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Degradation of 1,4-dioxane in water with heat- and Fe -activated persulfate oxidation

机译:热活化和铁活化的过硫酸盐氧化降解水中的1,4-二恶烷

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摘要

This research investigated the 1,4-dioxane (1,4-D) degradation efficiency and rate during persulfate oxidation at different temperatures, with and without Fe~(2+) addition, also considering the effect of pH and persulfate concentration on the oxidation of 1,4-D. Degradation pathways for 1,4-D have also been proposed based on the decomposition intermediates and by-products. The results indicate that 1,4-D was completely degraded with heat-activated persulfate oxidation within 3-80 h. The kinetics of the 1,4-D degradation process fitted well to a pseudo-first-order reaction model. Temperature was identified as the most important factor influencing the 1,4-D degradation rate during the oxidation process. As the temperature increased from 40 to 60 °C, the degradation rate improved significantly. At 40 °C, the addition of Fe~(2+) also increased the 1,4-D degradation rate. Interestingly, at 50 and 60 °C, the 1,4-D degradation rate decreased slightly with the addition of Fe~(2+). This reduced degradation rate may be attributed to the rapid conversion of Fe~(2+) to Fe~(3+) and the production of an Fe(OH)_3 precipitate which limited the ultimate oxidizing capability of persulfate with Fe~(2+) under higher temperatures. Higher persulfate concentrations led to higher 1,4-D degradation rates, but pH adjustment had no significant effect on the 1,4-D degradation rate. The identification of intermediates and by-products in the aqueous and gas phases showed that acetaldehyde, acetic acid, glycolaldehyde, glycolic acid, carbon dioxide, and hydrogen ion were generated during the persulfate oxidation process. A carbon balance analysis showed that 96 and 93 % of the carbon from the 1,4-D degradation were recovered as by-products with and without Fe~(2+) addition, respectively. Overall, persulfate oxidation of 1,4-D is promising as an economical and highly efficient technology for treatment of 1,4-D-contaminated water.
机译:本研究研究了在添加和不添加Fe〜(2+)的情况下,在不同温度下过硫酸盐氧化过程中1,4-二恶烷(1,4-D)的降解效率和速率,同时考虑了pH和过硫酸盐浓度对氧化的影响1,4-D。还基于分解中间体和副产物提出了1,4-D的降解途径。结果表明1,4-D在3-80小时内被热活化的过硫酸盐氧化完全降解。 1,4-D降解过程的动力学非常适合拟一级反应模型。温度被认为是影响氧化过程中1,4-D降解速率的最重要因素。随着温度从40°C升高到60°C,降解率显着提高。在40°C时,Fe〜(2+)的添加也提高了1,4-D的降解率。有趣的是,在50和60°C下,添加Fe〜(2+)后1,4-D降解速率略有下降。降低的降解速率可能归因于Fe〜(2+)向Fe〜(3+)的快速转化以及Fe(OH)_3沉淀的产生,从而限制了过硫酸盐与Fe〜(2+)的最终氧化能力。 )在更高的温度下。较高的过硫酸盐浓度导致较高的1,4-D降解速率,但调节pH值对1,4-D降解速率无明显影响。在水相和气相中的中间体和副产物的鉴定表明,在过硫酸盐氧化过程中产生了乙醛,乙酸,乙醇醛,乙醇酸,二氧化碳和氢离子。碳平衡分析表明,分别添加和不添加Fe〜(2+)的副产物分别回收了1,4-D降解的碳96%和93%。总体而言,过硫酸盐氧化1,4-D是一种经济高效的处理1,4-D污染水的技术。

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