Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating
<p> Basra crude oil was hydro treated in trickle–bed reactor using cobalt - molybdenum alumina as a Catalyst. The reaction range temperatures was598 – 648 k, while LHSV was 0.7 – 2 hr<sup>-1</sup>. The pressure and H<sub>2</sub>/Oil for all experiments keep constant...
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doaj-f31d7b621e734160a37e60f0487fa6952020-11-24T22:22:43ZengTikrit UniversityTikrit Journal of Engineering Sciences1813-162X2312-75892013-05-01173132Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro TreatingMuzher M. IbrahimAbdulhalim A. MohamedAyser T. Jarallah<p> Basra crude oil was hydro treated in trickle–bed reactor using cobalt - molybdenum alumina as a Catalyst. The reaction range temperatures was598 – 648 k, while LHSV was 0.7 – 2 hr<sup>-1</sup>. The pressure and H<sub>2</sub>/Oil for all experiments keep constant at 3Mpa and 300 L/L respectively.</p><p> Desulphurization and demutualization kinetics were studied and found that the kinetics of sculpture removal is of first – order, and the kinetic of vanadium and nickel removal is of second – order.</p><p> Activation energy were calculated and their value are 24.03, 745.86, 63.90 KJ / mole, respectively for sculpture, vanadium, and nickel.</p>http://www.tj-es.com/ojs/index.php/tjes/article/view/190Hydrodesulphurization kinetic, Cobalt-molybdenum, catalyst, Trickle bed reactor, Hydro demetalization kinetic |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Muzher M. Ibrahim Abdulhalim A. Mohamed Ayser T. Jarallah |
spellingShingle |
Muzher M. Ibrahim Abdulhalim A. Mohamed Ayser T. Jarallah Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating Tikrit Journal of Engineering Sciences Hydrodesulphurization kinetic, Cobalt-molybdenum, catalyst, Trickle bed reactor, Hydro demetalization kinetic |
author_facet |
Muzher M. Ibrahim Abdulhalim A. Mohamed Ayser T. Jarallah |
author_sort |
Muzher M. Ibrahim |
title |
Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating |
title_short |
Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating |
title_full |
Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating |
title_fullStr |
Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating |
title_full_unstemmed |
Kinetics of Sulfur, Vanadium and Nickel Removal from Basra Crude Oil Hydro Treating |
title_sort |
kinetics of sulfur, vanadium and nickel removal from basra crude oil hydro treating |
publisher |
Tikrit University |
series |
Tikrit Journal of Engineering Sciences |
issn |
1813-162X 2312-7589 |
publishDate |
2013-05-01 |
description |
<p> Basra crude oil was hydro treated in trickle–bed reactor using cobalt - molybdenum alumina as a Catalyst. The reaction range temperatures was598 – 648 k, while LHSV was 0.7 – 2 hr<sup>-1</sup>. The pressure and H<sub>2</sub>/Oil for all experiments keep constant at 3Mpa and 300 L/L respectively.</p><p> Desulphurization and demutualization kinetics were studied and found that the kinetics of sculpture removal is of first – order, and the kinetic of vanadium and nickel removal is of second – order.</p><p> Activation energy were calculated and their value are 24.03, 745.86, 63.90 KJ / mole, respectively for sculpture, vanadium, and nickel.</p> |
topic |
Hydrodesulphurization kinetic, Cobalt-molybdenum, catalyst, Trickle bed reactor, Hydro demetalization kinetic |
url |
http://www.tj-es.com/ojs/index.php/tjes/article/view/190 |
work_keys_str_mv |
AT muzhermibrahim kineticsofsulfurvanadiumandnickelremovalfrombasracrudeoilhydrotreating AT abdulhalimamohamed kineticsofsulfurvanadiumandnickelremovalfrombasracrudeoilhydrotreating AT aysertjarallah kineticsofsulfurvanadiumandnickelremovalfrombasracrudeoilhydrotreating |
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1725767043222863872 |