1. Introduction
CFs are among the most widely used reinforcing materials in the manufacture of Fibre-Reinforced Polymers (FRPs). CFs can be fabricated into forms such as fabric, woven, yarn (continuous), or chopped (short fibres), while thermoset polymers are commonly used as the matrix in CFRP manufacturing [
1]. The most utilised CFs are polyacrylonitrile (PAN)-based, known for their ease of production and ability to retain mechanical properties under extreme conditions. Other fibres, such as aramid, boron, and basalt, are also used, but to a lesser extent compared to glass and carbon fibres. Natural fibres are also being explored, although their potential is currently limited, mainly due to poor compatibility between fibres (polar and hydrophilic properties) and the polymeric matrices available on the market (non-polar properties) [
2,
3].
In recent years, CFRPs have gained significant attention across industries such as aerospace, automotive, wind energy, leisure, and sports due to their outstanding chemical, physical, and mechanical properties [
4,
5]. These properties arise from the combination of CFs’ low density and high strength, which give CFRPs a lightweight nature, making them ideal for high-performance applications [
6]. The polymer matrix also provides stability against compression, allowing CFRPs to be used in structures exposed to extreme conditions [
7,
8]. However, the growing use of CFRPs has led to increased production and, consequently, a rise in waste. Historically, end-of-life (EoL) CFRPs were disposed of through landfilling, incineration, or grinding into fillers—all of which pose environmental challenges. In addition, the high production cost of virgin CFs highlights the need for sustainable and economically viable recycling methods [
9]. Several recycling techniques have been developed, but the process remains complex due to the heterogeneous nature of CFRPs, composed of a matrix and reinforcement. Therefore, selecting the right recycling method is critical. Among the existing methods, mechanical, thermal, and chemical recycling stand out [
6,
10].
Mechanical recycling involves grinding the composite into smaller pieces for reuse in CFRP manufacturing. Thermal recycling decomposes the polymer matrix at high temperatures, leaving the fibres intact for recovery [
11]. Chemical recycling focuses on depolymerising the resin matrix to reclaim the fibres. Thermal and chemical recycling have more potential than mechanical processes because they can produce continuous fibres, whereas mechanical recycling typically yields chopped fibres, which are less useful for high-performance applications [
12].
Even though technological advancements in CFRP recycling have made significant strides and remain an active area of research, several challenges persist. These include incomplete resin removal, structural damage to CFs caused by extreme processing conditions, and inadequate surface characteristics of CFs for proper resin adhesion, which is crucial for manufacturing high-value composite materials. To address these challenges, the present investigation focuses on two recently developed chemical recycling methods for CFRPs with thermoset epoxy resin as the matrix: solvent-based solvolysis, and plasma-enhanced solvolysis and the subsequent effect of sizing on the mechanical properties. Notably, chemical recycling (commonly referred to as solvolysis) has been identified as the method that causes the least damage to fibres during the recovery process [
12].
Solvolysis involves the chemical decomposition of polymers into mono- and oligomers. However, this process is considered high-risk because it often requires the use of strong chemicals, elevated temperatures, and pressures, which, if not carefully controlled, could lead to hazardous conditions, including unwanted side reactions or incomplete resin degradation. To mitigate these risks, solvolysis at low temperatures—typically below 200 °C—and atmospheric pressure have been explored. Conducting the reaction under such mild conditions requires the use of acids, bases, or catalysts [
10]. For instance, a study by Peng et al. [
13] demonstrated the effectiveness of this approach by performing solvolysis at 200 °C under ambient pressure for 4 h using a polyethylene glycol/NaOH system. The experiment achieved a decomposition efficiency of 84.1–93%, with the reclaimed CFs exhibiting minimal resin residues, a slightly oxidised carbon structure, and a mildly reduced degree of graphitisation, as confirmed through various characterisation techniques. Furthermore, the tensile strength of the recovered CFs was preserved at 94–96% of the pristine fibres, indicating the success of this method. In this research, epoxy-based CFRPs are recycled using low-temperature, low-pressure solvent-based solvolysis, employing a 10% KOH solution in ethylene glycol (EG). The use of KOH offers several advantages over NaOH, including higher solubility in ethylene glycol, enhanced catalytic activity, and better control of reaction pathways. These properties allow for more efficient resin decomposition while reducing potential structural damage to the fibres. Additionally, KOH is less corrosive, which further contributes to preserving the integrity of the recycled fibres. The solvent is reused across multiple experiments to maximise efficiency and minimise waste. Plasma-enhanced solvolysis, on the other hand, represents a novel and promising technology that combines the benefits of chemically assisted solvolysis with plasma chemistry. This approach has been explored in only a few studies, making it an innovative method for CFRP recycling. In our previous work [
12], the use of nitric acid as a solvent was proposed, augmented with nitrogen plasma, to generate a variety of reactive species. These reactive species facilitate the rapid degradation of the resin. Plasma-enhanced solvolysis has been shown to require significantly less time than conventional HNO
3 solvolysis while reclaiming fibres with mechanical properties comparable to virgin CFs. This innovative recycling method is used in this study to produce recycled fibres and study the sizing effect on their properties.
The goal of recycling EoL CFRP parts is to reclaim high-quality recycled carbon fibres (rCFs) for valuable applications. However, rCFs often have inert surfaces, resulting in poor adhesion to the matrix and reduced interlaminar shear strength, which can lead to delamination or sudden failure without visible damage [
8]. Achieving strong fibre-matrix adhesion is crucial; better bonding increases the energy required to separate the fibres, thus enhancing overall performance. Fibre sizing, the application of a polymeric coating to the fibres, is one way to improve fibre-matrix adhesion. Sizing enhances resistance to environmental degradation and mechanical stress during handling and transportation while improving the interface quality between the fibres and matrix. Common sizing agents include epoxy resins, polyurethane, and polyamide, with the choice depending on the application [
7]. Recently, the incorporation of nanomaterials, such as carbon nanotubes (CNTs) or nanoparticles with diverse morphologies, into sizing agents has gained attention for their unique chemical and mechanical properties [
14].
As CFRP recycling advances, new characterisation methods are needed to assess the quality and integrity of rCFs accurately. Conventional methods often struggle to evaluate fibre loss and degradation during recycling, limiting process optimization. Therefore, novel techniques are required to provide insights into the physical properties of rCFs, such as morphology, distribution, and breakage. To address this, a novel optical microscopy-based quantification method is developed in this work to assess filament loss that may occur during the recycling process by accurately quantifying the number of filaments. While the proposed method focuses on the post-recycling evaluation, it serves as a valuable starting point for the development of further methodologies aimed at real-time monitoring of fibre quality during the recycling process. Such advancements could enable optimised recycling procedures and the production of high-quality fibres, not only in lab or pilot-scale settings but also in industrial-scale applications.
In summary, this study investigates the effects of fibre sizing on the properties of rCFs recovered from two chemical recycling processes: chemically assisted solvolysis and plasma-assisted solvolysis, applied to EoL automotive parts. The novelty of this work lies in the continuous exploration of sizing as a means to restore and enhance the properties of rCFs, specifically in conjunction with a novel plasma-assisted solvolysis method. Furthermore, the development of a custom Python-based image analysis script for quantifying filament loss introduces a new tool for evaluating the efficiency of recycling processes and assessing filament quality with higher accuracy and reproducibility. The morphological characteristics of rCFs were analysed using scanning electron microscopy (SEM), and their structural stability post-recycling was evaluated through thermogravimetric analysis (TGA) and Raman spectroscopy. Additionally, an automated optical microscopy analysis was introduced to measure filament loss during recycling. Tensile tests were performed on both recycled and sized fibres (single fibres and yarns) to evaluate the effects of recycling and sizing on their mechanical properties.
2. Materials and Methods
2.1. Materials
EoL tubular parts from automotive, with dimensions O.D 6 cm, I.D 5.5 cm, and H 20 cm, were supplied by B&T composites (Florina, Greece) fabricated with Tenax
®-E STS40 (Teijin, Tokyo, Japan) continuous fibre via filament winding. The physical and mechanical properties of those CFs are listed below in
Table 1.
For chemical-assisted solvolysis, the following chemical substances were used: potassium hydroxide (KOH, wt/wt 10% solution, purity > 99.9%, Honeywell) in ethylene glycol (EG, purity > 99.5%, Fisher Chemical, Waltham, MA, USA), while for plasma-assisted solvolysis: acetone (2-propanone, wt/wt 99.8%, Fisher Chemical), nitric acid (HNO3, wt/wt 65%, Honeywell), hydrogen peroxide (H2O2, wt/wt 30%, Carlo Erba reagents, Milan, Italy), and nitrogen gas (N2, purity > 99.9%, EVOXA, Paris, France).
Hydrosize
® HP2-06 (Michelman, Aubange, Belgium) was the commercial polymeric coating used for the sizing of rCFs. Its properties are presented in
Table 2. It is an anionic/nonionic phenoxy aqueous dispersion that acts as a sizing agent for fibres, enhancing their compatibility with each matrix, and promoting the mechanical performance of the final composite.
For the preparation of samples for optical microscopy and tensile tests, the SR1710/SD8822 structural epoxy system from Fibremax Composites (Volos, Greece) was used (
Table 3). SR1710/SD8822 is a two-component epoxy system that cures at 25 °C for 24 h and post-cures at 40 °C for an additional 24 h.
Five different sample categories are studied in this manuscript, and for the reader’s convenience, they will be referenced according to
Table 4.
2.2. Recycling of EoL Parts
2.2.1. Chemical-Assisted Solvolysis
The solvolysis process was conducted in a 2 L unpressurised batch reactor equipped with a reflux condenser and a nitrogen supply. A 10% KOH solution in ethylene glycol (EG) was used as the solvent. The solvolysis reaction took place at 190 °C for a minimum duration of 6 h. The CF tubes were secured using a stainless-steel wire basket, which held the filaments in place to reduce entanglement during the process. The secure sample was subsequently introduced into a preheated 10% KOH solution in ethylene glycol at 60 °C (to facilitate easier dissolution of KOH in EG). The mixture was then heated to a temperature range of 190–195 °C. Periodically, the reactor was opened to monitor the process. After 6 h, the stainless steel wire basket containing the CF was removed from the reactor and allowed to drip. Once the CF had cooled to room temperature, it was cleaned using tap water with a small amount of surfactant. The CF was then left to dry. The final CF mass was obtained after drying at 105 °C. The remaining KOH solution in ethylene glycol was collected for reuse in the next process.
2.2.2. Plasma-Assisted Solvolysis
Plasma-assisted solvolysis involves 5 discrete steps, namely, material pre-treatment, plasma-assisted solvolysis, rCF cleaning, liquid waste regeneration, and flue gas scrubbing. A detailed flow chart is presented in our previous work [
15]. Initially, the CFRPs are treated in a 4 M HNO
3 solution for matrix swelling and then enter the plasma reactor, where they are treated up to complete matrix dissolution. The flue gas produced during plasma-assisted solvolysis flows through a wet scrubber containing a dilute HNO
3-H
2O
2 solution so that the emitted NO
x is partially converted to HNO
3. When the HNO
3 concentration of the scrubbing liquid reaches 4 to 6 M, it is collected and used for the CFRPs pre-treatment. When the plasma-assisted solvolysis is completed, the liquid waste is regenerated by adding small amounts of H
2O
2 and is reused in the next solvolysis cycle. The continuously recovered fibres are mechanically collected, washed with acetone, and dried naturally.
Figure 1 illustrates the plasma-in-bubbles reactor set-up. This type of plasma was chosen as it leads to the production of active species close to the composite surface, while at the same time the plasma-induced shockwaves inside the liquid favour the mass transport of resin fragments from the solid to the liquid phase [
16]. The reactor consists of a 2 L glass container where CFRPs and concentrated (65% wt/wt) HNO
3 are placed. The vessel is positioned on a stainless steel plate, which is the grounded electrode of the reactor. The powered electrode is a stainless-steel tube of ¼ in diameter that is immersed in the solution and through which the gas enters the liquid and produces bubbles. The electrode is powered by a high-frequency generator (30 kHz signal generator IGBT143, Martignoni Elettrotecnica, Vestone, Italy) through a voltage amplifier (IGBT163, Martignoni Elettrotecnica). A high-voltage 1000:1 passive probe (P6015A, LeCroy, Chestnut Ridge, NY, USA) is adjusted on the power line to record the applied voltage, while the current flow of the system is calculated by recording the voltage drop (100:1 passive voltage probe, Hameg HZ53, Hameg Instruments, Mainz, Germany) across a 6.5 Ω resistance attached between the stainless-steel plate and the ground. Recording the applied voltage and the current flow allows the calculation of the process power consumption [
16]. In this work, the N
2 flow rate, the HNO
3 solution volume, and the power consumption were kept equal to 4 Lmin
−1, 1.2 L, and 250 W correspondingly so that the temperature of the solution is stabilised to ~80 °C about 10 min after plasma ignition. The total time required for the complete matrix dissolution and the recovery of CFs was about 5 h.
The energy and cost efficiency of the two recycling methods—chemically assisted solvolysis and plasma-assisted solvolysis—are critical factors for industrial scalability. Chemically assisted solvolysis operates under relatively mild conditions, such as low temperature and atmospheric pressure, resulting in lower energy consumption compared to high-temperature methods like pyrolysis. The use of a 10% potassium hydroxide solution in ethylene glycol further optimises costs through solvent reuse, though longer reaction times and solvent recovery processes remain challenges for scaling. Plasma-assisted solvolysis offers faster reaction times at approximately 80 °C, significantly reducing processing duration while ensuring effective resin removal. Despite its higher energy demands due to the plasma system, the process benefits from efficient resource utilisation, as liquid waste streams and flue gases can be recycled within the system. While both methods are at a low technology readiness level (TRLs 3–5), their laboratory-scale energy profiles can provide valuable information for optimising cost-effectiveness and resource efficiency, facilitating their development toward industrial adoption.
2.3. Fibre Treatment
Solvolyzed CFs tend to exhibit an inactive surface, which results in composites with reduced mechanical performance. This decline is primarily attributed to the recycling process, which disrupts the alignment of the fibre tow and strips functional groups from the surface. In cases where the recycling process is particularly intense or involves harmful catalysts, the structural integrity of the fibres can also be compromised, although this can be monitored and mitigated. The lack of fibre-matrix covalent bonds weakens the adhesion between the fibres and the matrix. To improve these properties, a commonly employed method involves the application of polymeric coatings on the fibres, known as sizing. Sizing’s role is to protect the fibres during processing, to enhance the adhesion between the fibre and the matrix, as well as to aid the fibres to regain the mechanical properties they possess as virgin CFs. These solutions consist of a film former, lubricants, and additives, such as coupling agents and/or additives dispersed in water [
17].
In this work, sizing is applied using a pilot-scale continuous sizing line (
Figure 2). The line consists of seven serially installed elements, which are briefly introduced here, with full details available in our previous work [
14]. The process begins with the let-off tension creel, which feeds the fibre into a furnace while maintaining the required tension in coordination with the take-up winder. The furnace is used (if needed) to remove any resin residues from the recycling process by adjusting the temperature between 300 °C and 600 °C, depending on the specific requirements. Afterwards, fibre passes through the sizing bath, where a coating solution is applied via bath rollers, and the excess solution is removed by squeeze rollers to ensure uniform coverage. The fibre then moves into the drying furnace, where solvent evaporation and coating solidification occur. The process is controlled by a feed roller system, with speeds ranging from 0.2 to 2 m/min, depending on production needs. At the end of the line, the fibre is collected by a mechanical traverse system and take-up winder, powered by a constant-torque motor.
Ideally, recycled CFs should remain continuous. However, depending on the recycling process and handling, the fibres may be cut randomly. When this occurs, the fibres must be rejoined using pneumatic splicing. This method involves overlapping the separated yarn ends and bonding them with turbulent air, creating a strong connection [
18], using a splicer (Airbond, Pontypool, UK). In the early stages of process development, splicing was necessary to achieve continuous yarns. However, as the process was optimised, no splicing was needed. Once the continuous yarn is reclaimed, the spool is mounted on the sizing line. The sizing bath is filled with the commercial sizing solution Hydrosize
® HP2-06 (Michelman, Aubange, Belgium), with a solid content of 1%, as described in
Section 2.1. The hydrasize sizing agent used here is a phenoxy dispersion in an amine emulsifier. Phenoxy resins in a mixture with amines will generate a hydroxyl group in the polymeric chain through the interaction of the phenoxy ester or ether with the amine group. The hydroxyl group will promote the covalent bonding of the sizing polymer to the rCF surface through either dehydration or esterification reactions with -OH or -COOH groups that already exist in the rCF surface. In addition, the hydroxyl group will enhance h-bonding interactions between the sizing polymer and rCF surface, thus leading to a stronger attachment.
2.4. Optical Microscopy Analysis Preparation
Optical microscopy is a characterisation technique that requires meticulous sample preparation with a flawless surface finish. Any imperfections, surface texture, or contaminants can significantly impact the accuracy of the analysis. Therefore, it is essential to prepare samples with a high-quality surface to prevent the microscope from capturing any irregularities that could interfere with the results.
The samples prepared for this research were aligned, enclosed in disc-shaped moulds, and impregnated with epoxy resin. To ensure that the fibres remained stretched and properly aligned throughout the curing period before placing them into the moulds, fibres were kept under tension on a metallic plate, and resin droplets were carefully applied using a pipette. The impregnated samples were then placed in an oven at 50 °C for 24 h. After curing, each specimen was cut into 1 cm pieces and embedded perpendicularly in a 30 mm diameter cylindrical mould. The fibres were held vertically with a small clamp and placed at the bottom of the mould, ensuring they stood upright and perpendicular to the surface. Each mould contained five samples, and additional resin was poured over them. The same curing procedure was followed, and after removal from the moulds, the specimens were ground and polished as detailed in
Table 5 and
Table 6.
2.5. Characterization Methods
To evaluate the effectiveness and impact of each recycling method on the fibre surface, samples were examined using SEM (TM3030Plus Tabletop Microscope, HITACHI, Tokyo, Japan) at magnifications up to ×1000. By scanning the surface of the samples, it was possible to identify the amount of residual resin remaining after the recycling process and to assess any potential surface damage. Five different samples per case were analysed, scanning the entire surface area of each and capturing representative images, which are presented in the Results section.
TGA (NETZSCH Proteus Thermal Analysis 8.0.2, Selb, Germany) was used to evaluate total mass loss at a specific temperature range, which is an indication of resin residue after the completion of the recycling process, as well as a quantitative determination of the polymeric coating that has been added to the recycled fibres. Furthermore, the structural integrity of the fibres can also be identified through this method, as any detection of significant weight loss would indicate potential fibre structural damage. TGA analysis was conducted in a nitrogen (N
2) atmosphere with a flow rate of 50 mL/min, heating the samples to 900 °C at a rate of 10 °C/min. Further investigation on the structural behaviour was performed by Raman spectroscopy. The Raman spectra of fibres were collected using a Renishaw InVia (H43662 model, Gloucestershire, UK) equipped with a laser line emitting at a wavelength of 785 nm and a 50× objective lens. Raman spectra were recorded in the range from 500 cm
−1 to 4000 cm
−1, and the region between 500 cm
−1 and 3000 cm
−1 was analysed using home-made software compiled in MATLAB
® (version R2020a), following a procedure reported by Tagliaferro et al. [
19].
XPS measurements were performed to identify the surface functional groups of carbon fibres at three different stages: Ref_CF, Pl_rCF, and Sized_Pl_rCF. This technique, with its shallow sampling depth of a few atomic layers, provides both qualitative and quantitative insights into surface modifications. The measurements were conducted using a UHV Prevac spectrophotometer (Rogow, Poland) equipped with a VG Scienta XM 780 monochromator and an Al Kα radiation source (1486.6 eV). High-resolution (HR) XPS spectra were recorded at a pass energy of 50 eV, with an energy step size of 50–100 meV. The binding energy scale was calibrated by setting the binding energy of the aliphatic carbon C1s peak to 284.8 eV. All spectra were analysed using CasaXPS Version 2.3.23 PR1 software. Due to limited availability, this method was applied specifically to Ref_CF, Pl_rCF, and Sized_Pl_rCF, as they demonstrated the best results from SEM and TGA analysis.
An Olympus BX53M microscope (Olympus, Tokyo, Japan) with a brightfield observation method and a camera resolution of 5760 × 3600 pixels was used for the inspection of the polished specimens described in
Section 2.4. For image captioning and analysis, the Olympus Stream Motion software v 2.5.3 was utilized. Additionally, the Panorama feature was employed to combine multiple images into one, simplifying the analysis of the samples.
A tensile testing machine (WD100 TE machine, Jinan Testing Equipment IE Corporation, Jinan, China) was used to measure the tensile strength of carbon fibres, according to ASTM D4018 [
20]. The tensile test specimens were impregnated with the SR1710/SD8822 (as presented in
Section 2.1) and consolidated. The testing parameters of the machine were set as follows: the tensile rate was 2 mm/min with a load cell of 5 kN. The specimens were untabbed, requiring a distance of 150 mm between the grips. Five specimens of each kind of fibre were tested. To calculate tensile strength (MPa), the following formulas were used:
where:
UTS: Ultimate Tensile Strength (MPa)
P: maximum load measured in tensile test, N;
ρf: fibre density, g/m3;
MUL: fibre mass per unit length, g/m; and
A: unit conversion factor (1 if load in N).
MUL: mass per unit length, g/m;
W1: mass of the specimen, g; and
L: length of the specimen, m.
For the single fibre tensile test, individual filaments were carefully selected from a fibre bundle. Each filament was mounted on a paper frame with a 25 × 10
−3 m gauge length, and the top and bottom ends were securely glued to the frame. The entire frame was then positioned in the grips of the tensile testing machine with a load cell of 5 N. Before initiating the test, the edges of the paper frame were cut with scissors to release the fibre. The test was conducted at a constant crosshead speed of 1 mm/min until the fibre reached the point of breakage. Ten specimens of each kind of fibre were tested. To calculate the tensile strength (MPa), the following classic formula for normal stresses was used:
where:
UTS: Ultimate tensile strength (MPa)
P: maximum load measured in the tensile test, N; and
A: area of single fibre cross-section, mm2.
4. Conclusions
The aim of this study was to investigate the impact of two chemical recycling methods—chemically-assisted and plasma-assisted solvolysis—on the morphology and properties of CFs derived from end-of-life CFRP automotive parts, as well as the effect of sizing application on these recycled fibres. SEM analysis was used to examine fibre surface morphology, revealing that chemically assisted solvolysis left some resin residues, while plasma-assisted solvolysis was more effective at removing them. Sized fibres displayed a smooth surface with a uniform coating distribution. The structural integrity of both the retrieved and sized fibres was assessed through TGA and Raman spectroscopy. TGA measurements confirmed that all fibre types maintained their structural integrity, showing no mass loss up to 900 °C. Comparing Raman spectra, it became evident that plasma-assisted solvolysis more effectively retains fibre integrity by limiting the introduction of disorder and reducing residual resin, whereas traditional solvolysis showed the presence of functional groups such as C=O and OH, suggesting the residual presence of epoxy resin together with an advance oxidation of the surface.
Additionally, the study compared different methods for analysing optical microscopy images, each with specific strengths and limitations. Olympus software emerged as the fastest method, enabling immediate analysis post-image capture, but it struggled with dense or overlapping fibres. ImageJ, though more time-consuming, proved to be very consistent, offering a step-by-step process that ensured high accuracy. Its watershed algorithm was particularly effective in segmenting overlapping or adjacent fibres, enhancing precision. Finally, a Python script was developed, allowing for automated and efficient analysis with faster processing times.
To determine the effect of sizing on the properties of recycled CFs, XPS analysis was conducted. The results showed an increase in functional groups on the fibre surfaces, which improved their mechanical properties. Tensile tests confirmed that both sized and unsized recycled fibres exhibited a reduction in tensile strength of approximately 10% compared to reference fibres, as expected with recycled materials. However, the application of sizing significantly enhanced the tensile strength of the recycled fibres, mitigating the negative effects of recycling, such as fibre damage, misalignment, and reduced matrix adhesion.
While plasma-assisted solvolysis proved to be more effective at removing resin, both chemical recycling methods successfully reclaimed the fibres. The application of sizing further enhanced the performance of the recycled fibres by improving their mechanical strength and mitigating the drawbacks of the recycling process, demonstrating that sizing plays a crucial role in restoring the functionality of recycled carbon fibres.
5. Outlook and Future Directions
This study puts emphasis on the critical role of chemical recycling and surface modification techniques in advancing the sustainability and functionality of carbon fibre-reinforced composites. However, to fully integrate these processes into industrial applications, further research and development are required.
One promising direction for future research involves optimising chemical recycling methods to minimise structural disruptions during fibre recovery. By refining solvent systems and process parameters, it may be possible to reclaim fibres with enhanced structural and surface properties, further reducing the gap between recycled and virgin fibres. Moreover, with optimised processes, it could be possible to achieve complete resin removal during recycling, eliminating the need for additional post-treatment steps to address residual resin. This approach would enhance the overall efficiency of the recycling process and ensure that the recovered fibres are immediately suitable for surface modification processes, such as sizing, which are essential for restoring fibre-matrix adhesion and mechanical performance.
Advancements in surface modification methods also offer significant potential. The incorporation of nanomaterials, such as carbon nanotubes or nanoparticles, into sizing formulations could introduce multifunctional properties with enhanced mechanical performance, improved thermal stability, or electrical conductivity. Such innovations would broaden the application scope of recycled carbon fibres, enabling their use in more demanding composite applications.
Automation and real-time monitoring of recycling processes represent another critical area for development. The Python-based image analysis introduced in this study demonstrates the potential for quantitative evaluation of fibre quality, but further refinement is needed to enable real-time integration into recycling workflows. Automated feedback systems could provide valuable data to adjust process parameters dynamically, ensuring consistent and high-quality fibre recovery.
Finally, scaling up these recycling processes from laboratory to industrial scale will be key to addressing the growing demand for sustainable composite materials. This will require collaboration between industry stakeholders, researchers, and policymakers to develop efficient, cost-effective, and environmentally friendly recycling solutions. Establishing standardised evaluation methods for recycled fibres and demonstrating their reliability in real-world applications will be essential to gaining industry acceptance and fostering broader adoption.