Optimisation of Process Parameters to Maximise the Oil Yield from Pyrolysis of Mixed Waste Plastics
Open accessAbstract
The study sought to optimise process parameters of thermal pyrolysis of mixed waste plastic (MWP) to maximise pyrolytic oil yield. High-density polyethylene (HDPE), polypropylene (PP), and polystyrene (PS) were used as feedstocks for pyrolysis. Response surface methodology (RSM) and Box–Behnken design (BBD) were used to optimise the pyrolysis process. The optimisation was carried out by varying three independent variables, namely, reaction temperature (460–540 °C), residence time (30–150 min), and size of MWP feedstock (5–45 mm), to increase the liquid oil yield. A BBD matrix was used to generate the design of the experiments, and 15 experiments were conducted. The highest liquid oil yield of 75.14 wt% was obtained by optimising the operating parameters, which were a reaction temperature of 535.96 °C, a reaction time of 150 min, and a feedstock particle size of 23.99 mm. A model was developed to determine the relationships among the independent variables, and analysis of variance (ANOVA) was used to investigate their impact on maximising oil yield. ANOVA results showed that the temperature and residence time had the maximum impact on oil yield, followed by feedstock size. Physicochemical analysis of the properties of the plastic pyrolytic oil (PPO) revealed that the crude PPO obtained from the MWP had higher water (0.125 wt%) and sulfur content (5.12 mg/kg) and lower flash point (<20 °C) and cetane index (32), which makes it unsuitable for use as an automobile fuel. However, these issues can be resolved by upgrading the PPO using different posttreatment techniques, such as distillation and hydrotreatment.
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Liquid oil yields from mixed waste plastic pyrolysis can be approximately 48-75 wt.%, heavily influenced by feedstock composition, process temperature, residence time, reactor design, catalysts, and pre-treatment such as sorting to remove PVC and PET.
“Typical product yield ranges from mixed waste plastic pyrolysis can vary significantly; for instance, liquid oil yields can be approximately 48-75 wt.%, and these are heavily influenced by feedstock composition (with polyolefins favoring higher oil yields), process temperature, residence time, reactor design, and the application of catalysts, as well as pre-treatment methods like sorting to remove”
From Biofuels, E-Fuels, and Waste-Derived Fuels: Advances, Challenges, and Future Directions (2025) · cites this paper as [330]
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References 56 · Cited by 30
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- Authors
- Faisal, F., Rasul, M. G., Chowdhury, A. A., & Jahirul, M. I.
- Affiliations
- Central Queensland University (AU)
- Fuel and Energy Research Group, School of Engineering and Technology, Central Queensland University, Rockhampton, QLD 4702, Australia
- Corresponding author
- Chowdhury, Ashfaque Ahmed
- Venue
- Sustainability
- Publisher
- MDPI AG
- Published
- 2024-03-22
- Volume
- 16
- Issue
- 7
- Pages
- 2619
- ISSN
- 2071-1050 (ISSN-L)
- OpenAlex
- W4393068958
- Cited by
- 30
- References
- 56
- Citations by year
- 2026: 18 · 2025: 11 · 2024: 1
- FWCI
- 3.28
- Type
- journal article
- Language
- en
- Open access
- gold
- doi.org
- Licence
- Locations
- Sustainability (publishedVersion, cc-by)
- RePEc: Research Papers in Economics (submittedVersion)
- Funders
- CRC-P project (CRCPEIGHT000194, RSH/6017)
- Advanced Queensland Industry Research Fellowship project (CRCPEIGHT000194, RSH/6017)
- Topics
- Physical Sciences › Engineering › Biomedical Engineering › Thermochemical Biomass Conversion Processes
- Physical Sciences › Materials Science › Materials Chemistry › Thermal and Kinetic Analysis
- Physical Sciences › Environmental Science › Waste Management and Disposal › Municipal Solid Waste Management
- Keywords
- plastic waste pyrolysis, high-density polyethylene, polypropylene, polystyrene, reaction temperature, residence time, feedstock particle size, process parameter optimization, oil upgrading, hydrotreating, distillation
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