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Biofilm Dynamics and Kinetics during High-Rate Sulfate Reduction under Anaerobic Conditions

机译:厌氧条件下高速率硫酸盐还原过程中的生物膜动力学和动力学。

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摘要

The sulfate kinetics in an anaerobic, sulfate-reducing biofilm were investigated with an annular biofilm reactor. Biofilm growth, sulfide production, and kinetic constants (Km and Vmax) for the bacterial sulfate uptake within the biofilm were determined. These parameters were used to model the biofilm kinetics, and the experimental results were in good agreement with the model predictions. Typical zero-order volume rate constants for sulfate reduction in a biofilm without substrate limitation ranged from 56 to 93 μmol of SO24-cm−3 h−1 at 20°C. The temperature dependence (Q10) of sulfate reduction was equivalent to 3.4 at between 9 and 20°C. The measured rates of sulfate reduction could explain the relatively high sulfide levels found in sewers and wastewater treatment systems. Furthermore, it has been shown that sulfate reduction in biofilms just a few hundred micrometers thick is limited by sulfate diffusion into biofilm at concentrations below 0.5 mM. This observation might, in some cases, be an explanation for the relatively poor capacity of the sulfate-reducing bacteria to compete with the methanogenic bacteria in anaerobic wastewater treatment in submerged filters.
机译:用环形生物膜反应器研究了厌氧,减少硫酸盐的生物膜中的硫酸盐动力学。确定了生物膜中细菌被硫酸盐吸收的生物膜生长,硫化物生成和动力学常数(Km和Vmax)。这些参数用于模拟生物膜动力学,实验结果与模型预测吻合良好。在没有底物限制的情况下,生物膜中硫酸盐还原的典型零级体积速率常数范围为56至93μmolSO 2 4-cm -3 h -1 在20°C下。硫酸盐还原的温度依赖性(Q10)在9至20°C之间等于3.4。测得的硫酸盐还原速率可以解释下水道和废水处理系统中相对较高的硫化物含量。此外,已经表明,仅几百微米厚的生物膜中硫酸盐的还原受到硫酸盐在低于0.5mM的浓度下扩散进入生物膜的限制。在某些情况下,该观察结果可以解释在水下过滤器中厌氧废水处理中,硫酸盐还原菌与产甲烷菌竞争能力相对较弱。

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