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Waste-to-energy: Pyrolysis-gasification conversion of packaging waste from both micro and macro perspectives

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dc.contributor.author Yao, Zhitong
dc.contributor.author Makepa, Denzel Christopher
dc.contributor.author Poddar, Sourav
dc.contributor.author Reinm¨oller, Markus
dc.contributor.author Bertelsen, Michael
dc.contributor.author Jiang, Jingjing
dc.contributor.author Tong, Jiayao
dc.contributor.author Cui, Jiuzhuo
dc.contributor.author Liu, Jie
dc.contributor.author Miguel De Cachinho Cordeiro, Ivan
dc.date.accessioned 2026-03-10T07:43:31Z
dc.date.available 2026-03-10T07:43:31Z
dc.date.issued 2025-03-25
dc.identifier.citation Yao, Z., Makepa, D. C., Poddar, S., Reinmöller, M., Bertelsen, M., Jiang, J., ... & Cordeiro, I. M. D. C. (2025). Waste-to-energy: pyrolysis-gasification conversion of packaging waste from both micro and macro perspectives. Case Studies in Thermal Engineering, 71, 106228. en_US
dc.identifier.uri https://ir.cut.ac.zw:8080/xmlui/handle/123456789/699
dc.description.abstract The increasing volume of packaging waste, a representative component of municipal solid waste, has raised considerable environmental concerns. The present study conducted a detailed inves tigation into kinetic and thermodynamic of pyrolysis-gasification for post-consumer beverage cartons (BCs). Subsequently, the conversion was simulated using reactive force field molecular dynamics (ReaxFF-MD) to outline a proposed conversion pathway. Techno-economic assessment (TEA) was then conducted to evaluate economic performance of BCs conversion at different scales. The BCs decomposition could be divided into four stages of <375, 375–500, 500–800 and 800–900 ◦C with mass loss of 51.3–60.6, 19.0–25.3, 4.9–12.3 and 2.5–4.7 wt%, respectively. Fourier transform infrared spectrometry and mass spectrometry confirmed the evolution of fins, alkynes, and diolefins. The mean activation energy was calculated to be 60.2 kJ mol􀀀1 within conversion of <0.60, which increased significantly to 205.9 kJ mol􀀀1 for greater conversions. Positive changes in enthalpy and Gibbs free energy confirmed the endothermic and non- spontaneous nature of the pyrolysis-gasification reaction. The products generated and reactions involved in ReaxFF-MD simulation corresponded with the mass spectrometry results, indicating that β-scission of radicals was the predominant pathway for olefin formation. TEA analysis revealed that larger plants (45000 tonnes/a) had greater revenue potential, profitability, and positive returns on investment. en_US
dc.language.iso en en_US
dc.publisher Science direct en_US
dc.subject Packaging waste en_US
dc.subject Post consumer-beverage cartons en_US
dc.subject Pyrolysis-gasification conversion en_US
dc.subject ReaxFF-MD simulation en_US
dc.subject Techno-economic analysis en_US
dc.title Waste-to-energy: Pyrolysis-gasification conversion of packaging waste from both micro and macro perspectives en_US
dc.type Article en_US
dc.identifier.orcid 0000-0002-9180-2329 en_US
dc.identifier.orcid 0000-0003-2333-0283 en_US
dc.identifier.orcid 0009-0003-5251-8434 en_US
dc.identifier.orcid 0000-0001-8188-5469 en_US
dc.identifier.orcid 0009-0002-3124-3198 en_US
dc.identifier.orcid 0000-0002-6487-4618 en_US
dc.identifier.orcid 0009-0006-5272-538X en_US
dc.identifier.orcid 0009-0006-5272-538X en_US
dc.identifier.orcid 0000-0002-0313-8641 en_US
dc.identifier.orcid 0000-0002-6496-383X en_US


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