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优化曝气策略以提高脱氮效率:末端气体再循环曝气在固定床生物膜反应器中的应用。

Optimized aeration strategies for nitrogen removal efficiency: application of end gas recirculation aeration in the fixed bed biofilm reactor.

机构信息

College of Civil Engineering and Architecture, Zhejiang University of Technology, Hangzhou, 310014, China.

College of Environment, Zhejiang University of Technology, 310014, CNo. 18 Chaowang Road, Hangzhou, 310014, People's Republic of China.

出版信息

Environ Sci Pollut Res Int. 2019 Sep;26(27):28216-28227. doi: 10.1007/s11356-019-06050-9. Epub 2019 Jul 31.

Abstract

Aeration strategy played an important role in reactor performance. In this study, when superficial upflow air velocity (SAV) decreased from 0.16 to 0.08 cm s, low dissolved oxygen concentration (DO) of 2.0 mg L occurred in reactor. The required depth for anoxic microenvironment in biofilm decreased from 902.3 to 525.9 μm, which enhanced the growth of denitrifying bacteria and total nitrogen (TN) removal efficiency. However, decreasing aeration intensity resulted in insufficient hydraulic shear stress, which led to weak biofilm matrix structure. Mass biofilm detachment and reactor deterioration then occurred after 87 days of operation. An end gas recirculation aeration strategy was proposed to separately manipulate DO and aeration intensity. Low DO and high aeration intensity were simultaneously achieved, which enhanced the metabolism of denitrifying bacteria (such as Flavobacterium sp., Pseudorhodobacter sp., and Dok59 sp.) and EPS-producing bacteria (such as Zoogloea sp. and Rhodobacter sp.). Consequently, high TN removal performance (82.1 ± 2.7%) and stable biofilm structure were achieved.

摘要

曝气策略在反应器性能中起着重要作用。在这项研究中,当表向上流空气速度(SAV)从 0.16cm/s 降低到 0.08cm/s 时,反应器中出现了低溶解氧浓度(DO)为 2.0mg/L 的情况。缺氧微生物环境所需的生物膜深度从 902.3μm 降低到 525.9μm,这促进了反硝化细菌的生长和总氮(TN)去除效率。然而,降低曝气强度会导致水力剪切应力不足,从而导致生物膜基质结构较弱。经过 87 天的运行后,大量生物膜脱落,导致反应器恶化。提出了末端气体再循环曝气策略来分别控制 DO 和曝气强度。同时实现了低 DO 和高曝气强度,这增强了反硝化细菌(如黄杆菌属、假单胞菌属和 Dok59 属)和 EPS 产生菌(如动胶菌属和红杆菌属)的代谢。因此,实现了高 TN 去除性能(82.1±2.7%)和稳定的生物膜结构。

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