This study focused on the water quality of a river in Wuhan City, China, which is surrounded by ponds that were transformed into a bypass multipond wetland system to improve river water quality. The bypass multipond wetland system included surface-flow artificial wetlands, modified partition ponds, aeration reoxygenation ponds, ecological ponds, and other processes. After the stable operation of the process, the water transparency was higher than 60 cm and the dissolved oxygen (DO) was higher than 5 mg/L, while the ammonia nitrogen (NH3-N) concentration was less than 1.0 mg/L, total phosphorus (TP) was lower than 0.2 mg/L, and chemical oxygen demand (COD) was lower than 20 mg/L, achieving the treatment target. After monitoring the results of each process, the process which best enhanced the water transparency enhancement was the surface-flow of the artificial wetlands and ecological ponds. The aeration reoxygenation pond had the best effect on DO enhancement. The processes that most affected NH3-N and TP removal were the surface-flow artificial wetlands and ecological ponds. The modified parthenogenic pond had the greatest effect on COD removal. The bypass multipond wetland system not only improved the river water quality but also enhanced the river landscape, and can act as a reference for similar river water quality improvement actions.

  • Surface flow artificial wetlands use artificial water plants instead of substrate to reduce retrofitting costs.

  • Improved parthenogenic pond set up as deep water and shallow water can work better.

  • The use of aeration-microbial bacterial agent can remove pollutants better.

  • Artificial water plants are used in ecological ponds to provide more attachment sites for microorganisms.

Graphical Abstract

Graphical Abstract

Over the past few decades, China has suffered from severe water quality degradation due to industrial economy-oriented development (Wang & Xiong 2022). In the process, a large amount of domestic and industrial wastewater is directly discharged into rivers, resulting in the serious degradation of river water quality (Hsu et al. 2019). The destruction of urban rivers not only has a major impact on the urban landscape but also seriously impacts the physical and mental health of nearby residents. Therefore, urban river management is an urgent matter. Among river water quality management techniques, artificial wetlands and stabilization ponds have had some of the best effects on improving water quality (Bai et al. 2020; Xu et al. 2022).

As a green ecological water purification process, artificial wetlands are widely used in wastewater treatment because of their low cost, ease of operation, eco-friendliness, and aesthetics (Wang et al. 2022). Artificial wetlands consist of substrates, aquatic plants, and microorganisms that purify wastewater through the synergistic biological, chemical, and physical effects of microorganisms, plants, and substrates (Wei et al. 2020; Xu et al. 2021). Microorganisms play a key role in removing pollutants from artificial wetlands and can degrade pollutants into insoluble or harmless substances (Kumar & Dutta 2019; Zhu et al. 2021). Aquatic plants are an important part of artificial wetlands and can directly remove pollutants from wastewater through absorption and sorption (Zhou et al. 2018b; Gu et al. 2021). Artificial wetland substrates play an important role in pollutant removal, not only by providing a place for the growth and reproduction of microorganisms but also by pollutant sorption (Lu et al. 2021). Artificial wetlands have been widely used in China and other regions of the world over the past two decades as surface water discharge standards have increased (Yu et al. 2022).

Stabilization ponds have the advantages of simplicity, low construction and operating costs, low energy consumption, and sustainability (Abd-Elmaksoud et al. 2021). They provide a completely natural purification process and are increasingly used in wastewater treatment (Ho et al. 2017). Stabilized ponds can be divided into aerobic, parthenogenic, and anaerobic ponds, according to their dissolved oxygen (DO) content (Butler et al. 2015). Different types of stabilization ponds provide better purification; among these, partition ponds stabilize organic matter and remove biochemical oxygen demand from wastewater (Schwarz et al. 2019). Although stabilization ponds are widely used, this low-cost technology is now facing the dilemma of either upgrades or replacement because of more stringent effluent discharge standards (Ho & Goethals 2020). For this reason, artificial wetlands in combination with stabilization ponds were used in the current study, along with the addition of bio-bacteria and artificial plants to enhance the water quality of the river.

In this study, the water quality of a river with a bypass multipond wetland system in China was evaluated. The bypass multipond wetland system was selected to enhance the river water quality after studying and comparing domestic and foreign river treatment technologies and the actual river conditions. Using actual topography, the ponds around the river were converted into surface-flow artificial wetlands, improved parthenogenic ponds, aeration reoxygenation ponds, and ecological ponds. Using artificial plants instead of wetland substrates in the surface-flow artificial wetlands simplified the wetland modification and reduced the modification cost. In the parthenogenic pond, deep water and shallow water areas were set up to not only improve the treatment efficiency of the parthenogenic ponds, but also have landscape effects. In the aeration reoxygenation pond, microbial bacteria were injected into the ecological pond with the water flow. Many artificial plants were planted in the ecological ponds to provide a large amount of habitat for microorganisms. The main aims of the study were: (1) to renovate existing ponds and use the renovation process to enhance river water quality; (2) to achieve the following water quality objectives: DO > 5 mg/L, ammonia as nitrogen (NH3-N) <1.0 mg/L, total phosphorus (TP) <0.2 mg/L, chemical oxygen demand (COD) < 20 mg/L, and water transparency >60 cm.

Study area overview

The project was located in the East Lake New Technology Development Zone in Wuhan City, Hubei Province, China. It has a subtropical climate with an average annual temperature between 15.9 and 17.9 °C, and a calendar year average of 16.4 °C. The total annual precipitation is 889.2–1,862.6 mm, with an average precipitation of 1,347.7 mm. The sunshine hours are between 1,450 and 2,050 h, and the climate is warm and humid with four distinct seasons, abundant heat, precipitation, light, rain, and heat in the same season. The location map of the study area is shown in Figure 1.
Figure 1

Location map of the study area.

Figure 1

Location map of the study area.

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At the beginning of the study, the river water was relatively turbid with low transparency, and the main pollution sources were domestic sewage and agricultural water discharge, as shown in Table 1. Using the existing topography, the fishponds and lotus ponds around the river were transformed into surface-flow artificial wetlands, improved parthenogenic ponds, aeration reoxygenation ponds, and ecological ponds to form a bypass multipond wetland system to improve river water quality. The system had a design influent of 15,000 m3/d, covered an area of approximately 103,490 m2, and had a water residence time of approximately 21.42 d.

Table 1

River water quality and target water quality

Water quality indicatorspHCOD (mg/L)NH3-N (mg/L)TP (mg/L)DO (mg/L)Transparency (cm)
Test section average 7.39 34 2.198 0.44 1.87 17 
Target water quality — <20 <1.0 <0.2 >5 >60 
Water quality indicatorspHCOD (mg/L)NH3-N (mg/L)TP (mg/L)DO (mg/L)Transparency (cm)
Test section average 7.39 34 2.198 0.44 1.87 17 
Target water quality — <20 <1.0 <0.2 >5 >60 

COD, chemical oxygen demand; NH3-N, ammonia nitrogen; TP, total phosphorus; DO, dissolved oxygen.

Sampling point setting

Five sampling points were set up: at the inlet of the bypass multipond wetland system, the outlet of each process, and the outlet of the system; these were denoted as P1, P2, P3, P4, and P5, respectively. The sampling points were set up as shown in Figure 1.

Water quality testing methods

The water quality testing methods in this study are shown in Table 2.

Table 2

Water quality testing methods

Testing itemsTesting method
pH Portable pH meter method 
DO (mg/L) Portable DO meter method 
COD (mg/L) Potassium dichromate method (HJ828-2017) 
NH3-N (mg/L) Nascent reagent spectrophotometry (HJ535-2009) 
TP (mg/L) Ammonium molybdate spectrophotometric method (GB11893-1989) 
Transparency Seidel disk method 
Testing itemsTesting method
pH Portable pH meter method 
DO (mg/L) Portable DO meter method 
COD (mg/L) Potassium dichromate method (HJ828-2017) 
NH3-N (mg/L) Nascent reagent spectrophotometry (HJ535-2009) 
TP (mg/L) Ammonium molybdate spectrophotometric method (GB11893-1989) 
Transparency Seidel disk method 

DO, dissolved oxygen; COD, chemical oxygen demand; NH3-N, ammonia nitrogen; TP, total phosphorus.

Water quality improvement process

Technology route

Based on the water quality characteristics of the treated river and site conditions, the existing fishponds and lotus ponds were transformed into units such as surface-flow artificial wetlands, improved parthenogenic ponds, aeration reoxygenation ponds, and ecological ponds. The resulting bypass multipond wetland system was used to treat the river water. This process not only improved the water quality and enhanced the landscape effects but also increased species diversity. The technical route is illustrated in Figure 2.
Figure 2

Technical route.

Figure 2

Technical route.

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Surface flow artificial wetlands

In this study, the pollution sources are mainly domestic sewage and agricultural wastewater discharge. Surface flow artificial wetlands effectively remove suspended matter and nutrients from water due to their plants, substrates, and microbial communities (Xu et al. 2021). These effectively treat domestic and agricultural wastewater (Yang et al. 2018; Li et al. 2020). Surface flow artificial wetlands are widely used because of their advantages, such as low construction, operation, and maintenance costs (Ma et al. 2020). In this study, after considering pond renovation costs, treatment effects, and landscape effects, surface-flow artificial wetlands were selected and used as the treatment process at the front end of the multipond wetland system.

In this study, two ponds were converted into surface-flow artificial wetlands. Each surface-flow artificial wetland was equipped with a waterproof layer and a planting layer at the bottom, and no filler layer was installed. The planting layer was separated from the waterproof layer using coir mats, upon which 30 cm of planting soil was placed. Side banks were laid using cedar stakes and tarpaulins to improve the pond's waterproofing performance. Aquatic plants in the surface-flow artificial wetlands included aquatic, submerged, and artificial water plants. Aquatic plants provide a large root surface area for microorganisms, and the oxygen transported to the inter-root sediment forms a clear aerobic zone near the root hairs, enhancing the redox potential of the inter-root zone and thus promoting the attachment, growth, and reproduction of aerobic bacteria, which facilitates pollutant removal (Fang et al. 2021). Plants in an artificial wetland help transfer oxygen from the atmosphere to the roots, but half of the oxygen is taken up by the plants for respiration (Shukla et al. 2021). The surface-flow artificial wetlands were mainly planted with aquatic plants, such as Phragmites australis (Cav.) Trin. ex Steud., Canna indica L., and Thalia dealbata Fraser. Submerged plants can absorb nutrients directly from the water and play an important role in wetland nutrient removal (Mu et al. 2020). Submerged plants, such as Myriophyllum elatinoides Gaudich., Hydrilla verticillata (Linn. f.) Royle var. rosburghii Casp., and Vallisneria natans (Lour.) Hara, were the main species planted. Artificial water plants were used to replace the artificial wetland fill. Artificial water plants can provide a surface for biofilm growth and are effective at removing nutrients (Qiu et al. 2021). The surface-flow artificial wetlands occupied a total area of 40,753.53 m2, with a design water depth of 0.5 m, a hydraulic retention time of 4.35 d, and a hydraulic load of 0.12 m3/(m2·d). The structure of the surface-flow artificial wetland is shown in Figure 3.
Figure 3

Structure of surface-flow wetlands.

Figure 3

Structure of surface-flow wetlands.

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Improved facultative pond

The domestic wastewater in this study contained more pollutants and the partition ponds can degrade a large amount of organic matter in domestic wastewater (Sunarsih et al. 2020); therefore, partition ponds were installed after the surface-flow artificial wetlands. Parthenogenic ponds are large open ponds prone to the vertical stratification of heat, pH, and DO (Buchanan et al. 2018). This is because parthenogenic ponds can provide a suitable living environment for aerobic, anaerobic, and parthenogenic microorganisms. The overall performance of the parthenogenic ponds is based on the symbiotic relationship between aerobic and anaerobic microorganisms and algae.

In the present study, the pond was transformed into a parthenogenic pond. To enhance the effect of the parthenogenic pond on nutrient removal, the parthenogenic pond was set up using cedar stakes and divided into two parts: a shallow water area and a deep water area. The shallow water area was set up within 5 m of the pond's side bank and was established as a surface-flow artificial wetland. It was mainly planted with aquatic plants such as C. indica, T. dealbata, and P. australis. The waterproof, filler, and planting layers were set at the bottom of the shallow water area. The waterproof layer included plain soil compaction and a geotechnical protection membrane. The filler layer was set up with a 30 cm volcanic rock fill. The planting layer was placed on the upper layer of the filler layer, and a coir mat was used to separate the filler layer from the planting soil. The deep water area was set up with artificial water plants and the bottom was isolated from the substrate using coconut coir mats. The improved partition pond covered a total area of 27,074.44 m2, with a design water depth of 0.5 m in the shallow water and 1.8 m in the deep water, a hydraulic residence time of 8.31 d, and a hydraulic load of approximately 0.22 m3/(m2·d). The improved facultative pond structure is shown in Figure 4.
Figure 4

Structure diagram of the improved facultative pond.

Figure 4

Structure diagram of the improved facultative pond.

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Aeration reoxygenation pond

Maintaining high DO concentrations is essential for the survival of higher life forms in aquatic ecosystems (Mayo & Abbas 2014). Therefore, in this study, an aeration reoxygenation pond was set up after the improvement of the parthenogenic pond. Selection of an appropriate aeration method was also crucial. One study illustrated that there was no significant difference in the COD removal between continuous aeration, intermittent aeration, and non-aerated systems, but there was a significant effect on nitrogen removal from wastewater (Uggetti et al. 2016). Intermittent aeration helped achieve aerobic and anoxic conditions to achieve higher nitrogen removal concentrations (Liu et al. 2019). According to previous research, intermittent aeration can reduce the photosynthetic process of plants, but 4 h of intermittent aeration per day has very little effect on plants (Fan et al. 2013). Intermittent aeration of 4–6 h per day not only reduces aeration costs, but also improves nitrogen and organic removal efficiency (Shukla et al. 2021).

To improve the nitrogen removal rate in the water column, intermittent aeration was used to restore the DO in the water column. Microbial agents, mainly ammonia nitrogen agents, were added to the aeration reoxygenation pond. The synergistic effect of artificial aeration and microbial agents can effectively enhance the anti-pollution ability of the ecosystem and the self-purification ability of the water body, thereby removing pollutants from the water body and improving the water quality of the river (Li et al. 2021). The injected microbial agents flowed into the subsequent treatment facility under water flow. The dosing frequency was twice per week, and the dosing volume was 20 L each time. The aeration reoxygenation pond covered an area of 3,298.74 m2, with a design water depth of 1.5 m, a hydraulic retention time of a 0.2 d, and an aeration time of 6 h per day. In the aeration reoxygenation pond, four groups of fountain aerators (model ZL-CFA1500) were set up, with a power of 1.5 KW and an oxygenation capacity of 0.9–1.1 kgO2/h.

Ecological ponds

Two ponds were transformed into ecological ponds, mainly with aquatic plants and animals. Aquatic plants are the main producers in aquatic ecosystems and are critical for the management of the water environment. Plant remediation is an economical and aesthetic solution to many global environmental problems, and to the use of plants to remove and accumulate pollutants in the environment, which involves using plants to mitigate, transfer, stabilize, or degrade pollutants in soil, sediment, and water (Lu et al. 2018; Nash et al. 2020). Aquatic plants not only provide habitats for various aquatic animals but also enhance the biodiversity and stability of aquatic ecosystems (Zhou et al. 2018a). Aquatic animals can reduce phytoplankton biomass and debris in the water column through their filtering properties, thereby improving the water quality and clarity (Gao et al. 2017).

Aquatic plants, submerged plants, and artificial plants were planted in the ecological ponds, into which aquatic animals were then introduced. The plants used were mainly submerged species, such as M. elatinoides, H. verticillata, and V. natans, and aquatic plants such as P. australis, T. dealbata, and C. indica. Aquatic animals were fish (such as Ctenopharyngodon idella and Lateolabrax maculatus), snails, and shrimp. The ecological ponds covered an area of 25,461.43 m2, with a design water depth of 0.8 m, a hydraulic retention time of approximately 8.56 d, and a hydraulic load of approximately 0.09 m3/(m2·d).

Cost comparison

Technologies that can achieve the goal of water quality treatment are mainly divided into two types: in-situ treatment and bypass treatment. To choose the better process based on cost, this study focused on comparing the cost of in-situ treatment technology and bypass treatment technology. A comparison of the technology costs is presented in Table 3.

Table 3

Comparison of technology costs

ItemsLand costsEcosystem constructionOperation management
In-situ treatment technology Major measures Riverside-related equipment occupies land Aeration, biological contact oxidation tank, biological bacterium, submerged plants, artificial floating island, etc. Plant harvesting, labor costs, electricity costs, etc. 
Costs Lower Due to the limitation of area, there are fewer techniques for the arrangement, fewer plants to grow, and lower costs Less plant volume harvested, lower equipment running costs, lower costs 
Bypass treatment technology Major measures Fish ponds, lotus ponds Surface flow artificial wetland, modified parthenogenic pond, aeration reoxygenation pond, ecological pond Plant harvesting, labor costs, electricity costs, etc. 
Costs Higher Deploying more treatment techniques, planting more plants, and higher costs High plant harvesting volume, more equipment, and higher operating costs 
ItemsLand costsEcosystem constructionOperation management
In-situ treatment technology Major measures Riverside-related equipment occupies land Aeration, biological contact oxidation tank, biological bacterium, submerged plants, artificial floating island, etc. Plant harvesting, labor costs, electricity costs, etc. 
Costs Lower Due to the limitation of area, there are fewer techniques for the arrangement, fewer plants to grow, and lower costs Less plant volume harvested, lower equipment running costs, lower costs 
Bypass treatment technology Major measures Fish ponds, lotus ponds Surface flow artificial wetland, modified parthenogenic pond, aeration reoxygenation pond, ecological pond Plant harvesting, labor costs, electricity costs, etc. 
Costs Higher Deploying more treatment techniques, planting more plants, and higher costs High plant harvesting volume, more equipment, and higher operating costs 

The study was conducted over a period of 4 months, with samples taken from 9:00 to 10:00 am daily. Samples were taken every ten days for a total of 12 times. The measurement indices mainly included water transparency, DO, COD, NH3-N, and TP.

Transparency improvement effect

As shown in Figure 5, the bypass multipond wetland system enhanced the water transparency, and the main contributing processes were the surface-flow artificial wetlands and ecological ponds. At the beginning of the system operation, the main reason for the increase in water transparency was physical settling. After 20 d of system operation, the plants grew to maturity, and the transparency increased as larger particles were removed from the water column due to interception and adsorption by the plants. The transparency stabilized after approximately 70 d of system operation. From the monitoring results of each process, the processes with better transparency enhancement were the surface-flow artificial wetlands and ecological ponds. More aquatic plants are planted in these two areas, resulting in better interception and adsorption of particulate matter from the water column, thereby enhancing transparency. Aquatic animals placed in the ecological ponds were also able to remove particulate matter and play a role in improving transparency. In the improved partition pond, the artificial wetland fill arranged in the shallow water area could adsorb and retain particulate matter, but as there were fewer of these areas in the shallow water area, the increase in water transparency was insignificant. In this region, the main reason for transparency enhancement was physical sedimentation. In the aeration reoxygenation ponds, the transparency was not significantly improved due to lower residence time, aeration disturbance, etc. After the stable operation of the system, the transparency of the system effluent increased to more than 60 cm and up to 68 cm, reaching the treatment target of >60 cm.
Figure 5

Transparency improvement effect.

Figure 5

Transparency improvement effect.

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Dissolved oxygen improvement effect

As shown in Figure 6, the DO concentration of the water body increased after treatment by the bypass multipond wetland system, and the aeration reoxygenation pond played a major role. At the beginning of the system operation, the aerator in the aeration reoxygenation pond was turned on, and the DO concentration began to rise rapidly through manual forced aeration. The DO stabilized after approximately 60 d of system operation. From each process monitoring unit, the aeration reoxygenation pond played the greatest role in increasing the DO concentration in the water by forced aeration through the fountain aerator. The surface-flow artificial wetlands also reoxygenated the water, mainly due to the disturbance caused by the flow of the water, surface disturbance of the water, etc. In addition, the growth and maturation of aquatic plants results in not only the absorption of harmful substances in sewage, but also provides oxygen to the water (Zhao et al. 2020). When the oxygen produced by plant photosynthesis is delivered to the root zone in excess of the plant's needs, it diffuses outward from the root surface, allowing some recovery of DO in the water column. In the improved parthenogenic pond, the DO in the water column did not change significantly, mainly because of the longer residence time, slower water flow, and reduced disturbance, which caused the DO to change significantly. In addition, more microorganisms act on pollutants in this area, consuming a large amount of DO in the water and causing the DO to decline. The DO concentration in the ecological pond was also enhanced, and the main effect was the same as that in the surface-flow artificial wetlands. After the stable operation of the system, the DO concentration of the system effluent was increased to more than 5 mg/L, reaching a maximum of 5.43 mg/L and meeting the treatment target of DO concentrations >5 mg/L.
Figure 6

DO improvement effect.

Figure 6

DO improvement effect.

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Ammonia nitrogen removal effect

As shown in Figure 7, NH3-N was effectively removed after treatment by the bypass multipond wetland system, and the surface-flow artificial wetlands and ecological ponds achieved the best results. In the early stage of system operation, aquatic plants in the surface-flow artificial wetlands and ecological ponds grew and absorbed large amounts of nutrients, resulting in a decrease in the NH3-N concentration. After approximately 50 d of system operation, the NH3-N concentration stabilized. From the monitoring results of each process, it was observed that the surface-flow artificial wetlands and ecological ponds achieved the best NH3-N removal. In the surface-flow artificial wetlands, the main reason for the removal of NH3-N was the synergistic plant–microbe action. Plants require large amounts of nutrients for growth, and their physical effects, such as retention and adsorption, can also remove NH3-N from the water column. The roots of aquatic plants gather a large number of microorganisms, which can promote microbial denitrification due to oxygen release from the roots and the formation of an anoxic–anaerobic–aerobic environment. In addition, many microorganisms are attached to the artificial water plants, enabling the removal of NH3-N due to the microbial action. In the parthenogenic pond, many microorganisms were present, which can remove certain pollutants; however, the limited concentration of DO made the removal of NH3-N ineffective. The NH3-N removal was less effective in the aeration reoxygenation pond because of the shorter residence time and aeration disturbance. Because the aeration reoxygenation pond had microbial bacterial agents and the artificial plants in the ecological ponds provided more microbial attachment sites, the NH3-N removal effect was better in these ponds. After the stable operation of the system, the NH3-N of the system effluent was reduced to <1.0 mg/L, meeting the treatment target of this study.
Figure 7

NH3-N removal effect.

Figure 7

NH3-N removal effect.

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Chemical oxygen demand removal effect

As can be seen from Figure 8, the COD was effectively reduced, and the process with the best removal effect was the improved parthenogenic pond. The main mechanisms of organic matter removal are sedimentation and the filtration of suspended solids, plant uptake, and microbial biodegradation under aerobic or anaerobic conditions (Achak et al. 2019). During the operation of the system, the microbial decomposition of organic matter was the main reason for the COD reduction. In addition, there was physical sedimentation, plant interception, adsorption, and other mechanisms involved. The COD concentration stabilized after 60 d of system operation. From the operational effect of each process, the process with the best COD removal effect was the improved parthenogenic pond. In surface-flow artificial wetlands, the COD was reduced by the microbial decomposition and plant interception of organic matter. In the improved parthenogenic ponds, there was an anaerobic environment that allowed organic matter to be decomposed by microorganisms, resulting in a significant reduction in the COD. In the aeration reoxygenation pond, the COD reduction effect was not obvious due to the short residence time of water in this pond. Aeration disturbance caused fluctuations in the COD in the aeration reoxygenation pond, along with other phenomena. The principle of COD removal in ecological ponds was the same as that in surface flow artificial wetlands. After the stable operation of the system, the COD of the system effluent was reduced to <20 mg/L, with a minimum of 15 mg/L, meeting the treatment target of <20 mg/L in this study.
Figure 8

COD removal effect.

Figure 8

COD removal effect.

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Total phosphorus removal effect

As can be seen from Figure 9, TP was effectively removed from the water during the operation of the system, and the processes with the best TP removal were the surface-flow artificial wetlands and ecological ponds. During the operation of the system, the mechanisms of TP removal included plant uptake and microbial action. After 60 d of system operation, the TP in the water body stabilized. According to the monitoring results of each process, the surface-flow artificial wetlands and ecological ponds were more effective in removing TP. In the surface-flow artificial wetlands, phosphorus was directly absorbed and converted into substances required for plant growth. When plants matured, they were harvested, which lowered the TP level in the water body. In addition, physical sedimentation and plant interception were also involved. An anaerobic environment existed in the improved parthenogenic pond. In this environment, excess phosphorus was absorbed by microorganisms, which remove phosphorus by absorbing and enriching it in the body. A short hydraulic residence time and aeration disturbance existed in the aeration reoxygenation ponds, making TP removal there ineffective. The removal of TP in the ecological ponds was the same as that in the surface-flow artificial wetlands. After the stable operation of the system, the TP of the system effluent was reduced to <0.20 mg/L, and the lowest was 0.17 mg/L, achieving the treatment target of TP concentrations <0.20 mg/L in this study.
Figure 9

TP removal effect.

Figure 9

TP removal effect.

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In this study, by reasonably modifying the ponds around the river, the river water passed through a bypass multipond wetland system consisting of surface-flow artificial wetlands, improved parthenogenic ponds, aeration reoxygenation ponds, and ecological ponds. After 4 months of treatment by this system, the water quality of the river reached the treatment targets of DO >5 mg/L, NH3-N <1.0 mg/L, TP <0.2 mg/L, COD <20 mg/L, and transparency >60 cm. After monitoring the results of each process, it was found that the processes with best transparency enhancement were the surface-flow artificial wetlands and ecological ponds. The aeration reoxygenation pond had the best effect on the DO enhancement. The processes that most effectively removed NH3-N and TP were the surface-flow artificial wetlands and ecological ponds, while the process with the best effect on COD removal was the improved parthenogenic pond. After treatment, the water quality was enhanced and the landscape was improved, which demonstrates the application value of this wetland system. These results can provide a reference for similar river water enhancements.

This research did not receive any specific grant from funding agencies in the public, commercial, or not-for-profit sectors.

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

The authors declare there is no conflict.

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