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H_2O_2湿式氧化处理含酸性红B染料模拟废水的研究 被引量:39

Treatment of Acid Red B-containing water by wet peroxide oxidation
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摘要 用H2 O2 作氧化剂 ,在连续式的压力反应器内探索了WPO(过氧化氢湿式氧化法 )、CWPO(催化过氧化氢湿式氧化法 )氧化降解含酸性红B染料模拟废水的过程 ,分别考察温度、压力、氧化剂量及催化剂对反应过程与对象污染物降解的影响规律 .结果表明 ,与常规湿式氧化法相比 ,WPO能在较低的温度和压力下降解结构稳定的有机物 ,在 2 2 0℃、8min、0 1MPa时 ,含1 5 0 0mg·L-1 酸性红B染料模拟废水的COD和色度的去除率分别达到 6 0 5 0 %和 96 80 % .同时发现 ,通过升温和增加过氧化氢的投加量不能够使废水COD和色度的去除率进一步提高 ,故引入Cu2 + 作催化剂来实现CWPO过程 ,在 2 2 0℃、8min、0 1MPa条件下 ,CWPO对同一废水的COD和色度的去除率分别达到 82 5 0 %和 99 71 % .通过计算得出CWPO与WPO相比基于COD的表观活化能降低了 6 5 93 % . Oxidation of Acid Red B in water by wet peroxide oxidation (WPO) and catalytic wet peroxide oxidation (CWPO) was explored in a continuous pressure reactor, using H_2O_2 as the oxidant. The effect of temperature, pressure, oxidant dose and catalyst on the oxidation process and the degradation efficiency was studied. The results indicated that Acid Red B can be degraded in WPO which have the stable structure at lower temperature and pressure compared with the traditional wet air oxidation, and 60.50% of COD removal and 96.80% of colour reduction were achieved at 220℃ for 8?min, at 0.1?MPa when the initial concentration of Acid Red B-containing water was 1500?mg·L^(-1). The COD and colour removal efficiency cannot be improved by increasing the temperature and raising the peroxide dosage, when Cu^(2+) was introduced into the CWPO process, 82.50% COD removal and 99.71% colour reduction were obtained at 220℃ and 0.1?MPa for 8?min. Through calculation, the activation energy of CWPO decrease by 65.93% compared with WPO.
出处 《环境科学学报》 CAS CSCD 北大核心 2004年第5期809-814,共6页 Acta Scientiae Circumstantiae
基金 国家自然科学基金项目 ( 2 98770 0 9 2 0 2 770 10 ) 教育部骨干教师基金项目
关键词 H2O2 酸性红B染料 染料废水 废水处理工艺 湿式氧化处理工艺 过氧化氢 COD 色度 hydrogen peroxide wet peroxide oxidation acid red B
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参考文献7

  • 1Chunmei Zhu,Liangyan Wang,Linren Kong,et al.Photocatalytic degradation of AZO dyes by supported TiO2 + UV in aqueous solution[J].Chemosphere,2000,41:303-309
  • 2Daneshvar N,Salari D,Khataee A R.Photocatalytic degradation of azo dye acid red 14 in water:investingation of the effect of operational parameters[ J].Journal of Photochemistry and Photobiology A:Chemistry,2003(157):111-116
  • 3Jiantuan Ge,Jiuhui Qu.Degradation of azo dye acid red B on manganese dioxide in the absence and presence of ultrasonic irradiation[J].Journal of Hazardous Materials B,2003,100:197-207
  • 4Mcclung S M,Lemley A T.Electrochemical treatment of acid dye wastewater[ A ].204th Meeting of the American Chemical Society[C].Washington D C,1992
  • 5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
  • 6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
  • 7吴超飞,王刚,杨波,吴海珍,任源,韦朝海.催化氧化法处理含甲醛毒性有机废水的工程试验[J].环境工程,2002,20(2):7-9. 被引量:30

二级参考文献12

  • 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.
  • 8许海梁,杨卫身,周集体,杨凤林.蒽醌染料的电解处理研究[J].环境保护科学,1998,24(4):14-16. 被引量:17
  • 9许海梁,杨卫身,周集体,杨凤林.偶氮染料废水的电解处理[J].化工环保,1999,19(1):32-36. 被引量:27
  • 10陈传好,谢波,任源,吴超飞,韦朝海.Fenton试剂处理废水中各影响因子的作用机制[J].环境科学,2000,21(3):93-96. 被引量:557

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