Effect of controlled aeration on COD and nitrogen removal in aerated constructed wetlands used for effluent polishing

曝气 流出物 芦苇 化学需氧量 环境工程 反硝化 废水 水力停留时间 环境科学 人工湿地 硝化作用 污染物 污水处理 湿地 氮气 化学 生态学 有机化学 生物
作者
Hafiz Ihsan-Ul-Haq Khan,Cornelis Groot,Otto Schepers,D. Van Oirschot,Mireille Martens,Frederik Ronsse,Diederik P.L. Rousseau
出处
期刊:Journal of environmental chemical engineering [Elsevier BV]
卷期号:10 (3): 108043-108043 被引量:5
标识
DOI:10.1016/j.jece.2022.108043
摘要

Aerated wetland (AW) technology is typically used in high oxygen demand situations. This study however investigated its applicability for further polishing of effluents of both a municipal and an industrial wastewater treatment plant. Different aeration and pollutant removal strategies were tested, all under high hydraulic loading rate conditions (0.69 m3.m−2.d−1, 12h hydraulic retention time). The experiments were done on two 350 m² horizontal subsurface flow constructed wetlands (HSSF CW), filled with expanded clay aggregates (Argex™) and planted with common reed (Phragmites australis). Each CW was divided into three equal zones, each equipped with forced bed aeration (FBA™). For this study, continuous (100% on) and time-based (50%-time on/off) aeration were compared versus set dissolved oxygen levels controlled by oxygen sensors (3–4, 2–3 and 1–2 mgO2. L−1 in each zone, and 2–3 mgO2. L−1 in zone 1 and no aeration in zones 2 and 3, designated as 2–3/0/0). Results showed near 100% nitrification for all aeration regimes. Chemical oxygen demand (COD) removal was between 18% and 33% during high aeration (100%, 50%, 3–4 and 2–3 mgO2. L−1) but was reduced (1–15%) during the most limiting aeration modes (1–2 and 2–3/0/0 mgO2. L−1). Denitrification was limited for municipal effluent, however, reasonable NO3-N removal (31–72%) was noted for industrial effluent. The optimal balance between removal efficiency and energy consumption was found to be for the 2–3 mgO2. L−1 aeration setting, consuming 6.9–11.2 Wh.m−3. The outcomes of this study can be helpful for implementing aerated CWs as a tertiary treatment.
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