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电化学(中英文) ›› 2006, Vol. 12 ›› Issue (4): 412-415. 

• 研究论文 • 上一篇    下一篇

三相流化床电极反应器深度处理制浆废水

吴丹;史启才;周集体;贾保军;   

  1. 大连理工大学化工学院,大连理工大学化工学院,大连理工大学环境与生命学院,大连理工大学环境与生命学院 辽宁大连116012,辽宁大连116012,辽宁大连116023,辽宁大连116023
  • 收稿日期:2006-11-28 修回日期:2006-11-28 出版日期:2006-11-28 发布日期:2006-11-28

Deep Treatment of Pulping Wastewater Using Three Phase Fluidized Bed Electrode Reactor

WU Dan~   

  1. (1*),SHI Qi-cai~(1),ZHOU Ji-ti~(2),JIA Bao-jun~(2)(1.College of Chemical Engineering,Dalian University of Technology,Dalian 116012,Liaoning,China,2.School of Environmental and Biological Science and Technology,Dalian University of Technology,Dalian 116023,Liaoning,China
  • Received:2006-11-28 Revised:2006-11-28 Published:2006-11-28 Online:2006-11-28

摘要: 应用三相流化床电极反应器(新型电化学反应器)处理制浆废水.研究了曝气量、槽电压、溶液pH值及FeSO4浓度等因素对电解效果的影响.结果表明,该反应器深度处理制浆废水的最佳工艺条件为:槽电压20 V,曝气量为0.3 m3.h-1,FeSO4浓度为1000 mg.L-1,pH值≈2.5,反应时间为90 m in时COD去除率为70.1%.

关键词: 三相流化床电极, 活性炭, 制浆废水

Abstract: Treatment of pulping wastewater by using a novel electrochemical reactor,i.e.the three phase fluidized bed electrode,reactor were invesigated.The effects of air flow rate,applied voltage,pH value and FeSO_(4) concentration on electrolysis efficiency were investigated.It was clearly shown that the 20 V of voltage,0.3 m~(3) h~(-1) of air flow rate,1000 mg L~(-1) of FeSO_(4) concentration and pH≈2.5 were its best conditions.COD removal could be 70.1% under these conditions.

Key words: Three phase fluidized bed electrode, Activated carbon, Pulping wastewater

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