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Alternating anoxic/oxic condition combined with step-feeding mode for nitrogen removal in granular sequencing batch reactors (GSBRs)

机译:交替的缺氧/有氧条件与分步进料模式相结合,可在粒状测序间歇反应器(GSBR)中脱氮

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Alternating anoxic/oxic condition combined with step-feeding mode (AASF) has been reported to be an efficient method for nitrogen removal in granular sequencing batch reactor by our previous work. As carbonitrogen (C/N) ratio is one of the key factors impacting nitrogen removal efficiency, batch experiments using granules with a mean size of 1.3 mm under AASF were carried out for nitrogen removal from synthetic wastewater with C/N ratio of 5:1 and 3:1, respectively. It was found that over 90% nitrogen efficiency could be achieved for both C/N of 5 and 3. Furthermore, over 2 months operation was maintained for treating the wastewater with C/N ratio of 5:1 to investigate the long-term stability of granules under the new operational strategy. The results showed that AASF mode in GSBR could achieve over 85% nitrogen removal efficiency with great stability for long-term stability. This indicated that alternating anoxic/oxic condition combined with step-feeding mode is an effective strategy for nitrogen removal even from wastewater with low C/N ratio in granular sequencing batch reactor.
机译:据报道,交替的缺氧/有氧条件与分步进料模式(AASF)相结合是我们以前的工作在粒状测序间歇反应器中脱氮的有效方法。由于碳/氮(C / N)比是影响脱氮效率的关键因素之一,因此在AASF下使用平均粒径为1.3 mm的颗粒进行了批量实验,以从C / N为5的合成废水中脱氮。 :1和3:1。发现在C / N为5和3的情况下,氮效率均可以达到90%以上。此外,在2个月的处理中,以C / N为5:1的废水进行处理以研究长期稳定性。新操作策略下的颗粒结果表明,GSBR中的AASF模式可以达到85%以上的脱氮效率,并且具有长期稳定性。这表明交替的缺氧/缺氧条件与分步进料方式相结合是一种有效的策略,即使在粒序分批反应器中从低C / N比的废水中脱氮也是如此。

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