Enhanced denitrification and organics removal in hybrid wetland columns: Comparative experiments
Introduction
With unique advantages of low energy consumption and operating cost, constructed wetlands have been increasingly used in wastewater treatment. Pollutants are removed in a wetland system via a complex variety of physical, chemical and biological processes that are still not fully understood. The performance of the wetlands is often limited in terms of nitrogen removal, due to a lack of methods to balance conflicting conditions required for organics removal, nitrification and denitrification.
In a wetland system nitrogen is typically removed from wastewater primarily via the classic biodegradation route (i.e. ammonification, autotrophic nitrification, followed by heterotrophic denitrification), while other processes such as plant uptake and sorption–desorption also contribute to the removal (Vymazal, 2007). Regarding the biodegradations and eventual removal of nitrogen, significant alternative routes have been discovered, in particular anaerobic ammonium oxidation (Dong and Sun, 2007, Paredes et al., 2007). However, to date researchers have not been able to consistently implement the alternative biodegradation routes in the wetlands, and the classic denitrification route is still relied upon as the major mechanism for nitrogen removal.
One of the major problems associated with the classic nitrogen route is the lack of organic carbon for denitrification, due to the dependability of synthesis and activity of denitrifying enzymes on organic carbon availability (Lavrova and Koumanova, 2010). In an efficient wetland, substantial removal of organics (by aerobic decomposition) tends to occur prior to nitrification. As such, organics in the raw wastewater are not available for denitrification, and the classic route of nitrification cannot be completed; this often causes the TN level of the wastewater to remain virtually unchanged, while the nitrification of ammonia increases the nitrate level and acidity of the wastewater.
To overcome this problem, two options may be taken: (1) adding external sources of carbon directly into the wastewater, or (2) providing controlled release of organics from wetland media inside wetland matrices. The first option has already been put into practice (Songliu et al., 2009) at a cost of increased operating expenses. Regarding the second option, little information is available from the literature. The traditional substrates used in treatment wetlands are gravel and soil; neither provides a sufficient organic source for denitrification, and few studies have investigated the use of more organic-rich materials in the wetlands. In addition to nitrogen removal, existing literatures provide little information about the role of organic-rich materials in wetland systems for the removal of other pollutants (i.e. phosphorus, coliforms), despite their potential as alternative substrates (Gray et al., 2000).
This study had been planned to investigate the combination of three wetland systems with traditional (gravel) and alternative substrates (wood mulch and zeolite) for removing organic, inorganic pollutants and coliforms, emphasizing on meeting the conflicting conditions required for organics and nitrogen removal without adding external organics. The objectives of this study are two-fold: (1) to monitor the efficiency of alternative substrates, and (2) to investigate the stability of system performance under different operating conditions in terms of pollutant loadings.
Section snippets
Synthetic wastewater
Synthetic wastewater was used in this study that had pollutant concentration similar to domestic wastewater in Australia (Department of Environment, Department of Health and Water Corporation, 2005). The synthetic wastewater was prepared using (g in 1 L tap water): 0.02–0.07 C6H12O6, 0.07–0.22 NH4Cl, 0.01–0.03 KH2PO4, 0.11–0.34 CaCl2·2H2O, 0.32–0.92 MgSO4·7H2O, 0.15–0.44 NaHCO3, 0.12–0.36 NaCl, 0.005–0.03 FeSO4·7H2O, and 0.005–0.03 ZnSO4·7H2O. In every 25 L of the wastewater, 1–2 L domestic sewage
Overall performance of the three systems
The average influent hydraulic loading to system 1, 2 and 3 was 0.41, 0.65, 0.40 m3/m2 d, respectively. Table 2 represents average influent and effluent pollutant concentration (average of 13 sets of data), across each wetland along with, removal efficiencies. Table 3 represents overall removal efficiencies across the three systems. Overall, the results showed high TN removal percentages (>72%) across the three systems, within the range of variations in hydraulic loading and influent pollutant
Conclusions
Overall, organic mulch substrate enhanced total nitrogen removal in first stage VF columns due to availability of organic carbon from mulch substrate, thereby fostering denitrification. Removal of NH4–N was further enhanced in third stage VF columns (with zeolite) through substrate adsorption. Higher removal of biodegradable organics depleted the amount of organic carbon in zeolite VF columns, resulting in nitrate accumulation in the effluent. High efficiencies of E. coli removal were achieved
Acknowledgements
The authors would like to thank Monash Research Graduate School and Department of Civil Engineering, Monash University, Australia for sponsoring Tanveer Saeed’s Ph.D. studies.
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