Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil
Abstract Boehmite nanoparticles and NaY nanozeolite were synthesized by co-precipitation and hydrothermal methods, respectively, and characterized by XRD, FT-IR, TG-DTA, BET, and SEM techniques. XRD and BET analyses demonstrated the formation of boehmite nanoparticles with a surface area of 350 m2/g...
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2025-01-01
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author | Ehsan Amini Kamran Ahmadi Alimorad Rashidi Amir Ali Youzbashi Mehran Rezaei Sakineh Mesgar |
author_facet | Ehsan Amini Kamran Ahmadi Alimorad Rashidi Amir Ali Youzbashi Mehran Rezaei Sakineh Mesgar |
author_sort | Ehsan Amini |
collection | DOAJ |
description | Abstract Boehmite nanoparticles and NaY nanozeolite were synthesized by co-precipitation and hydrothermal methods, respectively, and characterized by XRD, FT-IR, TG-DTA, BET, and SEM techniques. XRD and BET analyses demonstrated the formation of boehmite nanoparticles with a surface area of 350 m2/g and high crystallinity NaY nanozeolite with a surface area of 957 m2/g. In order to evaluate the effect of the content of the mesoporous boehmite nanoparticles on the catalytic performance of the Residue Fluid Catalytic Cracking (RFCC) catalyst, alumina active matrix-based and silica inactive matrix-based catalysts were prepared. Results actually demonstrated that the acidity of the zeolite composition improved with the addition of boehmite nanoparticles. On the other hand, in equal zeolite content, the alumina active matrix-based catalyst possessed higher acidity (NC30B20, 3.44 mmol NH3/g catalyst) than the silica inactive matrix-based catalyst (NC30B0, 2.31 mmol NH3/g catalyst). Microactivity tests (MAT) demonstrated that, with equal zeolite content, active matrix-based catalysts exhibited higher catalytic performance than inactive matrix-based catalyst. Furthermore, the active matrix-based catalyst (NC30B20) with a surface area of 370 m2/g showed the optimum catalytic performance in the RFCC process. The synthesized NC30B20 catalyst with 20 wt% mesoporous boehmite nanoparticles as an active matrix and 30 wt% zeolite nanoparticles balanced with silica had the highest gasoline yield (42 wt%) and gasoline selectivity (65.1 wt%). The catalytic performance test results showed that in equal MAT conversion (almost 64 wt%), the synthesized NC30B20 catalyst had higher catalytic performance than the commercial catalyst. |
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id | doaj-art-01e6fcaf6d184276b869906c507361f9 |
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language | English |
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spelling | doaj-art-01e6fcaf6d184276b869906c507361f92025-01-19T12:21:36ZengNature PortfolioScientific Reports2045-23222025-01-0115111810.1038/s41598-025-85723-7Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oilEhsan Amini0Kamran Ahmadi1Alimorad Rashidi2Amir Ali Youzbashi3Mehran Rezaei4Sakineh Mesgar5Research Department of Semiconductors, Material and Energy Research CenterResearch Department of Semiconductors, Material and Energy Research CenterNanotechnology Research Center, Research Institute of Petroleum IndustryResearch Department of Semiconductors, Material and Energy Research CenterSchool of Chemical, Petroleum and Gas Engineering, Iran University of Science and TechnologyDepartment of Organic Chemistry, Faculty of Chemistry, University of MazandaranAbstract Boehmite nanoparticles and NaY nanozeolite were synthesized by co-precipitation and hydrothermal methods, respectively, and characterized by XRD, FT-IR, TG-DTA, BET, and SEM techniques. XRD and BET analyses demonstrated the formation of boehmite nanoparticles with a surface area of 350 m2/g and high crystallinity NaY nanozeolite with a surface area of 957 m2/g. In order to evaluate the effect of the content of the mesoporous boehmite nanoparticles on the catalytic performance of the Residue Fluid Catalytic Cracking (RFCC) catalyst, alumina active matrix-based and silica inactive matrix-based catalysts were prepared. Results actually demonstrated that the acidity of the zeolite composition improved with the addition of boehmite nanoparticles. On the other hand, in equal zeolite content, the alumina active matrix-based catalyst possessed higher acidity (NC30B20, 3.44 mmol NH3/g catalyst) than the silica inactive matrix-based catalyst (NC30B0, 2.31 mmol NH3/g catalyst). Microactivity tests (MAT) demonstrated that, with equal zeolite content, active matrix-based catalysts exhibited higher catalytic performance than inactive matrix-based catalyst. Furthermore, the active matrix-based catalyst (NC30B20) with a surface area of 370 m2/g showed the optimum catalytic performance in the RFCC process. The synthesized NC30B20 catalyst with 20 wt% mesoporous boehmite nanoparticles as an active matrix and 30 wt% zeolite nanoparticles balanced with silica had the highest gasoline yield (42 wt%) and gasoline selectivity (65.1 wt%). The catalytic performance test results showed that in equal MAT conversion (almost 64 wt%), the synthesized NC30B20 catalyst had higher catalytic performance than the commercial catalyst.https://doi.org/10.1038/s41598-025-85723-7MesoporousNanoboehmiteNanozeoliteRFCC catalystCatalytic cracking |
spellingShingle | Ehsan Amini Kamran Ahmadi Alimorad Rashidi Amir Ali Youzbashi Mehran Rezaei Sakineh Mesgar Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil Scientific Reports Mesoporous Nanoboehmite Nanozeolite RFCC catalyst Catalytic cracking |
title | Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil |
title_full | Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil |
title_fullStr | Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil |
title_full_unstemmed | Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil |
title_short | Synergetic effects of nano-boehmite and Y nano-zeolite on catalytic cracking of residue oil |
title_sort | synergetic effects of nano boehmite and y nano zeolite on catalytic cracking of residue oil |
topic | Mesoporous Nanoboehmite Nanozeolite RFCC catalyst Catalytic cracking |
url | https://doi.org/10.1038/s41598-025-85723-7 |
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