2022
DOI: 10.1016/j.matlet.2021.131472
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Enhanced catalytic conversion of palm oil into biofuels by Cr-incorporated sulphated zirconia

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Cited by 11 publications
(16 citation statements)
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“…The absorption peaks at 995-1003, 1049-1096, 1134-1157, and 1227 cm −1 are S-O symmetric vibrations, S-O asymmetric vibrations, S=O symmetry vibrations, and S=O asymmetric vibrations [34][35][36]. The peak with low intensity in the area of 1404 cm −1 is the stretching vibration of S=O, indicating the formation of SO 3 species on the surface of ZrO 2 [37]. The presence of characteristic bands of ZrO 2 -SO 4 proves that the impregnation of H 2 SO 4 on ZrO 2 has been successfully carried out.…”
Section: Functional Group Characterization For Zro 2 -Somentioning
confidence: 96%
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“…The absorption peaks at 995-1003, 1049-1096, 1134-1157, and 1227 cm −1 are S-O symmetric vibrations, S-O asymmetric vibrations, S=O symmetry vibrations, and S=O asymmetric vibrations [34][35][36]. The peak with low intensity in the area of 1404 cm −1 is the stretching vibration of S=O, indicating the formation of SO 3 species on the surface of ZrO 2 [37]. The presence of characteristic bands of ZrO 2 -SO 4 proves that the impregnation of H 2 SO 4 on ZrO 2 has been successfully carried out.…”
Section: Functional Group Characterization For Zro 2 -Somentioning
confidence: 96%
“…SZ-0.8-600 catalyst with the highest total acidity showed the lowest monoclinic peak intensity. The addition of a high concentration of H 2 SO 4 causes a large number of SO 4 2− ions to cover the surface of ZrO 2 , decreasing crystallinity [37,38]. The intensities of the monoclinic peaks at temperatures of 800 and 900 • C were higher than those at 600 and 700 • C. This occurred because the high calcination temperature caused SO 4 2− ions to decompose from the catalyst surface, increasing the crystallinity of the catalyst.…”
Section: Zro 2 -So 4 Crystal Structure Characterizationmentioning
confidence: 98%
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“…75 As a result, hydrocracking took place efficiently, thus leading to high CPO conversion. According to Utami et al 76 the transition metal, in this case, zirconium, had a Lewis acid feature that could promote the cracking process of longer chain hydrocarbons into shorter ones. The active site that adsorbed the hydrogen atom of H 2 gas was subsequently transferred into the compound to be cracked down and later would eventually be replaced with a hydrocarbon molecule through the cracking reaction catalyzed by the Brønsted acid site on the catalyst.…”
Section: Hydrocracking Processmentioning
confidence: 99%