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首页> 外文期刊>Separation and Purification Technology >Reduction of chromium(VI) by pyrite in dilute aqueous solutions
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Reduction of chromium(VI) by pyrite in dilute aqueous solutions

机译:黄铁矿在稀水溶液中还原六价铬

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摘要

Hexavalent chromium is a known toxic and mobile contaminant in the environment. Reduction of Cr(VI) using Fe(II) compounds is one of the most common practices in dealing with Cr(VI) as a contaminant. Among the various Fe(II) salts suggested for Cr(VI) treatment, pyrite, also a potential waste as well as a natural mineral, has been suggested. This study investigated the abiotic reduction of Cr(VI) by pyrite under dark and anaerobic conditions. The effect of pertinent chemical properties such as the initial Cr(VI) concentration, the amount of pyrite, temperature, and pH on the pyrite reduction of Cr(VI) was studied. The results showed that the rate of Cr(VI) reduction were strongly dependent on pH. A maximum rate at pH 3 was observed; at pH>3.0, the initial rate of Cr(VI) reduction decreased as the pH increased and at pH < 3.0, the rates increased as pH increased. The rates of pyrite oxidation by Cr(VI) from pH 2.0 to 11.0 were found to be zero-order with respect to the concentration of initial Cr(VI) and second order with respect to the ratio of pyrite surface area to solution volume. The activation energy of the Cr( VI) reduction in the temperature range of 10-50 °C was 73 kJ/mol. The relatively high activation energy indicated that surface reaction controlled the reduction rate over this temperature range. Based on the results, it is seen that Cr(VI) reduction reaction took place in two distinct stages each involved with multiple steps. The first stage involved the dissolution of pyrite under acidic conditions that released Fe(II) and S_2~(2-) ions which were then readily oxidized by Cr(VI) with the production of Cr(III), Fe(III), and SO_4~(2-) species. In the presence of Cr(VI), direct oxidation of pyrite took place at rate slower than the above redox reactions. Immediately upon the depletion of Cr(VI), reaction between Fe(III) and excessive pyrite resulted in the generation of Fe(II) species, however.
机译:六价铬是环境中已知的有毒和易移动的污染物。使用Fe(II)化合物还原Cr(VI)是处理Cr(VI)作为污染物的最常见实践之一。在建议用于Cr(VI)处理的各种Fe(II)盐中,已提出了黄铁矿,它也是一种潜在的废物,也是一种天然矿物。这项研究调查了在黑暗和厌氧条件下黄铁矿对Cr(VI)的非生物还原。研究了相关化学性质(例如初始Cr(VI)浓度,黄铁矿的量,温度和pH值)对Cr(VI)的黄铁矿还原的影响。结果表明,Cr(VI)的还原速率强烈依赖于pH值。在pH 3时观察到最大速率;在pH> 3.0时,Cr(VI)的初始还原速率随pH的升高而降低,而在pH <3.0时,Cr(VI)的还原速率随pH的升高而升高。发现从pH 2.0到11.0的Cr(VI)腐蚀黄铁矿的速率相对于初始Cr(VI)的浓度为零级,而相对于黄铁矿表面积与溶液体积的比率,则为二阶。 Cr(VI)还原在10-50°C的温度范围内的活化能为73 kJ / mol。较高的活化能表明表面反应控制了该温度范围内的还原速率。根据结果​​,可以看出Cr(VI)还原反应发生在两个不同的阶段,每个阶段都涉及多个步骤。第一阶段涉及在酸性条件下溶解黄铁矿,释放出Fe(II)和S_2〜(2-)离子,然后这些离子容易被Cr(VI)氧化,生成Cr(III),Fe(III)和SO_4〜(2-)种类在Cr(VI)的存在下,黄铁矿的直接氧化以比上述氧化还原反应慢的速率发生。 Cr(VI)耗尽后,Fe(III)与过量黄铁矿之间的反应立即导致生成Fe(II)物种。

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