Catalytic co-pyrolysis of teak wood sawdust and polystyrene: Effect of process parameters on yield and properties of pyrolysis oil

• Waste biomass and plastics were co-pyrolysed for pyrolysis oil production. • The maximum pyrolysis oil (51.58 wt.%) was found to be 30 wt.% PS blending. • The use of catalysts at 5 and 10 wt.% promoted selectivity for aromatic hydrocarbons. • Characterisation of char confirmed enhanced properties by blending PS. The present study explores the thermo-catalytic co-pyrolysis of waste teak wood sawdust (TWS) and polystyrene (PS) using a semi-batch reactor. The experiments were performed at varying temperatures (450-550 °C), biomass-to-plastic ratios (10-50 wt.%), and catalyst loadings (5-20 wt.% of CaO and MgO). The physicochemical analysis of TWS and PS revealed HHV values of 19.50 and 43.18 MJ kg -1 , and oxygen contents of 45.40% and 0.43%, respectively. TGA results showed major biomass degradation occurring between 150-550 °C, while the FTIR analysis identified key functional groups, including C-H, C=C, -OH, and C=O. Thermal pyrolysis at 500 °C produced a 46.05% liquid yield, while the addition of 30 wt.% PS increased yield by 5.53%. The resultant pyrolytic oil exhibited an improved carbon content (81.37%) and a higher heating value (37.85 MJ kg -1 ). The GC-MS analysis demonstrated a 59.69% increase in hydrocarbon yield at 30 wt.% PS while acids and ketones reduced by 4.58% and 9.74%, respectively. The addition of CaO (5 wt.%) and MgO (10 wt.%) enhanced the deoxygenation, aromatisation, and cracking reactions, resulting in selectivity towards aromatic hydrocarbons. The catalytic pyrolytic oil yielded 62% total hydrocarbons, with the aromatic fraction accounting for 56% of the total. The NMR study further confirmed the shifting of the hydrogen from oxygen-containing compounds towards aromatic structures. Furthermore, blending PS at a dynamic ratio decreased the char yield, whereas adding catalysts increased it. The catalytic char showed increased ash content and demonstrated alkaline pH. Overall, the thermo-catalytic co-pyrolysis has significant potential to contribute to the circular economy by converting waste into renewable fuels and chemicals.

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Journal
Energy Nexus
Published
2026-02-09
DOI
https://doi.org/10.1016/j.nexus.2026.100668
Primary Topic
Thermochemical Biomass Conversion Processes
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article
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article

Catalytic co-pyrolysis of teak wood sawdust and polystyrene: Effect of process parameters on yield and properties of pyrolysis oil

Ranjeet Kumar Mishra, Tanushka Florence Panicker
Energy Nexus
Thermochemical Biomass Conversion Processes
article

Catalytic co-pyrolysis of teak wood sawdust and polystyrene: Effect of process parameters on yield and properties of pyrolysis oil

Ranjeet Kumar Mishra, Tanushka Florence Panicker
article en

Abstract

• Waste biomass and plastics were co-pyrolysed for pyrolysis oil production. • The maximum pyrolysis oil (51.58 wt.%) was found to be 30 wt.% PS blending. • The use of catalysts at 5 and 10 wt.% promoted selectivity for aromatic hydrocarbons. • Characterisation of char confirmed enhanced properties by blending PS. The present study explores the thermo-catalytic co-pyrolysis of waste teak wood sawdust (TWS) and polystyrene (PS) using a semi-batch reactor. The experiments were performed at varying temperatures (450-550 °C), biomass-to-plastic ratios (10-50 wt.%), and catalyst loadings (5-20 wt.% of CaO and MgO). The physicochemical analysis of TWS and PS revealed HHV values of 19.50 and 43.18 MJ kg -1 , and oxygen contents of 45.40% and 0.43%, respectively. TGA results showed major biomass degradation occurring between 150-550 °C, while the FTIR analysis identified key functional groups, including C-H, C=C, -OH, and C=O. Thermal pyrolysis at 500 °C produced a 46.05% liquid yield, while the addition of 30 wt.% PS increased yield by 5.53%. The resultant pyrolytic oil exhibited an improved carbon content (81.37%) and a higher heating value (37.85 MJ kg -1 ). The GC-MS analysis demonstrated a 59.69% increase in hydrocarbon yield at 30 wt.% PS while acids and ketones reduced by 4.58% and 9.74%, respectively. The addition of CaO (5 wt.%) and MgO (10 wt.%) enhanced the deoxygenation, aromatisation, and cracking reactions, resulting in selectivity towards aromatic hydrocarbons. The catalytic pyrolytic oil yielded 62% total hydrocarbons, with the aromatic fraction accounting for 56% of the total. The NMR study further confirmed the shifting of the hydrogen from oxygen-containing compounds towards aromatic structures. Furthermore, blending PS at a dynamic ratio decreased the char yield, whereas adding catalysts increased it. The catalytic char showed increased ash content and demonstrated alkaline pH. Overall, the thermo-catalytic co-pyrolysis has significant potential to contribute to the circular economy by converting waste into renewable fuels and chemicals.

Energy NexusVol. 21
Manipal Academy of Higher Education (IN)
Openalex Percentile: Top 63%
Thermochemical Biomass Conversion Processes
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