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Effect of Oxygen Supply on Bioleaching Sediments Contaminated by Heavy Metals

机译:供氧对重金属污染的生物浸出沉积物的影响

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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-bedbioleaching of sediment using elemental sulfur (S°) as leaching agent is performed.Controlled S° oxidation is an essential task for optimizing the bioleaching process. Theeffect of oxygen supply on acidification, S° oxidation and Me solubilization and sulfurrelated yield coefficients was studied in a suspension reactor and a lab-scale percolatorsystem. Variation of oxygen supply was realized by controlling the gas flow and oxygenconcentration in the aeration gas. Oxygen consumption rates during suspension leachingwere not affected until the dissolved oxygen concentration was reduced below 0.05 mg/L.The growth of S° oxidizing autotrophic bacteria was stoichiometrically balancedresulting 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 anoxygen supply of 7.5 mol_(O_2)/mol_(S°). Lowering to 0.5 mol_(O_2)/mol_(S°)resulted in retardingacidification and Me solubilization. Both the microbial S° oxidation and Me solubilizationwere correlated with the oxygen supply, revealing that control of the aerationregime offers a suitable means for optimizing solid-bed leaching performance.
机译:对被重金属污染的沉积物的生物修复工艺 (Me)已在试验规模上进行了开发和测试。在核心阶段,固床 使用元素硫(S°)作为浸出剂对沉积物进行生物浸出。 控制S°氧化是优化生物浸出过程的重要任务。这 供氧对酸化,S°氧化,Me增溶和硫的影响 在悬浮反应器和实验室规模的渗滤器中研究了相关的产率系数 系统。通过控制气流和氧气实现氧气供应的变化 曝气中的浓度。悬浮浸出过程中的耗氧率 直到溶解氧浓度降低到0.05 mg / L以下才对碳氢化合物产生影响。 S°氧化自养细菌的生长在化学计量上达到平衡 得出Y_(O_2 / S)为1.21 g / g。氧气供应量在150至0.5 mol_(O_2)/ mol_(S°)之间变化 超过28 d的固体床浸出。达到最大Me溶解度已达到 氧气供应量为7.5 mol_(O_2)/ mol_(S°)。降低至0.5 mol_(O_2)/ mol_(S°) 导致减速 酸化和Me增溶。微生物S°氧化和Me增溶 与氧气供应相关,揭示了对通气的控制 这种方法为优化固相床浸出性能提供了一种合适的手段。

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