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使用交替泵送流序批式生物膜反应器从生活污水强度的合成废水中去除氮和磷。

Nitrogen and phosphorus removal from domestic strength synthetic wastewater using an alternating pumped flow sequencing batch biofilm reactor.

作者信息

Rodgers Michael, Wu Guangxue, Zhan Xinmin

机构信息

Department of Civil Engineering and National Centre for Biomedical Engineering Science, National University of Ireland, Galway, Ireland.

出版信息

J Environ Qual. 2008 May 2;37(3):977-82. doi: 10.2134/jeq2007.0361. Print 2008 May-Jun.

Abstract

Nutrient removal from domestic strength synthetic wastewater by an alternating pumped flow sequencing batch biofilm reactor (APFSBBR) was investigated in this laboratory study. The APFSBBR comprised two reactor tanks (Reactors 1 and 2) with two identical biofilm modules of vertical tubular plastic media with a high specific surface area, one in each tank. The APFSBBR was operated in cycles of four phases: fill, anaerobic, aerobic, and draw. During the fill phase, Reactor 1 was half-filled with domestic strength synthetic wastewater. During the subsequent anaerobic phase, most of the phosphorus release took place from the submerged biofilm in this reactor. In the aerobic phase, the wastewater was circulated by pumps between Reactors 1 and 2, resulting in denitrification at the start of the aerobic phase due to low oxygen concentrations, followed by nitrification and luxury uptake of phosphorus when oxygen concentrations increased. During the draw phase, Reactor 2 was half-emptied of the treated water. At the chemical oxygen demand (COD), total nitrogen (TN), and total phosphorus (TP) loading rates on the total biofilm area of 3.20 g COD, 0.33 g TN, and 0.06 g TP m(-2) d(-1), the removal efficiencies were 97, 85, and 92% for COD, TN, and TP, respectively.

摘要

在本实验室研究中,对交替泵送流序批式生物膜反应器(APFSBBR)去除生活污水强度合成废水中的营养物质进行了研究。APFSBBR由两个反应池(反应池1和反应池2)组成,每个反应池中都有一个相同的、具有高比表面积的垂直管状塑料介质生物膜模块。APFSBBR按四个阶段循环运行:进水、厌氧、好氧和排水。在进水阶段,反应池1中装入一半生活污水强度的合成废水。在随后的厌氧阶段,该反应池中大部分磷从淹没的生物膜中释放出来。在好氧阶段,废水通过泵在反应池1和反应池2之间循环,由于氧浓度低,在好氧阶段开始时发生反硝化作用,随后随着氧浓度的增加进行硝化作用和磷的过量吸收。在排水阶段,反应池2排出一半处理后的水。在化学需氧量(COD)、总氮(TN)和总磷(TP)在总生物膜面积上的负荷率分别为3.20 g COD、0.33 g TN和0.06 g TP m(-2) d(-1)时,COD、TN和TP的去除效率分别为97%、85%和92%。

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