臭氧氧化法处理反渗透浓缩垃圾渗滤液

采用臭氧氧化法处理经反渗透膜处理后的浓缩垃圾渗滤液，考察了反应时间、臭氧投量、pH和温度对COD，色度以及浓缩液中腐殖酸的去除影响，通过BOD₅/COD变化分析了臭氧氧化对浓缩液生化性的提高作用。结果表明：在pH 8.0，温度30℃，臭氧投量5 g/h，反应时间90 min的条件下，浓缩液的COD、色度以及浓缩液中腐殖酸的去除率分别达到67.6%、98.0%和86.1%， BOD₅/COD从0.008提升到0.26，生化性有很大提高。     

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。     

阳极氧化联合电-Fenton氧化深度处理垃圾渗滤液

采用多孔碳素阴极、Ti/SnO2-Sb2O5-IrO2阳极构建电化学氧化系统用于渗滤液的深度处理。研究结果表明,所构建的电化学氧化系统通过阳极氧化和电-Fenton氧化2种机制降解有机污染物;处理过程中阴极表面形成的沉淀物对TOC和COD的衰减也产生了影响。在阴极电位为-1.0 V、Fe2+初始浓度为0.5 mmol/L的条件下,电化学处理120 min获得了58%的TOC去除;处理480 min COD去除率为55%,NH3-N去除率为99%,TN去除率为60%,色度几乎被完全去除。GC-MS分析结果表明,渗滤液中以腐殖质类物质为主的有机化合物被降解为分子量相对较小的有机物,直至完全矿化。联合阳极氧化和电-Fenton氧化机制的电化学处理方法为垃圾渗滤液深度处理提供了新的选择。     

太阳光Fenton法处理垃圾渗滤液中有机污染物

研究利用太阳光Fenton法处理垃圾渗滤液。根据太阳光辐射强度随时间的变化规律，选择重庆7、8月份的晴天，在中午12：00到下午14：00时进行试验，研究太阳光辐射时间、pH值、Fenton试剂用量对垃圾渗滤液COD去除率的影响。研究结果表明：太阳光Fenton法对垃圾渗滤液的COD有较好的去除效果，COD去除率达86.2%。太阳光Fenton法处理垃圾渗滤液的优化条件是：日光辐射时间为120 min，pH值为2.5，Fe²⁺浓度为5 mmol/L，H₂O₂浓度为570 mmol/L。同时，论文还对太阳光Fenton法处理垃圾渗滤液的动力学进行分析。研究结果显示：太阳光Fenton法处理垃圾渗滤液，其表观动力学方程为-dC/dt=2.6×10^-8×P^1.92×F^1.79×E^1.67。     

TiO2光催化降解水中土霉素的动力学研究

环境中抗生素的出现及其引起的危害正受到越来越多的关注。以高压汞灯为光源，选用较为广泛的抗生素土霉素（OTC）为处理对象。考察了初始质量浓度、反应过程中光照、催化剂投加量、溶液起始pH、溶液中DOM和NO^-₃对光催化降解的影响，研究了其光降解动力学。结果表明，TiO₂光催化氧化法能够有效去除水中半微量的OTC，OTC的光降解过程符合一级反应动力学模型；UV/TiO₂联用工艺对TOC也有很好的去除效果，反应90 min，TOC去除率可达74%；OTC的初始浓度从30 mg/L增大到90 mg/L，反应速率从0.0619 min^-1降低到0.0130 min^-1；随着光催化剂投加量的增大，光降解速率常数先增大后减小；增加溶液的pH值，速率常数逐渐减小；溶液中的DOM和NO^-₃也可以影响光降解效率。     

臭氧预氧化-BAF工艺深度处理垃圾渗滤液

以广东省江门市垃圾填埋场垃圾渗滤液为研究对象，对经SBR生化处理和聚合硫酸铁混凝后的垃圾渗滤液，采用臭氧-BAF(曝气生物滤池)工艺进行深度处理。该工艺优点在于：臭氧高级氧化技术使大分子有机污染物降解成二氧化碳和水，或者小分子有机污染物，有利于后继BAF的生化处理，且臭氧处理过后废水的色度明显降低，是废水处理的有效方法之一。而后采用曝气生物滤池对垃圾渗滤液进行进一步处理，对COD进一步去除。结果表明，当臭氧的加入量为150 mg/L，BAF停留时间＞4 h，出水COD低于85 mg/L，稳定达到国家GB 16889-1997《生活垃圾填埋污染控制标准》一级排放标准，臭氧氧化法处理每吨垃圾渗滤液的费用为4.8元。     

直接红染料的臭氧脱色与中间产物研究

以直接红B模拟染料废水为研究对象，考察了臭氧化过程中染料溶液的吸光度和TOC的变化，同时利用离子色谱仪和GC/MS对染料的降解过程进行了分析，最后用发光细菌法检测了染料溶液急性毒性的变化。结果表明，臭氧对染料的降解符合一级反应动力学，20 min时对染料的脱色率达到99.2%；反应40 min后TOC减少32.55%，染料分子有97.8%的S被氧化为SO^2-₄，偶氮键被臭氧化为N₂，分子中的仲胺基小部分转化成游离NH⁺₄和NO^-₃；在臭氧化过程前期新生成的醛类和酰胺类物质使溶液急性毒性迅速上升，25 min后溶液毒性开始逐渐下降。     

臭氧辅助UV/Fenton法处理电镀添加剂生产废水

采用臭氧辅助光芬顿法处理电镀添加剂生产废水，考察双氧水、FeSO₄·7H₂O、pH和反应时间等因素对废水COD和UV₂₅₄去除的影响。实验结果表明，pH=4，臭氧通入量为0.25 g，双氧水的投加量93.3 mL/L，FeSO₄·7H₂O投加量为5.3 g/L，最佳反应时间为30 min，COD和UV₂₅₄去除率分别达到92.64%和87.95%。这表明，臭氧辅助光芬顿法对电镀添加剂生产废水处理效果显著，处理时间大大减少。     

活性炭纤维上4-氯酚及焦化废水尾水的O3催化氧化降解实验研究

选择YT-1000型活性炭纤维（ACF）作为催化剂，考察ACF与O₃协同作用催化降解水溶液中4-氯酚的最佳反应条件，并将该条件应用于焦化废水生物处理尾水中难降解有机污染物的催化氧化。ACF表面具有丰富的微孔结构，对4-氯酚有良好的吸附作用，在动力学上提高了其与O3反应的起始浓度，并且在ACF表面含氧、含氮等基团的催化作用下发生氧化反应，1 L浓度为100 mg/L的4-氯酚水样中投加2 g ACF反应6 min时，吸附作用对TOC的去除率为43.4%，而ACF协同O₃作用时的TOC去除率提高到72.5%，协同增效作用为67.1%；在选定的反应条件下，ACF协同O₃降解焦化废水生物处理尾水，60 min时的TOC与色度的去除率分别达到56.8%和96.3%。上述研究过程证明了吸附作用与催化作用的协同能有效降解生物过程不能降解的焦化废水中惰性有机污染物。     

微波-Fenton 氧化-PAFSi 絮凝法处理含油废水简

采用微波-Fenton氧化-PAFSi絮凝法处理含油废水，结果表明，200 mL水样先经微波辐射6 min，在pH=2，H₂O₂（30%）3.5 g/L，Fe²⁺ 1.3 g/L的条件下氧化4 h后，采用聚硅酸铝铁（Al：Fe：Si=10：2：1）和聚丙烯酰胺在pH=8时进行絮凝实验，处理后废水浊度、SS、COD、含油量和色度分别降低了99.46%、96.66%、91.94%、97.97%和95.00%，且经处理后废水的BOD₅/COD由原水的0.04提高到0.53。实验还分析了含油废水的降解机理。     

Biogeochemical processes at the fringe of a landfill leachate pollution plume: potential for dissolved organic carbon, Fe(II), Mn(II), NH4, and CH4 oxidation

Various redox reactions may occur at the fringe of a landfill leachate plume, involving oxidation of dissolved organic carbon (DOC), CH4, Fe(II), Mn(II), and NH4 from leachate and reduction of O2, NO3 and SO4 from pristine groundwater. Knowledge on the relevance of these processes is essential for the simulation and evaluation of natural attenuation (NA) of pollution plumes. The occurrence of such biogeochemical processes was investigated at the top fringe of a landfill leachate plume (Banisveld, the Netherlands). Hydrochemical depth profiles of the top fringe were captured via installation of a series of multi-level samplers at 18, 39 and 58 m downstream from the landfill. Ten-centimeter vertical resolution was necessary to study NA within a fringe as thin as 0.5 m. Bromide appeared an equally well-conservative tracer as chloride to calculate dilution of landfill leachate, and its ratio to chloride was high compared to other possible sources of salt in groundwater. The plume fringe rose steadily from a depth of around 5 m towards the surface with a few meters in the period 1998-2003. The plume uplift may be caused by enhanced exfiltration to a brook downstream from the landfill, due to increased precipitation over this period and an artificial lowering of the water level of the brook. This rise invoked cation exchange including proton buffering, and triggered degassing of methane. The hydrochemical depth profile was simulated in a 1D vertical reactive transport model using PHREEQC-2. Optimization using the nonlinear optimization program PEST brought forward that solid organic carbon and not clay minerals controlled retardation of cations. Cation exchange resulted in spatial separation of Fe(II), Mn(II) and NH4 fronts from the fringe, and thereby prevented possible oxidation of these secondary redox species. Degradation of DOC may happen in the fringe zone. Re-dissolution of methane escaped from the plume and subsequent oxidation is an explanation for absence of previously present nitrate and anaerobic conditions in pristine groundwater above the plume. Stable carbon isotope (delta13C) values of methane confirm anaerobic methane oxidation immediately below the fringe zone, presumably coupled to reduction of sulfate, desorbed from iron oxide. Methane must be the principle reductant consuming soluble electron-acceptors in pristine groundwater, thereby limiting NA for other solutes including organic micro-pollutants at the fringe of this landfill leachate plume.     

Treatment of landfill leachate by electrochemical oxidation and anaerobic process.

The removal performance of typical refractory organic compounds in landfill leachate was investigated during the electrochemical (EC) oxidation and anaerobic process combined treatment system in this paper. The results indicated that the treatment of landfill leachate by the combined system was highly effective. The toxicity of leachate was notably decreased after the electrochemical oxidation process and the biodegradability was improved. The concentration of the organic acid with low molecular weight in the leachate increased from 28% to 90% based on the biodegradability assays after the EC oxidation process. The anaerobic digestion could further remove the residual organic compounds. At a hydraulic retention time (HRT) of 16 hours and an organic loading rate (OLR) of 8 kg COD/m3 d, the concentration of COD, SS, ALK, VA, N-TKN, N-NH4+ and P-PO4(3)- [corrected] in UASB effluent were 532, 12, 6744, 400, 540, 455 and 11.6 mg/L, respectively, with approximately 90% removal efficiency of COD. The organic compounds in the landfill leachate revealed different degradation characteristics in the combined system. p-chloroaniline, bisphenol A, 6-methyl-2-phenyl-quinoline, dimethylnaphthaline and N'-(2-methyl-4-chlorophenyl)-N-cyclohexyformamidine, classified into the first group in this paper, were completely removed by the EC oxidation and did not reappear in the effluent of the UASB reactor. Phenylacetic acid, 3-methyl-indole and N-cyclohexyl-acetamide, called the second group, were completely removed, but reappeared in the UASB reactor. 4-methyl-phenol, 3,4-dihydroisoquinoline, 2(3H)-benzothiazolone, exo-2-hydroxycineole and benzothiazole, the third group, were degraded little in the EC oxidation process, but extensively removed by the anaerobic process. Benzoic acid, benzenepropanoic acid and 2-cyano-3,5-dimethyl-1-hydroxypyrrole, the fourth group, concentration obviously increased in the EC process, but was completely removed in the UASB reactor. The content of volatile fatty acids (VFAs) markedly increased from 0.68% in the leachate to 16.18% in the effluent from the electrochemical oxidation process (EC(effl)). In addition, the degradation rate of organic compounds from the landfill leachate was different in the EC oxidation and anaerobic process.     

Using FeGAC/H2O2 process for landfill leachate treatment

Due to the growing concern of highly contaminated landfill leachate problems in Taiwan, an innovative advanced catalytic oxidation (FeGAC/H(2)O(2)) process was developed and employed in this research to treat the landfill leachate from central Taiwan. Experimental results indicated that the FeGAC/H(2)O(2) process could effectively remove organic compounds from landfill leachate. The presence of iron oxide coated granular activated carbon (FeGAC) greatly improved the oxidative ability of H(2)O(2) for the removal of humic acids, fulvic acids and non-humic substance from leachate. For instance, at pH 6, the removal efficiencies of FeGAC/H(2)O(2) and H(2)O(2) processes were 70% and 8%, respectively. FeGAC/H(2)O(2) combined both advantages of FeGAC and H(2)O(2) where FeGAC had good organics adsorption ability and could effectively catalyse the hydrogen peroxide oxidation reaction for organics removal.     

生物流化床厌氧氨氧化脱氮处理垃圾渗滤液的研究

采用厌氧流化床反应器 (AFB)作为厌氧氨氧化反应器 ,对垃圾渗滤液脱氮进行了研究。以模拟废水完成了反应器的启动 ,然后加入一定比例的垃圾渗滤液 ,对垃圾渗滤液厌氧氨氧化脱氮的影响因素进行了研究 ,取得了较好的脱氮效果。实验表明 ,厌氧氨氧化脱氮对高氨氮浓度的垃圾渗滤液的处理具有较大的潜力。     

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。     

Methane balance of a bioreactor landfill in Latin America

This paper presents results from a methane (CH4) gas emission characterization survey conducted at the Loma Los Colorados landfill located 60 km from Santiago, Chile. The landfill receives approximately 1 million metric tons (t) of waste annually, and is equipped with leachate control systems and landfill gas collection systems. The collected leachate is recirculated to enable operation of the landfill as a bioreactor. For this study, conducted between April and July 2000, a total of 232 surface emission measurements were made over the 23-ha surface area of the landfill. The average surface flux rate of CH4 emissions over the landfill surface was 167 g x m(-2) x day(-1), and the total quantity of surface emissions was 13,320 t/yr. These values do not include the contribution made by "hot spots," originating from leachate pools caused by "daylighting" of leachate, that were identified on the landfill surface and had very high CH4 emission rates. Other point sources of CH4 emissions at this landfill include 20 disconnected gas wells that vent directly to the atmosphere. Additionally, there are 13 gas wells connected to an incinerator responsible for destroying 84 t/yr of CH4. The balance also includes CH4 that is being oxidized on the surface of the landfill by meth-anotrophic bacteria. Including all sources, except leachate pool emissions, the emissions were estimated to be 14,584 t/yr CH4. It was estimated that less than 1% of the gas produced by the decomposition of waste was captured by the gas collection system and 38% of CH4 generated was emitted to the atmosphere through the soil cover.     

Investigation of 1,4-dioxane originating from incineration residues produced by incineration of municipal solid waste

As a groundwater contaminant, 1,4-dioxane is of considerable concern because of its toxicity, refractory nature to degradation, and rapid migration within an aquifer. Although landfill leachate has been reported to contain significant levels of 1,4-dioxane, the origin of 1,4-dioxane in leachate has not been clarified until now. In this study, the origins of 1,4-dioxane in landfill leachate were investigated at 38 landfill sites and three incineration plants in Japan. Extremely high levels of 1,4-dioxane 89 and 340 microg l(-1), were detected in leachate from two of the landfill sites sampled. Assessments of leachate and measurement of 1,4-dioxane in incineration residues revealed the most likely source of 1,4-dioxane in the leachate to be the fly ash produced by municipal solid waste incinerators. Effective removal of 1,4-dioxane in leachate from fly ash was achieved using heating dechlorination systems. Rapid leaching of 1,4-dioxane observed from fly ash in a sequential batch extraction indicated that the incorporation of a waste washing process could also be effective for the removal of 1,4-dioxane in fly ash.     

凤眼莲去除垃圾渗滤液中的COD、NH3-N和TP

在静态水培实验条件下,对不同浓度垃圾渗滤液条件下凤眼莲的生长状况及其净化效果进行了研究。结果表明,在高浓度(COD 3 546.7 mg/L、NH3-N 527.5 mg/L、TP 8.02 mg/L)垃圾渗滤液条件下(HCL)凤眼莲全部被毒害致死,在中浓度(COD 1 233.3 mg/L、NH3-N 182.9 mg/L、TP 2.83 mg/L)垃圾渗滤液条件下(MCL)生长状况差,生物量减少为实验前的32.6%。在低浓度(COD 660.0 mg/L、NH3-N 99.7 mg/L、TP 1.59 mg/L)垃圾渗滤液条件下(LCL)能够正常生长,且对低浓度垃圾渗滤液有较好的净化效果。24 d后COD、NH3-N和TP的去除率分别为85.9%,99.8%和84.8%。COD与NH3-N均达到《生活垃圾填埋场污染控制标准(GB16889-2008)》排放标准,TP达到《地表水环境质量标准(GB 3838-2002)》Ⅳ类排放标准。