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Abstract:
The catalytic hydrogenation of petroleum resin (PR) to high value-added hydrogenated PR (HPR) represents a forward-looking technology for upgrading the pyrolysis petroleum by-product. Herein, flower-like and pure-phase supported nickel phosphide catalysts were controllably fabricated through a hydrotalcite strategy with red phosphorous as the P source. The PR hydrogenation activity of the catalysts followed the order of Ni2P/Al2O3 > NiP2/Al2O3 > Ni/Al2O3 > imp-Ni2P/Al2O3 catalysts (prepared by the impregnation method). Such enhanced performance of Ni2P/Al2O3 could be ascribed to small nickel phosphide particle size and rich active Niδ+ species. Notably, the sulfur contents of PR were effectively reduced from 55.4 (C5PR) and 72.3 ppm (C9PR) to 3.8 and 7.9 ppm after hydrogenation by Ni2P/Al2O3. Meanwhile, Ni2P/Al2O3 also exhibited good stability with the hydrogenation degree of HC5PR maintaining at 94.39 % after 100 h. Our work provides a promising nickel phosphide catalyst with outstanding hydrogenation activity, hydrodesulfurization ability, and stability toward PR hydrogenation. © 2022 Elsevier Ltd
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Chemical Engineering Science
ISSN: 0009-2509
Year: 2022
Volume: 264
4 . 7
JCR@2022
4 . 1 0 0
JCR@2023
ESI HC Threshold:74
JCR Journal Grade:2
CAS Journal Grade:2
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ESI Highly Cited Papers on the List: 0 Unfold All
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30 Days PV: 2
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