Pyrolysis of high-density polyethylene: Degradation behaviors, kinetics, and product characteristics

Natesakhawat, Sittichai; Weidman, Jennifer; Garcia, Stephanie; Means, Nicholas C.; Wang, Ping

doi:10.1016/j.joei.2024.101738

Title: Pyrolysis of high-density polyethylene: Degradation behaviors, kinetics, and product characteristics

Journal Article · Thu Jul 04 00:00:00 EDT 2024 · Journal of the Energy Institute

DOI: https://doi.org/10.1016/j.joei.2024.101738 · OSTI ID:2432329

^[1];

^[1]; Means, Nicholas C. ^[1]; Wang, Ping ^[1]

National Energy Technology Lab. (NETL), Pittsburgh, PA (United States)

Pyrolysis is a promising technology for converting plastic waste into valuable raw materials while offering a potential solution to the global plastic pollution crisis. In this study, the thermal pyrolysis of high-density polyethylene (HDPE) is investigated in a drop tube reactor under nearly isothermal conditions. The impact of reaction temperature and gas/volatile residence time on carbon conversion and product distribution is examined across a range of 500–900°C and 3.6–32.2s, respectively. Non-condensable gas products detected by online mass spectrometry are H₂, CH₄, C₂H₄, C₂H₆, C₃H₆, and C₃H₈. At elevated temperatures and prolonged residence time, H₂ yield reaches as high as 8.6 wt% of the initial HDPE mass due to intensified cracking reactions of C₂–C₃ hydrocarbons and long-chain aliphatic compounds. Consequently, pyrolysis tars consist mainly of polycyclic aromatic hydrocarbons (PAHs) with 5–7 rings, accompanied by visible coke deposition within the reactor. HDPE decomposition to volatiles is an endothermic process and it is complete at a temperature between 492°C and 525°C, depending on the heating rate employed, from non-isothermal thermogravimetric analysis and differential scanning calorimetry (TGA-DSC) measurements. The thermal degradation of HDPE pellets follows the two-dimensional nucleation growth model for conversion levels up to 0.8 with an apparent activation energy of 259–270 kJ/mol and a pre-exponential factor of 4.83 × 10¹⁷–1.37 × 10¹⁹ min^-1, determined from various isoconversional methods such as Flynn-Wall-Ozawa (FWO), Kissinger-Akahira-Sunose (KAS), and Starink, along with Criado's master plots. Further, these findings provide valuable insights into optimizing process parameters and refining reactor design for pyrolysis, which can be integrated with gasification and reforming processes to enhance hydrogen production on a larger scale.

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Research Organization:: National Energy Technology Laboratory (NETL), Pittsburgh, PA, Morgantown, WV, and Albany, OR (United States)

Sponsoring Organization:: USDOE Office of Fossil Energy and Carbon Management (FECM)

OSTI ID:: 2432329

Journal Information:: Journal of the Energy Institute, Journal Name: Journal of the Energy Institute Vol. 116; ISSN 1743-9671

Publisher:: ElsevierCopyright Statement

Country of Publication:: United States

Language:: English

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