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Ammonium Removal by the Oxygen-Limited Autotrophic Nitrification-Denitrification System

机译:限氧自养硝化-反硝化系统脱铵

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摘要

The present lab-scale research reveals the potential of implementation of an oxygen-limited autotrophic nitrification-denitrification (OLAND) system with normal nitrifying sludge as the biocatalyst for the removal of nitrogen from nitrogen-rich wastewater in one step. In a sequential batch reactor, synthetic wastewater containing 1 g of NH4+-N liter−1 and minerals was treated. Oxygen supply to the reactor was double-controlled with a pH controller and a timer. At a volumetric loading rate (Bv) of 0.13 g of NH4+-N liter−1 day−1, about 22% of the fed NH4+-N was converted to NO2-N or NO3-N, 38% remained as NH4+-N, and the other 40% was removed mainly as N2. The specific removal rate of nitrogen was on the order of 50 mg of N liter−1 day−1, corresponding to 16 mg of N g of volatile suspended solids−1 day−1. The microorganisms which catalyzed the OLAND process are assumed to be normal nitrifiers dominated by ammonium oxidizers. The loss of nitrogen in the OLAND system is presumed to occur via the oxidation of NH4+ to N2 with NO2 as the electron acceptor. Hydroxylamine stimulated the removal of NH4+ and NO2. Hydroxylamine oxidoreductase (HAO) or an HAO-related enzyme might be responsible for the loss of nitrogen.
机译:本实验室规模的研究表明,利用常规硝化污泥作为生物催化剂,一步一步从富氮废水中去除氮的限氧自养硝化-硝化(OLAND)系统的实施潜力。在顺序间歇式反应器中,处理了包含1 g NH4 + -N升 -1 和矿物质的合成废水。用pH控制器和计时器双重控制向反应器的氧气供应。在0.13 g NH4 + -N升 -1 -1 的体积负荷率(Bv)下,约占饲料的22% NH4 + -N转换为NO2 - -N或NO3 - -N,剩余38%为NH4 + > -N,其余40%主要作为N2除去。氮的比去除率约为50毫克N升 -1 -1 ,相当于16毫克N g的挥发性悬浮固体 -1 -1 。假定催化OLAND过程的微生物是由铵氧化剂主导的普通硝化器。推测OLAND系统中的氮损失是通过将NO4 -作为电子受体将NH4 + 氧化为N2发生的。羟胺促进了NH4 + 和NO2 -的去除。羟胺氧化还原酶(HAO)或与HAO相关的酶可能是造成氮损失的原因。

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