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高度氧化法(AOP)的特性及其在废水处理中的应用(下) | ||||||||||||||||||||||||||||||||||||||||||||||||||
作者:孙贤波等 文章来源:上海环境科学 点击数 更新时间:2004/4/18 21:41:35 文章录入:ahaoxie 责任编辑:ahaoxie | ||||||||||||||||||||||||||||||||||||||||||||||||||
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3 AOP法应用 表3列举了国外高度氧化法的应用研究实例。 表3 高度氧化法的应用研究实例[1,13~16]
近年来,AOP法在一定范围内已投入应用。美国密西根州从1994年开始将该法用于处理受有机氯化物污染的地下水, Mont-Valerien水处理厂就采用O3/UV来氧化处理来自Seine River原水中所含的阿特拉津,在南加州建造了世界上最大的H2O2/O3法净水设施,已于2000年正式运行。在法国已经将O3/H2O2过程同活性炭过滤结合,应用于水处理厂中。英国、荷兰等国为了去除和分解水中的农药,准备在普通净水厂中增加H2O2/O3法净水设施;德国、澳大利亚、法国和荷兰已采用O3/UV和H2O2/O3法来处理垃圾填埋渗透废水[1~4]。 4 结语 AOP法虽有其独特的优点,但目前处理成本较高,对含大量自由基清除剂(Scavenger),如碳酸根离子和重金属离子的废水氧化效果差。废水中有悬浮颗粒物存在时,必须预先去除,否则也会影响氧化效果。这些问题均有待深入研究解决。 5 参考文献 1 藤江幸一等.高度酸化处理技術(AOP)の现状と今後の展望.第37回日本水環境学会セミナー,1999. 2 Glaze W H.Drinking-water treatment with ozone.Environ Sci Technol,1987, 21(3):224~230. 3 Susan J Masten.Simon H R Davies.There are more than 40 municipal wastewater treatment plants in the united states that have ozonation facilities.Environ Sci Technol,1994,28:181A~185A. 4 Yao C C,Haag W R. Rate constants for direct reaction of ozone with several drinking water contaminates.Wat Res,1991,25:761~773. 5 Haag W R,Yao C C.Rate constans for reaction of hydroxyl radicals with several drinking water contaminants.Eniron Sci Technol,1995,26:1005~1013. 6 Glaze W H,Koga M,Cancilla D.Ozonation byproducts.2 improvement of an aqueous-phase derivatiztion method for the detedtion of formaldehyde and other carbonyl compounds formed by the ozonation of drinking water.Environ Sci Technol,1989,23:838~847. 7 Olson T M,Barbier P F.Oxidation kinetics of natural organic matter by sonolysis and ozone.Wat Res,1994,28:1383~1391. 8 Rook J J.Haloforms in drinking water.J Am Wat Works Assoc,1976,68:168~172. 9 Amy G L,Tan L,Davis M K.The effects of ozonation and activated carbon adorption on trihalomethane speciation.Wat Res,1991,25:191~202. 10 Xie Y,Reckhow D A.Identification of trihaloacetaldehydes in ozonated and chlorinated fulvic acid solutions.Analyst 1993,118:71~72. 11 Duguet J P,Brodard E,Dussert B,etc.Improvement in the effectiveness of ozonation of drinking water through the use of hydrogen peroxide.Ozone Sci Engng,1995,7:241~258. 12 Miller S.Disinfection products in water treatment.Environ Sci Technol, 1993,27:2292~2294. 13 Clasus H,Gerhard S, Oliver S, etc.Oxidation degradation of AOC COD by different advanced oxidation processes: A comparative study with two samples of a pharmaceutical wastewater.Wat Sci Technol,1997,35(4):257~264. 14 Antonio M,Santiago E,Gabriele S.How and why combine chemical and biological processes for wastewater treatment.Wat Sci Technol,1997, 35(4):321~327. 15 Jurg H.Inter-calibration of OH radical sources and water quality parameters.Wat Sci Technol,1997,35(4):1~8. 16 Vinodgopal K,Peller T,Markogon O,etc.Ultrasonic miveralization of a reactive textile azo dyes Remazol black B.Water Research,1998, 32(12):3646~3650.
作者孙贤波,男,1973年生,1999年毕业于复旦大学环境与工程系硕士、助教。上海市科委资助项目,编号002312029。 |
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