某生活垃圾卫生填埋场渗滤液的梯度分离与表征

目前,渗滤液中污染物的粒度分布及其在渗滤液污染控制中的作用日益受到关注。通过系列微滤膜(1.2μm及0.45μm)对某生活垃圾卫生填埋场渗滤液各处理单元的渗滤液进行梯度分离,发现悬浮物对COD、浊度的影响较大;COD主要在胶体态和可溶解态间分配,不同渗滤液中的分配情况不同;磷主要与胶体、悬浮物以各种形式结合而存在;细胶粒和溶解态等小分子对TN的贡献大;不同粒度物质对pH的影响不明显;总残渣在可溶态组分中所占比例较大。膜微滤处理渗滤液可以有效的去除一部分物质,使COD、TP、TN、浊度、电导率都有不同程度的降低,pH逐渐升高,但对总N、残渣的去除效果不好。     

"老龄期"填埋场渗滤液COD蒸发规律研究

"老龄期"填埋场渗滤液由于可生化性差而难于处理.采用常规蒸发、减压蒸发和载气蒸发处理不同pH值的"老龄期"渗滤液.实验结果表明,3种蒸发方式下,冷凝液COD下降过程中均存在明显的浓度转折点,转折点之后COD维持较低水平,为"老龄期"渗滤液的"三分处理法"提供理论依据.与常规蒸发相比,减压蒸发和载气蒸发的前期冷凝液COD较高,且浓度转折点偏后.     

渗滤液回流量对生物反应器型垃圾填埋的影响

利用3个生物反应器研究了回流量的大小对模拟填埋场厌氧处理城市生活垃圾的影响。0号罐设定渗滤液不回流,1号罐和2号罐采取渗滤液回流措施,其回流量分别是10L/d(反应器体积的10.5%),20L/d(反应器体积的21%)。试验结果表明:1号罐中的甲烷产量和甲烷含量都要优于0号罐和2号罐。在2号罐中渗滤液回流量相对提高1倍后,其pH会下降而VFA和COD的浓度会有相应的增加。相对于10L的渗滤液回流量,高回流量(20L)有利于产甲烷化的启动和提高填埋气的产量和甲烷含量。但在反应后一阶段,高回流量(20L)导致产气量比低回流量的(10L)减少34.83%左右。     

废铁屑-改性粉煤灰联用处理铬渣渗滤液

针对铬渣严重污染环境问题,以"以废治废"为研究目标,采用室内静态实验方法,进行废铁屑-改性粉煤灰联用处理铬渣渗滤液中Cr(Ⅵ)和总铬实验研究。实验结果表明,废铁屑与聚合氯化铝改性粉煤灰联用处理Cr(Ⅵ)和总铬效果优于单独采用其中一种物质;处理Cr(Ⅵ)浓度208 mg/L、总铬浓度260 mg/L的200 mL高浓度含铬废水最佳反应条件为:反应时间30 min,总投加量40 g,配比为1:1, pH值4.1,对应Cr(Ⅵ)去除率99.93%,总铬去除率99.72%。处理后水质满足《污水综合排放标准》(GB 8978-1996)要求。     

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.     

生活垃圾卫生填埋场渗滤液处理系统工程设计

本文从工程的角度出发对垃圾填埋场渗滤液处理系统工程设计中的几个重点、难点计算参数,以及目前国内外几个典型垃圾填埋场的渗滤液处理工艺流程、处理效果做了介绍,并在此基础上提出了几点建议     

城市固体废物生物处理方法及其可行性

生物反应堆是通过强化微生物转化和降解有机废物的能力进行处理固体废物的一种方法。本文分别对好氧生物处理、厌氧生物处理和兼性生物处理的机理、影响因素以及各污染物质的迁移转化规律进行综合分析。研究表明生物反应堆具有明显的社会、环境、经济效益，是实现可持续发展的一条重要途径，为以后的研究和应用提供可靠的理论依据。     

生物反应器填埋场渗滤液及其处理对策

根据垃圾的降解和稳定机理分析了生物反应器填埋场渗滤液的动态变化规律，并对其处理对策进行了探讨。生物反应器填埋场前期产生的渗滤液可全部回灌，后期再根据实际情况排放处理部分过量的渗滤液。在对渗滤液水量和水质全面直观认识后，再对生物反应器填埋场渗滤液处理工艺进行针对性的选择和设计，并宜采用物化法处理方式。     

EFFECTS OF COAL PILE RUNOFF ON STREAM QUALITY AND MACROINVERTEBRATE COMMUNITIES1

Samples of coal pile runoff, Georges Creek water, and macrobenthos above and below two coal storage areas along Georges Creek, Allegany County, Maryland, were collected in July, August, and September 1982, and February and July 1983. Coal pile runoff was collected under high- and low-flow conditions. Water samples were analyzed for Hg, Zn, As, Fe, Mn, Al, SO₄^?2, pH, filterable and non-filterable residue, conductivity and acidity. Leachate from coal piles along Georges Creek contained high concentrations of heavy metals, particularly manganese, aluminum and zinc. Iron and sulfate were very high and the pH ranged from 1.4 to 3.1. Georges Creek water had much lower concentrations of metals, iron and sulfate and a pH of about 7.0. The distribution of macrobenthos in Georges Creek showed the effects of both runoff from coal storage piles and periodic drought. Brillouin's diversity index values were low even in areas which did not dry. Densities of tubificid worms and chironomid larvae were very high above the coal storage areas where organic inputs were high. At all the rest of the sampling stations, macroinvertebrate densities were very low. Where coal pile runoff enters Georges Creek, it compounds the effects of periodic drought and further stresses the aquatic community.     

中试规模动力波吹脱技术分离老龄化垃圾渗滤液中的高浓度氨氮

为解决老龄化垃圾渗滤液的脱氨难题,采用动力波吹脱技术对老龄化垃圾渗滤液进行氨氮吹脱分离,探究了吹脱时间、pH、气液比、温度和进水氨氮浓度对吹脱效能的影响。单因素实验结果表明：前3 h吹脱去除率增长最快,5 h后吹脱去除率变化较小;高pH下游离氨占比增大,对吹脱更为有利,pH为10.5左右时的工艺最为经济;动力波吹脱适用温度范围广,在10 ℃和25 ℃时,去除率可达72.62%和90.68%;增加气液比可提高吹脱效率,但当气液比超过129后,吹脱效果增幅不明显;氨氮浓度对吹脱去除率的影响较小。正交实验结果显示：温度方差最大,pH、气液比方差次之,进水氨氮浓度方差最小,即表明温度对动力波吹脱脱氨影响最为显著;pH、气液比也是重要影响因素;初始氨氮浓度对吹脱效率影响不显著。在25 ℃、pH=10.5、气液比为129时,吹脱5 h的最优条件下,氨氮去除率约91.25%~94.15%。相比传统吹脱工艺,动力波吹脱技术能大幅提高氨氮分离效率。