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紫外光/二氧化钛及紫外光/二氧化钛/化学氧化剂工艺用于去除二氧化钛水悬浮液中的腐殖酸、铬和铜。

UV/TiO2 and UV/TiO2/chemical oxidant processes for the removal of humic acid, Cr and Cu in aqueous TiO2 suspensions.

作者信息

Jung J-T, Choi J-Y, Chung J, Lee Y-W, Kim J-O

机构信息

Department of Civil Engineering, Kangnung National University, Gangneung-daehangno 120, Gangneung, Gangwon-do, 210-702, Korea.

出版信息

Environ Technol. 2009 Mar;30(3):225-32. doi: 10.1080/09593330802503750.

Abstract

The objective of this study was to investigate the treatment efficiency of UV/TiO2 and UV/TiO2/chemical oxidant processes for the removal of humic acid and hazardous heavy metals in aqueous TiO2 suspensions. The reaction rate (k) of humic acid and hazardous heavy metals by UV/TiO2 was higher than that of UV illumination alone or TiO2 alone. The removal efficiency for humic acid and Cr(VI) at acid or neutral pH values was higher than that at basic pH values. However, the removal efficiency for Cu(II) at acid pH values was smaller compared with that at neutral or basic pH values. The reaction rate (k) of humic acid and hazardous heavy metals in the TiO2 concentration range of 0.1-0.3 g l(-1) increased with increasing TiO2 dosage. However, amounts higher than a TiO2 dosage of 0.3 g l(-1) reduced the removal efficiency for humic acid and hazardous heavy metals because of the shielding effect on the UV light penetration in the aqueous solution caused by the presence of excessive amounts of TiO2. The addition of oxidants to the UV/TiO2 system showed an increase in degradation efficiency for the treatment of humic acid and hazardous heavy metals. The optimal concentration of oxidants was: H2O2 50 mg l(-1), O3 20 g m(-3) and K2S2O8 50 mg l(-1), respectively. The degradation efficiency of UV/TiO2/oxidant systems for the removal of humic acid and hazardous heavy metals was much greater when H2O2 was used as the oxidant.

摘要

本研究的目的是调查紫外光/二氧化钛(UV/TiO₂)以及紫外光/二氧化钛/化学氧化剂工艺在去除TiO₂水悬浮液中腐殖酸和有害重金属方面的处理效率。UV/TiO₂对腐殖酸和有害重金属的反应速率(k)高于单独的紫外光照或单独的TiO₂。在酸性或中性pH值下,腐殖酸和Cr(VI)的去除效率高于碱性pH值下的。然而,酸性pH值下Cu(II)的去除效率低于中性或碱性pH值下的。在TiO₂浓度范围为0.1 - 0.3 g l⁻¹时,腐殖酸和有害重金属的反应速率(k)随TiO₂用量增加而增大。然而,TiO₂用量高于0.3 g l⁻¹时,由于过量TiO₂对水溶液中紫外光穿透产生屏蔽效应,腐殖酸和有害重金属的去除效率降低。向UV/TiO₂体系中添加氧化剂可提高腐殖酸和有害重金属的降解效率。氧化剂的最佳浓度分别为:H₂O₂ 50 mg l⁻¹、O₃ 20 g m⁻³和K₂S₂O₈ 50 mg l⁻¹。当使用H₂O₂作为氧化剂时,UV/TiO₂/氧化剂体系去除腐殖酸和有害重金属的降解效率更高。

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