木质素磺酸盐氧化降解的研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
造纸业每年排放大量的木质素。由于木质素其本身结构特点,在环境中难以被转化和消除,造成了严重的环境污染和资源浪费。如何解决造纸废水的污染问题、开发造纸废水处理新技术、实现可持续发展,是至今尚未完全解决的技术难题,也是世界各国造纸业和环境保护部门的研究重点。
     低温等离子体技术是近年来新兴起的一项新型水处理氧化技术,它兼具高能电子辐射、紫外光解、臭氧氧化等方面的共同作用,具有降解速率快、处理范围广、无污染、易操作等优点。本文利用介质阻挡放电低温等离子体,采取空气气动雾化方法,对木质素磺酸盐进行降解;同时还研究木质素的臭氧氧化降解,以期获得一种工业废液的高效绿色处理方法,为解决日益严重的环境问题提供帮助。
     臭氧氧化降解实验结果表明,在常温常压下木质素就能被臭氧氧化降解。反应时间、催化剂种类等对反应的影响较大,而超声波、温度等条件的影响很小。在实验条件下,CuSO4或TiO2/α-Al2O3催化剂有利于木质素磺酸钠的臭氧氧化降解反应,而且,臭氧氧化降解反应在木质素降解率为80%左右时达到平衡。
     以紫外可见光谱(UV)、红外光谱(FTIR)和1H NMR谱等对木质素磺酸盐降解前后进行了表征结果说明,介质阻挡放电低温等离子体空气气动雾化法可以降解木质素磺酸盐水溶液。木质素磺酸盐降解率的高低受电极间隙、输出电压、催化剂种类、催化剂用量、反应时间等工艺条件的影响。本实验的优化条件为:以硫酸铜为催化剂,电极间隙2 cm、输出电压3000 V、频率10 KHz、反应时间2.3 ms、催化剂用量3.2%条件下,浓度1g/L的木质素磺酸盐,降解率可达50%。
The emissions of a large number of lignin from paper industry results in serious environmental pollution and resource waste. Because of having its own structural characteristics, lignin is very difficult to be transformed and eliminated in the nature environment. How to solve the problem of water pollution, develop new treatment technology for papermaking wastewater, realize society sustainable development are the difficult problems which haven't been fully solved in the international paper industry till now and have become the research priorities of paper industry and environmental protecting departments of countries all over the world.
     Non-thermal plasma oxidation is a new advanced oxidation technology developed recently, which has the synergystic degradation function from high energy electron radiation, UV photolysis, pyrolysis to ozone oxidation. It is different from the traditional degradation method, this new oxidation technology with the advantages of speedy degradation rate, wide handling range, no pollution, and easy to operate can effectively remove hardly degradable substances from industry wastewater. In this thesis we used dielectric barrier discharge (DBD) plasma or used ozone to degrade lignin.
     The results of ozone oxidation showed that lignin can be degraded under ambient temperature and atmosphere pressure. Among process condition, catalyst or reaction time had remarkable effect on lignin oxidative degradation rate. However, reaction temperature or ultrasonic had little effect on the degradation rate. CUSO4 or TiO2 /α-Al2O3 catalyst was beneficial to the reaction of lignin oxidative degradation. Under test conditions the reaction of lignin oxidative degradation would reach equilibrium when the lignin degradation rate was about 80%.
     The reaction of lignin oxidation degradation using DBD plasma carried out by gas-jet expansion method. The degradation of lignosulfonate during this process was characterized by UV, FTIR and 1H NMR spectroscopy. The test results indicated that non-thermal plasma technology was effective to degrade lignosulfonate. The effect of electrode spacing, plasma voltage, catalysts, concentration of catalyst or reaction times on degradation rate was separately studied. Optimum process condition were determined:concentration of lignosulfonate was 1 g/L, electrode spacing was 2 cm, the amount of catalyst CUSO4 was 3.2%, plasma voltage was 3 KV, plasma frequency was 10 KHz, plasma reaction time was 2.3 ms. Under this reaction condition the degradation rate of lignosulfonate can achieved to 50%.
引文
[1]国家经贸委.造纸工业“十五”规划.1http://www.cas.cn/html/Dir/2001/08/27/7994.htm
    [2]贺延龄.废水的厌氧处理[M].北京:中国轻工业出版社,1998.
    [3]雍永智.我国几种工业废水治理研究-造纸工业废水[M].北京:化学工业出版社,1988.
    [4]吕炳南,温沁雪,陈志强.制浆造纸工业废水污染控制方法及研究进展[J].哈尔滨建筑大学学报,2001,(6):48-52.
    [5]刘飞跃,徐银崧.纳米半导体光催化氧化木质素制香兰素初探[J].纤维素科学与技术,2006,14(1):16.
    [6]蒋挺大.木质素[M].北京:化学工业出版社,2001.
    [7]陈立祥,章怀云.木质素生物降解及其应用研究进展[J].中南林学院学报,2003,23(1):79-85.
    [8]陈子爱,邓小晨.微生物处理利用秸秆的研究进展[J].中国沼气,2006,24(3):31-35.
    [9]谭东.木质素的提取及应用[J].广西化工,1994,23(4):6-13.
    [10]陈克利,任承霞,石淑兰等.桦木硫酸盐木素的分离及结构分析[J].中国造纸学报,1999(14):9-14.
    [11]李友明,陈中豪.木素苯基丙烷结构单元经典式的表达与计算[J].中国造纸学报,1999(14):98-100.
    [12]Sharma R. K., Wooten J. B., Baliga V. L., et al. Characterization of chars from pyrolysis of lignin [J]. Fuel,2004,83:1469~1482.
    [13]L.Khezmi, A.Chetouani, B.Taouk,R. et al Production and characterisation of activated carbon from wood components in powder:Cellulose, lingin, xylan [J]. Powder Technology,2005,157: 48~56.
    [14]中野准三.木质素的化学[M].北京:中国轻工出版社,1984,22-23.
    [15]FAIXO. Neue Aspekte zur Lignin verwendung in Green Mengen [J]. Das Papier,1992,(12): 733.
    [16]CHEN R, WU G. Modified lignosulfonates as adhesive [J]. J Appl Polym Sci,1994,52(3): 437.
    [17]ZD YBAK W T. Anionic bituminous emulsions [P]. US Patents:4427449,1984.
    [18]SON J,NEALE G H,HORNOF V. Interfacial tension and behavior characteristics of petroleum sulfonate lignosulfonate mixtures [J]. Can J Chem Eng,1982,60(5):684.
    [19]高玉杰.废纸再生实用技术[M].北京:化学工业出版社,2003.
    [20]丁春生,刘宏远,王卫文等.高效气浮技术设备及其在造纸废水处理中的应用[J].浙江工业大学学报,2001,29(4):398.
    [21]江红光,梅荣武.高效浅层气浮技术在造纸废水处理中的应用[J],环境污染与防治,2003(4):180.
    [22]吕波.涡凹气浮法在再生浆造纸废水处理中的应用[J].工业水处理,2003,23(12):72.
    [23]刘晓静,吴昊,甘聃等.废纸再生造纸废水治理新工艺-涡凹气浮法[J].中国资源综合利用,2007,25(6):24-25.
    [24]刘成波.活性炭吸附法去除废纸造纸废水中COD[J].纸和造纸,2003(4):66-68.
    [25]王森,张安龙.造纸废水回用的研究[J].江苏造纸,2005,34(3):45-48.
    [26]宫克.改性膨润土对工业废水的脱色[J].沈阳大学学报,2002,14(4):104.
    [27]万金泉,周清华.废纸脱墨制浆废水特点及治理[J].中华纸业,2003,21(3):58.
    [28]万金泉,陈中豪.废纸脱墨废水絮凝生化二级处理的研究[J].中国造纸学报,1997(12):82.
    [29]刘斌,张梅.造纸废水混凝处理研究[J].内蒙古石油化工,2005(6):1-3.
    [30]Petzold G, Nebel A, Buchhammer H M, et al. Preparation and characterization of different polyelectrolyte complexes and their application as flocculants [J]. Colloid Polym Sci,1998, 276(2):125~130.
    [31]李尔,范跃华.采用强化混凝法提高污水处理效能[J].华中科技大学学报(城市科学版),2002,19(3):92-94.
    [32]江霜英,高廷耀.上海污水二期工程污水化学强化处理的试验研究[J].上海环境科学,2002,21(1):40-42.
    [33]邹龙生,王国庆.有机絮凝剂的现状和未来[J].化工技术与开发,2002,31(4):22-24.
    [34]严三强,邓正栋.微生物絮凝剂及其在污水处理中的应用[J].四川环境化学,2003,22(2):31-34.
    [35]聂艳秋,唐正斌.酸化-UBF-混凝法处理制浆造纸废水[J].中国给水排水,2002,18(6):75.
    [36]杨玲.用于造纸废水处理的膜分离技术研究进展[J].四川理工学院学报(自然科学版),2005,18(2):62-65.
    [37]张克峰,邢丽贞,张彦浩等.膜化学技术在造纸废水深度处理中的应用研究[J].环境工程,2004,22(4):10-12.
    [38]黄江丽,施汉昌.MF与UF组合工艺处理造纸废水研究[J].中国给水排水,2003,19(6):13-15.
    [39]刘俊超译.限制营养盐的生物膜预处理是提高活性污泥处理制浆和造纸废水的有效方法[J].造纸信息,2002(12):14.
    [40]谭绍早,陈震华.聚丙烯腈纳滤膜的制备及对造纸废水的截流性能[J].中国造纸学报,2002(2):63-66.
    [41]金永灿.化学纸浆的氧脱木质素[J],纤维素科学与技术,1998,6(2):5-14.
    [42]朱光灿,吕锡武,宋海亮等.脱水素工艺处理造纸废水的实践与机理[J].环境污染治理技术与设备,2002(10):64-67.
    [43]许力.超声波膜电解技术碱回收效果的实验研究[J].兰州铁道学院学学报(自然科学版)
    2003,22(1):127.
    [44]张玉蕴.浅析造纸厂废水分段处理技术[J].山西建筑,2003,29(4):254.
    [45]吴忆宁,刘士锐,任南琪等.臭氧化处理造纸废水的实验研究[J].哈尔滨商业大学学报(自然科学版),2003,19(4):394
    [46]易封萍.臭氧-混凝法处理造纸废水[J].工业水处理,2001,21(1):34.
    [47]Glaze W H., Kang J W, ChaPin D H. The chemistry of water treatment.Processes involving ozone, hydrogen peroxide and ultraviolet radiation [J]. Ozone Sci.&Eng.,1987,9(4):335.
    [48]R.C.Weast, M.J.Astle, W.H.Bayer.CRC Handbook of Chemistry and Physics (CRC Handbook) [M]. Florida:CRC.Press.Inc.Boca Raton,1985.
    [49]Haag W.R, Yao C.C. Rate constants for reaction of hydroxy radicals with several drinking water contaminants [J]. Environ.Sci.Teehnol,1992,26:1005~1013.
    [50]Clasus Hofl, Gerhard sigl, Oliver Specht, et al. Oxidation of AOC COD by different advanced oxidation processes:A comparative study with two samples of a pharmaceutical waste-water [J]. Wat.Sci.Technol,1997,35(4):257~264.
    [51]Jurg Hoigne. Inter-calibration of OH radical sources and water quality parameters [J]. Wat.Sci.Technol.,1997,35(1):1~8.
    [52]Vinodgopal K. Peller Tulie, Oksana Markogon, et al. Ultrasonic mineralization of a reactive textile azo dyes Remazol black B [J]. Water Research,1998,32(12):3646~3650.
    [53]Fujishima A, Honda K. Electrochemical photolysis of water at a semiconductor electode [J]. nature,1972,238(5358):37~38.
    [54]Anderson M A. Amsterkam[C]. Proceedings of the First International Conference on TiO2 Photocatalytic Purification and Treatment of Water and Air.New York.,1993.
    [55]雷乐成主编.水处理高级氧化技术[M].北京:化学工业出版社,2001.
    [56]Sattler C, L de Oliveira, TzschirnerM, et al.Solar photocatalytic water detoxification of paper mill effluents [J]. Energy,2004,29:835.
    [57]Tinucci L, Borgarello E, et al. Treatment of industrial wastewaters by photocatalytic oxidation on TiO2, photocatalytic purification and Treatment of water and elsevier science publishers [J]. Amsterdam,1993:585.
    [58]Mansilla H D, et al. ZnO-catalytsed photodegration of kraft blackliquor [J]. Photochem. 1994, (78):267.
    [59]崔玉民,朱亦仁,王克中.用复相光催化剂WO3/a-Fe2O3/W深度处理造纸废水的研究[J].感光科学与光科学,2001,19(2):131-138.
    [60]M Cristina Yeber, Jaime Rodriguez, Juanita Freer, et al. Photocatalytic degradation of cellulose bleaching effluent by supoported TiO2 and ZnO [J]. Chemosphere,2000,41:1193.
    [61]Perez M, et al. photocatalytic treatment of paper pulpbleach effluents[J]. Quim Anal,1997, 16(3):211.
    [62]朱亦仁,解恒参,张振超.TiO2光催化氧化法处理草浆纸厂废水的研究[J].安全与环境学报,2005,5(1):20-22.
    [63]任朝华.絮凝-纳米二氧化钛光催化氧化法处理造纸废水[J].纸和造纸,2007,26(4):68-70.
    [64]刘德启,汪守建,牛明改等.负载亚甲基蓝光敏氧化法处理造纸废水研究[J].环境污染治理技术与设备,2002,3(11):60.
    [65]唐受印,戴友芝.废水处理水热氧化技术[M].北京:化学工业出版社,2002
    [66]Akolekar D B, Bhargava S K. Catalytic wet oxidation:An environ-mental solution for organic pollution removal from paper and pulp industrial waste liquor [J]. Applied Catalysis A:General,2002,236:255~262.
    [67]Pintar A, Besson M, Gallezot P. Catalytic wet air oxidation of kraft bleach olant effluents in a trickle-bed reactor over a Ru/Tio catalyst [J]. Applied Catalysis B:Environmental,2001,31: 275~290.
    [68]周丹,呼世斌,张涛.Fenton氧化-粉煤灰处理造纸废水的研究[J].西北农林科技大学学报(自然科学版),2004,33(6):156-158.
    [69]Martin Fox, Tatsuya Noike. Wet oxidation pretreatment for the increase in anaerobic biodegradability of newspaper waste [J]. Bioresource Technology,2004,91:273.
    [70]Foussard J N, Debellefontaine H, et al. Efficient elimination of organic liquid wastes:Wet air oxidation [J]. Environ Eng,1989,115(2):367~385.
    [71]Emanuel N M, Denisof E T, Maizus J R. Liquid phase oxidation of hydrocarbons [M]. New York:Plenum Press,1967.
    [72]解恒参,朱亦仁.高级氧化技术在造纸废水处理中的研究进展[J].江苏环境科技,2004,17(4):30-33.
    [73]杜艳芬,韩卿,张荣莉.超临界水氧化法处理废水[J].西南造纸,2001(4):13.
    [74]Kruse A, Schmieder H. Supercritical oxidation in water and carbon dioxide Environ Prog,1998,17(4):234~239
    [75]王亮,王书众,张钦明等.含油废水的超临界水氧化反应机理及动力学特性[J].西安交通大学学报,2006,40(1):115-119.
    [76]戴航,黄卫红,钱晓良.超临界水氧化法处理造纸废水的初步研究[J].工业水处理,2000,20(8):23-26.
    [77]孙德智.环境工程中的高级氧化技术[M].北京:化学工业出版社,2002,310-330,169-210.
    [78]周珊,陆晓华,吴晓晖等.超声技术降解造纸黑液[J].湖北师范学院学报(自然科学版),2002,22(2):21.
    [79]李志建,李可成,周明.超声波-厌氧生化法处理碱法草浆黑液的研究[J].环境科学技术,2000,89(5):42-44.
    [80]钱伯兔.沉淀-超声波气浮-接触氧化法处理退浆废水[J].新疆环境保护,1999,21(4):33-36.
    [81]刘汝鹏,于水利,曲莹.双氧水强化微电解法深度处理造纸中段废水的研究[J].给水排水,2006,32(3):48-52.
    [82]幸福堂,刘成焱,刘红.电凝聚法处理造纸中段废水的研究[J].工业水处理,2005,25(4):40-43.
    [83]孙金勇,庄云龙.电絮凝法用于处理废纸脱墨废水[J].上海造纸,2004,35(2):49-51.
    [84]景峰,王耀新,宋文菊.试论电化学-凝聚法处理造纸废水[J].黑龙江环境通报,2000,24(2):81-82.
    [85]任拥政,章北平,张晓昱等.铁炭微电解对造纸黑液的脱色处理[J].水处理技术,2006,32(4):68-70.
    [86]叶匀分,王志宏,李承瑞.采用高过电位阳极处理废水中酚的研究[J].上海化工,1999,24(11):18-21.
    [87]杨润昌,周书天.含酚废水湿式电化学氧化处理研究[J],湘潭大学自然科学学报,2001,23(3):55-58.
    [88]方建章,黄少斌.厌氧-混凝工艺处理造纸厂终端废水试验研究[J].环境科学与技术,2001(4):32.
    [89]陈志强.采用厌氧-好氧技术处理制浆造纸废水[J].中国造纸,2003,22(7):27.
    [90]杜书田,邢海涛,衣守志.造纸厂废水回用处理工艺方案可行性分析[J].环境保护,2007,29(2):29-33.
    [91]张艳凤,孙艳铃,边江凤.废水零排放在废纸造纸废水中的应用[J].宁夏工程技术,2007,6(2):147-149.
    [92]王裕金,白斌,高莉.水解酸化-厌氧-好氧-混凝工艺处理造纸废水[J].新乡师范高等专科学校学报,2002,16(2):35.
    [93]Youngseob Yu, Seoklwan Hwang. Augmentation of secondary organics for enhanced pretreatment of thermomechanical pulping wastewater in biological acidogenesis [J]. Process Biochemistry,2003,38(10):1489.
    [94]蒋佩霞,黄江丽,张小杰.AAB式生物处理高浓度造纸废水[J].环境工程.1994,12(1):11-13.
    [95]Hiroshi Kajikawaeta. Degradation of benzylether bonds of lignin by ruminal microbes[J]. FEMS Microbiology letters of European.2000,187(7):15~20.
    [96]韩彪.水解-好氧工艺处理造纸中段废水[J].污染防治技术,2003,16(3):97-98.
    [97]Chen Yuancai, Zhan Huaiyu, Chen Zhonghao, et al. Study on the treatment of the sulfate pulp CEH bleaching effluents with the coagulation-anaerobic acidifcation-aeration package reactor [J]. Water Research,2003,37:2106
    [98]刘素英,高心红,池明军.造纸废水的生物后处理工艺探讨[J].西北轻工业学院学报,2002,20(3):85.
    [99]汤武平,陈季华,杨波.氧化沟结合水解工艺处理造纸废水[J].中国给水排水,2001,17(5):54.
    [100]刘晓华,黄俊.处理造纸废水的生化物理法[J].成都纺织高等专科学校学报,2002,19(3):21.
    [101]曲景奎,周桂英,隋智慧等.HCR工艺在造纸废水治理中的应用[J].环境污染治理技术与设备,2002,3(1):74.
    [102]刘俊超译.SBR工艺在造纸废水处理的应用实例[J].国际造纸,2003,22(5):58.
    [103]夏汉平.人工湿地处理污水的机理与效率[J].生态学杂志,2002,21(4):51.
    [104]伍建东.制浆造纸废水的生物处理技术[J].造纸科学与技术,2002,21(1):34.
    [105]张洪芬,李绪谦,王春来等.土壤渗滤法治理湿地水环境污染[J].城市环境与城市生态,2003,16(6):210.
    [106]王庆九,唐亮,柏益芜.造纸废水处理人工湿地系统规划研究[J].重庆环境科学,2003,25(1):328.
    [107]韩勤友,徐雅娟,高升平.生物塘-人工湿地联合技术处理制浆造纸废水工程实践[J].陕西环境,2003,19(3):12.
    [108]余永东,童茜炜.地表漫流-地表流湿地工艺在处理废纸造纸生产废水[J].工业水处理,2003,23(12):59.
    [109]M.Tuomela, M.Vikman,A.Hatakka, et al. Biodegradation of lignin in a ompost environment: a review [J], Bioresource Technology,2000(72):169~183.
    [110]李晨陶.二氧化钛光催化降解木质素类模型物-紫丁香醇[D].天津科技大学博士论文,2009.
    [111]H.Erdtman Resrarch,1950,3:63.
    [112]http://www.coronalab.com/denglizijieshao.htm
    [113]陈瑜.低温等离子体降解染料废水的实验研究[D].东北师范大学,2008.
    [114]陆泉芳,俞洁.辉光放电等离子体处理有机废水研究进展[J].水处理技术,2007,33(1):9-15.
    [115]A K SHARMA, G B JOSEPHSON, DMCAMAIONI. Destruction of pentachlorophenol using glow discharge plasma process [J]. Enviro Sci Technol.,2000,34:2267~2272.
    [116]李胜利,李劲,王泽文等.脉冲电晕放电对印染废水脱色效果的实验研究[J].环境科学,1996,17(1):13-15
    [117]刘小春,冯长根.水中高压脉冲放电的光辐射研究[J].北京理工大学学报,1999,19(1):8212.
    [118]Clause M, Trousselirf R, Annie F, et al. Method for Hydroxy alkylating Cbaoeyelic AromatieEthers[P]. PCT Int.APPI.WO9637452.
    [119]G.Wu, M.Heitz. J.Wood Chem. Teehnol.1995 (15)189.
    [120]TaarbankoV.E et al. React.Kinet.Catal.Lett.,1995,55(1):161~170.
    [121]Van Ness, J.H., "Encyclopedia of Chemical Technology", Vol.23,3rd ed., John Wiley&Sons, New York,1983,704~717.
    [122]袁履冰,丁勇.香兰素合成及分离技术进展[J].现代化工,1990,1:33-35.
    [123]Minisci, F., Citterio, A., Giordano, C. Acc. Chem. Res.1983,16,27.
    [124]Minisci, F., Maggioni, P. Chim. Ind.1979,61,101.
    [125]Leopold, B.; Malmstro M.I.L. Acta Chem. Scand.1951,5,936.
    [126]Leopold, B. Acta Chem. Scand.1952,6,38.
    [127]Brickman, W. J.; Purves, C. B. J. Am. Chem. Soc.1953,75,4336.
    [128]Pew,J.C.J.Am.Chem. Soc.1955,77,2831.
    [129]Gogotov A F,Rybalchekno N A,Mkaovskaya T l,etal.Catalytic Nitobenzene Oxidation of Lignins[J].Nnak,Ser.Khim,1996(12):3004-3007.
    [130]W.G.Glasser etal.Encyclopedia of Polymer Scinece and Engnieering, Wiley,New York,1987:795.
    [131]Deseano Cobos. Production of vhallin from sugarcane bgaasese[J]. Tecnol.Cienc.Educ,1990, 6(2):32~38.
    [132]张宏书,钟洽.蔗渣碱木质素制紫丁香醛和香兰素的研究:Ⅰ.蔗渣碱木质素低分子氧化产 物的制备[J].纤维素科学与技术,1994,(2):155-161.
    [133]Arabanko. A study of vanillin Production form lingins:Catalytic oxidation and isolation[J]. Int.SymP.wood.PulPingCghem,8(3),319~324.
    [134]罗廉,李杰.木素磺酸制取香兰素的氧化反应[J].化学反应工程与工艺,1990,6(4):53-59.
    [135]Gogotov etal. Oxidation of lingin by menas of nirtobenzene:is catalysis possible? Chem. Susatnibale Dev.,1996,4(1):67.
    [136]Nugyne Thi Bieh Thuy etal.Catalyticoxidation of lingin to vanillin[J].Tap Chi Hoa Hoc, 1992,30(2):11~12,15.
    [137]Luo X L, Zhan H Y, Chai X S, et al. A novel method for determination of aromatic aldehyde monomers in lignin degradation liquor [J]. Industrial & Engineering Chemistry Research, 2009,48(5):2713~2716.
    [138]Dagley S, Evans W C, Ribbons D W. New pathways in the oxidative metabolism of aromatic compounds by micro-organisms [J]. Nature,1960,188:560~566.
    [139]Garcia S, Latge J P, Prevostm C, et al. Wood degradation by white rot fungi:cytochemical studies using lignin peroxidase-immuno-globulin-gold complexes [J]. Applied and Environmental Microbiology,1987,53(10):2384~2387.
    [140]Chun H, Wang Y Z, Tang H X. Destruction of phenol aqueous solution by photocatalysis or direct photolysis [J]. Chemosphere,2000,41:1205~1209.
    [141]Antonaraki S, Androulaki E, Dimotikali D, et al. Photolytic degradation of all chlorophenols with polyoxometallates and H2O2 [J]. Photochem Photobiol A:Chem,2002,148:191~197.
    [142]Doong R A, Chen C H, Maithreepala R A, et al. The influence of pH and cadmium sulfide on the photocatalytic degradation of 2-chlorophenol in titanium dioxide suspensions [J]. Water Res,2001,35:2873~2880.
    [143]James C W, Thomas J. Sonochemical dechlorination of hazardous wastes in aqueous systems [J]. Waste Manage,1995,15:303~309.
    [144]Giovanni D R, Gabriel D G. Removal and destruction of toxic micropolluting organic compounds from waste waters by a combined NF and SCWO process[J]. Desalination,2001, 138:61-64.
    [145]Malik M A, Ghaffar A. Water purification by electrical discharges[J]. Plasma Sources Sci Technol,2001,10:82~91.
    [146]Lin K J, Cooper J W, Nickelsen M G, et al. Decomposition of aqueous solutions of phenol using high energy electron beam irradiation-a large scale study[J]. Appl Radiat Isot,1995,46: 1307~1316.
    [147]Clements J S, Sato M, Davis R H. Preliminary investigation of prebreakdown phenomena and chemical reactions using a pulsed highvoltage discharge in water [J]. IEEE Trans Ind Appl.,1987:IA-23:224~235.
    [148]Beltran-Heredia J, Torregrosa J, Dominguez J R, et al. Treatment of black-olive wastewaters by ozonation and aerobic biological degradation[J]. Water Research,2000,34(14): 3515~3522.
    [149]Gracia R, Cortes S, Sarasa J, et al. TiO2-catalysed ozonation of raw Ebro river water[J]. Water Research,2000,34(5):1525~1532.
    [150]陈银生,张新胜,常胜等.脉冲放电等离子体降解废水中有机物的作用机理探索[J].环境科学学报,2005,25(1):113-116.
    [151]吴向阳,仰榴青,储金宇等.低温等离子体处理废液技术[J].化工环保,2002,22(2):111-114.
    [152]Ma Y S, Chang C N, Chiang Y P, et al. Photocatalytic degradation of lignin using Pt/TiO2 as the catalyst [J]. Chemosphere,2008,71(5):998~1004.
    [153]王雪莲,王林格,黄勇.木质素磺酸盐在UV/H2O2下的降解[J].林产化学与工业,2007,27(3):98-102.
    [154]赵瑶兴,孙祥玉.有机分子结构光谱鉴定[M].北京:科学出版社,2003:35-36.
    [155]竹涛,李坚,梁文俊等.低温等离子体技术控制污水处理厂恶臭气体[J].环境工程,2008,26(5):9-12.
    [156]朱承驻,董文博,侯惠奇.等离子体技术降解茜素红水溶液的机理研究[J].上海环境科学,2003,22(11):760-764.
    [157]Mista W, Kacprzyk R. Decomposition of toluene using non-thermal plasma reactor at room temperature [J]. Catalysis Today,2008,137:345~349.

© 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