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Regeneration of activated carbon by fenton and photofenton oxidation for the treatment of phenol wastewater

机译:芬顿和光芬顿氧化再生活性炭处理苯酚废水

摘要

Advanced Oxidation Processes have emerged as promising technologies for the recovery of carbons saturated with aromatic molecules, owing to their potency to degrade a wide range of organic pollutants by the generation of very reactive and non selective free hydroxyl radicals. The purpose of this work is to study the adsorption of phenol on activated carbons (ACs) and the consecutive in-situ regeneration of carbon by Fenton oxidation. Two different processes have been carried out: - the first one is based on a complete batch system in order to investigate the influence of Fe2+ and H2O2 concentrations; - the second one consists in a continuous fixed bed adsorption, followed by a batch circulation of the Fenton’s reagent through the saturated AC bed, to examine the efficiency of the real process. Two different activated carbons have been also studied: a both micro- and mesoporous AC (L27) and an only microporous one (S23). In the batch reactor containing a 1 g/L phenol solution, the optimal conditions found for pollutant mineralization in the homogeneous Fenton system (Fe2+ = 10 mmol/L, [H2O2] = 1000 mmol/L, corresponding to 6.5 times the stoechiometric amount for complete mineralization) are not the best for AC regeneration: a continuous reduction of adsorption capacity of L27 from 100% to 23% is observed after 3 oxidations, due to the decrease of both AC weight and surface area. Higher concentration of Fe2+ (20 mmol/L) and lower concentration of H2O2 (2 times the stoechiometry) lead to a 50% recovery of the initial adsorption capacity during at least 4 consecutive cycles for L27, while about 20% or less for S23. In the consecutive continuous adsorption/batch oxidation process, the regeneration efficiency reaches 30% to 40% for L27 after two cycles whatever the feed concentration (0.1 g/L or 1 g/L of phenol) and less than 10% for S23 (0.1 g/L of phenol). During oxidation step, Total Organic Carbon removal is found to reach a limit, probably due to the formation of Fe3+/organic acid complex, hindering Fe2+ regeneration. Such complexes are stable in usual Fenton conditions, but can be destroyed by UV radiation. A photo-Fenton test performed on L27 indeed shows almost complete mineralization and improved recovery of AC adsorption capacity although not complete (56% after two cycles).
机译:先进的氧化工艺已成为一种有前景的技术,可用于回收被芳香族分子饱和的碳,这是由于先进的氧化工艺可通过产生非常活泼且非选择性的游离羟基来降解多种有机污染物。这项工作的目的是研究苯酚在活性炭(ACs)上的吸附以及Fenton氧化法对碳的连续原位再生。已经进行了两个不同的过程:-第一个过程基于完整的批处理系统,以研究Fe2 +和H2O2浓度的影响; -第二个步骤是连续的固定床吸附,然后分批循环Fenton的试剂通过饱和的AC床,以检查实际工艺的效率。还研究了两种不同的活性炭:微孔和中孔AC(L27)和唯一的微孔AC(S23)。在含有1 g / L苯酚溶液的间歇式反应器中,在均质Fenton系统中发现污染物矿化的最佳条件(Fe2 + = 10 mmol / L,[H2O2] = 1000 mmol / L,相当于化学计量的6.5倍)。完全矿化)不是最适合AC再生的方法:3次氧化后,由于AC重量和表面积的减少,L27的吸附容量从100%连续降低到23%。 Fe27 +的较高浓度(20 mmol / L)和H2O2的较低浓度(化学计量的2倍)导致L27在至少四个连续的循环中恢复了初始吸附容量的50%,而S23则约为20%或更少。在连续的连续吸附/分批氧化过程中,无论进料浓度(0.1 g / L或1 g / L的苯酚)如何,两个循环后L27的再生效率均达到30%至40%,而S23的再生效率低于10%(0.1克/升的苯酚)。在氧化步骤中,发现总有机碳去除达到极限,这可能是由于形成了Fe3 + /有机酸络合物,从而阻碍了Fe2 +的再生。这样的络合物在通常的芬顿条件下是稳定的,但是可以被紫外线辐射破坏。在L27上进行的光芬顿测试确实显示出几乎完全的矿化作用,并且改善了AC吸附能力的恢复,尽管还不完全(两次循环后为56%)。

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