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Sustained persulfate activation using solid iron: Kinetics and application to ciprofloxacin degradation

机译:固体铁持续过硫酸盐活化:动力学及其在环丙沙星降解中的应用

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Characterization of persulfate activation by solid iron was performed to determine kinetic parameters and control variables. The solid iron activated persulfate system was then used to demonstrate the degradation of the fluoroquinoline antibiotic ciprofloxacin. This study established the persulfate activation using solid iron takes place via a zero-order mechanism. Persulfate reaction rates were found to be linear fuhctions of iron rod surface area, with a maximum reaction rate constant of 8.4 x 10(-7) mol L-1 s(-1) established at the highest iron rod surface area tested. Persulfate reaction rates increased with the current applied to an iron rod up to a current density of 8.2 mA cm(-2) after which the rate plateaued. A maximum rate of 7.1 x 10(-2) mol L-1 s(-1) was established with applied current compared to 4.3 x 10(-2) mol L-1 s(-1) without current, when the same surface area of the iron rod was in solution. At a starting concentration of 0.121 mmol L-1, ciprofloxacin removal of 95% was achieved in 15 min. A ciprofloxacin transformation product matrix containing core quinolone structures was formed and then degraded by 90%, with total organic carbon removal of 44%. The corresponding defluorination was >95%, suggesting that solid iron activated persulfate may offer an advantage for destruction of some fluorinated compounds. Hydroxyl radicals were identified as the dominant radicals in the degradation process. Ciprofloxacin removal was independent of the applied current despite the increased persulfate activation under the same conditions. (C) 2016 Elsevier B.V. All rights reserved.
机译:进行了固体铁对过硫酸盐活化的表征,以确定动力学参数和控制变量。然后使用固体铁活化的过硫酸盐体系来证明氟喹啉抗生素环丙沙星的降解。这项研究确定了使用固态铁的过硫酸盐活化是通过零级机制进行的。发现过硫酸盐的反应速率是铁棒表面积的线性函数,在测试的最高铁棒表面积下,最大反应速率常数为8.4 x 10(-7)mol L-1 s(-1)。过硫酸盐的反应速率随施加到铁棒上的电流而增加,直至电流密度达到8.2 mA cm(-2),此后速率趋于平稳。在相同的表面上,施加电流时的最大比率为7.1 x 10(-2)mol L-1 s(-1),相比之下,不施加电流时的最大比率为4.3 x 10(-2)mol L-1 s(-1)铁棒区域已溶解。在起始浓度为0.121 mmol L-1的条件下,在15分钟内可去除95%的环丙沙星。形成了包含核心喹诺酮结构的环丙沙星转化产物基质,然后降解90%,总有机碳去除率为44%。相应的脱氟率> 95%,这表明固体铁活化的过硫酸盐可能为破坏某些氟化物提供优势。羟基自由基被认为是降解过程中的主要自由基。尽管在相同条件下过硫酸盐活化增加,环丙沙星的去除与施加电流无关。 (C)2016 Elsevier B.V.保留所有权利。

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