Oxidative Desulfurization of Kerosene in Batch Reactor using Magnetite Mesoporous Silica Composite Zeolite Catalyst

The petroleum refining sector has increasingly prioritized the creation of clean fuel as a crucial priority. The objective of this project is to generate environmentally friendly fuel through the use of a straightforward and uncomplicated method. Using a novel synthetic nano-catalyst, batch oxidative desulfurization (ODS) eliminates sulfur compounds in Kerosene. The new Catalyst's silica nano-particle support is initially manufactured utilizing the sol-gel technique. Subsequently, the support is employed to fabricate a synthetic composite nano-catalyst composed of ferric oxide, utilizing the techniques devised for extracting a novel synthetic handcrafted (Fe2O3/composite support) Nano-catalyst. The composite supports used for the robust studies on the desulfurization process contain different levels of HY-zeolite (100 percent Nano silica). These levels include 10% HY-zeolite + 90% Nano silica, 20% HY-zeolite + 80% Nano silica, and 30% HY-zeolite + 70% Nano silica. The supports and manufactured Catalyst underwent characterization tests, including SEM, XRD, XRF, TGA, FTIR, BET, and particle size distribution. The tests showed an ideal distribution of the active metal (Fe), different surface structures, and a high active metal dispersion were achieved. The prominent locations are identified as limited in number, and the catalysts exhibit metal-support solid interaction. The existing Catalyst's performance was evaluated using a batch reactor. The assessment involved testing the Catalyst at different reaction temperatures (303 to 393 K) and batch times (30 to 120 minutes) while varying HY-zeolite quantities in the composite supports.

Authors

Institutions

Publication Details

Journal
Journal of Petroleum Research and Studies
Published
2024-09-22
DOI
https://doi.org/10.52716/jprs.v14i3.804
Primary Topic
Catalysis and Hydrodesulfurization Studies
Type
article
Field-Weighted Citation Impact
0.00
Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Oxidative Desulfurization of Kerosene in Batch Reactor using Magnetite Mesoporous Silica Composite Zeolite Catalyst

Ban A. Al-Tabbakh, Aysar Talib Jarullah, Ahmed K. Hussein
Journal of Petroleum Research and Studies
Catalysis and Hydrodesulfurization Studies
article

Oxidative Desulfurization of Kerosene in Batch Reactor using Magnetite Mesoporous Silica Composite Zeolite Catalyst

Ban A. Al-Tabbakh, Aysar Talib Jarullah, Ahmed K. Hussein
article en

Abstract

The petroleum refining sector has increasingly prioritized the creation of clean fuel as a crucial priority. The objective of this project is to generate environmentally friendly fuel through the use of a straightforward and uncomplicated method. Using a novel synthetic nano-catalyst, batch oxidative desulfurization (ODS) eliminates sulfur compounds in Kerosene. The new Catalyst's silica nano-particle support is initially manufactured utilizing the sol-gel technique. Subsequently, the support is employed to fabricate a synthetic composite nano-catalyst composed of ferric oxide, utilizing the techniques devised for extracting a novel synthetic handcrafted (Fe2O3/composite support) Nano-catalyst. The composite supports used for the robust studies on the desulfurization process contain different levels of HY-zeolite (100 percent Nano silica). These levels include 10% HY-zeolite + 90% Nano silica, 20% HY-zeolite + 80% Nano silica, and 30% HY-zeolite + 70% Nano silica. The supports and manufactured Catalyst underwent characterization tests, including SEM, XRD, XRF, TGA, FTIR, BET, and particle size distribution. The tests showed an ideal distribution of the active metal (Fe), different surface structures, and a high active metal dispersion were achieved. The prominent locations are identified as limited in number, and the catalysts exhibit metal-support solid interaction. The existing Catalyst's performance was evaluated using a batch reactor. The assessment involved testing the Catalyst at different reaction temperatures (303 to 393 K) and batch times (30 to 120 minutes) while varying HY-zeolite quantities in the composite supports.

Journal of Petroleum Research and StudiesVol. 14(3)
Research Institute of Petroleum Exploration and Development (CN), University of Petroleum (ID), University of Tikrit (IQ)
Openalex Percentile: Top 85%
Catalysis and Hydrodesulfurization Studies
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.

Oxidative Desulfurization of Kerosene in Batch Reactor using Magnetite Mesoporous Silica Composite Zeolite Catalyst — Ban A. Al-Tabbakh, Aysar Talib Jarullah, et al. · Journal of Petroleum Research and Studies (2024) | TGRS Research Map | TGRS