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电过硫酸盐氧化法处理橙 II 染料废水。

Electro-peroxone treatment of Orange II dye wastewater.

机构信息

State Key Joint Laboratory of Environmental Simulation and Pollution Control, School of Environment, Tsinghua University, Beijing 100084, China.

出版信息

Water Res. 2013 Oct 15;47(16):6234-43. doi: 10.1016/j.watres.2013.07.042. Epub 2013 Aug 6.

DOI:10.1016/j.watres.2013.07.042
PMID:23973257
Abstract

Degradation of a synthetic azo dye, Orange II, by electro-peroxone (E-peroxone) treatment was investigated. During the E-peroxone process, ozone generator effluent (O2 and O3 gas mixture) was continuously sparged into an electrolysis reactor, which was equipped with a carbon-polytetrafluorethylene (carbon-PTFE) cathode to electrochemically convert the sparged O2 to H2O2. The in-situ generated H2O2 then reacted with the sparged O3 to produce •OH, which can oxidize ozone-refractory organic pollutants effectively. Thus, by simply combining conventional ozonation and electrolysis processes, and using a cathode that can effectively convert O2 to H2O2, the E-peroxone process degraded Orange II much more effectively than the two processes individually. Complete decolorization and 95.7% total organic carbon (TOC) mineralization were obtained after 4 and 45 min of the E-peroxone treatment, respectively. In comparison, only 55.6 and 15.3% TOC were mineralized after 90 min of the individual ozonation and electrolysis treatments, respectively. In addition to its high efficiency, the E-peroxone process was effective over a wide range of pH (3-10) and did not produce any secondary pollutants. The E-peroxone process can thus provide an effective and environmentally-friendly alternative for wastewater treatment.

摘要

采用电过氧(E-peroxone)处理技术研究了合成偶氮染料橙 II 的降解。在 E-peroxone 过程中,臭氧发生器废气(O2 和 O3 气体混合物)连续鼓入电解反应器中,在该反应器中装有碳-聚四氟乙烯(碳-PTFE)阴极,以电化学方式将鼓入的 O2 转化为 H2O2。然后,原位生成的 H2O2 与鼓入的 O3 反应生成•OH,可有效氧化臭氧难降解的有机污染物。因此,通过简单地结合常规的臭氧氧化和电解过程,并使用能够有效将 O2 转化为 H2O2 的阴极,E-peroxone 工艺比两种单独的工艺降解橙 II 更为有效。分别经过 4 和 45 min 的 E-peroxone 处理后,橙 II 完全脱色,TOC 总有机碳(95.7%)矿化。相比之下,在单独的臭氧氧化和电解处理 90 min 后,TOC 分别仅矿化了 55.6%和 15.3%。除了高效外,E-peroxone 工艺在广泛的 pH 值(3-10)范围内有效,并且不产生任何二次污染物。因此,E-peroxone 工艺可为废水处理提供一种有效且环保的替代方法。

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