Please use this identifier to cite or link to this item: https://hdl.handle.net/20.500.14279/33197
Title: Effect of Polyethylene Pyrolysis Oil Hydrotreatment on the Pt/Al2O3 Catalyst: Experimental Characterization
Authors: Adamou, Panayiota 
Harkou, Eleana 
Bumajdad, Ali 
De Jong, Xander 
Van Haute, Maarten 
Constantinou, Achilleas 
Al-Salem, Sultan Majed 
Major Field of Science: Medical and Health Sciences
Field Category: Clinical Medicine
Keywords: Catalysts;Coke;Platinum;X-ray photoelectron spectroscopy
Issue Date: 16-Apr-2024
Source: ACS Omega, 2024, vol. 9 , iss. 17 , pp. 19057-19062
Volume: 9O
Issue: 17
Start page: 19057
End page: 19062
Journal: ACS Omega 
Abstract: The dramatic increase in plastics production, coupled with a low recycling and recovery rate, has been a major challenge for sustainable practices and combating climate change. Hydrotreatment processing to upgrade fuel oils is a well-known process in the petroleum industry. In this work, we aim to investigate the catalyst properties before and after the hydrotreatment of pyrolysis oil derived from plastics, namely, linear low-density polyethylene, as no such report is available in the literature. Granular and powder forms of the Pt/Al2O3 catalyst were used in this study with characterization methods executed as such: transmission electron microscopy, X-ray photoelectron spectroscopy (XPS), X-ray diffraction (XRD), thermogravimetric analysis (TGA), and IR-RIS. XRD data show that the crystallinity of the catalyst support was unaffected by the hydrotreatment without any residues left, as the characteristic diffraction peaks were indicated for the crystalline phase of the support as 37.4, 39.8, 46.3, and 67.3°. In addition, the TGA experiments revealed that the carbon deposition on the spent catalyst was higher, as indicated by the higher weight loss (15.359%) compared to the fresh catalyst sample (11.43%). XPS analysis showed that the carbon deposition is more intense on the granular spent catalyst, as the intensity of the peaks is some 15 times greater than the peaks from the fresh catalyst. Also, compared to the observed peaks of the powder catalyst, less coke is formed. The band at 1624.05 cm-1 from the IR-RIS spectra was attributed to a shifted C=O band from the coke formation. The extension of these investigations using different catalysts to improve their characteristics and performance and to inhibit coke deposition will contribute to the incorporation of such processes in industry as well as the cost of fuels.
URI: https://hdl.handle.net/20.500.14279/33197
ISSN: 24701343
DOI: 10.1021/acsomega.3c09729
Rights: Attribution-NonCommercial-NoDerivatives 4.0 International
Type: Article
Affiliation : Cyprus University of Technology 
Kuwait University 
Kuwait Petroleum Research and Technology B.V. 
Kuwait Institute for Scientific Research 
Publication Type: Peer Reviewed
Appears in Collections:Άρθρα/Articles

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