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111.
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.  相似文献   
112.
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。  相似文献   
113.
以邻苯二甲酸二[2-乙基己]酯(DEHP)和邻苯二甲酸二丁酯(DBP)为研究对象,以废水污泥和填埋场沥出液为接种物,在严格厌氧环境下,进行了苯二甲酸酯生物降解的研究试验。结果表明,DBP有较好的可降解性,去除率大于95%;而DEHP在填埋场沥出液培养样中去除率小于30%;但当接种物为消化污泥时,DEHP的去除率为89.7%。产甲烷的微生物群在邻苯二甲酸二酯的降解过程中起着非常重要的作用。  相似文献   
114.
为了解垃圾渗滤液作培养液时草本植物种子萌发的情况。以黑麦草和高羊茅两种草本植物种子为研究材料,分别研究了垃圾填埋场渗滤液处理站的渗滤液原液、渗滤液生物处理出水以及渗滤液最终出水在6个不同配比的稀释溶液(V渗滤液/V蒸馏水=1/0,3/1,1/1,1/2,1/3,1/4)下对这两种种子萌发的影响。结果显示:随着渗滤液稀释强度的降低,种子的发芽势、发芽率、发芽指数和活力指数均增加,V渗滤液/V蒸馏水为1/3时,种子发芽率均为最高,黑麦草种子发芽率达96%,高羊茅种子发芽率达79%。用渗滤液作培养液时,更有利于黑麦草种子的萌发;用最终出水作培养液时,更有利于种子的萌发。这两种不同的渗滤液,在不同配比的稀释浓度下对种子的发芽率、发芽势、发芽指数和活力指数等均具有显著的生理作用。  相似文献   
115.
厌氧-好氧生物反应器填埋工艺特性研究   总被引:1,自引:0,他引:1  
基于生物反应器填埋技术,研究1种填埋场地循环操作的厌氧-好氧生物反应器填埋工艺,设计了该工艺模拟装置并研究了其运行工艺特性.厌氧阶段主要通过渗滤液回灌控制反应器工艺条件,主要试验结果为,pH值,R1在 6周后可上升至6.7~7.8,R2在17周内一直低于6.8;渗滤液COD浓度,R1在13周时下降至10?617 mg/L,R2在5周后上升至60?000 mg/L后长期趋于稳定;填埋气累计产量,R1在8周达到44%,R2几乎不产气.衡量稳定化可以分别采用渗滤液pH、COD浓度及BOD5/COD的减少率、填埋气的累计产率等指标来判断,并据此转换为好氧填埋运行.好氧阶段主要是通过强制通风来减少恶臭和水分,主要试验结果为,通风19d氨气浓度降为1.16 mg/m3,通风23d后恶臭浓度降为19;通风14d后含水率降为26%.完成此阶段的工艺指标值可依据矿化垃圾开采的最终用途确定.对主要试验数据进行了数值模拟.厌氧-好氧填埋过程的微生物演替经RISA分析,有4个优势菌群,一些兼性菌群在厌氧-好氧阶段起着重要的承前启后作用.  相似文献   
116.
生活垃圾焚烧厂贮坑沥滤液的负压蒸发预处理研究   总被引:3,自引:0,他引:3  
采用负压蒸发法处理上海市某大型生活垃圾焚烧发电厂贮坑沥滤液,实验研究了沥滤液蒸发过程中冷凝液组分的变化特征.结果表明:生活垃圾焚烧厂贮坑沥滤液中含有高质量浓度的挥发性污染物,低碳醇和碳原子数不大于7的挥发性有机酸(VFA)约占沥滤液中有机碳质量浓度的50%;沥滤液直接蒸发可将原液转化为原液量的84%,不含氨氮,有机物质量浓度为原液的21%,且90%以上为VFA及低碳醇的冷凝液,以及有机物质量浓度浓缩了4.4倍,适于焚烧处理的浓缩液;通过蒸发处理,沥滤液的处理难度大大降低,蒸发用能可取自焚烧热能回收后的低温位热能,降低了蒸发处理的费用.   相似文献   
117.
With the increase of urbanization, municipal solid waste has also increased. Therefore, the need for solid waste management is also increasing compared with earlier decades. Composting is a good option for the recycling of solid waste; however, it produces leachate, which requires proper treatment systems to prevent environmental degradation. Due to high chemical oxygen demand (COD) concentrations in compost leachate, anaerobic treatment is the best option for handling the effluent, and an anaerobic baffled reactor (ABR) is one such anaerobic reactor that can be used for its treatment. Because of high ammonia and heavy metal concentrations, as well as the possibility of sludge washout in ABRs, it is important to use proper media, such as zeolite, which can reduce inhibition effects and sludge washout from the reactor. Anaerobic treatment, especially during the methanogenesis phase, is sensitive, and pH and alkalinity are parameters that influence the treatment. Therefore, adjusting these parameters within a normal range is very important to the proper functioning of anaerobic systems. In this study, a pilot‐scale ABR was used, and the last 4 of the 8 ABR compartments were filled with zeolite. The bioreactor was operated at hydraulic retention times (HRT) of 3, 4, and 5 days, with zeolite filling ratios of 10%, 20%, and 30%, and influent COD concentrations of 10,000, 20,000, and 30,000 milligrams per liter (mg/L). In this study, pH value was 6.43 ± 0.1, 6.96 ± 0.3, and 6.96 ± 0.25 at filling ratios of 10%, 20%, and 30%, respectively. According to the results, in all filling ratios, no significant changes were observed in the pH value when the organic loading rate increased and its amount was within a constant range. Influent alkalinity was equal to 2015 ± 510, 2884 ± 505, and 4154 ± 233 milligrams of calcium carbonate per liter (mg CaCO3/L) at influent COD concentrations of 10,000, 20,000, and 30,000 mg/L, respectively, and in effluent, they were 2536 ± 336, 3379 ± 639, and 4377 ± 325 mg CaCO3/L, respectively. The amount of alkalinity in the effluent increased compared with the alkalinity in the influent. The results show that the amount of alkalinity in the influent and effluent was similar, and the alkalinity enhancement was lower when the filling ratio was increased from 10% to 20%, and 20% to 30%. Comparisons of the results from zeolite with and without biofilm showed that, in cases of zeolite with biofilm, the amounts of silica and oxygen decreased and the amount of carbon increased, and it showed the formation of biofilm on the surface of zeolite. In addition, the absence of sodium in the zeolite with the biofilm indicated that sodium was exchanged with ammonium ions. According to the results, zeolite can be used in anaerobic reactors as a medium, and it also reduces fluctuations in pH and alkalinity at different organic loading rates, providing a normal range for anaerobic treatment.  相似文献   
118.
垃圾渗滤液层状砂箱参数拟合试验及模拟   总被引:1,自引:0,他引:1  
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。  相似文献   
119.
The estimation of leachate quantities produced in landfills is necessary to dimension the treatment plants allowing to reduce the polluting load of these effluents and consequently avoid their negative impacts on the environment. Different leachate quantification methods were used in this study to assess the leachate volume produced at the Oum Azza landfill. The water balance method give comparable estimations of leachate production to the Ouled Berjal landfill ratio. The first method showed average values between 487 and 495 m3/day for 2015, 2018, and 2019, and at the same time, the second method gave values between 470 and 477 m3/day for the same years. In contrast, the World Bank ratio showed high values that vary between 2260 and 2295 m3/day for 2015, 2018, and 2019. The on-site data and the statistical analysis showed us that the World Bank ratio is not adapted for the estimation of the leachates produced in Oum Azza landfill, while the water balance and the ratio of Ouled Berjal landfill allowed to give comparable results to reality.  相似文献   
120.
Leachate generated in a landfill may not be treated by conventional biological treatment due to its nature and complexity. The process of forming aerobic granules in batch sequencing reactors having features such as; reducing the settling process time and saving energy consumption and high decomposition rate have been noticed by researchers. In the present study, the structure of sequencing batch reactors (SBRs) was evaluated for the formation of granules, which were subsequently utilized for the treatment of landfill leachate. The experiment was initiated by using the GSBR, containing 1200 ml with different apparatuses, to develop granular sludge, and synthetic wastewater was added to reinforcement. The selected parameters for the operational hydraulic retention time (HRT) of the wastewater (6-h cycles) included feeding, idle, aeration, settling, and discharge. Furthermore, the controlled conditions were the dissolved oxygen (DO) range of 2–2.2 mg/L, temperature range of 20–23℃, and pH of 7.5–8.3. The chemical oxygen demand (COD), mixed liquor suspended solids (MLSS), and sludge volume index (SVI) daily were measured at the influent and effluent of GSBR reactor. The main properties of aerobic granular sludge were identified during the research procedures, and the remarkable settling and potent, high-density microbial structure of the granules were confirmed. The mean size of the formulated granules was estimated at 7.46 ± 1.8 mm, and the volume of the biomass also increased from approximately 1607 to 4137 mg/L through the granulation process. Moreover, 98% of the influent chemical oxygen demand (COD) could be removed by the formulated granular sludge, and the final-stage organic loading rate was estimated at 5.65 COD/m3/day. According to the results, GSBRs could be employed for the formulation of aerobic granular sludge for the treatment of landfill leachate.  相似文献   
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