Research Progress in Chitin/Chitosan-Based Biomass Adhesives: Extraction Processes, Composite and Chemical Modification
Abstract
1. Introduction
2. Fundamental Characteristics of Chitin/Chitosan
3. Preparation and Purification Technologies of Chitin/Chitosan
3.1. Source of Raw Materials
3.2. Extraction Process
3.3. Structure and Performance Characterization
3.4. Performance Testing Framework for Chitin-Based Biopolymer Adhesives
3.5. Correlation of Key Parameters with Bonding Performance in Chitosan-Based Adhesives
3.6. Performance Comparison Between Composite-Modified Adhesive and the Original Adhesive
3.7. Main Application Fields of Chitosan and Its Chemically Modified Derivatives
4. Preparation Technology of Chitin/Chitosan-Based Biomass Adhesives
4.1. Pure Chitosan Adhesive
4.2. Composite-Modified Adhesive
4.2.1. Composite with Natural Polymers
4.2.2. Composite with Synthetic Polymer
4.2.3. Nano-Composite Modification
4.3. Chemically Modified Adhesive
4.3.1. Crosslinking Modification
4.3.2. Graft Copolymer Modification
4.3.3. Functional Modification
4.4. Biomineralization and Biomimetic Adhesive Design
4.4.1. Simulated Biological Adhesion Mechanism
4.4.2. Strategies for Enhancing Biomineralization
5. Conclusions and Future Outlook
5.1. Conclusions
- Research Progress and Mechanisms of Chitin/Chitosan-Based Biomass Adhesives
5.2. Current Challenges
5.3. Future Development Direction
Author Contributions
Funding
Institutional Review Board Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Raw Material Category | Specific Source | Main Distribution Acquisition Pathway | Chitin/Chitosan Content (dry weight) | Advantages & Characteristics | References |
|---|---|---|---|---|---|
| Marine Biomass Waste | Shrimp shells (e.g., Penaeus, Macrobrachium) | Seafood processing waste; global annual production exceeds 6 million tons, concentrated in coastal fishery processing zones | Chitin: 15–25%; Chitosan (after deacetylation): 8–18% | Centralized source, large output, mature extraction process, high industrial potential | [41,42,43] |
| Crab shells (e.g., Portunus, Scylla) | Seafood processing waste; annual production exceeds 3 million tons; chitin content higher than shrimp shells | Chitin: 20–30%; Chitosan (after deacetylation): 12–22% | High chitin purity, lower impurity (protein, mineral) content, relatively low extraction cost | [1,42,44,45] | |
| Lobster shells (e.g., Homarus americanus) | High-end seafood processing waste; mainly distributed in North America, Europe, and coastal China | Chitin: 18–28%; Chitosan (after deacetylation): 10–20% | Large chitin molecular weight, excellent mechanical properties, suitable for high-performance adhesive raw materials | [43,46] | |
| Other Sources | Cicada slough (e.g., Cryptotympana atrata) | Terrestrial insect waste; widely distributed in temperate and subtropical regions; obtainable via manual collection or farming | Chitin: 10–18%; Chitosan (after deacetylation): 6–14% | Free from marine salt impurities; no complex desalting steps required during extraction; product purity easily controlled | [42,47] |
| Fungal cell walls (e.g., yeast, mold) | Microbial fermentation industry waste (e.g., Saccharomyces cerevisiae residue); artificially cultured fungi (e.g., Aspergillus niger) | Chitin: 5–12%; Chitosan (naturally present in some fungi): 3–8% | Scalable production via microbial fermentation; not limited by season or geography; composition easily adjustable | [48,49] | |
| Squid cartilage, Cuttlebone | Cephalopod seafood processing waste; relatively low yield; concentrated in deep-sea fishery processing zones | Chitin: 8–15%; Chitosan (after deacetylation): 5–10% | Unique chitin structure (low crystallinity), good solubility, easy modification, suitable for biomedical adhesives | [43,49] |
| Process Category | Specific Process Step | Core Parameters | Process Characteristics | Application Suitability (Adhesive Scenarios) | References |
|---|---|---|---|---|---|
| Traditional Extraction Methods | Demineralization (Acid/Alkali Method) | Acid type: Hydrochloric acid/Sulfuric acid; Concentration: 5–15%; Temperature: 20–80 °C; Time: 1–6 h; Solid-to-liquid ratio: 1:10–1:20 | High efficiency in removing calcium salts and other minerals (removal rate > 95%), low cost, industrially mature, but high acid consumption, prone to equipment corrosion and wastewater pollution | Suitable for large-scale production of general wood adhesive raw materials, e.g., chitin extraction from shrimp/crab shells; subsequent neutralization required to treat residual acid | [52,53] |
| Deproteinization (Acid/Alkali Method) | Alkali type: Sodium hydroxide; Concentration: 4–10%; Temperature: 60–100 °C; Time: 2–8 h; Solid-to-liquid ratio: 1:8–1:15 | Protein removal rate > 90%, process easily controlled, but high temperature and strong alkali may degrade chitin molecular chains and reduce molecular weight | Suitable for preparing medium- to low-strength adhesives (e.g., paper bonding); subsequent molecular weight adjustment needed to avoid insufficient bonding strength | [54,55] | |
| Deacetylation (Preparation of Chitosan) | Alkali type: Sodium hydroxide; Concentration: 30–50%; Temperature: 80–120 °C; Time: 2–10 h; Stirring rate: 100–300 rpm | Controllable degree of deacetylation (DD) (50–95%), but energy-intensive, difficult alkali recovery, and may cause chitosan degradation | Adjustable DD to suit different adhesives: High DD (>80%) chitosan, with more amino groups, suitable for cross-linking with aldehydes to prepare high-strength wood adhesives | [49,56] | |
| Green Extraction Technologies | Enzymatic Hydrolysis (Deproteinization/Demineralization) | Enzyme type: Protease (alkaline/neutral protease), phosphatase; Enzyme activity: 1000–5000 U/g; Temperature: 30–50 °C; pH: 6–9; Time: 4–12 h | Environmentally friendly, non-corrosive, protein removal rate > 85%, minimal damage to chitin molecular chains, but enzyme cost is high (approximately 2–3 times that of acid/alkali method) and reaction cycle is long | Suitable for high-purity adhesive raw materials (e.g., medical/dental adhesives), avoiding chemical residue affecting biocompatibility | [57,58,59] |
| Microbial Fermentation (Full-process Extraction) | Strain: Bacillus/Yeast; Fermentation temperature: 25–37 °C; pH: 5–8; Fermentation time: 24–72 h; Carbon-to-nitrogen ratio: 10–20:1 | Simultaneous demineralization and deproteinization, no chemical reagents required, high product purity (chitin purity > 90%), but fermentation cycle is long and yield is low | Suitable for laboratory-scale small-batch preparation of high-purity chitosan for antibacterial adhesives (e.g., composite adhesives inhibiting wood mold) | [60,61] | |
| Ultrasound/Microwave-Assisted Extraction (Enhanced Demineralization/Deproteinization) | Ultrasound power: 200–500 W; Microwave power: 300–800 W; Assistance time: 10–60 min; Combined with acid/alkali method | Reduces traditional process time by 30–60%, lowers acid/alkali consumption by 20–40%, but requires specialized equipment and has high scale-up costs | Adaptable for upgrading existing industrial acid/alkali methods, improving production efficiency of wood adhesive raw materials and reducing energy consumption | [62,63,64,65] | |
| Purification & Refining Processes | Impurity Removal (Decolorization/Desalting) | Decolorizing agent: Activated carbon/Hydrogen peroxide; Concentration: 1–5%; Temperature: 40–60 °C; Desalting: Deionized water dialysis/Ion exchange resin | Decolorization rate > 80%, ash content reduced to <1%, but activated carbon may adsorb some chitosan, reducing recovery yield | Used for high-transparency adhesives (e.g., packaging adhesives) or medical adhesives, avoiding impurities affecting appearance and biosafety | [66] |
| Degree of Deacetylation (DD) Control | Stepwise deacetylation: Multiple treatments with low-concentration alkali (10–20% NaOH); Temperature gradient: 60 → 80 → 100 °C; Time: 1–3 h/step | DD precision control ±2%, enabling preparation of chitosan with specific DD (e.g., 60%, 80%) to meet different cross-linking requirements | High DD (>80%) suitable for aldehyde cross-linking (e.g., dialdehyde starch); low DD (50–60%) suitable for acidic cross-linking (e.g., citric acid); used for wood/paper adhesives | [67,68] | |
| Molecular Weight Control (Degradation/Fractionation) | Degradation: Hydrogen peroxide (concentration 0.5–2%)/Ultrasound (300–600 W); Fractionation: Ethanol precipitation (concentration 30–70%) | Molecular weight adjustable from 1 × 104 to 1 × 106 Da, narrow distribution (PDI 1.2–1.8), but degradation may introduce oxygen-containing impurities | Low molecular weight (<1 × 105 Da) chitosan suitable for low-viscosity coating adhesives (e.g., plywood); high molecular weight (>5 × 105 Da) used for high-strength structural adhesives | [69] |
| Adhesive Type | Curing Temperature | Curing Time | Curing Pressure | Test Standard | Reference |
|---|---|---|---|---|---|
| CS-PAA@Ca2+ | 120 °C | 6.5 min | 1 MPa | Industry-standard severe “4+4+1” test: boiling water immersion for 4 h → drying for 20 h → boiling water re-immersion for 4 h → cold water immersion for 1 h, followed by testing | [86] |
| Hemicellulose–Chitosan Composite Adhesive | 120 °C | 2.5 min | 1.67 MPa | European Standards EN 204, EN 205 | [87] |
| SM/DCS Composite Adhesive | 120 °C | 6 min | 1 MPa | No specific standard; experimental conditions: 30 °C, 99% relative humidity (RH), continued for 30 d, observing mold growth | [13] |
| CSC-G Carboxylated Chitosan–Glucose Adhesive | 140–200 °C (optimum 160 °C) | 1–10 min (optimum 3 min) | 1 MPa | Chinese Standards GB/T 9846-2015, GB/T 17657-2013 | [72] |
| Chitosan–Dopamine Composite Adhesive | Room temperature—120 °C | 2 h | Adjusted as needed (no explicit pressure specified in some cases) | No specific standard; experimental conditions applied | [88] |
| Key Parameter | Influence Pattern on Bonding Performance | Specific Manifestations | References |
|---|---|---|---|
| Degree of Deacetylation (DD) | Positive correlation dominates; higher DD favors improved bonding strength and water resistance. | When DD ≥ 90%, wet shear strength is significantly increased (e.g., reaching 1.40 MPa for CS-PB adhesive). Increased amino group (-NH2) content enhances hydrogen bonding/electrostatic interactions with wood hydroxyl groups and crosslinking reactivity. Excessively high DD (>95%) may reduce solubility due to increased crystallinity, slightly weakening interfacial bonding. | [9,89,90] |
| Molecular Weight (Mw) | Medium molecular weight (50,000–300,000 Da) is optimal; too low or too high is detrimental. | Low Mw (<50,000 Da): High penetration but weak cohesion, dry shear strength < 1.5 MPa. Medium Mw: Balances penetration and cohesion, dry shear strength can reach 2.3–5.6 MPa. High Mw (>500,000 Da): High viscosity, poor penetration, prone to forming “starved glue lines,” resulting in decreased wet strength. | [71] |
| Crosslinking Density | Moderate crosslinking is optimal; either too high or too low impairs performance. | Low crosslinking density: Loose network, poor water resistance (wet strength < 0.5 MPa). Moderate crosslinking (e.g., GL/C = 1:1): Forms a dense three-dimensional network, achieving dry strength > 2.0 MPa and wet strength > 0.8 MPa. Excessively high crosslinking density: Increased brittleness, stress concentration at the interface, leading to decreased bonding strength. | [21,90] |
| Reagent Name | Reagent Type | Function Description | Reference |
|---|---|---|---|
| Sodium Tripolyphosphate (TPP) | Ionic Crosslinking Agent | Interacts electrostatically with the amino groups of chitosan to form ionic crosslinks, facilitating the preparation of nanoparticles and enhancing their stability and dispersibility. | [96] |
| Glutaraldehyde | Covalent Crosslinking Agent | Undergoes a Schiff base reaction with chitosan amino groups to form imine crosslinks, constructing a porous network structure that enhances adsorption capacity and thermal stability. | [30] |
| Citric Acid (CA) | Crosslinker/Solvent | Dissolves chitosan and facilitates supramolecular self-assembly via ionic and hydrogen bonding. After hot-pressing, ester and amide bonds form, enabling viscosity modulation and improving water resistance. | [9] |
| Glycerol Triglycidyl Ether (GTE) | Epoxy Modifier | Epoxidizes lignosulfonate by introducing epoxy groups, enhancing crosslinking reactions with amino and hydroxyl groups of chitosan, and constructing a dense three-dimensional network. | [21] |
| 1,4-Phenylenediboronic Acid (PBA) | Dynamic Covalent Crosslinker | Forms boronic ester dynamic bonds with lignin-derived 3,4-dihydroxybenzaldehyde, which subsequently reacts with chitosan amino groups to form imine bonds, endowing the adhesive with recyclability and high bonding strength. | [90] |
| Poly(sodium 4-styrenesulfonate) (PSS) | Polyanionic Electrolyte | Forms polyelectrolyte complexes (PECs) with cationic chitosan via electrostatic interactions, stabilizing the system. Simultaneously, π-π stacking occurs with lignin, improving compatibility. | [9] |
| 3,4-Dihydroxybenzaldehyde (DBA) | Functional Monomer/Crosslinking Intermediate | Reacts with 1,4-phenylenediboronic acid to generate a dialdehyde-containing monomer, which then forms imine bonds with chitosan, constructing a dynamic crosslinked network that enhances bonding strength and mildew resistance. | [90] |
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Luo, Y.; Zhang, Z.; Zuo, J.; Zhang, L. Research Progress in Chitin/Chitosan-Based Biomass Adhesives: Extraction Processes, Composite and Chemical Modification. Polymers 2026, 18, 337. https://doi.org/10.3390/polym18030337
Luo Y, Zhang Z, Zuo J, Zhang L. Research Progress in Chitin/Chitosan-Based Biomass Adhesives: Extraction Processes, Composite and Chemical Modification. Polymers. 2026; 18(3):337. https://doi.org/10.3390/polym18030337
Chicago/Turabian StyleLuo, Yizhang, Ziying Zhang, Jiachen Zuo, and Libo Zhang. 2026. "Research Progress in Chitin/Chitosan-Based Biomass Adhesives: Extraction Processes, Composite and Chemical Modification" Polymers 18, no. 3: 337. https://doi.org/10.3390/polym18030337
APA StyleLuo, Y., Zhang, Z., Zuo, J., & Zhang, L. (2026). Research Progress in Chitin/Chitosan-Based Biomass Adhesives: Extraction Processes, Composite and Chemical Modification. Polymers, 18(3), 337. https://doi.org/10.3390/polym18030337
