Sustainable and Advanced Strategies for Bioremediation of Highly Contaminated Wastewater
Abstract
1. Introduction
2. Highly Contaminated Wastewater
2.1. Leachate
2.2. Distillery Wastewater
2.3. Pharmaceutical Wastewater
2.4. Brewery Wastewater
2.5. Paper Industry Wastewater
2.6. Municipal Wastewater
2.7. Field-Level Applications of Bioremediation
3. Fundamental Principles of Bioremediation Technology
Bioaugmentation and Biostimulation
4. Naturally Occurring Potential for Biodegradation
5. Synthetically Engineered Potential for Biodegradation
6. Future Perspectives
7. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Wastewater Type | COD, mg O2/L | BOD5, mg O2/L | Other Contamination Indicators | Treatment Example | Reference |
---|---|---|---|---|---|
Industrial– Distillery | 80,000–100,000 | 40,000–60,000 | pH 3.9–4.5 TN 680–900 mg/L EC 6.3–6.7 ms/cm Dark brown colour | COD reduced following treatment in a two-stage bioreactor: Pseudomonas putida 44% and Aeromonas sp. 66%, within 24 h. | [22,23] |
Landfill Leachate | 100–79,000 | 3–25,000 | pH 5.8–8.5 TSS 13–5000 mg/L TN 5–13,000 mg/L | COD removal efficiency through SBR treatment ranges from 62 to 75%, data significantly vary depending on landfill age and climatic conditions. | [35] |
Industrial– Pharmaceutical | 250–60,000 | 1–21,000 | pH 6.6–9.4 TSS 60–360 mg/L EC 518–2840 ms/cm | MBR technology for pharmaceutical industry wastewater removed over 95% of COD and 99% of BOD. | [26] |
Industrial– Breweries | 80,000–90,000 | 8000–65,000 | pH 5.1 TN 730–778 mg/L TP 367–385 mg/L | Highly loaded brewery wastewaters treated with P. ostreatus, COD removal rate was 77%. | [28] |
Industrial– Pulp and Paper | 6300–6500 | 860–950 | pH 5.5 TSS 1309 mg/L Intense colouration, dissolved lignin, high concentration of chlorinated compounds | Highly loaded wastewaters from the paper industry treated with Bacillus subtilis and Micrococcus luteus, COD removal percentage 97%, BOD 87% over 9 days. | [36] |
Municipal | 500–1200 | 200–600 | pH 7.5 TSS 258–282 mg/L TN 50–55 mg/L TP 7.4–7.5 mg/L Turbidity 221–244 NTU | Treatment in an aerobic MBR removed 89% of COD value. | [33] |
Environmental Components | Soil, Water, Sediment |
---|---|
Inoculum Concentration | Optimal amount of added autochthonous/exogenous microbiological cultures for a successful biodegradation process |
Oxygen Concentration | Depends on the specific needs of individual microorganisms; obligate aerobes, obligate anaerobes, facultative anaerobes, aerotolerant anaerobes, microaerophiles |
Metal Concentration | Essential metal concentration is necessary, heavy metal concentration is inhibitory |
Moisture | Depends on the environmental component; the optimal ratio is 60% |
Salinity | Halotolerant (0–5% NaCl), mildly to extremely halophilic microorganisms (2–30% NaCl) |
Nutrients (C:N:P) | 100:10:1 |
Temperature | 20–30 °C; enzyme activity range and highest efficiency of biodegradation |
pH | 6–8 |
Type of Method | Removal Efficiency | Applicability | Cost-Effectiveness | System Scalability | Environmental Footprint | Process Implementation Time | References |
---|---|---|---|---|---|---|---|
Biostimulation | Enhanced biodegradation increases with increased microbial activity, with an average improvement of 80% to over 90. Some by-products remain as partially degraded compounds. | In situ application for the treatment of contaminated soil layers and surface waters by adding nutrients, oxygen, or electron donors/acceptors. Ex situ application in reactor systems to optimise the biodegradation process. Possible complications include excessive stimulation of the process (overgrowth of biomass and lack of oxygen in the soil pores). | A cost-efficient process. The operating costs include the procurement of nutrients (substrate, nutrients, and oxygen) and transport vehicles to bring them to the intended location, without the need for expensive equipment. | High scalability for the specified process. Easy expansion of scalability from pilot plants to large wastewater treatment plants and contaminated areas. | It is an innovative green treatment method, as it only minimally disturbs the natural balance of ecosystems. No additional energy consumption is required. | The achievable contamination reduction is 50–70% over several months, depending on the initial contaminant load and the chosen treatment approach (in situ field application vs. ex situ reactor systems). | [53,64,65] |
Bioaugmentation | It significantly accelerates the degradation rate of persistent organic pollutants. Studies show varying effectiveness and the possibility of partial degradation of xenobiotics. Both indigenous and exogenous microbial communities require association with biostimulation techniques. | Broadly applicable for ex situ (biofilters, reactor systems) and in situ applications (field sites, surface water, and groundwater). Process control (C/N/P, pH, and dissolved oxygen) is required to maintain biomass viability and metabolic activity in the field. | Less costly than conventional physico-chemical treatment processes, as only reactors for the cultivation of biomass are required as process equipment. The process costs increase with the energy requirement if larger quantities of biomass have to be produced (aeration, mixing). | Favourable scale-up potential from laboratory to pilot plant and field applications but requires strain adaptation. Ex situ implementation is often limited by competing interactions between introduced strains and the indigenous microbiota. | Favourable ecological effects, as natural microorganisms are used as inoculum, thus eliminating the need for costly and aggressive chemicals. Particular caution is required when genetically modified strains are used, as they could be competitive with indigenous strains in the ecosystem. | When using tested microbial consortia and under controlled conditions, optimal degradation kinetics generally require weeks to months to fully remediate a site while maintaining environmental safety and reducing by-product production. | [56,66,67] |
In situ bioremediation | A number of variables influence efficacy, including chemical composition, bioavailability of contaminants to microorganisms, environment, and appropriate process control. | Application of a biodegradation technique in situ at the site of contamination without relocation. This includes techniques such as biosparging, bioventing, biostimulation, bioaugmentation, and phytoremediation, which require a minimum of physical intervention. | This approach is less costly than ex situ treatment as it does not require excavation, transport, or processing in specialised facilities. Infrastructure investment costs are limited to minor construction projects, process control equipment, biomass spraying systems and water recirculation devices. The overall implementation of the project takes longer. | High adaptability—the process can be adapted to the size of the contamination site. For smaller areas, there are technical solutions such as injection wells and special drainage systems, while for larger sites, methods for irrigation with nutrients or the application of biomass are used. Maintaining uniform process conditions proves difficult in extensive, heterogeneous areas. | The most environmentally sustainable remediation approach that only minimally disturbs the balance of ecosystems. As no material transport is required, the risk of secondary emissions is eliminated and environmental damage caused by excavation work is avoided. Energy consumption is limited to the operation of pumps and compressors. | The biodegradation process requires a longer duration, as natural degradation processes are slow by nature and often take years. This makes long-term monitoring necessary. For urgent remediation scenarios involving highly toxic contaminants, treatment in an ex situ reactor is a more suitable alternative. | [68,69,70] |
Ex situ bioremediation | Exceptionally high efficiency under controlled conditions enables complete degradation with more than 99% contaminant removal. Strict process control (pH, temperature, and agitation) combined with biofilters removes virtually all known organic contaminants. | Applicable when physical access to contaminated zones is possible, e.g., industrial wastewater streams. High implementation complexity with excavation, transport, multi-stage treatment, and subsequent by-product/sludge management. Requires constant monitoring by operators, full process automation, and comprehensive maintenance support. Technically more demanding than in situ processes. | Significant initial costs due to excavation, transport, reactor system, plant design, and waste management. Treatment is faster and more efficient, reducing long-term monitoring costs. Economic compensation can be achieved through anaerobic reactor treatment with biogas production. | The scalability is high—it ranges from small reactor systems for limited quantities of wastewater to larger technical units for the treatment of large quantities, which require higher investment costs. Spatial and temporal components become significant challenges for scaling. | Moderate sustainability and environmental footprint compared to passive methods; higher resource requirements for excavation/transport fuel and process energy requirements. Better resource utilisation is achieved through biogas production during anaerobic treatment or recycling of wastewater. Long-term benefits for the ecosystem result from the rapid removal of contaminants. | Rapid contaminant removal. In specially designed reactors with contaminant-specific inoculum, biodegradation takes place within days to weeks. Complete remediation of the site is achieved within months, whereas years are required for passive treatment methods. | [70,71,72] |
SBR (Sequencing Batch Reactor) | A well designed and operated SBR system achieves 90–98% removal of COD, BOD, and suspended solids. The system has proven itself with an 85% COD reduction in wastewater from the textile industry, 97% reduction in initial BOD5 levels in landfill leachate, and 95% ammonia removal. Batch operation improves microbial resistance to toxic conditions. | Excellent for wastewater treatment through different process cycles: inoculation, aeration, settling, and discharge of wastewater. Suitable for various wastewater streams, including landfill leachate, wastewater from the food/pharmaceutical industry, and wastewater from the agricultural industry. | A cost-effective and efficient process that does not require separate tanks, clarifiers, or sedimentation tanks—all treatment takes place in a single reactor tank, which significantly reduces investment costs. Although the operating costs include the energy required to implement the process, these are offset by the rapid completion of treatment and the high quality of the wastewater, resulting in long-term savings. | Excellent scalability: from household/commercial SBR units to large municipal SBR plants. Small systems use a single reactor, while larger plants require parallel SBR units (modular operation). Effective automatic cycle monitoring by the operators is essential. | Low environmental footprint. Space-efficient design eliminates the need for separate basins. Intermittent operating mode: no continuous oxygen supply required—aeration is phased (pumps are deactivated during settling and draining phases). Extended endogenous respiration reduces the production of active sludge as secondary waste. | A fast cyclical process with daily operating cycles of 5–8 h ensures a constant, visible daily treatment performance. Although the settling time is extended to 60 min, this duration is justified as it eliminates the need for additional clarifiers. | [73,74,75] |
MBR (Membrane Bioreactor) | A high-efficiency system—100% removal of suspended solids and up to 99% reduction in COD and BOD values. The wastewater often fulfils the legal discharge standards without the need for additional treatment. It is not effective at removing nutrients (N/P) unless designed with anoxic phases or chemical precipitation. It has the best removal efficiency compared to other biological treatment methods. | In practise, it is suitable for treating a wide range of municipal and industrial wastewater that place high demands on wastewater quality. The system can be used as a larger stationary plant or as a smaller mobile unit in containers. It is a complex treatment system that combines activated sludge and membrane processes. Automation is essential. It is the most technologically sophisticated of all biological treatment systems. | High costs in terms of investment and maintenance. In addition to the activated sludge module, additional filtration equipment such as cleaning systems, pumps, and similar components is required. Considerable energy expenditure for operation: sludge aeration and pressure for membrane processes. Additional filtration or disinfection is not required. The costs are justified by the high efficiency of the process. | Scaling is feasible in practice—from small modular field units to large municipal wastewater treatment plants. Most systems consist of several membrane modules. Larger scaling means higher costs, but also higher process efficiency (larger systems are more energy efficient per wastewater flow unit). | The high energy consumption means that more space is required, but this is offset by returning the wastewater to the cycle at a high quality. The production of sewage sludge is reduced by up to 30% compared to conventional biological methods, as the biomass remains in the system for longer. The plant requires less space, which minimises the need for construction. The process remains ecologically sustainable due to its high purification performance. | The targeted degradation of contaminants is achieved by a high inoculum mass, which enables treatment within a few hours. Membranes continuously separate the treated wastewater stream, eliminating the sedimentation time. This results in a fast, highly efficient treatment process with continuous water inflow and outflow. | [76,77,78] |
Contaminant Type | Chemical Formula | Natural Degradation Potential | Synthetic Degradation Potential | Reference |
---|---|---|---|---|
PAH (Polycyclic Aromatic Hydrocarbons) | CnHn | Pseudomonas aeruginosa, Mycobacterium sp., and Rhodococcus sp. | Cycloclasticus sp. P1 | [87,88] |
Phenol | C6H5OH | Microbial consortium: Acinetobacter sp., Bacillus sp., and Pseudomonas sp. | Rhodococcus sp. CS-1 | [89,90] |
Dioxins | C12H10-XClX | Bacillus megaterium, Norcardiopsis sp., and Geobacillus sp. | Sphingomonas wittichii RW1 | [91,92] |
Diesel | C12H23 | Bacillus cereus, Bacillus sphaericus, Bacillus fusiformis, and Acinetobacter junii | Pseudomonas fluorescens HK44, Pseudomonas putida KT2442 | [93,94] |
Heavy Metals (Cadmium) | Cd | Eichhorina crassipes, Thlaspi caerulescens | Escherichia coli JM109, Pseudomonas putida 06909, Bacillus subtilis BR151 (pTOO24) | [95] |
Pesticides (DDT) | C14H9Cl5 | Chryseobacterium sp., Trametes versicolor | Rhodococcus sp. IITR0 | [96,97] |
Pharmaceuticals (Erythromycin) | C37H67NO13 | Penicillium oxalicum RJJ-2, Penicillium restrictum, and Trametes versicolor | Delftia lacustris RJJ-61 | [98,99] |
Plastic (Polyethylene, PE) | (C2H4)n | Rhodococcus ruber, Penicillium simplicissimum, Streptomyces sp., and Brevibacillus borstelensis | Pseudomonas sp. AKS2 | [100,101] |
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Vuković Domanovac, M.; Volf, M.; Šabić Runjavec, M.; Terzić, I. Sustainable and Advanced Strategies for Bioremediation of Highly Contaminated Wastewater. Processes 2025, 13, 2250. https://doi.org/10.3390/pr13072250
Vuković Domanovac M, Volf M, Šabić Runjavec M, Terzić I. Sustainable and Advanced Strategies for Bioremediation of Highly Contaminated Wastewater. Processes. 2025; 13(7):2250. https://doi.org/10.3390/pr13072250
Chicago/Turabian StyleVuković Domanovac, Marija, Mirela Volf, Monika Šabić Runjavec, and Ivana Terzić. 2025. "Sustainable and Advanced Strategies for Bioremediation of Highly Contaminated Wastewater" Processes 13, no. 7: 2250. https://doi.org/10.3390/pr13072250
APA StyleVuković Domanovac, M., Volf, M., Šabić Runjavec, M., & Terzić, I. (2025). Sustainable and Advanced Strategies for Bioremediation of Highly Contaminated Wastewater. Processes, 13(7), 2250. https://doi.org/10.3390/pr13072250