广州城市污泥中重金属的含量、排放通量及农用风险评价

分析了广州市中心城区5个主要的污水处理厂污泥的基本理化性质和7种重金属(Cr、Cu、Mn、Ni、Pb、Cd和Zn)在不同雨期的浓度变化,估算了广州市污水处理厂污泥重金属的年排放通量,并对其污泥农用做了潜在风险评价。结果表明,各污水厂污泥均达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)对重金属的排放要求,污泥的基本理化性质满足《城镇污水处理厂污泥处置农用泥质》(CJ/T309-2009)标准,沥滘、猎德、京溪和大坦沙污水厂的污泥重金属满足CJ/T309-2009要求,而西朗污水处理厂2013年12月采集的污泥中Cu和Cd未达标。通过估算,广州市污水处理厂污泥中Cr、Cu、Mn、Ni、Pb、Cd和Zn的年排放通量分别为16.1、18.8、90.3、5.9、7.9、0.2和48.3 t。通过Hakanson生态风险评估,污泥在农用过程中除西朗污水处理厂污泥重金属危害为中等风险,其他厂污泥属于低风险。     

芦苇和香蒲在人工湿地城市污泥处理系统中的应用

用有机玻璃材料做成模拟人工湿地,分别种植芦苇和香蒲考察2种模拟植物湿地对城市污泥干化和稳定化、污泥中营养元素和重金属去除效果,并和空白湿地对比。实验污泥取自当地污水厂二沉池,污水处理采用厌氧池加氧化沟工艺。模拟人工湿地进泥负荷为0.72 kg TS/(m2.d),进泥中TS平均含量为5.58 g/L,pH为6.80。实验期为1年,采用间歇式进泥,渗滤液月采集测样一次,湿地剩余污泥2月1次。实验结果受天气和气候影响较大,处理效果夏季好于冬季,出水水质和剩余污泥的干化及稳定效果芦苇湿地好于香蒲湿地。剩余污泥中各种重金属含量低于污泥农用标准中各重金属离子浓度要求。结果表明,人工湿地植物净化系统对城市污泥有较好的脱水和稳定化效果。     

污水厂出水回用于污泥焚烧烟气的净化

开展了污水处理厂出水回用于污泥焚烧烟气净化的实验研究。生化出水净化吸收污泥焚烧烟气的效果与气水比、进气浓度、进水pH、进水碱度和水温等因素有关。研究结果表明,气水比10∶1,进水pH为7条件下,生化出水能够有效吸收污泥焚烧烟气中的各种污染物质,出气中气体污染物低于《生活垃圾焚烧污染控制标准》（GB18485-2001）的排放限值要求,吸收后出水各指标均低于《污水综合排放标准》（GB8978-1996）中污染物排放限值的要求。该工艺脱硫效率可达90%,具有系统简单可靠、以废治废、不产生二次污染等优点。     

MBBR-SA工艺处理模拟大豆深加工废水厌氧出水及污泥减量化

针对大豆深加工高浓度有机废水厌氧出水的特点,采用移动床生物膜反应器-沉淀池-厌氧池(MBBR-SA)工艺进行处理,重点考察了其COD去除、脱氮以及污泥减量化的性能。处理前厌氧出水水质参数为COD 1 350～1 851 mg/L、TN 45～73 mg/L和TP 35～55 mg/L。结果表明,经过70 d的运行,在最佳水力停留时间(HRT)1.68 d与最佳回流比0.75条件下,出水平均COD、TN和NH4+-N浓度分别为91.5、12.4和11.4 mg/L,分别达到了《城镇污水处理厂污染物排放标准》二级标准、二级标准和一级B标准,其平均去除率分别为96.0%、87.4%和88.3%;该工艺未排放剩余污泥,其表观污泥产率为0.13,比MBBR降低了43.5%,具有明显的污泥减量化特性。     

城市污水厂污水污泥的热值测定分析方法研究

建立热力学指标是污水生物处理过程热力学分析的基础工作,目前仍缺乏污水污泥化学能测试的标准方法。采用IKA C5000型自动热量计对某城市二级污水处理厂进水、出水、初沉污泥、剩余污泥、混合污泥和脱水污泥进行了热值测定,样品前处理采用103～105℃烘干获得干燥基,用苯甲酸进行加标回收。参照煤的发热量测定方法得到样品的高位热值。试验结果显示：出水干燥基的热值为05 kJ/g,进水干燥基的热值为4 kJ/g以上,各工艺段的污泥干燥基热值较高,基本都在12 kJ/g以上,接近右江褐煤水平。测定结果的标准偏差≤±0.452%,相对标准偏差≤±0.136%。通过同一批样品的元素分析及Dulong公式理论推算,发现2种方法可得到相似的结果。     

热水解对缺氧/好氧膜生物反应器同步处理污水及污泥减量的影响研究

研究了剩余污泥热水解后的回流对缺氧/好氧膜生物反应器(AOMBR)同步处理污水及污泥减量的影响。试验通过与常规AOMBR工艺对比,考察了污泥热水解回流量对系统污泥浓度、污泥产率、出水水质的影响。试验结果表明,当热水解污泥回流量分别为剩余污泥量的100%、75%、50%时,热水解会一定程度提高系统的污泥浓度,但污泥总量却分别削减了20.2%、21.2%和13.1%,系统污泥产率分别下降了46%、54%和33%,剩余污泥排放量分别削减了100%、75%、50%。两套工艺的平均出水COD、NH+4-N、TN分别在40、3、5mg/L以下,均能达到《城镇污水处理厂污染物排放标准》(GB 18918—2002)的一级A排放标准。因此,热水解污泥的回流并不会对系统的出水水质产生明显影响,同时能够显著削减污泥总量。     

3种组合工艺处理农村生活污水

进行了厌氧折流板反应器-垂直潜流人工湿地(ABR-VSFCW)、复合厌氧反应器-水平潜流人工湿地(HAR-HSFCW)、膨胀颗粒污泥床-人工快速渗滤系统(EGSB-CRI)3种组合工艺处理农村生活污水的研究。结果表明,在温度为10~29℃,进水COD为325.3~386.5 mg/L的条件下,3种组合工艺对COD均有较高的处理效果,当厌氧段HRT大于16 h时,3种组合工艺出水COD浓度均达到了我国《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准;EGSB-CRI、HAR-HSFCW对TP的去除效果较好,出水TP浓度均达到了我国《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级B标准,且显著优于ABR-VSFCW,ABR-VSFCW出水TP浓度达到了二级标准;ABR-VSFCW、HAR-HSFCW、EGSB-CRI出水NH+4-N浓度分别为25.24~42.20、29.59~41.60和9.80~15.35 mg/L,其出水NH+4-N浓度达到了我国《城镇污水处理厂污染物排放标准》(GB 18918-2002)二级标准;3种组合工艺对TN的去除效果无明显差异,去除率仅为23.9%~46.4%。因此,EGSB-CRI对农村生活污水的处理效果最好,HAR-HSFCW次之,ABR-VSFCW较差。     

超声波处理回流剩余污泥对SBR工艺的污泥减量效能

在SBR中试系统中,采用较高声能密度较短时间的超声波处理剩余污泥后回流至系统连续运行20 d的方式进行污泥减量,通过分析测定系统MLSS、累计排泥量以及系统出水水质指标,考察了系统污泥减量效果及污泥回流对系统污水处理效果的影响。结果表明,对SBR系统2/3的剩余污泥用声能密度为1 W/mL的超声波预处理6 min后回流至SBR系统。SBR系统最终需处置的污泥量减少了45.64%,获得了理想的污泥减量效果。污泥回流后SBR系统对SS、COD、TN以及NH4+-N的去除效果均无明显变化,仅出水TP含量略高于对照的SBR,出水水质仍能达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级B标准。     

微波法制备污泥活性炭研究

采用微波加热法,以污水厂剩余污泥为原料,磷酸为污泥活化剂制备污泥活性炭.微波功率、辐照时间和磷酸浓度对污泥活性炭吸附性能具有显著影响,在最佳工艺条件微波功率480 W、辐照时间315 s和磷酸浓度40%条件下制得的活性炭碘值301 mg/g,比表面积168 m2/g,污泥中重金属绝大部分被固化.与传统商品炭相比,污泥炭孔隙结构以中孔为主.利用该活性炭处理城市生活污水处理厂出水,COD去除率可达87%以上,污泥炭的吸附等温线用Langmuir等温吸附模型进行描述.     

中国城镇污水处理厂运行状况调查分析

根据问卷调查资料和抽样监测数据,分析了中国城镇污水处理厂的工艺水平、实际运行负荷、水质稳定性以及剩余污泥处理处置等方面的现状与问题.通过调查分析可知,近年来,中国的城镇污水处理事业得到了前所未有的发展,但城镇污水处理工作中也存在着一些明显不足,其主要表现为:(1)由于配套管网建设滞后和运行费用不足等问题,导致实际污水处理量未能与污水处理能力保持同步增长.近1/3数量的污水处理厂的运行负荷率低于70%,造成1/4以上的污水处理能力被闲置.(2)污水处理厂出水水质的稳定性普遍不高,一些传统的处理工艺则更差.(3)污泥不经脱水即随意外运、乱弃的现象已有很大改观,但绝大部分污泥都未经稳定化处理,更为严重的是仍有少部分污泥无任何处置措施.     

城市生活垃圾填埋场渗滤液生化处理过程中重金属离子问题

我国对城市生活填埋场渗滤液处理技术的研究主要集中在COD与NH4 -N的去除上,对渗滤液中重金属离子的专项研究几乎未见报道.本文首先总结了国内外城市生活垃圾渗滤液中重金属的种类及浓度,在渗滤液中的存在状态,渗滤液中重金属与其他成分(有机物、氨氮)的相互作用关系,辨证分析了重金属在渗滤液生化处理过程中的有益作用和毒性,归纳了重金属在渗滤液生化处理过程中的变化规律,同时总结分析了重金属的去除技术.     

Study of colloidal content and associated heavy metals in landfill leachate: a case study of El-Akader landfill site: Jordan

Landfill leachate samples were collected anaerobically at six locations at the El-Akader landfill site in North Jordan. The collected leachate samples were separated into size fractions with special attention to the distribution of colloids and associated heavy metals. The fraction sizes were 1.2 μm. The maximum concentrations of heavy metals in the analysed leachate samples were Cd 0.6 μg/l, Ni 25 μg/l, Zn 245 μg/l, Cu 15 μg/l and Pb 2.50 μg/l. In the dissolved particular matter the heavy metals concentration ranges were Cd 0.1–1.1 μg/l, Ni 0.35–1.5 μg/l, Zn 85–105 μg/l, Cu 0–0.95 μg/l and Pb 0.5–2.5 μg/l.     

Hybrid zero valent iron (ZVI)/H2O2 oxidation process for landfill leachate treatment with novel nanosize metallic calcium/iron composite

A novel nanosize metallic calcium/iron dispersed reagent was synthesized and tested as coagulant/catalyst in a hybrid zero valent iron (ZVI)/H₂O₂ oxidation process to treat leachate. Two different types of leachates, one from municipal solid waste (MSW) tipping hall (MSWIL) and second from an MSW landfill site (MSWLL), were collected and characterized. The morphology, elemental composition, and mineral phases of the nano-Ca/CaO and nano-Fe/Ca/CaO were characterized by scanning electron microscopy–electron dispersive spectroscopy (SEM-EDS) and x-ray powder diffraction (XRD) analysis. The coagulation process with 2.5 g L^?1 nano-Ca/CaO attained 64.0, 56.0, and 20.7% removal of color, chemical oxygen demand (COD), and total suspended solids (TSS) in MSWLL. With only 1.0 g L^?1 of nano-Fe/Ca/CaO, relatively high color, COD and TSS removal was achieved in MSWLL at 67.5, 60.2, and 37.7%, respectively. The heavy metal removal efficiency reached 91–99% after treatment with nano-Fe/Ca/CaO in both leachate samples. The coupling process, using 1.0 g L^?1 of nano-Fe/Ca/CaO and 20 mM H₂O₂ doses, achieved enhancement removal of color, COD, and TSS, up to 95%, 96%, and 66%, respectively, without initial pH control. After this treatment, the color, COD, TSS, and heavy metals were significantly decreased, fitting the Korean discharge regulation limit. A hybrid coupled zero valent iron (ZVI)/H₂O₂ oxidation process with novel nanosized metallic calcium/iron dispersed reagent proved to be a suitable treatment for dealing with leachate samples.

Implications: Conventional treatments (biological or physicochemical) are not sufficient anymore to reach the level of purification needed to fully reduce the negative impact of landfill leachates on the environment. This implies that new treatment alternatives species must be proposed. A coupled zero valent iron (ZVI)/H₂O₂ oxidation process proved to be a suitable treatment for dealing with leachate samples. Coagulation with nFe/Ca/CaO allows 91–99% of heavy metals removal. The coupled coagulation–oxidation process by nFe/Ca/CaO reveals excellent ability to treat leachate. After coupled treatment the color, COD, and TSS were also much lower than the discharge regulation limit.     

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。     

夏季潮滩对上海老港垃圾填埋场渗滤液氮、磷净化效果研究

垃圾填埋产生的渗滤液造成的环境污染问题El益严重。采用自然湿地对垃圾渗滤液净化有诸多优点,而相关的研究较少。根据渗滤液的不同浓度和不同滞留时间的净化效果不同,采用实验室模拟和培养的方法来研究老港垃圾填埋场附近潮滩对垃圾渗滤液营养盐N、P的净化效果。研究发现：夏季老港中、低潮滩在较短滞留时间（6h）内对各浓度渗滤液中N、P的净化效果不明显,而在较长滞留时间内（96h）中、低潮滩对各浓度渗滤液净化效果明显,净化后污水中N、P含量可达到排放标准;垃圾渗滤液质量分数为5％时,潮滩对N、P的净化效果最为明显。     

Performance evaluation of intermediate cover soil barrier for removal of heavy metals in landfill leachate

This pilot-scale study evaluated the use of intermediate cover soil barriers for removing heavy metals in leachate generated from test cells for co-disposed fly ash from municipal solid waste incinerators, ash melting plants, and shredder residue. Cover soil barriers were mixtures of Andisol (volcanic ash soil), waste iron powder, (grinder dust waste from iron foundries), and slag fragments. The cover soil barriers were installed in the test cells' bottom layer. Sorption/desorption is an important process in cover soil bottom barrier for removal of heavy metals in landfill leachate. Salt concentrations such as those of Na, K, and Ca in leachate were extremely high (often greater than 30 gL(-1)) because of high salt content in fly ash from ash melting plants. Concentrations of all heavy metals (nickel, manganese, copper, zinc, lead, and cadmium) in test cell leachates with a cover soil barrier were lower than those of the test cell without a cover soil barrier and were mostly below the discharge limit, probably because of dilution caused by the amount of leachate and heavy metal removal by the cover soil barrier. The cover soil barriers' heavy metal removal efficiency was calculated. About 50% of copper, nickel, and manganese were removed. About 20% of the zinc and boron were removed, but lead and cadmium were removed only slightly. Based on results of calculation of the Langelier saturation index and analyses of core samples, the reactivity of the cover soil barrier apparently decreases because of calcium carbonate precipitation on the cover soil barriers' surfaces.     

干电池中重金属的浸出特性及危害研究

所有的家用干电池中都或多或少含有不同种类的重金属。这些重金属进入环境并达到一定含量后 ,其毒性对人体健康和生物圈会造成潜在危害。而电池进入填埋场后是否会发生壳体破损并造成重金属污染 ?本文针对废干电池进入填埋场后 ,重金属的释放和污染情况进行了试验研究。结果表明 ,电池壳体可有效阻止电池中重金属的释放 ,即便是在破损后对渗滤液中重金属的贡献也是微乎其微的。     

渗滤液中污染物的粒度分布及其应用

渗滤液是一种难于处理的废水.论述了渗滤液中污染物的粒度分布.指出了不同粒度污染物中胶体态组分富含难降解有机物和重金属,其性质稳定,含量较高,对渗滤液的处理工艺选择和去除效果影响重大.最后对渗滤液的资源化进行了初步探讨.     

Temporal evolution of polycyclic aromatic hydrocarbons (PAHs) in sludge from wastewater treatment plants: comparison between PAHs and heavy metals

This paper presents results on the presence and temporal variability of the 16 PAHs recommended by the EPA in primary, secondary and digested sewage sludge over a year. The sewage sludges originated from the Guadalete wastewater treatment plant (WWTP) site in Jerez de la Frontera (Cádiz, Spain). These organic pollutants have been extracted from the sewage sludge by microwave energy. High performance liquid chromatography coupled with diode array (HPLC-DAD) or fluorescence (HPLC-FL) detectors have been used. The results showed that total PAHs concentration varied between 1,945 ng g(-1) dry matter (DM) for primary sludges collected in March and 10,100 ng g(-1) DM for primary sludge collected in June. Generally, concentrations of PAHs were higher in compost and digested sludge than in fresh one. On the other hand, the highest concentration of PAHs were found on summer. This thing is associated to the traffic increase from inland zones to the coast (Jerez de la Frontera is very near to beaches). Finally, this paper present a comparative study of the American an European legislation concluding that the limits of concentrations established are not exceeded. In addition heavy metals were analysed. The origin of PAHs and heavy metals seems to be different.     

渗滤液中污染物的粒度分布及其应用

渗滤液是一种难于处理的废水.论述了渗滤液中污染物的粒度分布.指出了不同粒度污染物中胶体态组分富含难降解有机物和重金属,其性质稳定,含量较高,对渗滤液的处理工艺选择和去除效果影响重大.最后对渗滤液的资源化进行了初步探讨.