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Evaluating Enhanced Sulfate Reduction and Optimized Volatile Fatty Acids (VFA) Composition in Anaerobic Reactor by Fe (Ⅲ) Addition

机译:添加Fe(Ⅲ)评估厌氧反应器中硫酸盐还原反应的增强和最佳挥发性脂肪酸(VFA)的组成

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Anaerobic reactors with ferric iron addition have been experimentally demonstrated to be able to simultaneously improve sulfate reduction and organic matter degradation during sulfate-containing wastewater treatment. In this work, a mathematical model is developed to evaluate the impact of ferric iron addition on sulfate reduction and organic carbon removal as well as the volatile fatty acids (VFA) composition in anaerobic reactor. The model is successfully calibrated and validated using independent long-term experimental data sets from the anaerobic reactor with Fe (Ⅲ) addition under different operational conditions. The model satisfactorily describes the sulfate reduction, organic carbon removal and VFA production. Results show Fe (Ⅲ) addition induces the microbial reduction of Fe (Ⅲ) by iron reducing bacteria (IRB), which significantly enhances sulfate reduction by sulfate reducing bacteria (SRB) and subsequently changes the VFA composition to acetate-dominating effluent. Simultaneously, the produced Fe (Ⅱ) from IRB can alleviate the inhibition of undissociated H_2S on microorganisms through iron sulfide precipitation, resulting in further improvement of the performance. In addition, the enhancement on reactor performance by Fe (Ⅲ) is found to be more significantly favored at relatively low organic carbon/SO_4~(2-) ratio (e.g., 1.0) than at high organic carbon/SO_4~(2-) ratio (e.g., 4.5). The Fe (Ⅲ)-based process of this work can be easily integrated with a commonly used strategy for phosphorus recovery, with the produced sulfide being recovered and then deposited into conventional chemical phosphorus removal sludge (FePO_4) to achieve FeS precipitation for phosphorus recovery while the required Fe (Ⅲ) being acquired from the waste ferric sludge of drinking water treatment process, to enable maximum resource recovery/reuse while achieving high-rate sulfate removal.
机译:实验证明,添加三价铁的厌氧反应器能够同时改善含硫酸盐废水处理过程中硫酸盐的还原和有机物的降解。在这项工作中,建立了一个数学模型来评估三价铁添加对厌氧反应器中硫酸盐还原和有机碳去除以及挥发性脂肪酸(VFA)组成的影响。该模型已成功使用来自厌氧反应器的独立长期实验数据集并在不同操作条件下添加Fe(Ⅲ)进行了成功校准和验证。该模型令人满意地描述了硫酸盐的还原,有机碳的去除和VFA的产生。结果表明,添加铁(Ⅲ)可引起还原铁细菌(IRB)对微生物的还原,从而显着增强硫酸盐还原菌(SRB)对硫酸盐的还原作用,随后将VFA组成改变为醋酸盐为主的出水。同时,IRB生成的Fe(Ⅱ)可以减轻硫化铁沉淀对未解离的H_2S对微生物的抑制作用,从而进一步提高了性能。此外,发现在相对较低的有机碳/ SO_4〜(2-)比(例如1.0)下,与高有机碳/ SO_4〜(2-)相比,铁(Ⅲ)对反应器性能的增强更为显着。比率(例如4.5)。这项工作的基于Fe(Ⅲ)的工艺可以很容易地与常用的磷回收策略相结合,将产生的硫化物回收,然后沉积到常规的化学除磷污泥(FePO_4)中,从而实现FeS沉淀,从而回收磷。从饮用水处理过程中的废铁污泥中获取所需的Fe(Ⅲ),以实现最大的资源回收/再利用,同时实现高速率的硫酸盐去除。

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  • 来源
    《Environmental Science & Technology》 |2015年第4期|2123-2131|共9页
  • 作者单位

    Advanced Water Management Centre, The University of Queensland, St. Lucia, Queensland 4072, Australia;

    Key Laboratory of Industrial Ecology and Environmental Engineering, Ministry of Education, School of Environmental Science and Technology, Dalian University of Technology, Dalian 116024, China;

    Advanced Water Management Centre, The University of Queensland, St. Lucia, Queensland 4072, Australia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
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  • 入库时间 2022-08-17 13:59:41

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