Dipartimento di Scienze Chimiche, Università di Padova, Italy.
Chemosphere. 2010 Jan;78(5):620-5. doi: 10.1016/j.chemosphere.2009.10.046. Epub 2009 Nov 13.
This paper reports investigations on electrochemical removal of Cr(III) from a real wastewater sample from a 4x10(4)m(3)d(-1) purification plant located in the leather district of Arzignano (Italy). A crucial point evaluated is the relation between Cr(III) abatement and the reduction of total organic carbon and chemical oxygen demand. Here we present the results of different abatement approaches including advanced oxidation processes (AOPs) and electrocoagulation applied separately or in series. Neither of these methods show satisfactory results when applied alone. In particular, AOPs are completely inefficient owing to the formation of Cr(VI), which is more soluble than Cr(III). Almost total depletion (99.7%) of the recalcitrant fraction of Cr(III) is successfully achieved by combining ozonization and electrocoagulation processes. The results are consistent with the abatement of Cr in its hexavalent form by fast precipitation as NH(4)Fe(CrO(4))(2).
本文报道了从位于意大利阿尔齐尼亚诺(Arzignano)皮革区的一座 4x10(4)m(3)d(-1) 净化厂的实际废水样品中电化学去除 Cr(III)的研究。评估的一个关键点是 Cr(III)去除与总有机碳和化学需氧量减少之间的关系。本文介绍了不同去除方法的结果,包括单独或串联应用的高级氧化工艺(AOPs)和电絮凝。当单独应用时,这些方法都没有令人满意的结果。特别是,由于 Cr(VI)的形成,AOPs 完全无效,因为 Cr(VI)比 Cr(III)更易溶解。通过将臭氧化和电絮凝过程相结合,可以成功地将难处理的 Cr(III)的顽固部分几乎完全耗尽(99.7%)。结果与通过快速沉淀为 NH(4)Fe(CrO(4))(2)以六价形式去除 Cr 的效果一致。