Synergistic Integration of Enzyme and Microbial Platforms for Sustainable Management of Pharmaceutical Pollutants: Towards a Greener Pharmaceutical Lifecycle
Simple Summary
Abstract
1. Dilemmas in Pharmaceutical Pollution Control: From Conventional Shortcomings to the Inevitability of Biological Synergy
1.1. Environmental Fate and Ecological Risks of Pharmaceutical Pollutants
1.2. Applicability Boundaries and Limitations of Conventional Treatment Technologies
1.3. Limitations of Single Biotechnology: Respective Dilemmas of Enzymatic Catalysis and Microbial Degradation
1.4. Synergistic Integration: The Inevitable Direction to Break Through Bottlenecks
2. Deconstruction of Synergistic Mechanisms: Complementarity and Enhancement of Enzyme and Microbial Platforms
2.1. Cascade Degradation: Temporal Coupling of Synergistic Catalysis
2.2. Symbiotic Protection: Contribution of Microbial Microenvironments to Enzyme Stability
2.3. Functional Complementarity: Unification of Rapid Initiation and Deep Mineralization
3. Construction of Synergistic Platforms: From Enhancement Strategies to Engineering Applications
3.1. Co-Immobilization Technology: Construction of Artificial Synergistic Systems
3.2. Biofilm Platforms: Natural Synergistic Ecosystems
3.3. Synthetic Biology-Engineered Bacteria: From Single Cells to Multifunctional Platforms
3.4. Treatment Efficacy for Typical Pharmaceutical Pollutants
4. Towards Green Pharmaceuticals: Closed-Loop Value and Future Prospects of Synergistic Governance
4.1. Paradigm Shift from End-of-Pipe Treatment to Full-Cycle Management
4.2. Closed-Loop Value of Synergistic Platforms: Resource Recovery and Process Integration
4.3. Challenges and Constraints: From Laboratory to Practical Application
4.4. Future Research Directions: Intelligent Regulation and Multi-Omics Guidance
5. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Drug Category | Representative Drug | Environmental Matrix | Detected Concentration Range | Main Sources | Ecological Risk (RQ) | References |
|---|---|---|---|---|---|---|
| Antibiotics | Ciprofloxacin | Surface water | nd–14.3 μg/L | Aquaculture wastewater, domestic sewage | 3.5–40.6 | [4,6,7] |
| Sulfamethoxazole | Surface water | nd–2.8 μg/L | Domestic sewage, medical wastewater | 0.1–3.53 | [4,6,16] | |
| Tetracycline | Sludge | 89–2300 μg/kg | Aquaculture wastewater | - | [10,16] | |
| Ofloxacin | Sludge | 2300 μg/kg (average) | Domestic sewage | - | [16] | |
| Anti-inflammatory drugs | Diclofenac | Surface water | nd–1.2 μg/L | Domestic sewage | <0.1 | [12,16] |
| Ibuprofen | WWTP effluent | 0.1–2.5 μg/L | Domestic sewage | <0.1 | [12,13] | |
| Hormones | Octylphenol | Sludge | 1179 ng/g (average) | Industrial/domestic sewage | - | [12] |
| Triclosan | Sludge | 1505 ng/g (average) | Personal care products | - | [12] | |
| Antiviral drugs | Various ARVs | Surface water | nd–3.2 μg/L | Medical wastewater | To be assessed | [6,18] |
| Pesticides | Diuron | Surface water | nd–0.8 μg/L | Agricultural runoff | 0.1–0.5 | [15,19] |
| Technology Type | Removal Mechanism | Advantages | Disadvantages | Example Drug Applications | References |
|---|---|---|---|---|---|
| Coagulation–flocculation | Charge neutralization, bridging adsorption | Simple operation, low cost, suitable for large scale | Low removal efficiency for dissolved drugs, large sludge production | Hydrophobic drugs | [1] |
| Adsorption | Physical/chemical adsorption | High removal rate, simple equipment | Phase transfer only (non-degradative), high adsorbent regeneration cost | Multiple drugs | [21,22] |
| Membrane separation | Sieving, charge repulsion | High separation efficiency, no chemical addition | Membrane fouling, high energy consumption, difficult concentrate disposal | Large molecule drugs | [23] |
| Electrocoagulation | In situ coagulant generation | Wide applicability, no external chemicals required | High energy consumption, electrode consumption | Antibiotics | [24,25] |
| Ozonation | Direct oxidation/·OH oxidation | Rapid reaction, no sludge production | Potential generation of toxic byproducts, complex equipment | Drugs with unsaturated structures | [26] |
| Photocatalysis | ·OH oxidation | Complete mineralization possible, utilizes solar energy | Difficult catalyst recovery, limited scalability | Multiple drugs | [27,28,29] |
| Electrochemical oxidation | Direct/indirect oxidation | Strong oxidation capacity, good controllability | High energy consumption, limited electrode life | Refractory drugs | [26,30] |
| Fenton oxidation | ·OH oxidation | Rapid reaction, simple equipment | Narrow pH range applicability, iron sludge generation | Multiple drugs | [26,30] |
| Environmental Factor | Primary Inactivation Mechanism | Molecular-Level Explanation | Representative Data/Case | Reference(s) |
|---|---|---|---|---|
| pH deviation from optimum | Alteration of active site ionization state; induction of non-native association/aggregation | Change in protonation state of catalytic residues; surface charge alterations leading to aggregation | EstGtA2 forms a non-native associated state (300 nm apparent particle size) resistant to unfolding up to 95 °C at specific pH | [36] |
| Elevated temperature | Enhanced thermal vibration; conformational collapse; activity/stability trade-off | Disruption of hydrogen bonds and hydrophobic interactions; competition between kinetic acceleration and inactivation | Laccase tends to inactivate above 45 °C | [37] |
| High ionic strength | Charge screening promoting aggregation; direct inhibition of active sites | “Salting-out” effect disrupting the hydration layer; interference with metal cofactors by metal ions/halides | Fe(III) and Cu(II) significantly inhibit BPA conversion | [37] |
| Combined stress (pH + temperature) | Synergistic acceleration of inactivation | Inactivation follows first-order kinetics (kd); faster inactivation as conditions deviate from optimum | Serine protease exhibits minimal kd at pH 9 and 37 °C | [38] |
| Parameter | Free Enzyme | Immobilized Enzyme | Improvement Factor | Reference(s) |
|---|---|---|---|---|
| Unit cost | ~1 USD/cm3 | ~0.107 USD/cm3 | ~90% reduction | [43] |
| Residual activity after 6 h at 50 °C | 40.63% | >85% | ~2-fold increase | [44] |
| Residual activity after 6 h UV exposure | 7.23% | 92.88% | ~13-fold increase | [44] |
| Optimal temperature | 50 °C | 55–60 °C | 5–10 °C increase | [45] |
| Number of reusability cycles | 1 | 9 cycles with ~50% retention | Multiple cycles | [46] |
| Storage stability | Days to weeks | >50% activity after 8 weeks | Significantly extended | [46] |
| Synergy Strategy | Specific Technology | Carrier/Platform | Key Features | Advantages | Limitations |
|---|---|---|---|---|---|
| Co-immobilization | Polymer entrapment | Alginate, PVA | Physical entrapment | Simple operation, low cost | High mass transfer resistance |
| COF immobilization | Covalent organic frameworks | Porous armor, co-localization | Enzyme protection, good substrate diffusion | Complex synthesis | |
| MOF immobilization | Metal–organic frameworks | High surface area, tunable pore size | High stability | Biocompatibility needs optimization | |
| Mimetic microcompartment composite | Ferritin shell | Multi-enzyme assembly, cofactor cycling | 7× efficiency ↑, 10× cost ↓ | Complex design | |
| Biofilm | Natural biofilm | EPS matrix | Extracellular enzyme retention, community metabolism | High stability, self-renewal | Difficult regulation |
| Engineered biofilm | CsgA scaffold | SpyTag/SpyCatcher fusion | Modular design, programmable | Long construction cycle | |
| Cofactor regulation | Biofilm | Induced formation by cofactor exchange | Enhanced stress tolerance | Complex mechanism | |
| Engineered bacteria | Surface display | Bacterial surface | Enzymes displayed on cell surface | Overcomes substrate transmembrane limitation | Limited display efficiency |
| Intracellular expression | Cytoplasm | Intracellular expression of engineered enzymes | Utilizes intracellular metabolism | Substrates require transmembrane transport | |
| Multi-enzyme intracellular assembly | Artificial microcompartment | Mimics bacterial microcompartments | Efficient cascade catalysis | Difficult assembly |
| Drug Category | Specific Drug | Synergy Platform Type | Platform Composition | Experimental Conditions | Removal Efficiency | Key Findings | Cost Analysis |
|---|---|---|---|---|---|---|---|
| Tetracyclines | Tetracycline | Mimetic microcompartment multi-enzyme complex | FerTiG (Tet(X4) + GDH + Ferritin) | Glucose-driven, room temperature | >90% (24 h) | 10× cost reduction, 7× efficiency improvement, strong stress resistance | 10-fold cost reduction via cofactor recycling; glucose as low-cost driving fuel |
| Fluoroquinolones | Ciprofloxacin | Engineered biofilm | E. coli CsgA-laccase fusion | Flow system, room temperature | 85% (48 h) | Long-term stable operation, modular design | Economical due to self-regenerating biofilm; no external enzyme supplementation required |
| Sulfonamides | Sulfamethoxazole | Microbial consortium + enzyme | Oriented microbial consortium-based compound enzyme | Wastewater treatment conditions | 70–80% | Simultaneous ARGs removal | Cost-effective using agricultural/food residues (vine pruning, brewer’s spent grains) as enzyme production substrate; 50 U·L−1 low enzyme concentration |
| Anti-inflammatory drugs | Diclofenac | Laccase + microorganism | Free laccase + activated sludge | Batch experiment | 75% | Laccase pretreatment enhances biodegradation | Moderate cost; reduces subsequent biotreatment burden |
| Pesticides | Diuron | Engineered bacteria (intracellular expression) | B. megaterium expressing CYP450 BM3 | TB medium | 65% (5 d) | 45% in synthetic wastewater, 15% in municipal wastewater | Requires IPTG induction; cost of heterologous expression system |
| Diuron | Engineered microalgae (chloroplast expression) | C. reinhardtii expressing CYP450 BM3 | Light culture | 52% | Wild type only 6% | Lower cost than bacterial system; light-driven, no inducer required | |
| Plastic monomers | PET (methodological reference) | Surface displays dual enzymes | E. coli displaying PETase + MHETase | 37 °C | 3.85 mM/d | 51× improvement over free enzyme, reusable | High reusability (3 cycles retain 30% activity); reduces long-term costs |
| Multiple drugs | 14 drugs | WWTP (biofilm) | Activated sludge process | Actual WWTP | >90% (majority) | Triclosan and octylphenol still persisted in sludge | Low operational cost for existing infrastructure; sludge disposal adds expense |
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Share and Cite
Sun, Z.; Chen, P.; Ge, X.; Zhang, W.; Liu, H. Synergistic Integration of Enzyme and Microbial Platforms for Sustainable Management of Pharmaceutical Pollutants: Towards a Greener Pharmaceutical Lifecycle. Biology 2026, 15, 804. https://doi.org/10.3390/biology15100804
Sun Z, Chen P, Ge X, Zhang W, Liu H. Synergistic Integration of Enzyme and Microbial Platforms for Sustainable Management of Pharmaceutical Pollutants: Towards a Greener Pharmaceutical Lifecycle. Biology. 2026; 15(10):804. https://doi.org/10.3390/biology15100804
Chicago/Turabian StyleSun, Zhongshan, Peitao Chen, Xiangyang Ge, Weiguo Zhang, and Huanmin Liu. 2026. "Synergistic Integration of Enzyme and Microbial Platforms for Sustainable Management of Pharmaceutical Pollutants: Towards a Greener Pharmaceutical Lifecycle" Biology 15, no. 10: 804. https://doi.org/10.3390/biology15100804
APA StyleSun, Z., Chen, P., Ge, X., Zhang, W., & Liu, H. (2026). Synergistic Integration of Enzyme and Microbial Platforms for Sustainable Management of Pharmaceutical Pollutants: Towards a Greener Pharmaceutical Lifecycle. Biology, 15(10), 804. https://doi.org/10.3390/biology15100804

