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催化湿式氧化法处理高浓度染料废水的研究 被引量:12

Degradation of High Concentration Dye Wastewater by Catalytic Wet Air Oxidation
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摘要 通过共沉淀法制备了Co-Zn复合氧化物催化剂,用于催化湿式氧化处理高浓度分散红玉染料废水。结果表明,在400℃焙烧制得的Co-Zn摩尔比为1∶1的催化剂氧化活性较高,当分散红玉染料废水的COD为10000mg/L、反应温度为150℃、反应压力1.0~1.2MPa时,反应60分钟,COD去除率达到80%。 Co-Zn complex oxide catalysts for catalytic wet air oxidation of high concentration dye wastewater containing Disperse Rubine S-2GFL were prepared by coprecipitation methods.The results showed that Co-Zn(1∶1)catalyst calcined at 400℃ exhibited better activity,the highest COD removal efficiency was achieved to 80% after 60 minutes reaction when the reaction conditions were 150℃,1.0-1.2MPa,COD of Qisperse Rubine dye wastewater 10000mg/L.
作者 王鹏 孙柳
出处 《染料与染色》 CAS 2006年第5期53-55,共3页 Dyestuffs and Coloration
关键词 湿式氧化 催化剂 分散红玉S-2GFL 染料废水 COD去除率 wet air oxidation catalyst Disperse Rubine S-2GFL dye wastewater COD removal efficiency
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  • 1刘东方,丁耘,李江华.混凝剂处理染料及其中间体废水应用[J].城市环境与城市生态,1997,10(2):11-14. 被引量:10
  • 2王爱民,曲久辉,姜桂兰.电化学方法降解酸性红B研究[J].环境科学,2003,24(2):108-111. 被引量:38
  • 3[3]Mishra V S,Vijaykumar V,Joshi J B.Wet air oxidation[J].Ind Eng Chem Res,1995,34(1):2 -48
  • 4[4]Neri G,Pistone A,Milone C,Galvagno S.Wet air oxidation of p-coumaric acid over promoted ceria catalysts[J].Applied Catalysis B:Environmental,2002,38:321-329
  • 5[5]Oliviero L,Barbier J,Duprez D.Catalytic wet oxidation of phone and acrylic acid over RuPC and Ru-CeO2 PC catalyst[J].Appl Catal,2000,25:267-275
  • 6张世鸿,涂学炎,杨中民,李自弘,杨英,钱彪,洪品杰.模拟废水丁二酸的催化湿式氧化处理[J].环境科学,2003,24(1):107-112. 被引量:24
  • 7[7]Alejandre A,Medina F,Fortuny A,Salagre P,Sueiras J E.Characterisation of copper catalysts and activity for the oxidation of phenol aqueous solutions[J].Applied Catalysis B:Environmental,1998,16:53-67
  • 8[8]Pintar A,Levee J.Catalytic oxidation of organics in aqueous solutions:kinetics of phenol oxidation[J].Journal of Catalysis,1992,135:345 -354

二级参考文献26

  • 1张宗恩,徐传宁.废铁屑净化偶氮染料废水及其机理的研究[J].上海环境科学,1995,14(10):25-27. 被引量:20
  • 2[1]Ch Comninellis, A Nerini. Anodic oxidation of phenol in the presence of NaCl for wastewater treatment. J. Appl. Electrochem., 1995,25: 23~28.
  • 3[2]Traatti S. Electrochemistry and environment: The Role of Electrocatalysis. Int. J. Hydrogen Energy, 1995, 20( 10):835 ~ 844.
  • 4[3]Do J S, Yeh W C. Paired electrooxidative degradation of phenol with in situ electrogenerated hydrogen peroxide and hypochlorite. J. Appl. Electrochem., 1996, 26: 673~678.
  • 5[4]Marco Panizza et al. Electrochemical treatment of wastewater containing polyaromatic organic pollutants. War. Rcs.,2000, 34(9): 2601 ~ 2605.
  • 6[5]Tomat R. Electrochemical oxidation of toluene promoted by OH radicals. J. Appl. Electrochem. , 1984, 14: 1~8.
  • 7[6]Comninellis Ch,C Pulgarin. Anodic oxidation of phenol for waste water treatment. J. Appl. Electrochem. , 1991, 21:703 ~ 708.
  • 8Levec J. Wet oxidation processes for treating industrial wastewaters. Chem. Biochem. Eng. Q., 1997, 11 (1):47~58.
  • 9Josef Prousek. Advanced oxidation processes for water treatment. Chemical processes. Chem. Listy. , 1996, 90:229~237.
  • 10Luck F. A review of industrial catalytic wet oxidation processes. Catalysis Today, 1996, 27:195~202.

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