State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, P.O. Box 2650, 73 Huanghe Road, Nangang District, Harbin, Heilongjiang Province 150090, China.
State Key Laboratory of Urban Water Resource and Environment, School of Environment, Harbin Institute of Technology, P.O. Box 2650, 73 Huanghe Road, Nangang District, Harbin, Heilongjiang Province 150090, China.
Chemosphere. 2018 Dec;212:837-844. doi: 10.1016/j.chemosphere.2018.08.160. Epub 2018 Aug 31.
Micro-aerobic condition has proven to be effective in enhancing sulfide oxidation to elemental sulfur (S) during integrated simultaneous desulfurization and denitrification process (ISDD). In this study we investigated and compared the performance and microbial community of ISDD process operating under initially anoxic, then micro-aerobic and finally switch back to anoxic condition. For all the three tested scenarios, comparable bioreactor performance in terms of sulfate (95.0 ± 4.4%, 90.6 ± 3.8%, 89.8 ± 3.5%) and nitrate (∼100%) removal was achieved. However, a shift of ISDD bioreactor from micro-aerobic to anoxic environment clearly increased the S production (30.6%), relative to that at initial anoxic condition (14.2%). Further anoxic bioreactor operation with different influent nitrate concentrations also obtained satisfactory performance particularly in terms of S production. Microbial community analysis results showed that functional microorganisms selectively enriched at micro-aerobic condition, particularly sulfide-oxidizing bacteria (SOB), could also function well and enhance S production when bioreactor switching from micro-aerobic to anoxic environment. We proposed that micro-aerobic strategy could function as a bio-selector and provide a new idea in functional microorganisms selectively enrichment for wastewater treatment.
微氧条件已被证明在同时脱硫和反硝化(ISDD)过程中有效促进硫化物氧化为元素硫(S)。在这项研究中,我们研究并比较了初始缺氧、然后微氧最后再回到缺氧条件下运行的 ISDD 工艺的性能和微生物群落。在所有三个测试场景中,硫酸盐(95.0±4.4%、90.6±3.8%、89.8±3.5%)和硝酸盐(~100%)去除方面,生物反应器的性能相当。然而,与初始缺氧条件相比,ISDD 生物反应器从微氧环境切换到缺氧环境时,S 的产量明显增加(30.6%)。进一步在不同进水硝酸盐浓度下进行缺氧生物反应器运行,也获得了令人满意的性能,特别是在 S 产量方面。微生物群落分析结果表明,在微氧条件下选择性富集的功能微生物,特别是硫氧化菌(SOB),在生物反应器从微氧切换到缺氧环境时也能很好地发挥作用并提高 S 的产量。我们提出,微氧策略可以作为生物选择器,为废水处理中功能微生物的选择性富集提供新的思路。