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Article

Treatment of Dairy Farm Runoff in Vegetated Bioretention Systems Amended with Biochar

by
Md Yeasir A. Rahman
,
Nicholas Richardson
,
Mahmood H. Nachabe
and
Sarina J. Ergas
*
Department of Civil & Environmental Engineering, University of South Florida, Tampa, FL 33620, USA
*
Author to whom correspondence should be addressed.
These authors contributed equally to this work.
Water 2024, 16(10), 1347; https://doi.org/10.3390/w16101347
Submission received: 13 April 2024 / Revised: 4 May 2024 / Accepted: 6 May 2024 / Published: 9 May 2024
(This article belongs to the Section Wastewater Treatment and Reuse)

Abstract

:
Nitrogen and fecal indicator bacteria (FIB) in runoff from concentrated animal feeding operations (CAFOs) can impair surface and groundwater quality. Bioretention systems are low impact nature-based technologies that can effectively treat CAFO runoff if modified with an internal water storage zone (IWSZ) or amended with biochar. In this study, the performances of four pilot-scale modified bioretention systems were compared to assess the impacts of (1) amending bioretention media with biochar and (2) planting the systems with Muhlenbergia. The system with both plants and biochar amendment had the best performance, with an average of 5.58 log reduction in E. coli and 98% removal of total nitrogen (TN). All systems treated the first pore volume well as new runoff flushed the treated water from the IWSZ. Biochar improved TN and FIB removal due to its high capacity to adsorb or retain ammonium (NH4+), dissolved organic nitrogen, dissolved organic carbon, and E. coli. Planting improved performance, possibly by increasing rhizosphere microbial activity.

1. Introduction

Runoff from concentrated animal feed operations (CAFOs) carries organic matter, suspended solids, nutrients (nitrogen [N] and phosphorus [P]), and pathogens that can impair surface and ground water quality [1,2]. These contaminants can cause eutrophication, fish deaths, economic losses, and nitrate (NO3) and pathogen contamination of drinking water supplies [3]. When used for irrigation, runoff from CAFOs has also been shown to contaminate vegetable crops with fecal indicator bacteria (FIB) [4]. For example, groundwater polluted by livestock wastes was responsible for contaminating vegetable crops with E. coli O157: H7, which is associated with food-borne illnesses [5]. Although FIBs, such as E. coli and Enterococci, are usually not pathogenic, their presence indicates potential fecal contamination of water [6].
Nature-based solutions (NBSs) for CAFO runoff include vegetated buffer strips, bioretention systems, lagoons, and constructed wetlands. These technologies are designed to remove organic matter and suspended solids from runoff; however, they often have low removal rates for dissolved nutrients due to high loading rates and limited hydraulic retention times [7]. Additionally, NBSs are not designed with alternating aerobic/anaerobic zones that promote biological nitrification and denitrification processes. Ibekwe et al. [8] reported that constructed wetlands removed only 16% of ammonium (NH4+), 25% of total nitrogen (TN), and 33% of phosphate (PO4−3). Similarly, increases in total kjeldahl nitrogen and chemical oxygen demand concentrations and leaching of nitrate (NO3) (11–45 mg/L) were observed in vegetated buffer strips due to insufficient nitrification/denitrification [9].
A wide range of removal efficiencies have been reported for FIBs in NBSs. For example, in California’s San Joaquin Valley (USA), log E. coli reductions ranged from 0.51 to 1.30 for four wetlands treating irrigation runoff [10]. Similarly, minimal retention of FIB (0.16 log removal) was observed for vegetative buffer strips treating dairy runoff [11]. Rusciano and Obropta [12] investigated the effectiveness of sand bioretention systems for the treatment of manure slurry runoff and found 0.37–2.7 log fecal coliform reductions of over 13 simulated runoff events. Although several studies have separately investigated FIB or nitrogen removal in NBSs, there is a lack of research comprehensively investigating both FIB and nitrogen removal in NBSs treating CAFO runoff.
Bioretention systems are a type of NBS consisting of a shallow depression containing the following layers of engineered porous media (top to bottom): (i) topsoil, mulch, or compost as surface layer with or without plants; (ii) sand or sand with alternative filtration medium; and (iii) a gravel drainage layer. A modified bioretention system design includes a saturated internal water storage zone (IWSZ), which is created using an elevated outlet pipe [13]. The IWSZ promotes the development of anoxic conditions to facilitate denitrification. For carbon limited runoff, an electron donor, such as woodchips or elemental sulfur pellets, may be added to the IWSZ [14] to enhance both nitrogen and FIB removal [13,15].
A wide variability in FIB removals has been reported for bioretention systems (conventional and/or modified) [16,17,18]. E. coli removal in bioretention systems is influenced by attachment, straining, predation, competition, and die-off [19,20]. Attachment is impacted by media properties and surface characteristics, FIB microbiology, and physico-chemical properties of the suspending fluid (e.g., pH and ionic strength), whereas straining is controlled by the pore and particle sizes of the porous medium [18,21,22,23]. Conventional sand media has a low specific surface area (SA) (0.1 m2/g) [24] and narrow pore size distribution (10–150 µm) [25]. Therefore, amendment of sand with a material having a high SA and micro-porous structure could enhance FIB removal [26].
Biochar is a low-cost carbon-rich by-product of the pyrolysis of waste organic feedstocks, such as wood or animal waste, under oxygen-limited conditions. In crop studies, biochar amendment has been shown to help retain soil moisture, nutrients, and organic carbon and to enhance microbial activity, nitrogen fixation, and plant growth [27,28]. These improvements are due to the high cation exchange capacity (CEC), SA, and microporous structure of biochar.
Several prior studies have investigated biochar amendment of bioretention systems to enhance N removal. Rahman et al. [26] found that the high CEC of biochar increased NH4+ retention in bioretention columns treating urban runoff. Adsorbed NH4+ was oxidized to NO3 when aerobic conditions were present during the antecedent dry period (ADP) between runoff events. Berger et al. [29] found that biochar improved denitrification in woodchip biofilters used for stormwater treatment by reducing dissolved oxygen concentrations and increasing biomass density and water retention. Although biochar amendment improved nitrogen removal in modified bioretention systems treating urban runoff [26,30,31], there is limited information on its ability to enhance CAFO runoff treatment, where FIB and nitrogen concentrations can be an order of magnitude higher. In a prior study by our group [32], we investigated the effect of biochar type, biochar fraction, hydraulic loading rate (HLR), and ADP on nitrogen and organic carbon removal in laboratory columns treating CAFO runoff. However, this study did not include an IWSZ or plants and did not comprehensively analyze both FIB and nitrogen removal.
Prior research is conflicted about the effect of embedded vegetation on nutrient and FIB removal in bioretention systems [33,34,35,36]. Chandrasena et al. [37] found that vegetation had a net negative effect on E. coli survival in biofilters. Conversely, Skorobogatov et al. [38] stated that plant roots can negatively impact the media by forming macropores, preferential flow paths, and non-uniform breakthrough, leading to poorly treated runoff. Parker et al. [39] suggested that plants indirectly affected FIB removal, by influencing infiltration rate. Interactions between filtration medium and plants play an important role in water quality [40]. In constructed wetlands, the role of plant-root-associated microbes promote N transformation processes and the secretion of antimicrobial products for pathogen removal [41]. Biochar addition has been shown to dramatically increase plant biomass growth (by a factor of 24) in constructed wetlands systems treating landfill leachate, which contributes to nutrient uptake and rhizosphere microbial activity [42]. However, no prior studies have investigated the effect of vegetation on nutrient and FIB removal in modified bioretention systems amended with biochar.
The overall goal of this research was to comprehensively investigate the effect of biochar and plants on FIB and nitrogen removal in modified bioretention systems treating CAFO runoff. The specific objectives were to test pilot-scale modified bioretention units for their performance in FIB and nitrogen removal under varying ADPs (1) with and without biochar amendment and (2) with and without vegetation. This is the first study to investigate the use of modified biochar amended bioretention systems for managing both nutrients and FIB in CAFO runoff.

2. Materials and Methods

2.1. Porous Medium

Sand was purchased from Seffner Rock and Gravel (Tampa, FL, USA). The sand had a hydraulic conductivity of 13 cm/h, which was within the range suggested for bioretention systems [43]. It had a porosity (n) of 35% ± 0.95, moisture content at field capacity of 23.24% ± 0.96 (by wt.%), and a bulk density of 1.56 ± 0.14 g/cc. The sand contained 0.27% coarse-grain (>1 mm), 9.5% medium-grain (1−0.6 mm), and 90% fine-grain (0.6−100 μm) particles [44].
Biochar used in this study was donated by Biochar Supreme (Everson, WA, USA). The biochar was derived from wood that was pyrolyzed at 900–1000 °C and had a SA of 537 ± 60.15 m2/g and a CEC of 10.57 cmol/kg. It had a low bulk density (0.10 g/cm3) and high water-holding capacity (874 gH2O/100 g biochar). The high pore volume of 0.36 cm3/g included 0.19 cm3/g micro-pore volume and 0.15 cm3/g meso-pore volume. Additional characteristics of the biochar can be found in Rahman et al. [26].

2.2. Semi-Synthetic Dairy Runoff

Fresh dairy manure was collected from South Tampa Farm (Tampa, FL, USA). The manure was mixed with stormwater from Lake Benke, a stormwater pond on the University of South Florida Campus (Tampa, FL, USA). The solution was allowed to settle overnight, after which the supernatant was screened through a 0.25 mm mesh and stored until use. Semi-synthetic dairy runoff was prepared by mixing 60% of the screened supernatant with 40% additional pond water. The target concentrations for N-species were 35 mg/L NH4+-N, 1.0 mg/L NOx-N, and 45 mg/L dissolved organic nitrogen (DON). Concentrations of FIBs were 8.63 × 106 ± 7.07 × 106 CFU/100 mL for E. coli and 5.43 × 106 ± 4.14 × 106 CFU/100 mL for Enterococci. These values were consistent with concentrations observed in prior field studies of CAFO runoff [14,45,46,47].

2.3. Pilot-Scale Bioretention Systems

Four pilot-scale modified bioretention systems were constructed in cylindrical polyethylene containers with a 77 cm diameter and a 100 cm height (Figure 1), containing (i) sand (S), (ii) sand with plants (S+P), (iii) biochar-amended sand (BC), and (iv) biochar-amended sand with plants (BC+P). A perforated PVC underdrain pipe with an upturned outlet elbow was used to create an IWSZ in each unit. From the bottom up, the units contained (i) 7.6 cm downgraded white river gravel (0.3 cm), (ii) 30.5 cm IWSZ filter medium, (iii) 46 cm unsaturated zone filter medium, (iv) 2.5 cm gravel (1.3 cm), and (v) 15 cm free board as a ponding layer at the top. For the S and S+P units, the IWSZ and unsaturated zone media consisted of the sand described above. Both sand and biochar were freshly collected prior to construction. For the BC and BC+P units, the IWSZ contained sand amended with biochar at a 45% fraction (by volume), and the unsaturated zone contained sand with biochar at a 35% fraction (by volume). Biochar fractions were selected to optimize water quality improvements without damaging hydraulic performance, based on results from our prior research [32]. A filter fabric was placed in between the drainage layer and IWSZ layer to avoid wash-out of fine particles. Note that the IWSZ did not contain wood chips due to the high dissolved organic carbon content (737 ± 200 mg/L) of the dairy runoff, which could promote denitrification.
S+P and BC+P units were planted with Muhlenbergia capillaris (Muhly Grass), which was purchased from a local nursery. Muhlenbergia capillaris is a native Florida perennial, that attracts wildlife and has favorable light and moisture requirements, growth rate, and mature plant density and spread. Each system had one Muhlenbergia, resulting in a plant density of one plant/1.2 m2. After planting, the systems were watered with stormwater pond water periodically for three months to promote the growth of roots and biomass before performing dairy runoff experiments. After acclimation, seven semi-synthetic dairy runoff events were studied with varying ADPs between 2 and 21 days. During each event, all four systems were fed semi-synthetic dairy runoff at an HLR of 0.05 cm3/cm2/min (flow rate of 3.7 mL/s). In Events 1–5, the systems were fed runoff for a duration of 240 min, with a total influent flow volume of 0.89 L. In Events 6 and 7, the systems were fed runoff for a duration of 240 min, with a total influent flow volume of 1.0 L. Influent and effluent samples were collected every 15 to 30 min over the duration of the events.

2.4. Water Quality Analysis

E. coli were enumerated in duplicate at three dilutions using the EPA Method 1603 membrane filter method with modified membrane-thermotolerant Escherichia coli agar (m-TEC) [48]. Dilutions for microbial enumeration were performed in phosphate-buffered saline solution.
An Orion 5-Star meter (Thermo Scientific, Beverly, MA, USA) was used to measure pH and conductivity following Standard Methods 2510 B [49]. NH4+ and NOx (NO3-N + NO2-N) were measured using a Timberline Ammonia Analyzer (Timberline Instruments, Boulder, CO, USA). TN was measured using a Shimadzu TOC-V CSH TOC/TN Analyzer (Shimadzu Scientific Instruments, Columbia, MD, USA). DON was calculated by subtracting total inorganic nitrogen (TIN = NH4+ + NOx) from TN. Method-detection limits for NH4+, NOx, and TN were 0.05 mg/L, 0.05 mg/L, and 0.03 mg/L, respectively. Effluent flow rates were measured gravimetrically to assess hydraulic performance and calculate pollutant mass-load reductions.

2.5. Data Analysis

Concentrations of E. coli in feed solutions were measured at the start and end of each experiment to confirm that growth/death did not occur in the feed tanks during the experimental period. Log removal values were calculated using
E .   c o l i   logremoval = logC / C 0
where C0 and C are the influent and effluent concentrations, respectively.
Mass removals of TOC, NH4+, DON, NOx, and TN (RTOC, RNH4+, RDON, RNOx, and RTN) were calculated using
R x = 1 N C 0 V 0 CV C 0 V 0 N × 100 %
where N is the total number of effluent samples, C0 and C are the influent and effluent concentrations (mg/L), and V0 and V are the influent and effluent volumes (L). Duplicate influent samples were collected at the beginning of each event and C0 concentrations were assumed to remain constant over each runoff event.
Statistical analysis was conducted using JMP 16.0.0 (SAS Institute, Cary, NC, USA). One-way analysis of variance (ANOVA) with a significance threshold set at 95% (p = 0.05) was used to determine statistically significant differences between the datasets. Note that due to differences in water retention, the time for effluent to discharge from the units varied. Therefore, the total number of samples (n) collected within the first 90 min varied between systems. For statistical tests between systems, n values for BC, BC+P, S, and S+P were 54, 57, 59, and 56, respectively.

3. Results and Discussion

3.1. Hydraulic Performance

The average influent and effluent flow rate for each system during each storm event is shown in Figure 2. The influent was fed at a steady HLR of 0.05 cm3/cm2/min (flow rate = 3.7 mL/s) during each event, resulting in ponding at the top of the bioretention systems followed by slow drainage. The total effluent flow volumes observed from each event for each system are shown in Figure S2. Note that moisture losses between events are affected by both the presence of plants, which increase evapotranspiration, and the ADP (Figure 2). However, if moisture losses are disregarded, the difference between the influent and effluent flow rate gives the average rate of head build-up over time in the ponding layer. A lower flow rate implies slower infiltration through the medium, therefore a longer hydraulic residence time.
The hydraulic performance of the biochar-amended system that was planted with Muhlenbergia (BC+P) remained consistent through all seven events, while the performance of the other systems steadily declined over time. Although changes in hydraulic conductivity were not measured over time, plant roots have been shown to increase soil hydraulic conductivity [50]. Muhlenbergia has an extensive root system, which can provide additional flow pathways and pore space, potentially increasing the permeability and infiltration capacity of the media. Additionally, the sand and biochar mixture had a greater fraction of coarse- and medium-grained particles compared to sand alone. Although, Koivusalo et al. [51], reported that biochar amendment had no impact on the hydrologic performance of biofilters, Brown and Hunt [52] found that fine particles caused clogging and a reduction in permeability in modified bioretention systems. Results from these studies highlight the need to remove fine particles in bioretention media prior to construction.
Excessive ponding and piling of water can diminish the feasibility of these systems in practice. Since the hydraulic head builds up over time, longer or more extreme storm events can lead to overflowing and poorly treated runoff. While overflow did not occur during these studies, additional research is necessary to understand the long-term feasibility of these systems under varying HLRs. In contrast, longer retention times due to low effluent flow rates can improve FIB and N removal, which is discussed further below.

3.2. Fecal Indicator Bacteria Removal

Average E. coli log removals for the pilot-scale systems are shown in Table 1. In order to elucidate removal mechanisms, log removals are shown as each “pore volume” (PV) of dairy runoff flushed through the system. The highest log E. coli removals were observed as the first PV exited the systems. This represented the water that was stored in the IWSZ during the ADP between stormwater applications, in which die-off was the major removal mechanism. Long retention times in the anoxic IWSZ over the ADP could have resulted in high E. coli die-off, explaining the best treatment performances during the first PV. After one PV, log E. coli removals reveal the systems’ treatment during an event, when straining and attachment are the major removal mechanisms. Since lower log E. coli removals were observed after multiple PVs, larger runoff events will have poorer overall treatment.
As shown in Table 1, the best performance was observed in the bioretention system with both biochar and plant presence (BC+P). Note that plant presence only significantly improved performance when the system was amended with biochar. The quantity of microorganisms living in the rhizosphere is several orders of magnitude higher than that in bulk soils [53]. Plants can improve FIB die-off through predation and competition by rhizosphere microbes or inactivation by antimicrobial compounds from root exudates [54]. It is well known that the addition of biochar to soil aids in plant growth by retaining nutrients and providing a good habitat for beneficial microbes in the rhizosphere [55,56]. More biomass growth was observed in the BC+P system than the S+P system, as shown in Figure S1. The symbiotic relationship between plant presence and biochar amendment for biofilm and plant growth enhanced E. coli die-off.
Plant roots have been shown to increase FIB transport in some studies by creating preferential flow paths through the media [57]. This may explain the slight decrease in FIB removal when Muhlenbergia was planted in sand media (Table 1). Even though the effluent flow rates of S and S+P systems were similar (Figure 2), preferential flow paths may have caused a greater fraction of the influent from the S+P system to bypass the media. The S+P system only decreased in performance after two PVs, which indicates treatment processes occurring during the runoff event rather than during the ADP. Therefore, these results suggest that plant presence decreased E. coli straining and attachment in the sand only medium. The addition of Muhlenbergia improved FIB die-off, yet preferential flow pathways led to a decrease in attachment and straining. Without biochar amendment to promote attachment and enhance plant growth, the addition of Muhlenbergia led to a poorer overall treatment.
Overall, FIB removal performance was improved with biochar amendment, even without the presence of plants. The BC system had higher average log E. coli removals than the S system for all PVs, suggesting that biochar increased die-off, attachment, or straining of E. coli. Biochar’s ability to increase overall microbial biomass in the IWSZ [29] may have led to more competition with E. coli during the ADP. During the storm event, the high SA and biochar surface chemistry could have resulted in a greater affinity for E. coli attachment. A similar study by Mohanty and Boehm [58] at significantly lower influent E. coli concentrations suggested that biochar has a high affinity for E. coli attachment from biochar-amended sand filters treating urban runoff.
Although this study did not compare bioretention systems with and without an IWSZ, data were compared with our prior research [44] where the same CAFO runoff was treated in sand- and biochar-amended columns without an IWSZ. The modified systems with an IWSZ achieved a 40% higher E. coli removal for experiments conducted at the same ADP and HLR [44]. Similarly, Liu et al. [15] found a significant increase in E. coli removals when an IWSZ was included in bioretention systems treating stormwater runoff. The presence of an IWSZ lengthens the retention times and creates anoxic conditions that favor E. coli die-off. In a recent review study by Biswal et al. [59], a range of 0.78–4.23 log removals were reported from biochar-amended bioretention systems treating urban runoff. Although differences in influent concentrations, loading rates, and system design directly impact E. coli removal, the results in this study show promising improvements in FIB removal in systems treating CAFO runoff.

3.3. Nitrogen Removal

The average influent TN concentration of the semi-synthetic dairy farm runoff was 71.3 ± 18.7 mg N/L, consisting of 28.3 ± 7.69 mg N/L of NH4+, 43.4 ± 19.4 mg N/L of DON, and negligible NOx. The average influent TOC concentration of the runoff was 636 ±270 mg/L. Removal efficiencies of TN, NH4+, DON, and TOC for the four modified bioretention systems are shown in Figure 3. Effluent NOx concentrations are shown in Figure 4 rather than as removal efficiencies since influent concentrations were below detection limits. Effluent NH4+ and TN concentration profiles over time for the four bioretention systems for a 4.5 h storm event (Event 5) are shown in Figure 5 and Figure 6.
Median TN removals of >90% were observed in the biochar-amended systems, with the highest TN removal in the BC+P system at 98.5%. These removal efficiencies were higher than the typical range of TN removal for biochar-amended bioretention systems treating urban runoff (32–61%) [59]. Higher influent TN concentrations in the CAFO runoff most likely led to higher removal efficiencies. A regression analysis was carried out with average TN, TOC, and log E. coli removals for each runoff event vs. event number (see Figures S3–S5). TN removal was negatively correlated with event number (and therefore time) in the S (R2 = 0.88) and S+P (R2 = 0.92) systems; however, TN removal efficiency remained fairly constant in the BC (R2 = 0.63) and BC+P (R2 = 0.41) systems. There was no significant correlation of any other water quality parameter with event number. The results indicate that biochar addition helps to maintain TN removal performance over time in modified bioretention systems treating CAFO runoff.
Significantly higher NH4+ removals were observed in biochar-amended systems compared with un-amended systems (Figure 3B). The highest (92.5% ± 4.28) and lowest (65.7% ± 24.5) removal efficiencies were observed in BC+P and S systems, respectively. NH4+ removal mainly depends on (i) media adsorption, (ii) nitrification, and (iii) plant uptake. As shown in Figure 4, the S+P system had lower effluent NH4+ concentrations compared with the S system during the first 90 min. The lower initial NH4+ concentrations in the plant-amended systems suggests that plants and/or rhizosphere microbes assimilated NH4+ retained in the media during the ADP. Once the pore water in the IWSZ flushed through the S+P system (90–270 min), effluent NH4+ concentration gradually increased and was almost equivalent to concentrations in the S system by the end of the event. Both biochar-amended systems had significantly lower effluent NH4+ concentrations than the unamended systems (Figure 3B), suggesting that NH4+ was adsorbed to biochar in the unsaturated zone. In our previous laboratory-scale study with unmodified biofilters, the high CEC of biochar was able to increase NH4+ retention during the application period, resulting in higher nitrification activity during the oxic period between storm events [32].
As shown in Figure 5 and Figure 6, effluent NH4+ and TN concentrations followed similar breakthrough trends. With low effluent TN concentrations from 0–90 min, the effluent N from the S+P unit consisted mostly of DON (Figure 3C) or NOx (Figure 4). DON removal largely depends on either adsorption or ammonification followed by nitrification. As biochar enhances soil microbial activity due to its high surface area and porosity [60], enhanced adsorption and ammonification resulted in significantly higher average DON (<99%) removals in the BC and BC+P systems.
Significantly lower effluent NOx concentrations were observed for biochar-amended systems compared to sand systems, as shown in Figure 4. As influent dairy runoff had high organic carbon content, it was hypothesized that TOC retained in the IWSZ due to adsorption onto biochar was utilized as an electron donor for denitrification. Significantly higher TOC removals were also observed in the systems amended with biochar (Figure 3D). In a similar study on bioretention systems treating commercial nursery runoff, biochar was found to increase NO3 removal, yet this study relied on woodchips as the carbon source, rather than adsorbed TOC [61]. In the S and S+P systems, a lack of adsorbed TOC in the IWSZ likely limited denitrification.
For all N-species, systems with plants achieved higher removal efficiencies compared to systems without plants (Figure 3). Prior research with planted and unplanted bioretention systems also showed that both NH4+ and NO3 are taken up by plants [62,63]. Denitrification is also favored by enhanced microbial activity and the availability of organic carbon in the rhizosphere due to the presence of root exudates and sloughed-off root tissues [64]. Planting the systems with Muhlenbergia increased median TN removals by an average of 7.5% due to enhanced microbial activity in the rhizosphere and plant uptake.

4. Conclusions

Fecal indicator bacteria (FIB) and N removal mechanisms were investigated in modified bioretention systems used for the treatment of dairy farm runoff, with and without biochar and with and without plants. Biochar increased FIB removal, most likely due to its high SA and affinity for E. coli attachment. The highest FIB removals were observed as the first flush of water retained in the IWSZ exited the systems and then declined over time as the biochar surface reached its adsorption capacity. The high SA and CEC of biochar also enhanced NH4+ and DON removal during infiltration, which facilitated ammonification and nitrification during the ADP. Higher TOC adsorption in the IWSZ in systems containing biochar favored denitrification, resulting in higher TN removal. Plants improved both FIB and TN removals in biochar-amended systems, most likely by increasing rhizosphere microbial activity and assimilation, facilitating predation and competition leading to FIB die-off and enhancing biological N removal mechanisms. This is the first study showing that biochar-amended bioretention systems treating CAFO runoff can effectively remove high loads of TN and FIB.

Supplementary Materials

The following supporting information can be downloaded at https://www.mdpi.com/article/10.3390/w16101347/s1: Figure S1: Photographs of the two planted pilot-scale bioretention systems after 12 runoff experiments: (a) S+P system and (b) BC+P system. Figure S2: effluent flow volumes for each event. Figures S3–S5: Regression analysis of water quality data vs. event. Table S1: List of acronyms.

Author Contributions

Conceptualization, M.Y.A.R., M.H.N. and S.J.E.; methodology, M.Y.A.R., S.J.E. and M.H.N.; formal analysis, M.Y.A.R. and N.R.; investigation, M.Y.A.R.; resources, M.H.N. and S.J.E.; data curation, M.Y.A.R.; writing—original draft preparation, M.Y.A.R. and N.R.; writing—review and editing, M.H.N. and S.J.E.; visualization, M.Y.A.R. and N.R.; supervision, M.H.N. and S.J.E.; project administration, M.H.N. and S.J.E.; funding acquisition, M.H.N. and S.J.E. All authors have read and agreed to the published version of the manuscript.

Funding

This material is based upon work supported by the Florida Department of Agriculture and Consumer Services Office of Agricultural Water Policy (Contract Number 025851) and the National Science Foundation (NSF) under Grant No. 1930451.

Data Availability Statement

Datasets are available on request from Sarina J. Ergas ([email protected]).

Acknowledgments

The authors would like to acknowledge Nicolas Truong and Steve Youssef and the staff at the University of South Florida Botanical Gardens for their assistance with this project.

Conflicts of Interest

The authors declare no conflicts of interest.

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Figure 1. Schematic diagrams of (left to right) sand-modified bioretention cell with plants (S+P), sand-modified bioretention cell (S), biochar-amended modified bioretention cell with plants (BC+P), and biochar-amended modified bioretention cell (BC). Units are in cm.
Figure 1. Schematic diagrams of (left to right) sand-modified bioretention cell with plants (S+P), sand-modified bioretention cell (S), biochar-amended modified bioretention cell with plants (BC+P), and biochar-amended modified bioretention cell (BC). Units are in cm.
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Figure 2. Average influent and effluent flow rates (mL/s) from each system during each runoff event. The antecedent dry period (ADP) for each event is shown in parentheses.
Figure 2. Average influent and effluent flow rates (mL/s) from each system during each runoff event. The antecedent dry period (ADP) for each event is shown in parentheses.
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Figure 3. Box and whisker plots of N-species and TOC removal efficiencies for events 1–7: (A) TN, (B) ammonium (NH4+), (C) DON, and (D) TOC. Labels with different letters show statistically significant differences in mass removals.
Figure 3. Box and whisker plots of N-species and TOC removal efficiencies for events 1–7: (A) TN, (B) ammonium (NH4+), (C) DON, and (D) TOC. Labels with different letters show statistically significant differences in mass removals.
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Figure 4. Effluent NOx concentrations for Events 1–7 (outliers excluded). Mean values are displayed above each box. Labels with different letters represent statistically significant differences in effluent concentrations.
Figure 4. Effluent NOx concentrations for Events 1–7 (outliers excluded). Mean values are displayed above each box. Labels with different letters represent statistically significant differences in effluent concentrations.
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Figure 5. Pollutant breakthrough curve for NH4+ for four modified bioretention systems during Event 5.
Figure 5. Pollutant breakthrough curve for NH4+ for four modified bioretention systems during Event 5.
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Figure 6. Pollutant breakthrough curve for TN for four modified bioretention systems during Event 5.
Figure 6. Pollutant breakthrough curve for TN for four modified bioretention systems during Event 5.
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Table 1. Average log E. coli removals for each system over different PVs. For each column, values with different letters represent statistically significant differences.
Table 1. Average log E. coli removals for each system over different PVs. For each column, values with different letters represent statistically significant differences.
Average Log Removals *
SystemPV ≤ 1 (Time ≤ 90 min)1 < PV ≤ 2 (90 min < Time ≤ 180 min)PV > 2 (Time > 180 min)Total
BC5.25 ± 1.81 (a, b)3.64 ± 1.58 (b)3.96 ± 2.02 (a, b)4.24 ± 2.09 (b)
BC+P6.22 ± 1.65 (a)5.55 ± 2.19 (a)4.82 ± 2.31 (a)5.58 ± 1.89 (a)
S4.60 ± 1.93 (b)3.84 ± 1.69 (b)3.50 ± 1.59 (b)4.03 ± 1.79 (b)
S+P4.84 ± 2.20 (b)3.95 ± 2.05 (b)3.02 ± 1.71 (a, b)3.99 ± 2.11 (b)
Notes: * For statistical tests between pore volumes, n values varied according to the following: PV < 1, n = 17 (BC), 20 (BC+P), 22 (S), 19 (S+P); 1 < PV ≤ 2, n = 21 for all systems; PV > 2, n = 16 for all systems.
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Rahman, M.Y.A.; Richardson, N.; Nachabe, M.H.; Ergas, S.J. Treatment of Dairy Farm Runoff in Vegetated Bioretention Systems Amended with Biochar. Water 2024, 16, 1347. https://doi.org/10.3390/w16101347

AMA Style

Rahman MYA, Richardson N, Nachabe MH, Ergas SJ. Treatment of Dairy Farm Runoff in Vegetated Bioretention Systems Amended with Biochar. Water. 2024; 16(10):1347. https://doi.org/10.3390/w16101347

Chicago/Turabian Style

Rahman, Md Yeasir A., Nicholas Richardson, Mahmood H. Nachabe, and Sarina J. Ergas. 2024. "Treatment of Dairy Farm Runoff in Vegetated Bioretention Systems Amended with Biochar" Water 16, no. 10: 1347. https://doi.org/10.3390/w16101347

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