In total, four biobed-biopurification systems (BBPS) were made for treating the wastewater: BBPS1, BBPS2, BBPS3 and BBPS4, and the substrates used in biobeds were rice husk, soil, vermicompost, gravel and sand as an adsorbent in different proportion according to the design and treatment needs. Five litres of primary treated effluent were provided to every setup and the effluents were analysed after different retention intervals, i.e., 0 h, 24 h, 48 h and 72 h for different physio-chemical properties. The findings of the experiment showed that the BBPS1, BBPS2, BBPS3 and BBPS4 was highly efficient to remove organic impurities but much less efficient to eliminate physical impurity. Much faster removal of the pollutants was achieved in the BBPS1 and BBPS2 in comparison to BBPS3 and BBPS4. Both the beds BBPS1 and BBPS2 created favourable circumstances for organic contaminants to biodegrade as for biological oxygen demands (BOD) removal efficiency was 55.35% and 56.44% and chemical oxygen demands (COD) removal efficiency was 85.15% and 70.90%, respectively. Both the setups, i.e., BBPS1 and BBPS 2 are also much more efficient for the removal of biogenic contaminants, i.e., 85.71% and 73.20% for nitrate and 65.12% and 76.99% for phosphate, respectively. Overall, the performance of BBPS2 proved excellent in comparison to other setups by calculation of its removal efficiency percent for different parameters.

  • Natural treatment systems were tested for the treatment of sewage water.

  • Mechanism includes adsorption, microbial breakdown, and phytoaccumulation.

  • BBPS1 and BBPS2 are more efficient compared to BBPS3 and BBPS4.

  • Canna indica has demonstrated significant efficiency in the removal of pollutants.

Domestic wastewater is one of the major threats to water resources in India (CPCB 2015). As reported by Central Pollution Control Board (CPCB) India, there is a notable difference between the total quantity of wastewater produced, which is 61,754 million litre per day (m3/d)(106 L d−1), and the total volume of wastewater discharged after treatment, which is 2,2963 m3/d. Consequently, a substantial volume of untreated sewage (38,791 m3/d) is discharged into aquatic environments. Considering a low probability of thorough treatment for wastewater, it is predicted that by 2051, rural as well as urban India will produce 50,000 m3/d and 120,000 of sewage, respectively (Shukla et al. 2021). India's rural population lacks wastewater treatment facilities, and hence, in the current environment, developing a sewage treatment plant for all of the country's rural population is economically unsustainable. As a result, sewage is immediately released into the environment without any processing, which leads to water pollution, thus decreasing the amount of freshwater (CPCB 2015).

On the other hand, as farming has grown tremendously over the past few years in order to meet the need for food and as a means of subsistence, for a growing number of people, enormous quantities of organic materials have been produced. Globally, rice husk material, a by-product of rice milling operations, is a major agricultural waste generated nowadays (Tu Nguyen et al. 2022). India as an agricultural country generates a significant amount of rice husk annually, and burning is the easiest preferred way to get rid of this kind of waste. Because rice husk burning releases a lot of carbon dioxide and carbon monoxide, it is quite dangerous. As per Mor et al. (2016), rice husk accounts for one-fifth of the world's rice production, or around 545 million metric tons, and India generates between 18 and 22 million tons of rice husk annually (Patel et al. 2022). Consequently, as a way to decrease this waste's impact on the natural environment, proper management is required. Because of its lack of economic value, rice husk reduction during rice processing poses problems with waste disposal. Similarly, because of its low density, managing and transferring rice husk ash is also challenging. When rice is processed, a large portion of it undergoes burning or is dumped as waste. As an alternative, rice husk can be burned in brick kilns to provide fuel and as building materials (Pushpakumara & Mendis 2022). Several investigators use different forms of rice husk for the treatment of contaminants including textile dyes and other organic chemicals. Numerous dyes, such as Methylene Blue (Alver et al. 2020), Crystal Violet (Homagai et al. 2022), Brilliant Vital Red (Rehman et al. 2011), Direct Red-31 and Direct Orange-26, Congo Red (Shaban et al. 2017) and Safranin-T (Gun et al. 2022) were adsorbed by rice husk, rice bran, and rice ash. Few studies have been focused now on the use of agricultural waste, i.e., rice husk as an adsorbent in combination with other filter media in the treatment of domestic sewage (Jóźwiakowski et al. 2018). While many media have been employed to detoxify wastewater, agricultural waste has received very little attention, especially rice husk, soil and vermicompost, in combination with constructed wetland media, i.e., gravel and sand (Cizeikiene et al. 2018) in biobed–biopurification systems (BBPSs).

Adsorption by various media (biomixture, gravel, and sand), decomposition by microbial activity, and phytoaccumulation by plant uptake are the main methods of treatment in BBPSs (Singh et al. 2021, 2022; Pérez-Villanueva et al. 2022). Thus, management of solid waste and treatment of sewage water in BBPSs is a potential growth field regarding simultaneous management of waste generation (Shukla et al. 2021; Yadav et al. 2021; Nzengung & Gugolz 2022; Singh et al. 2023). This technology may also overcome the drawbacks of other advanced techniques of wastewater management such as ozonation (Rekhate & Srivastava 2020), advanced oxidation (Hassaan & El Nemr 2017), UV radiation in wastewater management due to their high maintenance and operation costs, periodic electrode replacement, and limited reduction in elevated biochemical oxygen demand (BOD) and chemical oxygen demand (COD) levels. Other methods are also effective in treating wastewater like non-ionic polyacrylamide and poly acrylamide-co-acrylic acids (Hamza et al. 2024) and applications of metal-organic frameworks (MOFs) (Manzoor et al. 2024), but their production process is more complex and needs more professionalism for their operation, thus making them non-sustainable and non-preferable solutions. Therefore, more environmentally friendly alternative technologies are recommended. Among them, constructed wetlands (CWs) and BBPSs, constitute an effective natural treatment technology, with low operational and maintenance costs, simple and easy operation and less environmental impact for wastewater management. Furthermore, the primary goal of creating BBPSs is to let locals manage their sewage on their own without needing help from the municipality that is responsible for the sewage system. Furthermore, the installation of the aforementioned facilities promotes blue water conservation by repurposing the treated water for activities such as vehicle washing, backyard gardening, borewell replenishment, and toilet flushing.

Sampling site and sample collection

Sampling was done from primary treated residential wastewater which was obtained from Bhagwanpur Sewage Treatment Plant, Varanasi for the study, located at 25°16′21″ N latitude and 83°00′16″ E longitude, at an elevation of 74.518 m above mean sea level (Figure 1). Before collecting the samples, the collection bottles were acid-washed and dried. Amber glass bottles were used for collecting samples. The effluent was analysed initially before it was batched into the mesocosm BBPS. For each setup, 5 L of primary treated wastewater was provided, and the effluents were analysed at various hydraulic retention times (HRT), i.e., 0, 24, 48 and 72 h for different physio-chemical properties, viz. pH, electrical conductivity (EC), total dissolved solid (TDS), BOD, COD, phosphates , nitrates , chloride (Cl), alkalinity, hardness, and the samples were analysed by following the methods given by APHA 2017.
Figure 1

Map of the sampling area.

Figure 1

Map of the sampling area.

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Design of the BBPSs

BBPSs were designed in total to treat wastewater as BBPS1 (Figure 2(a)), BBPS2 (Figure 2(b)), BBPS3 (Figure 2(c)) and BBPS4 (Figure 2(d)). The material used for designing the rectangular structure was made using Kadappa slabs in the dimensions shown: 40 cm (l) × 20 cm (b) × 22 cm (h) with total surface area of 800 m² and volume of 17,600 m3. The specifications of all the treatment setups are given in Figure 2; in all setups, the upper 3 cm area remains unfilled to capture water entering into the structure. BBPS1, BBPS2, and BBPS4 were planted with Canna indica, which was used as a macrophyte for enhanced phytoaccumulation, which was compared with the unplanted BBPS3 setup. For uniform aeration, perforated pipes were inserted from above to the bottom of all the setups.
Figure 2

Schematic representation of different treatment setups: (a) BBPS1; (b) BBPS2; (c) BBPS3; and (d) BBPS4.

Figure 2

Schematic representation of different treatment setups: (a) BBPS1; (b) BBPS2; (c) BBPS3; and (d) BBPS4.

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Preparation of adsorbent and biomixture

Substrates used in all the BBPS structures were rice husk, soil, vermicompost, gravel and sand as adsorbents in different proportions according to the design and treatment needs. Before being used in this study, rice husk was collected from a neighbouring rice mill and sieved (IS 460:1962, 710 μm). After thoroughly cleaning the rice husk in distilled water, it was dried in an oven set at 100 °C for a few hours. The soil used in the BBPS structure was collected with a spade from the upper layer (0–25 cm) from the field of IESD, BHU, Varanasi, and was dried for some days, and ground and sieved through a 0.5-mm sieve to obtain uniformity. The soil provides sufficient organic material, especially in the early stages of the system, to support microbial activity, modify rice husk composition, and support plant development. Vermicompost was procured from a nearby agricultural facility in the Varanasi region; vermicompost is used to increase porosity, and thus, the adsorption of contaminants in the media. All the substrates were selected according to their ease of availability. Biomixture was prepared by mixing a definite proportion of rice husk (50%), soil (25%), and vermicompost (25%) together. Gravel and sand used in the treatment process were also washed thoroughly 5–7 times to dissolve any adhered impurity and dried properly before use. The maximum hydraulic loading rate of all the treatment setups is similar, i.e., 0.006 L/(m², cycle). The maximum flow rate of the setups was calculated by multiplying the hydraulic loading rate by the surface area of the setups which was 4.8 m3/cycle. Empty bed contact time (EBCT) is equal to the volume of the empty bed divided by the flow rate, for these setups per cycle EBCT equals 3,666.6 min (for 72 h cycle). The Brauner–Emmet–Teller (BET) method is a commonly used technique to calculate the surface area of porous materials, including sand and gravel, based on nitrogen adsorption isotherms. However, the BET method itself does not directly calculate porosity. Instead, it helps in estimating the surface area, which can be related to porosity when combined with other parameters such as the material's bulk and particle densities. BET analysis of gravel and sand reveals that the surface area of gravel was 3.079 m2/g and sand was 1.2897 m2/g, and the pore radius of gravel was 23.462 and sand was 17.285 A°.

Analytical methods

The effluent collected at different HRTs was examined using standard techniques for various physico-chemical parameters, namely pH, EC, TDS, BOD, COD, phosphates, nitrates, chloride, alkalinity and hardness; after sample collection, unstable parameters like pH, temperature, EC and TDS, were assessed immediately by using a portable multi-parameter (Hanna HI98194), to reduce the inaccuracies that occur over time as a result of the chemical and biological interactions between the sample and the environment (Hutton 1983). Sample collection, storage, transfer and other testing criteria were followed in compliance with the American Public Health Association guidelines (2017). The samples were analysed for BOD by Winkler's azide modification method, whereas nitrate and phosphate were estimated by the UV spectrophotometric method (Shimadzu UV1900 series). The minima, maxima, average and standard deviation values of the studied parameters have been determined based on the test results, along with the standard deviations (Table 1).

Table 1

Contaminant concentration in all the treatment setups

ParametersPrimary treated effluent
BBPS1
BBPS 2
BBPS3
BBPS4
Min–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SD
pH 7.9–8.3 8.05 ± 0.19 5.9–8.6 6.61 ± 1.06 5–6.9 5.82 ± 0.66 7.2–8.5 7.71 ± 0.48 7–7.8 7.51 ± 0.26 
EC (μs/cm) 362.2–1565 1110.11 ± 481.55 257–1567 825.5 ± 393.11 300–1022 735.62 ± 271.78 757–2267 1319.13 ± 455.49 1032–2123 1273.12 ± 386.69 
TDS (mg/L) 181.1–785.2 555.05 ± 240.77 128.5–783.5 412.75 ± 196.55 150–511 367.81 ± 135.88 378.5–1133.5 659.56 ± 227.74 516–1061.5 636.56 ± 193.34 
BOD (mg/L) 50.89–83.84 66.22 ± 2.80 7.32–12.89 9.43 ± 1.94 7.246–12.21 9.67 ± 1.73 10.9–20.22 14.60 ± 3.14 7.95–15.89 13.78 ± 3.62 
COD (mg/L) 220–297 266 ± 31.34 190–259 226.5 ± 22.01 170–210 188.63 ± 13.66 109–230 200.5 ± 38.74 210–260 228.63 ± 17.26 
Nitrate (mg/L) 120.91–96.15 179.2 ± 25.14 16.36–54.72 25.48 ± 13.73 25.33–97.36 47.87 ± 27.21 65.36–177.36 136.23 ± 35.83 65.36–91.81 80.75 ± 10.36 
Chloride (mg/L) 35.0385–99.21 75.98 ± 24.25 21.07–82.21 46.47 ± 22.39 11.071–35.46 21.21 ± 9.06 19.07–84.22 64.84 ± 20.64 19.07–84.22 64.84 ± 20.64 
Phosphate (mg/L) 0.035–0.34 0.244 ± 0.13 0.01–0.25 0.08 ± 0.08 0.01–0.09 0.06 ± 0.04 0.01–0.46 0.19 ± 0.15 0.26–1.95 1.09 ± 0.64 
Hardness (mg/L) 295–395 352.875 ± 30.44 70–200 125.63 ± 41.45 104–198 126.12 ± 27.90 200–390 307.12 ± 59.18 224–342 276.63 ± 39.571 
Alkalinity (mg/L) 376–967 761.5 ± 235.8 125.63–41.45 100 ± 789 124–389 233.13 ± 92.72 400–840 659.12 ± 167.31 440–1000 613.88 ± 191.42 
ParametersPrimary treated effluent
BBPS1
BBPS 2
BBPS3
BBPS4
Min–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SDMin–maxAverage ± SD
pH 7.9–8.3 8.05 ± 0.19 5.9–8.6 6.61 ± 1.06 5–6.9 5.82 ± 0.66 7.2–8.5 7.71 ± 0.48 7–7.8 7.51 ± 0.26 
EC (μs/cm) 362.2–1565 1110.11 ± 481.55 257–1567 825.5 ± 393.11 300–1022 735.62 ± 271.78 757–2267 1319.13 ± 455.49 1032–2123 1273.12 ± 386.69 
TDS (mg/L) 181.1–785.2 555.05 ± 240.77 128.5–783.5 412.75 ± 196.55 150–511 367.81 ± 135.88 378.5–1133.5 659.56 ± 227.74 516–1061.5 636.56 ± 193.34 
BOD (mg/L) 50.89–83.84 66.22 ± 2.80 7.32–12.89 9.43 ± 1.94 7.246–12.21 9.67 ± 1.73 10.9–20.22 14.60 ± 3.14 7.95–15.89 13.78 ± 3.62 
COD (mg/L) 220–297 266 ± 31.34 190–259 226.5 ± 22.01 170–210 188.63 ± 13.66 109–230 200.5 ± 38.74 210–260 228.63 ± 17.26 
Nitrate (mg/L) 120.91–96.15 179.2 ± 25.14 16.36–54.72 25.48 ± 13.73 25.33–97.36 47.87 ± 27.21 65.36–177.36 136.23 ± 35.83 65.36–91.81 80.75 ± 10.36 
Chloride (mg/L) 35.0385–99.21 75.98 ± 24.25 21.07–82.21 46.47 ± 22.39 11.071–35.46 21.21 ± 9.06 19.07–84.22 64.84 ± 20.64 19.07–84.22 64.84 ± 20.64 
Phosphate (mg/L) 0.035–0.34 0.244 ± 0.13 0.01–0.25 0.08 ± 0.08 0.01–0.09 0.06 ± 0.04 0.01–0.46 0.19 ± 0.15 0.26–1.95 1.09 ± 0.64 
Hardness (mg/L) 295–395 352.875 ± 30.44 70–200 125.63 ± 41.45 104–198 126.12 ± 27.90 200–390 307.12 ± 59.18 224–342 276.63 ± 39.571 
Alkalinity (mg/L) 376–967 761.5 ± 235.8 125.63–41.45 100 ± 789 124–389 233.13 ± 92.72 400–840 659.12 ± 167.31 440–1000 613.88 ± 191.42 

Bolded values signify maximum reduction.

Formula 1 is used to calculate the mean removal efficiency (R) of all the treatment setups by using the mean concentration of contaminants in influent (Cin) and the mean concentration of contaminants in effluent (Cout).
(1)
Determination of the mass removal rates (MRRs) for the primary contaminants (nitrate, phosphate, BOD and COD) present in the treated water was also done along with removal efficiency. MRRs were calculated using the following formula:
(2)
where A is the area of the treatment structures in m2, Qin and Qout are the volume of wastewater used as influent and drawn as effluent per cycle of the treatment (m3/cycle), Cin and Cout represent the mean concentrations of pollutants in wastewater before entering and after leaving the treatment structures (g/m3).

Statistical methods

Excel 2019 was used to calculate the minima, maxima, mean and standard deviation for each parameter. A 3D trend was created using Origin Pro 2023. Since the majority of information collected was not distributed according to a normal distribution, a correlation matrix plot among each of the variables was created using the Spearman correlation test.

Physico-chemical properties of sewage effluent (primary treated)

Samples of sewage water were taken from the primary settling tank at the sewage treatment facility at Bhagwanpur and were initially examined for several physico-chemical parameters. Table 1 displays the min–max and average–standard deviation of all the physico-chemical properties of the effluent, indicating its alkaline character; the pH of sewage water was neutral to slightly alkaline. The slightly alkaline nature, i.e., 8.05 indicates that the wastewater may be alkaline due to the washing area of the residential town. EC, which corresponds to the dominating ions that are the result of ion exchange and solubilisation in water, is a key factor in determining whether it is suitable for irrigation. The EC of effluent varies with an average mean of 1110.11 μs/cm. The effluent's EC has a strong positive correlation with TDS, having an average range of 555.05 mg/L. Sewage effluent had an average total alkalinity of 761 mg/L. The data showed that pH, EC and TDS were within the limits described in the revisions made to CPCB 2017 for its safe release into the in-land surface water and on-land irrigation. Nitrate levels in the effluent samples with min–max were 21.87–196.15 mg/L. The nitrate concentration in sewage effluent corresponds to the household stuff, runoffs from agricultural fields, cattle yards, etc. According to various reports, sewage discharge is a significant source of phosphate from a variety of sources, which causes eutrophication of aquatic bodies (Vymazal & Kröpfelová 2008; Gizińska-Górna et al. 2020). The phosphate content of the effluent ranged from 0.04 to 0.34 mg/L with an average concentration of 0.24 mg/L. BOD is typically employed as an index to quantify the level of organic contamination in wastewater, which can be decomposed by bacteria under anaerobic conditions. Variations in the BOD of the effluent ranged from 50.89 to 83.84 mg/L with an average of 66.22 mg/L, whereas the values of COD varied from 220 to 297 mg/L. Other parameters are described more elaborately in Table 1.

Performance of different treatment setups

Performance of BBPS1

After the experiment was completed, the results showed that the pH level decreased from its initial average value of 8.05–6.61, and that the EC and TDS values also gradually decreased and were somewhat lesser than the influent concentration, while increasing the HRT. After treatment, the effluent collected from the setups has lower values of BOD and COD, and the values fall within the range of CPCB standards 2017, which was initially above the permissible limits of standards. It was noticed that poor BOD and COD removal by BBPS1 was seen at lower HRTs, i.e., 0–24 h but it steadily increased with increasing HRT (Figure 8). In influent wastewater, the COD values varied from 220 to 297 mg/L; after 72 h of treatment, they dropped to 190–226.5 mg/L. The values obtained after treatment suggest that the COD concentration after treatment also falls within the permissible value stipulated by CPCB 2017. Nitrate values ranged from 120.93 to 196.15 mg/L in influent wastewater, with an average value of 179.21 mg/L. After 72 h of HRT, it was reduced to 25.48 ± 13.73 mg/L, with the maximum removal of 85.7% in BBPS1; it is demarcated here that in this setup, the nitrate level reduced and the values are almost similar to the secondary treated sewage, which is within the permissible limit of standards. In this setup, there is efficient removal of biogenic contaminants along with BOD and COD. As observed in the mechanism behind the treatment involved, most probably, the adsorption and plant uptake as in this setup, gravel and sand bed act like adsorbents and there is a possibility of adhesion of contaminants on the BBPS media. The porous structures of gravel and sand as well as interstitial spaces can be occupied by contaminants either through Vander wall forces or chemisorption. Media can also be prone to biofilm formation which is the main reason behind organic contaminants’ degradation, and thus, the formation of microbial film occurs, which produces aerobic and anaerobic zones in the system. Aerobic decomposition occurs more quickly than chemoautotrophic breakdown because chemoheterotrophic bacteria, those that live in the presence of free oxygen, have far greater metabolic rates than chemoautotrophic bacteria. Aerobic bacteria employ oxygen as the ultimate electron acceptor after oxidising organic molecules, releasing carbon dioxide, ammonia and other stable substances. A detailed study of BBPS1 performance is described in the graph plotted in Figure 3(a). Spearman correlation matrix was observed as pH was highly correlated with hardness (0.92), phosphate (0.92), BOD (0.99) and COD (0.98), which determines that pH of the sample affects organic contaminants’ degradation. EC is very highly correlated with TDS (0.99), nitrate (0.99), alkalinity (0.99), chloride (0.99), and hardness (0.99). TDS was highly correlated with COD (0.95) and phosphate (0.99). BOD has a weak positive correlation with hardness (0.86), phosphate (0.88) and nitrate (0.88). COD, on the other hand, is highly correlated with nitrate (0.93), phosphate (0.90) and hardness (0.91). Phosphate is highly correlated with alkalinity (0.99), chloride (0.99) and hardness (0.99). Total hardness moderately correlates with sulphate (0.52). Overall, most of the parameters were highly correlated with each other, except some (Figure 3(b)).
Figure 3

(a) Performance of BBPS1 and (b) Spearman correlation plot of BBPS1.

Figure 3

(a) Performance of BBPS1 and (b) Spearman correlation plot of BBPS1.

Close modal

Performance of BBPS2

After treatment in the integrated BBPS, the BOD content in sewage decreased to 7.24 mg/L. At the outflow from this bed, the mean EC concentration was 735.63 μs/cm and the mean COD concentration was reduced to 188.63 mg/L. Nitrate and phosphate were recorded as 179.21 and 0.24 mg/L in the influent and were reduced to 47.87 and 0.07 mg/L, respectively, after treatment. The values obtained were somewhat close to the values reported in an earlier study (Patel et al. 2022). The levels of organic pollutants, specifically BOD and COD, in the wastewater treated by BBPS2 using Canna indica were below the permissible limits defined by CPCB 2017. In this setup, the efficiency of nitrate removal was about 73.28%, which is almost comparable to BBPS1. But this setup shows that the removal performance of most of the parameters is quicker than BBPS1, i.e., at lower HRTs, as in this setup, biomixture acts as a source of labile carbon which helps in the rapid uptake and degradation of contaminants. Biodegradation is faster and more efficient than adsorption, which is the only mechanism of contaminant removal in BBPS1. Notably, a successful mechanism for nitrate removal in BBPS2 is nitrification, followed by canonical denitrification, as in BBPS1, as both rely on distinct microbial mechanisms. From the plant rhizospheric region to the media, nitrifying bacteria transform ammonical nitrogen into nitrate – this process is called nitrification, which is an aerobic process (Maltais-Landry et al. 2009; Zhou et al. 2017). Nitrification further leads towards an anaerobic process of denitrification which is the main cause of nitrate dissipation from the treatment structure. There is a possibility of inhibition of denitrification in the BBPS1-like structure due to the absence of labile carbon (Ding et al. 2012; Wu et al. 2012; Shen et al. 2015). Thus, the addition of biomixture in BBPS 1 can enhance the carbon source, and thus, the denitrification process, which leads to nitrate reduction in the setup, though the result reported high removal of nitrate in BBPS1. Because it occasionally exceeded the permissible value, the wastewater quality exiting the system for EC and TDS did not meet the standards outlined in the 2016 Regulations for wastewater released into aquatic bodies (Figure 4(a)). The rising EC and TDS were most probably due to the ions generated during the organic contaminant degradation. Nonetheless, for organic contaminants, the removal efficiency values were high – 56.45% for BOD and 70.91% for COD. Because of the hypoxic and oxygen-deprived conditions they create, beds are utilised in combination systems to maximise the elimination of nitrogen and organic pollutants. The Spearman correlation matrix observed in most of the parameters is highly correlated to each other (Figure 4(a)); only phosphate is moderately correlated with other parameters, whereas BOD has very little correlation with phosphate (0.56).
Figure 4

(a) Performance of BBPS2 and (b) Spearman correlation plot of BBPS2.

Figure 4

(a) Performance of BBPS2 and (b) Spearman correlation plot of BBPS2.

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Performance of BBPS3

Only a slight decrease in the amounts of organic pollutants in this bed was observed. The vetiver grass planted was not stabilised and this setup operated further with only biomixture. The outcome of the experiment showed that the pH value of the effluent from the setup decreased from its initial average value of 8.05–7.7, but the EC and TDS values gradually increased from 54.30 to 45.70%, respectively, while HRT also increased. Additionally, at lower HRTs, i.e., 0 or 24 h, BBPS3 removal of BOD and COD was ineffective, but it steadily increased with increasing HRT though not very efficient in comparison to the above two setups. The variation of COD concentration was 220–297 mg /L in influent wastewater, after 72 h of HRT it was reduced to 200.5 mg/L. Influent nitrate values ranged from 120.92 to 195.15 mg/L with an average value of 179.21 mg/L, after 72 h of HRT, it was reduced to 136.23 mg/L with the maximum removal of 23.98% in BBPS3. The concentration of chloride also decreased from 75.9 to 64.8 mg/L. A detailed study of BBPS3 performance is described in the graph plotted in Figure 5(a). It was shown in the Spearman correlation matrix that pH had a negative correlation with the total EC (−0.75) and TDS (−0.75). EC and TDS had a more negative weak correlation with most of the parameters. BOD, COD, and nitrate are highly correlated with other parameters, except phosphate which has a moderate correlation (Figure 5(b)).
Figure 5

(a) Performance of BBPS3 and (b) Spearman correlation plot of BBPS3.

Figure 5

(a) Performance of BBPS3 and (b) Spearman correlation plot of BBPS3.

Close modal

Performance of BBPS4

This setup is more efficient than BBPS3, as in this setup, macrophyte Canna acts like an agent to enhance the remediation of BOD and COD removal efficiencies that were 37.9 and 85.9%, respectively. This could be related to the Canna indica plant's capacity to adsorb organic particles, as shown by previous research. After 72 h treatment, it was observed that the values of parameters were reduced to BOD 13.78, COD 228.63 and nitrate 80.75 mg/L. These figures demonstrate that, in comparison to the results recorded at the outlet from the BBPS3 which was unplanted, the amounts of organic pollutants were cut by 50% in this bed. This might be because the root zone is creating more micro-aerobic zones, which facilitate quicker biological degradation and increased mineralisation. Furthermore, as seen by the data spanning the full research period, the effluent from the BBPS2, BBPS3, and BBPS4 beds had EC and TDS values higher than the standards' permissible limit (Ma et al. 2020). The use of Canna and the vertical flow of sewage into the bottom of the bed decreased the amount of oxygen that was transported and diffused into the bed through the atmosphere, which caused the anaerobic condition (Figure 6(a)). In the presence of inorganic ions that function as electron acceptors, such as , Mn4+, Fe3+, and CO2, organic matter undergoes transformation under the anaerobic conditions prevalent in beds (Ayaz et al. 2020). The Spearman correlation matrix was observed as pH having a negative weak correlation with EC (−0.43), TDS (−0.43) and phosphate (−0.96). On the other hand, the correlation of EC and TDS with other parameters are also very weak. In contrast, BOD is highly correlated with hardness and alkalinity, COD and nitrate with values of 0.95,0.97 and 0.97, respectively. The correlation of phosphate is not aligned with many of the parameters as most of them have a weak correlation with phosphate (Figure 6(b)).
Figure 6

(a) Performance of BBPS4 and (b) Spearman correlation plot of BBPS4.

Figure 6

(a) Performance of BBPS4 and (b) Spearman correlation plot of BBPS4.

Close modal

Percent removal efficiency of pollutants in all setups

The test results indicated that BBPS1, BBPS2, BBPS3, and BBPS4 were more or less efficient at removing organic and biogenic impurities. Among all the setups, BBPS2 shows a reduction in most of the parameters, viz. BOD 56, COD 70 and nitrate 73%, but much less efficient at eliminating physical impurities (EC31 and TDS 33%). Simultaneously, noticeable variations were identified among the various phases of treatment: the main pollutants were eliminated considerably more quickly in BBPS1 and BBPS2. Both the BBPS1 and BBPS2 beds created favourable circumstances that led to organic contaminants' biodegradation BOD 55.35 and 56.44%, respectively, and COD 85.15 and 70.9%. Both the setups, i.e., BBPS1 and BBPS2, are also much more efficient for the removal of biogenic contaminant nitrate, 85.7 and 73.2%, respectively (Figure 7, Table 2). Numerous other factors might have impacted the process of contaminant removal in the BBPS system which includes the sewage loading method, oxygen availability, the bed's hydraulic pressure and pollution load, the type of plants utilised and the material used as adsorbent media (Marzec et al. 2018), in addition to batch dosing of wastewater, i.e., 1 L water at every 2 h, and perforated pipes for aeration. According to earlier studies, the periodic occurrences of wet as well as dry periods may have significantly improved atmospheric oxygen transport and created favourable circumstances for the oxidative degradation of organic contaminants and nitrification (Jia 2010). Similar reduction values were also obtained for alkalinity, hardness and chloride in all the setups with the maximum in BBPS2 (69, 64.2 and 29.0%, resp.). Figure 8 represents the removal efficiency of different treatment setups at different HRTs, which indicates that there is much difference in the contaminant concentration when comparing 0–72 h; on the other hand, both BBPS1 and BBPS2 show lesser BOD, nitrate and hardness content at 72 h when compared to 0 h. All the parameters show more or less reduction in all the setups except EC and TDS when compared between 0 and 72 h. Figure 9 represents the 3D model of the trend in contaminant removal in different treatment setups; BBPS1 and BBPS2 show a similar trend of removal in comparison to BBPS3 and BBPS4.
Table 2

Concentration and removal efficiency of parameters in different set ups of biobed at different HRT

ParametersBBPS1
BBPS2
BBPS3
BBPS4
0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)
pH 8.05 7.76 7.25 6.61 17.89 8.05 7.70 7.44 7.18 4.35 8.05 8.17 7.89 7.71 4.22 8.05 7.84 7.59 7.51 6.71 
EC 1110.11 974.01 903.75 825.50 25.64 1110.11 953.88 860.13 760.63 31.48 1110.11 1210.38 1287.01 1319.13 −18.82 1101.11 1510.25 1462.38 1273.13 −14.69 
TDS 555.06 487.01 451.88 412.75 25.63 555.06 476.94 430.06 367.81 33.74 555.06 605.19 643.50 659.56 −18.83 555.06 755.13 731.19 636.56 −14.68 
BOD 22.22 9.93 55.31 22.22 9.68 56.43 22.22 14.61 34.25 22.22 13.78 37.98 
COD 266.01 253.50 247.88 226.50 14.85 266.01 232.25 215.75 188.63 29.09 266.01 256.01 233.63 200.50 24.63 266.01 267.88 252.88 228.63 14.05 
Alkalinity 761.50 623.63 511.13 426.38 44.01 761.50 460.38 372.88 233.13 69.38 761.50 748.63 664.88 659.13 13.44 761.50 728.63 678.75 613.88 19.39 
Hardness 352.88 229.63 166.13 125.63 64.40 352.88 242.25 173.25 126.13 64.26 352.88 333.38 330.13 307.13 12.96 352.88 310.88 287.12 276.63 21.61 
Chloride 75.99 63.78 53.17 46.47 38.85 75.99 51.66 30.67 21.23 72.06 75.99 73.53 70.30 64.84 14.67 75.99 78.78 77.79 70.72 6.94 
Nitrate 179.21 102.49 57.13 25.49 85.77 179.21 103.99 74.09 47.87 73.29 179.21 164.53 143.89 136.23 23.98 179.21 132.62 88.84 80.75 54.94 
Phosphate 0.24 0.17 0.11 0.09 0.63 0.24 0.08 0.15 0.06 75.00 0.24 0.22 0.23 0.19 20.83 0.24 0.44 0.77 1.09 −354.1 
ParametersBBPS1
BBPS2
BBPS3
BBPS4
0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)0 h24 h48 h72 hRemoval efficiency (%)
pH 8.05 7.76 7.25 6.61 17.89 8.05 7.70 7.44 7.18 4.35 8.05 8.17 7.89 7.71 4.22 8.05 7.84 7.59 7.51 6.71 
EC 1110.11 974.01 903.75 825.50 25.64 1110.11 953.88 860.13 760.63 31.48 1110.11 1210.38 1287.01 1319.13 −18.82 1101.11 1510.25 1462.38 1273.13 −14.69 
TDS 555.06 487.01 451.88 412.75 25.63 555.06 476.94 430.06 367.81 33.74 555.06 605.19 643.50 659.56 −18.83 555.06 755.13 731.19 636.56 −14.68 
BOD 22.22 9.93 55.31 22.22 9.68 56.43 22.22 14.61 34.25 22.22 13.78 37.98 
COD 266.01 253.50 247.88 226.50 14.85 266.01 232.25 215.75 188.63 29.09 266.01 256.01 233.63 200.50 24.63 266.01 267.88 252.88 228.63 14.05 
Alkalinity 761.50 623.63 511.13 426.38 44.01 761.50 460.38 372.88 233.13 69.38 761.50 748.63 664.88 659.13 13.44 761.50 728.63 678.75 613.88 19.39 
Hardness 352.88 229.63 166.13 125.63 64.40 352.88 242.25 173.25 126.13 64.26 352.88 333.38 330.13 307.13 12.96 352.88 310.88 287.12 276.63 21.61 
Chloride 75.99 63.78 53.17 46.47 38.85 75.99 51.66 30.67 21.23 72.06 75.99 73.53 70.30 64.84 14.67 75.99 78.78 77.79 70.72 6.94 
Nitrate 179.21 102.49 57.13 25.49 85.77 179.21 103.99 74.09 47.87 73.29 179.21 164.53 143.89 136.23 23.98 179.21 132.62 88.84 80.75 54.94 
Phosphate 0.24 0.17 0.11 0.09 0.63 0.24 0.08 0.15 0.06 75.00 0.24 0.22 0.23 0.19 20.83 0.24 0.44 0.77 1.09 −354.1 
Figure 7

Percent removal efficiency of different treatment setups.

Figure 7

Percent removal efficiency of different treatment setups.

Close modal
Figure 8

Removal efficiency of different parameters in different set ups at 0-, 24-, 48-, and 72-h intervals.

Figure 8

Removal efficiency of different parameters in different set ups at 0-, 24-, 48-, and 72-h intervals.

Close modal
Figure 9

3D model of trend in contaminant removal.

Figure 9

3D model of trend in contaminant removal.

Close modal

Mass removal rates

One may ascertain the function of plants and biomixture in eliminating organic and biogenic materials by contrasting the values shown in Table 3 (the approximate concentrations of each naturally occurring component that plants and biobed medium absorb). The MRR, which compares the quantity of an element eliminated to the unit of surface area of a BBPS system, is a metric that may be utilised for this purpose. Table 3 compares the theoretical MRR values (calculated using Formula (2)) for the main contaminants, i.e., nitrate, phosphate, BOD and COD for each bed. The obtained value shows the removal of all the biogenic and organic parameters, but the MRR value for BOD was the maximum. Accordingly, BBPS1 and BBPS2 performed much more efficiently in comparison to others for the removal of nitrate phosphate and BOD.

Table 3

Mass removal rate of all the treatment setups

Nitrate MRR (g/m2/cycle) 
BBPS1 0.61 
BBPS2 0.35 
BBPS3 −0.65 
BBPS4 −0.02 
Phosphate 
BBPS1 0.01 
BBPS2 0.01 
BBPS3 −0.00 
BBPS4 −0.01 
BOD  
BBPS1 0.21 
BBPS2 0.22 
BBPS3 0.16 
BBPS4 0.17 
COD  
BBPS1 −1.24 
BBPS2 −0.81 
BBPS3 −0.94 
BBPS4 −1.26 
Nitrate MRR (g/m2/cycle) 
BBPS1 0.61 
BBPS2 0.35 
BBPS3 −0.65 
BBPS4 −0.02 
Phosphate 
BBPS1 0.01 
BBPS2 0.01 
BBPS3 −0.00 
BBPS4 −0.01 
BOD  
BBPS1 0.21 
BBPS2 0.22 
BBPS3 0.16 
BBPS4 0.17 
COD  
BBPS1 −1.24 
BBPS2 −0.81 
BBPS3 −0.94 
BBPS4 −1.26 

Rice husk's inclusion in biomixture facilitates easy growth and adhesion of microorganisms due to its larger surface area and presence of labile carbon. As a result, any biological reactions occurring in a reactor using rice husk as the carbon source can be proved faster than the other methods. As a result of the experiment, BBPS2 shows a fast removal effect at lower HRT. Thus, in this experiment, to enhance the reaction rate of BBPS1 which corresponds to the conventional constructed wetland structure, rice husk as a biomixture was added as an additional media in combination with gravel and sand (BBPS2), which results in higher removal efficiency for most of the parameters. Likewise, this research also shows that the effectiveness of contaminant removal in BBPS1 and BBPS2 is very high in comparison to BBPS3 and BBPS4 because the filter material, i.e., only biomixture, has lost its ability to sorb substances, and there is a possibility that the reactor might chock after an interval. Thus, BBPS3 and BBPS4 need additional media to filter larger particles, as the presence of sand and gravel can also act as filter media that enhance the interaction among iron (Fe), calcium (Ca) and aluminium (Al) in the sand or gravel substrate through adsorption and precipitation (Arias et al. 2001). The capacity of a BBPS to remove contaminants like phosphorus may, therefore, be dependent on the contents of minerals present in the substrates, thus lacking in them, and reducing the adsorption capacity of BBPS3 and BBPS4. The remedial capacity for total nitrogen by the tested BBPS1 and BBPS2 was very high, as the elimination of nitrogen from the denitrification and nitrification processes changes compounds that contain nitrogen, making sewage reusable. For this reason, researchers of the majority of research suggest that single-stage systems, i.e., either single media or media without plant, cannot accomplish a high efficiency of pollutant treatment since many processes cannot take place in one bed at the same time. The current findings support this observation. The most obvious finding from this experiment suggests that the hybrid setup, i.e., BBPS2, with more beds, offering the ability to produce both aerobic and anaerobic conditions, as well as filtration capacity and phytoaccumulation properties to the rhizosphere effect, showed an improved efficiency in reducing contaminants that were lacking in BBPS3 and BBPS4.

Additionally, the adsorbent used in a reactor must possess some qualities like quick and easier separation, favourable transportation, chemical, mechanical and heat stability, fouling resistance, regenerating ability, insoluble to the liquid in contact, a large area of pores, excellent efficiency, appropriate pore size and volume, uniformity, availability, easy to regenerate and must cost effective to use. Being ecologically sustainable, yet using straightforward processing techniques, this study fulfils all the criteria. The primary advantage of this research is that C. indica and biomixture along with gravel and sand as adsorbent and filter media can be good candidates for removing organic and biogenic compounds faster at low HRTs and can be used for wastewater treatment generated at the grassroot level and for the treatment at own level without integration of municipal corporations. Additionally, it can also be used in impoverished nations with significant effluent discharge of millions of litres per day because this eco-technology is particularly advantageous because of its minimal maintenance requirements.

The authors are thankful to the Central Instrument Laboratory of IESD for providing their laboratory. This research was not funded by any project grant or funding agency. The University Grant Commission, Government of India provided fellowship to the first and other authors. The corresponding author acknowledges IOE for partial support in conducting this research work.

A.S. contributed to the idea of the article, literature search, and original draft making; G.S. and P.S. contributed to writing and editing, V.K.M. contributed to supervision, critical review of the work, and contribution towards editing of the manuscript.

This research was not funded by any project grant or funding agency.

All relevant data are included in the paper or its Supplementary information.

The authors declare there is no conflict.

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