Advanced Water Management Centre, The University of Queensland , St. Lucia, Queensland 4072, Australia.
Environ Sci Technol. 2015 Feb 17;49(4):2123-31. doi: 10.1021/es504200j. Epub 2015 Jan 29.
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 H2S 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/SO4(2-) ratio (e.g., 1.0) than at high organic carbon/SO4(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 (FePO4) 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.
添加三价铁的厌氧反应器已被实验证明能够在处理含硫酸盐废水时同时提高硫酸盐还原和有机物降解。本工作开发了一个数学模型来评估添加三价铁对硫酸盐还原和有机碳去除以及厌氧反应器中挥发性脂肪酸(VFA)组成的影响。该模型使用添加 Fe(III)的厌氧反应器在不同操作条件下的独立长期实验数据集进行了成功的校准和验证。该模型很好地描述了硫酸盐还原、有机碳去除和 VFA 生成。结果表明,添加 Fe(III)会诱导铁还原菌(IRB)还原 Fe(III),这显著增强了硫酸盐还原菌(SRB)的硫酸盐还原作用,随后改变 VFA 组成,使出水以乙酸为主。同时,IRB 产生的 Fe(II)可通过铁硫化物沉淀缓解未解离 H2S 对微生物的抑制作用,从而进一步提高性能。此外,发现与高有机碳/SO4(2-)比(例如,4.5)相比,在相对低的有机碳/SO4(2-)比(例如,1.0)下,Fe(III)对反应器性能的增强更为显著。本工作中的基于 Fe(III)的工艺可以很容易地与常用的磷回收策略集成,生成的硫化物被回收并沉淀到常规的化学除磷污泥(FePO4)中,从而在实现磷回收的同时实现 FeS 沉淀,而所需的 Fe(III)则从饮用水处理过程中的废铁污泥中获得,以实现最大的资源回收/再利用,同时实现高硫酸盐去除率。