Application of Water Hyacinth for Phytoremediation of Ammoniacal Nitrogen
Abstract
1. Introduction
1.1. Background on Ammoniacal Nitrogen Pollution
1.2. Environmental Impact and Health Risks
1.3. Overview of Phytoremediation
1.4. Aquatic Macrophytes for Ammoniacal Nitrogen Removal
2. Water Hyacinth: Botanical and Biological Characteristics
2.1. Taxonomy and Morphology
2.2. Growth and Reproduction
2.3. Nutrient Uptake Mechanisms
2.4. Adaptability to Different Water Conditions
3. Mechanisms of Ammoniacal Nitrogen Removal
3.1. Uptake and Assimilation by Water Hyacinth
3.2. Conversion Processes
3.3. Distinguishing Plant Assimilation and Microbial Transformation
3.4. Conceptual Nitrogen Mass Balance in Water Hyacinth Systems
3.5. Impact on Nitrogen Cycle
4. Effectiveness of Water Hyacinth in Ammoniacal Nitrogen Phytoremediation
| Study | Macrophyte | Duration/HRT | Influent NH3-N (mg/L) | Effluent NH3-N (mg/L) | Removal (%) | System Context | Mechanistic Indications | Key Notes |
|---|---|---|---|---|---|---|---|---|
| [15] | Pistia stratiotes | 14 days | 12.14 | 3.49 | 71.25 ± 5.8 | Mixed wastewater | Likely assimilation + adsorption | Also reduced Cu (76.7%) and TDS (22.6%) |
| [16] | Ipomoea aquatica | 8 days | 10.2 | 0.28 | 97.3 | Batch system | High uptake; short HRT suggests strong assimilation | Best NH3-N removal among tested species |
| Salvinia minima | 8 days | 10.2 | 1.03 | 89.9 | Batch | Likely assimilation | Better COD removal | |
| Lemna minor | 8 days | 10.2 | 2.00 | 80.4 | Batch | Surface assimilation dominant | — | |
| Centella asiatica | 8 days | 10.2 | 2.13 | 79.1 | Batch | Likely assimilation | — | |
| [85] | Canna lily | 18 weeks | — | — | 45.65–100 | Constructed wetland | Variable; influenced by flooding and decay | NH3 increase during weeks 14 and 18 |
| [8] | Eichhornia crassipes | 20 days | 24 (first 10 d) | ~8 (first 10 d) | >80 (first phase) | Comparative plant study | Likely assimilation; efficiency declined over time | Inferior to A. calamus and C. indica |
| Acorus calamus/Canna indica | 20 days | 24 | <2 | >90 | Rooted emergent system | Likely sustained uptake | Better long-term performance | |
| [86] | Eichhornia crassipes | 14 days | 4.20 ± 0.10 | 3.1 | 74 | Wastewater | Assimilation + possible microbial role | Best phosphate removal (98%) |
| [87] | Eichhornia crassipes | 1 month | 2.5 | <0.01 | ~99 | Aquaculture water | Likely assimilation; low loading | 65% plant survival |
| [41] | Eichhornia crassipes | 2 months | TKN: 42.2 | — | 30.8 | Pond system | Lower NH3-N removal vs. duckweed | Better COD removal |
| Factor | Optimal Range/Condition | Impact on Efficiency |
|---|---|---|
| Water Temperature | 25–30 °C | Enhances metabolic activity and nutrient uptake; growth slows below 15 °C |
| pH Level | 6.0–8.0 | Neutral to slightly alkaline pH supports optimal growth and NH3-N uptake |
| Ammoniacal Nitrogen (NH3-N) | 100–150 mg/L (optimal); >200 mg/L (toxic) | High NH3-N boosts uptake but may inhibit growth if excessive |
| Salinity | <1.66% NaCl | High salinity causes chlorosis and necrosis, limiting plant survival |
| Plant Age | Young plants preferred | Younger roots have higher oxygen release and nutrient absorption capacity |
| Harvest Frequency | Every 2–3 weeks (varies by system) | Prevents decay and nutrient release; maintains optimal biomass productivity |
| Sunlight Availability | High solar radiation | Boosts photosynthesis and biomass growth; rainy seasons reduce efficiency |
| Retention Time | 8–44 days (depending on wastewater type) | Longer retention improves NH3-N removal but may slow throughput |
| Nutrient Load | Moderate nutrient levels | Excessive nutrients may cause toxicity; balanced load supports steady uptake |
| Water Depth | 14–15 cm (recommended) | Prevents anaerobic conditions and odor; supports aerobic microbial activity |
| Sl. No. | Case Study | Water Type/Location | Scale | Duration/Retention Time | NH3-N Removal Efficiency | Reference |
|---|---|---|---|---|---|---|
| 1. | Domestic wastewater | Pond effluent (India) | Laboratory | 24 days | 67% removal | [88] |
| 2. | Domestic wastewater | Institutional WWTP (Malaysia) | Pilot | 21 days | 85% removal | [74] |
| 3. | Municipal wastewater | City effluent (Tanzania) | Pilot | 44 days | 81% removal | [78] |
| 4. | Polluted river | Waigang River (China) | Field | 1 year | From 5.2 mg/L to 3.5 mg/L (48.6% removal) | [89] |
| 5. | Polluted river | Waigang River (China) | Field | 3 years | 86.5% removal | [90] |
5. Benefits and Limitations
5.1. Environmental and Economic Benefits
5.2. Challenges and Limitations
5.3. Potential for Large-Scale Implementation
| Aspect | Details and Examples | References |
|---|---|---|
| Environmental Benefits | Efficient removal of ammoniacal nitrogen (NH3-N), nitrate, and nitrite (>95% under controlled conditions). Reduction in nutrient pollution in wastewater and improvement of water quality in lakes, rivers, and industrial effluents. | [1,91] |
| Economic Benefits | Low-cost alternative compared to conventional nitrification–denitrification systems; minimal energy, chemical, and infrastructure requirements. Harvested biomass can be converted into bioethanol (0.09 mL/mL culture) and nutrient-rich vermicompost. | [84,91] |
| Key Challenges and Limitations | Rapid proliferation (up to 50 kg/m2) may obstruct waterways, reduce light penetration and dissolved oxygen, and displace native species. Decaying biomass can reintroduce nutrients if not harvested. Performance is sensitive to climatic conditions; salinity > 2.5 g NaCl/L and pH < 5 induce phytotoxic stress and reduce nitrogen uptake. Biomass may accumulate contaminants, requiring safe disposal through composting, anaerobic digestion, or controlled incineration. | [84,91] |
| Real-World Performance | Municipal wastewater treatment achieved 81–85% NH3-N removal over 21–44 days depending on influent concentration and plant density. Semiconductor effluent treatment achieved 77.48% NH3-N removal under optimized conditions (pH 8.51, 8.47 days retention, 21.39 g/L plant density). | [1,84] |
| Large-Scale Implementation Potential | Suitable for decentralized wastewater treatment in developing regions. Long-term remediation projects demonstrated substantial NH3-N reduction in a 10.5 km2 eutrophic lake and 5000 m2 riverine system (86.5% removal with systematic harvesting). Performance stability enhanced through response surface methodology (RSM) optimization and integration with multi-stage systems. | [1,84] |
| Requirements for Large-Scale Success | Strong institutional frameworks, environmental monitoring, regulated biomass harvesting and safe reuse strategies (composting, bioenergy generation), and community participation are essential for sustainable implementation. | [91,92] |
6. Advances and Innovations
6.1. Integration with Other Remediation Technologies
| Integration Type | Mechanism and Synergistic Advantage | Key Pollutants Removed | Removal Efficiency | Outcome and Benefit | References |
|---|---|---|---|---|---|
| Water Hyacinth + Constructed Wetland | Rhizosphere oxygenation enhances microbial nitrification–denitrification; combined plant–microbe action stabilizes the nitrogen cycle |
| 85–95% N removal 90–95% COD/BOD reduction | Improved nutrient and organic load removal, which reduces eutrophication | [78,94] |
| Water Hyacinth + Microbial Biofilms | Biofilm formation on roots supports nitrifiers and denitrifiers; faster conversion of NH4+ → NO3− → N2 |
| 80–90% total nitrogen | Boosted microbial nitrogen cycling and stability under variable loads | [93,95] |
| Water Hyacinth + Physicochemical Treatment | Adsorption via hydroxyl, carbonyl, and carboxyl groups; acts as a polishing stage post-coagulation or filtration |
| 70–90% metal and nutrient removal | Reduced toxicity, lower effluent TSS, improved water clarity | [59,96] |
| Water Hyacinth + Anaerobic Digestion | Biomass used as feedstock for methane generation; digestate reused as fertilizer |
| 58% CH4 in the produced biogas | Circular bioeconomy: renewable energy and nutrient recycling | [91,93] |
| Water Hyacinth + Multi-Stage Hybrid System (e.g., with Canna indica/Acorus calamus) | Sequential plant use: E. crassipes for rapid uptake, rooted macrophytes for long-term polishing |
| >95% N and P removal in optimized systems | High resilience, long-term sustainability | [8,84] |
6.2. Policy and Management Strategies
7. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Treatment Method | Efficiency for NH3-N Removal | Advantages | Limitations | Relative Performance of Water Hyacinth | References |
|---|---|---|---|---|---|
| Nitrification–Denitrification (Activated Sludge) | 80–95% | Reliable and consistent; controlled biological process | High energy demand; chemical inputs; skilled operation required | Water hyacinth achieves comparable removal (81–97%) under optimized conditions but with lower operational cost and slower kinetics | [1,28,84] |
| Ion Exchange/Adsorption Systems | 85–95% | Rapid and selective removal | Expensive resins; regeneration waste | Water hyacinth provides a low-cost, low-maintenance alternative but offers less precise process control | [1] |
| Membrane Bioreactors (MBR) | 90–99% | High precision; compact design | Membrane fouling; high maintenance and energy cost | Water hyacinth may serve as pre-treatment to reduce nutrient loading prior to MBR application | [28] |
| Constructed Wetlands (Rooted Macrophytes) | 70–95% | Sustainable; low energy requirement | Large land area required; limited hydraulic capacity | Integration with floating water hyacinth can enhance nitrogen removal via combined assimilation and microbial processes | [10,18] |
| Chemical Precipitation/Air Stripping | 60–80% | Rapid removal; suitable for high concentrations | Chemical sludge production; pH adjustment required | Water hyacinth avoids chemical sludge generation but requires longer retention times | [84] |
| Water Hyacinth (Eichhornia crassipes) | 77–97% (system-dependent) | Low cost; minimal energy input; biomass valorization potential | Slower treatment rate; requires harvesting; performance depends on environmental conditions | — | [1,84,91] |
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Kar, S.; Paul, S.; Singh, R.K.; Parveen, S.; Hossain, K.; RoyChowdhury, A. Application of Water Hyacinth for Phytoremediation of Ammoniacal Nitrogen. Nitrogen 2026, 7, 27. https://doi.org/10.3390/nitrogen7010027
Kar S, Paul S, Singh RK, Parveen S, Hossain K, RoyChowdhury A. Application of Water Hyacinth for Phytoremediation of Ammoniacal Nitrogen. Nitrogen. 2026; 7(1):27. https://doi.org/10.3390/nitrogen7010027
Chicago/Turabian StyleKar, Sayanti, Souvik Paul, Rohit Kumar Singh, Saba Parveen, Kaizar Hossain, and Abhishek RoyChowdhury. 2026. "Application of Water Hyacinth for Phytoremediation of Ammoniacal Nitrogen" Nitrogen 7, no. 1: 27. https://doi.org/10.3390/nitrogen7010027
APA StyleKar, S., Paul, S., Singh, R. K., Parveen, S., Hossain, K., & RoyChowdhury, A. (2026). Application of Water Hyacinth for Phytoremediation of Ammoniacal Nitrogen. Nitrogen, 7(1), 27. https://doi.org/10.3390/nitrogen7010027

