Madax 8 Farm
- Commissioning expected date
Horizontal subsurface flow constructed wetland for pig slurry treatment, preceded by physical pre-treatment. Inverted trapezoidal cross-section with impermeable liner and gravel-sand fill. Macrophyte roots enhance microbial degradation. Influent percolates without surface flooding. Hydraulic retention enables mechanical filtration, while plants transport oxygen to root zones. Reductions achieved for Total Nitrogen, Electrical Conductivity, Settleable Solids, CH₄ and NH₃ emissions.
OPERATION
The slurry is separated into liquid and solid fractions using mechanical separation equipment. If there is enough space, the separation may be further enhanced by a subsequent decantation step. Most of the phosphorus and a substantial portion of the nitrogen are retained in the solid fraction, which is a product that is easier to transport longer distances. This technique is fully applicable to the intensive pig rearing sector, as demonstrated at implemented sites.
The liquid fraction flows to a horizontal subsurface flow constructed wetland, characterized by an inverted trapezoidal cross-section lined with an impermeable double-layer plastic membrane to prevent filtration into the subsoil and avoid any leakage to the environment. Inside this passive biological treatment system for pig slurry, the influent enters by gravity across a required 5% slope, percolating subsurface through the main filling material—a gravel bed—without flooding the surface. The system contains macrophyte vegetation (e.g., Phragmites australis, Juncus, Typha, Apium nodiflorum) rooted in a sand layer that rests on the gravel.
As the liquid moves through the substrate, mechanical filtration occurs, and prolonged hydraulic retention times (3–5 days) allow effective purification. Simultaneously, wetland plants transport oxygen to submerged root zones, fostering microbial communities that biologically degrade pollutants and organic matter.
PERFORMANCE
Nitrogen (as NO₃⁻ and NH₄⁺) is absorbed by the plants, thus reducing ammonia (NH₃) losses to the atmosphere. Based on experimental data, the treated effluent contains N-NO₃⁻: 3.9–5.8 mg/L and N-NO₂⁻: <0.021 mg/L (raw slurry: 1.6–6.1 mg/L N-NO₃⁻; decanted slurry: 1.9–6.3 mg/L N-NO₃⁻). These anions arise from natural biological oxidation of NH₃, common in passive systems. Possible emissions of nitrous oxide (N₂O) are kept low with proper management of operational parameters. Suspended solids and Biological Oxygen Demand (BOD) are also reduced.
The treated effluent exits via a drainage pipe at the outlet, collected by gravity into a final collection pond, and can be reused in agriculture (e.g., through fertigation), since it contains remaining N and/or P. Specifically, it reduces total nitrogen load by up to 50%, complying with the 170 kg N/ha/year limit of the Nitrates Directive, and supplies 60–120 kg P₂O₅/ha and 350–550 kg K₂O/ha (seasonal variation), thus closing the nutrient cycle through industrial symbiosis between livestock farming and agriculture.
Energy consumption is very low but not zero: main equipment includes homogenization agitation (5.5–15 kW), a feed pump/phase separator (1.5 kW for 2–10 m³/h), and transfer pumps (0.75 kW each). Periodic harvesting of vegetation/biomass, which can be used as co-substrate for anaerobic digestion or as feedstock for composting, and removal of accumulated organic matter are done as part of proper management. Care should be taken to address possible cross-media effects.
Reference documents related to the innovative technique
The integrated treatment system is designed to process the entire slurry volume generated by the farm, with the decantation unit and number of constructed wetland cells sized accordingly to match actual production. The system achieves a 20% reduction in total volume from raw slurry to purified effluent. This volume reduction, combined with the significant decrease in N concentration, results in a substantial reduction in the agricultural land required for sustainable application. Under the Nitrates Directive (170 kg N/ha/year), the treated effluent requires up to 50% less land compared to raw slurry, transforming a challenging waste management issue into a manageable, circular solution that facilitates compliance with environmental regulations while recovering valuable water and nutrients for agricultural use.
Associated main production process(es) and product(s): The Main process is an integrated system to treat raw pig slurry through phase separation, decantation, and a horizontal subsurface flow constructed wetland. The products are a solid fraction and a purified effluent suitable for irrigation and its reuse.
Production data: 15 m3
Project partners
Technology provider
As compared to:
Compared to the individual BAT techniques established in Commission Implementing Decision (EU) 2017/302 —such as mechanical separation, anaerobic digestion, external drying tunnels, aerobic digestion, nitrification-denitrification systems, and composting— the integrated constructed wetland system represents a superior solution due to its holistic and sustainable approach.
While individual techniques address only a fraction of the problem —mechanical separation reduces solids but not dissolved nutrients, anaerobic digestion generates digestate with a high nitrogen load without eliminating pathogens, drying tunnels consume large amounts of energy without treating the liquid effluent, nitrification-denitrification requires intensive technical control and chemical reagents, and composting only manages the solid fraction— the wetland system integrates the entire treatment cycle from source.
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We do not have the required information, but we have the following data that may be useful in this section. Energy consumption in a constructed wetland system is mainly associated with three pieces of equipment: (i) Agitation of raw slurry in the homogenization tank to prevent sedimentation (equipment rated between 5.5–15 kW, depending on the volume to be homogenized); (ii) Feed pump and operation of the phase separator (throughput ranging from 2 m³/h to 10 m³/h, with a motor of 1.5 kW); (iii) Transfer pumps for wetland cell filling and effluent recirculation (three-phase pumping equipment, 380V / 50Hz, with a 0.75 kW motor).
As mentioned in section 5.4.1, the integrated treatment system (phase separation, decantation, constructed wetlands) achieved a 50% reduction in NH₃ emissions from raw pig slurry to purified effluent. Physical removal of nitrogen loads combined with biological processes in wetlands limits ammonia volatilization, demonstrating effective mitigation of gaseous emissions and sustainable livestock waste management.
Based on experimental data recorded in different seasons for the fractions of raw slurry, settled slurry, and treated slurry (drying pond), the average values of nitrogen in the form of nitrate (NO₃⁻ x 0.226 = N-NO₃⁻) and nitrite (NO₂⁻ x 0.3043 = N-NO₂⁻) are:
• Raw slurry: N-NO₃⁻: 1.6 – 6.1 mg/L; N-NO₂⁻: <0.021 – 0.77 mg/L
• Settled slurry: N-NO₃⁻: 1.9 – 6.3 mg/L; N-NO₂⁻: <0.021 mg/L
• Treated slurry: N-NO₃⁻: 3.9 – 5.8 mg/L; N-NO₂⁻: <0.021 mg/L
These values do not derive directly from the applied technique but rather reflect natural processes of the nitrogen cycle, where the NH₃ present in the slurry is biologically oxidized to N-nitrate and N-nitrite. This is an expected phenomenon in passive biological treatment systems such as constructed wetlands.
Total Nitrogen average values:
Raw slurry: 2.13 – 1.37 g/L
Settled slurry: 1.47–1.08 g/L
Purified slurry: 1.05 – 0.59 g/L
Total Phosphorus average values:
Raw slurry: 170 – 30 mg/L
Settled slurry: 40-5 mg/L
Purified slurry: 10 – 1 mg/L
As a clarifying example, one of the full-scale pilot farm has approximately 2750 places for breeding sows and 232 places for replacement sows. Based on RD 306/2020 (Royal Decree 306/2020, of February 11, establishing basic standards for the management of intensive pig farms, and amending the basic regulations for the management of extensive pig livestock farms), these generate a total annual production of liquid and semi-liquid manure of 14605 m³ (14025 m³ correspond to sows with piglets of 0-6 kg and 580 m³ to replacement sows), assuming a density close to 1000 kg/m³ according to experimental data.
Raw slurry (untreated) is considered the "zero treatment" scenario and serves as the baseline against which the system's efficiency is compared. Its average total nitrogen (TN) concentration is 2,13 g/L, representing an annual load of 31,11 tons of TN.
Following integral treatment (solid-liquid separation, settling, and wetlands), the volume of purified slurry is reduced to 11684 m³ (a 20% decrease in total volume), with a TN concentration of 1,05 g/L, equivalent to 12,27 tons per year.
Industrial symbiosis resource flow:
The main benefit of the synergy lies in the circularity of the resource's nutrients, utilizing it both as a fertilizer and as a water source.
In 2022, the investments required to implement an integrated treatment system with constructed wetlands for a 2000-head farrowing farm amounted to €193500. This included the installation of the phase separator (€51500, corresponding to its assembly, platform, cover, and excluding the equipment), the construction of the decanters with a mobile cover (€30000), and the construction of 15 constructed wetlands with vegetation (€90000). Annual operation and maintenance costs totaled €31561, corresponding to labor (€9091), electricity consumption (€2240), spare parts and maintenance (€4000), and depreciation (€16230), for an annual treated volume of 14605 m³. The maintenance cost of the integrated constructed wetland system was €2.16/m³.