4.7 Article

Improving the performance of vertical flow constructed wetlands by modifying the filtering media structure

Journal

ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH
Volume 28, Issue 40, Pages 56852-56864

Publisher

SPRINGER HEIDELBERG
DOI: 10.1007/s11356-021-14389-1

Keywords

Vertical flow constructed wetlands; Bed configuration; Particle size; Flow profiles; Clogging; Organics removal; Nitrogen removal

Funding

  1. Spanish Dept. of Economy and Competitiveness [CTM2011-28384]

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The research showed that for subsurface vertical flow constructed wetlands treating municipal wastewater, adding a layer of fine sand can significantly improve treatment efficiency, leading to higher removal rates of total suspended solids and biological oxygen demand without clogging issues.
The aim of this research was to study the influence of the bed media configuration and particle size on the treatment efficiency of subsurface vertical flow (VF) constructed wetlands (CWs) treating municipal wastewater. Two outdoor pilot units (VF1 and VF2, planted with Phragmites australis) with the configuration C1 were operated in parallel for 2 years at similar surface loading rates of 9.7 +/- 3.2 (VF1) and 10.1 +/- 3.3 (VF2) g biological oxygen demand (BOD5)/m(2)center dot day (19.5 +/- 6.4 (VF1) and 20.4 +/- 6.2 (VF2) g chemical oxygen demand (COD)/m(2)center dot day). A different configuration C2 was used during the third year at 16.9 +/- 4.6 (VF1) and 18.2 +/- 3.0 (VF2) g BOD5/m(2)center dot day and 26.0 +/- 7.2 (VF1) and 28.0 +/- 4.7 (VF2) g COD/m(2)center dot day. Two different filtering materials (1-3-mm sand for VF1 and 2-6-mm fine gravel for VF2) were used for configuration C1. The same units were modified after 2 years of operation by adding a 10-cm layer of fine sand (0-2 mm) on the top (configuration C2). In C1 conditions, the unit with the coarse material VF2 showed significantly (p < 0.05) lower removal efficiencies of total suspended solids (TSS) and BOD5 than VF1, and both units failed to meet the BOD5 discharge limit. In C2 conditions, removal efficiencies reached 82% TSS, 97% BOD5, 76-81% ammonia, and 60-66% TN, without significant differences between VF1 and VF2 units. Removal efficiencies were significantly higher for configuration C2 than that for C1, due to the positive effect of the upper fine sand layer. The presence of this fine sand layer doubled the water retention time and increased the removal rates, while the infiltration rates were high enough for an operation free of clogging.

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