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Macroscale and microscale analyses of nitrification and denitrification in biofilms attached on membrane aerated biofilm reactors

机译:膜曝气生物膜反应器上附着的生物膜中硝化和反硝化的宏观和微观分析

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A membrane aerated biofilm reactor (MABR), in which O_2 was supplied from the bottom of the biofilm and NH_4~+ and organic carbon were supplied from the biofilm surface, was operated at different organic carbon loading rates and intra-membrane air pressures to investigate the occurrence of simultaneous chemical oxygen demand (COD) removal, nitrification and denitrification. The spatial distribution of nitrification and denitrification zones in the biofilms was measured with microelectrodes for O_2, NH_4~+, NO_2~-, NO_3~- and pH. When the MABR was operated at approximately 1.0 g-COD/m~2/day of COD loading rate, simultaneous COD removal, nitrification and denitrification could be achieved. The COD loading rates and the intra-membrane air pressures applied in this study had no effect on the startup and the maximum rates of NH_4~+ oxidation in the MABRs. Microelectrode measurements showed that O_2 was supplied from the bottom of the MABR biofilm and penetrated the whole biofilm. Because the biofilm thickness increased during the operations, an anoxic layer developed in the upper parts of the mature biofilms while an oxic layer was restricted to the deeper parts of the biofilms. The development of the anoxic zones in the biofilms coincided with increase in the denitrification rates. Nitrification occurred in the zones from membrane surface to a point of ca. 60 μm. Denitrification mainly occurred just above the nitrification zones. The COD loading rates and the intra-membrane air pressures applied in this study had no effect on location of the nitrification and denitrification zones.
机译:膜曝气生物膜反应器(MABR),其中从生物膜的底部提供O_2,从生物膜的表面提供NH_4〜+和有机碳,在不同的有机碳加载速率和膜内气压下运行同时发生化学需氧量(COD)去除,硝化和反硝化的过程。用O_2,NH_4〜+,NO_2〜-,NO_3〜-和pH微电极测量了生物膜中硝化和反硝化区的空间分布。当MABR以大约1.0 g-COD / m〜2 / day的COD负载速率运行时,可以同时去除COD,硝化和反硝化。本研究中使用的COD加载速率和膜内气压对MABR的启动和最大NH_4〜+氧化速率没有影响。微电极测量表明,O_2是从MABR生物膜的底部提供的,并穿透了整个生物膜。由于生物膜的厚度会在操作过程中增加,因此在成熟生物膜的上部会形成一个缺氧层,而将氧化层限制在该生物膜的较深部分。生物膜中缺氧区域的发展与反硝化速率的增加相吻合。硝化作用发生在从膜表面到大约一点的区域。 60微米反硝化主要发生在硝化区的正上方。在这项研究中使用的化学需氧量加载速率和膜内气压对硝化和反硝化区的位置没有影响。

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