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A novel anammox granules-circulating expanded granular sludge bed reactor for the efficient circulation and retention of floating anammox granules

机译:一种新型厌氧菌颗粒循环式膨胀颗粒污泥床反应器,可有效地循环和保留浮游厌氧菌颗粒

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In application of anammox process, the operation of the conventional expanded granular sludge bed reactor (EGSB(conv).) is severely limited by the blocking and decay of floating anammox granules.To address this emerging issue, a novel three-phase separator configuration was designed and an anammox granules circulating EGSB (EGSBGC) was proposed in this study. In the EGSBGC, an influent scour on floating granules, whose effect was confirmed by simulation with a three-dimensional flow model, was obtained by integrating the external three-phase separator with the influent and the external cycle. After 166-d operation, the nitrogen removal efficiency of the EGSBGC reached 75.6%, being 1.28-times that of the EGSB(conv.) (58.9%). The sludge concentration in the main body of the EGSBGC reached 3112 +/- 65 mg/L, compared with 2613 +/- 42 mg/L in the EGSB(conv.) (p < 0.05). Moreover, the severe granules blockage and decay problem that is frequently encountered in the EGSB(conv.) no longer occurred in the EGSB(GC). The relative abundance of anammox bacteria in granules from the three-phase separator of the EGSB(GC) was 29.7%, significantly higher than that from the EGSB(conv.) (16.1%, p < 0.05). The blockage and decay of granules in the three-phase separator of the EGSB(conv.) led to an obvious proliferation of heterotrophic bacteria, with their relative abundance increased by 9.4% compared with the seed sludge (38.6% vs. 29.2%). This study proposed a practical three-phase separator configuration to sustain efficient and stable operation of anammox processes toward the promotion of granules circulation, retention and reaction. (C) 2019 Published by Elsevier Ltd.
机译:在厌氧氨氧化工艺的应用中,常规的膨化颗粒污泥床反应器(EGSB(conv)。)的运行受到漂浮的厌氧氨氧化镁颗粒的阻塞和腐烂的严重限制。这项研究提出了厌氧菌颗粒循环EGSB(EGSBGC)。在EGSBGC中,通过将外部三相分离器与进水和外部循环集成在一起,获得了漂浮颗粒上的进水冲刷,其效果已通过三维流动模型的仿真得到了证实。 166天运行后,EGSBGC的脱氮效率达到75.6%,是EGSB(conv。)(58.9%)的1.28倍。 EGSBGC主体中的污泥浓度达到3112 +/- 65 mg / L,而EGSB(conv。)中则为2613 +/- 42 mg / L(p <0.05)。此外,在EGSB(conv。)中经常遇到的严重的颗粒堵塞和腐烂问题在EGSB(GC)中不再发生。 EGSB(GC)三相分离器中颗粒中厌氧菌的相对丰度为29.7%,显着高于EGSB(conv。)的颗粒中的厌氧菌(16.1%,p <0.05)。 EGSB(conv。)三相分离器中颗粒的堵塞和腐烂导致异养细菌明显增殖,与种子污泥相比,它们的相对丰度提高了9.4%(38.6%对29.2%)。这项研究提出了一种实用的三相分离器配置,以维持厌氧氨氧化工艺的高效稳定运行,从而促进颗粒的循环,保留和反应。 (C)2019由Elsevier Ltd.发布

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