RETRACTED: A Critical Review on Recycling Composite Waste Using Pyrolysis for Sustainable Development
Abstract
:1. Introduction
- The increased utilization of composites in mass-production automobiles resulting from the development of high-volume thermoplastic composite-based technologies [3].
- The first significant group of wind turbines made of composite materials approaching their End-of-Life (EOL) in 2019–2020 and preparing to be dismantled [1].
- The COVID-19 epidemic hastening the retirement of airplanes (airplane mass decommissioning is predicted in the 2020s) [5].
1.1. Composite Material Applications
1.1.1. Aerospace
1.1.2. Automotive
1.1.3. Marine
1.1.4. Wind Energy
1.1.5. Construction and Infrastructure
2. Review of Recycling Technologies
3. Recovery of CFRC/GFRC Utilizing Pyrolysis
3.1. Pyrolysis: Controlled Atmospheres
3.1.1. Vacuum Atmosphere
3.1.2. Nitrogen Atmosphere
3.1.3. Superheated Steam Atmosphere
3.2. Microwave Pyrolysis
3.3. Pyrolysis on Wind Turbine
4. Pyrolysis Products and Their Reuse
5. Discussion
- In an appropriate experimental facility, how well does pyrolysis perform for mixed and polluted scrape? In the majority of the work in the literature, there has been no mention of an FBR or any other reactor capable of processing mixed and polluted wastes.
- Determination of the optimal variables of pyrolysis and post-pyrolysis are necessary in order to better comprehend the impact of pyrolysis. For further enhancement of the quality of the recovered fibers, research on the optimum variables of pyrolysis is needed.
- In the literature, there is a gap in the examination of financial and energy-based evaluation of pyrolysis. The data will show that recycled fibers are better for the environment than EOL landfilling. Mathematical modeling may be built to show how pyrolysis and post-pyrolysis processing changes—as well as other important parameters—affect the cost and environmental effect.
- There are currently no commercially viable products created from short, thin, and nonaligned recovered fibers obtained by pyrolysis. More study on the use of recovered fibers is needed.
- When pyrolyzing a recycled composite, there is no information on fiber grading and fractionation to remove short fibers and retain excellent purity and strength without losing part of the fiber.
- How can the original fiber length and strength be preserved following pyrolysis? The longer the starting fiber, the longer the recovered fiber—although better understanding of the effects of thermal and oxidation treatment is needed to enhance product quality and lower costs.
- The lack of sizing on recycled fiber surfaces is a key study topic. This might result in inadequate adhesion among the polymer and recovered fibers, resulting in poor mechanical characteristics. The mechanical characteristics of recycled fibers might be significantly improved by pyrolysis resizing.
- Pyrolysis improved the mechanical characteristics of recovered fibers when contrasted with incineration, gasification, mechanical, and chemical techniques. On the other hand, an inappropriate set of pyrolysis conditions has a detrimental impact on these characteristics (such as poor heating rates and high residence time). This compromise will not be accepted if the recovered fibers are to be used in a high-grade composite application.
- It is unclear what effect fiber reclamation has on the performance of composites when compared to virgin and recovered composites with similar structures.
6. Conclusions and Future Research
- Mechanical separation, incineration, gasification, and slower pyrolysis in a kiln are costly or yield low characteristic fibers. Pyrolysis may be a realistic and promising approach, because it is efficient in recovery and produces high characteristic fibers. The essential pyrolysis variables, their influence on fiber characteristics, and the re-use of recycled fibers for new composites were highlighted in this paper.
- A successful commercial-scale pyrolysis program was implemented in Germany and the United Kingdom, and they have the ability to recycle CFRC in various forms. They may also recover longer and cleaner CFs, thanks to the big furnace and continuous flow.
- Pyrolysis, like any other recycling process, has several drawbacks, the most problematic of which is the probability of char development on the resultant fiber surface. Due to char, the mechanical characteristics of the recovered fibers will be substantially decreased. Chemical treatment and post-heating of the fibers both help to reduce char formation, but only to a limited extent.
- Pyrolysis in a nitrogen gas environment, unlike vacuum pyrolysis, may recycle both CFRC and GFRC.
- In pyrolysis, using a superheated steam atmosphere improves heat transmission, which accelerates the thermal breakdown and supports eliminating oxygen from the reactor. In comparison to other pyrolysis atmospheres, recycling CFRC with superheated steam leads to high retention of CF mechanical characteristics.
- According to the study, the higher the value of recycled CF, the lower the pyrolysis temperature.
- Microwave pyrolysis has enhanced the rate of heat while consuming a smaller quantity of energy, without interfering with the basic principle of pyrolysis. The method may recycle both CFRC and GFRC fibers while preserving greater mechanical characteristics.
- Both the oxidizing (air) and thermal (N2) atmospheres were important in determining surface properties. Surface defects were discovered in an oxidizing atmosphere, resulting in a decrease in TS and crystallite size. As a result, for a successful recycling process, a regulated and optimum temperature and residence duration in post-pyrolysis is advantageous.
- Recycling CFRC/GFRC by pyrolysis has great potential, since it recovers precious fibers and produces gas and liquid products.
- According to published research, the breakdown temperature of resin is complete between 450–500 °C in the case of GRFC. Meanwhile, CFRC breakdown temperatures are between 450–600 °C, depending on kind and whether it is cured or uncured. For post-pyrolysis in the air atmosphere, 500–600 °C was found to be the optimal temperature for oxidizing char and cleaning the fiber surface.
- It is important to identify the material cost reductions that may be achieved by using rCF. While rCF are cheaper than virgin fibers, they are inherently different from them, which has restricted the entry of rCF into the vCF market. Based on cost and performance, the task will be to modify the material in such a way that virgin fiber is replaced with recycled fiber.
- In the case of carbon fiber composite materials, pyrolysis can result in fibers that are short in length and discontinuous. There are certain advantages to using these fibers, such as: cost-effectiveness, light weight, a 3-dimensional complexity in the panels, and a secondary structure for airplane interiors. Thermochemically converted recycled fibers demonstrate good mechanical characteristics compared to virgin fibers.
- Recycled carbon fiber products in automobile applications deliver lighter and stronger components at high volume manufacturing rates, as well as considerable cost savings. Nonaligned and short fibers tend to generate excellent quality, 3D complicated, lightweight constructions for components and panels with complex forms.
- How effective/feasible is pyrolysis for mixed and polluted composite wastes?
- It is necessary to gain a better understanding of the influence of operational factors (heating temperature, reaction time, chemical solvent) on CF/GF. Further research into the optimum parameters is necessary to improve the quality of CF/GF.
- The impact of fiber recovery on composite quality (in comparison to vCF/vGF and remanufactured composites with rCF/rGF using the same structures) is unclear.
- How can rCF/rGF strength and length be compared to vCF/vGF using this method? Additional performance improvements will need a better understanding of pyrolysis interactions with chemical treatment.
- How could the total costs of the recycling and remanufacturing of composites be lowered so that pyrolysis may be used as a recycling technique on a large scale?
- The use of rCF/rGF after recovery from pyrolysis is a current field of study; such studies may play a major role in enhancing the characteristics of the products generated from them.
- Crosslinking of fibers also limits reusing of rCF/rGF in new composites. If RFs are re-aligned in the same way as vCF/vGF, their potential uses could be improved.
- Chemical treatment plays a role in improving the mechanical and physical characteristics of rCF/rGF. This involves research into the reaction of functional groups to resin interactions. Chemical treatment at the connection between these functional groups and the resin matrix may also be involved.
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
ACMs | Advanced Composite Materials |
Al | Aluminum |
ATR | Attenuated total reflection |
CF | Carbon fiber |
CFRC | Carbon fiber-reinforced composite |
CFRP | Carbon-fiber reinforced polymer |
DTG | Differential thermogravimetry |
E | Young modulus |
E&E | Electrical and Electronic equipment |
EOL | End-of-Life |
FBP | Fluidized-bed process |
FRC | Fiber-reinforced composites |
FTIR | Fourier-transform infrared |
GC | Chromatography |
GF | Glass fiber |
GFRC | Glass fibre reinforced composite |
GFRP | Glass-fiber reinforced polymer |
GS | Gravity separation |
IATA | International Air Transport Association |
MS | Mass spectroscopy |
NA | Nitrogen atmosphere |
NMP | N-methyl-2-pyrrolidinone |
PP | Polypropylene |
rCF | recycled carbon fiber |
rGF | recycled glass fiber |
RT | Room Temperature |
SC | Secondary combustion |
SEM | Scanning electron microscope |
SGRE | Siemens Gamesa Renewable Energy |
SMC | Sheet molding compound |
TG | Thermogravimetric analysis a |
TGA | Thermogravimetric analysis |
TS | Tensile strength |
vCF | Virgin carbon fiber |
VCS | Vacuum centrifugal separation |
vGF | Virgin glass fiber |
VP | Vacuum pyrolysis |
WPCBs | Waste printed circuit boards |
XPS | X-ray photoelectron spectroscopy |
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No. | References | Material | Reactor | Pyrolysis Products (wt%) | Application | Process Parameters | Oxidation Treatment | ||
---|---|---|---|---|---|---|---|---|---|
Solid | Liquid | Gas | |||||||
1 | Onwudili et al. [62] | CF from reinforced thermosets | Lab-scale batch reactor | 73.1 | 23.8 | 2.3 | Commercial LDPE | N2: 5 dm3/h, 500 °C, 45 min | 500 °C |
2 | Onwudili et al. [62] | GF from reinforced thermosets | Lab scale- batch reactor | 65.9 | 25.7 | 8.4 | Commercial LDPE | N2+SC: 500 °C, 30 min, 20 °C/min | 500 °C |
3 | Onwudili et al. [74] | Carbon reinforced composite plastic (CRCP) | 300 mL mini autoclave reactor | 72–77 | 22–25 | 2–4 | N2: 400–500 °C, <30 min SC: 450 °C, 2 h. | 450 °C | |
4 | Meyer et al. [60] | High tenacity CF | Lab scale TGA | - | - | - | Aerospace | N2: (60 mL/ min), 900 °C, 10 °C/min | 600 °C 60 cm3/min |
5 | Giorgini et al. [92] | GF from laminates waste | Batch reactor | 40–45 | 35–40 | 15–20 | 500–600 °C 150 min | 500 or 600 °C 10 to 60 min | |
6 | Giorgini et al. [93] | (1) Uncured T700S, 12 K CF (2) Cured T700S, 12 K CF | Batch Pilot plant | 65–70 55–60 | 10–15 25–30 | 15–20 15–20 | New composit | 450–600 °C 150 min, 8 °C/min | 500–600 °C |
7 | Zhou and Qiu [71] | WPCBs (GF) | A lab-scale reactor | 75.7 | 20 | 4.3 | - | VP: 600 °C, 30 min | - |
8 | Zhou et al. [72] | WPCBs (GF) | A lab-scale reactor | 72.2 | 21.45 | 6.35 | - | VCS: 400 °C, 1200 rpm, 6–10 min | - |
9 | Bradna and Zima [98] | Epoxy resin with CF | Py-GC/MS | - | - | - | - | 700 °C | |
10 | Nahil and Williams [99] | Polybenzoxazine resin with woven CF | Static bed batch reactor | 70–83.6 | 14–24.6 | 0.7–3.8 | Activated carbon fibers | N2: 350–700 °C, 60 min, 5 °C/min | 500 °C |
11 | Long et al. [73] | WPCBs (GF) | - | 74.7 | 15 | 10.3 | - | (1) VP: 550 °C, 120 min (2) GS + calcination: 600 °C, 10 min | - |
12 | Greco et al. [100] | Cured CF | - | - | - | - | Aeronautic | 550 °C, 20 min | 550 °C, 90 min |
13 | Cunliffe et al. [101] | (1) Thermoset polyester/styrene resin with GF (12%) (2) Thermoset polyester/styrene resin with GF (30%) (3) Phenolic resin with GF (31%) (4) Phenolic resin with CF (5) Epoxy resin with GF and CF (45%) (6) Polypropylene resin with GF tape (75%) (7) Vinylester resin with GF woven (70%) | Static-Bed reactor | 38.3–82.9 32.6 84.4–94.3 65 65.3–81.7 78.9 83.4 | 14.5–47.4 64.1 5.1–12 30.4 18–31.7 20 15 | 2.6–14.4 3.3 0.6–4.6 4.6 0.2–3 1.1 1.6 | Autombile, electric and circuit board | N2: 200 cm3/min 350–800 °C 60 min | 400−800 °C |
14 | Cunliffe and Williams [102] | Commercial polyester/GF (30%) automotive waste | Fixed Bed reactor | 39.3 | 39.6 | 5.8 | Autombile | N2: 3000 cm3/min 450 °C, 90 min | Muffle furnace 450 °C |
15 | Stoeffler et al. [103] | Cured & uncured CF | batch oven | - | - | - | Aerospace | 400 °C | - |
16 | Torres et al. [104] & Torres et al. [105] | GF polyester from SMC | Stainless steel Autoclave | 72.6–82.6 | 9.7–14.9 | 6.1–12.8 | Recovery of GF for composite | N2: 1 dm3/min 300–700 °C 30 min | - |
17 | López et al. [106] | T300/3 k CF | pilot-scale | 58.4–61.5 | 28.5–30.7 | 10–10.9 | - | 350–700 °C | 500 °C |
18 | López et al. [107] | GF from Polyester fiber glass | Thermolytic reactor | 68 | 24 | 8 | Ceramic | 550 °C 180 min | 1450 °C |
19 | Yun et al. [91] | GFRP from the Byproduct | TGA | - | - | - | - | N2: 200 mL/min RT-900 °C 5–20 °C/min | - |
20 | Yun et al. [108] | GFRP from the Byproduct | Batch Type Pyrolyzer Thermo Balance Reactor Wire Mesh Reactor | - - 20–80 | - - 15–50 | - - 5–15 | - - - | (1) N2: 1 L/min 500–900 °C 15 °C/min (2) N2: 0.315 L/min500–800 °C N2: 1 L/min (3) 600–1000 2,4,6,8 and 10 s | - - - |
Thermal Analysis | Mechanical Testing | Morphological Testing | Others |
---|---|---|---|
TGA ATR-FTIR | TS (MPa), E(MPa), Elongation (%) | SEM, AFM, XPS | Adhesion, Micro bond, fiber pullout, Image analysis for fiber length distribution |
Reference | Fiber Output | TS (MPa) | E (MPa) | Elongation (%) | Diameter | Stiffness | Fiber Length (mm) |
---|---|---|---|---|---|---|---|
Onwudili et al. [62] | GF | 11 | 428 | - | - | - | - |
Stoeffler et al. [103] | CF | 680–720% increase | 680% increase | 20–35% increase | 6.5 | - | 5.6 |
Giorgini et al. [92] | GF | 14 | 530 | - | - | - | - |
López et al. [106] | CF | 2537–2544 | 210–220 | - | 6.70–7.00 | - | |
Nahil and Williams [99] | CF | 2340–3270 910–1250 | 230–233 182–233 | 0.91–1.25 - | - - | - - | - - |
Greco et al. [100] | CF | - | 8% reduction | - | 6.2 | 14% reduction | - |
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Abdallah, R.; Juaidi, A.; Savaş, M.A.; Çamur, H.; Albatayneh, A.; Abdala, S.; Manzano-Agugliaro, F. RETRACTED: A Critical Review on Recycling Composite Waste Using Pyrolysis for Sustainable Development. Energies 2021, 14, 5748. https://doi.org/10.3390/en14185748
Abdallah R, Juaidi A, Savaş MA, Çamur H, Albatayneh A, Abdala S, Manzano-Agugliaro F. RETRACTED: A Critical Review on Recycling Composite Waste Using Pyrolysis for Sustainable Development. Energies. 2021; 14(18):5748. https://doi.org/10.3390/en14185748
Chicago/Turabian StyleAbdallah, Ramez, Adel Juaidi, Mahmut A. Savaş, Hüseyin Çamur, Aiman Albatayneh, Samer Abdala, and Francisco Manzano-Agugliaro. 2021. "RETRACTED: A Critical Review on Recycling Composite Waste Using Pyrolysis for Sustainable Development" Energies 14, no. 18: 5748. https://doi.org/10.3390/en14185748
APA StyleAbdallah, R., Juaidi, A., Savaş, M. A., Çamur, H., Albatayneh, A., Abdala, S., & Manzano-Agugliaro, F. (2021). RETRACTED: A Critical Review on Recycling Composite Waste Using Pyrolysis for Sustainable Development. Energies, 14(18), 5748. https://doi.org/10.3390/en14185748