the center of the slough from the fringe of a landfill-derived ammonium plume in the underlying aquifer, resulting in transport of relatively low concentrations of ammonium to the slough sediments with dilution and dispersion as the primary attenuation mechanism. In contrast, during wet conditions (high water table), leachate-contaminated groundwater discharged upward near the upgradient slough bank, where ammonium concentrations in the aquifer where high. Relatively high concentrations of ammonium and other leachate constituents also were transported laterally through the slough porewater to the downgradient bank in wet conditions. Concentrations of the leachate-associated constituents chloride, ammonium, non-volatile dissolved organic carbon, alkalinity, and ferrous iron more than doubled in the slough porewater on the upgradient bank during wet conditions. Chloride, non-volatile dissolved organic carbon (DOC), and bicarbonate acted conservatively during lateral transport in the aquifer and slough porewater, whereas ammonium and potassium were strongly attenuated. Nitrogen isotope variations in ammonium and the distribution of ammonium compared to other cations indicated that sorption was the primary attenuation mechanism for ammonium during lateral transport in the aquifer and the slough porewater. Ammonium attenuation was less efficient, however, in the slough porewater than in the aquifer and possibly occurred by a different sorption mechanism. A stoichiometrically balanced increase in magnesium concentration with decreasing ammonium and potassium concentrations indicated that cation exchange was the sorption mechanism in the slough porewater. Only a partial mass balance could be determined for cations exchanged for ammonium and potassium in the aquifer, indicating that some irreversible sorption may be occurring.Although wetlands commonly are expected to decrease fluxes of contaminants in riparian environments, enhanced attenuation of the leachate contaminants in the slough sediment porewater compared to the aquifer was not observed in this study. The lack of enhanced attenuation can be attributed to the fact that the anoxic plume, comprised largely of recalcitrant DOC and reduced inorganic constituents, interacted with anoxic slough sediments and porewaters, rather than encountering a change in redox conditions that could cause transformation reactions. Nevertheless, the attenuation processes in the narrow zone of groundwater/surface-water interaction were effective in reducing ammonium concentrations by a factor of about 3 during lateral transport across the slough and by a factor of 2 to 10 before release to the surface water. Slough porewater geochemistry also indicated that the slough could be a source of sulfate in dry conditions, potentially providing a terminal electron acceptor for natural attenuation of organic compounds in the leachate plume.     

Performances of mesophilic anaerobic digestion systems treating poultry mortalities

Abstract

A closed‐loop anaerobic digestion system consisting of a leachbed (LB) and an upflow anaerobic sludge blanket (UASB) was tested as an alternative for the disposal of poultry mortalities. This paper compares the performances of three LB‐UASB treatment systems with different initial moisture contents in the LBs. Each LB was loaded with one chicken and 5, 10 or 18 liters of water. The LBs initially carried out the hydrolysis/acidification phase while the UASBs the methanogenesis phase. Due to repeated inoculation by the UASBs, the LBs with 10 and 18 liters of water started producing methane on day 5, while the one with 5 liters of water on day 19. However, methane production rates were low before day 40 for the LB with 10 liters of water and day 60 for the other LBs. Methane production gradually improved as the LBs continued to receive ungranulated sludge from the UASBs. The LBs eventually became balanced methane reactors. Continued balanced fermentation in the LBs resulted in leachates with very low substrate concentrations that could no longer support high‐rate methanogenesis in the UASBs. Consequently, methane production rates from the UASBs decreased quickly while that from the LBs reached peak levels. Cumulative methane production from each LB eventually exceeded that from its connecting UASB. After 118 days of digestion, 414, 437 and 470 liters of methane were produced from the three systems, respectively. Cumulative methane production from the LBs with 5 and 18 liters of water accounted for 63% of the total methane produced from their respective systems. The LB with 10 liters of water produced 75% of the total methane from that system. Methane yields ranged from 0.485 to 0.554 m³ (Kg TS) ¹. About 86% of the initial dry weight was biodegraded. All three systems performed very well with little operational problems. Overall, the system that started with 10 liters of water in the LB performed the best. Strategy for enhancing system performances and implementing farm applications are discussed.     

生活垃圾焚烧厂垃圾渗滤液处置技术

介绍生活垃圾焚烧厂垃圾渗滤液的特性和国内外对生活垃圾焚烧厂渗滤液几种常见的处置方法,并从经济性、技术工艺、运行等方面分析对比了几种处置方式的优劣。结合焚烧厂渗滤液处理工程设计、运行实践经验,总结了焚烧厂垃圾渗滤液工程设计要点。     

PCR-DGGE研究处理垃圾渗滤液序批式生物膜反应器(SBBR)中的细菌多样性

为了研究序批式生物膜反应器中的细菌多样性及其脱氮的微生物学机理,为工艺改进提供依据,从同步高效去除垃圾渗滤液中高氨氮和高COD的SBBR生物膜和渗滤液原水中采集微生物样品并提取微生物总DNA,使用细菌通用引物对（GC341F/907R）从总DNA中成功扩增出目标16S rDNA片段,然后对扩增的16S rDNA进行DGGE,对凝胶染色并进行条带统计分析和切胶测序,使用序列数据进行同源性分析并建立了系统发育树.结果表明,该驯化后的SBBR生物膜和渗滤液原水中都有比较丰富的细菌多样性,驯化的生物膜细菌主要来自渗滤液原水,而且生物膜细菌在反应器正常运行时不会出现明显的群落结构变化;在该SBBR中有多种硝化细菌与反硝化细菌、好氧反硝化细菌和厌氧氨氧化细菌共存,说明该反应器中可能同时存在全程硝化反硝化、同步硝化反硝化和厌氧氨氧化3种脱氮方式.研究结果为SBBR脱氮微生物机理研究提供了一些有价值的参考依据.     

移动床生物膜反应器对垃圾渗滤液短程硝化研究

采用好氧移动床生物膜反应器（MBBR）对经过厌氧脱碳处理的垃圾渗滤液进行了深度短程硝化研究,考察了在中温（25℃）条件下DO浓度、pH值、C/N等因素对氨氮去除效果和短程硝化效果的影响.结果表明,在进水氨氮浓度为400　mg·L^-1,HRT为24 h情况下,当控制DO为2　mg·L^-1、pH值在8左右和C/N小于3时,氨氮去除率能达到70%以上,亚硝酸盐氮的积累率高达90％.间歇试验证明了该生物膜反应器中亚硝化菌的数量和活性要远高于硝化菌.该移动床生物膜工艺可以选择性固定和积累氨氧化细菌,从而实现较高的氨氮去除率和稳定的亚硝酸盐氮积累率.     

垃圾渗滤液层状砂箱参数拟合试验及模拟

基于相似模拟条件,研究了垃圾渗滤液污染物在层状含水层中运移规律,通过数值模拟方法拟合了层状含水层的渗透性及弥散度,利用拟合参数分析了阜新垃圾填埋场有机污染物在地下环境中的迁移和时空分布规律,该实验和数值模型较好地反映了层状土中污染物渗漏的基本特征,对预测、控制渗滤液污染地下水提供了一种有效的方法。     

苏州垃圾填埋生命周期清单分析

采用理论计算和实测相结合的方法,求得了苏州七子山垃圾填埋埋场的生命周期清单。实践证明,理论计算和实测相结合是清单分析的有效方法,对今后的同类研究具有参考意义。研究中获得的清单包括生活垃圾的收集和运输、垃圾填埋的物耗和能耗,以及每吨填埋垃圾所排放的大气和水污染物的量,并考察了填埋气用于发电后对清单的影响。这些结果可以为众多的产品生命周期评价提供数据支持。     

生活垃圾填埋场甲烷自然减排的新途径:厌氧与好氧的共氧化作用

采用暴雨过后垃圾填埋表层30～60 cm的覆土、表层1.5 m以下的垃圾,以及刚刚开挖出来的9年矿化垃圾进行硫酸盐还原菌阳性反应试验,结果表明生活垃圾填埋体不同填埋层都存在不同数量级的硫酸盐还原菌,且底层矿化垃圾中的硫酸盐还原菌的数量最多,表层覆土中最少.颗粒大小比例为50%:50%的垃圾样品表现出最佳的甲烷好氧与厌氧...