Malaysian
Journal of Analytical Sciences Vol 20 No 2 (2016): 296 - 302
OXIDATION
OF COMMERCIAL PETRONAS DIESEL WITH TERT-BUTYL HYDROPEROXIDE OVER POLYMOLYBDATE
ALUMINA SUPPORTED CATALYST MODIFIED WITH ALKALINE EARTH METALS
(Pengoksidaan
Diesel Komersial Petronas dengan Tert-Butil Hidroperoksida bersama Pemangkin
Polimolibdenum Diubahsuai dengan Logam Alkali)
Wan Nazwanie Wan Abdullah, Rusmidah Ali*, Wan Azlee Wan Abu Bakar
Department
of Chemistry, Faculty of Science,
Universiti Teknologi Malaysia, 81310 UTM Johor Bahru, Johor, Malaysia
*Corresponding author: rusmidah@kimia.fs.utm.my
Received: 9
December 2014; Accepted: 9 October 2015
Abstract
Due to strict environmental legislation
for ultra-low sulfur diesel fuels, increasing technical and operational
challenges are imposed to conventional hydrodesulfurization (HDS) technology.
Therefore, catalytic oxidative desulfurization (Cat-ODS) has been suggested to
be an alternative method to replace a conventional method which is hydrodesulfurization.
In this study, catalytic oxidation of commercial diesel was performed using an
oil-soluble oxidant, tert-butyl hydroperoxide (TBHP), over polymolybdate
supported on alumina MoO3-PO4/Al2O3 catalyst.
A commercial Petronas diesel with 440 ppmw of total sulfur was employed to
evaluate the elimination of sulfur compounds. Besides, the percentage of sulfur
removal was measured by (GC-FPD). Alkaline earth metals, such as
Calcium (Ca), Barium (Ba) and Strontium (Sr) were introduced on the surface of
MoO3-PO4/Al2O3. The results showed
that the catalytic activity decreased in the order, Ca/MoO3-PO4/Al2O3>Sr/MoO3-PO4/Al2O3>
Ba/MoO3-PO4/Al2O3. The Ca/MoO3-PO4/Al2O3
catalyst was characterized by XRD and FESEM. XRD results showed that the best
catalyst was highly amorphous while FESEM micrograph illustrated an aggregation
and agglomeration of various particle sizes. The catalytic activity of Ca/MoO3-PO4/Al2O3
catalyst with various Ca/Mo ratios were also studied. When the Ca/Mo ratio was
15:85, the sulfur removal was the
highest (79%) at 45ºC, 30 min and O/S molar ratio 3.0 with solvent =
dimetylformamide (DMF), diesel/solvent ratio = 1.0.
Keywords: Oxidative desulfurization, commercial diesel,
tert-butyl hydroperoxide, alkaline earth metals, polymolybdate,
dimetylformamide
Abstrak
Disebabkan undang-undang alam
sekitar yang ketat untuk bahan api sulfur diesel ultra-rendah, peningkatan
cabaran teknikal dan operasi dikenakan kepada hydropenyahsulfuran konvensional
teknologi (HDS). Oleh itu, penyahsulfuran oksidatif mengunakan pemangkin
(Cat-ODS) telah dicadangkan untuk menjadi satu kaedah alternatif untuk
menggantikan kaedah konvensional iaitu hydopenyahsulfuran. Dalam kajian ini,
pengoksidaan diesel komersial telah dijalankan menggunakan oksida larut minyak,
tert-butil hidroperoksida (TBHP) dan
mangkin molibdena berpenyokong alumina, MoO3-PO4/Al2O3.
Diesel komersial Petronas yang mengandungi sulfur 440 ppmw telah digunakan
untuk menilai penyahsulfuran. Selain itu, peratusan penyingkiran sulfur telah
diukur menggunakan (GC-FPD). Logam alkali, seperti Kalsium (Ca), Barium (Ba)
dan Strontium (Sr) telah dicelup pada permukaan MoO3-PO4/Al2O3
pemangkin. Hasil kajian menunjukkan bahawa aktiviti pemangkin menurun mengikut
susunan, Ca/MoO3-PO4/Al2O3 > Sr/MoO3-PO4/Al2O3
> Ba/MoO3-PO4/Al2O3. Pemangkin
Ca/MoO3-PO4/Al2O3 telah dicirikan
menggunakan XRD dan FESEM. Keputusan XRD menunjukkan pemangkin yang terbaik
adalah sangat amorfus manakala FESEM mikrograf menggambarkan satu aglomerasi
dalam pelbagai saiz zarah. Aktiviti pemangkin Ca/MoO3-PO4/Al2O3
dengan pelbagai nisbah Ca/Mo telah juga dikaji. Apabila nisbah Ca/Mo adalah
15:85, penyingkiran sulfur adalah tertinggi (79%) pada keadaan optimum: 45ºC,
30 min dan nisbah O/S molar = 3.0 dengan pelarut = dimetilformamida (DMF),
nisbah diesel/pelarut = 1.0.
Kata kunci: penyahsulfuran oksidatif, diesel
komersial, tert-butil hidroperoksida, logam alkali, polimolibdena,
dimetil-formamida
References
1. Chica, A.,
Corma, A. and Dómine M. E. (2006). Catalytic oxidative desulfurization (ODS) of
diesel fuel on a continuous fixed-bed reactor. Journal of Catalysis, 242: 299 – 308.
2. Abdullah, W. N.
W., Bakar, W. A. W. A. and Ali, R. (2014). Catalytic oxidative desulfurization
of diesel fuel utilizing a polymolybdate alumina supported catalyst:
Characterization, catalytic activity and mechanistic study. Reaction Kinetic Mechanism and Catalyst,
114:547 – 560.
3. Lifeng, W.,
Baode, S., Frances, H. Y. and Ralph, T. Y. (2012). Effects of aromatics on
desulfurization of liquid fuel by p-complexation and carbon adsorbents. Chemical Engineering Society, 73:208 –
217.
4. Tam, P. S.,
Kittrell, J. R. and Eldridge J. W. (1990). Desulfurization of fuel oil by
oxidation and extraction. 1. Enhancement of extraction oil yield. Industrial & Engineering Chemistry Research, 29(3): 321 – 324.
5. Wan Abu Bakar,
W. A., Ali, R., Abdul Kadir, A. A. and Wan Mokhtar, W. A. (2012). Effect of
transition metal oxides catalyst on oxidative desulfurization of model diesel. Fuel Processing Technology, 101: 78 –
84.
6. Malka, K. and
Tatiboue, J. M. (1998). A two-step
preparation of silica-supported calcium-molybdenum catalysts. Journal of
Catalysis, 175: 204 – 212.
7. Chang,
J., Wang, A., Liu, J., Li, X. and Hu, Y. (2010). Oxidation of
dibenzothiophene with cumene hydroperoxide on MoO3/SiO2
modified with alkaline earth metals. Catalysis
Today, 149: 122 – 126.
8. Wan Abdullah, W.
N., Wan Abu Bakar W. A., Ali R. and Embong Z. (2015). Oxidative desulfurization
of commercial diesel catalyzed by tert-butyl hydroperoxide polymolybdate on
alumina: Optimization of Box-Behnken design. Clean Technologies and
Environment Policy, 17: 433 – 441.
9. Jones, C., Cole, K. J., Taylor, S. H., Crudace, M. J. and Hutchings, G.
J. (2009). Copper
manganese oxide catalysts for ambient temperature carbon monoxide oxidation:
Effect of calcination on activity.
Journal of Molecular Catalysis A: Chemical,
305:121 – 124.