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在 25°C 下运行的厌氧氨氧化膨胀反应器同步脱氮除磷。

Simultaneous nitrogen removal and phosphorus recovery using an anammox expanded reactor operated at 25 °C.

机构信息

Department of Civil and Environmental Engineering, Graduate School of Engineering, Tohoku University, 6-6-06 Aramaki Aza Aoba, Aoba-ku, Sendai, Miyagi, 980-8579, Japan; Center for Material Cycles and Waste Management Research, National Institute for Environmental Studies, Tsukuba, 305-8506, Japan.

Graduate School of Environmental Studies, Tohoku University, 6-6-06 Aramaki Aza Aoba, Aoba-ku, Sendai, Miyagi, 980-8579, Japan.

出版信息

Water Res. 2020 Apr 1;172:115510. doi: 10.1016/j.watres.2020.115510. Epub 2020 Jan 17.

Abstract

While anammox is a cost-effective nitrogen treatment process for wastewater with high nutrient strength, phosphorus remains untouched during this process and needs further treatment. In this study, the nitrogen removal and phosphorus recovery were achieved simultaneously at 25 °C using an anammox expanded bed. A stable high nitrogen removal efficiency of 83.7 ± 4.8% at a 1500 mgN/L influent total nitrogen concentration and a phosphorus removal efficiency of 94.2 ± 1.2% at 100 mg P/L influent total phosphorus were obtained during continuous operation. The effects of the nitrogen loading rate, hydraulic retention time (HRT), pH, Ca and PO concentration on the phosphorus removal was verified in the long-term operation of the reactor. The sludge produced contained a high content of phosphorus mainly in the form of hydroxyapatite (HAP), and the sludge composition strongly reflected the nitrogen and phosphorus loading. The structure of the anammox-HAP composite granules was illustrated by the use of fluorescence in situ hybridization (FISH) and Raman spectroscopic mapping analysis. The results in this study indicate that by controlling the operation parameters, it is possible to integrate a high efficiency phosphorus recovery with the anammox process, and significantly reduce the nutrient loading for further wastewater treatment.

摘要

虽然厌氧氨氧化是一种具有成本效益的高营养强度废水氮处理工艺,但在此过程中磷未被触及,需要进一步处理。在这项研究中,在 25°C 下使用厌氧氨氧化膨胀床同时实现了氮的去除和磷的回收。在连续运行过程中,进水总氮浓度为 1500mgN/L 时,氮去除率稳定在 83.7±4.8%,进水总磷浓度为 100mgP/L 时,磷去除率为 94.2±1.2%。在反应器的长期运行中,验证了氮负荷率、水力停留时间(HRT)、pH 值、Ca 和 PO 浓度对磷去除的影响。产生的污泥中含有大量的磷,主要以羟基磷灰石(HAP)的形式存在,污泥组成强烈反映了氮磷的负荷。使用荧光原位杂交(FISH)和拉曼光谱映射分析说明了厌氧氨氧化-HAP 复合颗粒的结构。本研究结果表明,通过控制操作参数,可以将高效磷回收与厌氧氨氧化工艺集成,显著降低进一步废水处理的营养负荷。

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