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[硫酸盐与Fe(Ⅱ) EDTA-NO/Fe(Ⅲ) EDTA的厌氧还原过程特性及微生物群落分析]

[Anaerobic Reduction Process Characteristics and Microbial Community Analysis for Sulfate and Fe(Ⅱ) EDTA-NO/Fe(Ⅲ) EDTA].

作者信息

Zhang Yu, Wan Fang, Zhou Ji-Ti

机构信息

Key Laboratory of Industrial Ecology and Environmental Engineering(MOE), School of Environmental Science and Technology, Dalian University of Technology, Dalian 116024, China.

出版信息

Huan Jing Ke Xue. 2017 Nov 8;38(11):4706-4714. doi: 10.13227/j.hjkx.201704227.

Abstract

Based on biological flue gas desulfurization technology (Bio-FGD) and chelating absorption-biological regeneration technology (BioDeNO), simultaneous desulfurization and denitrification by biological methods combined with chelating absorption technology has been proposed in this study. This technique uses an alkaline absorption liquid with Fe(Ⅱ) EDTA to absorb the SO and NO in the flue gas. In this study, an attempt is made to simultaneously remove sulfate (SO) and Fe(Ⅱ) EDTA-NO/Fe(Ⅲ) EDTA, which are the SO and NO absorption byproducts in an anaerobic reactor. The results indicate that average removal efficiencies for SO and Fe(Ⅱ) EDTA-NO of 95.16% and 96.61%, respectively, were achieved when the hydraulic residence time (HRT) and pH were controlled at 16 h and 7.0. The reduction products of SO were mainly in the form of S in the liquid phase and hydrogen sulfide (HS) in the gas phase, while the reduction products of Fe(Ⅱ) EDTA-NO was N. The reduction of Fe(Ⅲ) EDTA could be achieved at all stages of the operation, however, the reduction rate decreases with a reduction in the HRT. In the fifth stage, the main sulfate-reducing bacteria (SRB) in the reactor was , a heterotrophic denitrifying bacteria, and two types of sulfur autotrophic denitrifying bacteria, and , which coexisted. Two genera of bacteria that can also reduce sulfur, and were also identified in the reactor.

摘要

基于生物烟气脱硫技术(Bio-FGD)和螯合吸收-生物再生技术(BioDeNO),本研究提出了将生物法与螯合吸收技术相结合的同时脱硫脱硝技术。该技术使用含Fe(Ⅱ)EDTA的碱性吸收液来吸收烟气中的SO和NO。在本研究中,尝试同时去除厌氧反应器中SO和NO的吸收副产物硫酸根(SO)和Fe(Ⅱ)EDTA-NO/Fe(Ⅲ)EDTA。结果表明,当水力停留时间(HRT)和pH分别控制在16 h和7.0时,SO和Fe(Ⅱ)EDTA-NO的平均去除效率分别达到95.16%和96.61%。SO的还原产物主要以液相中的S和气相中的硫化氢(HS)形式存在,而Fe(Ⅱ)EDTA-NO的还原产物为N。在运行的各个阶段都能实现Fe(Ⅲ)EDTA的还原,然而,还原速率随HRT的降低而降低。在第五阶段,反应器中的主要硫酸盐还原菌(SRB)为异养反硝化细菌以及两种硫自养反硝化细菌,它们共存。反应器中还鉴定出了另外两种也能还原硫的细菌属。

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