Submitted:
22 May 2026
Posted:
25 May 2026
You are already at the latest version
Abstract

Keywords:
1. Introduction
2. Structure and Properties of Lignin
3. Lignin Conversion and Biochar Production
3.1. Pyrolysis of Lignin
3.2. Hydrothermal Carbonization
3.3. Process-Structure Relationships
4. Functionalization of Lignin-Derived Biochar
4.1. Chemical Activation
4.2. Heteroatom Doping
4.3. Metal Impregnation and Hybrid Functionalization
4.4. Surface Oxidation and Polarity Control
4.5. Functionalization-Performance Relationships
5. Applications of Lignin-Derived Biochar
5.1. Adsorption of Emerging Contaminants
5.1.1. Pharmaceuticals and Antibiotics
5.1.2. Personal Care Products and Endocrine-Disrupting Compounds
5.1.3. Microplastics and Nanoplastics
5.1.4. PFAS
5.2. Controlled Release Systems Based on Lignin-Derived Biochar
5.2.1. Controlled Release Fertilizers
5.2.2. Controlled Release of Pesticides
Herbicides
Insecticides and Other Pesticides
6. Challenges and Future Perspectives
6.1. Lignin Heterogeneity and Feedstock Variability
6.2. Limited Understanding of Molecular-Level Mechanisms
6.3. Process Optimization and Scalability
6.4. Balancing Adsorption Strength and Release Performance
6.5. Need for Lignin-Specific Studies
6.6. Functionalization and Hybrid Material Design
6.7. Environmental and Economic Assessment
6.8. Future Research Directions
7. Conclusions and Integration in the Circular Bioeconomy
Author Contributions
Conflicts of Interest
References
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| Lignin precursor | Pyrolysis / synthesis conditions | Activation / modification | Key properties | Dominant mechanism | Application / performance | Reference |
|---|---|---|---|---|---|---|
| Kraft lignin in black liquor | Pyrolysis (850 °C) | Self-activation + N-doping | Surface area: 1124 m²·g⁻¹; porous structure | π–π interactions, electrostatic attraction | Methyl orange adsorption | [52] |
| Kraft lignin | Microwave pyrolysis | H₃PO₄ activation | Surface area: 635–1055 m²·g⁻¹; micro/mesoporous | Pore filling, electrostatic interactions | Methylene blue and amoxicillin removal | [53] |
| Alkali lignin | Pyrolysis (800 °C) | Potassium tartrate activation | Surface area: 1911 m²·g⁻¹; microporous | π–π interactions, pore filling | Methyl orange adsorption | [54] |
| Organosolv lignin | Pyrolysis (500–900 °C) | H₃PO₄ activation | >1000 m²·g⁻¹; micro/mesoporous | Hydrophobic interactions, pore filling | Pharmaceutical adsorption | [55] |
| Lignosulfonate | Pyrolysis (850 °C) | CaCO₃ templating | Surface area: 2944 m²·g⁻¹; hierarchical porosity | Pore trapping, diffusion | Antibiotic adsorption | [56] |
| Biorefinery lignin | Pyrolysis (800 °C) | KHCO₃ + melamine (N-doping) | Surface area: 3423 m²·g⁻¹; highly porous | π–π interactions, electrostatic attraction | Methylene blue adsorption | [57] |
| Lignin (various) | Pyrolysis (600 °C) | ZnCl₂ activation | Developed porosity; aromatic structure | π–π interactions, pore filling | Dye adsorption | [39] |
| Lignin | Pyrolysis (900 °C) | FeCl₃ / H₃PO₄ / KOH activation | 467–1389 m²·g⁻¹; micro/mesoporous | Hydrophobic + electrostatic interactions | Nanoplastics adsorption | [58] |
| Lignin-based magnetic biochar | Hydrothermal (200 °C) | Fe₃O₄ modification | Magnetic, 152 m²·g⁻¹ | Electrostatic + redox interactions | Cr(VI) + dye removal | [59] |
| Organosolv lignin | NR | Fe₃O₄ nanoparticles | Functionalized surface | Adsorption + catalytic effects | Textile dye removal | [60] |
| Lignin precursor | Pyrolysis / synthesis conditions | Activation / modification | Key properties | Dominant mechanism | Application / performance | Reference |
|---|---|---|---|---|---|---|
| Industrial alkaline lignin (IAL) | Hydrothermal carbonization/activation; optimum synthesis reported at 220 °C | Porous carbon from IAL + urea, extrusion granulation | Specific surface area 1923.51–1935.5 m²·g⁻¹; pore volume 0.82 cm³·g⁻¹ | Nutrient adsorption in porous carbon + diffusion-limited release | Slow-release N fertilizer; soil-column tests showed lower cumulative leaching of NH₄⁺-N, NO₃⁻-N and total N than conventional urea | [78] |
| Wood-derived lignin + activated biochar | Bio-coating material prepared from wood waste; applied as coating on urea fertilizer | Palmitoyl-chloride-grafted lignin (PCL) + activated biochar (ABC) | Hydrophobic coating; water contact angle 90.72°; ABC with high surface area and hierarchical porosity | Hydrophobic barrier + pore-regulated ion transport | Coated slow-release urea; nitrogen release persistence for 40 days in soil; also reduced Cr accumulation in rice roots in hydroponics | [79] |
| Lignosulfonate / lignin sulfonate | Coating process for urea (not pyrolysis-based; lignin coating, not LDB) | Acetylation with decanoyl chloride to reduce hydrophilicity | Biodegradable coating membrane; diffusion coefficient modeled for N release | Diffusion-controlled release across lignin-derived coating | Controlled-release urea fertilizer; study demonstrates delayed nutrient transfer and models effective diffusion coefficient through the coating | [80] |
| Sodium lignosulfonate | High-speed emulsification + ultrasonic dispersion; crosslinking with p-phenylenediamine diazonium salt | Nano-delivery formulation | Particle size 80–150 nm; UV-shielding behavior | Encapsulation + pH-responsive diffusion/release | Avermectin nanoformulation; anti-photolysis stability reported as 3–4× that of free avermectin, with pH-responsive controlled release | [81] |
| Sodium lignosulfonate (self-assembled lignin microspheres) | Self-assembly of SL-CTAB colloidal spheres (not pyrolysis-based; lignin carrier, not LDB) | Surfactant-assisted microsphere formation | Uniform colloidal spheres; AVM encapsulation with high loading reported in abstract/snippet | Encapsulation + UV protection + sustained release | Avermectin carrier; lignin microspheres protect AVM against photodegradation and act as a controlled/sustained-release shell | [82] |
| Lignosulfonate granules | Enzymatic granulation using laccase (not pyrolysis-based; lignin carrier, not LDB) | 100% lignosulfonate-based biodegradable solid carrier | Granular biobased carrier | Matrix dissolution + diffusion-controlled herbicide release | Dicamba delivery; complete release after 48 h according to HPLC analysis | [83]) |
| Lignin particle-stabilized microcapsules | Pickering emulsion template + interfacial polymerization (not pyrolysis-based; lignin carrier, not LDB) | Lignin-polyurea microcapsules | Spherical capsules with double-layer shell; mean diameter 10–100 μm | Barrier-controlled sustained release + photoprotection | Avermectin carrier with anti-photolysis and sustained-release performance | [84] |
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