Chemical Transformations and Papermaking Potential of Recycled Secondary Cellulose Fibers for Circular Sustainability
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Abstract
1. Introduction
1.1. Global Context: Cellulose Fibers as Renewable Resources and the Circular Economy in the Paper Industry
1.1.1. Cellulose Fibers as Renewable Biomaterials
1.1.2. The Paper Industry and the Circular Economy
1.2. Significance of Recycling Waste Paper for Sustainability
2. Sources and Properties of Secondary Cellulose Fiber
2.1. Overview of Primary vs. Secondary Fibers
2.2. Main Waste Paper Sources
2.3. Quality Parameters and Contaminants Affecting Fiber Chemistry
3. Chemical and Structural Effects of Fiber Recycling
3.1. Dimensional and Morphological Changes
3.2. Chemical Composition and Functional Group Alterations
3.3. Chemical and Enzymatic Modification Strategies for Recycled Fibers
3.3.1. Cellulose Nanomaterials from Recycled Pulp and Their Use in Recycled Paper
3.3.2. Green Functionalization Routes: Cationic/Biobased Systems and Surface Modification
3.3.3. Synergistic Enzyme Systems and Integration with Biorefinery Concepts
3.4. Hornification and Fiber Swelling Behavior
3.5. Crystallinity and Cell Wall Structure
3.5.1. From Hydrated Networks to Compact Walls
3.5.2. Crystallinity Changes and What They Mean
3.5.3. Pore Size Distribution and Accessibility
3.5.4. Microfibril Arrangement and Mechanics
3.5.5. How Refining and Treatments Interact with Crystallinity
3.5.6. Tools to Measure and Monitor
- XRD/WAXS for CI, crystallite size, and peak broadening;
- Solid-state 13C NMR for crystalline vs. amorphous fractions and paracrystalline disorder;
- FTIR/Raman band ratios linked to order and hydrogen-bonding environment;
- WRV/FSP and NMR relaxometry for bound water and accessible porosity;
- AFM/SEM for surface fibrillation and wall densification.
3.5.7. Implications for Circular Use
3.6. Surface Chemistry and Fiber Reactivity
3.7. Fines Formation and Its Role in Recycled Fiber Systems
3.7.1. Origins and Types of Fines in Recycling
3.7.2. Effects of Fines on Suspension Behavior, Drainage, and Retention
3.7.3. Contributions of Fines to Sheet Structure and Properties
3.7.4. Chemical Interactions and “Anionic Trash”
3.7.5. Interplay with Hornification and Crystallinity
3.7.6. Process Control and Management Strategies
- Fractionation and white-water management. Hydrocycloning and fine-screening can remove grit and macro-contaminants while allowing retention of beneficial fibrillar fines. White-water clarification (DAF, save-all filters) prevents uncontrolled fines accumulation and closes the mass balance without overloading the headbox [72,83].
- Optimized refining. Light, targeted refining increases external fibrillation (beneficial fines) without excessive fiber cutting that would flood the system with detrimental fines. Refining intensity and specific edge load should be tuned to grade: packaging vs. print/tissue require different fines spectra [103,131].
- Retention/fixation programs. Sequential addition of fixatives (e.g., polyamines, PAC) to immobilize anionic trash on fines, followed by strength aids and a microparticle system, improves fines capture and drainage. Proper ionic strength and pH enhance floc architecture and release in the forming zone [53,64,104,132].
3.7.7. Implications for Circular Performance
3.8. Influence of Additives, Fillers, and Contaminants on Fiber Chemistry
3.9. Relationship Between Chemical and Morphological Degradation of Recycled Fibers
3.9.1. Drying-Induced Coupling: From Chemistry to Structure
3.9.2. Accessibility Feedbacks: From Structure Back to Chemistry
3.9.3. Hemicellulose Depletion and Fines Formation: Chemical–Mechanical Interactions Governing Bonding in Recycled Fibers
3.9.4. Lignin Oxidation Pathways and the Optical–Mechanical Tradeoffs in Recycled Fiber Systems
3.9.5. Surface Charge Dynamics, Contaminant Interactions, and Their Impact on Fiber Network Mechanics
3.9.6. Macroscopic Manifestations of Coupled Chemical and Morphological Degradation in Recycled Cellulose Fibers
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- Lower tensile, burst, and often tear strength, attributable to shorter, stiffer fibers with reduced bonding area and to chemically weakened chains (lower DP).
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- Slower drainage and higher steam demand, caused by fines build-up and altered surface charge; densified walls also release water less readily in pressing.
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- Greater variability in sizing and printability, due to mosaic hydrophilicity/hydrophobicity from residual sizes and latexes on less-wettable surfaces.
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- Higher cationic demand and unstable wet-end chemistry, reflecting the combined effects of increased carboxyls, DCSs, and mineral fines.
3.9.7. Integrated Diagnostics for Correlating Chemical, Structural, and Performance Metrics Across Scales
- WRV/FSP (swelling) and XRD/FTIR/NMR (apparent crystallinity and hydrogen-bonding environment) to track hornification.
- DP (viscometry or SEC) for cellulose chain length; zeta potential and cationic demand for surface charge state.
- AFM/SEM for fibrillation and surface topography; fines/ash fractionation to characterize the fines spectrum.
3.9.8. Coupled Mitigation Strategies Integrating Chemical, Morphological, and Process Controls in Recycled Fiber Systems
- Gentle, targeted refining to restore external fibrillation and reopen access without excessive cutting (controls morphology, improves chemistry access).
- Selective enzymatic conditioning (low-dose endoglucanase/xylanase) or mild surface carboxymethylation to expose/reactivate sites and accelerate polymer uptake, while avoiding deep chain scission (improves chemistry, aided by morphological reopening).
- Wet-end sequencing (fixative → strength aid → microparticle) with ionic-strength/pH control to out-compete DCSs and stabilize floc architecture (chemistry control supporting structure).
- Contaminant management (detackifiers, talc, enhanced screening/DAF) to reduce hydrophobe carryover that would otherwise lock in poor wettability on densified walls.
- Drying profile moderation (temperature and residence time) and periodic virgin fiber supplementation to limit step-changes in hornification and restore long-fiber bonding scaffolds.
3.10. Mitigation Strategies and Chemical Approaches to Preserve Fiber Integrity
3.10.1. Physical and Process-Based Mitigation
3.10.2. Enzymatic and Biochemical Treatments
3.10.3. Chemical Surface Modification
3.10.4. Wet-End Chemistry Optimization
3.10.5. Thermal and Drying Control
3.10.6. Integrated Approach and Future Outlook
4. Influence of Recycled and Reused Fibers on Papermaking Performance
4.1. Impact of Recycled and Reused Secondary Cellulose Fibers on Paper Strength and Quality
4.2. Mechanical, Structural, and Surface Property Evolution in High-Recycled-Content Papers
4.3. Effect of Recycled and Reused Fibers on Dewatering and Drying Behavior
4.4. Influence of Recycling Cycles of Fibers on Paper Quality: Evolution of Mechanical and Optical Parameters with Successive Reuse
4.4.1. Mechanical Properties: Typical Trajectories Across Cycles
4.4.2. Optical Properties: Brightness, Shade, Opacity, and Print Uniformity
5. Environmental and Economic Impact of Fibers Recycle and Reuse
5.1. Comparison of Energy, Water, and CO2 Footprints: Primary vs. Secondary Fibers
- Recycled pulping avoids wood preparation and most chemical pulping stages, so total process energy per tonne is typically lower. Literature and industry LCAs report 20–60% lower process energy for many recycled grades compared with virgin equivalents, with the upper end for de-inking-free streams (e.g., Old Corrugated Containers (OCC) for packaging) and the lower end where de-inking and high consistency dispersion are required. Mills equipped with CHP/cogeneration further reduce the cradle-to-gate footprint by displacing grid electricity and improving steam efficiency [26,31].
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- Recycled mills often operate with tighter water circuits; despite wash steps in de-inking, specific make-up water can be similar or lower than virgin mills when white-water closure and DAF are implemented. Reported savings range from 15 to 50% relative to virgin kraft baselines, but local water management (e.g., loop closure vs. purge for DCS control) drives outcomes [135,178].
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- Several mechanisms reduce net GHGs: (i) avoided landfill prevents methane from anaerobic decomposition of paper, (ii) lower process energy (especially with CHP/renewables) cuts Scope 1–2 emissions, and (iii) biogenic carbon retention in recycled products extends storage time. Practical, cited rules-of-thumb indicate that recycling one tonne of paper avoids both energy use and GHG emissions, while meta-analyses show 20–70% lower cradle-to-gate GHG intensity depending on furnish and mill configuration [24,29]. When de-inking is intensive and electricity is carbon-intensive, the advantage narrows; conversely, clean OCC streams in efficient mills deliver the largest benefit.
5.2. Economic Efficiency: Cost Savings, Employment, and Waste Reduction
5.3. Contribution to the Circular Economy and Resource Conservation
5.3.1. Pathways Toward Circularity and Sustainable Resource Utilization
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- Material circularity:
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- Forest and biodiversity pressure:
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- Water and chemical stewardship:
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- Design for recyclability
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- System value restoration
5.3.2. Practical Implications for Mills and Policymakers
- Pair collection quality (source-separated streams, EN 643 adherence) with mill-side contaminant control (detackifiers, improved screening, DAF) to maximize both environmental gains and economic yield.
- Invest in energy efficiency and CHP to compound the GHG advantage of recycled operations; monitor steam per tonne and drying profiles to capture easy wins.
- Use real-time wet-end metrics (zeta potential, cationic demand, ines/ash) to stabilize retention and drainage, cutting energy and chemical overuse.
- Encourage design-for-recycling across the value chain (inks, adhesives, barrier choices) to improve de-inkability and fiber recovery, sustaining the sector’s circular performance.
6. Research Gaps and Future Perspectives
- Selective enzymatic surface modification prior to secondary refining increases external fibrillation without significant DP reduction, resulting in measurable improvements in bonding after three or more recycling cycles.
- Dual nanocellulose systems combining cationic and anionic fibrils yield superior strength enhancement compared with single-component CNF additives when applied to hornified fibers from advanced recycling loops.
- Bio-based polymer grafting (e.g., chitosan–CMC hybrids) can establish more resilient hydrogen-bond networks that retain bonding efficiency during subsequent drying–rewetting events and over multiple recycling cycles.
- TEMPO-oxidized nanocellulose produced from recycled pulps exhibits reinforcement efficiencies comparable to CNF from virgin sources when normalized to carboxyl content and fibril aspect ratio.
- Enzymatic pre-loosening of fiber walls reduces refining energy demand in closed-loop water circuits while maintaining strength improvements when scaled from laboratory to pilot-plant environments.
7. Conclusions
- Wet-end chemistry should be continuously monitored and adjusted through online charge and turbidity sensors to stabilize electrokinetic conditions.
- Refining intensity and chemical dosing should be tailored to furnish composition, aiming to maximize bonding fines while limiting detrimental fiber shortening.
- Sequential dosing of fixatives, cationic starch or PAE, and microparticles should be optimized by timing and mixing energy to enhance fines fixation and minimize additive waste.
- Periodic ash purging, combined with filler make-up strategies, should be implemented to maintain optical uniformity and thermal efficiency in drying.
- Detackifier and mineral surface treatments must be integrated into de-inking circuits to minimize stickies deposition and ensure cleaner white water systems.
- Developing bio-based and biodegradable polymers as multifunctional fixatives and retention agents compatible with closed water loops;
- Implementing machine-learning-based models to predict fines generation, floc structure evolution, and retention performance under varying conditions;
- Exploring the synergistic use of nanocellulose, biopolymers, and smart fillers to improve strength and optical properties at reduced fiber input;
- Investigating water and energy integration strategies that couple wet-end optimization with wastewater treatment and heat recovery systems.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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| Parameter/Feature | Description of Change During Recycling | Effect on Fiber Properties | Impact on Paper Quality |
|---|---|---|---|
| Fiber length | Progressive shortening due to mechanical cutting during pulping and refining. | Reduced fiber–fiber contact area; lower bonding potential. | Decreased tensile and tear strength; need for virgin fiber blending. |
| Fiber width and cross-section | Collapse of cell wall and lumen; irregular cross-sectional shape. | Reduced flexibility and swelling capacity. | Lower bonding and sheet density; poor surface smoothness. |
| Hornification | Irreversible hydrogen bonding during drying leading to wall stiffening. | Loss of swelling ability and rehydration potential. | Reduced tensile strength and poor rewetting behavior. |
| External fibrillation | Loss of surface fibrils due to repeated refining and washing. | Smoother surface, reduced bonding sites. | Decreased fiber bonding and sheet strength. |
| Internal fibrillation | Reduced delamination between cell wall layers. | Limited flexibility and swelling. | Weaker fiber bonding, poorer formation. |
| Fines content | Accumulation of small fiber fragments and cell wall debris. | Increased density but reduced drainage. | Higher smoothness but lower bulk and tear strength. |
| Fiber curl and kink | Increase in fiber distortions with repeated mechanical treatment. | Reduced conformability and orientation in the sheet. | Lower tensile strength, but higher bulk and softness. |
| Surface roughness | Smoothing of fiber surface due to fibril loss. | Reduced surface area and reactivity. | Lower bonding efficiency and coating adhesion. |
| Crystallinity | Increase in crystalline regions due to drying and hornification. | Higher stiffness, lower water absorption. | Reduced flexibility and bonding potential. |
| Fines and ash accumulation | Retention of inorganic fillers and fines in recycled pulp. | Altered fiber chemistry and zeta potential. | Affects drainage, strength, and optical properties. |
| Recycling Stage/ Condition | Degree of Polymerization (DP) | Water Retention Value (WRV) | Freeness (CSF)/Drainage | Representative References |
|---|---|---|---|---|
| Virgin/never-dried pulp | Highest DP; cellulose chains largely intact with minimal hydrolysis or oxidative damage. | High WRV, reflecting fully developed swelling capacity and accessible internal pore structure. | Baseline freeness determined by initial refining; used as reference for subsequent recycling behavior. | [82,92] |
| After first drying/first recycling cycle (no special treatment) | Pronounced initial decrease in DP compared with virgin pulp; largest relative drop often observed between cycle 0 and cycle 1. | Marked decrease in WRV due to hornification and partial collapse of the pore structure; reduced swelling and flexibility. | In many chemical pulps with fines retained, freeness tends to drop (slower drainage) mainly at the first cycle; in systems with fines loss, freeness can increase. | [93,94] |
| 2–3 recycling cycles (no special treatment) | Further DP decrease, but the rate of decline is generally lower than in the first cycle; values begin to approach a plateau influenced by fiber origin and prior aging. | WRV continues to decline with each drying/recycling event, then tends toward a lower steady state; loss of hemicelluloses and increased crystallinity are commonly reported. | Reported trends depend on pulp type and system closure; some studies show continued freeness drop with fines accumulation, others report stabilization or slight increase when fines are lost. | [93,95] |
| ≥4–5 recycling cycles (no special treatment) | Gradual, smaller DP decreases; molecular weight distribution increasingly influenced by oxidative history and prior thermal/chemical exposure rather than the number of cycles alone. | WRV typically remains at a relatively low level; hornification is largely developed and additional recycling induces only limited further changes in swelling. | Freeness behavior strongly process-dependent; in many laboratory studies further changes are modest, but in closed industrial systems fines management and additional refining can dominate drainage trends. | [92,93,96] |
| Recycled fibers with mitigating treatments (e.g., chemical swelling, refining, or enzymatic/chemical re-swelling) | DP can be maintained or only moderately reduced if oxidative severity is controlled; some treatments intentionally trade slight DP loss for improved bonding. | WRV can partially recover or even increase relative to untreated recycled pulp due to re-swelling, increased charge, or enhanced fibrillation. | Refining-based strategies typically reduce freeness (slower drainage) because of increased fibrillation and fines content; chemical/enzymatic swelling without intensive refining has a milder impact on drainage. | [48,94,97] |
| Strategy/System | Representative Mechanism | Observed Effects (Qualitative) | Representative References |
|---|---|---|---|
| CNF/nanocellulose from recycled or waste fibers | TEMPO-mediated or other oxidation followed by mechanical fibrillation of recycled or waste-paper pulps | CNF from recycled paper or waste fibers shows morphology and properties comparable to CNF from virgin fibers; used as wet-end additive or in fiber blends, it improves tensile strength and stiffness of recycled-paper-based materials | [50,65,109] |
| Dual CNF systems (anionic + cationic) in recycled paper | Cationization of CNF and combination with enzymatically produced anionic micro/nanofibers | Fully cellulose-based dual CNF system acts as both strength and retention aid; breaking length of recycled paper increased by ≈46.5%, outperforming synthetic polyacrylamide | [65] |
| Bio-based polymer and polysaccharide functionalization of recycled fibers | Use of chitosan, CMC, starch and other biodegradable polymers as strengthening agents and cross-linkers | Significant improvement of tensile properties and dimensional stability in recycled-fiber-based materials (shown for cotton recycled fibers) | [102] |
| Surface modification of pulps from mixed waste papers | Deinking and surface treatments applied to mixed waste corrugated carton and office paper pulps | Changes in surface chemistry, charge and roughness documented; basis for targeted surface functionalization and improved compatibility with additives | [86] |
| Silane-based cellulose modification (composites context) | Formation of siloxane bonds between functionalized silanes and cellulose hydroxyl groups | Improved interfacial adhesion, hydrophobicity and mechanical properties in cellulose-based composites | [110] |
| Enzymatic refining of recycled fibers | Use of cellulases and hemicellulases as refining aids | Energy savings up to ≈20% and improved bonding and drainage when enzymatic refining complements mechanical refining | [105,107] |
| Cellulase/cellulase–xylanase pretreatment | Selective modification of fiber surface and hemicellulose content | Increased external fibrillation and WRV; altered surface composition; potential enhancement of flexibility and bonding | [111] |
| Laccase/laccase–mediator systems on recycled pulps | Oxidative modification and partial delignification of fiber surfaces | Improved fiber-bonding capacity, tensile and compressive strengths of unbleached recycled pulps | [86,112] |
| Category | Typical Components | Chemical Effects on Fibers | Management and Control Strategies |
|---|---|---|---|
| Sizing agents | Alkyl ketene dimer (AKD), Alkenyl succinic anhydride (ASA), Rosin size | React with cellulose hydroxyl groups forming hydrophobic ester bonds; uneven distribution causes hydrophobic patches; reduces fiber wettability and bonding potential. | Optimize pH and temperature during recycling; use mild oxidative or enzymatic treatments to remove residual hydrophobes; employ retention aids for uniform dispersion. |
| Fillers and coating pigments | Calcium carbonate (CaCO3), Kaolin (Al2Si2O5(OH)4), Titanium dioxide (TiO2) | Block hydrogen-bonding sites, reduce swelling, and increase anionic demand; enhance opacity and brightness but weaken tensile strength if excessive. | Balance filler content by grade; control pH to prevent CaCO3 dissolution; apply optimized retention and drainage aids; partial purge of mineral fines when necessary. |
| Retention and strength aids | Cationic starch, PAE resin, Polyacrylamides (PAMs), Bentonite, Colloidal silica | Improve flocculation and inter-fiber bonding; adsorption limited by hornification and DCS interference; high charge demand in recycled systems. | Use sequential addition (fixative → strength aid → microparticle); monitor cationic demand; adjust polymer dosage and mixing intensity. |
| Dissolved and colloidal substances (DCSs) | Degraded hemicelluloses, dispersants, surfactants, extractives, latex residues | Increase anionic charge, compete with cationic polymers, destabilize flocs; adsorb on fines and fibers, leading to stickies and deposit formation. | Employ fixatives (polyamines, PAC, alum); use DAF and washing to reduce DCSs; maintain balanced white-water chemistry. |
| Inks and pigments | Carbon black, Organic dyes, Metal oxide pigments, Binder polymers | Alter fiber surface energy and zeta potential; create hydrophobic regions that interfere with sizing and bonding; may cause brightness reduction. | Use optimized flotation and surfactant chemistry; peroxide bleaching for optical recovery; minimize ink fragmentation during pulping. |
| Stickies and adhesives | Latex, Polyvinyl acetate (PVA), Styrene–butadiene rubber (SBR), Hot-melt adhesives | Hydrophobic and pressure-sensitive materials deposit on fibers and equipment; disrupt hydrogen bonding and cause sheet defects. | Apply detackifiers (talc, bentonite, PAC); control temperature and pH to minimize tackiness; install fine screening to remove macro-stickies. |
| Coating binders and latex residues | SBR, PVA, Acrylic copolymers | Modify zeta potential and drainage; contribute to hydrophobic surface areas and non-uniform sizing response; generate oligomers during degradation. | Use enzymatic pre-treatment to hydrolyze residues; adjust retention programs to manage increased hydrophobicity; enhance washing stages. |
| Treatment Type | Representative Mechanism | Typical Strength Improvement Trend | Key Notes/ Conditions | Representative References |
|---|---|---|---|---|
| Chemical modification (e.g., TEMPO, CMC grafting) | Increased surface carboxylation, enhanced swelling and charge balance, improved polymer adsorption | Moderate–high tensile and bonding gains when oxidation is controlled; improved internal bonding and sometimes tear strength | Performance depends on pulp type, oxidation severity, and degree of polymerization (DP) loss; over-oxidation can reduce strength or increase brittleness | [151,155,156,157] |
| Enzymatic treatment (e.g., cellulases, xylanases) | Selective hydrolysis of amorphous/hemicellulosic regions; fiber-wall loosening and external fibrillation | Low–moderate tensile gains; improved bonding, sometimes at reduced refining energy | Dosage-sensitive; best results when mild treatment is integrated with refining strategy; excessive hydrolysis may shorten fibers or weaken the sheet | [105,106,108] |
| Laccase-mediator or laccase-only systems | Selective lignin activation and phenolic crosslinking; increased surface charge and functional groups | Moderate strength improvements (tensile, burst, sometimes wet strength), particularly in lignin-containing or OCC furnishes | Effect strongly influenced by mediator type and pulp lignin content; brightness and kappa number may also change | [93,136,156] |
| Nanocellulose reinforcement (CNF/CNF from virgin or recycled pulp) | High-surface-area fibrils fill interfiber voids and create a nanoscale bonding network | High tensile-strength gains and improved stiffness at relatively low addition levels; often strongest reinforcement among the listed strategies | Drainage and dewatering become limiting at higher dosages; effect depends on nanocellulose type (CNF vs. CNC), fibril morphology and dispersion quality | [158,159,160,161] |
| Combined enzymatic–mechanical fibrillation | Enzyme-assisted loosening of the fiber wall that facilitates subsequent mechanical fibrillation | Moderate–high strength gains with reduced specific refining energy compared with purely mechanical routes | Synergistic effects when mild enzymatic pretreatment is followed by optimized mechanical refining; effectiveness depends on enzyme type and treatment time | [105,108,162] |
| Study (Year) | System Boundaries | Functional Unit | Key Findings/Conclusions |
|---|---|---|---|
| [174] | Cradle-to-gate; EU kraft pulp mill and recycled pulp line | 1 ton paper | Recycling generally lowers energy use and GHG emissions; results sensitive to electricity mix and recycling rate. |
| [175] | Cradle-to-grave; packaging paper loop | 1 ton packaging paper | Recycled fibers reduce carbon footprint but may increase water impacts depending on deinking configuration. |
| [176] | Cradle-to-gate; Asian mixed-furnish mill | 1 ton newsprint | Deinking step dominates energy demand; recycled furnish beneficial unless low-quality waste increases rejects. |
| [177] | Consequential LCA; EU circular-economy scenario | 1 ton recovered fiber | Increasing recycling rate shifts burdens upstream; marginal benefits decrease after ~75% recovery. |
| [18,19] | EU industry-level LCA synthesis | Sector-wide | Recycling outperforms virgin production in GHGs; trade-offs exist in water use and effluent loads depending on water-loop closure. |
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Pătrăucean-Patrașcu, C.-I.; Gavrilescu, D.-A.; Gavrilescu, M. Chemical Transformations and Papermaking Potential of Recycled Secondary Cellulose Fibers for Circular Sustainability. Appl. Sci. 2025, 15, 13034. https://doi.org/10.3390/app152413034
Pătrăucean-Patrașcu C-I, Gavrilescu D-A, Gavrilescu M. Chemical Transformations and Papermaking Potential of Recycled Secondary Cellulose Fibers for Circular Sustainability. Applied Sciences. 2025; 15(24):13034. https://doi.org/10.3390/app152413034
Chicago/Turabian StylePătrăucean-Patrașcu, Corina-Iuliana, Dan-Alexandru Gavrilescu, and Maria Gavrilescu. 2025. "Chemical Transformations and Papermaking Potential of Recycled Secondary Cellulose Fibers for Circular Sustainability" Applied Sciences 15, no. 24: 13034. https://doi.org/10.3390/app152413034
APA StylePătrăucean-Patrașcu, C.-I., Gavrilescu, D.-A., & Gavrilescu, M. (2025). Chemical Transformations and Papermaking Potential of Recycled Secondary Cellulose Fibers for Circular Sustainability. Applied Sciences, 15(24), 13034. https://doi.org/10.3390/app152413034

