Plataforma Solar de Almería-CIEMAT, Carretera de Senés Km 4, 04200 (Tabernas, Almería), Spain.
J Hazard Mater. 2012 Apr 15;211-212:131-7. doi: 10.1016/j.jhazmat.2011.09.008. Epub 2011 Sep 12.
The optimal photocatalyst concentration for industrial wastewater treatment in current photoreactor designs is several hundreds of milligrams per liter. However, the elimination of emerging contaminants (ECs), which are present at extremely low concentrations in waste water treatment plants (WWTP) effluents might be accomplished at much lower catalyst (TiO(2)) concentrations. One of the main drawbacks of reducing catalyst loading below the optimum is the loss of useful photons which instead are transmitted through the TiO(2) suspension without being absorbed by the catalyst. Accordingly, in this work, laboratory and solar pilot-scale experiments were performed with real WWTP effluents to evaluate the kinetics of photocatalytic degradation of 52 emerging contaminants under realistic (ppb) concentrations. The analysis of the samples was accomplished by solid phase extraction (SPE) followed by liquid chromatography-mass spectrometry (LC-MS). In view of the results, low concentrations of TiO(2) of the order of tens of milligrams per liter were found to be insufficient for the degradation of the ECs in photoreactors with a short light-path length (29 cm). However, it was established that solar reactors of diameters of several hundreds of millimetres could be used for the efficient removal of ECs from WWTP effluents. The results presented show a general methodology for selecting the most efficient reactor diameter on the basis of the desired catalyst concentration.
在当前光反应器设计中,用于工业废水处理的最佳光催化剂浓度为每升数百毫克。然而,对于在废水处理厂(WWTP)废水中存在的新兴污染物(ECs)的消除,可能可以在更低的催化剂(TiO2)浓度下完成。将催化剂负载降低到最佳水平以下的一个主要缺点是有用光子的损失,这些光子反而会穿过 TiO2 悬浮液而不会被催化剂吸收。因此,在这项工作中,使用实际的 WWTP 废水在实验室和太阳能中试规模实验中进行了研究,以评估在实际(ppb)浓度下 52 种新兴污染物的光催化降解动力学。通过固相萃取(SPE)和液相色谱-质谱(LC-MS)对样品进行了分析。根据结果,发现光程长度较短(29 厘米)的光反应器中,数十毫克每升的低浓度 TiO2 不足以降解 ECs。然而,已经确定数百毫米直径的太阳能反应器可以用于从 WWTP 废水中有效去除 ECs。所呈现的结果展示了一种基于所需催化剂浓度选择最有效反应器直径的一般方法。