高铁酸钾与臭氧联用处理印染废水的试验研究
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摘要
印染废水具有成分复杂、难降解有机污染物含量高、色度高、COD_(Cr)值高、含盐量高等特点,传统物化、生化处理工艺对有的废水难以达标排放,特别是色度降解尤为困难。强化印染废水处理工艺,研究新的处理技术,实现废水达标排放和中水回用是企业迫切的需求。
     本文尝试应用高铁酸钾和臭氧联用的新方法处理含染料废水。该方法利用高铁酸钾的氧化性以及絮凝性与臭氧共同作用,破坏染料的发色基团,打开芳香环,生成分子量较小且无色的降解中间产物,甚至最终降解成为CO_2和H_2O,达到脱色和降解有机物的目的。
     通过比较单独高铁酸钾或单独臭氧以及联用处理100 mg/L活性艳红X-3B模拟废水的脱色效果和COD_(Cr)去除率,结果表明,联用处理4min后完全脱色,COD_(Cr)的去除率达46%。联用处理的脱色效果明显好于单独电晕处理和单独臭氧处理。验证了高铁酸钾和臭氧联用存在协同效应。
     通过高铁酸钾与臭氧联用降解三种活性染料和三种酸性染料的实验发现,活性染料在10 min内脱色率均可达到95%以上。活性染料降解速度要明显快于酸性染料。在同一类型染料下,降解速度蒽醌染料>单偶氮染料>双偶氮染料。从总体上说,高铁酸钾和臭氧联用处理对于染料废水的脱色十分迅速,在降解效率和处理时间上有一定的优越性。
     本文证实了高铁酸钾和臭氧联用处理染料废水有明显的协同效应,处理效率高、适用性强,占地面积小、降解速度快,能耗小,能够改善染料废水的可生化性,便于后续生化处理达标排放或中水回用,适宜于难降解印染废水的预处理。
The extile wastewater was of complicated component,by a high content of refractory organic pollutants,high colority,high chemical oxygen demand and salt content,traditional physicochemical,biochemical treatment process was difficult to discharge some wastewater,color degradation was particularly difficult.Strengthen the treatment process of extile wastewater,research new treatment technology to achieve the demand of discharge to reach standard of wastewater discharge and reclaimed water reuse.
     The combination technology of potassium ferrate and ozone is a new kind of wastewater process,it utilizes the oxidizability and flocculability of potassium ferrate,the synergism of potassium ferrate and ozone,destroy the chromophoric groups,open the aromatic ring to produce the degrade products of smaller molecular weight and colorless,and even become to CO_2 and H_2O,achieve the purpose of decoloration and degradation of organic matter.
     Comparison the decoloration and COD_(Cr) degradation of 100 mg/L reactive red X-3B dye wastewater by potassium ferrate alone,ozone alone and potassium ferrate combined ozone,the results showed that with the combined process 4 minutes,the decoloration removal entirely and the COD_(Cr) removal 46%.the efficiency of potassium ferrate combined ozone was better than potassium ferrate alone and ozone alone.Verify the synergistic effect of potassium ferrate combined ozone.
     Using potassium ferrate combined ozone to degradation three types of reactive dyes and acid dyes,reactive dyes could decoloration more than 95%within 10 minutes.The degradation of reactive dyes was faster than acid dyes.In the same type of dye,the degradation rate was anthraquinone dye>monoazo dye>disazo dye.Generally speaking potassium ferrate combined ozone for decoloration of dye wastewater was very rapidly and had superiority in degradation efficiency and processing time.
     The paper confirmed the treatment of potassium ferrate combined ozone had synergistic effect obviously,high efficiency,high treatment efficiency,small floor area,decomposes quickly and its,less energy consumption,improve the biodegradability of dye wastewater,suitable for the pretreatment of extile wastewater.
引文
[1]王建洪,沈健.印染废水的处理及回用技术[J].能源环境保护,2005,19(4):42-44.
    [2]金芸,游革新.印染废水处理新进展[J].武汉科技学院学报,2005,18(9):50-52.
    [3]国家环保局,纺织总会,八五研究项目组.纺织工业污染源控制研究报告[R].北京:中国环境出版社,1994.
    [4]张自杰.环境工程手册:水污染防治卷[M].北京:高等教育出版社,1996.
    [5]王凯军,左剑恶,甘海南,等.UASB工艺的理论与工程实践[M].北京:中国环境科学出版社,2000,21(7):4-7.
    [6]K.Santhy,E Selvapathy.Removal of reactive dyes from wastewater by adsorption on coir pith activated carbon[J].Bioresource Technology,2006,97:1329-1336.
    [7]阎存仙,罗浸.煤灰吸附去除活性艳蓝X-BR[J].上海交通大学学报,1998,2:126-129.
    [8]姚福琪,张占吉,王孟歌.炉灰脱色剂对分散红染料废水的脱色处理研究[J].河北化工,2004,2:45-47.
    [9]杨宇翔,陈荣三.硅藻土脱色机理及其在印染废水的应用研究[J].工业水处理,1999,19:15-17.
    [10]Emin Erdem,G(u|¨)lay C(o|¨)lgecen,Ramazan Donat.The removal of textile dyes by diatomite earth[J].Journal of Colloid and Interface Science,2005,282:314-319.
    [11]裴振琦,韩式荆.用聚矾超滤膜从染色废水中回收染料[J].环境化学,1985,4(2):1-4.
    [12]吴开芬.用超滤法处理靛蓝废水[J].环境科学进展,1998,6(z):124-127.
    [13]Ting Hui Liu,Matsuurat,Sourirujon S.Effect of Membrane Material Sand Average Pore Size on Reverse Osmosis Separation of Dyes[J].Ind Eng Chem Prod Dev,1983,22:77-85.
    [14]鲍廷镛,方孟伟.反渗透法处理锦纶染色废水[J].水处理技术,1981,7(4):19-21.
    [15]A.Akbari,S.Desclaux,J.C.Rouch,R Aptel,J.C.Remigy.New UV-photografted nanofiltration membranes for the treatment of colored textile dye effluents.Journal of Membrane Science,2006,286:342-350.
    [16]Oliveira L.C.A.,Rios R.V.R.A.,Fabris J.D.,et al.Activated carbon/iron oxide magnetic composites for the adsorption of contaminants in water.Carbon,2002,40(12):2177-2183.
    [17]傅炎初,吴树森,王世容.用离子浮选法处理印染废水中的活性染料的研究[J].印染助剂,1992,2(8):11-17.
    [18]张宏伟,杨芳,季民.气浮过滤处理印染废水[J].城市环境与生态,2001,1(6):1-3.
    [19]Hang J Y,Huang S D.Removal of Organic Dyes(Direct Blue) from synthetic wastewater by Adsorptive Bubble Separation Techniques[J].Sci Technol,1993,27(6):1169-1175.
    [20]李振宇.反应萃取法处理染料中间体废水[J].环境科学,2001,22(6):57.
    [21]张林生,蒋岚岚.染料废水的混凝脱色特性及机理分析[J].东南大学学报(自然科学版),2000,30(4):72-76.
    [22]Tak-Hyun Kim,Chulhwan Park,Eung-Bai Shin,Sangyong Kim.Decolorization of disperse and reactive dye solutions using ferric chloride[J].Desalination,2004,161:49-58.
    [23]Bao-Yu Gao,Qin-Yan Yue,Yan Wang,Wei-Zhi Zhou.Color removal from dye-containing wastewater by magnesium chloride[J].Journal of Environmental Management,2007,82:167-172.
    [24]D.Rajkumar,Byung Joo Song,Jong Guk Kim.Electrochemical degradation of Reactive Blue 19 in chloride medium for the treatment of textile dyeing wastewater with identification of intermediate compounds[J].Dyes and Pigments,2007,72:1-7.
    [25]汪群慧.复极性粒子群电极用于印染废水的处理[J].南京化工学院学报,1990,12(3):69-71.
    [26]韩洪军.铁屑-碳粒法处理工业废水[J].环境保护,1991,33(3):881-884.
    [27]赵少陵,贾金平.活性炭纤维电极法处理印染废水的应用研究[J].上海环境科学,1997,16(5):24-27.
    [28]贾金平,杨骥等.活性炭纤维电极法处理染料废水机理初探[J].环境科学,1997,18(6):31-34.
    [29]L.Daniliuc.Performance and Economic Aspects of the Treatment of Effluents by Electro-Flocculation Using the Dequaflox Process[J].Tribune de l' Ean(in French), 1995,48(576):37-39.
    [30]Simons son D.Electrochemistry for cleaner environment[J].Chemical Society Reviews,1997,26(3):181-190.
    [31]Comninellis C,Pulgrin C.Electrochemical wastewater treatment using high overvoltage anodes[J].Appl Electrochem,1991,23:108-112.
    [32]Naumcayk J,Sxpyrkowicz L,Gramdi F Z.Electrochemical treatment of textile wastewater[J].Water Sci Technol,1996,33(7):17-24.
    [33]Nicola M,Badea T.Wastewater treatment using electrochemical oxidation of organic pollutants[J].Sci Technol Environ,1996,3(1):35-40.
    [34]Idil Arslan Alaton,Senem Teksoy.Acid dyebath effluent pretreatment using Fenton's reagent:Process optimization,reaction kinetics and effects on acute toxicity.Dyes and Pigments,2007,73:31-39.
    [35]李绍锋,张秀忠,张德明,等.Fenton试剂氧化降解活性染料的试验研究[J].给水排水,2002,28(3):46-49.
    [36]S.Salman Ashraf,Muhammad A.Rauf,Seham Alhadrami.Degradation of Methyl Red using Fenton's reagent and the effect of various salts[J].Dyes and Pigments,2006,69:74-78.
    [37]徐向荣,王文华,李华斌.Fenton试剂处理酸性染料废水的研究[J].环境导报,1997,6:23-24.
    [38]杨大春,张光辉,顾平.Fenton-微滤工艺处理印染废水研究[J].中国给水排水,2003,19(3):46-48.
    [39]Guohua Chen,Lecheng Lei,Xijun Hu,Po Lock Yue.Kinetic study into the wet air oxidation of printing and dyeing wastewater[J].Separation and Purification Technology,2003,31:71-76.
    [40]Xijun Hu,Lecheng Lei,Guohua Chen,et al.On the degradibility of printing and dyeing wastewater by wet air oxidation[J].Wat Res,2001,35(8):2078-2080.
    [41]Yan Liu,Dezhi Sun.Development of Fe_2O_3-CeO_2-TiO_2/g-Al_2O_3 as catalyst for catalytic wet air oxidation of methyl orange azo dye under room condition[J].Applied Catalysis B:Environmental,2007,72:205-211.
    [42]S.H.Lin,S.J.Ho.Catalytic wet-air oxidation of high strength industrial wastewater[J].Applied Catalysis B,Environmental.1996,9:133-147.
    [43]Hu Chun,Wang Yizhong.Decolorization and biodegradability of photocatalytic treated azo dyes and wool textile wastewater[J].Chemosphere,1999,39(12): 2107-2115.
    [44]王九思,蒲艳玲,李玉金,王明权.负载型YiO_2光催化氧化降解甲基橙的实验研究.甘肃科学学报,2006,03:120-122.
    [45]W.Z.Tang,H.An.UV/TiO_2 photo-catalytic oxidation of commercial dyes in aqueous solutions[J].Chemosphere,1995,31(9):4157-4170.
    [46]赵玉光,李湘中.生物-光催化反应器系统处理印染废水的研究[J].环境科学学报,1998,18(4):373-379.
    [47]张晓敏,宗汉兴,汪德耀,张义平.光催化氧化降解活性艳红X-3B模拟染料废水试验.水资源保护,2006,22(4):68-70.
    [48]李芳柏,古国榜.絮凝-光催化处理实际染料废水的研究[J].土壤与环境,1999,8(3):189-192.
    [49]Laura W.Lackey,Richard O.Mines Jr.,Philip T.McCreanor.Ozonation of acid yellow 17 dye in a semi-batch bubble column[J].Journal of Hazardous Materials B,2006,138:357-362.
    [50]Fulya G(o|¨)k(?)en,Y(u|¨)lay A.(O|¨)zbelge.Enhancement of biodegradability by continuous ozonation in Acid Red-151 solutions and kinetic modeling[J].Chemical Engineering Journal,2006,114:1-3.
    [51]章飞芳,Yediler Ayfer,张青,等.臭氧氧化活性染料及其降解产物毒性研究[J].精细化工,2003,20(11):682-685.
    [52]A.H.Konsowa.Decolorization of wastewater containing direct dye by ozonation in a batch bubble column reactor[J].Desalination,2003,158:233-240.
    [53]费庆志,许芝.臭氧氧化降解含染料废水的研究[J].环境污染治理技术与设备,2003,4(6):24-26.
    [54]陶媛,胡祺昊,王黎明,关志成.超声技术降解染料废水的实验研究[J].高电压技术,28(120):47-49.
    [55]S.Vajnhandl,A.Majcen Le Marechal.Ultrasound in textile dyeing and the decolouration mineralization of textile dyes[J].Dyes and Pigments,2005,65:89-101.
    [56]胡文容,裴海燕.超声强化O_3氧化偶氮染料的特性[J].科学通报,2001,46(24):2049-2051.
    [57]张翼,张晖,吴峰,等.超声-Fenton法处理偶氮染料橙黄Ⅱ的研究[J].环境污染治理技术与设备,2001,4(11):48-51.
    [58]李亚新,李莉,马志敏等.塑料孔板波纹填料厌氧生物滤池法处理印染废水试验的研究[J].中国给水排水,1995,11(5):16-19.
    [59]闫庆松.厌氧+好氧+煤渣吸附处理偶氮染料废水的研究[J].工业水处理,2000,20:19-22.
    [60]顾晓扬,汪晓军,林德贤,等.Fenton试剂—曝气生物滤池处理酸性玫瑰红印染废水[J].工业水处理,2006,26:28-31.
    [61]黄民生,孙萍,朱莉.微生物絮凝剂的研制及其絮凝条件.环境科学,2000,21(1):23-26.
    [62]李强,张玉臻,陈明,等.吸附型生物絮凝剂ZL5-2的制备及在水处理上的应用,工业水处理,2005,25(9):43-45.
    [63]许良,邱慧琴.多功能水处理药剂高铁酸钾的研制及应用研究[J].净水技术,2004,(4).
    [64]裴慧霞,李福祥,吕志平,等.高铁酸钾稳定性研究进展[J].山西化工,2007,(4).
    [65]Schreyer J M,Oxkwerman L T.Stability of the ferrate(Ⅵ) ion in aqueous solution[J].Anal Chem,1951(23):1312-1314.
    [66]王立立,曲久辉,王忠秋,等.高铁稳定性及其影响因素的研究[J].东北电力学院学报,1999,19(1):6-9.
    [67]江冬青,夏天.分光光度法研究高铁酸钾在碱性介质中的反应动力学[J].现代仪器,2003(3):27-29.
    [68]贾汉东,马宁,孙红宾.FeO42-离子在水溶液中稳定性的研究[J].郑州大学学报,1999(1):67-69.
    [69]张铁锴.水溶液中Fe(Ⅵ)化合物的稳定性研究[D].大庆:大庆石油大学,2005.
    [70]高玉梅,贾汉东.光照对高铁酸盐溶液稳定性的影响[J].应用化学,2004,21(4):425-427.
    [71]Stuart L,Wang Baohui,Xu Gang,et al.Solid plase modifiers of the Fe(Ⅵ)cathode:effects on the surperiron battery[J].Electro Chemistry Communications,1999,1(11):527-531.
    [72]贾汉东,鲍改玲.过渡金属离子对高铁酸盐溶液稳定性的影响[J].电池,2004,34(6):430-431.
    [73]朱启安,王树峰,黄伯清,等.提高高铁酸钾产率和稳定性的方法[J].精细化工,2006,23(6):593-596.
    [74]Ettel V,Veprek-Siska J.Reaction of very pure sub-stances decomposition of ferrates in alkaline solutions[J].Collect Chem Commum,1969,344(12):2182-2188.
    [75]高艳娇,张勇,王平.高铁酸钾的合成及其处理低温低浊水源水[J].净水技术,2006,(2).
    [76]张彦平,许国仁,程恒卫,等.绿色氧化剂高铁酸钾研究进展[J].工业水处理,2007,(8).
    [77]冉亮,周俊,郝祥忠,等.高铁酸钾的研究现状[J].安徽化工,2007,(1).
    [78]储金宇,吴春笃,陈万金.臭氧技术及应用[M].北京:化学工业出版社,2002.
    [79]Staelin,et al.Ozonation of chlorophenols by product and toxicity[J].Environ.Sci & Technol,1982,16(676):118.
    [80]Roberto Andreozzi,et al.Oxidative degration ozone in a nelectrohy draulic discharbe reactor[J].Catalysis Today,1999,53:51-59.
    [81]Trapido.M,Versuniay,Hentanen.J.K.Ozonation of chlorophenols.by product and toxicity[J].Evirontech,1997,18:325.
    [82]徐新华,赵伟荣.水与废水的臭氧处理,北京:化学工业出版社,2003,9.
    [83]T.Khayamian.Analysis of 2,4,6-trinitrotoluene,Pentaerythritol Tetranitrate and Cyclo-1,3,5-trimethylene-2,4,6-trinetramine Using Negative Corona Discharge Ion Mobility Spectrometry[J].Talanta,2003,59:327-333.
    [84]A.L(?)pez-L(?)pez,J.S.Pic,H.Debellefontaine,Ozonation of azo dye in a semi-batch reactor:A determination of the molecular and radical contributions[J].Chemosphere,2007,66(11):2120-2126.
    [85]朱丽勤,何瑾馨,陈小立.染色废水臭氧氧化催化剂研制及其应用性能[J].东华大学学报(自然科学版),2005,31(1):772-775.
    [86]Sandra Gomes de Moraes,Renato Sanches Freire,Nelson Duran.Degradation and toxicity reduction of textile effluent by combined photocatalytic and ozonation processes[J]:Chemosphere,2000,40(4):369-37.
    [87]戴晓红,田俊莹,姚晓庆.UV+O_3+H_2O_2法处理活性染料的研究.针织工业,2006,3:65-66.
    [88]胡文容,钱梦禄,高廷耀.超声强化O_3技术在水处理中应用的研究[J].环境导报,1997,5:3-6.
    [89]E Dahi.Physicochemical aspect of disinfection of water by means of ultrasound and ozone[J].Water Research,1996,10:667-684.
    [90]王莉莉,杨孙楷.O_3/H_2O_2组合法处理染料中间体废水的研究[J].环境污染与防治,1994,16(5):11-14.
    [91]危想平,肖鹏.活性炭-臭氧处理印染废水试验[J].印染,2004,20:5-7.
    [92]Jans,Urshoigne,Jurg.Activated carbon black catalyzed transformation of aqueous ozone into·OH radicals[J].Science and Engineering,1998,20(1):67-89.
    [93]潘理黎,严国奇,郑飞燕,等.高压电晕与臭氧联用降解对硝基苯酚[J].环境科学,2005,26(6):115-118.
    [94]王冠一,周志军,郑攀峰,等.液电效应催化臭氧处理4种偶氮染料废水的研究.辽宁化工,2007,36:474-477.
    [95]曲久辉,林谡,王立立,等.高铁酸盐的溶液稳定性及其在水质净化中的应用[J].环境科学学报,2001,21(z1):106-109.
    [96]姜洪泉,于秀娟,王鹏,等.高铁酸钾预氧化去除水中苯酚及其机理[J],中国给水排水,2003,19(13):74-75.
    [97]杨中三.臭氧对印染废水的处理探讨[J],山东纺织经济,2007,(6):110-112.
    [98]水和废水监测分析方法(Ⅲ)[M].国家环保局《水和废水监测分析方法》编委会.北京:中国环境科学出版社,1998:354-356.
    [99]Standardisation Committee Europe,Iodoimetric method for the determination of ozone in a process gas,001/87(F),International Ozone Association,1987.
    [100]K.Kadirvelu,M.Palanival,R.Kalpana,et al.Activated carbon from an agricultural by-product,for the treatment of dyeing industry wastewater[J].Bioresource Technology,2000,74:263-265.
    [101]Drogaris G;Weiland P.Coalescence behavior of gas bubbles in aqueous solutions of n-alcohols and fatty acids.Chemical Engineering Science,1983,38:1501-1506.
    [102]高鸿宾.有机化学[M].北京:高等教育出版社.1999.
    [103]刘亚纳,严建华,李晓东.滑动弧等离子体处理酸性橙Ⅱ废水[J].化工学报,2008,59(1):221-227.
    [104]Nulsun H.Ince,G6kce Tezcanli-G(u|¨)yer.Impacts of pH and molecular structure on ultrasonic degradation of azo dyes[J].Ultrasonics,2004,42:591-596.

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