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Design and Evaluation of a Co–Mo-Supported Nano Alumina Ultradeep Hydrodesulfurization Catalyst for Production of Environmentally Friendly Diesel Fuel in a Trickle Bed Reactor
In the present work, a nanocatalyst, γ-Al 2 O 3 nanoparticle-supported CoMo, was prepared experimentally and evaluated through a hydrodesulfurization (HDS) process for removing dibenzothiophene (DBT) from diesel fuel systematically in a trickle bed reactor (TBR). The results of the prepared catalyst...
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Published in: | ACS omega 2020-06, Vol.5 (21), p.12081-12089 |
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Main Authors: | , , , |
Format: | Article |
Language: | English |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | In the present work, a nanocatalyst, γ-Al
2
O
3
nanoparticle-supported CoMo, was prepared experimentally
and evaluated through a hydrodesulfurization (HDS) process for removing
dibenzothiophene (DBT) from diesel fuel systematically in a trickle
bed reactor (TBR). The results of the prepared catalyst characterization
tests (scanning electron microscopy, X-ray diffraction (XRD), XRD
phase quantification, and Brunner–Emmett–Teller) showed
good distribution of active metals (CoMo), difference in surface morphology,
and high dispersion of active metals. The catalyst exhibited good
metal–support interactions without impacting the surface area
significantly. A fully automated TBR reactor was used to evaluate
the activity of the prepared catalyst in the HDS process at ranges
of operating conditions: temperatures (250–350 °C), pressures
(6–10 bar), liquid hourly space velocities (LHSV) (1–3
h
–1
), and the activity of the prepared catalyst
were compared to a commercial catalyst based on Co–Mo/γ-alumina.
The results showed an obvious enhancement in the HDS process using
the homemade nanocatalyst compared to the commercial catalyst. It
has also been found that an increase in temperature led to an increase
in the conversion from 68.77 to 91.57%, a little positive effect on
conversion when pressure was increased, and a significant decrease
in conversion (from 91.57 to 75.58%) as LHSV was increased. A kinetic
model was developed for the HDS process to estimate kinetic parameters
and apply the parameters in reactor design. The developed model showed
that the DBT concentration in diesel fuel can be reduced significantly,
3000–240 ppm, at the optimum experimental conditions. |
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ISSN: | 2470-1343 2470-1343 |
DOI: | 10.1021/acsomega.0c00295 |