Centro de Investigación y Desarrollo Tecnológico en Electroquímica (CIDETEQ), Parque Tecnológico Sanfandila, Pedro Escobedo, Querétaro, 76703, Mexico.
Centro de Investigación y Desarrollo Tecnológico en Electroquímica (CIDETEQ), Parque Tecnológico Sanfandila, Pedro Escobedo, Querétaro, 76703, Mexico.
Chemosphere. 2019 Jun;224:698-706. doi: 10.1016/j.chemosphere.2019.02.101. Epub 2019 Feb 23.
Iron-supported catalyst on granular activated carbon was prepared for its use in heterogeneous Fenton reaction coupled to an in situ HO electro-generation. For this process, an electrolysis cell was employed, using carbon felt as cathode and graphite as anode. A solution of HO (electrogenerated at a rate of 30 mg L h) was obtained using a current intensity of 12 mA. In order to promote the decomposition of HO to OH, a Carbon-Fe catalyst was used. This catalyst was prepared by incipient wet impregnation using FeSO as precursor salt to obtain samples with 9% wt of iron. Samples were characterized by EDX, FTIR and XPS spectroscopy before and after wastewater treatment using phenol as model molecule. Two iron oxidation states on the samples were found, Fe and Fe. The ratio between Fe/Fe was 1.29 which was later reduced to 0.92 after Fenton process; this might be associated with the metal oxidation (Fe to Fe) occurring during Fenton-reaction, thus indicating that HO decomposition was carried out by Fe on carbon surface. Detection and quantification of hydroxyl radical were carried out by fluorescence spectroscopy, obtaining a radical concentration of 3.5 μM in solution. Iron in solution were determined, showing a concentration of 0.1 mg L, making evident that the supported metal is stable and the reaction is carried out in a heterogeneous phase. Results showed an environmentally friendly process that can generate reagents in situ, with high efficiencies in the degradation of pollutants and minimizing the formation of toxic byproducts, which are common in conventional treatments.
铁负载于颗粒状活性炭上的催化剂,用于非均相 Fenton 反应与原位 HO 的电化学生成相结合。为此,采用了一个电解池,以碳纤维毡为阴极,石墨为阳极。通过电流强度为 12mA,以 30mg/L/h 的速率产生 HO。为了促进 HO 分解为 OH,使用了碳-铁催化剂。该催化剂采用 FeSO 作为前驱体盐的初始湿浸渍法制备,以获得铁含量为 9wt%的样品。在使用苯酚作为模型分子进行废水处理前后,对样品进行了 EDX、FTIR 和 XPS 光谱分析。在样品上发现了两种铁的氧化态,Fe 和 Fe。Fe/Fe 的比值为 1.29,在 Fenton 过程后降低到 0.92;这可能与 Fenton 反应过程中金属氧化(Fe 到 Fe)有关,表明 HO 的分解是由碳表面上的 Fe 进行的。通过荧光光谱法检测和定量羟基自由基,溶液中自由基的浓度为 3.5μM。溶液中的铁也被测定,浓度为 0.1mg/L,这表明负载的金属是稳定的,反应是在非均相进行的。结果表明,该工艺环保,可原位生成试剂,对污染物的降解效率高,同时最大限度地减少了传统处理中常见的有毒副产物的形成。
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