多段生化法处理煤化工废水的生产性实验研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
近年来,随着我国煤化工行业的蓬勃发展,废水排放量增大、水质复杂、处理率低等问题也日益明显,水体污染形势严峻。2006年哈尔滨气化厂因排放废水中污染物浓度超标,严重污染松花江水体水质而被环保总局挂牌督办。为使出水水质达到《废水综合排放标准》(GB8978-1996)中一级标准的要求,新建污水处理站采用多段生化法:水解酸化—接触氧化—混凝沉淀—曝气生物滤池处理工艺。清水池出水送到电站冲灰系统,与原有冲灰水混合后冲灰,冲灰水经过灰坝粉煤灰深度处理后排入松花江。
     本文概述了煤化工废水的来源、水质特点及国内外对该类废水处理工艺的研究和应用现状;介绍了哈尔滨煤化工有限公司污水处理站的工艺流程、设计参数和构筑物情况;系统地论述了污水处理站所采用各生化工艺的特点。本文通过在现场对整个工艺的的启动,深入研究了多段生化工艺处理煤化工废水的启动特性,重点探讨了启动过程中各工艺主要指示指标的变化情况和原因,以及各工艺单元微生物种群的变化。本文还较为系统的研究了启动完成后稳定运行阶段各工艺单元的运行效果、对各主要污染物质的去除效率和污染物降解过程中存在的规律,还对运行过程中主要影响因素对运行效果的影响进行了分析。此外本文还研究了处理站正常运行和检修或事故时灰坝粉煤灰对废水中污染物的吸附降解情况。
     得出主要结论如下:采用水解酸化—接触氧化—混凝沉淀—曝气生物滤池工艺处理煤化工废水经工程实际调试与运行表明,其技术可靠,经济合理。运行结果表明,COD、BOD5、氨氮、总酚的平均去除率分别为95.8%、98.2%、88.4%、97.6%,出水水质达到《污水综合排放标准》(GB8978-1996)的一级排放标准要求,并且该工艺具有占地面积小、运行稳定、费用低和抗冲击负荷能力强等优点。
     本论文的结果对煤化工废水处理的发展和实践起到重要的理论指导作用,对今后的运行和其他相关废水处理工程的设计和调试运行起到很好的示范作用和指导意义。
Over the past years, as the development of coal-chemical engineering industry, the proportion of discharge amount of beer wastewater is becoming larger and larger. The issue of wastewater discharge volume augmenting, complex quality and low treatment efficiency is becoming increasingly obvious and water pollution pricks up. Harbin Gas Plant was listed on supervision by the Environmental Protection Agency in 2006 because the pollutants concentration was much higher than the standard and caused serious contamination of Songhua River. For the sake of making the effluent meets the first discharge standard of the Integrated Wastewater Discharge Standard (GB8978-1996), the new sewage treatment station adopts the method of multi-stage chemical and biological treatment process: hydrolytic acidification-contact oxidation-coagulation and sedimentation-biological aerated filter treatment process. The rinsing pond effluent is sent to the power station ash washing system, where it is mixed with the former ash washing water. After advanced treatment by fly ash of the ash dam, the effluent is discharged into the Songhua River.
     This paper generalizes the sources, characteristics of coal-chemical engineering wastewater, presents research situation in treating such kind of wastewater and introduces the treatment process, design parameter and structures of the wastewater station in Harbin Coal-chemical Engineering Co. Ltd. It also discusses the characteristic of the treatment process. Based on the practical start-up of the system, start-up characteristics of the process treating coal-chemical wastewater are deeply studieded.The variation and reason of the main indicatoion index and the microbial population change in the start-up process are emphasized. This paper systematically investigates disposal effect of each unit, and disposal efficiency、rule of main pollutants degradation under stable operation stage are also analyzed. In addition it also examined the fly ash adsorption and degradation of pollutants in wastewater under the condition of normal operation and maintenance or incidents of the treatment station.
     The main conclusions are as follows: Practical operation demonstrates that treatment of coal-chemical engineering wastewater by hydrolytic acidification-contact oxidation-coagulation and sedimentation-biological aerated filter process is technologically reliable and economically reasonable. The debugging and operating practice shows that average removal efficiencies of COD、BOD5、ammonia nitrogen and total phenol are more than 95.8%、98.2%、88.4%、97.6%, the effluent is good enough to meet the first discharge standard of the Integrated Wastewater Discharge Standard(GB8978-1996), and the process has advantages as small-land use、steady operation、low expenses and high-level inflexibility.
     This paper has significant theoretical guidance function in the development and practice for the coal-chemical engineering wastewater treatment, as well as playing a very good and exemplary role in guiding the future operation and other related treatment projects design and debugging.
引文
1单明军,吕艳丽,丛蕾.焦化废水处理技术.化学工业出版社.2007
    2王永树,吴成强.射流气浮出游技术在焦化废水预处理过程中的应用.柳钢科技.2008,1:43-45
    3李瑞华,韦朝海,魏光涛.组合出油系统在焦化废水预处理过程中的应用.燃料与化工.2009,1(40):45-48
    4杨平,王彬.生物法处理焦化废水评述.化工环保.2005,21(3):144-149
    5葛文准,容旻辉,陈一申.焦化废水生物处理技术研究.上海环境科学.1992,4(11):7-10
    6 Nakhla G F, Suidan MT.Anaerobic toxic wastewater treatment: dilution effects.Journal of Hazardous Materials.1995,42(1):71-86
    7 Sulidan M T, Strubler Charles E, Kao Shu-Wen, et al.Treatment of coal gasification wastewater with anaerobic filter technology.Journal WPCF.1983,55(7):1263-1270
    8 Nakhla G F, Suidan MT.Control of anaerobic GAC reactors treating inhibitory wastewaters.JOURNAL WPCF.1990,62(1):65-72
    9 Fang Herbert H P, Chan On-Chim.Toxicity of phenol towards anaerobic bio-granules.Water Research.1997,31(9):2229-2242
    10 Zhang Min, Joo Hwa Tay, Yi Qian, et al.Coke plant wastewater treatment by fixed biofilm system for COD and NH3-N removal.Water Research.1998,32(2):519-527
    11赵建夫.焦化废水中难降解有机物在厌氧酸化-好氧生物处理过程中的降解机理研究.中国环境科学.1991,11(4):261-265
    12卢建杭,王红斌,刘维屏.焦化废水中有机污染物的混凝去除作用机理探讨.工业水处理.2000,20(6):20-22
    13刘和,王晓云,陈英旭.固定化微生物技术处理含酚废水.中国给水排水.2004,19:53-55
    14 Wiesel.Degradation of polycyclicaromatic hydrocarbon by an immobilized mixed bacteria culture.Microbial Biotechnol.2005,39:110-116
    15 Lee S T.Biodegration of pyridine by freely and suspended immobilized pimel bacter sp.App Microbiol Biotechnol.2005,4l:652-657
    16杜鸿章.焦化污水催化湿式氧化净化技术.工业水处理.1996,16(6):11-13
    17 LEVEC J.Catalytic Oxidation of Toxic Organics in Aqueous Solition. Applied Catalysis.2005,63:1
    18 KULKARNIU, DIXIT SG.Destruction of Phenol from Wastewater by Oxidation with SO3-O2 Ind.Eng.Chen.Res.2005,30:91
    19 PING N.Treatment of organic pollutants in coke plant wastewater by the method of ultrasonic irradiation, catalytic oxidation and activated sludge. Separation and Purification Technology.2005,41(2):133-139
    20 Byung R L.Biological degradation and chemical oxidation characteristics of coke-oven wastewater.Water.Air and Soil Pollution.2006,(146):23-33
    21左晨燕.芬顿氧化/混凝协同处理焦化废水生物出水的研究.环境保护.2005,(5):31-34
    22刘红,张林霞,吴克明.吸附-氧化法处理焦化废水的研究.工业水处理.2003,23(5):35-37
    23王槐三,何炳林.吸附树脂在废水处理中的应用.成都科技大学学报.1982,(4):75-77
    24张兆春.长焰煤吸附焦化废水污染物的研究.山东矿业学院学报.1996,15(2):205-209
    25陈光柱.MBR污水处理工艺在煤化工企业的应用.中氮肥.2008,1(1):24-26
    26 Miguel M.Integration of nanofiltration/steam stripping for the treatment of coke plant ammoniacal wastewaters.Journal of Membrane Science.2004,(242):87-95
    27王凯军.低浓度污水厌氧—水解处理工艺.北京:中国环境科学出版社.1996
    28王凯军,徐晓鸣,郑元景.水解—好氧生物处理工艺应用实例.环境工程.1991,9(4):3-7
    29陈新宇,陈翼孙.水解酸化生物接触氧化处理难降解丁苯橡胶废水的研究.给水排水.1998,23(2):32-35
    30刘炎,杨平,方治华等.生物流化床中生物膜特性与反应器效率的关系.环境科学进展.1999,(75):113-122
    31陈声贵,徐木启,曹宏等.活性污泥运转效能的生物监测.应用与环境生物学报.2002,8(4):438-442.
    32 Madony P, Davoli D, Chierici E, et al.Comparativate analysis of the activated sludge microfauna in several sewage treatment works.Water Research.2004,27:1485-1491
    33贺延龄.废水的厌氧生物处理.中国轻工业出版社.1998
    34冯敏.现代水处理技术.化学工业出版社.2006:104-105
    35周律.厌氧生物反应器的启动及其影响因素.工业水处理.2006,16(5):1-3.
    36何辰庆.微生物生理学.辽宁大学出版社.1994
    37杨健等.水解酸化—好氧工艺处理丙醇工业废水.重庆环境科学.1999,21(4):26-29
    38何苗,张晓健,曲福平等.焦化废水中芳香族化合物及杂环化合物在活性污泥法处理中的去除特性.中国给水排水.1997,13(1):14-17
    39李世善.水解酸化-UASB-AB工艺在抗生素生产废水处理工程中的应用.给水排水.2002,28(5):44-49
    40张自杰.排水工程(下册)第四版.北京:中国建筑工业出版社.2000
    41 Zhao Xinmin, Michael Rodgers, Edmond O’Reilly.Biofilm Growth and Characteristics in an Altemating Pumped Sequencing Batch Biofilm Reactor.Water Research.2006,40(4):817-825
    42江萍,黎俊,张文涛.生物接触氧化法处理有机废水的进展.环境与开发.2002,15(4):6-7
    43 Maerin thuller, Martin H. Schroth, et al.Modeling of a Microbial Growth Experiment with Bioclogging in a Two-Dimensional Saturated Porous Media Flow Field.Journal of Contaminant Hydrology.2005,21(5):37-62
    44 Ganzarczyk.Second Stage Activated Sludge Treatment of Coke-plant Effluent.Water Research.2005,(7):1137-1157
    45 Yasui H, Shibata M.An innovative approach to reduce the sludge production in the activated sludge process.Water Science & Technology.1994,30(9):11-20
    46 R Pujol, M Hamon, X Kandel, et al.Biofilters. Flexible,Reliable Biological Reactor.Water Science & Technology.1994,29(10-11):33-38
    47 Yong Chung, Yong Chan Choi.A Demonstration Scaling-up of The Dissovled Air Flotation.Water Research.2006,34(3):817-824
    48 D Codiasse.Improving water quality by reducing coagulant dose, a case study at the Sidi Said Maachou Water Treatment Plant (Morocco).Water Science and Technology:Water Supply.v4,n5-6,2004,p271-276
    49 Dentel S K, Gossett J M.Mechanisms of coagulation with aluminum salts.J.Am Water Works Assoc.1988,80(4):187
    50 Dentel S K. Coagulation control in water treatment.CRC Critical Reviews in Environmental Control.1991,21(1):41
    51 Takao Hasegawa, et al. Method and flocculant for watertreatment.USP4,923,629(2005)
    52姚金华.混凝剂与絮凝剂.中国环境科学出版社.1992
    53 Davis.Improving Dye Waste Water Treatment.American Dye stuff Report.Mareh,1991
    54 Won-Seok Chang, Seok - Won Hong, Jookyu Park.Effct of zeo-lite media for the treatment of textile wastewater in biological aerated filter.Process Biochemistry.2002,37:693-698
    55徐亚明,蒋彪.曝气生物滤池的原理及工艺.工业水处理.2002,22(6):1-5
    56邢洪亮.曝气生物滤池在焦化废水处理中的应用.中氮肥.2009,3(2):19-21
    57邱立平,杜茂安,冯琦.二段曝气生物滤池处理生活污水的试验研究.环境工程.2001,19(2):22-24
    58马军,邱立萍.曝气生物滤池及其研究进展.环境工程.2002,20(3):7-11
    59 Lomova M A, et al.Biological purification of waste waters.SU: 546-568.1973
    60 Brown, et al.Nutrient for stimulating aerobic bacteria.US:4727031.1988
    61 Amar D, Partos J.The use of an upflow fixed bed reactor for treatment of a primary settled domestic sewage.Water Research.1986,20(1):9-14
    62 Rathi G, Avanaugh K, Clifford W.Bacterial populations in a biological nutrient removel plant.Water Science & Technology.1994,29(7):25-34
    63 Wang Shaobin, Bo joo Y, Choueib A, et al.Removal of Dyes from Aqueous Solution Using Fly Ash and Red Mud. Water Research.2005,39(1):129-138
    64 Kao Pingchung, Tzeng Jau Hwan, Huang Tsz Ling, et al.Removal of Chorophenols from Aqueous Solution by Fly Ash.J Hazard Mater.2000,76(2):237-249
    65 StamondisVc, et al.Determination of Bio1ogica1 Removal of organic Constituents in Queneh Wateers From High-BTV Coal Gasification Pilots.Water Reserch.1980,14:1248-1263
    66 CooPer R.L, et al.The Blological treatmen tof Carbonizatlon Effluents.Water Researeh.1972,7:1137-1157
    67国家环境保护总局水和废水监测分方法编委会.水和废水监测分析方法(第四版).北京:中国环境科学出版社. 2002
    68 Dinopoulouq, et al.Anaerobic acidogenesis of a complex wastewater.I.The influence of operation parameters on reactor performance. Biotechnol.2002,31(9):958-968
    69王彩霞.城市污水处理新技术.中国建筑工业出版社.1998:164-175
    70林晓利.SBR法处理屠宰废水氨氮升高原因分析及改进措施.环境保护科学.2007,33(2):29-30
    71沈耀良,王宝贞.水解酸化工艺及其应用研究.哈尔滨建筑大学学报.1999, 32(6):35-38
    72沈连峰,申艳萍,刘文霞等.物化-水解酸化-A/O组合法处理焦化废水.水处理技术.2007,No.9 (Vol.33):90-93
    73 Liu Y.Dynamique de croissance de biofilm nitrifiant appliquéaux tracitoment dex eaux.Thesis INSA-Toulouse.2005
    74 Stamoudis Vassilis C, Luthy Richard G.Determination of biological removal of organic constituents in quench waters from high-BTU coal-gasification pilot plants.Water Research.1980,14(5):1143-1156
    75 Hockenbury M R, Grady C P L.Inhibition of nitrification-effects of selected organic compounds.JOURNAL WPCF.1977,49(3):768-777
    76 Lee N M, Welander T.Reduing sludge producting in aerobic wastewater treatment through manipulation of the ecosystem.Water Research.2006,30(8):1781-1790
    77顾夏声.水处理微生物学基础.中国建筑工业出版社.1987:25-30
    78 Dyreborg Soren, Erik Arvin.Inhibition of nitrification by creosote-contaminated water.Water Research.1995,29(6):1603-1606
    79 Warrer J.Stable foams and sludge bulking:the largest remaining problems.J CIWEM.1998,12(10):368-374
    80 Paul Pitt, et al.J WPCF. 62(2), 143-150(1990).
    81 Tipping P J.Foaming in activated sludge processes;an operator′s overview.J CIWEM.1995,9(7):281-290
    82 M. Kobyaa, H. Hiza, E. Senturka, et al.Treatment of potato chips manufacturing wastewater by electrocoagulation.Desalination.2006,190:201-211
    83李彦光,郭金华.JY-202复合混凝剂在焦化废水处理中的应用.工业水处理.2004,24(6):71-73
    84彭贤玉.Fenton-混凝沉淀法处理焦化废水的试验研究.湖南大学工程硕士学位论文.2006
    85涂传青,徐国勋.聚合氯化铝铁的形态分布特征研究.净水技术.2004,23(4):4-6
    86李风亭,张善发,赵艳.混凝剂与絮凝剂.北京:化学工业出版社.2005:25
    87吴克明,夏钧峰,范志功等.混凝-气浮法处理焦化废水.工业安全与环保.2008,34(10):1-3
    88王洪宇,陈福泰,王亚宜.聚合氯化铁与三氯化铁吸附电中和特性的比较研究.中国给排水.2006,22(5):60-63
    89徐海宏,李满.PAC与PAM复合絮凝剂处理矿井水的研究.煤炭科学技术.2006,34(4):83-85
    90姚珺.焦化废水中有机污染物经厌氧酸化后对好氧生物降解性能的影响.中国环境科学.1998,18(3):276-279
    91刘鹤年.厌氧/好氧生物脱氮-絮凝法处理焦化废水.化工环保.1995,15(6):343-346
    92刘雨,赵庆良,邓兴灿.生物膜法污水处理技术.北京:中国建筑工业出版社.2000
    93 Rebecca Moore, Joanne Quarmby, Tom Stephensn.The effects of media size on the performance of biological aerated filters.Water Science & Technology.2001,35(10):2514-2522
    94 Borgen R, et al.Biol Sol.1978,15(4):445-449
    95 Park J W, Granczar, Czyk J J.Gravity separation of biomass washed out from aerated submerged filter.Enviromental Technology.1994,15:945-955
    96江萍,胡九成.国产轻质球形陶粒用预曝气生物滤池的研究.环境科学学报.2002,22(4):460-464
    97张林军.上向流与下向流曝气生物滤池启动与挂膜特征研究.徐州工程学院院报.2005,20(1):53-57
    98刘荣光,罗辉荣,汪义强等.滤池气水反冲洗机理综述与初探.重庆建筑大学学报.1998,20(6):7-11
    99张杰,陈秀荣.曝气生物滤池反冲洗的特征.环境科学.2003,24(5):86-91
    100王彩霞.城市污水处理新技术.中国建筑工业出版社.1998:164-175
    101 Fdz-polanco F, et al.Spatial distribution of heterotrphs and nitrifiersin a submerged biofilter for nitrification.Water Research.2000,34(16):4081-4089
    102 Smith A J, et al.High-rate sewage treatment using biological aerated filters.Iwem.1992,6:112
    103 A dachi S, et al.Reclamation and reuse of wastewater by biological aerated filter process.Water Science & Technology.1991,24(9):195-204.
    104 Y. S. Cao, G. J. Alaerts.Influence of Reactor Type and Shear Stress on Aerobic Biofilm Morphology, Population and Kinetics.Water Research.1995,29(1):107-118
    105 O. Lahav, E. Artzi, S. Tarre, M. Green.Ammonium Removal Using a Novel Unsaturated Flow Biological Filter with Passive Aeration.Water Research.2001,35(2):397-404
    106沈耀良,王宝贞.废水生物处理新技术-理论与应用.北京:中国环境科学出版社.2006
    107邱立平.曝气生物滤池处理生活污水的运行特征及生态学研究.哈尔滨工业大学博士学位论文.2003

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700