Dpto. Ingeniería Química y QI. ETSIIyT, Universidad de Cantabria, Av. de los Castros s/n, 39005 Santander, Spain.
Water Res. 2012 May 15;46(8):2579-90. doi: 10.1016/j.watres.2012.02.015. Epub 2012 Feb 19.
This work investigates the formation of oxidation by-products during the electrochemical removal of ammonium using BDD electrodes from wastewaters containing chlorides. The influence of the initial chloride concentration has been experimentally analyzed first, working with model solutions with variable ammonium concentration and second, with municipal landfill leachates. Two different levels of chloride concentration were studied, i) low chloride concentrations ranging between 0 and 2000 mg/L and, ii) high chloride concentrations ranging between 5000 and 20,000 mg/L. Ammonium removal took place mainly via indirect oxidation leading to the formation of nitrogen gas and nitrate as the main oxidation products; at high chloride concentration the formation of nitrogen gas and the rate of ammonium removal were both favored. However, chloride was also oxidized during the electrochemical treatment leading to the formation of free chlorine responsible of the ammonium oxidation, together with undesirable products such as chloramines, chlorate and perchlorate. Chloramines appeared during the treatment but they reached a maximum and then started decreasing, being totally removed when high chloride concentrations were used. With regard to the formation of chlorate and perchlorate once again the concentration of chloride exerted a strong influence on the formation kinetics of the oxidation by-products and whereas at low chloride concentrations, chlorate appeared like an intermediate compound leading to the formation of perchlorate, at high chloride concentrations chlorate formation was delayed significantly and perchlorate was not detected during the experimental time. Thus this work contributes first to the knowledge of the potential hazards of applying the electro-oxidation technology as an environmental technology to deal with ammonium oxidation under the presence of chloride and second it reports efficient conditions that minimize or even avoid the formation of undesirable by-products.
本工作研究了在含有氯化物的废水中使用 BDD 电极电化学去除铵时氧化副产物的形成。首先通过实验分析了初始氯化物浓度的影响,在具有可变铵浓度的模型溶液中进行了工作,其次在城市垃圾渗滤液中进行了工作。研究了两种不同的氯化物浓度水平,i)低氯化物浓度范围为 0 至 2000mg/L,和 ii)高氯化物浓度范围为 5000 至 20000mg/L。铵的去除主要通过间接氧化进行,导致氮气和硝酸盐的形成作为主要的氧化产物;在高氯化物浓度下,氮气的形成和铵的去除速率都得到了促进。然而,氯化物也在电化学处理过程中被氧化,形成负责铵氧化的游离氯,以及氯胺、氯酸盐和高氯酸盐等不良产物。氯胺在处理过程中出现,但达到最大值后开始减少,当使用高氯化物浓度时完全去除。至于氯酸盐和高氯酸盐的形成,氯化物浓度再次对氧化副产物的形成动力学产生强烈影响,而在低氯化物浓度下,氯酸盐作为中间化合物出现,导致高氯酸盐的形成,在高氯化物浓度下,氯酸盐的形成明显延迟,在实验期间未检测到高氯酸盐。因此,本工作首先有助于了解在存在氯化物的情况下将电氧化技术作为环境技术应用于铵氧化的潜在危害,其次报告了有效条件,可以最小化甚至避免不良副产物的形成。