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EGSB 反应器中微生物空间分布和活性在高负荷和低负荷脱氮脱硫中的影响。

Influence of microbial spatial distribution and activity in an EGSB reactor under high- and low-loading denitrification desulfurization.

机构信息

State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin, 150090, China; National Technology Innovation Center of Synthetic Biology, Tianjin Institute of Industrial Biotechnology, Chinese Academy of Sciences, Tianjin, 300308, China; Key Laboratory of Environmental Biotechnology, Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing, 100085, China.

Research Center for Eco-environmental Engineering, Dongguan University of Technology, Dongguan, 523808, China.

出版信息

Environ Res. 2021 Apr;195:110311. doi: 10.1016/j.envres.2020.110311. Epub 2020 Oct 29.

Abstract

To characterize the impact of reactor configuration and influent loading on elemental sulphur (S) recovery during denitrification desulfurization, a laboratory-scale expanded granular sludge bed (EGSB) reactor was established under two influent acetate/nitrate/sulphide loadings; the water flow velocity, microbial community, and functional genes at different heights were investigated. There was no S generated when acetate/nitrate/sulphide loadings were set to 0.95/0.60/1.05 kg/m.d (low-loading). Furthermore, there were no typical denitrifying sulphide oxidizing bacteria under this condition, and Syntrophobacter, Anaerolineaceae genera were predominant in the reactor. As the influent loading was doubled (high-loading), S recovery increased to 87%; the bacterial distribution was relatively homogeneous with sulphide oxidation genera (Thauera) being predominant. Neither nirK nor sqr genes were detected in the low-loading sample at a height of 50 cm. The sqr/sox ratios of low-loading stage were 2.50 (10 cm), 0.94 (30 cm), and 0 (50 cm), and the ratios of the high-loading stage were 1.38 (10 cm), 1.33 (30 cm), and 1.08 (50 cm). A hydrodynamics analysis indicated that the water flow velocity was homogenous throughout the reactor. Appropriate reactor configuration and operation parameters play an important role in the efficient regulation of S recovery during denitrification desulfurization.

摘要

为了研究反应器构型和进水负荷对反硝化脱硫过程中元素硫(S)回收的影响,在两种不同的进水乙酸盐/硝酸盐/硫化物负荷条件下,建立了实验室规模的膨胀颗粒污泥床(EGSB)反应器;考察了不同高度的水力学特性、微生物群落和功能基因。当乙酸盐/硝酸盐/硫化物负荷设定为 0.95/0.60/1.05 kg/m.d(低负荷)时,没有生成 S。此外,在这种条件下,没有典型的反硝化硫氧化细菌,而反应器中主要的微生物是Syntrophobacter 和 Anaerolineaceae 属。当进水负荷增加一倍(高负荷)时,S 的回收率增加到 87%;细菌分布相对均匀,主要的硫化物氧化菌(Thauera)占主导地位。在低负荷样品中,在 50 cm 高度处没有检测到 nirK 或 sqr 基因。低负荷阶段的 sqr/sox 比值分别为 2.50(10 cm)、0.94(30 cm)和 0(50 cm),高负荷阶段的比值分别为 1.38(10 cm)、1.33(30 cm)和 1.08(50 cm)。水力学分析表明,整个反应器的水流速度均匀。适当的反应器构型和操作参数在反硝化脱硫过程中高效调节 S 回收中起着重要作用。

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