| [1] Gupta V K, Ali I, Saini V K.Removal of chlorophenols from wastewaterusing red mud：an aluminum industry waste[J].EnvironmentalScience & Technology, 2004, 38(14)：4012-4018.
[2] 王旭刚, 孙丽蓉.五氯酚的污染现状及其转化研究进展[J].环境科学与技术, 2009, 32(8)：93-100.
[3] Wiley V.Ullmann’s encyclopedia of industrial chemistry[M].NewYork：Wiley-VCH, 2011：160-196.
[4] Jung M W, Ahn K H, Lee Y H, et al.Adsorption characteristics ofphenol and chlorophenols on granular activated carbons (GAC)[J].Microchemical Journal, 2001, 70(2)：123-131.
[5] Sze M F F, McKay G.An adsorption diffusion model for removal ofpara-chlorophenol by activated carbon derived from bituminouscoal[J].Environmental Pollution, 2010, 158(5)：1669-1674.
[6] Estevinho B N, Martins I, Ratola N, et al.Removal of 2, 4-dichlorophenoland pentachlorophenol from waters by sorption using coal flyash from a Portuguese thermal power plant[J].Journal of HazardousMaterials, 2007, 143(1/2)：535-540.
[7] Monsalvo V M, Mohedano A F, Rodriguez J J.Activated carbonsfrom sewage sludge：application to aqueous-phase adsorption of 4-chlorophenol[J].Desalination, 2011, 277(1/2/3)：377-382.
[8] Ku Y, Chen K Y, Lee K C.Ultrasonic destruction of 2-chlorophenolin aqueous solution[J].Water Research, 1997, 31(4)：929-935.
[9] Hao Hongwei, Wu Minsheng, Chen Yifang, et al.Cavitation-induced duced pyrolysis of toxic chlorophenol by high frequency ultrasonicirradiation[J].Environmental Toxicology, 2003, 18(6)：413-417.
[10] 施汉昌, 赵胤慧.氯酚废水的生物处理技术的研究与进展[J].化学通报, 1998(8)：1-5.
[11] 王晓东, 张光辉, 顾平, 等.水体中氯酚类污染物的生物降解性研究进展[J].中国给水排水, 2008, 24(16)：17-21.
[12] Kaballo H P, Zhao Yuangang, Wilderer P A.Elimination of pchlorophenolin biofilm reactors-a comparative study of continuousflow and sequenced batch operation [J].Water Science and Technology, 1995, 31(1)：51-60.
[13] Shi X Y, Sheng G P, Li X Y, et al.Operation of a sequencing batchreactor for cultivating autotrophic nitrifying granules [J].BioresourceTechnology, 2010, 101(9)：2960-2964.
[14] Khan M Z, Mondal P K, Sabir S, et al.Bioremediation of 2-chlorophenol containing wastewater by aerobic granules-kineticsand toxicity[J].Journal of Hazardous Materials, 2011, 190(1/2/3)：222-228.
[15] Carucci A, Milia S, Cappai G, et al.A direct comparison amongst different technologies(aerobic granular sludge, SBR and MBR) forthe treatment of wastewater contaminated by 4 -chlorophenol [J].Journal of Hazardous Materials, 2010, 177(1/2/3)：1119-1125.
[16] Lee D J, Chen Y Y, Show K Y, et al.Advances in aerobic granuleformation and granule stability in the course of storage and reactoroperation[J].Biotechnology Advances, 2010, 28(6)：919-934.
[17] 顾荷炎, 张兴旺, 李中坚, 等.微生物燃料电池协同处理含氯酚废水[J].科学通报, 2007, 52(18)：2214-2216.
[18] Atuanya E I, Purohit H J, Chakrabarti T.Anaerobic and aerobicbiodegradation of chlorophenols using UASB and ASG bioreactors[J].World Journal of Microbiology & Biotechnology, 2000, 16(1)：95-98.
[19] Oh W D, Lim P E, Seng C E.Kinetic modeling of bioregeneration ofchlorophenol-loaded granular activated carbon in simultaneous adsorptionand biodegradation processes[J].Bioresource Technology, 2012(114)：179-187.
[20] Glaze W H.An overview of advanced oxidation processes ：currentstatus and kinetic models.in：chemical oxidation technologies fornineties [M].Lancester USA：Technomic Publishing Company, 1994：1-9.
[21] Rodrigo M A, Michaud P A, Duo I, et al.Oxidation of 4-chlorophenolat boron-doped diamond electrode for wastewater treatment [J].Journal of the Electrochemical Society, 2001, 148(5)：60-64.
[22] Munoz M, de Pedro Z M, Casas J A, et al.Assessment of the generationof chlorinated by products upon Fenton-like oxidation ofchlorophenols at different conditions[J].Journal of Hazardous Materials, 2011, 190(1/2/3)：993-1000.
[23] Chen G, Wang Z, Xia D.Electrochemically reductive dechlorinationof micro amounts of 2, 4, 6-trichlorophenol in aqueous mediumon molybdenum oxide containing supported palladium[J].Electrochimica Acta, 2004, 50(4)：933-937.
[24] 杜连柱.氯酚污染地下水的强化原位生物修复技术[D].长春：吉林大学, 2008 |