垃圾渗滤液生化出水的脱色研究

分别采用脉冲电解法、混凝沉淀法、芬顿氧化法、高铁酸钾氧化法对垃圾渗滤液生化出水进行处理,考察了处理效果。结果表明：铁电极电解法和芬顿试剂氧化法均能脱除垃圾渗滤液的色度,去除有机物质。铁电极电解对色度的去除率可达98．4％,COD去除率可达84．4％;芬顿试剂氧化对色度的去除率可达99％,COD去除率可达85．8％。两种方法均能使出水达到排放标准。同时比较了各种处理方法的运行成本,在达到同样出水标准的前提下,铁电极电解运行成本远低于芬顿试剂氧化,为3．67元／t水,而芬顿试剂药剂成本为8．67元／t水。     

聚铁混凝-臭氧-BAF对晚期垃圾渗滤液深度处理的研究

联合运用聚铁混凝-臭氧-曝气生物滤池(BAF)对晚期垃圾场的渗滤液进行深度处理。在废水进水COD=601mg/L,色度=400倍时,提出最佳工艺条件:聚铁0.6 mL/L,臭氧用量144 mg/L,BAF停留时间7 h。研究表明,聚铁去除大部分悬浮性有机物,臭氧降解难生物降解有机物并提高废水的可生化性,BAF进一步降解有机物,最终出水COD为75 mg/L,深度处理成本仅为5.5元/t。     

垃圾填埋场渗滤液物化深度处理研究

通过Fenton法和结合聚合硫酸铁的混凝作用,实现垃圾渗滤液氧化塘出水COD的深度处理;并利用水泥水化产物的凝胶物质,强化COD去除率。30％H2O2投加量为0．75mL／L、七水硫酸亚铁投加量为1．5g／L、n（H2O2）：n（Fe^2＋）=1．2：1（摩尔比）时,Fenton法对渗滤液COD的去除率可达52％;水灰比为2：1、搅拌24h的水泥水化物将Fenton法的出水pH值从4调至10,该工艺流程总的COD去除率为73．6％,较普通的Ca（OH）2调节法提高9．3％,出水COD可以从进水的1200mg／L降至315mg／L。     

生活垃圾渗滤液处理工艺探讨

分析了国内生活垃圾（以下简称垃圾）渗滤液的特点,探讨了一种比较科学的垃圾渗滤液处理工艺：沉淀-厌氧处理-MBR-纳滤处理,并且分析了各段工艺的原理、特点以及其作用。     

UASB-FEO-氨吹脱-CASS工艺在垃圾渗滤液处理中的应用

针对垃圾渗滤液可生化性差、氨氮含量高等特点和国内处理工艺现状,采用UASB-FEO-氨吹脱-CASS工艺处理合肥市龙泉山城市垃圾填埋场垃圾渗滤液。介绍了工艺的重要构筑物及其设计参数。运行实践表明,整套装置运行平稳,出水水质满足设计要求。根据出水水质对该工艺进行技术分析以及运行结果的讨论,并与新发布的技术规范及排放标准进行对比分析。     

Prediction of Leachate Level in Kimpo Metropolitan Landfill Site by Total Water Balance

Kimpo metropolitan landfill has received various kinds of wastessince January 1992. The leachate level was measured to be 10.3 m in May 1995 and the level increased to 12.2 m in August 1996. Therefore, to prove the reason for the increasing leachate level, we calibrated hydraulic conductivity of each waste andintermediate layer using the HELP (Hydrologic Evaluation ofLandfill Performance) model. The leachate generation data measured from February 1993 to October 1995 was used in the model calibration. As a result of a model calibration, we obtained anaverage infiltration ratio and used this in analysis of the total water balance to predict elevation of leachate level. Main causes of the elevation of the leachate level were the high water content of the waste and the degradation of the leachate-drainage system caused by the subsidence of a naturalbarrier layer.     

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.     

Evolution on qualities of leachate and landfill gas in the semi-aerobic landfill

To study the characteristics of stabilization in semi-aerobic landfill, large-scale simulated landfill was constructed based on the semiaerobic landfill theory. Consequently, the concentrations of chemical oxygen demand (COD), ammonia nitrogen, and nitrite nitrogen, and the pH value in leachate, as well as the component contents of landfill gas composition (methane, carbon dioxide, and oxygen) in landfill were regularly monitored for 52 weeks. The results showed that COD and ammonia concentrations declined rapidly and did not show the accumulating rule like anaerobic landfill, and remained at about 300 and 100 mg/L, respectively, after 48 weeks. Meanwhile, the descending rate reached 98.9% and 96.9%, respectively. Nitrate concentration increased rapidly after 24 weeks and fluctuated between 220–280 mg/L after 43 weeks. The pH values were below 7 during the first 8 weeks and after that leachates appeared to be alkaline. Carbon dioxide was the main composition in landfill gas and its concentration remained at a high level through the whole stabilization process. The average contents of carbon dioxide, oxygen, and methane varied between 19 vol.%–28 vol.%, 2 vol.%–8 vol.%, and 5 vol.%–13 vol.%, respectively. A relative equilibrium was reached after 48 weeks. The highest temperature in the landfill chamber could amount to 75.8 degrees centigrade.     

Landfill leachate treatment methods: A review

Landfilling of municipal waste is still a major issue of the waste management system in Europe. The generated leachate must be appropriately treated before being discharged into the environment. Technologies meant for leachate treatment can be classified as follows (i) biological methods, (ii) chemical and physical methods. Here we review briefly the main processes currently used for the landfill leachates treatments.     

光催化氧化降解垃圾渗滤液中溶解性有机物

研究了UV-TiO2光催化氧化降解垃圾渗滤液过程中溶解性有机物(DOM)的变化特征。结果表明:在适宜条件下,UV-TiO2光催化氧化降解垃圾渗滤液的色度、COD和DOC的去除率分别可达97%、72%和60%;紫外光谱分析说明渗滤液DOM中包括多种含有共轭双键、羰基的大分子有机物及多环芳香类化合物,不同光催化处理液中DOM具有基本一致的结构单元和官能团;红外光谱分析说明渗滤液DOM中含有大量包括羟基、羧基、氨基和苯环的芳香族化合物,在光催化处理液中这几种官能团都能被有效降解;GC/MS分析结果表明,渗滤液DOM中含有72种有机污染物,醇类、羧酸和酮类分别为25、14和12种;在光催化72 h处理液中,有机物减少为44种;酯类和醇类较多,分别为12种和16种;酮类8种,羧酸没有检出。