Low-Temperature Upcycling of Polyethylene into Fuel-Range Hydrocarbons: An Innovative Approach on the Feed-Catalyst Bed Design

The energy-intensive nature of the catalytic pyrolysis of plastic for fuel production remains a major challenge in the renewable energy field. To address this, the feed-catalyst bed of a vertical tubular pyrolysis reactor was optimized to upcycle polyethylene (PE) into fuel-range hydrocarbons. Using a dual-stage feed-catalyst bed design (feed-to-catalyst ratio of 5:1), 86.1 wt % conversion of PE was achieved at 300 °C. Compared to the single-stage design, this design improved conversion by 1.68-fold, attributed to the sequential cracking effect. This effect was amplified when a set of zeolites with a 12-membered ring (faujasite and mordenite) was incorporated, achieving a gasoline selectivity of 55.9%. The enhanced performance demonstrates that the dual-stage catalyst bed offers a promising design strategy for enabling low-temperature plastic upcycling with potential applications in renewable carbon resources.

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Publication Details

Journal
ACS Sustainable Chemistry & Engineering
Published
2026-02-09
DOI
https://doi.org/10.1021/acssuschemeng.5c12683
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
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article

Low-Temperature Upcycling of Polyethylene into Fuel-Range Hydrocarbons: An Innovative Approach on the Feed-Catalyst Bed Design

Shinya Furukawa, Kai Qi Tan, Siew Chun Low, Duanxing Li
ACS Sustainable Chemistry & Engineering
Thermochemical Biomass Conversion Processes
article

Low-Temperature Upcycling of Polyethylene into Fuel-Range Hydrocarbons: An Innovative Approach on the Feed-Catalyst Bed Design

Shinya Furukawa, Kai Qi Tan, Siew Chun Low, Duanxing Li
article en

Abstract

The energy-intensive nature of the catalytic pyrolysis of plastic for fuel production remains a major challenge in the renewable energy field. To address this, the feed-catalyst bed of a vertical tubular pyrolysis reactor was optimized to upcycle polyethylene (PE) into fuel-range hydrocarbons. Using a dual-stage feed-catalyst bed design (feed-to-catalyst ratio of 5:1), 86.1 wt % conversion of PE was achieved at 300 °C. Compared to the single-stage design, this design improved conversion by 1.68-fold, attributed to the sequential cracking effect. This effect was amplified when a set of zeolites with a 12-membered ring (faujasite and mordenite) was incorporated, achieving a gasoline selectivity of 55.9%. The enhanced performance demonstrates that the dual-stage catalyst bed offers a promising design strategy for enabling low-temperature plastic upcycling with potential applications in renewable carbon resources.

ACS Sustainable Chemistry & EngineeringVol. 14(7)
Universiti Sains Malaysia (MY), The University of Osaka (JP)
Openalex Percentile: Top 62%
Thermochemical Biomass Conversion Processes
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