Seccion Departamental Ingenieria Quimica, Universidad Autonoma de Madrid, Ctra. Colmenar km 15, 28049 Madrid, Spain.
Seccion Departamental Ingenieria Quimica, Universidad Autonoma de Madrid, Ctra. Colmenar km 15, 28049 Madrid, Spain.
J Hazard Mater. 2017 Jun 5;331:45-54. doi: 10.1016/j.jhazmat.2017.02.017. Epub 2017 Feb 14.
CWPO has proved to be effective for the treatment of representative pharmaceuticals (sulfamethoxazole, atenolol, metronidazole, diltiazem, trimethoprim and ranitidine) in different water matrices (ultrapure water, surface water, WWTP effluent and hospital wastewater). Complete removal of the pollutants and the aromatic intermediates was achieved using the stoichiometric dose of HO, a catalyst (FeO/γ-AlO) load of 2gL, pH 3 and temperature of 50-75°C. Accordingly, the ecotoxicity was reduced to negligible values. The degradation was faster when the pharmaceuticals were together, being the reaction time for the elimination of the most refractory species (metronidazole) shortened from 4h to 1h. The mineralization of the drugs was fairly different, being the most reactive species those containing several aromatic rings (X∼80%) and the most refractory that bearing an imidazolium ring (X∼35%). The water matrix affected the kinetics of the process but in all cases complete conversion of the drugs was reached within 1h. The presence of dissolved organic matter (surface water) seemed to promote drugs degradation while the occurrence of inorganic ions (real WTTP and hospital effluents) partially inhibited it due to scavenging effects. Remarkably, the process was successfully operated at the typical concentrations of main micropollutant sources (μgL).
过一硫酸盐(CWO)已被证实可有效处理多种不同水基质(超纯水、地表水、污水处理厂出水和医院废水)中的代表性药物(磺胺甲噁唑、阿替洛尔、甲硝唑、地尔硫卓、甲氧苄啶和雷尼替丁)。在 HO 的化学计量剂量(一种催化剂(FeO/γ-Al2O3)的负载量为 2 g/L、pH 值为 3、温度为 50-75°C)作用下,可完全去除污染物和芳香族中间体,从而降低毒性。当药物共存时,降解速度更快,最难去除的物质(甲硝唑)的反应时间从 4 小时缩短至 1 小时。药物的矿化程度差异较大,含多个芳环的物质(X∼80%)反应性最强,含咪唑环的物质(X∼35%)最难去除。水基质会影响反应动力学,但在所有情况下,药物在 1 小时内均可完全转化。溶解有机物(地表水)的存在似乎促进了药物降解,而无机离子(实际污水处理厂和医院废水)的存在则由于清除作用而部分抑制了降解。值得注意的是,该工艺可在主要微量污染物源(μgL)的典型浓度下成功运行。