Improving denitrification in an aquaculture wetland using fish waste - a case study
Introduction
Cost-efficient, end-of-pipe techniques for removing nitrate from recirculating aquaculture system (RAS) effluent are required to reduce nitrogen discharge from aquaculture farms. Constructed wetlands are man-made treatment systems successfully applied in many parts of the world for treating municipal, agricultural, and industrial wastewater (Verhoeven and Meuleman, 1999). They are mechanically simple but biologically complex systems. Nutrient / pollutant removal happens in a rather “uncontrolled” manner based on biological and biochemical processes affected by interactions between plants, microorganisms, and the sediment (Kadlec and Knight, 1996).
Where space allows, constructed wetlands may also be established for treating dilute aquaculture effluent. To improve effectiveness of such engineered systems, underlying factors governing nutrient removal processes need to be understood and ultimately controlled. Several studies have investigated the efficiency of subsurface- and horizontal-flow constructed wetlands treating aquaculture effluent (e.g., Schulz et al., 2003; Schulz et al., 2004; Sindilariu et al., 2007; Sindilariu et al., 2008; Sindilariu et al., 2009; Dalsgaard et al., 2018). Schulz et al. (2004) investigated the effect of hydraulic retention time (HRT) in three parallel, 350 m2 free water surface (FWS) wetlands treating effluent from a flow-through rainbow trout (Oncorhynchus mykiss) farm. Mean total nitrogen removal rates of 0.45, 0.71, and 0.82 g/m2/d at HRTs of 3.5, 5.5, and 11 h, respectively, were found, and the authors concluded that a shorter HRT favored aerobic conditions and hindered denitrification. Dalsgaard et al. (2018) investigated longitudinal and seasonal nutrient removal rates in a FWS wetland treating effluent from a Danish Model Trout Farm (MTF) type I (Jokumsen and Svendsen, 2010). The wetland was characterized by a relatively short retention time (7.7 h), and a miniscule net removal of nitrate-N was observed in spring (February–June) with area-based removal rate constants (kA) averaging 0.1 ± 0.1 m/d. This was succeeded by a small net production of nitrate-N from July to January, and it was argued that denitrification was limited by high oxygen concentrations and low organic carbon availability.
In comparison, a two-year monitoring study in eight constructed wetlands associated with Danish MTFs type III found average removal rates of 1.5–1.9 g NO3-N/m2/d (Svendsen et al., 2008). All eight wetlands were characterized by relatively long HRTs (20–50 h), and farm effluent concentrations were higher in organic carbon and nitrate-N than in the wetland study by Dalsgaard et al. (2018) (approximately 10.0 versus 3.5 mg total BOD5/l, and 6.6 versus 3.4 mg NO3-N/l).
These average removal rates are, however, still relatively low compared to other denitrification technologies applied in aquaculture (van Rijn et al., 2006) and the current, more or less passive, operation of aquaculture wetlands prevents many Danish farmers from increasing their production because of exceeding their discharge allowance (Danish Ministry of the Environment, 2012).
A study by Suhr et al. (2013) demonstrated that RAS sludge may be used as a cost-free carbon source in a single-sludge denitrification process aimed at removing nitrogen from fish farm effluent. By mixing nitrate-rich effluent from a production unit with carbon-rich sludge in a heterotrophic denitrification reactor, nitrogen was removed at a maximum rate of 124.8 ± 15.7 g NO3-N/m3 reactor/d. The study highlighted that C/N ratios and HRT are essential parameters with respect to maximizing nitrogen removal in this type of setup.
As an alternative (or in addition) to using a separate, rather complex filter set-up as the one by Suhr et al. (2013), we hypothesized that the sludge denitrification process may be exploited within the basins of an existing constructed wetland. To examine this, an 11-week field study was carried out with the aim of improving overall nitrogen removal in a constructed FWS wetland treating effluent from a Danish Model Trout Farm type III. The objective of the study was to mix internally generated, carbon-rich sludge effluent with increasing proportions of nitrate-rich effluent in a wetland side stream and measure the effect on overall nitrogen removal rates.
Section snippets
Fish farm and operation
The study was carried out at a Danish MTF type III producing approximately 600 t rainbow trout/y. The inlet water to the farm consisted of ~25 l/s of groundwater and ~25 l/s of drainage water, which was recovered from below the associated constructed wetland and equally distributed into six independent RAS units. Each unit contained two parallel raceways, sludge cones, drum filters, and a fixed bed biofilter, and recirculation flows were generated via airlifts. Each biofilter was separated into
Nitrogen removal
Increasing the inflow of nitrate-rich effluent to wetland stream 2 led to a significant increase in overall nitrogen removal of the entire wetland (CW; Table 3, Table 4). The area-based TN removal rate for the whole wetland increased from a baseline value of 1.4 ± 0.2 to 3.9 ± 0.8 g/m2/d at the highest manipulated flow (flow 3). This improvement was principally due to a significant increase in wetland stream 2 nitrate removal (in area delimited by station J), increasing from a baseline value of
Summary and future prospects
This case study demonstrated that nitrogen removal in an aquaculture wetland can be improved by using internally generated sludge/fish waste as a carbon source for denitrification in an anoxic part of the wetland. As a side effect, some additional removal of phosphorous may be achieved via the enhanced denitrification activity. Through flow manipulations, it was demonstrated that the farm was able to significantly reduce the discharge of nitrogen and its overall environmental impact(Table 4).
Authors contributions
Mathis von Ahnen participated in the design of the study, carried out the sampling and drafted the manuscript. Per Bovbjerg Pedersen participated in the design of the study and helped to draft the manuscript. Johanne Dalsgaard participated in the design of the study and coordination and helped to draft the manuscript. All authors read and approved the final manuscript.
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgements
This research was funded by the Ministry of Food, Agriculture and Fisheries of Denmark and by the European Union through the European Maritime and Fisheries Fund (EMFF). We thank the fish farmer for allowing us access to his facilities and the farm manager for helpful assistance during the study. In addition, we thank laboratory technician Ulla Sproegel, Brian Møller, and Dorthe Frandsen (DTU Aqua) for invaluable technical assistance in the laboratories.
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