紫外光催化氧化-原子吸收分光光度法测定垃圾渗滤液中重金属的研究

本文采用二氧化钛为催化剂,通过使用光催化氧化的消解方法对垃圾渗滤液样品进行前处理,再用原子吸收分光光度法测定垃圾渗滤液中的重金属,并与常用消解方法进行对比,探讨了紫外光照射时间、紫外灯功率、H2O2的用量等因素对消解效果所产生的影响,选取了消解垃圾渗滤液的最佳条件,讨论了方法的准确度与精密度。     

Evaluation of groundwater flow patterns around a dual-screened groundwater circulation well

Dual-screened groundwater circulation wells (GCWs) can be used to remove contaminant mass and to mix reagents in situ. GCWs are so named because they force water in a circular pattern between injection and extraction screens. The radial extent, flux and direction of the effective flow of this circulation cell are difficult to measure or predict. The objective of this study is to develop a robust protocol for assessing GCW performance. To accomplish this, groundwater flow patterns surrounding a GCW are assessed using a suite of tools and data, including: hydraulic head, in situ flow velocity, measured hydraulic conductivity data from core samples, chemical tracer tests, contaminant distribution data, and numerical flow and transport models. The hydraulic head data show patterns that are consistent with pumping on a dual-screened well, however, many of the observed changes are smaller than expected. In situ thermal perturbation flow sensors successfully measured horizontal flow, but vertical flow could not be determined with sufficient accuracy to be useful in mapping flow patterns. Two types of chemical tracer tests were utilized at the site and showed that much of the flow occurs within a few meters of the GCW. Flow patterns were also assessed based on changes in contaminant (trichloroethylene, TCE) concentrations over time. The TCE data clearly showed treated water moving away from the GCW at shallow and intermediate depths, but the circulation of that water back to the well, except very close to the well, was less clear. Detailed vertical and horizontal hydraulic conductivities were measured on 0.3 m-long sections from a continuous core from the GCW installation borehole. The measured vertical and horizontal hydraulic conductivity data were used to construct numerical flow and transport models, the results of which were compared to the head, velocity and concentration data. Taken together, the field data and modeling present a fairly consistent picture of flow and transport around the GCW. However, the time and expense associated with conducting all of those tests would be prohibitive for most sites. As a consequence, a sequential protocol for GCW characterization is presented here in which the number of tools used can be adjusted to meet the needs of individual sites. While not perfect, we believe that this approach represents the most efficient means for evaluating GCW performance.     

Repeated use of MAP decomposition residues for the removal of high ammonium concentration from landfill leachate

The residues of magnesium ammonium phosphate (MAP) decomposed by heating under alkali conditions were repeatedly used as the sources of phosphate and magnesium for the removal of high ammonium concentration from landfill leachate. Up to 96% of ammonium in MAP powder could be released under the following conditions: NH4(+):OH- molar ratio, 1:1; temperature, 90 degrees C; heating time, 2 h. Fourier transform infrared spectra and X-ray diffraction analysis of MAP before and after heating demonstrated that MAP was mainly transformed to amorphous magnesium sodium phosphate (MgNaPO4), which makes it possible for the NH4(+) to replace Na+ in MgNaPO4 to form more stable struvite. Successful ammonium removal was achieved by using the MAP decomposition residues as the sole phosphate and magnesium sources. The ammonium removal decreased gradually following the increase of MAP reuse cycles, and in the 6th cycle, ammonium removals of 84% and 62% were achieved for synthetic wastewater and landfill leachate, respectively. Analysis of the surfaces of MAP powders acquired at different reuse cycles using scanning electron microscopy with energy dispersive X-ray suggested that the existence of calcium, kalium and aluminum ions in landfill leachate might have inhibited the formation of MAP through competition with ammonium ions for phosphate ions. It is estimated that reuse of MAP for 3 cycles could save about 44% chemical costs.     

城市垃圾填埋场渗滤液中污染物检测与分析

垃圾渗滤液水质复杂,危害性大,对其无害化处理尚未得到很好解决。溶解性有机物(DOM)是导致渗滤液处理难以达标的主导性污染物。采用GC-MS技术可将渗滤液中DOM标识划分为亲水性和疏水性两类物质,为DOM的针对性处理提供了新的思路。采用ICP-AES从渗滤液中检测出美国环境保护局颁布的13种优先污染重金属中的11种,其含量大幅超标。废弃的电子材料、颜料涂料、电池以及药物等物质的不分类收集是导致渗滤液中重金属浓度超标、毒性增强的主要原因。在垃圾渗滤液处理领域,认为BOD5/COD小于0.3就不可以采用生物法处理的传统观点已经不符合实验与工程现实。通过检测与分析,掌握了垃圾渗滤液的水质特性与污染源头,能够为制定切实可行的处理方案提供借鉴。     

城市污水厂污泥倾倒对海洋生物的毒性研究

以广州市和佛山市的5个城市污水处理厂的污泥为实验对象,选取费氏弧菌、蒙古裸腹溞、卤虫、裸项栉鰕虎鱼仔鱼4种不同营养级的海洋生物为受试对象,结合化学分析方法,研究广州区域周边污水污泥浸出液的生物毒性效应。结果显示各污水污泥浸出液的毒性均较大,且浸出液的Cu污染浓度较高;广州市污水污泥对4种受试生物的毒性效应要高于佛山市。从污泥毒性对受试生物的选择性方面分析,发现卤虫筛分能力强且灵敏度高,而费氏弧菌则相关性好且方法简捷。研究结果为反映城市污泥的生物毒性强度和选择合适毒性评价受试生物提供基础数据。     

Solar photocatalytic treatment of landfill leachate using a solid mineral by-product as a catalyst

The treatment of municipal solid waste landfill leachate in a pilot plant made up of solar compound parabolic collectors, using a solid industrial titanium by-product (WTiO₂) containing TiO₂ and Fe(III) as a photocatalyst, was investigated. In the study evidence was found showing that the degradation performed with WTiO₂ was mainly due to the Fe provided by this by-product, instead of TiO₂. However, although TiO₂ had very little effect by itself, a synergistic effect was observed between Fe and TiO₂. The application of WTiO₂, which produced coupled photo-Fenton and heterogeneous catalysis reactions, achieved a surprisingly high depuration level (86% of COD removal), higher than that reached by photo-Fenton using commercial FeSO₄ (43%) in the same conditions. After the oxidation process the biodegradability and toxicity of the landfill leachate were studied. The results showed that the leachate biodegradability was substantially increased, at least in the first stages of the process, and again that WTiO₂ was more efficient than FeSO₄ in terms of increasing biodegradability.     

Application of hydration reaction on the removal of recalcitrant contaminants in leachate after biological treatment

Leachate contains amounts of non-biodegradable matters with COD range of 400–1500 mg/L after the biological treatment, and should be removed further to attain the Chinese discharge standards. Hydration reaction has the potential to combine and solidify some recalcitrant substances, and thus could be applied as the advanced leachate treatment process. It was found that COD and NH₃N decreased from 485 to <250 mg/L and 91 to 10 mg/L, with the removal rate over 50% and 90% in the first 6 d, respectively, and COD and NH₃N removal capacity were around 23.7 and 9.2 mg/g under the test conditions. The percentage of the substances with low Mn range of <1000 decreased from 32.9% to 3.2% in leachate after hydration reaction. Tricalcium aluminate, tricalcium silicate and dicalcium silicate were the most activity compounds successively for the pollutant removal in leachate, and hydration reaction could be the option for the advanced wastewater treatment process thereafter.     

山谷型填埋场渗滤液现场实验研究

以稳定渗滤液为处理对象,通过对其在山谷型填埋场覆盖层进行亚表面灌溉,研究了不同植被条件下植物的适应性、渗滤液水量削减负荷、COD和氨氮的去除率,以及灌溉对大气环境的影响。研究表明:夹竹桃是最适合进行渗滤液灌溉处理的植被;高羊茅作为草本植物,可作为夹竹桃的替代,也可与夹竹桃复种,形成双层植被;在渗滤液灌溉水力负荷为6mm/d、COD平均值为890mg/L、氨氮平均值为240mg/L的情况下,各灌溉区灌溉水量可削减50%～80%,COD平均去除率在90%以上,氨氮平均去除率在96%以上。     

几种模拟处理方式污泥淋出液重金属与养分特征

为了减少城市污泥重金属对农田的污染,更好地实现污泥农业资源化利用,通过盆栽实验研究不同处理(对照、黑网、附Fe黑网、附Fe黑网+K2SO4及附Fe黑网+玉米)对城市污泥淋出液重金属和养分含量等的影响。结果表明,黑网可降低污泥淋出液的Zn﹑Cd总量,且没有减少污泥淋出液中氮、磷和钾的总量。Fe(OH)3可使淋出液中Zn总量降低,但同时也显著减少了淋出液中的磷总量。K2SO4可降低淋出液中的Cu总量,且促进Fe结合磷的释放。玉米的种植可使污泥的总重降低,同时玉米籽粒和茎叶重金属含量达到饲料标准。综合来看,任何处理每次淋出液的Cu、Zn、Pb、Cd浓度均符合农田灌溉水标准,淋出液氮、磷、钾量占原污泥中氮、磷、钾总量的比例(0.98%～9.88%)远远大于重金属元素(Cu,Zn,Pb,Cd)占原污泥对应重金属总量的比例(0.04%～0.41%),污泥淋出液作为农田灌溉水进行肥水利用将是污泥农业资源化利用的适合途径,同时黑网+玉米处理可能是较理想的污泥综合处理利用方式。     

三峡库区垃圾渗滤液-城镇污水合并处理时的重金属含量研究

应用微波消解-电感耦合等离子体发射光谱法（ICP-OES）测定三峡库区垃圾渗滤液、渗滤液城镇污水合并处理厂进、出水以及剩余污泥中重金属元素的浓度。结果表明,合并处理后,除5个污水厂出水Ni超标（浓度为59.79～104.30 μg/L）外,其余重金属元素均低于GB 18918-2002污水排放标准;剩余污泥中的总重金属含量在15.31～27.73 g/kg之间,各元素含量均远低于污泥农用标准。因此,在目前各合并处理厂的运行条件下,控制渗滤液与城镇污水比例在1∶2 700～1∶50（V/V）范围内,渗滤液汇入生活污水进行合并处理是解决渗滤液重金属污染的有效方式。