城镇污水处理厂污水污泥重金属稳定实验研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
城市污水处理厂污泥(sewage sludge)的最终处置是国内外共同面临的难题和挑战。经国内现有的污泥处理技术处理后的污泥中有机物含量高,易腐烂,有恶臭,并含有寄生虫卵、病原微生物、重金属和多种化合物质,由此看出污染成分复杂,特别是重金属的处理,无法达到卫生填埋标准,重金属通常具有急性或慢性毒性,会以各种方式毒害人体,如致癌或非直接地引发某些疾病。已经造成了环境污染等一系列严重的后果。因此解决好污泥处理处置问题已成为一项非常紧迫的任务。
     在重金属废物的处理中大部分都需进行稳定化处理,以达到无害化的目的。常规重金属稳定化技术种类很多,但在用于重金属废物的处理时都有局限性,特别是这些技术都受pH值变化的影响,当pH值较低时,重金属离子会再溶出,没有达到重金属废物长期稳定化的目的,在废物的最终处置中,将会对环境造成二次污染。针对这些问题,国际上提出了高效的化学稳定化药剂进行无害化处理,并成为危险废物无害化处理的研究热点。本论文主要研究内容为污泥泥质分析和污泥中重金属稳定。论文实验以西安污水处理厂污泥为研究对象,得出结论西安市污水污泥镉Cd、汞Hg、铅Pb、铜Cu、锌Zn、镍Ni总量均超出《农用污泥中污染物控制标准》(GB4248-84)规定的农用适用污泥中污染物最高允许含量,污水厂的浸出液重金属铅Pb超出《危险废物鉴别标准浸出毒性鉴别》(GB5085.3-2007)规定的最高允许含量;对高分子重金属螯合剂(EP-110)稳定重金属的机理研究表明,EP-110能够与重金属离子以共价键连接,形成空间结构稳定的高分子螯合物;EP-110药剂处理各种金属离子的PH值范围在3.0~11.0内有效;得出最佳投药量结论,EP-110/重金属含量(W/W): EP-110/Cu~(2+)为(6.5~7.5/1)、EP-110/Ni~(2+)为(7.0~8.0/1)、EP-110/Pb~(2+)为(1.5~2.5/1)、EP-110/Zn~(2+)为(8.5~9.5/1)、EP-110/Cd~(2+)为(3.5~4.5/1)、EP-110/Hg~(2+)为(2.0~2.5/1);应用重金属螯合剂处理污泥中重金属,处理对象较多,形成的重金属螯合物稳定,污泥指标符合国家颁布的污泥卫生填埋等各项标准。
The final disposition of city sewage sludge is a difficult problem and a challenge which both domestic and abroad have to face. Domestic technology of dealing with sewage sludge is too simple. Moreover, the organics content of sewage sludge which has been discharged is very high. They are easy to get corrupt, have malodor, and they also contain parasitic ovum, pathogenic microorganism, heavy metal and many compounds. So, we can see that the composition of pollution is very complicated, especially for the dealing with heavy metal, which is very difficult to get the standard of sanitary landfill. Heavy metal usually contains the acute or chronic toxicity that can contaminate human body in many ways. For instance, they can result in cancer or indirectly result in some disease. which has brought out a series of serious consequence, like environment pollution, etc. So, dispose of sewage sludge problem has become an urgent task.
     During the process of disposing the waste of heavy metal, mostly, stabilizing treatment is needed to reach the purpose of innocent treatment. There are many categories of conventional technology of heavy metal stabilizing treatment, but there is also some limits when these categories are used on the deposition for heavy metal. Especially, these technologies can be influenced by pH value. When pH valve is low, heavy metal ions will be stripping again, then, the purpose of long–term stabilizing treatment of heavy metal would not be obtained. During the final waste disposal, environment will suffer the secondary pollution. Be aimed a these problems, using a high performance chemistry stabilizing medicament to deposit the innocent treatment has been put forward, which also become a studying hot spot of innocent treatment of depositing the dangerous waste. This paper mainly studies on the qualitative and quantitative analysis of sewage sludge, and the heavy metal desactivation of sewage sludge. The experiment of thesis will choose the sludge that is from XiAn sewage plant as a studying objective, Allowable maximal pollution contents , foul water factory infusion liquid heavy metal in the farm-oriented sludge suitable for use reaching conclusion Xi An City foul water sludge cadmium Cd , mercury Hg , lead Pb , copper Cu , zinc Zn , nickel Ni all quantity regulation without exception exceeding《pollution controls a standard in farm-oriented sludge》(GB4248-84) , lead Pb exceed《dangerous good-for-nothing distinguishes a standard leaching out toxicity being distinguished》(GB5085.3-2007) regulation maximal allow contents. Conclusion of experiment: using heavy metal sequester to deposit is more across-the-aboard, holding a comparative high rate of wiping for each index,Heavy metal chelating agent nature of the polymer analysis,Heavy metal chelating agent that the mechanism of heavy metal passivation , to EP-110 connect to heavy metal ions with covalent bond, a spatial structure of the polymer stability chelates;(EP-110)Pharmacy deal with all kinds of metal ions,The Range of pH is 3.0~11.0. After processing the metal ion content lower than the emission standards; The optimum dosage of conclusions,EP-110/Heavy Metal Content(W/W): EP-110/Cu~(2+)(6.5~7.5:1)、EP-110/Ni~(2+)(7.0~8.0:1)、EP-110/Pb~(2+)(1.5~2.5:1)、EP-110/Zn~(2+)(8.5~9.5:1)、EP-110/Cd~(2+)(3.5~4.5:1)、Hg2(+2.0~2.5:1);the amount of throwing the dose is few, so that the cost of deposition can be reduced more. and use compound heavy metal sequester to deposit the heavy metal that exists in the sludge, which already get an obvious effect. It comes up to the every standard of sanitary landfill of Chinese decree.
引文
[1]陈静生,周家义.中国水环境金属研究[M].北京:中国环境科学出版社,1998
    [2]张清敏,陈卫平,胡国臣等.污泥有效利用研究进展[J].农业环境保护.2000,19(1):58~61
    [3]Council of the European Economic Communities,[J]Directive Conceerning Urban Wastewater Treatment(91/271/EEC),off,J.Eur.Commmunities,L135/40~52,1991
    [4]杨琦,刘广立,钱易.污水处理与处置技术的新发展[J].上海环境科学,1999年第18第3期
    [5]黄渭澄等.电镀三废处理[M].成都:四川科学技术出版社,1998
    [6]佟玉衡,实用废水处理技术[M].北京:化学工业出版社,1998
    [7]赵丽华,赵中一.固体废弃物处理技术现状[J].环境科学动态,2002,(3):26~27
    [8]Bouveng,H.O.Control of Mercury in Effluents From Chlorine Plants.J.Pure Applied Chem[J].29(1979):75~79
    [9]Robinson,A.and J.Sum.Sulfide Precipitation of Heavy Metal[J].USEPA 600/2-80-139,1980.6
    [10]Feigenbaum.H.N.Removing Heavy Metals in Textile Waste[J],Ind.Wastes 1979.7/8:34~38
    [11]Minear,R,A,and J.W.Patterson Carbonate Precipitation Treatment for Cadmium[D],Paper Presented at the 8th WWEMA Industrial Pollution Conference,Houston.TX,1980.6.5
    [12]Rohrer,K.L.Chemical Precipitants for Lead-Bearing Wastewater.Ind.Water Eng[J],1975:13~17
    [13]Crandall,C,J.and J.R.Rongdenberg.Wastewater Lead Oxide Treatment of Lead Acid Battery Manufacturing Wastewater.Paper Presented at the 29th Annual Purdue Industrial Waste Conference.West Lafayette[M].In,1974.5
    [14]蔡全英,莫测辉等.化学方法降低城市污泥的重金属含量及其前景分析[J].土壤与环境.1999,8(4):309~313
    [15]Jakobsen,K.and R.Laska.Advanced Treatment Methods for Electroplating Wastes.Poll[J].Eng,1977.10
    [16]Winning Heavy Maste from Waste Stream.Chem[J].Eng.78(1971):65~64
    [17]The Cost of Clean Water,vol.Ⅲ,Industrial Waste Profiles[J],No.1.Blast furnace and steel Mills[J],FWPCA Publication(Washington,DC:USDI 1967)
    [18]汪大羽,徐新华,宋爽.工业废水中专项污染物处理手册[M].北京:化学工业出版社,2000
    [19]Skovronek,H.S.and M.K.Stinson,Advanced Treatment Approaches for Metal Finishing Wastewater[J],Part1 and Part2.Plating Surface Fin.1977.10:30~38;1977.11:24~31
    [20]Crampton,D.and P.Wilmoth Reverse Osmosis in the Metal Finishing Industry.Metal Fin[J].1982.3 [21Klein,E.W.and J.DelPico.RO Comes of Age for Plating Pollution Control[J],Prod.Fin.1974(38)
    [22]盛桂浓.国外处理重金属矿山废水的几种方法[J].冶金环保情报资料,1985(2)
    [23]蒋建国,吴学龙等.重金属稳定化技术现状与发展[D].新疆环境保护.2000,22(1):006~010
    [24]吴桢芬,王华等.生活垃圾焚烧中重金属行为的研究进展[J].资源开发与市场,2006.22
    [25]孙颖,陈玲等.污泥中重金属性质分析及处理方法实验研究[J].江苏环境科技.2003.12.(16.4)
    [26]张芳,王惠民.污泥无害化和综合利用途径研究[J].环境动态科学.1997,(3):12~14
    [27]李国学,孟凡等.添加钝化剂对污泥堆肥处理中重金属(Cu,Zn,Mn)形态影响[J].中国农业大学学报.2000,5(1):105~111
    [28]宋菲,郭玉文.镉、锌、铅复合污染对菠菜的影响[J].农业环境保护.1996,15(1):9~14
    [29]马运宏,范瑜等.重金属在土壤-作物系统中迁移分布规律的分析[J].江苏环境科技.1995,(1):8~10
    [30]葛俊,许旭等.垃圾焚烧重金属污染物的控制现状[J].环境科学研究.2001,14(3):62~64
    [31]李建新,严建华等.垃圾焚烧飞灰中重金属稳定化处理[J].热力发电.2003,(12):35~40
    [32]李润东.城市生活垃圾焚烧飞灰熔融实验研究[D].浙江大学博士学位论文,2002,114~118
    [33]吴清仁.生态建材与环保[M].化学工业出版社.2003
    [34]聂永丰.三废处理工程技术手册(固体废物卷)[M].北京工业出版社.2004.444~460
    [35]严捍东.电镀污泥与海滩淤泥复合材料烧制陶粒重金属固化效果的试验分析[J]化工进展.2005,24(4):383~386
    [36]刘天亮.厌氧固化城市污泥中重金属的研究[D].北京:清华大学环境工程系,1986
    [32]蒋建国,王伟等.危险废物稳定化/固化技术的现状与发展[J].环境科学进展,1998,6(1):55
    [38]王锐刚,韩怀芬.重金属螯合剂处理危险废物的研究进展[J].环境技术.2003.2
    [39] F.P.Dwyer,D.P.Mellor.Chelating Agents and Metal Chelates[J],1964
    [40] Yost,K.J.and A.Scarfi.Factors Affecting Copper Solubility in Electroplating Water,J.Water Poll.Control Fed[J].51(1979):7
    [41] Robinson,A.and J.Sum.Sullide Precipitation of Heavy Metals[J].UsPeA600/2-80-139,1980.6
    [42]安淼,周棋等.城市污泥中重金属的形态分布合处理方法的研究[D].农业环境科学学报.2003,22(2):199~202
    [43]中国环境监测总站译.固体废物试验分析评价手册[M].中国环境科学出版社,1992
    [44]张瑞娜,赵由才等.生活垃圾焚烧飞灰的处理处置方法[J].苏州科技学院学报,2003,16(1)22~29
    [45]蒋建国,王伟等.高分子螯合剂捕集重金属Pb 2+的机理研究[J].环境科学,1997,18(2):31~33
    [46]张衍国,奉化等.城市污水污泥焚烧过程中的重金属迁移特性.[J].环境保护,2000,12:35~36
    [47]张益,赵由才.生活垃圾焚烧技术[M].北京化学工业出版社.2000,56~57
    [48]Bosecker K.Bacterial metal recovery and detoxification of industrial waste[J].Biotechnol Bioeng Conf.1985,(17):575~586
    [49]Couillord D,chartier M.Major factors influencing bacterial leaching of heavy metals from anaerobic sludge[J].Environ Pollution.1994,(85):175~184
    [50]Tessier A W,el al.Sequential extraction procedure for the speciation of particulate trace metals[J].Anal Chem.1997.51(7):844~850