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活性污泥膜生物反应器中的铁形态和铁形态转化。

Iron speciation and iron species transformation in activated sludge membrane bioreactors.

机构信息

School of Civil and Environmental Engineering, The University of New South Wales, Sydney, NSW 2052, Australia.

出版信息

Water Res. 2010 Jun;44(11):3511-21. doi: 10.1016/j.watres.2010.03.031. Epub 2010 Mar 31.

DOI:10.1016/j.watres.2010.03.031
PMID:20399481
Abstract

Iron speciation and iron species transformation were investigated in three membrane bioreactors (MBRs) differing in feed iron concentration (and oxidation state) and the presence or absence of an anoxic chamber to simulate various feed stream conditions and operational configurations. The concentration of dissolved Fe(II) was below detection limit (i.e., <0.1microM) in all chambers while the concentration of dissolved Fe(III) was found to be around 0.25microM. H(2)O(2) was detected as a quasi-stable reactive oxygen species with concentrations in the muM range in all MBR chambers. H(2)O(2) acted as the primary potential oxidant of Fe(II) in the anoxic chamber. Batch experiments showed that the rate constant for oxygenation of dissolved Fe(II) in the liquid phase of the activated sludge compartment was as high as 78M(-1)s(-1). The half-life time of dissolved Fe(II) in all chambers was found to be no longer than 1min. The stability constants of the Fe(III)SMP complexes were far from uniform. A large quantity of Fe(II) (over 0.036% of the sludge dry mass) was found to be adsorbed by the bacterial flocs suggesting the active reduction of adsorbed Fe(III). The content of adsorbed Fe(II) was found to increase if the MBR was supplied with iron in the Fe(II) form. Over 60% of iron fed to the reactors was converted to highly insoluble ferric oxyhydroxide in all MBRs. A model has been developed which satisfactorily describes the oxidation of Fe(II) in the activated sludge liquid phase and which provides valuable insight into the relative importance of redox processes occurring which mediate the speciation of iron in the system.

摘要

研究了三种膜生物反应器(MBR)中铁的形态和铁形态的转化,这三种 MBR 在进料铁浓度(和氧化态)以及缺氧室的存在与否方面存在差异,以模拟各种进料流条件和操作配置。所有腔室中溶解的 Fe(II)浓度均低于检测限(即 <0.1μM),而溶解的 Fe(III)浓度约为 0.25μM。在所有 MBR 腔室中均检测到 H(2)O(2)作为准稳定的活性氧物质,浓度在μM 范围内。H(2)O(2)在缺氧室中充当 Fe(II)的主要潜在氧化剂。批处理实验表明,溶解在活性污泥区液相中的 Fe(II)被氧化的速率常数高达 78M(-1)s(-1)。所有腔室中溶解的 Fe(II)的半衰期均发现不超过 1 分钟。Fe(III)SMP 配合物的稳定常数远非均匀。大量的 Fe(II)(超过污泥干质量的 0.036%)被发现被细菌絮体吸附,这表明吸附的 Fe(III)被主动还原。如果 MBR 以 Fe(II)形式供应铁,则发现吸附的 Fe(II)含量增加。在所有 MBR 中,超过 60%的铁被转化为高度不溶性的铁氧氢氧化物。已经开发了一种模型,该模型可以很好地描述活性污泥液相中 Fe(II)的氧化,并为发生的氧化还原过程的相对重要性提供了有价值的见解,这些过程介导了系统中铁的形态。

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