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分步进料分配比对异养-硫自养组合工艺 ABR 系统去除高浓度高氯酸盐性能的影响。

The effect of step-feeding distribution ratio on high concentration perchlorate removal performance in ABR system with heterotrophic combined sulfur autotrophic process.

机构信息

Tianjin Key Laboratory of Aquatic Science and Technology, School of Environmental and Municipal Engineering, Tianjin Chengjian University, Jinjing Road 26#, Tianjin 300384, PR China.

Tianjin Key Laboratory of Aquatic Science and Technology, School of Environmental and Municipal Engineering, Tianjin Chengjian University, Jinjing Road 26#, Tianjin 300384, PR China.

出版信息

J Hazard Mater. 2021 Jun 5;411:125151. doi: 10.1016/j.jhazmat.2021.125151. Epub 2021 Jan 14.

Abstract

In a lab-scale anaerobic baffled reactor (ABR) with eight compartments, the heterotrophic and sulfur autotrophic processes were combined to remove perchlorate. And then, the step-feeding distribution ratio of the heterotrophic perchlorate reduction unit (HPR unit) was optimized to achieve efficient removal of high concentration perchlorate. Under the optimized step-feeding distribution ratio, the perchlorate removal efficiency reached to 99.8% with the influent concentration of 1300 mg/L, indicating that the removal performance of step-feeding was better than that of normal-feeding. A mass balance results showed that the perchlorate removal capacity of the C1-C5 compartments were 11.8 ± 0.6, 13.2 ± 0.2, 11.7 ± 1.0, 8.8 ± 0.2 and 9.8 ± 1.0 g/d during the stage VIII, indicating that the step-feeding can effectively relieve pollutant loading of C1 compartment and improve the perchlorate removal capacity of the C2-C5 compartments. Moreover, the high-throughput sequencing analysis showed that bacterial community was significant difference between the HPR and sulfur autotrophic perchlorate removal (SAPR) units. Principal component analysis (PCA) showed that perchlorate removal was more positive correlation with the forward compartments than the posterior compartments of HPR unit. The study confirms that the optimized step-feeding ratio is beneficial to remove the high concentration perchlorate via combining heterotrophic and sulfur autotrophic processes.

摘要

在一个具有八个隔室的实验室规模厌氧折流板反应器 (ABR) 中,将异养和硫自养过程相结合以去除高氯酸盐。然后,优化了异养高氯酸盐还原单元 (HPR 单元) 的分步进料分配比,以实现高效去除高浓度高氯酸盐。在优化的分步进料分配比下,当进水浓度为 1300mg/L 时,高氯酸盐去除效率达到 99.8%,表明分步进料的去除性能优于常规进料。质量平衡结果表明,在第八阶段,C1-C5 隔室的高氯酸盐去除能力分别为 11.8±0.6、13.2±0.2、11.7±1.0、8.8±0.2 和 9.8±1.0g/d,表明分步进料可以有效缓解 C1 隔室的污染物负荷,并提高 C2-C5 隔室的高氯酸盐去除能力。此外,高通量测序分析表明,HPR 和硫自养高氯酸盐去除 (SAPR) 单元中的细菌群落存在显著差异。主成分分析 (PCA) 表明,高氯酸盐去除与 HPR 单元的前向隔室比后向隔室更呈正相关。该研究证实,通过结合异养和硫自养过程,优化的分步进料比有利于去除高浓度高氯酸盐。

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