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Effect of Oxygen Supply on Bioleaching Sediments Contaminated by Heavy Metals

机译:氧气供应对重金属污染的生物浸涂沉积物的影响

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A bioremediation process for sediments contaminated by heavy metals (Me) has been developed and tested on a pilot scale. In the core stage, solid-bed bioleaching of sediment using elemental sulfur (S°) as leaching agent is performed. Controlled S° oxidation is an essential task for optimizing the bioleaching process. The effect of oxygen supply on acidification, S° oxidation and Me solubilization and sulfur related yield coefficients was studied in a suspension reactor and a lab-scale percolator system. Variation of oxygen supply was realized by controlling the gas flow and oxygen concentration in the aeration gas. Oxygen consumption rates during suspension leaching were not affected until the dissolved oxygen concentration was reduced below 0.05 mg/L. The growth of S° oxidizing autotrophic bacteria was stoichiometrically balanced resulting in Y_(O_2/S) of 1.21 g/g. The oxygen supply varied between 150 and 0.5 mol_(O_2)/mol_(S°) over 28 d of solid-bed leaching. Maximum Me solubilization was reached already at an oxygen supply of 7.5 mol_(O_2)/mol_(S°). Lowering to 0.5 mol_(O_2)/mol_(S°) resulted in retarding acidification and Me solubilization. Both the microbial S° oxidation and Me solubilization were correlated with the oxygen supply, revealing that control of the aeration regime offers a suitable means for optimizing solid-bed leaching performance.
机译:由重金属(Me)的污染沉积物生物修复过程已被开发并在中试规模进行测试。在核心阶段,使用元素硫(S°)作为浸出剂进行沉淀的固体床生物浸出。控制S 0氧化是用于优化生物浸出过程的一项重要任务。供氧对酸化的影响,S°氧化和Me增溶和硫产量相关系数在悬浮反应器和实验室规模的渗滤器系统进行了研究。氧气供应的变化通过控制曝气气体中的气体流量和氧浓度来实现。悬浮液的浸出过程中氧的消耗率并没有受到影响,直到溶解的氧浓度降低小于0.05毫克/升。 °S的生长氧化自养菌是化学计量平衡,导致1.21克/克Y_(O_2 / S)。氧气供给过固体床浸出的28 d 150和0.5 mol_(O_2)/ mol_(S°)之间变化。最大我溶解在氧气供给7.5 mol_(O_2)/ mol_(S°)已经达到。降低至0.5 mol_(O_2)/ mol_(S°)导致延迟酸化和Me溶解。既微生物S 0氧化和Me增溶用氧气供给相关,揭示了曝气政权报价的对照用于优化固体床浸出性能的适当手段。

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